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
- Authority
- JP
- Japan
- Prior art keywords
- slurry
- region
- gas
- oxidative decomposition
- bcr
- 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
Links
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 (https=) | 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 (https=) |
| EP (1) | EP3268341B1 (https=) |
| JP (1) | JP6882182B2 (https=) |
| KR (1) | KR102727963B1 (https=) |
| CN (1) | CN107531602B (https=) |
| BR (1) | BR112017019452B1 (https=) |
| CA (1) | CA2979681A1 (https=) |
| EA (1) | EA034735B1 (https=) |
| ES (1) | ES2880688T3 (https=) |
| LT (1) | LT3268341T (https=) |
| MX (1) | MX2017011729A (https=) |
| MY (1) | MY188141A (https=) |
| PL (1) | PL3268341T3 (https=) |
| PT (1) | PT3268341T (https=) |
| SG (2) | SG11201707399XA (https=) |
| WO (1) | WO2016149060A1 (https=) |
Families Citing this family (3)
| 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)
| 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 |
| US7608732B2 (en) * | 2005-03-08 | 2009-10-27 | Eastman Chemical Company | Optimized liquid-phase oxidation |
| US7683210B2 (en) | 2004-09-02 | 2010-03-23 | Eastman Chemical Company | Optimized liquid-phase oxidation |
| US7355068B2 (en) * | 2006-01-04 | 2008-04-08 | Eastman Chemical Company | Oxidation system with internal secondary reactor |
| 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 |
| US7816556B2 (en) * | 2006-03-01 | 2010-10-19 | Eastman Chemical Company | Polycarboxylic acid production system employing enhanced multistage oxidative digestion |
| 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 |
-
2015
- 2015-03-13 US US14/657,523 patent/US20160264511A1/en not_active Abandoned
-
2016
- 2016-03-11 MY MYPI2017001308A patent/MY188141A/en unknown
- 2016-03-11 SG SG11201707399XA patent/SG11201707399XA/en unknown
- 2016-03-11 ES ES16765474T patent/ES2880688T3/es active Active
- 2016-03-11 LT LTEP16765474.8T patent/LT3268341T/lt unknown
- 2016-03-11 MX MX2017011729A patent/MX2017011729A/es unknown
- 2016-03-11 KR KR1020177029210A patent/KR102727963B1/ko active Active
- 2016-03-11 JP JP2017548128A patent/JP6882182B2/ja active Active
- 2016-03-11 WO PCT/US2016/021912 patent/WO2016149060A1/en not_active Ceased
- 2016-03-11 SG SG10201908521R patent/SG10201908521RA/en unknown
- 2016-03-11 CA CA2979681A patent/CA2979681A1/en active Pending
- 2016-03-11 BR BR112017019452-0A patent/BR112017019452B1/pt active IP Right Grant
- 2016-03-11 EP EP16765474.8A patent/EP3268341B1/en active Active
- 2016-03-11 PL PL16765474T patent/PL3268341T3/pl unknown
- 2016-03-11 PT PT167654748T patent/PT3268341T/pt unknown
- 2016-03-11 CN CN201680027722.3A patent/CN107531602B/zh active Active
- 2016-03-11 EA EA201792031A patent/EA034735B1/ru not_active IP Right Cessation
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