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US4357244A Expired / Lapsed US ⏱️ 0.0 years remaining

Method for removing suspended solids from a liquid

Assignee: Chevron USA Inc
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Filing: 1981-02-04
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Granted: 1982-11-02
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Expires: 2001-02-04
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Abstract

Abstract Disclosed is a gravity settler for separating finely divided solids such as coal fines from a liquid such as a mixture of coal oil and agglomerating agent by agglomeration. A feed slurry comprising finely divided solids and a liquid mixture of product oil and an agglomerating agent is discharged into a specially shaped duct which promotes formation of agglomerated solids while minimizing turbulence in the remainder of the vessel. The agglomerated solids separate from the liquid by gravity and are washed as they leave the settler while the clarified liquid is discharged from the top of the settler. A method for separating suspended solids from a liquid by agglomeration is also disclosed.

Inventors

  • 👤 Phillip R. Bose

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-08 19:06
CPC Classifications
C; C10; C10G; C10G31/00; C10G31/09; B; B01; B01D; B01D21/00; B01D21/0039; B01D21/0042; B01D21/02; B01D21/24; B01D21/2427; B01D21/2488; C10G1/00; C10G1/04; C10G1/045

Claims Analysis

Total Claims: 7
Claim 1
Independent Claim 306 words
A method for separating a clarified liquid hydrocarbonaceous oil and an agglomeration agent from a slurry of said liquid hydrocarbonaceous oil and finely divided suspended solids wherein said slurry is charged to a settling zone and held there to allow said solids to agglomerate and separate by gravitation, a clarified and essentially solids-free liquid comprising said hydrocarbonaceous oil and said agglomerating agent is recovered from an upper portion of said settling zone, and settled agglomerated solids are withdrawn from a lower portion of said vessel, wherein the improvement comprises: (1) discharging said slurry upwardly into a mixing zone within an intermediate or upper portion of said vessel; (2) forming within said mixing zone a mixture of said slurry with a downflowing recirculated liquid stream comprising said hydrocarbonaceous oil and said agglomerating agent; (3) forming from said mixture a first portion of agglomerated solids of a size large enough to settle by gravitation and a partially settled liquid by circulating said mixture downwardly into a separating zone positioned below said mixing zone and separating said first agglomerate portion from said mixture by gravitation; (4) forming from said partially settled liquid a second portion of agglomerated solids of a size large enough to settle by gravitation and a further settled liquid by circulating at least a portion of said partially settled liquid upwardly through a quiet zone horizontally surrounding said mixing zone and there separating said second agglomerate portion from said further settled liquid by gravitation; (5) providing at least a portion of said recirculated liquid stream by circulating at least a portion of said further settled liquid from said quiet zone into said mixing zone; (6) circulating to said settling zone a portion of at least one of the following: said partially settled liquid from said separating zone and said further settled liquid from said quiet zone.
Claim 2
Independent Claim 306 words
A method for separating a clarified liquid hydrocarbonaceous oil and an agglomeration agent from a slurry of said liquid hydrocarbonaceous oil and finely divided suspended solids wherein said slurry is charged to a settling zone and held there to allow said solids to agglomerate and separate by gravitation, a clarified and essentially solids-free liquid comprising said hydrocarbonaceous oil and said agglomerating agent is recovered from an upper portion of said settling zone, and settled agglomerated solids are withdrawn from a lower portion of said vessel, wherein the improvement comprises: (1) discharging said slurry upwardly into a mixing zone within an intermediate or upper portion of said vessel; (2) forming within said mixing zone a mixture of said slurry with a downflowing recirculated liquid stream comprising said hydrocarbonaceous oil and said agglomerating agent; (3) forming from said mixture a first portion of agglomerated solids of a size large enough to settle by gravitation and a partially settled liquid by circulating said mixture downwardly into a separating zone positioned below said mixing zone and separating said first agglomerate portion from said mixture by gravitation; (4) forming from said partially settled liquid a second portion of agglomerated solids of a size large enough to settle by gravitation and a further settled liquid by circulating at least a portion of said partially settled liquid upwardly through a quiet zone horizontally surrounding said mixing zone and there separating said second agglomerate portion from said further settled liquid by gravitation; (5) providing at least a portion of said recirculated liquid stream by circulating at least a portion of said further settled liquid from said quiet zone into said mixing zone; (6) circulating to said settling zone a portion of at least one of the following: said partially settled liquid from said separating zone and said further settled liquid from said quiet zone.
