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BR9913891A - Processo para recuperação por destilação de monoetileno glicol de alta pureza - Google Patents

Processo para recuperação por destilação de monoetileno glicol de alta pureza

Info

Publication number
BR9913891A
BR9913891A BR9913891-3A BR9913891A BR9913891A BR 9913891 A BR9913891 A BR 9913891A BR 9913891 A BR9913891 A BR 9913891A BR 9913891 A BR9913891 A BR 9913891A
Authority
BR
Brazil
Prior art keywords
monoethylene glycol
high purity
distillation
recovery process
distillation recovery
Prior art date
Application number
BR9913891-3A
Other languages
English (en)
Other versions
BR9913891B1 (pt
Inventor
Till Adrian
Bernd Bessling
Hans Hasse
Frans Vansant
Gerhard Theis
Original Assignee
Basf Ag
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 Basf Ag filed Critical Basf Ag
Publication of BR9913891A publication Critical patent/BR9913891A/pt
Publication of BR9913891B1 publication Critical patent/BR9913891B1/pt

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C29/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
    • C07C29/74—Separation; Purification; Use of additives, e.g. for stabilisation
    • C07C29/76—Separation; Purification; Use of additives, e.g. for stabilisation by physical treatment
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C29/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
    • C07C29/74—Separation; Purification; Use of additives, e.g. for stabilisation
    • C07C29/76—Separation; Purification; Use of additives, e.g. for stabilisation by physical treatment
    • C07C29/80—Separation; Purification; Use of additives, e.g. for stabilisation by physical treatment by distillation

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Abstract

"PROCESSO PARA RECUPERAçãO POR DESTILAçãO DE MONOETILENO GLICOL DE ALTA PUREZA" A invenção diz respeito a um processo para obter-se monoetileno glicol altamente puro de produto de hidrólise de oxido de etileno por destilação, por meios de desidratação sob pressão, preferivelmente em uma cascata, desidratação a vácuo, e subseq³ente destilação pura. Em conformidade ao processo inventivo, a coluna de desidratação de pressão ou pelo menos a primeira coluna de desidratação de pressão da cascata (2, 3, 4) tem uma seção de extração com pelo menos um estágio de separação, preferivelmente de 2 a 10 estágios de separação, especialmente de 3 a 6 estágios, e naquela parte da corrente de topo de coluna(s) de desidratação (2, 3, 4) é (são) repartida(s) com a seção de extração.
BRPI9913891-3A 1998-09-23 1999-09-21 processo para a purificação de monoetileno glicol a partir do produto de hidrólise do óxido de etileno. BR9913891B1 (pt)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
DE19843652.1 1998-09-23
DE19843652A DE19843652A1 (de) 1998-09-23 1998-09-23 Verfahren zur Herstellung von hochreinem Monoethylenglykol
PCT/EP1999/006967 WO2000017140A1 (de) 1998-09-23 1999-09-21 Verfahren zur herstellung von hochreinem monoethylenglykol

Publications (2)

Publication Number Publication Date
BR9913891A true BR9913891A (pt) 2001-07-03
BR9913891B1 BR9913891B1 (pt) 2011-01-11

Family

ID=7881987

Family Applications (1)

Application Number Title Priority Date Filing Date
BRPI9913891-3A BR9913891B1 (pt) 1998-09-23 1999-09-21 processo para a purificação de monoetileno glicol a partir do produto de hidrólise do óxido de etileno.

Country Status (20)

Country Link
US (1) US6514388B1 (pt)
EP (1) EP1115681B1 (pt)
JP (1) JP4427189B2 (pt)
KR (1) KR100670881B1 (pt)
CN (1) CN1183077C (pt)
AR (1) AR020654A1 (pt)
AT (1) ATE234799T1 (pt)
AU (1) AU6466399A (pt)
BR (1) BR9913891B1 (pt)
CA (1) CA2345140C (pt)
DE (2) DE19843652A1 (pt)
ES (1) ES2194518T3 (pt)
ID (1) ID29489A (pt)
MY (1) MY122385A (pt)
PL (1) PL196671B1 (pt)
RU (1) RU2237649C2 (pt)
SA (1) SA99200782B1 (pt)
TW (1) TW498061B (pt)
UA (1) UA60381C2 (pt)
WO (1) WO2000017140A1 (pt)

