WO1998034912A1 - Verfahren zur abtrennung von 6-aminocapronsäurenitril aus mischungen, die 6-aminocapronsäurenitril und ein imin enthalten - Google Patents
Verfahren zur abtrennung von 6-aminocapronsäurenitril aus mischungen, die 6-aminocapronsäurenitril und ein imin enthalten Download PDFInfo
- Publication number
- WO1998034912A1 WO1998034912A1 PCT/EP1998/000505 EP9800505W WO9834912A1 WO 1998034912 A1 WO1998034912 A1 WO 1998034912A1 EP 9800505 W EP9800505 W EP 9800505W WO 9834912 A1 WO9834912 A1 WO 9834912A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- distillation
- aminocapronitrile
- imine
- mixture
- column
- Prior art date
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C253/00—Preparation of carboxylic acid nitriles
- C07C253/32—Separation; Purification; Stabilisation; Use of additives
- C07C253/34—Separation; Purification
Definitions
- the present invention relates to a process for the distillative separation of 6-aminocapronitrile from mixtures (I) which contain 6-aminocapronitrile and an imine (II).
- Imines in particular tetrahydroazepine of the formula, are formed as by-products
- 6-aminocapronitrile is mainly used for fiber production via caprolactam as an intermediate or by direct polymerization to nylon 6.
- the 6-aminocapronitrile must have a high purity, the removal of tetrahydroazepine being known to cause problems.
- EP-A-497 333 describes a process according to which a mixture comprising 6-aminocapronitrile and tetrahydroazepine is reacted with an alkaline compound.
- the alkaline compound must be used in excess of the stoichiometrically required amount and the 6-aminocapronitrile must be distilled off from the reaction mixture obtained at greatly reduced pressure.
- a process for the distillative removal of 6-aminocapronitrile from mixtures (I) which contain 6-aminocapronitrile and an imine (II) was characterized in that the distillation is carried out in a distillation column and that at least one level of Distillation column found the distillation mixture has an average mean residence time of at least 5 minutes.
- Mixtures (I) can be obtained in a manner known per se by partial hydrogenation of adiponitrile, for example by a process according to EP-A-161 419, EP-A-77 911, US-A-4,389,348, US-A-4, 601 , 859, WO 93/1207, DE-A 42 35 466,
- the hydrogenation gives a mixture which contains 6-aminocapronitrile, hexamethylenediamine, an imine (II) and optionally adiponitrile.
- a mixture (I) which essentially contains 6-aminocapronitrile and an imine (II) can be obtained from this mixture, for example by distillation.
- Suitable imine (II) are aromatic, preferably aliphatic, such as acyclic or in particular cyclic imines, and mixtures thereof, particularly preferably tetrahydroazepine.
- Distillation apparatuses which have a pressure drop from 1 to 1000 mbar, preferably 3 to 300 mbar, from the bottom to the top, the pressure in the bottom being advantageously in the range from 10 to 1000 mbar and in the top in the range from 30 to 300 mbar.
- the distillation can be carried out in several, such as 2 or 3 columns, advantageously in a single column.
- the distillation mixture has at least one, preferably 1 to 15, particularly preferably 1 to 7, in particular 1, 2 or 3, levels of the distillation column having an average average residence time of at least 5 minutes, preferably at least 15 minutes, in particular at least 45 minutes.
- the distillation mixture is preferably removed from the distillation column on at least one level, passed through a residence time tank and fed back to the distillation column.
- the return can take place to the deduction level or to a level above or below the deduction level.
- the reflux from the distillation column can first be recycled through a retention tank and then back into the distillation column.
- the removal of distillation liquid from the column, passing through the residence time vessel, returning it to the distillation column and, if appropriate, circulation of the liquid in the residence time vessel can be carried out using apparatuses known per se, such as pumps, the return to the take-off level of the distillation column, in particular in the case of a tray column, or to a level above, in particular in the case of a packing column, or below the take-off level.
- Distillation of the mixture (I) can advantageously be carried out in the presence of carbon dioxide.
- Carbon dioxide can be added to the distillation mixture before or preferably during the distillation in the form of a compound which releases carbon dioxide under the distillation conditions, such as ammonium carbonate, ammonium carbamate or urea, or mixtures of such compounds, these compounds in pure form or in a liquid diluent, such as one or several components of the mixture (I) can be added, or in the form of solid, liquid or preferably gaseous carbon dioxide, for example in the form of a gas containing carbon dioxide or in particular in the form of pure gaseous carbon dioxide containing only the usual impurities.
- a compound which releases carbon dioxide under the distillation conditions such as ammonium carbonate, ammonium carbamate or urea, or mixtures of such compounds
- these compounds in pure form or in a liquid diluent such as one or several components of the mixture (I) can be added, or in the form of solid, liquid or preferably gaseous carbon dioxide, for example in the form of a gas containing carbon dioxide or in particular in the form of
- the carbon dioxide content in the distillation mixture should be 0.1 to 100 mol carbon dioxide per mol imine function of the imine (II).
