CN105367468A - Preparation method of rubber vulcanization accelerator selenium dimethyldithiocarbamate - Google Patents
Preparation method of rubber vulcanization accelerator selenium dimethyldithiocarbamate Download PDFInfo
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- HXKCUQDTMDYZJD-UHFFFAOYSA-N Methyl selenac Chemical compound CN(C)C(=S)S[Se](SC(=S)N(C)C)(SC(=S)N(C)C)SC(=S)N(C)C HXKCUQDTMDYZJD-UHFFFAOYSA-N 0.000 title claims abstract description 27
- 238000013040 rubber vulcanization Methods 0.000 title claims abstract description 26
- 238000002360 preparation method Methods 0.000 title claims description 22
- ROSDSFDQCJNGOL-UHFFFAOYSA-N Dimethylamine Chemical compound CNC ROSDSFDQCJNGOL-UHFFFAOYSA-N 0.000 claims abstract description 62
- QGJOPFRUJISHPQ-UHFFFAOYSA-N Carbon disulfide Chemical compound S=C=S QGJOPFRUJISHPQ-UHFFFAOYSA-N 0.000 claims abstract description 51
- 238000003756 stirring Methods 0.000 claims abstract description 25
- 239000007788 liquid Substances 0.000 claims abstract description 24
- 239000002736 nonionic surfactant Substances 0.000 claims abstract description 21
- 238000000034 method Methods 0.000 claims abstract description 19
- MCAHWIHFGHIESP-UHFFFAOYSA-N selenous acid Chemical compound O[Se](O)=O MCAHWIHFGHIESP-UHFFFAOYSA-N 0.000 claims abstract description 16
- 239000000047 product Substances 0.000 claims abstract description 15
- 238000006243 chemical reaction Methods 0.000 claims abstract description 14
- 238000000926 separation method Methods 0.000 claims abstract description 11
- 239000007787 solid Substances 0.000 claims abstract description 11
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 11
- 239000002253 acid Substances 0.000 claims abstract description 7
- 238000001035 drying Methods 0.000 claims abstract description 5
- 239000012467 final product Substances 0.000 claims abstract description 5
- 230000035484 reaction time Effects 0.000 claims abstract description 5
- 238000007873 sieving Methods 0.000 claims abstract description 5
- BUGBHKTXTAQXES-UHFFFAOYSA-N Selenium Chemical compound [Se] BUGBHKTXTAQXES-UHFFFAOYSA-N 0.000 claims description 18
- 229910052711 selenium Inorganic materials 0.000 claims description 18
- 239000011669 selenium Substances 0.000 claims description 18
- 229940091258 selenium supplement Drugs 0.000 claims description 18
- BVTBRVFYZUCAKH-UHFFFAOYSA-L disodium selenite Chemical compound [Na+].[Na+].[O-][Se]([O-])=O BVTBRVFYZUCAKH-UHFFFAOYSA-L 0.000 claims description 15
- 229960001471 sodium selenite Drugs 0.000 claims description 15
- 239000011781 sodium selenite Substances 0.000 claims description 15
- 235000015921 sodium selenite Nutrition 0.000 claims description 15
- MZGNSEAPZQGJRB-UHFFFAOYSA-N dimethyldithiocarbamic acid Chemical compound CN(C)C(S)=S MZGNSEAPZQGJRB-UHFFFAOYSA-N 0.000 claims description 12
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 claims description 6
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims description 4
- QGJOPFRUJISHPQ-NJFSPNSNSA-N carbon disulfide-14c Chemical compound S=[14C]=S QGJOPFRUJISHPQ-NJFSPNSNSA-N 0.000 claims description 4
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 claims description 2
- 229910017604 nitric acid Inorganic materials 0.000 claims description 2
- CNRSFABRUUZKQD-UHFFFAOYSA-N OC=O.OC=O.[SeH2] Chemical compound OC=O.OC=O.[SeH2] CNRSFABRUUZKQD-UHFFFAOYSA-N 0.000 abstract 1
- 238000004519 manufacturing process Methods 0.000 description 8
- 238000002844 melting Methods 0.000 description 8
- 230000008018 melting Effects 0.000 description 8
- 239000002994 raw material Substances 0.000 description 6
