山东大学学报(工学版)
山東大學學報(工學版)
산동대학학보(공학판)
JOURNAL OF SHANDONG UNIVERSITY(ENGINEERING SCIENCE)
2014年
4期
72-77
,共6页
李飞%孙奉仲%史月涛%马磊
李飛%孫奉仲%史月濤%馬磊
리비%손봉중%사월도%마뢰
场协同%阻力特性%传热特性%管排阻力修正系数%相对场协同率
場協同%阻力特性%傳熱特性%管排阻力脩正繫數%相對場協同率
장협동%조력특성%전열특성%관배조력수정계수%상대장협동솔
field synergy%resistance characteristic%heat transfer characteristic%bundle resistance correction coefficient%rate of relative field synergy
为分析前排绕流扰动对后排管换热及阻力的影响规律,以4列多排(2~10)管束为研究对象,建立稳定的热态流场,采用错列及顺列2种方式,分析传热及流动特性在不同管排数下的变化规律;定量分析管排数对阻力特性的影响规律,定义了管排阻力修正系数,并根据实验数据给出了其在不同管排数下的取值;根据场协同理论定义了相对场协同率的概念,用以表征不同管排数下其总体换热效率相对实际最大换热的比值。研究结果表明,管间绕流为管束换热器管排影响规律的主要原因,10排及以上管束流场均匀,管间绕流影响最小,场协同角较小,10排以内采用管排系数进行修正。
為分析前排繞流擾動對後排管換熱及阻力的影響規律,以4列多排(2~10)管束為研究對象,建立穩定的熱態流場,採用錯列及順列2種方式,分析傳熱及流動特性在不同管排數下的變化規律;定量分析管排數對阻力特性的影響規律,定義瞭管排阻力脩正繫數,併根據實驗數據給齣瞭其在不同管排數下的取值;根據場協同理論定義瞭相對場協同率的概唸,用以錶徵不同管排數下其總體換熱效率相對實際最大換熱的比值。研究結果錶明,管間繞流為管束換熱器管排影響規律的主要原因,10排及以上管束流場均勻,管間繞流影響最小,場協同角較小,10排以內採用管排繫數進行脩正。
위분석전배요류우동대후배관환열급조력적영향규률,이4렬다배(2~10)관속위연구대상,건립은정적열태류장,채용착렬급순렬2충방식,분석전열급류동특성재불동관배수하적변화규률;정량분석관배수대조력특성적영향규률,정의료관배조력수정계수,병근거실험수거급출료기재불동관배수하적취치;근거장협동이론정의료상대장협동솔적개념,용이표정불동관배수하기총체환열효솔상대실제최대환열적비치。연구결과표명,관간요류위관속환열기관배영향규률적주요원인,10배급이상관속류장균균,관간요류영향최소,장협동각교소,10배이내채용관배계수진행수정。
Experimental studies, establishing a stable thermal state flow field with 4 tube rows and multiple columns ( varied from 2 to 10) in staggered and in-line arrangement, were carried out to analyze the rules of the heat transfer and flow characteristics under different tube rows to obtain the influence rules of flowing around front tubes on the resistance of back rows.In order to obtain the influence rules of the number of tube rows on the resistance characteristics, bundle resistance correction coefficient was defined and values were given according to a series of experimental data.Rate of relative field synergy based on the field synergy principle was defined to characterize the ratio of the overall heat transfer efficiency relative to the actual maximum heat transfer with different numbers of tube rows.The results showed that the flow disturbance around the tail was the major factor in the deterioration of the resistance and the enhancement of the heat transfer, the flow fields up to 10 rows were well-distributed with the minimum influence of the flow disturbance around the tail and small synergy angles, the flow fields within 10 rows should be corrected with tube row correction factor.