CN106883142B - A kind of method for being catalyzed hydrogen cyanide and the hydroxypropionitrile of ethylene oxide synthesis 3 - Google Patents

A kind of method for being catalyzed hydrogen cyanide and the hydroxypropionitrile of ethylene oxide synthesis 3 Download PDF

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CN106883142B
CN106883142B CN201510945447.0A CN201510945447A CN106883142B CN 106883142 B CN106883142 B CN 106883142B CN 201510945447 A CN201510945447 A CN 201510945447A CN 106883142 B CN106883142 B CN 106883142B
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reaction
hydrogen cyanide
hydroxypropionitriles
oxirane
ethylene oxide
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CN106883142A (en
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张磊
滕启亮
吴磊
胡学
胡学一
方云
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FUSHUN SHUNTE CHEMICAL Co.,Ltd.
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Jiangnan University
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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C253/00Preparation of carboxylic acid nitriles
    • C07C253/16Preparation of carboxylic acid nitriles by reaction of cyanides with lactones or compounds containing hydroxy groups or etherified or esterified hydroxy groups
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J31/00Catalysts comprising hydrides, coordination complexes or organic compounds
    • B01J31/02Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides
    • B01J31/0201Oxygen-containing compounds
    • B01J31/0202Alcohols or phenols
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J31/00Catalysts comprising hydrides, coordination complexes or organic compounds
    • B01J31/26Catalysts comprising hydrides, coordination complexes or organic compounds containing in addition, inorganic metal compounds not provided for in groups B01J31/02 - B01J31/24
    • B01J35/19

Abstract

Using the immobilized boron trifluoride of activated alumina and 1, the complex compound of 2 pentanediols, by Catalytic Cyanation hydrogen 3 hydroxypropionitriles are synthesized with reacting ethylene oxide.Using this method, remove neutralization reaction mixture without a large amount of acid in course of reaction, also do not produce a large amount of inorganic salts, be the reaction that Atom economy is 100%;Reaction scheme is short, operating procedure is few, product separation is easy, is to react easily to operate;Under the conditions of low-temp reaction, hydrogen cyanide is the reaction of safe operation without the risk largely overflowed in system.

