Technology for continuously producing alkyl amide propyl group betaine
An alkylamidopropyl sugar beet and process technology, which is applied in the field of continuous production technology of amphoteric surfactants, can solve the problems that the product quality is difficult to maintain stable, the production efficiency is difficult to be further improved, and the energy consumption is high, and the utilization rate of equipment is improved. , Conducive to the expansion of production capacity and the effect of improving production efficiency
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Embodiment 1
[0021] Embodiment 1: take coconut oil as raw material continuous production cocamidopropyl betaine
[0022] Cocoic acid 220kg / h, N, N-dimethylaminopropylamine 173kg / h enters in the static mixer, through 52 ℃ of first heat exchanger mixed materials temperature, then further be warming up to 108 ℃ by the second heat exchanger, then Enter the condensation reactor, heat up to 162°C (at normal pressure) through a jacket oil bath (jacket oil bath temperature 170°C), and after staying in the reactor for 3h, enter the vacuum flasher (pressure 0.03MPa) at 350kg / h, After deamination, the material is cooled to 93°C by the second heat exchanger and then enters the quaternization reactor. After reacting at 95°C for 2 hours, it is cooled to 52°C by the first heat exchanger and enters the adjustment tank for adjustment to obtain the finished product. Under the conditions of the present embodiment, the production capacity of cocamidopropyl betaine is 1100kg / h.
Embodiment 2
[0023] Embodiment 2: Methyl dodecanoate is continuous production of lauryl amidopropyl betaine as raw material
[0024] Methyl dodecanoate 320kg / h, N, N-dimethylaminopropylamine 150kg / h enters in the static mixer, passes through the first heat exchanger and mixes material temperature 58 ℃, further heats up to 97 ℃ after passing through the second heat exchanger ℃, then enter the condensation reactor, and heat up to 155°C (at normal pressure) through a jacket oil bath (jacket oil bath temperature 160°C). After staying in the reactor for 2h, enter the vacuum flasher at 370kg / h (pressure 0.01 MPa), the material after deamination is cooled to 87°C by the second heat exchanger, then enters the quaternization reactor, reacts at 90°C for 2 hours, enters the first heat exchanger to cool to 60°C, enters the adjustment tank for adjustment, and obtains the finished product . Under the conditions of the present embodiment, the production capacity of cocamidopropyl betaine is 2000kg / h.
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