- the distillation of the mixture (I) can advantageously be carried out with the addition of a compound (III) which is inert to 6-aminocapronitrile under the distillation conditions and whose boiling point under the distillation conditions is above the boiling point of 6-aminocapronitrile.
- Suitable compounds (III) are compounds from the group of aromatics, the aliphatics, such as acyclic and cyclic aliphatics, and aliphatic-aromatic compounds. These compounds can carry substituents, such as a hydroxyl, keto, ester, alkyl, aryl, cycloalkyl, arylalkyl group, preferably a nitrile or amino group, or several identical or different such groups.
- the compound (III) can consist of a compound or mixtures of such compounds.
- Compounds (III) are advantageous which can be converted into hexamethylenediamine, preferably 6-aminocapronitrile, in a simple manner, such as by hydrogenation, for example with a gas containing molecular hydrogen in the presence of a catalyst.
- the products obtained in this reaction can advantageously be reused in the process according to the invention.
- the difference in boiling points between the amine (I) and the compound (IV) should be 1 to 15 200 ° C, preferably 5 to 100 ° C under the distillation conditions.
- the compound (III) can be added to the mixture (I) before or during the distillation.
- the compound (III) can be added to the mixture (I) before the distillation in a manner known per se in customary mixing apartments.
- the compound (III) can be added to the mixture (I) during the distillation by feeding the compound (III) into the distillation apparatus, preferably in the bottom region.
- the 6-aminocaproic acid nitrile is obtained as the top product. If the mixture (I) contains adipodi-35 nitrile, this can in particular be removed via a side draw and advantageously returned to the mentioned complete or preferably partial hydrogenation.
- the overhead discharge collected in stationary operation over a period of 16 h contained 10 0.6% hexamethylenediamine and 0.13% tetrahydroazepine.
- the procedure was as in the comparative example, with the difference that the reflux was passed through a residence time thermostat at 100 ° C. before being fed to the column.
- the residence time in the container was 30 minutes.
- the top discharge collected in stationary operation over a balance period of 17 h contained, in addition to 6-aminocapronitrile, 0.6% hexamethylenediamine and 0.12% tetrahydroazepine.
- the overhead discharge collected over a balance period of 17 h in stationary operation contained, in addition to 6-aminocapronitrile, 0.6% hexamethylenediamine and 0.11% tetrahydroazepine.
- the overhead discharge collected over a period of 16 h in stationary operation contained, in addition to 6-aminocapronitrile, 0.6% hexamethylenediamine and 0.013% tetrahydroazepine.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Abstract
Description
Claims
Priority Applications (8)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE59801520T DE59801520D1 (de) | 1997-02-07 | 1998-01-30 | Verfahren zur abtrennung von 6-aminocapronsäurenitril aus mischungen, die 6-aminocapronsäurenitril und ein imin enthalten |
EP98905375A EP0961768B1 (de) | 1997-02-07 | 1998-01-30 | Verfahren zur abtrennung von 6-aminocapronsäurenitril aus mischungen, die 6-aminocapronsäurenitril und ein imin enthalten |
JP53372698A JP2001512430A (ja) | 1997-02-07 | 1998-01-30 | 6−アミノカプロニトリル及びイミンを含む混合物からの6−アミノカプロニトリルの除去 |
US09/367,068 US6169199B1 (en) | 1997-02-07 | 1998-01-30 | Method for separating 6-aminocaproic acid nitrile from mixtures containing 6-aminocaproic acid nitrile and an imine |
BR9807189-0A BR9807189A (pt) | 1997-02-07 | 1998-01-30 | Processo para remoção por destilação de 6-aminocapronitrila de misturas (i) que compreendem 6-aminocapronitrila e uma imina (ii) |
AU60982/98A AU6098298A (en) | 1997-02-07 | 1998-01-30 | Method for separating 6-aminocaproic acid nitrile from mixtures containing 6-aminocaproic acid nitrile and an imine |
