BULLETIN OF THE UNIVERSITY OF TEXAS NO. 189 Four Times a Month. SCIENTIFIC SERIES NO. 19. JULY 1, 1911 Bureau of Economic Geology and Technology The Composition of 1exas G..,oals and Lignites and The Use of Producer Gas in 1exas PUBLISHED BY THE UNIVERSITY OF TEXAS AUSTIN, TEXAS E'1t.tered tJI 1ec<>nd-c'lass mail matter at -the postoffice at Austin, .}.'exas \ , i , I ~Uttj·l" ·I' ; tl th-1''.i.J. \ . . ' ~,, 1/> .> J'• 242-711-2500-4,40 BULLETIN OF THE UNIVERSITY OF TEXAS NO. 189 Four Times a Month. SCIENTIFIC SERIES NO. 19. JULY 1, 1911 The Composition of Texas G"oa/s and Lignites and The Use of Producer Gas tn Texas BY WM. B. PHILLIPS Director of the Bureau of Economic Geology and Technology S. H. WORRELL Chief of the Testing Laboratory DRURY McN. PHILLIPS • PUBLISHED BY THE UNIVERSITY OF TEXAS AUSTIN, TEXAS Entered as second-class mail matter at the postojfice at Austin, Texas TABLE OF CONTENTS. PAGE. INTRODUCTION .............. ... . . .... .. .. .. . . .. .. ...... 3-4 CHAPTER I...... ... . . ...... .. .... .. . . .. . .. .. ... .. .. .... 5 Ooal.-Demand far Information-Coal Fields-Railroad Facilities-Production of Coal and Lignite-Tables of Analyses-Discussion-Value of Products from Gas-works in the United States-Fuel and Illuminating Gas-Heat­ing power of Texas Coals-Analyses of Coals Not Now Used. CHAPTER II. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 37 Lignite.-Extent of Fields-Geological Formations­Flora and Fauna of Coal Beds in General-Tables of Analyses-Discussion-Analyses of Lignites Not Now Used. CHAPTER III. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 59 The Use of Producer Gas in Texas.-Installations of Producers-Lignite Fields in United States-Tests o.f Texas Lignite in Fuel Testing Plant, St. Louis-Estab­lishments in Texas-Producers and Gas Engines Used in Texas-Tables of Producer Operations-Analyses of Pro­ducer Gas-Heat Units in Producer Gas-Gas Engine and Producer Considered as a Compact System-Economy from Use of Producer Gas-Cost of Fuel per Horse-power Hour-Producer Gas from Lignite to be Chief Source of Power. '·"'ft. MAR 11 19\4 INTRODUCTION This Bulletin on The Composition of Texas Coals and Lig­nites and the Use of Producer Gas in Texas has been prepared for the purpose of supplying the numerous requests for in­formation respecting the character of our fuels. There has been no geological survey in Texas since 1892, and nearly all of the publications of that survey, 1888-1892, are now out of print, as are also the publications of the Uni­versity Mineral Survey, 1901-1905. There have been three special publications on the subject of Texas Coals and Lignites. The first of these was a pamphlet entitled "Preliminary Re­port on the Utilization of Lignite," by E. T. Dumble, State Geologist, November 18, 1891. This was followed, in 1892, by his comprehensive ''Report OR the Brown Coal and Lignite of Texas,'' in which he discussed the character, formation, oc­currence, and fuel uses of our lignites. Of this excellent re­port there are still some copies on hand for distribution, price, 20 cents for unbound and 25 cents for bound copies. The Texas Geological Survey was discontinued in 1892, and there were no further publications until the establishment of the University Mineral Survey in 1901. This survey was dis­continued in 1905. In May, 1902, it issued Bulletin No. 3, entitled ''Coal, Lig­nite and Asphalt Rocks;" in which were given sections of coal and lignite seams and many detailed analyses. The edition of this Bulletin has long since been exhausted, and there is not a single copy that can be sent out. In the meantime there has been a considerable development of coal and lignite mining in Texas, the combined production having increased from 1,104,­953 tons, valued at $1,907,024, in 1901. to 2,108,179 tons, val­ued at $3,771,089, in 1910. During this period the production of lignite alone has increased from 303,155 tons, valued at $251,288, to 979,232 tons, valued at $941,700. During the last few years there has been a marked increase in the use of lig­nite in gas-producers, the gas thus made going to gas engines for the generation of power. Lignite is also used in gas-pro­ducers for fuel to be employed in the burning of lime, etc. Bulletin of the University of Texas In the chapter on ''The Use of I~ignite in Gas Producers,'' pre­pared by Mr. Drury McN. Phillips, at his own expense, this matter is discussed. Considering the great extent of the lignite fields in Texas, probably in excess of 60,000 square miles, an area larger than the entire State of Georgia, and the fact that every variety of this fuel is to be found here, and further, that it affords the cheapest and best fuel in the State, with the possible ex­ception of natural gas in certain favored localities, for many commercial purposes, it is well within reason to believe that this fuel will be our chief industrial reliance for power. Since 1895 the production of lignite has increased from 124,343 tons, valued at $111,908, to 979,232 tons. valued at $941,700. During this period of 16 years the production of coal has increased about 200 per cent, while that of lignite has increased about 700 per cent. The investigations on coal an__1~ ~ ~ _..'.:__!~__::__~____::__~~ f"1 ~~~~B.T.U.B.T.U. ~-~_!_ 1518 -----------4.09 47.95138.89 9.07 2.45 50.001 40.55 9.45 2.00 66.70 5.35 10.851 1.47 69.!\5 5.58i 11.32 1.54 11,052 12,!i66 1.29 80.6 1518 1519 --------..--3.46 48.84 36.61 11.09 2.09 60.70; 37.93111.37 2.17 66.651 5.65 7.46 3.62 69.04 5.94; 7.731 3.75 12,036 12,4701 1.321 82.51. 1519 1520 -----------9.40 33.08: 40.09 17.43 1.28 36.521 44.26 19.22 1.42 62.551 4.14 8.07 1.63 64.06 4.57'1 8.921 1.81 11,149; 12,3171 1.41 87.1 1520 1521 ----------6.01 38.16i 36.82 18.11 1.96 41.00 89.56 19.44 1.28 58.85 4.63 9.60, 0.78 63.22 4.87 10.32 0.87 11,472' 12,324, 1.62[ 101.2, 152~ 152"2 -----------12.60 31.721 42.98 12.80 1.84 86.26 49.12 14.62 2.11 56.87 3.891 11.14, 1.07 64.88 4.45 12.71 1.23 10,656 12,190 l.48: 92.5 152_ 1523 -----------12.21 31.93 41.12 14.74 1.73 87.52 46.83 15.65 1.08 59.40 3.37 8.o5: J.58 67.07 3.73 0.17 1.80 10,575 12,017 I.441 oo.ol 1s2~ 1524 -----------12.56 34.13 41.99 11.82 1.63 89.04 48.03 12.00 1.87 58.331 8.'/5 11.171 1.22 66.72 4.30 12.78' l .40 10,873 11,81H 1.621101.2[ 1!\24 1525 -----------8.12 29.62 46.84 15.42 1.56 82.24 49.90 17.86 1.70 fi0.191 8.64 8.31 1.72 65.521 S.99i 9.05 1.88 11,515 12,53~ 1.24 77.G, 1525 1526 -----------5.95 33.08 44.79 16.18 2.00 S5.18 47.63 17.19 2.13 57.85 3.93 12.90J 1.14 61.521 4.18' 13.72 1.22 11,450 12,175 1.46 91.21 1526 1527 -----------6.84 29.17 42.48 21.51 2.82 31.32 45.60 22.08 3.03 57.86 3.99 5.231 2.70 62.08[ 4.29 5.62 2.90 11,493 12,338 1.36 85.0 1527 1528 -----------5.31 31.24 38.69 24.76 4.76 33.00 40.86 26.14 5.03 57.13 3.80 2.34 1.69 60.34 4.12 2.58 1.79 11,171 11,797 1.42 88.7 1528 1529 -----------5.36 81.91 43.03 19.70 2.04 33.72 45.47 20.81 2.16 59.27, 3.96 8.35 1.49 62.43 4.19 8.83 1.58 11,450 12,099 1.10 68.71 1529 1530 -----------5.46 35.66 49.17 9.71 1.61 87.72 52.01 10.27 1.71 70.48 4.95 6.60 1.16 74.56 5.24 6.99 1,23 12,0031 13,755 1.36 85.0 1530 1631 -----------5.83 33.20 48.15 17.82 1.51 35.26 4!J.83 18.91 2.77 60.90 4.00 6.26 2.58 64.68 4.25 6.66 2.74 11,448; 12,157 1.27 79.4 1631 1532 -----------4.31 35.61 44.55 15.63 3.00 37.22 .f6.56 16.22 3.H 58.27 4.88 6.74 1.82 66.57 5.11 7.05 1.91 12,264! 12,817 1.40 87.5 1632 1533 -----------4.00 31.78 42.04 22.18 2 .89 33.11 43 .80 23.09 S.49 58.01 4.06 6.62 2.74 60.43 4.231 6.90 2.86 11,524: 12,005 1.44 90.0 1533 1534 -----------13.44 84.86 36.87 15.3~ 2.54 40.28 42.0'2 17.70 2.94 50.94 4.41 11.86 1.46 58.86 5.10113.71 1.69 9,609'1 11,101 1.60 100.0 1634 Average ____ 7.40 84.82 41.74 10.04 -2.19 37.65 45.06 17.29 2.38 60.01f 4.25 8.aaj 1.76 64.79 4.59 9.00 1.90 11,245 12,oafi 1.40 87.5Ave. Tea;as Coals and Lignites The Tertiary Coals here represented are Nos. 1518, 1519, 1520 and 1521, the two former from Webb county, Laredo district, and the two latter from Maverick county, Eagle Pass district. The Webb county coals are higher in volatile and combustible matter and sulphur, and lower in ash and moisture than the Maverick county coals, the fixed carbon being about the same. The Ter­tiary coals from these counties show a considerable difference in the composition of the ash, as will appear further along. The Carboniferous coals, Nos. 1522 to 1534, inclusive, show a marked range in composition. On the average they contain more moist­ure, fixed carbon, ash and sulphur, with less volatile and com­bustible matter than the Tertiary coals. From the composition of the ash of the Texas coals it may be concluded that while the coal was forming there were con­siderable variations in the character of the vegetation and in the character and amount of the sediments washed in. If we allow that the rate of accumulation of vegetable matter is 100 tons per acre per century and allow, also, for the differences in density and composition, it is likely that the rate of the formation of coal will not exceed one foot in 10,000 years. During such a period there would probably be many opportunities for climatic changes affecting the character of the vegetation, and for changes in the nature of the sediments mixed with the coal while >.t was form­ing. In these coals, as mined, the following variations in composi­ tion were observed: From To Average Moisture . . . . . . . . . . . . . . . . . . . . . . 3.46 1344 7.40 Volatile and Combustible Matter. 29.17 48.84 34.82 Fixed Carbon . . . . . . . . . . . . . . . . . . 36.37 49.17 41.74 Ash ........................... 9.07 24.76 16.04 Sulphur . . . . . . . . . . . . . . . . . . . . . . . 1.28 4.76 2.19 Carbon . . . . . . . . . . . . . . . . . . . . . . . . 50.94 70.48 60.01 Hydrogen . . . . . . . . . . . . . . . . . . . . . 3.37 5.65 4.25 Oxygen . . . . . . . . . . . . . . . . . . . . . . . 2.34 12.90 8.33 Nitrogen . . . . . . . . . . . . . . . . . . . . . . 0.78 3.62 1.76 British Thermal Units .......... .. 9,609 12,264 11,245 On dry basis these become : Volatile and Combustible Matter. 31.32 50.70 37.65 Fixed Carbon ................ . 37.93 52.01 45.06 A.sh ... . ...................... . 9.45 26.14 17.29 Bulletin of the University of Texas From To Average Sulphur . . . . . . . . . . . . . . . . . . . . . . . 1.28 5.03 2.38 Carbon . . . . . . . . . . . . . . . . . . . . . . . 58.86 74.56 64.79 Hydrogen . . . . . . . . . . . . . . . . . . . . . 3.73 5.94 4.59 Oxygen . . . . . . . . . . . . . . . . . . . . . . . 2.58 13.72 9.00 Nitrogen . . . . . . . . . . . . . . . . . . . . . . 0.87 '3.75 1.90 British Thermal Units. . . . . . . . . . 11,101 13,755 12,035 Without considering, for the present, the things that ultimately comprise coal and lignite, such as carbon, hydrogen, oxygen, nitrogen, etc., we may regard such fuel as made up, essentially, of five things, viz., moisture (ordinary water), volatile and com­bustible matter, fixed carbon, ash and sulphur. As to moisture, but little need be said. It is water which exists as such in the coal as it exists in a great many things in nature, in wood, in earth, in many rocks, etc. It is given off from coal at all ordinary temperatures, and is completely driven off at or a little above the boiling point of water, 212 degrees Fahren­heit. It is of no value in the coal, and, in fact, is an objec­tion, for it detracts from the heating power. An amount of coal equivalent to the amount of water present must be used to evaporate the water before any appreciable heat is derived from the burning of the coal. On the average, Texas coals, as mined, contain nearly 7% pounds of water in each one hundred pounds, or nearly 150 pounds in a ton of 2000 pounds (short ton) . If we allow that, on the average, it requires one pound of these coals to evaporate 10 pounds of water from and at 212 degrees Fah­renheit we would have to use 15 pounds of coal from every ton, or 450 pounds from each 30-ton car, to drive the moisture out. This amount of coal, 450 pounds per carload, is to be subtracted from the coal which is used for heating, as it is employed merely in driving the water out of the coal. We do not know what is the average amount of water in our coals as they are received and used. It is sometimes a question of the weather, whether the coal has been rained on or not while it was in transit, and whether the coal is stored under shelter or not, after being received. But the storing of coal brings up other questions which are not pertinent at this time. The loss of heating power in certain coals that are stored for some time enters in here, but this loss may be, in part, counter­ Tea:as Coals and Lignites balanced by the increased dryness of the coal. The danger of spontaneous combustion in stored coal has also to be con­sidered. In the purchase of coal on analysis it is customary to specify that the moisture shall not exceed such and such a percentage, the amount so allowed varying according to circumstances. In comparing one coal with another it is best to reduce the analyses to the same basis, and the most convenient one is the dry, or water-free, basis. For practical purposes it is necessary to consider the relative amounts of water which these coals would contain, as received, but on this subject we have very little data. It is seldom, or never, the case that coal as received contains the same amount of water as it did when it was mined. Unless it is exposed to wet weather, be­tween the shipping and the delivery points, coal will lose water and decrease in weight. But this decrease in weight does not necessarily imply a loss in efficiency, looking at the matter from the standpoint of loss of moisture only. If, at the same time, there should be a loss of volatile and combustible matter, which could be used as a source of heat, the questions raised are of a different sort. The next thing that coal contains is volatile and comhustible matter which can be used as a source of heat. Water is volatile matter, but it can not be used for heating. The volatile matter that coal contains is also combustible matter, so we use the term ''volatile and combustible.'' As has been already remarked, Texas coals, as mined, con­tain from 29.17 to 48.84 per cent. of volatile and combustible matter, the average being 34.82 per cent. In other words, our coals contain a little more than one-third of their weight of volatile and combustible matter. What is this substance 1 To answer this question in detail would take us into highly technical discussions, with which this publication has but little to do. The expression "volatile and combustible matter" is taken to include those substances, simple or complex, which are given off from coal at temperatures a little above that of boil­ing water to full red heat, with excl1ision of air. The air must be excluded or the solid matter of the coal will begin to burn. If we take a finely ground sample of coal and heat it at the Bulletin of the University of Texas temperature of boiling water, or a little above, it will lose weight, and this loss is water. If we take this same sample and heat it in a crucible with a closely-fitting cover up to full red heat (about 1000 degrees Fahrenheit) we get an additional loss of weight, .and this loss is volatile and combustible matter. There will be left in the crucible :fixed carbon and ash, which will be considered later. This volatile and combustible matter is not a simple substance, like water, but is composed of gases and smoke. The gases vary a good deal in composition, and so, also, does the smoke, although not to so great an extent. The amount and nature, and, consequently, the value of this volatile and combustible matter, depends on a number of things, among them being the nature of the coal itself, the size of the coal treated, the rapidity in the increase of temperature, the final temperature, the temperature of the space into which the products evolved are carried, the mass of the coal, the time factor, etc. Most of the gases thus obtained are combustible, but at times and under certain conditions we have, also, water and carbonic acid, which are not combustible at all. The term volatile and combustible matter does not, there­fore, always mean that all of the material can be burned, and thus afford heat. At times there are certain gases evolved which can not be burned again, e. g., water and carbonic acid. If the coal be thoroughly dried and water is afterwards found as a part of the volatile and combustible matter it has doubt­less been produced during the operation, and is not an essential part of the coal. Disregarding the water and the carbonic acid (although, at times, they are important factors), the constituents of the vola­tile and combustible matter that claim our attention especially are the gases that can be burned and which, thus, are a source of heat. These are carbon monoxide, marsh gas (which com­poses 95 per cent of the best Texas natural gas), ethane, a group of gases known as "illuminants," and hydrogen. Oxy­gen and nitrogen are also present, the latter in considerable amounts if there is much air present. It is perfectly true that "any statement as to the character of the gases or volatile products evolved from coal at specified temperatures has little value unless it is accompanied by a clear description of the conditions prevailing, and particularly of the Te'X 15.56 --­25.94 Oxide of Iron. --­23.03 14.74 3.38 9.84 13.56 22.94 13.26 15.40 13.56 28.02 20.64 4 .00 3.68 22.02 24.37 28.02 13.42 --­16.ll Lime. --­4.69 2.56 0.91 0.64 16.08 14.85 22.08 4.21 1.16 1.35 6.68 1.08 2.16 0.81 trace 1.56 20.73 --­5.00' Mae-Oxide of Su!Dhurlc nesla. Mangan-Acid. ese. --­--­--­none l.75 4.57 trace 3.52 0.36 0.80 0.80 0.70 -------­trace --­-----­-------­12.19 1.42 1.16 10.97 1.43 trace 12.87 trace trace 2.84 trace -------­trace 1.47 trace trace ------­6.64 1.50 1.67 trace ---------­0.84 1.34 0.96 -------­trace 2.25 2.32 1.91 trace 15.00 --­--­--­0.73 0.22 4.42 Per-cent. of Ash In Coal as Mined. --­9.07 ll.09 17.43 18.11 12.80 14.74 ll.32 15.42 16.18 21.51 24.76 19.70 9.71 17 .82 15.53 22.18 15.33 --­16.04 The Tertiary coals, from the Rio Grande Field, are Nos. 1518, 1519, 1520, 1521, the first two being from Webb county, La­redo district, and the last two from Maverick county, Eagle Pass district. The ash of these coals shows a considerable d1f­ference in composition. The Webb county co!:lls are low in silica and high in oxide of iron, with a medium content of alumina, lime and sulphuric acid. The Maverick county coals are high in silica and low in oxide of iron and sulphuric acid. As these coals are supposed to be of the same geological age and to have been formed under relatively the same conditions, we may infer that the vegetation from which they were made was of a different character, and that the in-wash of sediments varied a good deal. The coals of the Carboniferous formation also show consid­erable differences with respect to the composition of the ash, and this likewise would lead one to suppose that the character of the vegetation varied a good deal during the coal-forming 2-T. C. Bulletin of the University of Texas period. In these coals the silica varies from 29.14 to 54.34 per cent. ; the alumina from 13.10 to 32.40 per cent.; the oxide of iron from 3.68 to 28.02 per cent.; the lime from a trace to 22.08 per cent.; the magnesia from a trace to 2.25 per cent., and the sulphuric acid (combined not free) from a trace to 15.00 per cent. It is impossible to observe these analyses without reaching the conclusion that the character of the coal-forming vegeta­tion changed a good deal during Carboniferous times, from plants which secreted a comparatively small amount of silica to those secreting a large amount. This observation also holds true with respect to the oxide of iron, alumina, lime and sul­phuric acid, for the composition of the ash of coal is closely related to that of the plants from which the coal was made. Of course, the washing in of sediments which became mechan­ically mixed with the decaying vegetation has also to be consid­ered, but, aside from this, the ash of coal is largely the ash of the plants forming the coal. There are many interesting things found in the ash of coal, besides those already given, and in two Texas coals, both from Thurber, Erath county, copper was found in very small amounts. In a speculative way the occurrence of copper in the ash of these coals may be connected with the occurrence of copper in the Permian beds which lie to the west of the Carboniferous formation in Texas, and which are geologically above this formation. For domestic purposes, where no great heat is required, more consideration is given to the quantity of ash in coal than to its fusibility. For boiler use, however, the fusibility (clinkering) of coal is a factor of great importance. Coal that clinkers badly, i. e., coal that has an easily fusible ash, is almost sure to give more or less trouble. It clings to the grate-bars, interferes with the draft and causes, at times, serious losses. Such clinkering troubles generally attend the use of coal whose ash is high in oxide of iron. On the contrary, coals whose ash is composed chiefly of silica and alumina, or silica, alumina and lime, do not clinker so readily. As a rule, red ash coals clinker much more easily than white or gray ash coals. The design and construction of the grate and fire-box and