化学工程
化學工程
화학공정
CHEMICAL ENGINEERING
2014年
6期
33-37,47
,共6页
杨富军%陈小龙%王光培%陈枫
楊富軍%陳小龍%王光培%陳楓
양부군%진소룡%왕광배%진풍
泡状管%数值模拟%强化传热%压降阻力%传热性能评价准则
泡狀管%數值模擬%彊化傳熱%壓降阻力%傳熱性能評價準則
포상관%수치모의%강화전열%압강조력%전열성능평개준칙
bubbly pipe%numerical simulation%heat transfer enhancement%pressure drop%performance evaluation criteria
针对泡状管管壳式换热器,采用FLUENT软件对其进行管程和壳程耦合传热的整体数值模拟,并将模拟结果与具有相同形式相同换热面积的光滑圆管换热器对比。通过结果对比分析泡状管强化传热的效果、压降及总传热系数的差异;评价泡状管壳式换热器的传热性能。结果表明:相比圆管,泡状管表面形状的变化对管壳两侧均起到强化传热的作用,同时管程流动阻力增大,但壳程阻力有所降低。总体传热系数较圆管有较大幅度提高。综合考虑总传热系数和压降,泡状管对壳程传热性能提升明显。
針對泡狀管管殼式換熱器,採用FLUENT軟件對其進行管程和殼程耦閤傳熱的整體數值模擬,併將模擬結果與具有相同形式相同換熱麵積的光滑圓管換熱器對比。通過結果對比分析泡狀管彊化傳熱的效果、壓降及總傳熱繫數的差異;評價泡狀管殼式換熱器的傳熱性能。結果錶明:相比圓管,泡狀管錶麵形狀的變化對管殼兩側均起到彊化傳熱的作用,同時管程流動阻力增大,但殼程阻力有所降低。總體傳熱繫數較圓管有較大幅度提高。綜閤攷慮總傳熱繫數和壓降,泡狀管對殼程傳熱性能提升明顯。
침대포상관관각식환열기,채용FLUENT연건대기진행관정화각정우합전열적정체수치모의,병장모의결과여구유상동형식상동환열면적적광활원관환열기대비。통과결과대비분석포상관강화전열적효과、압강급총전열계수적차이;평개포상관각식환열기적전열성능。결과표명:상비원관,포상관표면형상적변화대관각량측균기도강화전열적작용,동시관정류동조력증대,단각정조력유소강저。총체전열계수교원관유교대폭도제고。종합고필총전열계수화압강,포상관대각정전열성능제승명현。
Considering the coupled heat transfer between tube pass and shell pass,a numerical simulation of a whole tube-and-shell heat exchanger with bubbly pipe was carried out by using commercial codes of Fluent.The simulation results were compared with those of smooth pipe heat exchanger with same structure and surface area. The heat transfer enhancement and factors of pressure drop difference were discussed by comparing the results of the two kinds of heat exchanger.And the bubbly pipe heat exchanger performance was also reviewed.The results reveal that bubbly pipe can remarkably enhance the heat transfer on both side of the tube,and the overall heat transfer coefficient increases significantly than that of smooth pipe.The tube side pressure drop of bubbly pipe heat exchanger is higher than that of smooth pipe heat exchanger,but shell side pressure drop is lower.The performance evaluation criteria (PEC)show that bubbly pipe can improve the heat transfer performance in shell pass than smooth pipe.