US4433065A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for the preparation of hydrocarbons from carbon-containing material
Assignee: Shell USA Inc
•
Filing: 1982-03-05
•
Granted: 1984-02-21
•
Expires: 2002-03-05
Abstract
Abstract Pulverized coal is converted by means of a gaseous mixture and partial oxidation into synthesis gas which is subsequently utilized as a feedstock for the production of hydrocarbons. A gaseous mixture containing non-converted synthesis gas and low boiling hydrocarbons is separated from the higher boiling hydrocarbons and recycled to the coal conversion step.
Inventors
- 👤 Maarten J. VAN DER Burgt
- 👤 Sikke J. A. Boelema
- 👤 Willem J. A. H. Schoeber
- 👤 Pieter L. Zuideveld
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-27 10:46
CPC Classifications
C; C10; C10G; C10G2/00; C10G2/30; C10G2/32; C07; C07C; C07C1/00; C07C1/02; C07C1/04; C07C1/0485; F; F01; F01K; F01K23/00; F01K23/02; F01K23/06; F01K23/067; Y; Y02; Y02E; Y02E20/00; Y02E20/16; Y02E20/18
Claims Analysis
Total Claims: 9
Claim 1
Independent Claim
282 words
A process for the preparation of hydrocarbons from coal comprising the following steps: (a) a finely comminuted coal is converted by gasification at a temperature from 1050° to 2000° C. in the presence of oxygen and steam into a gas mixture consisting substantially of carbon monoxide and hydrogen; (b) the gas mixture obtained in step (a) is partially converted into a aromatic hydrocarbon mixture with the use of a bifunctional crystalline silicate catalyst which (i) is capable of adsorbing more than 3% by weight of water at 25° C. and saturated water vapor pressure after dehydration at 400° C. in vacuo, and (ii) has, in the dehydrated form, the following gross composition, expressed in moles of the oxides: (1.0±0.3)(R).sub.2/n O. a Fe.sub.2 O.sub.3. b Al.sub.2 O.sub.3. c Ga.sub.2 O.sub.3. y(d SiO.sub.2 +e GeO.sub.2), wherein R=one or more mono- or bivalent cations, a≧0.1, b≧0, c≧0, a+b+c=1, y≧10, d≧0.1, e≧0, d+e=1, and n=the valency of R, and (iii) which contains one or more metal components with catalytic activity for conversion of an H 2 /CO mixture into hydrocarbons and/or oxygen-containing hydrocarbons; (c) the product of step (b) is separated into a liquid containing hydrocarbon with at least 3 carbon atoms and a gas containing unconverted hydrogen, carbon monoxide, nitrogen and resultant hydrocarbon gases; and (d) at least a part of the gas product of step (c) is separated into (i) a gas consisting substantially of hydrogen, (ii) a gas consisting substantially of carbon monoxide, nitrogen and argon, and (iii) a gas consisting substantially of methane and ethane and wherein at least a part of gas (i) is recycled to step (b) and at least a part of gas (iii) is recycled to step (a).
Claim 2
Dependent Claim
282 words
A process for the preparation of hydrocarbons from coal comprising the following steps: (a) a finely comminuted coal is converted by gasification at a temperature from 1050° to 2000° C. in the presence of oxygen and steam into a gas mixture consisting substantially of carbon monoxide and hydrogen; (b) the gas mixture obtained in step (a) is partially converted into a aromatic hydrocarbon mixture with the use of a bifunctional crystalline silicate catalyst which (i) is capable of adsorbing more than 3% by weight of water at 25° C. and saturated water vapor pressure after dehydration at 400° C. in vacuo, and (ii) has, in the dehydrated form, the following gross composition, expressed in moles of the oxides: (1.0±0.3)(R).sub.2/n O. a Fe.sub.2 O.sub.3. b Al.sub.2 O.sub.3. c Ga.sub.2 O.sub.3. y(d SiO.sub.2 +e GeO.sub.2), wherein R=one or more mono- or bivalent cations, a≧0.1, b≧0, c≧0, a+b+c=1, y≧10, d≧0.1, e≧0, d+e=1, and n=the valency of R, and (iii) which contains one or more metal components with catalytic activity for conversion of an H 2 /CO mixture into hydrocarbons and/or oxygen-containing hydrocarbons; (c) the product of step (b) is separated into a liquid containing hydrocarbon with at least 3 carbon atoms and a gas containing unconverted hydrogen, carbon monoxide, nitrogen and resultant hydrocarbon gases; and (d) at least a part of the gas product of step (c) is separated into (i) a gas consisting substantially of hydrogen, (ii) a gas consisting substantially of carbon monoxide, nitrogen and argon, and (iii) a gas consisting substantially of methane and ethane and wherein at least a part of gas (i) is recycled to step (b) and at least a part of gas (iii) is recycled to step (a).
Claim 3
Dependent Claim
34 words
The process of claim 1 wherein at least part of the gas recovered in step (c) is combusted in a gas turbine to form a hot combustion gas during which process energy is generated.
Claim 4
Dependent Claim
25 words
The process of claim 2 wherein at least part of the finely comminuted coal is dried by at least part of the hot combustion gas.
Claim 5
Dependent Claim
44 words
The process of claim 1 wherein the reaction mixture is indirectly cooled in step (b) with the aid of water which is converted into steam and at least part of this steam is used to indirectly dry at least part of the carbon-containing material.
Claim 6
Dependent Claim
32 words
The process of claim 1 wherein at least part of the gas substantially consisting of carbon monoxide, nitrogen and argon is combusted in a gas turbine during which operation energy is generated.
Claim 7
Dependent Claim
28 words
The process of claim 1 wherein a mixture of finely comminuted coal, oxygen and steam is passed into a gasification reactor at a linear velocity of 10-100 m/sec.
Claim 8
Dependent Claim
33 words
The process of claim 1 wherein step (b) is carried out at a temperature of 200°-500° C., a pressure of 1-150 bar and a space velocity of 50-5000 Nl of gas/l of catalyst/hour.
Claim 9
Dependent Claim
33 words
The process of claim 1 wherein the separation of step (c) is carried out at a pressure ranging from 20 to 100 bar absolute and a temperature ranging from 0° to -70° C.
References Cited (Backward Citations)
US2713590A
Cited
US2697713A
Cited
US3161461A
Cited
GB957260A
Cited
US4094650A
Cited
GB1436963A
Cited
GB1501284A
Cited
US4022591A
Cited
US3941820A
Cited
US4092825A
Cited
GB2006819A
Cited
US4218388A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1987-02-20 | 1987-08-22 | 1988-02-21 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1991-02-20 | 1991-08-22 | 1992-02-21 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1995-02-20 | 1995-08-22 | 1996-02-21 | $7700.00 | Window Closed / Lapsed |