New cold-level utilization scheme for cascade three-level rankine cycle using the cold energy of liquefied natural gas

The topic of this study is the intermediate fluid vaporizer gasification system for a liquefied natural gas floating storage regasification unit. To reduce the loss of heat exchange, the primary distributary cascade three-level Rankine cycle is optimised based on the cascade three-level Rankine cycl...
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Gespeichert in:

Autor*in:	Yao Shouguang [verfasserIn] Xu Likang [verfasserIn] Tang Liang [verfasserIn]

Format:	E-Artikel
Sprache:	Englisch

Erschienen:	2019

Schlagwörter:	liquefied natural gas three-level rankine cycle power generation distributary

Übergeordnetes Werk:	In: Thermal Science - VINCA Institute of Nuclear Sciences, 2006, 23(2019), 6 Part B, Seite 3865-3875
Übergeordnetes Werk:	volume:23 ; year:2019 ; number:6 Part B ; pages:3865-3875

Links:	Link aufrufen Link aufrufen Link aufrufen Journal toc

DOI / URN:	10.2298/TSCI171012239Y

Katalog-ID:	DOAJ001700782

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allfields	10.2298/TSCI171012239Y doi (DE-627)DOAJ001700782 (DE-599)DOAJ59388dc974b449fe811291090a5a17b2 DE-627 ger DE-627 rakwb eng TJ1-1570 Yao Shouguang verfasserin aut New cold-level utilization scheme for cascade three-level rankine cycle using the cold energy of liquefied natural gas 2019 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier The topic of this study is the intermediate fluid vaporizer gasification system for a liquefied natural gas floating storage regasification unit. To reduce the loss of heat exchange, the primary distributary cascade three-level Rankine cycle is optimised based on the cascade three-level Rankine cycle that uses the cold energy of liquefied natural gas to generate power. The optimized primary distributary cascade three-level Rankine cycle is then compared with the original cascade three Rankine cycle established under the same conditions. Then, a secondary distributary cascade three-level Rankine cycle is proposed. Results show that under a liquefied natural gas flow of 175 t/h, the primary distributary cascade three-level Rankine cycle system exhibits a maximum net output power of 4130.72 kW and an exergy efficiency of 23.78%, which is higher than that of the typical cascade three-level Rankine cycle. Moreover, the net output power and exergy efficiency of the primary distributary cascade three-level Rankine cycle system increased by 3.71% and by 3.84%, respectively. The secondary distributary cascade three-level Rankine cycle system exhibits a maximum net output power of 4143.75 kW and an exergy efficiency of 23.85%. liquefied natural gas three-level rankine cycle power generation distributary Mechanical engineering and machinery Xu Likang verfasserin aut Tang Liang verfasserin aut In Thermal Science VINCA Institute of Nuclear Sciences, 2006 23(2019), 6 Part B, Seite 3865-3875 (DE-627)514240016 (DE-600)2241319-4 23347163 nnns volume:23 year:2019 number:6 Part B pages:3865-3875 https://doi.org/10.2298/TSCI171012239Y kostenfrei https://doaj.org/article/59388dc974b449fe811291090a5a17b2 kostenfrei http://www.doiserbia.nb.rs/img/doi/0354-9836/2019/0354-98361800239Y.pdf kostenfrei https://doaj.org/toc/0354-9836 Journal toc kostenfrei GBV_USEFLAG_A SYSFLAG_A GBV_DOAJ GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_39 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_65 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_95 GBV_ILN_105 GBV_ILN_110 GBV_ILN_151 GBV_ILN_161 GBV_ILN_170 GBV_ILN_206 GBV_ILN_213 GBV_ILN_230 GBV_ILN_285 GBV_ILN_293 GBV_ILN_370 GBV_ILN_602 GBV_ILN_702 GBV_ILN_2001 GBV_ILN_2003 GBV_ILN_2005 GBV_ILN_2006 GBV_ILN_2008 GBV_ILN_2009 GBV_ILN_2010 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2015 GBV_ILN_2020 GBV_ILN_2021 GBV_ILN_2025 GBV_ILN_2027 GBV_ILN_2031 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2050 GBV_ILN_2055 GBV_ILN_2056 GBV_ILN_2057 GBV_ILN_2061 GBV_ILN_2108 GBV_ILN_2111 GBV_ILN_2119 GBV_ILN_2190 GBV_ILN_4012 GBV_ILN_4037 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4249 GBV_ILN_4305 GBV_ILN_4306 GBV_ILN_4307 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4335 GBV_ILN_4338 GBV_ILN_4367 GBV_ILN_4700 AR 23 2019 6 Part B 3865-3875
