EA009402B1 - Способ и устройство для вдувания кислорода в реактор химического синтеза - Google Patents

Способ и устройство для вдувания кислорода в реактор химического синтеза Download PDF

Info

Publication number
EA009402B1
EA009402B1 EA200601115A EA200601115A EA009402B1 EA 009402 B1 EA009402 B1 EA 009402B1 EA 200601115 A EA200601115 A EA 200601115A EA 200601115 A EA200601115 A EA 200601115A EA 009402 B1 EA009402 B1 EA 009402B1
Authority
EA
Eurasian Patent Office
Prior art keywords
oxygen
catalyst bed
reactor
annular
gas
Prior art date
Application number
EA200601115A
Other languages
English (en)
Russian (ru)
Other versions
EA200601115A1 (ru
Inventor
Иоганнес Коволль
Макс Хайнритц-Адриан
Лотар Земрау
Original Assignee
Уде Гмбх
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 Уде Гмбх filed Critical Уде Гмбх
Publication of EA200601115A1 publication Critical patent/EA200601115A1/ru
Publication of EA009402B1 publication Critical patent/EA009402B1/ru

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/30—Injector mixers
    • B01F25/31—Injector mixers in conduits or tubes through which the main component flows
    • B01F25/313—Injector mixers in conduits or tubes through which the main component flows wherein additional components are introduced in the centre of the conduit
    • B01F25/3133—Injector mixers in conduits or tubes through which the main component flows wherein additional components are introduced in the centre of the conduit characterised by the specific design of the injector
    • B01F25/31332—Ring, torus, toroidal or coiled configurations
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/30—Injector mixers
    • B01F25/31—Injector mixers in conduits or tubes through which the main component flows
    • B01F25/313—Injector mixers in conduits or tubes through which the main component flows wherein additional components are introduced in the centre of the conduit
    • B01F25/3132—Injector mixers in conduits or tubes through which the main component flows wherein additional components are introduced in the centre of the conduit by using two or more injector devices
    • 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
    • B01J8/025—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 shaped bed
    • 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
    • B01J8/0278—Feeding reactive fluids
    • 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
    • C01B3/386—Catalytic partial combustion
    • 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
    • C01B2203/025—Processes for making hydrogen or synthesis gas containing a partial oxidation step
    • C01B2203/0261—Processes for making hydrogen or synthesis gas containing a partial oxidation step containing a catalytic partial oxidation step [CPO]

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Combustion & Propulsion (AREA)
  • Engineering & Computer Science (AREA)
  • Fluid Mechanics (AREA)
  • Physics & Mathematics (AREA)
  • Health & Medical Sciences (AREA)
  • General Health & Medical Sciences (AREA)
  • Inorganic Chemistry (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)
EA200601115A 2003-12-19 2004-12-10 Способ и устройство для вдувания кислорода в реактор химического синтеза EA009402B1 (ru)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE10359744A DE10359744A1 (de) 2003-12-19 2003-12-19 Verfahren und Vorrichtung zum Eindüsen von Sauerstoff in einen Synthesereaktor
PCT/EP2004/014050 WO2005063373A1 (de) 2003-12-19 2004-12-10 Verfahren und vorrichtung zum eindüsen von sauerstoff in einen synthesereaktor

Publications (2)

Publication Number Publication Date
EA200601115A1 EA200601115A1 (ru) 2006-12-29
EA009402B1 true EA009402B1 (ru) 2007-12-28

Family

ID=34672921

Family Applications (1)

Application Number Title Priority Date Filing Date
EA200601115A EA009402B1 (ru) 2003-12-19 2004-12-10 Способ и устройство для вдувания кислорода в реактор химического синтеза

Country Status (12)

Country Link
US (1) US8043577B2 (enExample)
EP (1) EP1694430B1 (enExample)
JP (1) JP5132938B2 (enExample)
AT (1) ATE489163T1 (enExample)
DE (2) DE10359744A1 (enExample)
DK (1) DK1694430T3 (enExample)
EA (1) EA009402B1 (enExample)
EG (1) EG25659A (enExample)
ES (1) ES2356824T3 (enExample)
NO (1) NO20063258L (enExample)
PL (1) PL1694430T3 (enExample)
WO (1) WO2005063373A1 (enExample)