the method of firing have also a good deal to do with clinker­ing. T6xas Coals and Lignites We have thus far considered as briefly as possible four of the five things that comprise coal, moisture, volatile and com­bustible matter, fixed carbon and ash. In addition to these, and forming a part of the volatile and combustible matter is sulphur. This may exist in coal as a sulphide (chiefly sulphide of iron, or pyrite), as a sulphate (chiefly as sulphate of lime, gyp­sum) and in certain obscure organic compounds whose nature is not clearly understood. On burning coa.l a part of the sulphur is removed and a part remains, the proportions varying according to the nature of the coal, the method of combustion, etc. As a rule, the sul­phur in organic combination is removed, going off in the vola­tile and combustible matter, the sulphur in the pyrite present is partly removed, while the sulphur in the sulphates is hardly affected. In Texas coals, as mined, the sulphur varies from 1.28 to 4.76 per cent., the average being 2.19 per cent. No in­vestigations were made to determine the character of the sul­phur-bearing compounds in Texas coals. Some of them, e. g., the coal from the old Young Mine, at Keeler, Palo Pinto county, from one of the seams at Thurber, Erath county, and from Rock Creek, Parker county, carry sulphur varying from 4.76 to 2.82, considerably above the average of the State at large. Sulphur in coal, even up to 5 per cent., is not as injurious to boilers as is commonly supposed. The five things in coal that ha.ve now been considered com­prise what is known as the proximate composition and the analy­sis that determines them is called a ''proximate analysis.'' When we go further and determine the elemental composition of coal, the analysis is called an "ultimate analysis." In this, as in the proximate analysis, we determine the moisture, ash and sulphur, but instead of the volatile and combustible matter and fixed car­bon there is determined the amount of carbon, hydrogen, oxygen and nitrogen, as separate items. This has also been done for Texas coals, as mined, and the re­sults are given in the Table on p. 10. The carbon varies from 50.94 to 70.48 per cent., the average being 60.01 per cent. The average percentage of fixed carbon in these coals, as by proxi­mate analysis, is 41.74, but the percentage of carbon is 60.01, Bulletin of the University of Texas which means that there is a loss of carbon in the volatile and combustible matter. The ultimate analysis recovers this. The hydrogen varies from 3.37 to 5.65 per cent., the average being 4.25 per cent. The oxygen varies from 2.34 to 12.90 per cent., the average being 8.32 per cent. The nitrogen varies from 0.78 to 3.62 per cent., the average being 1.76 per cent. A number of years ago the term "disposable hydrogen" was introduced in coal analyses, and it meant the hydrogen that remained after calculating all of the oxygen present as water, and deducting from the total hydrogen the hydrogen in this amount of water The amount of this disposable hydrogen was supposed to '.have an important bearing on the value of the coal for gas-making. Be this as it may, we have calculated the percentages of dispos­able hydrogen in Texas coals on a dry basis. The results are as follows: Analysis No. 1 --------------------------------­63 ----------------------------------­! ----------------------------------­'---------------------------------­4 ----------------------------------­6 -----------------------------------­6 ---------------------------------­11 ------------------------------------­S2 ---------------------------------­33 ------------------------------------­42 -----------------------------------· --­ ~~~~~~~~~~~~~~! 9 -------------------------------------­10 ------------------------------------­S7 ------------------------------------­11 -----------------------------------­ Disposable Hydrogen.Total Hydrogen. Per Cent. Per Cent. of Total. 68.79 4.17 2.66 70.72 6.09 3.60 74.82 1-~~~-1-~~~~ Average -----------------------------4.66 3.24 4.40 3.27 5.65 4.42 4.83 3.23 6.08 3.39 4.14 2.97 4.92 8.64 4.68 3.41 4.40 8.48 4.04 2.33 l:~ ll 5.16 4.15 6.85 4.08 3.77 2.56 4.67 8.27 78.23 66.87 66.78 71.74 74.00 73.65 77.95 f)T.67 61.39 66.50 55.69 51l.OO 73.95 76.49 80.58 75.33 67.90 70.02 69.58 For the key to these numbers see page 27. For a similar table for lignite see page 51. In these coals the disposable hydrogen varies from 2.29 (Olmos mine-run), to 4.42 per cent. (Cannel Coal Company), the Texas Coals and Lignites average being 3.24 per cent. Expressed as percentage o.f the total hydrogen, the range is from 55.69 (Olmos washed nut) to 80.58 per cent. (Strawn Coal Mining Company). There is a remarkable difference between the coals and the lignites not only with respect to the amount of the disposable hydrogen, but also with respect to its percentage of the total hydrogen. The much larger amount of oxygen which the lignites con­tain, in comparison with the coals, leaves a proportionately smaller amount of hydrogen for the hydrocarbons and free hy­drogen. Whether or no the amount of disposable hydrogen in coal may be taken as an index of its value for gas-making is a ques­tion yet to be decided with respect to our coals, under standard conditions. It is a part of the investigation planned and already begun. T'he part that oxygen plays in coal has been the subject of much investigation. It is a highly technical matter, and need not con­cern us now. It may suffice to say that it affects the gas-making qualities of coal by influencing the amount of hydrogen avail­able for the formation of the hydrocarbons an<1 of free hydro­gen. The larger the amount of oxygen present, if we al­low that all of it has to combine with hydrogen as water, the less 'hydrogen will there be for the formation of useful compounds in the gas. It may be possible that the water thus formed is resolved into its constituent gases at higher temperatures, and in the presence of free carbon. We need not, however, go into such matters now. The Table giving the disposable hydrogen in the coals should be compared with a similar Table for lignites on page 51. The nitrogen in coal is an important constituent from the standpoint of the recovery of by-products. From it can be made ammonium sulphate, which is the starting point in the manu­ facture of many other ammonia compounds, anhydrous ammo­ nia, etc. The percentage of nitrogen in Texas coals, as mined, varies from 0.78, as in a Maverick county coal, to 3.62, as in a Webb county coal. The Tertiary coals show the highest and the low­est percentages of nitrogen. In the Carboniferous coals the range is from 1.07, as in a Wise county coal, to 2.74, as in a Palo Pinto Bulletin of the University of Texas county coal. The proportion of the total nitrogen in coal that is recoverable as ammonia varies within wide limits, and it is practically impossible to give a general average. The yield of sulphate of ammonia per ton of coal has varied from 7 pounds, as in the Jameson producer, to 70.6 pounds, as in the Mond pro­ducer, using coal with 1.50 per cent. of nitrogen. The nature of the coal and the method of treatment determine the yield of sulphate of ammonia, and there is such a diversity here that no general rule can be given. But under ordinary conditions of gas-making a yield of from 20 to 25 pounds of sulphate of am­monia per ton of coal is within the limits of current practice. Some authorities1 have stated that 14.50 per cent. of the total nitrogen may be given off as ammonia, 1.56 per cent. as cyan­ogen, 35.26 per cent. remaining as elementary nitrogen, and 48.68 per cent. being held in the coke. It will doubtless be some years before there is much interest in the recovery of by-products from Texas coals. The coal treated in retorts for making gas does not cut much figure in the trade, inasmuch as oil and water gas and natural gas are the chief gaseous fuels at present. The recovery of by-products from producer-gas is not now commercially attractive, chiefly on account of the lack of a central plant to which the concen­trated ammoniacal liquors could be sent for treatment. The total quantity of such liquors produced in the State is not known, but the distances separating the different establishments are such as to forbid the assembling of the liquor. In 1908 the total value of all of the products from gas works and recovery ovens, using coal, in the United States was $64,­660,040, which value was $8,912,964 less than for the year 1907. In 1907 the last returns available, the amount of coal carbon­ized in Texas in 7 establishments, was 28,282 tons, and the quantity of gas produced was 251,233,400 cubic feet. Of this quantity, 53,281,311 cubic feet were sold for illuminating pur­poses, the price per 1000 cubic feet being $1.66. There were 5old for fuel purposes 167,885,909 cubic feet at $1.33 per thou­rmnd. The total quantity of coal gas sold was 221,167,220 cubic feet, at an average price of $1.41 per thousand. The quantity of gas unaccounted for was 30,066,180 cubic feet. 'J. D. Pennock, Trans. Amer. Inst. Min. Engrs.,Vol. XXI, p. 808. Te;a;as Goals and Lignites In the same year, 1907, the quantity of oil and water gas produced in Texas, in 10 establishments, was 591,644,500 cubic feet. Of this quantity 191,529,8'03 cubic feet were, sold for illuminating purposes, at $1.35 per thousand, and 335,849,977 cubic fe'et were sold for fuel purposes, at $1.27 per thousand. The total quantity of oil and water gas sold was 527,379,780 · eubic feet, at $1.30 per thousand. The quantity of gas un­accounted for was 64,264,720 cubic feet. The total uuantitv (lf gas made in 'l'exas in 1907 was thus 842,877,900 cubic feet, of which 251,233,400 cubic feet, or 29.81 per cent., w.ere coal gas and 591,644,500 cubic feet, or 70.19 per cent., were oil and water gas. The total quantity of gas sold for illuminating purposes was 243,811,114 cubic feet, of which 52,281,311 cubic feet, or 21.03 per cent., were made from coal, and 191,529,803 cubic feet or 78.97 per cent., were oil and water gas. The total quantity cf gas sold for fuel purposes was 503,735,886 cubic feet, of which 167,885,909 cubic feet, or 33.33 per cent., were made from coal, and 335,849,977 cubic feet or 66.67 per cent., were oil and water gas. Of the total gas for illuminating purposes coal gas comprised 21.03 per cent., while it comprised 33.33 per cent. of the gas sold for fuel purposes. These statistics are from returns made to the United States Geological Survey, and are entirely exclusive of natural gas. In 1907 seven establishments in Texas produced 225,394 gal­ lons of coal-tar, valued at $12,707, or 5.6 cents a gallon. The yield of tar per ton of coal was 7.97 gallons. The production of gas-coke, in 1907, was 12,049 tons. No am­ monia compounds were produced. The yield of coal-gas per ton of coal carbonized was 12,411 cubic feet. There are no statistics available on the heating or illuminating power of this coal-gas, nor on the character or source of the coal carbonized. We do not know how much of the coal made into gas was Texas coal, nor what the prospects are, if any, for the use of these coals in this direction. But if all of the coal thus used had come from Texas it would have formed a very small proportion of the total coal produc­ tion, and in total value at the mines would not have exceeded $75,000. The strong tendency, in gas-making, is towards oil and water Bulletin of the University of Texas gas, not towards coal-gas. With respect to gas-making, the best outlook for both coal and lignite is in the direction of producer­gas to be used direct as fuel, or in gas-engines for power. The investigations which have been begun by this Bureau along these lines are particularly pertinent at this time. HEAT VALUE OF TEXAS COALS. The heat value of fuels is expressed in British Thermal Units. (B. T. U.) This term signifies the amount of heat required to raise the temperature of one pound of water from 50 degree.5 85 .58 38.48 36.55 28.82 38.10 84.53 37.11 49.05 38.12 38.46 40 .82 34.28 d 2 ~ 0 "'~ ~ 87.99 40.18 42.53 37 .10 46.30 53.00 37.37 42.00 38.35 36.93 32.35 37.20 37.28 40.94 41.69 37.04 49.21 48 .13 48 .73 35.02 33 .961 43.02 36.89 41.07 .ci --· < 16.79 15.26 13.42 7.82 10.55 . 2.81 24.62 16.56 20.77 23.89 26.95 30.34 24.72 19.23 15.90 11.11 9.17 10.51 7.75 20.46 18.82 16.80 0 z .!I ., ~ , ' o • I j !' 0 't'j:o l § l . 't:l:0 . § I : • ·~ ~ 0 I I J-4 z . 1~ ~ • -e ; ·a~ . -e ! ci ! . : i ci ~ rtl ~ ~~ ~ rf.J Q,) ;::j J..t o:s ' • I ::J""' o:s • • Q,) I . ~ l . I Q,) • .,c:i _::,;: ·,,rn .£..,• ..... """ ' 4>,C Q,) 0 I ,_, ~.o 1V 0 ""' Cl \ bl) Cl Q,) ' :::f I ba Cl C) ~ +:>CJ~ -­ ~ =s ss~ 't:I I ::s ise~ 't:I , I t::s o t o i Q,) bl) i o i o Q,) ti.I) ~-g ~ s~ .;.:CC) p., ~ I -38~ .~ ~ ~ ~8~ .~ i ~ I ~ ~ i ~ t g ~ ~ I ~ ~ !i ~8 >. ~I ·;;;8 I ~ 1· !I' __<_____ ~~~~.::__-~1_::__:::__~,_::__,__ ~_.'.:_, __~z z A oo ~ ..: 1535 35.30 36.33 28.851 7.52 0.00 56.15 32.241 ll.Gl111.45 11.36 3.07! 10.76 1.04 63.93' 4.7511 11).6-J -1.62 7,003 12,215 1.28! 80.0 -:15a5 1536 3~.29. 40.31 18.50 6.00 1.20 61.36 2~.l'.' 10.47, 1.84 4:.01. 3. 25; 13.82 0.73 61.0~: 4.8~ 20.5: 1.()) 7,~ 11,470 1.421 88.7 15?6 1537 3~.40, 36.88 21.22 6.60 0.!H 66.94 32.86; 10.201 l .47 42.24· 3.1~1 1().07 1.00 65.40, 4.8., 16.52 1.56 7,~ 12,166 1.SO 81.2 1537 1588 32.79 37.09 22.91 7.21 1.18 55.2() 34.10. 10.70! 1.76 41.()l 3.2.>; 13.82 0.73 61.03 1· 4.85. 20.57 1.09 7,763 11,551 1.32 8'2.5 1538 1 Wl9 3'1.72\ 34.26 22.73 8.29 1.04' 54.02 34.82 11.161.60 41.031 3.1'.!1 ll.O'.l 0.85 M.24. 4.'191 16.00 1.31 7,697 11,792 1.20 75.0 153g 1 154() 32.271 44.30 15.26 8.17 2.3Ji 65.41 22.54'. 12.05, 3.42 38.56 2.85' H.85 0.00 06.% ·1.2'2 21.94 1.43 7,383 10,00l 1.37 85.6 1540 1 1541 33.63i 46.78. 7.45 12.14 o.99, 10.;19 11.24'. 18.271 i.so 3R.7BI 2.70: rn.s9 o.sr, 58.441 4.07: ~.42 l .3o 7,350 11,oss J .37 85.6 1541 1542 31.521 44.49117.48 6.51 0.93 64..JBl 25.57, 9. 45 1.36 41.15 3.J6. H.68 0.8560.101 4.!n --.91 1.27 8,046 11,750 1.39 86.9 1542 1 1 1543 29.07, 28.96 24.47 17.60 3.29i 40.84 34.49, 24.671 4.~5 38.6512.72 i 7.32 1.40, 54.~, 3.86, 10.33 1.98 7,489 10,489 l.44 90.0 1543 1544 29.86j 51.00 10.00 9.1~ 0.91; ~2.7~ H.26, 13.0'2 1.80 43.17 3.29112.781 0.83 61.51~ 4 .70, 18.23 1.19 7,929 11,305 1.39 . 86.8 154~ 1 1545 36.16; 33.lOi 19.00 10.7" 0.4C> ol.00 31.26. 16.70· 0.64 34.93 3.17113.69! 0.8954.7., 1.98; 21.46 1.40 7,518 10,994 1.35 84.4 1540 1 1 1 1546 31.96i 39,53, 23.05 5.~6 1.46, 58.10, 33.89 8.05 2.1~ 43.851 3.321 13.051 0.85164.45 4.~9; 19.19 1.26 8,053 11,837 1. 46 91.2 1546 1547 35.00 45.Zl l. ,11 .60 7..ID 0.471. 70. 21 B.~21 11.77 0.7., 40.00 • 2.911 12.01 1.41 62.12 4.o2; 18.66 2.20 7,567 11,751 1.16 72.5 1547 1 1548 34.23' 41.74, 19.85 4.87 0.56 63.47 70.19' 6.34 0.86 42.27 2.87114.831 1.05164.271 4.37/ 22.55 1.61 7,691 11,694 1.33 83 .l 1548 1 1 _ 1519 3:L87: 45.88; 3.41 16.84 O.OS! 09.39 5.16! 25.45 1.04 ~'. 2.30i ll .15i__:_:~I 51.50 3.49: 16.87 _!~ 6,474 9,790!~.1873.7 ~:'_4~ 1 Avcraga 33.37· 40.39 17.241 ll.00 J .12 60.611 25.88. B.st1 1.68 40.Ia' 3.031 12.291 1.181 60.23 4.55 18.45_J.47 7,614 11,427 1.33 83.1 Average Texas Coals and I/ignites The variations in these analyses are as follows: Material as mined- From. To. Average. Moisture .......... .. ........ . . . 29.07 36.16 33.37 Volatile and Combustible Matter .. 28.96 51.00 40.39 Fixed Carbon ................ . 3.41 24.47 17.24 Ash ......................... . 4.87 17.60 9.00 Sulphur ............... ....... . 0.40 3.29 1.12 Carbon ................ . ..... . 34.93 43.85 40.13 Hydrogen .... . ...... .. ...... . . 2.30 3.37 3.03 Oxygen ...... . .... . .......... . 10.67 14.85 12.29 Nitrogen ...................... . 0.85 141 1.18 Heating Power, B. T. U ........ . 6,474 8,053 7,614 On dry basis these become : Volatile and Combustible Matter .. 40.84 72.72 60.61 Fixed Carbon ................. . 5.16 34.82 25.88 Ash . . ....................... . 6.34 25.45 13.51 Sulphur ...................... . 0.64 4.65 1.68 Carbon ................ .. .... . 51.50 65.40 (i0.23 Hydrogen ..... . ... . ........... . 3.49 5.13 4.55 Oxygen ...................... . 10.33 2291 18.45 Nitrogen ... . .............. .. . . 1.09 2.20 1.47 Heating Power, B. T. U .. . .. .... . 9;790 12,215 11,427 Specific Gravity ... . .......... . 1.16 1.44 1.33 Weight per cubic foot. Lbs ..... . 72.5 90.0 83.1 OO'MPOSITTON OF THE ASH OF TEXAS LIGNITES. .AnslysisNo. 1535 1536 1537 1538 1539 1540 1541 1542 1543 15H 1545 1546 1547 1548 1549 Average Silica. 63.{0 40.46 30.H 21.64 33.06 27.44 23.20 42.20 47.04 40.60 59.00 25.64 38.73 33.00 53.04 38.57 Alumina. 12.27 16.92 13.48 16.20 16.77 28.87 11.94 23.02 28 .18 34.26 20.11 19.08 23.00 25.84 24.68 20.64 Oxide of Iron. 5.95 8.32 11.70 11.10 8.47 Z4.S5 5.08 Z.02 18.32 2.02 3.69 12.92 6.00 7.40 7.70 9.04 Lime. none 15.60 23.59 25.23 23 .08 7.00 38.17 ]5.93 6.64 12.ffi 10.58 18.68 24.11 22.32 10.59 16.84 Mag·nesla. trace 1.22 0.88 I !.36 I 1.38 trace 1.00 2.12 trace trace 0.48 1.76 trace trace 0.94 i Oxide of Mangan- Sulphuricl Analysi• Acid. , N<:>. ese. ___I___• 13.71 I 1535 1.00 15.54 I 1535 --------·­ 3.32 14.22 15.37 2.00 18.01 1538 trace 17.10 15.~9 0.52 10.45 1540 1.60 7.79 I 1541 trace 12.81 trace 4.58 9.52 0.48 5.47 20.92 trace 8.51 ----------11.32 trace 3.53 0.81 lZ.90 1542 1543 154! 1545 1546 1547 1548 1549 Average Bulletin of the University of Texas In these lignites the following variations in the composition of the ash are to be noted. From. To. Average. Per cent. of ash.... . . . ....... . . 4.87 17.60 9.00 Silica ... . .. . ..... . ... ........ . 21.64 63.40 38.57 Alumina ................. . ... . 11.94 34.26 20.64 Oxide of Iron . . . ..... . ... .. .. . . 2.02 24.85 9.04 Lime ........ . ............... . 0.00 38.17 16.84 Sulphuric Acid ... .. . .... . .... . 3.53 20.92 12.90 With the lignites, as with the coals, there is a considerable va­riation in the composition of the ash, leading to the conclusion that the conditions, with respect to vegetation and the in-wash of sediments, varied within wide limits. On comparing the composition of the ash o.f these lignites with that of the coals given on page 17 it is seen that the lignite ash carried considerably less silica, alumina, and oxide of iron than the coal ash, but considerably more lime and combined sulphuric acid. What deductions may be made from these facts does not now appear except that it is probable that the vegetation forming the coal was different from that forming the lignite. and also that the in-wash of extraneous materials was different during the process of the formation of these beds. Whether the coal and lignite beds have been formed ''in situ'' or by ''drift,'' or by a combination of these two methods is an open question. It is likely that conditions varied a gooJ deal not only in the coal period as a whole, but also locally, and, to some extent, while the same seam was being made. It may be of interest to give a list of the principal fossil fauna and flora that have been found in different coal beds. and the list that follows is taken from James Tonge 's Coal, 1907. FAUNA. Amphibia. All belonging to the Labyrinthodont order. Fish. Many different kinds, both large and small, shark, etc. Many geologists hold to the opinion that what is known as '' Oannel'' coal is of marine origin, on account of the prevalence of the remains of fish, shells, etc. TeJa;as Coals and Lignites Insects. Not very abundant. One specimen of Orthoptera has been found with a spread of wing of nearly two feet. Myriopoda ("Thousand Legs"). Quite common. Arachnida (Spiders). Both spiders and scorpions have been found. Xiphosura (Crabs). Fairy well distributed. Schizopoda (Shrimps). Ostracoda (Oyster-like forms). Abundant but £ometimes very small. Brachiopoda. Mollusca, both uni-and bi-valve. Brachiopoda. Well represented in carboniferous limestone, but not plentiful in the coal measures themselves. Vermes (Worms). Fairly plentiful, as borings, tracks, etc. FLORA. A great deal of work has been done in the study of the fossil flora of the coal measures and the coal beds themselves. Of late years the chief interest has centered around the study of fossil flora from the standpoint of stratigraphical succession. The re­sults of such researches are to be compared with the work nf the stratigraphical and structural geologist who looks at the prob­lem from the standpoint of the sequence of rocks. The flora of the coal measures is represented by Lycopods, moss-like plants, some of them growing to a height of 50 feet and more. Calamites. Reed-like plants, akin to our "horse-tails." Very common in coal measures. Coniferae. Cone-bearing trees and shrubs, pine, cedar, etc. They appear for the first time in the coal measures. Cordiates. Some of the Lycopods were more than fifty feet in height ana represented the maximum devlopment of the club moss. It is a notable fact that in many of the so-called "flaming" coals there are large quantities of the spores of this gigantic club moss. The bark of this club moss is, perhaps, the most common fosil plant in the coal measures, and is to be observed in a great many places. In paleobotany there is still some confusion in nomenclature, Bitlletin of the University of Texas for it is one of the younger sciences, dating back not more than 35 or 40 years. During tbe period of its existence, 1888-1892, the Texas Geo­logical Survey did much valuable work on the fossil remains found in the coal measures of this State, but since that time nothing has been done by the State itself, and but little by out­side investigators. There is an impression-quite erroneous-that such studies are too ''scientific,'' that they do not touch upon matters of practical importance. On this point we will quote Mr. James Tonge, W estbougbton, England, a notable authority on coal, and tbe inventor of the Hydraulic Mining Cartridge, which has done more for the protection of human life and property in coal mines than almost any appliance that could be men­tioned. In bis book on "Coal,'' 1907, page 83, he says: "It is from the Palaeo-botar:ist that the mining student seeks information as to the mode of formation of the seams, in­formation which can only be derived from a close and intimate knowledge of the botany of carboniferous plant remains." The truth is that so-called ''scientific'' work and practical work must go hand-in-hand. There is no hard and fast line of separation between them. What is pure science today is tbe basis of great enterprises tomorrow, and the scientist in the laboratory is fore-runner to the manager of the factory. The analyses that have so far been given and discussed rep­resent samples of lignites that were secured .from the mines by an agent of the University Mineral Survey in 1901-1902. In order to bring the matter down to date and present new and detailed analyses, the operating companies were asked to send in typical samples of the material they were mining and shipping. These samples were, for the most part. received in tin cans, with close-fitting covers. In those cases in which the moisture runs much below the normal the samples did n'ot come in such cans, and, therefore, show a less amount of moist­ure than is usually found in our lignites. As the analyses are given on the samples "as received,'' an,l on the dry, or waterfree basis, also they may readily be com­ pared with each other. The analyses of these ''Company samples'' are as follows: Al'fALYl'IES OF TEXAS LIGNITES-OOMP~NY SAMPLES. BY S. H. WORRELL, 1910-1011. 