MXPA05012621A - Procedimiento para preparar caprolactama mezclando oxima de ciclohexanona a una mezcla de reaccion bajo condiciones de flujo turbulentas. - Google Patents

Procedimiento para preparar caprolactama mezclando oxima de ciclohexanona a una mezcla de reaccion bajo condiciones de flujo turbulentas.

Info

Publication number
MXPA05012621A
MXPA05012621A MXPA05012621A MXPA05012621A MXPA05012621A MX PA05012621 A MXPA05012621 A MX PA05012621A MX PA05012621 A MXPA05012621 A MX PA05012621A MX PA05012621 A MXPA05012621 A MX PA05012621A MX PA05012621 A MXPA05012621 A MX PA05012621A
Authority
MX
Mexico
Prior art keywords
reaction mixture
tube
cyclohexanone oxime
admixture
channels
Prior art date
Application number
MXPA05012621A
Other languages
English (en)
Inventor
Peter Wei-Hae Cheng
Original Assignee
Dsm Ip Assets Bv
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 Dsm Ip Assets Bv filed Critical Dsm Ip Assets Bv
Publication of MXPA05012621A publication Critical patent/MXPA05012621A/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
    • B01J19/26—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
    • 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
    • B01F25/312—Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof
    • B01F25/3124—Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof characterised by the place of introduction of the main flow
    • B01F25/31242—Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof characterised by the place of introduction of the main flow the main flow being injected in the central area of the venturi, creating an aspiration in the circumferential part of the conduit
    • 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
    • B01F25/312—Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof
    • B01F25/3121—Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof with additional mixing means other than injector mixers, e.g. screens, baffles or rotating elements
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07D—HETEROCYCLIC COMPOUNDS
    • C07D201/00—Preparation, separation, purification or stabilisation of unsubstituted lactams
    • C07D201/02—Preparation of lactams
    • C07D201/04—Preparation of lactams from or via oximes by Beckmann rearrangement
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07D—HETEROCYCLIC COMPOUNDS
    • C07D223/00—Heterocyclic compounds containing seven-membered rings having one nitrogen atom as the only ring hetero atom
    • C07D223/02—Heterocyclic compounds containing seven-membered rings having one nitrogen atom as the only ring hetero atom not condensed with other rings
    • C07D223/06—Heterocyclic compounds containing seven-membered rings having one nitrogen atom as the only ring hetero atom not condensed with other rings with hetero atoms or with carbon atoms having three bonds to hetero atoms with at the most one bond to halogen, e.g. ester or nitrile radicals, directly attached to ring carbon atoms
    • C07D223/08—Oxygen atoms
    • C07D223/10—Oxygen atoms attached in position 2
    • 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
    • B01J2219/00049—Controlling or regulating processes
    • B01J2219/00164—Controlling or regulating processes controlling the flow

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Other In-Based Heterocyclic Compounds (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Nitrogen And Oxygen Or Sulfur-Condensed Heterocyclic Ring Systems (AREA)
  • Spinning Or Twisting Of Yarns (AREA)

Abstract

La invencion se refiere a un procedimiento para preparar caprolactama mezclando oxima de ciclohesanona a una mezcla de reaccion que comprende caprolactama y acido sulfurico usando un dispositivo de mezclado, dicho dispositivo de mezclado comprendiendo (i) un tubo a traves del cual puede fluir la mezcla de reaccion, y (ii) canales dispuestos alrededor del tubo, dichos canales abriendose en el tubo, el procedimiento comprendiendo: hacer pasar la mezcla de reaccion a traves del tubo, y alimentar la oxima de ciclohexanona a la mezcla de reaccion a traves de uno o mas de dichos canales, en donde Re > 5,000, Re siendo el numero de Reynolds como se define por (.V.D/(, en donde ( = densidad (en kg/m3) de la mezcla de reaccion que se alimenta al tubo; V = velocidad de la mezcla de reaccion, V siendo definida como W/A, en donde W es la velocidad de flujo (en m3/s) de la mezcla de reaccion que se alimenta al tubo y A es el area de seccion transversal del tubo (en m2) al nivel en donde los canales se abren en el tubo; D = diametro del tubo al nivel en donde los canales se abren en el tubo (en m); ( = viscosidad de la mezcla de reaccion que se alimenta al tubo (en Pa(s).
MXPA05012621A 2003-05-23 2004-05-17 Procedimiento para preparar caprolactama mezclando oxima de ciclohexanona a una mezcla de reaccion bajo condiciones de flujo turbulentas. MXPA05012621A (es)

Applications Claiming Priority (5)

