# US 10,371,015 B2 · Supercritical CO2 generation system for parallel recuperative type > Agents: this data is available as JSON from the patentgrep API and MCP server — see https://patentgrep.com/llms.txt - Number: US 10,371,015 B2 - Document ID: US10371015B2 - Status: Granted - Kind: B2 - Application number: 15/698,436 - Filed: 2017-09-07 - Published: 2018-05-24 - Granted: 2019-08-06 - Earliest claimed: 2016-11-24 - Assignees: Doosan Heavy Industries Construction Co., Ltd - Applicants: Doosan Heavy Industries & Construction Co., Ltd - Inventors: Cheol Rae Jeong; Seung Gyu Kang; Jeong Ho Hwang; Byoung Gu Bak; Eung Chan Lee - Web page: https://patentgrep.com/patent/US10371015B2 ## CPC - F01K 25/103: {Carbon dioxide (F01K25/065 takes precedence)} - F01D 15/10: Adaptations for driving, or combinations with, electric generators - F01K 13/006: {Auxiliaries or details not otherwise provided for} - F01K 21/00: Steam engine plants not otherwise provided for - F01K: STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES (gas-turbine or jet-propulsion plants F02; nuclear power plants, engine arrangements therein G21D) - F01D: NON-POSITIVE DISPLACEMENT MACHINES OR ENGINES, e.g. STEAM TURBINES (machines or engines for liquids F03; non-positive displacement pumps F04D) ## Abstract A supercritical CO2 generation system for a parallel recuperative type capable of improving generation efficiency and saving costs is disclosed. According to the supercritical CO2 generation system according to the exemplary embodiment, a compression ratio of a turbine can be increased by arranging recuperators in parallel, thereby maximizing work of the turbine. ## Claims ### Claim 1 A supercritical CO2 generation system comprising: a compressor compressing a working fluid; a pre-cooler for cooling the working fluid and supplying pre-cooled working fluid to the compressor; a heat exchanger unit including first and second heaters configured to heat the working fluid; first and second turbines respectively driven by the working fluid; and a recuperator unit including a first recuperator and a second recuperator installed in parallel to each other such that the working fluids cooled by passing through the first and second recuperators are mixed with each other at a downstream side of the recuperator unit and supplied to the pre-cooler, the recuperator unit exchanging heat between the working fluid having passed through the first and second turbines and the working fluid having passed through the compressor to cool the working fluid having passed through the first and second turbines, wherein the working fluids having passed through the second heater and the second recuperator, respectively, are mixed at an upstream side of the first heater, and wherein the mixed working fluids are heated by the first heater and then supplied to the first turbine. ### Claim 2 (depends on 1) The supercritical CO2 generation system of claim 1, wherein the working fluid having passed through the compressor is branched to the heat exchanger unit and the recuperator unit from a downstream side of the compressor, respectively. ### Claim 3 (depends on 1) The supercritical CO2 generation system of claim 1, wherein the working fluid having passed through the first turbine is transmitted to the first recuperator to be cooled, and wherein the working fluid having passed through the second turbine is transmitted to the second recuperator to be cooled. ### Claim 4 (depends on 1) The supercritical CO2 generation system of claim 1, wherein the first heater is arranged on a high temperature side of the system and the second heater is arranged on a low temperature side of the system, wherein the first recuperator includes a high temperature recuperator and the second recuperator includes a low temperature recuperator, and wherein the working fluid branched from a downstream side of the compressor is transmitted to the second heater and the first and second recuperators, respectively. ### Claim 5 (depends on 1) The supercritical CO2 generation system of claim 1, wherein the working fluid transmitted to the first recuperator exchanges heat with the working fluid having passed through the first turbine to be heated and then is supplied to the second turbine. ### Claim 6 (depends on 1) The supercritical CO2 generation system of claim 1, wherein the first turbine is arranged on a high pressure side of the system, and the second turbine is arranged on a low pressure side of the system, and wherein the working fluid is supplied to the first turbine at a flow rate greater than that of the working fluid supplied to the second turbine. ### Claim 7 (depends on 6) The supercritical CO2 generation system of claim 6, wherein the flow rate of the working fluid supplied to the first turbine is a sum of the flow rates of the working fluids supplied to the second heater and the second recuperator. ### Claim 8 (depends on 1) The supercritical CO2 generation system of claim 1, wherein each of the first and second heaters and the first and second recuperators includes a heat exchanger having a high temperature operation region and a low temperature operation region, and wherein each heat exchanger is controlled to keep constant a temperature difference between the high