WO2019095245A1 - Method for synthesizing methylene disulfonate compound - Google Patents

Method for synthesizing methylene disulfonate compound Download PDF

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WO2019095245A1
WO2019095245A1 PCT/CN2017/111504 CN2017111504W WO2019095245A1 WO 2019095245 A1 WO2019095245 A1 WO 2019095245A1 CN 2017111504 W CN2017111504 W CN 2017111504W WO 2019095245 A1 WO2019095245 A1 WO 2019095245A1
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methylene disulfonate
synthesizing
acid
disulfonate compound
compound
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PCT/CN2017/111504
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French (fr)
Chinese (zh)
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张民
刘鹏
王军
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石家庄圣泰化工有限公司
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Priority to KR1020187023253A priority Critical patent/KR102101982B1/en
Priority to PCT/CN2017/111504 priority patent/WO2019095245A1/en
Publication of WO2019095245A1 publication Critical patent/WO2019095245A1/en

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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D327/00Heterocyclic compounds containing rings having oxygen and sulfur atoms as the only ring hetero atoms

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  • the invention belongs to the technical field of battery electrolyte additives, and relates to a battery electrolyte additive, a methylene disulfonate compound, and particularly relates to a method for synthesizing a methylene disulfonate compound.
  • the synthesis method of the invention is simple, the yield is high, the obtained product has high purity, low moisture content and low acid value, and the application to the battery electrolyte can greatly improve the performance of the electrolyte.
  • the methylene disulfonate compound can be used as a pharmaceutical preparation for treating leukemia and the like in animals, and the sulfonic acid group contained in the structure can react with alcohol, phenol, thiol and the like under certain conditions, and its unique structure. It has a huge role in the synthesis of heterocyclic drugs.
  • the application of methylene disulfonate compounds in lithium battery electrolyte additives has been gradually developed.
  • the methylene disulfonate compound is used in lithium battery electrolyte additives, which can be remarkable. Improve battery performance, increase battery rechargeability and cycle characteristics.
  • the moisture content and acid value of the methylene disulfonate compound prepared by the prior method are relatively high, and are applied to the battery to cause decomposition, flatulence and bulging of the electrolyte, which not only fails to improve the performance of the battery, but also significantly The performance of the battery is lowered, and therefore, the moisture content and acid value of the added additive must be strictly controlled.
  • a sulfonyl chloride is reacted with silver carbonate to obtain silver sulfonate, and then silver sulfonate is reacted with diiodomethane, and R is a hydrogen atom or a methyl group:
  • the raw material diacetate used in this production method is very expensive and not easily available, and the alkane disulfonic acid which is additionally used as a raw material is also expensive to affect its industrial application.
  • This method reduces the production cost to a certain extent, but the yield is low and can only reach about 50%. Moreover, the obtained product has high moisture content and high acid value, affecting the performance applied to the battery, and has no industrial value.
  • the present invention provides a method for synthesizing a methylene disulfonate compound, which has a mild and stable synthesis process, and greatly improves the yield and product quality.
  • the structural formula of the methylene disulfonate compound of the present invention is as shown in the following II: R 1 and R 2 are independently a hydrogen atom or a C 1-4 alkyl group in which a hydrogen atom may be substituted by a halogen atom; n is 1 to 4 An integer; and when n is an integer from 2 to 4, n R 1 and n R 2 may be the same or different;
  • a method for synthesizing a methylene disulfonate compound which is synthesized by reacting an alkanedisulfonic acid with a formaldehyde compound in the presence of a dehydrating agent, wherein the dehydrating agent is a neutral dehydrating agent, and the alkane disulfonic acid is used.
  • the sulfonic acid compound of the formula I controlling the molar ratio of the formaldehyde compound to the alkanedisulfonic acid ⁇ 1; wherein R 1 and R 2 are independently a hydrogen atom or a C 1-4 alkane which may be substituted by a halogen atom n is an integer from 1 to 4; and when n is an integer from 2 to 4, n R 1 and n R 2 may be the same or different;
  • the molar ratio of the formaldehyde compound to the alkanedisulfonic acid is (1 - 1.3): 1.
  • Formaldehyde compound Do not use too much, otherwise it will increase the moisture content of the final product, so the molar ratio to the alkanedisulfonic acid should be controlled to be (1-1.3):1.
  • the reaction temperature was controlled to be less than 100 ° C, and the atmospheric pressure reaction time was 1-2 h.
  • the reaction temperature is controlled to be less than 100 ° C in order to better remove moisture, and to prevent the partial contact of the methylene disulfonate compound caused by condensation after evaporation of water to entrap moisture into the crystal, resulting in an increase in the moisture content of the product.
  • the three-stage temperature control method is adopted in the reaction process.
  • the temperature in the first stage is the lowest, the temperature in the third stage is second, and the temperature in the second stage is the highest. Specifically: the temperature is controlled at 20-30 ° C for 15-20 min, then the temperature is controlled at 50-90 ° C for 30-50 min, then the temperature is controlled at 30-50 ° C for 20-25 min, but the temperature of the third stage is higher than the first The height of one stage is lower than that of the second stage.
  • the low temperature reaction at 20-30 °C is to make the reaction process mild, avoiding the reaction being too intense at high temperature, causing by-product formation and water doping, which acts as a buffer; then controlling the high temperature reaction at 50-90 °C is In order to promote the reaction, the conversion rate is accelerated; finally, at a low temperature of 30-50 ° C, it is a slowing process of the reaction, allowing it to stabilize the continuous reaction, while the final stage of cooling can prevent the cooling time from being long and the temperature difference is large after the reaction is completed.
  • the crystal encapsulates moisture defects. Three-stage temperature control can greatly shorten the response
  • the molar ratio of the dehydrating agent to the alkanedisulfonic acid is (1-1.3):1.
  • the neutral dehydrating agent is selected from one or a combination of anhydrous magnesium sulfate, anhydrous sodium sulfate, anhydrous calcium sulfate, molecular sieves, and silica gel.
  • the formaldehyde compound is selected from the group consisting of paraformaldehyde, anhydrous formaldehyde, and three One or several combinations of alkane.
  • the mixture containing the methylene disulfonate compound is separated by adding an extractant thereto for extraction, and then the extract is subjected to decolorization, suction filtration, concentration, crystallization, and drying to obtain a methylene disulfonate compound.
  • the extracting agent is a mixture of one or more of dichloromethane, chloroform, carbon tetrachloride, ethyl acetate, methyl acetate and isopropyl acetate, and the mass ratio of the extracting agent to the alkanedisulfonic acid is (4-10): 1.
  • the amount of extractant is the key to achieve the extraction effect. Too little will make the extraction incomplete, resulting in low yield; too much will increase the difficulty and time of subsequent extraction agent, and will also cause partial hydrolysis, affecting the yield and quality of the product. .
