Cogeneration and Heat Recovery in the Industrial Process

Related to energy requirements for non-cellulose i. e. polyester production as an energy-intensive process, potential saving options are proposed. From the process data, it is evident that unit operations need electric and thermal energy in significant amounts. At the same time, improved energy mana...
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Autor*in:	Vujasinović, E. [verfasserIn] Mihelić-Bogdanić, A. [verfasserIn] Budin, R. [verfasserIn]

Format:	E-Artikel
Sprache:	Englisch ; Kroatisch

Erschienen:	2007

Schlagwörter:	Energy consumption cogeneration flue gases fuel savings

Übergeordnetes Werk:	In: Kemija u Industriji - Croatian Society of Chemical Engineers, 2017, 56(2007), 11, Seite 551-555
Übergeordnetes Werk:	volume:56 ; year:2007 ; number:11 ; pages:551-555

Links:	Link aufrufen Link aufrufen Journal toc Journal toc

Katalog-ID:	DOAJ041257219

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allfields	(DE-627)DOAJ041257219 (DE-599)DOAJe4bd1e5d5c1c4f559c33231804173bcf DE-627 ger DE-627 rakwb eng hrv QD1-999 Vujasinović, E. verfasserin aut Cogeneration and Heat Recovery in the Industrial Process 2007 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier Related to energy requirements for non-cellulose i. e. polyester production as an energy-intensive process, potential saving options are proposed. From the process data, it is evident that unit operations need electric and thermal energy in significant amounts. At the same time, improved energy management could be realized by applying a combined heat and power system (CHP) instead of the usually used process with separate heat and power production. In addition, the boiler flue gases with a sufficiently high outlet temperature could be used for combustion air preheating.Considering industrial process data, a calculation and comparison between the primary energy demand for conventional, CHP system and flue-gas heat recovery is presented. Comparison between separate heat and electricity production i.e. the conventional system with an overall efficiency of 55.6 % and CHP with efficiency of 85 %, shows an absolute efficiency increase of 29.4 %. Using an air preheater for combustion air temperature increasing saves 5.6 % of the fuel and at the same time diminishes thermal pollution because the exhaust flue-gas temperature becomes 77.3 °C instead of 204 °C. Conclusively, cogeneration and flue-gas heat recovery presentsfuel savings, which also implies economic and environmental benefits. Energy consumption cogeneration flue gases fuel savings Chemistry Mihelić-Bogdanić, A. verfasserin aut Budin, R. verfasserin aut In Kemija u Industriji Croatian Society of Chemical Engineers, 2017 56(2007), 11, Seite 551-555 (DE-627)474384195 (DE-600)2170074-6 13349090 nnns volume:56 year:2007 number:11 pages:551-555 https://doaj.org/article/e4bd1e5d5c1c4f559c33231804173bcf kostenfrei http://pierre.fkit.hr/hdki/kui/vol56/broj11/551.pdf kostenfrei https://doaj.org/toc/0022-9830 Journal toc kostenfrei https://doaj.org/toc/1334-9090 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_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_105 GBV_ILN_110 GBV_ILN_138 GBV_ILN_151 GBV_ILN_152 GBV_ILN_161 GBV_ILN_170 GBV_ILN_187 GBV_ILN_213 GBV_ILN_230 GBV_ILN_250 GBV_ILN_281 GBV_ILN_285 GBV_ILN_293 GBV_ILN_602 GBV_ILN_647 GBV_ILN_702 GBV_ILN_2014 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 56 2007 11 551-555
spelling	(DE-627)DOAJ041257219 (DE-599)DOAJe4bd1e5d5c1c4f559c33231804173bcf DE-627 ger DE-627 rakwb eng hrv QD1-999 Vujasinović, E. verfasserin aut Cogeneration and Heat Recovery in the Industrial Process 2007 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier Related to energy requirements for non-cellulose i. e. polyester production as an energy-intensive process, potential saving options are proposed. From the process data, it is evident that unit operations need electric and thermal energy in significant amounts. At the same time, improved energy management could be realized by applying a combined heat and power system (CHP) instead of the usually used process with separate heat and power production. In addition, the boiler flue gases with a sufficiently high outlet temperature could be used for combustion air preheating.Considering industrial process data, a calculation and comparison between the primary energy demand for conventional, CHP system and flue-gas heat recovery is presented. Comparison between separate heat and electricity production i.e. the conventional system with an overall efficiency of 55.6 % and CHP with efficiency of 85 %, shows