JP2005516058A5 - - Google Patents

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Publication number
JP2005516058A5
JP2005516058A5 JP2003563990A JP2003563990A JP2005516058A5 JP 2005516058 A5 JP2005516058 A5 JP 2005516058A5 JP 2003563990 A JP2003563990 A JP 2003563990A JP 2003563990 A JP2003563990 A JP 2003563990A JP 2005516058 A5 JP2005516058 A5 JP 2005516058A5
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JP
Japan
Prior art keywords
reaction mixture
reaction
density
methyl acetate
heavy phase
Prior art date
Legal status (The legal status 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 status listed.)
Granted
Application number
JP2003563990A
Other languages
English (en)
Japanese (ja)
Other versions
JP4263103B2 (ja
JP2005516058A (ja
Filing date
Publication date
Priority claimed from US10/058,547 external-priority patent/US6677480B2/en
Application filed filed Critical
Publication of JP2005516058A publication Critical patent/JP2005516058A/ja
Publication of JP2005516058A5 publication Critical patent/JP2005516058A5/ja
Application granted granted Critical
Publication of JP4263103B2 publication Critical patent/JP4263103B2/ja
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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JP2003563990A 2002-01-28 2003-01-09 重質相密度測定の使用による酢酸製造におけるプロセス制御 Expired - Fee Related JP4263103B2 (ja)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US10/058,547 US6677480B2 (en) 2002-01-28 2002-01-28 Process control in production of acetic acid via use of heavy phase density measurement
PCT/US2003/000503 WO2003064364A1 (en) 2002-01-28 2003-01-09 Process control in production of acetic acid via use of heavy phase density measurement

Publications (3)

Publication Number Publication Date
JP2005516058A JP2005516058A (ja) 2005-06-02
JP2005516058A5 true JP2005516058A5 (enExample) 2006-01-05
JP4263103B2 JP4263103B2 (ja) 2009-05-13

Family

ID=27609612

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2003563990A Expired - Fee Related JP4263103B2 (ja) 2002-01-28 2003-01-09 重質相密度測定の使用による酢酸製造におけるプロセス制御

Country Status (14)

Country Link
US (1) US6677480B2 (enExample)
EP (1) EP1470098B1 (enExample)
JP (1) JP4263103B2 (enExample)
KR (1) KR100922945B1 (enExample)
CN (1) CN1279011C (enExample)
AT (1) ATE431814T1 (enExample)
BR (1) BR0306690A (enExample)
CA (1) CA2466904C (enExample)
DE (1) DE60327690D1 (enExample)
ES (1) ES2327401T3 (enExample)
MX (1) MXPA04007238A (enExample)
MY (1) MY125742A (enExample)
TW (1) TWI247003B (enExample)
WO (1) WO2003064364A1 (enExample)