- 238000004073 vulcanization Methods 0.000 description 5
- 239000000243 solution Substances 0.000 description 3
- 238000003912 environmental pollution Methods 0.000 description 2
- 239000011265 semifinished product Substances 0.000 description 2
- 230000002195 synergetic effect Effects 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- 244000043261 Hevea brasiliensis Species 0.000 description 1
- GNVMUORYQLCPJZ-UHFFFAOYSA-M Thiocarbamate Chemical compound NC([S-])=O GNVMUORYQLCPJZ-UHFFFAOYSA-M 0.000 description 1
- DKVNPHBNOWQYFE-UHFFFAOYSA-N carbamodithioic acid Chemical compound NC(S)=S DKVNPHBNOWQYFE-UHFFFAOYSA-N 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000004132 cross linking Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 239000012990 dithiocarbamate Substances 0.000 description 1
- 150000004659 dithiocarbamates Chemical class 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 229920001971 elastomer Polymers 0.000 description 1
- ZOOODBUHSVUZEM-UHFFFAOYSA-N ethoxymethanedithioic acid Chemical compound CCOC(S)=S ZOOODBUHSVUZEM-UHFFFAOYSA-N 0.000 description 1
- 238000009472 formulation Methods 0.000 description 1
- 231100000053 low toxicity Toxicity 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 229920003052 natural elastomer Polymers 0.000 description 1
- 229920001194 natural rubber Polymers 0.000 description 1
- 238000010057 rubber processing Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- QAZLUNIWYYOJPC-UHFFFAOYSA-M sulfenamide Chemical compound [Cl-].COC1=C(C)C=[N+]2C3=NC4=CC=C(OC)C=C4N3SCC2=C1C QAZLUNIWYYOJPC-UHFFFAOYSA-M 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
- 238000001308 synthesis method Methods 0.000 description 1
- 150000003557 thiazoles Chemical class 0.000 description 1
- 150000003558 thiocarbamic acid derivatives Chemical class 0.000 description 1
- 239000004636 vulcanized rubber Substances 0.000 description 1
- 239000012991 xanthate Substances 0.000 description 1
- RKQOSDAEEGPRER-UHFFFAOYSA-L zinc diethyldithiocarbamate Chemical compound [Zn+2].CCN(CC)C([S-])=S.CCN(CC)C([S-])=S RKQOSDAEEGPRER-UHFFFAOYSA-L 0.000 description 1
Landscapes
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
本发明公开一种橡胶硫化促进剂二甲基二硫代氨基甲酸硒的制备方法,包括如下步骤:在搅拌状态下依次加入规定量的二甲胺溶液、亚硒酸溶液和非离子表面活性剂至纯水中,控制温度在0-40℃,然后开始滴加规定量的二硫化碳液体,控制1-4小时的反应时间,滴加完毕后,升温至30-40℃,搅拌0.5-2小时,反应结束后,用酸溶液调节反应液pH值为6-7,再搅拌0.5-2小时后,进行固液分离,采用常规的固体烘干、粉碎、过筛方法对二甲基二硫代氨基甲酸硒产物进行处理,从而得到最终产品二甲基二硫代氨基甲酸硒。
The invention discloses a method for preparing a rubber vulcanization accelerator selenium dimethyl dithiocarbamate, which comprises the following steps: sequentially adding specified amounts of dimethylamine solution, selenous acid solution and nonionic surfactant in a stirring state To pure water, control the temperature at 0-40°C, then start to drop a specified amount of carbon disulfide liquid, control the reaction time of 1-4 hours, after the dropwise addition, raise the temperature to 30-40°C, stir for 0.5-2 hours, After the reaction, use an acid solution to adjust the pH value of the reaction solution to 6-7, and then stir for 0.5-2 hours, then carry out solid-liquid separation, and use conventional solid drying, crushing, and sieving methods to remove the dimethyldithioamino The selenium formate product is processed to obtain the final product, selenium dimethyldithiocarbamate.
Description
技术领域technical field
本发明涉及橡胶硫化促进剂领域,确切地说是指一种橡胶硫化促进剂二甲基二硫代氨基甲酸硒的制备方法。The invention relates to the field of rubber vulcanization accelerators, in particular to a preparation method of a rubber vulcanization accelerator selenium dimethyl dithiocarbamate.
