本文分两部分。分别探讨鼓泡搅拌槽内的气液分散和传质特性。
This paper consists of two parts dealing with gas-liquid dispersion and mass transfer characteristics in stirred vessel.
论文针对环己烷液相无催化氧化的五釜串联鼓泡搅拌反应器生产装置(BSTR)，建立了氧化装置的过程数学模型。
A model of five-bubble-stirred-tank reactor (BSTR) for industrial uncatalyzed oxidation process of cyclohexane was established to predict and optimize the the industrial production.
比较了环流反应器、槽式搅拌反应器、鼓泡塔式反应器对白油收率和质量的影响。
The influence of the internal circulating reactor on yield and quality of white oil is compared with that of circulating reactor, gate agitatingreactor and bubbling tower reactor.
应用推荐