CN101486748A - Preparation of 5,7-diene cholesterol - Google Patents

Preparation of 5,7-diene cholesterol Download PDF

Info

Publication number
CN101486748A
CN101486748A CNA2008100592992A CN200810059299A CN101486748A CN 101486748 A CN101486748 A CN 101486748A CN A2008100592992 A CNA2008100592992 A CN A2008100592992A CN 200810059299 A CN200810059299 A CN 200810059299A CN 101486748 A CN101486748 A CN 101486748A
Authority
CN
China
Prior art keywords
diene
cholesteryl ester
preparation
bromo
reaction
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
Application number
CNA2008100592992A
Other languages
Chinese (zh)
Other versions
CN101486748B (en
Inventor
姚祥华
王昌泽
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Zhejiang NHU Co Ltd
Original Assignee
Zhejiang NHU Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Zhejiang NHU Co Ltd filed Critical Zhejiang NHU Co Ltd
Priority to CN2008100592992A priority Critical patent/CN101486748B/en
Publication of CN101486748A publication Critical patent/CN101486748A/en
Application granted granted Critical
Publication of CN101486748B publication Critical patent/CN101486748B/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Steroid Compounds (AREA)

Abstract

The invention discloses a preparation method of 5, 7-diene cholesteryl ester which serves as important intermediate in production of vitamin D3. The preparation method adopts a special effective catalyzer which is the combination of a superfine sodium carbonate and a triethyl orthoformate. Compared with the prior art, the preparation method obviously has the advantages of less side effect, higher reaction and recovery rate, lower cost and less environmental pollution.

Description

A kind of preparation method of 5,7-diene cholesteryl ester
Technical field
The present invention relates to the preparation method of important intermediate 5,7-diene cholesteryl ester of Vitamin D3 500,000 I.U/GM.
Background technology
5,7-diene cholesteryl ester is for generating the important intermediate of pre-D3 (7-dehydrocholesterol), and reaction formula is as follows:
Figure A200810059299D00031
5,7-diene 4,6-diene
The employed catalyzer of this reaction traditional method is benzenethiol, peroxy acid, triethylamine, liquefied ammonia, alkaline metal fluoride cpd, pyridines etc.Wherein reported in literature is the most effective is liquefied ammonia.Adopt above-mentioned catalyzer, target product 5,7-diene cholesteryl ester selectivity is bad, and yield is about 58-62%, and a spot of water is unfavorable for that reaction carries out fully in the reaction system, and especially triethylamine, liquefied ammonia are very big to environmental influence.
At the existing problem of above-mentioned catalyzer, we have sought a kind of effective catalyzer: ultra-fine yellow soda ash and triethyl orthoformate combination catalyst.
Summary of the invention
Technical problem to be solved by this invention is to overcome the defective that above-mentioned prior art exists, provide that a kind of raw material is easy to get, the gentle easily control of reaction conditions 5, the preparation method of 7-diene cholesteryl ester, select special effective catalyzer for use: ultra-fine yellow soda ash and triethyl orthoformate combination catalyst, what play debromination is yellow soda ash, through be ground into ultra-fine after, increase its specific surface area, can improve speed of response, increase reaction yield.Catalyzer of the present invention is the catalyzer that a kind of selectivity is good, security is good, and the reaction conditions gentleness is not subject to poisoning of impurity, and environmentally friendly.
For this reason, the present invention adopts following technical scheme: a kind of 5, the preparation method of 7-diene cholesteryl ester, in the presence of organic solvent, with catalyst 7-bromo cholesteryl ester, the crystallization of reaction postcooling, 5,7-diene cholesteryl ester.
As the further of technique scheme improved and replenish, the present invention takes following technical measures:
The preparation method of above-mentioned 5,7-diene cholesteryl ester, catalyzer is the combination catalyst of ultra-fine yellow soda ash and triethyl orthoformate, and the particle diameter of the ultra-fine yellow soda ash of catalyzer is the 50-200 order, and this catalyzer has improved speed of response greatly, has increased reaction yield.
The preparation method of above-mentioned 5,7-diene cholesteryl ester is characterized in that the mol ratio of 7-bromo cholesteryl ester and catalyzer (calculating with triethyl orthoformate) is 1:0.3-2.0, preferred 1:0.5-0.7.
Above-mentioned 5, the preparation method of 7-diene cholesteryl ester, reaction raw materials 7-bromo cholesteryl ester is 7-bromo cholesterol benzoate and 7-bromo cholesterol acetate, it is aromatic hydrocarbons and acid amides that reaction solvent is selected organic solvent for use, particularly dimethylbenzene, a trimethylbenzene and DMF temperature of reaction are 80 ℃-150 ℃, preferred 100-130 ℃.
This reaction produces a spot of water and is steamed after the triethyl orthoformate reaction, thereby has guaranteed to remain in the reaction system anhydrous, has avoided the influence of water to reaction yield, has also promoted molecular balance to move to target product.Use its target product 5,7-diene cholesteryl ester yield of aforesaid combination catalyzer to be about 75-78%.
The present invention has following beneficial effect: the reaction conditions gentleness of this method, and side reaction is few, and flow process is short, and technological operation is simple; Environmental pollution is few, has avoided the pollution to water of pollution that triethylamine, liquefied ammonia cause air and metal fluoride.The reaction yield height, production cost is low, is fit to scale operation.
The invention will be further described below in conjunction with embodiment.
Embodiment
Embodiment 1
Get 7-bromo cholesterol benzoate, 30.0 grams (content 85%, 0.0447mol) after the 500mL four-hole bottle adds vacuum-drying, dimethylbenzene 200ML, ultra-fine yellow soda ash 3.0 grams, triethyl orthoformate 4mL (0.0243mol), be warming up to 125 ℃ of timing insulations 2 hours, be warming up to 130 ℃ again and continued insulation reaction 2 hours, collection unit is divided fraction, and the raw material peak is considered as reacting completely less than 2.0% after testing.Reaction is finished and to be cooled to room temperature and to filter, and decompression and solvent recovery is to doing, 26.4 grams of weighing (content about 65%, yield 78.7%).Get 5 through acetone recrystallization, get Precalciferol3 (7-dehydrocholesterol) after 7-diene cholesterol benzoate (content the reaches 85%) saponification reaction.
Embodiment 2
Get 7-bromo cholesterol acetate, 30.0 grams (content 85%, 0.0502mol) after the 500mL four-hole bottle adds vacuum-drying, dimethylbenzene 200ML, ultra-fine yellow soda ash 3.0 grams, triethyl orthoformate 5mL (0.0304mol), be warming up to 115 ℃ of timing insulations 4 hours, collection unit is divided fraction, and the raw material peak is considered as reacting completely less than 1.0% after testing.Reaction is finished and to be cooled to room temperature and to filter, and decompression and solvent recovery is to doing, 25.0 grams of weighing (content about 65%, yield 76.0%).
Embodiment 3
The particle diameter of combination catalyst yellow soda ash is to the influence of product yield
The particle diameter of yellow soda ash Yellow soda ash (industrial goods) Ultra-fine yellow soda ash (100 order)
Product yield % 70 78.5
Embodiment 4
Be that raw material is adjusted the influence of the amount of different catalysts (triethyl orthoformate) to yield with 7-bromo cholesterol benzoate below:
Raw material and catalyst molar ratio Assembly catalyze molar product yield % Single catalyst article molar yield %
1.0:0.54 78.7 65
1.0:0.61 76.0 64
1.0:0.30 66.8 56
1.0:1.0 69.1 57
1.0:2.0 65.2 55