40 59 12 57 13 14 16 41 17 56 18 36 20 21 22 23 55 44 £8 25 26 39 29 Av'rage A! Received. Dry Basis. Heating Power. Proximate Analysis. I Ultimate Analysis. Proximate Analysis. Ultimate Analysis British 1~~~~~~~~~1-~~~~~~~~-l-~~~~~~~~IThermal Units. 'g~ g I I Zl~ g I I .sgi,; ~ ~ . .sgi,; o~ ~,o ct> b ~ d 0 ~ ! ~.g~ .-. ~ g~ 'd .i::l ,g ~ tlJ) O ..... ~ ·v :§0:2! ~ ~ '3 :i 'g ~ z!l ~8~ ~ ....-,.., [f; 29.28 34.()2 29.041 6.66 .57 39.61 3.08 19.71 1.09 48.10 41.05 10.85 .80 56.00 4.35 26.48 1.54 7,283 10,220 40 15.001 43.61 32.71 8.68i .94 49.47 8.58 20.951 1.38 51.30 38.48 10.22 1.10 58.20 4.21 24.65 1.62 8,78'J 10,340 59 29.94 39.03 21.09 109.. 94341 .55 37.70 2.93 17.481 1.46 55.70 30.09 14.31 .78 53.80 4.18 24.95 2.06 6,291 8,979 12 7.30 45.62 36.65 .51 58.78 4.43 16.371 2.18 49.21 39.53 11.26 .45 63.4() 4.78 17.76 2.35 10,411 11,230 67 29.96 41.68 22.24 6.12 .70 44.0l 2.88 14.76, 1.67 59.50 81.75 8.75 1.00 62.77 4.11 21.14 2.23 6,903 9,855 13 22.40' 42.68 24.77 10.15 .55 45.34 3.85 16.00' 1.71 55.00 31.91 13.09 1.33 58.42 4.96 20.00 2.20 8,156 10,510 14 24.36 33.891 25.64 16.11 .74 42.13 3 .60 11.761 1.30 44.80 33.89 21.31 .97 55.69 4.75 15.57 1.71 7,068 9,344 16 36.64 28.33: 21.02 8.01 .41 36.16 2.79 15.021 .rn 44.70 42.63 12.67 .64 57.oo 4.40 23.70 1.53 6,717 l0,600 41 29.. 20 36. 92!21 .• 00; 6_.86 .58, 43.29 3.37 15.491 un 52.14 ss.22 9.64 .81 61.H 4.75 21.95 1.71 7,442 10,510 17 10 80 41 20 38 92 9 06 .61 i 48.80 2.81 25.991 1.91 46.18 43.63 10.20 .68 54.70 3.15 29.13 2.14 9,670 10,840 56 31.24 40.29 21.07 7.40 .73139.73 3.23 16.301 1.37 58.60 30.64 10.76 1.05 57.77 4.70 23.74 1.98 6.727 9,782 18 I 27.20 40.90 27.09, 4.81 .48 44.72 3.73 17.921 1.14 56.18 37.20 6.62 .65 61.42 5.12 24.63 1.56 7,682 10,540 36 25.58 39.37 25.301 9.75 .60 42.57 3.99 16.12 1.39 52.90 33.99 13.11 .80 57.20 6.36 21.67 1.86 7,532 10,120 20 37.26 31.85 24.81 6.08 .57 38.10 3.16 13.74 1.09 50.76 39.54 9.70 .90 60.72 5.00 21.92 1.73 6,416 10,226 21 I 27.50 35.201 27.30 10.00 .731 43.20 3.lZ 14.48 .73 48.54 37.65 18 .81 1.00 59.58 4.29 19.99 1.33 7,040 9,709 22 31.121 33.95122.66 12.27 .93, 39.04 3.24 12.481 .93 49.28 32.90 17.82 1.34 56.67 4.70 18.14 1.83 6,688 9,709 23 12.601 44.75 33.90, 8.75 .631 56.34 3.99 16.64 1.05 51.20 38.78 10.02 .72 64.20 4.56 19.30 1.20 9,774 11,182 65 12.621' 37.91 36.21 18.26 .48: 50.18 3.53 17.901' 2.05 43.38 41.43 15.19 .54 67.42 4.03 20.48 2.34 9,525 10,900 44 80.20 33.231 28.8! 7.73 .69 42.72 2.84 14.36 1.46 47.60 41.31 11.09 .98 61.20 4.06 20.58 2.09 6,920 10,030 28 30.34[ 31.141 30.66i 4.86 .61 42.10 3.33 17.56 1.20 49.00 44.00 7.00 ,frl 60.47 4.78 25.20 1.70·1 6,797 9,957 25 25.64135.55 30.281 8.581 .96 43.00 3.45 17.17 1.25 47.80 4-0.71 11.49 1.29 57.~ 4.63 23.09 1.68 7,459 10,000 26 20.64 36.24i 32.61, 10.48 .70 46.70 3.54 15.951 1.99 46.66 41.12 13.22 .80 liS.81 4.46 20.21 2.50 8,262 10,410 39 ~.12. 34.801_:6.61 6.97 .82 40.16 2.60 15.57 1.76 50.52 89.20 10.28 1.20 00.16 8.82 22.96 6,690 9,856 29 2.58, 25.17f 37.59 1 28.451--s::i9---:&i '44.08 --s.35-16.49 W 6Q.48 iill.7i---:OO 56.85--;:4822.201.867:6fil10,212 Average Bulletin of the University of Texas The key to these ''Company samples'' is as follows: Analysis No. 40. Alba Lignite Co., Alba, Wood county. 59. Alba-Malakoff Lignite Co., Alba, Wood county. 12. American Lignite Briquette Co., Rockdale, Milam county. 57. American Lignite Briquette Co., Rockdale, Milam county. 13. Bear Grass Coal Co., Jewett, Leon county. 14. Bertetti Coal Co., Lytle, Medina county. 16. Carr Wood & Coal Co., Lytle, Medina county. 41. Como Lignite Co., Como, Hopkins county. 17. Consumers' Lignite Co., Alba and Hoyt, Wood county. 56. Consumers' Lignite Co., Alba and Hoyt, Wood county. 18. Cookville Coal & Lumber Co., Mt. Pleasant, Titus county. 36. Edgewood Coal & Fuel Co., Wills Point, Van Zandt county. 20. Houston County Coal & Manufacturing Co., Crockett, Houston county. 21. Independence Mining Co., Phelan, Bastrop county. 22. Lone Sta.r Lignite Mining Co., Como, Hopkins county. 23. Melcher Coal & Clay Co., 0 'Quinn, Fayette county. 55. Rockdale Coal Co., Hicks, Lee county. 44. Rockdale Consolidated Coal Co., R.ockdale, Milam county. 28. Rockdale Lignite Co., Rockdale, Milam county. 25. Rowlett & Wells, Rockdale, Milam county. 26. Southwestern Fuel & Manufacturing Co., Calvert, Robert­son county. 39. Texas Coal Co., Rockdale, Milam county. 29. Vogel &Lorenz, Rockdale, Milam county. Note.-The Alba-Malakoff Lignite Company is successor to the Alba Lignite Company. The Vogel Coal & Manufacturing Com­pany is successor to Vogel & Lorenz. Analysis No. 44, Rockdale Consolidated Coal Company, repre­sents lignite sampled at the works of the Austin White Lime Company. McNeil, Travis county, January 13, 1911. The lignite-producing counties are: Bastrop, Fayette, Hop­kins, Houston, Leon, Medina, Milam, Rains, Robertson, Van Zandt and Wood. Texas Coals and Lignites The supplies of lignite in Texas are practically inexhaustible for the next thousand years even should we use ten times as much as we are now using. A sample of lignite was received from the Como Coal Com­pany, Como, Hopkins county, too late for the incorporation of the analysis in the body of this Bulletin and in the Tables. It had the following compositon: PROXIMATE ANALYSIS. DRY BASIS. Percent. Volatile Matter ..................................... 39.50 Fixed Carbon ...................... . ...... . .... .. .. 49.38 Ash ................................................ 11.12 100.00 Sulphur . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 1.01 Heating Power, B. T. U ...............................11,680 ULTIMATE ANALYSIS· DRY BASIS. Per cent. Carbon . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 62.59 Hydrogen ................ , . . . . . . . . . . . . . . . . . . . . . . . . . 4.84 Oxygen . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 18.12 Nitrogen . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 2.32 Sulphur . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 1.01 Ash . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 11.12 100.00 As received, the sample contained 34.0 per cent. of moisture. The variations in these analyses are as follows:: SAMPLES AS RECEIVED. From. To. Average. Moisture . . . . . . . . . . . . . . . . . . . . . . 7.30 37.26 25.17 Volatile and Combustible matter. 20. 33 45.62 37.59 Fixed Carbon . . . . . . . . . . . . . . . . . 21.09 38.92 28.45 Ash . . . . . . . . . . . . . . . . . . . . . . . . . . 4.81 16.11 8.79 Sulphur . . . . . . . . . . . . . . . . . . . . . . . 0.41 0.96 0.65 Carbon . . . . . . . .. . . . . . . . . . . . . . . . 36.16 58.78 44.08 Bulletin of the University of Texas Hydrogen . . . . . . . . . . . . ... . . . . . . Oxygen . . . . . . . . . . . . . . . . . . . . . . . Nitrogen . . . . . . . . . . . . . . . . . . . . . . . Heating Power, B. T. U. . . . . . . . . . On a dry basis these become: Volatile and Combustible matter .. Fixed Carbon ....... . . . . .. ... . . Ash .... ... ....... . .. . ....... . Sulphur .. .... .............. .. . Carbon . ....... . ....... . .. . .. . Hydrogen .... . ..... .. ... .. .... . Oxygen . ... . . ........ . ... . ... . Nitrogen ............. . .. . .... . Heating Power, B. T. U .. ... .. .. . From. 2.60 11.76 0.73 6,291 From. 43.38 30.09 6.62 0.45 53.80 3.15 15.57 1.20 8,979 To. 4.43 25.99 21.8 10,411 To. 59.50 44.00 21.31 1.34 64.20 5.36 29.13 2.58 11,510 Average. 3.35 16.49 1.47 7,661 Average. 50.48 37.81 11.71 0.90 58.85 4.48 22.20 1.86 10,212 Tea;as Coals and Lign·ites PROXIMATE ANALYSES OF TEXAS LiGNITE~ALPHABETIOAJ,LY ARRANGED­ DRY BASIS. BY S. H . WORRELL. Number and Description of Sample. 40. Alba Lignite Co.Alba, Wood County_____________ 59. Alba-Malakoff Lignite Co.Alba, Wood County______________ 12. American Lignite Briquette Co. Rockdale, Milam County_________ 'Ol. American Lignite Briquette Co. Rockdale, Milam County________ 13. Bear Grass Coal Co. Jewett, Leon County -----------­14. Bertetti Coal Co. Lytle, Medina County____________ 16. Carr Wood & Coal Co. Lytle, Medina County ---­------­n. Como Lignite Co. Como, Hopkins County --------­17. Consumers Lignite Co. Alba and Hoyt,. Wood County__ i6. Consumers Lignite Co. Alba and Hoyt, Wood County__ 18. Oookvllle Coal & J,umber Co. Mt. Pleasant, Titus County_____ 86. Edgewood Coal & Fuel Co. Wills Point, Van Zandt County_ 20. Houston County Coal & Mfg. Co. Crockett, Houston County______ El. Independence Mining Co. Phelan, Bastrop County_________ 22 . Lone Star Lignite Mining Co. Como, Hopkins County____ ______ 23. Melcher Coal & Clay Co. O'Quinn, Fayette County________ 65. Rockdale C'oal Co . Hicks, Lee County____ __ _________ 44. Rockdale Consolidated Coal Co. Rockdale, Milam County______ __ 28. Rockdale Lignite Co. Rockdale, Milam County________ _ 25. Rowlett & Wells. Rockdale, M!lam County_________ t6. S. W. Fuel & Mfg. Co . Calvert, Robertson County_____ i9. Texas Coal Go. Rockdale, Milam County________ _ !9. Vogel & Lorenz. Rockdale, Milam County_________ Average -----------------­----· ~ - Volatile and Fixed Com- Carbon. bustlble. 48.10 41.05 51.30 38.48 56.70 3Cl.C19 49.21 39.53 59.50 31.75 56.00 31.91 44.80 I 33.89 44.70 46.63 52 .14 38.22 46.18 43.63 58.60 30.64 56.18 37.20 52.90 33.99 Ash. Sulphur. 10.85 .80 10.l!'l 1.10 14.31 .78 11.26 .45 8.75 1.00 13.00 1.33 21.31 .rr. 12.67 .64 9.64 I .81 10.20 .68 10.76 1.05 6.62 .65 13.11 .80 Heating Power B. T. U. 10,220 10,340 8,979 11,230 9,850 10,510 9,344 10,600 10.510 10,840 9,782 10,540 10,120 ' I 50.76 39.54 9.70 .90 10,226 I 1.00 9,70Q 48.54 37.65 13.81 I 49.28 32.90 17.82 1.34 9,709 11,182 51.20 38.78 10.02 .72 43.38 41.43 15.19 10,900 .54 41.31 11.00 10,000 47.60 .98 9,757 44.00 7.00 49.00 .87 1.29 10,000 47.80 fil.71 11.49 13.22 .80 10,410 45.66 41 .12 50.52 39.20 10.28 1.20 9,856 10,212 37.81 11.71 .90 00.48 The heat units in perfectly dry lignite compare fairly well with the heat units in Texas coals as they are mined, but the heat units in lignite as received at points of consumption are much lower than in dry lignite and much lower than they are in coal. But this is the very point not covered in this Bulletin. We have no means of knowing, except in a few cases, how much moisture lignites contain as they are used. In comparing one lignite with another or lignite with coal for practical purposes it is necessary to know how much moisture they contain, for upon 4-T. C. Bulletin of the University of Texas this depends, to a great extent, their value as fuel. The follow­ing Table shows how great the differences in composition of lig­:cites may be, according as they are considered with the moisture, they contain or on a dry basis. Average composition of Texas lignites with moisture and with­out moisture: With 25 per cent. of moisture. Dry. Volatile and Combustible matter. . . . . . . . . . . 37.59 50.48 Fixed Carbon . . . . . . . . . . . . . . . . . . . . . . . . . . . 28.45 37.81 Ash. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 8.79 11.71 Sulphur . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 0.65 0.90 Heating Power, B. T. U...... .. .. ......... 7,661 10,212 The percentages for any intermediate amount of water may readily be calculated from the "dry" analysis. In comparing one lignite wtih another it is necessary to know how much water they contain, and what the composition would be if reduced to a dry basis. But since it is impracticable to dry lignite before it is used, and since it is customary to use it as soon as possible after it is mined, the amount of water it contains, as it is 1tSed, is a very important consideration. A case has recently been reported to ns in which the heating power of a certain lignite, as received at the works, was 6,410 B. T. U., the moisture being 31.45 per cent. Theoretically a pound of this lignite should evaporate 6.63 pounds of water from and at 212 degrees Fahrenheit. The returns reported an actual evaporative power per pound of lignite, of 3.25 pounds of water. or less than 50 per cent. of the theoretical evaporative power. While a part of this loss may have been due to an uneconomical installation, yet it does not appear that this would account for all of it. In dealing with lignite we have to remember that we have a fuel which may contain a full third of its weight of water, .md that, aside from this, the volatile and combustible matter, and, we suspect, the fixed carbon also, is different not only in amount, but in quality, from such substances in coal. In producer practice and in ordinary steam installations these Tev.cas Coals and Lignites facts must be borne in mind, and both the producer and the fire­box grates and air inlets designed accordingly_ There is a marked difference in lignites, and a producer, for instance, de­signed and built for a certain lignite, and which gives gooil "e­sults from it is not necessarily suited for all lignites. Nor is it merely a question of design and construction. The actual handling 0£ the plant is, perhaps, of even greater importance. So far as we are aware, there is no successful traveling grate used in lignite firing. There are traveling grates that are used with a mixture of soft coal and lignite, but none operating suc­cessfully on lignite alone. Hand-firing, with a boiler similar in type to the Dutch, or Dutch-oven, boiler has given, we under­stand, the best results from lignite. It is hoped that the experi­ments to be carried on this winter in the new power-house at the University will give accurate data on some of these questions. DISPOSABLE HYDROGEN IN TEXAS LIGNITES-DRY BASIS. .Analysis No. (() -­----------------------------­ Total '-iydrogen . 4.35 Disposable Hydrogen. Per Cent. Per Cent. of Total. 1.10 25.29 59 12 -------------------...--------­-----------------------­------­ 4.21 4.18 1.19 1.12 28.26 26.79 f/l 13 ---------­------------------­----------·-------------------­ 4.'78 4.11 2.59 1.52 54.19 36.98 1' ------------------------------­ 4.96 2.50 50.40 16 ----------------------------­ 4.75 2.84 59.79 41 ----------------------­-------­ 4.40 2.94 33.18 17 ------­-----------------------­ 4.75 2.06 43.37 56 ------------------------------­ 3.15 none none 18 ------------------------------­ 4.70 1.79 38.08 36 20 -------..--------------------­---------------------------­ 5.12 5.36 2.10 2.70 41.00 50.26 21 ------------------------­-----­ 5.03 2.34 46.12 22 23 --------...--------·----------­----------------------------­ 4.29 4.70 1.84 2.47 42.89 52.55 55 ----------------------------­ 4.56 2.20 48.24 "' -----------------------------­ 4.03 1.52 37.71 !8 25 ----------------------------­-----------------------------­ 4.00 4.78 1.73 1.69 42.61 35.35 21! -----------------------------­ 4.63 1.79 ~.66 39 29 -----------­---------------­_______________________________.. 4.46 3.82 1.98 1.00 42.39 ~.18 Average -----------------­ 4.48 1.87 41.74 The first thing to attract attention in this Table, as compared with the Table giving the disposable hydrogen in Texas coals, page 20, is that while the total hydrogen in the lignites is very nearly the same as in the coals ( 4.48 and 4.66), the percentage of disposable hydrogen in the lignites is much less than in the coals (1.87 and 3.24). The amount of disposable hydrogen, Bulletin of the University of Texa,s expressed as. percentage of the total hydrogen, is also much less in the lignites than in the coals ( 41.74 and 69,53). In more than half of the lignites the disposable hydrogen was less than one per cent., while in the coals there was not a single case in which it fell below 2.29 per cent From the standpoint of the disposable hydrogen expressed as percentage of the total hydrogen there were only five cases out of twenty­three in which it rose above 50 per cent. in the lignites, while in the coals there was not a single case in which it fell below 54 per cent. From the standpoint of the gas-maker, whether illuminating or fuel gas, retort or producer, these facts are of considerable moment, for they indicate radical differences in these fuels with respect to the composition and value of the gas to be ob­tained from them under standard conditions. There is very little data to be obtained with referenec to the use of lignite for making gas in retorts, its principal use, in gas-making, being in the producer. If the plans that have been made for the further study of our coals and lignites can be carried out, we shall have more to say on this subject later. In the meantime there will be found in the chapter on ''The Use of Producer Gas in Texas" a compact statement of the progress that has been made in Texas within the last few years, together with some observations on the tendency of the industry. This chapter hM been prepared especially for this Bulletin by ?.Ir. Drury :Jic.N'. Ph.illips. who has visited nearly eve1·y plant in Texas that is making producer-gas, after having had considerable practical experience in pro­ ducer work, and the application of machinerv to such problems. In order to arrani:re in one eonvenient form the different ~malyses that have been made on Texas lignites, we quote those f!iven in ~fr. E. T. Dumble's report on Brown Coal and J,ig­ uite, 1892. The proximate analyse~ and key are given first, and then the ultimate analyses. The examinations made at the coal testing plant of the United States Geological Survey will ~}so be found in Chap­ ter III, 1'exas Goals and Lignites PROXIMATE ANALYSES OF TEXAS LIGNITES, COMPILED FROM E. T. DUMBLE'S "BROWN COAL AND LIGNITE, 1892." Volatile and Fixed Moisture. Combustible. Carbon. Ash. Sulphur. 8.35 41.28 42.73 6.40 1.24 12.40 36.37 37.77 13.60 not det'd 13.28 59.86 18.52 8.32 not det'd 11.11 57.05 26.46 4.50 .f5{ 10.60 36.12 38.16 15.12 3.51 15.80 39.42 39.78 4.99 not det'd 7.17 40.55 34.27 17.19 2.24 20.29 32.67 26.58 17.50 ! 3.11 12.43 38.37 38.90 8.60 1.84 6.25 54.05 33.47 6.27 .69 16.56 45.10 32.89 5.49 not det'd 8.41 38.41 28.65 23.38 .74 16.50 36.07 37.17 8.60 1.66 10.35 39.03 43.25 6.87 I .50 12.00 42.00 82.00 13.00 not det'd 13.25 40.62 36.47 8.40 1.26 15.89 42.24 34.46 6.85 1.06 6.50 46.64 ?8.02 17.72 2.22 20.80 &2.08 22.67 3.97 .48 10.17 39.52 36.60 12.80 .95 16.45 40.24 35.89 8.95 1.17 13.51 45.36 32.44 8.15 .88 13.10 37.24 41.22 6.07 2.36 10.11 18.26 9.67 37.37 43.51 S9.5'1 I 24.39 29.53 89.90 27.59 8.70 10.ots 1.15 2.46 .76 Analysis. A. ·-------------------­ B. -------------------­ C. -------------------­D.1 ------------------­E. 1 ------------------­F . -------------------­G.• ------------------­ H.2 -----------------­ 1.a ----------·-------­ J.1 ------------------­ K .1 ------------------­ L.a ------------------­¥ -------------------­ N. -------------------­ 0 . -------------------­ P. -------------------­ Q.• ------------------­ R.1 -----------------­ S. -------------------­ T .1 -----------------­ U.• ------------------­ V.• -----------------­ W .1 -----------------­ X.a ------------------­ y. -------------------­ z.• ------------------­ 1. Average of two analyses. 2. Average of four analyses. 3. Averai:e of five analyses. 