JP2011518879A5 - - Google Patents

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Publication number
JP2011518879A5
JP2011518879A5 JP2011507416A JP2011507416A JP2011518879A5 JP 2011518879 A5 JP2011518879 A5 JP 2011518879A5 JP 2011507416 A JP2011507416 A JP 2011507416A JP 2011507416 A JP2011507416 A JP 2011507416A JP 2011518879 A5 JP2011518879 A5 JP 2011518879A5
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JP
Japan
Prior art keywords
scrubber solvent
reactor
methyl iodide
scrubber
absorption tower
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JP2011507416A
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English (en)
Japanese (ja)
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JP5438758B2 (ja
JP2011518879A (ja
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Priority claimed from PCT/US2009/002505 external-priority patent/WO2009134332A2/en
Publication of JP2011518879A publication Critical patent/JP2011518879A/ja
Publication of JP2011518879A5 publication Critical patent/JP2011518879A5/ja
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Publication of JP5438758B2 publication Critical patent/JP5438758B2/ja
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JP2011507416A 2008-04-29 2009-04-23 複数の溶媒のオプションを有する吸収器を有するメタノールカルボニル化システム Active JP5438758B2 (ja)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
US12579108P 2008-04-29 2008-04-29
US61/125,791 2008-04-29
PCT/US2009/002505 WO2009134332A2 (en) 2008-04-29 2009-04-23 Methanol carbonylation system having absorber with multiple solvent options

Publications (3)

Publication Number Publication Date
JP2011518879A JP2011518879A (ja) 2011-06-30
JP2011518879A5 true JP2011518879A5 (enExample) 2012-03-01
JP5438758B2 JP5438758B2 (ja) 2014-03-12

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JP2011507416A Active JP5438758B2 (ja) 2008-04-29 2009-04-23 複数の溶媒のオプションを有する吸収器を有するメタノールカルボニル化システム

Country Status (20)

Country Link
US (3) US8318977B2 (enExample)
EP (2) EP2303447B1 (enExample)
JP (1) JP5438758B2 (enExample)
KR (1) KR101584387B1 (enExample)
CN (1) CN102036746B (enExample)
AR (1) AR074142A1 (enExample)
AU (2) AU2009241843B2 (enExample)
BR (1) BRPI0910840B1 (enExample)
CA (2) CA2722267C (enExample)
CL (1) CL2009001004A1 (enExample)
DE (1) DE11001538T8 (enExample)
ES (2) ES2523719T3 (enExample)
MX (2) MX2010011850A (enExample)
MY (2) MY156898A (enExample)
NZ (1) NZ588778A (enExample)
RU (1) RU2469783C2 (enExample)
TR (1) TR201108313T3 (enExample)
TW (2) TWI562983B (enExample)
WO (1) WO2009134332A2 (enExample)
ZA (1) ZA201007562B (enExample)

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US8895786B2 (en) 2011-08-03 2014-11-25 Celanese International Corporation Processes for increasing alcohol production
US9663437B2 (en) 2011-09-13 2017-05-30 Celanese International Corporation Production of acetic acid with high conversion rate
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US8802902B2 (en) 2011-12-30 2014-08-12 Celanese International Corporation Pressure driven distillation for ethanol production and recovery from hydrogenation process
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US8859810B2 (en) 2012-08-21 2014-10-14 Celanese International Corporation Process for recovering permanganate reducing compounds from an acetic acid production process
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US9233907B1 (en) * 2014-11-14 2016-01-12 Celanese International Corporation Reducing hydrogen iodide content in carbonylation processes
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CN104437004B (zh) * 2014-11-25 2016-04-06 赛鼎工程有限公司 一种适合低温甲醇洗过程中控制硫化氢尾气浓度的方法
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CN110573485B (zh) * 2018-07-02 2021-11-02 株式会社大赛璐 乙酸的制备方法
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