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CN103539809B - Two silicic acid dichloro propyl ester compound of fire retardant second dioxy support and preparation method thereof - Google Patents

Two silicic acid dichloro propyl ester compound of fire retardant second dioxy support and preparation method thereof Download PDF

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CN103539809B
CN103539809B CN201310557260.4A CN201310557260A CN103539809B CN 103539809 B CN103539809 B CN 103539809B CN 201310557260 A CN201310557260 A CN 201310557260A CN 103539809 B CN103539809 B CN 103539809B
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flame retardant
silicon tetrachloride
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王彦林
董信
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Shandong Industry Research Institute Zhongke High End Chemical Industry Technology Research Institute Co ltd
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Suzhou University of Science and Technology
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Abstract

本发明涉及一种阻燃剂乙二氧撑双硅酸二氯丙酯化合物及其制备方法,该化合物的结构如下式所示:制备方法为:在30℃以下,向四氯化硅的有机溶液中滴加相对于四氯化硅2倍摩尔环氧氯丙烷,于50℃反应2h;再滴入相对于四氯化硅0.5倍摩尔的乙二醇,而后在65-80℃反应7-10h;再降至50℃以下,再滴加相对于四氯化硅1-1.5倍摩尔环氧氯丙烷,在70-85℃反应5-8h,经纯化处理,得阻燃剂乙二氧撑双硅酸二氯丙酯;本发明化合物含有硅与氯两种阻燃元素,协同阻燃效能高,适合用作聚氯乙烯、聚氨酯、环氧树脂和不饱和树脂等材料的阻燃剂;制备工艺简单,成本低,易于实现工业化生产。The invention relates to a flame retardant ethylenedioxyethylene disilicate dichloropropyl compound and a preparation method thereof. The structure of the compound is shown in the following formula: The preparation method is: below 30°C, dropwise add 2 times mole of epichlorohydrin relative to silicon tetrachloride to the organic solution of silicon tetrachloride, react at 50°C for 2 hours; then drop into the organic solution of silicon tetrachloride 0.5 Doubling moles of ethylene glycol, then react at 65-80°C for 7-10h; then drop below 50°C, then dropwise add 1-1.5 times moles of epichlorohydrin relative to silicon tetrachloride, and react at 70-85°C 5-8h, after purification treatment, the flame retardant ethylenedioxyethylene bisilicate dichloropropyl ester is obtained; the compound of the present invention contains two kinds of flame retardant elements silicon and chlorine, and the synergistic flame retardant effect is high, and is suitable for use as polyvinyl chloride, A flame retardant for materials such as polyurethane, epoxy resin and unsaturated resin; the preparation process is simple, the cost is low, and industrial production is easy to realize.

Description

阻燃剂乙二氧撑双硅酸二氯丙酯化合物及其制备方法Flame retardant ethylenedioxyethylene disilicate dichloropropyl ester compound and preparation method thereof

技术领域technical field

本发明涉及一种阻燃剂乙二氧撑双硅酸二氯丙酯化合物及其制备方法,具体涉及一种阻燃剂二[三(二氯丙氧基)硅酰氧基]乙烷化合物及其制备方法,该化合物硅氯双元素协同阻燃效能高,适合用作聚氯乙烯、聚氨酯、环氧树脂与不饱和树脂等材料的阻燃剂。The invention relates to a flame retardant ethylenedioxyethylene bisilicate dichloropropyl ester compound and a preparation method thereof, in particular to a flame retardant bis[tri(dichloropropoxy)silyloxy]ethane compound According to the preparation method thereof, the compound has high synergistic flame retardant effect of silicon and chlorine dual elements, and is suitable for being used as a flame retardant for materials such as polyvinyl chloride, polyurethane, epoxy resin and unsaturated resin.

背景技术Background technique

由于科学技术与经济的快速发展,人们的安全意识不断增强,促进了阻燃剂工业的快速发展。从欧盟1986年公布发现多溴二苯醚阻燃剂燃烧时产生有害物质以后,卤系阻燃剂的使用受到了限制,但由于卤系阻燃剂综合性价比优良,目前还难以找到理想的替代物,因而无卤化进程不会太快,但是研究开发高效卤系阻燃剂以减少阻燃剂的添加量,从而降低燃烧时的毒性,已成为阻燃剂的重要研究方向。多种阻燃剂复配产生协同阻燃效应可以提高阻燃效能,而设计分子结构中含有多种阻燃元素,而通过分子内多种阻燃元素协同阻燃增效,提高阻燃效能,是实现高效阻燃剂的更有效方法。Due to the rapid development of science, technology and economy, people's safety awareness has been continuously enhanced, which has promoted the rapid development of the flame retardant industry. Since the European Union announced in 1986 that polybrominated diphenyl ether flame retardants produced harmful substances when they burned, the use of halogenated flame retardants has been restricted. However, due to the excellent overall cost performance of halogenated flame retardants, it is still difficult to find ideal alternatives. Therefore, the non-halogenation process will not be too fast, but research and development of high-efficiency halogenated flame retardants to reduce the amount of flame retardants added, thereby reducing the toxicity during combustion, has become an important research direction for flame retardants. The synergistic flame retardant effect produced by the compounding of various flame retardants can improve the flame retardant performance, and the designed molecular structure contains a variety of flame retardant elements, and through the synergistic flame retardant and synergistic effect of various flame retardant elements in the molecule, the flame retardant performance can be improved. It is a more effective way to achieve high-efficiency flame retardants.

