SA518391224B1 - طريقة لإنتاج الأيزوسيانات - Google Patents

طريقة لإنتاج الأيزوسيانات

Info

Publication number
SA518391224B1
SA518391224B1 SA518391224A SA518391224A SA518391224B1 SA 518391224 B1 SA518391224 B1 SA 518391224B1 SA 518391224 A SA518391224 A SA 518391224A SA 518391224 A SA518391224 A SA 518391224A SA 518391224 B1 SA518391224 B1 SA 518391224B1
Authority
SA
Saudi Arabia
Prior art keywords
production capacity
transition period
during
excess phosgene
period
Prior art date
Application number
SA518391224A
Other languages
English (en)
Inventor
بلاتن بيتر
توماس كنوف د.
ستيفان فيرسهوفن د.
مانتسل ديرك
Original Assignee
كوفيسترو ديوتشلاند ايه جي
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 كوفيسترو ديوتشلاند ايه جي filed Critical كوفيسترو ديوتشلاند ايه جي
Publication of SA518391224B1 publication Critical patent/SA518391224B1/ar

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C263/00Preparation of derivatives of isocyanic acid
    • C07C263/10Preparation of derivatives of isocyanic acid by reaction of amines with carbonyl halides, e.g. with phosgene

Landscapes

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

Abstract

يتعلق الاختراع بطريقة مستمرة continuously operated method لإنتاج أيزوسيانات for producing isocyanates بتفاعل الأمينات المناظرة corresponding amines مع الفوسجين phosgene. عند تغيير سعة الإنتاج المستهدفة changing the target production capacity بدءاً من الحالة الأولية starting state بسعة إنتاج محددة with a specified production capacity والانتهاء بحالة نهائية end state بسعة إنتاجية مختلفة with a different production capacity، الفوسجين الفائض الحالي current excess phosgene بالفترة الانتقالية at the time of the transition period بين الحالة الأولية starting state والحالة النهائية end state ، التغيير بتدفق كتلة الأمينات the change of the amine mass flow يبدأ خلال الزمن المذكور said time ، على الأقل مساوياً لـ at least equal to ويفضل أن يكون أكبر من فائض الفوسجين greater than the excess phosgene خلال فترة الإنتاج production period عندما تكون السعة الإنتاجية production capacity بالحالة الأولية starting state قبل بدء الفترة الانتقالية transition period ؛ ومتوسط فائض الفوسجين average excess phosg
SA518391224A 2015-09-30 2018-03-28 طريقة لإنتاج الأيزوسيانات SA518391224B1 (ar)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
EP15187592 2015-09-30
PCT/EP2016/073036 WO2017055311A1 (de) 2015-09-30 2016-09-28 Verfahren zur herstellung von isocyanaten

Publications (1)

Publication Number Publication Date
SA518391224B1 true SA518391224B1 (ar) 2022-08-29

Family

ID=54252077

Family Applications (1)

Application Number Title Priority Date Filing Date
SA518391224A SA518391224B1 (ar) 2015-09-30 2018-03-28 طريقة لإنتاج الأيزوسيانات

Country Status (8)

Country Link
US (1) US10280135B2 (ar)
EP (1) EP3356324B1 (ar)
JP (1) JP6913083B2 (ar)
KR (1) KR20180059520A (ar)
CN (1) CN108137488B (ar)
HU (1) HUE060897T2 (ar)
SA (1) SA518391224B1 (ar)
WO (1) WO2017055311A1 (ar)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP3524591A1 (en) * 2018-02-13 2019-08-14 Covestro Deutschland AG Process for the preparation of isocyanates
KR102578617B1 (ko) * 2020-12-03 2023-09-13 에스케이씨 주식회사 자일릴렌디이소시아네이트 조성물 및 이를 포함하는 중합성 조성물
WO2022147830A1 (zh) * 2021-01-11 2022-07-14 万华化学集团股份有限公司 一种制备多异氰酸酯的方法及反应装置
WO2023208946A1 (de) 2022-04-27 2023-11-02 Covestro Deutschland Ag Verfahren zur wiedergewinnung von rohstoffen aus isocyanurat-haltigen polyurethanprodukten

