US176610A - Improvement in processes of manufacturing illuminating-gas - Google Patents
Improvement in processes of manufacturing illuminating-gas Download PDFInfo
- Publication number
- US176610A US176610A US176610DA US176610A US 176610 A US176610 A US 176610A US 176610D A US176610D A US 176610DA US 176610 A US176610 A US 176610A
- Authority
- US
- United States
- Prior art keywords
- gas
- coal
- wood
- retorts
- retort
- 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
- 238000000034 method Methods 0.000 title description 8
- 238000004519 manufacturing process Methods 0.000 title description 5
- 239000007789 gas Substances 0.000 description 26
- 239000003245 coal Substances 0.000 description 20
- 239000002023 wood Substances 0.000 description 18
- 229930195733 hydrocarbon Natural products 0.000 description 13
- 150000002430 hydrocarbons Chemical class 0.000 description 13
- 239000004215 Carbon black (E152) Substances 0.000 description 8
- 239000003034 coal gas Substances 0.000 description 6
- 230000005484 gravity Effects 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 239000000571 coke Substances 0.000 description 2
- 238000004821 distillation Methods 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 230000001105 regulatory effect Effects 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- UFWIBTONFRDIAS-UHFFFAOYSA-N Naphthalene Chemical compound C1=CC=CC2=CC=CC=C21 UFWIBTONFRDIAS-UHFFFAOYSA-N 0.000 description 1
- 241000183024 Populus tremula Species 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000007865 diluting Methods 0.000 description 1
- 239000003085 diluting agent Substances 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- VKYKSIONXSXAKP-UHFFFAOYSA-N hexamethylenetetramine Chemical compound C1N(C2)CN3CN1CN2C3 VKYKSIONXSXAKP-UHFFFAOYSA-N 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 238000005201 scrubbing Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
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
- either the lower or middle retort may be used for the hydrocarbons.
- FREDERICK H EIGHBAUM, OF DETROIT, MICHIGAN.
- any suitable bench of retorts preferably such as are described in my Letters Patent, numbered respectively 164,022 and 1 68,006, and in my application for Letters Patent filed February 8, 1876, and furnished with an apparatus for supplying liquid hydrocarbons, substantially such as described in my Letters Patent numbered 165,800, and where a bench of three retorts, set 'triangularly, is used, I place wood in one of the lower retorts, and coal in the other lower retort, and admit hydrocarbon in a liquid form into the upper Where such retorts are set vertically,
- the retorts are charged with coal in the usual way, and With wood as described in my said Letters Patent and application, and the gas distilled both from the wood and coal pass up into the upper retort, which preferably should have an inclosed retort into which the fluid hydrocarbon is introduced, but the same may be omitted, and the hydroearbonmay be admitted directly into the upper retort in a solid form or in a liquid or vaporized form, as may be preferred. It will be observed, however, that I prefer to subject the coal to an exhaustive distillation, for the purpose of enhancing the production of coal-gas, the quantity of which may be increased nearly twenty-five per cent.
- the volume of the same which is great and of small specific gravity, uniting and combining, overtakes and carries along the gas produced from the hydrocarbons, which is comparatively small in volume but of greater specific gravity than the other gases named, and, at the same time, the three gases, uniting, form a single homogeneous fixed illuminating-gas.
- the retorts being.
- the volume or proportion of wood-gas will be greater than that of coalgas, but, as the wood-gasis a perfect diluent both for coal and hydrocarbon gases, the wood-gases will mingle freely and unite with y the other gases without waste or deposit from either of them and the gas which would resalt from the coal and wood alone, being deficientin illun-iinating power, can be sufliciently enriched by the hydrocarbon gas to any desired degree by regulating the flow of the hydrocarbon into its proper retort, or by regulating the charge of solid hydrocarbons in such retort. It is apparent, however, that in constructing benches of retorts espe'cially for the use of this process, 'the sizes of the retorts designed respectively for wood or coal may be changed to suit convenience.
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Description
v UNITED TATES PATENT GFFIGE.
' retort.
either the lower or middle retort may be used for the hydrocarbons.
FREDERICK H. EIGHBAUM, OF DETROIT, MICHIGAN.
IMPROVEMENT m PROCESSES OF MANUFACTURING ILLUMlNATlNG-GAS.
Specification formin g part of Letters Patent No. 176,610, dated'April 25, 1876; application filed March 22, 1876.
same bench. of retorts, at the same time, andfrom the combination of the three gases, producing a fixed or permanent illuminatinggas of a certain desired candle-power.
In order that those skilled in the art may know how to use my process, I now proceed to describe the same.