  • the crystallization is carried out by continuous cooling, and is kept at -10 to -15 ° C for 10-15 minutes, and then cooled to -30 to -40 ° C at a rate of 1-2 ° C / min to complete crystallization.
  • the control of the crystallization mode and conditions of the present invention is to prevent entrapment of water during the crystallization process, resulting in an increase in moisture content and affecting the properties and properties of the product.
  • the method for producing the methylene disulfonate compound has the advantages of low cost and remarkable economic benefit; the reaction process is mild and stable; the alkanedisulfonic acid can be solid or liquid, and the reactant can be directly reacted or in the solvent.
  • the reaction is carried out in a simple and easy process.
  • the advantage of the reaction yield of the alkanedisulfonic acid and the formaldehyde compound is more than 75%, and the yield is improved by more than 25% compared with the prior art, and a qualitative leap is achieved.
  • the acid value and moisture content are also greatly reduced, and this effect causes the flatulence and bulging of the battery to be lowered.
  • the invention particularly emphasizes the use of a neutral dehydrating agent, which is to promote the reaction and increase the conversion rate on the one hand, and to combine with water if an acidic dehydrating agent such as phosphorus pentoxide is used in our research.
  • an acidic dehydrating agent such as phosphorus pentoxide
  • the important reason that the low can only reach about 50% (such as the patent document with the application number of 200780014629.X), the micro-environment is easily overlooked, and the seemingly insignificant influence is very large.
  • the present invention particularly emphasizes that the molar ratio of the formaldehyde compound to the alkanedisulfonic acid is ⁇ 1, and the amount of the formaldehyde must be excessive.
  • the purpose is not to complete the reaction of the alkanedisulfonic acid, but to create a disulfonic acid.
  • the stable presence of the methyl ester compound avoids the problem of yield reduction due to hydrolysis of the methylene disulfonate compound and avoids an increase in the acid value. If the amount of the alkanedisulfonic acid is excessive, the above effect cannot be achieved.
  • the nuclear magnetic spectrum is 1 H-NMR (400 MHz, CD3CN) ⁇ (ppm): 5.72 (s, 2H), 2.33 (s, 4H), 1.33 (s, 4H) 0.90 (s, 6H).
  • the moisture content was measured to be 15 ppm and the acid value was 17 ppm.
  • Example 2 Compared with Example 1, an acidic catalyst such as phosphorus pentoxide was used, and the other conditions were the same, and 996.4 g of a product was obtained, the calculated yield was 53%, the detected moisture content was 58 ppm, and the acid value was 70 ppm.
  • an acidic catalyst such as phosphorus pentoxide was used, and the other conditions were the same, and 996.4 g of a product was obtained, the calculated yield was 53%, the detected moisture content was 58 ppm, and the acid value was 70 ppm.
  • Example 2 Compared with Example 1, 1760 g (10 mol) of methanedisulfonic acid and 261 g (8 mol) of 92% paraformaldehyde were added, and the other conditions were the same, 821.2 g of the product was obtained, the calculated yield was 54.6%, and the detected moisture content was 60 ppm. The acid value is 80 ppm.
  • the obtained filtrate was concentrated to obtain crystals, and the obtained crystals were dried at 40 ° C and 10 mmHg for 6 hours to obtain 4.7 g of methylene methanesulfonate methane as a pale brown crystal.
  • the yield was 50%, the detected moisture content was 65 ppm, and the acid value was 86 ppm. .
  • the obtained filtrate was concentrated to obtain crystals, and the obtained crystals were dried at 40 ° C and 10 mmHg for 6 hours to obtain 7.0 g of light brown crystals of methylene chloride of 1,2-ethanedisulfonate, the calculated yield was 69.2%, and the detected moisture content was 73 ppm. , acid value of 90ppm.
  • the development and application of battery additives is to improve and improve the performance of the battery.
  • the acid value and moisture content of the additive affect the performance of the battery, which also affects the life of the electrolyte. If the acid value and moisture content are high, it is easy to cause acid hydrolysis and deterioration. The gas is scrapped and affects the high and low temperature stability of the battery.
  • the methylene disulfonate compound prepared above is added as an additive to the same electrolyte in the same amount, and the performance of the battery is tested for comparison and verification.
  • the diaphragm is made of ceramic diaphragm to form a soft pack battery. After injecting the electrolyte, it is assembled into a soft pack battery in the glove box, and it is tested after standing for 8 hours. The application performance was tested and the results were as follows.
  • the battery was activated by charging and discharging at a temperature of 25 ° C at a constant temperature of 25 ° C, respectively, and then charged and discharged at 1 °C under a cycle of 45 ° C.
  • the cycle test results are shown in Table 1.
  • Battery discharge retention rate at different rates discharge the battery to 3.0V with a constant current of 0.5C, and put it on hold 5min, then charged to a voltage of 4.5V or more with a constant current of 0.5C, and charged at a constant voltage, the current is 0.05C, left for 5min, and then discharged at a constant current of 0.2C, 1C, 1.5C, 2C to a voltage of 3.0V.
  • battery high-temperature storage performance evaluation 60 ° C / 30D and 85 ° C / 7D storage performance test, the following list 3 is the battery after the standard charge and discharge, then stored at 60 ° C for 30 days and 85 ° C for 7 days, then measure the battery capacity retention Rate and capacity recovery rate.
  • Table 4 battery low-temperature storage performance evaluation; Table 4 is to put the battery in the low temperature box, separately controlled The temperature was -30 ° C or -40 ° C, the hold time was 240 min, and then the capacity retention of the battery was measured.

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Abstract

The present invention discloses a method for synthesizing a methylene disulfonate compound, which is related to the technical field of battery electrolyte additives. The methylene disulfonate compound is synthesized by reacting an alkanedisulfonic acid with a formaldehyde compound in the presence of a dehydrating agent. The dehydrating agent is a neutral dehydrating agent. The alkanedisulfonic acid is a sulfonic acid compound represented by formula I. The molar ratio of the formaldehyde compound to the alkanedisulfonic acid is ≥1, in which R1 and R2 are independently a hydrogen atom, a C1-C4 alkyl optionally substituted with a halogen atom, n is an integer from 1 to 4, and when n is an integer from 2 to 4, n instances of R1 and n instances of R2 may be the same or different. The synthesis method of the present invention is simple and high in yield. The product has a high purity, low moisture content, and low acid value. The product can drastically increase the performance of a battery electrolyte.

