AU2001240616A1 - Method for processing a liquid hydroformylation discharge - Google Patents
Method for processing a liquid hydroformylation dischargeInfo
- Publication number
- AU2001240616A1 AU2001240616A1 AU2001240616A AU4061601A AU2001240616A1 AU 2001240616 A1 AU2001240616 A1 AU 2001240616A1 AU 2001240616 A AU2001240616 A AU 2001240616A AU 4061601 A AU4061601 A AU 4061601A AU 2001240616 A1 AU2001240616 A1 AU 2001240616A1
- Authority
- AU
- Australia
- Prior art keywords
- hydroformylation
- boiling
- products
- pressure
- liquid
- 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.)
- Abandoned
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C45/00—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds
- C07C45/49—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by reaction with carbon monoxide
- C07C45/50—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by reaction with carbon monoxide by oxo-reactions
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Abstract
A liquid output from a continuous hydroformylation, which comprises essentially aldehydes, high-boiling by-products, a homogeneously dissolved hydroformylation catalyst, unreacted olefins, low-boiling by-products and dissolved synthesis gas, is worked up by a process in which a) the liquid hydroformylation output is depressurized in a first depressurization stage to a pressure which is from 2 to 20 bar below the reactor pressure, resulting in separation into a liquid phase and a gas phase, and b) the liquid phase obtained in the first depressurization stage is depressurized in a second depressurization stage to a pressure which is lower than the pressure of the first depressurization stage, resulting in separation into a liquid phase comprising essentially high-boiling by-products of the hydroformylation, the homogeneously dissolved hydroformylation catalyst and small amounts of hydroformylation product and unreacted olefin and a gas phase comprising essentially the major part of the hydroformylation product, unreacted olefin and low-boiling by-products.
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE10006489 | 2000-02-14 | ||
| DE10006489A DE10006489A1 (en) | 2000-02-14 | 2000-02-14 | Process for working up a liquid hydroformylation discharge |
| PCT/EP2001/001582 WO2001058844A2 (en) | 2000-02-14 | 2001-02-13 | Method for processing a liquid hydroformylation discharge |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| AU2001240616A1 true AU2001240616A1 (en) | 2001-08-20 |
Family
ID=7630846
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| AU2001240616A Abandoned AU2001240616A1 (en) | 2000-02-14 | 2001-02-13 | Method for processing a liquid hydroformylation discharge |
Country Status (11)
| Country | Link |
|---|---|
| US (1) | US6727391B2 (en) |
| EP (1) | EP1255720B2 (en) |
| JP (1) | JP2004506602A (en) |
| KR (1) | KR100742423B1 (en) |
| CN (1) | CN1223568C (en) |
| AT (1) | ATE249411T1 (en) |
| AU (1) | AU2001240616A1 (en) |
| DE (2) | DE10006489A1 (en) |
| ES (1) | ES2207608T5 (en) |
| MY (1) | MY131816A (en) |
| WO (1) | WO2001058844A2 (en) |
Families Citing this family (19)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2005042458A2 (en) | 2003-10-21 | 2005-05-12 | Basf Aktiengesellschaft | Method for the continuous production of aldehydes |
| JP4736392B2 (en) * | 2004-10-14 | 2011-07-27 | 三菱化学株式会社 | Method for producing aldehyde |
| CN100526279C (en) * | 2006-04-11 | 2009-08-12 | 中国科学院兰州化学物理研究所 | Process of continuously preparing n-pentanal |
| MX2010014570A (en) | 2008-07-03 | 2011-08-15 | Dow Technology Investments Llc | Process of controlling heavies in a recycle catalyst stream. |
| DE102009016651B4 (en) | 2009-04-07 | 2011-11-17 | Oxea Gmbh | Process for the preparation of aldehydes |
| DE102009016652A1 (en) * | 2009-04-07 | 2010-10-14 | Oxea Gmbh | Process for working up a liquid hydroformylation discharge |
| CN102826976B (en) * | 2011-06-17 | 2015-04-15 | 中国石油化工股份有限公司 | Method for adjusting ratio of butyraldehyde to isobutyraldehyde in propylene catalytic preparation |
| CN102826968B (en) * | 2011-06-17 | 2015-07-22 | 中国石油化工股份有限公司 | Continuous hydroformylation for preparing aldehydes by adopting liquid-phase circulation way |
