摘要
为克服传统设计模型的缺陷 ,在传质传热分析基础上 ,建立了烃水混合物立式多管式降膜蒸发冷凝器传热设计的管长方向等距积分模型 ,并对模型进行求解。实例证明 。
For conquering limitation of the traditional design, based on the mass and heat transfer in the vertical multi tube falling film evaporate condenser of hydrocarbon gas vapor mixture, the isometric integral model along the tube was established and evaluated. Its applicability was proved by example.
出处
《石油化工设备》
CAS
2001年第3期20-22,共3页
Petro-Chemical Equipment