BR112013028740A2 - reator de amoximação para a produção de oxima de ciclo-hexanona - Google Patents

reator de amoximação para a produção de oxima de ciclo-hexanona

Info

Publication number
BR112013028740A2
BR112013028740A2 BR112013028740A BR112013028740A BR112013028740A2 BR 112013028740 A2 BR112013028740 A2 BR 112013028740A2 BR 112013028740 A BR112013028740 A BR 112013028740A BR 112013028740 A BR112013028740 A BR 112013028740A BR 112013028740 A2 BR112013028740 A2 BR 112013028740A2
Authority
BR
Brazil
Prior art keywords
approximation
reactor
internal
reaction
cyclohexanone oxime
Prior art date
Application number
BR112013028740A
Other languages
English (en)
Other versions
BR112013028740B1 (pt
Inventor
Alessandro Del Seppia
Elena Ghirardo
Original Assignee
Versalis Spa
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 Versalis Spa filed Critical Versalis Spa
Publication of BR112013028740A2 publication Critical patent/BR112013028740A2/pt
Publication of BR112013028740B1 publication Critical patent/BR112013028740B1/pt

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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/08Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with moving particles
    • B01J8/10Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with moving particles moved by stirrers or by rotary drums or rotary receptacles or endless belts
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/18Stationary reactors having moving elements inside
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/005Separating solid material from the gas/liquid stream
    • B01J8/006Separating solid material from the gas/liquid stream by filtration
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/20Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium
    • B01J8/22Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium gas being introduced into the liquid
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/20Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium
    • B01J8/22Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium gas being introduced into the liquid
    • B01J8/224Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium gas being introduced into the liquid the particles being subject to a circulatory movement
    • B01J8/226Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium gas being introduced into the liquid the particles being subject to a circulatory movement internally, i.e. the particles rotate within the vessel
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C249/00Preparation of compounds containing nitrogen atoms doubly-bound to a carbon skeleton
    • C07C249/04Preparation of compounds containing nitrogen atoms doubly-bound to a carbon skeleton of oximes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008Controlling the process
    • B01J2208/00017Controlling the temperature
    • B01J2208/00106Controlling the temperature by indirect heat exchange
    • B01J2208/00115Controlling the temperature by indirect heat exchange with heat exchange elements inside the bed of solid particles
    • B01J2208/00141Coils
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008Controlling the process
    • B01J2208/00017Controlling the temperature
    • B01J2208/00106Controlling the temperature by indirect heat exchange
    • B01J2208/00115Controlling the temperature by indirect heat exchange with heat exchange elements inside the bed of solid particles
    • B01J2208/0015Plates; Cylinders
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008Controlling the process
    • B01J2208/00017Controlling the temperature
    • B01J2208/00106Controlling the temperature by indirect heat exchange
    • B01J2208/00168Controlling the temperature by indirect heat exchange with heat exchange elements outside the bed of solid particles
    • B01J2208/00212Plates; Jackets; Cylinders
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00796Details of the reactor or of the particulate material
    • B01J2208/00823Mixing elements
    • B01J2208/00831Stationary elements
    • B01J2208/0084Stationary elements inside the bed, e.g. baffles
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00796Details of the reactor or of the particulate material
    • B01J2208/00823Mixing elements
    • B01J2208/00858Moving elements
    • B01J2208/00867Moving elements inside the bed, e.g. rotary mixer
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00796Details of the reactor or of the particulate material
    • B01J2208/00893Feeding means for the reactants
    • B01J2208/00902Nozzle-type feeding elements
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00796Details of the reactor or of the particulate material
    • B01J2208/00893Feeding means for the reactants
    • B01J2208/00911Sparger-type feeding elements
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00796Details of the reactor or of the particulate material
    • B01J2208/00938Flow distribution elements
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049Controlling or regulating processes
    • B01J2219/00245Avoiding undesirable reactions or side-effects
    • B01J2219/00247Fouling of the reactor or the process equipment
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2601/00Systems containing only non-condensed rings
    • C07C2601/12Systems containing only non-condensed rings with a six-membered ring
    • C07C2601/14The ring being saturated