Description

一种二磺酸亚甲酯化合物的合成方法Method for synthesizing a methylene disulfonate compound 技术领域Technical field
本发明属于电池电解液添加剂的技术领域,涉及一种电池电解液添加剂二磺酸亚甲酯类化合物,具体涉及该类二磺酸亚甲酯化合物的合成方法。本发明合成方法简单,收率高,所得产品纯度高,水分含量少,酸值低,应用到电池电解液中可大大改善电解液的性能。The invention belongs to the technical field of battery electrolyte additives, and relates to a battery electrolyte additive, a methylene disulfonate compound, and particularly relates to a method for synthesizing a methylene disulfonate compound. The synthesis method of the invention is simple, the yield is high, the obtained product has high purity, low moisture content and low acid value, and the application to the battery electrolyte can greatly improve the performance of the electrolyte.
背景技术Background technique
二磺酸亚甲酯化合物可用作治疗动物中白血病等的药物制剂,结构中所含有的磺酸基团,在一定条件下可以与醇、酚、硫醇等基团反应,其独特的结构在合成杂环药物中有着巨大的作用。近年来,随着新能源技术的发展,二磺酸亚甲酯化合物在锂电池电解液添加剂的应用也逐渐的开发出来,二磺酸亚甲酯化合物用于锂电池电解液添加剂,可以显著的改善电池性能,增加电池的可重复充电次数以及循环特性。但是现有方法制备的二磺酸亚甲酯化合物水分含量和酸值偏高,应用到电池中造成电解液分解、胀气和鼓包,严重的不仅不能起到改善电池性能的作用,反而还会显著降低电池的性能,因此,所加添加剂的水分含量和酸值必须严格控制。The methylene disulfonate compound can be used as a pharmaceutical preparation for treating leukemia and the like in animals, and the sulfonic acid group contained in the structure can react with alcohol, phenol, thiol and the like under certain conditions, and its unique structure. It has a huge role in the synthesis of heterocyclic drugs. In recent years, with the development of new energy technologies, the application of methylene disulfonate compounds in lithium battery electrolyte additives has been gradually developed. The methylene disulfonate compound is used in lithium battery electrolyte additives, which can be remarkable. Improve battery performance, increase battery rechargeability and cycle characteristics. However, the moisture content and acid value of the methylene disulfonate compound prepared by the prior method are relatively high, and are applied to the battery to cause decomposition, flatulence and bulging of the electrolyte, which not only fails to improve the performance of the battery, but also significantly The performance of the battery is lowered, and therefore, the moisture content and acid value of the added additive must be strictly controlled.
现有的制备二磺酸亚甲酯化合物的方法包括几种下述方法:Existing methods for preparing methylene disulfonate compounds include several of the following methods:
(1)先采用磺酰氯与碳酸银反应得到磺酸银,之后磺酸银与二碘甲烷反应,R为氢原子或甲基:(1) First, a sulfonyl chloride is reacted with silver carbonate to obtain silver sulfonate, and then silver sulfonate is reacted with diiodomethane, and R is a hydrogen atom or a methyl group:
Figure PCTCN2017111504-appb-000001
Figure PCTCN2017111504-appb-000001
然而,这种方法使用的原料碳酸银和二碘甲烷昂贵且反应慢、收率低。However, the raw materials used in this method are expensive and slow in reaction with silver carbonate and diiodomethane, and the yield is low.
(2)采用烷烃二磺酸等与二乙酸亚甲酯等反应,R'与R"独立地为氢原子或烷基:(2) Alkane disulfonic acid or the like is reacted with methylene diacetate or the like, and R' and R" are independently a hydrogen atom or an alkyl group:
Figure PCTCN2017111504-appb-000002
Figure PCTCN2017111504-appb-000002
然而,这种制造方法采用的原料二乙酸亚甲酯非常昂贵且不容易获得,并且另外作为原料的烷烃二磺酸也昂贵影响其在工业领域的应用。However, the raw material diacetate used in this production method is very expensive and not easily available, and the alkane disulfonic acid which is additionally used as a raw material is also expensive to affect its industrial application.
(3)在脱水剂的存在下使甲醛化合物与选自各自由特定式表示的烷烃二磺酸碱金属盐(如式1)和烷烃二磺酸碱土金属盐(如式2)的至少一种烷烃二磺酸盐反应:(3) at least one of a formaldehyde compound and an alkali metal salt of an alkanedisulfonate (such as Formula 1) and an alkane disulfonate alkaline earth metal salt (such as Formula 2) each represented by a specific formula in the presence of a dehydrating agent. Alkane disulfonate reaction:
Figure PCTCN2017111504-appb-000003
Figure PCTCN2017111504-appb-000003
该方法在一定程度上降低了生产成本,但是使用的两种原料烷烃二磺酸碱金属盐(如式1)和烷烃二磺酸碱土金属盐(如式2)依旧价格昂贵且不易获得。This method reduces the production cost to some extent, but the two raw materials of the alkane disulfonic acid alkali metal salt (such as Formula 1) and the alkane disulfonate alkaline earth metal salt (such as Formula 2) are still expensive and difficult to obtain.
(4)在脱水剂的存在下使甲醛化合物与链烷二磺酸反应制备:(4) Preparing a formaldehyde compound with an alkanedisulfonic acid in the presence of a dehydrating agent:
Figure PCTCN2017111504-appb-000004
Figure PCTCN2017111504-appb-000004
该种方法在一定程度上降低了生产成本,但是收率低,仅能达到50%左右, 且所得产物的水分含量高、酸值高,影响应用到电池中的性能,没有工业价值。This method reduces the production cost to a certain extent, but the yield is low and can only reach about 50%. Moreover, the obtained product has high moisture content and high acid value, affecting the performance applied to the battery, and has no industrial value.
