CN1876636A - Cyclopentane1,2-diimide preparation method - Google Patents
Cyclopentane1,2-diimide preparation method Download PDFInfo
- Publication number
- CN1876636A CN1876636A CN 200510049977 CN200510049977A CN1876636A CN 1876636 A CN1876636 A CN 1876636A CN 200510049977 CN200510049977 CN 200510049977 CN 200510049977 A CN200510049977 A CN 200510049977A CN 1876636 A CN1876636 A CN 1876636A
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- Prior art keywords
- pentamethylene
- imide
- preparation
- acid
- organic solvent
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- 238000002360 preparation method Methods 0.000 title claims description 16
- 229910000071 diazene Inorganic materials 0.000 title abstract 3
- 239000003960 organic solvent Substances 0.000 claims abstract description 18
- 239000002253 acid Substances 0.000 claims abstract description 13
- 150000003839 salts Chemical class 0.000 claims abstract description 3
- RGSFGYAAUTVSQA-UHFFFAOYSA-N pentamethylene Natural products C1CCCC1 RGSFGYAAUTVSQA-UHFFFAOYSA-N 0.000 claims description 43
- 125000004817 pentamethylene group Chemical group [H]C([H])([*:2])C([H])([H])C([H])([H])C([H])([H])C([H])([H])[*:1] 0.000 claims description 42
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 claims description 26
- -1 amine salt Chemical class 0.000 claims description 22
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 18
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 claims description 18
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 claims description 18
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims description 16
- 238000007363 ring formation reaction Methods 0.000 claims description 14
- 229910000147 aluminium phosphate Inorganic materials 0.000 claims description 13
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims description 10
- IXCSERBJSXMMFS-UHFFFAOYSA-N hydrogen chloride Substances Cl.Cl IXCSERBJSXMMFS-UHFFFAOYSA-N 0.000 claims description 6
- 229910000041 hydrogen chloride Inorganic materials 0.000 claims description 6
- 239000007789 gas Substances 0.000 claims description 5
- 238000009413 insulation Methods 0.000 claims description 5
- 239000000463 material Substances 0.000 claims description 5
- 238000007670 refining Methods 0.000 claims description 4
- 238000001816 cooling Methods 0.000 claims description 3
- 239000012266 salt solution Substances 0.000 claims description 3
- 238000000034 method Methods 0.000 abstract description 17
- 239000002994 raw material Substances 0.000 abstract description 6
- 238000005516 engineering process Methods 0.000 abstract description 2
- 238000003786 synthesis reaction Methods 0.000 abstract description 2
- AYVGBNGTBQLJBG-UHFFFAOYSA-N [3-(hydroxymethyl)cyclopentyl]methanol Chemical compound OCC1CCC(CO)C1 AYVGBNGTBQLJBG-UHFFFAOYSA-N 0.000 abstract 3
- 238000011084 recovery Methods 0.000 description 7
- 238000006243 chemical reaction Methods 0.000 description 6
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 150000008065 acid anhydrides Chemical class 0.000 description 3
- WFDIJRYMOXRFFG-UHFFFAOYSA-N Acetic anhydride Chemical compound CC(=O)OC(C)=O WFDIJRYMOXRFFG-UHFFFAOYSA-N 0.000 description 2
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- 238000004821 distillation Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 230000001476 alcoholic effect Effects 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- LFVGISIMTYGQHF-UHFFFAOYSA-N ammonium dihydrogen phosphate Chemical compound [NH4+].OP(O)([O-])=O LFVGISIMTYGQHF-UHFFFAOYSA-N 0.000 description 1
- 238000003763 carbonization Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 239000003317 industrial substance Substances 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
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- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
The invention relates the organic synthesis method, especially the preparing method of cyclopentane 1, 2- diimide. The method comprises the following steps: dissolving the cyclopentane 1, 2-diformamide in organic solvent, then it reacting with acid salt, and getting the cyclopentane 1, 2- diimide. The invention has the characters of modifying the technology and improving the productivity. The invention has the advantages of reducing the preparing time, raw material, cost and pollution.
Description
Technical field
The present invention relates to a kind of methodology of organic synthesis, relate in particular to a kind of pentamethylene 1, the preparation method of 2-imide.
