Coal slurry preheater and coal gasification system and method using the same

Patent metadata

Field	Value
Publication number	US-10502489-B2
Application number	US-201615004250-A
Country	US
Kind code	B2
Filing date	Jan 22, 2016
Priority date	Jan 23, 2015
Publication date	Dec 10, 2019
Grant date	Dec 10, 2019

Abstract

This invention involves with a gasification system, which includes a gasifier, which gasifier comprises a gasification chamber for producing syngas from coal slurry and a quench chamber for cooling the syngas from the gasification chamber. The mentioned gasification system also comprises preheater located in the quench chamber for utilizing heat in the quench chamber to preheat the coal slurry before the coal slurry enters the gasification chamber. Wherein, the preheater comprises a pipe device defining a passage for the coal slurry to pass through, the passage in communication with the gasification chamber and upstream of the gasification chamber in a flow direction of the coal slurry. This invention also involves with a preheater used in the mentioned gasification system and the gasification method of the mentioned gasification device.

First claim

What is claimed is:

1. A gasification system, comprising:
a gasifier comprising a gasification chamber and a quench chamber, wherein the gasification chamber is configured to produce syngas from a coal slurry, and the quench chamber is configured to cool the syngas from the gasification chamber by transferring heat into a quench liquid;
a coal slurry source; and
a preheater located in the quench chamber at least partially below a liquid level of the quench liquid, wherein the preheater comprises a passage extending between a first coal slurry inlet and a coal slurry outlet, the first coal slurry inlet is coupled to the coal slurry source, the coal slurry outlet is coupled to a second coal slurry inlet into the gasification chamber, and the preheater is configured to transfer heat from the quench liquid to the coal slurry in the passage to preheat the coal slurry before the coal slurry enters the gasification chamber through the second coal slurry inlet.

2. The gasification system according to claim 1 , further comprising a downcomer pipe configured to flow the syngas from the gasification chamber into the quench chamber below the liquid level of the quench liquid, and wherein the first passage of the preheater is disposed between an outer face of the downcomer pipe and an inner face of the quench chamber.

3. The gasification system according to claim 2 , wherein the preheater comprises a pipe substantially wound as a cylinder, the cylinder having an outer diameter smaller than an inner diameter of the quench chamber and an inner diameter larger than an outer diameter of the downcomer pipe.

4. The gasification system according to claim 3 , wherein the cylinder is radially closer to the quench chamber than the downcomer pipe.

5. The gasification system according to claim 3 , wherein the pipe is spirally wound or is corrugated folded.

6. The gasification system according to claim 1 , wherein the quench liquid comprises water, the liquid level comprises a water level of the water, and the preheater is arranged under the water level at a normal operational condition in the quench chamber.

7. The gasification system according to claim 1 , further comprising a high pressure pump connected between the coal slurry outlet of the preheater and the second coal slurry inlet into the gasification chamber.

8. The gasification system according to claim 1 , further comprising a high pressure pump upstream of the first coal slurry inlet of the preheater.

9. The gasification system according to claim 1 , comprising a bypass conduit coupled to the first coal slurry inlet and the coal slurry outlet, wherein the bypass conduit extends outside of the gasifier to bypass the preheater, wherein at least one valve is configured to control flows of the coal slurry through the passage in the preheater and through the bypass conduit.

10. The gasification system according to claim 1 , wherein the preheater is disposed only in the quench chamber entirely below a bottom wall of the gasification chamber.

11. A gasification system, comprising:
a gasifier comprising a gasification chamber and a quench chamber, wherein the gasification chamber is configured to produce a syngas from a coal slurry, and the quench chamber is configured to cool the syngas from the gasification chamber by transferring heat into a quench liquid;
a coal slurry source;
a preheater located in the quench chamber, wherein the preheater comprises a passage extending between a first coal slurry inlet and a coal slurry outlet, the first coal slurry inlet is coupled to the coal slurry source, the coal slurry outlet is coupled to a second coal slurry inlet into the gasification chamber, and the preheater is configured to transfer heat from the quench chamber to the coal slurry in the passage to preheat the coal slurry before the coal slurry enters the gasification chamber through the second coal slurry inlet; and
a downcomer pipe configured to flow the syngas from the gasification chamber into the quench chamber, wherein the downcomer pipe comprises a first end coupled to the gasification chamber and a second end disposed below a liquid level of the quench liquid in the quench chamber, wherein the preheater is disposed about the downcomer pipe, and wherein the preheater is disposed between the first end of the downcomer pipe and a bottom of the quench chamber.

12. The gasification system according to claim 11 , wherein the preheater comprises an annular structure disposed about the downcomer pipe, wherein the preheater has an outer diameter smaller than an inner chamber diameter of the quench chamber and an inner diameter larger than an outer pipe diameter of the downcomer pipe, and wherein the preheater is disposed between an outer face of the downcomer pipe and an inner face of the quench chamber and is arranged entirely below the first end of the downcomer pipe.

13. The gasification system according to claim 11 , wherein the quench chamber comprises the quench liquid disposed at the liquid level, and the preheater is submerged in the quench liquid entirely below the liquid level.

14. The gasification system according to claim 11 , further comprising a high pressure pump connected between the coal slurry outlet of the preheater and the second coal slurry inlet into the gasification chamber.

15. The gasification system according to claim 11 , further comprising a high pressure pump upstream of the first coal slurry inlet of the preheater.

16. The gasification system according to claim 11 , wherein the preheater comprises a pipe that is spirally wound or is corrugated folded.

17. The gasification system according to claim 11 , wherein the preheater is disposed only in the quench chamber entirely below a bottom wall of the gasification chamber.

Assignees

• Air Prod & Chem

Inventors

• Yu Liang
• Xue Junli
• Bi Xijing
• Lv Jing

Classifications

• C10J2300/1884

  with one stream being synthesis gas · CPC title

• F27D13/00 Primary

  Apparatus for preheating charges; Arrangements for preheating charges · CPC title

• C10J2300/1861

  Heat exchange between at least two process streams · CPC title

• C10J2300/0926

  Slurries comprising bio-oil or bio-coke, i.e. charcoal, obtained, e.g. by fast pyrolysis of biomass · CPC title

• C10J3/506

  for entrained flow gasifiers · CPC title