背景技术Background technique
二硫代氨基甲酸盐类化合物主要用作橡胶硫化过程中的超速促进剂。与其它类型的硫化促进剂相比,二硫代氨基甲酸盐类促进剂具有硫化速度很快、硫化温度低、分散性能好、交联度高、毒性低等优点,但易焦烧、硫化平坦性差。使用硫代氨基甲酸盐类促进剂可制得拉伸应力较大的硫化橡胶,但拉伸强度和扯断伸长率比使用次磺酰胺类促进剂低。Dithiocarbamate compounds are mainly used as super speed accelerators in the rubber vulcanization process. Compared with other types of vulcanization accelerators, dithiocarbamate accelerators have the advantages of fast vulcanization speed, low vulcanization temperature, good dispersion performance, high degree of crosslinking, and low toxicity, but they are easy to scorch and vulcanize flat Poor sex. The use of thiocarbamate accelerators can produce vulcanized rubber with higher tensile stress, but the tensile strength and elongation at break are lower than those of sulfenamide accelerators.
研究表明,当两种超速硫化促进剂并用时,会产生协同效应,其原因可能是促进剂并用时易混溶,形成了在橡胶中溶解度较大和化学活性较大的成盐化合物。目前橡胶加工行业中普遍采用两种或多种促进剂并用的硫化体系,有文献报道黄原酸盐/二乙基二硫代氨基甲酸锌促进剂并用硫化天然橡胶时,具有积极的协同效应。Studies have shown that when two ultra-fast vulcanization accelerators are used together, there will be a synergistic effect. The reason may be that the accelerators are easily miscible when used together, forming a salt-forming compound with greater solubility in rubber and greater chemical activity. At present, the vulcanization system in which two or more accelerators are used in combination is commonly used in the rubber processing industry. It has been reported in the literature that when xanthate/zinc diethyldithiocarbamate accelerator is used in combination with vulcanized natural rubber, it has a positive synergistic effect.
二甲基二硫代氨基甲酸硒作为硫代氨基甲酸盐类中的一种,其主要作用体现为与噻唑类并用于NR、IIR、SBR,在浅色制品中不变色,在低硫耐热配方中更有效,其也还能作为硫化剂使用。Selenium dimethyl dithiocarbamate is one of the thiocarbamates. Its main function is to combine with thiazoles for NR, IIR, and SBR. It does not change color in light-colored products, and is heat-resistant in low-sulfur products More effective in formulations, it can also be used as a vulcanizing agent.
目前,还没文献或资料公开二甲基二硫代氨基甲酸硒的合成方法,需要弥补这片空白。At present, there is no literature or information to disclose the synthesis method of selenium dimethyl dithiocarbamate, and this gap needs to be filled.
发明内容Contents of the invention
针对上述缺陷,本发明解决的技术问题在于提供一种橡胶硫化促进剂二甲基二硫代氨基甲酸硒的制备方法。For above-mentioned defect, the technical problem that the present invention solves is to provide a kind of preparation method of rubber vulcanization accelerator selenium dimethyl dithiocarbamate.
为了解决以上的技术问题,本发明提供的橡胶硫化促进剂二甲基二硫代氨基甲酸硒的制备方法,包括如下步骤:In order to solve the above technical problems, the preparation method of rubber vulcanization accelerator dimethyl dithiocarbamate selenium provided by the invention comprises the steps:
在搅拌状态下依次加入规定量的二甲胺溶液、亚硒酸溶液和非离子表面活性剂至纯水中,控制温度在0-40℃,然后开始滴加规定量的二硫化碳液体,控制1-4小时的反应时间,滴加完毕后,升温至30-40℃,搅拌0.5-2小时,反应结束后,用酸溶液调节反应液pH值为6-7,再搅拌0.5-2小时后,进行固液分离,采用常规的固体烘干、粉碎、过筛方法对二甲基二硫代氨基甲酸硒产物进行处理,从而得到最终产品二甲基二硫代氨基甲酸硒;其中:Add specified amount of dimethylamine solution, selenous acid solution and non-ionic surfactant to pure water sequentially under stirring state, control the temperature at 0-40°C, then start to drop specified amount of carbon disulfide liquid, control 1- The reaction time is 4 hours. After the dropwise addition is completed, the temperature is raised to 30-40°C and stirred for 0.5-2 hours. Solid-liquid separation, using conventional solid drying, crushing, and sieving methods to process the selenium dimethyl dithiocarbamate product, so as to obtain the final product selenium dimethyl dithiocarbamate; wherein:
二甲胺、二硫化碳、亚硒酸和非离子表面活性剂的化学计量摩尔比为1:0.8-1.2:0.2-0.25:0.01-0.025mol。The stoichiometric molar ratio of dimethylamine, carbon disulfide, selenous acid and nonionic surfactant is 1:0.8-1.2:0.2-0.25:0.01-0.025mol.
