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   沉淀塔 的翻译结果: 查询用时:0.473秒
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沉淀塔
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  settling column
     Settling column of fluidized bed and its applications in precipitation of high quality coarse diuranate are described.
     介绍了流化床沉淀塔在沉淀优质粗粒重铀酸盐工业生产中的应用结果。
短句来源
  sediment tower
     Oriental Demolishing of a Coal-washing Building and a Sediment Tower
     洗煤楼和沉淀塔的控爆拆除
短句来源
     A New Type Sediment Tower White Water Reclaiming System
     新型沉淀塔白水回收系统成功投入应用
短句来源
     Successful application of a new type sediment tower white water reclaiming system indicates that advanced tower structure and a white water reclaiming system in accordance with the production process are most important.
     新型沉淀塔白水回收系统对单台和两台纸机的成功实践表明,选择和设计较为先进的沉淀塔结构,并根据本单位生产工艺,设计适应沉淀塔工作特点的白水回收系统至关重要。
短句来源
  settling tower
     And a new method for calculating the diameter of thickening equipment with central feeding, such as, rake thickener, deep cone thickner, settling tower, thickening hopper etc, according to properties and states of fluid movement proposed by the author.
     并应用其运动性状提出了计算耙式浓缩机、深锥浓缩机、沉淀塔和浓缩漏斗等中央给料浓缩设备的直径计算新方法。
短句来源
  “沉淀塔”译为未确定词的双语例句
     The diameter and height of testing fluidized-bed are 400 mm and 3200 mm. It has a simple structure and adaptability for concentration variation of solution. The operation is easy and steady and it will have a broad application in the industry.
     试验用流化床沉淀塔直径为400mm,高3200mm,结构简单,易稳定操作,对料液浓度变化适应性强,具有广阔的工业应用前景。
短句来源
     The diameter and height of the tested fluidized-bed equipment were 400 mm and 3200 mm. Its structure was simple, and it had good adaptabilily for variation in the solution concentration. It was operated easily and steadily and it will be expected to have broad industrial use.
     实验用流化床沉淀塔直径为400mm,高3200mm,结构简单,易稳定操作,对料液浓度变化适应性强,具有广阔的工业应用前景。
短句来源
     When PAC and CG_A were used synergistically, the number of total particulates of final effluent was 11000 per liter, membrane factor (MF) value was 40~60, however, in a similar way except that CG_A was omitted, the two values of disposed wastewater were 68000 and 13~16 respectively. The experiment results showed that CG_A and fluidized sedimentation tower were very efficient in removing superfine particulates from water.
     当单独投加PAC时 ,出水的微细颗粒数为 6 80 0 0个 /L ,滤膜系数为 13~ 16 ,而PAC与CG~A配合使用时 ,出水的微细颗粒数为 110 0 0个 /L ,滤膜系数为 40~ 6 0 ,显示CG~A和流化床沉淀塔具有良好的去除超微细颗粒的能力 . 还讨论了强化混凝的机理 .
短句来源

 

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      settling column
    A simple procedure, using settling column experiment data, for calibration is proposed.
          
    The characteristics of the settling curve, and the possibility that it is influenced by the height of the settling column of solids, can be predicted from yield stress measurements.
          
    Settling velocities of Humber-Ouse SPM, sampled in situ and measured using a settling column, maximized at 1.5?mm s-1 and exhibited hindered settling at higher SPM concentrations.
          
    A study was carried out in a specially designed settling column to investigate the settling characteristics of effluents arising from Karachi tanneries.
          
    vs loading rate and detention time were constructed using data obtained from settling column.
          
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      settling tower
    The method is called the 'settling tower' and consists in taking sequential pictures of particles falling under gravity in calm air.
          
    The mean Vs was measured with the 'settling tower' with less than 12% error, while the standard deviation of the Vs distribution was estimated with less than 51% error.
          
    The reason for the small overestimation of Vs for Lycopodium spores by the 'settling tower' method is discussed.
          
    Preliminary measurements shows that, the 'settling tower' could be of great practical interest for measuring the distribution of Vs of maize pollen as well as other types of pollen or spores.
          
    The settling velocity of suspended particles near the bottom was measured with the use of a settling tower in the laboratory.
          
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    The formulae for designing the thickening equipment both in this country and abroad are not based on the properties and states of fluid movement. This paper describes properties and states of fluid movement by using "potential function", "flow function", continuity equation and Laplacian equation established by fluid mechanics. And a new method for calculating the diameter of thickening equipment with central feeding, such as, rake thickener, deep cone thickner, settling tower, thickening hopper etc, according...

    The formulae for designing the thickening equipment both in this country and abroad are not based on the properties and states of fluid movement. This paper describes properties and states of fluid movement by using "potential function", "flow function", continuity equation and Laplacian equation established by fluid mechanics. And a new method for calculating the diameter of thickening equipment with central feeding, such as, rake thickener, deep cone thickner, settling tower, thickening hopper etc, according to properties and states of fluid movement proposed by the author.

