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Method for continuously preparing tetrabenzylthiuram disulfide by using micro-reaction device

A technology of tetrabenzylthiuram disulfide and micro-reaction device, applied in the direction of organic chemistry and the like, can solve problems such as non-compliance with national environmental protection and energy-saving production, difficult to meet market demand, unstable product quality, etc., and achieve good The effect of industrial application prospects, excellent product quality, and easy control of operating conditions

Active Publication Date: 2018-08-03
山东斯递尔化工科技有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

There are four main defects in this process: 1. A large amount of alkali and acid are consumed in the production process, and the cost is high; 2. In the condensation and oxidation reactions, raw materials need to be added dropwise, the reaction time is long, and the energy consumption is high; 3. Discharge The waste water contains a relatively high concentration of inorganic sodium salts, which brings pressure to the governance, and it is difficult to experiment with "clean and green" production, which does not meet the requirements of the national environmental protection and energy-saving production; 4. The quality of the produced products is unstable and the appearance is poor. It is difficult to meet the needs of the market

Method used

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  • Method for continuously preparing tetrabenzylthiuram disulfide by using micro-reaction device
  • Method for continuously preparing tetrabenzylthiuram disulfide by using micro-reaction device

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0034] Take 50ml of dibenzylamine with a content of 98% and dissolve it in 200ml of absolute ethanol, and take 18.5ml of carbon disulfide. Use a metering pump to pass the two-phase solution through a Y-shaped mixer and into a reactor with a pipe diameter of 10 mm at a flow rate of 5 mL / min. The residence time of the reaction liquid in the reactor was 10 min, and the temperature was 25°C. The reaction solution was taken after one cycle of reaction. Take 15ml of 27.5% hydrogen peroxide and the above reaction solution through the Y-type mixer with a metering pump, and pass it into a reactor with a pipe diameter of 10mm at a flow rate of 5mL / min. The residence time of the reaction solution in the reactor was 10 min, and the temperature was 30°C. After one cycle of reaction, the reaction solution is taken, filtered to obtain a filter cake, and dried to obtain tetrabenzylthiuram disulfide. The filtrate can be reused and refined after the content is reduced. The obtained finished...

Embodiment 2

[0036] Take 50ml of dibenzylamine with a content of 98% and dissolve it in 200ml of absolute ethanol, and take 18.5ml of carbon disulfide. Use a metering pump to pass the two-phase solution through a Y-shaped mixer and into a reactor with a pipe diameter of 10 mm at a flow rate of 2.5 mL / min. The residence time of the reaction liquid in the reactor is 20min, and the temperature is 25°C. The reaction solution was taken after one cycle of reaction. Take 15ml of 27.5% hydrogen peroxide and the above reaction solution through the Y-type mixer with a metering pump, and pass it into a reactor with a pipe diameter of 10mm at a flow rate of 2.5mL / min. The residence time of the reaction liquid in the reactor is 20min, and the temperature is 30°C. After one cycle of reaction, the reaction solution is taken, filtered to obtain a filter cake, and dried to obtain tetrabenzylthiuram disulfide. The filtrate can be reused and refined after the content is reduced. The obtained finished pro...

Embodiment 3

[0038] Take 50ml of dibenzylamine with a content of 98% and dissolve it in 200ml of absolute ethanol, and take 18.5ml of carbon disulfide. Use a metering pump to pass the two-phase solution through the Y-shaped mixer and into a reactor with a pipe diameter of 10 mm at a flow rate of 1.667 mL / min. The residence time of the reaction liquid in the reactor is 30min, and the temperature is 25°C. The reaction solution was taken after one cycle of reaction. Take 15ml of 27.5% hydrogen peroxide and the above reaction solution through the Y-type mixer with a metering pump, and pass it into a reactor with a pipe diameter of 10mm at a flow rate of 1.667mL / min. The residence time of the reaction liquid in the reactor is 30min, and the temperature is 30°C. After one cycle of reaction, the reaction solution is taken, filtered to obtain a filter cake, and dried to obtain tetrabenzylthiuram disulfide. The filtrate can be reused and refined after the content is reduced. The obtained finish...

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Abstract

The invention relates to the field of production of rubber auxiliaries and in particular discloses a method for continuously preparing tetrabenzylthiuramdisulfide by utilizing a microreaction device. The method for continuously preparing tetrabenzylthiuramdisulfide by utilizing the microreaction device is characterized in that carbon disulfide and a solution obtained by mixing dibenzylamine and a solvent are fed into a micromixer in the microreaction device by virtue of a metering pump, are fully mixed and then are fed into a microreactor in the microreaction device for carrying out condensation reaction, so that a dibenzyl dithioformic acid solution is obtained; and the dibenzyl dithioformic acid solution and hydrogen peroxide are fed into the micromixer by virtue of the metering pump, are fully mixed and then are fed into the microreactor for carrying out oxidation reaction, and filtering and drying are carried out, so that tetrabenzylthiuramdisulfide is obtained. The method disclosed by the invention has the advantages that raw materials required by reaction are fewer, the reactant conversion rate is higher, byproducts are fewer, the reaction selectivity is higher, and the product quality is excellent.

Description

(1) Technical field [0001] The invention relates to the production field of rubber additives, in particular to a method for continuously preparing tetrabenzylthiuram disulfide by using a micro-reaction device. (2) Background technology [0002] Tetrabenzylthiuram disulfide, referred to as TBzTD, has the following structural formula: [0003] . [0004] Tetrabenzylthiuram disulfide is mainly used as a rubber vulcanization accelerator. It is one of the rubber accelerator thiuram products. It is an ultra-fast vulcanization accelerator and is suitable for natural rubber, butadiene rubber, isoprene rubber, and styrene-butadiene rubber. , nitrile rubber, butyl rubber, EPDM rubber and latex, the vulcanization acceleration effect is similar to TMTD, the vulcanization speed is slightly slower than TMTD, but the stability is better than TMTD. TBzTD is widely used in the manufacture of wires and cables, tires, tapes, colored transparent products, footwear, heat-resistant products, ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C333/32
CPCC07C333/14C07C333/32
Inventor 朱嘉震田旭王金才赵新远尹传祥赵文超
Owner 山东斯递尔化工科技有限公司