US4424065A
Expired / Lapsed
US
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Method for the gasification and preparation of a water-carbon slurry
Assignee: RUHRKOLE AKTIENGESELLSCHAFT
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Filing: 1981-09-14
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Granted: 1984-01-03
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Expires: 2001-09-14
Abstract
Abstract A method of particulate-carbon recovery from the product gas in a coal gasification process of the type using water-carbon slurry combusted with oxygen in a reactor uses water scrubbing for the product gas to obtain particulate carbon together with ash. Certain ash content is trapped in carbon particles which have a tendency of lumping together. The carbon and ash fraction is treated with liquid hydrocarbon for carbon particle wetting and facilitating separation of ash. The recovered carbon is ground to break down bigger carbon particles and sent through a wet-particle separator; carbon particles which pass a predetermined mesh size, e.g., approximately 63 micron mesh, are sent back to the reactor for mixing with the water-carbon slurry inlet for further combustion. The bigger fractions of carbon are either ground down to size again, or diverted for other uses. Recycling carbon particles which pass a 63 micron mesh and are almost devoid of ash improves the carbon utilization and significantly reduces total ash formed. The abrasion damage on components because of ash is also reduced.
Inventors
- 👤 Josef Langhoff
- 👤 Ju/ rgen Seipenbusch
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-06 08:37
CPC Classifications
B; B03; B03B; B03B5/00; B03B5/48; B03B9/00; B03B9/005; Y; Y10; Y10S; Y10S48/00; Y10S48/07
Claims Analysis
Total Claims: 21
Claim 1
Independent Claim
219 words
A method in gasification of a feed-stock containing water-carbonaceous material slurry comprising the following steps: a. reacting a water-carbonaceous material slurry with oxygen in a reactor to form a product gas containing solid material comprising unburnt carbon particles and ash; b. removing said product gas and said solid material from the reactor; c. treating said gas and solid material with water to remove the solid material from the gas and to form a slurry of water and the solid material; d. treating said slurry of water and solid material with an oil additive to cause oil-wetting and cause particulate agglomeration of particulate carbon in said solid material, and consequently to facilitate separating ash from said unburnt carbon particles; e. separating agglomerated unburned carbon particles having a predetermined mesh size range from said slurry such that the carbon particles separated have a substantially decreased ash content by admitting the slurry with a horizontal velocity into a container for separation of particulate sizes, using substantially vertical baffles in the container; and f. feeding back the separated carbon particles of said predetermined mesh size to the reactor for being reintroduced into the reactor with the feed stock, whereby abrasive wear in the reactor is reduced because of reduced ash feedback in the carbon fed back to be mixed with the feed stock.
Claim 2
Independent Claim
219 words
A method in gasification of a feed-stock containing water-carbonaceous material slurry comprising the following steps: a. reacting a water-carbonaceous material slurry with oxygen in a reactor to form a product gas containing solid material comprising unburnt carbon particles and ash; b. removing said product gas and said solid material from the reactor; c. treating said gas and solid material with water to remove the solid material from the gas and to form a slurry of water and the solid material; d. treating said slurry of water and solid material with an oil additive to cause oil-wetting and cause particulate agglomeration of particulate carbon in said solid material, and consequently to facilitate separating ash from said unburnt carbon particles; e. separating agglomerated unburned carbon particles having a predetermined mesh size range from said slurry such that the carbon particles separated have a substantially decreased ash content by admitting the slurry with a horizontal velocity into a container for separation of particulate sizes, using substantially vertical baffles in the container; and f. feeding back the separated carbon particles of said predetermined mesh size to the reactor for being reintroduced into the reactor with the feed stock, whereby abrasive wear in the reactor is reduced because of reduced ash feedback in the carbon fed back to be mixed with the feed stock.
Claim 3
Dependent Claim
47 words
The method as in claim 1 wherein the step of separating said agglomerated unburned carbon particles by separation of particulate sizes comprises wet separation by letting in said slurry of water and said solid material with a horizontal velocity into a tank containing three substantially vertical baffles.
Claim 4
Dependent Claim
45 words
The method as in claim 2 wherein separation by particulate sizes consists in sorting particles of 63 micron mesh size for return to mix with said feedstock, and particles above 63 micron mesh size to be dewatered and subjected to further size reduction by grinding.
Claim 5
Dependent Claim
54 words
The method as in claim 1 which includes a step of water removal and thickening of the slurry containing water and said carbonaceous solid material, prior to the step of treating with a fluid additive, the thickening being to achieve a carbonaceous solid material weight of between 200 and 500 grams/liter of the slurry.
