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ECONOMIC ANALYSES AND PERFORMANCE STUDY OF THREE AMMONIA-ABSORPTION CYCLES USING HEAT RECOVERY ABSORBER

机译:利用热回收吸收器对三种氨吸收循环的经济分析和性能研究

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摘要

Economic analyses of some sources of energy, such as biogas, liquefied petroleum gas, ordinary flat plate and evacuated tubular collectors, have been carried out for operating absorption cycles with and without heat recovery absorber. Water-ammonia, NaSCN-NH_3 and LiNO_3-NH_3 have been selected as the working fluids in the cycles. Use of a heat recovery absorber, in addition to the primary absorber in the conventional absorption cycles, improves the system performances by about 20-30% in the H_2O-NH_3 mixture and 33-36% in the NaSCN-NH_3 and LiNO_3-NH_3 mixtures. Consequently, there is a considerable reduction in their energy costs. For the set of operating conditions under study, the cost is reduced by about 25% in the H_2O-NH_3 cycle and by about 30% in the NaSCN and LiNO_3-ammonia cycles.
机译:对于带有或不带有热回收吸收器的吸收循环,已经对某些能源进行了经济分析,例如沼气,液化石油气,普通平板和真空管式收集器。在循环中选择了水氨,NaSCN-NH_3和LiNO_3-NH_3作为工作流体。除传统吸收循环中的主吸收器外,还使用热回收吸收器,在H_2O-NH_3混合物中将系统性能提高约20-30%,在NaSCN-NH_3和LiNO_3-NH_3混合物中将系统性能提高约33-36% 。因此,大大降低了他们的能源成本。对于正在研究的一组工作条件,在H_2O-NH_3循环中成本降低了约25%,在NaSCN和LiNO_3-氨循环中成本降低了约30%。

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