原水将被反渗透膜组件脱盐。
膜组件具有一定的重量。
本文也探讨了膜组件的优化设计、膜污染等问题。
The design and optimization of membrane distillation units and membrane pollution are also studied in this paper.
通过膜组件的空气，可以用于膜蒸馏渗透液的冷却。
Air passing through a membrane component can be used for cooling membrane distillation penetrating fluid.
本实用新型涉及一种中空纤维压力式生物反应膜组件。
The utility model relates to a hollow fiber pressure biological reaction membrane component.
中空纤维膜组件浸没于有效体积为27l的生物反应器中。
A hollow fiber membrane module was immersed in bioreactor having 27l of working volume.
通过对膜过程、膜以及膜组件的介绍，概述了膜分离技术。
Information on membrane separation techniques, membrane processing, the membranes and its components was reviewed.
缠绕式膜组件消除了沟流现象，并有利于壳程流体的径向混合。
With helical wound module, channeling phenomenon can be relieved, and hollows fiber membranes can act as spacer in the shell.
研究了膜组件构造、膜曝气、反冲洗和化学清洗对膜污染的影响。
The effect of membrane unit construction, membrane aeration, back washing, and chemical cleaning on membrane fouling was investigated.
一种中空纤维膜组件封装外壳，解决提高封装效率，改善封装效果。
The utility model relates to a packaging housing for a hollow fiber membrane assembly, which raises packaging efficiency and improves packaging effect.
最后通过对膜组件的清洗，探讨了膜污染的原因和膜清洗的有效方法。
Analysis the characteristics of Membrane Bioreactor, this thesis discusses the plasma modified membrane modules for the treated effects of domestic wastewater.
本论文建立了膜组件分立的沸石膜乙苯脱氢模试装置，年产量25吨。
In this paper, a module-separated ethylbenzene dehydrogenation reactor is set up, which can produce 25 tons styrene per year.
膜组件可直接浸没在生物反应器内；也可将膜组件设在生物反应器外。
Themembrane assembly may be immersed directly inside or set outside the biological reactor.
本发明公开了一种污水脱氮控制方法及反应装置、生物膜组件、反应器。
The invention discloses a sewage denitrification control method, a reaction device, a biological membrane assembly and a reactor.
膜组件运行操作方式对获得稳定的膜通量，延缓、降低膜污染至关重要。
The membrane operational modes are of great importance to producing a satisfied filtrate flux, and lessening membrane fouling.
在使用超滤装置之前，请务必阅读以下关于膜组件注意事项，并请遵照执行。
Before using super filer device, make sure reading the notice following about membrane subassembly and obeying it.
而组件单元装置是由框式中空纤维膜组件、框式换热组件、气液分离器组成的。
A unit device consists of frame type hollow fiber membrane units, frame type heat exchange units and gas-liquid separators.
膜生物反应器工艺中，系统构型、膜组件和生物反应器是中试设计中的关键因素。
The process configuration, membrane module and bioreactor are the critical elements of a membrane bioreactor (MBR) design.
研究了错流方式的板式膜组件的切向流速、时间、压力、温度等对渗透通量的影响。
The effects on flux of tangential flow rate, time, pressure and temperature were investigated.
膜材料选用了聚酰亚胺，膜组件类型选用了中空纤维，膜过程操作方式选用了加压式。
Membrane material USES polyimide, the model of module USES hollow fiber, the process of practicing USES pressure process.
本实验选用普通的工业滤布来制作动态膜组件，首先研究了操作简便的自生生物动态膜。
In this thesis, the membrane module was made up of common filter cloth, and the self-forming bio-dynamic membrane (SFDM) was studied in the first because of its simple and convenient manipulation.
本系统将压缩、吸收工艺和膜分离法有机结合，减少了膜组件的数量，降低了装置成本。
The system combines the compressing and absorbing technique with the membrane separating method organically, reduces the quantity of the membrane component and reduces the cost of the device.
分析了MBR运行的进水要求和污泥特征，阐述了不同膜组件布置方式下的沉积层控制方法。
The hydraulic condition and sludge character of MBR are analyzed, the methods to control depositing layer with different arrangement plan of membrane module are expounded.
采用水力计算方法对中空纤维膜组件进行优化设计，发现膜的几何尺寸对产水量的影响很大。
In optimization design for hollow fiber membrane module by using hydraulic calculation, it was found that the geometric dimension has great effect on water yield.
根据试验提出了“并联运行的平板膜组件中，通量最大的膜优先衰减且衰减幅度最大”的观点。
A viewpoint that the flux of membrane with the largest flux in parallel-operated modules would decrease first was presented.
指出了高性能膜的研制以及膜组件的改进将会使渗透汽化法在燃料乙醇生产中得到更加广泛的应用。
It was pointed out that pervaporation will be used more widely in anhydrous ethanol production with the development of high performance membrane and the improvement of membrane modules.
端面自锁连接卷式反渗透膜组件在严重污染的进水水质条件下性能稳定，具有很好的清洗恢复性能。
The spiral-wound reverse osmosis membrane elements with iLEC interlocking endcaps show stable performance and very good cleaning…
利用“通量阶式递增法”测定了两种膜组件的临界通量，在此基础上考察了次临界通量下的运行特性。
Critical flux region for two membrane modules was measured by using "flux step-wise" method, and then the operating characteristics at sub-critical flux were investigated.
利用“通量阶式递增法”测定了两种膜组件的临界通量，在此基础上考察了次临界通量下的运行特性。
Critical flux region was measured by using "flux step-wise" method, and the the operating characteristics at sub-critical flux were investigated.
利用“通量阶式递增法”测定了两种膜组件的临界通量，在此基础上考察了次临界通量下的运行特性。
Critical flux region was measured by using "flux step-wise" method, and the the operating characteristics at sub-critical flux were investigated.
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