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

reator de amoximação para a produção de oxima de ciclo-hexanona reator de amoximação para a produção de oxima de ciclo-hexanona, que compreende: (a) um vaso de reator equipado com um agitador, (b) um sistema de filtração interno, (c) uma serpentina de evaporação de amônia líquida interna, (d) um distribuidor toroidal de amônia gasosa interno, (e) um distribuidor toroidal externo de ciclo-hexanona, (f) um distribuidor toroidal de peróxido de hidrogênio interno; (g) um tubo de aspiração cilíndrico interno; (h) uma jaqueta de refrigeração externa. o referido reator de amoximação permite a obtenção de uma melhor mistura dos componentes da reação de amoximação e maximizar ambos os coeficientes de transferência de calor e os coeficientes de transferência de massa. além disso, o referido reator de amoximação permite aumentar o tempo de empacotamento do catalisador utilizado na reação de amoximação sobre o sistema de filtração (por exemplo, os fenômenos de entupimento), de modo a evitar a necessidade de realizar as retrolavagens com nitrogênio. além disso, o referido reator de amoximação não necessita de unidades de separação a jusante externas para separar o catalisador a partir da mistura de reação obtida a partir da reação de amoximação.
BR112013028740A 2011-05-09 2012-04-27 reator de amoximação para a produção de oxima de ciclo-hexanona BR112013028740B1 (pt)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CN201110209393.3A CN102773048B (zh) 2011-05-09 2011-05-09 生产环己酮肟的氨肟化反应器
PCT/EP2012/057746 WO2012152600A1 (en) 2011-05-09 2012-04-27 Ammoximation reactor for cyclohexanone oxime production

Publications (2)

Publication Number Publication Date
BR112013028740A2 true BR112013028740A2 (pt) 2017-01-24
BR112013028740B1 BR112013028740B1 (pt) 2020-04-14

Family

ID=46044669

Family Applications (1)

Application Number Title Priority Date Filing Date
BR112013028740A BR112013028740B1 (pt) 2011-05-09 2012-04-27 reator de amoximação para a produção de oxima de ciclo-hexanona

Country Status (12)

Country Link
US (1) US10525429B2 (pt)
EP (1) EP2707128B1 (pt)
JP (1) JP6058638B2 (pt)
KR (1) KR101941313B1 (pt)
CN (1) CN102773048B (pt)
BR (1) BR112013028740B1 (pt)
ES (1) ES2786002T3 (pt)
HU (1) HUE049692T2 (pt)
MY (1) MY166458A (pt)
PL (1) PL2707128T3 (pt)
TW (1) TWI538899B (pt)
WO (1) WO2012152600A1 (pt)

Families Citing this family (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103214393B (zh) * 2013-04-27 2014-08-20 湖南百利工程科技股份有限公司 一种酮的肟化方法
CN103551085A (zh) * 2013-11-08 2014-02-05 神马实业股份有限公司 一种用于环己酮氨肟化反应的催化剂分离装置
CN104860842B (zh) * 2015-05-13 2018-02-23 南京工业大学 一种基于膜分布的无溶剂绿色氨肟化工艺
EP3235560A1 (de) 2016-04-22 2017-10-25 Evonik Röhm GmbH Verfahren zur durchführung einer heterogen-katalysierten reaktion
CN106040108B (zh) * 2016-06-30 2018-09-14 湘潭大学 气-液-固三相反应器及连续催化氧化合成草甘膦的方法
CN108530316B (zh) * 2018-05-10 2023-07-04 中国平煤神马集团尼龙科技有限公司 一种固定床热回收式氨肟化反应系统
CN110787766B (zh) * 2019-10-10 2020-06-23 浙江工业大学 一种制备脂肪酸丁酯的塔式反应装置及工艺
CN112174850B (zh) * 2019-10-11 2022-11-22 福建天辰耀隆新材料有限公司 一种环己酮肟制备方法
CN111644121B (zh) * 2020-06-09 2022-02-11 常州市新鸿医药化工技术有限公司 一种三氯丙酮的加氢脱氯装置及其方法
CN112426957A (zh) * 2020-12-31 2021-03-02 湖南中天元环境工程有限公司 一种非均相氨肟化反应分离装置及方法
CN114789054A (zh) * 2021-01-25 2022-07-26 中国石油天然气股份有限公司 NiO/SiO2催化剂及其制备方法和应用
JP2024520502A (ja) 2021-05-28 2024-05-24 レーム・ゲーエムベーハー アルキル(メタ)アクリレートを製造するための反応器および方法
JP2024520503A (ja) 2021-05-28 2024-05-24 レーム・ゲーエムベーハー アルキルメタクリレートを製造するための反応器および方法
CN113877493B (zh) * 2021-08-24 2023-06-27 浙江中巨海锐科技有限公司 一种环十二酮溶液肟的连续化制备系统及方法
WO2023110831A1 (en) 2021-12-17 2023-06-22 Ineos Europe Ag Filtration device
CN114653328A (zh) * 2022-03-25 2022-06-24 中国科学院过程工程研究所 一种内置膜搅拌反应器
CN114712926B (zh) * 2022-04-18 2024-07-05 成都思达能环保设备有限公司 用于正极材料前驱体共沉淀反应设备的浓缩设备

