中国机械工程
中國機械工程
중국궤계공정
CHINA MECHANICAl ENGINEERING
2012年
13期
1611-1615
,共5页
古新%董其伍%王珂%刘敏珊
古新%董其伍%王珂%劉敏珊
고신%동기오%왕가%류민산
管壳式换热器%强化传热%压力损失%斜向流%实验
管殼式換熱器%彊化傳熱%壓力損失%斜嚮流%實驗
관각식환열기%강화전열%압력손실%사향류%실험
shell-- and-- tube heat exchanger%heat transfer enhancement%pressure loss%sidelingflow%experiment
弓形折流板换热器壳程流体横向冲刷换热管时存在流动阻力大和传热死区大等缺点,折流杆换热器壳程流体纵向流动,但当壳程流体雷诺数Re较小时传热性能不佳。为克服上述缺点,研究开发了一种新型高效节能的斜向流管壳式换热器,该换热器壳程流体总体呈纵向流动,局部区域流体倾斜冲刷换热管束。对斜向流换热器与折流板换热器和折流杆换热器传热与流阻性能的对比实验研究表明,在同等壳程流体流量下,斜向流管壳式换热器的传热系数、压降和综合性能均介于折流板换热器与折流杆换热器之间。研究结果为管壳式换热器升级换代提供了一种新技术和新装备,也为热力系统中换热器选型和结构优化设计提供了重要依据。
弓形摺流闆換熱器殼程流體橫嚮遲刷換熱管時存在流動阻力大和傳熱死區大等缺點,摺流桿換熱器殼程流體縱嚮流動,但噹殼程流體雷諾數Re較小時傳熱性能不佳。為剋服上述缺點,研究開髮瞭一種新型高效節能的斜嚮流管殼式換熱器,該換熱器殼程流體總體呈縱嚮流動,跼部區域流體傾斜遲刷換熱管束。對斜嚮流換熱器與摺流闆換熱器和摺流桿換熱器傳熱與流阻性能的對比實驗研究錶明,在同等殼程流體流量下,斜嚮流管殼式換熱器的傳熱繫數、壓降和綜閤性能均介于摺流闆換熱器與摺流桿換熱器之間。研究結果為管殼式換熱器升級換代提供瞭一種新技術和新裝備,也為熱力繫統中換熱器選型和結構優化設計提供瞭重要依據。
궁형절류판환열기각정류체횡향충쇄환열관시존재류동조력대화전열사구대등결점,절류간환열기각정류체종향류동,단당각정류체뢰낙수Re교소시전열성능불가。위극복상술결점,연구개발료일충신형고효절능적사향류관각식환열기,해환열기각정류체총체정종향류동,국부구역류체경사충쇄환열관속。대사향류환열기여절류판환열기화절류간환열기전열여류조성능적대비실험연구표명,재동등각정류체류량하,사향류관각식환열기적전열계수、압강화종합성능균개우절류판환열기여절류간환열기지간。연구결과위관각식환열기승급환대제공료일충신기술화신장비,야위열력계통중환열기선형화결구우화설계제공료중요의거。
There are some disadvantages in segmental baffle heat exchanger for the transversal flow over tubes in its shell side,such as the high flow resistance,large heat transfer dead region,and so on. The fluid flows longitudinally in the shell side of rod baffle heat exchanger, but the heat transfer performance is not perfect when the Reynolds number in shell side is low. For overcoming above men- tioned disadvantages, a kind of new efficient and energy saving shell--and--tube heat exchanger with sideling flow in shell side was developed, the fluid flowed longitudinally in general, and the fluid in some local regions flowed over tubes inclinedly. Contrast experiments on heat transfer and flow resist- ance performances among this new kind of heat exchanger and segmental baffle heat exchanger, rod baffle heat exchanger were carried out, it is indicated that with the same fluid flow in shell side, the heat transfer coefficient,pressure drop, and over--all performance of sideling flow heat exchanger lie in between of those of segmental baffle heat exchanger and rod baffle heat exchanger. With this new kind of heat exchanger, the new technique and products are provided for the upgrade and update of shell--and--tube heat exchanger,and the important basis are also provided by research results for the structure selection and optimization design of heat exchangers in thermal system.