勃劳特换热器的性能  

Performance of Bfowder Type Heat Exchanger

作　　者：周绪美[1] 陈建铭[1] 张鹏远 冯元鼎[1] 丁华 

机构地区：[1]北京化工大学化学工程系

出　　处：《高校化学工程学报》1995年第3期284-288,共5页Journal of Chemical Engineering of Chinese Universities

摘　　要：勃劳特换热器的性能周绪美，陈建铭，张鹏远，冯元鼎，丁华（北京化工大学化学工程系）关键词勃劳特换热器；压降１引言在生产过程中，气体与气体之间进行热量交换的换热器，在性能评比时，应该用两项指标来衡量。其一是单位产品所需传热面积要小，其二是单位压降的传热膜...Study on the fluld dynamics and heat transfer performance of Browder type heat exchanger was experimentally carried out.Equations for calculating shell side convective heat transfer coefficie nt and pressure drop were regressed. Com parison was made between the K calculated with the regressed equation and that determined from a similar heat exchanger under industrial operation.The difference was less than 9%.The equations can be used in heat exchanger design. Browder type and Lurgi type heat exchangers were compared experimentally.The results show that under the same flow rate, inlet and outlet temperatures of the fluid both heat exchangers have higher heat transfer coefficients than conventional ones and the values are of fairly equal, but the pressure drop in the Browder type heat exchanger is remarkably lower than that in the Lurgis.

关 键 词：勃劳特换热器 压降 换热器 

分 类 号：TQ051.5[化学工程] TB657.5[一般工业技术—制冷工程]