KR10-1999-7007155A KR100492200B1 (ko) | 1997-02-07 | 1998-01-30 | 6-아미노카프로산 니트릴 및 이민을 함유하는 혼합물로부터 6-아미노카프로산 니트릴의 분리 방법 |
CA002280887A CA2280887A1 (en) | 1997-02-07 | 1998-01-30 | Method for separating 6-aminocaproic acid nitrile from mixtures containing 6-aminocaproic acid nitrile and an imine |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19704613.4 | 1997-02-07 | ||
DE19704613A DE19704613A1 (de) | 1997-02-07 | 1997-02-07 | Verfahren zur Abtrennung von 6-Aminocapronsäurenitril aus Mischungen, die 6-Aminocapronsäurenitril und ein Imin enthalten |
Publications (1)
Publication Number | Publication Date |
---|---|
WO1998034912A1 true WO1998034912A1 (de) | 1998-08-13 |
Family
ID=7819565
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/EP1998/000505 WO1998034912A1 (de) | 1997-02-07 | 1998-01-30 | Verfahren zur abtrennung von 6-aminocapronsäurenitril aus mischungen, die 6-aminocapronsäurenitril und ein imin enthalten |
Country Status (15)
Country | Link |
---|---|
US (1) | US6169199B1 (de) |
EP (1) | EP0961768B1 (de) |
JP (1) | JP2001512430A (de) |
KR (1) | KR100492200B1 (de) |
CN (1) | CN1152856C (de) |
AU (1) | AU6098298A (de) |
BR (1) | BR9807189A (de) |
CA (1) | CA2280887A1 (de) |
DE (2) | DE19704613A1 (de) |
ES (1) | ES2163253T3 (de) |
ID (1) | ID22345A (de) |
MY (1) | MY120020A (de) |
TR (1) | TR199901916T2 (de) |
TW (1) | TW438745B (de) |
WO (1) | WO1998034912A1 (de) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2002044135A1 (de) * | 2000-11-30 | 2002-06-06 | Basf Aktiengesellschaft | Verfahren zur reduzierung des gehalts an einem ungesättigten amin in einer mischung enthaltend ein amin und ein nitril |
WO2003099768A1 (de) * | 2002-05-28 | 2003-12-04 | Basf Aktiengesellschaft | Verfahren zur reduzierung des gehalts an einem ungesättigten amin in einer mischung enthaltend ein aminonitril, ein diamin, ein dinitril oder deren gemische |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6716977B1 (en) | 2003-06-17 | 2004-04-06 | E. I. Du Pont De Nemours And Company | Method for making caprolactam from impure ACN wherein ammonia and water are removed from crude caprolactam in a simple separation step and then THA is removed from the resulting caprolactam melt |
US6858728B2 (en) * | 2003-06-17 | 2005-02-22 | Invista North America S.A.R.L. | Method for making caprolactam from impure ACN in which THA is not removed until after caprolactam is produced |
US7060819B2 (en) * | 2003-09-15 | 2006-06-13 | Invista North America S.A.R.L. | Process for producing hexamethylenediamine and aminocapronitrile from adiponitrile, wherein the hexamethylenediamine contains less than 100 ppm tetrahydroazepine |
US7094528B2 (en) * | 2004-06-30 | 2006-08-22 | Kimberly-Clark Worldwide, Inc. | Magnetic enzyme detection techniques |
US7208632B2 (en) * | 2004-09-10 | 2007-04-24 | Invista North America S.A R.L. | Separation of 6-aminocapronitrile and hexamethylenediamine from a mixture comprising hexamethylenediamine, 6-aminocapronitrile and tetrahydroazepine |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5133838A (en) * | 1991-02-28 | 1992-07-28 | E. I. Du Pont De Nemours And Company | Purification of 6-aminocapronitrile |
US5153351A (en) * | 1992-01-06 | 1992-10-06 | E. I. Du Pont De Nemours And Company | Removal of tetrahydroazepine (tha) from 6-aminocapronitrile by reaction with reactive methylene compounds |
US5162567A (en) * | 1992-02-27 | 1992-11-10 | E. I. Du Pont De Nemours And Company | Purification of 6-aminocapronitrile |
US5192399A (en) * | 1991-01-30 | 1993-03-09 | E. I. Du Pont De Nemours And Company | Purification of aminonitriles or diamines |
Family Cites Families (8)
Publication number | Priority date | Publication date | Assignee | Title |
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US4389348A (en) | 1981-10-26 | 1983-06-21 | Allied Corporation | Selective hydrogenation of dinitrile to omega-aminonitrile and supported rhodium-containing catalyst therefor |
US4489348A (en) * | 1982-09-23 | 1984-12-18 | Gordon W. Hueschen | Video camera synchronizer |
