A kind of continuous production method of trimethylallyl ammonium chloride
A technology of trimethylallyl ammonium chloride and production method, applied in chemical instruments and methods, preparation of amino compounds, preparation of organic compounds, etc., can solve the problem of increasing the unit consumption of raw materials and production costs, process safety, and product quality. Risks, difficult removal of reaction heat, etc., to achieve the effects of stable storage, shortened reaction time, and small back-mixing
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0052] The continuous production method of the trimethylallyl ammonium chloride that this example provides, concrete implementation is as follows:
[0053] (1) The liquefied trimethylamine in the trimethylamine raw material tank and the allyl chloride in the allyl chloride raw material tank are continuously pumped into the first tubular reactor 3 by a metering pump to react to produce trimethylene Propylammonium chloride, control the temperature in the first tubular reactor 3 to be 15°C, the pressure to be 1.2MPa, and the residence time to be 22s; the temperature in the second tubular reactor 4 to be 20°C, the pressure to be 1.0MPa, and the residence time For 188s, the temperature in the third tubular reactor 5 is 45°C, the pressure is 0.8MPa, the residence time is 1360s, and each water inlet 2 in the production device is opened, so that the total water intake is 150kg / h, and the water that passes into is Deionized water is used to dissolve the trimethylallyl ammonium chloride...
Embodiment 2
[0062] The continuous production method of the trimethylallyl ammonium chloride that this example provides, concrete implementation is as follows:
[0063] (1) The liquefied trimethylamine in the trimethylamine raw material tank and the allyl chloride in the allyl chloride raw material tank are continuously pumped into the first tubular reactor 3 by a metering pump to react to produce trimethylene Propylammonium chloride, control the temperature in the first tubular reactor 3 to be 25°C, the pressure to be 1.6MPa, and the residence time to be 20s; the temperature in the second tubular reactor 4 to be 30°C, the pressure to be 1.5MPa, and the residence time For 138s, the temperature in the third tubular reactor 5 is 50°C, the pressure is 1.1MPa, the residence time is 1035s, and each water inlet 2 in the production device is opened, so that the total water intake is 300kg / h, and the water that passes into is Deionized water is used to dissolve the trimethylallyl ammonium chloride...
Embodiment 3
[0069] The continuous production method of the trimethylallyl ammonium chloride that this example provides, concrete implementation is as follows:
[0070] (1) The concentration in the trimethylamine raw material tank is respectively 30% aqueous solution trimethylamine and the allyl chloride in the allyl chloride raw material tank are continuously pumped into the first tubular reactor 3 by a metering pump to make it react and produce Trimethylallyl ammonium chloride, control the temperature in the first tubular reactor 3 to be 40°C, the pressure to be 1.0MPa, and the residence time to be 35s, and the temperature in the second tubular reactor 4 to be 50°C and the pressure to be 1.0 MPa, residence time is 188s, temperature in the 3rd tubular reactor 5 is 50 ℃, pressure is 0.9MPa residence time is 1435s, temperature in the 4th tubular reactor is 40 ℃, pressure is 0.7MPa residence time is 235s and Open each water inlet 2 in the production device, so that the total water intake is ...
PUM
| Property | Measurement | Unit |
|---|---|---|
| boiling point | aaaaa | aaaaa |
Abstract
Description
Claims
Application Information
Login to View More 
