CN1321637A - Preparation method of tellurium diethyl dithiocarbamate - Google Patents
Preparation method of tellurium diethyl dithiocarbamate Download PDFInfo
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- CN1321637A CN1321637A CN 01105884 CN01105884A CN1321637A CN 1321637 A CN1321637 A CN 1321637A CN 01105884 CN01105884 CN 01105884 CN 01105884 A CN01105884 A CN 01105884A CN 1321637 A CN1321637 A CN 1321637A
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- diethyldithiocarbamate
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- 229940116901 diethyldithiocarbamate Drugs 0.000 title claims abstract description 16
- 238000002360 preparation method Methods 0.000 title claims abstract description 7
- ILXWFJOFKUNZJA-UHFFFAOYSA-N ethyltellanylethane Chemical group CC[Te]CC ILXWFJOFKUNZJA-UHFFFAOYSA-N 0.000 title claims abstract 5
- 229910052714 tellurium Inorganic materials 0.000 claims abstract description 42
- PORWMNRCUJJQNO-UHFFFAOYSA-N tellurium atom Chemical compound [Te] PORWMNRCUJJQNO-UHFFFAOYSA-N 0.000 claims abstract description 42
- LMBWSYZSUOEYSN-UHFFFAOYSA-N diethyldithiocarbamic acid Chemical compound CCN(CC)C(S)=S LMBWSYZSUOEYSN-UHFFFAOYSA-N 0.000 claims abstract description 24
- 238000006243 chemical reaction Methods 0.000 claims abstract description 14
- 229950004394 ditiocarb Drugs 0.000 claims abstract description 13
- 238000000034 method Methods 0.000 claims abstract description 13
- 239000003513 alkali Substances 0.000 claims abstract description 9
- 239000012670 alkaline solution Substances 0.000 claims abstract description 8
- HEMHJVSKTPXQMS-UHFFFAOYSA-M sodium hydroxide Inorganic materials [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 41
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 claims description 24
- 239000000243 solution Substances 0.000 claims description 16
- 235000011121 sodium hydroxide Nutrition 0.000 claims description 15
- 235000011118 potassium hydroxide Nutrition 0.000 claims description 8
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 claims description 6
- UIIMBOGNXHQVGW-UHFFFAOYSA-M Sodium bicarbonate Chemical compound [Na+].OC([O-])=O UIIMBOGNXHQVGW-UHFFFAOYSA-M 0.000 claims description 5
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Substances [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 claims description 3
- 229910000029 sodium carbonate Inorganic materials 0.000 claims description 3
- 235000017550 sodium carbonate Nutrition 0.000 claims description 3
- 238000007796 conventional method Methods 0.000 claims description 2
- 239000011541 reaction mixture Substances 0.000 claims description 2
- 235000017557 sodium bicarbonate Nutrition 0.000 claims description 2
- 229910000030 sodium bicarbonate Inorganic materials 0.000 claims description 2
- 239000003795 chemical substances by application Substances 0.000 claims 2
- 239000002253 acid Substances 0.000 claims 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims 1
- 229910052500 inorganic mineral Inorganic materials 0.000 claims 1
- 239000011707 mineral Substances 0.000 claims 1
- 235000010755 mineral Nutrition 0.000 claims 1
- 229910052760 oxygen Inorganic materials 0.000 claims 1
- 239000001301 oxygen Substances 0.000 claims 1
- 235000015320 potassium carbonate Nutrition 0.000 claims 1
- 239000003518 caustics Substances 0.000 abstract description 3
- 239000002994 raw material Substances 0.000 abstract description 2
- 239000002245 particle Substances 0.000 description 7
- 239000000047 product Substances 0.000 description 6
- 238000004519 manufacturing process Methods 0.000 description 5
- 238000002844 melting Methods 0.000 description 5
- 230000008018 melting Effects 0.000 description 5
- 229910003069 TeO2 Inorganic materials 0.000 description 4
- LAJZODKXOMJMPK-UHFFFAOYSA-N tellurium dioxide Chemical compound O=[Te]=O LAJZODKXOMJMPK-UHFFFAOYSA-N 0.000 description 4
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
- 229920002943 EPDM rubber Polymers 0.000 description 3
