US4022680A
Expired / Lapsed
US
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Hydrogen donor solvent coal liquefaction process
Assignee: ExxonMobil Technology and Engineering Co
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Filing: 1975-12-17
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Granted: 1977-05-10
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Expires: 1995-12-17
Abstract
Abstract A process for liquefying a particulate coal feed to produce useful petroleum-like liquid products, particularly by steps which include: (a) contacting, in a liquefaction zone, said coal feed with a hydrogen donor solvent at temperature and pressure sufficient to hydroconvert and liquefy the coal (b) separating the product from the liquefaction zone by distillation into fractions inclusive of a liquid fraction which contains at least 30 weight percent, and preferably at least 50 weight percent hydrogen donor compounds, particularly those fractions boiling within about the 350 DEG -850 DEG F. range, and preferably within about the 400 DEG -700 DEG F. range, (c) hydrogenating said liquid fraction in a hydrogenation zone, (d) adding to said liquid fraction a solvent characterized as a low molecular weight heterocyclic oxygen or heterocyclic sulfur compound containing, within a molecule, from 2 to about 6 fused rings one or more of which is a five- or six-membered heterocyclic ring having 4 to 5 carbon atoms and from 1 to 2 atoms of oxygen or sulfur, and (e) recycling the hydrogenated liquid solvent mixture to said coal liquefaction zone.
Inventors
- 👤 Peter S. Maa
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-26 08:53
CPC Classifications
C; C10; C10G; C10G1/00; C10G1/04; C10G1/042; C10G1/06; C10G1/065
Claims Analysis
Total Claims: 24
Claim 1
Independent Claim
195 words
A process for producing coal liquids by the conversion of coal at coal liquefaction conditions, which comprise: passing through a liquefaction zone at temperatures ranging from about 700° F to about 950° F, and pressures ranging from about 300 psia to about 300 psia, coal slurried in a solvent containing at least about 0.8 percent donatable hydrogen, based on the weight of solvent, to which has been added in quantity ranging from about 3 to about 50 percent, based on the weight of total solvent, a polar, stable compound characterized as i. a low molecular weight heterocyclic oxygen compound containing from two to about six fused rings, one or more of which is a five- or six-membered heterocyclic ring having from 4 to 5 carbon atoms in the nucleus, and from one to two atoms of oxygen; or ii. a low molecular weight heterocyclic sulfur compound containing from two to about six fused rings, one or more of which is a five- or six-membered heterocyclic ring having from 4 to 5 carbons atoms in the nucleus, and from one to two atoms of sulfur sufficient to increase the yields of liquids produced from said coal.
Claim 2
Dependent Claim
195 words
A process for producing coal liquids by the conversion of coal at coal liquefaction conditions, which comprise: passing through a liquefaction zone at temperatures ranging from about 700° F to about 950° F, and pressures ranging from about 300 psia to about 300 psia, coal slurried in a solvent containing at least about 0.8 percent donatable hydrogen, based on the weight of solvent, to which has been added in quantity ranging from about 3 to about 50 percent, based on the weight of total solvent, a polar, stable compound characterized as i. a low molecular weight heterocyclic oxygen compound containing from two to about six fused rings, one or more of which is a five- or six-membered heterocyclic ring having from 4 to 5 carbon atoms in the nucleus, and from one to two atoms of oxygen; or ii. a low molecular weight heterocyclic sulfur compound containing from two to about six fused rings, one or more of which is a five- or six-membered heterocyclic ring having from 4 to 5 carbons atoms in the nucleus, and from one to two atoms of sulfur sufficient to increase the yields of liquids produced from said coal.
Claim 3
Dependent Claim
18 words
The process of claim 1 wherein the added compound is one containing one heterocyclic atom in its nucleus.
Claim 4
Dependent Claim
23 words
The process of claim 2 wherein the added compound is one containing from 8 to about 36 carbon atoms in a total molecule.
Claim 5
Dependent Claim
30 words
The process of claim 1 wherein the added compound is comprised of from two to three fused rings, at least one of which contains one heterocyclic atom in its nucleus.
Claim 6
Dependent Claim
11 words
The process of claim 4 wherein the heterocyclic atom is oxygen.
Claim 7
Dependent Claim
26 words
The process of claim 3 wherein said added compound is present in amounts of from about 5 to about 20 weight percent, based on total solvent.
Claim 8
Dependent Claim
24 words
The process of claim 2 wherein said added compound is one boiling within a range of from about 250° F. to about 850° F.
Claim 9
Dependent Claim
22 words
The process of claim 7 wherein said added compound boils within a range of from about 290° F. to about 700° F.
Claim 10
Dependent Claim
42 words
The process of claim 7 wherein said added compound is introduced into said liquefaction zone in admixture with a recycle stream produced within said coal liquefaction process, said recycle stream boiling within the range from about 350° F. to about 850° F.
