Flow boiling of ammonia in a plain and a low finned horizontal tube

Publikation: Beitrag in FachzeitschriftArtikelForschungPeer-Review

Autoren

  • S. Kabelac
  • H.-J. de Buhr

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Details

Titel in ÜbersetzungEbullition en éncoulement d'ammoniac dans un tube lisse ou un tube ailetté
OriginalspracheEnglisch
Seiten (von - bis)41-50
Seitenumfang10
FachzeitschriftInternational Journal of Refrigeration
Jahrgang24
Ausgabenummer1
Frühes Online-Datum30 Nov. 2000
PublikationsstatusVeröffentlicht - Jan. 2001

Abstract

Experimental data of the local heat transfer coefficient of flow boiling ammonia in dependence of vapor fraction, mass flux and local heat flux is presented. Two horizontal test sections of 450 mm length and an inner diameter of 10 mm have been used, one being a plain tube, one being a spirally low finned tube. A constant wall temperature boundary has been aimed for the test section by heating with a fluid condensing on the tube outside. Local heat transfer coefficients and pressure drops have been measured in the range -40<Tsat<4 °C, 0<x<0.9, 50<m<150 kg/m2s and 2<ΔTw<15 K with resulting heat fluxes of 17<q<75 kW/m2. The vapor quality is denoted as x, m is the mass flux and ΔTw the wall superheat. The measured data is carefully evaluated using a finite element model of the tube with regard to the circumferential heat flow distribution. The smooth tube results are compared with recently published data and the correlation from Zuercher, and with the correlations of Steiner and Kattan. The results of the low finned tube are not matched by any known correlation.

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Flow boiling of ammonia in a plain and a low finned horizontal tube. / Kabelac, S.; de Buhr, H.-J.
in: International Journal of Refrigeration, Jahrgang 24, Nr. 1, 01.2001, S. 41-50.

Publikation: Beitrag in FachzeitschriftArtikelForschungPeer-Review

Kabelac S, de Buhr HJ. Flow boiling of ammonia in a plain and a low finned horizontal tube. International Journal of Refrigeration. 2001 Jan;24(1):41-50. Epub 2000 Nov 30. doi: 10.1016/S0140-7007(00)00066-9
Kabelac, S. ; de Buhr, H.-J. / Flow boiling of ammonia in a plain and a low finned horizontal tube. in: International Journal of Refrigeration. 2001 ; Jahrgang 24, Nr. 1. S. 41-50.
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title = "Flow boiling of ammonia in a plain and a low finned horizontal tube",
abstract = "Experimental data of the local heat transfer coefficient of flow boiling ammonia in dependence of vapor fraction, mass flux and local heat flux is presented. Two horizontal test sections of 450 mm length and an inner diameter of 10 mm have been used, one being a plain tube, one being a spirally low finned tube. A constant wall temperature boundary has been aimed for the test section by heating with a fluid condensing on the tube outside. Local heat transfer coefficients and pressure drops have been measured in the range -40<Tsat<4 °C, 02s and 2<ΔTw<15 K with resulting heat fluxes of 172. The vapor quality is denoted as x, m is the mass flux and ΔTw the wall superheat. The measured data is carefully evaluated using a finite element model of the tube with regard to the circumferential heat flow distribution. The smooth tube results are compared with recently published data and the correlation from Zuercher, and with the correlations of Steiner and Kattan. The results of the low finned tube are not matched by any known correlation.",
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Download

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AU - Kabelac, S.

AU - de Buhr, H.-J.

N1 - Funding Information: Financial support of the Arbeitsgemeinschaft industrieller Forschungsvereinigungen (AiF) (German work group on industrial research) and the Forschungsrat Kältetechnik (FKT) (German refrigeration research association) is gratefully acknowledged. Copyright: Copyright 2017 Elsevier B.V., All rights reserved.

PY - 2001/1

Y1 - 2001/1

N2 - Experimental data of the local heat transfer coefficient of flow boiling ammonia in dependence of vapor fraction, mass flux and local heat flux is presented. Two horizontal test sections of 450 mm length and an inner diameter of 10 mm have been used, one being a plain tube, one being a spirally low finned tube. A constant wall temperature boundary has been aimed for the test section by heating with a fluid condensing on the tube outside. Local heat transfer coefficients and pressure drops have been measured in the range -40<Tsat<4 °C, 02s and 2<ΔTw<15 K with resulting heat fluxes of 172. The vapor quality is denoted as x, m is the mass flux and ΔTw the wall superheat. The measured data is carefully evaluated using a finite element model of the tube with regard to the circumferential heat flow distribution. The smooth tube results are compared with recently published data and the correlation from Zuercher, and with the correlations of Steiner and Kattan. The results of the low finned tube are not matched by any known correlation.

AB - Experimental data of the local heat transfer coefficient of flow boiling ammonia in dependence of vapor fraction, mass flux and local heat flux is presented. Two horizontal test sections of 450 mm length and an inner diameter of 10 mm have been used, one being a plain tube, one being a spirally low finned tube. A constant wall temperature boundary has been aimed for the test section by heating with a fluid condensing on the tube outside. Local heat transfer coefficients and pressure drops have been measured in the range -40<Tsat<4 °C, 02s and 2<ΔTw<15 K with resulting heat fluxes of 172. The vapor quality is denoted as x, m is the mass flux and ΔTw the wall superheat. The measured data is carefully evaluated using a finite element model of the tube with regard to the circumferential heat flow distribution. The smooth tube results are compared with recently published data and the correlation from Zuercher, and with the correlations of Steiner and Kattan. The results of the low finned tube are not matched by any known correlation.

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