US4070268A
Expired / Lapsed
US
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Solvent recovery in a coal deashing process
Assignee: Kerr McGee Corp
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Filing: 1976-06-01
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Granted: 1978-01-24
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Expires: 1996-06-01
Abstract
Abstract An improved coal deashing process wherein coal is mixed with a first dissolving solvent, heated, solubilized and flashed to provide a prepared mixture. The flashing is effected at a temperature below about 650° F. to increase the amount of the first dissolving solvent in the prepared mixture. The prepared mixture then is mixed with a second dissolving solvent to produce a feed mixture which is subjected to two or more successive phase separations. Insoluble coal products present are separated from the feed mixture in a first separation zone and the soluble coal products are recovered from the first and the second dissolving solvents in a second separation zone. The second dissolving solvent is recovered from the first and the second heavy fractions and the second light fraction for recycling to aid in producing the feed mixture. The first dissolving solvent is recovered from the first and second flash zones. This results in an enhanced recovery of the first dissolving solvent for recycle for utilization in the initial solubilization of the coal.
Inventors
- 👤 Robert E. Davis
- 👤 Roger A. Baldwin
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-27 19:11
CPC Classifications
C; C10; C10G; C10G1/00; C10G1/006; C10G1/04
Claims Analysis
Total Claims: 9
Claim 1
Independent Claim
346 words
A process comprising: mixing in a first mixing zone a first dissolving solvent with coal; solubilizing the coal at elevated temperatures and pressures and flashing the mixture comprising the first dissolving solvent, the soluble coal products and the insoluble coal products to provide a prepared mixture; mixing in a second mixing zone the prepared mixture with a second dissolving solvent to provide a feed mixture; introducing the feed mixture into a first separation zone; maintaining the temperature level in the first separation zone in the range of from about 460° F. to about 620° F., and maintaining the pressure level in the first separation zone in the range of from about 650 psig to about 1000 psig; separating the feed mixture in the first separation zone into a first heavy fraction and a first light fraction comprising the soluble coal products, some of the first dissolving solvent and some of the second dissolving solvent; withdrawing the first light fraction from the first separation zone; heating the first light fraction; introducing the first light fraction into a second separation zone; maintaining the temperature level in the second separation zone in the range of from about 630° F. to about 900° F., and maintaining the pressure level in the second separation zone in the range of from about 650 psig to about 1000 psig; separating the first light fraction in the second separation zone into a second light fraction comprising some of the second dissolving solvent and some of the first dissolving solvent, and a second heavy fraction; withdrawing the second fraction from the second separation zone; flashing the second light fraction to produce one stream comprising the first dissolving solvent and one other stream comprising the second dissolving solvent; passing the second dissolving solvent separated from the second light fraction to the second mixing zone for mixing with the prepared mixture to aid in providing the feed mixture; and passing the first dissolving solvent separated from the second light fraction to the first mixing zone for mixing with the coal to aid in providing the prepared mixture.
Claim 2
Dependent Claim
346 words
A process comprising: mixing in a first mixing zone a first dissolving solvent with coal; solubilizing the coal at elevated temperatures and pressures and flashing the mixture comprising the first dissolving solvent, the soluble coal products and the insoluble coal products to provide a prepared mixture; mixing in a second mixing zone the prepared mixture with a second dissolving solvent to provide a feed mixture; introducing the feed mixture into a first separation zone; maintaining the temperature level in the first separation zone in the range of from about 460° F. to about 620° F., and maintaining the pressure level in the first separation zone in the range of from about 650 psig to about 1000 psig; separating the feed mixture in the first separation zone into a first heavy fraction and a first light fraction comprising the soluble coal products, some of the first dissolving solvent and some of the second dissolving solvent; withdrawing the first light fraction from the first separation zone; heating the first light fraction; introducing the first light fraction into a second separation zone; maintaining the temperature level in the second separation zone in the range of from about 630° F. to about 900° F., and maintaining the pressure level in the second separation zone in the range of from about 650 psig to about 1000 psig; separating the first light fraction in the second separation zone into a second light fraction comprising some of the second dissolving solvent and some of the first dissolving solvent, and a second heavy fraction; withdrawing the second fraction from the second separation zone; flashing the second light fraction to produce one stream comprising the first dissolving solvent and one other stream comprising the second dissolving solvent; passing the second dissolving solvent separated from the second light fraction to the second mixing zone for mixing with the prepared mixture to aid in providing the feed mixture; and passing the first dissolving solvent separated from the second light fraction to the first mixing zone for mixing with the coal to aid in providing the prepared mixture.