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 3
- 229920001971 elastomer Polymers 0.000 description 3
- 238000001914 filtration Methods 0.000 description 3
- 125000001449 isopropyl group Chemical group [H]C([H])([H])C([H])(*)C([H])([H])[H] 0.000 description 3
- 238000011017 operating method Methods 0.000 description 3
- 238000005406 washing Methods 0.000 description 3
- 239000000654 additive Substances 0.000 description 2
- 230000000996 additive effect Effects 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- TYJJADVDDVDEDZ-UHFFFAOYSA-M potassium hydrogencarbonate Chemical compound [K+].OC([O-])=O TYJJADVDDVDEDZ-UHFFFAOYSA-M 0.000 description 2
- 239000002244 precipitate Substances 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 150000003497 tellurium Chemical class 0.000 description 2
- 238000001291 vacuum drying Methods 0.000 description 2
- 238000004073 vulcanization Methods 0.000 description 2
- OFDISMSWWNOGFW-UHFFFAOYSA-N 1-(4-ethoxy-3-fluorophenyl)ethanamine Chemical compound CCOC1=CC=C(C(C)N)C=C1F OFDISMSWWNOGFW-UHFFFAOYSA-N 0.000 description 1
- KXDHJXZQYSOELW-UHFFFAOYSA-M Carbamate Chemical compound NC([O-])=O KXDHJXZQYSOELW-UHFFFAOYSA-M 0.000 description 1
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 1
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 1
- LSNNMFCWUKXFEE-UHFFFAOYSA-N Sulfurous acid Chemical compound OS(O)=O LSNNMFCWUKXFEE-UHFFFAOYSA-N 0.000 description 1
- 230000032683 aging Effects 0.000 description 1
- 239000012752 auxiliary agent Substances 0.000 description 1
- 239000007853 buffer solution Substances 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 150000004659 dithiocarbamates Chemical class 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000010292 electrical insulation Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005187 foaming Methods 0.000 description 1
- 150000007522 mineralic acids Chemical class 0.000 description 1
- 239000011259 mixed solution Substances 0.000 description 1
- 229910017604 nitric acid Inorganic materials 0.000 description 1
- 239000008055 phosphate buffer solution Substances 0.000 description 1
- 238000012805 post-processing Methods 0.000 description 1
- 239000011736 potassium bicarbonate Substances 0.000 description 1
- 235000015497 potassium bicarbonate Nutrition 0.000 description 1
- 229910000028 potassium bicarbonate Inorganic materials 0.000 description 1
- 229910000027 potassium carbonate Inorganic materials 0.000 description 1
- 235000011181 potassium carbonates Nutrition 0.000 description 1
- 230000036632 reaction speed Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- XHGGEBRKUWZHEK-UHFFFAOYSA-L tellurate Chemical compound [O-][Te]([O-])(=O)=O XHGGEBRKUWZHEK-UHFFFAOYSA-L 0.000 description 1
Abstract
Description
本发明涉及二乙基二硫代氨基甲酸碲的制备方法。The invention relates to a preparation method of tellurium diethyldithiocarbamate.
二乙基二硫代氨基甲酸碲,简称TDEC,是三元乙丙胶制品生产过程中的添加剂。其结构式为: Tellurium diethyldithiocarbamate, TDEC for short, is an additive in the production process of EPDM rubber products. Its structural formula is:
由于三元乙丙胶具有优秀的耐臭氧、较高的热稳定性(485℃)、好的耐热老化性能、耐气候、耐化学品、耐油以及优秀的电绝缘性能,使其主要用于耐热运输带,电线、电缆、密封垫圈等。二乙基二硫代氨基甲酸碲(TDEC)是属于二硫代氨基甲酸盐类快速硫化促进剂,它不仅可以提高三元乙丙胶的硫化效率,降低能耗,重要的是它可以提高制品的发泡均匀性和机械强度。因此,TDEC是三元异丙胶制品生产中重要的助剂。Because EPDM rubber has excellent ozone resistance, high thermal stability (485°C), good heat aging resistance, weather resistance, chemical resistance, oil resistance and excellent electrical insulation properties, it is mainly used in Heat-resistant conveyor belts, wires, cables, gaskets, etc. Tellurium diethyldithiocarbamate (TDEC) is a rapid vulcanization accelerator belonging to the dithiocarbamate class. It can not only improve the vulcanization efficiency of EPDM rubber, reduce energy consumption, but more importantly, it can improve the quality of products. Excellent foaming uniformity and mechanical strength. Therefore, TDEC is an important additive in the production of ternary isopropyl rubber products.
