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.
它也用来关闭反应器，可以从100%的动力降到7%动力（残留的延迟的热量造成）。
The control rods are also used to shut the reactor down from 100% power to about 7% power (residual or decay heat).
利用化学反应器模型及理论可以定量地描述动物的消化过程，阐述动物采取的消化对策和分析食物的消化动力等。
Chemical reactor model is very useful to characterize the animal gut quantitatively and help us to interpret the digestive strategies of animals.
与厌氧-缺氧-好氧-缺氧连续式短程生物脱氮工艺比较，反应器的总体积可以缩小20%，曝气动力消耗可以节省30.8%。
Compared with anaerobic-anoxic-oxic continuous process, the process in this paper will be reduced by 20% in volume and 30.8% in power consumption.
中浓纸浆在升流式反应器中的流体动力学性能影响到反应器的反应质量和反应器前后设备的设计及选型。
The flow dynamics property of medium consistency pulp in up-flow re actor affects the reaction quality and design and selection of the devices prior to and after the reactor.
引入莫诺特方程建立了反应器基质降解的数学模型，并测出其动力学参数。
Using monod equation built mathematical model describing organic compound degradation in reactor and measured its dynamics parameters.
本文介绍了当前多相光催化反应体系中反应动力学模型以及反应器数模研究领域内的主要方法及成果。
This article introduces the main existing methods and achievements in the field of the math models of reaction kinetics and reactor of the heterogeneous photocatalysis reaction system.
以C100型阳离子交换树脂作为催化剂，在间歇搅拌釜式反应器中测定了甲醇和醋酸合成醋酸甲酯的本征反应动力学。
The main work is as followings:The kinetics of the synthesis of methyl acetate was measured in a batch stirred reactor with C100 cation exchange resin as catalyst.
在固定床加压反应器和加压热天平上，对五种中国气化用煤及其煤焦进行了加氢气化的动力学研究。
Kinetic characteristics of hydrogasification for five Chinese coals and their chars are investigated at pressure using a fixed-bed reactor and a thermobalance.
采用积分反应器，研究了吡啶氯化反应中催化剂失活动力学。
The catalyst deactivation kinetics of pyridine chlorination was investigated in an integral fixed reactor.
本文阐述了醚化反应器的特点及其动力学反应器的计算方法，并分析了影响醚化反应器的主要因素。
The properties of methyltertiarybutyl ether reactor and the calculation methods of the kinetic reactor are introduced. The major factors which effect the reactor are analyzed.
采用自行研制的微分型种分反应器，在较为单一的条件下了研究铝酸钠溶液中的晶体长大动力学。
The kinetics of crystal growth was studied with a self-designed differential reactor that can be performed on a relatively single condition.
描述了在批式反应器和连续流搅拌反应器(CSTR)中酶动力学拆分对映异构体的不同之处。
The difference between a continuous stirred tank reactor (CSTR) and a batch reactor was analyzed for the enzymatic kinetic resolution of enantiomers.
与L - h模型相比较微观动力学在反应器的设计模拟工作中有更广的适用范围。
The application range of micro kinetics is wider than L-H model in simulation design of reactors.
温度动力学基于反应器的热量平衡。
The temperature model was based on a heat balance of reactor.
在直流流动积分反应器中常压下研究了C207催化剂甲醇分解反应本征动力学。
The intrinsic kinetics of the methanol decomposition at atmospheric pressure over C207 catalyst are studied in a tubular-flow integral reactor.
采用等温积分反应器，测试了KD306型耐硫甲烷化催化剂的本征动力学，建立了幂函数动力学模型。
The intrinsic kinetics of KD306 type sulfur tolerant methanation catalyst was studied in an isothermal integrated reactor and the reaction model of power functions type was established.
反应动力学对反应器操作的多态起着重要作用。
Reaction kinetics was found to play an important role in the multiplicity of states.
从探讨丙烯聚合工艺中环管反应器流体动力学模型着手，介绍环管反应器循环泵功率的计算方法。
A fluid dynamical model of the materials in a loop reactor for polypropylene production is suggested and the power of the circulating pump of the reactor is calculated by means of Newitt correlation.
本文根据AAFEB反应器特性，建立了AAFEB反应器的过程动力学模型。
Based on characteristic of AAFEB reactor, the process kinetic models of AAFEB reactor have been developed in this paper.
探讨了生物接触氧化反应系统降解有机物的反应动力学模式，并给出了各反应器的动力学参数和方程。
The kinetics model of bio-contact oxidation to decompose organic matter was probed into, and the kinetics parameter and kinetics equation were obtained.
常压下使用等温积分反应器研究了B110中温变换反应的本征动力学模型。
The intrinsic kinetic model of shift reaction over B110 high-temperature shift catalyst has been investigated in an isothermal integral-reactor.
目的研究一体式膜生物反应器（IMBR）中活性污泥增殖动力学参数随温度的变化规律。
The experiment systematically studies the activated sludge in IMBR which has the tendency of following the temperature change.
采用固定床恒温积分反应器，对YS—6型银催化剂进行乙烯氧化本征动力学研究。
Research for intrinsic kinetics of ethylene oxidation on the YS-6 Silver Catalyst is done by using a fixed bed constant temperature integral reactor.
对气液强相互作用下滴流床反应器内的流体动力学进行了分析讨论。
The theoretical analyses of the hydrodynamics under a strong interaction flow regime were conducted and data of the bed averaged dynamic liquid holdup were obtained.
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.
研究了在复合环流反应器中，用络合铁催化剂液相催化氧化脱除H2S的吸收反应动力学、催化剂再生反应动力学及吸收-再生反应联合动力学。
The reactors were applied to liquid-phase-reactive absorption of H2S with ferric coordination compound as catalyst. Kinetics of reactive absorption and catalyst regeneration were investigated.
本文针对催化裂化工业装置的提升管反应器以三集总催化裂化反应动力学模型为基础，利用工业装置的现场数据对模型中的参数进行了拟合。
Based on three lumping kinetic model of catalytic cracking, the parameters in the model are estimated with actual operation data of a commercial catalytic cracking riser.
本文针对催化裂化工业装置的提升管反应器以三集总催化裂化反应动力学模型为基础，利用工业装置的现场数据对模型中的参数进行了拟合。
Based on three lumping kinetic model of catalytic cracking, the parameters in the model are estimated with actual operation data of a commercial catalytic cracking riser.
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