Claim 6
Dependent Claim
19 words
The method as in claim 4 wherein the thickening is to achieve a carbonaceous material weight of 350 grams/liter.
Claim 7
Dependent Claim
40 words
The method as in claim 4 wherein the step of treating with a fluid additive comprises thickening by adding sufficient weight of commercial heating oil and mixing thoroughly so as to gain a weight increase of between 5% and 20%.
Claim 8
Dependent Claim
24 words
The method as in claim 6 wherein the commercial heating oil is German EL grade, and the weight increase is between 8% and 10%.
Claim 9
Dependent Claim
18 words
The method as in claim 6, wherein the predetermined mesh size for particulate size separation is 0.5 mm.
Claim 10
Dependent Claim
22 words
The method as in claim 6, including the step of grinding the thickened slurry to achieve a particulate size of 0.1 mm.
Claim 11
Dependent Claim
39 words
The method as in claim 6 including the step of treating particulate carbon which is of a size other than said predetermined size, with a binder material after washing, and subsequently compacting into any required shape for further use.
Claim 12
Independent Claim
164 words
A method of gasification of a feedstock containing water-carbonaceous material slurry, comprising the steps of: a. reacting the slurry with oxygen in a reactor to form a product gas containing entrained particulate solid material containing carbon particles and ash; b. scrubbing said product gas with water to form scrubbed clean product gas and a slurry of water together with solid material; c. decreasing the water content of said solid material; d. treating said water-solid material slurry with a known grade of oil additive to facilitate agglomeration of carbon particles and to facilitate separating ash; e. subjecting the treated water-solid material slurry by admitting said slurry under horizontal velocity into a container to cause wet particulate separation in said container using substantially vertical baffles, to obtain carbon particles of a predetermined mesh size such that the carbon particles obtained have a substantially decreased ash content; and f. feeding back carbon particles of said predetermined mesh size to be mixed with said feedstock for carbon recovery.
Claim 13
Independent Claim
164 words
A method of gasification of a feedstock containing water-carbonaceous material slurry, comprising the steps of: a. reacting the slurry with oxygen in a reactor to form a product gas containing entrained particulate solid material containing carbon particles and ash; b. scrubbing said product gas with water to form scrubbed clean product gas and a slurry of water together with solid material; c. decreasing the water content of said solid material; d. treating said water-solid material slurry with a known grade of oil additive to facilitate agglomeration of carbon particles and to facilitate separating ash; e. subjecting the treated water-solid material slurry by admitting said slurry under horizontal velocity into a container to cause wet particulate separation in said container using substantially vertical baffles, to obtain carbon particles of a predetermined mesh size such that the carbon particles obtained have a substantially decreased ash content; and f. feeding back carbon particles of said predetermined mesh size to be mixed with said feedstock for carbon recovery.
Claim 14
Dependent Claim
26 words
The method as in claim 11 including the step of grinding separated particulate carbon particles which are of a size bigger than said predetermined mesh size.
Claim 15
Dependent Claim
35 words
The method as in claim 11, wherein the step of decreasing the water content is so as to achieve a carbonaceous solid material weight of between 200 and 500 grams/liter of the water-solid material slurry.
Claim 16
Dependent Claim
12 words
The method as in claim 13 wherein the weight is 350 grams/liter.
Claim 17
Dependent Claim
36 words
The method as in claim 11 wherein the step of treating comprises thickening the slurry by adding sufficient weight of commercial heating oil and mixing, so as to gain a weight increase of 5% to 20%.
Claim 18
Dependent Claim
27 words
The method as in claim 15 wherein the commercial heating oil is German EL grade, and the weight increase is in the range of 8% to 10%.
Claim 19
Dependent Claim
14 words
The method as in claim 16 wherein the predetermined mesh size is 0.5 mm.
Claim 20
Dependent Claim
21 words
The method as in claim 16 which includes the step of grinding the thickened slurry to a size of 0.1 mm.
Claim 21
Dependent Claim
20 words
The method as in claim 11 wherein the step of decreasing the water content comprises using a centrifuge water separator.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1987-01-02 | 1987-07-04 | 1988-01-03 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1991-01-02 | 1991-07-04 | 1992-01-03 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1995-01-02 | 1995-07-04 | 1996-01-03 | $7700.00 | Window Closed / Lapsed |