Method for producing rubber vulcanization accelerator NS by two-dropping method
A technology for rubber vulcanization and accelerators, which is applied in the production of rubber vulcanization accelerator NS and rubber vulcanization accelerator N-tert-butyl-2-benzothiazole sulfenamide by two-drop method, which can solve the problem of low yield of accelerator NS and other issues, to achieve the effect of simple process
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Examples
Embodiment 1
[0008] Get 75 grams of tert-butylamine and join in the reaction kettle, under the condition of 40 ℃ and rotating speed of 600 rpm, with a flow rate of 2ml / min, add accelerator mass content 85% M50g, isopropanol 75g slurry, simultaneously with The flow rate of 1ml / min is added the oxidizing agent sodium hypochlorite that available chlorine is 16mg / 100ml, and dropwise time is 2.0 hours, judges reaction terminal point with starch potassium iodide test paper, when test paper turns black, stop adding sodium hypochlorite dropwise. After the reaction is completed, suction filtration, water washing, filtration, and drying are used to obtain the rubber accelerator NS product. The purity of the accelerator NS reaches more than 98.7%, and the yield reaches 95.2%.
Embodiment 2
[0010] Get 75 grams of tert-butylamine and join it in the reaction kettle. Under the conditions of 50° C. and a rotating speed of 600 rpm, with a flow rate of 2 ml / min, add accelerator mass content 87% M50g, isopropanol 75g slurry, and simultaneously The flow rate of 1ml / min is added the oxidizing agent sodium hypochlorite that available chlorine is 17mg / 100ml, and dropwise time is 2.0 hours, judges reaction terminal point with starch potassium iodide test paper, when test paper turns black, stops dripping sodium hypochlorite. After the reaction is completed, suction filtration, water washing, filtration, and drying are used to obtain the rubber accelerator NS product. The purity of the accelerator NS reaches more than 98.8%, and the yield reaches 95.3%.
Embodiment 3
[0012] Get 75 grams of tert-butylamine and join in the reaction kettle, under the condition of 60°C and rotating speed of 600 rpm, with a flow rate of 2ml / min, add accelerator mass content 90% M50g, isopropanol 75g slurry, simultaneously with The flow rate of 1ml / min is added the oxidizing agent sodium hypochlorite that available chlorine is 18mg / 100ml, and dropwise time is 2.0 hours, judges reaction terminal point with starch potassium iodide test paper, when test paper turns black, stop adding sodium chlorate dropwise. After the reaction is completed, suction filtration, water washing, filtration, and drying are used to obtain the rubber accelerator NS product. The purity of the accelerator NS reaches more than 98.9%, and the yield reaches 95.4%.
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More 