Apparatus and method for pyrolyzing coal with wide particle size distribution

Patent metadata

Field	Value
Publication number	US-9862890-B2
Application number	US-201214384940-A
Country	US
Kind code	B2
Filing date	Mar 16, 2012
Priority date	Mar 16, 2012
Publication date	Jan 9, 2018
Grant date	Jan 9, 2018

Abstract

A carbonization apparatus for coal with wide particle size distribution, a carbonization apparatus unit, and a carbonization method using the apparatus. The apparatus includes a char discharge outlet, a combustion heating chamber, a coal feeding inlet, a pyrolysis gas exhausting pipe, and two partition plates between which a pyrolysis gas channel is formed. Orifices are provided on the partition plates to form a gas flow path from the fuel bed to the pyrolysis gas channel. The pyrolysis gas channel in the carbonization apparatus permits the gaseous products generated from coal pyrolysis to flow out in a timely manner.

First claim

What is claimed is:

1. A carbonization apparatus for coal with wide particle size distribution, comprising: a char discharge outlet ( 1 ), a combustion heating chamber ( 3 ), a coal feeding inlet ( 5 ), and a pyrolysis gas exhausting pipe ( 4 ), characterized in that two partition plates between which a pyrolysis gas channel ( 2 ) is formed are further provided in the carbonization apparatus, and orifices are provided on the partition plates to form a gas flow path from a fuel bed to the pyrolysis gas channel ( 2 ).

2. The carbonization apparatus according to claim 1 , characterized in that each of the partition plates is a plate ( 9 ) having sieved orifices, or a plate ( 10 ) having a window blind structure formed by arranging many solid plates in parallel with intervals.

3. The carbonization apparatus according to claim 1 , characterized in that the pyrolysis gas channel ( 2 ) has its upper part closed and is connected with the pyrolysis gas exhausting pipe ( 4 ), and there is a certain distance between the top end of the channel and a top roof of the carbonization apparatus to enable even fuel feeding.

4. The carbonization apparatus according to claim 1 , characterized in that the lower end of the pyrolysis gas channel ( 2 ) is open to the char discharge outlet ( 1 ) mounted on the bottom of the carbonization apparatus, which is used to discharge char in the pyrolysis gas channel ( 2 ).

5. The carbonization apparatus according to claim 1 , characterized in that a plate-type internal ( 6 ) is further provided in the carbonization apparatus; the plate-type internal ( 6 ) being mounted perpendicular to the upper and lower surfaces of the carbonization apparatus, wherein one end of the plate-type internal ( 6 ) is connected to one heating wall ( 8 ) and the plate-type internal ( 6 ) extends from the heating wall ( 8 ) into the fuel bed.

6. A carbonization apparatus unit for coal with wide particle size distribution, which consists of numbers of the carbonization apparatus of claim 1 arranged in parallel, wherein the upper part of the pyrolysis gas channel ( 2 ) in each carbonization apparatus is connected to its respective pyrolysis gas exhausting pipe ( 4 ), the pyrolysis gas exhausting pipe ( 4 ) from each carbonization apparatus are connected to a main gas collection pipeline ( 7 ), and gaseous pyrolysis products exhaust from the main gas collection pipeline ( 7 ).

7. The carbonization apparatus unit according to claim 6 , characterized in that each of the partition plates is a plate ( 9 ) having sieved orifices, or a plate ( 10 ) having a window blind structure formed by arranging many solid plates in parallel with intervals.

8. The carbonization apparatus unit according to claim 6 , characterized in that a plate-type internal ( 6 ) is further provided in each carbonization apparatus; the plate-type internal ( 6 ) being mounted perpendicular to the upper and lower surfaces of the carbonization apparatus, wherein one end of the plate-type internal ( 6 ) is connected to one heating wall ( 8 ) and the plate-type internal ( 6 ) extends from the heating wall ( 8 ) into the fuel bed.

9. A carbonization method for coal with wide particle size distribution using the carbonization apparatus of claim 1 , the carbonization method comprising the steps of:
1) loading the coal for pyrolysis into the carbonization apparatus via the coal feeding inlet ( 5 ), wherein the coal is packed in both sides of the pyrolysis gas channel ( 2 );
2) heating the coal for pyrolysis in the carbonization apparatus by raising the temperature of a heating wall ( 8 ) with heat generated in the combustion heating chamber ( 3 ), and by utilizing heat carried by gaseous pyrolysis products when they flow to the pyrolysis gas channel ( 2 );
3) collecting the gaseous pyrolysis products into the pyrolysis gas channel ( 2 ) through the orifices on the wall surface of the pyrolysis gas channel ( 2 ) and exhausting them from the carbonization apparatus through the pyrolysis gas exhausting pipe ( 4 ); and
4) discharging a solid product from the char discharge outlet ( 1 ).

10. The carbonization method for coal with wide particle size distribution according to claim 9 , characterized in that a plate-type internal ( 6 ) is further provided in the carbonization apparatus, wherein the plate-type internal ( 6 ) extends into the fuel bed to enhance the heat and mass transfer by the plate-type internal ( 6 ).

Assignees

• Xu Goangwen
• Han Jiangze
• Wu Rongcheng
• Zhang Chun
• Gao Shiqiu
• Zhang Juwei
• Inst Process Eng Cas

Inventors

• Xu Goangwen
• Han Jiangze
• Wu Rongcheng
• Zhang Chun
• Gao Shiqiu
• Zhang Juwei

Classifications

• C10B27/02

  with outlets arranged at different levels in the chamber · CPC title

• C10B53/04 Primary

  of powdered coal · CPC title

• C10B47/02

  with stationary charge · CPC title

• C10B5/10

  with heat-exchange devices · CPC title

• C10B47/16

  with indirect heating means both inside and outside the retorts · CPC title