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Process for the operation of an absorption heat pump and heat pump for the performance of the process

机译:用于操作吸收热泵的过程以及用于执行该过程的热泵

摘要

In a discontinuously operated absorption heat pump, unsaturated solvent flows in a first phase from a container (1) to a stripper (3), in which refrigerant is driven off and, after a separation in the container (1), is liquefied in a condenser (4). Heat is liberated here. During a second phase, the hot solvent flows from the container (1) through a heat exchanger (6), where heat is liberated, and back to the container (1). During a third phase, liquid refrigerant flows from the condenser (4) through an evaporator (5), where it takes up heat from the surroundings. The evaporated refrigerant then reaches the heat exchanger (6) and, in common with circulating solvent, the container (1). It is absorbed again by the solvent, heat being liberated in the heat exchanger (6). During the then succeeding fourth = first phase, a circulation from the container (1) via the heat exchanger (6) to the stripper (3) and back to the container is switched in when the solvent becomes weak in refrigerant. The heat supplied to the stripper (3) is liberated in the heat exchanger (6), i.e. a direct heating operation takes place. IMAGE
机译:在不连续运行的吸收式热泵中,不饱和溶剂在第一阶段从容器(1)流入汽提塔(3),在汽提塔中驱除制冷剂,然后在容器(1)中分离后被液化。冷凝器(4)。热量在这里被释放。在第二阶段中,热溶剂从容器(1)通过热交换器(6)流动,在热交换器中释放热量,然后返回容器(1)。在第三阶段,液态制冷剂从冷凝器(4)流经蒸发器(5),从那里吸收周围的热量。然后,蒸发的制冷剂到达热交换器(6),并与循环溶剂一起到达容器(1)。它再次被溶剂吸收,热量在热交换器(6)中释放。在随后的第四阶段,即第一阶段,当溶剂在制冷剂中变弱时,切换从容器(1)通过热交换器(6)到汽提塔(3)再回到容器的循环。提供给汽提塔(3)的热量在热交换器(6)中释放,即进行直接加热操作。 <图像>

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