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1·The precise model of the CSTR is not necessary for design of control system.

控制系统的设计不需要CSTR系统的精确模型。

2·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；

3·A small discrepancy is due to the fact that the RNN only approximates the first-principles CSTR model.

一个小的差异是由于这样的事实，RNN CSTR采用的仅仅是近似模型。

4·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。

5·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。

6·Two limiting conditions of thermal stability in the design of continuous-flow stirred tank reactor (CSTR) were developed.

给出了全混流反应器定态热稳定性对全混流反应器设计的两个限制条件。

7·The nonlinear dynamic equation of CSTR can be built on the basis of materiel equivalency by the mechanism modeling method.

连续搅拌反应釜可以根据反应物料的衡算式建立非线性动力学方程。

8·When the same amount of organic matters is removed from all compartments, the longer HRT will result in CSTR flow pattern.

当各格室去除有机物量相同时，HRT越长则其混合流态越趋于CSTR流态。

9·The strategy based global feedback linearization for nonlinear system is developed for continuous stirred tank reactor (CSTR).

针对典型化工非线性对象连续搅拌槽反应器（CSTR） ，研究了基于反馈线性化的预测函数控制方法。

10·Plug flow reactor(PFR) and Continuous stirred tank reactor(CSTR) were studied to compare their performance for treating dairy manure.

对推流式反应器（PFR）和完全混合式反应器（CSTR）用于牛粪液厌氧消化的性能进行了比较研究。