气—液式热管换热器在硫酸工业中的应用研究

本文研制的气－液式热管换热器应用于硫酸生产中ＳＯ３气体的余热回收。它具有传热性能好、流动阻力小、寿命长、体积小、节能效果显著和易清垢等优点。     

中温换热器检查及修复方案

经分析认为中温换热器缺陷出现的主要原因是H2 S腐蚀。采取更换短管以及补焊上段下管板的措施进行修复 ,取得了满意的效果     

换热网络数值模拟稳定性分析

换热网络的数值模拟在换热网络的定量分析中起着重要作用。但在模拟计算中,有时表现出数值稳定性差。提高数值稳定性的方法,目前多通过改善算法来实现。本文通过对换热网络数值模拟的误差分析,提出了误差放大因子的概念,并依此选择迭代变量。通过对迭代变量的选择,达到提高换热网络数值模拟稳定性的目的。     

管道化溶出系统中大型套管式换热器的热补偿设计及组焊

以单内管套管式换热器为例 ,分析了管道化溶出系统大型套管式换热器热补偿的设计方法 ,重点分析了内外管膨胀差的补偿及其弯管部分的结构设计。另外 ,对一些与热补偿相关的结构 ,如封闭环的设置也进行了必要的分析     

大型管壳式换热器管-管板连接的可靠性措施

从材料性能、管孔的结构及加工要求、管与管板的连接形式等影响换热器管与管板连接接头强度的因素出发 ,结合乙烯大型换热器E EA12 3F的制造提出了管与管板连接接头的可靠性措施     

单填料函滑动管板式换热器密封结构的设计

自行设计了一台单填料函滑动管板式换热器代替进口设备，运转良好。本文着重介绍该设备密封结构的设计。     

乙炔吸收系统倒开车实现装置产品快速合格

中国石油吉林石化公司聚乙烯厂700kt/a乙烯装置老区采用溶剂吸收技术脱出乙炔精制乙烯工艺。多年来,乙炔吸收塔塔顶回流泵开车初期不上量问题一直制约着装置开车进度。经过摸索,技术人员尝试对开车流程进行调整,攻克了难题。文中对该装置具体的调整措施进行了阐述。     

梯形纵肋管束换热器传热及流阻特性研究

本文对纵肋管束换热器的传热、阻力特性进行了试验研究，得出传热特性和阻力特性关系式，并着重分析梯形纵肋管束换热器的特性。进一步探讨了管束节距、肋片高度对传热及流阻的影响情况。与相同结构的光管管束比较，换热增加１０％－３５％，而流阻最高增加４８％，最低情况下，低于光管。文中指出具有梯形纵肋的管束呈现出一种特殊的传热及流阻规律，它不但可获得较低的流动阻力，而且传热得以进一步强化。     

GRAPHICAL SOLUTION OF MULTISTAGE FLUIDIZED BED HEAT EXCHANGER

The design of multistage fluidized beds for heat exchange necessitates the solution of the mass and energy balance equations combined with the equilibrium relations for each stage. This paper presents a novel way of applying well known methodology to a different technology, one where it has not been widely applied.

In the present work a McCabe-Thiele type of graphical approach is presented for both counter-current and cross-current contacting multiple fluidized beds. The necessary equations for a multistage calciner are developed and the application of the proposed method is demonstrated. Generalized fluidized bed efficiency for counter-current and cross-current multiple fluidized bed is presented.     

Experiences from using heat integration software to determine retrofit opportunities within a refinery process

Heat integration techniques can be used to optimize the energy requirement for both new and retrofit plant designs. Software tools for identifying retrofit options are becoming available. This paper reports our experiences from using heat exchanger network (HEN) optimization software for a retrofit case study of an oil refinery process. The HEN optimization software was used to automate the search for the most beneficial retrofit designs following the twostage process proposed by Asante and Zhu. The software provided three potential retrofit designs. Results from this analysis were used as the basis of a rigorous mass and energy balance simulation of the plant. The simulation corroborated the energy savings, but there were some important differences. The simulation required 20% more heat exchange area. Furthermore, the retrofit design involving one topology change was shown to be less economic than an alternative design. These differences are discussed and a revised methodology is proposed.