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US4322221A
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Process for the superatmospheric gasification of solid carbonaceous materials
Assignee: Beazer East Inc
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Filing: 1980-08-21
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Granted: 1982-03-30
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Expires: 2000-08-21
Abstract
Abstract A process is disclosed for gasifying solid carbonaceous material at elevated temperature and pressure to produce a gas consisting of carbon monoxide and hydrogen, which comprises forming a slurry at atmospheric pressure of the carbonaceous material with a liquid having a specific gravity of from 1.1 to 1.9, a boiling temperature of at least 70° F., a latent heat of vaporization less than about 200 BTU per pound, a critical temperature which is less than the incipient coking temperature of the carbonaceous material, a stability at temperatures up to 600° F., an essentially inert chemical reaction with the carbonaceous material at temperatures less than about 600° F., an immiscibility with water or solubility in water at no more than 5%, and a dissolving ability for hydrogen sulfide at temperatures of from -40 to 250° F., and raising the formed slurry to a pressure of at least the gasification pressure and vaporizing said liquid and gasifying said carbonaceous material, either in the same or in separate steps. Examples of suitable slurrying liquids are: carbon tetrachloride, carbon disulfide, trichloroethylene, bromoethane, chlorobenzene, methane dichloride, chloroform, or mixtures thereof.
Inventors
- 👤 John F. Kamody
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-05 16:02
CPC Classifications
C; C10; C10J; C10J3/00; C10J3/46; C10J3/466; C10J3/48; C10J3/50; C10J3/506; C10J3/72; C10J3/78; C10J3/82; C10J3/84; C10J2300/00; C10J2300/09; C10J2300/0913; C10J2300/093; C10J2300/0953; C10J2300/0956; C10J2300/0959; C10J2300/0969; C10J2300/0973; C10J2300/0976; C10J2300/18; C10J2300/1807; Y; Y10; Y10S; Y10S48/00; Y10S48/02; Y10S48/07
Claims Analysis
Total Claims: 15
Claim 1
Independent Claim
64 words
In a process for gasifying solid carbonaceous material at elevated temperature and pressure to produce a gas containing carbon monoxide and hydrogen, the improvement which comprises forming a slurry at atmospheric pressure of the carbonaceous material with carbon disulfide and raising said formed slurry to a pressure of at least the gasification pressure and simultaneously vaporizing the carbon disulfide and gasifying said carbonaceous material.
Claim 2
Dependent Claim
64 words
In a process for gasifying solid carbonaceous material at elevated temperature and pressure to produce a gas containing carbon monoxide and hydrogen, the improvement which comprises forming a slurry at atmospheric pressure of the carbonaceous material with carbon disulfide and raising said formed slurry to a pressure of at least the gasification pressure and simultaneously vaporizing the carbon disulfide and gasifying said carbonaceous material.
Claim 3
Dependent Claim
115 words
The process of claim 1 wherein the said carbon disulfide is admixed with a second different fluid whose properties have a specific gravity of from 1.1 to 1.9, a boiling temperature of at least 70° F., a latent heat of vaporization less than about 200 btu per pound, a critical temperature which is less than the incipient coking temperature of the carbonaceous material, a stability at temperatures up to 600° F., an essentially inert chemical reaction with the carbonaceous material at temperatures less than about 600° F., an immiscibility with water or solubility in water at no more than 5%, and a dissolving ability for hydrogen sulfide at temperatures of from -40° to 250° F.
Claim 4
Dependent Claim
12 words
The process of claim 2 wherein said second fluid is carbon tetrachloride.
Claim 5
Dependent Claim
27 words
The process of claim 3 wherein the ratio of carbon tetrachloride to carbon disulfide is such as to closely match the density of the solid carbonaceous material.
Claim 6
Dependent Claim
17 words
The process of claim 2 wherein said second fluid is trichloroethylene, bromoethane, chlorobenzene, methane dichloride, or chloroform.
Claim 7
Dependent Claim
22 words
The process of claim 2 wherein said second fluid is any mixture of carbon tetrachloride, trichloroethylene, bromoethane, chlorobenzene, methane dichloride, or chloroform.