Background technology
Existing synthetic pentamethylene 1,2-imide method is with pentamethylene 1, the 2-diformamide is a raw material, through sodium hydroxide hydrolysis, refining pentamethylene 1,2-dioctyl phthalate, this step reaction yield is 78%, pentamethylene 1, and the 2-dioctyl phthalate is after diacetyl oxide, acid anhydridesization, underpressure distillation is purified again, the acid anhydrides thing is under toluene is made solvent, and logical ammonia is re-refined, and two step yields are 73.92%, if with raw material pentamethylene 1, it only is 57.66% that the 2-diformamide comes calculated yield.
The main drawback of this method is that when acid changed acid anhydrides into, raw materials used was diacetyl oxide, and the acid anhydrides thing has carbonization phenomenon under hot conditions when underpressure distillation is purified, and total recovery is low, raw materials cost is high.
Summary of the invention
In order to solve above-mentioned technical problem, the invention provides a kind of total recovery height, pentamethylene 1 that raw materials cost is low, the preparation method of 2-imide.
To achieve the above object, the present invention has adopted following technical scheme:
A kind of pentamethylene 1, the preparation method of 2-imide comprises the steps:
A) with pentamethylene 1, the 2-diformamide is put in the organic solvent, is heated to 40～55 ℃ of dissolvings, adds acid then, makes to separate out behind the material salify to obtain amine salt;
B) above-mentioned amine salt being heated to temperature is 220～260 ℃ of dissolving cyclizations, standing demix then, and the upper strata is pentamethylene 1, and the 2-imide obtains pentamethylene 1, the 2-imide again after organic solvent is refining.
As preferably, a) organic solvent described in the step is preferably a kind of in methyl alcohol, ethanol, the toluene.Organic solvent most preferably be ethanol.
As preferably, a) acid described in the step is preferably a kind of in sulfuric acid, hydrochloric acid, hydrogen chloride gas and the phosphoric acid.The concentration that most preferably is of acid is 85% phosphoric acid.
As preferably, b) temperature of dissolving cyclization is 240～245 ℃ in the step.
As preferably, after a) material becomes to salt out in the step, be incubated 20～35 minutes down at 40～55 ℃, cooling is cooled to about 5～15 ℃ with icy salt solution again, is incubated 20～35 minutes, and insulation finishes, centrifuge dripping, oven dry obtains amine salt again.
The present invention prepares pentamethylene 1, the method for 2-imide, with pentamethylene 1, the 2-diformamide in organic solvent with sour salify, cyclization makes pentamethylene 1 again, the 2-imide.Characteristics of the present invention are to have improved technological process, have improved the yield of target compound.With three-step reaction in the former method, change the reaction of two steps into simultaneously, reduce the time of preparation and the kind and the consumption of industrial chemicals, reduced production cost, also reduced the pollution of whole process of production simultaneously environment.
Embodiment
Below in conjunction with specific embodiment the present invention is made a detailed explanation.
Embodiment 1
Salify in the 1000ml reaction flask, drops into the ethanol of 500g95%, 100g pentamethylene 1, the 2-diformamide is heated to 40～55 ℃ of dissolvings, dissolving drips 147g phosphoric acid fully, separates out after making the material salify, drips and finishes, in the cold water cooling after 30 minutes of insulation under 40～55 ℃ the condition, temperature is about 10 ℃ in being cooled to icy salt solution again, is incubated 30 minutes, insulation finishes, and centrifuge dripping advances the drying room oven dry, oven dry obtains about amine salt 225g, and the alcoholic acid consumption is 68g.
Cyclization in the 500ml reaction flask, drops into the above-mentioned amine salt that obtains of 200g, and, dissolving cyclization with the heating of oil temperature, 2 hours ring-closure reactions of 220～250 ℃ of insulation reaction of temperature finish in being heated to, put into and leave standstill pot, leave standstill branch lower floor phosphoric acid ammonia salt, the upper strata is pentamethylene 1, the 2-imide, get pentamethylene 1 then after toluene is refining, 2-imide 65g, yield are 82.15%, the fusing point of product is 85-87 ℃, and content is 〉=99%.
The chemical equation of above-mentioned process is as follows:
Embodiment 2
Get 100g pentamethylene 1,2-diformamide and 128g98% sulfuric acid adopt and make amine salt 225g as embodiment 1 described method, and amine salt is a yield 100%.With the cyclization under 260 ℃ of conditions of gained amine salt, obtain pentamethylene 1 again, 2-imide 66.82g, total recovery is 74.99%.
