GB810916A - Utilization of by-products from manufacture of 2,5-dimethyl-piperazine - Google Patents
Utilization of by-products from manufacture of 2,5-dimethyl-piperazineInfo
- Publication number
- GB810916A GB810916A GB2348756A GB2348756A GB810916A GB 810916 A GB810916 A GB 810916A GB 2348756 A GB2348756 A GB 2348756A GB 2348756 A GB2348756 A GB 2348756A GB 810916 A GB810916 A GB 810916A
- Authority
- GB
- United Kingdom
- Prior art keywords
- dimethyl
- piperazines
- boiling
- isopropanolamine
- heated
- 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.)
- Expired
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D295/00—Heterocyclic compounds containing polymethylene-imine rings with at least five ring members, 3-azabicyclo [3.2.2] nonane, piperazine, morpholine or thiomorpholine rings, having only hydrogen atoms directly attached to the ring carbon atoms
- C07D295/02—Heterocyclic compounds containing polymethylene-imine rings with at least five ring members, 3-azabicyclo [3.2.2] nonane, piperazine, morpholine or thiomorpholine rings, having only hydrogen atoms directly attached to the ring carbon atoms containing only hydrogen and carbon atoms in addition to the ring hetero elements
- C07D295/023—Preparation; Separation; Stabilisation; Use of additives
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
- Catalysts (AREA)
Abstract
In the manufacture of 2.5-dimethyl-piperazines by heating isopropanolamine with an hydrogenation catalyst, the 2.5-dimethyl-piperazines are separated from the higher boiling material which is heated with a hydrogenation catalyst at a temperature in the range 130-300 DEG C. to give at least one of the compounds 2.5-dimethyl-pyrazine and 2.5-dimethyl-piperazines. The relative yields of 2.5-dimethylpyrazine and 2.5-dimethyl-piperazines is dependent partly on the hydrogenation catalyst used. For example, copper chromite, copper powder and the less active nickel catalysts favour the formation of 2.5-dimethyl-pyrazine whereas the more active nickel catalysts, e.g. Raney nickel and the finely-divided nickel formed by the reduction of precipitated nickel hydroxide, favour the formation of cis- and trans-2.5-dimethyl-piperazines. If some of the by-product material is mixed with isopropanolamine and heated with an hydrogenation catalyst to a temperature in the range 130-300 DEG C. less of the by-product material is formed than when the isopropanolamine is used alone. The high-boiling by-product material may be heated at atmospheric or superatmospheric pressure and preferably 5 to 15 per cent of catalyst is used based on the combined weight of the catalyst and by-product material. The process may be carried out continuously by recycling the higher boiling by-products but advantageously from one quarter to half of the high boiling by-product is withdrawn from the system and may be treated separately. In the examples: (a) a high-boiling fraction of the residue obtained after separating 2.5-dimethyl-piperazines from a mixture obtained by heating isopropanolamine with a hydrogenation catalyst is heated at 200 DEG C. under pressure with Raney nickel to give 2.5-dimethyl-pyrazine and 2.5-dimethyl-piperazines; (b) a mixture of isopropanolamine, a high-boiling residue from a previous reaction and Raney nickel is heated to 200 DEG C. to give 2.5-dimethyl-piperazines with very little high-boiling residue; (c) a higher-boiling fraction from a previous reaction, isopropanolamine and reduced nickel hydroxide are heated to 200 DEG C. to give 2.5-dimethyl-pyrazine, and 2.5-dimethyl-piperazines with a very little high-boiling residue; (d) isopropanolamine, a high-boiling residue from a previous reaction, and copper powder are heated to 200 DEG C. to give 2.5-dimethyl-pyrazine and 2.5-dimethyl-piperazines with very little higher boiling residue; (e) isopropanolamine, a high-boiling residue from a previous reaction and a supported nickel catalyst are heated to 200 DEG C. to give 2.5-dimethyl-pyrazine, 2.5-dimethyl-piperazines and a small amount of high-boiling residue; (f) isopropanolamine, a high-boiling residue from a previous reaction and Raney nicel are heated to 200 DEG C. to give mainly 2.5-dimethylpiperazines; and (g) the process of (f) is carried out continuously at 195-205 DEG C. to give mainly 2.5-dimethylpiperazines.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB2348756A GB810916A (en) | 1955-01-11 | 1957-07-24 | Utilization of by-products from manufacture of 2,5-dimethyl-piperazine |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US481264A US2810722A (en) | 1955-01-11 | 1955-01-11 | Utilization of by-products from manufacture of 2, 5-dimethylpiperazine |
GB2348756A GB810916A (en) | 1955-01-11 | 1957-07-24 | Utilization of by-products from manufacture of 2,5-dimethyl-piperazine |
Publications (1)
Publication Number | Publication Date |
---|---|
GB810916A true GB810916A (en) | 1959-03-25 |
Family
ID=26256547
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB2348756A Expired GB810916A (en) | 1955-01-11 | 1957-07-24 | Utilization of by-products from manufacture of 2,5-dimethyl-piperazine |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB810916A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112920056A (en) * | 2021-01-29 | 2021-06-08 | 山东达民化工股份有限公司 | Method for producing isopropanolamine and 1, 2-propane diamine by cracking 2, 5-dimethylpiperazine |
-
1957
- 1957-07-24 GB GB2348756A patent/GB810916A/en not_active Expired
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112920056A (en) * | 2021-01-29 | 2021-06-08 | 山东达民化工股份有限公司 | Method for producing isopropanolamine and 1, 2-propane diamine by cracking 2, 5-dimethylpiperazine |
CN112920056B (en) * | 2021-01-29 | 2022-12-23 | 山东达民化工股份有限公司 | Method for producing isopropanolamine and 1, 2-propanediamine by cracking 2, 5-dimethylpiperazine |
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