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102006054415A1 (de) * 2006-11-16 2008-05-21 Uhde Gmbh Verfahren und Vorrichtung zum Eindüsen von Sauerstoff in ein einen Synthesereaktor durchströmendes Reaktionsgas
DE102006060507A1 (de) * 2006-12-19 2008-06-26 Basf Se Reaktor zur Durchführung einer Reaktion zwischen zwei fluiden Edukten an einem Katalysatorbett mit Vorvermischen der fluiden Edukte in einer Einmischvorrichtung
DE102007027881B4 (de) * 2007-06-13 2012-02-16 Outotec Oyj Verfahren und Vorrichtung zur Mischung von Gasen
DE102008010422A1 (de) * 2008-02-21 2009-09-03 Uhde Gmbh Fixiervorrichtung für Katalysatorpartikel
AR075787A1 (es) 2009-03-05 2011-04-27 Uhde Gmbh Procedimiento y dispositivo para retener el catalizador en forma de particulas arrastradas ingresantes
DE102009011375A1 (de) 2009-03-05 2010-09-23 Uhde Gmbh Verfahren zur Niederhaltung von angeströmten Katalysatorpartikeln
DE102015209874A1 (de) 2015-05-29 2016-12-01 Thyssenkrupp Ag System zur Eindüsung einer reaktiven gashaltigen Komponente in einen Synthesereaktor
US10933395B1 (en) * 2019-08-26 2021-03-02 Uop Llc Apparatus for catalytic reforming hydrocarbons having flow distributor and process for reforming hydrocarbons

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2361623A (en) * 1943-04-16 1944-10-31 Phillips Petroleum Co Catalyst chamber
US4741885A (en) * 1985-09-11 1988-05-03 Uhde Gmbh Vessel for the generation of synthesis gas
EP0473870A1 (de) * 1990-08-30 1992-03-11 Uhde GmbH Reformer, insbesondere autothermer Sekundärreformer
US20020098136A1 (en) * 2001-01-23 2002-07-25 Nicholas Vanderborgh Device for staged addition of heat to a reactor

Family Cites Families (29)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US262692A (en) * 1882-08-15 Elevator
US2518583A (en) * 1945-06-27 1950-08-15 Universal Oil Prod Co Catalytic reactor
US2584391A (en) * 1947-03-29 1952-02-05 Universal Oil Prod Co Apparatus for effecting fluidized contact between solid particles and fluid mediums
US2632692A (en) * 1949-01-18 1953-03-24 Hydrocarbon Research Inc Multiple bed catalyst apparatus
US2809981A (en) * 1953-02-27 1957-10-15 Exxon Research Engineering Co Method of carrying out homogeneous vapor phase reactions
US2954281A (en) * 1954-09-27 1960-09-27 Stone & Webster Eng Corp Method and apparatus for the fluidized catalytic treatment of fluid reactants
US3208833A (en) * 1963-05-01 1965-09-28 Universal Oil Prod Co Fluid distributing means for packed chambers
US3685971A (en) * 1970-07-06 1972-08-22 Universal Oil Prod Co Flow distributing apparatus
BE789153A (fr) * 1971-09-23 1973-03-22 Aquitaine Petrole Perfectionnement a la fabrication du styrene
GB1449205A (en) * 1973-11-06 1976-09-15 Exxon Research Engineering Co Distribut-ng a gas-liquid mixture in a reactor vessel
US4166834A (en) * 1977-09-27 1979-09-04 John Zink Company Air injector nozzle for secondary reformer
US4223843A (en) * 1978-03-16 1980-09-23 Texaco Inc. Air distribution apparatus
US4372920A (en) * 1979-07-13 1983-02-08 Ammonia Casale S.A. Axial-radial reactor for heterogeneous synthesis
JPS5852692B2 (ja) * 1979-11-08 1983-11-24 日揮株式会社 接触反応器
GB2065492B (en) 1979-12-21 1983-10-19 Uop Inc Fluid distributor for fixed-bed catalytic reaction zones
JPS5876134A (ja) 1981-11-02 1983-05-09 Toyo Eng Corp 複数の円筒状反応室を有する球形反応器とその使用法
US4443551A (en) * 1982-01-11 1984-04-17 Texaco Inc. Method and new distributor for delivering high velocity gas from a gas distributor through a nozzle with decreased erosion in the nozzle
US4994239A (en) * 1984-02-03 1991-02-19 Phillips Petroleum Company Catalyst regeneration
US4595145A (en) * 1984-10-01 1986-06-17 Texaco Inc. Air distribution apparatus for a fluid catalytic cracking catalyst regenerator
US4705621A (en) * 1985-03-22 1987-11-10 Mobil Oil Corporation Catalytic reactor system with crosscurrent liquid and gasflow
DK155979C (da) * 1987-05-20 1989-10-30 Haldor Topsoe As Fordelingselement til fordeling af gas til en reaktor
US4865820A (en) * 1987-08-14 1989-09-12 Davy Mckee Corporation Gas mixer and distributor for reactor
DE3829215A1 (de) 1988-08-29 1990-03-08 Uhde Gmbh Reaktor zur durchfuehrung katalytischer gasreaktionen mit einem druckfesten mantel und je einem kugelboden am stirnseitigen aussenrand
DE3829214A1 (de) 1988-08-29 1990-03-08 Uhde Gmbh Reaktor zur durchfuehrung katalytischer gasreaktionen mit einer mehrzahl von kaltgaszufuehrungen
US5043500A (en) * 1989-12-20 1991-08-27 Uop Use of steam eductor to supply oxygen for oxidative reheating in dehydrogenation of C3 + hydrocarbons
US5439859A (en) * 1992-04-27 1995-08-08 Sun Company, Inc. (R&M) Process and catalyst for dehydrogenation of organic compounds
IT1255710B (it) 1992-10-01 1995-11-10 Snam Progetti Procedimento integrato per produrre olefine da miscele gassose contenenti metano
US5935489A (en) * 1997-04-25 1999-08-10 Exxon Research And Engineering Co. Distributed injection process and apparatus for producing synthesis gas
AU2001251334A1 (en) * 2000-04-05 2001-10-23 Hydrogen Burner Technology, Inc. Pulsed flow, fuel-processing system

