石油炼制与化工
石油煉製與化工
석유련제여화공
PETROLEUM PROCESSING AND PETROCHEMICALS
2009年
10期
25-29
,共5页
孙荷静%朱冬生%吴治将%唐新宜
孫荷靜%硃鼕生%吳治將%唐新宜
손하정%주동생%오치장%당신의
波纹管%降膜流动%强化传热%蒸发式冷凝器
波紋管%降膜流動%彊化傳熱%蒸髮式冷凝器
파문관%강막류동%강화전열%증발식냉응기
corrugated tube%falling film flow%heat transfer enhancement%evaporative condenser
应用CFD软件模拟分析流体在竖波纹管和竖直圆管内的降膜流动情况,采用立式蒸发式冷凝器试验平台,在不同喷淋密度下,测量温度和流量等参数,计算波纹管管内各相间传热传质系数,并与相同参数(流速、温度)条件下圆管管内传热传质系数进行比较.模拟结果表明,在相同的喷淋密度下,波纹管竖管内水膜分布较圆管均匀;试验结果表明,随着喷淋密度在一定范围内增加,水膜传热系数、空气水当量传热系数、总传热传质系数均增大,且波纹管的传热性能明显优于圆管.
應用CFD軟件模擬分析流體在豎波紋管和豎直圓管內的降膜流動情況,採用立式蒸髮式冷凝器試驗平檯,在不同噴淋密度下,測量溫度和流量等參數,計算波紋管管內各相間傳熱傳質繫數,併與相同參數(流速、溫度)條件下圓管管內傳熱傳質繫數進行比較.模擬結果錶明,在相同的噴淋密度下,波紋管豎管內水膜分佈較圓管均勻;試驗結果錶明,隨著噴淋密度在一定範圍內增加,水膜傳熱繫數、空氣水噹量傳熱繫數、總傳熱傳質繫數均增大,且波紋管的傳熱性能明顯優于圓管.
응용CFD연건모의분석류체재수파문관화수직원관내적강막류동정황,채용입식증발식냉응기시험평태,재불동분림밀도하,측량온도화류량등삼수,계산파문관관내각상간전열전질계수,병여상동삼수(류속、온도)조건하원관관내전열전질계수진행비교.모의결과표명,재상동적분림밀도하,파문관수관내수막분포교원관균균;시험결과표명,수착분림밀도재일정범위내증가,수막전열계수、공기수당량전열계수、총전열전질계수균증대,차파문관적전열성능명현우우원관.
Falling film flow in vertical corrugated tube and circular tube was simulated by CFD software respectively,and a vertical evaporative condenser test platform was adopted to measure the temperature and flow rate under various spray densities.The heat and mass transfer coefficient of each phase interface inside corrugated tube was calculated based on the experimental data,and it was compared with that of inside circular tube under the same conditions.Simulation results indicate that at the same spray density,the water-film distribution in vertical corrugated tube is better than that of in circular tube.Experimental results show that with the increase of spray density in a certain range,the heat transfer coefficient of water-film,equivalent beat transfer coefficient of air-water and total heat and mass transfer coefficient increase.In addition,the heat transfer performance of corrugated tube is significantly better than that of circular tube.