CN101891761B - Method for catalytically synthesizing triethyl phosphate by phase transfer - Google Patents
Method for catalytically synthesizing triethyl phosphate by phase transfer Download PDFInfo
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- DQWPFSLDHJDLRL-UHFFFAOYSA-N triethyl phosphate Chemical compound CCOP(=O)(OCC)OCC DQWPFSLDHJDLRL-UHFFFAOYSA-N 0.000 title claims abstract description 33
- 238000000034 method Methods 0.000 title claims abstract description 12
- 230000002194 synthesizing effect Effects 0.000 title abstract 2
- GUCVHDYRKMSBOJ-UHFFFAOYSA-M sodium;diethyl phosphate Chemical compound [Na+].CCOP([O-])(=O)OCC GUCVHDYRKMSBOJ-UHFFFAOYSA-M 0.000 claims abstract description 26
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 22
- 239000003960 organic solvent Substances 0.000 claims abstract description 13
- 238000006243 chemical reaction Methods 0.000 claims abstract description 11
- 239000003444 phase transfer catalyst Substances 0.000 claims abstract description 11
- 238000003786 synthesis reaction Methods 0.000 claims abstract description 9
- 230000015572 biosynthetic process Effects 0.000 claims abstract description 8
- 239000003054 catalyst Substances 0.000 claims abstract description 8
- 238000004519 manufacturing process Methods 0.000 claims abstract description 7
- 239000006227 byproduct Substances 0.000 claims abstract description 6
- 239000002994 raw material Substances 0.000 claims abstract description 6
- 239000006081 fluorescent whitening agent Substances 0.000 claims abstract description 5
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Natural products CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 claims description 19
- 238000010992 reflux Methods 0.000 claims description 19
- DENRZWYUOJLTMF-UHFFFAOYSA-N diethyl sulfate Chemical compound CCOS(=O)(=O)OCC DENRZWYUOJLTMF-UHFFFAOYSA-N 0.000 claims description 13
- 229940008406 diethyl sulfate Drugs 0.000 claims description 13
- 239000007788 liquid Substances 0.000 claims description 13
- 238000003756 stirring Methods 0.000 claims description 12
- 239000002904 solvent Substances 0.000 claims description 10
- WEVYAHXRMPXWCK-UHFFFAOYSA-N Acetonitrile Chemical compound CC#N WEVYAHXRMPXWCK-UHFFFAOYSA-N 0.000 claims description 9
- HTZCNXWZYVXIMZ-UHFFFAOYSA-M benzyl(triethyl)azanium;chloride Chemical compound [Cl-].CC[N+](CC)(CC)CC1=CC=CC=C1 HTZCNXWZYVXIMZ-UHFFFAOYSA-M 0.000 claims description 8
- MVPPADPHJFYWMZ-UHFFFAOYSA-N chlorobenzene Chemical compound ClC1=CC=CC=C1 MVPPADPHJFYWMZ-UHFFFAOYSA-N 0.000 claims description 8
- JRMUNVKIHCOMHV-UHFFFAOYSA-M tetrabutylammonium bromide Chemical compound [Br-].CCCC[N+](CCCC)(CCCC)CCCC JRMUNVKIHCOMHV-UHFFFAOYSA-M 0.000 claims description 8
- CSNNHWWHGAXBCP-UHFFFAOYSA-L Magnesium sulfate Chemical compound [Mg+2].[O-][S+2]([O-])([O-])[O-] CSNNHWWHGAXBCP-UHFFFAOYSA-L 0.000 claims description 7
- UIIMBOGNXHQVGW-UHFFFAOYSA-M Sodium bicarbonate Chemical class [Na+].OC([O-])=O UIIMBOGNXHQVGW-UHFFFAOYSA-M 0.000 claims description 7
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical class [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 claims description 7
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 claims description 5
- LZZYPRNAOMGNLH-UHFFFAOYSA-M Cetrimonium bromide Chemical compound [Br-].CCCCCCCCCCCCCCCC[N+](C)(C)C LZZYPRNAOMGNLH-UHFFFAOYSA-M 0.000 claims description 4
- NTIZESTWPVYFNL-UHFFFAOYSA-N Methyl isobutyl ketone Chemical compound CC(C)CC(C)=O NTIZESTWPVYFNL-UHFFFAOYSA-N 0.000 claims description 4
