The present invention relates to a supercritical carbon dioxide generation system of a parallel recuperative type capable of enhancing power generation efficiency and reducing costs. The supercritical carbon dioxide generation system of a parallel recuperative type according to the present invention can maximize work of a turbine by increasing a compression ratio of the turbine since recuperators are arranged in parallel. Moreover, the supercritical carbon dioxide generation system can maximize heat exchanging efficiency through distribution of a flow rate since heat transfer temperature distribution among a plurality of heaters and a high temperature part and a low temperature part of the recuperators is uniform. Even if there is a temperature difference of a high temperature fluid outlet between two recuperators, a mixing effect toward the low temperature part is insignificant since the recuperators are arranged in parallel, and there is no risk in operation since a free cooler maintains inlet temperature of a compressor by a flow rate of a cooling source. Furthermore, the supercritical carbon dioxide generation system can reduce costs since UA of a heat exchanger is small when generating the same power in comparison with existing cycles. The supercritical carbon dioxide generation system comprises: a compressor for compressing working fluid; a plurality of heat exchanger for receiving heat from an external heat source and heating the working fluid; a plurality of turbines operated by the working fluid; a plurality of recuperators, which are mounted in parallel and exchange heat between the working fluid passing the turbine and the working fluid passing the compressor and cool the working fluid passing the turbine; and a free cooler for cooling the working fluid first cooled in the recuperators to supply to the compressor.
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