US191883A - Improvement in processes for the manufacture of gas - Google Patents
Improvement in processes for the manufacture of gas Download PDFInfo
- Publication number
- US191883A US191883A US191883DA US191883A US 191883 A US191883 A US 191883A US 191883D A US191883D A US 191883DA US 191883 A US191883 A US 191883A
- Authority
- US
- United States
- Prior art keywords
- gas
- coal
- copper
- carbon
- volume
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- 238000004519 manufacturing process Methods 0.000 title description 10
- 238000000034 method Methods 0.000 title description 10
- 239000007789 gas Substances 0.000 description 82
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 38
- 229910052799 carbon Inorganic materials 0.000 description 28
- 150000002430 hydrocarbons Chemical class 0.000 description 26
- RYGMFSIKBFXOCR-UHFFFAOYSA-N copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 24
- 229910052802 copper Inorganic materials 0.000 description 24
- 239000010949 copper Substances 0.000 description 24
- 239000003034 coal gas Substances 0.000 description 22
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 18
- VGGSQFUCUMXWEO-UHFFFAOYSA-N ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 14
- 125000000383 tetramethylene group Chemical group [H]C([H])([*:1])C([H])([H])C([H])([H])C([H])([H])[*:2] 0.000 description 14
- 239000004215 Carbon black (E152) Substances 0.000 description 12
- 239000003245 coal Substances 0.000 description 10
- 125000002534 ethynyl group Chemical group [H]C#C* 0.000 description 10
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 10
- 239000007787 solid Substances 0.000 description 10
- 125000004429 atoms Chemical group 0.000 description 8
- 239000001257 hydrogen Substances 0.000 description 8
- 229910052739 hydrogen Inorganic materials 0.000 description 8
- 239000007788 liquid Substances 0.000 description 8
- 239000000126 substance Substances 0.000 description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 8
- UHOVQNZJYSORNB-UHFFFAOYSA-N benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 6
- UFHFLCQGNIYNRP-UHFFFAOYSA-N hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 6
- 229910052742 iron Inorganic materials 0.000 description 6
- 240000005020 Acaciella glauca Species 0.000 description 4
- 229910000881 Cu alloy Inorganic materials 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 238000010438 heat treatment Methods 0.000 description 4
- 235000003499 redwood Nutrition 0.000 description 4
- 238000000926 separation method Methods 0.000 description 4
- BKOOMYPCSUNDGP-UHFFFAOYSA-N 2-Methyl-2-butene Chemical group CC=C(C)C BKOOMYPCSUNDGP-UHFFFAOYSA-N 0.000 description 2
- 235000007575 Calluna vulgaris Nutrition 0.000 description 2
- BVKZGUZCCUSVTD-UHFFFAOYSA-N Carbonic acid Chemical compound OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 description 2
- 241000353097 Molva molva Species 0.000 description 2
- 239000005864 Sulphur Substances 0.000 description 2
- 230000003416 augmentation Effects 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 230000003197 catalytic Effects 0.000 description 2
- 239000004927 clay Substances 0.000 description 2
- 229910052570 clay Inorganic materials 0.000 description 2
- 239000000571 coke Substances 0.000 description 2
- 239000004020 conductor Substances 0.000 description 2
- 238000009792 diffusion process Methods 0.000 description 2
- 230000003292 diminished Effects 0.000 description 2
- 230000003467 diminishing Effects 0.000 description 2
- 238000004821 distillation Methods 0.000 description 2
- 150000002431 hydrogen Chemical class 0.000 description 2
- MHAJPDPJQMAIIY-UHFFFAOYSA-N hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- NINIDFKCEFEMDL-UHFFFAOYSA-N sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 2
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
Definitions
- This invention has for its object to improve the quality and increase the quantity of gas obtained by distilling coal in retorts,-
- the converting-retort should be heated externally by a fire, by which it can be kept at a cherry-red heat, and the gas, after passing through the converter, should be conveyed to v the condensers and purifiers through a pipe of ample size, so that it may pass off freely without back pressure.
- the gas may be carried not only through the hydraulic main, but also through the condensers, before it passes to the converter; but in this or any case in which most of the aqueous vapor as well as tar would be separated from the gas before it reaches the converter, w it will bedesirable to introduce water, or the vapor of water, with the gas into the converter, which may be done in any convenient way, to the extent of about a pint of water, or an equivalent quantity of steam, for every thousand cubic feet of gas.
- the volumes of all molecules in the gaseous or vaporous state are the same-that is to say, the quantities of matter represented by the fOlmultB CH4, 02H. 0282, 051136,
- the advantagegained by the use of copper as the heated surface to which crude coal-gas may be exposed, and by which the volume of the gas may be increased without diminishing its illuminating power, arises principally from this, that the gas can be exposed to red-hot copper without any carbon being separated from it, whereas, in contact with iron or other metal, although the volume of the gas would be increased, its illuminatin g power wouid be diminished, carbon being deposited in the solid form.
