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US4558651A Expired / Lapsed US ⏱️ 0.0 years remaining

Fired heater for coal liquefaction process

Assignee: International Coal Refining Co
•
Filing: 1983-10-19
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Granted: 1985-12-17
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Expires: 2003-10-19
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Abstract

Abstract A fired heater for a coal liquefaction process is operated under conditions to maximize the slurry slug frequency and thereby improve the heat transfer efficiency. The operating conditions controlled are (1) the pipe diameter and pipe arrangement, (2) the minimum coal/solvent slurry velocity, (3) the maximum gas superficial velocity, and (4) the range of the volumetric flow velocity ratio of gas to coal/solvent slurry.

Inventors

  • 👤 David H. S. Ying
  • 👤 Wayne T. McDermott
  • 👤 Edwin N. Givens

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-30 18:56
CPC Classifications
C; C10; C10G; C10G1/00; C10G1/06; C10G1/065

Claims Analysis

Total Claims: 11
Claim 1
Independent Claim 124 words
A method of operating a fired heater for heating a three-phase mixture of hydrogen gas and a coal/solvent slurry flowing from a slurry preparation stage to a dissolver stage in a coal liquefaction process comprising: (1) passing the three-phase mixture through the fired heater by way of a substantially horizontal pipe; (2) passing the coal/solvent slurry through said pipe at a superficial velocity greater than 5 feet per second (1.52 m/sec) and less than 25 feet per second (7.62 m/sec); (3) the pipe diameter being less than 6 inches (15.2 cm); (4) maintaining the gas superficial velocity to be less than 3 feet per second (0.91 m/sec); and (5) maintaining the volumetric flow velocity ratio of gas to coal/solvent slurry between 0.1 and 0.7.
Claim 2
Independent Claim 124 words
A method of operating a fired heater for heating a three-phase mixture of hydrogen gas and a coal/solvent slurry flowing from a slurry preparation stage to a dissolver stage in a coal liquefaction process comprising: (1) passing the three-phase mixture through the fired heater by way of a substantially horizontal pipe; (2) passing the coal/solvent slurry through said pipe at a superficial velocity greater than 5 feet per second (1.52 m/sec) and less than 25 feet per second (7.62 m/sec); (3) the pipe diameter being less than 6 inches (15.2 cm); (4) maintaining the gas superficial velocity to be less than 3 feet per second (0.91 m/sec); and (5) maintaining the volumetric flow velocity ratio of gas to coal/solvent slurry between 0.1 and 0.7.
Claim 3
Dependent Claim 19 words
A method according to claim 1 wherein the pipe length to diameter ratio is greater than 100 to 1.
Claim 4
Dependent Claim 18 words
A method according to claim 1 wherein the residence time within the heater is 10 minutes or less.
Claim 5
Dependent Claim 18 words
The method according to claim 1 wherein the outlet temperature of the heater is 650°-850° F. (343°-454° C.).
Claim 6
Dependent Claim 31 words
The method according to claim 1 wherein the pipe length to diameter ratio is greater than 100 to 1 and the residence time within the heater is 10 minutes or less.
Claim 7
Dependent Claim 23 words
The method according to claim 1 wherein the pipe is inclined at an angle in the direction of flow of approximately one degree.
Claim 8
Dependent Claim 19 words
A method according to claim 6 wherein the pipe length to diameter ratio is greater than 100 to 1.
Claim 9
Dependent Claim 18 words
A method according to claim 6 wherein the residence time within the heater is 10 minutes or less.
Claim 10
Dependent Claim 18 words
The method according to claim 6 wherein the outlet temperature of the heater is 650°-850° F. (343°-454° C.
Claim 11
Dependent Claim 31 words
The method according to claim 6 wherein the pipe length to diameter ratio is greater than 100 to 1 and the residence time within the heater is 10 minutes or less.

References Cited (Backward Citations)

US3855070A Cited
US3951615A Cited
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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) 1988-12-16 1989-06-17 1989-12-17 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1992-12-16 1993-06-17 1993-12-17 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1996-12-16 1997-06-17 1997-12-17 $7700.00 Window Closed / Lapsed

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