| CN102826971B (en) * | 2011-06-17 | 2015-01-07 | 中国石油化工股份有限公司 | Application method of catalyst in continuous hydroformylation process |
| JP6255007B2 (en) | 2013-03-27 | 2017-12-27 | 株式会社クラレ | Method for producing dialdehyde |
| CN110637003B (en) | 2017-05-16 | 2022-11-04 | 巴斯夫欧洲公司 | Hydroformylation process for large scale production of aldehydes and/or alcohols |
| CN113179638B (en) * | 2018-11-29 | 2023-11-28 | 陶氏技术投资有限责任公司 | Hydroformylation process |
| CN111320533B (en) * | 2019-10-28 | 2023-02-24 | 中国海洋石油集团有限公司 | Method for separating liquid discharge of butene hydroformylation reaction |
| WO2021160448A1 (en) | 2020-02-11 | 2021-08-19 | Basf Se | Low-pressure hydroformylation of diisobutene |
| KR20220037341A (en) * | 2020-09-17 | 2022-03-24 | 주식회사 엘지화학 | Manufacturing method of aldehyde and apparatus for manufacturing aldehyde |
| CN113041962B (en) * | 2021-04-01 | 2023-05-26 | 南京延长反应技术研究院有限公司 | Reaction system and method for preparing butyraldehyde by propylene carbonylation |
| CN114082210B (en) * | 2021-11-29 | 2022-11-04 | 万华化学集团股份有限公司 | Recovery method and recovery system for waste gas and waste liquid in hydroformylation unit |
| EP4630394A1 (en) | 2022-12-06 | 2025-10-15 | Dow Technology Investments LLC | Process of controlling heavies in a recycle catalyst stream |
| WO2026008361A1 (en) | 2024-07-01 | 2026-01-08 | Basf Se | Process for utilizing at least one waste stream from oxo synthesis plants |
Family Cites Families (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4148830A (en) * | 1975-03-07 | 1979-04-10 | Union Carbide Corporation | Hydroformylation of olefins |
| DE2965158D1 (en) * | 1979-03-21 | 1983-05-11 | Davy Mckee London | Hydroformylation process |
| DE3301591A1 (en) | 1983-01-19 | 1984-07-19 | Basf Ag, 6700 Ludwigshafen | METHOD FOR CONTINUOUS HYDROFORMYLATION OF OLEFINICALLY UNSATURATED COMPOUNDS |
| GB2192182B (en) * | 1986-07-01 | 1990-05-23 | Davy Mckee | Process for the production of aldehydes |
| JPH0768157B2 (en) * | 1988-08-02 | 1995-07-26 | 三菱化学株式会社 | Hydroformylation method |
| US5001274A (en) * | 1989-06-23 | 1991-03-19 | Union Carbide Chemicals And Plastics Company Inc. | Hydroformylation process |
| US5410091A (en) † | 1994-06-02 | 1995-04-25 | Quimica Oxal C.A. | Rhodium catalyzed oxo process in tubular reactor |
| DE19530698A1 (en) | 1995-08-21 | 1997-02-27 | Basf Ag | Process for working up a liquid hydroformylation discharge |
| US5883265A (en) * | 1997-04-15 | 1999-03-16 | Union Carbide Chemicals & Plastics Technology Corporation | Processes for producing epsilon caprolactones and/or hydrates and/or esters thereof |
-
2000
- 2000-02-14 DE DE10006489A patent/DE10006489A1/en not_active Withdrawn
-
2001
- 2001-02-05 MY MYPI20010492A patent/MY131816A/en unknown
- 2001-02-13 DE DE50100605T patent/DE50100605D1/en not_active Expired - Lifetime
- 2001-02-13 ES ES01911637T patent/ES2207608T5/en not_active Expired - Lifetime
- 2001-02-13 JP JP2001558396A patent/JP2004506602A/en active Pending
- 2001-02-13 KR KR1020027010467A patent/KR100742423B1/en not_active Expired - Fee Related
- 2001-02-13 AT AT01911637T patent/ATE249411T1/en not_active IP Right Cessation
- 2001-02-13 WO PCT/EP2001/001582 patent/WO2001058844A2/en not_active Ceased
- 2001-02-13 CN CNB018048528A patent/CN1223568C/en not_active Expired - Lifetime
- 2001-02-13 EP EP01911637A patent/EP1255720B2/en not_active Expired - Lifetime
- 2001-02-13 US US10/203,293 patent/US6727391B2/en not_active Expired - Lifetime
- 2001-02-13 AU AU2001240616A patent/AU2001240616A1/en not_active Abandoned
Also Published As
| Publication number | Publication date |
|---|---|
| CN1223568C (en) | 2005-10-19 |
| US20030013919A1 (en) | 2003-01-16 |
| MY131816A (en) | 2007-09-28 |
| JP2004506602A (en) | 2004-03-04 |
| DE50100605D1 (en) | 2003-10-16 |
| EP1255720B1 (en) | 2003-09-10 |
| ES2207608T5 (en) | 2009-06-15 |
| ATE249411T1 (en) | 2003-09-15 |
| WO2001058844A3 (en) | 2002-04-04 |
| US6727391B2 (en) | 2004-04-27 |
| WO2001058844A2 (en) | 2001-08-16 |
| EP1255720A2 (en) | 2002-11-13 |
| KR20020076305A (en) | 2002-10-09 |
| EP1255720B2 (en) | 2009-04-15 |
| KR100742423B1 (en) | 2007-07-24 |
| ES2207608T3 (en) | 2004-06-01 |
| DE10006489A1 (en) | 2001-08-16 |
| CN1400961A (en) | 2003-03-05 |
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