Conceptual and basic design of a novel integrated cogeneration power plant energy system
A novel integrated system, including air separation unit (ASU), coal gasification, solid oxide fuel cell (SOFC), carbon dioxide (CO2) transcritical cycle, steam cycle with liquefied natural gas (LNG) vaporization is configured and analyzed. ASU provides the required oxygen for SOFC and oxy-fuel powe...
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Veröffentlicht in: | Energy (Oxford) 2017-05, Vol.127, p.516-533 |
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description | A novel integrated system, including air separation unit (ASU), coal gasification, solid oxide fuel cell (SOFC), carbon dioxide (CO2) transcritical cycle, steam cycle with liquefied natural gas (LNG) vaporization is configured and analyzed. ASU provides the required oxygen for SOFC and oxy-fuel power generation system. Coal gasification provides syngas which is utilized as a part of the essential heat source. Electrical power is generated by SOFC, steam and CO2 oxy-fuel cycles. LNG is vaporized to provide the cold energy and also is utilized as the fuel in the SOFC and CO2 oxy fuel cycles. Sensitivity of the process performance to the major operating parameters is studied. Effect of the LNG flow rate, turbine inlet temperature (TIT), CO2 oxy-fuel cycle pressure ratio and SOFC operating parameters are investigated. The obtained results indicate that the net electrical power is 5.97 × 105 kW, in the condition that TIT = 900 °C, rp,c = 28, Vcell = 0.85 and Uf = 0.8. In this process rate of the utilized LNG is 1.10 × 108 kg.h−1 and rate of the captured CO2 is 1.03 × 104 kg.h−1. Also 1.36 × 107 kg h−1 syngas, 1.38 × 107 kg.h−1 liquid oxygen (LO2), 3.37 × 107 kg.h−1 liquid nitrogen (LN2) and 1.00 × 108 kg.h−1 NG are produced.
•A novel integrated system including air separation unit (ASU) and coal gasification is proposed.•Electrical power is generated by SOFC, steam and CO2 oxy-fuel cycles.•LNG vaporizes to provide the cold energy and also is utilized as the fuel. |
doi_str_mv | 10.1016/j.energy.2017.03.127 |
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•A novel integrated system including air separation unit (ASU) and coal gasification is proposed.•Electrical power is generated by SOFC, steam and CO2 oxy-fuel cycles.•LNG vaporizes to provide the cold energy and also is utilized as the fuel.</description><identifier>ISSN: 0360-5442</identifier><identifier>EISSN: 1873-6785</identifier><identifier>DOI: 10.1016/j.energy.2017.03.127</identifier><language>eng</language><publisher>Oxford: Elsevier Ltd</publisher><subject>Air separation ; Air separation and liquefaction ; Carbon cycle ; Carbon dioxide ; Carbon sequestration ; CO2 capture ; Coal gasification ; Cogeneration ; Cycle ratio ; Electric power ; Electric power generation ; Electric power plants ; Energy ; Flow rates ; Flow velocity ; Fluidized bed combustion ; Fuel cells ; Fuel cycles ; Fuel technology ; Inlet temperature ; Liquefied natural gas ; Liquid nitrogen ; Liquid oxygen ; LNG cold recovery ; Natural gas ; Oxy-coal combustion ; Oxy-fuel ; Oxygen ; Parameter sensitivity ; Power generation ; Power plants ; Pressure ratio ; SOFC cycle ; Solid oxide fuel cells ; Steam electric power generation ; Synthetic fuels ; Temperature effects ; Vaporization</subject><ispartof>Energy (Oxford), 2017-05, Vol.127, p.516-533</ispartof><rights>2017 Elsevier Ltd</rights><rights>Copyright Elsevier BV May 15, 2017</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c334t-b73915d27dee5f319fdeb74cd7c5f72ae0ee0caec7989dcab7110fec77e4a24e3</citedby><cites>FETCH-LOGICAL-c334t-b73915d27dee5f319fdeb74cd7c5f72ae0ee0caec7989dcab7110fec77e4a24e3</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://dx.doi.org/10.1016/j.energy.2017.03.127$$EHTML$$P50$$Gelsevier$$H</linktohtml><link.rule.ids>314,780,784,3550,27924,27925,45995</link.rule.ids></links><search><creatorcontrib>Mehrpooya, Mehdi</creatorcontrib><creatorcontrib>Sharifzadeh, Mohammad Mehdi Moftakhari</creatorcontrib><title>Conceptual and basic design of a novel integrated cogeneration power plant energy system</title><title>Energy (Oxford)</title><description>A novel integrated system, including air separation unit (ASU), coal gasification, solid oxide fuel cell (SOFC), carbon dioxide (CO2) transcritical cycle, steam cycle with liquefied natural gas (LNG) vaporization is configured and analyzed. ASU provides the required oxygen for SOFC and oxy-fuel power generation system. Coal gasification provides syngas which is utilized as a part of the essential heat source. Electrical power is generated by SOFC, steam and CO2 oxy-fuel cycles. LNG is vaporized to provide the cold energy and also is utilized as the fuel in the SOFC and CO2 oxy fuel cycles. Sensitivity of the process performance to the major operating parameters is studied. Effect of the LNG flow rate, turbine inlet temperature (TIT), CO2 oxy-fuel cycle pressure ratio and SOFC operating parameters are investigated. The obtained results indicate that the net electrical power is 5.97 × 105 kW, in the condition that TIT = 900 °C, rp,c = 28, Vcell = 0.85 and Uf = 0.8. In this process rate of the utilized LNG is 1.10 × 108 kg.h−1 and rate of the captured CO2 is 1.03 × 104 kg.h−1. Also 1.36 × 107 kg h−1 syngas, 1.38 × 107 kg.h−1 liquid oxygen (LO2), 3.37 × 107 kg.h−1 liquid nitrogen (LN2) and 1.00 × 108 kg.h−1 NG are produced.