Claims (10)

1, a kind of preparation method of 5,7-diene cholesteryl ester is in the presence of organic solvent, with catalyst 7-bromo cholesteryl ester, the crystallization of reaction postcooling gets 5,7-diene cholesteryl ester, it is characterized in that the catalyzer that reacts used is yellow soda ash and triethyl orthoformate combination catalyst.
2, the preparation method of 5,7-diene cholesteryl ester according to claim 1 is characterized in that catalyzer is the combination catalyst of ultra-fine yellow soda ash and triethyl orthoformate.
3, the preparation method of 5,7-diene cholesteryl ester according to claim 2, the particle diameter that it is characterized in that the ultra-fine yellow soda ash of combination catalyst is the 50-200 order.
4, the preparation method of 5,7-diene cholesteryl ester according to claim 1 is characterized in that the mol ratio of 7-bromo cholesteryl ester and catalyzer (calculating with triethyl orthoformate) is 1:0.3-2.0.
5, the preparation method of 5,7-diene cholesteryl ester according to claim 4 is characterized in that the mol ratio of 7-bromo cholesteryl ester and catalyzer (calculating with triethyl orthoformate) is 1:0.5-0.7.
6, the preparation method of 5,7-diene cholesteryl ester according to claim 1 is characterized in that described organic solvent is aromatic hydrocarbons and acid amides.
7, the preparation method of 5,7-diene cholesteryl ester according to claim 6 is characterized in that described organic solvent is dimethylbenzene, a trimethylbenzene and DMF.
8, the preparation method of 5,7-diene cholesteryl ester according to claim 1 is characterized in that temperature of reaction is 80 ℃-150 ℃.
9, the preparation method of 5,7-diene cholesteryl ester according to claim 8 is characterized in that temperature of reaction is 100 ℃-130 ℃.
10, the preparation method of 5,7-diene cholesteryl ester according to claim 1 is characterized in that described raw material 7-bromo cholesteryl ester is 7-bromo cholesterol benzoate and 7-bromo cholesterol acetate.
CN2008100592992A 2008-01-15 2008-01-15 Preparation method of preparation of 5,7-diene cholesterol Expired - Fee Related CN101486748B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2008100592992A CN101486748B (en) 2008-01-15 2008-01-15 Preparation method of preparation of 5,7-diene cholesterol

