JP2016514741A5 - - Google Patents
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- Publication number
- JP2016514741A5 JP2016514741A5 JP2016504519A JP2016504519A JP2016514741A5 JP 2016514741 A5 JP2016514741 A5 JP 2016514741A5 JP 2016504519 A JP2016504519 A JP 2016504519A JP 2016504519 A JP2016504519 A JP 2016504519A JP 2016514741 A5 JP2016514741 A5 JP 2016514741A5
- Authority
- JP
- Japan
- Prior art keywords
- premixer
- stream
- caprolactam
- pressure
- water
- 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
- JBKVHLHDHHXQEQ-UHFFFAOYSA-N epsilon-caprolactam Chemical compound O=C1CCCCCN1 JBKVHLHDHHXQEQ-UHFFFAOYSA-N 0.000 claims description 90
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 44
- 238000000034 method Methods 0.000 claims description 31
- 238000004519 manufacturing process Methods 0.000 claims description 16
- 238000006116 polymerization reaction Methods 0.000 claims description 16
- 238000002156 mixing Methods 0.000 claims description 13
- 239000004952 Polyamide Substances 0.000 claims description 12
- 229920002647 polyamide Polymers 0.000 claims description 12
- 238000000605 extraction Methods 0.000 claims description 11
- 229920000642 polymer Polymers 0.000 claims description 10
- 125000004122 cyclic group Chemical group 0.000 claims description 9
- 230000003068 static effect Effects 0.000 claims description 9
- 239000000155 melt Substances 0.000 claims description 8
- 239000008187 granular material Substances 0.000 claims description 6
- 238000005469 granulation Methods 0.000 claims description 6
- 230000003179 granulation Effects 0.000 claims description 6
- 150000003951 lactams Chemical class 0.000 claims description 6
- 230000003134 recirculating effect Effects 0.000 claims description 6
- 230000015556 catabolic process Effects 0.000 claims description 5
- 238000006731 degradation reaction Methods 0.000 claims description 5
- 230000008018 melting Effects 0.000 claims description 5
- 238000002844 melting Methods 0.000 claims description 5
- 239000000654 additive Substances 0.000 claims description 4
- 238000000354 decomposition reaction Methods 0.000 claims description 4
- 239000011552 falling film Substances 0.000 claims description 4
- 238000012856 packing Methods 0.000 claims description 4
- 230000001174 ascending effect Effects 0.000 claims description 2
- 239000000284 extract Substances 0.000 claims description 2
- 238000010438 heat treatment Methods 0.000 claims description 2
- 238000004064 recycling Methods 0.000 claims 1
- 230000000630 rising effect Effects 0.000 claims 1
- 239000000047 product Substances 0.000 description 7
- 229920002292 Nylon 6 Polymers 0.000 description 6
- 238000006243 chemical reaction Methods 0.000 description 5
- 230000007423 decrease Effects 0.000 description 5
- 239000000539 dimer Substances 0.000 description 4
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 239000011541 reaction mixture Substances 0.000 description 3
- 239000007795 chemical reaction product Substances 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 238000005336 cracking Methods 0.000 description 2
- 238000007711 solidification Methods 0.000 description 2
- 230000008023 solidification Effects 0.000 description 2
- 230000000996 additive effect Effects 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 239000007806 chemical reaction intermediate Substances 0.000 description 1
- 230000015271 coagulation Effects 0.000 description 1
- 238000005345 coagulation Methods 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000002269 spontaneous effect Effects 0.000 description 1
- 239000003381 stabilizer Substances 0.000 description 1
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| EP13161146.9 | 2013-03-26 | ||
| EP13161146.9A EP2784102B1 (de) | 2013-03-26 | 2013-03-26 | Verfahren und Vorrichtung zur kontinuierlichen Rückführung von Extraktwässern im Polyamidherstellungsprozess |
| PCT/EP2014/051660 WO2014154379A1 (de) | 2013-03-26 | 2014-01-28 | Verfahren und vorrichtung zur kontinuierlichen rückführung von extraktwässern im polyamidherstellungsprozess |
Publications (3)
| Publication Number | Publication Date |
|---|---|
| JP2016514741A JP2016514741A (ja) | 2016-05-23 |
| JP2016514741A5 true JP2016514741A5 (enExample) | 2018-05-10 |
| JP6393308B2 JP6393308B2 (ja) | 2018-09-19 |