- the advantage arising from the use of copper therefore, does not consist, merely or principally, in its being a good conductor of heat, and thus afl'ordin g the means of conveying the requisite heat to the crude gas to convert the hydrocarbon vapors into fixed or permanent gases but it consists in a peculiar catalytic action which :the heated copper exerts in causing some of the liquids or other hydrocarbons contained in crude coal-gas to split up into gaseous hydrocarbons, the molecules of which contain a smaller number of atoms than do those from which they are produced, so that the volume of the gas is increased, while at the same time the copper, at the temperature required to produce the foregoing effect, causes no material deposition of carbon from any of the hydrocarbons present. It therefore causes an increase of volume without any diminution of illuminating power.
- V 1 The hereinbefore-deseribed process of :manufacturing coal-gas, which consists in distilling coal and leading the gas so obtained,
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Solid Fuels And Fuel-Associated Substances (AREA)
Description
UNITED S'rA'rEs PATENT Orrren.
THOMAS BOVERTON REDWOOD, OF FAIRLAlVN, .FINCHLEY, ENGLAND.
IMPROVEMENT IN PROCESSES FOR THE MANUFACTURE OF GA S.
Specification forming part of Letters Patent No. 191.883, dated June 12, 1877; application filed August 28, 1876; patented in England, June 23, 1876, for 14 years.
To all whom it may concern:
Be it known that I, THOMAS BOVERTON REDWOOD, of Fairlawn, Finchley, in the county of Middlesex, England, have invented new and useful Improvements in the Manufacture of Gas for Burning, which improvements are fully set forth in the following specification.
This invention has for its object to improve the quality and increase the quantity of gas obtained by distilling coal in retorts,-
as now usual. For this purpose I cause the gas, as it issues from a retort, or while it contains a portion, at least, of the condensible 1 vapor which is. generated,together with thegas, to come into contact with heated copper oralloy of copper, so arranged as to expose a large extent of surface to the gas. I prefer to pass the gas immediately, as it issues from the hydraulic main, through a heated retort packed full of copper tubessay of an inch diameter-so that an extended heated surface may be exposed to the gas without Inatime improved, as will hereinafter fully be explained.'
The converting-retort should be heated externally by a fire, by which it can be kept at a cherry-red heat, and the gas, after passing through the converter, should be conveyed to v the condensers and purifiers through a pipe of ample size, so that it may pass off freely without back pressure.
In cases where it may be desired to get a larger quantity of tar than would be produced by operating in the foregoing way, the gas may be carried not only through the hydraulic main, but also through the condensers, before it passes to the converter; but in this or any case in which most of the aqueous vapor as well as tar would be separated from the gas before it reaches the converter, w it will bedesirable to introduce water, or the vapor of water, with the gas into the converter, which may be done in any convenient way, to the extent of about a pint of water, or an equivalent quantity of steam, for every thousand cubic feet of gas.
When the coal employed in the process yields a gas of very high illuminating power,
permanent gases, including olefiant gas, (0 B butylene, (0,1 1,) and acetylene, (0 kb,) marshgas, (0H,.) It also contains other hydrocarbons which,at common temperatures, exist as liquids, but the vapors of which remain in a state of diffusion in the gas to a slight extent at common temperatures, and to a greater extent when hot. Among these liquid bydrocarbons is am ylene, (O H,) and other homologous bodies, as well as benzole((J lH and its homologies. Second, the light-giving properties of these I hydrocarbons, and of the coal-gas containing them, depend mainly upon the proportion of carbon contained in a given volume of the gas or vapor when burned as a source of light. Thus, among the permanent gases, marsh-gas, which contains the smallest proportion of carbon, gives, in burning, the smallest amount of light, while butylene and acetylene burn with a highly luminous flame. The presence of too much carbon, however, is objectionable in a gas to be used for burning as a source of light, because it gives a smoky flame, and on this account oletiant gas, bntylene, and acetylene could not be burned alone,
and are valuable only for the purpose of en I riching or increasing the light-giving properties of poor gases, such as marsh-gas, hydrogen, and carbonic oxide.
Third, the chemical formulae appending to the foregoing hydrocarbons represent in each case a molecule of the substances, such molecules consisting, in most cases, of several atoms of each of the elements presentnamely, carbon (C) and hydrogen (H)--the figures attached to the letters in the formulae indicating the numbers of the atoms of those elements.
Fourth, the volumes of all molecules in the gaseous or vaporous state are the same-that is to say, the quantities of matter represented by the fOlmultB CH4, 02H. 0282, 051136,
U H which are the formulae, respectively,
of marsh-gas, olefiant gas, butylene, acetylene, amylene, and benzole, when existing inthe state of gas or vapor, occupy the same space and as the carbon and h yd rogen are present in the same proportion in olefiant gas and butylene, the only diiference being that the molecule of butylene contains twice as many atoms or twice as much matter as the molecule of olefiant gas, it follows, as a necessary consequence, that if, by any means, the molecules of butylene could be split in two, one volume of the butylene would thus make two volumes of olefiant gas. So, also, if a molecule of benzole could be split into three, it might be converted into three times its volume of the valuable light-giving gas, acetylene, a minute quantity of which is usually present in coal-gas.