- UIHCLUNTQKBZGK-UHFFFAOYSA-N Methyl isobutyl ketone Natural products CCC(C)C(C)=O UIHCLUNTQKBZGK-UHFFFAOYSA-N 0.000 claims description 4
- 239000012043 crude product Substances 0.000 claims description 3
- 238000007036 catalytic synthesis reaction Methods 0.000 claims description 2
- 230000035484 reaction time Effects 0.000 claims description 2
- 238000002390 rotary evaporation Methods 0.000 claims description 2
- 125000003944 tolyl group Chemical group 0.000 claims description 2
- 239000012046 mixed solvent Substances 0.000 abstract description 6
- 239000000047 product Substances 0.000 abstract description 5
- 238000003912 environmental pollution Methods 0.000 abstract description 4
- 238000009776 industrial production Methods 0.000 abstract description 4
- 239000003153 chemical reaction reagent Substances 0.000 abstract description 3
- 238000003408 phase transfer catalysis Methods 0.000 abstract description 3
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 abstract description 2
- 229910052698 phosphorus Inorganic materials 0.000 abstract description 2
- 239000011574 phosphorus Substances 0.000 abstract description 2
- 239000002699 waste material Substances 0.000 abstract description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 6
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- 230000007935 neutral effect Effects 0.000 description 3
- 238000002360 preparation method Methods 0.000 description 3
- 150000003242 quaternary ammonium salts Chemical class 0.000 description 3
- 239000008096 xylene Substances 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 2
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 2
- 238000009835 boiling Methods 0.000 description 2
- 230000007812 deficiency Effects 0.000 description 2
- -1 diethyl phosphate anion Chemical class 0.000 description 2
- IXCSERBJSXMMFS-UHFFFAOYSA-N hydrogen chloride Substances Cl.Cl IXCSERBJSXMMFS-UHFFFAOYSA-N 0.000 description 2
- 229910000041 hydrogen chloride Inorganic materials 0.000 description 2
- 238000010534 nucleophilic substitution reaction Methods 0.000 description 2
- 239000012074 organic phase Substances 0.000 description 2
- XHXFXVLFKHQFAL-UHFFFAOYSA-N phosphoryl trichloride Chemical compound ClP(Cl)(Cl)=O XHXFXVLFKHQFAL-UHFFFAOYSA-N 0.000 description 2
- BDZBKCUKTQZUTL-UHFFFAOYSA-N triethyl phosphite Chemical compound CCOP(OCC)OCC BDZBKCUKTQZUTL-UHFFFAOYSA-N 0.000 description 2
- 125000001931 aliphatic group Chemical group 0.000 description 1
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 1
- 125000003118 aryl group Chemical group 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 229920002301 cellulose acetate Polymers 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 239000013530 defoamer Substances 0.000 description 1
- 238000004043 dyeing Methods 0.000 description 1
- 229920001971 elastomer Polymers 0.000 description 1
- 230000032050 esterification Effects 0.000 description 1
- 238000005886 esterification reaction Methods 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 150000002430 hydrocarbons Chemical group 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 239000012038 nucleophile Substances 0.000 description 1
- 239000012044 organic layer Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000000575 pesticide Substances 0.000 description 1
- 239000012071 phase Substances 0.000 description 1
- 230000026731 phosphorylation Effects 0.000 description 1
- 238000006366 phosphorylation reaction Methods 0.000 description 1
- 239000005648 plant growth regulator Substances 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 239000004014 plasticizer Substances 0.000 description 1