and low temperature operation regions. ### Claim 9 (depends on 2) The supercritical CO2 generation system of claim 2, wherein the working fluid branched to the recuperator unit from the downstream side of the compressor is branched to the first and second recuperators, respectively. ### Claim 10 A supercritical CO2 generation system comprising: a compressor compressing a working fluid; a low temperature heater and a high temperature heater supplied heat from an external heat source to heat the working fluid; a high pressure turbine driven by the working fluid heated by passing through the low temperature heater and the high temperature heater; a low temperature recuperator and a high temperature recuperator installed in parallel to each other and configured to recuperate the working fluid passing through the compressor; a low pressure turbine driven by the working fluid recuperated by the high temperature recuperator; a pre-cooler cooling the working fluid primarily cooled by the high temperature recuperator and the low temperature recuperator and supplying the pre-cooled working fluid to the compressor; and a separator branching the working fluid passing through the compressor to the low temperature heater, the low temperature recuperator and the high temperature recuperator, respectively, wherein the working fluids having passed through the low temperature heater and the high temperature recuperator, respectively, are mixed at an upstream side of the high temperature heater and then are heated by the high temperature heater to be supplied to the high pressure turbine. ### Claim 11 A supercritical CO2 generation system comprising: a compressor compressing a working fluid; a low temperature heater and a high temperature heater supplied heat from an external heat source to heat the working fluid; a high pressure turbine driven by the working fluid heated by passing through the low temperature heater and the high temperature heater; a low temperature recuperator and a high temperature recuperator installed in parallel to each other and configured to recuperate the working fluid passing through the compressor; a low pressure turbine driven by the working fluid recuperated by the high temperature recuperator; a pre-cooler cooling the working fluid primarily cooled by the high temperature recuperator and the low temperature recuperator and supplying the pre-cooled working fluid to the compressor; a first separator branching the working fluid passing through the compressor to the low temperature heater, the low temperature recuperator, and the high temperature recuperator, respectively; and a second separator branching the working fluid branched to the low temperature recuperator and the high temperature recuperator from the first separator, respectively, wherein the working fluids having passed through the low temperature heater and the high temperature recuperator, respectively, are mixed at an upstream side of the high temperature heater and then are heated by the high temperature heater to be supplied to the high pressure turbine. ### Claim 12 (depends on 11) The supercritical CO2 generation system of claim 11, wherein the working fluid having passed through the high pressure turbine is transmitted to the high temperature recuperator to be cooled and the working fluid having passed through the low pressure turbine is transmitted to the low temperature recuperator to be cooled. ### Claim 13 (depends on 11) The supercritical CO2 generation system of claim 11, wherein the working fluid branched from a downstream side of the compressor is transmitted to the low temperature heater and the low temperature and high temperature recuperators, respectively. ### Claim 14 (depends on 13) The supercritical CO2 generation system of claim 13, wherein the working fluid transmitted to the high temperature recuperator exchanges heat with the working fluid having passed through the high pressure turbine to be heated and then is supplied to the low pressure turbine. ### Claim 15 (depends on 14) The supercritical CO2 generation system of claim 14, wherein the working fluid is supplied to the high pressure turbine at a flow rate greater than that of the working fluid supplied to the low pressure turbine. ### Claim 16 (depends on 15) The supercritical CO2 generation system of claim 15, wherein the flow rate of the working fluid supplied to the high pressure turbine is a sum of the flow rates of the working fluids supplied to the low temperature heater and the low temperature recuperator. ### Claim 17 (depends on 11) The supercritical CO2 generation system of claim 11, wherein each of the high and low temperature heaters and the high and low temperature recuperators includes a heat exchanger having a high temperature operation region and a low temperature operation region, and wherein each heat exchanger is controlled to keep constant a temperature difference between the high and low temperature operation regions. ### Claim 18 (depends on 11) The supercritical CO2 generation system of claim 11, wherein the working fluids cooled by passing through the low temperature recuperator and the high temperature recuperator are mixed with each other at an upstream side of the pre-cooler to be supplied to the pre-cooler.