Indirect heat drying method for particulate matter, refined-coal production method, indirect heat drying device, and refined-coal production device

Patent metadata

Field	Value
Publication number	US-9670431-B2
Application number	US-201314423858-A
Country	US
Kind code	B2
Filing date	Sep 18, 2013
Priority date	Nov 16, 2012
Publication date	Jun 6, 2017
Grant date	Jun 6, 2017

Abstract

The purpose of the present invention is to provide an indirect heat drying method and a refined-coal production method, with which the stability of carrier-gas pressure balance can be improved when using indirect heat dryers to dry particulate matter. This indirect heat drying method for particulate matter uses two indirect heat dryers, and is provided with: a step (A) in which particulate matter is dried in a first indirect heat dryer; and a step (B) in which the particulate matter is further dried in a second indirect heat dryer to obtain dried particulate matter. The indirect heat drying method for particulate matter is characterized by being further provided with a step (C) in which first microparticles included in a carrier gas discharged from the first indirect heat dryer are recovered and mixed with the particulate matter supplied to step (B); and a step (D) in which second microparticles included in a carrier gas discharged from the second indirect heat dryer are recovered and mixed with the dried particulate matter obtained in step (B).

First claim

The invention claimed is:

1. An indirect heat drying method for a particulate matter, using two indirect heat drying units each comprising a rotary cylinder located to be freely rotatable around an axis, plural heating tubes arranged inside the rotary cylinder to be parallel with the axis, and a carrier gas passing means that supplies a carrier gas from one out of two sides of the rotary cylinder to be discharged into the other side, the method comprising:
step (A) of supplying the carrier gas into first one of the indirect heat drying units to produce a co-current flow relative to the flow of the particulate matter, thereby drying the particulate matter, and
step (B) of supplying the carrier gas into second one of the indirect heat drying units to produce a counterflow against the flow of the particulate matter, thereby drying the particulate matter further, and
the method further comprising:
step (C) of recovering first fine particles contained in the carrier gas discharged from the first indirect heat drying unit, and mixing the first fine particles with the particulate matter to be supplied to step (B), and
step (D) of recovering second fine particles contained in the carrier gas discharged from the second indirect heat drying unit, and mixing the second fine particles with the dried particulate matter yielded through step (B).

2. The indirect heat drying method for particulate matter according to claim 1 , wherein the second fine particles recovered through step (D) have an average particle diameter of 10 μm or less.

3. The indirect heat drying method for particulate matter according to claim 1 , wherein the ratio by mass of the second fine particles recovered in step (D) to the dried particulate matter yielded through step (B) is from 1/99 to 1/3 both inclusive.

4. A refined-coal production method, comprising:
step (α) of mixing particulate porous coal with an oil to yield a raw material slurry,
step (β) of heating the raw material slurry to yield a dehydrated slurry,
step (γ) of separating the dehydrated slurry into a porous refined-coal and an oil, and
step (δ) of drying the separated porous refined-coal,
wherein in step ( 67 ), the indirect heat drying method for a particulate matter that is recited in claim 1 is used.

5. An indirect heat drying device, comprising a first indirect heat drying unit and a second indirect heat drying unit,
each of the indirect heat drying units comprising a rotary cylinder located to be freely rotatable around an axis, plural heating tubes arranged inside the rotary cylinder to be parallel with the axis, and a carrier gas passing means that supplies a carrier gas from one out of two sides of the rotary cylinder to be discharged into the other side,
the indirect heat drying device being arranged to receive a dried matter yielded from the first indirect heat drying unit as a matter to be dried in the second indirect heat drying unit, and
the carrier gas passing means being a means that supplies the carrier gas into the first indirect heat drying unit to produce a co-current flow relative to the flow of a matter to be dried in the first indirect heat drying unit, and that supplies the carrier gas into the second indirect heat drying unit to produce a counterflow against the flow of the matter to be dried in the second indirect heat drying unit;
the drying device further comprising:
a first recovering means that recovers first fine particles contained in the carrier gas discharged from the first indirect heat drying unit,
a first mixer that mixes the first fine particles with a particulate matter to be supplied into the second indirect heat drying unit,
a recovering means that recovers second fine particles contained in the carrier gas discharged from the second indirect heat drying unit, and
a second mixer that mixes the second fine particles with a dried matter yielded from the second indirect heat drying unit.

6. The refined-coal production device, comprising:
a mixer that mixes a particulate porous coal with an oil to yield a raw material slurry,
a heater that heats the raw material slurry to yield a dehydrated slurry,
a solid/liquid separator that separates the dehydrated slurry into a porous refined-coal and an oil, and
a drier that dries the separated porous refined-coal,
wherein the drier is the indirect heat drying device recited in claim 5 .

7. A refined-coal production method, comprising:
step (α) of mixing particulate porous coal with an oil to yield a raw material slurry,
step (β) of heating the raw material slurry to yield a dehydrated slurry,
step (γ) of separating the dehydrated slurry into a porous refined-coal and an oil, and
step (δ) of drying the separated porous refined-coal,
wherein in step (δ), the indirect heat drying method for a particulate matter that is recited in claim 2 is used.

8. A refined-coal production method, comprising:
step (α) of mixing particulate porous coal with an oil to yield a raw material slurry,
step (β) of heating the raw material slurry to yield a dehydrated slurry,
step (γ) of separating the dehydrated slurry into a porous refined-coal and an oil, and
step (δ) of drying the separated porous refined-coal,
wherein in step (δ), the indirect heat drying method for a particulate matter that is recited in claim 3 is used.

Assignees

• Kobe Steel Ltd

Inventors

• Kinoshita Shigeru
• Takahashi Yoichi
• Watanabe Hiroki
• Katsushima Shinichi

Classifications

• F26B21/25

  partly outside the drying enclosure · CPC title

• C10L9/08

  by heat treatments, e.g. calcining · CPC title

• C10L2290/06

  Heat exchange, direct or indirect · CPC title

• F26B5/08

  by centrifugal treatment · CPC title

• C10L2290/50

  Screws or pistons for moving along solids · CPC title