- 230000009257 reactivity Effects 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 238000007086 side reaction Methods 0.000 description 1
- 239000007790 solid phase Substances 0.000 description 1
- 239000003381 stabilizer Substances 0.000 description 1
- 239000007858 starting material Substances 0.000 description 1
- 238000001308 synthesis method Methods 0.000 description 1
- 238000010189 synthetic method Methods 0.000 description 1
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- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Abstract
本发明涉及一种相转移催化合成磷酸三乙酯的方法。是以磷酸二乙酯钠盐为原料,加入相转移催化剂,在有机溶剂和水体系中加入乙基化试剂,生成的磷酸三乙酯,经分离提纯得到成品。本发明与现有技术相比,所用的催化剂成本较低,采用有机溶剂和水作为混合溶剂,有机溶剂可以循环使用,对环境友好,降低了合成成本,不仅对磷酸二乙酯钠盐进行了再利用,将废弃物转化为具有实用价值的有机磷资源,减少了环境污染,而且为磷酸三乙酯的工业生产提供了新的途径。该方法不仅具有反应步骤少,操作简便,收率高,产品纯度高,易于工业化生产,而且减少了荧光增白剂生产过程中的副产物磷酸二乙酯钠盐的环境污染。The invention relates to a method for synthesizing triethyl phosphate by phase transfer catalysis. Diethyl phosphate sodium salt is used as raw material, phase transfer catalyst is added, and ethylating reagent is added to the organic solvent and water system to form triethyl phosphate, which is separated and purified to obtain the finished product. Compared with the prior art, the present invention has lower catalyst cost, adopts organic solvent and water as the mixed solvent, and the organic solvent can be recycled, which is environmentally friendly and reduces the synthesis cost. Reusing wastes into organic phosphorus resources with practical value reduces environmental pollution and provides a new way for the industrial production of triethyl phosphate. The method not only has the advantages of fewer reaction steps, simple operation, high yield, high product purity and easy industrial production, but also reduces the environmental pollution of the by-product diethyl phosphate sodium salt in the production process of the fluorescent whitening agent.
Description
技术领域 technical field
本发明涉及一种有机合成的方法,尤其是相转移催化合成制备磷酸三乙酯的方法。The invention relates to a method for organic synthesis, in particular to a method for preparing triethyl phosphate by phase-transfer catalytic synthesis.
背景技术 Background technique
磷酸三乙酯分子式为(CH3CH2O)3PO,英文名Triethyl Phosphate,简称TEP。分子量182.16,是一种无色透明液体,熔点-56.5℃,沸点215~216℃,相对密度1.064(20/4℃),全溶于水,易溶于乙醇、乙醚、苯等有机溶剂,但随着温度上升在水中会逐渐水解。作为一种高沸点溶剂,磷酸三乙酯的用途十分广泛。在橡胶和塑料中,可用作增塑剂、催化剂、溶剂、稳定剂、固化剂和软化剂等;是制备农药的主要原料之一;也可用于植物生长调节剂,消泡剂,乙酸纤维的染色助剂,荧光灯玻璃涂料等的生产。目前国内外报道的制备磷酸三乙酯的合成主要有两条路线。一条是U.S.6673955报导,以三氯氧磷为磷酰化试剂,再与乙醇反应得到化合物,这种合成方法由于生成氯化氢副产物,在反应过程中导致产物分解,收率和纯度降低。U.S.2636048通过通入氮气排出生成的氯化氢,导致大量乙醇损失,也使产率有所降低。目前生产磷酸三乙酯的工艺普遍存在收率(50%~60%)较低等问题(如:《湖北工业大学学报》第22卷第5期63~65页“磷酸三乙酯合成新工艺研究”)。另一条路线,U.S.3136805报导,以亚磷酸三乙酯为起始原料,在碱性条件下用双氧水氧化得到磷酸三乙酯。这种合成方法的不足是:亚磷酸三乙酯会水解进而导致磷酸三乙酯的收率降低。因此必须严格控制pH值来减少副反应的发生。现有的荧光增白剂生产过程中的副产物磷酸二乙酯钠都不同程度存在污染环境、难以处理等问题。The molecular formula of triethyl phosphate is (CH 3 CH 2 O) 3 PO, the English name is Triethyl Phosphate, TEP for short. Molecular weight 182.16, is a colorless transparent liquid, melting point -56.5 ° C, boiling point 215 ~ 216 ° C, relative density 1.064 (20/4 ° C), completely soluble in water, easily soluble in organic solvents such as ethanol, ether, benzene, etc., but As the temperature rises, it will gradually hydrolyze in water. As a high boiling point solvent, triethyl phosphate is widely used. In rubber and plastics, it can be used as plasticizer, catalyst, solvent, stabilizer, curing agent and softener, etc.; it is one of the main raw materials for the preparation of pesticides; it can also be used as plant growth