Claim 11
Dependent Claim
22 words
The process of claim 9 wherein the recycle stream boils within a range of from about 400° F to about 700° F.
Claim 12
Dependent Claim
22 words
The process of claim 10 wherein said recycle stream boils within a range of from about 400° F. to about 700° F.
Claim 13
Dependent Claim
36 words
The process of claim 1 wherein the slurry of coal is also contacted with molecular hydrogen in said liquefaction zone at a treat rate of from about 1 to about 6 weight percent (MAF coal basis).
Claim 14
Dependent Claim
22 words
The process of claim 1 wherein the temperature maintained within the reaction zone ranges from about 800° F to about 850° F.
Claim 15
Dependent Claim
22 words
The process of claim 1 wherein the pressure maintained within the reaction zone ranges from about 800 psia to about 2000 psia.
Claim 16
Dependent Claim
19 words
The process of claim 1 wherein the solvent contains from about 1.2 to about 3 percent of donatable hydrogen.
Claim 17
Dependent Claim
25 words
The process of claim 1 wherein the solvent is admixed with the coal to provide a solvent-to-coal ratio ranging from about 0.8:1 to about 4:1.
Claim 18
Dependent Claim
87 words
A process for producing coal liquids which comprises: liquefying a slurry of coal in a hydrogen-donor solvent at coal liquefaction conditions in the presence of an added compound characterized as a low molecular weight heterocyclic sulfur compound containing from two to three fused rings, one or more of which is a five- or six-membered heterocyclic ring having from 4 to 5 carbon atoms, at least one of which contains one heterocyclic sulfur atom in its nucleus, sufficient to increase the yields of liquids produced from said coal.
Claim 19
Dependent Claim
87 words
A process for producing coal liquids which comprises: liquefying a slurry of coal in a hydrogen-donor solvent at coal liquefaction conditions in the presence of an added compound characterized as a low molecular weight heterocyclic sulfur compound containing from two to three fused rings, one or more of which is a five- or six-membered heterocyclic ring having from 4 to 5 carbon atoms, at least one of which contains one heterocyclic sulfur atom in its nucleus, sufficient to increase the yields of liquids produced from said coal.
Claim 20
Dependent Claim
178 words
A process for liquefying a particulate coal feed to produce useful petroleum-like liquid products, in a series of steps which includes: (a) contacting, in a liquefaction zone, said coal feed which is slurried in a hydrogen donor solvent at temperature and pressure sufficient to hydroconvert and liquefy the coal (b) separating the product from the liquefaction zone by distillation into fractions inclusive of a liquid fraction boiling within about a 350°-850° F range, and which contains at least 30 weight percent hydrogen donor compounds, (c) hydrogenating said liquid 350°-850° F fraction in a hydrogenation zone, (d) adding to said 350°-850° F liquid fraction from about 3 to about 50 weight percent of a solvent characterized as a low molecular weight heterocyclic oxygen or heterocyclic sulfur compound containing, within a molecule, from two to about six fused rings, one or more of which is a five- or six-membered heterocyclic ring having 4 to 5 carbon atoms and from one to two atoms of oxygen or sulfur, and (e) recycling the hydrogenated liquid solvent mixture to said coal liquefaction zone.
Claim 21
Dependent Claim
178 words
A process for liquefying a particulate coal feed to produce useful petroleum-like liquid products, in a series of steps which includes: (a) contacting, in a liquefaction zone, said coal feed which is slurried in a hydrogen donor solvent at temperature and pressure sufficient to hydroconvert and liquefy the coal (b) separating the product from the liquefaction zone by distillation into fractions inclusive of a liquid fraction boiling within about a 350°-850° F range, and which contains at least 30 weight percent hydrogen donor compounds, (c) hydrogenating said liquid 350°-850° F fraction in a hydrogenation zone, (d) adding to said 350°-850° F liquid fraction from about 3 to about 50 weight percent of a solvent characterized as a low molecular weight heterocyclic oxygen or heterocyclic sulfur compound containing, within a molecule, from two to about six fused rings, one or more of which is a five- or six-membered heterocyclic ring having 4 to 5 carbon atoms and from one to two atoms of oxygen or sulfur, and (e) recycling the hydrogenated liquid solvent mixture to said coal liquefaction zone.
Claim 22
Dependent Claim
22 words
The process of claim 18 wherein the fraction of about 350°-850° F range contains at least 50 weight percent hydrogen donor compounds.
Claim 23
Dependent Claim
19 words
The process of claim 19 wherein the fraction is one boiling within a range of from about 400°-700° F.
Claim 24
Dependent Claim
24 words
The process of claim 18 wherein from about 5 to about 20 percent of the heterocyclic compound is added to the hydrogen donor solvent.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1980-05-09 | 1980-11-08 | 1981-05-10 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1984-05-09 | 1984-11-08 | 1985-05-10 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1988-05-09 | 1988-11-08 | 1989-05-10 | $7700.00 | Window Closed / Lapsed |