Micro-channels Fin-and-Tube Evaporator Design Using CO2 as Working Fluid

碩士 === 國立中央大學 === 機械工程研究所 === 98 === An investigation of micro-channels fin-and-tube evaporator design using CO2 as working fluid is described and a design program is also developed. The design method is based on thermal balance design. Because there is neither fin-and-tube evaporator for CO2 nor th...

Full description

Bibliographic Details
Main Authors: Yu-wei Jeng, 鄭于瑋
Other Authors: Chien-yuh Yang
Format: Others
Language:zh-TW
Published: 2010
Online Access:http://ndltd.ncl.edu.tw/handle/91239080354192909927
id ndltd-TW-098NCU05489032
record_format oai_dc
spelling ndltd-TW-098NCU054890322016-04-20T04:17:47Z http://ndltd.ncl.edu.tw/handle/91239080354192909927 Micro-channels Fin-and-Tube Evaporator Design Using CO2 as Working Fluid 二氧化碳冷媒微流道扁平管蒸發器設計 Yu-wei Jeng 鄭于瑋 碩士 國立中央大學 機械工程研究所 98 An investigation of micro-channels fin-and-tube evaporator design using CO2 as working fluid is described and a design program is also developed. The design method is based on thermal balance design. Because there is neither fin-and-tube evaporator for CO2 nor the experimental results, apply water as working fluid in the program, and compare the design results with experimental results. Then using the same procedure design the micro-channels fin-and-tube evaporator for CO2. For CO2, after the dryout quality, the heat transfer coefficient decreases by quality increasing. And it can’t achieve thermal balance design. According to this reason, the heat transfer coefficient in the dryout region is not included in thermal balance. Moreover, CO2 heat transfer coefficient is high, and it makes the resistance between air side and refrigerant side unbalanced. The heat exchanger for water is not suitable for CO2. Chien-yuh Yang 楊建裕 2010 學位論文 ; thesis 124 zh-TW
collection NDLTD
language zh-TW
format Others
sources NDLTD
description 碩士 === 國立中央大學 === 機械工程研究所 === 98 === An investigation of micro-channels fin-and-tube evaporator design using CO2 as working fluid is described and a design program is also developed. The design method is based on thermal balance design. Because there is neither fin-and-tube evaporator for CO2 nor the experimental results, apply water as working fluid in the program, and compare the design results with experimental results. Then using the same procedure design the micro-channels fin-and-tube evaporator for CO2. For CO2, after the dryout quality, the heat transfer coefficient decreases by quality increasing. And it can’t achieve thermal balance design. According to this reason, the heat transfer coefficient in the dryout region is not included in thermal balance. Moreover, CO2 heat transfer coefficient is high, and it makes the resistance between air side and refrigerant side unbalanced. The heat exchanger for water is not suitable for CO2.
author2 Chien-yuh Yang
author_facet Chien-yuh Yang
Yu-wei Jeng
鄭于瑋
author Yu-wei Jeng
鄭于瑋
spellingShingle Yu-wei Jeng
鄭于瑋
Micro-channels Fin-and-Tube Evaporator Design Using CO2 as Working Fluid
author_sort Yu-wei Jeng
title Micro-channels Fin-and-Tube Evaporator Design Using CO2 as Working Fluid
title_short Micro-channels Fin-and-Tube Evaporator Design Using CO2 as Working Fluid
title_full Micro-channels Fin-and-Tube Evaporator Design Using CO2 as Working Fluid
title_fullStr Micro-channels Fin-and-Tube Evaporator Design Using CO2 as Working Fluid
title_full_unstemmed Micro-channels Fin-and-Tube Evaporator Design Using CO2 as Working Fluid
title_sort micro-channels fin-and-tube evaporator design using co2 as working fluid
publishDate 2010
url http://ndltd.ncl.edu.tw/handle/91239080354192909927
work_keys_str_mv AT yuweijeng microchannelsfinandtubeevaporatordesignusingco2asworkingfluid
AT zhèngyúwěi microchannelsfinandtubeevaporatordesignusingco2asworkingfluid
AT yuweijeng èryǎnghuàtànlěngméiwēiliúdàobiǎnpíngguǎnzhēngfāqìshèjì
AT zhèngyúwěi èryǎnghuàtànlěngméiwēiliúdàobiǎnpíngguǎnzhēngfāqìshèjì
_version_ 1718228307306086400