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Liquefaction of oxyfuel flue gases: experimental results and modeling of heat transfer coefficients for pure CO2
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| Veröffentlicht in: | Energy procedia 51(2014), Seite 109-118 |
|---|---|
| Personen und Körperschaften: | , , , |
| Titel: | Liquefaction of oxyfuel flue gases: experimental results and modeling of heat transfer coefficients for pure CO2/ T. Küster, R. Eggers |
| Format: | E-Book-Kapitel |
| Sprache: | Englisch |
| veröffentlicht: |
28 August 2014
|
| Gesamtaufnahme: |
: Energy procedia, 51(2014), Seite 109-118
, volume:51 |
| Schlagwörter: | |
| Quelle: | Verbunddaten SWB Lizenzfreie Online-Ressourcen |
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| 520 | |a In this paper heat transfer coefficients for film condensation of carbon dioxide under elevated pressures are presented. The examined pressure ranges from 16-30 bars with a constant mass flow of 12 kg/h CO2. Therefore, a pilot plant for cryogenic liquefaction of CO2has been built. In the installed tube in tube condenser cooling media temperatures from -25 °C to -45 °C were used. During the experiment heat transfer coefficients between 4500 and 13000 W/(m2K) were determined. Afterwards the experimental data were compared to common correlations for film condensation. The aim was to prove whether the influence of the elevated pressure can be predicted. Finally, all correlations could predict the heat transfer under elevated pressures in a suitable manner, concerning the uncertainties in modeling and determination of heat transfer coefficients. Nevertheless not all correlations could predict the influence of elevated pressures equally well. | ||
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| author | Küster, Thorsten, Eggers, Rudolf |
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| author_facet | Küster, Thorsten, Eggers, Rudolf, Technische Universität Hamburg-Harburg, Technische Universität Hamburg-Harburg, Technische Universität Hamburg-Harburg Institut für Thermische Verfahrenstechnik, Technische Universität Hamburg-Harburg Institut für Thermische Verfahrenstechnik |
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| contents | In this paper heat transfer coefficients for film condensation of carbon dioxide under elevated pressures are presented. The examined pressure ranges from 16-30 bars with a constant mass flow of 12 kg/h CO2. Therefore, a pilot plant for cryogenic liquefaction of CO2has been built. In the installed tube in tube condenser cooling media temperatures from -25 °C to -45 °C were used. During the experiment heat transfer coefficients between 4500 and 13000 W/(m2K) were determined. Afterwards the experimental data were compared to common correlations for film condensation. The aim was to prove whether the influence of the elevated pressure can be predicted. Finally, all correlations could predict the heat transfer under elevated pressures in a suitable manner, concerning the uncertainties in modeling and determination of heat transfer coefficients. Nevertheless not all correlations could predict the influence of elevated pressures equally well. |
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| spelling | Küster, Thorsten 1983- VerfasserIn (DE-588)1123648042 (DE-627)877242836 (DE-576)481853758 aut, Liquefaction of oxyfuel flue gases experimental results and modeling of heat transfer coefficients for pure CO2 T. Küster, R. Eggers, 28 August 2014, Diagramme, Text txt rdacontent, Computermedien c rdamedia, Online-Ressource cr rdacarrier, In this paper heat transfer coefficients for film condensation of carbon dioxide under elevated pressures are presented. The examined pressure ranges from 16-30 bars with a constant mass flow of 12 kg/h CO2. Therefore, a pilot plant for cryogenic liquefaction of CO2has been built. In the installed tube in tube condenser cooling media temperatures from -25 °C to -45 °C were used. During the experiment heat transfer coefficients between 4500 and 13000 W/(m2K) were determined. Afterwards the experimental data were compared to common correlations for film