spelling	10.2298/TSCI171012239Y doi (DE-627)DOAJ001700782 (DE-599)DOAJ59388dc974b449fe811291090a5a17b2 DE-627 ger DE-627 rakwb eng TJ1-1570 Yao Shouguang verfasserin aut New cold-level utilization scheme for cascade three-level rankine cycle using the cold energy of liquefied natural gas 2019 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier The topic of this study is the intermediate fluid vaporizer gasification system for a liquefied natural gas floating storage regasification unit. To reduce the loss of heat exchange, the primary distributary cascade three-level Rankine cycle is optimised based on the cascade three-level Rankine cycle that uses the cold energy of liquefied natural gas to generate power. The optimized primary distributary cascade three-level Rankine cycle is then compared with the original cascade three Rankine cycle established under the same conditions. Then, a secondary distributary cascade three-level Rankine cycle is proposed. Results show that under a liquefied natural gas flow of 175 t/h, the primary distributary cascade three-level Rankine cycle system exhibits a maximum net output power of 4130.72 kW and an exergy efficiency of 23.78%, which is higher than that of the typical cascade three-level Rankine cycle. Moreover, the net output power and exergy efficiency of the primary distributary cascade three-level Rankine cycle system increased by 3.71% and by 3.84%, respectively. The secondary distributary cascade three-level Rankine cycle system exhibits a maximum net output power of 4143.75 kW and an exergy efficiency of 23.85%. liquefied natural gas three-level rankine cycle power generation distributary Mechanical engineering and machinery Xu Likang verfasserin aut Tang Liang verfasserin aut In Thermal Science VINCA Institute of Nuclear Sciences, 2006 23(2019), 6 Part B, Seite 3865-3875 (DE-627)514240016 (DE-600)2241319-4 23347163 nnns volume:23 year:2019 number:6 Part B pages:3865-3875 https://doi.org/10.2298/TSCI171012239Y kostenfrei https://doaj.org/article/59388dc974b449fe811291090a5a17b2 kostenfrei http://www.doiserbia.nb.rs/img/doi/0354-9836/2019/0354-98361800239Y.pdf kostenfrei https://doaj.org/toc/0354-9836 Journal toc kostenfrei GBV_USEFLAG_A SYSFLAG_A GBV_DOAJ GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_39 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_65 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_95 GBV_ILN_105 GBV_ILN_110 GBV_ILN_151 GBV_ILN_161 GBV_ILN_170 GBV_ILN_206 GBV_ILN_213 GBV_ILN_230 GBV_ILN_285 GBV_ILN_293 GBV_ILN_370 GBV_ILN_602 GBV_ILN_702 GBV_ILN_2001 GBV_ILN_2003 GBV_ILN_2005 GBV_ILN_2006 GBV_ILN_2008 GBV_ILN_2009 GBV_ILN_2010 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2015 GBV_ILN_2020 GBV_ILN_2021 GBV_ILN_2025 GBV_ILN_2027 GBV_ILN_2031 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2050 GBV_ILN_2055 GBV_ILN_2056 GBV_ILN_2057 GBV_ILN_2061 GBV_ILN_2108 GBV_ILN_2111 GBV_ILN_2119 GBV_ILN_2190 GBV_ILN_4012 GBV_ILN_4037 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4249 GBV_ILN_4305 GBV_ILN_4306 GBV_ILN_4307 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4335 GBV_ILN_4338 GBV_ILN_4367 GBV_ILN_4700 AR 23 2019 6 Part B 3865-3875
