化工学报
化工學報
화공학보
JOURNAL OF CHEMICAL INDUSY AND ENGINEERING (CHINA)
2014年
10期
3811-3819
,共9页
郭震%郎红方%周帼彦%朱凌云%杨锦春%朱辉%朱冬生
郭震%郎紅方%週幗彥%硃凌雲%楊錦春%硃輝%硃鼕生
곽진%랑홍방%주귁언%주릉운%양금춘%주휘%주동생
三叶孔板%支撑板间距%对流%模型%传热%压降
三葉孔闆%支撐闆間距%對流%模型%傳熱%壓降
삼협공판%지탱판간거%대류%모형%전열%압강
trefoil-hole baffle%baffle space%convection%model%heat transfer%pressure drop
三叶孔板换热器是一种新型纵向流换热器,由于其具有传热效率高、压降低、抗振结构性能优越等诸多优点而广泛应用于核电行业。搭建三叶孔板换热器壳程传热与压降测试平台,对传热和压降的测量结果进行不确定度分析。对4台三叶孔板换热器模型进行实验研究,结果表明随着Reynolds数的增大,壳程对流传热系数和压降在对数坐标内线性增大;在Reynolds数相同的情况下,随着支撑板间距的增大,三叶孔板换热器壳程Nusselt数逐渐减小,压降逐渐降低,同时压力梯度逐渐减小。为了进一步分析说明三叶孔板换热器壳程传热与阻力性能,基于Bell-Delaware法设计了具有相同结构参数的折流板换热器。与折流板换热器的对比结果表明:三叶孔板换热器壳程Nusselt数平均为折流板换热器的1.25倍,壳程整体压力平均为折流板换热器的0.77,综合性能平均为折流板换热器的1.62倍。
三葉孔闆換熱器是一種新型縱嚮流換熱器,由于其具有傳熱效率高、壓降低、抗振結構性能優越等諸多優點而廣汎應用于覈電行業。搭建三葉孔闆換熱器殼程傳熱與壓降測試平檯,對傳熱和壓降的測量結果進行不確定度分析。對4檯三葉孔闆換熱器模型進行實驗研究,結果錶明隨著Reynolds數的增大,殼程對流傳熱繫數和壓降在對數坐標內線性增大;在Reynolds數相同的情況下,隨著支撐闆間距的增大,三葉孔闆換熱器殼程Nusselt數逐漸減小,壓降逐漸降低,同時壓力梯度逐漸減小。為瞭進一步分析說明三葉孔闆換熱器殼程傳熱與阻力性能,基于Bell-Delaware法設計瞭具有相同結構參數的摺流闆換熱器。與摺流闆換熱器的對比結果錶明:三葉孔闆換熱器殼程Nusselt數平均為摺流闆換熱器的1.25倍,殼程整體壓力平均為摺流闆換熱器的0.77,綜閤性能平均為摺流闆換熱器的1.62倍。
삼협공판환열기시일충신형종향류환열기,유우기구유전열효솔고、압강저、항진결구성능우월등제다우점이엄범응용우핵전행업。탑건삼협공판환열기각정전열여압강측시평태,대전열화압강적측량결과진행불학정도분석。대4태삼협공판환열기모형진행실험연구,결과표명수착Reynolds수적증대,각정대류전열계수화압강재대수좌표내선성증대;재Reynolds수상동적정황하,수착지탱판간거적증대,삼협공판환열기각정Nusselt수축점감소,압강축점강저,동시압력제도축점감소。위료진일보분석설명삼협공판환열기각정전열여조력성능,기우Bell-Delaware법설계료구유상동결구삼수적절류판환열기。여절류판환열기적대비결과표명:삼협공판환열기각정Nusselt수평균위절류판환열기적1.25배,각정정체압력평균위절류판환열기적0.77,종합성능평균위절류판환열기적1.62배。
Shell-and-tube heat exchanger with trefoil-hole baffles (STHX-TH) is a new type of longitudinal-flow heat exchanger which is widely used in nuclear industry due to its higher heat transfer efficiency, lower pressure, superior anti-vibration performance and many other advantages. In order to analyze the thermal-hydraulic performance of STHX-TH, an experimental test platform was established. Then four STHXs-TH with different baffle spaces were tested. The experimental data were reliable and accurate. Heat transfer coefficient and pressure drop decreased linearly with increasing Reynolds number in double logarithmic coordinates. Heat transfer coefficient and pressure drop decreased with increasing baffle space at the same Reynolds number. With the same mass flow, pressure gradient decreased with increasing baffle space. In order to comparatively understand the shell-side heat transfer and pressure drop performance of STHX-TH, a shell-and-tube heat exchanger with segmental baffles (STHX-SB) with similar geometric parameters with STHX-TH (No.2) was designed. Shell-side heat transfer coefficient and pressure drop of STHX-SB were calculated with the Bell-Delaware method, and compared with those of STHX-TH. The comparative study showed that convective heat transfer coefficient of STHX-TH was 1.25 times of that of STHX-SB, pressure drop of STHX-TH was 0.77 time of that of STHX-SB, andNus/Δps of STHX-TH was 1.62 times of that of STHX-SB.