Claim 8
Dependent Claim
59 words
In a process for gasifying a solid carbonaceous material at elevated temperature and pressure, the improvement which comprises forming a slurry with the carbonaceous material and carbon disulfide at atmospheric pressure, raising the slurry to a pressure of at least the gasification pressure, and evaporating the carbon disulfide from said carbonaceous material prior to gasification of said carbonaceous material.
Claim 9
Dependent Claim
59 words
In a process for gasifying a solid carbonaceous material at elevated temperature and pressure, the improvement which comprises forming a slurry with the carbonaceous material and carbon disulfide at atmospheric pressure, raising the slurry to a pressure of at least the gasification pressure, and evaporating the carbon disulfide from said carbonaceous material prior to gasification of said carbonaceous material.
Claim 10
Dependent Claim
15 words
The process of claim 7 wherein the said carbon disulfide is admixed with carbon tetrachloride.
Claim 11
Dependent Claim
44 words
The process of claim 8 wherein the carbonaceous material recovered upon evaporation of the slurrying fluid is purged with gaseous carbon disulfide to eliminate traces of carbon tetrachloride in the void volume of the carbonaceous material prior to the gasification of the carbonaceous material.
Claim 12
Dependent Claim
27 words
The process of claim 8 wherein the ratio of carbon disulfide to carbon tetrachloride is such as to closely match the density of the solid carbonaceous material.
Claim 13
Dependent Claim
185 words
A process for the superatmospheric gasification of a solid carbonaceous material which comprises: (a) forming a slurry of said carbonaceous material at atmospheric pressure with a recycle fluid consisting of carbon disulfide, carbon tetrachloride, trichloroethylene, bromoethane, chlorobenzene, methane dichloride or chloroform, or mixture of these compounds; (b) pumping said slurry to a pressure of at least the gasification pressure; (c) gasifying the carbonaceous material and simultaneously evaporating said recycle slurrying fluid within a gasifier; (d) scrubbing the resultant product gas with a chilled solution of scrubbing fluid which is essentially the same as said recycle fluid, thereby condensing said evaporated recycle fluid while simultaneously condensing water vapor from said product gas, absorbing sulfur compounds and other soluble compounds from said product gas, and physically removing particulates from said product gas; (e) treating said scrubbing fluid to remove accumulated particulates and sulfur compounds; (f) separating said scrubbing fluid from said condensed water; (g) forming a recycle fluid from a portion of the scrubbing fluid; and (h) recycling the recycle fluid to step (a), whereby substantially no reaction of recycle fluid occurs when gasifying the carbonaceous material.
Claim 14
Dependent Claim
185 words
A process for the superatmospheric gasification of a solid carbonaceous material which comprises: (a) forming a slurry of said carbonaceous material at atmospheric pressure with a recycle fluid consisting of carbon disulfide, carbon tetrachloride, trichloroethylene, bromoethane, chlorobenzene, methane dichloride or chloroform, or mixture of these compounds; (b) pumping said slurry to a pressure of at least the gasification pressure; (c) gasifying the carbonaceous material and simultaneously evaporating said recycle slurrying fluid within a gasifier; (d) scrubbing the resultant product gas with a chilled solution of scrubbing fluid which is essentially the same as said recycle fluid, thereby condensing said evaporated recycle fluid while simultaneously condensing water vapor from said product gas, absorbing sulfur compounds and other soluble compounds from said product gas, and physically removing particulates from said product gas; (e) treating said scrubbing fluid to remove accumulated particulates and sulfur compounds; (f) separating said scrubbing fluid from said condensed water; (g) forming a recycle fluid from a portion of the scrubbing fluid; and (h) recycling the recycle fluid to step (a), whereby substantially no reaction of recycle fluid occurs when gasifying the carbonaceous material.
Claim 15
Dependent Claim
24 words
The process of claim 11 wherein at least some of the condensed water from step (f) is atomized into said gasifier of step (c).
References Cited (Backward Citations)
US2735787A
Cited
GB165423A
Cited
US2016804A
Cited
US2560478A
Cited
US3140123A
Cited
US3762133A
Cited
US4060397A
Cited
US3929429A
Cited
US4020144A
Cited
US4115081A
Cited
US4156594A
Cited
US4153427A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1985-03-29 | 1985-09-28 | 1986-03-30 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1989-03-29 | 1989-09-28 | 1990-03-30 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1993-03-29 | 1993-09-28 | 1994-03-30 | $7700.00 | Window Closed / Lapsed |