本发明用光伏产业的副产物四氯化硅为原料制备了硅和氯两元素协同阻燃剂乙二氧撑双硅酸二氯丙酯,四氯化硅中的硅和氯都是优良的阻燃元素,硅系阻然剂本身具有优异的热稳定性,硅可以在燃烧时形成致密的硅炭层,有效的防熔体滴落和阻燃抑烟性能,是目前低烟、低毒阻燃材料开发的重点之一。把两个优良的阻燃元素设计在同一分子结构中,产生协同阻燃效应,能发挥理想的阻燃效果。本发明化合物属对称的多酯结构,具有优良的阻燃增塑性。The present invention uses silicon tetrachloride, a by-product of the photovoltaic industry, as a raw material to prepare silicon and chlorine two-element synergistic flame retardant ethylenedioxyethylene bisilicate dichloropropyl ester, and both silicon and chlorine in silicon tetrachloride are excellent Flame retardant element, silicon-based flame retardant itself has excellent thermal stability, silicon can form a dense silicon carbon layer during combustion, effective in preventing melt dripping and flame retardant and smoke suppression, and is currently a low-smoke, low-toxicity One of the key points in the development of flame retardant materials. Designing two excellent flame retardant elements in the same molecular structure produces a synergistic flame retardant effect and can exert an ideal flame retardant effect. The compound of the invention has a symmetrical polyester structure and has excellent flame retardancy and plasticizing properties.

发明内容Contents of the invention

本发明的目的之一在于提出用四氯化硅制备一种阻燃剂二[三(二氯丙氧基)硅酰氧基]乙烷化合物,其阻燃性好,可克服现有技术中的不足。One of the purposes of the present invention is to propose to prepare a kind of flame retardant bis[three (dichloropropoxy) silyloxy] ethane compound with silicon tetrachloride, its flame retardancy is good, can overcome the existing technology lack of.

为实现上述发明目的,本发明采用了如下技术方案:In order to realize the above-mentioned purpose of the invention, the present invention has adopted following technical scheme:

阻燃剂二[三(二氯丙氧基)硅酰氧基]乙烷化合物,其特征在于,该化合物的结构如下式所示:Flame retardant bis[tri(dichloropropoxy)silyloxy]ethane compound is characterized in that the structure of the compound is shown in the following formula:

本发明的另一目的在于提出一种阻燃剂二[三(二氯丙氧基)硅酰氧基]乙烷的制备方法,其原料廉价易得,工艺简单,设备投资少,易于规模化生产,该方法为:Another object of the present invention is to propose a method for preparing a flame retardant bis[tri(dichloropropoxy)silyloxy]ethane, the raw material of which is cheap and easy to obtain, the process is simple, the investment in equipment is small, and it is easy to scale up production, the method is:

用氮气置换掉反应容器内的空气,加入有机溶剂和四氯化硅,在搅拌下,用冷水浴冷却,使反应体系温度降低到30℃以下,滴加相对于四氯化硅2倍摩尔的环氧氯丙烷,滴加过程控制反应温度不高于40℃,滴完后,升温至50℃,保温反应2h;再滴入相对于四氯化硅0.5倍摩尔的乙二醇,以滴加速度控制反应温度不高于55℃,滴完后升温至65-80℃,反应7-10h;待HCl气体放完后,再将体系降温至50℃以下,滴加相对于四氯化硅1-1.5倍摩尔环氧氯丙烷,以滴加速度控制反应温度不高于60℃,滴完后,将体系温度升至70-85℃,保温反应5-8h,检测溶液PH=5-6为反应终点。经纯化处理,得阻燃剂二[三(二氯丙氧基)硅酰氧基]乙烷。Replace the air in the reaction vessel with nitrogen, add an organic solvent and silicon tetrachloride, cool with a cold water bath under stirring, reduce the temperature of the reaction system to below 30°C, and add dropwise 2 times the molar amount of silicon tetrachloride For epichlorohydrin, the dropwise addition process controls the reaction temperature not to be higher than 40°C. After the drop is completed, the temperature is raised to 50°C, and the temperature is kept for 2 hours; Control the reaction temperature not to be higher than 55°C, raise the temperature to 65-80°C after dropping, and react for 7-10 hours; after the HCl gas is released, cool the system down to below 50°C, and add dropwise the relative silicon tetrachloride 1- 1.5 times the mole of epichlorohydrin, control the reaction temperature not higher than 60°C at the rate of addition, after the drop, raise the temperature of the system to 70-85°C, keep the temperature for 5-8 hours, and test the solution pH=5-6 as the reaction end point . After purification, the flame retardant bis[tri(dichloropropoxy)silyloxy]ethane was obtained.

如上所述的有机溶剂为乙腈、二氧六环、二氯乙烷、四氯化碳或乙二醇二甲醚,其有机溶剂体积(ml)的量为四氯化硅质量(g)的3-4倍。The above-mentioned organic solvent is acetonitrile, dioxane, ethylene dichloride, carbon tetrachloride or ethylene glycol dimethyl ether, and the amount of its organic solvent volume (ml) is the amount of silicon tetrachloride quality (g) 3-4 times.

