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BR9914560A - Reformador de vapor, e, processo para produzir hidrogênio que contenha concentrações de monóxido de carbono e de dióxido de carbono abaixo de um nìvel mìnimo definido - Google Patents

Reformador de vapor, e, processo para produzir hidrogênio que contenha concentrações de monóxido de carbono e de dióxido de carbono abaixo de um nìvel mìnimo definido

Info

Publication number
BR9914560A
BR9914560A BR9914560-0A BR9914560A BR9914560A BR 9914560 A BR9914560 A BR 9914560A BR 9914560 A BR9914560 A BR 9914560A BR 9914560 A BR9914560 A BR 9914560A
Authority
BR
Brazil
Prior art keywords
carbon dioxide
steam reformer
produce hydrogen
carbon monoxide
defined level
Prior art date
Application number
BR9914560-0A
Other languages
English (en)
Inventor
David J Edlund
William A Pledger
Original Assignee
Ida Tech Llc
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
Priority claimed from PCT/US1998/021670 external-priority patent/WO1999019456A1/en
Priority claimed from US09/190,917 external-priority patent/US6376113B1/en
Priority claimed from US09/291,447 external-priority patent/US6221117B1/en
Application filed by Ida Tech Llc filed Critical Ida Tech Llc
Publication of BR9914560A publication Critical patent/BR9914560A/pt

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Classifications

    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/50—Separation of hydrogen or hydrogen containing gases from gaseous mixtures, e.g. purification
    • C01B3/501—Separation of hydrogen or hydrogen containing gases from gaseous mixtures, e.g. purification by diffusion
    • C01B3/503—Separation of hydrogen or hydrogen containing gases from gaseous mixtures, e.g. purification by diffusion characterised by the membrane
    • C01B3/505—Membranes containing palladium
    • 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
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/24—Stationary reactors without moving elements inside
    • B01J19/2475—Membrane reactors
    • 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
    • B01J8/005—Separating solid material from the gas/liquid stream
    • B01J8/006—Separating solid material from the gas/liquid stream by filtration
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/008—Details of the reactor or of the particulate material; Processes to increase or to retard the rate of reaction
    • B01J8/009—Membranes, e.g. feeding or removing reactants or products to or from the catalyst bed through a membrane
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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    • 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
    • B01J8/0242—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 flow within the bed being predominantly vertical
    • B01J8/0257—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 flow within the bed being predominantly vertical in a cylindrical annular shaped bed
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    • B01J8/0285—Heating or cooling the reactor
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    • 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
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    • C01B3/382—Multi-step processes
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    • C01B3/58—Separation of hydrogen or hydrogen containing gases from gaseous mixtures, e.g. purification by contacting with solids; Regeneration of used solids including a catalytic reaction
    • C01B3/586—Separation of hydrogen or hydrogen containing gases from gaseous mixtures, e.g. purification by contacting with solids; Regeneration of used solids including a catalytic reaction the reaction being a methanation reaction
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00—Fuel cells; Manufacture thereof
    • H01M8/06—Combination of fuel cells with means for production of reactants or for treatment of residues
    • H01M8/0606—Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants
    • H01M8/0612—Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants from carbon-containing material
    • H01M8/0625—Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants from carbon-containing material in a modular combined reactor/fuel cell structure
    • H01M8/0631—Reactor construction specially adapted for combination reactor/fuel cell
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Abstract

"REFORMADOR DE VAPOR, E, PROCESSO PARA PRODUZIR HIDROGêNIO QUE CONTENHA CONCENTRAçõES DE MONóXIDO DE CARBONO E DE DIóXIDO DE CARBONO ABAIXO DE UM NìVEL MìNIMO DEFINIDO". Um sistema de processamento de combustível (fig. 27) é divulgado. O sistema inclui um reformador de vapor (12) adaptado para produzir hidrogênio a partir de um carregamento de alimentação consistindo de água e pelo menos um de um carregamento de alimentação de um álcool e um hidrocarboneto. O hidrogênio é produzido reagindo-se o carregamento de alimentação na presença de um catalisador de reforma (102). O fluxo de produto é passado através de um módulo de membrana seletiva para o hidrogênio (54), no qual o fluxo permeado é refinado para remover o monóxido de carbono e o dióxido de carbono permutados e o fluxo de subproduto é comburido para aquecer o reformador.
BR9914560-0A 1998-10-14 1999-04-14 Reformador de vapor, e, processo para produzir hidrogênio que contenha concentrações de monóxido de carbono e de dióxido de carbono abaixo de um nìvel mìnimo definido BR9914560A (pt)

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
PCT/US1998/021670 WO1999019456A1 (en) 1997-10-15 1998-10-14 Steam reformer with internal hydrogen purification
US09/190,917 US6376113B1 (en) 1998-11-12 1998-11-12 Integrated fuel cell system
US09/291,447 US6221117B1 (en) 1996-10-30 1999-04-13 Hydrogen producing fuel processing system
PCT/US1999/008166 WO2000022690A1 (en) 1998-10-14 1999-04-14 Fuel processing system

Publications (1)

Publication Number Publication Date
BR9914560A true BR9914560A (pt) 2001-06-26

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BR9914560-0A BR9914560A (pt) 1998-10-14 1999-04-14 Reformador de vapor, e, processo para produzir hidrogênio que contenha concentrações de monóxido de carbono e de dióxido de carbono abaixo de um nìvel mìnimo definido

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EP (1) EP1138096B1 (pt)
JP (3) JP3898892B2 (pt)
BR (1) BR9914560A (pt)
CA (1) CA2345966C (pt)
WO (1) WO2000022690A1 (pt)

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