4. Averai:e of three analyses. Key to analyses of lignites compiled from ''Brown Coal and Lignite, Dumble, ' ' 1892 : A. Anderson county. From an outcrop on Caddo Creek, about seventeen miles northeast of Palestine: thickness, about two feet. B. Angelina county. C. Atascosa county, near Somerset: thickness; 5 feet 3 inches to 5 feet 6 inches. D. Bowie county, near New Boston: thickness, 12 feet. One of the analyses shows 1.45 per cent. of ash, with 76.41 per cent. of volatile and combustible matter and 10.62 per cent. of fixed carbon. E . Caldwell county. Burdett Wells. F. Cass county. Stone Bluff. G. Cherokee County. Bean's Creek, six miles south of Alto; near Jacksonville ; McBee 's school house. H. Fayette county. Manton Bluff: thickness, up to 15 feet. On 0 'Q·uinn creek the lignite is of excellent quality and has a thickness up to 8 feet. Bulletin of the University of Texas I. Harrison county. Robertson's Ferry and Rocky Ford, Sa­bine river; McCathern Creek: thickness, 2 to 6 feet. J. Henderson county. C. M. Walters headright: thickness, up to 6 feet. K. Hopkins county, near Sulphur Springs: thickness, up to 16 feet. L. Houston county. Hyde's Bluff and Westmoreland Bluff, Trinity river; J. Bethel headright; Wallace headright, near Calthorp : thickness, 4 to 6 feet. M. Lee county. Blue Branch: thickness, 6 feet. N. Leon county, near Jewett: thickness, up to 9 feet. 0. Limestone comity. Head's Prairie. P. Medina county. Lytle: thickness, 5 feet. Q. Milam county. Rockdale: thickness, 4 to 6 feet. R. Morris county. Pruit place: thickness, iess than 2 feet. S. Panola county. Mineral Springs Ridge, near Beckville: thickness, 4 1-2 feet. T. Rains county. Emory, and seven miles east. U. Robertson county. Little Brazos; Calvert Bluff: thick­ness, 3 to 7 feet. V. Rusk county. Iron Mountain; Graham's Lake, 12 miles west of Henderson : thickness, 3 to 6 feet. W. San .Augustine county. Sabine and .Angelina rivers: thickness, 6 to 15 feet. X. Smith county. Southwest of Tyler, 8 ¥2 miles; south of Tyler, 6 miles; southeast of Tyler, 12 miles; west of Lin­dale, 3 miles : thickness, 3 feet and upwards. Y. Shelby county. South of Timpson, 7 miles: thiclmess, 4 to 5 feet. Z. Wood county. .Alba and Mineola: thickness, 8 feet. Texas Goals and Lignites ULTIMATE ANALYSIS OF '£EXAS BROWN COALS-FROM: "'BROWN COAL AND LIGNITE," DUMBLE, 1892. Ozygen County. Moisture. Carbon. Hydree-P.n. and Ash. Sulphur. Nitrogen. ---------,-----1----1-----1-------­Anderson ---------------------53.06 4.06 24.12 17.74 1.00 Bowle ------------10.67 69.84 3.10 26.97 9.10 1.00 Oherokee -------------------66.67 3.81 22.08 5.83 1.64 Grllltg ------------12.00 60. 79 4.96 23.68 9.27 .88 Harrison --------13.35 66.32 3.95 21.56 8.97 2.20 Houston ---------------------63.09 3.64 22.56 9.68 1.00 Lee -------------16.50 62.48 3.21 20.80 11.56 1.95 Leon --------------------------63.60 4.08 24.00 7.79 .55 lfedina --------13.25 60.92 2.57 25.34 9.70 1.47 Milam ----------------------60.93 4.12 22.27 11.86 1.32 Milam ----------17. 75 62.50 5.45 20.84 7.54 .97 J4llam ---------18.25 64.50 5.37 20.76 8.56 .81 Morris ----------8.56 69.87 4.70 24.35 8.66 2.42 Rains ----------------------57.04 4.01 24.48 13.35 1.11 Rains ------------------------59.32 2.80 20.27 16.63 .98 RQbertson -------------------58.16 4.46 13.11 12.77 1.50 Robertson ------16.40 65.14 5.29 19.28 9.21 1.1& Rusk -------------16.63 58.93 4.20 22.14 10.09 4.64 San AU2'UStine ----------------61.12 3.32 24.53 7.75 3.31> ltmith ------------9.83 57.40 3.00 23.31 14.74 .9& Webb (outcrop) _ -----------59.28 3.29 16.98 17 .56 .89 wood ------------1__1_0_.8&__1__56_._s_s-l·--4_._29__1__24_.13__1__1_4_.3_9_1__._84_ Anrage -----13.67 60.98 4.01 22.16 11.01 i 1.48 ~-------'-----------------~------­ The calculated heat units of some of the Texas lignites were also given by Mr. Dumble as follows: British Thermal Units. Dry. From Medina county. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 11,320 From Milam county . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 11,169 From Milam county . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 11,278 From Robertson county . . . . . . . . . . . . . . . . . . . . . . . . . . . 11,320 In order to compare the heat units in lignite as actually deter­mined with those obtained by calculation, we have prepared a Table based on our recent analyses. The Goutal formula. (p. 25), was used for the calculations based on ;>roximate analyses and the DuLong formula for those based on ultimate analyses. The results are as follows : Bulletin of the University of Texas Heating Power, B. T. U. Dry. Theoretical 1---------------1 Evaporation Analysis No. Calculated. in Pounds of Water from From From and at 212° F. Proximate Ultimate Determined. .per Pound of Analysis. Analysis. Lignite. Dry. An examination of this Table shows that the Goutal formula applied to the calculation of heat units from the proximate analysis of lignites gives on the average, results that are 22.30 per cent. higher than the heat units obtained by actual deter­mination. It is, therefore, unreliable and can not be used with 1t reasonable degree of accuracy. The modified DuLong formula, applied to ultimate analyses of lignites gives, on the average. results that are 4.10 per cent. lower than the determined heat units. and may he userl for ap­proximate results. Applied to proximnte analyses of coal. the Goutal formula gives results which, on the average, are 10.67 per cent. too high, and the modified DuLong formula. applied to ultimate analyses gives results which. on the average. are almost the same as those obtainerl in the calorimeter. In this connection the Table on p. 26 may be consulted. In the Table giving the calculated heat units in Texas lignites we have included a calculation of the theoretical evaporation in pounds of water from and at 212 degrees Fahrenheit per ponnd of lignite. dry basis. The results vary from 9.29 to 11.62 ponnds of water per ponnd of lignite. the g<>neral average Texas Coals and Lignites being 10.56, dry basis. In actual practice the efficiency of lig­nite as a fuel under steam boilers varies according to circum­stances, and no rule of general application can be given. It is stated that one of the railroads in 'l'exas will soon begin a. series of tests with lignite as fuel for locomotives. If this work is undertaken, the results will be of great interest. and value. It is likely that tests will be made during the coming winter at the new power house of the University with reference to sta­tionary boilers. CHAPTER IIL THE USE OF PRODUCER GAS IN TEXAS. BY DRURY MCNEILL PHILLIPS. During the last few years there has been a marked increase in the use of lignite for making gas in gas-producers. The gas thus made is used for power, e. g. in gas engines of special design, or for fuel, e. g. for burning lime, etc. So far as known, this gas is not used in Texas for burning brick, sewer­pipe, tiling, etc., although it would certainly be well adapted for such purposes. The use of lignite for making gas is confined to the above mentioned purposes. No illuminating gas is made from this material, although an excellent light could be supplied by use of some of the well known types of incandescent mantles, such as the W elsbach, etc. There have been installed in this State 56 producers for making gas. Of this number there are now 17 in active opera­tion, representing 12,270 engine horse-power. Of the 36 estab­lishments that have been recorded 6 are now out of commis­sion, 3 make fuel gas for burning lime, 1 uses coal from New Mexico, 1 coal from Colorado, 1 now uses natural gas and 1 uses a mixture of semi-anthracite from Arkansas and Texas lignite. This leaves 23 establishments that use Texas lignite exclusively. The consumption of lignite at these plants is about 180 tons per 24 hours, and the total gas engine horse­power is 12,270. Most of the installations are of comparatively small size, for out of the total 11,490 engine horse-power in operation 7,700 (=67 per cent.) are represented by two plants. This leaves only 3,790 horse-power to be divided among 21 plants. 'The three cement plants, at Eagle Ford, Harry and San An­tonio, represent at present 8,300 horse-power, and, upon the addition of the 600 horse-power at San Antonio, they will rep­resent 8,900 horse-power. But the success that has been reached in the smaller plants Bullet,in of the University of 1'exas indicates the adaptability of the producer and gas engine to re­quirements varying from 50 to 250 horse power, quite as well as to the larger uses. The producer plants in Texas are scattered over a wide area, from Kingsville to Gainesville and from San Angelo to Hunts­ville. In visiting the 26 establishments that were upon the itinerary there was necessary a total travel of more than 2,500 miles, and if all of the plants had been visited, the trip would have involved nearly 4.000 miles. This circumstance has an im­portant bearing on the utilization of the by-prcducts, such as tar and ammoniacal liquor, for it means that they would have to be transported over considerable distances tt' some central plant for treatment. This is out of the question now, so that the utilization of the tar and ammoniacal liquor is possible only at the large plants. Ko attempt is made to make use of these b~r-products, save that a little of the tar is used as fuel and a little for "creosoting" telephone and electric light poles, etc. The cost of the lignite, delivered, varies from 90 cents to $3.65 a ton, according to distance from the mines, amount in­volved in the contract, etc. The average value of the lignite mined in the State in 1910, at the mines. was 96 cents, the pro­duction having been 979,232 tons, the largest in the history of the industry. The word of prophecy uttered by Mr. E. T. Dumble, State Geologist, in 1891, in his pamphlet, ''The Utili­zation of Lignite,'' and repeated, in 1892, in his ''Brown Coal and Lignite,'' is now being fulfilled, and there appears to be no reason to doubt that there will be a further and larger de­velopment of this source of power. The supplies of lignite of all kinds is certainly beyond all question. In the United States there are about 123,700 square miles of li1?Dite territorr distributed as follows: Alabama ... . . .. .. .. ..... . . .. .. ....... . ......... . . . 6.000 A.rkansas ....... ..... . . . ......................... . 5,900 Louisiana . . . ....... ............. . .......... . . . . . .. . 8,800 l\Iontana ....... . ......... ... ... . ...... . ....... . .. . 7,000 :North Dakota . . .. . ..... . ............... . . .. . ..... . 31,000 South Dakota . .. . .. . ....... . ......... . . . ..... . . .. . 4,000 Tennessee .......... ...... ............ ........... . 1,000 Texas . . . ....... . ..... . ... .... .... · · .. · . .. .... .... . 60,000 123,700 Te;xas Coals and Lignites The lignite area in Texas comprises nearly one-half of the en­ tire known area in the United States and is nearly as large as the entire State of Missouri. Practically all varieties of lignite are found here, and there is offered a wide choice to the designers of producer plants, even inclusive of material that carries 75 per cent. of volatile and combustible matter. There is no inten­ tion, in this paper, to prepare a dissertation on gas­ producers or to enter into the details of the design and construc­ tion of producer-gas plants. We wish merely to give the chief results of personal observation at 26 plants that were visited anJ information derived by correspondence with ten other plants. It may not be amiss to say that the writer has served his time in the shops of the Allis-Chalmers Company, Chicago, and West Allis, and was afterwards in the gas department of an establish­ment in Texas that used 60 tons of lignite a day in gas-producers. He endeavors to look at the matter from a practical standpoint, · and has visited by far the larger number of producer plants in Texas for the purpose of acquainting himself with what is now being done here. It is beyond question that a very active interest is now being shown in the use of producer-gas made from lignite, and as ex­ perience is gained both in the handling of the various types of producers, and, more especially, in the design and construction of engines for using large volumes of a gas of low heating power, the use of lignite will be extended. The total producer horse-power, operating on lignite in Texas, is now (about) 13,000, while the total engine horse-power is 12,270. In such use of lignite Texas exceeds all of the other States combined, as it exceeds, in lignite area, all of the other States. In certain favored localities within reach of the natural gas fields of Clay and Wichita Counties, Texas, and of the Caddo fields in Louisiana, lignite faces a serious competitor. This com­ petition, however, is not manifested throughout the State at large, and even in north Texas, where natural gas is available, some of the larger establishments prefer lignite. The question of competition from natural gas, excellent as this fuel is, is more academic than practical. So far as is known, only one la.rge es­ tablishment is to change from producer-gas to natural gas, while its near-by neighbors will continue to us~ lignite. Bulletin of the University of Texas It is a question of relative economy into which many diverse factors enter1 and we do not discuss them here. If there is any one thing that stands out more prominently than others, as the result of these observations and investigations, it is that the best results in producer-gas engine practice are likely to follow from a consideration of the plant as a compact unit, a unit in which the producer is a part of the engine and the engine a part of the producer. We do not mean to say that good results are not obtained by the use of a producer not specially designed for the engine or by the use of an engine not specially design~d for the producer. As a matter of fact, good results are obtained in establish­ments where the producer is designed and built without particu­lar reference to the type of engine to be used, as also where the engine is supposed to handle the gas from almost any kind of standard producer. But we believe that better results, more uniform and more economical, can be secured by designin~ the producer for the engine and the engine for the producer. Producer and engine must be regarded as a compact and symmetrical unit to do a cer­tain thing at all times to the best advantage. Furthermore, a producer and engine designed to operate on a certain kind of fuel can not be expected to give as good results on some other kind of fuel. Within certain limits, to be de­termined when the plant is designed, the results should not vary excessively, but they will vary, through no fault of producer or engine, if the character of the fuel is materially changed. There is a wide variation in the composition of lignite, and this varia­tion gives rise to differences in the amount and nature of the gas, the tar and ammoniacal liquor. An engine designetl to operate on a rich gas will certainly not work to its rated capacity on a poor gas. It is not fed on ma. terial that it can utilize. It can not do its work, any more than a strong man, accustomed to strong food, can do his work on milk toast. If the heat units are not in the gas, the engine cer­tainly can not get them out, and if the heat units are not in his gas, the lime-burner certainly can not burn his charge. It is not a question of tuyeres, or gas-ports or air valves; it is a ques­tion of heat units in the gas. In B'ulletin No. 416, United States Geological Survey, 1909, T exas Coals and Lignites ''Recent Development of the Producer-Gas Power Plant in the United States,'' by Robert H. Fernald, there is given a list of 16 installations in Texas. T'hese were as follows, by localities : Blooming Grove, Corpus Christi, (near) Dallas, Garwoo·J, Gatesville, Leonard, Mart, Mineola, Rockport, Royse, Smith­ville, Stephenville, Taylor, Teague and Yorktown. With the ex­ception of the plants at Royse and Taylor, which used anthra­cite, all of these used lignite. To Mr. Fernald's list we have added 20 more, so that there are now 36 gas-producer plants in the State, with 5 out of commission. The total producer horse­power, as given by Mr. Fernald, was 8,001, and t'he total engine power was 7 ,616. We have increased these to (about) 13,000 and 12,270, respectively. To those who wish to inform themselves as to the progress of producer-gas practice in the United States and to acquire concise and accurate knowledge of the possibilities in this direc­tion we would commend Mr. F ernald's paper. It may be of interest to give here a list of the producer plants mentioned by Mr. Fernald, and we have prepared a Table to set forth the main facts. This table gives the number of producers in each State, the total producer horse-power, the total engine horse-power and the fuel used, together with the number of producer plants, the producer horse-power and the engine horse-power expressed as percentages of the respective totals. In this table under the term ''bituminous coal'' is included also sub-bituminous coal, under the term "anthracite" is in­cluded semi-anthracite, and under the term " lignite" is in­cluded brown coal. '!'ABLE SHOWING PRODUCER-GA'3 PLAN'.rS IN '!'HE UNl'l'ED S'l'A'l'ES-ARRANGED FROM FERNALD, 1909. Percentage Total No. of Producer­State. Producer hors&­Plants. power. 3 260 Alaska ---------------------­ Alabama ------------------­ 1 250 Arkansas ------------------­ 1 75 6 4,422 ~~W~gr~ia--:=::::==:::=::===:l Colorado -------------------' ~~!~~~~~~~~--=~==============Dist. of Columbia__________ i! Flcrida ---------------------' Idaho -----------------------' Illinois ----__ ---------------1 Iowa -----------------------­ Indiana ---------------------, Kansas --------------------­ ~~Yl~i~~~-~==================i Maryland -------------------i Massachusetts --------------' Michigan -------------------i st~£ii!~a====================-------------------i Nebraska ! Nevada ---------------------i New Han1pshire ----··-------1 ~:: tr:r:i~~ =============::::! New York -.-----------------/ North Carolina -------------, North Dakota -------------1 Ohio ------------------------! g:~=~~m~--=:::=::::::=====::j Pennsylvania ---------------' Pcrto Rico _________________! 2 8 16 3 8 z 29 17 8 13 2 3 2 10 25 16 16 17 1 18 1 2 37 3 37 4 8 19 6 2 4.2 s 560 1,405 7 ,430 200 875 3,000 400 3,087 9,847 902 1,330 70 810 766 1,220 7,385 2,631 1,871 13,147 60 1,291 200 1,000 6,657 260 7,964 2,180 497 1,855 6!l5 200 4,299 60 Total EngineHorse-Fuel. pow~ ~~tt~~·'!~~~--~~-~~-~~~-~~~~~~:~~=:::::::::::::::I 100 Anthracite -------------------------------------.. 422 420 1,090 1,251 not given 683 1,543 400 2,688 3,138 898 1,383 70 310 65 685 3,324 I 2,656 1,769 3,1: 1, 144 150 635 2,480 260 4,540 1,680 478 1,670 Bit1,1minous Coal and Anthra~it•.l---------------1 Wood and Anthraci~e --------------------------i Lignite and Anthracite--------------------------1 Bituminous Coal and Anthracite---------------1 Anthracite --------------------------------------! Anthracite --------------------·-----------------' Bituminous Coal and Anthracite"--------------1 Anthracite --------------------------------------1 Bituminous Ooal and Anthracite_______________ , Bituminous Coal and AnthracitC---------------1 Anthracite -------------------------------------­ Bituminous Coal and Anthracite_______________' Anthracite -------------------------------------­ Bituminous Coal and Anthracite______________ _ Anthracite -------------------------------------­Anthracite -------------------------------------­ Bituminous Coal, Ooke and Anthracite____ ____ Anthracite ------___ ----------------------------­Anthracite -------------------------------------­ ~~t~~~~~s-~~-~~-~~~-~~~~~~:!~:::::~::=::::::=i Anthracite ____ ----------------------------------1 Anthracite --------------------------------------' Anthracite --------------------------------------J Bituminous Coal and Anthracite---------------· Anthracite ___ -----------------------------------' Bituminous Coal and Anthracite---------------J Bituminous Coal and Anthracite---------------, Anthracite -------------------------------------­ Bituminous Coal and Anthrnrite---------------· :; f~~~~!~~~s-~-~~~~-~!~-~~~·--~~-~~~~:!~::~:::::::! 1,846 Bituminous Coal and Anthraclte..--------------1 not &iven Anthracite --------------------------------------! of Total No. .62 .21 .21 1.05 .42 1.68 3.36 .21 .62 1.68 .42 6.00 3.57 1.68 2.73 .42 .62 .42 2.10 5.25 $.36 3.36 3.57 .21 3.78 .21 .42 7.77 .62 7.77 .84 1.68 3.99 1.22 .42 8.82 .62 of Pro­ducer horse­power. .21 .20 .06 3.5& .45 l.13 6.01 .16 .70 2.4..~ .32 2.50 7.96 .73 1.07 .05 .65 .61. .98 5.98 2.13 1.43 10.64 .04 l.04 .16· .81 6.39 .21 6.45 1.76 .40 1.50 .56 .16 S.48 .04 Iof Engine I horse­power. I .Oil .40 .10 .68 .68 1.76 2.02 1I -----------­ i I J.10 2.49 .64 4.35 5.08 .G4 2.24 .11 .50 .10 .94 5.38 4.14 2.86 5.77 .09 l.85 .24 1.0'2 2.91 .42 7.35 2.72 .77 2.70 .92 .32 2.98 Rhode Island ----· ----------; South Dakota ______________: 'l1ennessee -------------------~ rrexnS ----------------------! ~;~~o~f-::::::::::::::::::::1 Virginia -------------------­Washington ---------------­Wisconsin -----------------­Wyoming ------------------­ 4 2,375 18 2,336 2 150 i 16 8,~~ i 2 1 00 1 1 13 1;110 7 810 26 9,306 1 65 1 626 2,029 100 7,~~ not given 496 810 7,741 65 Total ----··--------------1 481 128.268 I 61,585 Bituminowi Ooal and Anthracite---------------j Anthracite -------------------------------------­ Anthracite ------· ------------------------------­ Lignite, Bituminous Ooal and Anthracite______ Anthracite -------------------------------------­Anthracite ------------------------------------­ Bituminous Ooal· and Anthracite_______________ Lignite and Anthracite ------------------------­ Bituminous ooal and Anthracite______________ _ Llgnit.e -----------------------------------------_ .84 3.78 .42 3.36 .42 .21 2.73 1.47 5.46 .21 1.92 1.88 .12 6.48 .22 .06 .9() .65 7.M .06 1.01 3.28 .16 12.33 .31 .70 1.31 12.