Embodiment 3
Get 100g pentamethylene 1,2-diformamide and 131g36% hydrochloric acid adopt and make amine salt 136g as embodiment 1 described method, and amine salt is a yield 92.5%.With the cyclization under 225 ℃ of conditions of gained amine salt, obtain pentamethylene 1 again, 2-imide 56.8g, total recovery is 63.75%.
Embodiment 4
Get 100g pentamethylene 1,2-diformamide and 47g hydrogen chloride gas feed pentamethylene 1 with hydrogen chloride gas, make amine salt 142g in the 2-diformamide ethanolic soln, and amine salt is a yield 96.6%.With the cyclization under 225 ℃ of conditions of gained amine salt, obtain pentamethylene 1 again, 2-imide 65.2g, total recovery is 73.18%.
Embodiment 5
Get 100g pentamethylene 1,2-diformamide and 147g phosphoric acid use the methyl alcohol of 500g to do organic solvent, adopt the preparation amine salt method as embodiment, and making amine salt is 224g, and yield is 99.6%, and the consumption of methyl alcohol is 100g.
Cyclization prepares pentamethylene 1, the method for 2-imide, as implement as described in 1.
Embodiment 6
Get 100g pentamethylene 1,2-diformamide and 147g phosphoric acid use the toluene of 500g to do organic solvent, adopt the preparation amine salt method as embodiment, and making amine salt is 222g, and yield is 98.7%, and the consumption of methyl alcohol is 95g.
Cyclization prepares pentamethylene 1, the method for 2-imide, as implement as described in 1.
Table 1 is a pentamethylene 1, and 2-diformamide throwing amount is 100 (g), uses sulfuric acid, hydrochloric acid, hydrogenchloride, 85% phosphoric acid salify synopsis in ethanol.
| Embodiment | Acid | Acid throwing amount (g) | Salify thing amount (g) | Yield (%) | The cyclization temperature (℃) | The output of product (g) | Total recovery (%) |
| Embodiment 1 | 98% sulfuric acid | 128 | 225 | 100 | 260 | 66.82 | 74.99 |
| Embodiment 2 | 36% hydrochloric acid | 131 | 136 | 92.52 | 225 | 56.8 | 63.75 |
| Embodiment 3 | Hydrogen chloride gas | 47 | 142 | 96.6 | 225 | 65.2 | 73.18 |
| Embodiment 4 | 85% phosphoric acid | 147 | 225 | 100 | 240 | 73.2 | 82.15 |
Table 1
From top form as can be seen, pentamethylene 1,2-diformamide throwing amount is 100 (g), during with 85% phosphoric acid salify, total recovery is the highest in ethanol.
Table 2 is a pentamethylene 1, and 2-diformamide throwing amount is 100 (g), and 85% phosphoric acid salify is adopted in acid, and organic solvent contrasts salifiable influence.
| Embodiment | Organic solvent | Organic solvent throwing amount (g) | 85% phosphoric acid throwing amount (g) | Salify thing amount (g) | Salify yield (%) | Organic solvent consumes (g) |
| Embodiment 1 | Methyl alcohol | 500 | 147 | 224 | 99.6 | 100 |
| Embodiment 5 | Ethanol | 500 | 147 | 225 | 100 | 68 |
| Embodiment 6 | Toluene | 500 | 147 | 222 | 98.7 | 95 |
Table 2
From top form as can be seen, pentamethylene 1,2-diformamide throwing amount is 100 (g), adopts 85% phosphoric acid when organic solvent is selected ethanol for use, the consumption of organic solvent.
Claims (7)
1. pentamethylene 1, the preparation method of 2-imide is characterized in that this preparation method comprises the steps:
A) with pentamethylene 1, the 2-diformamide is put in the organic solvent, is heated to 40～55 ℃ of dissolvings, adds acid then, makes to separate out behind the material salify to obtain amine salt;
B) above-mentioned amine salt being heated to temperature is 220～260 ℃ of dissolving cyclizations, standing demix then, and the upper strata is pentamethylene 1, and the 2-imide obtains pentamethylene 1, the 2-imide again after organic solvent is refining.
2. a kind of pentamethylene 1 as claimed in claim 1, the preparation method of 2-imide is characterized in that a) organic solvent described in the step is preferably a kind of in methyl alcohol, ethanol, the toluene.