Application Number Priority Date Filing Date Title
EP03076592 2003-05-23
EP03076589 2003-05-23
EP03076590 2003-05-23
EP03076591 2003-05-23
PCT/EP2004/005338 WO2004113287A1 (en) 2003-05-23 2004-05-17 Process for preparing caprolactam by admixture of cyclohexanone oxime to a reaction mixture under turbulent flow conditions

Publications (1)

Publication Number Publication Date
MXPA05012621A true MXPA05012621A (es) 2006-02-08

Family

ID=33479744

Family Applications (3)

Application Number Title Priority Date Filing Date
MXPA05012689A MXPA05012689A (es) 2003-05-23 2004-05-17 Proceso continuo para preparar caprolactamas.
MXPA05012621A MXPA05012621A (es) 2003-05-23 2004-05-17 Procedimiento para preparar caprolactama mezclando oxima de ciclohexanona a una mezcla de reaccion bajo condiciones de flujo turbulentas.
MXPA05012688A MXPA05012688A (es) 2003-05-23 2004-05-17 Proceso para preparar carrolactama por medio de la redistribucion de beckman.

Family Applications Before (1)

Application Number Title Priority Date Filing Date
MXPA05012689A MXPA05012689A (es) 2003-05-23 2004-05-17 Proceso continuo para preparar caprolactamas.

Family Applications After (1)

Application Number Title Priority Date Filing Date
MXPA05012688A MXPA05012688A (es) 2003-05-23 2004-05-17 Proceso para preparar carrolactama por medio de la redistribucion de beckman.

Country Status (15)

Country Link
US (3) US7339056B2 (es)
EP (3) EP1626953B1 (es)
JP (3) JP5014791B2 (es)
KR (3) KR20060006088A (es)
CN (2) CN1842519B (es)
AT (3) ATE465991T1 (es)
BR (3) BRPI0410604A (es)
DE (3) DE602004026866D1 (es)
EA (3) EA009914B1 (es)
MX (3) MXPA05012689A (es)
MY (2) MY140436A (es)
PL (1) PL1628955T3 (es)
TW (3) TWI335317B (es)
UA (1) UA83663C2 (es)
WO (3) WO2004103963A1 (es)

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102399188B (zh) * 2010-09-10 2014-02-19 北京化工大学 一种贝克曼重排反应方法
WO2012141993A1 (en) 2011-04-09 2012-10-18 Amyris, Inc. Process for preparing hexamethylenediamine and polyamides therefrom
CN102229553B (zh) * 2011-05-06 2012-10-10 清华大学 一种多段重排由环己酮肟制备己内酰胺的系统及方法
CN103007869B (zh) * 2011-09-20 2015-02-25 中国石油化工股份有限公司 一种己内酰胺重排反应的三液相进料喷嘴
CN105085354B (zh) * 2014-05-07 2018-09-28 中国石油化工股份有限公司 一种己内酰胺制备方法
TW202128630A (zh) 2019-11-11 2021-08-01 荷蘭商卡普三世責任有限公司 工業規模上用於生產ε-己內醯胺及硫酸銨之方法及設備
CN115073343B (zh) * 2022-06-29 2023-09-29 中国天辰工程有限公司 一种不副产硫酸铵的己内酰胺合成方法

