Method and apparatus for heating fluidizing agent and use

Patent metadata

Field	Value
Publication number	US-2024253001-A1
Application number	US-202218562039-A
Country	US
Kind code	A1
Filing date	May 19, 2022
Priority date	May 20, 2021
Publication date	Aug 1, 2024
Grant date	—

Abstract

The invention relates to a method and an apparatus for heating a fluidizing agent for a fluidized bed reactor in which the fluidizing agent is fed to the fluidized bed reactor. The fluidizing agent is heated by heat of the process gas and/or heat of flue gas in at least one heat exchanger in which the heat of the process gas and/or the heat of the flue gas is utilized after the fluidized bed reactor, and the heated fluidizing agent is fed to the bottom of the fluidized bed reactor. Further, the invention relates to the use of the method.

First claim

1 . A method for heating a fluidizing agent for a fluidized bed reactor in which the fluidizing agent is fed to the fluidized bed reactor, wherein the method comprises
treating raw material comprising plastic by gasifying in the fluidized bed reactor selected from a fluidized bed gasifier having at least one fluidized bed comprising a bed material to form process gas, heating the fluidizing agent which is steam by heat of the process gas and cooling the process gas in a first heat exchanger, supplying the fluidizing agent to a second heat exchanger, and heating the fluidizing agent by heat of flue gas and cooling the flue gas in the second heat exchanger wherein the heat of the process gas and the heat of the flue gas formed in a bed material heating device is utilized after the fluidized bed reactor, and feeding the heated fluidizing agent to a bottom of the fluidized bed reactor.

2 . (canceled)

3 . The method according to claim 1 , wherein the process gas is supplied to the heat exchanger in which the process gas is cooled and the fluidizing agent is heated.

4 . The method according to claim 1 , wherein the process gas is supplied from the fluidized bed reactor to a cyclone in which at least bed material is separated, and the process gas is supplied from the cyclone to the heat exchanger in which the process gas is cooled and the fluidizing agent is heated.

5 . The method according to claim 1 , wherein the process gas is a product gas from a gasifier.

6 . The method according to claim 1 , wherein the flue gas is supplied to the heat exchanger, in which the flue gas is cooled and the fluidizing agent is heated.

7 . The method according to claim 1 , wherein the bed material of the fluidized bed reactor is heated in the bed material heating device, and the flue gas from the bed material heating device is supplied to the heat exchanger, in which the flue gas is cooled and the fluidizing agent is heated.

8 . The method according to claim 1 , wherein the flue gas from the bed material heating device is supplied to a cyclone in which bed material is separated from the flue gas, and the flue gas is supplied to the heat exchanger.

9 - 10 . (canceled)

11 . An apparatus for heating a fluidizing agent for a fluidized bed reactor, in which the apparatus comprises the fluidized bed reactor and the fluidizing agent is fed to the fluidized bed reactor, wherein
the fluidized bed reactor is a fluidized bed gasifier having at least one fluidized bed comprising a bed material in which raw material comprising plastic is treated by gasifying to form process gas, and the apparatus comprises at least one bed material heating device in which a flue gas is formed, and at least two heat exchangers in which the fluidizing agent which is steam is heated by heat of the process gas and the process gas is cooled in a first heat exchanger and the fluidizing agent is heated by heat of the flue gas and the flue gas is cooled in a second heat exchanger, wherein the heat of the process gas and the heat of the flue gas is utilized after the fluidized bed reactor, and at least one feeding means for feeding the heated fluidizing agent to a bottom of the fluidized bed reactor.

12 . The apparatus according to claim 11 , wherein the apparatus comprises the bed material heating device in which the bed material is heated.

13 . The apparatus according to claim 11 , wherein the heat exchanger is arranged after the bed material heating device in which the bed material of the fluidized bed reactor is heated and from which the flue gas is supplied to the heat exchanger.

14 . The apparatus according to claim 11 , wherein the apparatus comprises at least one cyclone, and the heat exchanger is arranged after the cyclone in which the bed material is separated from the process gas and from the flue gas.

15 - 16 . (canceled)

17 . A use of the method according to claim 1 , wherein the method is used in a production of hydrocarbons, treatment of plastic containing raw material, gasification, pyrolysis, heat-treatment process, catalytic cracking or their combinations.

Assignees

• Teknologian Tutkimuskeskus Vtt Oy

Inventors

• Nieminen Matti

Classifications

• C10J3/46

  Gasification of granular or pulverulent flues in suspension · CPC title

• C10J3/80

  with arrangements for preheating the blast or the water vapour · CPC title

• B01J8/1836 Primary

  Heating and cooling the reactor (B01J8/42 takes precedence) · CPC title

• C10J2300/1253

  by injecting hot gas · CPC title

• C10J2300/0946

  Waste, e.g. MSW, tires, glass, tar sand, peat, paper, lignite, oil shale · CPC title