发明内容Summary of the invention
本发明为解决上述问题,提供了一种二磺酸亚甲酯化合物的合成方法,合成过程温和稳定,大大提高了收率和产品质量。本发明所述二磺酸亚甲酯化合物的结构式如下II所示:R1和R2独立地为氢原子或者氢原子可以被卤素原子取代的C1-4烷基;n为1至4的整数;并且当n为2至4的整数时,n个R1和n个R2可以相同或不同;In order to solve the above problems, the present invention provides a method for synthesizing a methylene disulfonate compound, which has a mild and stable synthesis process, and greatly improves the yield and product quality. The structural formula of the methylene disulfonate compound of the present invention is as shown in the following II: R 1 and R 2 are independently a hydrogen atom or a C 1-4 alkyl group in which a hydrogen atom may be substituted by a halogen atom; n is 1 to 4 An integer; and when n is an integer from 2 to 4, n R 1 and n R 2 may be the same or different;
Figure PCTCN2017111504-appb-000005
Figure PCTCN2017111504-appb-000005
本发明为实现其目的采用的技术方案是:The technical solution adopted by the present invention for achieving the purpose is:
一种二磺酸亚甲酯化合物的合成方法,在脱水剂存在下,采用链烷二磺酸与甲醛类化合物反应合成,所述脱水剂采用中性脱水剂,所述链烷二磺酸采用式I结构的磺酸化合物,控制甲醛类化合物与链烷二磺酸的摩尔比≥1;其中,R1和R2独立地为氢原子或者氢原子可以被卤素原子取代的C1-4烷基;n为1至4的整数;并且当n为2至4的整数时,n个R1和n个R2可以相同或不同;A method for synthesizing a methylene disulfonate compound, which is synthesized by reacting an alkanedisulfonic acid with a formaldehyde compound in the presence of a dehydrating agent, wherein the dehydrating agent is a neutral dehydrating agent, and the alkane disulfonic acid is used. The sulfonic acid compound of the formula I, controlling the molar ratio of the formaldehyde compound to the alkanedisulfonic acid ≥1; wherein R 1 and R 2 are independently a hydrogen atom or a C 1-4 alkane which may be substituted by a halogen atom n is an integer from 1 to 4; and when n is an integer from 2 to 4, n R 1 and n R 2 may be the same or different;
Figure PCTCN2017111504-appb-000006
Figure PCTCN2017111504-appb-000006
甲醛类化合物与链烷二磺酸的摩尔比为(1-1.3):1。甲醛类化合物的 用量不宜过多,否则会造成最终产物水分含量的增多,因此需控制在与链烷二磺酸的摩尔比为(1-1.3):1。The molar ratio of the formaldehyde compound to the alkanedisulfonic acid is (1 - 1.3): 1. Formaldehyde compound Do not use too much, otherwise it will increase the moisture content of the final product, so the molar ratio to the alkanedisulfonic acid should be controlled to be (1-1.3):1.
控制反应温度小于100℃,常压反应时间为1-2h。将反应温度控制在小于100℃是为了更好的除去水分,防止因水分蒸发后冷凝造成的局部与其接触的二磺酸亚甲酯化合物将水分包裹到晶体中,造成产物水分含量升高。The reaction temperature was controlled to be less than 100 ° C, and the atmospheric pressure reaction time was 1-2 h. The reaction temperature is controlled to be less than 100 ° C in order to better remove moisture, and to prevent the partial contact of the methylene disulfonate compound caused by condensation after evaporation of water to entrap moisture into the crystal, resulting in an increase in the moisture content of the product.
反应过程中采用三段式控温方式,第一阶段的温度最低,第三阶段的温度次之,第二阶段温度最高。具体为:先将温度控制在20-30℃反应15-20min,然后控制温度50-90℃反应30-50min,然后控制温度30-50℃反应20-25min,但是第三阶段的温度要比第一阶段的高,比第二阶段的低。先20-30℃低温反应是为了让反应过程温和,避免一下子就在高温下反应过于剧烈,造成副产物生成和水分的掺杂,起到缓冲的作用;再控制50-90℃高温反应是为了促进反应进行,加快转化速率;最后在30-50℃低温,是对反应的一个放缓过程,让其稳定持续的反应,同时最后一阶段降温可以防止反应结束后冷却时间长、温差大造成晶体包裹水分的缺陷。三段式控温,可大大缩短反应挥洒件The three-stage temperature control method is adopted in the reaction process. The temperature in the first stage is the lowest, the temperature in the third stage is second, and the temperature in the second stage is the highest. Specifically: the temperature is controlled at 20-30 ° C for 15-20 min, then the temperature is controlled at 50-90 ° C for 30-50 min, then the temperature is controlled at 30-50 ° C for 20-25 min, but the temperature of the third stage is higher than the first The height of one stage is lower than that of the second stage. The low temperature reaction at 20-30 °C is to make the reaction process mild, avoiding the reaction being too intense at high temperature, causing by-product formation and water doping, which acts as a buffer; then controlling the high temperature reaction at 50-90 °C is In order to promote the reaction, the conversion rate is accelerated; finally, at a low temperature of 30-50 ° C, it is a slowing process of the reaction, allowing it to stabilize the continuous reaction, while the final stage of cooling can prevent the cooling time from being long and the temperature difference is large after the reaction is completed. The crystal encapsulates moisture defects. Three-stage temperature control can greatly shorten the response
脱水剂与链烷二磺酸的摩尔比为(1-1.3):1。The molar ratio of the dehydrating agent to the alkanedisulfonic acid is (1-1.3):1.
所述中性脱水剂选自无水硫酸镁、无水硫酸钠、无水硫酸钙、分子筛、硅胶中的一种或几种组合。The neutral dehydrating agent is selected from one or a combination of anhydrous magnesium sulfate, anhydrous sodium sulfate, anhydrous calcium sulfate, molecular sieves, and silica gel.
所述的甲醛类化合物选自多聚甲醛、无水甲醛、三
Figure PCTCN2017111504-appb-000007
烷中的一种或几种组合。
The formaldehyde compound is selected from the group consisting of paraformaldehyde, anhydrous formaldehyde, and three
Figure PCTCN2017111504-appb-000007
One or several combinations of alkane.
对含有二磺酸亚甲酯化合物的混合物进行分离具体为:向其中加入萃取剂进行萃取,然后将萃取液经脱色、抽滤、浓缩、结晶、干燥,得到二磺酸亚甲酯化合物。 The mixture containing the methylene disulfonate compound is separated by adding an extractant thereto for extraction, and then the extract is subjected to decolorization, suction filtration, concentration, crystallization, and drying to obtain a methylene disulfonate compound.
萃取剂采用二氯甲烷、三氯甲烷、四氯化碳、乙酸乙酯、乙酸甲酯、乙酸异丙酯中的一种或几种的混合物,萃取剂与链烷二磺酸的质量比为(4-10):1。萃取剂的用量是实现萃取效果的关键,过少会使萃取不彻底,造成收率低;过多会增加后续除萃取剂的难度和时间,也会造成部分水解,影响产品的收率和品质。The extracting agent is a mixture of one or more of dichloromethane, chloroform, carbon tetrachloride, ethyl acetate, methyl acetate and isopropyl acetate, and the mass ratio of the extracting agent to the alkanedisulfonic acid is (4-10): 1. The amount of extractant is the key to achieve the extraction effect. Too little will make the extraction incomplete, resulting in low yield; too much will increase the difficulty and time of subsequent extraction agent, and will also cause partial hydrolysis, affecting the yield and quality of the product. .
结晶时采用连续降温的方式,先于-10~-15℃保温10-15分钟,然后以1-2℃/min的速率降温至-30~-40℃,完成结晶。本发明结晶方式和条件的控制,是为了防止在结晶的过程中包裹进水,造成水分含量升高,影响产物的性质和性能。The crystallization is carried out by continuous cooling, and is kept at -10 to -15 ° C for 10-15 minutes, and then cooled to -30 to -40 ° C at a rate of 1-2 ° C / min to complete crystallization. The control of the crystallization mode and conditions of the present invention is to prevent entrapment of water during the crystallization process, resulting in an increase in moisture content and affecting the properties and properties of the product.