an absolute efficiency increase of 29.4 %. Using an air preheater for combustion air temperature increasing saves 5.6 % of the fuel and at the same time diminishes thermal pollution because the exhaust flue-gas temperature becomes 77.3 °C instead of 204 °C. Conclusively, cogeneration and flue-gas heat recovery presentsfuel savings, which also implies economic and environmental benefits. Energy consumption cogeneration flue gases fuel savings Chemistry Mihelić-Bogdanić, A. verfasserin aut Budin, R. verfasserin aut In Kemija u Industriji Croatian Society of Chemical Engineers, 2017 56(2007), 11, Seite 551-555 (DE-627)474384195 (DE-600)2170074-6 13349090 nnns volume:56 year:2007 number:11 pages:551-555 https://doaj.org/article/e4bd1e5d5c1c4f559c33231804173bcf kostenfrei http://pierre.fkit.hr/hdki/kui/vol56/broj11/551.pdf kostenfrei https://doaj.org/toc/0022-9830 Journal toc kostenfrei https://doaj.org/toc/1334-9090 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_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_105 GBV_ILN_110 GBV_ILN_138 GBV_ILN_151 GBV_ILN_152 GBV_ILN_161 GBV_ILN_170 GBV_ILN_187 GBV_ILN_213 GBV_ILN_230 GBV_ILN_250 GBV_ILN_281 GBV_ILN_285 GBV_ILN_293 GBV_ILN_602 GBV_ILN_647 GBV_ILN_702 GBV_ILN_2014 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 56 2007 11 551-555
allfields_unstemmed	(DE-627)DOAJ041257219 (DE-599)DOAJe4bd1e5d5c1c4f559c33231804173bcf DE-627 ger DE-627 rakwb eng hrv QD1-999 Vujasinović, E. verfasserin aut Cogeneration and Heat Recovery in the Industrial Process 2007 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier Related to energy requirements for non-cellulose i. e. polyester production as an energy-intensive process, potential saving options are proposed. From the process data, it is evident that unit operations need electric and thermal energy in significant amounts. At the same time, improved energy management could be realized by applying a combined heat and power system (CHP) instead of the usually used process with separate heat and power production. In addition, the boiler flue gases with a sufficiently high outlet temperature could be used for combustion air preheating.Considering industrial process data, a calculation and comparison between the primary energy demand for conventional, CHP system and flue-gas heat recovery is presented. Comparison between separate heat and electricity production i.e. the conventional system with an overall efficiency of 55.6 % and CHP with efficiency of 85 %, shows an absolute efficiency increase of 29.4 %. Using an air preheater for combustion air temperature increasing saves 5.6 % of the fuel and at the same time diminishes thermal pollution because the exhaust flue-gas temperature becomes 77.3 °C instead of 204 °C. Conclusively, cogeneration and flue-gas heat recovery presentsfuel savings, which also implies economic and environmental benefits. Energy consumption cogeneration flue gases fuel savings Chemistry Mihelić-Bogdanić, A. verfasserin aut Budin, R. verfasserin aut In Kemija u Industriji Croatian Society of Chemical Engineers, 2017 56(2007), 11, Seite 551-555 (DE-627)474384195 (DE-600)2170074-6 13349090 nnns volume:56 year:2007 number:11 pages:551-555 https://doaj.org/article/e4bd1e5d5c1c4f559c33231804173bcf kostenfrei http://pierre.fkit.hr/hdki/kui/vol56/broj11/551.pdf kostenfrei https://doaj.org/toc/0022-9830 Journal toc kostenfrei https://doaj.org/toc/1334-9090 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_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_105 GBV_ILN_110 GBV_ILN_138 GBV_ILN_151 GBV_ILN_152 GBV_ILN_161 GBV_ILN_170 GBV_ILN_187 GBV_ILN_213 GBV_ILN_230 GBV_ILN_250 GBV_ILN_281 GBV_ILN_285 GBV_ILN_293 GBV_ILN_602 GBV_ILN_647 GBV_ILN_702 GBV_ILN_2014 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 56 2007 11 551-555
allfieldsGer	(DE-627)DOAJ041257219 (DE-599)DOAJe4bd1e5d5c1c4f559c33231804173bcf DE-627 ger DE-627 rakwb eng hrv QD1-999 Vujasinović, E. verfasserin aut Cogeneration and Heat Recovery in the Industrial Process 2007 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier Related to energy requirements for non-cellulose i. e. polyester production as an energy-intensive process, potential saving options are proposed. From the process data, it is evident that unit operations need electric and thermal energy in significant amounts. At the same time, improved energy management could be realized by applying a combined heat and power system (CHP) instead of the usually used process with separate heat and power production. In addition, the boiler flue gases with a sufficiently high outlet temperature could be used for combustion air