目前,TDEC一般是通过可溶性的碲盐与二乙基二硫代氨基甲酸钠反应而获得的。但由于可溶性碲盐如亚硫酸碲、四氯化碲等稳定性比较差,很容易水解成氧化碲,在与二乙基二硫代氨基甲酸钠反应时不能得到均匀相的二乙基二硫代氨基甲酸碲。因此,三元异丙胶制品生产过程中由于该助剂中有效组分的减少而使用量增加,使得制品的生产成本提高和资源的浪费。At present, TDEC is generally obtained by reacting soluble tellurium salt with sodium diethyldithiocarbamate. However, due to the poor stability of soluble tellurium salts such as tellurium sulfite and tellurium tetrachloride, they are easily hydrolyzed into tellurium oxide, and diethyldithiocarbamate in a homogeneous phase cannot be obtained when reacting with sodium diethyldithiocarbamate. Tellurium Carbamate. Therefore, in the production process of the ternary isopropyl rubber product, the usage amount increases due to the reduction of the effective components in the auxiliary agent, which increases the production cost of the product and wastes resources.
本发明的目的在于提供一种新的制备二乙基二硫代氨基甲酸碲的方法,该方法将能够获得均匀相的二乙基二硫代氨基甲酸碲,从而可以克服现有技术所存在的上述缺陷。The purpose of the present invention is to provide a new method for preparing tellurium diethyldithiocarbamate, the method will be able to obtain tellurium diethyldithiocarbamate of homogeneous phase, thereby can overcome the existing problems of the prior art the aforementioned deficiencies.
本发明的技术构思是这样的:Technical concept of the present invention is such:
本发明以稳定性好的氧化碲为原料,用苛性碱如氢氧化钠或氢氧化钾溶解氧化碲,然后控制一定的反应条件,将碲的碱溶液与二乙基二硫代氨基甲酸钠反应制备得到均匀相以及颗粒大小均匀的二乙基二硫代氨基甲酸碲。The present invention uses tellurium oxide with good stability as raw material, dissolves tellurium oxide with caustic alkali such as sodium hydroxide or potassium hydroxide, and then controls certain reaction conditions to prepare by reacting tellurium alkaline solution with sodium diethyldithiocarbamate A homogeneous phase and uniform particle size tellurium diethyldithiocarbamate are obtained.
实现本发明目的的技术方案:The technical scheme that realizes the object of the present invention:
本发明所说的方法包括如下步骤:Said method of the present invention comprises the steps:
①碲溶液的制备:① Preparation of tellurium solution:
用碱液溶解氧化碲,使之成为碲的溶液,碱液的浓度为0.1~2moll-1。碱的浓度小于0.1moll-1,氧化碲不能完全溶解在苛性碱溶液中;而大于2moll-1时,形成的碲酸盐易析出,不能得到均匀的碲的碱溶液;Tellurium oxide is dissolved with lye to make a solution of tellurium, and the concentration of lye is 0.1-2moll -1 . When the alkali concentration is less than 0.1moll -1 , tellurium oxide cannot be completely dissolved in the caustic solution; and when it is greater than 2moll -1 , the formed tellurate is easy to precipitate, and a uniform tellurium alkaline solution cannot be obtained;
碲的碱溶液中碲的浓度对下一步的反应并无实质性的影响,但一般以0.02~0.08moll-1为宜;The concentration of tellurium in the alkaline solution of tellurium has no substantial influence on the next reaction, but generally 0.02~0.08moll -1 is appropriate;
