化学工程
化學工程
화학공정
CHEMICAL ENGINEERING
2010年
3期
1-4
,共4页
王群昌%马学虎%薄守石%苏风民%陈宏霞%陈嘉宾
王群昌%馬學虎%薄守石%囌風民%陳宏霞%陳嘉賓
왕군창%마학호%박수석%소풍민%진굉하%진가빈
第2类吸收式热泵%管内降膜%螺旋管%ABSIM模拟
第2類吸收式熱泵%管內降膜%螺鏇管%ABSIM模擬
제2류흡수식열빙%관내강막%라선관%ABSIM모의
absorption heat-transformer%falling film inside tubes%spiral tube%ABSIM simulation
分别考察了在垂直螺旋管内降膜式第2类吸收热泵系统中,溶液流量、循环热水流量、操作温度对吸收器传热传质系数、系统性能系数COP及热效率E_(th)的影响.实验结果表明:随着溶液流量的增加,吸收器的传热传质系数也逐渐增大,而COP与E_(th)则有下降趋势;增加循环热水流量,吸收器传热传质系数也增大,但对COP与E_(th)的影响却较小;对于操作温度,吸收器传热传质系数会随着废热温度的升高而增大,随着冷却水温度的降低而增大.同时,通过软件ABSIM的模拟计算,得到的数据与实验数据吻合较好.
分彆攷察瞭在垂直螺鏇管內降膜式第2類吸收熱泵繫統中,溶液流量、循環熱水流量、操作溫度對吸收器傳熱傳質繫數、繫統性能繫數COP及熱效率E_(th)的影響.實驗結果錶明:隨著溶液流量的增加,吸收器的傳熱傳質繫數也逐漸增大,而COP與E_(th)則有下降趨勢;增加循環熱水流量,吸收器傳熱傳質繫數也增大,但對COP與E_(th)的影響卻較小;對于操作溫度,吸收器傳熱傳質繫數會隨著廢熱溫度的升高而增大,隨著冷卻水溫度的降低而增大.同時,通過軟件ABSIM的模擬計算,得到的數據與實驗數據吻閤較好.
분별고찰료재수직라선관내강막식제2류흡수열빙계통중,용액류량、순배열수류량、조작온도대흡수기전열전질계수、계통성능계수COP급열효솔E_(th)적영향.실험결과표명:수착용액류량적증가,흡수기적전열전질계수야축점증대,이COP여E_(th)칙유하강추세;증가순배열수류량,흡수기전열전질계수야증대,단대COP여E_(th)적영향각교소;대우조작온도,흡수기전열전질계수회수착폐열온도적승고이증대,수착냉각수온도적강저이증대.동시,통과연건ABSIM적모의계산,득도적수거여실험수거문합교호.
The effects of solution flow rate, circular hot water flow rate and operating temperature on the heat and mass transfer coefficients of absorber, coefficient of performance COP, and thermal efficiency E_(th) were investigated in an absorption heat-transformer (AHT) system with falling film inside vertical spiral tubes. The experimental results show that the heat and mass transfer coefficients of absorber increase with the increase of solution flow rate in falling film and circular hot water. The COP and E_(th) decrease with the increase of falling film flow rate, and there is little influence on COP and E_(th) of the AHT system with the increase of circular hot water flow rate. The heat and mass transfer coefficients increase with the increase of waste heat temperature and the decease of cooling water inlet temperature. The calculations of computer code Absorption Simulation (ABSIM) agree well with the experimental data.