Family Cites Families (34)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4422976A (en) 1981-04-07 1983-12-27 Mitsui Toatsu Chemicals, Incorporated Continuous preparation of organic isocyanates
DE3327274A1 (de) 1983-07-28 1985-02-07 Bayer Ag, 5090 Leverkusen Verfahren zur herstellung von phosgen unter gleichzeitiger erzeugung von dampf
DE3736988C1 (de) 1987-10-31 1989-03-23 Bayer Ag Verfahren zur kontinuierlichen Herstellung von organischen Mono- und Polyisocyanaten
DE4443642A1 (de) 1994-12-08 1996-06-13 Bayer Ag Kontinuierliches Verfahren zur Herstellung von organischen Isocyanaten
DE10158160A1 (de) 2001-11-28 2003-06-12 Basf Ag Herstellung von Isocyanaten in der Gasphase
DE10222023A1 (de) 2002-05-17 2003-11-27 Bayer Ag Verfahren zur Herstellung von Isocyanaten in der Gasphase
EP1371633A1 (en) 2002-06-14 2003-12-17 Bayer Ag Process for the purification of mixtures of toluenediisocyanate incorporating a dividing-wall distillation column
EP1371634A1 (en) 2002-06-14 2003-12-17 Bayer Ag Process for the purification of mixtures of toluenediisocyanate
ES2271171T3 (es) 2002-10-22 2007-04-16 Bayer Materialscience Ag Procedimiento para la purificacion de toluendiisocianato que incorpora una columna de destilacion de pared divisoria para la purificacion final.
DE10260084A1 (de) 2002-12-19 2004-07-01 Basf Ag Auftrennung eines Stoffgemisches aus Clorwasserstoff und Phosgen
DE10307141A1 (de) 2003-02-20 2004-09-02 Bayer Ag Verfahren zur Herstellung von (Poly)isocyanaten in der Gasphase
DE10333929A1 (de) 2003-07-25 2005-02-24 Bayer Materialscience Ag Herstellung von Mischungen von Di- und Polyisocyanaten der Diphenylmethanreihe mit hohen Gehalten an 4,4'-Methylendiphenyldiisocyanat und 2,4'-Methylendiphenyldiisocyanat
DE10349504A1 (de) 2003-10-23 2005-05-25 Bayer Technology Services Gmbh Verfahren zur Herstellung von Isocyanaten in der Gasphase
DE10359627A1 (de) 2003-12-18 2005-07-21 Bayer Materialscience Ag Verfahren zur Herstellung von Diisocyanaten
DE102004032871A1 (de) 2004-07-07 2006-02-09 Bayer Materialscience Ag Verfahren zur Herstellung von Polyisocyanaten durch adiabate Phosgenierung von primären Aminen
DE102004041777A1 (de) 2004-08-28 2006-03-02 Bayer Materialscience Ag Verfahren und Vorrichtung zur Herstellung von Phosgen
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DE102006058634A1 (de) 2006-12-13 2008-06-19 Bayer Materialscience Ag Verfahren zur Herstellung von Isocyanaten in der Gasphase
DE102006058633A1 (de) 2006-12-13 2008-06-19 Bayer Materialscience Ag Verfahren zur Herstellung von Isocyanaten in der Gasphase
DE102007061688A1 (de) 2007-12-19 2009-06-25 Bayer Materialscience Ag Verfahren und Mischaggregat zur Herstellung von Isocyanaten durch Phosgenierung primärer Amine
DE102008009761A1 (de) 2008-02-19 2009-08-27 Bayer Materialscience Ag Verfahren zur Herstellung von Isocyanaten
US8829232B2 (en) 2008-08-07 2014-09-09 Basf Se Process for preparing aromatic isocyanates
DE102008061686A1 (de) 2008-12-11 2010-06-17 Bayer Materialscience Ag Verfahren zur Herstellung von Isocyanaten in der Gasphase
DE102009032413A1 (de) 2009-07-09 2011-01-13 Bayer Materialscience Ag Verfahren zur Herstellung von Isocyanaten
DE102010029235A1 (de) * 2010-05-21 2011-11-24 Evonik Degussa Gmbh Hydrophile Polyisocyanate
CN102527312B (zh) 2010-12-29 2013-09-04 万华化学集团股份有限公司 一种快速混合反应器及其应用
US8816126B2 (en) * 2011-09-02 2014-08-26 Basf Se Process for preparing isocyanates
WO2013029918A1 (de) 2011-09-02 2013-03-07 Basf Se Verfahren zur herstellung von isocyanaten
US20150018575A1 (en) 2011-09-30 2015-01-15 Dow Global Technologies Llc Highly segregated jet mixer for phosgenation of amines
EP2586770A1 (de) 2011-10-27 2013-05-01 Basf Se Verfahren zur Herstellung von Isocyanaten und/oder Polyisocyanaten

Also Published As

Publication number Publication date
JP2018529722A (ja) 2018-10-11
EP3356324B1 (de) 2022-10-05
HUE060897T2 (hu) 2023-04-28
US20180265457A1 (en) 2018-09-20
KR20180059520A (ko) 2018-06-04
CN108137488B (zh) 2021-02-26
EP3356324A1 (de) 2018-08-08
CN108137488A (zh) 2018-06-08
US10280135B2 (en) 2019-05-07
JP6913083B2 (ja) 2021-08-04
WO2017055311A1 (de) 2017-04-06

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