    国内外浓缩设备直径的设计公式,没有从浓缩设备内流体运动的性质和状态出发建立物理基础,为此,本文根据流体力学中“势函数”、“流函数”、连续性方程式和拉普拉斯方程式论述了浓缩设备中流体的运动性状。并应用其运动性状提出了计算耙式浓缩机、深锥浓缩机、沉淀塔和浓缩漏斗等中央给料浓缩设备的直径计算新方法。

    The process of preparing ammonium diuranete with high quality and coarse grain is presented,which was precipitated by fluidization technique in sulfuric acid-ammonium sulfate or sulfuric acid-chloride solution system. In sulfuric acid-ammonium sulfate solution system, the product produced by conventional agitation-precipitation method contains 63. 18% of U and 13. 3%of SO42-, and the percentage of particles with diameter >40/zm is 33. 91%. Under the optimum conditions with fluidization techique the values are...

    The process of preparing ammonium diuranete with high quality and coarse grain is presented,which was precipitated by fluidization technique in sulfuric acid-ammonium sulfate or sulfuric acid-chloride solution system. In sulfuric acid-ammonium sulfate solution system, the product produced by conventional agitation-precipitation method contains 63. 18% of U and 13. 3%of SO42-, and the percentage of particles with diameter >40/zm is 33. 91%. Under the optimum conditions with fluidization techique the values are 69. 94%,3. 7% and 75. 87% respectively. In the sulfuric acid-chloride solution system,the product obtained by agitation method in factory contains 58% of U and 5% of Cl-, and the percentage of particles size >40um is 1. 6%. By using fluidization method the values are 68%,0. 22% and 41. 46% respectively. The diameter and height of testing fluidized-bed are 400 mm and 3200 mm. It has a simple structure and adaptability for concentration variation of solution. The operation is easy and steady and it will have a broad application in the industry.

    论述了采用流态化技术从硫酸-硫酸铵、硫酸-氯化物溶液体系中沉淀制取优质、粗粒重铀酸铵的研究工作。在硫酸-硫酸铵溶液体系中,铀工厂常规搅拌沉淀产品含U63.18%,SO_4~(2-)13.3%,产品粒度≥40μm者占33.91%;采用流态化技术沉淀,在最佳条件下,沉淀产品含U69.94%,SO_4~(2-)3.7%,产品粒度≥40μm者占75.87%。在硫酸-氯化物溶液体系中,铀工厂常规搅拌沉淀产品含U58%,Cl~-5%产品粒度≥40μm者只占1.6%;采用流态化技术沉淀产品含U68%,Cl~-0.22%,产品粒度≥40μm占41.46%。试验用流化床沉淀塔直径为400mm,高3200mm,结构简单,易稳定操作,对料液浓度变化适应性强,具有广阔的工业应用前景。

    The process of preparing ammonium diuranete with high quality and coarse grain is presented, which was precipitated by fluidization technique in sulfuric acid-ammonium sulfate or sulfuric acid-chloride solution system. In sulfuric acid-ammonium sulfate solution system, the product produced by conventional agitation-precipitation method contains 63. 18% of U and 13. 3%of SO42-, and the percentage of particles with diameter>40 um is 33. 91%. Under the optimum conditions with fluidization techique the values are...

    The process of preparing ammonium diuranete with high quality and coarse grain is presented, which was precipitated by fluidization technique in sulfuric acid-ammonium sulfate or sulfuric acid-chloride solution system. In sulfuric acid-ammonium sulfate solution system, the product produced by conventional agitation-precipitation method contains 63. 18% of U and 13. 3%of SO42-, and the percentage of particles with diameter>40 um is 33. 91%. Under the optimum conditions with fluidization techique the values are 69. 94% ,3.7% and 75. 87% respectively. In the sulfuric acid-chloride solution system,the product obtained by agitation method in factory contains 58% of U and 5% of Cl-, and the percentage of particles size >40 um is 1. 6%. By using fluidization method the values are 68%,0. 22% and 41. 46% respectively. The diameter and height of testing fluidized-bed are 400 mm and 3200 mm. It has a simple structure and adaptability for concentration variation of solution. The operation is easy and steady and it will have a broad application in the industry.

    论述了采用流态化技术从硫酸-硫酸铵、硫酸-氯化物溶液体系中沉淀制取优质、粗粒重铀酸铵的研究工作。在硫酸-硫酸铵溶液体系中,铀工厂常规搅拌沉淀产品含U63.18%,SO_4~(2-)13.3%,产品粒度≥40μm者占33.91%;采用流态化技术沉淀,在最佳条件下,沉淀产品含U69.94%,SO_4~(2-)3.7%,产品粒度≥40μm者占75.87%。在硫酸-氯化物溶液体系 中,铀工厂常规搅拌沉淀产品含U58%,Cl~-5%产品粒度≥40μm者只占1.6%;采用流态化技术沉淀产品含U68%,Cl~-0.22%,产品粒度≥40μm占41.46%。试验用流化床沉淀塔直径为400mm,高3200mm,结构简单,易稳定操作,对料液浓度变化适应性强,具有广阔的工业应用前景。

     
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