首页> 外文会议>AIChE spring meeting;Global congress on process safety >Consequences of High-Pressure Tube Ruptures in Low-Pressure Liquid-Filled Shell Heat Exchangers
【24h】

Consequences of High-Pressure Tube Ruptures in Low-Pressure Liquid-Filled Shell Heat Exchangers

机译:低压注液壳式换热器中高压管破裂的后果

获取原文

摘要

Shell-tube type heat exchangers are often used to exchange heat between a highpressurefluid and a low-pressure fluid. The pressure difference between these two fluidscould be significantly high. In the event of a partial or full rupture of a tube, a problem mayarise in that a transient pressure rise phenomenon could occur due to the flashing of the highpressure sub-cooled fluid in the tube into the low-pressure shell, which may cause the shell torupture with subsequent damage to equipment. This paper presents a dynamic model todescribe the transient phenomenon occurring on the shell-side following various scenarios oftube rupture.The spatial and temporal aspects of the flow transients along the pressure safety valve riserare accounted for by solving the one-dimensional continuity and momentum hyperbolic partialdifferential equations as applied to the liquid-filled riser. The dynamics of the attached pipingsystem are also accounted for via two mechanistic models; the first is based on an inertialresistiveassumption of the fluids in this system, while the other is based on the assumption ofanechoic perturbations passing through a long section of the attached piping. The latter isjustified in cases where the attached piping is long enough such that reflections from thedownstream end do not interfere with transients occurring in the shell during the initial phaseof fluid flashing into the shell-side following rupture. The various phases of this phenomenonare described, however the paper focuses on the initial phase of the phenomenon duringwhich shell overpressure may be encountered. The model is applied to two ethylene heatersin tandem; the first uses propylene on the shell-side to heat the ethylene on the tube side,while the second uses methanol, also on the shell-side. The ratio between the shell designpressure to the tube design pressure in these two heaters are 0.169 and 0.154, respectively,hence the motivation to accurately model the transients involved in this phenomenon. Thepractical aspects and discussion around the dynamic response of PSVs, rupture disks andattached piping systems are emphasized throughout the paper.
机译:壳管式热交换器通常用于在高压之间进行热交换 流体和低压流体。两种流体之间的压力差 可能会很高。如果管子部分或全部破裂,可能会出现问题 产生的原因是由于高压的闪动可能会出现瞬时压力上升现象 管中的压力过冷的流体进入低压壳体,这可能导致壳体 破裂,继而损坏设备。本文提出了一个动态模型 描述以下各种情况下在壳侧​​发生的瞬态现象 管破裂。 沿压力安全阀立管流动瞬态的空间和时间方面 通过解决一维连续性和动量双曲偏 微分方程应用于充液提升管。附属管道的动力学 系统还通过两个机械模型进行解释;第一个基于惯性电阻 该系统中流体的假设,而另一个则基于以下假设: 消声扰动穿过所连接管道的一长段。后者是 如果所连接的管道足够长,以至于来自管道的反射,则是合理的。 在初始阶段,下游端不干扰外壳中发生的瞬变 破裂后,液体会闪蒸到壳侧。这种现象的各个阶段 进行了描述,但是本文着重于该现象的初始阶段 可能会遇到哪种外壳超压。该模型适用于两个乙烯加热器 串联第一种是在壳侧使用丙烯加热在管侧的乙烯, 而第二种在壳侧使用甲醇。外壳设计之间的比例 这两个加热器中的灯管设计压力分别为0.169和0.154, 因此,有动机对这种现象所涉及的瞬态进行精确建模。这 PSV,破裂盘和破裂的动态响应的实际方面和讨论 整篇论文都强调了连接的管道系统。

著录项

相似文献

  • 外文文献
  • 中文文献
  • 专利
获取原文

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号