US100432A - Improvement in the manufacture of illuminating-gas from coal and other materials - Google Patents
Improvement in the manufacture of illuminating-gas from coal and other materials Download PDFInfo
- Publication number
- US100432A US100432A US100432DA US100432A US 100432 A US100432 A US 100432A US 100432D A US100432D A US 100432DA US 100432 A US100432 A US 100432A
- Authority
- US
- United States
- Prior art keywords
- coal
- gas
- illuminating
- improvement
- manufacture
- 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
- 239000003245 coal Substances 0.000 title description 17
- 238000004519 manufacturing process Methods 0.000 title description 2
- 239000000463 material Substances 0.000 title 1
- 150000001875 compounds Chemical class 0.000 description 10
- 239000003921 oil Substances 0.000 description 6
- 238000000034 method Methods 0.000 description 5
- 239000002802 bituminous coal Substances 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000002480 mineral oil Substances 0.000 description 1
- 235000010446 mineral oil Nutrition 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000010298 pulverizing process Methods 0.000 description 1
- 238000009877 rendering Methods 0.000 description 1
- 239000003079 shale oil Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B57/00—Other carbonising or coking processes; Features of destructive distillation processes in general
- C10B57/04—Other carbonising or coking processes; Features of destructive distillation processes in general using charges of special composition
- C10B57/06—Other carbonising or coking processes; Features of destructive distillation processes in general using charges of special composition containing additives
Definitions
- the process of mixing the lump or crude coal and the compound is exceedingly simple. It consists in merely putting the two together and mixing them thoroughly in any convenient man tier. They may be run through a stirringmill; or they may be stirred well together by hand with a shovel or otherwise. It is best that the coal to be thus treated should not be in such large masses or lumps that it will not hold the compound well distributed through it when the mixing has been once accomplished.
- the proportions I would recommend are one ton of the compound to two tons of crude or lump coal to produce a satisfactory gas. An inferior coal that will produce gas of only a low illuminating-power will, when thus treated, yield a rich and highly-illuminating gas.
- the proportions given above may of course be varied according to the quantity of the coal employed and the degree of illuminating-power desired in the gas.
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Solid Fuels And Fuel-Associated Substances (AREA)
Description
UNITED STATES PATENT OFFICE.
GEORGE MCKENZIE, ()F GLASGOW, SCOTLAND.
IMPROVEMENT IN THE MANUFACTURE OF lLLUMlNATlNG-GAS- FROM COAL AND OTHER MATERIALS.
Specification forming part of Letters Patent No. IO0A32, dated March 1, 1870.
- which Letters Patent of the United States were issued to me on the 9th day of July, 1867, and numbered 6 6,511 and in order that others skilled in the artmay be enabled to make and use my invention, I will proceed to desoribeit.
The improved compound to which I have referred above is fully described in the specification forming a part of the aforesaid patent, and to that patent I refer for detailed and specific information as to the method of making said compound, only remarking here that it consists of bituminous coal finely pulverized and then intimately mixed with shale-oil or other mineral oil. The proportions of oil and coal stated in said specification as those which I had found to be the most desirable for the purpose were one ton of coal to thirty gallons of oil. This mixture of pulverized coal and oil constitutes a substance readily susceptible of minute divisions. Since the issue of the abovementioned patent I have discovered that I attain a more desirable result by mixing this compound with lump-coal, that will not of itself yield gas of sufficient illuminating-power, than I do by pulverizing and combining with oil the entire coal used as gasstock.
The process of mixing the lump or crude coal and the compound is exceedingly simple. It consists in merely putting the two together and mixing them thoroughly in any convenient man tier. They may be run through a stirringmill; or they may be stirred well together by hand with a shovel or otherwise. It is best that the coal to be thus treated should not be in such large masses or lumps that it will not hold the compound well distributed through it when the mixing has been once accomplished. The proportions I would recommend are one ton of the compound to two tons of crude or lump coal to produce a satisfactory gas. An inferior coal that will produce gas of only a low illuminating-power will, when thus treated, yield a rich and highly-illuminating gas. The proportions given above may of course be varied according to the quantity of the coal employed and the degree of illuminating-power desired in the gas.
The attempt has been made to use the above compound in connection with crude or lump coal by distilling each in separate retorts and then mixing their products, thus enriching the poorer gas from the crude coal with the superior gas from the compound; but I have found by experiment that the process herein described as my invention gives a much preferable result.
The special advantages of my invention are twofold: first, saving expense by rendering it necessary to pulverize only comparatively a small amount of coal to be mixed with oil, and, second, greatly facilitating the process of distillation in the retort.
I- do not of course limit myself to any particular proportions of crude coal and the compound referred to, nor to any special method of putting them together; but
What I do claim, and desire to secure by Letters Patent, is-- The process of treating coal whereby its illuminating-gas-produeingqualities areimproved, by mixing with it, either previous to or while submitting it to the action of heat for the evolution of gas, the compound of pulverized coal and oil referred to, substantially as and for the purposes specified.
GEORGE MCKENZIE.
Witnesses:
THOS. A. MAsTEEsoN, J. P. FITCH.
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US100432A true US100432A (en) | 1870-03-01 |
Family
ID=2169894
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US100432D Expired - Lifetime US100432A (en) | Improvement in the manufacture of illuminating-gas from coal and other materials |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US100432A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2756198A (en) * | 1954-05-04 | 1956-07-24 | Koppers Co Inc | Low temperature tar conversion to high temperature tar in high temperature coking chambers |
-
0
- US US100432D patent/US100432A/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2756198A (en) * | 1954-05-04 | 1956-07-24 | Koppers Co Inc | Low temperature tar conversion to high temperature tar in high temperature coking chambers |
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