MX2014002685A - Reactor de circuito de chorro que tiene nanofiltracion. - Google Patents

Reactor de circuito de chorro que tiene nanofiltracion.

Info

Publication number
MX2014002685A
MX2014002685A MX2014002685A MX2014002685A MX2014002685A MX 2014002685 A MX2014002685 A MX 2014002685A MX 2014002685 A MX2014002685 A MX 2014002685A MX 2014002685 A MX2014002685 A MX 2014002685A MX 2014002685 A MX2014002685 A MX 2014002685A
Authority
MX
Mexico
Prior art keywords
membrane separation
reactor
homogeneous
loop reactor
jet loop
Prior art date
Application number
MX2014002685A
Other languages
English (en)
Inventor
Dirk Fridag
Marc Becker
Robert Franke
Bart Hamers
Markus Priske
Original Assignee
Evonik Degussa Gmbh
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 Evonik Degussa Gmbh filed Critical Evonik Degussa Gmbh
Publication of MX2014002685A publication Critical patent/MX2014002685A/es

Links

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
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/24—Stationary reactors without moving elements inside
    • 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
    • B01J8/0065—Separating solid material from the gas/liquid stream by impingement against stationary members
    • 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
    • B01J19/2415—Tubular reactors
    • B01J19/2435—Loop-type 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
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/24—Stationary reactors without moving elements inside
    • B01J19/2445—Stationary reactors without moving elements inside placed in parallel
    • 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
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/26—Nozzle-type reactors, i.e. the distribution of the initial reactants within the reactor is effected by their introduction or injection through nozzles
    • 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
    • B01J4/00—Feed or outlet devices; Feed or outlet control devices
    • B01J4/001—Feed or outlet devices as such, e.g. feeding tubes
    • B01J4/002—Nozzle-type elements
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C45/00—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds
    • C07C45/49—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by reaction with carbon monoxide
    • C07C45/50—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by reaction with carbon monoxide by oxo-reactions
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C45/00—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds
    • C07C45/49—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by reaction with carbon monoxide
    • C07C45/50—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by reaction with carbon monoxide by oxo-reactions
    • C07C45/505—Asymmetric hydroformylation
    • 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
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/24—Stationary reactors without moving elements inside

Abstract

La invención se refiere a un dispositivo para la reacción de catálisis homogenea, continua, de un líquido con un gas y opcionalmente un fluido adicional, en donde el dispositivo comprende al menos un reactor que tiene una circulación de líquido externa accionada por una bomba, y en donde el dispositivo tiene al menos una etapa de separación por membrana que preferentemente detiene la catálisis homogenea. El objetivo de la invención es especificar un dispositivo que permita las reacciones de catálisis homogenes de fase gas/líquido, en particular hidroformilaciones, que operan con separación por membrana del catalizador para realizarse de manera económica a una escala industrialmente relevante. Dicho objetivo se logra en cuanto se proporciona un reactor de circuito de chorro como el reactor, y que la bomba y la etapa de separación por membrana se disponen en el mismo circuito de líquido externo.
MX2014002685A 2011-09-09 2012-09-07 Reactor de circuito de chorro que tiene nanofiltracion. MX2014002685A (es)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE102011082441A DE102011082441A1 (de) 2011-09-09 2011-09-09 Strahlschlaufenreaktor mit Nanofiltration
PCT/EP2012/067513 WO2013034690A1 (de) 2011-09-09 2012-09-07 Strahlschlaufenreaktor mit nanofiltration

Publications (1)

Publication Number Publication Date
MX2014002685A true MX2014002685A (es) 2014-04-14

Family

ID=46832383

Family Applications (1)

Application Number Title Priority Date Filing Date
MX2014002685A MX2014002685A (es) 2011-09-09 2012-09-07 Reactor de circuito de chorro que tiene nanofiltracion.

Country Status (11)

Country Link
US (2) US9149780B2 (es)
EP (1) EP2753421B1 (es)
JP (1) JP2014526372A (es)
KR (1) KR101647239B1 (es)
CN (1) CN103906565B (es)
DE (1) DE102011082441A1 (es)
ES (1) ES2729101T3 (es)
MX (1) MX2014002685A (es)
SG (1) SG11201400458QA (es)
WO (1) WO2013034690A1 (es)
ZA (1) ZA201402509B (es)

Families Citing this family (20)

