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4.1 Apparams for heal: exc 1anger testing 43 first cross-over valve at r00111 temperature. On exiting the reversing heat exchanger it passes through the second cross-over valve and into the CO2 sublilTIing heat exchanger (C02-MHE . On exiting the C02-MHE the gas stremTI is divided into two parts. One part passes through the by-pass valve and enters the return channel of the C02-1vIHE. The other part is diverted through the LN2 heat exchanger valve, and thl'ough the liquid nitrogen ' eat exchanger (LN2-HX). The LN2-HX is simply a copper tube imillersed in a LN2 bath. The proportion of the fluid iverted through the LN2-HX is controlled by the by-pass and LN2-HX valves. The combined stream then flows through the return channel of the C02-MHE, through the second cross-over valve, through the return chmmel of the H20 -MHE and is exhausted to atmosphere tlu'ough the first cross-over valve. Plate 4.1 Photograph showing overall apparatus layout. The cross-over valves l11ay be rotated through 90° using the actuator. They' are both rotated simultaneously . Every rotation of the cross-over valves swaps or reverses the inlet and outlet streams of the H20-MHE while retaining unidirectional flow in the C02-MHE. The liquid nitrogen bath is thermally shielded by a second liquid nitrogen bath referred to as the outer bath or guard vessel. This is done to n1inilllise boil-off in the inner bath, due to heat leak from the surroundings. The heat exchangers, cross-over valves, actuator by-pass and LN2-HX valves, and LN2 baths are suspended inside, fron1 the lid of, a stainless steel VaCUUlTI vessel. ThePDF Image | CO2 removal from air for alkaline fuel cells operating with liquid H2
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