~ .10 Bulletin of the University of Texas An examination of this Table shows that there were in the United States, at that time, 1908-1909, 481 producer plants, of which Texas had 16, or 3.36 per cent., ranking twelfth. Of pro­ducer horse-power there were 123,268, o·f which Texas had 8,001, or 6.48 per cent., ranking fourth. Of engine horse-power there were 61,585, of which Texas had 7,616, or 12.33 per cent., rank­ing second. This is in respect of all kinds of fuel, bituminous coal, anthracite and lignite. But when we consider the use of lignite alone, for there is very little bituminous coal or anthracite used in producers in Texas, the situation is radically changed. According to the data in Mr. Fernald's paper, there were in the United States 9,275 producer horse-power from lignite, viz: 625 in Colorado, 50 in Oklahoma, 7,985 in T'exas, 550 in Washington and 65 in Wyom­ing. Of th 9,275 lignite producer horse-power Texas had 7,985, or 86.10 per cent. of the total. There were 8,570 engine horse­power derived from producers operated on lignite distributed as follows: Colorado 380, Oklahoma 50, Texas 7,525, Washing­ton 550, Wyoming 65. Of the 8,570 engine horse-power derived from lignite, Texas was credited with 7,525, or 87.8 per cent. of the total. Texas has not only the largest output of lignite, more than double that of any other State, and the largest lignite area, twice that of any other State, it also utilizes its lignite for mak­ing gas to the extent of 87.8 per cent. of the total engine power thus derived in the entire country. North Dakota has 31,000 square miles of lignite area, being next to Texas in this respect, and mines about 400,000 tons of lignite a year, but at the time of the preparation of Mr. Fer­nald's report there was not a single lignite gas-producer in that 8tate. It may, therefore, be said with entire accuracy that Texas leads the country in area, production and utilization o.f lignite. In Bulletin No. 261, 1905, United States Geological Survey, there are given the results of testing two Texas lignites in the coal testing plant at St. Louis. These tests were under the care of Mr. Robert H. Fernald. The producer was a No. 7 Wood, 250 horse-power. The engine was a three-cylinder vertical Westing­house gas engine, rated at 225 brake horse-power. It was belted to a six-pole 175-kilowatt Westinghouse direct-current generator. Without going into all of the details of the work conducted Texas Coals and Lignites there we will give the chief results as set forth in the above­mentioned Bulletin. The first test was made on lignite from the Houston County Coal & Manufacturing Company, Crockett, Houston County. The analysis of the lignite used was as follows: Percent. Moisture . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 33.50 Volatile matter . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 8~.34 Fixed carbon . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 23.80 Ash . . . . . . . . . . . . . . . . . . . . . . . . . ... . . . . . . . . . . . . . . . . . . . 10.36 Sulphur . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 0.63 Heating Power, B. T. U.. . . . . . . . . . . . . . . . . . . . . . . . . . . . 7,267 Duration of test, ..............................hours 21.67 Total coal consumed in producer... ...........pounds 12,800 Moisture in coal...........................per cent. 33.50 Dry coal consumed in producer...............pounds 8,510 Refuse from dry coal .......................per cent. 15.85 Total refuse from coal. ......................pounds 1,327 Total combustible consumed in producer.......pounds 7 ,183 LIGNITE CONSUMED, POUNDS PER HOUR. Lignite consumed in producer ...................... . 590 Dry lignite consumed in producer................... . 393 Combustible consumed in producer ................. . 332 Equivalent lignite used by producer plant........... . 660 Equivalent dry lignite used by producer plant..... . 439.5 Equivalent combustible used by produce2· plant...... . 371.3 BRITISH THERMAL UNITS. Per pound of lignite as fired ........ . .... . ....... . 7,267 Per pound of dry lignite............. ............ . 10,928 Per pound of combustible........................ . 12,945 Per cubic foot of standard gas................... . 169.7 From standard gas per pound dry lignite burned in producer .................................. . 7,260 From standard gas per hour per brake horse-power .. 12,230 GAS PRODUCED, CUBIC FEET (reduced to standard). Total ........................................ . 363,654 Per hour ........................ . .............. . 16,800 Per pound lignite consumed in producer.......... . 28.4 Per pound dry lignite consumed in producer...... . 42.7 Per pound combustible consumed in producer...... . 50.6 Bulletin of the University of Texas Per pound equivalent lignite used by producer plant 25.5 Per pound equivalent dry coal used by producer plant 38.2 Per pound equivalent combustible used by producer plant . . . . . . . . . . . . . . . . . . . . . . . . . . ... . . . . . . . . . . . 45.3 HORSE-POWER DEVELOPED. Average electrical horse-power available for outside purposes . . . . . . . . . . . . . . . . . . . . . . . . . . . .... . . . . . . . . 187 Average electrical horse-power developed at switch­board . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 198 Average brake horse-power1 available for outside pur­ poses . . . . . . . . . . . . . . . . . . .. . . . . . . . . . . . . . . . . . . . . . . 220 Average brake horse-power developed at engine . . . . . . 233 1Based on an assumed efficiency of 85 per cent. for generator and belt. LIGNITE CONSUMED IN PRODUCER, POUNDS PER HORSE-POWER HOUR. Per electrical horae-power available for outside pur­poses _----------------------------------------------­ Per electrical horse-power developed at switch-board_ Per brake horse-power• available for outside purposes Per brake horse-power1 developed at engine____________ Equivalent pounds used by prodecer plant per electrl· cal horse-power available for outside purposes____ Equivalent pounds used by producer plant per electri­ cal horse-power developed at switch-board_________ Equivalent pounds used by producer plant per brake horse-power available for outside purposes_________ Equivalent pounds used by producer plant per brake horse-power developed at engine___________________ Coal as Fired. 3.16 2.98 2.68 2.54 3.53 3.34 3.00 2.83 Dry Com- Coal. ! bustible. 2.10 L78 1.99 1.68 1.79 1.51 1.69 1.43 2.35 1.99 2.22 1.88 2.2» 1.6!> 1.99 1.60 •Based on an assumed efficiency of 85 per cent. for generator and belt. AVERAGE COMPOSITION OF PRODUCER-GAS BY VOLUME. Per cent. Carbon dioxide . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 11.10 Carbon monoxide . . . . . . . . ... . . . . . . . . . . . . . . . . . . . . . . 14.43 Hydrogen . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . ... . . . . . . . . 10.54 Methane . . . . . . . . . . . . . . . . . . . . . . . . ... . . . . . . . . . . . . . 7. 48 Nitrogen . . . . . . . . . . . . . . . . . . . . . . ... . . . . . . . . . . . . . . . 56.22 Oxygen . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 0.22 ''The gas from this lignite was not ;;o rich as that from the North Dakota lignite that was tested, but it was higher in heat units than is the gas obtained from ordinary soft coal. The lig­nite was more difficult to handle in the producer than bituminous coal. but by frequent poking and by supplying the right amount Texas Coals and Lignites of air to the producer the bed was kept in good condition, and at the end of the thirty-hour test it was possible to break up the clinkers in the bed, requiring the removal of only a few ashes before beginning a new test. This lignite yielded a large amount of tar of the same kind as the North Dakota lignite, yellow and sticky. As a producer fuel it is better than many grades of bituminous coal.'' Another test was made on lignite from the mines of the Con­sumers' Lignite Company, at Hoyt, Wood County, Texas. This lignite had the following composition: Per cent. Moisture ........ . . . ....... ....... . .... . . ....... . 33.71 Volatile matter .. ................................. . 29.25 Fixed carbon . . . .................... . . .. . .. . .. .. . 29.76 Ash ......... . . . .. . .. ... ... . ... . .. . ..... . ...... . 7.28 Sulphur .............. ..... . .. . ... ......... .. .. . 0.53 Heating power B. T. U ... ................... ....... 7,348 Duration of test .............. ..... .. .... ....hours 19.33 Total lignite consumed in producer.. . . . .......pounds 9,050 Moisture in lignite ................... ......per cent. 33.71 Dry lignite consumed in producer. . . . . . . ..... pounds 5,999 Refuse from dry lignite...... .. ............ per cent. 10.98 Total refuse from lignite .....................pounds 658.7 Total combustible consumed in producer . . ....pounds 5,340.3 LIGNITE CONSUMED, POUNDS PER HOUR Lignite consumed in producer .................. ... . 468 Dry lignite consumed in producer ....... . .. . .. . ... . . 310.3 Combustible consumed in producer . ........ . . .. . . . . . 276.2 Equivalent lignite used by producer plant ........ .. . . 519.5 Equivalent dry lignite used by producer plant. ... .. . . 344.4 Equivalent combustible used by producer plant . .. .. . . 306.6 BRITISH THERMAL UNITS. Per pound of lignite as fired .. . . . ..... . .. . ......... . 7,348 Per pound of dry lignite ....... . ...... . ........... . 11,086 Per pound of combustible ........ ... ..... ......... . 12,450 Per cubic foot of standard gas . ..... . . . . .. ......... . 156.2 From standard gas per pound dry lignite burned in pro­ ducer . . ............ .. . ............ . ........... . 8,060 From standard gas per hour per brake horse-power . .. . 10,570 Bulletin of the University of 1'exas GAS PRODUCED, CUBIC FEET (reduced to standard). Total ........................................... . 309,140 Per hour .... . ................... . ............... . 16,009 Per pound lignite consumed in producer............ . 34.2 Per pound dry lignite consumed in producer......... . 51.6 Per pound combustible consumed in producer.... .. .. . 57.9 Per pound equivalent lignite used by producer plant.. 30.8 Per pound equivalent dry lignite used by producer plant 46.4 Per pound equivalent combustible used by producer plant ..................... · ··· · · · · · · ··· · · · · · · · · · 52.2 HORSE-POWER DEVELOPED. Average electrical horse-power available for outside pur­poses . . ...... . .......... . ..... . .... . .......... . 189.6 Average electrical horse-power developed at switch­board . ........................... . .......... . . 201.2 Average brake horse-power1 available for outside pur­poses . .. . . .. .. .. .... . ... · .. ········· · ·········· 223 Average brake horse-power1 developed at engine... . . . 236.5 1Based on an assumed efficiency of 85 per cent. for generator and belt. LIGNITE CONSUMED, POUNDS PER HORSE-POWER HOUR. Coal as Fired. Dry Coal. Com­bustlble. Per electrical horse-power available for outside pur­poses ---------------------------------------------­Per electrical horse-power developed at switch-board__ Per brake horse-power available for outside purposes_Per brake horse-power developed at engine ___________ Equivale!lt pounds used by producer plnnt per electri­cal horse-power available for outside purposes___ Equivalent pounds used by producer plant per electri­cal horse-power developed at switch-board_________ Equivalent pounds used by producer plant per brake horse-power1 available for outside purposes_______ Equivalent pounds used by producer plant per brakehorse­power1 developed at engine.. _______________ 2.47 2.33 2.10 1.98 2.74 2.58 2.33 2.20 1.64 1.54 1.39 1.31 1.82 1.71 1.55 1.46 1.46 1.37 1.24 1.17 1.62 1.52 1.88 1.30 1Based on an assumed efficiency ol 85 per cent, for generator and belt. COMPOSITION OF PRODUCER-GAS BY VOLUME. Carbon dioxide ... . ......................... . .. . 9.60 Carbon monoxide . . . . .... . ............... . ..... . 18.22 Hydrogen . ........ . ....... . ............. .. . ... . . 9.63 Methane ....... . ............................... . 4.81 Nitrogen ....................................... . 57.53 Oxygen .. ...................................... . 0.20 Texas Coals and Lignites This lignite "gave highly satisfactory results in the producer, yielding a rich, uniform gas and a large amount of yellow tar. It is an excellent fuel for p-roducers." Tbe term ''combustible'' is used to designate dry coal minus refuse ; that is, the actual amount of combustible matter con­sumed for the gas made. T'he term ''equivalent coal'' refers to the coal actually used in the producer plus the coal equivalent of'the steam used in operating the producer. It represents the gross fuel consumption of the entire plant. In Bulletin No. 332, United States Geological Survey, 1908, there are given two producer-gas tests made on Texas lignite at the fuel testing plant, St. Louis. These are as follows: LIGNITE FROM J. J. OLSEN &SONS, MILAM COUNTY. Per cent. Moisture . . . .... . . . .... . ... .. ............... .... . 32.20 Volatile matter .......... .. ....... . . . ... . . . . . . .. . 30.11 Fixed carbon ................................. .. . 7,870 Ash ... ......... ........... ..................... . 8.87 Sulphur ..... . . . . . ..... . . . ........... .... ....... . 0.88 Heating power, B. T. U., car sample.. . ......... . .. . 7,870 Size as used: over one inch, 61 per cent.; l/2 inch to 1 inch, 18 per cent. ; 14 inch to lf2 inch, 8 per cent. ; under 1.4 inch, 13 per cent. Duration of test, 50 hours. Average electrical horse­power, 200.1. Average heating power, B. T. U., per cubic foot of gas, 171.8. ,Total coal fired, 25,000 pounds. ANALYSIS OF GAS BY VOLUME. Per cent. Carbon dioxide .. . ......... .. .... . .......... .. . . . 10.3 Carbon monoxide ........ . ..... . .... . . . ........ . 19.8 Hydrogen .................................. . ... . 14.8 Methane ......... . .. . ........ . .. .. .... . ....... . . 2.4 Nitrogen ....... . ..................... . .......... . 51.3 Oxygen . .... .. ..... . .......... . ......... . ...... . 0.7 Ethylene .......................... . ............... . 0.7 Bulletin of the University of Texas Lignite Dry Com­__________________,_a_s_Flr_e_d_._,__L_lg_n_it_e_. !' bustible. Liitnite consumed in producer per borse-power hour, pounds.Per electrical borse-power: ·I Commercially available -----------------------­Developed at switch-board -------------------­Per brake horse-power: 2.70 2.55 1.83 1.73 I, 11.. 0050 Commercially available ----------------------­Developed at engine --------------------------­ 2.29 2.17 1.50 1.47 1.35 I.28· Equivalent used by producer plant, pounds. I Per electrical horse-power: ! Commercially avai!&bla -----------------------i Developed at switch-board ------------------­i· Per brake horse-power: Commercially available ------------------------1 Developed at engine ---------------------------­ 2.90 2.75 2.47 2.33 1.97 1.86 1.67 1.fl8 1.7J 1.62 1.46 1.38 LIGNITE FROM HOYT, WOOD COU~TY. (probably from mines of Consumers' Lignite Company, W. B. P.): Per cent. Moisture .. ....... ........ _............. . ....... . 34.08 Volatile matter ........................ . . . .. .... . 33.15 Fixed carbon .. ... . ..... . ..... _................. . 25.32 Ash ..................... · .... · .. · · · ·· · · · · · · · · · · 7.45 Sulphur . ............ .. ......... .... ............ . 0.49 Heating power, B. T. U., car sample....... ........ . 7,497 Size as used: Over 1 inch, 68 per cent. ; 1/2 inch to 1 inch, 16 per cent. ; 14 inch to 112 inch, 7 per cent. ; under lJ.1, inch, 9 per cent. Duration of test, 50 hours. .fl. verage electrical horse­power, 193.4 Average heating power, B. T. U., per cubic foot of gas. 156.1. Total coal fired, 24,500 pounds. Analysis of gas by volume : Per cent. Carbon dioxide ............ . ......... . ...... . .. . 10.3 Carbon monoxide .............................. . 20.0 Hydrogen ............ . ............. .. . ......... . 15.4 Methane ........................... . ........ .. .. . 2.5 Nitrogen ...... . .. .... .................... .. .. .. . 51.8 Texas Coals and Lignites Lignite as Fired. ·------­ I Ll&"nlte consumed in producer per borsC'power hour, pounds. Per electrical horse-power: Oommercfally available -----------------------­Developed at ewiteh'board --------------------­ Per brake horse-power: Oommerelally avaflable ------------------------1 Developed at engine-----------------------------· Equivalent used by producer plant, pounds. Per electrical horse-power: Commercially available ----------------------­Developed at switch-board ----··---------------­ Per brake horse-power.: Oommerclally available -----------------------­Developed at engine ---------------------------­ 2.66 2.54 2.26 2.16 2.87 2.74 2.48 2.33 Dry Lignite. 1.75 L67 1.49 1.42 1.89 1.81 1.61 1.54 Com­ bustfble. 1.55 l.!I& 1.32 1.26 1.67 1.60 1.42 1.86 'rhe Westinghouse Machine Company, Pittsburg, Pa., in its Circular W. M. 503, September, 1909, gives the results of testing lignite from the mines of the Consumers' Iiignite Company, Hoyt, Wood County. Texas. The analysis of the lignite used was as follows: Per cent. Moisture ..... ... . ... .. . .......... ..... .. .. .. .. . . 23.83 Volatile matter ....... . . . ........ ... ..... .. ... . . . 38.32 Fixed carbon ....................... .. .......... . 29.22 Ash. .......... ...... .. . ...... .. ........ .. .. . ... . 8.63 Heating power, B. T. U..... .. ................... . 8,007 The engine was operated 72 hCYUrs. The total lignite fired was 16,970 pounds. The average load was 128 brake horse-power and the gross lignite per brake horse-power was 1.85 pounds. The gas was delivered throngh a line of 8-inch pipe over 650 feet long, with no correction for leaking or for gas consumed by three pilot lights burning continuously in the producer-house, laboratory and engine room. In another case, given by this Company, the same lignite being used, the following-statement is made: Duration of test ..................... ............46.5 hours Total lignite fired ...... . ... ..... ... .. . . . . .....12,693 pounds Heat value per pound ................. .......8,007 B. T. U. Total heat in-put=12,693,x8,007 .. ..... ...101,632,857 B. T. U. Total gas made (corrected to 62 degrees Fahrenheit and 30 inches barometer) .... ... ..... . .. . .612. 361 cubic feet or 49.03 cubic feet per pound of lignite fired. Total heat value of gas per cubic foot ...... . . .. .. 128.3 B. T~ U. Effective heat value of gas per cubic foot. .... .. . 117.1 B. T. U. Bulletin of the University of Texas Total output ............................78,565,816 B. T. U. Effective output ........................71,707,463 B. T. U. 78,565,816 Total efficiency--..................77.3 per cent. 101,632,857 71,717,463 Effective efficiency--... . . .........70.5 per cent. 101,632,857 The composition of the gas in this latter test was as follows : Per cent. Carbon dioxide . .. .. .............. .... .. . .. .. .. . 12.4 Oxygen ............................... ... . .. . ... . 0.9 Carbon monoxide ....................... , ...... . 13.3 Marsh gas ..................................... . 3.6 Hydrogen .......... .. ... .. ................ ... .. . 14.7 Nitrogen ........ .. ......... . ................... . 55.1 The Smith Gas Power Co., Lexington, Ohio, in its circular of recent date, gives the results of operating on Texas lignite at two establishments. In the one case the original plant was on steam power, using 80 horse-power, the cost for fuel and supplies be­ing $10.00, and £or labor $5.00 per 24 hours, total, $15.00. This plant changed to producer-gas. The cost of the lignite was $2.22 a ton, the average load on the engine was 80 horse-power, and the cost of fuel and supplies was $5.50, and £or labor $5.00 per 24 hours, total $11.50, as against $15.00 for steam. In the other case steam was also used, before the change to producer-gas was made, with an average load of 30 K. W. The plant is now operated on producer-gas made from lignite. 'rhe cost of the lig­nite is $1.20 a ton; the load is the same, and there is a saving of two tons of fuel per night. The producer-gas plants that have been established in ,Texas are as follows, by towns and counties : Those visited personally are marked with a •. Town. County. Altair* .............................. . ...........Colorado Amarillo ...........................................Potter Blooming Grove• .. ................................Navarro Brownwood . .. ........................... . ..........Brown Texas Coals and Lignites Calallen* .................................... .......Nueces Canadian .....