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MX2019002852A - Tubo reformador que tiene un catalizador estructurado y un balance de calor mejorado. - Google Patents

Tubo reformador que tiene un catalizador estructurado y un balance de calor mejorado.

Info

Publication number
MX2019002852A
MX2019002852A MX2019002852A MX2019002852A MX2019002852A MX 2019002852 A MX2019002852 A MX 2019002852A MX 2019002852 A MX2019002852 A MX 2019002852A MX 2019002852 A MX2019002852 A MX 2019002852A MX 2019002852 A MX2019002852 A MX 2019002852A
Authority
MX
Mexico
Prior art keywords
structured catalyst
structured
catalyst
improved heat
reformer tube
Prior art date
Application number
MX2019002852A
Other languages
English (en)
Inventor
Philippe Tadiello Jean-
Ulber Dieter
Gary Daniel
Prost Laurent
Basin Marie
Original Assignee
Air Liquide
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 Air Liquide filed Critical Air Liquide
Publication of MX2019002852A publication Critical patent/MX2019002852A/es

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    • 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
    • B01J19/2455—Stationary reactors without moving elements inside provoking a loop type movement of the reactants
    • B01J19/246—Stationary reactors without moving elements inside provoking a loop type movement of the reactants internally, i.e. the mixture circulating inside the vessel such that the upward stream is separated physically from the downward stream(s)
    • 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
    • B01J8/06—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 in tube reactors; the solid particles being arranged in tubes
    • 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
    • B01J8/02—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
    • B01J8/0285—Heating or cooling the reactor
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
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    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
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    • B01J19/325—Attachment devices therefor, e.g. hooks, consoles, brackets
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    • B—PERFORMING OPERATIONS; TRANSPORTING
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    • 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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    • C01B3/38—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts
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    • C01B3/38—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts
    • C01B3/384—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts the catalyst being continuously externally heated
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    • C01B2203/1052—Nickel or cobalt catalysts
    • C01B2203/1058—Nickel catalysts

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • General Health & Medical Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Inorganic Chemistry (AREA)
  • Fluid Mechanics (AREA)
  • Hydrogen, Water And Hydrids (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

Se presenta un tubo reformador para producir gas de síntesis mediante reformado con vapor de gases de alimentación que contienen hidrocarburos, en el que se usa un catalizador de reformado con vapor estructurado. De acuerdo con la invención, se dispone un tubo intercambiador de calor en el interior del catalizador estructurado, donde la corriente de gas de alimentación fluye en primer lugar a través del catalizador estructurado y posteriormente a contracorriente a través del tubo intercambiador de calor. Esto mejora el intercambio de calor entre la corriente del producto de gas de síntesis y el catalizador estructurado y la corriente de gas de alimentación que fluye a través de este, especialmente en la dirección radial.
MX2019002852A 2016-09-14 2017-09-05 Tubo reformador que tiene un catalizador estructurado y un balance de calor mejorado. MX2019002852A (es)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
EP16400041.6A EP3296255A1 (de) 2016-09-14 2016-09-14 Reformerrohr mit strukturiertem katalysator und verbessertem wärmehaushalt
PCT/EP2017/025252 WO2018050291A1 (en) 2016-09-14 2017-09-05 Reformer tube having a structured catalyst and improved heat balance

Publications (1)

Publication Number Publication Date
MX2019002852A true MX2019002852A (es) 2019-06-12

Family

ID=57391932

Family Applications (1)

Application Number Title Priority Date Filing Date
MX2019002852A MX2019002852A (es) 2016-09-14 2017-09-05 Tubo reformador que tiene un catalizador estructurado y un balance de calor mejorado.

Country Status (12)

Country Link
US (1) US11351517B2 (es)
EP (1) EP3296255A1 (es)
KR (1) KR102415731B1 (es)
CN (2) CN207709023U (es)
AU (1) AU2017326121B2 (es)
CA (1) CA3036416A1 (es)
DE (1) DE102016120167A1 (es)
EA (1) EA039256B1 (es)
MX (1) MX2019002852A (es)
MY (1) MY198732A (es)
SG (1) SG11201901946RA (es)
WO (1) WO2018050291A1 (es)

Families Citing this family (22)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP3296255A1 (de) 2016-09-14 2018-03-21 L'air Liquide, Société Anonyme Pour L'Étude Et L'exploitation Des Procédés Georges Claude Reformerrohr mit strukturiertem katalysator und verbessertem wärmehaushalt
MY193298A (en) 2016-11-09 2022-10-03 8 Rivers Capital Llc Systems and methods for power production with integrated production of hydrogen
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