US4378232A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method for production of acetylene
Assignee: Bergwerksverband GmbH
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Filing: 1980-12-18
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Granted: 1983-03-29
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Expires: 2000-12-18
Abstract
Abstract A method for the production of acetylene from coal and hydrogen is provided by electric arc heating. The coal has a content of volatile components (i.waf) from about 25 to 44 percent and a content of organic oxygen (i.waf) of less than 9 percent and is ground to a diameter of less than 0.5 mm. The coal is then separated into two to four grain size fractions and one of the grain size fractions is loaded on a hydrogen containing gas. The gas carrying the coal is heated by way of an electric arc with an energy of from about 5 to 20 kJ/l (in normal state). The ratio of electric power employed to coal stream is from about 4,000 to 40,000 kJ/kg coal. The coal is heated for a time duration about inversely proportional to the third root of the specific outer surface of the coal gain fraction. The resulting product gas is quenched with cold liquid hydrocarbons, with hydrogen or water. Acetylene yields of up to about 0.41 kg acetylene per kg coal can be obtained.
Inventors
- 👤 Cornelius Peuckert
- 👤 Herbert Baumann
- 👤 Dirk Bittner
- 👤 Jurgen Klein
- 👤 Harald Juntgen
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-04 11:33
CPC Classifications
C; C07; C07C; C07C1/00
Claims Analysis
Total Claims: 12
Claim 1
Independent Claim
166 words
A method for the production of acetylene comprising: grinding coal to less than 0.5 mm diameter, where the coal has a content of volatile components from about 25 to 44 percent and a content of organic oxygen of less than 9 percent; separating the coal into at least two grain size fractions; loading hydrogen containing gas with said grain size fractions of coal; feeding each of said grain size fractions which have been loaded into hydrogen containing gas to separate electric arc rectors; heating said grain size fractions, which have been loaded into hydrogen containing gas, in each of said reactors through an electric arc with an energy of from about 5 to 20 kJ/l and where the ratio of electric power to coal stream is from about 4,000 to 40,000 kJ/kg coal for a time duration about inversely proportional to the third root of the specific outer surface of the coal grain fraction; and quenching the resulting product gas with cold liquid hydrocarbons or water.
Claim 2
Independent Claim
166 words
A method for the production of acetylene comprising: grinding coal to less than 0.5 mm diameter, where the coal has a content of volatile components from about 25 to 44 percent and a content of organic oxygen of less than 9 percent; separating the coal into at least two grain size fractions; loading hydrogen containing gas with said grain size fractions of coal; feeding each of said grain size fractions which have been loaded into hydrogen containing gas to separate electric arc rectors; heating said grain size fractions, which have been loaded into hydrogen containing gas, in each of said reactors through an electric arc with an energy of from about 5 to 20 kJ/l and where the ratio of electric power to coal stream is from about 4,000 to 40,000 kJ/kg coal for a time duration about inversely proportional to the third root of the specific outer surface of the coal grain fraction; and quenching the resulting product gas with cold liquid hydrocarbons or water.
Claim 3
Dependent Claim
19 words
The method according to claim 1, wherein the content of volatile components is from about 30 to 40 percent.
Claim 4
Dependent Claim
12 words
The method according to claim 1, wherein the coal is bituminous coal.
Claim 5
Dependent Claim
12 words
The method according to claim 1, wherein the coal is subbituminous coal.
Claim 6
Dependent Claim
36 words
The method according to claim 1, wherein the specific outer surface of the coal ground to less than 0.5 mm is according to the Blaine method from about 0.5 to 2.0 m 2 /cm 3 .
Claim 7
Dependent Claim
43 words
The method according to claim 1, wherein in the grain size fraction distribution of the coal fraction employed, the medium slope of the grain charcteristic line amounts to from about 1.2 to 2.5 in the Rosin-Rammler-Sperling-Bennet-grid between passages of 10 to 80 percent.
Claim 8
Dependent Claim
185 words
In a process for the production of acetylene by direct transformation of brown or mineral coal in a gas containing hydrogen comprising the steps of: loading the gas containing hydrogen with such an amount of coal that the ratio of electric power to coal stream is from about 4,000 to 40,000 kJ/kg coal, heating the gas containing hydrogen and coal by an electric arc with an energy of from about 5 to 20KJ/l, and quenching the resulting product gas with cold liquid hydrocarbons, cold gas or water, the improvement comprising grinding the coal to less than 0.5 mm diameter, said coal having a content of volatile components of from about 25 to 44 percent and a content of organic oxygen of under 9 percent, separating the coal into from about 2 to 4 different coal grain size fractions, supplying each of these coal grain size fractions to a separate electric arc reactor, quenching the product gas after a dwell time in the hot gas, which dwell time is about inversely proportional to the third root of the specific outer surface of the individual coal fraction.
Claim 9
Dependent Claim
185 words
In a process for the production of acetylene by direct transformation of brown or mineral coal in a gas containing hydrogen comprising the steps of: loading the gas containing hydrogen with such an amount of coal that the ratio of electric power to coal stream is from about 4,000 to 40,000 kJ/kg coal, heating the gas containing hydrogen and coal by an electric arc with an energy of from about 5 to 20KJ/l, and quenching the resulting product gas with cold liquid hydrocarbons, cold gas or water, the improvement comprising grinding the coal to less than 0.5 mm diameter, said coal having a content of volatile components of from about 25 to 44 percent and a content of organic oxygen of under 9 percent, separating the coal into from about 2 to 4 different coal grain size fractions, supplying each of these coal grain size fractions to a separate electric arc reactor, quenching the product gas after a dwell time in the hot gas, which dwell time is about inversely proportional to the third root of the specific outer surface of the individual coal fraction.
Claim 10
Dependent Claim
19 words
The process according to claim 7, wherein the content of volatile components is from about 30 to 40 percent.
Claim 11
Dependent Claim
36 words
The process according to claim 7, wherein the specific outer surface of the coal ground to less than 0.5 mm is according to the Blaine method from about 0.5 to 2.0 m 2 /m 3 .
Claim 12
Dependent Claim
43 words
The process according to claim 7, wherein in the grain size fraction distribution of the coal fraction employed, the medium slope of the grain characteristic line amounts to from about 1.2 to 2.5 in the Rosin-Rammler-Sperling-Bennet-grid between passages of 10 to 80 percent.
References Cited (Backward Citations)
US4181504A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1986-03-28 | 1986-09-27 | 1987-03-29 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1990-03-28 | 1990-09-27 | 1991-03-29 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1994-03-28 | 1994-09-27 | 1995-03-29 | $7700.00 | Window Closed / Lapsed |