如上所述的经纯化处理为冷却至30℃,再减压蒸馏除去溶剂和过量的环氧氯丙烷(回收使用)及少量低沸点物,而后降温到60℃,再加入产品理论质量(g)2-3倍体积(ml)的石油醚洗涤,搅拌0.5h,转移至分液漏斗中静置分层,分出下层料液,减压蒸馏除去少量的石油醚。After the above-mentioned purification process, it is cooled to 30°C, and then the solvent, excess epichlorohydrin (recycled) and a small amount of low boiling point are removed by distillation under reduced pressure, and then the temperature is lowered to 60°C, and then the theoretical mass of the product (g) is added. Wash with 2-3 times the volume (ml) of petroleum ether, stir for 0.5 h, transfer to a separatory funnel to stand for stratification, separate the lower layer material liquid, and distill under reduced pressure to remove a small amount of petroleum ether.

如上所述的石油醚为石油醚的沸程在60-90℃或90-120℃。The petroleum ether mentioned above is petroleum ether with a boiling range of 60-90°C or 90-120°C.

发明人研究中发现乙二醇和四氯化硅很难溶合反应,呈果冻状不易扩散,且提高反应温度四氯化硅的挥发量又会增加,因此选用了先让1倍摩尔四氯化硅与2倍摩尔环氧氯丙烷反应,生成硅酸双酯后,再与乙二醇反应,克服了乙二醇和四氯化硅不易溶合的难题,也克服了四氯化硅高温易挥发的问题。In the research of the inventor, it was found that ethylene glycol and silicon tetrachloride were difficult to dissolve and react, and it was difficult to diffuse in a jelly shape, and the volatilization of silicon tetrachloride would increase when the reaction temperature was increased. Silicon reacts with 2 times the mole of epichlorohydrin to form a silicate diester, and then reacts with ethylene glycol, which overcomes the difficulty of ethylene glycol and silicon tetrachloride being difficult to dissolve, and also overcomes the high-temperature volatility of silicon tetrachloride The problem.

本发明阻燃剂二[三(二氯丙氧基)硅酰氧基]乙烷为黄色透明液体,产率为89.3%~93.4%,其闪点(开口杯):198±5℃,折光率:nD 25=1.4158,密度(25℃):1.3549g/cm3。其适合作为聚氯乙烯、聚乙烯醇、环氧树脂、不饱和树脂和聚氨酯等材料的阻燃剂之用。The flame retardant bis[tri(dichloropropoxy)silyloxy]ethane of the present invention is a yellow transparent liquid with a yield of 89.3% to 93.4%, its flash point (open cup): 198±5°C, refraction Ratio: n D 25 =1.4158, density (25°C): 1.3549 g/cm 3 . It is suitable as a flame retardant for materials such as polyvinyl chloride, polyvinyl alcohol, epoxy resin, unsaturated resin and polyurethane.

阻燃剂二[三(二氯丙氧基)硅酰氧基]乙烷的制备工艺原理如下式所示:The preparation process principle of flame retardant bis[tri(dichloropropoxy)silyloxy]ethane is shown in the following formula:

与现有技术相比,本发明的有益效果在于:Compared with prior art, the beneficial effect of the present invention is:

①本发明阻燃剂二[三(二氯丙氧基)硅酰氧基]乙烷化合物含有硅与氯两阻燃元素,其协同阻燃效能高,硅元素具有成炭作用,能有效防止材料受热熔融滴落而产生的二次燃烧。①The flame retardant bis[tri(dichloropropoxy)silyloxy]ethane compound of the present invention contains two flame retardant elements of silicon and chlorine, and its synergistic flame retardant efficiency is high, and the silicon element has a carbon-forming effect, which can effectively prevent The secondary combustion caused by the material being heated, melted and dripped.

②本发明阻燃剂二[三(二氯丙氧基)硅酰氧基]乙烷化合物是双酯结构,分子量大、挥发性低、增塑性好、对称性好,其物理化学性能稳定,与高分子材料相容性好,能适应于工程塑料的高温加工。2. The flame retardant bis[tri(dichloropropoxy)silyloxy]ethane compound of the present invention is a diester structure with large molecular weight, low volatility, good plasticity and good symmetry, and its physical and chemical properties are stable. It has good compatibility with polymer materials and can adapt to high temperature processing of engineering plastics.

③本发明以多晶硅产业的副产物四氯化硅为原料制备硅与氯协同阻燃剂二[三(二氯丙氧基)硅酰氧基]乙烷,为解决四氯化硅综合利用的难题提供了一条有效途径。③The present invention uses the by-product silicon tetrachloride of polysilicon industry as raw material to prepare silicon and chlorine synergistic flame retardant bis[tri(dichloropropoxy)silyloxy]ethane, in order to solve the problem of comprehensive utilization of silicon tetrachloride Puzzles provide an effective way.