preheating.Considering industrial process data, a calculation and comparison between the primary energy demand for conventional, CHP system and flue-gas heat recovery is presented. Comparison between separate heat and electricity production i.e. the conventional system with an overall efficiency of 55.6 % and CHP with efficiency of 85 %, shows an absolute efficiency increase of 29.4 %. Using an air preheater for combustion air temperature increasing saves 5.6 % of the fuel and at the same time diminishes thermal pollution because the exhaust flue-gas temperature becomes 77.3 °C instead of 204 °C. Conclusively, cogeneration and flue-gas heat recovery presentsfuel savings, which also implies economic and environmental benefits. Energy consumption cogeneration flue gases fuel savings Chemistry Mihelić-Bogdanić, A. verfasserin aut Budin, R. verfasserin aut In Kemija u Industriji Croatian Society of Chemical Engineers, 2017 56(2007), 11, Seite 551-555 (DE-627)474384195 (DE-600)2170074-6 13349090 nnns volume:56 year:2007 number:11 pages:551-555 https://doaj.org/article/e4bd1e5d5c1c4f559c33231804173bcf kostenfrei http://pierre.fkit.hr/hdki/kui/vol56/broj11/551.pdf kostenfrei https://doaj.org/toc/0022-9830 Journal toc kostenfrei https://doaj.org/toc/1334-9090 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_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_105 GBV_ILN_110 GBV_ILN_138 GBV_ILN_151 GBV_ILN_152 GBV_ILN_161 GBV_ILN_170 GBV_ILN_187 GBV_ILN_213 GBV_ILN_230 GBV_ILN_250 GBV_ILN_281 GBV_ILN_285 GBV_ILN_293 GBV_ILN_602 GBV_ILN_647 GBV_ILN_702 GBV_ILN_2014 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 56 2007 11 551-555
allfieldsSound	(DE-627)DOAJ041257219 (DE-599)DOAJe4bd1e5d5c1c4f559c33231804173bcf DE-627 ger DE-627 rakwb eng hrv QD1-999 Vujasinović, E. verfasserin aut Cogeneration and Heat Recovery in the Industrial Process 2007 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier Related to energy requirements for non-cellulose i. e. polyester production as an energy-intensive process, potential saving options are proposed. From the process data, it is evident that unit operations need electric and thermal energy in significant amounts. At the same time, improved energy management could be realized by applying a combined heat and power system (CHP) instead of the usually used process with separate heat and power production. In addition, the boiler flue gases with a sufficiently high outlet temperature could be used for combustion air preheating.Considering industrial process data, a calculation and comparison between the primary energy demand for conventional, CHP system and flue-gas heat recovery is presented. Comparison between separate heat and electricity production i.e. the conventional system with an overall efficiency of 55.6 % and CHP with efficiency of 85 %, shows an absolute efficiency increase of 29.4 %. Using an air preheater for combustion air temperature increasing saves 5.6 % of the fuel and at the same time diminishes thermal pollution because the exhaust flue-gas temperature becomes 77.3 °C instead of 204 °C. Conclusively, cogeneration and flue-gas heat recovery presentsfuel savings, which also implies economic and environmental benefits. Energy consumption cogeneration flue gases fuel savings Chemistry Mihelić-Bogdanić, A. verfasserin aut Budin, R. verfasserin aut In Kemija u Industriji Croatian Society of Chemical Engineers, 2017 56(2007), 11, Seite 551-555 (DE-627)474384195 (DE-600)2170074-6 13349090 nnns volume:56 year:2007 number:11 pages:551-555 https://doaj.org/article/e4bd1e5d5c1c4f559c33231804173bcf kostenfrei http://pierre.fkit.hr/hdki/kui/vol56/broj11/551.pdf kostenfrei https://doaj.org/toc/0022-9830 Journal toc kostenfrei https://doaj.org/toc/1334-9090 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_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_105 GBV_ILN_110 GBV_ILN_138 GBV_ILN_151 GBV_ILN_152 GBV_ILN_161 GBV_ILN_170 GBV_ILN_187 GBV_ILN_213 GBV_ILN_230 GBV_ILN_250 GBV_ILN_281 GBV_ILN_285 GBV_ILN_293 GBV_ILN_602 GBV_ILN_647 GBV_ILN_702 GBV_ILN_2014 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 56 2007 11 551-555
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callnumber-first	Q - Science
author	Vujasinović, E.
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topic_title	QD1-999 Cogeneration and Heat Recovery in the Industrial Process Energy consumption cogeneration flue gases fuel savings
topic	misc QD1-999 misc Energy consumption misc cogeneration misc flue gases misc fuel savings misc Chemistry
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title	Cogeneration and Heat Recovery in the Industrial Process
