# US 10,502,489 B2 · Coal slurry preheater and coal gasification system and method using the same

> Agents: this data is available as JSON from the patentgrep API and MCP server — see https://patentgrep.com/llms.txt

- Number: US 10,502,489 B2
- Document ID: US10502489B2
- Status: Granted
- Kind: B2
- Application number: 15/004,250
- Filed: 2016-01-22
- Published: 2017-01-05
- Granted: 2019-12-10
- Earliest claimed: 2015-01-23
- Assignees: Air Products and Chemicals, Inc.
- Applicants: Air Products and Chemicals, Inc.
- Inventors: Liang Yu; Junli Xue; Xijing Bi; Jing Lv
- Web page: https://patentgrep.com/patent/US10502489B2

## CPC

- F27D 13/00: Apparatus for preheating charges; Arrangements for preheating charges
- C10J 3/506: {for entrained flow gasifiers}
- C10J 3/526: {for entrained flow gasifiers}
- F27D 17/18: for preheating solid materials
- C10J 2300/0926: Slurries comprising bio-oil or bio-coke, i.e. charcoal, obtained, e.g. by fast pyrolysis of biomass
- C10J 2300/093: Coal
- C10J 2300/1861: Heat exchange between at least two process streams
- C10J 2300/1884: with one stream being synthesis gas
- Y02P 20/145: the feedstock being materials of biological origin
- F27D: DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
- C10J: PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES (synthesis gas from liquid or gaseous hydrocarbons C01B; underground gasification of minerals E21B43/295); CARBURETTING AIR OR OTHER GASES
- Y02P: CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS

## 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.

## Claims

### Claim 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.

### Claim 2 (depends on 1)

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.

### Claim 3 (depends on 2)

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.

### Claim 4 (depends on 3)

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

### Claim 5 (depends on 3)

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

### Claim 6 (depends on 1)

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.

### Claim 7 (depends on 1)

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.

### Claim 8 (depends on 1)

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

### Claim 9 (depends on 1)

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.

### Claim 10 (depends on 1)

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.

### Claim 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.

### Claim 12 (depends on 11)

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.

### Claim 13 (depends on 11)

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.

### Claim 14 (depends on 11)

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.

### Claim 15 (depends on 11)

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

### Claim 16 (depends on 11)

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

### Claim 17 (depends on 11)

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.