优选地,所述二甲胺溶液的浓度为:10-40wt%。Preferably, the concentration of the dimethylamine solution is: 10-40wt%.
优选地,所述亚硒酸溶液的浓度为:0.25-1mol/L。Preferably, the concentration of the selenous acid solution is: 0.25-1mol/L.
优选地,所述酸溶液由盐酸、醋酸或硝酸的一种或一种以上配制而成。Preferably, the acid solution is prepared from one or more of hydrochloric acid, acetic acid or nitric acid.
优选地,所述酸溶液的浓度为0.5-2mol/L。Preferably, the acid solution has a concentration of 0.5-2 mol/L.
另外,本发明再提供一种橡胶硫化促进剂二甲基二硫代氨基甲酸硒的制备方法,包括如下步骤:In addition, the present invention provides a method for preparing rubber vulcanization accelerator selenium dimethyl dithiocarbamate, comprising the steps of:
在搅拌状态下依次加入规定量的二甲胺溶液、亚硒酸钠溶液和非离子表面活性剂至纯水中,控制温度在0-40℃,然后开始滴加规定量的二硫化碳液体,控制1-4小时的反应时间,滴加完毕后,升温至30-40℃,搅拌0.5-2小时,反应结束后,用酸溶液调节反应液pH值为6-7,再搅拌0.5-2小时后,进行固液分离,采用常规的固体烘干、粉碎、过筛方法对二甲基二硫代氨基甲酸硒产物进行处理,从而得到最终产品二甲基二硫代氨基甲酸硒;其中:Add the specified amount of dimethylamine solution, sodium selenite solution and non-ionic surfactant to pure water in a stirring state, control the temperature at 0-40°C, then start to drop the specified amount of carbon disulfide liquid, control 1 The reaction time is -4 hours. After the dropwise addition is completed, the temperature is raised to 30-40° C. and stirred for 0.5-2 hours. After the reaction is completed, the pH value of the reaction solution is adjusted to 6-7 with an acid solution, and then stirred for 0.5-2 hours. Solid-liquid separation is carried out, and the selenium dimethyl dithiocarbamate product is processed by conventional solid drying, crushing and sieving methods, so as to obtain the final product selenium dimethyl dithiocarbamate; wherein:
二甲胺、二硫化碳、亚硒酸钠和非离子表面活性剂的化学计量摩尔比为1:0.8-1.2:0.2-0.25:0.01-0.025mol。The stoichiometric molar ratio of dimethylamine, carbon disulfide, sodium selenite and nonionic surfactant is 1:0.8-1.2:0.2-0.25:0.01-0.025mol.
优选地,所述二甲胺溶液的浓度为:10-40wt%。Preferably, the concentration of the dimethylamine solution is: 10-40wt%.
优选地,所述亚硒酸钠溶液的浓度为:0.25-1mol/L。Preferably, the concentration of the sodium selenite solution is: 0.25-1mol/L.
与现有技术相比,本发明的橡胶硫化促进剂二甲基二硫代氨基甲酸硒的制备方法,具有以下优点:Compared with prior art, the preparation method of rubber vulcanization accelerator dimethyl dithiocarbamate selenium of the present invention has the following advantages:
1、本发明在生产过程中无含盐废水排放,对环境污染小;1. The present invention does not discharge salty waste water during the production process, and has little environmental pollution;
2、本发明的方法减少了中间半成品的生产环节,生产周期短,降低了生产成本;2, the method of the present invention has reduced the production link of intermediate semi-finished product, and production cycle is short, has reduced production cost;
3、二甲基二硫代氨基甲酸硒产物的初熔点≥250℃,纯度≥99%以上。3. The initial melting point of the selenium dimethyl dithiocarbamate product is ≥ 250°C, and the purity is ≥ 99%.
附图说明Description of drawings
图1为本发明实施例中橡胶硫化促进剂二甲基二硫代氨基甲酸硒的制备方法的流程图,其中,SeDMC为二甲基二硫代氨基甲酸硒。Fig. 1 is the flowchart of the preparation method of rubber vulcanization accelerator selenium dimethyl dithiocarbamate in the embodiment of the present invention, wherein, SeDMC is selenium dimethyl dithiocarbamate.