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title_sort	cogeneration and heat recovery in the industrial process
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title_auth	Cogeneration and Heat Recovery in the Industrial Process
abstract	Related to energy requirements for non-cellulose i. e. polyester production as an energy-intensive process, potential saving options are proposed. From the process data, it is evident that unit operations need electric and thermal energy in significant amounts. At the same time, improved energy management could be realized by applying a combined heat and power system (CHP) instead of the usually used process with separate heat and power production. In addition, the boiler flue gases with a sufficiently high outlet temperature could be used for combustion air preheating.Considering industrial process data, a calculation and comparison between the primary energy demand for conventional, CHP system and flue-gas heat recovery is presented. Comparison between separate heat and electricity production i.e. the conventional system with an overall efficiency of 55.6 % and CHP with efficiency of 85 %, shows an absolute efficiency increase of 29.4 %. Using an air preheater for combustion air temperature increasing saves 5.6 % of the fuel and at the same time diminishes thermal pollution because the exhaust flue-gas temperature becomes 77.3 °C instead of 204 °C. Conclusively, cogeneration and flue-gas heat recovery presentsfuel savings, which also implies economic and environmental benefits.
abstractGer	Related to energy requirements for non-cellulose i. e. polyester production as an energy-intensive process, potential saving options are proposed. From the process data, it is evident that unit operations need electric and thermal energy in significant amounts. At the same time, improved energy management could be realized by applying a combined heat and power system (CHP) instead of the usually used process with separate heat and power production. In addition, the boiler flue gases with a sufficiently high outlet temperature could be used for combustion air preheating.Considering industrial process data, a calculation and comparison between the primary energy demand for conventional, CHP system and flue-gas heat recovery is presented. Comparison between separate heat and electricity production i.e. the conventional system with an overall efficiency of 55.6 % and CHP with efficiency of 85 %, shows an absolute efficiency increase of 29.4 %. Using an air preheater for combustion air temperature increasing saves 5.6 % of the fuel and at the same time diminishes thermal pollution because the exhaust flue-gas temperature becomes 77.3 °C instead of 204 °C. Conclusively, cogeneration and flue-gas heat recovery presentsfuel savings, which also implies economic and environmental benefits.
abstract_unstemmed	Related to energy requirements for non-cellulose i. e. polyester production as an energy-intensive process, potential saving options are proposed. From the process data, it is evident that unit operations need electric and thermal energy in significant amounts. At the same time, improved energy management could be realized by applying a combined heat and power system (CHP) instead of the usually used process with separate heat and power production. In addition, the boiler flue gases with a sufficiently high outlet temperature could be used for combustion air preheating.Considering industrial process data, a calculation and comparison between the primary energy demand for conventional, CHP system and flue-gas heat recovery is presented. Comparison between separate heat and electricity production i.e. the conventional system with an overall efficiency of 55.6 % and CHP with efficiency of 85 %, shows an absolute efficiency increase of 29.4 %. Using an air preheater for combustion air temperature increasing saves 5.6 % of the fuel and at the same time diminishes thermal pollution because the exhaust flue-gas temperature becomes 77.3 °C instead of 204 °C. Conclusively, cogeneration and flue-gas heat recovery presentsfuel savings, which also implies economic and environmental benefits.
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title_short	Cogeneration and Heat Recovery in the Industrial Process
url	https://doaj.org/article/e4bd1e5d5c1c4f559c33231804173bcf http://pierre.fkit.hr/hdki/kui/vol56/broj11/551.pdf https://doaj.org/toc/0022-9830 https://doaj.org/toc/1334-9090
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Cogeneration and Heat Recovery in the Industrial Process

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