④本发明制备方法先让四氯化硅与环氧氯丙烷反应生成硅酸双酯,然后再和乙二醇反应,克服了乙二醇在四氯化硅中难溶的问题,也有利于乙二醇与四氯化硅的定向反应,也克服了四氯化硅高温下反应易挥发的难题。4. The preparation method of the present invention first allows silicon tetrachloride and epichlorohydrin to react to generate silicate diester, and then reacts with ethylene glycol, which overcomes the insoluble problem of ethylene glycol in silicon tetrachloride, and is also conducive to The directional reaction of ethylene glycol and silicon tetrachloride also overcomes the problem that silicon tetrachloride is easily volatile under high temperature.

⑤本发明工艺中的溶剂和过量的环氧氯丙烷可直接回收利用,其原料易得,生产成本低,设备投资少,易于规模化生产,具有很好的应用及开发前景。5. The solvent and excess epichlorohydrin in the process of the present invention can be directly recycled, and its raw materials are easy to get, the production cost is low, the equipment investment is small, and it is easy to scale production, and has good application and development prospects.

附图说明Description of drawings

为了进一步说明产品的结构和性能特给出如下附图。In order to further illustrate the structure and performance of the product, the following drawings are given.

1、二[三(二氯丙氧基)硅酰氧基]乙烷的红外光谱图,详见说明书附图图1;1. For the infrared spectrogram of bis[tri(dichloropropoxy)silyloxy]ethane, see Figure 1 of the accompanying drawing for details;

图1表明,2960cm-1(带有氯基的C-H的伸缩振动);2882cm-1(C-H的伸缩振动);1460cm-1(C-H的弯曲振动);1429cm-1(带有氯基的C-H的弯曲振动);1111cm-1和783cm-1(Si-O-C的伸缩振动及弯曲振动);1047cm-1和968cm-1(C-O的伸缩振动二重峰);665cm-1(C-Cl的伸缩振动)。Figure 1 shows that 2960cm -1 (stretching vibration of CH with chlorine group); 2882cm -1 (stretching vibration of CH); 1460cm -1 (bending vibration of CH ) ; bending vibration); 1111cm -1 and 783cm -1 (stretching vibration and bending vibration of Si-OC); 1047cm -1 and 968cm -1 (double peak of stretching vibration of CO); 665cm -1 (stretching vibration of C-Cl ).

2、二[三(二氯丙氧基)硅酰氧基]乙烷的核磁光谱图,详见说明书附图图2;2. For the NMR spectrum of bis[tri(dichloropropoxy)silyloxy]ethane, see Figure 2 of the accompanying drawing for details;

图2表明,氘代氯仿作溶剂,δ4.46-4.50为-SiOCH2CHClCH2Cl中与氧相连的亚甲基的氢峰;δ4.38-4.44为-SiOCH(CH2Cl)2中与氧相连的次甲基的氢峰;δ4.04-4.10为-SiOCH2CH2OSi-中亚甲基的氢峰;δ3.96-4.01为-SiOCH2CHClCH2Cl中氯亚甲基的氢峰;δ3.65-3.76为-SiOCH2CHClCH2Cl和-SiOCH(CH2Cl)2中氯甲基的氢峰;δ7.26为氘代氯仿交换的质子峰。Figure 2 shows that deuterated chloroform is used as a solvent, and δ4.46-4.50 is the hydrogen peak of the methylene connected to oxygen in -SiOCH 2 CHClCH 2 Cl ; The hydrogen peak of the methine linked by oxygen; δ4.04-4.10 is the hydrogen peak of the methylene in -SiOCH 2 CH 2 OSi-; δ3.96-4.01 is the hydrogen of the chloromethylene in -SiOCH 2 CHClCH 2 Cl Peak; δ3.65-3.76 is the hydrogen peak of chloromethyl in -SiOCH 2 CHClCH 2 Cl and -SiOCH(CH 2 Cl) 2 ; δ7.26 is the proton peak of deuterated chloroform exchange.

具体实施方式detailed description

以下结合具体实施例对本发明的技术方案作进一步说明。The technical solution of the present invention will be further described below in conjunction with specific embodiments.

