Documents disponibles écrits par cet auteur

Charge reduction experimental investigation of CO2 single-phase flow in a horizontal micro-channel with constant heat flux conditions / Maxime Ducoulombier in International journal of refrigeration, Vol. 34 N° 4 (Juin 2011) 

Public ISBD [article]  in International journal of refrigeration > Vol. 34 N° 4 (Juin 2011) . - pp. 827-833 Titre : Charge reduction experimental investigation of CO2 single-phase flow in a horizontal micro-channel with constant heat flux conditions Titre original : Numéro spécial: étude expérimentale sur la réduction de la charge en CO2 en écoulement monophasique à l'intérieur d'un micro-canal horizontal sous des conditions de flux thermique constant Type de document : texte imprimé Auteurs : Maxime Ducoulombier, Auteur ; Stéphane Colasson, Auteur ; Philippe Haberschill, Auteur Année de publication : 2011 Article en page(s) : pp. 827-833 Note générale : Génie Mécanique Langues : Anglais (eng) Mots-clés : Carbon  dioxide  Micro-channel  Pressure  drop  Heat  transfer  Single-phase  flow  Experimental Index. décimale : 621.5 Energie pneumatique. Machinerie et outils. Réfrigération Résumé : The use of carbon dioxide as alternative refrigerant in refrigeration plants and heat pumps has been focused recently. Through the specific properties of CO2, the use of very compact heat exchangers is relevant and the technology of micro-channel heat exchangers rises as a suitable solution. The experimental investigation of CO2 flow in a single micro-channel with an inner diameter of 529 μm is planned with an original test section. This test section is initially dedicated for further CO2 two-phase flow analysis. The local heat transfer coefficients are estimated with micro-thermocouples stuck on the micro-channel wall. The pressure drop is also measured. This paper presents the first results in single-phase pressure drop and heat transfer and exhibits promising coming data in two-phase flow pressure drop and heat transfer for mass velocity between 200 kg/m2/s and 1400 kg/m2/s and working saturation temperature between −10 °C and 5 °C. The results stress on the good accuracy of suitable classical laws to predict pressure drop and heat transfer in single-phase flow in micro-channel. DEWEY : 621.5 ISSN : 0140-7007 En ligne : http://www.sciencedirect.com/science/article/pii/S0140700711000260 [article] Charge reduction experimental investigation of CO2 single-phase flow in a horizontal micro-channel with constant heat flux conditions = Numéro spécial: étude expérimentale sur la réduction de la charge en CO2 en écoulement monophasique à l'intérieur d'un micro-canal horizontal sous des conditions de flux thermique constant [texte imprimé] / Maxime Ducoulombier, Auteur ; Stéphane Colasson, Auteur ; Philippe Haberschill, Auteur . - 2011 . - pp. 827-833. Génie Mécanique Langues : Anglais (eng) in International journal of refrigeration > Vol. 34 N° 4 (Juin 2011) . - pp. 827-833 Mots-clés : Carbon  dioxide  Micro-channel  Pressure  drop  Heat  transfer  Single-phase  flow  Experimental Index. décimale : 621.5 Energie pneumatique. Machinerie et outils. Réfrigération Résumé : The use of carbon dioxide as alternative refrigerant in refrigeration plants and heat pumps has been focused recently. Through the specific properties of CO2, the use of very compact heat exchangers is relevant and the technology of micro-channel heat exchangers rises as a suitable solution. The experimental investigation of CO2 flow in a single micro-channel with an inner diameter of 529 μm is planned with an original test section. This test section is initially dedicated for further CO2 two-phase flow analysis. The local heat transfer coefficients are estimated with micro-thermocouples stuck on the micro-channel wall. The pressure drop is also measured. This paper presents the first results in single-phase pressure drop and heat transfer and exhibits promising coming data in two-phase flow pressure drop and heat transfer for mass velocity between 200 kg/m2/s and 1400 kg/m2/s and working saturation temperature between −10 °C and 5 °C. The results stress on the good accuracy of suitable classical laws to predict pressure drop and heat transfer in single-phase flow in micro-channel. DEWEY : 621.5 ISSN : 0140-7007 En ligne : http://www.sciencedirect.com/science/article/pii/S0140700711000260

Two-phase pressure drop in return bends / Miguel Padilla in International journal of refrigeration, Vol. 34 N° 8 (Décembre 2011) 

Public ISBD [article]  in International journal of refrigeration > Vol. 34 N° 8 (Décembre 2011) . - pp. 1854–1865 Titre : Two-phase pressure drop in return bends : Experimental results for R-410A Titre original : Chute de pression diphasique dans les coudes de retour : résultats expérimentaux obtenus avec le R-410A Type de document : texte imprimé Auteurs : Miguel Padilla, Auteur ; Rémi Revellin, Auteur ; Philippe Haberschill, Auteur Année de publication : 2012 Article en page(s) : pp. 1854–1865 Note générale : Génie mécanique Langues : Anglais (eng) Mots-clés : Two-phase  flow  Pressure  drop  Refrigerant  Experimentation Résumé : This study presents 238 pressure drop data points measured for two-phase flow of R-410A in horizontal return bends. The tube diameter (D) varies from 7.90 to 10.85 mm and the curvature ratio (2R/D) from 3.68 to 4.05. The mass velocity ranges from 179 to 1695 kg m−2 s−1 and the saturation temperatures from 4.6 °C to 20.7 °C. Preliminary tests show that the recovery length necessary for a correct pressure drop measurement downstream of the return bend is less than 20D, for the experimental conditions covered in this study. The singular pressure drop is determined by subtracting the regular pressure drop in straight tube from the total pressure drop. The experimental data are compared against four available correlations found in the literature. The present experimental database for the return bend pressure drop is presented in the Appendix A. ISSN : 0140-7007 En ligne : http://www.sciencedirect.com/science/article/pii/S0140700711000727 [article] Two-phase pressure drop in return bends = Chute de pression diphasique dans les coudes de retour : résultats expérimentaux obtenus avec le R-410A : Experimental results for R-410A [texte imprimé] / Miguel Padilla, Auteur ; Rémi Revellin, Auteur ; Philippe Haberschill, Auteur . - 2012 . - pp. 1854–1865. Génie mécanique Langues : Anglais (eng) in International journal of refrigeration > Vol. 34 N° 8 (Décembre 2011) . - pp. 1854–1865 Mots-clés : Two-phase  flow  Pressure  drop  Refrigerant  Experimentation Résumé : This study presents 238 pressure drop data points measured for two-phase flow of R-410A in horizontal return bends. The tube diameter (D) varies from 7.90 to 10.85 mm and the curvature ratio (2R/D) from 3.68 to 4.05. The mass velocity ranges from 179 to 1695 kg m−2 s−1 and the saturation temperatures from 4.6 °C to 20.7 °C. Preliminary tests show that the recovery length necessary for a correct pressure drop measurement downstream of the return bend is less than 20D, for the experimental conditions covered in this study. The singular pressure drop is determined by subtracting the regular pressure drop in straight tube from the total pressure drop. The experimental data are compared against four available correlations found in the literature. The present experimental database for the return bend pressure drop is presented in the Appendix A. ISSN : 0140-7007 En ligne : http://www.sciencedirect.com/science/article/pii/S0140700711000727