regulator, defoamer, cellulose acetate The production of dyeing auxiliaries, fluorescent glass coatings, etc. The synthesis of the preparation triethyl phosphate reported at home and abroad mainly contains two routes at present. One is that US6673955 reports that phosphorus oxychloride is used as a phosphorylation reagent and then reacted with ethanol to obtain a compound. This synthesis method is due to the generation of hydrogen chloride by-products, which cause product decomposition during the reaction process, resulting in reduced yield and purity. US2636048 discharges the hydrogen chloride generated by feeding nitrogen, which causes a large amount of ethanol loss and reduces the yield. The current production of triethyl phosphate generally has problems such as low yield (50% to 60%) (such as: "New Technology for Triethyl Phosphate Synthesis" on pages 63 to 65 of the fifth issue of "Journal of Hubei University of Technology" volume 22 Research"). Another route, US3136805 report, takes triethyl phosphite as starting material, obtains triethyl phosphate with hydrogen peroxide oxidation under alkaline conditions. The deficiency of this synthetic method is: triethyl phosphite can be hydrolyzed and then causes the yield of triethyl phosphate to reduce. Therefore, the pH value must be strictly controlled to reduce the occurrence of side reactions. The by-product sodium diethyl phosphate in the existing fluorescent whitening agent production process has problems such as polluting the environment and being difficult to handle to varying degrees.
发明内容 Contents of the invention
本发明的目的就在于针对上述现有技术的不足,提供一种相转移催化合成磷酸三乙酯的方法。The purpose of the present invention is just to provide a kind of method for the synthesis of triethyl phosphate by phase transfer catalysis for the above-mentioned deficiencies in the prior art.
本发明的目的是通过以下技术方案实现的:The purpose of the present invention is achieved through the following technical solutions:
相转移催化合成磷酸三乙酯的制备方法,包括以下顺序和步骤:各原料加入量是以mol计The preparation method of phase-transfer catalyzed synthesis of triethyl phosphate comprises the following sequence and steps: the amount of each raw material added is in mol
a、将荧光增白剂生产过程中的副产物磷酸二乙酯钠盐与相转移催化剂按1∶0.01~0.15mol、投入到装有回流冷凝器、加料漏斗、搅拌装置和温度计的反应器中,再按每摩尔磷酸二乙酯钠盐加入有机溶剂400ml~800ml,水0~200ml;a. Put the by-product diethyl phosphate sodium salt and phase transfer catalyst in the production process of fluorescent whitening agent into the reactor equipped with reflux condenser, feeding funnel, stirring device and thermometer according to 1:0.01~0.15mol , then add 400ml to 800ml of organic solvent and 0 to 200ml of water per mole of diethyl phosphate sodium salt;
b、加热搅拌使磷酸二乙酯钠盐和催化剂溶解,升温至回流;b, heat and stir to dissolve diethyl phosphate sodium salt and catalyst, and heat up to reflux;
c、加入硫酸二乙酯,磷酸二乙酯钠盐与硫酸二乙酯的投料摩尔比为1∶0.5~3mol;C, add diethyl sulfate, the molar ratio of diethyl phosphate sodium salt and diethyl sulfate is 1: 0.5~3mol;
d、保持回流反应温度70~100℃,反应时间4~10h,冷却,抽滤,得黄色溶液;d. Keep the reflux reaction temperature at 70-100°C for a reaction time of 4-10 hours, cool down, and filter with suction to obtain a yellow solution;
e、用饱和碳酸氢钠洗至中性,再用水洗两次后用饱和氯化钠洗一次,最后用无水硫酸镁干燥;e. Wash with saturated sodium bicarbonate to neutrality, then wash twice with water, wash once with saturated sodium chloride, and finally dry with anhydrous magnesium sulfate;
f、旋蒸溶剂得到磷酸三乙酯粗品,黄色透明液体;f, rotary evaporation of solvent to obtain triethyl phosphate crude product, yellow transparent liquid;
g、再经减压蒸馏得纯的磷酸三乙酯,无色透明液体。g. Distill under reduced pressure to obtain pure triethyl phosphate, a colorless transparent liquid.