3. a kind of pentamethylene 1 as claimed in claim 2, the preparation method of 2-imide is characterized in that a) organic solvent described in the step most preferably is ethanol.
4. as claim 1 or 2 or 3 described a kind of pentamethylene 1, the preparation method of 2-imide is characterized in that a) acid described in the step is preferably a kind of in sulfuric acid, hydrochloric acid, hydrogen chloride gas and the phosphoric acid.
5. a kind of pentamethylene 1 as claimed in claim 4, the preparation method of 2-imide is characterized in that it is 85% phosphoric acid that a) acid described in the step most preferably is concentration.
6. a kind of pentamethylene 1 as claimed in claim 1, the preparation method of 2-imide is characterized in that b) temperature of dissolving cyclization is 240～250 ℃ in the step.
7. a kind of pentamethylene 1 as claimed in claim 1, the preparation method of 2-imide, after it is characterized in that a) material becomes to salt out in the step, be incubated 20～35 minutes down at 40～55 ℃, cooling is cooled to about 5～15 ℃ with icy salt solution again, be incubated 20～35 minutes, insulation finishes, centrifuge dripping, and oven dry obtains amine salt again.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2005100499773A CN100424077C (en) | 2005-06-07 | 2005-06-07 | Cyclopentane1,2-diimide preparation method |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2005100499773A CN100424077C (en) | 2005-06-07 | 2005-06-07 | Cyclopentane1,2-diimide preparation method |
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| Publication Number | Publication Date |
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| CN1876636A true CN1876636A (en) | 2006-12-13 |
| CN100424077C CN100424077C (en) | 2008-10-08 |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2012254982A (en) * | 2011-06-08 | 2012-12-27 | Lab Servier | Synthesis process, and crystalline form of 4-{3-[cis-hexahydrocyclopenta[c]pyrrol-2(1h)-yl]propoxy}benzamide hydrochloride and pharmaceutical composition containing the same |
| CN104387313A (en) * | 2014-10-22 | 2015-03-04 | 滨海博大化工有限公司 | Preparation method of 1,2-cyclopentadicarboximide |
| CN106866495A (en) * | 2017-03-30 | 2017-06-20 | 济南爱思医药科技有限公司 | One kind synthesis imido method of ring penta |
| CN108569994A (en) * | 2018-06-01 | 2018-09-25 | 滨海博大化工有限公司 | The synthetic method of 1,2- of one kind rings, penta dicarboximide |
| CN112851563A (en) * | 2020-12-30 | 2021-05-28 | 安徽金鼎医药股份有限公司 | Synthesis process of N-amino-3-azabicyclo [3,3,0] octane hydrochloride |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| SU657022A1 (en) * | 1977-05-05 | 1979-04-15 | Харьковский научно-исследовательский институт эндокринологии и химии гормонов | Method of obtaining imide of cyclopentane-1,2-dicarboxylic acid |
| CN1314340A (en) * | 2000-03-21 | 2001-09-26 | 山东省医药工业研究所 | Method for preparing cyclopentane imide |
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2005
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2012254982A (en) * | 2011-06-08 | 2012-12-27 | Lab Servier | Synthesis process, and crystalline form of 4-{3-[cis-hexahydrocyclopenta[c]pyrrol-2(1h)-yl]propoxy}benzamide hydrochloride and pharmaceutical composition containing the same |
| CN104387313A (en) * | 2014-10-22 | 2015-03-04 | 滨海博大化工有限公司 | Preparation method of 1,2-cyclopentadicarboximide |
| CN106866495A (en) * | 2017-03-30 | 2017-06-20 | 济南爱思医药科技有限公司 | One kind synthesis imido method of ring penta |
| CN106866495B (en) * | 2017-03-30 | 2019-11-19 | 济南爱思医药科技有限公司 | A kind of imido method of synthesis ring penta |
| CN108569994A (en) * | 2018-06-01 | 2018-09-25 | 滨海博大化工有限公司 | The synthetic method of 1,2- of one kind rings, penta dicarboximide |
| CN112851563A (en) * | 2020-12-30 | 2021-05-28 | 安徽金鼎医药股份有限公司 | Synthesis process of N-amino-3-azabicyclo [3,3,0] octane hydrochloride |
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| Publication number | Publication date |
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| CN100424077C (en) | 2008-10-08 |
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