CN101778666B - 用于在固定床催化剂上进行液相和气相的三相反应的反应器 - Google Patents

用于在固定床催化剂上进行液相和气相的三相反应的反应器 Download PDF

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CN101778666B
CN101778666B CN200880025631.1A CN200880025631A CN101778666B CN 101778666 B CN101778666 B CN 101778666B CN 200880025631 A CN200880025631 A CN 200880025631A CN 101778666 B CN101778666 B CN 101778666B
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reactor
distributor
distributor plates
liquid phase
opening
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CN101778666A (zh
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M·贝希特尔
B·黑普费尔
M·维勒
A·戴斯
R·盖尔
S·伊泽尔伯恩
J·索特尔
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BASF SE
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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
    • 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
    • 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
    • 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
    • B01J8/0449—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 cylindrical beds
    • B01J8/0453—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 cylindrical 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
    • B01J8/0492—Feeding reactive fluids
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C7/00—Purification; Separation; Use of additives
    • C07C7/148—Purification; Separation; Use of additives by treatment giving rise to a chemical modification of at least one compound
    • C07C7/163—Purification; Separation; Use of additives by treatment giving rise to a chemical modification of at least one compound by hydrogenation
    • C07C7/167—Purification; Separation; Use of additives by treatment giving rise to a chemical modification of at least one compound by hydrogenation for removal of compounds containing a triple carbon-to-carbon bond
    • 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
    • B01J2208/00548—Flow
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
    • C10G2400/20—C2-C4 olefins

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Physics & Mathematics (AREA)
  • Fluid Mechanics (AREA)
  • General Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Analytical Chemistry (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Water Supply & Treatment (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
CN200880025631.1A 2007-06-21 2008-06-20 用于在固定床催化剂上进行液相和气相的三相反应的反应器 Active CN101778666B (zh)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
US94546107P 2007-06-21 2007-06-21
US60/945,461 2007-06-21
PCT/EP2008/057832 WO2008155399A1 (de) 2007-06-21 2008-06-20 Reaktor zur durchführung einer dreiphasenreaktion einer flüssigen und einer gasförmigen phase an einem katalysatorfestbett

Publications (2)

Publication Number Publication Date
CN101778666A CN101778666A (zh) 2010-07-14
CN101778666B true CN101778666B (zh) 2012-10-10

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Country Link
US (1) US9011790B2 (enExample)
EP (1) EP2170494B1 (enExample)
JP (1) JP5276098B2 (enExample)
KR (1) KR101509274B1 (enExample)
CN (1) CN101778666B (enExample)
AT (1) ATE520455T1 (enExample)
BR (1) BRPI0812907A2 (enExample)
CA (1) CA2691642C (enExample)
MY (1) MY147674A (enExample)
RU (1) RU2466784C2 (enExample)
TW (1) TWI458553B (enExample)
WO (1) WO2008155399A1 (enExample)