本发明的目的是通过以下技术方案实现的:The purpose of the present invention is achieved through the following technical solutions:
有机溶剂包括甲苯、二甲苯、氯苯、乙腈或甲基异丁基酮。相转移催化剂为苄基三乙基氯化铵、十六烷基三甲基溴化铵或四丁基溴化铵。Organic solvents include toluene, xylene, chlorobenzene, acetonitrile or methyl isobutyl ketone. The phase transfer catalyst is benzyltriethylammonium chloride, cetyltrimethylammonium bromide or tetrabutylammonium bromide.
有益效果:本发明与现有技术相比,所用的催化剂成本较低,采用有机溶剂和水作为混合溶剂,有机溶剂可以循环使用,对环境友好,降低了合成成本,不仅对磷酸二乙酯钠盐进行了再利用,将废弃物转化为具有实用价值的有机磷资源,减少了环境污染,而且为磷酸三乙酯的工业生产提供了新的途径。该方法不仅具有反应步骤少,操作简便,收率高,产品纯度高,易于工业化生产,而且减少了荧光增白剂生产过程中的副产物磷酸二乙酯钠盐的环境污染。Beneficial effects: compared with the prior art, the cost of the catalyst used in the present invention is lower, organic solvent and water are used as the mixed solvent, and the organic solvent can be recycled, which is friendly to the environment and reduces the synthesis cost, not only for sodium diethyl phosphate The salt is reused, the waste is converted into organic phosphorus resources with practical value, the environmental pollution is reduced, and a new way is provided for the industrial production of triethyl phosphate. The method not only has the advantages of fewer reaction steps, simple operation, high yield, high product purity and easy industrial production, but also reduces the environmental pollution of the by-product diethyl phosphate sodium salt in the production process of the fluorescent whitening agent.
具体实施方式 Detailed ways
下面结合实施例作进一步的详细说明:Below in conjunction with embodiment do further detailed description:
本发明的相转移催化合成磷酸三乙酯的方法以磷酸二乙酯钠盐为原料,加入相转移催化剂,在有机溶剂和水体系中加入乙基化试剂(以硫酸二乙酯为例),生成的磷酸三乙酯经分离提纯而得成品。这种酯化方法是亲核取代,有机相为硫酸二乙酯,固相为磷酸二乙酯钠盐,磷酸二乙酯钠盐在相应的相中生成磷酸二乙酯负离子,然后它作为一个亲核试剂,被相转移催化剂携带进入有机相中与硫酸二乙酯进行亲核取代反应。The method for the synthesis of triethyl phosphate by phase transfer catalysis of the present invention takes diethyl phosphate sodium salt as a raw material, adds a phase transfer catalyst, and adds an ethylating reagent (taking diethyl sulfate as an example) in an organic solvent and water system, The generated triethyl phosphate is separated and purified to obtain the finished product. This esterification method is nucleophilic substitution, the organic phase is diethyl sulfate, the solid phase is diethyl phosphate sodium salt, diethyl phosphate sodium salt generates diethyl phosphate anion in the corresponding phase, and then it acts as a The nucleophile is carried by the phase transfer catalyst into the organic phase for nucleophilic substitution reaction with diethyl sulfate.
