首页> 外文会议>Conference on Thermophysical Properties and Transfer Processes of New Refrigerants >INTENSIFICATION OF PROCESSES IN ENERGY EXCHANGERS FOR COOLING OR HEATING OF LIQUIDS BY MEANS OF GAS BUBBLING
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INTENSIFICATION OF PROCESSES IN ENERGY EXCHANGERS FOR COOLING OR HEATING OF LIQUIDS BY MEANS OF GAS BUBBLING

机译:通过气泡冷却或加热液体的能量交换器中的过程的增强

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In the traditionally applied heat exchangers the energy of cold and heat is transferred to users through a metal impermeable wall. Such a low effective method of energy transfer in combination with bulky and a high metal-intensity of these heat exchangers results in large expenditures of energy carriers both for their manufacturing and exploitation, and heat and cold production. In its turn, it results in additional fuel burning up. In many processes and technologies such heat exchangers can be replaced by the ones with using of bubbling of gaseous energy carrier through the cooled or heated users as liquids or gases. The energy carrier is supplied through the perforated surface in the volumes of users. Such energy exchangers are the alternative ecological safety and energy saving ones. The intensity of heat-and mass transfer increases by the factor of 20-500 in comparison with traditional heat exchangers by means of creation of specific hydraulic-acoustic regimes in two-phase gas-liquid mixture of bubbling gases and cooling or heating liquids. Here, the formed bubbles bubble the liquid in oscillating-pulsating regime. The rate of energy transfer can reach 24000 W/(m{sup}2·K) instead of 200-400 W/(m{sup}2·K) for the heat exchanger with heat transfer through the metal impermeable wall. Therefore, for transmission of one and the same amount of energy in comparable designs of energy exchangers the surface of the bubbler can be decreased by a factor of 100-200. Such energy exchangers result in enormous saving of fuel, energy carriers, metals, financial and human-effort expenditures in different branches of machine-building and petrochemical industries, as well as in processing products and of storing.
机译:在传统上施加的热交换器中,冷热的能量通过金属不可渗透的墙壁转移到用户。这种较大的能量转移的这种低有效的能量转移方法和这些热交换器的高金属强度会导致能量载体的大量支出,用于制造和剥削,以及热和冷轧。轮到它,它会导致额外的燃料燃烧。在许多过程和技术中,这种热交换器可以由与使用气态载体的鼓泡通过冷却或加热的用户作为液体或气体来代替。能量载体通过穿孔表面供应在用户体积中。这种能量交换器是替代生态安全节能和节能。与传统的热交换器通过在起泡气体和冷却或加热液体的两相气体混合物中的产生特定的液压声制度的形成,热量和传质的强度增加了20-500倍。这里,形成的气泡在振荡脉动状态下气泡液体。热交换器通过金属不可渗透的墙壁,能量传递速率可以达到24000W /(M {SUP} 2·k)代替200-400W /(M {SUP} 2·k),热交换器具有传热。因此,为了在能量交换器的相当设计中传输一种和相同的能量,可以降低推泡剂的表面100-200倍。这种能量交换机导致机器建设和石化行业的不同分支机构的燃料,能源载体,金属,金融和人力努力支出的巨大节省,以及加工产品和储存。

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