实施例1在装有搅拌器、温度计和高效回流冷凝管,并在冷凝管上口装有可极度膨胀密封套的250ml四口烧瓶中,用氮气置换掉瓶内的空气,加入60ml二氧六环和17g(11.47ml,0.1mol)四氯化硅,在搅拌下,用冷水浴冷却,使反应体系温度降低到30℃以下,滴加18.504g(15.68ml,0.2mol)环氧氯丙烷,滴加过程控制反应温度不高于40℃,滴完后,升温至50℃,保温反应2h;而后将回流冷凝管上口换装为干燥管,将3.1g(2.78ml,0.05mol)乙二醇滴入到四口烧瓶中,以滴加速度控制反应温度不高于55℃,滴完后升温至75℃,反应8h;待HCl气体放完后,再将体系降温至50℃以下,滴加11.10g(9.41ml,0.12mol)环氧氯丙烷,以滴加速度控制反应温度不高于60℃,滴完后,将体系温度升至80℃,反应5h,检测反应液PH=5-6为反应终点;减压蒸馏除去二氧六环和过量的环氧氯丙烷(回收使用)及少量低沸点物,而后降温到60℃,再加入90ml石油醚洗涤,搅拌0.5h,转移至分液漏斗中静置分层,分出下层料液,减压蒸馏除去少量的石油醚,得产品二[三(二氯丙氧基)硅酰氧基]乙烷。其产率为93.4%,闪点(开口杯):198±5℃,折光率:nD 25=1.4158,密度(25℃):1.3549g/cm3Example 1 In a 250ml four-neck flask equipped with a stirrer, a thermometer and a high-efficiency reflux condenser, and an extremely expandable sealing sleeve is installed on the upper mouth of the condenser, replace the air in the bottle with nitrogen, and add 60ml of dioxane ring and 17g (11.47ml, 0.1mol) of silicon tetrachloride, under stirring, cooled with a cold water bath, the temperature of the reaction system was reduced to below 30°C, and 18.504g (15.68ml, 0.2mol) of epichlorohydrin was added dropwise, During the dropwise addition process, the reaction temperature should not be higher than 40°C. After the dropwise addition, the temperature was raised to 50°C, and the temperature was kept for 2 hours; then, the upper port of the reflux condenser tube was replaced with a drying tube, and 3.1g (2.78ml, 0.05mol) of ethylene di Drop the alcohol into the four-necked flask, control the reaction temperature not higher than 55°C with the dropping speed, raise the temperature to 75°C after the drop, and react for 8 hours; after the HCl gas is released, cool the system down to below 50°C, drop 11.10g (9.41ml, 0.12mol) epichlorohydrin, control the reaction temperature not higher than 60°C at the rate of addition, after the drop, raise the temperature of the system to 80°C, react for 5 hours, and detect that the pH of the reaction solution is 5-6 The end of the reaction: Dioxane, excess epichlorohydrin (recycled) and a small amount of low boiling point are removed by vacuum distillation, then cooled to 60°C, then 90ml of petroleum ether is added for washing, stirred for 0.5h, and transferred to a separatory funnel Stand in the middle and separate the layers, separate the lower layer material liquid, and distill off a small amount of petroleum ether under reduced pressure to obtain the product bis[tris(dichloropropoxy)silyloxy]ethane. Its yield is 93.4%, flash point (open cup): 198±5°C, refractive index: n D 25 =1.4158, density (25°C): 1.3549 g/cm 3 .

实施例2在装有搅拌器、温度计和高效回流冷凝管,并在冷凝管上口装有可极度膨胀密封套的250ml四口烧瓶中,用氮气置换掉瓶内的空气,加入60ml四氯化碳和17g(11.47ml,0.1mol)四氯化硅,在搅拌下,用冷水浴冷却,使反应体系温度降低到30℃以下,滴加18.504g(15.68ml,0.2mol)环氧氯丙烷,滴加过程控制反应温度不高于40℃,滴完后,升温至50℃,保温反应2h;而后将回流冷凝管上口换装为干燥管,将3.1g(2.78ml,0.05mol)乙二醇滴入到四口烧瓶中,以滴加速度控制反应温度不高于55℃,滴完后升温至70℃,反应9h;待HCl气体放完后,再将体系降温至50℃以下,滴加9.34g(7.92ml,0.101mol)环氧氯丙烷,以滴加速度控制反应温度不高于60℃,滴完后,将体系温度升至75℃,反应8h,检测反应液PH=5-6为反应终点;减压蒸馏除去四氯化碳和过量的环氧氯丙烷(回收使用)及少量低沸点物,而后降温到60℃,再加入90ml石油醚洗涤,搅拌0.5h,转移至分液漏斗中静置分层,分出下层料液,减压蒸馏除去少量的石油醚,得产品二[三(二氯丙氧基)硅酰氧基]乙烷。其产率为89.3%,闪点(开口杯):198±5℃,折光率:nD 25=1.4158,密度(25℃):1.3549g/cm3Example 2 In a 250ml four-neck flask equipped with an agitator, a thermometer and a high-efficiency reflux condenser, and an extremely expandable sealing sleeve at the upper mouth of the condenser, replace the air in the bottle with nitrogen, and add 60ml tetrachloride Carbon and 17g (11.47ml, 0.1mol) of silicon tetrachloride, under stirring, cooled with a cold water bath, the temperature of the reaction system was reduced to below 30°C, and 18.504g (15.68ml, 0.2mol) of epichlorohydrin was added dropwise, During the dropwise addition process, the reaction temperature should not be higher than 40°C. After the dropwise addition, the temperature was raised to 50°C, and the temperature was kept for 2 hours; then, the upper port of the reflux condenser tube was replaced with a drying tube, and 3.1g (2.78ml, 0.05mol) of ethylene di Drop the alcohol into the four-necked flask, control the reaction temperature not higher than 55°C with the dropping speed, raise the temperature to 70°C after dropping, and react for 9 hours; after the HCl gas is released, cool the system down to below 50°C, drop 9.34g (7.92ml, 0.101mol) epichlorohydrin, control the reaction temperature not higher than 60°C at the rate of addition, after the drop, raise the temperature of the system to 75°C, react for 8 hours, and detect that the pH of the reaction solution is 5-6 The end of the reaction: carbon tetrachloride, excess epichlorohydrin (recycling) and a small amount of low boiling point are removed by distillation under reduced pressure, then the temperature is lowered to 60°C, then 90ml of petroleum ether is added for washing, stirred for 0.5h, and transferred to a separatory funnel Stand in the middle and separate the layers, separate the lower layer material liquid, and distill off a small amount of petroleum ether under reduced pressure to obtain the product bis[tris(dichloropropoxy)silyloxy]ethane. Its yield is 89.3%, flash point (open cup): 198±5°C, refractive index: n D 25 =1.4158, density (25°C): 1.3549 g/cm 3 .

