Synthesis process for 2-acrylamido-2-methyl propane sulfonic acid through continuous method
A technology based on methylpropanesulfonic acid and acrylamide, which is applied in the preparation of sulfonic acid, organic chemistry, etc., can solve the problems of insufficient yield and purity of synthetic products, cumbersome process operations, poor quality stability, etc., and improve product yield. The effect of high efficiency and quality stability, avoiding manual operation, and strong reaction stability
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Embodiment 1
[0018] The acrylonitrile with water content of 0.2% is added into the four-mouth glass container with stirring device through the flow meter by the metering pump at a flow rate of 420g / h, and simultaneously oleum, wherein free SO 3 The content is 3%, and the metering pump is added to the same container through the flow meter at a flow rate of 76g / h for mixing. The temperature in the mixing container is controlled by an ice-water bath to be 11±1°C, and the mixed liquid flows into the belt through the overflow port in the middle of the mixer. In the primary reactor with stirring paddle, at the same time, isobutene with a purity of 99.76% was vaporized and added to the primary reactor at a flow rate of 32 g / h. The overflow port in the middle of the first-stage reactor flows into the second-stage reactor with stirring paddle, and at the same time, isobutene with a purity of 99.76% is vaporized and added to the second-stage reactor at a flow rate of 16 g / h, and the reactor is contro...
Embodiment 2
[0021] The acrylonitrile with water content of 0.2% is added into the four-mouth glass container with stirring device through the flow meter by the metering pump at a flow rate of 420g / h, and simultaneously oleum, wherein free SO 3 The content is 2.0%, and it is added to the same container by a metering pump at a flow rate of 76 g / h through a flowmeter for mixing, and the temperature in the mixing container is controlled by an ice-water bath to 11±1 °C. The mixed solution flows into the primary reactor with a stirring paddle through the overflow port in the middle of the mixer, and at the same time, isobutene with a purity of 99.8% is vaporized and added to the primary reactor at a flow rate of 32 g / h, and the reactor is controlled by a water bath The internal temperature is 39±1°C. The mixed liquid flows into the secondary reactor with a stirring paddle through the overflow port in the middle of the primary reactor, and at the same time, isobutene with a purity of 99.8% is va...
Embodiment 3
[0024] Add acrylonitrile with a water content of 0.2% into a four-port glass container with a stirring device through a flow meter at a flow rate of 378g / h by a metering pump, and simultaneously fuming sulfuric acid, wherein free SO 3 The content is 3%, and it is added to the same container by a metering pump at a flow rate of 68.4 g / h through a flowmeter for mixing, and the temperature in the mixing container is controlled by an ice-water bath to 11±1 °C. The mixed liquid flows into the primary reactor with stirring paddle through the overflow port in the middle of the mixer. At the same time, isobutene with a purity of 99.78% is vaporized and then added to the primary reactor at a flow rate of 28.8g / h. The reactor is controlled by a water bath The internal temperature is 39±1°C. The mixed liquid flows into the secondary reactor with a stirring paddle through the overflow port in the middle of the primary reactor, and at the same time, isobutene with a purity of 99.78% is vap...
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