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DE102012202779A1 (de) 2012-02-23 2013-08-29 Evonik Oxeno Gmbh Verfahren und Vorrichtung zur technischen Hydroformylierung von Isobuten und zum Auftrennen des Produktgemisches
DE102012223572A1 (de) 2012-12-18 2014-06-18 Evonik Industries Ag Steuerung der Viskosität von Reaktionslösungen in Hydroformylierungverfahren
DE102013203117A1 (de) 2013-02-26 2014-08-28 Evonik Industries Ag Optimierte Trenntechnik zur Aufarbeitung von homogen katalysierten Hydroformylierungsmischungen
FR3003564B1 (fr) * 2013-03-19 2015-03-06 Arkema France Procede de metathese comprenant l'extraction de l'ethylene forme au moyen d'une membrane
DE102013208759A1 (de) 2013-05-13 2014-11-13 Evonik Industries Ag Abtrennung von Homogenkatalysatoren mittels einer geregelten Membrantrenneinheit
DE102013215004A1 (de) 2013-07-31 2015-02-05 Evonik Industries Ag Membrankaskade mit sinkender Trenntemperatur
DE102013221708A1 (de) 2013-10-25 2015-04-30 Evonik Industries Ag Strahlschlaufenreaktor mit Nanofiltration und Gasseparator
DE102014209421A1 (de) 2014-05-19 2015-11-19 Evonik Degussa Gmbh Membrangestützte Katalysatorabtrennung bei der Epoxidierung von cyclischen, ungesättigten C12-Verbindungen zum Beispiel Cyclododecen (CDEN)
CN106457192A (zh) * 2014-06-19 2017-02-22 沙特基础工业全球技术有限公司 增强的均相催化反应器系统
DE102017001093A1 (de) 2016-04-07 2017-10-26 Entex Rust & Mitschke Gmbh Entgasen bei der Extrusion von Kunststoffen mit Filterscheiben aus Sintermetall
DE102015001167A1 (de) 2015-02-02 2016-08-04 Entex Rust & Mitschke Gmbh Entgasen bei der Extrusion von Kunststoffen
US10155200B2 (en) 2015-02-18 2018-12-18 Evonik Degussa Gmbh Separation off of a homogeneous catalyst from a reaction mixture with the help of organophilic nanofiltration
CN106076211A (zh) * 2016-08-04 2016-11-09 中石化南京工程有限公司 一种气液两相射流反应器以及气液两相射流反应系统
CN106422994B (zh) * 2016-10-21 2022-10-18 北京沃特尔水技术股份有限公司 一种制备碳铵类汲取液的方法及设备
DE102017004563A1 (de) 2017-03-05 2018-09-06 Entex Rust & Mitschke Gmbh Entgasen beim Extrudieren von Polymeren
DE102018001412A1 (de) 2017-12-11 2019-06-13 Entex Rust & Mitschke Gmbh Entgasen beim Extrudieren von Stoffen, vorzugsweise von Kunststoffen
CN112654421B (zh) * 2018-09-05 2023-05-09 巴斯夫欧洲公司 用于进行两种不同密度的不混溶流体之间的反应的反应器
CN110201611B (zh) * 2019-05-30 2021-11-23 河南能源化工集团研究总院有限公司 一种用于烯烃氢甲酰化的三相流反应装置及其操作方法
CN114029026A (zh) * 2021-12-08 2022-02-11 上海市安装工程集团有限公司 一种循环加氢反应器
DE102021006375A1 (de) 2021-12-28 2023-06-29 CreativeQuantum GmbH Verfahren zur kontinuierlichen Herstellung von Methanol

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KR970703805A (ko) 1995-05-01 1997-08-09 유니온 카바이드 케미칼즈 앤드 플라스틱스 테크놀러지 코포레이션 막 분리방법(Membrane Separation)
DE19857409A1 (de) 1998-12-12 2000-06-15 Basf Ag Verfahren zur Herstellung von Aminen
US6350911B1 (en) 1998-12-12 2002-02-26 Basf Aktiengesellschaft Method for producing amines
DE10034360A1 (de) * 2000-07-14 2002-01-24 Oxeno Olefinchemie Gmbh Mehrstufiges Verfahren zur Herstellung von Oxo-Aldehyden und/oder Alkoholen
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DE10206214A1 (de) 2002-02-15 2003-08-28 Basf Ag Verfahren zur Herstellung von Aminen
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DE10308111A1 (de) 2003-02-26 2004-09-09 Bayer Technology Services Gmbh Verfahren zum Abtrennen von gelösten oder kolloidalen Feststoffen aus nicht wässrigen Lösungen
DE102005046250B4 (de) 2005-09-27 2020-10-08 Evonik Operations Gmbh Anlage zur Abtrennung von organischen Übergangsmetallkomplexkatalysatoren
DE102008041652A1 (de) 2008-08-28 2010-03-04 Evonik Oxeno Gmbh Vorrichtung und Verfahren für die kontinuierliche Umsetzung einer Flüssigkeit mit einem Gas
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DE102009001225A1 (de) 2009-02-27 2010-09-02 Evonik Oxeno Gmbh Verfahren zur Anreicherung eines Homogenkatalysators aus einem Prozessstrom

Also Published As

Publication number Publication date
CN103906565B (zh) 2017-05-24
DE102011082441A1 (de) 2013-03-14
JP2014526372A (ja) 2014-10-06
US9393537B2 (en) 2016-07-19
KR20140071416A (ko) 2014-06-11
CN103906565A (zh) 2014-07-02
ZA201402509B (en) 2015-12-23
US9149780B2 (en) 2015-10-06
US20140343327A1 (en) 2014-11-20
EP2753421B1 (de) 2019-04-10
ES2729101T3 (es) 2019-10-30
EP2753421A1 (de) 2014-07-16
SG11201400458QA (en) 2014-05-29
KR101647239B1 (ko) 2016-08-09
WO2013034690A1 (de) 2013-03-14
US20150336078A1 (en) 2015-11-26

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