System study on partial gasification combined cycle with CO{sub 2} recovery - article no. 051801
S partial gasification combined cycle with CO{sub 2} recovery is proposed in this paper. Partial gasification adopts cascade conversion of the composition of coal. Active composition of coal is simply gasified, while inactive composition, that is char, is burnt in a boiler. Oxy-fuel combustion of sy...
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description | S partial gasification combined cycle with CO{sub 2} recovery is proposed in this paper. Partial gasification adopts cascade conversion of the composition of coal. Active composition of coal is simply gasified, while inactive composition, that is char, is burnt in a boiler. Oxy-fuel combustion of syngas produces only CO{sub 2} and H{sub 2}O, so the CO{sub 2} can be separated through cooling the working fluid. This decreases the amount of energy consumption to separate CO{sub 2} compared with conventional methods. The novel system integrates the above two key technologies by injecting steam from a steam turbine into the combustion chamber of a gas turbine to combine the Rankine cycle with the Brayton cycle. The thermal efficiency of this system will be higher based on the cascade utilization of energy level. Compared with the conventional integrated gasification combined cycle (IGCC), the compressor of the gas turbine, heat recovery steam generator (HRSG) and gasifier are substituted for a pump, reheater, and partial gasifier, so the system is simplified. Furthermore, the novel system is investigated by means of energy-utilization diagram methodology and provides a simple analysis of their economic and environmental performance. As a result, the thermal efficiency of this system may be expected to be 45%, with CO{sub 2} recovery of 41.2%, which is 1.5-3.5% higher than that of an IGCC system. At the same time, the total investment cost of the new system is about 16% lower than that of an IGCC. The comparison between the partial gasification technology and the IGCC technology is based on the two representative cases to identify the specific feature of the proposed system. |
doi_str_mv | 10.1115/1.2938273 |
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Partial gasification adopts cascade conversion of the composition of coal. Active composition of coal is simply gasified, while inactive composition, that is char, is burnt in a boiler. Oxy-fuel combustion of syngas produces only CO{sub 2} and H{sub 2}O, so the CO{sub 2} can be separated through cooling the working fluid. This decreases the amount of energy consumption to separate CO{sub 2} compared with conventional methods. The novel system integrates the above two key technologies by injecting steam from a steam turbine into the combustion chamber of a gas turbine to combine the Rankine cycle with the Brayton cycle. The thermal efficiency of this system will be higher based on the cascade utilization of energy level. Compared with the conventional integrated gasification combined cycle (IGCC), the compressor of the gas turbine, heat recovery steam generator (HRSG) and gasifier are substituted for a pump, reheater, and partial gasifier, so the system is simplified. Furthermore, the novel system is investigated by means of energy-utilization diagram methodology and provides a simple analysis of their economic and environmental performance. As a result, the thermal efficiency of this system may be expected to be 45%, with CO{sub 2} recovery of 41.2%, which is 1.5-3.5% higher than that of an IGCC system. At the same time, the total investment cost of the new system is about 16% lower than that of an IGCC. The comparison between the partial gasification technology and the IGCC technology is based on the two representative cases to identify the specific feature of the proposed system.