Description

A kind of method for being catalyzed hydrogen cyanide and ethylene oxide synthesis 3- hydroxypropionitriles
Technical field
A kind of method for being catalyzed hydrogen cyanide and ethylene oxide synthesis 3- hydroxypropionitriles, belong to organic synthesis field and organic urge Change field.
Background technology
Endoxan is a kind of alkylating agent, is mainly used in tumour immunity, there is obvious inhibitory action to kinds of tumors.To not Homologous ray necrotizing angitis disease, dermatomyositis and polymyositis, chorionitis, have very strong indication, even after clinical remission Also medication is preferably maintained for a long time.It is clinically used for malignant lymphoma, Huppert's disease, leukaemia, breast cancer, oophoroma, uterine neck Cancer, prostate cancer, colon cancer, bronchiolar carcinoma, lung cancer etc., there is certain curative effect.It is comprehensive to can also be used for rheumatoid arthritis, Childhood Nephrotic Syndrome The treatment of simulator sickness and autoimmune disease.An important route for synthesizing endoxan is POCl3 and two (2- chloroethyls) 3- aminopropanols are added dropwise at low temperature in the mixture of amine reaction, and the most green approach for synthesizing 3- aminopropanols surely belongs to 3- hydroxyls Base propionitrile reduces.
The method of synthesis 3- hydroxypropionitriles mainly has acrylonitrile hydration, chlorethanol or bromoethanol and hydrogen cyanide reaction, epoxy Ethane and hydrogen cyanide reaction and fermentation method etc..
WO200387041 disclose acrylonitrile and sodium carbonate and sodium acid carbonate mixed aqueous solution at 110 degrees Celsius and Under 0.4MPa, 21% acrylonitrile conversion is 3- hydroxypropionitriles, 65% acrylonitrile conversion 3,3 '-itrile group propyl ether.Martinetz Dieter is combined into the high incomes of 3- hydroxypropionitriles up to 98% in the aqueous solution reclaimed water of vulcanized sodium and quaternary ammonium salt.Konstantinov will Acrylonitrile and concentrated sodium hydroxide reactant aqueous solution, acetaldehyde cyanhydrin yield reach 92%.Sugiyama Kazuo are utilized containing gold Belong to ambrose alloy and metallic nickel catalysis is lower and water reaction synthesizes 3- hydroxypropionitriles.
McGinley is reacted 4 hours in ethanol with chlorethanol and potassium cyanide, and the yield of 3- hydroxypropionitriles is 83%;By second After alcohol is changed to methanol, the yield of 3- hydroxypropionitriles brings up to 87%.Song Chunjun report sodium iodide catalysis chlorethanol with Cyaniding nak response, the yield of 3- hydroxypropionitriles bring up to 90%.Samejiama is reacted at 500 DEG C with chlorethanol with potassium cyanide 10 hours, the yield of 3- hydroxypropionitriles was 93%.Cao etc. is reported in the case where PEG400 coexists, and Cymag closes with chlorethanol reaction Yield into 3- hydroxypropionitriles is also 93%.
Oxirane under alkali metal or alkaline earth metal hydroxide effect, can directly synthesize 3- hydroxyls third with hydrogen cyanide Nitrile.The cost of material of this method is minimum, and synthetic route is most short, also most industrial value.At room temperature, oxirane and hydrogen Cyanic acid hardly reacts;Even if reaction temperature is brought up into 50 DEG C, the yield of 3- hydroxypropionitriles is little;Continue to improve reaction Temperature can increase operational danger, while improve no significant effect to the yield of target product.By hydrogen cyanide and alkali metal Hydroxide reaction is made corresponding alkali metal salt, these alkali metal salts under excess alkali metal hydroxide catalysis with epoxy Ethane, which reacts, generates 3- hydroxypropionitriles;Content that Terentjew etc. is delivered on Zhurnal Obshchei Khimii and This method has all been mentioned in US1914326 and DE577686.In order to further improve yield, DE570031 substitutes cyanogas Cymag is used in above-mentioned reaction, and the dissolubility of the calcium hydroxide of generation in reaction dissolvent is very low, has promoted and has reacted to life Carried out into 3- hydroxypropionitriles direction.But no matter be start material from Cymag or cyanogas, reaction will after terminating Gone to neutralize caused alkali metal hydroxide with acid, and generate substantial amounts of inorganic salts;Because contain cyanogen root in the raw material of the technique Ion, caused inorganic salts, which also need to special processing, just can discharge or recycle.US2453062 disclose hydrogen cyanide with The salt that tertiary amine is formed synthesizes 3- hydroxypropionitriles under base catalyst with reacting ethylene oxide, by the tertiary amine of generation through distillation after reaction Return to reduce to produce the amount of discarded object in course of reaction.
The technique that US2390519 discloses oxirane and hydrogen cyanide reaction synthesis 3- hydroxypropionitriles.Using product section The method of back-mixing, caused heat in course of reaction is removed in time;The raw material that reaction is had neither part nor lot in product is distilled into reuse, improved The overall utilization of raw material and the yield of product.
US2653162 discloses a kind of anion exchange resin catalyzed hydrogen cyanide of carboxylic acid type containing alkali metal and ring Oxidative ethane reaction synthesis target product.The amount of generation inorganic salts can be greatly reduced with this method.But utilize amberlite The basic activated site of fat and the combination of hydrogen cyanide, then generate target product, the operating efficiency of the technique with reacting ethylene oxide Obviously it is relatively low;In recent years, the patent of German Ying Chuan companies application further discloses the regeneration difficulty of the technique ion exchange resin, Therefore this method generates the problem of new, i.e. catalyst recovery is difficult.
US2459430 discloses magnesium hydroxide catalysis hydrogen cyanide and 3- hydroxypropionitriles, this method is synthesized with reacting ethylene oxide Solve the problems, such as to produce a large amount of inorganic salts discarded objects in above-mentioned technique, but the selectivity of product and yield are high not enough, it is right The purification of product improves requirement;Meanwhile hydrogen cyanide participated under conditions of higher than room temperature reaction also there is operating environment hydrogen Cyanic acid content exceedes the scope of safety.
In summary, the product yield of the hydration method of acrylonitrile is low;Chlorethanol and the method raw material raw material of hydrogen cyanide reaction It is expensive, product yield is not high, produce substantial amounts of inorganic salts discarded object the problems such as;Although oxirane and hydrogen cyanide reaction road Line segment, cost are low, but the largely yoke such as inorganic salts discarded object containing hydrogen cyanide will be handled by being also unable to escape.
The content of the invention
[the problem of intending to solve]
The present invention intends to solve that oxirane gives up with producing a large amount of inorganic salts in hydrogen cyanide reaction synthesis 3- hydroxypropionitrile techniques The problem of gurry;
The present invention intends to solve oxirane with there may be hydrogen in environment in hydrogen cyanide reaction synthesis 3- hydroxypropionitrile techniques Cyanic acid content exceedes the problem of safe range;
