JP2018513125A5 - - Google Patents

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Publication number
JP2018513125A5
JP2018513125A5 JP2017548128A JP2017548128A JP2018513125A5 JP 2018513125 A5 JP2018513125 A5 JP 2018513125A5 JP 2017548128 A JP2017548128 A JP 2017548128A JP 2017548128 A JP2017548128 A JP 2017548128A JP 2018513125 A5 JP2018513125 A5 JP 2018513125A5
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JP
Japan
Prior art keywords
slurry
region
gas
oxidative decomposition
bcr
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Application number
JP2017548128A
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English (en)
Japanese (ja)
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JP2018513125A (ja
JP6882182B2 (ja
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Publication date
Priority claimed from US14/657,523 external-priority patent/US20160264511A1/en
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Publication of JP2018513125A publication Critical patent/JP2018513125A/ja
Publication of JP2018513125A5 publication Critical patent/JP2018513125A5/ja
Application granted granted Critical
Publication of JP6882182B2 publication Critical patent/JP6882182B2/ja
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JP2017548128A 2015-03-13 2016-03-11 気泡塔反応器型分解装置、及びその使用方法 Active JP6882182B2 (ja)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
US14/657,523 US20160264511A1 (en) 2015-03-13 2015-03-13 Bubble column reactor based digester and method for its use
US14/657,523 2015-03-13
PCT/US2016/021912 WO2016149060A1 (en) 2015-03-13 2016-03-11 Bubble column reactor based digester andmethod for its use

Publications (3)

Publication Number Publication Date
JP2018513125A JP2018513125A (ja) 2018-05-24
JP2018513125A5 true JP2018513125A5 (enExample) 2020-07-30
JP6882182B2 JP6882182B2 (ja) 2021-06-02

Family

ID=56887404

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2017548128A Active JP6882182B2 (ja) 2015-03-13 2016-03-11 気泡塔反応器型分解装置、及びその使用方法

Country Status (16)

Country Link
US (1) US20160264511A1 (enExample)
EP (1) EP3268341B1 (enExample)
JP (1) JP6882182B2 (enExample)
KR (1) KR102727963B1 (enExample)
CN (1) CN107531602B (enExample)
BR (1) BR112017019452B1 (enExample)
CA (1) CA2979681A1 (enExample)
EA (1) EA034735B1 (enExample)
ES (1) ES2880688T3 (enExample)
LT (1) LT3268341T (enExample)
MX (1) MX2017011729A (enExample)
MY (1) MY188141A (enExample)
PL (1) PL3268341T3 (enExample)
PT (1) PT3268341T (enExample)
SG (2) SG10201908521RA (enExample)
WO (1) WO2016149060A1 (enExample)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US11203769B1 (en) * 2017-02-13 2021-12-21 Solugen, Inc. Hydrogen peroxide and gluconic acid production
US10000435B1 (en) * 2017-02-28 2018-06-19 Grupo Petrotemex, S.A. De C.V. Energy and environmentally integrated method for production of aromatic dicarboxylic acids by oxidation
CN119056494B (zh) * 2023-05-31 2025-11-14 中国石油化工股份有限公司 一种加氢催化剂及其制备方法和应用

Family Cites Families (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5200557A (en) * 1991-04-12 1993-04-06 Amoco Corporation Process for preparation of crude terephthalic acid suitable for reduction to prepare purified terephthalic acid
DE19843573A1 (de) * 1998-09-23 2000-03-30 Degussa Blasensäule und deren Verwendung
US7196215B2 (en) * 2001-06-04 2007-03-27 Eastman Chemical Company Process for the production of purified terephthalic acid
US7683210B2 (en) * 2004-09-02 2010-03-23 Eastman Chemical Company Optimized liquid-phase oxidation
US7608732B2 (en) * 2005-03-08 2009-10-27 Eastman Chemical Company Optimized liquid-phase oxidation
US7355068B2 (en) * 2006-01-04 2008-04-08 Eastman Chemical Company Oxidation system with internal secondary reactor
US7816556B2 (en) * 2006-03-01 2010-10-19 Eastman Chemical Company Polycarboxylic acid production system employing enhanced multistage oxidative digestion
US7326808B2 (en) * 2006-03-01 2008-02-05 Eastman Chemical Company Polycarboxylic acid production system employing cooled mother liquor from oxidative digestion as feed to impurity purge system
US7393973B2 (en) * 2006-03-01 2008-07-01 Eastman Chemical Company Polycarboxylic acid production system with enhanced residence time distribution for oxidative digestion
CN101531588B (zh) * 2008-03-13 2016-02-24 周向进 一种新的精对苯二甲酸的制造方法
CN202700501U (zh) 2012-05-15 2013-01-30 中国昆仑工程公司 适于kpta生产的无搅拌氧化和深度氧化反应系统
CN102731297B (zh) * 2012-07-11 2014-06-04 浙江大学 一种逐级升温氧化制备中纯度对苯二甲酸的方法

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