</description><identifier>ISSN: 0742-4795</identifier><identifier>EISSN: 1528-8919</identifier><identifier>DOI: 10.1115/1.2938273</identifier><language>eng</language><publisher>United States</publisher><subject>01 COAL, LIGNITE, AND PEAT ; 20 FOSSIL-FUELED POWER PLANTS ; BOILERS ; CAPTURE ; CARBON DIOXIDE ; CHARS ; COAL GASIFICATION ; COMBINED CYCLES ; COMBINED-CYCLE POWER PLANTS ; COMBUSTION ; COST ; GAS TURBINES ; INVESTMENT ; OXYFUEL COMBUSTION PROCESS ; POWER GENERATION ; STEAM ; SYNTHESIS GAS ; THERMAL EFFICIENCY</subject><ispartof>Journal of engineering for gas turbines and power, 2008-09, Vol.130 (5)</ispartof><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><link.rule.ids>230,315,781,785,886,27929,27930</link.rule.ids><backlink>$$Uhttps://www.osti.gov/biblio/21073804$$D View this record in Osti.gov$$Hfree_for_read</backlink></links><search><creatorcontrib>Xu, Y.J.</creatorcontrib><creatorcontrib>Jin, H.G.</creatorcontrib><creatorcontrib>Lin, R.M.</creatorcontrib><creatorcontrib>Han, W.</creatorcontrib><title>System study on partial gasification combined cycle with CO{sub 2} recovery - article no. 051801</title><title>Journal of engineering for gas turbines and power</title><description>S partial gasification combined cycle with CO{sub 2} recovery is proposed in this paper. Partial gasification adopts cascade conversion of the composition of coal. Active composition of coal is simply gasified, while inactive composition, that is char, is burnt in a boiler. Oxy-fuel combustion of syngas produces only CO{sub 2} and H{sub 2}O, so the CO{sub 2} can be separated through cooling the working fluid. This decreases the amount of energy consumption to separate CO{sub 2} compared with conventional methods. The novel system integrates the above two key technologies by injecting steam from a steam turbine into the combustion chamber of a gas turbine to combine the Rankine cycle with the Brayton cycle. The thermal efficiency of this system will be higher based on the cascade utilization of energy level. Compared with the conventional integrated gasification combined cycle (IGCC), the compressor of the gas turbine, heat recovery steam generator (HRSG) and gasifier are substituted for a pump, reheater, and partial gasifier, so the system is simplified. Furthermore, the novel system is investigated by means of energy-utilization diagram methodology and provides a simple analysis of their economic and environmental performance. As a result, the thermal efficiency of this system may be expected to be 45%, with CO{sub 2} recovery of 41.2%, which is 1.5-3.5% higher than that of an IGCC system. At the same time, the total investment cost of the new system is about 16% lower than that of an IGCC. The comparison between the partial gasification technology and the IGCC technology is based on the two representative cases to identify the specific feature of the proposed system.</description><subject>01 COAL, LIGNITE, AND PEAT</subject><subject>20 FOSSIL-FUELED POWER PLANTS</subject><subject>BOILERS</subject><subject>CAPTURE</subject><subject>CARBON DIOXIDE</subject><subject>CHARS</subject><subject>COAL GASIFICATION</subject><subject>COMBINED CYCLES</subject><subject>COMBINED-CYCLE POWER PLANTS</subject><subject>COMBUSTION</subject><subject>COST</subject><subject>GAS TURBINES</subject><subject>INVESTMENT</subject><subject>OXYFUEL COMBUSTION PROCESS</subject><subject>POWER GENERATION</subject><subject>STEAM</subject><subject>SYNTHESIS GAS</subject><subject>THERMAL EFFICIENCY</subject><issn>0742-4795</issn><issn>1528-8919</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2008</creationdate><recordtype>article</recordtype><recordid>eNqNi8tqAjEUQIO04PSx8A8udD3T3GSGZNZScedC9zZeY00ZE5kbWwbpv1fBD3B14HCOEBOUFSI271ipVltl9EgU2Chb2hbbB1FIU6uyNm0zFk_M31Ki1rUpxOdy4OwPwPm0HSBFOLo-B9fBl-OwC-RyuEhKh02Ifgs0UOfhN-Q9TBdnPm1A_UHvKf34foASrvO1iKkC2aCV-CIed65j_3rjs3ibfaym8zJxDmumkD3tKcXoKa8VSqOtrPV91T-4wEhO</recordid><startdate>20080915</startdate><enddate>20080915</enddate><creator>Xu, Y.J.</creator><creator>Jin, H.G.</creator><creator>Lin, R.M.</creator><creator>Han, W.