所说的碱包括氢氧化钠、氢氧化钾、碳酸钠、碳酸钾、碳酸氢钠或碳酸氢钾中的一种或一种以上;Said alkali includes one or more of sodium hydroxide, potassium hydroxide, sodium carbonate, potassium carbonate, sodium bicarbonate or potassium bicarbonate;
优选的为氢氧化钠或氢氧化钾;Preferred is sodium hydroxide or potassium hydroxide;
②二乙基二硫代氨基甲酸碲的合成:②Synthesis of tellurium diethyldithiocarbamate:
将步骤①所获得的碲的碱溶液与二乙基二硫代氨基甲酸钠进行反应,反应条件如下:The alkali solution of tellurium obtained by step 1. is reacted with sodium diethyldithiocarbamate, and the reaction conditions are as follows:
pH=7~11、反应温度20~80℃;pH=7~11, reaction temperature 20~80℃;
碲的碱溶液与二乙基二硫代氨基甲酸钠反应过程中,控制pH在7~11之间。如pH小于7,二乙基二硫代氨基甲酸钠和碲的碱溶液易分解,不能得到二乙基二硫代氨基甲酸碲;如pH大于11,碲不能完全沉淀,得率下降。During the reaction process of the alkaline solution of tellurium and sodium diethyldithiocarbamate, the pH is controlled between 7 and 11. If the pH is less than 7, the alkaline solution of sodium diethyldithiocarbamate and tellurium is easy to decompose, and tellurium diethyldithiocarbamate cannot be obtained; if the pH is greater than 11, tellurium cannot be completely precipitated, and the yield decreases.
pH的控制可以通过加入pH调节剂来实现,如可以加入pH缓冲溶液、无机酸如盐酸、醋酸、硝酸等;pH control can be achieved by adding a pH regulator, such as adding a pH buffer solution, inorganic acids such as hydrochloric acid, acetic acid, nitric acid, etc.;
反应温度为20~80℃,如反应温度低于20℃,反应不能完全,TDEC的得率下降;而反应温度大于80℃,反应速度太快,形成TDEC凝胶,对后处理增加困难,且颗粒大小不均匀;The reaction temperature is 20-80°C. If the reaction temperature is lower than 20°C, the reaction will not be complete, and the yield of TDEC will decrease; if the reaction temperature is higher than 80°C, the reaction speed will be too fast, and TDEC gel will be formed, which will increase the difficulty of post-processing, and Uneven particle size;
二乙基二硫代氨基甲酸钠最好先配制成溶液,浓度以5~20wt%为好;Sodium diethyldithiocarbamate is preferably first prepared into a solution, and the concentration is preferably 5-20wt%;
③分离:③Separation:
采用常规的方法,如过滤、洗涤、干燥等方法,从反应混合物中分离TDEC。TDEC is separated from the reaction mixture by conventional methods, such as filtration, washing, drying and the like.
采用上述公开的制备方法所获得的TDEC,能够获得均匀相的二乙基二硫代氨基甲酸碲,为降低三元异丙胶制品的生产成本提供了条件,且由上述公开的技术方案可见,本发明所述的方法,操作简便,易于实施,其得率可高于96%。The TDEC obtained by the above-mentioned disclosed preparation method can obtain tellurium diethyldithiocarbamate in a homogeneous phase, which provides conditions for reducing the production cost of ternary isopropyl rubber products, and it can be seen from the above-mentioned disclosed technical scheme, The method of the invention has the advantages of simple operation and easy implementation, and the yield can be higher than 96%.
以下将通过实施例实施例对本发明作进一步的说明。The present invention will be further described by way of examples below.