具体实施方式detailed description
为了本领域的技术人员能够更好地理解本发明所提供的技术方案,下面结合具体实施例进行阐述。In order for those skilled in the art to better understand the technical solutions provided by the present invention, the following will be described in conjunction with specific embodiments.
请参见图1,该图为本发明实施例中橡胶硫化促进剂二甲基二硫代氨基甲酸硒的制备方法的流程图,其中,SeDMC为二甲基二硫代氨基甲酸硒。Please refer to FIG. 1 , which is a flow chart of the preparation method of the rubber vulcanization accelerator selenium dimethyl dithiocarbamate in the embodiment of the present invention, wherein SeDMC is selenium dimethyl dithiocarbamate.
实施例1Example 1
本发明实施例提供的橡胶硫化促进剂二甲基二硫代氨基甲酸硒的制备方法,所用原料及其化学计量摩尔比为二甲胺:二硫化碳:亚硒酸:非离子表面活性剂=1:0.9:0.2:0.01。其工艺过程为:向盛有纯水的反应釜内,搅拌状态下依次加入二甲胺溶液、非离子表面活性剂、亚硒酸溶液,搅拌30min后滴加二硫化碳液体,滴加时间为2h,温度控制在25℃,后升温至40℃继续搅拌反应1小时,进行固液分离,固体烘干、粉碎、包装即可。二甲胺溶液的浓度为:30wt%。亚硒酸溶液的浓度为:0.8mol/L。The preparation method of the rubber vulcanization accelerator dimethyl dithiocarbamate selenium provided by the embodiment of the present invention, the raw materials used and the stoichiometric molar ratio thereof are dimethylamine: carbon disulfide: selenous acid: nonionic surfactant=1: 0.9:0.2:0.01. The process is as follows: add dimethylamine solution, non-ionic surfactant, and selenous acid solution to the reaction kettle filled with pure water in a stirring state, and add carbon disulfide liquid dropwise after stirring for 30 minutes. The dropping time is 2 hours. The temperature is controlled at 25°C, and then the temperature is raised to 40°C to continue stirring and reacting for 1 hour, and the solid-liquid separation is carried out, and the solid is dried, pulverized, and packaged. The concentration of the dimethylamine solution is: 30wt%. The concentration of selenous acid solution is: 0.8mol/L.
所得产品收率96.5%,初熔点为252--260℃,硒含量14.6%。The yield of the obtained product is 96.5%, the initial melting point is 252--260° C., and the selenium content is 14.6%.
实施例2Example 2
本发明实施例提供的橡胶硫化促进剂二甲基二硫代氨基甲酸硒的制备方法,所用原料及其化学计量摩尔比为二甲胺:二硫化碳:亚硒酸:非离子表面活性剂=1:1.1:0.25:0.015。其工艺过程为:向盛有纯水的反应釜内,搅拌状态下依次加入二甲胺溶液、非离子表面活性剂、亚硒酸溶液,搅拌50min后滴加二硫化碳液体,滴加时间为3h,温度控制在25℃,后升温至40℃继续搅拌反应1小时,进行固液分离,固体烘干、粉碎、包装即可。二甲胺溶液的浓度为:20wt%。亚硒酸溶液的浓度为:0.5mol/L。The preparation method of the rubber vulcanization accelerator dimethyl dithiocarbamate selenium provided by the embodiment of the present invention, the raw materials used and the stoichiometric molar ratio thereof are dimethylamine: carbon disulfide: selenous acid: nonionic surfactant=1: 1.1:0.25:0.015. The process is as follows: add dimethylamine solution, non-ionic surfactant, and selenous acid solution to the reaction kettle filled with pure water in a stirring state, and then add carbon disulfide liquid dropwise after stirring for 50 minutes. The dropping time is 3 hours. The temperature is controlled at 25°C, and then the temperature is raised to 40°C to continue stirring and reacting for 1 hour, and the solid-liquid separation is carried out, and the solid is dried, pulverized, and packaged. The concentration of the dimethylamine solution is: 20wt%. The concentration of selenous acid solution is: 0.5mol/L.
所得产品收率95.8%,初熔点为250--260℃,硒含量14.6%。The yield of the obtained product is 95.8%, the initial melting point is 250--260°C, and the selenium content is 14.6%.