Families Citing this family (28)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FI20040260A0 (fi) * 2004-02-18 2004-02-18 Forchem Oy Menetelmä mäntyöljyn jalostamiseksi
US7271293B2 (en) * 2004-03-02 2007-09-18 Celanese International Corporation Control method for process of removing permanganate reducing compounds from methanol carbonylation process
US7053241B1 (en) 2005-02-24 2006-05-30 Celanese International Corporation Acetic acid production methods incorporating at least one metal salt as a catalyst stabilizer
DE102007037848B4 (de) 2007-08-10 2009-09-10 Siemens Ag Kathode
US7619113B2 (en) * 2007-09-27 2009-11-17 Celanese International Corporation Method and apparatus for making acetic acid with improved purification
US7790919B2 (en) * 2008-03-17 2010-09-07 Lyondell Chemical Technology, L.P. Removing hydrocarbon impurities from acetic acid production process
US7790920B2 (en) * 2008-09-11 2010-09-07 Lyondell Chemical Technology, L.P. Preparation of acetic acid
US8431740B2 (en) 2010-07-21 2013-04-30 Equistar Chemicals, Lp Controlling decanter phase separation of acetic acid production process
US8461379B2 (en) * 2010-10-12 2013-06-11 Celanese International Corporation Production of acetic acid comprising feeding at least one reactant to a recycle stream
US8519182B2 (en) * 2010-10-18 2013-08-27 Lyondell Chemical Technology, L.P. Acetic acid production process
US8916727B2 (en) 2011-12-16 2014-12-23 Celanese International Corporation Production of acetic acid with enhanced catalyst stability
US9598342B2 (en) 2013-03-15 2017-03-21 Celanese International Corporation Production of acetic acid with enhanced catalyst stability
CN104513143A (zh) * 2013-09-26 2015-04-15 陶氏技术投资有限责任公司 加氢甲酰化方法
US9233907B1 (en) 2014-11-14 2016-01-12 Celanese International Corporation Reducing hydrogen iodide content in carbonylation processes
US9302975B1 (en) 2015-07-01 2016-04-05 Celanese International Corporation Process for flashing a reaction medium
US9512056B2 (en) * 2015-02-04 2016-12-06 Celanese International Corporation Process to control HI concentration in residuum stream
US9505696B2 (en) * 2015-02-04 2016-11-29 Celanese International Corporation Process to control HI concentration in residuum stream
US9382183B1 (en) 2015-07-01 2016-07-05 Celanese International Corporation Process for flashing a reaction medium
US9302974B1 (en) 2015-07-01 2016-04-05 Celanese International Corporation Process for producing acetic acid
RS63644B1 (sr) 2015-10-02 2022-10-31 Celanese Int Corp Postupak za proizvodnju sirćetne kiseline recikliranjem vode
US9957216B2 (en) 2015-11-13 2018-05-01 Celanese International Corporation Processes for producing acetic acid
US9908835B2 (en) 2015-11-13 2018-03-06 Celanese International Corporation Processes for purifying acetic and hydrating anhydride
US10807935B2 (en) 2018-11-02 2020-10-20 Celanese International Corporation Process for continuous acetic acid production
WO2021202270A1 (en) 2020-04-01 2021-10-07 Celanese International Corporation Processes for removing and/or reducing permanganate reducing compounds and alkyl iodides
WO2021247854A1 (en) 2020-06-03 2021-12-09 Celanese International Corporation Production and purification of acetic acid
EP4161888A1 (en) 2020-06-03 2023-04-12 Celanese International Corporation Process for acetic acid production by removing permanganate reducing compounds
KR20230019135A (ko) 2020-06-03 2023-02-07 셀라니즈 인터내셔날 코포레이션 공정 스트림으로부터 아세탈의 제거
CN113295819B (zh) * 2021-06-30 2024-08-13 内蒙古易高煤化科技有限公司 一种气相甲醇羰基氧化法制碳酸二甲酯的催化剂评价装置

Family Cites Families (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3769329A (en) 1970-03-12 1973-10-30 Monsanto Co Production of carboxylic acids and esters
US5026908A (en) 1984-05-03 1991-06-25 Hoechst Celanese Corporation Methanol carbonylation process
US5144068A (en) 1984-05-03 1992-09-01 Hoechst Celanese Corporation Methanol carbonylation process
US5001259A (en) 1984-05-03 1991-03-19 Hoechst Celanese Corporation Methanol carbonylation process
US5352415A (en) * 1993-09-29 1994-10-04 Hoechst Celanese Corporation Control system for acetic acid manufacturing process
US5374774A (en) * 1994-03-11 1994-12-20 Hoechst Celanese Corporation Control system for an acetic acid manufacturing process
US5474774A (en) 1994-03-25 1995-12-12 Jlb, Inc. Adhesion inhibiting composition
US5554790A (en) * 1994-04-04 1996-09-10 Daicel Chemical Industries, Ltd. Process for producing acetic anhydride and acetic acid
JP3308392B2 (ja) * 1994-06-02 2002-07-29 ダイセル化学工業株式会社 カルボニル化反応方法
KR100403367B1 (ko) * 1995-04-27 2004-03-26 다이셀 가가꾸 고교 가부시끼가이샤 아세트산제조법
GB9816564D0 (en) * 1998-07-31 1998-09-30 Bp Chem Int Ltd Process
GB9819079D0 (en) * 1998-09-03 1998-10-28 Bp Chem Int Ltd Carbonylation process
GB9825424D0 (en) 1998-11-19 1999-01-13 Bp Chem Int Ltd Process
US6103934A (en) * 1998-12-18 2000-08-15 Millennium Petrochemicals, Inc. Manufacturing and process control methods
US6552221B1 (en) * 1998-12-18 2003-04-22 Millenium Petrochemicals, Inc. Process control for acetic acid manufacture

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