allfields_unstemmed	10.2298/TSCI171012239Y doi (DE-627)DOAJ001700782 (DE-599)DOAJ59388dc974b449fe811291090a5a17b2 DE-627 ger DE-627 rakwb eng TJ1-1570 Yao Shouguang verfasserin aut New cold-level utilization scheme for cascade three-level rankine cycle using the cold energy of liquefied natural gas 2019 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier The topic of this study is the intermediate fluid vaporizer gasification system for a liquefied natural gas floating storage regasification unit. To reduce the loss of heat exchange, the primary distributary cascade three-level Rankine cycle is optimised based on the cascade three-level Rankine cycle that uses the cold energy of liquefied natural gas to generate power. The optimized primary distributary cascade three-level Rankine cycle is then compared with the original cascade three Rankine cycle established under the same conditions. Then, a secondary distributary cascade three-level Rankine cycle is proposed. Results show that under a liquefied natural gas flow of 175 t/h, the primary distributary cascade three-level Rankine cycle system exhibits a maximum net output power of 4130.72 kW and an exergy efficiency of 23.78%, which is higher than that of the typical cascade three-level Rankine cycle. Moreover, the net output power and exergy efficiency of the primary distributary cascade three-level Rankine cycle system increased by 3.71% and by 3.84%, respectively. The secondary distributary cascade three-level Rankine cycle system exhibits a maximum net output power of 4143.75 kW and an exergy efficiency of 23.85%. liquefied natural gas three-level rankine cycle power generation distributary Mechanical engineering and machinery Xu Likang verfasserin aut Tang Liang verfasserin aut In Thermal Science VINCA Institute of Nuclear Sciences, 2006 23(2019), 6 Part B, Seite 3865-3875 (DE-627)514240016 (DE-600)2241319-4 23347163 nnns volume:23 year:2019 number:6 Part B pages:3865-3875 https://doi.org/10.2298/TSCI171012239Y kostenfrei https://doaj.org/article/59388dc974b449fe811291090a5a17b2 kostenfrei http://www.doiserbia.nb.rs/img/doi/0354-9836/2019/0354-98361800239Y.pdf kostenfrei https://doaj.org/toc/0354-9836 Journal toc kostenfrei GBV_USEFLAG_A SYSFLAG_A GBV_DOAJ GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_39 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_65 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_95 GBV_ILN_105 GBV_ILN_110 GBV_ILN_151 GBV_ILN_161 GBV_ILN_170 GBV_ILN_206 GBV_ILN_213 GBV_ILN_230 GBV_ILN_285 GBV_ILN_293 GBV_ILN_370 GBV_ILN_602 GBV_ILN_702 GBV_ILN_2001 GBV_ILN_2003 GBV_ILN_2005 GBV_ILN_2006 GBV_ILN_2008 GBV_ILN_2009 GBV_ILN_2010 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2015 GBV_ILN_2020 GBV_ILN_2021 GBV_ILN_2025 GBV_ILN_2027 GBV_ILN_2031 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2050 GBV_ILN_2055 GBV_ILN_2056 GBV_ILN_2057 GBV_ILN_2061 GBV_ILN_2108 GBV_ILN_2111 GBV_ILN_2119 GBV_ILN_2190 GBV_ILN_4012 GBV_ILN_4037 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4249 GBV_ILN_4305 GBV_ILN_4306 GBV_ILN_4307 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4335 GBV_ILN_4338 GBV_ILN_4367 GBV_ILN_4700 AR 23 2019 6 Part B 3865-3875
allfieldsGer	10.2298/TSCI171012239Y doi (DE-627)DOAJ001700782 (DE-599)DOAJ59388dc974b449fe811291090a5a17b2 DE-627 ger DE-627 rakwb eng TJ1-1570 Yao Shouguang verfasserin aut New cold-level utilization scheme for cascade three-level rankine cycle using the cold energy of liquefied natural gas 2019 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier The topic of this study is the intermediate fluid vaporizer gasification system for a liquefied natural gas floating storage regasification unit. To reduce the loss of heat exchange, the primary distributary cascade three-level Rankine cycle is optimised based on the cascade three-level Rankine cycle that uses the cold energy of liquefied natural gas to generate power. The optimized primary distributary cascade three-level Rankine cycle is then compared with the original cascade three Rankine cycle established under the same conditions. Then, a secondary distributary cascade three-level Rankine cycle is proposed. Results show that under a liquefied natural gas flow of 175 t/h, the primary distributary cascade three-level Rankine cycle system exhibits a maximum net output power of 4130.72 kW and an exergy efficiency of 23.78%, which is higher than that of the typical cascade three-level Rankine cycle. Moreover, the net output power and exergy efficiency of the primary distributary cascade three-level Rankine cycle system increased by 3.71% and by 