本发明的有益效果是:The beneficial effects of the invention are:
本发明方法生产二磺酸亚甲酯化合物的成本低,经济效益显著;反应过程中温和稳定;链烷二磺酸可以是固体,也可以是液体,反应物可直接发生反应,也可在溶剂中进行反应,工艺过程简单易操作。实现了以链烷二磺酸与甲醛类化合物反应收率达75%以上的优势,相比现有技术收率提高25%以上,取得了质的飞跃。酸值和水分含量也大幅度降低,该效果使得电池的胀气和鼓包现象降低。The method for producing the methylene disulfonate compound has the advantages of low cost and remarkable economic benefit; the reaction process is mild and stable; the alkanedisulfonic acid can be solid or liquid, and the reactant can be directly reacted or in the solvent. The reaction is carried out in a simple and easy process. The advantage of the reaction yield of the alkanedisulfonic acid and the formaldehyde compound is more than 75%, and the yield is improved by more than 25% compared with the prior art, and a qualitative leap is achieved. The acid value and moisture content are also greatly reduced, and this effect causes the flatulence and bulging of the battery to be lowered.
本发明特别强调要用中性脱水剂,这么做一方面是为了促进反应的进行,提高转化率;另一方面是经我们研究,如果采用酸性脱水剂比如五氧化二磷等,那么与水结合后形成微酸环境,这将导致所合成的二磺酸亚甲酯化合物发生一定程度的水解,最终导致收率的下降,这也是为什么现有技术采用甲醛化合物与链烷二磺酸合成收率低只能达到50%左右的重要原因(比如申请号为200780014629.X的专利文献),该微环境很容易被忽略,看似不起眼影响却很大,目前也没有见对这方面的研究,现有技术未发现 该关键性原因,同时酸性脱水剂的使用还会使所合成的二磺酸亚甲酯化合物酸值偏高,影响在电池中的使用性能;如果采用碱性脱水剂,不仅会抑制正反应的进行,而且还会发生磺酸化合物与碱性物质的副反应,严重影响产品的收率和品质。The invention particularly emphasizes the use of a neutral dehydrating agent, which is to promote the reaction and increase the conversion rate on the one hand, and to combine with water if an acidic dehydrating agent such as phosphorus pentoxide is used in our research. After formation of a slightly acidic environment, this will lead to a certain degree of hydrolysis of the synthesized methylene disulfonate compound, which ultimately leads to a decrease in yield, which is why the prior art uses a formaldehyde compound and an alkanedisulfonic acid to synthesize a yield. The important reason that the low can only reach about 50% (such as the patent document with the application number of 200780014629.X), the micro-environment is easily overlooked, and the seemingly insignificant influence is very large. At present, there is no research on this aspect. Prior art has not been found The key reason, at the same time, the use of acidic dehydrating agent will also make the synthesized acid value of the methylene disulfonate compound higher, affecting the performance in the battery; if the alkaline dehydrating agent is used, it will not only inhibit the positive reaction. It is carried out, and a side reaction of the sulfonic acid compound with the alkaline substance may occur, which seriously affects the yield and quality of the product.
本发明特别强调要控制甲醛类化合物与链烷二磺酸的摩尔比≥1,必须是甲醛类物质过量,该目的并不是为了让链烷二磺酸反应完全,而是为了营造二磺酸亚甲酯化合物的稳定存在环境,可避免因二磺酸亚甲酯化合物水解而造成的收率降低问题,避免酸值的升高。如果是链烷二磺酸过量则是不能实现上述效果的,链烷二磺酸过量会导致部分二磺酸亚甲酯化合物水解,破坏二磺酸亚甲酯化合物的稳定环境,且链烷二磺酸过量会造成酸值偏高。这也是为什么现有技术收率低、酸值高的原因。The present invention particularly emphasizes that the molar ratio of the formaldehyde compound to the alkanedisulfonic acid is ≥1, and the amount of the formaldehyde must be excessive. The purpose is not to complete the reaction of the alkanedisulfonic acid, but to create a disulfonic acid. The stable presence of the methyl ester compound avoids the problem of yield reduction due to hydrolysis of the methylene disulfonate compound and avoids an increase in the acid value. If the amount of the alkanedisulfonic acid is excessive, the above effect cannot be achieved. The excess of the alkanedisulfonic acid causes the partial hydrolysis of the methylene disulfonate compound to destroy the stable environment of the methylene disulfonate compound, and the alkane II An excess of sulfonic acid will result in a high acid value. This is also the reason why the prior art has a low yield and a high acid value.
具体实施方式Detailed ways
下面结合具体实施例对本发明进行进一步的说明。The invention will now be further described in conjunction with specific embodiments.
一、具体实施例First, the specific embodiment
实施例1Example 1
在装有搅拌器、冷凝器和温度计的反应釜中,加入1760g(10mol)甲二磺酸和1204g(10mol)无水硫酸镁,在室温和搅拌下向其中加入359g(11mol)92%的多聚甲醛,添加完毕后,保持搅拌,先将温度控制在20-30℃反应15min,然后控制温度50-90℃反应30min,然后控制温度35-45℃反应20min,冷却至室温,向其中加入7050g二氯甲烷进行萃取,所的萃取液加入活性炭脱色,然后抽滤、浓缩,置于-10℃保温10min,然后以1℃/min的速率降温至-30℃,完成结晶,过滤,减压烘干,得到1447.6g类白色晶体甲烷二磺酸亚甲酯,计算其收率为77%。核磁图谱1H-NMR(400MHz,CD3CN) δ(ppm):5.33(s,2H),6.00(s,2H)。检测其水分含量10ppm,酸值15ppm。In a reaction vessel equipped with a stirrer, a condenser and a thermometer, 1760 g (10 mol) of methanedisulfonic acid and 1204 g (10 mol) of anhydrous magnesium sulfate were added, and 359 g (11 mol) of 92% was added thereto at room temperature with stirring. POM, after the addition is completed, keep stirring, first control the temperature at 20-30 ° C for 15 min, then control the temperature 50-90 ° C reaction for 30 min, then control the temperature 35-45 ° C reaction 20min, cool to room temperature, add 7050g Dichloromethane is extracted, the extract is decolorized by adding activated carbon, then filtered, concentrated, placed at -10 ° C for 10 min, then cooled to -30 ° C at a rate of 1 ° C / min, complete crystallization, filtration, drying under reduced pressure Dry, 1447.6 g of an off-white crystal methane methanesulfonate was obtained, and the yield was calculated to be 77%. Nuclear magnetic spectrum 1H-NMR (400MHz, CD3CN) δ (ppm): 5.33 (s, 2H), 6.00 (s, 2H). The moisture content was measured to be 10 ppm and the acid value was 15 ppm.