反应式如下:The reaction formula is as follows:
相转移催化剂为季铵盐类,具有以下结构:Phase transfer catalysts are quaternary ammonium salts with the following structure:
式中R1、R2、R3、R4分别为CnH2n+1(n=1~16)的脂肪族烃基或芳基。其中烃基可以是相同也可以不同。具体应用的季铵盐,如苄基三乙基氯化铵、十六烷基三甲基溴化铵、四丁基溴化铵等;具体应用的有机溶剂包括甲苯、二甲苯、氯苯、乙腈、甲基异丁基酮等。其中最佳的相转移催化剂是四丁基溴化铵,最佳的溶剂是甲苯,四丁基溴化铵在甲苯中的反应活性最高。In the formula, R 1 , R 2 , R 3 , and R 4 are respectively C n H 2n+1 (n=1-16) aliphatic hydrocarbon groups or aryl groups. Wherein the hydrocarbon groups may be the same or different. Quaternary ammonium salts for specific applications, such as benzyltriethylammonium chloride, cetyltrimethylammonium bromide, tetrabutylammonium bromide, etc.; organic solvents for specific applications include toluene, xylene, chlorobenzene, Acetonitrile, methyl isobutyl ketone, etc. Wherein the best phase transfer catalyst is tetrabutylammonium bromide, and the best solvent is toluene, and tetrabutylammonium bromide has the highest reactivity in toluene.
本发明将磷酸二乙酯钠盐、相转移催化剂及甲苯和水混合,缓慢升温至回流温度,加入硫酸二乙酯,恒温反应6h。反应结束后,冷却,抽滤,用饱和碳酸氢钠溶液洗至中性,水洗,饱和氯化钠洗,分出有机层,用无水硫酸镁干燥,旋蒸溶剂即得磷酸三乙酯粗品。The present invention mixes diethyl phosphate sodium salt, a phase transfer catalyst, toluene and water, slowly heats up to the reflux temperature, adds diethyl sulfate, and reacts at constant temperature for 6 hours. After the reaction, cool, filter with suction, wash with saturated sodium bicarbonate solution until neutral, wash with water, wash with saturated sodium chloride, separate the organic layer, dry with anhydrous magnesium sulfate, and rotate the solvent to obtain the crude product of triethyl phosphate .
所说的每1mol(合176.0g)的磷酸二乙酯钠盐及1mol(合154.18g)的硫酸二乙酯用水为:水为0~200ml,有机溶剂为400~800ml。所述的相转移催化剂为季铵盐类,加入的原料磷酸二乙酯钠盐与相转移催化剂的摩尔比为1∶0.01~0.15。Said every 1mol (together 176.0g) of diethyl phosphate sodium salt and 1mol (together to 154.18g) of diethyl sulfate is water: water is 0~200ml, and organic solvent is 400~800ml. The phase transfer catalyst is a quaternary ammonium salt, and the molar ratio of the added raw material diethyl phosphate sodium salt to the phase transfer catalyst is 1:0.01-0.15.
