AR120875A1 - Reactor de calentamiento eléctrico, un horno que comprende dicho reactor y un método para conversiones de gas que usa dicho reactor - Google Patents

Reactor de calentamiento eléctrico, un horno que comprende dicho reactor y un método para conversiones de gas que usa dicho reactor

Info

Publication number
AR120875A1
AR120875A1 ARP200103617A ARP200103617A AR120875A1 AR 120875 A1 AR120875 A1 AR 120875A1 AR P200103617 A ARP200103617 A AR P200103617A AR P200103617 A ARP200103617 A AR P200103617A AR 120875 A1 AR120875 A1 AR 120875A1
Authority
AR
Argentina
Prior art keywords
reactor
surface area
reactor tube
heating medium
external surface
Prior art date
Application number
ARP200103617A
Other languages
English (en)
Inventor
Der Ploeg Govert Gerardus Pieter Van
Original Assignee
Shell Int Research
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 Shell Int Research filed Critical Shell Int Research
Publication of AR120875A1 publication Critical patent/AR120875A1/es

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Classifications

    • 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
    • B01J8/0285—Heating or cooling the reactor
    • 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
    • B01J8/062—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 being installed in a furnace
    • 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
    • B01J8/0242—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
    • 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
    • B01J8/067—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
    • C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/32—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
    • C01B3/34—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
    • 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
    • C01B3/382—Multi-step processes
    • 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
    • C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/32—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
    • C01B3/34—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
    • 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
    • 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
    • B01J2208/00389—Controlling the temperature using electric heating or cooling elements
    • 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
    • B01J2208/0053—Controlling multiple zones along the direction of flow, e.g. pre-heating and after-cooling
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/02—Processes for making hydrogen or synthesis gas
    • C01B2203/0205—Processes for making hydrogen or synthesis gas containing a reforming step
    • C01B2203/0227—Processes for making hydrogen or synthesis gas containing a reforming step containing a catalytic reforming step
    • C01B2203/0233—Processes for making hydrogen or synthesis gas containing a reforming step containing a catalytic reforming step the reforming step being a steam reforming step
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/02—Processes for making hydrogen or synthesis gas
    • C01B2203/0205—Processes for making hydrogen or synthesis gas containing a reforming step
    • C01B2203/0227—Processes for making hydrogen or synthesis gas containing a reforming step containing a catalytic reforming step
    • C01B2203/0238—Processes for making hydrogen or synthesis gas containing a reforming step containing a catalytic reforming step the reforming step being a carbon dioxide reforming step
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/02—Processes for making hydrogen or synthesis gas
    • C01B2203/0283—Processes for making hydrogen or synthesis gas containing a CO-shift step, i.e. a water gas shift step
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/08—Methods of heating or cooling
    • C01B2203/0805—Methods of heating the process for making hydrogen or synthesis gas
    • C01B2203/085—Methods of heating the process for making hydrogen or synthesis gas by electric heating

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • General Health & Medical Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Inorganic Chemistry (AREA)
  • Physics & Mathematics (AREA)
  • Fluid Mechanics (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Silicon Compounds (AREA)

Abstract

La presente se refiere a un reactor de calentamiento eléctrico que tiene un área de superficie externa, una entrada y una salida, en donde (a) el reactor es un tubo rodeado por un medio de calentamiento eléctrico a una cierta distancia; (b) el medio de calentamiento eléctrico comprende láminas radiantes colocadas coaxialmente con respecto al tubo de reactor, en donde el área de superficie de la lámina mira hacia el área de superficie externa del tubo de reactor que define un área de superficie interna del medio de calentamiento eléctrico; (c) el área de superficie interna del medio de calentamiento cubre al menos 60% del área de superficie externa del tubo de reactor; y (d) la distancia entre el tubo de reactor y el medio de calentamiento se selecciona de manera que la relación del área de superficie interna del medio de calentamiento eléctrico con respecto al área de superficie externa del tubo de reactor esté en el rango de 0,7 a 3,0. Los procesos de calentamiento eléctrico exigen la gestión de un perfil de flujo de calor y de temperatura. En muchas aplicaciones, el flujo de calor es mayor cuando el flujo del proceso ingresa al reactor mientras tiene una temperatura más baja. Hacia la salida del tubo de reactor, el flujo de calor es menor mientras que el flujo de proceso tiene una temperatura más alta. La presente puede cumplir con este requisito. El reactor es útil en muchas tecnologías de calentamiento y conversión de gasa alta temperatura a escala industrial.
ARP200103617A 2019-12-23 2020-12-22 Reactor de calentamiento eléctrico, un horno que comprende dicho reactor y un método para conversiones de gas que usa dicho reactor AR120875A1 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
EP19219215 2019-12-23

Publications (1)

Publication Number Publication Date
AR120875A1 true AR120875A1 (es) 2022-03-23

Family

ID=69005515

Family Applications (1)

Application Number Title Priority Date Filing Date
ARP200103617A AR120875A1 (es) 2019-12-23 2020-12-22 Reactor de calentamiento eléctrico, un horno que comprende dicho reactor y un método para conversiones de gas que usa dicho reactor

Country Status (7)

