Method for continuously synthesizing PPS-OH
A technology for synthesizing hydroxypropanesulfonic acid pyridinium salt and pyridine, which is applied in organic chemistry and other fields, can solve problems such as difficulty in satisfying high-end electroplating customers, cumbersome separation process, and low production efficiency, so as to achieve suitable industrial production, reduce side reactions, and improve The effect of production efficiency
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[0029] Example 1:
[0030] Dissolve 2000g of sodium metabisulfite in 5450g of deionized water. After it is completely dissolved, add 2g of sodium sulfite and 0.2g of tetrabutylammonium bromide to the sodium metabisulfite solution. After stirring and mixing uniformly, the HSO3 - The mixed liquid is filtered through the membrane and then enters the metering pump, and then the HSO3 - The mixed solution of 1 was passed into the first microchannel reactor at a speed of 100g / min and 1910g of epichlorohydrin at a speed of 25.63g / min at the same time. The reaction temperature in the first microchannel reactor was adjusted to 50℃, and After the back pressure valve stabilizes the pressure of the first microchannel reactor at 2MPa, the reaction product in the first reaction unit of the microchannel reactor enters the second microchannel reactor, and at the same time the feed rate of 21.76g / min A mixture of 1620g pyridine and 1.62g 1,4,7,13-tetraoxa-10-aza-2,3-benzocyclopentadec-2-ene was pa...
Example Embodiment
[0032] Example 2:
[0033] Dissolve 2000g of sodium metabisulfite in 5450g of deionized water. After it is completely dissolved, add 5g of sodium sulfite and 0.4g of tetrabutylammonium bromide to the sodium metabisulfite solution. After stirring and mixing uniformly, the HSO3 - The mixed liquid is filtered through the membrane and then enters the metering pump, and then the HSO3 - The mixed solution of 1 was introduced into the first microchannel reactor at a rate of 100g / min and 1910g of epichlorohydrin at a rate of 25.62g / min at the same time. The reaction temperature in the first microchannel reactor was adjusted to 30°C, and the back pressure was adjusted. After the valve stabilizes the pressure of the first microchannel reactor at 2.5MPa, the reaction product in the first microchannel reactor enters the second microchannel reactor, and at the same time the feed rate of 21.77g / min to the second microchannel A mixture of 1620g pyridine and 3g 1,4,7,13-tetraoxa-10-aza-2,3-benzo...
Example Embodiment
[0035] Example 3:
[0036] Dissolve 2000g of sodium metabisulfite in 5450g of deionized water. After it is completely dissolved, add 3g of sodium sulfite and 0.4g of tetrabutylammonium bromide to the sodium metabisulfite solution. After stirring and mixing uniformly, the HSO3 - The mixed liquid is filtered through the membrane and then enters the metering pump, and then the HSO3 - The mixed solution of 1948g epichlorohydrin was introduced into the first microchannel reactor at a rate of 90g / min and 1948g epichlorohydrin at a rate of 23g / min. The reaction temperature in the first microchannel reactor was adjusted to 30°C, and the back pressure valve was adjusted. After the pressure of the first microchannel reactor was stabilized at 2.5MPa, the reaction product in the first microchannel reactor was allowed to enter the second microchannel reactor, and at the same time, to the second microchannel reactor at a feed rate of 22g / min Into the mixed solution of 1665g pyridine and 3g 1,4...
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