实施例3在装有搅拌器、温度计和高效回流冷凝管,并在冷凝管上口装有可极度膨胀密封套的250ml四口烧瓶中,用氮气置换掉瓶内的空气,加入60ml乙二醇二甲醚和17g(11.47ml,0.1mol)四氯化硅,在搅拌下,用冷水浴冷却,使反应体系温度降低到30℃以下,滴加18.504g(15.68ml,0.2mol)环氧氯丙烷,滴加过程控制反应温度不高于40℃,滴完后,升温至50℃,保温反应2h;而后将回流冷凝管上口换装为干燥管,将3.1g(2.78ml,0.05mol)乙二醇滴入到四口烧瓶中,以滴加速度控制反应温度不高于60℃,滴完后升温至80℃,反应7h;待HCl气体放完后,再将体系降温至55℃以下,滴加10.18g(8.62ml,0.11mol)环氧氯丙烷,以滴加速度控制反应温度不高于50℃,滴完后,将体系温度升至85℃,反应6h,检测反应液PH=5-6为反应终点;减压蒸馏除去乙二醇二甲醚和过量的环氧氯丙烷(回收使用)及少量低沸点物,而后降温到60℃,再加入90ml石油醚洗涤,搅拌0.5h,转移至分液漏斗中静置分层,分出下层料液,减压蒸馏除去少量的石油醚,得产品二[三(二氯丙氧基)硅酰氧基]乙烷。其产率为90.7%,闪点(开口杯):198±5℃,折光率:nD 25=1.4158,密度(25℃):1.3549g/cm3Example 3 In a 250ml four-necked flask equipped with an agitator, a thermometer and a high-efficiency reflux condenser, and an extremely expandable seal at the top of the condenser, replace the air in the bottle with nitrogen, and add 60ml of ethylene glycol Dimethyl ether and 17g (11.47ml, 0.1mol) of silicon tetrachloride, under stirring, cooled with a cold water bath, the temperature of the reaction system was reduced to below 30°C, and 18.504g (15.68ml, 0.2mol) of epoxy chloride was added dropwise Propane, the dropwise addition process controls the reaction temperature not to be higher than 40°C. After the drop, the temperature is raised to 50°C, and the heat preservation reaction is carried out for 2 hours; then the upper port of the reflux condenser is replaced with a drying tube, and 3.1g (2.78ml, 0.05mol) Ethylene glycol was dropped into the four-necked flask, and the reaction temperature was controlled by the dropping speed to not be higher than 60°C. After the drop, the temperature was raised to 80°C, and the reaction was carried out for 7 hours; after the HCl gas was released, the temperature of the system was lowered to below 55°C. Add 10.18g (8.62ml, 0.11mol) of epichlorohydrin dropwise, and control the reaction temperature at a rate not higher than 50°C. After the drop, raise the temperature of the system to 85°C, react for 6 hours, and check that the pH of the reaction solution is 5- 6 is the end point of the reaction; ethylene glycol dimethyl ether, excess epichlorohydrin (recycled) and a small amount of low boiling point are removed by distillation under reduced pressure, then the temperature is lowered to 60°C, and 90ml of petroleum ether is added for washing, stirred for 0.5h, and transferred to Put it into a separatory funnel and let it stand for stratification, separate the lower layer material liquid, and distill off a small amount of petroleum ether under reduced pressure to obtain the product bis[tris(dichloropropoxy)silyloxy]ethane. Its yield is 90.7%, flash point (open cup): 198±5°C, refractive index: n D 25 =1.4158, density (25°C): 1.3549 g/cm 3 .