Country Link
US (1) US20220410103A1 (es)
EP (1) EP4081337A1 (es)
CN (1) CN114845801A (es)
AR (1) AR120875A1 (es)
AU (1) AU2020412238B2 (es)
CA (1) CA3164121A1 (es)
WO (1) WO2021130107A1 (es)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2023016967A1 (en) * 2021-08-12 2023-02-16 Sabic Global Technologies B.V. Furnace including heating zones with electrically powered heating elements and related methods
CN115196595A (zh) * 2022-05-16 2022-10-18 西安交通大学 一种天然气制富氢合成气电热蒸汽重整炉
WO2024033187A1 (en) 2022-08-09 2024-02-15 Shell Internationale Research Maatschappij B.V. An electrically heated apparatus and a method of heating a fluid
WO2024084253A1 (en) * 2022-10-17 2024-04-25 Dow Global Technologies Llc Systems for directly heating electric tubes for hydrocarbon upgrading

Family Cites Families (25)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AT284988B (de) * 1967-12-18 1970-10-12 Glanzstoff Ag Plattenförmiges elektrisches Heizelement für Raumheizungszwecke
CY1118A (en) * 1975-10-06 1981-12-04 Thagard Technology Co Fluid wall reactors and their utilization in high temparature chemical reaction processes
CA2379892A1 (en) * 1999-07-29 2001-02-08 David Systems & Technology S.L. Plasma converter of fossil fuels into hydrogen-rich gas
CA2354927A1 (en) * 2000-08-11 2002-02-11 H. Power Corp. Fuel process and apparatus and control system
US7074373B1 (en) * 2000-11-13 2006-07-11 Harvest Energy Technology, Inc. Thermally-integrated low temperature water-gas shift reactor apparatus and process
DE10317197A1 (de) * 2003-04-15 2004-11-04 Degussa Ag Elektrisch beheizter Reaktor und Verfahren zur Durchführung von Gasreaktionen bei hoher Temperatur unter Verwendung dieses Reaktors
DE102006014197A1 (de) * 2006-03-28 2007-10-04 Bayerische Motoren Werke Ag Betriebsverfahren für ein System mit einem Reformer sowie mit einer das Reformat verarbeitenden Einheit
MX2009002103A (es) * 2006-08-29 2009-03-10 Univ Colorado Regents Conversion termico-solar rapida de biomasa a gas de sintesis.
KR100857703B1 (ko) * 2007-03-29 2008-09-08 삼성에스디아이 주식회사 반응 용기 및 반응 장치
WO2009091791A1 (en) * 2008-01-16 2009-07-23 Shell Oil Company A system and process for making hydrogen from a hydrocarbon stream
WO2011155962A1 (en) * 2010-06-08 2011-12-15 Sundrop Fuels, Inc. Various methods and apparatuses for an ultra-high heat flux chemical reactor
US9663363B2 (en) * 2009-06-09 2017-05-30 Sundrop Fuels, Inc. Various methods and apparatuses for multi-stage synthesis gas generation
US8814961B2 (en) * 2009-06-09 2014-08-26 Sundrop Fuels, Inc. Various methods and apparatuses for a radiant-heat driven chemical reactor
DE102011002749A1 (de) * 2011-01-17 2012-07-19 Wacker Chemie Ag Verfahren und Vorrichtung zur Konvertierung von Siliciumtetrachlorid in Trichlorsilan
US10961122B2 (en) * 2012-02-06 2021-03-30 Helbio S.A. Heat integrated reformer with catalytic combustion for hydrogen production
US9295961B2 (en) * 2012-03-26 2016-03-29 Sundrop Fuels, Inc. Various methods and apparatuses for internally heated radiant tubes in a chemical reactor
EP2644263A1 (de) * 2012-03-28 2013-10-02 Aurotec GmbH Druckgeregelter Reaktor
EP2774668A1 (en) * 2013-03-04 2014-09-10 Alantum Europe GmbH Radiating wall catalytic reactor and process for carrying out a chemical reaction in this reactor
KR20160021821A (ko) * 2013-06-17 2016-02-26 바스프 에스이 n-부텐의 1,3-부타디엔으로의 산화성 탈수 방법
KR101654119B1 (ko) * 2014-10-23 2016-09-06 한국과학기술연구원 헤테로 원자가 포함된 활성탄 촉매를 사용한 하이드로실란의 제조 방법)
DE102015004121A1 (de) 2015-03-31 2016-10-06 Linde Aktiengesellschaft Ofen mit elektrisch sowie mittels Brennstoff beheizbaren Reaktorrohren zur Dampfreformierung eines kohlenwasserstoffhaltigen Einsatzes
US20170106360A1 (en) * 2015-09-30 2017-04-20 Jay S. Meriam Isothermal chemical process
CN108232253B (zh) * 2016-12-15 2020-06-16 中国科学院大连化学物理研究所 一种燃料重整反应器
CN207422580U (zh) * 2017-10-25 2018-05-29 广东美的制冷设备有限公司 电加热管和具有其的空调室内机、空调器
CN108841424A (zh) * 2018-09-11 2018-11-20 史金麟 一种光催化生产烷烃的方法及装置

Also Published As

Publication number Publication date
EP4081337A1 (en) 2022-11-02
AU2020412238A1 (en) 2022-06-09
AU2020412238B2 (en) 2023-06-01
WO2021130107A1 (en) 2021-07-01
CN114845801A (zh) 2022-08-02
CA3164121A1 (en) 2021-07-01
US20220410103A1 (en) 2022-12-29

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