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EP2274343A1 (en) * 2008-05-02 2011-01-19 Basf Se Process and apparatus for continuously polymerizing cationically polymerizable monomers
EP2274339B1 (de) 2008-05-02 2015-11-11 Basf Se Verfahren und vorrichtung zur kontinuierlichen herstellung von polymerisaten durch radikalische polymerisation
US8177198B2 (en) * 2008-06-26 2012-05-15 Uop Llc Quench zone design using spray nozzles
EP2476482B2 (en) * 2011-01-18 2020-05-13 Neste Oyj Method and arrangement for feeding heat-sensitive materials to fixed-bed reactors
CN103084121B (zh) * 2011-10-27 2014-09-17 中国科学院大连化学物理研究所 一种气-液-固三相反应器及其应用
CN102442874B (zh) * 2011-10-28 2015-02-25 山东华懋新材料有限公司 恒温固定床丁烯氧化脱氢制备丁二烯的方法
FR2987280B1 (fr) * 2012-02-24 2014-02-28 IFP Energies Nouvelles Reacteur catalytique avec systeme de distribution a caissons
FR3006599B1 (fr) * 2013-06-10 2015-05-29 IFP Energies Nouvelles Plateau distributeur pour colonne de contact gaz/liquide avec systeme de distribution secondaire
KR102186555B1 (ko) 2013-07-12 2020-12-04 삼성전자주식회사 전자장치 및 전자장치의 정보 처리방법
EP2918332A1 (en) * 2014-03-14 2015-09-16 Morten Müller Ltd., ApS Scale collection and predistribution tray for vessel with downwards two-phase flow
CN105561887A (zh) * 2014-10-10 2016-05-11 天津汇康源科技有限公司 化工反应釜的催化反应结构
CN106554806B (zh) * 2015-09-25 2018-08-10 中国石油天然气股份有限公司 膨松床反应器及重油轻质化方法
CN105664805A (zh) * 2016-01-15 2016-06-15 中航黎明锦西化工机械(集团)有限责任公司 滴流床反应器分布器
CN106000242B (zh) * 2016-06-23 2018-08-24 中国船舶重工集团公司第七一八研究所 一种具有自适应进气功能的催化床结构
US10441932B2 (en) * 2017-06-28 2019-10-15 Uop Llc Apparatus for vapor-liquid distribution
FR3072306B1 (fr) * 2017-10-12 2019-10-18 IFP Energies Nouvelles Dispositif de melange et de distribution avec ouverture longitudinale
US11224849B2 (en) * 2017-12-21 2022-01-18 Uop Llc Scale collection device for downflow reactors
US10556212B2 (en) * 2017-12-21 2020-02-11 Uop Llc Scale collection device for downflow reactors
DE102018005694A1 (de) * 2018-07-19 2020-01-23 Linde Aktiengesellschaft Stoff- und/oder Wärmeaustauschkolonne und Verfahren zur Behandlung eines ersten Fluids und eines zweiten Fluids unter Verwendung einer Stoff- und/oder Wärmeaustauschkolonne
EP3604261A1 (de) 2018-08-02 2020-02-05 Omv Refining & Marketing Gmbh Verfahren zur aufreinigung von isobuten aus einem c4-strom und verfahrenstechnische anlage dafür
CN109200952B (zh) * 2018-11-15 2021-04-27 中石化炼化工程（集团）股份有限公司 一种气液混合组件及用于反应器的催化剂床层结构
US11298670B2 (en) * 2020-04-24 2022-04-12 Uop Llc Compact quench zone reactor internals
CN114452901B (zh) * 2020-10-21 2023-03-07 中国石油化工股份有限公司 催化反应单元以及反应蒸馏塔
CN112387219A (zh) * 2020-11-13 2021-02-23 华东理工大学 一种用于碳酸乙烯酯加氢的气化-反应一体化多段反应器
CN116351234B (zh) * 2023-03-23 2023-10-20 汇舸(南通)环保设备有限公司 烟气留驻时间延长装置及采用该装置的船用脱硫塔

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CN2834690Y (zh) * 2005-11-14 2006-11-08 中国石油化工集团公司 并流气液分配器

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US5484578A (en) * 1994-06-20 1996-01-16 Mobil Oil Corporation Two-phase distributor system for downflow reactors
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CN2834690Y (zh) * 2005-11-14 2006-11-08 中国石油化工集团公司 并流气液分配器

Also Published As

Publication number Publication date
BRPI0812907A2 (pt) 2014-12-09
ATE520455T1 (de) 2011-09-15
MY147674A (en) 2012-12-31
CA2691642A1 (en) 2008-12-24
TWI458553B (zh) 2014-11-01
CA2691642C (en) 2015-12-22
KR101509274B1 (ko) 2015-04-06
JP5276098B2 (ja) 2013-08-28
EP2170494A1 (de) 2010-04-07
WO2008155399A1 (de) 2008-12-24
JP2010530804A (ja) 2010-09-16
EP2170494B1 (de) 2011-08-17
RU2010101601A (ru) 2011-07-27
KR20100053503A (ko) 2010-05-20
TW200916192A (en) 2009-04-16
CN101778666A (zh) 2010-07-14
RU2466784C2 (ru) 2012-11-20
US9011790B2 (en) 2015-04-21
US20100185032A1 (en) 2010-07-22

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SE01 Entry into force of request for substantive examination
C53 Correction of patent of invention or patent application
CB03 Change of inventor or designer information

Inventor after: Bechtel Marcus

Inventor after: Hepfer Benjamin

Inventor after: Weiler Michael

Inventor after: Dais Ansgar

Inventor after: Rudolf Geier

Inventor after: Iselborn Stefan

Inventor after: J.Sauter

Inventor before: Bechtel Marcus

Inventor before: Hepfer Benjamin

Inventor before: Weiler Michael

Inventor before: Dais Ansgar

Inventor before: Rudolf Geier

Inventor before: Iselborn Stefan

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Free format text: CORRECT: INVENTOR; FROM: BECHTEL MARCUS HEPFER BENJAMIN WILLE MICHAEL DAISS ANDREAS GEIER REINER ISELBORN STEFAN TO: BECHTEL MARCUS HEPFER BENJAMIN WILLE MICHAEL DAISS ANDREAS GEIER REINER ISELBORN STEFAN SAUTER JOHN

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