</creator><scope>OTOTI</scope></search><sort><creationdate>20080915</creationdate><title>System study on partial gasification combined cycle with CO{sub 2} recovery - article no. 051801</title><author>Xu, Y.J. ; Jin, H.G. ; Lin, R.M. ; Han, W.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-osti_scitechconnect_210738043</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2008</creationdate><topic>01 COAL, LIGNITE, AND PEAT</topic><topic>20 FOSSIL-FUELED POWER PLANTS</topic><topic>BOILERS</topic><topic>CAPTURE</topic><topic>CARBON DIOXIDE</topic><topic>CHARS</topic><topic>COAL GASIFICATION</topic><topic>COMBINED CYCLES</topic><topic>COMBINED-CYCLE POWER PLANTS</topic><topic>COMBUSTION</topic><topic>COST</topic><topic>GAS TURBINES</topic><topic>INVESTMENT</topic><topic>OXYFUEL COMBUSTION PROCESS</topic><topic>POWER GENERATION</topic><topic>STEAM</topic><topic>SYNTHESIS GAS</topic><topic>THERMAL EFFICIENCY</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Xu, Y.J.</creatorcontrib><creatorcontrib>Jin, H.G.</creatorcontrib><creatorcontrib>Lin, R.M.</creatorcontrib><creatorcontrib>Han, W.</creatorcontrib><collection>OSTI.GOV</collection><jtitle>Journal of engineering for gas turbines and power</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Xu, Y.J.</au><au>Jin, H.G.</au><au>Lin, R.M.</au><au>Han, W.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>System study on partial gasification combined cycle with CO{sub 2} recovery - article no. 051801</atitle><jtitle>Journal of engineering for gas turbines and power</jtitle><date>2008-09-15</date><risdate>2008</risdate><volume>130</volume><issue>5</issue><issn>0742-4795</issn><eissn>1528-8919</eissn><abstract>S partial gasification combined cycle with CO{sub 2} recovery is proposed in this paper. Partial gasification adopts cascade conversion of the composition of coal. Active composition of coal is simply gasified, while inactive composition, that is char, is burnt in a boiler. Oxy-fuel combustion of syngas produces only CO{sub 2} and H{sub 2}O, so the CO{sub 2} can be separated through cooling the working fluid. This decreases the amount of energy consumption to separate CO{sub 2} compared with conventional methods. The novel system integrates the above two key technologies by injecting steam from a steam turbine into the combustion chamber of a gas turbine to combine the Rankine cycle with the Brayton cycle. The thermal efficiency of this system will be higher based on the cascade utilization of energy level. Compared with the conventional integrated gasification combined cycle (IGCC), the compressor of the gas turbine, heat recovery steam generator (HRSG) and gasifier are substituted for a pump, reheater, and partial gasifier, so the system is simplified. Furthermore, the novel system is investigated by means of energy-utilization diagram methodology and provides a simple analysis of their economic and environmental performance. As a result, the thermal efficiency of this system may be expected to be 45%, with CO{sub 2} recovery of 41.2%, which is 1.5-3.5% higher than that of an IGCC system. At the same time, the total investment cost of the new system is about 16% lower than that of an IGCC. The comparison between the partial gasification technology and the IGCC technology is based on the two representative cases to identify the specific feature of the proposed system.</abstract><cop>United States</cop><doi>10.1115/1.2938273</doi></addata></record> |
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subjects | 01 COAL, LIGNITE, AND PEAT 20 FOSSIL-FUELED POWER PLANTS BOILERS CAPTURE CARBON DIOXIDE CHARS COAL GASIFICATION COMBINED CYCLES COMBINED-CYCLE POWER PLANTS COMBUSTION COST GAS TURBINES INVESTMENT OXYFUEL COMBUSTION PROCESS POWER GENERATION STEAM SYNTHESIS GAS THERMAL EFFICIENCY |
title | System study on partial gasification combined cycle with CO{sub 2} recovery - article no. 051801 |
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