Claim 3
Dependent Claim 20 words
The method of claim 1 further comprising downwardly deflecting said slurry after said slurry is discharged into said mixing zone.
Claim 4
Independent Claim 304 words
A method for separating a clarified liquid hydrocarbonaceous oil and an agglomerating agent from a slurry of said liquid hydrocarbonaceous oil and finely divided suspended solids wherein said slurry is charged to a settling zone and held there to allow said solids to agglomerate and separate by gravitation, a clarified and essentially solids-free liquid comprising said hydrocarbonaceous oil and said agglomerating agent is recovered from an upper portion of said settling zone, settled agglomerated solids are conducted from a lower portion of said vessel into a washing zone wherein residual product on said agglomerated solids is removed by washing said solids with an upflowing stream of agglomerating agent, which stream then enters said lower portion of said vessel and mixes with the contents therein, and the resulting washed solids are withdrawn from a lower portion of said washing zone, wherein the improvement comprises: (1) discharging said slurry upwardly into a mixing zone located within an intermediate or upper portion of said vessel; (2) forming within said mixing zone a mixture of said slurry with a downflowing recirculated liquid stream comprising said hydrocarbonaceous oil and said agglomerating agent; (3) forming from said mixture a first portion of agglomerated solids of a size large enough to settle by gravitation and a partially settled liquid by circulating said mixture downwardly into a separating zone positioned above said washing zone and below said mixing zone and separating said first agglomerate portion from said mixture by gravitation; (4) forming from said partially settled liquid a second portion of agglomerated solids of a size large enough to settle by gravitation and a further settled liquid by circulating at least a portion of said partially settled liquid upwardly through a quiet zone horizontally surrounding said mixing zone and there separating said second agglomerate portion from said further settled liquid by gravitation;
Claim 5
Independent Claim 304 words
A method for separating a clarified liquid hydrocarbonaceous oil and an agglomerating agent from a slurry of said liquid hydrocarbonaceous oil and finely divided suspended solids wherein said slurry is charged to a settling zone and held there to allow said solids to agglomerate and separate by gravitation, a clarified and essentially solids-free liquid comprising said hydrocarbonaceous oil and said agglomerating agent is recovered from an upper portion of said settling zone, settled agglomerated solids are conducted from a lower portion of said vessel into a washing zone wherein residual product on said agglomerated solids is removed by washing said solids with an upflowing stream of agglomerating agent, which stream then enters said lower portion of said vessel and mixes with the contents therein, and the resulting washed solids are withdrawn from a lower portion of said washing zone, wherein the improvement comprises: (1) discharging said slurry upwardly into a mixing zone located within an intermediate or upper portion of said vessel; (2) forming within said mixing zone a mixture of said slurry with a downflowing recirculated liquid stream comprising said hydrocarbonaceous oil and said agglomerating agent; (3) forming from said mixture a first portion of agglomerated solids of a size large enough to settle by gravitation and a partially settled liquid by circulating said mixture downwardly into a separating zone positioned above said washing zone and below said mixing zone and separating said first agglomerate portion from said mixture by gravitation; (4) forming from said partially settled liquid a second portion of agglomerated solids of a size large enough to settle by gravitation and a further settled liquid by circulating at least a portion of said partially settled liquid upwardly through a quiet zone horizontally surrounding said mixing zone and there separating said second agglomerate portion from said further settled liquid by gravitation;
Claim 6
Dependent Claim 62 words
(5) providing at least a portion of said recirculated liquid stream by circulating at least a portion of said further settled liquid from said quiet zone into said mixing zone; (6) circulating to said settling zone a portion of at least one of the following: said partially settled liquid from said separating zone and said further settled liquid from said quiet zone.
Claim 7
Dependent Claim 62 words
(5) providing at least a portion of said recirculated liquid stream by circulating at least a portion of said further settled liquid from said quiet zone into said mixing zone; (6) circulating to said settling zone a portion of at least one of the following: said partially settled liquid from said separating zone and said further settled liquid from said quiet zone.

References Cited (Backward Citations)

US3306449A Cited
US2699379A Cited
US3236384A Cited
US3353676A Cited
US4075080A Cited
DE2740079A1 Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1985-11-01 1986-05-03 1986-11-02 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1989-11-01 1990-05-03 1990-11-02 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1993-11-01 1994-05-03 1994-11-02 $7700.00 Window Closed / Lapsed

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