US4601859A (en) | 1984-05-04 | 1986-07-22 | Allied Corporation | Selective hydrogenation of aliphatic dinitriles to omega-aminonitriles in ammonia with supported, finely dispersed rhodium-containing catalyst |
US4604859A (en) * | 1985-05-16 | 1986-08-12 | Sasaki Nouki Kabushiki Kaisha | Agricultural baler |
EP0933083A1 (de) | 1991-07-12 | 1999-08-04 | Dsm N.V. | Verfahren zur Reinigung von Serumalbumin |
DE4235466A1 (de) | 1992-10-21 | 1994-04-28 | Bayer Ag | Verfahren zur Herstellung von (cyclo)aliphatischen Aminonitrilen |
DE19500222A1 (de) | 1995-01-05 | 1996-07-11 | Basf Ag | Verfahren zur gleichzeitigen Herstellung von Caprolactam und Hexamethylendiamin |
DE19548289A1 (de) | 1995-12-22 | 1997-06-26 | Basf Ag | Verfahren zur gleichzeitigen Herstellung von Caprolactam und Hexamethylendiamin |
-
1997
- 1997-02-07 DE DE19704613A patent/DE19704613A1/de not_active Withdrawn
-
1998
- 1998-01-30 ID IDW990845A patent/ID22345A/id unknown
- 1998-01-30 BR BR9807189-0A patent/BR9807189A/pt not_active IP Right Cessation
- 1998-01-30 KR KR10-1999-7007155A patent/KR100492200B1/ko not_active IP Right Cessation
- 1998-01-30 DE DE59801520T patent/DE59801520D1/de not_active Expired - Lifetime
- 1998-01-30 CN CNB988039265A patent/CN1152856C/zh not_active Expired - Fee Related
- 1998-01-30 US US09/367,068 patent/US6169199B1/en not_active Expired - Fee Related
- 1998-01-30 JP JP53372698A patent/JP2001512430A/ja not_active Withdrawn
- 1998-01-30 ES ES98905375T patent/ES2163253T3/es not_active Expired - Lifetime
- 1998-01-30 EP EP98905375A patent/EP0961768B1/de not_active Expired - Lifetime
- 1998-01-30 AU AU60982/98A patent/AU6098298A/en not_active Abandoned
- 1998-01-30 TR TR1999/01916T patent/TR199901916T2/xx unknown
- 1998-01-30 CA CA002280887A patent/CA2280887A1/en not_active Abandoned
- 1998-01-30 WO PCT/EP1998/000505 patent/WO1998034912A1/de active IP Right Grant
- 1998-02-06 MY MYPI98000473A patent/MY120020A/en unknown
- 1998-02-07 TW TW087101633A patent/TW438745B/zh not_active IP Right Cessation
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5192399A (en) * | 1991-01-30 | 1993-03-09 | E. I. Du Pont De Nemours And Company | Purification of aminonitriles or diamines |
US5133838A (en) * | 1991-02-28 | 1992-07-28 | E. I. Du Pont De Nemours And Company | Purification of 6-aminocapronitrile |
US5153351A (en) * | 1992-01-06 | 1992-10-06 | E. I. Du Pont De Nemours And Company | Removal of tetrahydroazepine (tha) from 6-aminocapronitrile by reaction with reactive methylene compounds |
US5162567A (en) * | 1992-02-27 | 1992-11-10 | E. I. Du Pont De Nemours And Company | Purification of 6-aminocapronitrile |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2002044135A1 (de) * | 2000-11-30 | 2002-06-06 | Basf Aktiengesellschaft | Verfahren zur reduzierung des gehalts an einem ungesättigten amin in einer mischung enthaltend ein amin und ein nitril |
KR100823001B1 (ko) * | 2000-11-30 | 2008-04-16 | 바스프 에스이 | 아민 및 니트릴을 함유하는 혼합물 중 불포화 아민의함량을 감소시키는 방법 |
WO2003099768A1 (de) * | 2002-05-28 | 2003-12-04 | Basf Aktiengesellschaft | Verfahren zur reduzierung des gehalts an einem ungesättigten amin in einer mischung enthaltend ein aminonitril, ein diamin, ein dinitril oder deren gemische |
US7385073B2 (en) | 2002-05-28 | 2008-06-10 | Basf Aktiengesellschaft | Method for reducing the content of an unsaturated amine in a mixture containing an amino nitrile, a diamine, a dinitrile or mixtures thereof |
Also Published As
Publication number | Publication date |
---|---|
CN1252052A (zh) | 2000-05-03 |
EP0961768A1 (de) | 1999-12-08 |
ID22345A (id) | 1999-09-30 |
EP0961768B1 (de) | 2001-09-19 |
TW438745B (en) | 2001-06-07 |
ES2163253T3 (es) | 2002-01-16 |
CA2280887A1 (en) | 1998-08-13 |
MY120020A (en) | 2005-08-30 |
DE19704613A1 (de) | 1998-08-13 |
JP2001512430A (ja) | 2001-08-21 |
AU6098298A (en) | 1998-08-26 |
KR100492200B1 (ko) | 2005-06-02 |
US6169199B1 (en) | 2001-01-02 |
DE59801520D1 (de) | 2001-10-25 |
TR199901916T2 (xx) | 1999-12-21 |
CN1152856C (zh) | 2004-06-09 |
BR9807189A (pt) | 2000-01-25 |
KR20000070890A (ko) | 2000-11-25 |
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