••.................................Hemphill Corpus Christi* .....................................Nueces Dallas* ............................................Dallas Dittlinger* .........................................Comal Eagle Ford* ........................................Dallas Gainesville* .........................................Cooke Garwood* ........................................Colorado Gatesville* ..........................................Coryell Glen :B'lora .......................................Wharton Harry* .............................................Dallas Houston* ...........................................Harris Huntsville .........................................Walker Kingsville* .........................................Nueces Leonard* ................................. . ........Fannin Longview ...........................................Gregg McNeil* ............................................Travis Mart ...........................................McLennan Mineola* ............................................Wood Pittsburg* ..........................................Camp Rockport* ..........................................Aransas Round Rock* ...................................Williamson Royse* ...........................................Rockwall San Angelo ....................................Tom Green (near) San Antonio* ................. . ...............Bexar Smithville* .......................................Bastrop Stephenville* ........................................Erath Taylor* ........................................Williamson Teague* .........................................Freestone Terrell* ..........................................Kaufman Weatherford .......................................Parker Yorktown ..........................................DeWitt The plants at these places vary in capacity within wide limits, from one in which there is a 30 K. W. engine, with a producer using 1500 pounds of lignite a day, to one in whieh there are en­gines aggregating 4400 horse-power and using 60 tons of lignite per 24 hours. The plants at Royse and Taylor used anthracite when in opera­tion. The plant at Pittsburg uses a mixture of Arkansas semi-an­thracite and Texas lignite. The plant at Amarillo uses Colorado bituminous coal, and that at Canadian uses bituminous coal from New Mexico. The plants at McNeil, Round Rock and Dittlinger, which are fuel gas plants for burning lime, used Texas coal and lignite. There were 26 plants in operation on producer-gas at Bu.lletin of the University of Texas the time of the preparation of this report, June, 1911, but im­pending changes may alter this number. Of these there were 23 that used lignite exclusively, the estimated consumption being 180 tons per 24 hours. The aggregate gas engine horse-power at these 23 plants was 11,490. The total primary horse-power in Texas, used in establishments, etc., in the last census year was 319,37°1. The producers in use are made by the following firms : Bethlehem Steel Company, South Bethlehem, Penn. Fairbanks-Morse & Co., Chicago, Illinois. Elbert Harvey (Industrial Gas Company), New York. Herrick (Industrial Gas Company), New York. Irvin, J. H. McDonough, The Murray Company, Dallas, Texas. Power & Mining Machinery Company, Cudahy, Wisconsin. (Loomis-Pettibone Producer.) Smith Gas Power Company, Lexington, Ohio. The Westinghouse Machine Company, East Pittsburg, Penn. R. D. Wood & Company, Philadelphia, Penn. The gas engines that have been and are in use are made by the following firms : Alberger, Alberger Gas Engine Company, Buffalo, N. Y. Allis-Chalmers Company, West Allis, Wisconsin. Bethlehem Steel Company, Sauth Bethlehem, Penn. Buckeye, The Buckeye Engine Co., Salem, Ohio. Fairbanks-Morse & Co., Chicago, Illinois. Foos. The Foos Gas Engine Company, Springfield, Ohio. Muenzel. Minneapolis Steel & Machinery Co., Miuneapolis, Minn. Nash. The National Meter Co. , 1223 Wabash ave., Chicago, IU. Rathbun-Jones, The Rathbun-Jones Engineering Company, Toledo, Ohio. Snow. Snow Steam Pump Works, Buffalo, N. Y. Weber. The Weber Gas and Gasoline Engine Co., Kansas City, Missouri. The Westinghouse Machine Company, East Pittsburg, Penn. It may be worthy of note that of the nine producer and twelve engine manufacturers, there are but three that make both pro­ducer and engine, viz: The Bethlehem Steel Company, The Fair­banks-Morse Company and The Westinghouse Machine Company. The Bethlehem producers and engines are replacing Loomis­ Texas Coals and Lirrnites Pettibone producers and Snow engines in the only plant at which any of these types of equipment are in use This plant is the largest in the State, and, when completed, will be of about 4,400 horse-power. The Fairbanks-Morse equipment is used now at eight plants, aggregating 1,050 horse-power. There are in operation three Westinghouse installations of a total of 740 horse­power, which is being increased to 1,180. The Smith leads in the number of installations, there being now in operation ten plants of a total of 1,615 horse-power, which will be raised to eleven plants, with a total of 2,815 when producer operation is resumed at Dallas, and the plant at San Antonio doubled. R. D. Wood & Co. have six installations, only four of which were in opera­tion, with a total of 1,125 horse-power. The single Harvey plant is of 3,300 horse-power, but here producers are to be replaced by natural gas shortly. Other makes are represented by single installations. With regard to engines, the Bethlehem, replacing the Snow, will lead with 4,400 horse-power at a single plant, followed by Allis-Chalmers with 3,900 horse-power et two plants, Rathbun­Jones, with 1,235 at six plants to be increased to 1,835 at seven plants, and Fairbanks-Morse with 1,050 horse-power at eight plants. Following are: Westinghouse w~th 680 horse-power at three plants, now being increased to 1,060; Buckeye with 600 horse-power at one, now operating at 720 horse-power on natural gas and shortly to resume producer operation; Foos, with 325 horse-power at two plants, and Alberger with 250 horse-power at a single plant. The other makes are small and in single installa­tions. In number of plants, Fairbanks-Morse leads with eight, Rathbun-Jones has six, Westinghouse three, Allis-Chalmers nnd Foos two each and all others a single plant. The producer made by the Bethlehem Steel Company is used at the following establishment: Texas Portland Cement Com­pany, Harry (near) Dallas (being installed) . The Fairbanks-Morse is used by: G. M. Jackson, Garwood; G, C. Gifford Plantation, Glen Flora; Huntsville Electric Light & Power Company, Huntsville; Bayliss Earle, Mart; Rockport Ice & Light Company, Rockport; Smithville Light & Power Co., Smithville; Stephenville Light & Water Works, Stephen­ville; Teague .Electric Light & Power Co., Teague. The Harvey producer is used by the Southwestern States Port­ Bulletin of the University of Texas land Cement Company, Eagle Ford, (near) Dallas. The Herrick producer has been used by the Dittlinger Lime Co., Dittlinger. The Irvin producer is used at the shops of the Texas Midland Railway, Terrell. The Loomis-Pettibone producer is used by the Texas Portland Cement Company, Harry, (near) Dallas. The Smith producer is used by: The Home Light & Water Co., Blooming Grove ; Brownwood Water Works, Brown­wood; The People's Light Co., Corpus Christi; The Stan­ard-Tilton Milling Co., Dallas; Gainesville Electric Co., Gainesville; Gatesville Power & Light Co., Gatesville; Kings­ville Power Co., Kingsville; Mineola Light & Ice Co., Mineola; San Angelo Street Car Co., San Angelo; San Antonio Portland Cement Co., San Antonio, and ,The Yorktown Light & Ice Co., Yorktown. The Westinghouse producer is used by : The Arkansas & Texas Consolidated Ice & Coal Co., Pittsburg; Thti Canadian W~ter, Light & Power Co., Canadian; Amarillo Water, Light & Power Co., Amarillo, and by plants at Weatherford and Long­view, not now in operation. The R. D. Wood producer is used by: J. J . RichoJson, Al­tair; Nueces River Irrigation Co., Calallen; The People's Light Co., Corpus Christi; Houston Cotton-meal Mill, Houston; Aus­tin White Lime Co., McNeil; Round Rock White Lime Co., Round Rock. The Alberger gas engine is used by 1he San Angelo Street Car Co., San Angelo. The Allis-Chalmers gas engine is used by : San Antonio Portland Cement Co., San Antonio, and Southwestern States Portland Cement Co., Eagle Ford, (near) Dallas. The Bethlehem Steel Company's gas engine is used by: The Texas Portland Cement Company, Harry, (near) Dallas. The Buckeye gas engine is used by: The Stanard-Tilton Milling Co., Dallas. The Fairbanks-Morse & Co. 's gas engine is used where the Fairbanks-Morse producer is installed and reference is made to the list of producers. The Foos gas engine is used by: J. J . Richolson, Altair, and by the Nueces River Irrigation Co., Calallen. Texas Coals and Lignites 'rhe Muenzel gas engine is used by: The Gatesville Power & Light Co., Gatesville. The Nash gas engine is used by: The Gainesville Electric Co., Gainesville. The Rathbun-Jones gas engine is used by: The Home Light & Water Co., Blooming Grove; The People's Light Co., Corpus Christi ; Houston Cotton-meal Mill, Houston; Kingsville Power Co., Kingsville ; Mineola Light & Ice Co., Mineola; Yorktown Light & Ice Co., Yorktown. The Snow gas engine is used by: The Texas Portland Ce­ment Co., Harry, (near) Dallas. The Weber gas engine is used by: 'l'he Texas Midland Rail­way in the shops at Terrell. The Westinghouse gas engine is used where this type of pro­ducer is used and reference is made to the list of producers. TABLE OF PRODUCER PLANTS IN TEXAS. The plants visited personally are marked * The plants no longer in operation are marked t. Those using lignite exclusively are marked L The plant at Amarillo uses Colorado bituminous coal, and is being doubled. Canadian uses New Mexico bituminous coal. Pittsburg uses a mixture of Arkansas semi-anthracite and Texas lignite. Dallas uses natural gas now, but is sho".'t.ly to return to producers on lignite. At Harry, Bethlehem producers and en­gines are replacing Loomis-Pettibone producers and Snow en­gines. At San Antonio, Smith producers '.lnd Rathbun-Jones engine will increase the capacity to 1200 horse-power. Locality. L. Altair* ---------------------------­Amarillo -----------------------------­L. Blooming Grove* ----------------­L. Brownwood ----------------------­L. Oalallen* ------------------------­Canadian ---------------------------­ L. Corpus Ohrlstf• -----------------­Dallas• -----------------------------­tDittlinger* -------------------------­L. Eagle Ford* ---------------------­L. Gainesville* ---------------------­l.1. Garwood* ------------------------­L. Gatesville* -----------------------­.L. Glen Flora -----------------------­1.1. Harry• ---------------------------­L. Houston* ------------------------­},, Huntsville ----------------------­ L. Klngsvllle* -----------------------­t Leonard* ---------------------------­t Longview ---------------------------­McNeil* -----------------------------­ L. Mart -----------------------------­!,, Mineola* -------------------------­Pittsburg* --------------------------­ L. Rockport* -----------------------­ Round Rock* ------------------------­ t Royse* ______--------·--------------_ L. San Angelo ----------------------­ L. San Antonio* --------------------­!,. Smithville• ----------------------­ L. Stephenvllle* ---------------------­tTaylor• -----------------------------­ L. 'l'eague* --------------------------­},. Terrell* -------------------------­t Weatherford -----------------------­ L. Yorktown ------------------------­ Total Installed -----------------­ Total operating --------------­ 'l'ABLE OF PRODUOER PLANTS IN TEXAS. Producers. Gas Englne11. ,._N_u_m_b_e_r. / Kind. H01~e-power. Kind. Number. 1 fR. D. Wood & Oo.____________________ 1 :Westinghouse -------------------------­! Smith ---------------------------------­ 1 .Smith ---------------------------------­ 1 :R. D..wood & Oo._____________________ 2 ·westinghouse ------------------------­3 12 Wood, 1 Smith----------------------­3 ;Smith ---------------------------------­ .... 4 ~Herrick ---------------------------------1--------------Fuel gas for burning lime______ _ 3 - ;Z o Han•ey -------------------------------.• 3,300 Allis-Ohaimers ------------------­ 1 1 .Smith -----------·-----·----------------150 1Nash ----------------------------­ 0 1 ! Fulrbanks-Morse -----------------------' 200 1Falrbanks·Mors•3 ---------------­ 1 ,,.... ! .Smith ----·------------·-----------------1 80 Muenzel ------------------------­ 1 ;:::­ 1 il<'alrb;mks-Morse -----------------------200 Fairbanks-Morse ---------------­ 3 ll•thJehem, Loomis-Pettibone---------4,400 Bethlehem, Snow---------------­2 ,R. D. Wood & 00.----------------·---GOO Rathbun-Jones -----------------­ l• "" c:::j 1 l ] :l!'alrbnnks-Morse -----------------· ----: JOO Fairbanks-Morse ---------------­ ;: .... 1 .Smith ----------------------------------,' 100 Rathbun-Jones -----------------­ 1 1 :Fairbanks-Morse ----· -----------------50 Fairbanks-Morse ---------------­ <::! 1 2 !R· D. Wood & 00.-----------------------------------FU~! gas for burning lime,._____ _ 1 lWestlnghouse --------------------------1 !Westinghouse ------------------­ -"' ~ 1 1 1Falrbanks-Mors~ --··--------~·--------c-HlO Fairbanks-Morse ---------------­ ""· 1 ­ 1 ,Smith -----------------·-----------------1 90 Rathbun-Jones -----------------­ <..::: 1 1 1 1Westlngbouso --------------------------100 /Westinghouse ------------------­ c 1Falrbanks-Jlfors~ · ----------------------, 50 Fairbanks-Morse ---------------­ 1 :R. D. Wood & Co. ---------------------------------Fuel gas for burning lime__ 1 •Fairbanks-Morse -------------~-------­ ii ~~m~ ::::::::::::::::::::::::::::::::::; 1 :~~:~g:~~==~~~~~ :::::::::::::~::::::=:! 1 iFalrbanks-Morse ____ _ ______ __________ _!i !Fafrbanks-lllorse ---------------------­ 1 1 ~~~i1n-iii<>il80-::::::::~::::::::::::::::: 1 Smith ----------··----------------------­ 100 Foos -----------------------------1 880 Westinghouse -------------------1 li80-::::::::::::::::::: 60 Rathbun-Jones -----------------­ Texas Coals and Lignites Following is a brief description of the different plants vis­ited. .At some of these places it was not possible to secure more information that is here given.1 ALTAIR•. .An irrigation pumping plant on the Colorado river, Colo­rado county, operated by J. J. Richolson. One R. D. Wood & Co. 's suction up-draft producer and :fittings. The en­gine is a two-cylinder vertical Foos driving a single-phase high­lift centrifugal pump, through a 12-rope connection. The plant was designed and erected by the Southern Gas & Gasoline En­gine Company, Houston, but was not in operation. No one in authority could be seen, but the service is said to be satisfactory, when pumping is required. .AMARILLO. Amarillo Water, Light and Power Company. One Westinghouse producer rated at 440 horrn-power at sea level, one Westinghouse 18"x26" gas engine rated at 380 horse­power at sea level, direct connected to a Westinghouse 250 k. v. a. 2,300 volt generator. This equipment is now being du­plicated. The fuel is screened pea bituminous coal from Colorado, and costs $4.00 a ton. The following operating data is quoted from a letter from the Company: "May, 1911. ''Total coal, pounds, 192,487; hours of actual operation, 682; kilowatts generated, 88,250; average pounds of coal per kilowatt hour, 2.19; average run per day, 22 hours.'' This letter further states that the average load is 130 k. w., and that the gas will average 125 B. T. U. per -:mbic foot. The production of tar is a barrel in three months, this coming from the scrubbers and being full of lamp black. The water from the scrubbers goes to the sewer. Producers were installed here to replace steam, and entire satisfaction is expressed with the operation, as is shown by plans which contemplate a plant of 1,000 k. v. a. 'The places visited personally are marked with a • 6-T. C. Bulletin of the University of Texas BLOOMING GROVE.* The Home Light & Water Company. Equipment: One 60 horse-power Smith suction down-draft preducer; one Rathbun-Jones two-cylinder vertical gas engine of 60 horse-power. The engine is direct connected to a line shaft from which are driven an Allis-Chalmers generator, an Ingersoll-Rand two-cylinder air compressor for "blowing" a well from a depth of 200 feet, and a Fairbanks-Morse geared two-cylinder pump for lifting water from a surface tank 100 feet to a stand-pipe. The generator is an alternator o.l:' 17 k. w. at 2,200 volts, and operates about 12 hours a day, from noon un­til midnight, at an average load of 35 per cent The compres­sor requires about 25 horse-power, and operates about seven hours. The pump requires about 12 horse-power and operates about four hours. The average fuel consumption is about 1,600 pounds per 12 hours. The lignite used is from the mines of the Consumers' Lignite Company, Hoyt and Alba, Wood County, and costs $2.10 a ton, delivered. The producer is of an old type, similar to the one noticed at Mineola, i. e., the fire-containing shell rests dfrectly upon the foundation, the ashes being drawn by hand with long-handled shovels. Less tar was noticed here than at any plant visited, with the exception of the plant at Pittsburg, where the West­inghouse Tarless Producer is used. The jacket water is further heated in an exhaust heater and goes to the saturator at a tem­perature of about 140 degrees Fahrenheit, which can be in­creased to 170 degrees Fahrenheit. This producer, in addition to the gasoline engine-driven blower for starting, is further equipped with a hand blower so arranged as to be connected with the producer only when the mail!!. air inlet through the saturator is closed. It is used regu­larly to force gas to the engine for starting. The use o.l:' this hand blower does not seem to be required, as it was not observed elsewhere. The plant has been in operation about three years, during which time the repair account has been very small. The pipes in 1!he exhaust water heater are eaten up in 18 mouths. Texas Coals and Lignites BROWNWOOD. Brownwood Water Works. There is a 100 horse-power Smith producer here operating on lignite. We were unable to secure further information by correspondence. CALALLEN.* An irrigation pumping plant, operated by the Nueces River Irrigation Company, a co-operative farming enterprise. One No. 6 Wood suction up-draft producer a,nd standard fit­tings. The. engine is a three-cylinder vertical Faos, with rope drive to a 16-inch Worthington involute pump. This plant was not in operation at the time of visiting, but information was se­cured from the general manager and the operating engineer. The lignite used is from the mines ')f the Bear Grass Coal Company, Jewett, Leon county. The cost, on the producer floor, is $3.65 a ton. The engine is rated at 225 horse-power at 225 r. p. m. The guarantee calls for one brake horse-power from two and one­half pounds of lignite, as fired, and for the delivery of 6,500 gal­lons of water per minute on a lift of 83 feet. The plant was put in operation the first of January, 1911, but has not been run steadily for more than twelve hours at a time. There is no information as to consumption of lignite or details of operation. The producer is of the new Wood type, with the upper third of the producer walls and the top water­jacketed. From the jacket a pipe conveys water to the satu­rator for mixing water-vapor with air. The temperature of this air is kept at about 140 degrees Fahrenheit for normal op­erations. By increasing the temperature to 170 degrees Fah­renheit the tendency towards "clinkering" is arrested at an early stage. All of the water for engine and producer auxiliaries is taken from the main lift pipe through a two-inch line. The scrubber­water and tar are pumped back into the irrigation canal. It was at first intended to allow the waste water, tar, etc., to flow Bulletin of the University of Texas by gravity back into the river, but as the in-take for the Corpus Christi Water Works was but two miles below, the waste, etc., was taken back into the irrigation canal. It is not known how much ammonia the w'aste water carries, but at any rate it would probably not be sufficient to benefit vegatation under the condi­tions there. This plant was designed and installed by the Southern Gaa & Gasoline Engine Company, Houston. CANADIAN. Canadian Water, Light & Power Company. The equipment here consists of two producers of 100 horse­power each and two gas engines of 100 horse-power each, of Westinghouse make. The fuel is bituminous coal from New Mexico. This plant was not visited, and no further information could be secured by correspondence. CORPUS CHRISTI.