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    • 2. 发明授权
    • Sulfonation in continuous-flow microreactors
    • 连续流量微反应器中的磺化
    • US09227929B2
    • 2016-01-05
    • US13989277
    • 2011-11-22
    • Marc WinterFeixia Zhang
    • Marc WinterFeixia Zhang
    • C07C303/20C07C303/06
    • C07C303/20C07C303/06C07C309/46
    • A continuous flow process for sulfonating 1,2.diaminobenzene comprises introducing a sulfonation mixture into a microreactor inlet of a continuous flow microreactor to produce a flow of the sulfonation mixture through the continuous flow microreactor. The sulfonation mixture comprises 1,2 aminobenzene dissolved in a molar excess of sulfuric acid. The continuous flow microreactor comprises one or more individual fluidic modules each having various features with respect to channel width and thermal management. The process further comprises maintaining a reaction temperature of from about 150.230 deg C. in at least a portion of the individual fluidic modules while the sulfonation mixture flows from the microreactor inlet to the microreactor outlet. Thereupon, the sulfonation mixture is received from the microreactor outlet. Finally, a sulfonated reaction product is precipitated out of the sulfonation mixture received from the microreactor outlet. The sulfonated reaction product is 3,4.diaminosulfonic acid, free of doubly sulfonated impurities.
    • 用于磺化1,2-二氨基苯的连续流动方法包括将磺化混合物引入连续流微反应器的微反应器入口以通过连续流微反应器产生磺化混合物的流。 磺化混合物包含溶解在摩尔过量硫酸中的1,2氨基苯。 连续流微反应器包括一个或多个单独的流体模块,其各自具有关于通道宽度和热管理的各种特征。 该方法还包括在单个流体模块的至少一部分中保持约150.230℃的反应温度,同时磺化混合物从微反应器入口流到微反应器出口。 于是,从微反应器出口接收磺化混合物。 最后,磺化反应产物从从微反应器出口接收的磺化混合物中沉淀出来。 磺化反应产物为3,4-二氨基磺酸,不含双重磺化杂质。