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2008100592992A CN101486748B (en) 2008-01-15 2008-01-15 Preparation method of preparation of 5,7-diene cholesterol

Publications (2)

Publication Number Publication Date
CN101486748A true CN101486748A (en) 2009-07-22
CN101486748B CN101486748B (en) 2011-11-02

Family

ID=40889824

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2008100592992A Expired - Fee Related CN101486748B (en) 2008-01-15 2008-01-15 Preparation method of preparation of 5,7-diene cholesterol

Country Status (1)

Country Link
CN (1) CN101486748B (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102002518A (en) * 2010-10-28 2011-04-06 浙江大学 Method for preparing 7beta-hydroxyl-3beta cholesterol acetate from hydroxylase 3beta-cholesterol acetate
KR20160108599A (en) * 2011-07-28 2016-09-19 산산 왕 Composite collagen sponge and preparation method thereof

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
SU910654A1 (en) * 1980-07-31 1982-03-07 Ордена Трудового Красного Знамени Институт Биохимии Им.А.В.Палладина Ан Усср Process for producing 7-dehydrocholesterol benzoate
EP0084199B1 (en) * 1982-01-14 1987-04-29 Duphar International Research B.V Method of preparing delta 5,7-steroids

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102002518A (en) * 2010-10-28 2011-04-06 浙江大学 Method for preparing 7beta-hydroxyl-3beta cholesterol acetate from hydroxylase 3beta-cholesterol acetate
CN102002518B (en) * 2010-10-28 2015-05-13 浙江大学 Method for preparing 7beta-hydroxyl-3beta cholesterol acetate from hydroxylase 3beta-cholesterol acetate
KR20160108599A (en) * 2011-07-28 2016-09-19 산산 왕 Composite collagen sponge and preparation method thereof
KR101717266B1 (en) 2011-07-28 2017-03-16 산산 왕 Composite collagen sponge and preparation method thereof

Also Published As

Publication number Publication date
CN101486748B (en) 2011-11-02

Similar Documents

Publication Publication Date Title
JP2014528927A5 (en)
CN101612580A (en) A kind of catalyst for synthesis of diethyl oxalate employing carbon monoxide gas-phase catalytic coupling and preparation method thereof
CN103524306B (en) A kind of gas-phase catalytic hydrogenation prepares the method for difluoroethanol
WO2013155291A4 (en) Process for production of acrylic acid or its derivatives
CN107445830A (en) The method that ethyl glycolate oxidative dehydrogenation produces glyoxylic ester
CN101486748B (en) Preparation method of preparation of 5,7-diene cholesterol
CN107285979B (en) Method for preparing styrene by oxidative dehydrogenation of ethylbenzene
CN105503941A (en) Catalytic synthesis method of tri-iso-octyl phosphate
CN102942476A (en) Preparation method of linalyl acetate
CN111848448B (en) Preparation method of citronellonitrile
AU2014311940B2 (en) Process for the production of methacrylic acid
WO2010129029A3 (en) Vinyl ester production from acetylene and carboxylic acid utilizing heterogeneous catalyst
CN103450306B (en) A kind of synthetic method of pregnenolone acetic ester
CN103387495B (en) Method for the continuous production of carboxylic acid esters
CN107486191B (en) Iridium-based catalyst loaded on acid-treated carbon carrier and preparation method and application thereof
CN104557454A (en) Method for preparing high-quality ethanol through hydrogenating acetic acid
CN102295563A (en) Preparation method of trinexapac-ethyl
CN107445839B (en) Method for synthesizing glyoxylic ester
CN104610134A (en) Preparation method of 6-methyl-2-pyridyl methanol
CN103920502B (en) The Catalysts and its preparation method of ethyl acetate gas phase hydrogenation ethanol and application under a kind of temperate condition
CN103130633A (en) Method for producing p-methylacetophenone with fixed-bed reactor
CN111747837A (en) Synthesis method of trans-4-oxo-2-hexenal
CN103204835B (en) A kind of preparation method of butyrolactone
CN114315709B (en) Synthesis method of 4-trifluoromethyl nicotinic acid
CN103360214B (en) Method for synthesizing 3-butenyl-1-ol from 1,4-butanediol monocarboxylate

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20111102

Termination date: 20150115

EXPY Termination of patent right or utility model