Itake any suitable bench of retorts, preferably such as are described in my Letters Patent, numbered respectively 164,022 and 1 68,006, and in my application for Letters Patent filed February 8, 1876, and furnished with an apparatus for supplying liquid hydrocarbons, substantially such as described in my Letters Patent numbered 165,800, and where a bench of three retorts, set 'triangularly, is used, I place wood in one of the lower retorts, and coal in the other lower retort, and admit hydrocarbon in a liquid form into the upper Where such retorts are set vertically,
for wood or for coal, as may be preferred, but the upper one in'all instances must be used Where benches of five retorts are used, or six, in like manner, the lower retorts are used for coal or wood, and the upper ones, where six retorts are used, or the single upper one in a bench of fives, are used for the fluid hydrocarbons. It is a matter of convenience whether the wood shall be used in the retorts upon one side of the bench, and the coal in the retorts on the other side of the bench, or wood and coal are used alternately in the two lower retorts on each side, or wood and coal used in the same retort. The retorts are charged with coal in the usual way, and With wood as described in my said Letters Patent and application, and the gas distilled both from the wood and coal pass up into the upper retort, which preferably should have an inclosed retort into which the fluid hydrocarbon is introduced, but the same may be omitted, and the hydroearbonmay be admitted directly into the upper retort in a solid form or in a liquid or vaporized form, as may be preferred. It will be observed, however, that I prefer to subject the coal to an exhaustive distillation, for the purpose of enhancing the production of coal-gas, the quantity of which may be increased nearly twenty-five per cent. over that ordinarily obtained in gas-works, while its illuminating power is correspondingly reduced and its specific gravity lessened. It will also be found best in practice, where wood and coal are used in the same retort, to place the wood in the back end of the retort and the coal in the front end. The wood being in the hottest part of the retort and the coal in the coolest part, it follows that there is a rapid distillation of wood-gas, which flows to thefront of the retort, overtaking the vaporous gases of the coal, diluting and carrying the same along intothe mixing retort and there uniting and combining with the same, and both gases overtaking, absorbing, and uniting with the hydrocarbon gas.
As the gas produced from the coal and from the wood meet in the common upper retort, the volume of the same, which is great and of small specific gravity, uniting and combining, overtakes and carries along the gas produced from the hydrocarbons, which is comparatively small in volume but of greater specific gravity than the other gases named, and, at the same time, the three gases, uniting, form a single homogeneous fixed illuminating-gas. In the use of this process in benches already constructed, it will be obvious that the retorts, being. of the same size, and wood being more rapidly converted into gas than coal, and producing a much larger proportion of gas, the volume or proportion of wood-gas will be greater than that of coalgas, but, as the wood-gasis a perfect diluent both for coal and hydrocarbon gases, the wood-gases will mingle freely and unite with y the other gases without waste or deposit from either of them and the gas which would resalt from the coal and wood alone, being deficientin illun-iinating power, can be sufliciently enriched by the hydrocarbon gas to any desired degree by regulating the flow of the hydrocarbon into its proper retort, or by regulating the charge of solid hydrocarbons in such retort. It is apparent, however, that in constructing benches of retorts espe'cially for the use of this process, 'the sizes of the retorts designed respectively for wood or coal may be changed to suit convenience.
In the process described, the principal advantage will be found in convenience of application to benches of retorts now used for making coal-gas without any expensive change of construction in the economy of manufacture, since all the gases in the coal are extracted and the whole of the spent coke thus produced may be utilized for heating the benches, (for which it is quite suitable, although not tit for many of the purposes for which ordinary coke is used,) instead of becoming a nuisance, difficult of sale, and littering up the premises, as now, in gas-works; in the saving of expense in scrubbing or purifying, as this gas will be found to require less of either than coal-gas; and in the cleanness of the pipes, as this gas will remove all deposit and keep the pipes constantly free from naphthaline and other deposit. I do not pretend'that it is as cheap as the mode of manufacturing described in my application of Feb ruary 8, 1876, by which poor coal-gas is enriched by the addition of a very rich wood and hydrocarbon gas, or the mode described in my patents before referred to for making wood and hydrocarbon illuminating-gas, but
it will be found convenient of use, more economical than the coal-gas now made, and very convenient and economical where wood is expensive, and petroleum, or its products, are cheap, or where coal is cheap, but needs, in gas-making, an enriching-gas in order to meet public demands.
Having thus described my process, what I claim therein as new, and my invention, is-
The process, substantially as described, of I
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US176610A true US176610A (en) | 1876-04-25 |
Family
ID=2246017
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US176610D Expired - Lifetime US176610A (en) | Improvement in processes of manufacturing illuminating-gas |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US176610A (en) |
-
0
- US US176610D patent/US176610A/en not_active Expired - Lifetime
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