Coal reforming method and coal reforming apparatus

Patent metadata

Field	Value
Publication number	US-9309465-B2
Application number	US-201314415107-A
Country	US
Kind code	B2
Filing date	Jul 19, 2013
Priority date	Jul 20, 2012
Publication date	Apr 12, 2016
Grant date	Apr 12, 2016

Abstract

A coal reforming method includes: drying; performing carbonizing; and cooling. (1) In the drying, coal is classified into coarse coal and fine coal while being dried, and heat obtained by burning at least a portion of the fine coal and at least a portion of the carbonizing gas is used as a heat source during the drying or the carbonizing. (2) In the cooling, the char is classified while being cooled to separate fine char from the char, and heat obtained by burning at least a portion of the fine char and at least a portion of the carbonizing gas is used as a heat source during the drying or the carbonizing. At least any one of (1) and (2) is performed.

First claim

The invention claimed is:

1. A coal reforming method comprising:
classifying a coal into a coarse coal and a fine coal while drying the coal in a fluidized bed drying and classifying device;
performing carbonizing on the coarse coal, by a carbonizing device, so as to reform the coarse coal into a carbonizing gas and a char;
obtaining a heat by supplying at least a portion of the carbonizing gas or an external fuel, and at least a portion of the fine coal, to a combustor and burning the portions; and
supplying the heat obtained by burning the portions to at least one of the fluidized bed drying and classifying device and the carbonizing device as a heat source.

2. The coal reforming method according to claim 1 , further comprising:
mixing at least a portion of a flue gas discharged from the fluidized bed drying and classifying device with a combustion gas supplied from the combustor to the at least one of the fluidized bed drying and classifying device and the carbonizing device.

3. The coal reforming method according to claim 1 , further comprising:
supplying a further portion of the fine coal obtained by the fluidized bed drying and classifying device to the carbonizing device.

4. The coal reforming method according to claim 3 ,
wherein the further portion of the fine coal supplied to the carbonizing device is supplied to the carbonizing device after being formed singly or together with the coarse coal.

5. The coal reforming method according to claim 1 ,
wherein the carbonizing device is of an indirect heating type which is supplied with a heating gas from an outside source,
wherein the heating gas from the outside source is selected from the group consisting of a combustion gas discharged from the combustor, a gas obtained by mixing the combustion gas with another gas, a gas obtained by supplying the combustion gas to a heat exchanger, and a gas manufactured by using the external fuel, and
wherein the coal reforming method further includes supplying a heating gas discharged from the carbonizing device to the fluidized bed drying and classifying device.

6. The coal reforming method according to claim 1 , further comprising:
mixing at least a portion of a flue gas discharged from the fluidized bed drying and classifying device with a heating gas supplied to the fluidized bed drying and classifying device.

7. The coal reforming method according to claim 1 , further comprising:
supplying a gas, which is discharged from the carbonizing device and is different from the carbonizing gas, to the fluidized bed drying and classifying device as a heating gas; and
controlling a flow rate of the heating gas, which is a fluidizing gas supplied to the fluidized bed drying and classifying device, based on a moisture content of the coarse coal at an outlet of the fluidized bed drying and classifying device.

8. A coal reforming apparatus comprising:
a fluidized bed drying and classifying device which classifies a coal into a coarse coal and a fine coal while drying the coal;
a carbonizing device which performs carbonizing on the dried coarse coal, so as to reform said dried coarse coal into a carbonizing gas and a char; and
a combustor which is supplied with at least a portion of the carbonizing gas or an external fuel, and at least a portion of the fine coal and which supplies a heat, obtained by burning the carbonizing gas or the external fuel and the portion of the fine coal, to at least one of the fluidized bed drying and classifying device and the carbonizing device as a heat source.

9. The coal reforming apparatus according to claim 8 ,
wherein at least a portion of a flue gas discharged from the fluidized bed drying and classifying device is mixed with a combustion gas supplied from the combustor to the at least one of the fluidized bed drying and classifying device and the carbonizing device as the heat source.

10. The coal reforming apparatus according to claim 8 ,
wherein a further portion of the fine coal obtained by the fluidized bed drying and classifying device is supplied to the carbonizing device.

11. The coal reforming apparatus according to claim 10 , further comprising:
a forming machine which forms the fine coal singly or together with the coarse coal,
wherein the further portion of the fine coal obtained by the fluidized bed drying and classifying device is supplied to the carbonizing device after being formed singly or together with the coarse coal by the forming machine.

12. The coal reforming apparatus according to claim 8 ,
wherein the carbonizing device is of an indirect heating type which is supplied with a heating gas from an outside source,
wherein the heating gas from the outside source is selected from the group consisting of a combustion gas discharged from the combustor, a gas obtained by mixing the combustion gas with another gas, a gas obtained by supplying the combustion gas to a heat exchanger, and a gas manufactured by using the external fuel, and
wherein a heating gas discharged from the carbonizing device is supplied to the fluidized bed drying and classifying device.

13. The coal reforming apparatus according to claim 8 ,
wherein at least a portion of a flue gas discharged from the fluidized bed drying and classifying device is mixed with a heating gas supplied to the fluidized bed drying and classifying device as the heat source.

14. The coal reforming apparatus according to claim 8 , further comprising:
a controller,
wherein the carbonizing device supplies a gas, which is different from the carbonizing gas, to the fluidized bed drying and classifying device as a heating gas, and
the controller identifies a moisture content of the coarse coal at an outlet of the fluidized bed drying and classifying device, and controls a flow rate of the heating gas, which is a fluidizing gas supplied to the fluidized bed drying and classifying device, based on the moisture content of the coarse coal.

15. A coal reforming method comprising:
drying a coal by a dryer;
performing carbonizing on the dried coal by a carbonizing device, so as to reform the dried coal into a carbonizing gas and a char;
classifying the char while cooling the char by a fluidized bed cooling and classifying device to separate a fine char from the char;
obtaining a heat by supplying at least a portion of the carbonizing gas or an external fuel, and at least a portion of the fine char, to a combustor and burning the portions; and
supplying the heat obtained by burning the portions to at least one of the dryer and the carbonizing device as a heat source.

16. The coal reforming method according to claim 15 , further comprising:
supplying a flue gas discharged from the at least one of the dryer and the fluidized bed cooling and classifying device to the fluidized bed cooling and classifying device as a cooling gas.

17. The coal reforming method according to claim 15 , further comprising:
mixing at least a portion of a flue gas discharged from the dryer with a combustion gas supplied from the combustor to the at least one of the dryer and the carbonizing device.

18. The coal reforming method according to claim 15 ,
wherein the carbonizing device is of an indirect heating type which is supplied with a heating gas from an outside source,
wherein the heating gas from the outside source is selected from the group consisting of a combustion gas discharged from the combustor, a gas obtained by mixing the combustion as with another gas, a gas obtained by supplying the combustion gas to a heat exchanger, and a gas manufactured by us

Assignees

• Nippon Steel & Sumitomo Metal Corp
• Nippon Steel & Sumikin Eng Co

Inventors

• Kozuru Hiroyuki
• Kanei Akira
• Tomita Katsuyuki
• Kosuge Katsushi
• Kobayashi Atsushi

Classifications

• C10B53/04

  of powdered coal · CPC title

• F26B23/028

  using solid fuel; burning the dried product · CPC title

• C10B57/10 Primary

  Drying · CPC title

• F26B17/10

  with movement performed by fluid currents, e.g. issuing from a nozzle, {e.g. pneumatic, flash, vortex or entrainment dryers}(F26B3/08 takes precedence) · CPC title

• C10B47/30

  in rotary ovens or retorts · CPC title