化工学报
化工學報
화공학보
JOURNAL OF CHEMICAL INDUSY AND ENGINEERING (CHINA)
2015年
2期
51-57
,共7页
刘闪威%吴玉庭%崔武军%熊亚选%陈夏%鹿院卫%马重芳
劉閃威%吳玉庭%崔武軍%熊亞選%陳夏%鹿院衛%馬重芳
류섬위%오옥정%최무군%웅아선%진하%록원위%마중방
低熔点熔盐%强迫对流%对流传热系数
低鎔點鎔鹽%彊迫對流%對流傳熱繫數
저용점용염%강박대류%대류전열계수
low-melting point molten salt%forced convection%convective heat transfer coefficient
熔融盐具有使用温度高、热稳定性和传热性能好等优点,被认为是太阳能热发电系统中最有前途的传热、蓄热介质之一。通过搭建槽式太阳能熔盐集热传热实验台,进行了低熔点熔盐管内受迫对流换热实验,获得了不同熔盐流速下套管式熔盐-水传热单元的总传热系数;通过最小二乘法获得了低熔点熔盐管内充分发展紊流段对流换热 Nusselt 数随 Reynolds 数的变化曲线和实验关联式,并与经典关联式进行了对比,结果表明,实验数据和Dittus-Boelter方程、Colburn方程、Seider-Tate方程以及Gnielinski方程最大偏差分别为+23%、+13%、?10%和?20%,实验数据和经典公式符合较好。
鎔融鹽具有使用溫度高、熱穩定性和傳熱性能好等優點,被認為是太暘能熱髮電繫統中最有前途的傳熱、蓄熱介質之一。通過搭建槽式太暘能鎔鹽集熱傳熱實驗檯,進行瞭低鎔點鎔鹽管內受迫對流換熱實驗,穫得瞭不同鎔鹽流速下套管式鎔鹽-水傳熱單元的總傳熱繫數;通過最小二乘法穫得瞭低鎔點鎔鹽管內充分髮展紊流段對流換熱 Nusselt 數隨 Reynolds 數的變化麯線和實驗關聯式,併與經典關聯式進行瞭對比,結果錶明,實驗數據和Dittus-Boelter方程、Colburn方程、Seider-Tate方程以及Gnielinski方程最大偏差分彆為+23%、+13%、?10%和?20%,實驗數據和經典公式符閤較好。
용융염구유사용온도고、열은정성화전열성능호등우점,피인위시태양능열발전계통중최유전도적전열、축열개질지일。통과탑건조식태양능용염집열전열실험태,진행료저용점용염관내수박대류환열실험,획득료불동용염류속하투관식용염-수전열단원적총전열계수;통과최소이승법획득료저용점용염관내충분발전문류단대류환열 Nusselt 수수 Reynolds 수적변화곡선화실험관련식,병여경전관련식진행료대비,결과표명,실험수거화Dittus-Boelter방정、Colburn방정、Seider-Tate방정이급Gnielinski방정최대편차분별위+23%、+13%、?10%화?20%,실험수거화경전공식부합교호。
Molten salt as one of the most promising heat transfer and heat storage media in the concentrating solar power (CSP) system has such advantages as high and wide liquid temperature, good heat transfer performance, low operation pressure and good thermal stability. An experimental study on turbulent convective heat transfer with low-melting point molten salt in a circular tube was conducted by using a self-made parabolic trough solar collecting and heat transfer system with molten salt. The total heat transfer coefficients from water to salt in a concentric tube heat exchanger at different flow rates were obtained. The change of Nusselt number of low-melting point molten salt with Reynolds number was calculated with the least-square method and the experimental correlation were obtained. Comparison was also made between experimental data and well-known convective heat transfer correlations, with the maximum deviations between the present data and curves predicted by Dittus-Boelter, Colburn, Seider-Tate, and Gnielinski equations of+23%,+13%?10%and?20%respectively.