The present invention intends to solve that hydrogen cyanide reacts the yields of 3- hydroxypropionitriles with oxirane and not high asked at ambient temperature Topic.
[technical scheme]
Technical solutions according to the invention are to be divided into the following steps:
(1) oxirane and hydrogen cyanide are added in the reactor with refrigerating plant and are well mixed, and control system Temperature is between -20 DEG C -5 DEG C;
(2) by BF3/ 1,2- pentanediol/activated alumina catalyst are added in reactant mixture;
(3) in -20 DEG C~15 DEG C stirring reactions 2~72 hours;Or in -20 DEG C~0 DEG C stirring reaction 8h, then at 0 DEG C -20 DEG C stirring reaction 24h;
(4) after reaction terminates, Filtration of catalyst obtains 3- hydroxypropionitrile products;
(5) catalyst is directly used in the reaction of catalytic epoxyethane and hydrogen cyanide without further processing.
[beneficial effects of the present invention]
With having seen the hydrogen cyanide of document report compared with the method for reacting ethylene oxide synthesis 3- hydroxypropionitriles, present invention tool There is following obvious beneficial effect.
(1) compared with the cyanide of alkali metal or alkaline-earth metal being the method for initiation material synthesis 3- hydroxypropionitriles, this The alkali metal of neutralization reaction generation or the hydroxide of alkaline-earth metal need not be removed after invention reaction with substantial amounts of inorganic acid, also not Generation largely needs inorganic salts to be processed;
(2) with hydrogen cyanide with the salt that tertiary amine is formed be initiation material synthesis 3- hydroxypropionitriles method compared with, the present invention The trimethylamine recycling of generation need not will be reacted by distilling, simplify synthesis technique significantly.
(3) hydrogen cyanide is catalyzed compared with the method for ethylene oxide synthesis 3- hydroxypropionitriles with magnesium hydroxide, the present invention is anti- The steam of hydrogen cyanide at a temperature of answering forces down, and operational danger is small.
(4) compared with these methods for having seen document report, do not make in the reaction of hydrogen cyanide and oxirane in the present invention With solvent, the ability that solvent separates with product is greatly reduced;
(5) compared with these methods for having seen document report, the separation of product rear catalyst of the invention and product is easy, Separation of solid and liquid can is only needed to separate target product with catalyst.
(6) compared with these methods for having seen document report, catalyst of the invention can be substantially increased with direct reuse The Atom economy of course of reaction.
Embodiment
Embodiment 1
2.70g hydrogen cyanide and 4.40g oxirane are put into the closed reactor with cooling device, stirred The stirring reaction 24h at 10 DEG C afterwards.The content of 3- hydroxypropionitriles is detected after the hydrogen cyanide for having neither part nor lot in reaction through sodium hypochlorite processing. As a result show that under this condition, hydrogen cyanide hardly reacts with oxirane.
Embodiment 2
2.70g hydrogen cyanide and 4.40g oxirane are put into the closed reactor with cooling device, stirred After add 4.0g sodium hydroxides, the stirring reaction 24h at 10 DEG C.After reaction terminates, handled through sodium hypochlorite and have neither part nor lot in reaction Hydrogen cyanide after detect 3- hydroxypropionitriles content.As a result show under this condition, hydrogen cyanide is also hardly sent out with oxirane Raw reaction.
Embodiment 3
2.70g hydrogen cyanide and 4.40g oxirane are put into the closed reactor with cooling device, stirred After add 0.2g boron trifluoride etherates, the stirring reaction 4h at -20 DEG C.After reaction terminates, handled through sodium hypochlorite Have neither part nor lot in the content that 3- hydroxypropionitriles are detected after the hydrogen cyanide of reaction.As a result show under this condition, the yield of 3- hydroxypropionitriles For 9.8%.
Embodiment 4
2.70g hydrogen cyanide and 4.40g oxirane are put into the closed reactor with cooling device, stirred After add 0.2g boron trifluoride etherates, 0.16g1,2- pentanediols, the stirring reaction 4h at -20 DEG C.Reaction terminates Afterwards, the content of 3- hydroxypropionitriles is detected after the hydrogen cyanide for having neither part nor lot in reaction through sodium hypochlorite processing.As a result show under this condition, The yield of 3- hydroxypropionitriles is 52%.
Embodiment 5
2.70g hydrogen cyanide and 4.40g oxirane are put into the closed reactor with cooling device, stirred After add 0.2g boron trifluoride etherates, 0.16g1,2- pentanediols, 1.0g activated aluminas, stirred at -10 DEG C anti- Answer 4h.After reaction terminates, the content of 3- hydroxypropionitriles is detected after the hydrogen cyanide for having neither part nor lot in reaction through sodium hypochlorite processing.As a result table It is bright under this condition, the yields of 3- hydroxypropionitriles is 70%.
Embodiment 6
By 0.2g boron trifluoride etherates, 0.16g1,2- pentanediols, 1.0g activated aluminas and 20mL dry diethyl ethers add Enter into the closed reactor with agitating device, white solid is filtered to obtain after 24h is stirred at room temperature.
2.70g hydrogen cyanide and 4.40g oxirane are put into the closed reactor with cooling device, stirring is equal It is even;Then the above-mentioned white solids of 1.0g, the stirring reaction 4h at -10 DEG C are added.After reaction terminates, handled with a small amount of sodium hypochlorite Have neither part nor lot in the content that 3- hydroxypropionitriles are detected after the hydrogen cyanide of reaction.As a result show under this condition, the yield of 3- hydroxypropionitriles Up to 86%.
Embodiment 7
2.70g hydrogen cyanide and 4.40g oxirane are put into the closed reactor with cooling device, stirring is equal It is even;Then the white solid added in 1.0g embodiments 6, the stirring reaction 4h at -10 DEG C, then the stirring reaction 4h at 10 DEG C. After reaction terminates, the content of detection 3- hydroxypropionitriles after the hydrogen cyanide for having neither part nor lot in reaction is handled with a small amount of sodium hypochlorite.As a result table It is bright under this condition, the high incomes of 3- hydroxypropionitriles is up to 93%.
Embodiment 8
2.70g hydrogen cyanide and 4.40g oxirane are put into the closed reactor with cooling device, stirring is equal It is even;Then the white solid added in 1.0g embodiments 6, the stirring reaction 4h at -10 DEG C, then the stirring reaction 24h at 10 DEG C. After reaction terminates, the content of detection 3- hydroxypropionitriles after the hydrogen cyanide for having neither part nor lot in reaction is handled with a small amount of sodium hypochlorite.As a result table It is bright under this condition, the high incomes of 3- hydroxypropionitriles is up to 97.3%.
Embodiment 9
2.70g hydrogen cyanide and 5.00g oxirane are put into the closed reactor with cooling device, stirring is equal It is even;Then the white solid added in 1.0g embodiments 6, the stirring reaction 4h at -10 DEG C, then the stirring reaction 24h at 10 DEG C. After reaction terminates, the hydrogen cyanide for having neither part nor lot in reaction is determined after adding appropriate sodium hydroxide solution.As a result show under this condition, As a result show the high conversion rate of hydrogen cyanide in 99%.