Family Cites Families (23)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2237365A (en) * 1938-11-28 1941-04-08 Ig Farbenindustrie Ag Production of oximes
CH454876A (de) 1966-01-14 1968-04-30 Inventa Ag Verfahren zur kontinuierlichen Herstellung von Lactamen
CH519448A (de) 1968-04-11 1972-02-29 Inventa Ag Mischvorrichtung
US3953438A (en) * 1975-02-07 1976-04-27 Eli Lilly And Company Preparation of cephalosporin ethers
US3914217A (en) * 1974-11-13 1975-10-21 Allied Chem Process for the preparation of lactams
DE2547025A1 (de) * 1974-11-13 1976-05-26 Allied Chem Verfahren zur herstellung von epsilon-caprolactam
JPS52135308A (en) * 1976-05-07 1977-11-12 Toa Nekken Kk Mixer for emulsifying water and oil
NL7609749A (nl) * 1976-09-02 1978-03-06 Stamicarbon Werkwijze voor de bereiding van lactamen uit cyclische oximen.
DE2845019A1 (de) * 1978-10-16 1980-04-30 Basf Ag Verfahren zur kontinuierlichen herstellung von epsilon -caprolactam durch beckmann'sche umlagerung
JPS61138529A (ja) * 1984-12-10 1986-06-26 Idemitsu Petrochem Co Ltd サイズ用乳化液の製造方法
DE3642314A1 (de) * 1986-12-11 1988-06-23 Basf Ag Verfahren zur herstellung von caprolactam durch beckmannsche umlagerung von cyclohexanonoxim
IT1204503B (it) * 1987-03-11 1989-03-03 Montedipe Spa Processo per la sintesi dell'epsiloncaprolattame
JPH0737435B2 (ja) * 1988-07-12 1995-04-26 三菱化学株式会社 オキシム類の製法
JP2576279Y2 (ja) * 1993-02-19 1998-07-09 敏克 清水 ボルドー液の調製装置
EP0785188A4 (en) * 1995-07-20 1998-12-02 Mitsubishi Chem Corp METHOD FOR PRODUCING YPSILON CAPROLACTAM
JPH1036332A (ja) * 1996-07-22 1998-02-10 Toray Ind Inc シクロヘキサノンオキシム塩酸塩の精製方法
JPH10180066A (ja) * 1996-12-26 1998-07-07 Jiinasu:Kk 微粒化方法及びその装置
US6333411B1 (en) * 1998-12-24 2001-12-25 Praxair Technology, Inc. Method for production of hydroxylammonium phosphate in the synthesis of caprolactam
WO2001094297A1 (en) * 2000-06-05 2001-12-13 Dsm N.V. Process for the production of cyclohexanone oxime
KR100843925B1 (ko) * 2000-06-05 2008-07-03 디에스엠 아이피 어셋츠 비.브이. 시클로헥사논 옥심의 제조방법
MXPA02011960A (es) * 2000-06-05 2003-07-14 Dsm Nv Procedimiento para la preparacion de ciclohexanona oxima.
JP4223694B2 (ja) * 2001-03-28 2009-02-12 住友化学株式会社 シクロヘキサノンオキシムの蒸発方法
AU2002347653A1 (en) 2001-11-26 2003-06-10 Dsm Ip Assets B.V. Process for recovering caprolactam

Also Published As

Publication number Publication date
JP5014792B2 (ja) 2012-08-29
EP1626953B1 (en) 2007-09-26
US20070060749A1 (en) 2007-03-15
TWI337991B (en) 2011-03-01
JP2007520445A (ja) 2007-07-26
WO2004113287A1 (en) 2004-12-29
CN1842519A (zh) 2006-10-04
EA200501858A1 (ru) 2006-06-30
DE602004009173T2 (de) 2008-06-26
BRPI0410577A (pt) 2006-06-20
DE602004032128D1 (de) 2011-05-19
EP1628955B1 (en) 2011-04-06
EP1633706A1 (en) 2006-03-15
MXPA05012689A (es) 2006-02-22
ATE504564T1 (de) 2011-04-15
CN104262223A (zh) 2015-01-07
US7339056B2 (en) 2008-03-04
BRPI0410604A (pt) 2006-06-20
KR101177137B1 (ko) 2012-08-24
TWI335318B (en) 2011-01-01
KR20060015616A (ko) 2006-02-17
JP2007500198A (ja) 2007-01-11
EA200501857A1 (ru) 2006-06-30
ATE465991T1 (de) 2010-05-15
EA009914B1 (ru) 2008-04-28
MY140436A (en) 2009-12-31
JP2007513061A (ja) 2007-05-24
DE602004026866D1 (de) 2010-06-10
EP1633706B1 (en) 2010-04-28
KR20060015615A (ko) 2006-02-17
EP1628955A1 (en) 2006-03-01
MXPA05012688A (es) 2006-02-22
WO2004103964A1 (en) 2004-12-02
UA83663C2 (ru) 2008-08-11
US20070083043A1 (en) 2007-04-12
EP1628955B9 (en) 2012-01-04
EA200501850A1 (ru) 2006-08-25
EA010840B1 (ru) 2008-12-30
WO2004103963A1 (en) 2004-12-02
TW200427658A (en) 2004-12-16
PL1628955T3 (pl) 2011-09-30
TW200505851A (en) 2005-02-16
KR101199719B1 (ko) 2012-11-08
US20070055061A1 (en) 2007-03-08
TWI335317B (en) 2011-01-01
KR20060006088A (ko) 2006-01-18
US7351820B2 (en) 2008-04-01
EP1626953A1 (en) 2006-02-22
EA009600B1 (ru) 2008-02-28
MY139965A (en) 2009-11-30
ATE374179T1 (de) 2007-10-15
CN1842519B (zh) 2011-06-15
DE602004009173D1 (de) 2007-11-08
JP5014791B2 (ja) 2012-08-29
US7358357B2 (en) 2008-04-15
TW200502217A (en) 2005-01-16
BRPI0410587A (pt) 2006-06-20

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