化工学报
化工學報
화공학보
JOURNAL OF CHEMICAL INDUSY AND ENGINEERING (CHINA)
2014年
10期
3884-3890
,共7页
气体%壁面过冷度%凝结%传热
氣體%壁麵過冷度%凝結%傳熱
기체%벽면과랭도%응결%전열
gas%wall subcooling%condensation%heat transfer
通过对竖直圆管外表面含不凝性气体蒸汽在中等壁面过冷度条件下的冷凝传热实验研究,分析了混合气体压力0.4~0.6 MPa、空气含量0.07~0.52以及壁面过冷度13~25℃时,蒸汽的冷凝换热特性,给出了冷凝传热过程中的经验关联式,并对氦气的存在及其对换热过程的影响进行了初步分析。结果表明:在混合气体压力及不凝性气体含量不变的条件下,壁面过冷度的降低利于冷凝传热系数的增长;所得到的经验关联式在低过冷度条件下能较好地对换热过程进行预测,且其与实验值的误差在±15%以内;实验条件下未发生氦气分层现象,相同不凝性气体质量分数条件下,氦气的存在会使冷凝传热系数降低约20%。
通過對豎直圓管外錶麵含不凝性氣體蒸汽在中等壁麵過冷度條件下的冷凝傳熱實驗研究,分析瞭混閤氣體壓力0.4~0.6 MPa、空氣含量0.07~0.52以及壁麵過冷度13~25℃時,蒸汽的冷凝換熱特性,給齣瞭冷凝傳熱過程中的經驗關聯式,併對氦氣的存在及其對換熱過程的影響進行瞭初步分析。結果錶明:在混閤氣體壓力及不凝性氣體含量不變的條件下,壁麵過冷度的降低利于冷凝傳熱繫數的增長;所得到的經驗關聯式在低過冷度條件下能較好地對換熱過程進行預測,且其與實驗值的誤差在±15%以內;實驗條件下未髮生氦氣分層現象,相同不凝性氣體質量分數條件下,氦氣的存在會使冷凝傳熱繫數降低約20%。
통과대수직원관외표면함불응성기체증기재중등벽면과랭도조건하적냉응전열실험연구,분석료혼합기체압력0.4~0.6 MPa、공기함량0.07~0.52이급벽면과랭도13~25℃시,증기적냉응환열특성,급출료냉응전열과정중적경험관련식,병대양기적존재급기대환열과정적영향진행료초보분석。결과표명:재혼합기체압력급불응성기체함량불변적조건하,벽면과랭도적강저리우냉응전열계수적증장;소득도적경험관련식재저과랭도조건하능교호지대환열과정진행예측,차기여실험치적오차재±15%이내;실험조건하미발생양기분층현상,상동불응성기체질량분수조건하,양기적존재회사냉응전열계수강저약20%。
An experimental investigation was conducted to evaluate the steam heat removal capacity in the presence of non-condensable gases (e.g. air, helium) over a vertical tube external surface under moderate wall subcooling. Under steam/air condition, condensation heat transfer coefficients were obtained under wall subcooling ranging from 13℃ to 25℃, total pressure ranging from 0.4 MPa to 0.6 MPa and air mass fraction ranging from 0.07 to 0.52. The experiments for the influence of wall subcooling on steam condensation heat transfer with a fixed pressure and air mass fraction were made. Under the same pressure with the same non-condensable gases mass fraction, the effect of wall subcooling on condensation heat transfer coefficient with non-condensable gases was negative. An empirical correlation for heat transfer coefficient was developed, covering all data points within 15%. Under steam/air/helium (simulating hydrogen) condition, the effect of helium mole fraction in non-condensable gases on heat transfer coefficient was investigated under wall subcooling ranging from 18℃ to 27℃, total pressure ranging from 0.53 MPa to 0.6 MPa, steam mass fraction ranging from 0.6 to 0.92 and helium mole fraction in non-condensable gases 0.3. The condensation heat transfer coefficients obtained from steam/air/helium condition were lower than those obtained from steam/air case. Helium stratification was not found under the experimental conditions. With the same non-condensable gases mass fraction, presence of helium lowered condensation heat transfer coefficient by around 20%.