用升流式石灰石滤池中和处理废水。
在升流式填料塔中，通过接种排硫硫杆菌形成稳定生物膜。
The stable bio-membrane came into being after inoculating a strain of Thiobacillus thioparus sp in aerobic up-flow packed tower.
报道了采用升流式厌氧污泥床(UASB)处理涤纶废水的试验结果。
This paper introduces the result of the research on the treatment of the terylene wastewater by UASB reactor.
介绍了升流式厌氧污泥床接触氧化工艺在处理高浓度酒精废水中的应用。
The application of UASB contact oxidation process in treating ethanol wastewater is presented.
本文根据酵母废液的水质特点，采用了常温升流式厌氧污泥床处理工艺，即温度在26。
Under normal temperature, UASB is adopted to treat yeast sewage according to yeast solution, specielty T=26.
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.
中浓纸浆是一种非常特殊的介质，中浓纸浆在升流式反应器中的运动特性关系到反应器的反应效率和反应质量。
The medium consistency pulp suspension is very special. The flow characteristic of medium consistency pulp in the up-flow reactor directly relates to the reaction efficiency and reaction quality.
利用接种了一株排硫杆菌的升流式填料塔反应器，在有氧的条件下，将水中的硫化物快速氧化为单质硫和硫酸根。
Under the condition of oxygen, some strain of microorganism is inoculated in a up-flow packed tower reactor in which the sulfide is converted into sulfur or sulfate.
对升流式厌氧-好氧曝气一体化滤池处理生活污水进行了试验研究，探讨了生物膜的形成及供气量、水力停留时间对处理效果的影响。
An experimental study of domestic sewage treatment by an integrated biological filter with up-flow anaerobic-anoxic aerated is presented in this paper.
作者利用自行研制的中浓纸浆漂白实验系统进行实验研究，对中浓纸浆在流经升流式反应器时的主要运动特性和流动机理进行了分析。
In this paper specific flow properties of medium consistency pulp in up-flow reactor at initial state of stable flow are studied and analyzed by using an equipment made by ourselves.
实验结果证实了升流式深床过滤过程中的生物反硝化反应动力学级数在1/ 2-1级之间，并与所建动力学模型基本吻合。图2，表1，参9。
The result approve that the order of reaction of bio-denitrification kinetics was about 1/2~1 and accord with the constructed model basically. 2figs. , 1tab. , 9refs.
实验结果证实了升流式深床过滤过程中的生物反硝化反应动力学级数在1/ 2-1级之间，并与所建动力学模型基本吻合。图2，表1，参9。
The result approve that the order of reaction of bio-denitrification kinetics was about 1/2~1 and accord with the constructed model basically. 2figs. , 1tab. , 9refs.
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