Fifth, by the application of heat to hydrocarbon gases and vapors a splitting up of the molecules in various ways may be effected, and the vapors of liquid hydrocarbon may thus be converted into permanent gases. The permanent hydrocarbon gases may also be broken up in the same way, and usually are broken up when subjected to a high temperature. It is thus, as is well-known, that ordinary coal gas may be increased in volume by exposing it to a strong heat; but, so far as my knowledge extends, in all attempts heretofore made to increase the volume of coalgas in this way, the light-giving properties of the gas have been destroyed or greatly injured, so as to render the method valueless to gas-makers. This has arisen from the fact that the two principal hydrocarbon gases contained in coal-gas namely, marsh-gas and olefiant gaswhen heated by bringing them into contact with most solid substances, at a red heat, are decomposed, olefiant gas being split into marsh-gas and solid carbon, which latter is deposited, and marsh-gas being split up into hydrogen and solid carbon, this latter change being attended by a doubling of the volume of gas.
No method of which I am aware has heretofore been proposed by which a splitting up 1 of the more complex hydrocarbon molecules,
and consequent augmentation of volume, can be effected without more than counterbalancin g the value of such effect by the destruction of other light-giving hydrocarbons and the depor sition of solid carbon from the gas. Hitherto attempts in this direction have been made by heating the gas in contact with iron, clay, or coke; and it is known that, in contact with these substances at ared heat, marsh-gas and olefiant gas are decomposed; hence the failures of such attempts.
Now, the advantagegained by the use of copper as the heated surface to which crude coal-gas may be exposed, and by which the volume of the gas may be increased without diminishing its illuminating power, arises principally from this, that the gas can be exposed to red-hot copper without any carbon being separated from it, whereas, in contact with iron or other metal, although the volume of the gas would be increased, its illuminatin g power wouid be diminished, carbon being deposited in the solid form. The advantage arising from the use of copper, therefore, does not consist, merely or principally, in its being a good conductor of heat, and thus afl'ordin g the means of conveying the requisite heat to the crude gas to convert the hydrocarbon vapors into fixed or permanent gases but it consists in a peculiar catalytic action which :the heated copper exerts in causing some of the liquids or other hydrocarbons contained in crude coal-gas to split up into gaseous hydrocarbons, the molecules of which contain a smaller number of atoms than do those from which they are produced, so that the volume of the gas is increased, while at the same time the copper, at the temperature required to produce the foregoing effect, causes no material deposition of carbon from any of the hydrocarbons present. It therefore causes an increase of volume without any diminution of illuminating power.
I The advantage gained by the use .of copper applied in the manner specified for effecting the separation of sulphur from coal-gas is "due to the fact that by heating crude coal-gas which contains bisulphide of carbon, as well as the vapor of water, the former is converted into sulphureted hydrogen and carbonic acid- ,thus OS2+2H20 H2S+OO2- I That this reaction takes place is well known but it has not hitherto been made available for facilitating the separation of bisulphide of carbon from coal-gas, because no method has ,been known by which the gas could be heated to the required extent without causing a deposition of carbon, and by that means injuring the illuminating power of the gas. In contact with red-hot copper, this change, as well as the other changes referred to, may be easily efl'eeted, and the sulphureted hydrogen =produced, together with that originally present in the gas, is easily removed by means of ;an oxidc-of-iron purifier.
\Vhat I claim is V 1. The hereinbefore-deseribed process of :manufacturing coal-gas, which consists in distilling coal and leading the gas so obtained,
with vapors generated with it, into contact with copper or an alloy of copper, kept in a highly-heated state,and arranged so as to expose a large extent of surface, substantially as set forth.
2. The hereiubeforedescribed process of manufacturing gas, which consists in distiL- ling coal, passing a stream of water-gas through the retorts during the distillation of the coal therein, and leading the combined products into contact with copper or an alloy of copper, kept in a highly-heated state, and
arranged so as to expose a large extent of surface, substantiallyas described.
'1. BOVERTON REDWOOD. Witnesses:
J. DEAN, T. J. OSMAN, Both of No. 17 GraceohurckStreetfllondon.
Publications (1)
Publication Number | Publication Date |
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US191883A true US191883A (en) | 1877-06-12 |
Family
ID=2261290
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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US191883D Expired - Lifetime US191883A (en) | Improvement in processes for the manufacture of gas |
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US (1) | US191883A (en) |
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- US US191883D patent/US191883A/en not_active Expired - Lifetime
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