实施例2Example 2
在装有搅拌器、冷凝器和温度计的反应釜中,加入1900g(10mol)1,2-乙烷二磺酸和1846g(13mol)无水硫酸钠,在室温和搅拌下向其中加入423g(13mol)92%的多聚甲醛,添加完毕后,保持搅拌,先将温度控制在23-25℃反应20min,然后控制温度60-80℃反应40min,然后控制温度30-40℃反应25min,冷却至室温,向其中加入9500g三氯甲烷(可替换成同质量的四氯化碳、乙酸乙酯、乙酸甲酯、乙酸异丙酯中的一种或多种)进行萃取,所的萃取液加入活性炭脱色,然后抽滤、浓缩,置于-15℃保温15min,然后以2℃/min的速率降温至-40℃,完成结晶,过滤,减压烘干,得到1585.7g类白色晶体1,2-乙烷二磺酸亚甲酯,计算其收率为78.5%。核磁图谱1H-NMR(400MHz,CD3CN)δ(ppm):3.83(s,4H),5.63(s,2H)。检测其水分含量13ppm,酸值15ppm。In a reaction vessel equipped with a stirrer, a condenser and a thermometer, 1900 g (10 mol) of 1,2-ethanedisulfonic acid and 1846 g (13 mol) of anhydrous sodium sulfate were added, and 423 g (13 mol) was added thereto at room temperature with stirring. 92% paraformaldehyde, after the addition, keep stirring, first control the temperature at 23-25 ° C for 20min, then control the temperature 60-80 ° C reaction for 40min, then control the temperature 30-40 ° C reaction for 25min, cool to room temperature Adding 9500 g of chloroform (which can be replaced by one or more of the same mass of carbon tetrachloride, ethyl acetate, methyl acetate, and isopropyl acetate) for extraction, and the extract is added to the activated carbon for decolorization. Then, suction filtration, concentration, incubated at -15 ° C for 15 min, then cooled to -40 ° C at a rate of 2 ° C / min, complete crystallization, filtration, drying under reduced pressure, to obtain 1585.7 g white crystals 1,2-B Methyl alkanedisulfonate was calculated to have a yield of 78.5%. Nuclear magnetic spectrum 1H-NMR (400 MHz, CD3CN) δ (ppm): 3.83 (s, 4H), 5.63 (s, 2H). The moisture content was 13 ppm and the acid value was 15 ppm.
实施例3Example 3
在装有搅拌器、冷凝器和温度计的反应釜中,加入2600g(10mol)4,4-二丙基甲烷二磺酸和1440g(12mol)无水硫酸镁(可替换成等摩尔的无水硫酸钠、无水硫酸钙、分子筛、硅胶的一种或多种),在室温和搅拌下向其中加入326g(10mol)92%的多聚甲醛(可替换成等摩尔的无水甲醛或三
Figure PCTCN2017111504-appb-000008
烷),添加完毕后,保持搅拌,先将温度控制在25-28℃反应18min,然后控制温度70-90℃反应50min,然后控制温度40-50℃反应20min,冷却至室温,向其中加入26000g四氯化碳进行萃取,所的萃取液加入活性炭脱色,然后抽滤、浓缩,置于-13℃保温13min,然后以1.5℃/min的速率降温至-35℃,完成结晶,过滤,40℃、10mmHg下干燥3h,得到晶体2110.7g,即4,4-二丙 基甲烷二磺酸亚甲酯,计算其收率为77.6%。核磁图谱为1H-NMR(400MHz,CD3CN)δ(ppm):5.72(s,2H),2.33(s,4H),1.33(s,4H)0.90(s,6H)。检测其水分含量15ppm,酸值17ppm。
In a reaction vessel equipped with a stirrer, a condenser and a thermometer, 2600 g (10 mol) of 4,4-dipropylmethanedisulfonic acid and 1440 g (12 mol) of anhydrous magnesium sulfate (which can be replaced with an equimolar anhydrous sulfuric acid) Sodium, anhydrous calcium sulfate, molecular sieve, one or more of silica gel), 326g (10mol) of 92% paraformaldehyde (can be replaced by equimolar anhydrous formaldehyde or three) at room temperature and stirring
Figure PCTCN2017111504-appb-000008
Alkane), after the addition, keep stirring, first control the temperature at 25-28 ° C for 18min, then control the temperature 70-90 ° C reaction for 50min, then control the temperature 40-50 ° C reaction 20min, cool to room temperature, add 26000g The carbon tetrachloride is extracted, the extract is decolorized by adding activated carbon, then filtered, concentrated, placed at -13 ° C for 13 min, then cooled to -35 ° C at a rate of 1.5 ° C / min, complete crystallization, filtration, 40 ° C After drying at 10 mmHg for 3 hours, 2110.7 g of crystals, that is, methylene methyl 4,4-dipropylmethanedisulfonate, was obtained, and the yield was calculated to be 77.6%. The nuclear magnetic spectrum is 1 H-NMR (400 MHz, CD3CN) δ (ppm): 5.72 (s, 2H), 2.33 (s, 4H), 1.33 (s, 4H) 0.90 (s, 6H). The moisture content was measured to be 15 ppm and the acid value was 17 ppm.
对比例1Comparative example 1
与实施例1相比,采用酸性催化剂如五氧化二磷,其余条件相同,获得产品996.4g,计算收率为53%,检测水分含量为58ppm,酸值70ppm。Compared with Example 1, an acidic catalyst such as phosphorus pentoxide was used, and the other conditions were the same, and 996.4 g of a product was obtained, the calculated yield was 53%, the detected moisture content was 58 ppm, and the acid value was 70 ppm.
对比例2Comparative example 2
与实施例1相比,加入1760g(10mol)甲二磺酸、261g(8mol)92%的多聚甲醛,其余条件相同,获得产品821.2g,计算收率为54.6%,检测水分含量为60ppm,酸值80ppm。Compared with Example 1, 1760 g (10 mol) of methanedisulfonic acid and 261 g (8 mol) of 92% paraformaldehyde were added, and the other conditions were the same, 821.2 g of the product was obtained, the calculated yield was 54.6%, and the detected moisture content was 60 ppm. The acid value is 80 ppm.
