压力容器
壓力容器
압력용기
2013年
10期
18-23,41
,共7页
郭土%马贵阳%何洋%王有龙%李武华
郭土%馬貴暘%何洋%王有龍%李武華
곽토%마귀양%하양%왕유룡%리무화
管壳式换热器%壳程压降%数值模拟%六分花格板
管殼式換熱器%殼程壓降%數值模擬%六分花格闆
관각식환열기%각정압강%수치모의%륙분화격판
shell -and -tube heat exchanger%shell side pressure drop%numerical simulation%sextant flower baffle
针对传统折流板换热器壳程压降大的特点,提出了一种新型的六分花格板换热器。建立了六分花格板换热器的物理模型,应用CFD技术,对六分花格板换热器的流动和传热性能进行了研究,并将结果与传统的弓形折流板换热器进行了比较。结果表明,在相同壳程进口流速下,六分花格板换热器压降为弓形折流板换热器的64%,壳程进口流速较低时两者的换热系数相差不大,综合性能比弓形折流板换热器提高40%。
針對傳統摺流闆換熱器殼程壓降大的特點,提齣瞭一種新型的六分花格闆換熱器。建立瞭六分花格闆換熱器的物理模型,應用CFD技術,對六分花格闆換熱器的流動和傳熱性能進行瞭研究,併將結果與傳統的弓形摺流闆換熱器進行瞭比較。結果錶明,在相同殼程進口流速下,六分花格闆換熱器壓降為弓形摺流闆換熱器的64%,殼程進口流速較低時兩者的換熱繫數相差不大,綜閤性能比弓形摺流闆換熱器提高40%。
침대전통절류판환열기각정압강대적특점,제출료일충신형적륙분화격판환열기。건립료륙분화격판환열기적물리모형,응용CFD기술,대륙분화격판환열기적류동화전열성능진행료연구,병장결과여전통적궁형절류판환열기진행료비교。결과표명,재상동각정진구류속하,륙분화격판환열기압강위궁형절류판환열기적64%,각정진구류속교저시량자적환열계수상차불대,종합성능비궁형절류판환열기제고40%。
For the high shell side pressure drop of the traditional baffle heat exchanger,a novel sextant flower baffled heat exchanger was put forward.The physical model of the novel heat exchanger was built, CFD software was used to obtain detailed shell-side fluid flow and heat transfer performances,compari-son was also made between the new and the traditional baffle heat exchanger.Results show that the pres-sure drop of the former is 64% of that of the latter with the same import velocity of shell side,when the import velocity is low,the difference of heat transfer coefficient between the two exchangers is minor,and the comprehensive performance of the former is 40% greater than that of the traditional baffle heat ex-changer.