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2361623A (en) * 1943-04-16 1944-10-31 Phillips Petroleum Co Catalyst chamber
US4741885A (en) * 1985-09-11 1988-05-03 Uhde Gmbh Vessel for the generation of synthesis gas
EP0473870A1 (de) * 1990-08-30 1992-03-11 Uhde GmbH Reformer, insbesondere autothermer Sekundärreformer
US20020098136A1 (en) * 2001-01-23 2002-07-25 Nicholas Vanderborgh Device for staged addition of heat to a reactor

Also Published As

Publication number Publication date
JP5132938B2 (ja) 2013-01-30
US20070100191A1 (en) 2007-05-03
NO20063258L (no) 2006-09-19
EP1694430B1 (de) 2010-11-24
DE502004011937D1 (de) 2011-01-05
EG25659A (en) 2012-05-08
WO2005063373A1 (de) 2005-07-14
DE10359744A1 (de) 2005-07-14
ATE489163T1 (de) 2010-12-15
US8043577B2 (en) 2011-10-25
EP1694430A1 (de) 2006-08-30
PL1694430T3 (pl) 2011-05-31
DK1694430T3 (da) 2011-02-28
JP2007516074A (ja) 2007-06-21
EA200601115A1 (ru) 2006-12-29
ES2356824T3 (es) 2011-04-13

Similar Documents

Publication Publication Date Title
US4960571A (en) Quench assembly design
AU758217B2 (en) Feed injection system for catalytic cracking process
SU1478995A3 (ru) Устройство дл производства синтез-газа
US6627161B1 (en) Horizontal FCC feed injection and distributor
JP2770233B2 (ja) 固体と流体との混合物から固体を分離する装置
EP1705167B1 (en) Process for the catalytic oxidation of hydrocarbons
RU2278144C2 (ru) Распределитель отработавшего катализатора
US3502445A (en) Apparatus for mixing fluids in concurrent downflow relationship
RU2001124836A (ru) Способ вторичного реформинга и горелка, предназначенная для его осуществления
EA009402B1 (ru) Способ и устройство для вдувания кислорода в реактор химического синтеза
US5358632A (en) FCC feed injection with non-quiescent mixing
JPH07482B2 (ja) 気体原料を酸化する方法および装置
US12330940B2 (en) Reactor and process for partial oxidation
JP2007516074A5 (enExample)
EA008891B1 (ru) Способ и устройство для вдувания кислорода с радиальным прохождением через катализатор
US20240307841A1 (en) Chemical processing vessels having plate grid distributors and methods of operating the same
US9561484B2 (en) Method for revamping a secondary reformer
EP1456325B1 (en) Process to regenerate spent fcc catalyst
RU2290988C2 (ru) Устройство для подачи газа в кипящий слой и способ осуществления подачи
SU1324679A1 (ru) Реактор дл окислени углеводородов
SU1535620A1 (ru) Реактор дл окислени углеводородов
KR102088414B1 (ko) 촉매 재생기
CA2021982C (en) Quench assembly design
RU2152249C1 (ru) Устройство для ввода реагентов в реактор оксихлорирования этилена
PL120323B1 (en) Method of oxidizing regeneration of spent catalyst of hydrocarbon raw material cracking and apparatus therefortora krekirovanija uglevodorodnogo syr'ja i ustrojjstvo dlja okisljajuhhejj regeneracii otrabotannogo katalizatora krekirovanija uglevodorodnogo syr'ja

Legal Events

Date Code Title Description
MM4A Lapse of a eurasian patent due to non-payment of renewal fees within the time limit in the following designated state(s)

Designated state(s): AM AZ KG MD TJ

MM4A Lapse of a eurasian patent due to non-payment of renewal fees within the time limit in the following designated state(s)

Designated state(s): BY KZ TM RU