对比例3Comparative example 3
在装有搅拌器、冷凝器和温度计的200ml四颈烧瓶中放置8.8g(0.05mol)甲烷二磺酸和7.1g(0.05mol)五氧化二磷。在室温和搅拌下向混合物中加入1.6g(0.05mol)92%的多聚甲醛。添加完毕后,将混合物加热至120℃并搅拌1h。然后将混合物冷却至室温,向其中加入100g二氯甲烷。搅拌1h之后,过滤出不溶性物质。浓缩所得的滤液得到晶体,在40℃和10mmHg下干燥所得的晶体6h,得到4.7g甲烷二磺酸亚甲酯的浅褐色晶体,计算收率为50%,检测水分含量为65ppm,酸值86ppm。In a 200 ml four-necked flask equipped with a stirrer, a condenser and a thermometer, 8.8 g (0.05 mol) of methane disulfonic acid and 7.1 g (0.05 mol) of phosphorus pentoxide were placed. 1.6 g (0.05 mol) of 92% paraformaldehyde was added to the mixture at room temperature with stirring. After the addition was completed, the mixture was heated to 120 ° C and stirred for 1 h. The mixture was then cooled to room temperature, and 100 g of dichloromethane was added thereto. After stirring for 1 h, the insoluble material was filtered off. The obtained filtrate was concentrated to obtain crystals, and the obtained crystals were dried at 40 ° C and 10 mmHg for 6 hours to obtain 4.7 g of methylene methanesulfonate methane as a pale brown crystal. The yield was 50%, the detected moisture content was 65 ppm, and the acid value was 86 ppm. .
对比例4Comparative example 4
在装有搅拌器、冷凝器和温度计的200ml四颈烧瓶中放置9.5g(0.05mol)1,2-乙烷二磺酸和8.5g(0.06mol)五氧化二磷。在室温和搅拌下向混合物中加入2.0g(0.06mol)92%的多聚甲醛。添加完毕后,将混合物加热至120℃并搅拌1h。然后将混合物冷却至室温,向其中加入100g二 氯甲烷。搅拌1h之后,过滤出不溶性物质。浓缩所得的滤液得到晶体,在40℃和10mmHg下干燥所得的晶体6h,得到7.0g1,2-乙烷二磺酸亚甲酯的浅褐色晶体,计算收率为69.2%,检测水分含量为73ppm,酸值90ppm。In a 200 ml four-necked flask equipped with a stirrer, a condenser and a thermometer, 9.5 g (0.05 mol) of 1,2-ethanedisulfonic acid and 8.5 g (0.06 mol) of phosphorus pentoxide were placed. 2.0 g (0.06 mol) of 92% paraformaldehyde was added to the mixture at room temperature with stirring. After the addition was completed, the mixture was heated to 120 ° C and stirred for 1 h. The mixture was then cooled to room temperature and 100 g of two were added thereto. Methyl chloride. After stirring for 1 h, the insoluble material was filtered off. The obtained filtrate was concentrated to obtain crystals, and the obtained crystals were dried at 40 ° C and 10 mmHg for 6 hours to obtain 7.0 g of light brown crystals of methylene chloride of 1,2-ethanedisulfonate, the calculated yield was 69.2%, and the detected moisture content was 73 ppm. , acid value of 90ppm.
二、应用试验Second, the application test
电池添加剂的开发和应用是为了改善和提高电池的性能,其中添加剂的酸值、水分含量影响电池的性能,同样影响着电解液的寿命,如果酸值和水分含量高易造成酸解变质、鼓气报废,影响电池的高低温稳定性,下面就上述制备的二磺酸亚甲酯化合物作为添加剂以相同的添加量添加到相同的电解液中,检测电池的性能,进行对比和验证。The development and application of battery additives is to improve and improve the performance of the battery. The acid value and moisture content of the additive affect the performance of the battery, which also affects the life of the electrolyte. If the acid value and moisture content are high, it is easy to cause acid hydrolysis and deterioration. The gas is scrapped and affects the high and low temperature stability of the battery. The methylene disulfonate compound prepared above is added as an additive to the same electrolyte in the same amount, and the performance of the battery is tested for comparison and verification.
将上述“一、具体实施例”所得产品添加到基础电解液中,添加量为基础电解液重量的1%,基础电解液的电池的电解液为:DC/EMC=1/3,LiPF6:1.1M FEC,PST,正负极集流体分布为铝箔和铜箔,隔膜采用陶瓷隔膜组成软包电池,注入电解液后,在手套箱中组装成软包电池,静置8小时后进行测试。检测应用性能,结果如下。The product obtained in the above "A. Specific Example" is added to the base electrolyte in an amount of 1% by weight of the base electrolyte, and the electrolyte of the battery of the base electrolyte is: DC/EMC = 1/3, LiPF 6 : 1.1M FEC, PST, the positive and negative current collectors are distributed in aluminum foil and copper foil. The diaphragm is made of ceramic diaphragm to form a soft pack battery. After injecting the electrolyte, it is assembled into a soft pack battery in the glove box, and it is tested after standing for 8 hours. The application performance was tested and the results were as follows.
1、在室温25℃恒温下分别以1/10C 3.0V到4.5V以上进行充放电对电池进行活化,随后在45℃条件下的循环均以1C充放电。循环测试结果见表1。1. The battery was activated by charging and discharging at a temperature of 25 ° C at a constant temperature of 25 ° C, respectively, and then charged and discharged at 1 °C under a cycle of 45 ° C. The cycle test results are shown in Table 1.
表1Table 1
Figure PCTCN2017111504-appb-000009
Figure PCTCN2017111504-appb-000009
2、不同倍率下电池放电保持率:将电池以0.5C恒流放电到3.0V,搁置 5min,然后以0.5C恒流充电到4.5V以上,并恒压充电,截至电流为0.05C,静置5min,再分别以0.2C、1C、1.5C、2C恒流放电至截至电压3.0V。记录0.2C、1C、1.5C、2C条件下的放电容量为D1,记录0.2C下的放电容量为D0,且基于0.2C下的放电容量,通过电池的放电容量保持率=[(D1-D0)/D0]×100%的公式计算得到电池在不同倍率下的放电容量保持率(测15支电池,取其平均值),各个电池在25℃条件,不同倍率下的放电容量保持率如表2所示。2. Battery discharge retention rate at different rates: discharge the battery to 3.0V with a constant current of 0.5C, and put it on hold 5min, then charged to a voltage of 4.5V or more with a constant current of 0.5C, and charged at a constant voltage, the current is 0.05C, left for 5min, and then discharged at a constant current of 0.2C, 1C, 1.5C, 2C to a voltage of 3.0V. Record the discharge capacity under the conditions of 0.2C, 1C, 1.5C, 2C as D1, record the discharge capacity at 0.2C as D0, and based on the discharge capacity at 0.2C, the discharge capacity retention rate through the battery = [(D1-D0) ) / D0] × 100% of the formula to calculate the discharge capacity retention rate of the battery at different rates (measured 15 batteries, take the average), the battery capacity at 25 ° C conditions, the discharge capacity retention rate at different rates as shown 2 is shown.
表2Table 2
Figure PCTCN2017111504-appb-000010
Figure PCTCN2017111504-appb-000010
3、电池高温储存性能评价:60℃/30D和85℃/7D存储性能测试,下列表3是电池经手标准充放电后再60℃存放30天和85℃存放7天,随后测量电池的容量保持率和容量恢复率。3, battery high-temperature storage performance evaluation: 60 ° C / 30D and 85 ° C / 7D storage performance test, the following list 3 is the battery after the standard charge and discharge, then stored at 60 ° C for 30 days and 85 ° C for 7 days, then measure the battery capacity retention Rate and capacity recovery rate.