Family
ID=47913316
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2016504519A Expired - Fee Related JP6393308B2 (ja) | 2013-03-26 | 2014-01-28 | ポリアミド製造プロセスにおける抽出水の連続的再循環方法およびその装置 |
Country Status (9)
| Country | Link |
|---|---|
| EP (1) | EP2784102B1 (enExample) |
| JP (1) | JP6393308B2 (enExample) |
| KR (1) | KR102106077B1 (enExample) |
| CN (1) | CN105073831B (enExample) |
| ES (1) | ES2564676T3 (enExample) |
| PL (1) | PL2784102T3 (enExample) |
| SA (1) | SA515361011B1 (enExample) |
| TW (1) | TWI630222B (enExample) |
| WO (1) | WO2014154379A1 (enExample) |
Families Citing this family (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| TWI662065B (zh) * | 2016-11-29 | 2019-06-11 | 德商伍德英汎達 費雪有限責任公司 | 於尼龍-6的生產中回收清洗水萃取物之技術 |
| CN107051345A (zh) * | 2017-01-25 | 2017-08-18 | 江苏永通新材料科技有限公司 | 一种用于生产聚酰胺切片的低聚物分离器 |
| CN114402012A (zh) * | 2019-05-01 | 2022-04-26 | 诺沃赫姆绿色添加剂4私人有限公司 | 再循环低共熔组合物 |
| CN114426769B (zh) * | 2020-09-22 | 2024-11-05 | 中国石油化工股份有限公司 | 己内酰胺水解开环聚合制备尼龙6过程中回收的己内酰胺及其环状低聚体混合物的应用 |
| JPWO2022196407A1 (enExample) * | 2021-03-16 | 2022-09-22 |
Family Cites Families (18)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE2501348C3 (de) * | 1975-01-15 | 1988-02-11 | Basf Ag, 6700 Ludwigshafen | Kontinuierliches Verfahren zur Herstellung von Polyamiden aus epsilon-Caprolactam |
| DE3729853A1 (de) | 1987-09-05 | 1989-03-23 | Basf Ag | Verfahren zur aufarbeitung von destillationsrueckstaenden, die bei der reinigung von caprolactam anfallen |
| US5077381A (en) | 1990-06-01 | 1991-12-31 | Basf Corporation | Constant compositioin recycle of nylon 6 polymerization wash water |
| DE4405161A1 (de) * | 1994-02-18 | 1995-08-24 | Huels Chemische Werke Ag | Verfahren zur kontinuierlichen hydrolytischen Polymerisation von Laurinlactam |
| DE19531990A1 (de) | 1995-08-30 | 1997-05-15 | Polymer Eng Gmbh | Verfahren zur kontinuierlichen Herstellung von Polyamid 6 unter Verwendung von Rücklactam |
| DE19752181A1 (de) * | 1997-11-25 | 1999-05-27 | Basf Ag | Verfahren zur Herstellung von Polyamiden |
| DE19752183A1 (de) * | 1997-11-25 | 1999-05-27 | Basf Ag | Verfahren zur kontinuierlichen Extraktion von Polyamid |
| DE19801267B4 (de) | 1998-01-15 | 2005-03-24 | Inventa-Fischer Gmbh | Verfahren zur Herstellung von PA-6 Granulat und dessen Verwendung |
| NL1010161C2 (nl) * | 1998-09-23 | 2000-03-24 | Dsm Nv | Proces voor de productie van polyamide-6 uitgaande èpsilon-caprolactam. |
| DE19905754A1 (de) * | 1999-02-11 | 2000-08-17 | Basf Ag | Verfahren zur Herstellung von Polyamid 6 mit geringem Extraktgehalt, hoher Viskositätsstabilität und kleiner Remonomerisierungsrate |
| DE19925906A1 (de) | 1999-06-07 | 2000-12-14 | Basf Ag | Verfahren zur Herstellung von Polyamiden aus Lactamen und Polyamid-Extrakten |
| DE19962573A1 (de) * | 1999-12-23 | 2001-07-05 | Basf Ag | Verfahren zur Herstellung von Polyamiden |
| US6479620B1 (en) * | 2001-06-01 | 2002-11-12 | E. I. Du Pont De Nemours And Company | Process for converting caprolactam to nylon 6 |
| CN101080259B (zh) * | 2004-12-15 | 2012-03-28 | 旭化成化学株式会社 | 工业蒸发装置 |
| JP2009535468A (ja) * | 2006-05-04 | 2009-10-01 | ウーデ インベンタ−フィッシャー アーゲー | ポリアミド顆粒を連続的に製造するための方法 |
| ATE492584T1 (de) * | 2006-10-24 | 2011-01-15 | Basf Se | Verwendung von wendelrohrverdampfern bei der herstellung von polyamiden |
| PL2376557T3 (pl) * | 2008-12-12 | 2017-09-29 | Basf Se | Sposób ciągłego wytwarzania kopoliamidów z laktamów i soli diamin i kwasów dikarboksylowych |
| PL2532698T3 (pl) * | 2011-06-08 | 2016-12-30 | Sposób i urządzenie do bezpośredniej, ciągłej modyfikacji stopionych polimerów |
-
2013
- 2013-03-26 PL PL13161146T patent/PL2784102T3/pl unknown
- 2013-03-26 EP EP13161146.9A patent/EP2784102B1/de active Active
- 2013-03-26 ES ES13161146.9T patent/ES2564676T3/es active Active
-
2014
- 2014-01-28 CN CN201480018316.1A patent/CN105073831B/zh active Active
- 2014-01-28 WO PCT/EP2014/051660 patent/WO2014154379A1/de not_active Ceased
- 2014-01-28 KR KR1020157020019A patent/KR102106077B1/ko active Active
- 2014-01-28 JP JP2016504519A patent/JP6393308B2/ja not_active Expired - Fee Related
- 2014-02-19 TW TW103105401A patent/TWI630222B/zh active
-
2015
- 2015-09-07 SA SA515361011A patent/SA515361011B1/ar unknown
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