Claim 3
Dependent Claim
75 words
The process of claim 1 defined further to include the steps of: withdrawing the first heavy fraction from the first separation zone; flashing the first heavy fraction to produce one stream comprising the second dissolving solvent and one other stream comprising most of the insoluble coal products; and passing the second dissolving solvent separated from the first heavy fraction to the second mixing zone for mixing with the prepared mixture to form the feed mixture.
Claim 4
Dependent Claim
75 words
The process of claim 1 defined further to include the steps of: withdrawing the second heavy fraction from the second separation zone; flashing the second heavy fraction to produce one stream comprising the second dissolving solvent and one other stream comprising most of the soluble coal products; and passing the second dissolving solvent separated from the second heavy fraction to the second mixing zone for mixing with the prepared mixture to form the feed mixture.
Claim 5
Dependent Claim
142 words
The process of claim 1 defined further to include the steps of: withdrawing the first heavy fraction from the first separation zone; flashing the first heavy fraction to produce one stream comprising the second dissolving solvent and one other stream comprising most of the insoluble coal products; passing the second dissolving solvent separated from the first heavy fraction to the second mixing zone for mixing with the prepared mixture to form the feed mixture; withdrawing the second heavy fraction from the second separation zone; flashing the second heavy fraction to produce one stream comprising the second dissolving solvent and one other stream comprising most of the soluble coal products containing less than 0.16% ash; and passing the second dissolving solvent separated from the second heavy fraction to the second mixing zone for mixing with the prepared mixture to form the feed mixture.
Claim 6
Dependent Claim
156 words
The process of claim 1 wherein the mixture of coal and a first dissolving solvent is solubilized and flashed defined further the steps of: liquefying the mixture of coal and the first dissolving solvent in a liquefaction zone by heating the mixture to a temperature of about 800° F. and maintaining the pressure level in the range of from about 1200 psig to about 2000 psig to substantially solubilize the coal; withdrawing the mixture from the liquefaction zone; flashing the mixture withdrawn from the liquefaction zone in a first flash zone to produce at least one stream of a prepared mixture comprising some of the first dissolving solvent, the insoluble coal products and the soluble coal products; and maintaining the temperature level in the first flash zone at a predetermined temperature level to maintain the desired amount of the first dissolving solvent remaining in the prepared mixture after flashing the mixture withdrawn from the liquefaction zone.
Claim 7
Dependent Claim
182 words
The process of claim 1 wherein the step of solubilizing and flashing the mixture to provide the prepared mixture is defined further to include the steps of: heating the mixture of coal and the first dissolving solvent withdrawn from the first mixing zone; adding gaseous hydrogen to the mixture of coal and first dissolving solvent; liquefying the mixture of coal, gaseous hydrogen and the first dissolving solvent in a liquefaction zone by heating the mixture to a temperature of about 800° F. and maintaining the present level in the range of from about 1200 psig to about 2000 psig to solubilize the coal so as to produce a mixture comprising the soluble coal products, the insoluble coal products, the first dissolving solvent and the gaseous hydrogen; withdrawing the mixture from the liquefaction zone; introducing the mixture withdrawn from the liquefaction zone into a gas separation zone; separating gaseous hydrogen from the mixture withdrawn from the liquefaction zone in the gas separation zone; and flashing the degassed mixture in a first flash zone to produce at least one stream comprising the prepared mixture.
Claim 8
Dependent Claim
50 words
The process of claim 6 defined further to include the step of: maintaining the temperature level in the first flash zone at a prdetermined temperature level to maintain the desired amount of the first dissolving solvent remaining in the prepared mixture after flashing the mixture withdrawn from the liquefaction zone.
Claim 9
Dependent Claim
39 words
The process of claim 7 wherein the step of maintaining the temperature level in the first flash zone is defined further to include the step of: maintaining the temperature level in the first flash zone below about 650° F.
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) | 1981-01-23 | 1981-07-25 | 1982-01-24 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1985-01-23 | 1985-07-25 | 1986-01-24 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1989-01-23 | 1989-07-25 | 1990-01-24 | $7700.00 | Window Closed / Lapsed |