首页> 外国专利> Heat transfer using closed thermal fluid circuit, to and from pressure swing adsorption or vacuum swing adsorption plant for oxygen enrichment, comprises use of phases of unequal energy flowrate

Heat transfer using closed thermal fluid circuit, to and from pressure swing adsorption or vacuum swing adsorption plant for oxygen enrichment, comprises use of phases of unequal energy flowrate

机译:使用闭合的热流体回路与变压吸附或真空变压吸附装置之间进行热交换以富集氧气,包括使用能量流率不相等的相

摘要

Continuous heat transfer in either direction, to and from a thermal recirculation circuit (4), employs a second energy flow, smaller than a first. The ratio of the second to first is at least the ratio of the active phase duration to that of the cycle. In the active phase, continuous heat transfer employs thermal heat exchange fluid leaving the main heat exchanger (12), whilst an energy flow equal to the difference between the two energy flows is stored in the form of a volumetric buffer of heat exchange fluid. During the inactive phase, continuous heat transfer is carried out using heat exchange fluid accumulated during the active phase. An Independent claim is included for the corresponding heating and cooling circuit. Preferred Features: The fluid is recirculated in closed circuit. In a slight variant, continuous heat exchange (extraction or introduction) is carried out by an auxiliary heat exchanger (24) placing thermal fluid accumulated, in thermal exchange with an auxiliary fluid. During the active phase, thermal exchange fluid is accumulated (34A,34B) equal to the volume of heat exchange fluid required by the main heat exchanger (12) during the active phase. The active phase lasts at least half the cycle duration.
机译:在任一方向上往返于热循环回路(4)的连续传热采用的是第二能量流,该能量流小于第一能量流。第二与第一的比率至少是有效阶段持续时间与循环的持续时间之比。在活动阶段,连续传热采用离开主热交换器(12)的热交换流体,而等于两个能量流之差的能量流以热交换流体的体积缓冲液形式存储。在非活动阶段期间,使用在活动阶段期间积累的热交换流体进行连续的热传递。相应的加热和冷却回路包括独立索赔。首选功能:流体在封闭回路中再循环。在一个小的变型中,通过辅助热交换器(24)进行连续的热交换(提取或引入),该辅助热交换器(24)放置积聚的热流体,与辅助流体进行热交换。在活动阶段期间,热交换流体积聚(34A,34B),等于活动阶段中主热交换器(12)所需的热交换流体的体积。活动阶段至少持续一半周期。

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