condensation. The aim was to prove whether the influence of the elevated pressure can be predicted. Finally, all correlations could predict the heat transfer under elevated pressures in a suitable manner, concerning the uncertainties in modeling and determination of heat transfer coefficients. Nevertheless not all correlations could predict the influence of elevated pressures equally well., CCS, oxyfuel, liquefaction, heat transfer, Eggers, Rudolf VerfasserIn (DE-588)1180428064 (DE-627)1067710973 (DE-576)520162811 aut, Technische Universität Hamburg-Harburg Sonstige Körperschaft (DE-588)2067664-5 (DE-627)103632417 (DE-576)192125400 oth, Technische Universität Hamburg-Harburg Institut für Thermische Verfahrenstechnik Sonstige Körperschaft (DE-588)10199933-1 (DE-627)562028404 (DE-576)278967213 oth, Enthalten in Energy procedia Amsterdam [u.a.] : Elsevier, 2009 51(2014), Seite 109-118 Online-Ressource (DE-627)598096337 (DE-600)2490671-2 (DE-576)306838575 1876-6102, volume:51 year:2014 pages:109-118, https://doi.org/10.1016/j.egypro.2014.07.012 Resolving-System Volltext, http://nbn-resolving.de/urn:nbn:de:gbv:830-882.027614 Resolving-System kostenfrei Volltext, https://doi.org/10.15480/882.2083 Resolving-System kostenfrei Volltext, https://hdl.handle.net/11420/2087 Resolving-System Volltext, http://nbn-resolving.de/urn:nbn:de:gbv:830-882.027614 LFER, LFER 2019-05-07T00:00:00Z |
| spellingShingle | Küster, Thorsten, Eggers, Rudolf, Liquefaction of oxyfuel flue gases: experimental results and modeling of heat transfer coefficients for pure CO2, In this paper heat transfer coefficients for film condensation of carbon dioxide under elevated pressures are presented. The examined pressure ranges from 16-30 bars with a constant mass flow of 12 kg/h CO2. Therefore, a pilot plant for cryogenic liquefaction of CO2has been built. In the installed tube in tube condenser cooling media temperatures from -25 °C to -45 °C were used. During the experiment heat transfer coefficients between 4500 and 13000 W/(m2K) were determined. Afterwards the experimental data were compared to common correlations for film condensation. The aim was to prove whether the influence of the elevated pressure can be predicted. Finally, all correlations could predict the heat transfer under elevated pressures in a suitable manner, concerning the uncertainties in modeling and determination of heat transfer coefficients. Nevertheless not all correlations could predict the influence of elevated pressures equally well., CCS, oxyfuel, liquefaction, heat transfer |
| title | Liquefaction of oxyfuel flue gases: experimental results and modeling of heat transfer coefficients for pure CO2 |
| title_auth | Liquefaction of oxyfuel flue gases experimental results and modeling of heat transfer coefficients for pure CO2 |
| title_full | Liquefaction of oxyfuel flue gases experimental results and modeling of heat transfer coefficients for pure CO2 T. Küster, R. Eggers |
| title_fullStr | Liquefaction of oxyfuel flue gases experimental results and modeling of heat transfer coefficients for pure CO2 T. Küster, R. Eggers |
| title_full_unstemmed | Liquefaction of oxyfuel flue gases experimental results and modeling of heat transfer coefficients for pure CO2 T. Küster, R. Eggers |
| title_in_hierarchy | Liquefaction of oxyfuel flue gases: experimental results and modeling of heat transfer coefficients for pure CO2 / T. Küster, R. Eggers, |
| title_short | Liquefaction of oxyfuel flue gases |
| title_sort | liquefaction of oxyfuel flue gases experimental results and modeling of heat transfer coefficients for pure co2 |
| title_sub | experimental results and modeling of heat transfer coefficients for pure CO2 |
| title_unstemmed | Liquefaction of oxyfuel flue gases: experimental results and modeling of heat transfer coefficients for pure CO2 |
| topic | CCS, oxyfuel, liquefaction, heat transfer |
| topic_facet | CCS, oxyfuel, liquefaction, heat transfer |
| url | https://doi.org/10.1016/j.egypro.2014.07.012, http://nbn-resolving.de/urn:nbn:de:gbv:830-882.027614, https://doi.org/10.15480/882.2083, https://hdl.handle.net/11420/2087 |
| urn | urn:nbn:de:gbv:830-882.027614 |