在通常的全动力应用下，内核里中子的产量是稳定的（保持一个数量不变），反应器处于临界状态。
During normal, full-power operation, the neutron population in a core is stable (remains the same) and the reactor is in a critical state.
既然反应器已经关闭，注入其中的硼酸数量有限以确保反应器能保持关闭的状态。
Although the reactor had been shut down, boric acid is added as a conservative measure to ensure the reactor stays shut down.
进而利用该模型及获取的参数对asbr反应器的实际运行状态进行动态模拟。
The biochemical dynamics of physical and chemical equilibrium equations and simultaneous equations, thereby establishing a complete dynamic model of ASBR reactor.
通过运用新型的内环流反应器对氯化苄光氯化反应机理和宏观状态的分析，建立了氯化苄氯化的连串反应动力学模型。
The kinetic model of consecutive reaction for chlorination of benzyl chloride was built by analyzing the reaction mechanism and macroscopic stage.
气含率和液体循环速率是气升式内环流反应器的主要流体力学特征，也是反应器运行过程中的重要状态参数。
Gas holdup and liquid circulation velocity are the mostly important hydrodynamic characters and state parameters of internal-loop airlift reactor.
利用基元反应机理数值模拟了H2／空气良好搅拌反应器（CSTR）系统的双稳定状态和点火过程。
The bistable states and ignition in an H2/air CSTR (continuous-flow stirred tank reactor) are numerically simulated based on the detailed chemistry.
流化床生物反应器动力消耗少、反应器内流化状态稳定、菌丝球可重复使用、产品易于分离纯化、生产成本较低，显示了明显的优越性。
The fluidized-bed bioreactor has advantages such as good ability of mass transport, lower energy requirement and easier purification of the product.
首先对反应器进行了气体流动模式检验实验，以确保在实际操作时，反应器内气体可以达到理想混合状态。
At first, flow pattern was tested for ensuring that the gas flow follow fully mixed pattern in actual experiment condition.
通过填料的选择、气液流动状态的比较和反应器长径比的考察，探讨了管式填料反应器中乙醛液相氧化合成过氧乙酸的新工艺。
The structure properties of tube reactor for production of DAP by means of concentration AP slurry with secondary ammoniation are investigated on experimental equipment.
通过填料的选择、气液流动状态的比较和反应器长径比的考察，探讨了管式填料反应器中乙醛液相氧化合成过氧乙酸的新工艺。
The structure properties of tube reactor for production of DAP by means of concentration AP slurry with secondary ammoniation are investigated on experimental equipment.
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