实施例1:Example 1:
取磷酸二乙酯钠盐176.0g、四丁基溴化铵12.89g、混合溶剂甲苯400ml和水30ml加入到装有回流冷凝器、加料漏斗、搅拌装置和温度计的反应器中,加热搅拌使磷酸二乙酯钠盐和四丁基溴化铵溶解,升温至回流,加入硫酸二乙酯154.18g,保持回流反应6h,冷却,抽滤,得黄色溶液,然后用饱和碳酸氢钠洗至中性,再用水洗两次后用饱和氯化钠洗一次,无水硫酸镁干燥,最后旋蒸溶剂得到磷酸三乙酯粗品,黄色透明液体,收率63.61%~91.30%,含量95%。减压蒸馏可得纯的磷酸三乙酯,无色透明液体,折射率n=1.4055,含量99%。Get 176.0g of diethyl phosphate sodium salt, 12.89g of tetrabutylammonium bromide, 400ml of mixed solvent toluene and 30ml of water and join in the reactor equipped with reflux condenser, feeding funnel, stirring device and thermometer, heat and stir to make phosphoric acid Dissolve diethyl ester sodium salt and tetrabutylammonium bromide, raise the temperature to reflux, add 154.18g diethyl sulfate, keep the reflux reaction for 6h, cool, and filter with suction to obtain a yellow solution, then wash with saturated sodium bicarbonate until neutral , washed twice with water and once with saturated sodium chloride, dried over anhydrous magnesium sulfate, and finally the solvent was rotary evaporated to obtain crude triethyl phosphate, a yellow transparent liquid with a yield of 63.61% to 91.30% and a content of 95%. Distill under reduced pressure to obtain pure triethyl phosphate, a colorless transparent liquid with a refractive index n=1.4055 and a content of 99%.
实施例2:Example 2:
取磷酸二乙酯钠盐176.0g、十六烷基三甲基溴化铵14.58g,混合溶剂二甲苯500ml和水80ml,加入到装有回流冷凝器、加料漏斗、搅拌装置和温度计的反应器中,加热搅拌使磷酸二乙酯钠盐和催化剂溶解,升温至回流,加入硫酸二乙酯154.18g,保持回流反应4h,冷却,抽滤,得黄色溶液,然后用饱和碳酸氢钠洗至中性,再用水洗两次后用饱和氯化钠洗一次,无水硫酸镁干燥,最后旋蒸溶剂得到磷酸三乙酯粗品,黄色透明液体,收率从62.70%~91.65%,含量95%。减压蒸馏可得纯的磷酸三乙酯,无色透明液体,折射率n=1.4055,含量99%。Get 176.0g of diethyl phosphate sodium salt, 14.58g of cetyltrimethylammonium bromide, 500ml of mixed solvent xylene and 80ml of water, and add them to the reactor equipped with reflux condenser, feeding funnel, stirring device and thermometer , heat and stir to dissolve diethyl phosphate sodium salt and catalyst, raise the temperature to reflux, add 154.18 g of diethyl sulfate, keep reflux reaction for 4 hours, cool, filter with suction to obtain a yellow solution, and then wash with saturated sodium bicarbonate to medium Then wash twice with water and once with saturated sodium chloride, dry over anhydrous magnesium sulfate, and finally spin the solvent to obtain crude triethyl phosphate, a yellow transparent liquid, with a yield of 62.70% to 91.65% and a content of 95%. Distill under reduced pressure to obtain pure triethyl phosphate, a colorless transparent liquid with a refractive index n=1.4055 and a content of 99%.
