化工学报
化工學報
화공학보
JOURNAL OF CHEMICAL INDUSY AND ENGINEERING (CHINA)
2015年
6期
2076-2081
,共6页
欧阳新萍%陈静竹%李泰宇
歐暘新萍%陳靜竹%李泰宇
구양신평%진정죽%리태우
热力学%传热%气液两相流%沸腾%内螺纹管
熱力學%傳熱%氣液兩相流%沸騰%內螺紋管
열역학%전열%기액량상류%비등%내라문관
thermodynamics%heat transfer%gas-liquid flow%boiling%internal thread tube
对3种不同螺纹结构的强化管的管内沸腾换热性能进行对比实验研究,采用R22为实验工质。3种强化管的内径和外径相同,分别为6.9 mm和7.92 mm;管外均为光滑表面,管内的强化结构参数则不同:螺纹的螺旋角变化范围为14°~18°,螺纹高为0.15~0.22 mm,螺纹槽宽度为0.1~0.2 mm。在给定进口和出口制冷剂的状态下,通过改变管内工质的质量流速,测试3根强化管的换热特性与质量流速的关系,并进行性能对比。实验结果表明:3种螺纹管管内沸腾传热系数分别比光管高出60%~80%,80%~120%和80%。分析认为,当流动处于层状流或者层状流与环状流的过渡区时,较大的螺旋角有利于换热;当流体处于环状流时,较多的螺纹头数有利于换热。
對3種不同螺紋結構的彊化管的管內沸騰換熱性能進行對比實驗研究,採用R22為實驗工質。3種彊化管的內徑和外徑相同,分彆為6.9 mm和7.92 mm;管外均為光滑錶麵,管內的彊化結構參數則不同:螺紋的螺鏇角變化範圍為14°~18°,螺紋高為0.15~0.22 mm,螺紋槽寬度為0.1~0.2 mm。在給定進口和齣口製冷劑的狀態下,通過改變管內工質的質量流速,測試3根彊化管的換熱特性與質量流速的關繫,併進行性能對比。實驗結果錶明:3種螺紋管管內沸騰傳熱繫數分彆比光管高齣60%~80%,80%~120%和80%。分析認為,噹流動處于層狀流或者層狀流與環狀流的過渡區時,較大的螺鏇角有利于換熱;噹流體處于環狀流時,較多的螺紋頭數有利于換熱。
대3충불동라문결구적강화관적관내비등환열성능진행대비실험연구,채용R22위실험공질。3충강화관적내경화외경상동,분별위6.9 mm화7.92 mm;관외균위광활표면,관내적강화결구삼수칙불동:라문적라선각변화범위위14°~18°,라문고위0.15~0.22 mm,라문조관도위0.1~0.2 mm。재급정진구화출구제랭제적상태하,통과개변관내공질적질량류속,측시3근강화관적환열특성여질량류속적관계,병진행성능대비。실험결과표명:3충라문관관내비등전열계수분별비광관고출60%~80%,80%~120%화80%。분석인위,당류동처우층상류혹자층상류여배상류적과도구시,교대적라선각유리우환열;당류체처우배상류시,교다적라문두수유리우환열。
An experimental study was carried out on the boiling heat transfer of R22 flowing inside three internal thread tubes with different geometrical parameters. Three enhanced tubes have the same inner and outer diameters, which are 6.9 mm and 7.92 mm respectively. The outside surface of the tube is smooth, while the inside enhanced structure is different. The variation range of the helix angle is from14° to18°, the thread height is between 0.15 mm and 0.22 mm, and the thread width is from 0.1 mm to 0.2 mm. The relationship between the heat transfer performance and the mass velocity in three enhanced tubes and a smooth tube was tested by changing the mass velocity of refrigerant under given condition of import and export of refrigerant, and their performance is compared. Experimental results indicate that the heat transfer coefficients of three internal thread tubes are 60%—80%, 80%—120%and 80%higher than that of smooth tube. Analysis suggests that the larger helix angle is advantageous to the heat transfer ,when fluid is on laminar flow or the transition of laminar flow and annular flow, and more of thread amount is advantageous to the heat transfer,when the fluid is on annular flow.