Patent US6326550B1 successfully refreshed from Google Patents.
← Back to Patent Explorer
US4198212A Expired / Lapsed US ⏱️ 0.0 years remaining

Coal gasification effluent treatment

Assignee: Lummus Technology LLC
•
Filing: 1978-08-17
•
Granted: 1980-04-15
•
Expires: 1998-08-17
📄 Original PDF 🌐 Google Patents 🔄 Sync Now

Abstract

Abstract Coal is gasified to produce a coal gasification effluent and a char residue. The char residue is cooled by indirect heat transfer in a char bed, and the coal gasification effluent is passed through the cool char bed to effect cooling of the coal gasification effluent, with tars and oil present in the effluent being absorbed by the char bed. In this manner, the gasification effluent is cooled without fouling of heat transfer surfaces, and tars and oils are effectively removed therefrom.

Inventors

  • 👤 Utah Tsao

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-03 04:52
CPC Classifications
C; C10; C10J; C10J3/00; C10J3/72; C10J3/82; C10J3/84; C10B; C10B49/00; C10B49/02; C10B49/04; C10B49/08; C10B49/10; C10J3/46; C10J3/48; C10J3/482; C10J3/54; C10J3/78; C10J2300/00; C10J2300/09; C10J2300/0913; C10J2300/093; C10J2300/0953; C10J2300/0959; C10J2300/0973; C10J2300/0976; C10J2300/18; C10J2300/1807; C10J2300/1861; C10J2300/1884; C10J2300/1892

Claims Analysis

Total Claims: 9
Claim 1
Independent Claim 170 words
In a process for the gasification of coal in a coal gasification zone to produce a solid char residue and a coal gasification effluent containing tar and oils, the improvements comprising: separately withdrawing said char and said coal gasification effluent from said coal gasification zone; suspending said withdrawn char in said withdrawn coal gasification effluent; passing said char suspended in said gasification effluent into a fluidized char bed maintained in a char cooling zone; cooling and maintaining char in said bed at a temperature of from 220° F. to 600° F. by indirect heat transfer, whereby said coal gasification effluent, containing tar and oils, passing through said cooled char bed is cooled and tar and oils are separated therefrom by absorbing the tar and oils on said char bed; and removing cooled char from the coal gasification process without recycle of any cooled char to the coal gasification zone by withdrawing cooled char from said char bed, whereby char produced in the coal gasification is cooled prior to removal thereof.
Claim 2
Dependent Claim 170 words
In a process for the gasification of coal in a coal gasification zone to produce a solid char residue and a coal gasification effluent containing tar and oils, the improvements comprising: separately withdrawing said char and said coal gasification effluent from said coal gasification zone; suspending said withdrawn char in said withdrawn coal gasification effluent; passing said char suspended in said gasification effluent into a fluidized char bed maintained in a char cooling zone; cooling and maintaining char in said bed at a temperature of from 220° F. to 600° F. by indirect heat transfer, whereby said coal gasification effluent, containing tar and oils, passing through said cooled char bed is cooled and tar and oils are separated therefrom by absorbing the tar and oils on said char bed; and removing cooled char from the coal gasification process without recycle of any cooled char to the coal gasification zone by withdrawing cooled char from said char bed, whereby char produced in the coal gasification is cooled prior to removal thereof.
Claim 3
Dependent Claim 23 words
The process of claim 1 wherein the char bed is cooled and maintained at a temperature of from 300° F. to 500° F.
Claim 4
Dependent Claim 26 words
The process of claim 2 wherein the char is steam stripped prior to withdrawal from the char cooling zone to strip entrained gases from the char.
Claim 5
Dependent Claim 16 words
The process of claim 3 wherein the withdrawn char is employed as fuel in a boiler.
Claim 6
Dependent Claim 17 words
The process of claim 2 wherein the coal gasification zone is a fluidized coal bed gasification reactor.
Claim 7
Dependent Claim 31 words
The process of claim 3 wherein the coal gasification zone is operated at a temperature of from 1200° F. to 2000° F. and a pressure of from 10 to 1500 psig.
Claim 8
Dependent Claim 19 words
The process of claim 6 wherein the char is cooled by indirect heat transfer with water to generate steam.
Claim 9
Dependent Claim 29 words
The process of claim 7 wherein the steam is generated at a temperature of from 280° F. to 550° F. and a pressure of from 35 to 1035 psig.

References Cited (Backward Citations)

US2689787A Cited
US2687950A Cited
US2591595A Cited
US3817723A Cited
US3852048A Cited
US3991557A Cited
US4049570A Cited
DE2541574A1 Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1983-04-15 1983-10-15 1984-04-15 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1987-04-15 1987-10-15 1988-04-15 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1991-04-15 1991-10-15 1992-04-15 $7700.00 Window Closed / Lapsed

Assigned Categories & Tags

No categories assigned to this patent yet.

Assign Category Tag