表3table 3
Figure PCTCN2017111504-appb-000011
Figure PCTCN2017111504-appb-000011
4、电池低温储存性能评价;下表4是将电池搁置在低温箱中,分别控 制温度为-30℃或-40℃,搁置时间240min,随后测量电池的容量保持率。4, battery low-temperature storage performance evaluation; Table 4 is to put the battery in the low temperature box, separately controlled The temperature was -30 ° C or -40 ° C, the hold time was 240 min, and then the capacity retention of the battery was measured.
表4Table 4
Figure PCTCN2017111504-appb-000012
Figure PCTCN2017111504-appb-000012

Claims (10)

  1. 一种二磺酸亚甲酯化合物的合成方法,在脱水剂存在下,采用链烷二磺酸与甲醛类化合物反应,然后对含有二磺酸亚甲酯化合物的混合物进行分离即得,其特征在于,所述脱水剂采用中性脱水剂,所述链烷二磺酸采用式I结构的磺酸化合物,控制甲醛类化合物与链烷二磺酸的摩尔比≥1;其中,R1和R2独立地为氢原子或者氢原子可以被卤素原子取代的C1-4烷基;n为1至4的整数;并且当n为2至4的整数时,n个R1和n个R2可以相同或不同;A method for synthesizing a methylene disulfonate compound, which is obtained by reacting an alkanedisulfonic acid with a formaldehyde compound in the presence of a dehydrating agent, and then separating the mixture containing the methylene disulfonate compound, and is characterized by Wherein the dehydrating agent is a neutral dehydrating agent, the alkanedisulfonic acid is a sulfonic acid compound of the formula I, and the molar ratio of the formaldehyde compound to the alkanedisulfonic acid is controlled to be ≥1; wherein R 1 and R 2 is independently a C 1-4 alkyl group in which a hydrogen atom or a hydrogen atom may be substituted by a halogen atom; n is an integer of 1 to 4; and when n is an integer of 2 to 4, n R 1 and n R 2 Can be the same or different;
    Figure PCTCN2017111504-appb-100001
    Figure PCTCN2017111504-appb-100001
  2. 根据权利要求1所述的一种二磺酸亚甲酯化合物的合成方法,其特征在于,甲醛类化合物与链烷二磺酸的摩尔比为(1-1.3):1。The method for synthesizing a methylene disulfonate compound according to claim 1, wherein the molar ratio of the formaldehyde compound to the alkanedisulfonic acid is (1 to 1.3):1.
  3. 根据权利要求1所述的一种二磺酸亚甲酯化合物的合成方法,其特征在于,控制反应温度小于100℃,反应时间为1-2h。The method for synthesizing a methylene disulfonate compound according to claim 1, wherein the reaction temperature is controlled to be less than 100 ° C and the reaction time is 1-2 h.
  4. 根据权利要求3所述的一种二磺酸亚甲酯化合物的合成方法,其特征在于,反应过程中采用三段式控温方式,第一阶段的温度最低,第三阶段的温度次之,第二阶段温度最高。The method for synthesizing a methylene disulfonate compound according to claim 3, wherein a three-stage temperature control mode is adopted in the reaction process, wherein the temperature in the first stage is the lowest, and the temperature in the third stage is second. The second stage has the highest temperature.
  5. 根据权利要求1所述的一种二磺酸亚甲酯化合物的合成方法,其特征在于,脱水剂与链烷二磺酸的摩尔比为(1-1.3):1。The method for synthesizing a methylene disulfonate compound according to claim 1, wherein the molar ratio of the dehydrating agent to the alkanedisulfonic acid is (1 to 1.3):1.
  6. 根据权利要求1所述的一种二磺酸亚甲酯化合物的合成方法,其特征在于,所述中性脱水剂选自无水硫酸镁、无水硫酸钠、无水硫酸钙、分子筛、硅胶中的一种或几种组合。The method for synthesizing a methylene disulfonate compound according to claim 1, wherein the neutral dehydrating agent is selected from the group consisting of anhydrous magnesium sulfate, anhydrous sodium sulfate, anhydrous calcium sulfate, molecular sieve, and silica gel. One or several combinations.
  7. 根据权利要求1所述的一种二磺酸亚甲酯化合物的合成方法,其特征在于,所述的甲醛类化合物选自多聚甲醛、无水甲醛、三
    Figure PCTCN2017111504-appb-100002
    烷中的一种 或几种组合。
    The method for synthesizing a methylene disulfonate compound according to claim 1, wherein the formaldehyde compound is selected from the group consisting of paraformaldehyde, anhydrous formaldehyde, and three
    Figure PCTCN2017111504-appb-100002
    One or several combinations of alkanes.
  8. 根据权利要求1所述的一种二磺酸亚甲酯化合物的合成方法,其特征在于,对含有二磺酸亚甲酯化合物的混合物进行分离具体为:向其中加入萃取剂进行萃取,然后将萃取液经脱色、抽滤、浓缩、结晶、干燥,得到二磺酸亚甲酯化合物。The method for synthesizing a methylene disulfonate compound according to claim 1, wherein the separation of the mixture containing the methylene disulfonate compound is carried out by adding an extractant thereto for extraction, and then The extract is subjected to decolorization, suction filtration, concentration, crystallization, and drying to obtain a methylene disulfonate compound.
  9. 根据权利要求1所述的一种二磺酸亚甲酯化合物的合成方法,其特征在于,萃取剂采用二氯甲烷、三氯甲烷、四氯化碳、乙酸乙酯、乙酸甲酯、乙酸异丙酯中的一种或几种的混合物,萃取剂与链烷二磺酸的质量比为(4-10):1。The method for synthesizing a methylene disulfonate compound according to claim 1, wherein the extracting agent is dichloromethane, chloroform, carbon tetrachloride, ethyl acetate, methyl acetate or acetic acid. A mixture of one or more of the propyl esters, the mass ratio of the extractant to the alkanedisulfonic acid is (4-10):1.
  10. 根据权利要求1所述的一种二磺酸亚甲酯化合物的合成方法,其特征在于,结晶时采用连续降温的方式,先于-10~15℃保温10-15分钟,然后以1-2℃/min的速率降温至-30~-40℃,完成结晶。 The method for synthesizing a methylene disulfonate compound according to claim 1, wherein the crystallization is carried out by means of continuous cooling, and the temperature is maintained at -10 to 15 ° C for 10-15 minutes, and then 1-2. The rate of °C/min was lowered to -30 to -40 ° C to complete crystallization.
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