Claims (5)

  1. A kind of 1. method for being catalyzed hydrogen cyanide and ethylene oxide synthesis 3- hydroxypropionitriles, it is characterised in that hydrogen cyanide and oxirane In BF3The lower synthesis 3- hydroxypropionitriles of/1,2- pentanediol/activated alumina composite catalyst catalysis.
  2. 2. according to the method described in right 1, between wherein the amount of substance ratio of hydrogen cyanide and oxirane is 1: 1 to 1: 1.5.
  3. 3. according to the method described in right 1, the wherein ratio of the amount of substance of catalyst BF3 and 1,2- pentanediol is 1: 0.6 to 1: 3 Between;Catalyst BF3With the gross mass of 1,2- pentanediols and the gross mass ratio of activated alumina between 0.02 to 0.3.
  4. 4. according to the method described in right 1, the wherein ratio of the quality of catalyst and raw material hydrogen cyanide between 0.001 to 0.2.
  5. 5. according to the method described in right 1, wherein reaction temperature and reaction time is characterised by, anti-between -20 DEG C to 0 DEG C 24h to 120h is answered, or 8-48h is reacted between temperature is increased into 0 to 20 DEG C again after reaction 1-8h between -20 DEG C to 0 DEG C.
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CN110498740A (en) * 2019-09-18 2019-11-26 重庆医药高等专科学校 A method of producing 3- hydracrylic acid
CN110577467A (en) * 2019-09-18 2019-12-17 重庆医药高等专科学校 Synthetic method of 3-hydroxypropionic acid

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2453062A (en) * 1946-06-04 1948-11-02 American Cyanamid Co Production of alkylene cyanohydrins
US2459430A (en) * 1946-05-04 1949-01-18 American Cyanamid Co Production of ethylene cyanohydrin
US2653162A (en) * 1951-08-22 1953-09-22 Rohm & Haas Synthesis of alkylene cyanohydrins
US3395172A (en) * 1964-08-01 1968-07-30 Basf Ag Continuous production of ethylene cyanohydrin
CN101472882A (en) * 2006-06-14 2009-07-01 赢创罗姆有限责任公司 Apparatus and process for continuously preparing ethylene cyanohydrin

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2459430A (en) * 1946-05-04 1949-01-18 American Cyanamid Co Production of ethylene cyanohydrin
US2453062A (en) * 1946-06-04 1948-11-02 American Cyanamid Co Production of alkylene cyanohydrins
US2653162A (en) * 1951-08-22 1953-09-22 Rohm & Haas Synthesis of alkylene cyanohydrins
US3395172A (en) * 1964-08-01 1968-07-30 Basf Ag Continuous production of ethylene cyanohydrin
CN101472882A (en) * 2006-06-14 2009-07-01 赢创罗姆有限责任公司 Apparatus and process for continuously preparing ethylene cyanohydrin

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