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Improving the Efficiency of Water Purification from Dissolved Gases at TPP

机译:在TPP提高溶解气体中水的净化效率

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The method for increasing the efficiency of thermal deaerators and calciners of a TPP is considered; it consists of the use of a turbulent mass transfer device with random small packing. Before entering the packed bed in water, air (decarbonization) or water vapor (deaeration) is supplied. Chaotic nozzle creates intense turbulent interaction mode of air (vapor) with water and splitting it into small bubbles; thus the specific surface area of the contact of phases significantly increases, and high efficiency of mass transfer (extraction of dissolved gases) is ensured. A turbulent mass transfer device is a circular channel with connections for connecting of the source water to a pipeline. Inzhekhim chaotic nozzle is used with large free volume (95%) and the specific surface area of 150-300 m~2/m~3. The nozzle is made of a thin metal strip that may have a rough surface and is retained in the channel by means of two grids. For the calculation of turbulent mixer, mathematical model of the flow structure is presented, which is built with the use of a one-parameter diffusion model and a semiempirical reverse mixing ratio. Accounting of interphase transfer of dissolved gases is carried out via volume source of weight. The equation to determine the weight source and calculation of its parameters is presented. In the particular case, transition to the cell model is made and an expression for calculating the profile of concentrations of dissolved gas is obtained along the channel with a nozzle. An example of calculating the efficiency of turbulent mixer upon removing dissolved carbon dioxide from water at a TPP is shown. Recommendations on the use of the considered technical device are given.
机译:考虑了提高TPP的热脱气炉和煅烧炉效率的方法;它包括使用带有随机小填料的湍流传质装置。在水中进入填充床之前,需要提供空气(脱碳)或水蒸气(脱气)。混沌喷嘴在空气(蒸气)与水之间形成强烈的湍流相互作用模式,并将其分裂成小气泡;因此,相接触的比表面积显着增加,并确保了高效率的传质(溶解气体的萃取)。湍流传质装置是带有用于将源水连接到管道的连接的圆形通道。 Inzhekhim混沌喷嘴使用的自由体积大(95%),比表面积为150-300 m〜2 / m〜3。喷嘴由金属薄带制成,该金属带可能具有粗糙的表面,并通过两个栅格固定在通道中。为了计算湍流混合器,给出了流动结构的数学模型,该模型是使用一参数扩散模型和半经验反向混合比建立的。溶解气体的相间转移的计算是通过体积重量源进行的。给出了确定重量来源及其参数计算的公式。在特定情况下,转换为单元模型,并使用喷嘴沿通道获得用于计算溶解气体浓度分布的表达式。示出了在TPP处从水中除去溶解的二氧化碳时计算湍流混合器效率的示例。给出了有关使用所考虑的技术设备的建议。

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