Families Citing this family (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2833951A1 (fr) * 2001-12-21 2003-06-27 Bp Chemicals Snc Procede de fabrication et de recuperation d'oxyde d'ethylene
CN100413833C (zh) * 2004-04-16 2008-08-27 中国石油化工股份有限公司上海石油化工研究院 环氧乙烷水合制乙二醇的方法
CN1321099C (zh) * 2005-09-28 2007-06-13 蓝仁水 从稀水溶液中浓缩低级多元醇的工艺方法
US8197645B2 (en) * 2005-12-29 2012-06-12 Basf Aktiengesellschaft Process for separating propylene glycol from aqueous compositions
TW200838838A (en) * 2006-12-22 2008-10-01 Dow Technology Investments Llc Process for reducing side-reactions during alkylene glycol and poly-alkylene glycol manufacturing
BRPI0920560B1 (pt) * 2008-10-09 2017-10-24 Shell Internationale Research Maartschappij B.V Processes for the recovery of monoetileno glycol from a catalyst purge current, and, for the manufacture of monoetilene glycol.
CN106242945A (zh) * 2008-11-10 2016-12-21 陶氏技术投资有限公司 用于生产低色素二醇的方法
PL217778B1 (pl) 2011-06-20 2014-08-29 Piotr Medoń Sposób osuszania glikolu i układ do osuszania glikolu
CN102951999B (zh) * 2012-11-15 2014-09-10 四川亚联高科技股份有限公司 一种乙二醇生产过程中的脱水方法
CN103553877B (zh) * 2013-10-22 2015-06-17 新疆天业（集团）有限公司 电石炉气制乙二醇中乙二醇精馏的方法
KR101527394B1 (ko) * 2014-01-06 2015-06-09 한국과학기술원 원료 내 회수대상물질을 회수하는 공정에 구비되는 저용해도 염 제거장치
KR102395386B1 (ko) * 2015-04-13 2022-05-09 삼성디스플레이 주식회사 고순도 글리콜계 화합물의 제조방법
ES2729155T3 (es) * 2015-12-16 2019-10-30 Repsol Sa Método para la preparación de glicoles
CN107867973A (zh) * 2016-12-31 2018-04-03 福建双环能源科技股份有限公司 一种乙二醇脱水装置及使用方法
GB201710508D0 (en) 2017-06-30 2017-08-16 Johnson Matthey Davy Technologies Ltd Process
KR102663736B1 (ko) 2017-11-23 2024-05-10 쉘 인터내셔날 리써취 마트샤피지 비.브이. 에틸렌 옥시드 및 에틸렌 글리콜 생산 방법
US20230312864A1 (en) * 2020-08-10 2023-10-05 Auriga Polymers, Inc. Process for purification of recovered glycol from chemical recycling of waste polyester
EP4567020A1 (de) 2023-12-06 2025-06-11 Basf Se Reinigung von kühlmittelzusammensetzungen

Family Cites Families (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2510548A (en) * 1947-06-20 1950-06-06 Lummus Co Multiple-effect distillation
DE1942094A1 (de) 1968-08-22 1970-02-26 Union Carbide Corp Verfahren zur Reinigung von verunreinigten Glykolen
US3847754A (en) * 1970-08-03 1974-11-12 Ppg Industries Inc Recovery of glycols from mixed glycol composition by distillation with acid treatment
IT972794B (it) * 1972-12-22 1974-05-31 Sir Soc Italiana Resine Spa Procedimento perfezionato per la produzione del glicole etilenico
DE3001727A1 (de) * 1980-01-18 1981-07-23 Hoechst Ag, 6000 Frankfurt Verfahren zur herstellung von hochreinem monoethylenglykol
DE3338488A1 (de) 1982-10-29 1984-05-03 Basf Ag, 6700 Ludwigshafen Verfahren zur gewinnung von temperaturempfindlichen produkten durch thermisch schonende destillation mittels eines mit einer destillationskolonne verbundenen duennschichtverdampfers und eine anordnung zur durchfuehrung des verfahrens
JPS6089439A (ja) 1983-10-24 1985-05-20 Mitsui Toatsu Chem Inc エチレングリコ−ルの製造方法
FR2564458B1 (fr) * 1984-05-15 1986-09-12 Atochem Procede de separation de l'ethyleneglycol sous forme concentree dans un procede de fabrication d'oxyde d'ethylene
DE19602116A1 (de) 1996-01-22 1997-07-24 Basf Ag Verfahren zur Gewinnung von Glykolen mit niedrigem Aldehydgehalt
RU2111949C1 (ru) * 1996-08-19 1998-05-27 Акционерное общество "Нижнекамскнефтехим" Способ извлечения моно- и диэтиленгликолей из кубового остатка процесса выделения моноэтиленгликоля

Also Published As

Publication number Publication date
DE59904662D1 (de) 2003-04-24
PL346752A1 (en) 2002-02-25
DE19843652A1 (de) 2000-03-30
JP2002526462A (ja) 2002-08-20
ID29489A (id) 2001-08-30
BR9913891B1 (pt) 2011-01-11
CN1183077C (zh) 2005-01-05
CA2345140A1 (en) 2000-03-30
PL196671B1 (pl) 2008-01-31
WO2000017140A1 (de) 2000-03-30
US6514388B1 (en) 2003-02-04
CN1319079A (zh) 2001-10-24
CA2345140C (en) 2009-06-16
RU2237649C2 (ru) 2004-10-10
MY122385A (en) 2006-04-29
KR100670881B1 (ko) 2007-01-18
ES2194518T3 (es) 2003-11-16
UA60381C2 (uk) 2003-10-15
ATE234799T1 (de) 2003-04-15
AR020654A1 (es) 2002-05-22
SA99200782B1 (ar) 2006-07-31
EP1115681B1 (de) 2003-03-19
EP1115681A1 (de) 2001-07-18
JP4427189B2 (ja) 2010-03-03
TW498061B (en) 2002-08-11
KR20010075294A (ko) 2001-08-09
AU6466399A (en) 2000-04-10

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Legal Events

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B06A Patent application procedure suspended [chapter 6.1 patent gazette]
B06A Patent application procedure suspended [chapter 6.1 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: 10 (DEZ) ANOS CONTADOS A PARTIR DE 11/01/2011, OBSERVADAS AS CONDICOES LEGAIS. 1- NAS LINHAS 19 E 20 DA PAGINA 9, ONDE SE LE: "...POR EXTRACAO DE VAPOR. O EFLUENTE EXTRATOR...", LEIA-SE: "...POR EXTRACAO DE VAPOR EM UM EXTRATOR (9). O EFLUENTE DO EXTRATOR...". 2- NA LINHA 1 DA PAGINA 10, ONDE SE LE: "...E E EXTRAIDA LIVRE DE...", LEIA-SE: "...E E EXTRAIDA PARA REMOCAO DE...".

B21A Patent or certificate of addition expired [chapter 21.1 patent gazette]

Free format text: PATENTE EXTINTA EM 11.01.2021