实施例3Example 3
本发明实施例提供的橡胶硫化促进剂二甲基二硫代氨基甲酸硒的制备方法,所用原料及其化学计量摩尔比为二甲胺:二硫化碳:亚硒酸:非离子表面活性剂=1:1.2:0.25:0.015。其工艺过程为:向盛有纯水的反应釜内,搅拌状态下依次加入二甲胺溶液、非离子表面活性剂、亚硒酸溶液,搅拌30min后滴加二硫化碳液体,滴加时间为4h,温度控制在8℃。后升温至40℃继续搅拌反应1小时,进行固液分离,液体舍弃,固体烘干、粉碎、包装即可。二甲胺溶液的浓度为:40wt%。亚硒酸溶液的浓度为:1mol/L。The preparation method of the rubber vulcanization accelerator dimethyl dithiocarbamate selenium provided by the embodiment of the present invention, the raw materials used and the stoichiometric molar ratio thereof are dimethylamine: carbon disulfide: selenous acid: nonionic surfactant=1: 1.2:0.25:0.015. The process is as follows: add dimethylamine solution, non-ionic surfactant, and selenous acid solution to the reaction kettle filled with pure water in a stirring state, and then add carbon disulfide liquid dropwise after stirring for 30 minutes. The dropping time is 4 hours. The temperature was controlled at 8°C. Afterwards, the temperature was raised to 40° C. and the stirring reaction was continued for 1 hour, the solid-liquid separation was carried out, the liquid was discarded, and the solid was dried, pulverized, and packaged. The concentration of the dimethylamine solution is: 40wt%. The concentration of selenous acid solution is: 1mol/L.
所得产品收率97.2%,初熔点为255--262℃,硒含量14.3%。The yield of the obtained product is 97.2%, the initial melting point is 255--262°C, and the selenium content is 14.3%.
实施例4Example 4
本发明实施例提供的橡胶硫化促进剂二甲基二硫代氨基甲酸硒的制备方法,所用原料及其化学计量摩尔比为二甲胺:二硫化碳:亚硒酸钠:非离子表面活性剂=1:0.9:0.2:0.01。其工艺过程为:向盛有纯水的反应釜内,搅拌状态下依次加入二甲胺溶液、非离子表面活性剂、亚硒酸钠溶液,搅拌30min后滴加二硫化碳液体,滴加时间为2h,温度控制在25℃,后升温至40℃继续搅拌反应1小时,进行固液分离,固体烘干、粉碎、包装即可。二甲胺溶液的浓度为:30wt%。亚硒酸钠溶液的浓度为:0.8mol/L。The preparation method of the rubber vulcanization accelerator selenium dimethyl dithiocarbamate provided by the embodiment of the present invention, the raw materials used and the stoichiometric molar ratio thereof are dimethylamine: carbon disulfide: sodium selenite: nonionic surfactant=1 :0.9:0.2:0.01. The process is as follows: add dimethylamine solution, non-ionic surfactant, and sodium selenite solution to the reaction kettle filled with pure water in a stirring state, and add carbon disulfide liquid dropwise after stirring for 30 minutes. The dropping time is 2 hours. , the temperature is controlled at 25°C, and then the temperature is raised to 40°C to continue stirring and reacting for 1 hour, and solid-liquid separation is carried out, and the solid is dried, pulverized, and packaged. The concentration of the dimethylamine solution is: 30wt%. The concentration of sodium selenite solution is: 0.8mol/L.
所得产品收率96.5%,初熔点为252--260℃,硒含量14.6%。The yield of the obtained product is 96.5%, the initial melting point is 252--260° C., and the selenium content is 14.6%.
实施例5Example 5
本发明实施例提供的橡胶硫化促进剂二甲基二硫代氨基甲酸硒的制备方法,所用原料及其化学计量摩尔比为二甲胺:二硫化碳:亚硒酸钠:非离子表面活性剂=1:1.1:0.25:0.015。其工艺过程为:向盛有纯水的反应釜内,搅拌状态下依次加入二甲胺溶液、非离子表面活性剂、亚硒酸钠溶液,搅拌50min后滴加二硫化碳液体,滴加时间为3h,温度控制在25℃,后升温至40℃继续搅拌反应1小时,进行固液分离,固体烘干、粉碎、包装即可。二甲胺溶液的浓度为:20wt%。亚硒酸钠溶液的浓度为:0.5mol/L。The preparation method of the rubber vulcanization accelerator selenium dimethyl dithiocarbamate provided by the embodiment of the present invention, the raw materials used and the stoichiometric molar ratio thereof are dimethylamine: carbon disulfide: sodium selenite: nonionic surfactant=1 :1.1:0.25:0.015. The process is as follows: add dimethylamine solution, non-ionic surfactant, and sodium selenite solution to the reaction kettle filled with pure water in a stirring state, and add carbon disulfide liquid dropwise after stirring for 50 minutes. The dropping time is 3 hours. , the temperature is controlled at 25°C, and then the temperature is raised to 40°C to continue stirring and reacting for 1 hour, and solid-liquid separation is carried out, and the solid is dried, pulverized, and packaged. The concentration of the dimethylamine solution is: 20wt%. The concentration of sodium selenite solution is: 0.5mol/L.