实施例3:Example 3:
取磷酸二乙酯钠盐176.0g、苄基三乙基氯化铵9.09g,混合溶剂氯苯600ml和水100ml,加入到装有回流冷凝器、加料漏斗、搅拌装置和温度计的反应器中,加热搅拌使磷酸二乙酯钠盐和催化剂溶解,升温至回流,加入硫酸二乙酯77.09g,保持回流反应7h,冷却,抽滤,得黄色溶液,然后用饱和碳酸氢钠洗至中性,再用水洗两次后用饱和氯化钠洗一次,无水硫酸镁干燥,最后旋蒸溶剂得到磷酸三乙酯粗品,黄色透明液体,收率从53.69%~91.30%,含量95%。减压蒸馏可得纯的磷酸三乙酯,无色透明液体,折射率n=1.4055,含量99%。Get diethyl phosphate sodium salt 176.0g, benzyltriethylammonium chloride 9.09g, mixed solvent chlorobenzene 600ml and water 100ml, join in the reactor that reflux condenser, addition funnel, stirring device and thermometer are housed, Heat and stir to dissolve diethyl phosphate sodium salt and catalyst, raise the temperature to reflux, add 77.09 g of diethyl sulfate, keep reflux reaction for 7 hours, cool, filter with suction to obtain a yellow solution, then wash with saturated sodium bicarbonate until neutral, Wash twice with water and once with saturated sodium chloride, dry over anhydrous magnesium sulfate, and finally spin evaporate the solvent to obtain crude triethyl phosphate, a yellow transparent liquid, with a yield ranging from 53.69% to 91.30% and a content of 95%. Distill under reduced pressure to obtain pure triethyl phosphate, a colorless transparent liquid with a refractive index n=1.4055 and a content of 99%.
实施例4:Example 4:
取磷酸二乙酯钠盐176.0g、四丁基溴化铵12.89g,混合溶剂甲基异丁基酮800ml和水120ml,加入到装有回流冷凝器、加料漏斗、搅拌装置和温度计的反应器中,加热搅拌使磷酸二乙酯钠盐和催化剂溶解,升温至回流,加入硫酸二乙酯154.18g,保持回流反应5h,冷却,抽滤,得黄色溶液,然后用饱和碳酸氢钠洗至中性,再用水洗两次后用饱和氯化钠洗一次,无水硫酸镁干燥,最后旋蒸溶剂得到磷酸三乙酯粗品,黄色透明液体,收率最高可达95.98%,含量95%。减压蒸馏可得纯的磷酸三乙酯,无色透明液体,折射率n=1.4055,含量99%。Take 176.0g of diethyl phosphate sodium salt, 12.89g of tetrabutylammonium bromide, 800ml of mixed solvent methyl isobutyl ketone and 120ml of water, and add them to the reactor equipped with reflux condenser, feeding funnel, stirring device and thermometer , heat and stir to dissolve diethyl phosphate sodium salt and catalyst, raise the temperature to reflux, add 154.18g diethyl sulfate, keep reflux reaction for 5h, cool, filter with suction to obtain a yellow solution, and then wash with saturated sodium bicarbonate to medium It was washed twice with water and then once with saturated sodium chloride, dried over anhydrous magnesium sulfate, and finally the solvent was rotary evaporated to obtain crude triethyl phosphate, a yellow transparent liquid, with a yield of up to 95.98% and a content of 95%. Distill under reduced pressure to obtain pure triethyl phosphate, a colorless transparent liquid with a refractive index n=1.4055 and a content of 99%.
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US3976619A (en) * | 1972-12-26 | 1976-08-24 | Monsanto Company | Flame retardant polymers containing phosphates |
US6673955B2 (en) * | 2001-11-27 | 2004-01-06 | Bayer Aktiengesellschaft | Preparation of triethyl phosphate |
CN101941988A (en) * | 2010-03-04 | 2011-01-12 | 浙江医药股份有限公司维生素厂 | Process for preparing triethyl phosphate by utilizing sodium diethyl phosphate |
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US3976619A (en) * | 1972-12-26 | 1976-08-24 | Monsanto Company | Flame retardant polymers containing phosphates |
US6673955B2 (en) * | 2001-11-27 | 2004-01-06 | Bayer Aktiengesellschaft | Preparation of triethyl phosphate |
CN101941988A (en) * | 2010-03-04 | 2011-01-12 | 浙江医药股份有限公司维生素厂 | Process for preparing triethyl phosphate by utilizing sodium diethyl phosphate |
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Na Ge et al.Novelties of solid-liquid phase transfer catalyzed synthesis of benzyl diethyl phosphate from the sodium salt of diethyl phosphate.《European Journal of Chemistry》.2011,第2卷(第2期),第269-271页. * |
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