•A novel integrated system including air separation unit (ASU) and coal gasification is proposed.•Electrical power is generated by SOFC, steam and CO2 oxy-fuel cycles.•LNG vaporizes to provide the cold energy and also is utilized as the fuel.</description><subject>Air separation</subject><subject>Air separation and liquefaction</subject><subject>Carbon cycle</subject><subject>Carbon dioxide</subject><subject>Carbon sequestration</subject><subject>CO2 capture</subject><subject>Coal gasification</subject><subject>Cogeneration</subject><subject>Cycle ratio</subject><subject>Electric power</subject><subject>Electric power generation</subject><subject>Electric power plants</subject><subject>Energy</subject><subject>Flow rates</subject><subject>Flow velocity</subject><subject>Fluidized bed combustion</subject><subject>Fuel cells</subject><subject>Fuel cycles</subject><subject>Fuel technology</subject><subject>Inlet temperature</subject><subject>Liquefied natural gas</subject><subject>Liquid nitrogen</subject><subject>Liquid oxygen</subject><subject>LNG cold recovery</subject><subject>Natural gas</subject><subject>Oxy-coal combustion</subject><subject>Oxy-fuel</subject><subject>Oxygen</subject><subject>Parameter sensitivity</subject><subject>Power generation</subject><subject>Power plants</subject><subject>Pressure ratio</subject><subject>SOFC cycle</subject><subject>Solid oxide fuel cells</subject><subject>Steam electric power generation</subject><subject>Synthetic fuels</subject><subject>Temperature effects</subject><subject>Vaporization</subject><issn>0360-5442</issn><issn>1873-6785</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2017</creationdate><recordtype>article</recordtype><recordid>eNp9kEtLxDAQx4MouK5-Aw8Bz615tJv2IsjiCxa8KHgLaTItKbtJTbIr--3NUs-ehoH5P-aH0C0lJSV0dT-W4CAMx5IRKkrCS8rEGVrQRvBiJZr6HC0IX5Girip2ia5iHAkhddO2C_S19k7DlPZqi5UzuFPRamwg2sFh32OFnT_AFluXYAgqgcHaD6c4lax3ePI_EPC0VS7huQSOx5hgd40uerWNcPM3l-jz-elj_Vps3l_e1o-bQnNepaITvKW1YcIA1D2nbW-gE5U2Qte9YAoIANEKtGib1mjVCUpJn1cBlWIV8CW6m32n4L_3EJMc_T64HClpy1lmQBqWr6r5SgcfY4BeTsHuVDhKSuSJoRzlXF-eGErCZWaYZQ-zDPIHBwtBRm0hAzM2gE7SePu_wS8lt36t</recordid><startdate>20170515</startdate><enddate>20170515</enddate><creator>Mehrpooya, Mehdi</creator><creator>Sharifzadeh, Mohammad Mehdi Moftakhari</creator><general>Elsevier Ltd</general><general>Elsevier BV</general><scope>AAYXX</scope><scope>CITATION</scope><scope>7SP</scope><scope>7ST</scope><scope>7TB</scope><scope>8FD</scope><scope>C1K</scope><scope>F28</scope><scope>FR3</scope><scope>KR7</scope><scope>L7M</scope><scope>SOI</scope></search><sort><creationdate>20170515</creationdate><title>Conceptual and basic design of a novel integrated cogeneration power plant energy system</title><author>Mehrpooya, Mehdi ; Sharifzadeh, Mohammad Mehdi Moftakhari</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c334t-b73915d27dee5f319fdeb74cd7c5f72ae0ee0caec7989dcab7110fec77e4a24e3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2017</creationdate><topic>Air separation</topic><topic>Air separation and liquefaction</topic><topic>Carbon cycle</topic><topic>Carbon dioxide</topic><topic>Carbon sequestration</topic><topic>CO2 capture</topic><topic>Coal gasification</topic><topic>Cogeneration</topic><topic>Cycle ratio</topic><topic>Electric power</topic><topic>Electric power generation</topic><topic>Electric power plants</topic><topic>Energy</topic><topic>Flow rates</topic><topic>Flow velocity</topic><topic>Fluidized bed combustion</topic><topic>Fuel cells</topic><topic>Fuel cycles</topic><topic>Fuel technology</topic><topic>Inlet temperature</topic><topic>Liquefied natural gas</topic><topic>Liquid nitrogen</topic><topic>Liquid oxygen</topic><topic>LNG cold recovery</topic><topic>Natural gas</topic><topic>Oxy-coal combustion</topic><topic>Oxy-fuel</topic><topic>Oxygen</topic><topic>Parameter sensitivity</topic><topic>Power generation</topic><topic>Power plants</topic><topic>Pressure