所得产品收率95.8%,初熔点为250--260℃,硒含量14.6%。The yield of the obtained product is 95.8%, the initial melting point is 250--260°C, and the selenium content is 14.6%.
实施例6Example 6
本发明实施例提供的橡胶硫化促进剂二甲基二硫代氨基甲酸硒的制备方法,所用原料及其化学计量摩尔比为二甲胺:二硫化碳:亚硒酸钠:非离子表面活性剂=1:1.2:0.25:0.015。其工艺过程为:向盛有纯水的反应釜内,搅拌状态下依次加入二甲胺溶液、非离子表面活性剂、亚硒酸钠溶液,搅拌30min后滴加二硫化碳液体,滴加时间为4h,温度控制在8℃。后升温至40℃继续搅拌反应1小时,进行固液分离,液体舍弃,固体烘干、粉碎、包装即可。二甲胺溶液的浓度为:40wt%。亚硒酸钠溶液的浓度为:1mol/L。The preparation method of the rubber vulcanization accelerator selenium dimethyl dithiocarbamate provided by the embodiment of the present invention, the raw materials used and the stoichiometric molar ratio thereof are dimethylamine: carbon disulfide: sodium selenite: nonionic surfactant=1 :1.2:0.25:0.015. The process is as follows: add dimethylamine solution, non-ionic surfactant, and sodium selenite solution to the reaction kettle filled with pure water in a stirring state, and add carbon disulfide liquid dropwise after stirring for 30 minutes. The dropping time is 4 hours. , the temperature was controlled at 8°C. Afterwards, the temperature was raised to 40° C. and the stirring reaction was continued for 1 hour, the solid-liquid separation was carried out, the liquid was discarded, and the solid was dried, pulverized, and packaged. The concentration of the dimethylamine solution is: 40wt%. The concentration of sodium selenite solution is: 1mol/L.
所得产品收率97.2%,初熔点为255--262℃,硒含量14.3%。The yield of the obtained product is 97.2%, the initial melting point is 255--262°C, and the selenium content is 14.3%.
与现有技术相比,本发明的橡胶硫化促进剂二甲基二硫代氨基甲酸硒的制备方法,具有以下优点:Compared with prior art, the preparation method of rubber vulcanization accelerator dimethyl dithiocarbamate selenium of the present invention has the following advantages:
1、本发明在生产过程中无含盐废水排放,对环境污染小;1. The present invention does not discharge salty waste water during the production process, and has little environmental pollution;
2、本发明的方法减少了中间半成品的生产环节,生产周期短,降低了生产成本;2, the method of the present invention has reduced the production link of intermediate semi-finished product, and production cycle is short, has reduced production cost;
3、二甲基二硫代氨基甲酸硒产物的初熔点≥250℃,纯度≥99%以上。3. The initial melting point of the selenium dimethyl dithiocarbamate product is ≥ 250°C, and the purity is ≥ 99%.
对所公开的实施例的上述说明,使本领域专业技术人员能够实现或使用本发明。对这些实施例的多种修改对本领域的专业技术人员来说将是显而易见的,本文中所定义的一般原理可以在不脱离本发明的精神或范围的情况下,在其它实施例中实现。因此,本发明将不会被限制于本文所示的这些实施例,而是要符合与本文所公开的原理和新颖特点相一致的最宽的范围。The above description of the disclosed embodiments is provided to enable any person skilled in the art to make or use the invention. Various modifications to these embodiments will be readily apparent to those skilled in the art, and the general principles defined herein may be implemented in other embodiments without departing from the spirit or scope of the invention. Therefore, the present invention will not be limited to the embodiments shown herein, but is to be accorded the widest scope consistent with the principles and novel features disclosed herein.
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