对于本实验反应器，通过气体进入反应器的速率-空速来表达甲烷水合速率。
For the experimental reactor, methane hydration rate is shown by gas input rate into reactor which is called as airspeed.
在实验中，反应器工作的温度在1600度，在500次反应后降到800度，但没有破坏催化剂。
In the experiments the reactor cycled up to 1, 600c then down to 800c over 500 times, without damaging the catalyst.
在实验中，反应器工作的温度在1600度，在500次反应后降到800度，但没有破坏催化剂。
In the experiments the reactor cycled up to 1,600c then down to 800c over 500 times, without damaging the catalyst.
这些为反应器的安全评估提供了理论和实验的参考依据。
The study provided theoretical basis for the design of reactor and the optimization of process operation.
这是生物反应器工程国家重点实验室的网页。
This is the homepage of the State Key Laboratory of Bioreactor Engineering.
本实验采用厌氧折流板反应器(abr)对碱法草浆中段废水进行了水解酸化预处理的研究。
The experiment makes use of Anaerobic Baffled Reactor (ABR) in the study of hydrolysis-acidification pretreatment on alkali straw pulp bleaching effluent.
实验研究了线-板式脉冲电晕放电烟气脱硫反应器的电极结构配置对脉冲能量利用的影响。
The influence of the electrode configuration of a wire-plate pulse corona discharge-based desulfurization reactor on pulsed energy utilization is investigated by tests.
所有这些实验结果均与前文提出的生物反应器设计模型具有很好的一致性。
All the experimental data are in excellent agreement with the bioreactor design model developed in the previous paper.
本文以实验为根据，论述了机械搅拌UASB反应器处理高浓度有机废水的成功启动过程。
The paper based on experiments, describes, the start-up process of the machinery stirring UASB reactor handling the high COD concentration organic wastewater.
本实验以蓖麻油为原料，位其在一装有催化剂的不锈钢反应器中进行裂解。
In this experiment, castor oil was pyrolyzed in a stainless steel tubular reactor packed with catalyst.
分别应用热天平和管式炉反应器对废电路板的热解行为进行实验研究。
The experimental study has been done in a thermo-gravimetric analyzer(TG) and in a laboratory scale tubular furnace reactor, respectively.
对脉冲电晕法治理甲苯有机废气进行了实验，考察了放电反应器结构及参数对其性能的影响。
Using pulse corona discharge to decompose toluene in air and the structure parameters of corona discharge reactors have been studied and optimized.
以大豆蛋白生产废水为原料，对厌氧折流板反应器进行了连续流有机废水发酵产氢实验。
Hydrogen production from soybean wastewater by anaerobic activated sludge was investigated in an anaerobic baffled reactor (ABR) under continuous flow condition in this paper.
实验结果表明：采用混凝沉淀预处理，膜生物反应器与反渗透膜系统组合工艺处理印染废水具有很好的效果。
In this article dyeing waste water was pretreated by chemical coagulation, then treated by combined process of anaerobic membrane bioreactor and reverse osmosis system.
采用分置式膜生物反应器（MBR）进行去除模拟废水中a-烯基磺酸钠（AOS）的实验。
Using split type membrane bioreactor ( MBR) can achieve effective removal of alpha olefin sulfonate (AOS)in simulant wastewater.
在实验室小型固定流化床反应器上考察了工艺参数对国产GOR- Q催化剂降低催化汽油烯烃的影响。
Based on fixed fluid bed reactor and GOR Q catalyst, the influence of process parameters on decreasing gasoline olefin was studied.
对以煤基微孔碳管为组件的碳膜曝气膜生物反应器（MABR）处理高浓度氨氮污水进行了实验研究。
The treatment of high concentration ammonia wastewater by a membrane aeration biological reactor(MABR) made of coal-based carbon tube membrane was studied in laboratory scale.
实验结果表明，该装置与加压积分反应器相比，具有简单、快速、省钱等优点。
The results show that this method is simpler, quicker and lower in cost than the pressure-integral reactor system.
在丁烯氧化脱氢反应过程的开发放大中，发现实验室反应器和工业规模反应器通过反应器壁的热反馈存在不同的影响。
In the developing the oxidative dehydrogenation of butene process, it is found that the effect of heat feedback through reactor wall is different between laboratory and commercial scale reactors.
在使用波导型微波化学反应器的实验研究中，多数液相化学反应都是在置于波导中心的试管或烧杯中进行。
Most of the liquid chemistry reaction could be put into a tube or a beaker inside the microwave chemistry experiment system.
实验表明：这类等离子体反应器中，旋流切向速度分量和轴向速度分量径向分布划分成近轴、过渡和近壁区。
The experimental results show that the tangential velocity and axial velocity components of the swirl flow along radial were divided into the near-axis, the transition and the near-wall zones.
在实验过程中，光电化学催化反应器中的阳极偏压由双显恒电位仪提供。
A bias-voltage between two electrodes is supplied by a potentiostat in the experiment.
研究了用交流屏障型等离子体反应器进行香烟烟雾气味控制的实验，并对结果进行了分析；
In addition, the experiments of odor control of cigarette smoke using the ac barrier-type plasma reactors were investigated and the results of the experiments were analyzed.
模型以反应器的分析为依据，用一系列连续搅拌式反应釜逼近管式反应器，并以五组实验温度分布作了校正。
A series of CSTR's were employed to simulate tubular reactor, being supplemented by checking with five sets of experimental temperature profiles.
建立反应器冷模实验装置，研究TA加氢精制反应器的流动状况。
The cold model experiment setting is set up to study the flow status for the reactor TA hydropurificafion.
在实验室小型固定床反应器上，以焦化汽油轻馏分为原料，进行了混合烯烃的叠合反应。
The oligomerization test of mixed olefins in light coke gasoline was carried out in a fixed bed reactor.
实验研究证明，通过改进搅拌的型式，改变反应器流场，能改善CHP分解反应器的温度分布。
By experiment, with changing stirring method and reactor fluid field, the temperature distribution of CHP decomposition reactor could be improved.
作者利用五个实验室规模的完全混合反应器进行较长时间的半连续培养，研究在氯化钠抑制下乙酸盐的厌氧降解。
A long-term semi-continuous cultivation was performed in five lab-scale complete mixed reactors in order to study the anaerobic degradation of acetate under NaCl inhibition.
将实验室规模的气升式反应器依照燕山化工二厂异丙苯氧化反应的生产能力进行了放大。
According to the capacity of isopropyl benzene oxidation reaction in Yansan chemical factory, the airlift reactor in our laboratory is amplified.
将实验室规模的气升式反应器依照燕山化工二厂异丙苯氧化反应的生产能力进行了放大。
According to the capacity of isopropyl benzene oxidation reaction in Yansan chemical factory, the airlift reactor in our laboratory is amplified.
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