Characteristics of frictional pressure drop of two-phase nitrogen flow in horizontal smooth mini channels in diabatic/adiabatic conditions
- 1. State Key Laboratory of Multiphase Flow in Power Engineering, Xi'an Jiaotong University, Xi'an, 710049 (China)
Description
The two-phase frictional pressure drop of nitrogen under diabatic and adiabatic conditions is investigated experimentally in two horizontal mini channels. The effects of factors in a variety, including the channel diameter, mass flux, heat flux, inlet pressure and vapor quality are examined on the frictional pressure drop and liquid-phase multiplier of the two-phase flow. The two-phase frictional pressure drop predicted by previous correlations from other studies are compared with the experimental results of this study, and the lowest mean absolute deviation is 18.3% for adiabatic conditions and 10.9% for adiabatic conditions. Based on the experimental results of nitrogen flow, two new correlations in the form of the Chisholm-C correlation are developed to predict the two-phase frictional pressure dropby involving the effect of surface tension, and the mean absolute deviation of which is 12.3% and 10.4% for the adiabatic and diabatic conditions respectively. The new correlations are also shown able to well predict the experimental frictional pressure drop of other studies under different experimental conditions.
Additional details
Identifiers
- DOI
- 10.1016/j.applthermaleng.2019.114312;
- PII
- S1359431119302674;
Publishing Information
- Journal Title
- Applied Thermal Engineering
- Journal Volume
- 162
- Journal Page Range
- vp.
- ISSN
- 1359-4311
- CODEN
- ATENFT
INIS
- Country of Publication
- United Kingdom
- Country of Input or Organization
- International Atomic Energy Agency (IAEA)
- INIS RN
- 55003906
- Subject category
- S42: ENGINEERING;
- Descriptors DEI
- HEAT FLUX; NITROGEN; PRESSURE DROP; SURFACE TENSION; TWO-PHASE FLOW; VAPORS
- Descriptors DEC
- ELEMENTS; FLUID FLOW; FLUIDS; GASES; NONMETALS; SURFACE PROPERTIES
Optional Information
- Copyright
- Copyright (c) 2019 Elsevier Ltd. All rights reserved.