3.84%, respectively. The secondary distributary cascade three-level Rankine cycle system exhibits a maximum net output power of 4143.75 kW and an exergy efficiency of 23.85%. liquefied natural gas three-level rankine cycle power generation distributary Mechanical engineering and machinery Xu Likang verfasserin aut Tang Liang verfasserin aut In Thermal Science VINCA Institute of Nuclear Sciences, 2006 23(2019), 6 Part B, Seite 3865-3875 (DE-627)514240016 (DE-600)2241319-4 23347163 nnns volume:23 year:2019 number:6 Part B pages:3865-3875 https://doi.org/10.2298/TSCI171012239Y kostenfrei https://doaj.org/article/59388dc974b449fe811291090a5a17b2 kostenfrei http://www.doiserbia.nb.rs/img/doi/0354-9836/2019/0354-98361800239Y.pdf kostenfrei https://doaj.org/toc/0354-9836 Journal toc kostenfrei GBV_USEFLAG_A SYSFLAG_A GBV_DOAJ GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_39 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_65 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_95 GBV_ILN_105 GBV_ILN_110 GBV_ILN_151 GBV_ILN_161 GBV_ILN_170 GBV_ILN_206 GBV_ILN_213 GBV_ILN_230 GBV_ILN_285 GBV_ILN_293 GBV_ILN_370 GBV_ILN_602 GBV_ILN_702 GBV_ILN_2001 GBV_ILN_2003 GBV_ILN_2005 GBV_ILN_2006 GBV_ILN_2008 GBV_ILN_2009 GBV_ILN_2010 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2015 GBV_ILN_2020 GBV_ILN_2021 GBV_ILN_2025 GBV_ILN_2027 GBV_ILN_2031 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2050 GBV_ILN_2055 GBV_ILN_2056 GBV_ILN_2057 GBV_ILN_2061 GBV_ILN_2108 GBV_ILN_2111 GBV_ILN_2119 GBV_ILN_2190 GBV_ILN_4012 GBV_ILN_4037 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4249 GBV_ILN_4305 GBV_ILN_4306 GBV_ILN_4307 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4335 GBV_ILN_4338 GBV_ILN_4367 GBV_ILN_4700 AR 23 2019 6 Part B 3865-3875
allfieldsSound	10.2298/TSCI171012239Y doi (DE-627)DOAJ001700782 (DE-599)DOAJ59388dc974b449fe811291090a5a17b2 DE-627 ger DE-627 rakwb eng TJ1-1570 Yao Shouguang verfasserin aut New cold-level utilization scheme for cascade three-level rankine cycle using the cold energy of liquefied natural gas 2019 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier The topic of this study is the intermediate fluid vaporizer gasification system for a liquefied natural gas floating storage regasification unit. To reduce the loss of heat exchange, the primary distributary cascade three-level Rankine cycle is optimised based on the cascade three-level Rankine cycle that uses the cold energy of liquefied natural gas to generate power. The optimized primary distributary cascade three-level Rankine cycle is then compared with the original cascade three Rankine cycle established under the same conditions. Then, a secondary distributary cascade three-level Rankine cycle is proposed. Results show that under a liquefied natural gas flow of 175 t/h, the primary distributary cascade three-level Rankine cycle system exhibits a maximum net output power of 4130.72 kW and an exergy efficiency of 23.78%, which is higher than that of the typical cascade three-level Rankine cycle. Moreover, the net output power and exergy efficiency of the primary distributary cascade three-level Rankine cycle system increased by 3.71% and by 3.84%, respectively. The secondary distributary cascade three-level Rankine cycle system exhibits a maximum net output power of 4143.75 kW and an exergy efficiency of 23.85%. liquefied natural gas three-level rankine cycle power generation distributary Mechanical engineering and machinery Xu Likang verfasserin aut Tang Liang verfasserin aut In Thermal Science VINCA Institute of Nuclear Sciences, 2006 23(2019), 6 Part B, Seite 3865-3875 (DE-627)514240016 (DE-600)2241319-4 23347163 nnns volume:23 year:2019 number:6 Part B pages:3865-3875 https://doi.org/10.2298/TSCI171012239Y kostenfrei https://doaj.org/article/59388dc974b449fe811291090a5a17b2 kostenfrei http://www.doiserbia.nb.rs/img/doi/0354-9836/2019/0354-98361800239Y.pdf kostenfrei https://doaj.org/toc/0354-9836 Journal toc kostenfrei GBV_USEFLAG_A SYSFLAG_A GBV_DOAJ GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_39 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_65 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_95 GBV_ILN_105 GBV_ILN_110 GBV_ILN_151 GBV_ILN_161 GBV_ILN_170 GBV_ILN_206 GBV_ILN_213 GBV_ILN_230 GBV_ILN_285 GBV_ILN_293 GBV_ILN_370 GBV_ILN_602 GBV_ILN_702 GBV_ILN_2001 GBV_ILN_2003 GBV_ILN_2005 GBV_ILN_2006 GBV_ILN_2008 GBV_ILN_2009 GBV_ILN_2010 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2015 GBV_ILN_2020 GBV_ILN_2021 GBV_ILN_2025 GBV_ILN_2027 GBV_ILN_2031 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2050 GBV_ILN_2055 GBV_ILN_2056 GBV_ILN_2057 GBV_ILN_2061 GBV_ILN_2108 GBV_ILN_2111 GBV_ILN_2119 GBV_ILN_2190 GBV_ILN_4012 GBV_ILN_4037 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4249 GBV_ILN_4305 GBV_ILN_4306 GBV_ILN_4307 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4335 GBV_ILN_4338 GBV_ILN_4367 GBV_ILN_4700 AR 23 2019 6 Part B 3865-3875
language	English
source	In Thermal Science 23(2019), 6 Part B, Seite 3865-3875 volume:23 year:2019 number:6 Part B pages:3865-3875
sourceStr	In Thermal Science 23(2019), 6 Part B, Seite 3865-3875 volume:23 year:2019 number:6 Part B pages:3865-3875
format_phy_str_mv	Article
institution	findex.gbv.de
topic_facet	liquefied natural gas three-level rankine cycle power generation distributary Mechanical engineering and machinery
isfreeaccess_bool	true
container_title	Thermal Science
authorswithroles_txt_mv	Yao Shouguang @@aut@@ Xu Likang @@aut@@ Tang Liang @@aut@@
publishDateDaySort_date	2019-01-01T00:00:00Z
hierarchy_top_id	514240016
id	DOAJ001700782
language_de	englisch
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callnumber-first	T - Technology
author	Yao Shouguang
spellingShingle	Yao Shouguang misc TJ1-1570 misc liquefied natural gas misc three-level rankine cycle misc power generation misc distributary misc Mechanical engineering and machinery New cold-level utilization scheme for cascade three-level rankine cycle using the cold energy of liquefied natural gas
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topic_title	TJ1-1570 New cold-level utilization scheme for cascade three-level rankine cycle using the cold energy of liquefied natural gas liquefied natural gas three-level rankine cycle power generation distributary
topic	misc TJ1-1570 misc liquefied natural gas misc three-level rankine cycle misc power generation misc distributary misc Mechanical engineering and machinery
topic_unstemmed	misc TJ1-1570 misc liquefied natural gas misc three-level rankine cycle misc power generation misc distributary misc Mechanical engineering and machinery
topic_browse	misc TJ1-1570 misc liquefied natural gas misc three-level rankine cycle misc power generation misc distributary misc Mechanical engineering and machinery
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title	New cold-level utilization scheme for cascade three-level rankine cycle using the cold energy of liquefied natural gas
ctrlnum	(DE-627)DOAJ001700782 (DE-599)DOAJ59388dc974b449fe811291090a5a17b2
title_full	New cold-level utilization scheme for cascade three-level rankine cycle using the cold energy of liquefied natural gas
author_sort	Yao Shouguang
journal	Thermal Science
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author_browse	Yao Shouguang Xu Likang Tang Liang
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author-letter	Yao Shouguang
doi_str_mv	10.2298/TSCI171012239Y
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title_sort	new cold-level utilization scheme for cascade three-level rankine cycle using the cold energy of liquefied natural gas
callnumber	TJ1-1570
title_auth	New cold-level utilization scheme for cascade three-level rankine cycle using the cold energy of liquefied natural gas