实施例4在装有搅拌器、温度计和高效回流冷凝管,并在冷凝管上口装有可极度膨胀密封套的250ml四口烧瓶中,用氮气置换掉瓶内的空气,加入60ml二氯乙烷和17g(11.47ml,0.1mol)四氯化硅,在搅拌下,用冷水浴冷却,使反应体系温度降低到30℃以下,滴加18.504g(15.68ml,0.2mol)环氧氯丙烷,滴加过程控制反应温度不高于40℃,滴完后,升温至50℃,保温反应2h;而后将回流冷凝管上口换装为干燥管,将3.1g(2.78ml,0.05mol)乙二醇滴入到四口烧瓶中,以滴加速度控制反应温度不高于55℃,滴完后升温至65℃,反应10h;待HCl气体放完后,再将体系降温至50℃以下,滴加12.03g(10.19ml,0.13mol)环氧氯丙烷,以滴加速度控制反应温度不高于60℃,滴完后,将体系温度升至70℃,反应7h,检测反应液PH=5-6为反应终点;减压蒸馏除去二氯乙烷和过量的环氧氯丙烷(回收使用)及少量低沸点物,而后降温到60℃,再加入90ml石油醚洗涤,搅拌0.5h,转移至分液漏斗中静置分层,分出下层料液,减压蒸馏除去少量的石油醚,得产品二[三(二氯丙氧基)硅酰氧基]乙烷。其产率为91.5%,闪点(开口杯):198±5℃,折光率:nD 25=1.4158,密度(25℃):1.3549g/cm3Example 4 In a 250ml four-neck flask equipped with a stirrer, a thermometer and a high-efficiency reflux condenser, and an extremely expandable sealing sleeve is installed at the upper mouth of the condenser, replace the air in the bottle with nitrogen, and add 60ml of dichloroethylene Alkane and 17g (11.47ml, 0.1mol) of silicon tetrachloride, under stirring, cooled with a cold water bath, the temperature of the reaction system was reduced to below 30°C, and 18.504g (15.68ml, 0.2mol) of epichlorohydrin was added dropwise, During the dropwise addition process, the reaction temperature should not be higher than 40°C. After the dropwise addition, the temperature was raised to 50°C, and the temperature was kept for 2 hours; then, the upper port of the reflux condenser tube was replaced with a drying tube, and 3.1g (2.78ml, 0.05mol) of ethylene di Alcohol was dropped into the four-necked flask, and the reaction temperature was controlled by the dropping speed to not be higher than 55°C. After the drop, the temperature was raised to 65°C, and the reaction was carried out for 10 hours; after the HCl gas was released, the system was cooled down to below 50°C, and added dropwise 12.03g (10.19ml, 0.13mol) epichlorohydrin, control the reaction temperature not higher than 60°C at the rate of addition, after the drop, raise the temperature of the system to 70°C, react for 7 hours, and detect that the pH of the reaction solution is 5-6 Reaction end point; Dichloroethane, excess epichlorohydrin (recycled) and a small amount of low boiling point are removed by vacuum distillation, then cooled to 60°C, then 90ml of petroleum ether is added for washing, stirred for 0.5h, and transferred to a separatory funnel Stand in the middle and separate the layers, separate the lower layer material liquid, and distill off a small amount of petroleum ether under reduced pressure to obtain the product bis[tris(dichloropropoxy)silyloxy]ethane. Its yield is 91.5%, flash point (open cup): 198±5°C, refractive index: n D 25 =1.4158, density (25°C): 1.3549 g/cm 3 .

实施例5在装有搅拌器、温度计和高效回流冷凝管,并在冷凝管上口装有可极度膨胀密封套的250ml四口烧瓶中,用氮气置换掉瓶内的空气,加入60ml乙腈和17g(11.47ml,0.1mol)四氯化硅,在搅拌下,用冷水浴冷却,使反应体系温度降低到30℃以下,滴加18.504g(15.68ml,0.2mol)环氧氯丙烷,滴加过程控制反应温度不高于40℃,滴完后,升温至50℃,保温反应2h;而后将回流冷凝管上口换装为干燥管,将3.1g(2.78ml,0.05mol)乙二醇滴入到四口烧瓶中,以滴加速度控制反应温度不高于55℃,滴完后升温至75℃,反应8h;待HCl气体放完后,再将体系降温至50℃以下,滴加12.95g(10.97ml,0.14mol)环氧氯丙烷,以滴加速度控制反应温度不高于60℃,滴完后,将体系温度升至80℃反应6h,检测反应液pH=5-6为反应终点;减压蒸馏除去乙腈和过量的环氧氯丙烷(回收使用)及少量低沸点物,而后降温到60℃,加入90ml石油醚洗涤,恒温60℃搅拌0.5h,转移至分液漏斗中静置分层,分出下层料液,减压蒸馏除去少量的石油醚,得产品二[三(二氯丙氧基)硅酰氧基]乙烷。其产率为92.6%,闪点(开口杯):198±5℃,折光率:nD 25=1.4158,密度(25℃):1.3549g/cm3Example 5 In a 250ml four-neck flask equipped with an agitator, a thermometer and a high-efficiency reflux condenser, and an extremely expandable seal at the top of the condenser, replace the air in the bottle with nitrogen, and add 60ml of acetonitrile and 17g (11.47ml, 0.1mol) of silicon tetrachloride, under stirring, cooled with a cold water bath to lower the temperature of the reaction system below 30°C, and dropwise added 18.504g (15.68ml, 0.2mol) of epichlorohydrin, and the dropwise addition process Control the reaction temperature not to be higher than 40°C. After dripping, raise the temperature to 50°C and keep it warm for 2 hours; then replace the top of the reflux condenser tube with a drying tube, and drop 3.1g (2.78ml, 0.05mol) of ethylene glycol into the In a four-necked flask, the reaction temperature is controlled at a rate of addition not higher than 55°C. After the drop, the temperature is raised to 75°C and reacted for 8 hours; after the HCl gas is released, the temperature of the system is lowered to below 50°C, and 12.95g ( 10.97ml, 0.14mol) of epichlorohydrin, the reaction temperature is controlled by the rate of addition to not be higher than 60°C, after the drop, the temperature of the system is raised to 80°C for 6 hours, and the pH of the reaction solution is detected to be 5-6 as the end point of the reaction; Remove acetonitrile, excess epichlorohydrin (recycled for use) and a small amount of low-boiling matter by distillation under pressure, then cool down to 60°C, add 90ml of petroleum ether to wash, stir at constant temperature 60°C for 0.5h, transfer to a separatory funnel to stand and separate , Separate the lower layer material liquid, and distill off a small amount of petroleum ether under reduced pressure to obtain the product bis[tri(dichloropropoxy)silyloxy]ethane. Its yield is 92.6%, flash point (open cup): 198±5°C, refractive index: n D 25 =1.4158, density (25°C): 1.3549 g/cm 3 .

