MY189567A - Reaction chamber for exothermic and endothermic reactions - Google Patents

Reaction chamber for exothermic and endothermic reactions

Info

Publication number
MY189567A
MY189567A MYPI2017701436A MYPI2017701436A MY189567A MY 189567 A MY189567 A MY 189567A MY PI2017701436 A MYPI2017701436 A MY PI2017701436A MY PI2017701436 A MYPI2017701436 A MY PI2017701436A MY 189567 A MY189567 A MY 189567A
Authority
MY
Malaysia
Prior art keywords
inner chamber
exothermic
pipes
discharge outlet
chamber
Prior art date
Application number
MYPI2017701436A
Inventor
Bin Halim Rasip Amin
Original Assignee
Bin Halim Rasip Amin
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Bin Halim Rasip Amin filed Critical Bin Halim Rasip Amin
Priority to MYPI2017701436A priority Critical patent/MY189567A/en
Priority to PCT/MY2018/050006 priority patent/WO2018199738A1/en
Priority to CN201880004743.2A priority patent/CN110545907B/en
Publication of MY189567A publication Critical patent/MY189567A/en

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B32/00—Carbon; Compounds thereof
    • C01B32/40—Carbon monoxide
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/0015—Feeding of the particles in the reactor; Evacuation of the particles out of the reactor
    • B01J8/004—Feeding of the particles in the reactor; Evacuation of the particles out of the reactor by means of a nozzle
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
    • B01J8/04—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds
    • B01J8/0446—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the flow within the beds being predominantly vertical
    • B01J8/0476—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the flow within the beds being predominantly vertical in two or more otherwise shaped beds
    • B01J8/048—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the flow within the beds being predominantly vertical in two or more otherwise shaped beds the beds being superimposed one above the other
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
    • B01J8/04—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds
    • B01J8/0496—Heating or cooling the reactor
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B32/00—Carbon; Compounds thereof
    • C01B32/50—Carbon dioxide
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/02—Fixed-bed gasification of lump fuel
    • C10J3/20—Apparatus; Plants
    • C10J3/22—Arrangements or dispositions of valves or flues
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008—Controlling the process
    • B01J2208/00017—Controlling the temperature
    • B01J2208/00106—Controlling the temperature by indirect heat exchange
    • B01J2208/00309—Controlling the temperature by indirect heat exchange with two or more reactions in heat exchange with each other, such as an endothermic reaction in heat exchange with an exothermic reaction
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00796—Details of the reactor or of the particulate material
    • B01J2208/00884—Means for supporting the bed of particles, e.g. grids, bars, perforated plates
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049—Controlling or regulating processes
    • B01J2219/00051—Controlling the temperature
    • B01J2219/00074—Controlling the temperature by indirect heating or cooling employing heat exchange fluids
    • B01J2219/00117—Controlling the temperature by indirect heating or cooling employing heat exchange fluids with two or more reactions in heat exchange with each other, such as an endothermic reaction in heat exchange with an exothermic reaction

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Inorganic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Carbon And Carbon Compounds (AREA)

Abstract

An apparatus (100) for simultaneous exothermic and endothermic reactions comprising a generally cylindrical outer chamber (1) having a top opening (11), a bottom discharge outlet (13), at least one gas outlet (15), and a throat (16) near the bottom discharge outlet (13); a cylindrical inner chamber (2) having perforations in its side and bottom, the inner chamber (2) coaxially disposed within the outer chamber (1); a plurality of interconnected pipes (3) between the inner (2) and outer chambers (1) and having at least one gas inlet (31) and at least one gas outlet (32), each pipe (3) having a top charging inlet (33) and a bottom discharge outlet (34); and at least a pair of electrodes (8) surrounding the inner chamber (2), wherein the inner chamber (2) can be charged with carbonaceous materials for the exothermic reaction while the pipes (3) can be pre-loaded with carbon-coated pellets for the endothermic reaction, such that the pipes (3) are able to absorb heat released from the exothermic reaction in the inner chamber (2).
MYPI2017701436A 2017-04-25 2017-04-25 Reaction chamber for exothermic and endothermic reactions MY189567A (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
MYPI2017701436A MY189567A (en) 2017-04-25 2017-04-25 Reaction chamber for exothermic and endothermic reactions
PCT/MY2018/050006 WO2018199738A1 (en) 2017-04-25 2018-02-12 Reaction chamber for exothermic and endothermic reactions
CN201880004743.2A CN110545907B (en) 2017-04-25 2018-02-12 Reaction chambers for exothermic and endothermic reactions

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
MYPI2017701436A MY189567A (en) 2017-04-25 2017-04-25 Reaction chamber for exothermic and endothermic reactions

Publications (1)

Publication Number Publication Date
MY189567A true MY189567A (en) 2022-02-17

Family

ID=63919009

Family Applications (1)

Application Number Title Priority Date Filing Date
MYPI2017701436A MY189567A (en) 2017-04-25 2017-04-25 Reaction chamber for exothermic and endothermic reactions

Country Status (3)

Country Link
CN (1) CN110545907B (en)
MY (1) MY189567A (en)
WO (1) WO2018199738A1 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111420618A (en) * 2020-05-08 2020-07-17 宿迁新亚科技有限公司 Uniform gas distribution device for raw material gas and carbon monoxide generating furnace with same
CN114950280B (en) * 2022-04-18 2025-02-14 浙江州工智能装备有限公司 A shell-and-tube heat exchanger and Fischer-Tropsch synthesis slurry bed reactor
CN119468027A (en) * 2024-10-31 2025-02-18 中国航空研究院 A small, lightweight, low-evaporation-rate horizontal airborne liquid hydrogen storage tank

Family Cites Families (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3128163A (en) * 1960-05-21 1964-04-07 Metallgesellschaft Ag Method of carrying out exothermic catalytic carbon monoxide-steam gas reactions
ZA911838B (en) * 1990-04-03 1991-12-24 Standard Oil Co Ohio Endothermic reaction apparatus
US6139810A (en) * 1998-06-03 2000-10-31 Praxair Technology, Inc. Tube and shell reactor with oxygen selective ion transport ceramic reaction tubes
GB2359764A (en) * 2000-03-01 2001-09-05 Geoffrey Gerald Weedon An endothermic tube reactor
IT1319549B1 (en) * 2000-12-14 2003-10-20 Methanol Casale Sa REACTOR FOR THE PERFORMANCE OF EXOTHERMAL OR ENDOTHERMAL HETEROGENEOUS REACTIONS
US7250151B2 (en) * 2002-08-15 2007-07-31 Velocys Methods of conducting simultaneous endothermic and exothermic reactions
US20090162268A1 (en) * 2007-12-19 2009-06-25 Air Products And Chemicals, Inc. Carbon Dioxide Separation Via Partial Pressure Swing Cyclic Chemical Reaction
KR101585550B1 (en) * 2013-12-11 2016-01-22 두산중공업 주식회사 Gasificaction reactor and method of manufacuturing cooling wall thereof
CN204063016U (en) * 2014-08-15 2014-12-31 中国东方电气集团有限公司 A kind of electrostatic field takes off the fluidized system that sodium prevents boiler heating surface from staiing

Also Published As

Publication number Publication date
CN110545907B (en) 2022-05-17
CN110545907A (en) 2019-12-06
WO2018199738A1 (en) 2018-11-01

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