实施例1Example 1
将40gTeO2加入到500ml 1mol l-1NaOH溶液中,加热至TeO2完全溶解。取10%(wt)2260g二乙基二硫代氨基甲酸钠溶液,控制反应温度为50℃,在搅拌的条件下滴加上述碲的NaOH溶液至二乙基二硫代氨基甲酸钠溶液中。在滴加过程中,用硼砂-磷酸氢二钾缓冲溶液(pH为8.4)调节系统的pH为8-9之间,鲜黄色沉淀即为TDEC。经过滤洗涤,在80℃下真空干燥,得到182gTDEC,其中碲含量为16.9%,熔点为110-118℃,颗粒大小2-10μm。Add 40g TeO2 into 500ml 1mol l -1 NaOH solution and heat until TeO2 is completely dissolved. Take 10% (wt) 2260g sodium diethyldithiocarbamate solution, control the reaction temperature to 50°C, add the above-mentioned NaOH solution of tellurium dropwise to the sodium diethyldithiocarbamate solution under stirring condition. During the dropwise addition, the pH of the system was adjusted between 8 and 9 with borax-dipotassium hydrogen phosphate buffer solution (pH 8.4), and the bright yellow precipitate was TDEC. After washing by filtration and vacuum drying at 80°C, 182g of TDEC was obtained, with a tellurium content of 16.9%, a melting point of 110-118°C, and a particle size of 2-10 μm.
实施例2Example 2
将40gTeO2加入到1000ml 0.5mol l-1KOH溶液中,加热至TeO2完全溶解。取10%(wt)2260g二乙基二硫代氨基甲酸钠溶液,控制反应温度为50℃,在搅拌的条件下滴加入上述碲的KOH溶液中。在滴加过程中,用0.1mol l-1HCl调节系统的pH为8-10之间,鲜黄色沉淀即为TDEC。经过滤洗涤,在80℃下真空干燥,得到177.5gTDEC,其中碲含量为18%,熔点为113-117℃,颗粒大小2-8μm。Add 40g TeO2 into 1000ml 0.5mol l -1 KOH solution and heat until TeO2 is completely dissolved. Take a 10% (wt) 2260 g sodium diethyldithiocarbamate solution, control the reaction temperature to 50° C., and add it dropwise into the KOH solution of tellurium under the condition of stirring. During the dropwise addition, adjust the pH of the system to 8-10 with 0.1mol l -1 HCl, and the bright yellow precipitate is TDEC. After filtration and washing, vacuum drying at 80°C yielded 177.5 g of TDEC with a tellurium content of 18%, a melting point of 113-117°C, and a particle size of 2-8 μm.
实施例3Example 3
采用与实施例1相同的操作方法,以KOH和NaOH(1∶1质量)的混合溶液取代NaOH,得到174gTDEC,其中碲含量为18.5%,熔点为113-117℃,颗粒大小2-8μm。Using the same operating method as in Example 1, replacing NaOH with a mixed solution of KOH and NaOH (1:1 by mass), 174 g of TDEC was obtained, wherein the tellurium content was 18.5%, the melting point was 113-117° C., and the particle size was 2-8 μm.
实施例4Example 4
采用与实施例1相同的操作方法,以碳酸钠溶液取代NaOH,得到160gTDEC,其中碲含量为19.5%,熔点为113-117℃,颗粒大小2-8μm。Using the same operating method as in Example 1, sodium carbonate solution was used instead of NaOH to obtain 160 g of TDEC, wherein the tellurium content was 19.5%, the melting point was 113-117° C., and the particle size was 2-8 μm.
实施例5Example 5
采用与实施例1相同的操作方法,以碳酸钾溶液取代NaOH,得到161gTDEC,其中碲含量为19.0%,熔点为113-117℃,颗粒大小2-8μm。Using the same operating method as in Example 1, potassium carbonate solution was used instead of NaOH to obtain 161 g TDEC, wherein the tellurium content was 19.0%, the melting point was 113-117° C., and the particle size was 2-8 μm.
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2001
- 2001-04-09 CN CN 01105884 patent/CN1202080C/en not_active Expired - Fee Related
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CN105669508A (en) * | 2014-11-05 | 2016-06-15 | 宁波硫华聚合物有限公司 | Preparation method of tellurium diethyl dithiocarbamate |
CN104447456B (en) * | 2014-11-05 | 2016-08-17 | 宁波硫华聚合物有限公司 | The preparation method of tellurium diethyl dithiocarbamate, the pre-dispersed masterbatch particles including it and preparation method thereof |
CN104529850A (en) * | 2014-12-25 | 2015-04-22 | 湖南大学 | Method for preparing (Z) type tellurium-sulfur olefin compound |
CN107903198A (en) * | 2017-11-30 | 2018-04-13 | 清远先导材料有限公司 | A kind of method of recycling TDEC |
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