表1乙二氧撑双硅酸二氯丙酯制备例主要工艺参数Table 1 The main process parameters of the preparation example of ethylenedioxyethylene disilicate dichloropropyl

本案发明人还将上述制备的乙二氧撑双硅酸二氯丙酯应用于聚氯乙烯中。参照:GB/T2406-2008《塑料燃烧性能试验方法-氧指数法》测样品的极限氧指数。取阻燃剂乙二氧撑双硅酸二氯丙酯、增塑剂邻苯二甲酸二辛酯(DOP)、协效阻燃剂三氧化二锑(Sb2O3)和聚氯乙烯(PVC)以不同比例混合均匀后,用挤出机挤出,制成直径为3mm的样条,并对其阻燃性能进行了测试,列出了部分试验结果如表2所示:The inventor of this case also applied the above-mentioned prepared ethylenedioxyethylene disilicate dichloropropyl to polyvinyl chloride. Reference: GB/T2406-2008 "Test Method for Combustion Performance of Plastics - Oxygen Index Method" to measure the limiting oxygen index of the sample. The flame retardant ethylenedioxyethylene disilicate dichloropropyl ester, the plasticizer dioctyl phthalate (DOP), the synergistic flame retardant antimony trioxide (Sb 2 O 3 ) and polyvinyl chloride ( PVC) was mixed evenly in different proportions, extruded with an extruder to make a sample with a diameter of 3mm, and its flame retardancy was tested, and some test results were listed as shown in Table 2:

表2乙二氧撑双硅酸二氯丙酯的阻燃性能数据Table 2 Flame retardant performance data of ethylenedioxyethylene disilicate dichloropropyl

实验表明,阻燃剂乙二氧撑双硅酸二氯丙酯与聚氯乙烯有很好的相容性,与Sb2O3有很好的阻燃协效性,具有良好的阻燃性能,成炭防滴落性能和增塑性能。Experiments show that the flame retardant ethylenedioxyethylene disilicate dichloropropyl has good compatibility with polyvinyl chloride , has good flame retardancy synergy with Sb2O3 , and has good flame retardancy , Charcoal anti-dripping performance and plasticizing performance.

Claims (5)

1. a preparation method for fire retardant two [three (compound) silicon acyloxy] ethane, it is characterized in that, the method is:
The air in reaction vessel is fallen with nitrogen replacement, add organic solvent and silicon tetrachloride, under agitation, with cooling bath cooling, make temperature of reaction system be reduced to less than 30 DEG C, drip the epoxy chloropropane relative to silicon tetrachloride 2 times moles, drip process control temperature of reaction not higher than 40 DEG C, after dripping off, be warming up to 50 DEG C, insulation reaction 2h; Instill the ethylene glycol relative to silicon tetrachloride 0.5 times mole again, control temperature of reaction not higher than 55 DEG C with rate of addition, after dripping off, be warming up to 65-80 DEG C, reaction 7-10h; After HCl gas discharges, again system is cooled to less than 50 DEG C, drip relative to silicon tetrachloride 1-1.5 times moles of epichlorohydrin, temperature of reaction is controlled not higher than 60 DEG C with rate of addition, after dripping off, system temperature is risen to 70-85 DEG C, insulation reaction 5-8h, detecting pH value of solution=5-6 is reaction end; Purifiedly process to obtain product fire retardant two [three (compound) silicon acyloxy] ethane, the structure of this compound is shown below:
In its formula, m is the integer of 0-3.
2. the preparation method of fire retardant two [three (compound) silicon acyloxy] ethane according to claim 1, it is characterized in that: described organic solvent is acetonitrile, dioxane, ethylene dichloride, tetracol phenixin or glycol dimethyl ether, its organic solvent volume milliliter number is 3-4 times of silicon tetrachloride quality grams.
3. the preparation method of fire retardant two [three (compound) silicon acyloxy] ethane according to claim 1, it is characterized in that: described purified process is that underpressure distillation removes desolventizing and excessive epoxy chloropropane and a small amount of low boilers, then cool to 60 DEG C, add the petroleum ether of product Theoretical Mass grams 2-3 times of volume milliliter number again, stir 0.5h, be transferred to stratification in separating funnel, separate lower floor's feed liquid, underpressure distillation removes a small amount of sherwood oil.
4. the preparation method of fire retardant two [three (compound) silicon acyloxy] ethane according to claim 3, is characterized in that: the boiling range of described sherwood oil is 60-90 DEG C or 90-120 DEG C.
5. the preparation method of fire retardant two [three (compound) silicon acyloxy] ethane according to claim 3, is characterized in that: described underpressure distillation removes desolventizing and excessive epoxy chloropropane is the solvent or epoxy chloropropane recovery use collected.
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