Family Cites Families (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB577581A (en) 1943-02-24 1946-05-23 Texaco Development Corp Improvements in or relating to the alkylation of organic compounds
FR2038694A5 (pt) 1969-03-27 1971-01-08 Progil
FR2076365A5 (pt) * 1970-01-13 1971-10-15 Naphtachimie Sa
DE3245312A1 (de) * 1982-12-08 1984-06-14 Hoechst Ag, 6230 Frankfurt Verfahren zum durchfuehren (bio-)chemischer reaktionen
US5324853A (en) * 1993-01-19 1994-06-28 Exxon Chemical Patents Inc. Process for the production of plasticizer and polyolesters
KR100208654B1 (ko) * 1996-12-03 1999-07-15 윤덕용 하단 천공된 드래프트관을 갖는 내부순환유동층 가스화 반응기
BE1011581A3 (fr) * 1997-12-01 1999-11-09 Solvay Catalyseur a base de zeolite, son utilisation et procede d'epoxydation en presence de ce catalyseur.
AU1935601A (en) * 1999-12-10 2001-06-18 Inca International S.P.A. Impeller draft tube agitation system for gas-liquid mixing in a stirred tank reactor
GB2418626B (en) * 2003-07-15 2007-03-14 Sasol Tech Pty Ltd Process for separating a catalyst from a liquid
SG123723A1 (en) 2004-12-22 2006-07-26 Sumitomo Chemical Co Process for producing cyclohexanone oxime
JP4577205B2 (ja) * 2004-12-22 2010-11-10 住友化学株式会社 シクロヘキサノンオキシムの製造方法
JP2007203207A (ja) * 2006-02-02 2007-08-16 Sumitomo Chemical Co Ltd スパージャー、それを用いた反応器およびオキシムの製造方法。
CN101116804B (zh) * 2006-07-31 2010-06-23 中国石油化工股份有限公司 一体化反应分离设备
US20100084350A1 (en) * 2008-10-06 2010-04-08 Jing Liu Systems and Methods for Continuous Multiphase Reaction and Separation
CN201596496U (zh) * 2010-01-19 2010-10-06 河北瑞通美邦工程有限公司 一种环己酮氨肟化反应器
CN201988375U (zh) 2011-03-04 2011-09-28 河北美邦工程科技有限公司 一种环己酮氨肟化反应催化剂分离装置
JP6058515B2 (ja) * 2013-10-04 2017-01-11 漢民科技股▲分▼有限公司 気相成膜装置

Also Published As

Publication number Publication date
US10525429B2 (en) 2020-01-07
JP2014523863A (ja) 2014-09-18
US20140093437A1 (en) 2014-04-03
EP2707128B1 (en) 2020-03-18
CN102773048A (zh) 2012-11-14
KR101941313B1 (ko) 2019-01-22
KR20140038445A (ko) 2014-03-28
PL2707128T3 (pl) 2020-08-10
TWI538899B (zh) 2016-06-21
CN102773048B (zh) 2017-06-06
TW201249783A (en) 2012-12-16
BR112013028740B1 (pt) 2020-04-14
JP6058638B2 (ja) 2017-01-11
EP2707128A1 (en) 2014-03-19
HUE049692T2 (hu) 2020-10-28
ES2786002T3 (es) 2020-10-08
WO2012152600A1 (en) 2012-11-15
MY166458A (en) 2018-06-27

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B06F Objections, documents and/or translations needed after an examination request according [chapter 6.6 patent gazette]
B07A Application suspended after technical examination (opinion) [chapter 7.1 patent gazette]
B09A Decision: intention to grant [chapter 9.1 patent gazette]
B16A Patent or certificate of addition of invention granted [chapter 16.1 patent gazette]

Free format text: PRAZO DE VALIDADE: 20 (VINTE) ANOS CONTADOS A PARTIR DE 27/04/2012, OBSERVADAS AS CONDICOES LEGAIS.