• The People's Light Company. The original plant here consisted of one Smith suction pro­ducer of 125 horse-power capacity, and one Rathbun-Jones three-cylinder vertical gas engine. The engine was clirect connected to a Westinghouse two-phase generator at 2,300 volts. This equipment was afterwards increa<;ed by a No. 6 Wood suction producer, rated at 300 horse-power, and a Rathbun­Jones engine similar to the one in use, but rated at 300 horse­power. It was found that the producer would not supply suffi­cient gas for rated capacity, so a larger Wood, No. 7, was in­stalled a few months ago by the manufacturer. Since that time there has been no trouble, the two Wood producers carrying the entire load, while the Smith producer is held in reserve. The large engine carries the entire lighting and power load from 6 a. m. to midnight, the small engine being then used. Both generators deliver two-phase current at 2,300 volts, but no attempt is made to synchronize. The lighting current is trans­formed to 110 volts, with some power current at 220 volts, and Texas Coals and Lignites the street car current is run through a rotary to 550 volts, di· rect current. The exhaust from the large engine is led through a heater for supplying water-vapor to the sa.turator, which is ar­ranged to serve both producers. The maximum temperature of the blast is 150 degrees Fahrenheit, which is not as high as has been found best at other plants where a similar arrangement is in use. It is questionable whether the exhaust from a 300 horse-pawer engine will furnish enough water-vapor for two producers of tliis size, particularly when the heater is at least 25 feet from the engine. When the large engine is shut down, six hours out of every twenty-four, the blast is not heated at all, as the small engine exhausts direct into the air. It is during this time that clinkering is most apt to occur. On full load the larger producer is charged with 200 pounds of lignite every hour, the smaller one with a like amO'unt every two hours, both being cleaned every morning. In general, the suction is proportioned to the size of the producers and the fuel consumed in each. Clinker troubles are frequent and serious, masses of such size and consistency as to require sledging on the end of a one-inch poker being of common occurrence. The repair bill for broken pokers is sometimes as much as $15.00 in a month. This trouble has not been observed elsewhere in so serious a form, and it seems likely that means for obviating it would more than repay the expense. Among other things, both the temperature and the wetness of the blast might be increased when a clinker is observed to be formi!:lg. All cooling, scrub­bing and jacket water is drawn direct from the bay (salt water) by small motor-driven centrifugal pumps, and all waste water and tar runs into the bay. Several hundred pounds of tar are produced daily, but no accurate measurements have been taken, and there is no attempt made to utilize this product. Salt water makes no appreciable difference in producer oper­ations, although heavy encrustations were observed at one or two points where a slight leak had developed in the out-let pip­ing from the engine-jackets. It seems natural to suppO'Se that in time such encrustation would be a .:;curce of trouble. It is understood that the original water-jacketed exhaust valves did give trouble on this account; at any rate, they have been re­placed by air-cooled valves. Various lignites have been tried Bulletin of the University of Texas here, such as Calvert, Crockett and Rockdale. The price of the Calvert lignite, delivered at the works, is $2.65 a ton, of the Crockett lignite $2.67 and of the Rockdale lignite $2.47. The operating labor consists of three firemen, two ash-men and two engineers. The firemen and ash-men are Mexicans, at $1.50 a day. Owing to the recent installation of the larger producer, no definite method of operation has been developed, nor are there any definite figures as to the consumption of fuel per kilowatt hour. Before the new producer was jnstalled and while th~ one then in use was being forced beyond its point of economy, the fuel consumption was more than five pounds per kilowatt hour. Of late, however, this has been reduced to a little over three pounds, and there is a probability of an additional reduc­tion, especially, if the combustible matter remaining in the ash is lessened by more frequent poking of the fuel bed and by drawing ashes oftener. Additional poke-holes and ash-doors have been made in the sides of the two Wood producers, but as these were not observed elsewhere in similar installations their usefulness may be questioned. DALLAS.* Stanard-Tilton Milling Company. Equipment: Three 200 horse-power Smith suction down­draft producers. One Buckeye twin tandem two-cylinder, double-acting horizontal gas engine, direct connected to a 500 kilowatt Westinghouse alternator, furnishing power for a flour mill. This plant is now operating on natural gas supplied by the Lone Star Gas Company, Fort Worth, from its wells in Clay county, 110 miles northwest of Dallas. As in­stalled, the engine would develop, on producer-gas, only 600 horse-power. On natural gas it develops 720 horse­power. The consumption of natural gas is about 250,­000 cubic feet for 8,000 kilowatt hours. Larger cylin­ders have been ordered and the engine is to be operated again on producer-gas, as the Company is enthusiastic over this form of power. No details of operation are available for publication Texas Goals and Lignites at this time, beyond the statement that there was no trouble from the producers. The heat units in the natural gas supplied to north Texas es­ tablishments, under the best conditions, may be taken at 980. The gas consists almost entirely of methane. DITTLINGER.* Dittlinger Lime Company. At this plant there are four Herrick up-draft producers for making fuel gas to be used in burning lime. The kilns are now being fitted to use oil, but the producers will not be dismantled. These producers have been . operated for about three years, and the change to oil is said to be on account of economy. The fuel used was coal from the mines of the Olmos Coal Company and the International Coal Mines Company, Eagle Pass, Maverick county, the consumption being te;n tons a day for 300 barrels of lime. Parallel operations on coal and oil showed that about 90 barrels of lime were obtained from the use of p:roducer-gas and 120 barrels from oil. The producers are set very close to the kilns, and there are two for each kiln. This arrangement is more like that of a re­verberatory furnace than a producer plant such as was operated at McNeil and Round Rock for burning lime. However this may be, the fact remains that this plant is changing to oil, and the other lime plants have not had success in using producer­gas. EAGLE FORD.* Southwestern States Portland Cement Company. Equipment: Six Harvey up-draft pressure producers and three 750 kilowatt Allis-Chalmers hori~ontal two-cylinder tan­dem double-acting gas engines. These engines have, on the main shaft, Allis-Chalmers generators of 2,300 volts supplying power for the ·establisment. The original installation consisted of two Allis-Chalmers en­gines, to which a third was recently added. Bulletin of the University of Texas It is understood that the demand for power has increased so much that it would become necessary to add two producers or to gt> on natural gas, with some corresponding changes in the en­gines. After full consideration the Company has decided to use nat­ural gas, without, however, dismantling the producer plant. The natural gas is supplied by the Lone Star Gas Comapny, which has pipe lines into Fort Worth, Dallas, etc., from Clay and Wichita counties. The writer worked in the gas department of this Company several months, and what is here given concerning the opera­tions is with permission. F'1cel. The fuel used was lignite from the mines of the Con­sumers' Lignite Company, Hoyt and Alba, Wood county, and Grand Saline, Van Zandt county. It cost $1.62 a ton, delivered. A sample of this lignite taken from the producer-floor gave the following analysis : Per cent. Moisture ........ . ............................. . 10.80 Volatile matter ................................. . 42.76 Fixed carbon ...................................... . 40.38 Ash ........ . ................................... . 6.06 100.00 Sulphur . . . . . . . . . . . . . . . ... . . . . . . . . . . . . . . . . . . . . . . . . 0.63 An ultimate analysis of this sample gave the following results: Dry Basis. Per cent. Carbon . . . . . . . . . . . . . . . . . . . . . . . . . . ... . . . . . . . . . . . . . 54.70 Hydrogen . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 3.15 Oxygen . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 29.13 Nitrogen . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 2.14 Ash . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . ... . . . . . . . . . . . . 10.20 Sulphur . . . . . . . . . . . . . . . . . . . . . . . . . . . . . ... . . . . . . . . . 0.68 100.00 Heating Power, B. T. U., Dry........................ 10,840 The lignite represented by the above analysis is much drier than it usually is. The following analysis represents material with about as much moisture as it generally contains. Texas Coals and Lignites Per cent. Moisture . . . . .. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 29.20 Volatile matter................................... 40.38 Fixed carbon . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 21.83 Ash . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 8.61 100.00 Sulphur ........................................ . 0.63 It is likely that this analysis more truly represents the lignite, as charged, than the one first given. The heat units in the lignite, as charged, are, on the average, 7,500 B. T. U. For convenience of reference we have prepared two Tables of producer operations involving the use of 233,920 pounds of lignite, and the.produe­tion of 66,740 kilowatt hours of energy, equivalent to 89,411 horse-power hours. These Tables represent two distinct, but not consecutive pe­riods of 24 hours each, and these periods were divided into 11 and 13-hour sub-periods. For the 11-hour periods the readings are hourly, while for the 13-hour periods only the totals are given. Produeer Number. TABLE I. l'RODUOER OPERATION~EXAS LIGNITE. Time. 1 St. Fuel press. lbs . lbs. Fuel lbs . St. press. lbs . 8 St. Fuel press. lbs . lbs. ' St. Fuel press. lbs. lbs. Fuel lbs . St. press. lbs. Fuel lbs. St. press. lbs . Gas press. In main. Inches. St. press. ave­rage lbs. Total fuel lbs. IPounds of Hours I fuel per-­1Kilo-Horse-K.W. H . P . watt. power. hour. hour. I a. m. ___ ~o·~.mni. -:: n a. m. 12 m. -----­1 p. m. ___ 2 p. m. --­3 p. m. ___ 4 p. m. ___ Ip, m. --­6 p. m. ___ 900 24 ;~ ~ 1,140 36 570 34 760 35 1,140 35! 950 45 570 s2 1,140 34 950 __..:'. 760 30 1 '.~~ ~~ 1,140 39 760 39 570 400501 41 950 40 760 38 950 40 1,330 ~ 190 27 950 ~:ng ~1 d!8 760 35 1,520 1,140 361 950 950 37 1,330 1,140 371 570 1,330 36 1,140 wo 36 950 570 36 380 760 ~! ~ 29 ~ 36 34 35 35 34 40 36 44 950 ~:J 190 1,140 1,140 1,330 1,140 l,520 190 none 29 1,140 29 ~g 570 ~~ 39 ~~gl 42 43 1,520 40 44 1,520 41 39 760 42 38 5701 40 34 9f>OI 39 36 950 50 37_1,33ol ~ 5.51 ~g 4,940 tgi 29, U~, 7.o 381 5,3201 6.0 37 6,080 5.5 3 38 81 6,27016.5 5,890, 4.5 37 1 6,080'\ 5.01 37 3,190 5.0: 861 4,5101 ~--3_91I 4,750. 1,250 1,675 3.9 2.9 i:ii8 i: :~ !:i U 1,440 1 1,929 3.7 2.S 1,500 2,010 4.0 3.0 1,620 2,170 3.9 2.9 1,560 2,000 3.81 2.s 1,6101 2,157 3 1 .. 8 9 I 2.8 1,710 2,2911 1.4 1,460 1,956 3.11 2.2 1,750 ---=~.:i~l _2~~ n nrs. av . and total 9,500 32 9,690 87 10,450 34 9,880 35 9,120 38 10,450 38 6.0 86 160 ,090 16,330 21,882 3.5 2.7 13 hrs. Total ___ 6,®--­-­-11 ,020 _____ _ 11,59() ______ 8,740 ______ 10,070 ------­-----­------­ -------­-------­ 57,190 15,300 20,502 3.7 2.8 24 hrs.Total ___ 15,580-----­ Hl,380 ______ 21,470 ___ ___ 21,470 ______ 17,860 _____ _ 20,520 _____ _ ---------------­ 116,280 31,630 42,384 3.7 2.8 TABLE II. PRODUCER OPERATIONs-TEXAS J,IGNITE. Producer Number. 1 2 3 5 6 Gas St. Pounds of press . press . Hours fuel per Time. St. St. St. St. st. St. In ave- Total Fuel press. Fuel press. Fuel press. Fuel press. Fuel press. Fuel press. main. rage fuel Kilo- Horse- K.-W. IH. P. lbs. lbs. lbs . lbs. lbs . lbs . lbs . lbs . lbs. lbs. ~~ Inches. 1 ~ ~_'_vatt. _power. hour.~ 8 a. m. ___ 1,520 20 760 25 mo 23 sso 27 760 22 760 2'I 6.5 24 4,750 1,350 1,809 3.5 2.6 9 a. m. · ___ 570 20 760 26 570 20 1,140 25 950 27 950 25 5.5 241 4,940 1,370 1,835 3.6/ 2.7 10 a. m. __ :SSO 21 190 ~ 1,710 20 760 25 380 21 570 26 5.0 23 3,990 1,400 1,876 2.9 2.2 11 a. m. __ 380 22 950 28 1,520 25 950 25 1,330 24 570 30 5.5 26 5,600 1,470 1,969 3.8/ 2.8 12 m. ----­ 760 31 760 39 950 33 1,330 38 950 80 570 86 4.5 3G 5,320I 1,440 1,929 3.71 2.8 1 p . m. ---950 34 1,520 39 1,520 83 1,140 39 960 30 7601 % 6.5 861 6,840! 1,600 2,144 4.S 3.2 2 I). m. ___ 760 25 760 31 1,330 25 1,900 82 950 % !l50 31 5.5 281 6,750 1,790 2,398 3.21 2.4 3 p. m. ___ 190 23 380 29 950 24 570 30 570 23 380 29 6.0 261 3,0401 1,280 1,715 2.41 1.8 4 p. m. ---380 23 380 29 670 24 190 29 190 23 330 29 6.0 261 2,0901 1,550 2,('(17 1.3 1.0 Op. m. ___ 1,140 24 760 30 1,1-10 25 190 30 760 23 760 so 5.5 27. 4,750 1,550 2,077. g.1 2.2 f p. m. ---1,140 23 760 30 190 25 760 29 670 23 ~~ 6.0 __2_7 1' 3,990 _ 1,210 _ 1,621 __.::..: __.::: 11 hrs. av. and t.otal 8,170 24 8,380 SO 11,020 25 9,810 30 8,850 25 7,220 80 5.6 271 51 ,000 16,010 21,458 3.2 2.4 ----__i___________ 18 hrs. Total ---11,000 ------8,290 ------10,590 ------11,780 ______ 11,410 ______ 1S,4!l0 ----------------------166,!i80 19,100 25, 594 3.5 2.G 24hrs. --·-1-:1--­ -ll'otal 19,190 17,670 22,610 21,090 19,760 20,710 ______ --------,--------117,640 35,110 47,047 3.3 2.S 1 Bulletin of the University of Texas The six Harvey producers were used. In Table I the total lig­nite charged was 116,280 pounds, i. e., 59,090 pounds in 11 hours and 57,190 pounds in 13 hours. The rate of charging was 5,190 pounds per hour for the 11-hour period and 4,399 pounds an hour for the 13-hour period. The rate of charging over the entire period of 24 hours was 4,845 pounds an hour. During the 11-hour period, when observations were taken hour­ly, the amount of lignite charged was 59,090 pounds, the average steam pressure (blower) was 36 pounds, the average gas pressure in the main was 6 inches, the total numbcr of kilowatt hours was 16,330 (=21,882 horse-power hours), and there was used 3.6 pounds of lignite per kilowatt hour (=---2.7 pounds per horse­power hour). It will be observed that there was a considerable variation in the number of pounds of fuel per kilowatt hour, from 1.9 to 4.1, but the general average was 3.6 pounds, worth 2.91 mills. Taking the cost of the lignite, delivered, as $1.62 a ton, the cost of the fuel per horse power hour was 2.18 mills. This, of course, is raw fuel cost, and does not )nclude the co!ilt of converting the lignite into gas. In Table II the total lignite charged was 117,640 pounds, i. e., 51,060 pounds in 11 hours and 66,580 pounds in 13 hours. The rate of charging was 4,642 pounds per hour for the 11-hour period and 5,122 pounds an hour for the 13-hour period. The rate of charging for the entire period of 24 hours was 4,902 pounds an hour. During the 11-hour period the total amount of lignite charged was 51,060 pounds, the average steam pres­sure (blower) was 27 pounds, the average gas pressure in the main was 5.6 inches, the total number of kilowatt hours was 16,010 ( 21,453 horse-power hours), and there was used 3.2 pounds of lignite per kilowatt hour (-2.4 pounds per horse­power hour). In this sub-period of 11 hours there was a somewhat greater range in the numbiir of pounds of lignite pe!" kilowatt hour than in Table I, i. e., from 1.3 to 4.3, but the general average was lower, 3.2 as against 3.6. During the entire period covered by these tables, 48 hours, there were used 233,920 pounds (=116.96 tons) of lignite, with a production of 66,740 kilowatt hours (=89,411 horse-power hours) of energy, or a general average of 3.5 pounds of lignite per kilowatt hour (=2.6 pounds per horse-power hour). With Texas Coals and Lignites lignite at $1.62 a ton, delivered, this represents a raw fuel cost of 2.83 mills per kilowatt hour (=2.11 mills per horse-power hour). 'l'ime of so.mp­ling. 8 a. m. --­9 a. m . --­10 a. m. -­11 a. m. -­12 m. 1 p . m. --­2 p . m. --­3 p. m. --­4 !J. m. --­5 p. m . --­6 p . m. --­ Average Gas pressure Inches of wate:. 6.5 6.0 6.5 7.0 6.0 6.5 6.5 4.6 5.0 5.0 7.5 5.91 Load I Kilo-ILignite when watts charged sampled. produced In preced- Kflo-In preced-Ing hour. ing hour.wntts. Pounds. 1,618 1,483 I 6,174 1,300 1,250 4,941) 1,150 1,240 6,130 1,600 1,170 4,750 1,350 1,440 6,320 1,650 1,500 6,080 1,500 1,620 6,270 1,550 1,660 6,890 1,700 1,610 6,080 1,650 1,710 3,100 1,750 1,460 4,510 1,600 i 1,750 - 4,750 - TABLE Ill. PRODUCER OPERATIONS-TO AOOOMPANY TABLE I-COMPOSITION OF GAS, ETO. Pound! of lignite Analysis of Gas. Nitro­gen. 63.4 67.6 58.8 62.1 58.9 64 .6 64.7 61.9 62.4 62.4 62.9 61.9 Heat. Power B. T. U. per ·cubic foot. 106.3 131.8 126.3 113.9 122.9 103.3 109.5 115.4 118.4 129.9 13D.9 119.8 Per K. W. hour. 3.9 4.1 4.1 8.7 4.0 3.9 3.8 S.8 1.9 3.1 2.1 3.5 Per H.P. hour. 2.9 3.1 3.1 2.8 3.0 2.9 2.8 2.8 1.4 2.2 2.0 2.0 - Oarbon dioxide. 8.4 11 .2 11.l 11.l 11.2 11.4 11.0 11.4 11.3 10.8 10.3 10.8 Carbon mon­ oxide. 14.8 16.4 16.8 15.3 16.0 13.8 13.3 14.4 14.0 12.0 11.7 14.8 Methane. .4 3.2 3.2 2.9 3.3 3.0 8.3 3.3 3.7 5.7 6.5 3.5 Ethy-Hydro­ gen.Jene. 2.3 8.9 .8 10.4 .7 8.8 .6 7.6 .5 10.2 .6 6.3 .s 6.3 .6 8.0 I .7 7.7 .6 7.9 .8 7.3 .s 8.1 Oxygen. 1.8 .4 .6 .4 .9 .5 .6 .4 .2 .7 .6 .6 TABL'.E IV. PRODUCER OPERATIONS-TO AOOOMPANY TABLE ll-OOMPOSITION OF GAS, ETO. Time of samp­ling. 8 a. m. --­9 a. m. ___ 10 a. m. __ 11 a. m. __ 12 m. ______ 1 p, m . --­2 p. m. ___ 3 p. m. ___ 4 p. m. ___ 5 p. m. ___ 6 p. m. --­ Average_ Load Kilo-Lignite Pounds of lignite Analysis of Gas. Heat. Gas when watts charged -Power pressure rnmpled. produced in preced-Per Per Oarhon B. T. U. inches of Kilo-inpreced-inghour. K. W. H.P. Oarhon mon-Methane. Ethy-Hydro-Oxygen. Nitro-per cubic water. watts. ing hour. Pounds. hour. hour. dioxide. oxid~. lene. gen. gen. foot. ~1 1,300 l.350"4:750--3.-5----2.-6------w.7 _13:6 _3.4__.-7---S.Z--~~116.0 5.5 1,400 1,370 4,940 3.6 2. 7 9.6 13.8 4.2 .2 8.4 .4 63.4 117.5 5.0 1,350 1,400 3,900 2.9 Z.2 10.6 14.6 4.4 .5 7.7 .5 62.7 124.6 5.5 1,500 1,470 5,600 3.8 2.8 8.2 14. 7 3.4 .1 11.8 1.0 60.8 121.8 4.5 I 1,550 1,440 5,320 3.7 2.8 11.8 1 11.4 4.6 .4 11.4 __________ 60.4 125.6 5.5 1,650 1,600 6,840 4.3 ! S.2 10.8 12.7 4.9 .5 9.4 .6 61.1 130.0 5.5 1,700 1,790 5,750 3.2 :1.4 10.2 11.6 6.1 .4 6.1 .9 64.7 125.3 6.0 1,250 l,~o S,040 I 2.4 1.8 10.2 8.2 7.6 .6 3.6 .6 69.2 131.0 6.0 1,500 1,550 2,090 1.3 1.0 10.1 9.3 7.5 .3 6.3 .9 65.6 131.0 1 5.s 1,600 1,550 4,750 I z.1 2.2 11.0 11.1 5.3 .8 10.5 .8 59.9 138.o -~~~1~1--3._3_ 2.5 10.6 17.6 2.8 .6 12.8 55.6 137.2 5.6 1,464 l,<56 4,642 S.2 2.4 10.3 12.6 4.8 .4 8.7 .50 62.4 127.1 1 Bulletin of the University of Texas From Table I it will be seen that the consumption of lignite was 116,280 pounds, and from Table III that the average heat units in the gas during this period were 119.8. The heat units in the gas were determined by calculation from the analysis, and were not determined in a calorimeter. The factors used in this calculation were as follows: Carbon monoxide . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 324. Methane . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 1010. Ethylene . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 1.580. Hydrogen . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 324. These factors differ somewhat from those commonly accepted for these substances, but were used at this establishment. The variations in composition were as follows : From. To. Average. Carbon dioxide . . . . . . . . . . . . . . . . . . . 8.4 11.4 10.8 Carbon monoxide . . . . . . . . . . . . . . . . 11.7 16.8 14.3 Methane . . . . . . . . . . . . . . . . . . . . . . . . . 0.4 6.5 3.5 Ethylene . . . . . . . . . . . . . . . . . . . . . . . . . 0.5 2.3 0.8 Hydrogen . . . . . . . . . . . . . . . . . . . . . . . . 6.3 10.4 8.1 Oxygen . . . . . . . . . . . . . . . . . . . . . . . . . . 0.2 1.8 0.6 Nitrogen . . . .. . . . . . . . . . ... . . . . . . . . . 57.6 64.7 61.9 Heat units .......................103.3 139.9 119.9 During the period represented by Table II the consumption of lignite was 117,640 pounds, and the average heat units in the gas were 127.1. The variations in composition were as follows: Fnm. To. Average. Carbon dioxide . . . . . . . . . . . . . . . . . . . 8.2 11.8 10.3 Carbon Inonoxide ................. 8.2 17.6 12.6 Methane . . . . . . . . . . . . . . . . . . . . . . . . . . 2.8 7.6 4.8 Ethylene . . . . . . . . . . . . . . . . . . . . . . . . . 0.1 0.8 0.4 Hydrogen . . . . . . . . . . . . . . . . . . . . . . . . 3.6 12.8 8.7 Oxygen . . . . . . . . . . . . . . . . . . . . . . . . . . 0.0 1.0 0.5 Nitrogen . . . . . . . . . . . . . . . . . . . . . . . . 