ratio</topic><topic>SOFC cycle</topic><topic>Solid oxide fuel cells</topic><topic>Steam electric power generation</topic><topic>Synthetic fuels</topic><topic>Temperature effects</topic><topic>Vaporization</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Mehrpooya, Mehdi</creatorcontrib><creatorcontrib>Sharifzadeh, Mohammad Mehdi Moftakhari</creatorcontrib><collection>CrossRef</collection><collection>Electronics & Communications Abstracts</collection><collection>Environment Abstracts</collection><collection>Mechanical & Transportation Engineering Abstracts</collection><collection>Technology Research Database</collection><collection>Environmental Sciences and Pollution Management</collection><collection>ANTE: Abstracts in New Technology & Engineering</collection><collection>Engineering Research Database</collection><collection>Civil Engineering Abstracts</collection><collection>Advanced Technologies Database with Aerospace</collection><collection>Environment Abstracts</collection><jtitle>Energy (Oxford)</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Mehrpooya, Mehdi</au><au>Sharifzadeh, Mohammad Mehdi Moftakhari</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Conceptual and basic design of a novel integrated cogeneration power plant energy system</atitle><jtitle>Energy (Oxford)</jtitle><date>2017-05-15</date><risdate>2017</risdate><volume>127</volume><spage>516</spage><epage>533</epage><pages>516-533</pages><issn>0360-5442</issn><eissn>1873-6785</eissn><abstract>A novel integrated system, including air separation unit (ASU), coal gasification, solid oxide fuel cell (SOFC), carbon dioxide (CO2) transcritical cycle, steam cycle with liquefied natural gas (LNG) vaporization is configured and analyzed. ASU provides the required oxygen for SOFC and oxy-fuel power generation system. Coal gasification provides syngas which is utilized as a part of the essential heat source. Electrical power is generated by SOFC, steam and CO2 oxy-fuel cycles. LNG is vaporized to provide the cold energy and also is utilized as the fuel in the SOFC and CO2 oxy fuel cycles. Sensitivity of the process performance to the major operating parameters is studied. Effect of the LNG flow rate, turbine inlet temperature (TIT), CO2 oxy-fuel cycle pressure ratio and SOFC operating parameters are investigated. The obtained results indicate that the net electrical power is 5.97 × 105 kW, in the condition that TIT = 900 °C, rp,c = 28, Vcell = 0.85 and Uf = 0.8. In this process rate of the utilized LNG is 1.10 × 108 kg.h−1 and rate of the captured CO2 is 1.03 × 104 kg.h−1. Also 1.36 × 107 kg h−1 syngas, 1.38 × 107 kg.h−1 liquid oxygen (LO2), 3.37 × 107 kg.h−1 liquid nitrogen (LN2) and 1.00 × 108 kg.h−1 NG are produced.
•A novel integrated system including air separation unit (ASU) and coal gasification is proposed.•Electrical power is generated by SOFC, steam and CO2 oxy-fuel cycles.•LNG vaporizes to provide the cold energy and also is utilized as the fuel.</abstract><cop>Oxford</cop><pub>Elsevier Ltd</pub><doi>10.1016/j.energy.2017.03.127</doi><tpages>18</tpages></addata></record> |
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subjects | Air separation Air separation and liquefaction Carbon cycle Carbon dioxide Carbon sequestration CO2 capture Coal gasification Cogeneration Cycle ratio Electric power Electric power generation Electric power plants Energy Flow rates Flow velocity Fluidized bed combustion Fuel cells Fuel cycles Fuel technology Inlet temperature Liquefied natural gas Liquid nitrogen Liquid oxygen LNG cold recovery Natural gas Oxy-coal combustion Oxy-fuel Oxygen Parameter sensitivity Power generation Power plants Pressure ratio SOFC cycle Solid oxide fuel cells Steam electric power generation Synthetic fuels Temperature effects Vaporization |
title | Conceptual and basic design of a novel integrated cogeneration power plant energy system |
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