The biogas yield and hydrogen yield increased with the increasing of OLR in CSTR.
在连续流反应器中，发酵气体产量和氢产量随负荷的增加而升高；
The control of process such as CSTR reactor can be very difficult due to their highly nonlinear nature.
对于像CSTR化学反应器的控制，由于其过程本身的严重非线性而变得十分困难。
The models of the non-isothermal CSTR and estimating algorithms have deen verified successfully at a pilot plant.
并把非等温过程模型的搅拌反应器模型和估计算法应用于实验装置上。
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