55.6 69.2 62.4 Heat units .......................116.0 138.0 127.1 There is not a well Inarked difference l1etween these gases and the fact that the average heat units are so close together would in­dicate that the gas, throughout the two periods, was of fairly uni­form quality. The amount of lignite charged per hour varied, for the entire Texas Coals and .Lignites six producers, from 2,090 pounds to 6,840 pounds, the amount so charged depending on the power requirements. There i& no practical difference in th;: heat units during the morning, from 8 to 12, and the afternoon, from 1 to 6 (120.6 and 125.7). The lowest heat units observed, 103.3, were at 1 p. m., when during the preceding hour, i. e., :from 12 to 1, there had been charged 6,270 pounds of lignite. The highest heat units ob­lilerved, 139.9, were at 6 p. m., when during the preceding hour, i. e., from 5 to 6, there had been charged 4,750 pounds of lignite. There was one time, 4 p. m., when the heat units were 131.0, with a charge of 2,090 pounds of lignite during the preceding hour. The producers, being of the pressure type. require to be blown with live steam at a pressure proportionate to the load. In this plant the steam is furnished by two horizontal fire tube boilers, crude oil fired, which also furnish steam at about 140 pounds for two ll-ir compressors; two oil pumps for furnishing crude oil at about 90 pounds pressure to the kilns; a city water pump; a battery of underwriters fire pumps; an exciter for use in starting and when it becomes nec­essary to shut off the producers; and the necessary boiler feed pumps. It would be impossible, from the data at hand, to ap­portion the fuel costs to the various d0partments using steam, although it is undoubtedly true that the six producers use more steam than the remainder of the equipment combined. The pressure on the producers has been observed to vary from a minimum of 19 pounds to a maximum of 46 pounds, a general average probably being close to 36 pounds. It is stated.thnt as much as 55 pounds has been carried, although at danger of blow­ing the various water seals in the line. About 60 barrels of crude oil are used under the boilers in twenty-four hours, and it is to avoid a large pa.rt of this expense that the c·hange to natural gas is being made. The amount of tar made is considerable, and the quality seems good. No definite figures are obtainable as to the quan­tity of this tar, but it is understood that at various times meas­urements have been made. Attempts have been made to utilize this product under the boilers, but without any noticeable suc­cess, and at present it is hauled away with the ash, at times being tlsed to surface roads. The arrangement of storage tanks 7-T. C. Bulletin of the University of Texas is such that it could readily be stored and barreled at a small cost. 'l'he waste water from coolers and scrubbers is allowed to flow away in open ditches, after first passing a trap designed +o catch such tar as is suspended in it. At times the supply of water for these purposes is rather scanty, a. further factor in the change to natural gas. The producers are arranged in three sets of two each, and there are but three coolers, three washers and two dry scrub­bers, in which excelsior is used, being changed every two months. Fires are cleaned regularly every other day on normal operation, although cases have been observed when all six were cleaned the same day. The system observed is to clean one producer of each set every day. This, however1 means that the set-that is, the two producers-are not operating at all satisfactorily while cleaning is going on. In general it has been shown to be best to lighten the load about four hours in the morning, and even then, back-firing, due to high hydrogen in the gas, is more frequent than at other times. The shifts change at 6 a. m. and the two ash men immediately start cleaning. The rule, when operating at full load, is one man to a producer, and while cleaning it is customary for four men to work on top of the producer that is being cleaned, leav­ing to the other two the firing of the remaining producers. It is in the necessity of poking these producers through the top that the great loss of gas occnrs, and it is not to be questioned that this loss is appreciable. On a still day it is almost impos­sible to remain long immediately over the producer, and the men are allowed breathing spells at the edge of the charging floor. The fuel is handled from the cars to overhead storage bins of about 300 tons capacity by a clam shell coal crane, and from the bins by four spouts to the charging floor between the two sets of producers. From the floor it is shoveled into the boppers, as before stated, by one man to a producer per shift. These men are Italians and negroes. They receive 20 cents an hour. In general, it may be said that though not clearly shown in the Tables given, the charging is heavier and more variable in the morning, while cleaning, and that beginning about noon, it becomes more regular and not so frequent. The fuel con­sumption has been observed to be less in a 13-hour run than in an 11-hour run, though the power output is greater. This, of Texas Coals and Lignites course, is due to the ''settling'' of the producers and the greater steadiness of operation. Similarly the gas is more apt to vary within wide ranges in the morning, to average low, and to ca.rry more hydrogen, while in the afternoon and night it is of more uniform quality, higher in heating power and lower in hydro­gen. Consequently, the fuel consumption per kilowatt hour during the night was generally lower than during the day, al­though this was not invariably the rule. GAINESVILLE.• Gainesville Electric Company. Equipment: One 150 horse-power Smith suction down-draft producer. One Nash three-cylinder vertical gas engine rated at 150 horse-power, but developing 135 horse-power. The engine is direct connected to a General Electric direct current gen­erator at 250 volts, 400 amperes, 250 r. p. m. This unit operates 24 hours a day for about two weeks and is then out half a day, Sunday. It is not of sufficient capacity to handle the night load, and is helped, for about four hours, by the steam plant. The engines operated by steam are: One Atlas cycloidal four-valve tandem compound; one Ball slide-valve and one Har­risburg four-valve. These engines are belted to five General Electric generators. The Ball engine iEt most frequently used and is belted to two D. C. generators, each of 360 amperes ca­pacity, at 125 volts. Fires are kept banked under two boikrs all the time, Arkan­sas slack coal being used, with a supply of ail for sudden de­mands. The consumption of coal, under the boilers, averages over 30 pounds per kilowatt hour, which seems abnormally high. The original plant here, as at many of the places visited, was steam. Increasing demands caused the installation of the pro­ducer-plant to use lignite two years age.. The producer-plant was at first used merely as an auxiliary to the steam plant, but it soon showed such economy in fuel that the steam plant is now the auxiliary. The lignite used is from the mines of the Consumers' Lignite Company, at Hoyt, Wood county, and costs $1.95 at the plant. B1tlletin of the University of Texas On normal operations less than five polmds of lignite are used per kilowatt hour. The operating force consists of three men per 24 hours, two of these being on duty from noon until midnight and one from midnight until noon. These men were ,111 employed in the old steam plant and had had no previous experience with pro­ducers. The producer is charged every three hours, and the fire is rodded down at a like interval. The grate is equipped with the air-shaker now supplied with this producer, and is given two or three "licks" every hour. An individual motor drives the elevator for the ashes, and these are drawn at irregular in­tervals. Some large masses of clinker were !loticed and the combustible matter left in the ashes was greater in amount than was observed at some other plants. The temperature of the blast was 140 degrees Fahrenheit, and the hot water was ob­tained both from an exhaust heater and the economizer. An increase of temperature of the blast to 160 degrees Fahrenheit can be readily attained. The scrubb~r is run by an individual motor. No attempt is made to save the tar or ammoniacal liquor. A small gasoline engine drives the blower and compressor, and the compressor may also be driven from the engine shaft. The lignite is screened before going to the producer, with a considerable loss in fine stuff. GARWOOD.• M:r. G. l\i. Jackson operates a pumping plant for irrigation purposes at this place. The equipment consists of one Fair­banks-Morse 200 horse-power suction producer and a FairbaRks­1\forse four-cylinder vertical 200 horse-power gas engine at 250 r. p. m. This engine drives an 18-inch American centrifugal pump through a .12-rope connection. The pump carries a guar­antee of 9,600 gallons a minute on a 42-foot lift. The auxiliary equipment for starting the producer, engine and pump is also of Fairbanks-Morse installation. The initial plant here consisted of a 175 horse-power Corliss mgine, operating from wood-fired boilers. Later, however, the Texas Coals and Lignites wood war; replaced by oil, and later still the steam equipment was changed to producer-gaR. 'l'he fuel cost with oil-fired boil" ers was $60.00 a day, while with producer-gas it rarely exceeds $12.00 a day, a:ad the service is better. The cost of the steam installation, which was second-hand, was $9,500, while the pi·o­ducer plant represents an investment •yf' $22,000. Operation is continuous four months in the year, and at a net saving of daily expenses of $30.00, the total saving during the season would be about $3,600.00. The lignite used is from the Burnet Fuel Company, Milano, Milam c01::nty, and cost,s $2.06 a ton at the works. The consumption of fuel is five tons in twenty-four hours. The producer is charged every two hours, the ash being shaken down just before charging. As usual with this type of producer, the air for gasification re­ceives its moisture from water in the ash-pit. This practice is apt to cause tremble from clinkering, but no serious annoy­ances of this kind have been observed here. The ash appeared to contain more combustible matter than should be allowed, but this might be prevented by admitting more steam with the air. Cooling, scrubbing and jacket water is obtained from a well by a belt-driven pump, the waste water and tar being pumped into the river. The tar is in a very finely divided condition, and there is no difficulty in forcing it through the waste-pipe. While no at­tempt has been made to save this tar, it is understood that of­fers for it are under consideration. No detailed information as to the actual consumption of fuel per brake horse-power was obtainable, but from the above figures s11ry hy the presence, in the cooler and Texas Coals and Lignites scrubber-water, of sufficient ammoniacal compounds to render its discharge into the bayou objectionable. 'l'he entire waste water, including the tarry matter, is firnt forced upward through broken coke which removes the tar, the remaining water being sprayed over six filter beds Before the installa­tion of the coke-columns and the filter beds it is stated that the waste water contained 9.6 grains of free and albuminoid am­ . monia per gallon, whereas now it contains not more than 0.02 grains per gallon. The yield of tar is stated to be about 500 pounds a day. The lignite used now is from the mines of the Houston County Coal & Manufacturing Company, Crockett, Houston county. It is screened throug:h a three-fourths-inch screen and over a three-eighths-inch screen. Analyses, by P. S. Tilson, Houston, of the Crockett lignite, as received, are as follows : 1 2 3 P er cen~. P er cent. Per cent. Moisture ........·.. ..... .. . . 131.45 12.88 28.16 Volatile and Combust. Matter. 30.80 47.57 43.60 Fixed Carbon ... .......... . 25.60 29.40 21.02 Ash .. . . ..... . ... ..... . .... . 12.75 10.15 6.64 Sulphur ... .. . ... .. ....... . . trace trace 0.58 Heating Power< B. 'l'. U.. . . . . 6,410 7,326 No. 1 is lignite screenings, through 3-4-inch and over 3-8-inch screen, charged into the producers. No. 2 is lignite used under boilers in another part of the plant. This shows an evaporation of 3.25 pounds of water, from and at 212 degrees Fahrenheit, per pound of fuel, which is equivalent to 10.6 pounds per boiler horse-power. Analyses of other lignites received at this plant have b~en made by Mr. Tilson as follows: 4 5 6 7 Per ct. Per ct. Per ct. P.ir ct. Moisture ..... . . . . . . . . . .. . . 23.11 27.20 19.42 33.83 Volatile & Combnst. Matter .39.84 41.28 43.12 38.83 Fixed Carbon .... .. ... ... .. 29.39 25.99 29.46 21.90 Ash .... .... .. ....... .. . . .. 6.78 4.89 7.08 4.84 Sulphur . . . . . . . . . . . . . ... . . . . 0.88 0.64 0.92 0.60 Heating Power, B. T. U. .....8,336 ;:;,114 7,695 6,158 Bulletin of the University of Texas 106 No. 4 is lignite from the Bear Grass Coal Company, Jewett, Leon county. No. 5 is lignite from the Bastrop Coal Company, Bastrop county. No. 6 is lignite from the Southwestern Fuel & Manufacturing Company, Calvert, Robertson county. No. 7 is lignite from the Consumers' Lignite Company, Hoyt and .Alba, Wood county. In these analyses the heating power was determined by lead­ button assay. The specifications call for a g_as of 140 B. T. U. per cubic foot, and the engine is to deliver a brake horse-power for each 10,000 effective heat units. No analyses of the gas were obtainable, although it is under­ stood that some were made when the plant was installed anrl tested. The consumption of lignite is stated to be 1.75 pounds per brake horse-power. HUNTSVILLN. Huntsville Electric Light & Power Company. Equipment: One Fairbanks-Morse producer of 100 hors&­power; one Fairbanks-Morse gas engine of 100 horse-power, belted to generator. The service is 24 hours, driving generator and ice machine of 12 tons capacity. The fuel is lignite screenings from the mines of the Houston County Coal & Manufacturing Company at Wooter's Spur, Houston county, and the consumption is 9,645 pounds per 24 hours. The cost of the fuel at the plant is 90 cents a ton. The tar is mixed with lignite screenings and is burned under the boilers. No use is made of the ammoniacal liquor. Leaky valves and stopping-up of pipes, due to poor tar extraction, ha~ given some trouble at this plant. The original installation here was steam, but there is a consid­erable sa.ving in fuel and labor since the introduction of the pro­ducer plant. This establishment was not visited personally, the above data 'having been supplied by the Company. Texas Coals and Lignites KINGSVILLE.• The Kingsville Power Company Equipment: One 100 horse-power Smith suction producer and one 100 horse-power Rathbun-Jones three-cylinder vertical gas engine. The producer is said to be of insufficient capacity to operate the engine at full load. The engine is belted to a Western Electric Company's alternator for supplying lighting current at night, being idle during the day. No records were obtainable concerning fuel consumption or power delivered, but from 1,800 to 2,000 pounds of lignite are used every night, the fuel coming from the mines of the Con­sumers' Lignite Company, Hoyt, Wood County. The exhaust from the engine is lead through a water-heater for supplying water-vapor to the saturator. The temperature of the blast varies from 140 degrees to 170 degrees Fahrenheit. The ash-pit of this producer is generally kept full of water to within a few inches of the grate to "settle the ashes." No coal is charged during the day, but the proc1ucer is filled when the engine is shut down in the morning and the ashes thoroughly drawn and new coal charged when the blower is started in the evening. From the time of starting the blower twenty minutes are gen­erally sufficient for securing good gas at the engine. In order to obtain additional power for use in a new cotton­seed oil mill there has recently been installed a 350 horse-power De La Vergne twin oil engine for using crude oil. The guaran­tee of this engine is a brake horse-power from 0.6 pound of oil. This engine has not been operated on full load, but tests have shown an efficiency a little higher than the guarantee. No attempt is made to recover the tar or ammoniacal liquor, nor is the tar burned under boilers in the ice plant belonging to the same Company. LEONARD.• Leonard Ice & Light Company. This plant has not been in operation for a year or more. The equipment consistsed of a 65 horse-power Fairbanks-Morse suc­tion up-draft producer and a Fairbanks-Morse single cylinder B11lletin of the University of Texas horizontal gas engine rated at 50 horse-pawer. The plant was in operation. but not continuously, for about two years. The fuel used was screened-lump lignite from the mines of the Consumers ' Lignite Company, Hoyt and Alba, Wood County, and cost $1.34 a ton, delivered. The Company changed hands and the producer power plant was turned over to the manufacturer. Since that till).e it has been dismantled and removed. The plant is now operated. by steam, lignite being used under the boilers. LONGVIEW. A Westinghouse producer and engine plant was installed here, to operate on lignite, but for some reason or other it was removed and no records concerning it are available. McNEIL ... A.. ustin ll'hite Lime Company. At this place there are two No. 101/2 R. D. Wood & Com­pany's producers, used for making fuel gas for burning lime. They have been working on washed nut coal from the Olmos Coal Company, Eagle Pass, Maverick county. Samples of this coal taken in person gave the following analysis: OLMOS W"\SHED NUT COAL. Per cent, Moisture . . . . . . . . . . . . . . . . . . . .. . . . . . . . . . . . . . . . . . . . . 4.20 Volatile and Combustible Matter. . . . . . . . . . . . . . . . . . . . 36.55 Fixed Carbon . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 32.35 Ash . . . . . . . . . . . . . . . . . . . . . . . . . . . . . ... . . . . . . . . . . . . . 26.90 Sulphur . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 0.71 Heating Power. B. T. U .... . ..... ... . . .. . ... . . ... . 9,772 Under the boilers this plant was using lignite (hand-fired) from the mines of the Rockdale Consolidated Coal Company, Rockdale, ::VIilam County. It was sampled in person and had the following composition : Texas Coals and Lignites LIGNITE FROM ROCKDALE CONSOLIDATED COAL COMPANY. Per cent. Moisture . . . . . . . . . . . . . . ... . . . . . . . . . . . . . . . . . . . . . . . . 12.62 Volatile and Combustible Matter. . . . . . . . . . . . . . . . . . . 38.11 Fixed Carbon . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. . . . 36.21 Ash . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . ... . . . . . . . . . . 13.06 Sulphur . . . . . . . . . . . . . . . . ... . ... . . . . . . . . . . . . . . . . . . . 0.48 Heating Power, B. T. U.... . . ... ... ..... .. ...... . . 9,525 The gas is passed directly into the kilns, through ordinary gas-ports, where it is mixed with air for combustion. No at­tempt is made to separate tar or ammoniacal compounds. For many years this establishment used wood for burning the white lime for which it has long been famous. On entering upon the manufacture of hydrated lime, the produc·ers were installed and have been in fairly continuous operation for a year or more. As is also the case with the Round Rock White Lime Company, a few miles away, there has not been much success at McNeil in using producer-gas for burning lime. The chief difficulty has been in controlling the quality of the gas. MART. Home Light & Power Company. Operator, Bayliss Earle, Waco. This plant is not in operation, and was not visited, but Mr. Earle gave the following details: The equipment consists of one 100 horse-power Fairbanks­Morse suction up-draft producer and one two-cylinder vertical gas engine of the same make, rated at 100 horse-power. During the cotton-ginning season this plant operates steadily at full load, with a fuel consumption of about 4,400 pounds of lignite from the mines of the Southwestern Fuel & Manufactur­ing Company, Calvert, Robertson county. It rarely operates except during the ginning season, but is held in reserve as an auxiliary to a steam-driven generator which is a part of an ice-plant. The gvs engine was the orig­inal installation, but the addition of the ice-plant made steam Biilletin of the University of Texas necessary, and it was not found economical to continue the gas­unit in continuous operation. The lignite which is used in the producer and under the boil­ers costs $1.55 a ton, delivered. Abaut a barrel of tar a day is produced when the gas-unit is in operation, and is used for tarring the butts and the cross-arms of poles used by the Com­pany. No attempt is made to save the ammoniacal liquor. MINEOLA."' Mineola Light & Ice Company. Equipment: One Smith suction down-draft producer of 100 horse-power, one Rathbun-Jones three-cylinder vertical gas en­gine rated to develop 90 brake horse-power on 80 cubic feet of gas of 135 B. T. U. per cubic foot, at 700 feet elevation. The engine drives a line shaft for two generators. The gas unit operates about 13 hours every night during the winter months and about 11 hours during the summer months. The winter load is greater than the summer load; and the con­sumption of fuel is correspondingly higher. Lignite screenings are used, 2,000 pounds a day in winter and 1,400 pounds in summer. Two boilers; of 80 and 50 horse-power, are used for the ice machines and for driving a 25 kilowatt Curtis horizontal tur­bine for the day load. These boilers are rarely operated at rated capacity, the average load seldom being over 110 horse­power. The fuel used under the boilers is the same as is used in the producer, lignite screenings, yet the consumption is about four times as great. In the original plant here, which was operated about seven years, there was an Ideal automatic engine. The producer­plant has been in operation three years, and has shown a net saving of $500 a year. It represents an investment of about $13,000. The lignite screenings, used in the producer, come from the mines of the Consumers' Lignite Company, Hoyt and Alba, Wood County. This fuel costs 90 cents a ton, delivered. Screened lump, which may be used, would cost $1.40, delivered. The producer is of an old type, the fire-containing body resting Texas Coals and Lignites directly upon the foundation and the a'.lhes falling into a pit from which they are drawn with long-handled shovels. The three charging holes in the top of the producer are absent and the fuel is fed directly inside the ring at the top, instead of