Study on the photocatalytic degradation of 13 kinds of benzoic acids in the fixed film flat-plate reactor have been conducted.
研究了13种苯甲酸类化合物在固定膜平板型反应器中的光催化降解。
The application of plate heat exchanger in heavy water system gives good experience for future research reactor design.
板式换热器在重水系统中的应用对研究堆的设计具有一定的参考价值。
The pressurized vessel of a nuclear reactor consists of three parts: the top cap, the ribbed tube-plate and the shells (the external shell and the bottom shell).
反应堆压力容器包括顶盖、加肋管板，壳体(外壳和底部壳体)三部分。
At a given electric field intensity when the wire-wire spacing is 0.6-1 times that of the wire-plate, the utilization of pulsed energy by the reactor will reach a maximum value.
在电场长度一定下，线线间距为线板间距的0.6 ~1倍时，反应器对脉冲能量的利用达到最大。
The influence of the electrode configuration of a wire-plate pulse corona discharge-based desulfurization reactor on pulsed energy utilization is investigated by tests.
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。
Using an inclined plate gas-liquid-solid separator UASB reactor followed by a biological contact oxidation process to treat fruit juice-producing wastewater, and excellent result is achieved.
采用斜板三相分离器uasb -生物接触氧化串联工艺处理果汁生产废水的工程实践，取得了良好的效果。
T he result that the presence of dielectric plate inside CGG changes the mode order will be useful for the design of the microwave chemical reactor based on CGG.
分析表明介质加载时圆形槽波导的模式次序要发生变化，为设计圆形槽波导微波化学反应器提供了依据。
A flat plat fixed-bed reactor for gas purification was designed, its structure, working principle, function of screen plate, guide baffle, gas receiver and filtration cap were introduced.
设计了一种用于气体净化的平板式固定床反应器，介绍了该反应器的结构、工作原理以及网板、导向板、气体收集箱、过滤盖等组件的功能。
According to the equipment working condition, the shell of oxidative dehydrogenation reactor should select American SA240-304h steel plate.
按设备工况，氧化脱氢反应器壳体应选用美国的SA240—304h钢板。
By calculating electrostatic field in the reactors, compare electric distributions of wire - plate -, wire - cylinder, wire - wire type reactors. Thereby optimized reactor-structure can be selected.
通过计算反应器内部静态电场，比较了线板式、线筒式、线线式反应器中的电场分布，从而可以选择较优的反应器结构。
The gas hold-up, circulation ratio and the volumetric transfer coefficient of liquid in reactor with a separate plate of different sizes were investigated.
研究了不同宽度的隔板式环流反应器中的气含率，循环比和体积传递系数。
The gas hold-up, circulation ratio and the volumetric transfer coefficient of liquid in reactor with a separate plate of different sizes were investigated.
研究了不同宽度的隔板式环流反应器中的气含率，循环比和体积传递系数。
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