abstract	The topic of this study is the intermediate fluid vaporizer gasification system for a liquefied natural gas floating storage regasification unit. To reduce the loss of heat exchange, the primary distributary cascade three-level Rankine cycle is optimised based on the cascade three-level Rankine cycle that uses the cold energy of liquefied natural gas to generate power. The optimized primary distributary cascade three-level Rankine cycle is then compared with the original cascade three Rankine cycle established under the same conditions. Then, a secondary distributary cascade three-level Rankine cycle is proposed. Results show that under a liquefied natural gas flow of 175 t/h, the primary distributary cascade three-level Rankine cycle system exhibits a maximum net output power of 4130.72 kW and an exergy efficiency of 23.78%, which is higher than that of the typical cascade three-level Rankine cycle. Moreover, the net output power and exergy efficiency of the primary distributary cascade three-level Rankine cycle system increased by 3.71% and by 3.84%, respectively. The secondary distributary cascade three-level Rankine cycle system exhibits a maximum net output power of 4143.75 kW and an exergy efficiency of 23.85%.
abstractGer	The topic of this study is the intermediate fluid vaporizer gasification system for a liquefied natural gas floating storage regasification unit. To reduce the loss of heat exchange, the primary distributary cascade three-level Rankine cycle is optimised based on the cascade three-level Rankine cycle that uses the cold energy of liquefied natural gas to generate power. The optimized primary distributary cascade three-level Rankine cycle is then compared with the original cascade three Rankine cycle established under the same conditions. Then, a secondary distributary cascade three-level Rankine cycle is proposed. Results show that under a liquefied natural gas flow of 175 t/h, the primary distributary cascade three-level Rankine cycle system exhibits a maximum net output power of 4130.72 kW and an exergy efficiency of 23.78%, which is higher than that of the typical cascade three-level Rankine cycle. Moreover, the net output power and exergy efficiency of the primary distributary cascade three-level Rankine cycle system increased by 3.71% and by 3.84%, respectively. The secondary distributary cascade three-level Rankine cycle system exhibits a maximum net output power of 4143.75 kW and an exergy efficiency of 23.85%.
abstract_unstemmed	The topic of this study is the intermediate fluid vaporizer gasification system for a liquefied natural gas floating storage regasification unit. To reduce the loss of heat exchange, the primary distributary cascade three-level Rankine cycle is optimised based on the cascade three-level Rankine cycle that uses the cold energy of liquefied natural gas to generate power. The optimized primary distributary cascade three-level Rankine cycle is then compared with the original cascade three Rankine cycle established under the same conditions. Then, a secondary distributary cascade three-level Rankine cycle is proposed. Results show that under a liquefied natural gas flow of 175 t/h, the primary distributary cascade three-level Rankine cycle system exhibits a maximum net output power of 4130.72 kW and an exergy efficiency of 23.78%, which is higher than that of the typical cascade three-level Rankine cycle. Moreover, the net output power and exergy efficiency of the primary distributary cascade three-level Rankine cycle system increased by 3.71% and by 3.84%, respectively. The secondary distributary cascade three-level Rankine cycle system exhibits a maximum net output power of 4143.75 kW and an exergy efficiency of 23.85%.
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container_issue	6 Part B
title_short	New cold-level utilization scheme for cascade three-level rankine cycle using the cold energy of liquefied natural gas
url	https://doi.org/10.2298/TSCI171012239Y https://doaj.org/article/59388dc974b449fe811291090a5a17b2 http://www.doiserbia.nb.rs/img/doi/0354-9836/2019/0354-98361800239Y.pdf https://doaj.org/toc/0354-9836
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up_date	2024-07-03T21:56:10.889Z
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Nicht das Richtige dabei?