Dynamic model for a heat exchanger tube rupture discharging a high-pressure flashing liquid into a low-pressure liquid-filled shell

Shell-tube type heat exchangers are often used to exchange heat between a high-pressure fluid and a low-pressure fluid. The pressure difference between these two fluids could be significantly high. In the event of a partial or full rupture of a tube, a problem may arise in that a transient pressure rise phenomenon could occur due to the flashing of the high-pressure sub-cooled fluid in the tube into the low-pressure shell, which may cause the shell to rupture with subsequent damage to equipment. This paper presents a dynamic model to describe the transient phenomenon occurring on the shell side following various scenarios of tube rupture. The spatial and temporal aspects of the flow transients along the pressure safety valve riser are accounted for by solving the one-dimensional continuity and momentum hyperbolic partial differential equations as applied to the liquid-filled riser. The dynamics of the attached piping system are also accounted for via two mechanistic models; the first is based on an inertial-resistive assumption of the fluids in this system, while the other is based on the assumption of anechoic perturbations passing through a long section of the attached piping. The latter is justified in cases where the attached piping is long enough such that reflections from the downstream end do not interfere with transients occurring in the shell during the initial phase of fluid flashing into the shell side following rupture. The various phases of this phenomenon are described, however the paper focuses on the initial phase of the phenomenon during which shell overpressure may be encountered. The model is applied to two ethylene heaters in 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 design pressure 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. The practical aspects and discussion around techniques to alleviate potential overpressure scenarios due to tube rupture are emphasized throughout the paper.     

锅炉屏式过热器近集箱处爆管原因分析及改进措施

某电厂锅炉屏式过热器管在近集箱处发生爆管,本文通过宏观形貌检查、化学成分分析、机械性能测试及金相组织分析等方法对其爆管原因进行了系统分析。根据分析结果推断:集箱或管子内异物堵塞,导致管子材质劣化,但仅更换炉内管段,未更换炉外材质劣化管段,最终在长期运行中发生爆管。最后针对具体失效原因,提出了普查屏过管、失效分析、清洁工程及加强监督等改进措施。     

微波处理沥青烟气的探讨研究

采用响应曲面分析法,对微波处理沥青尾气时,管式炉加热温度、沥青烟预热温度及流量对处理沥青烟的影响进行了分析。结果表明:微波高温加热处理沥青烟气的方法,大大提高了焚烧法处理沥青尾气的效率,并且具有成本降低、设备简单、易于操作、易于控制、系统阻力较小、污染小等特点,这一工艺的提出,也为沥青烟气的处理方法开拓了新的道路。     

300MW机组锅炉屏式过热器爆管原因分析

某电厂300MW机组锅炉在投产运行仅仅13260小时便发生了屏式过热器爆管事故,经初步分析该不锈钢管弯管是由于固溶化处理不当,在残余应力、热应力及氟离子等共同作用下,在奥氏体晶界薄弱处产生晶间腐蚀微裂纹,继而不断发展并最终造成爆管事故的发生。建议加强原材料验收检验及规范锅炉运行操作规程,以最大限度减少此类事故的发生。     

我国长管拖车安全技术发展综述

长管拖车作为专用气体储运装备实现国产化已有10余年时间,其关键部件——长管拖车气瓶(即大容积无缝钢瓶)由于充装介质多易燃、易爆、且具腐蚀性和毒性,具有较高的安全隐患和潜在危险,因此国家将其纳入特种设备进行全寿命安全监管。中国特种设备检测研究院作为长管拖车定期检验专业机构,累计检验长管拖车气瓶万余只,对其制造使用工况、典型失效模式和缺陷评定方法积累了大量数据。本文综述了我国长管拖车气瓶的制造使用现状、安全检验现状和发展趋势,为长管拖车在我国的安全使用及发展提供依据。     

薄壁三通管翻边成形工艺参数的确定

介绍了薄壁三通管翻边成形时预制孔形状及极限翻边高度的确定方法。     

旋转拉伸弯管法

弯管工艺是指将平直的管子按选定的半径和弯曲角度弯曲成形。管子冷弯的方法有好几种,此文讲述的是旋转拉伸弯管法。文章主要介绍旋转拉伸弯管法的原理,所用的基本工具及其功能,弯管的操作步骤等等。对如何生产合格的冷弯管子有一定的参考作用。     

感温自启动灭火管系统应用于密闭空间的试验研究

为了对比Novec 1230（全氟己酮）感温自启动灭火管系统与R236fa（六氟丙烷）感温自启动灭火管系统的灭火效率,采用火灾实体试验的方法,分析了不充压,0.88,1.81 MPa下2系统的灭火时间、破裂动作温度及降温冷却效果。研究结果表明:2种灭火管系统都成功灭火,且 R236fa灭火管系统灭火时间更短;2种灭火管系统的破裂动作温度均在80 ℃以上;不充压和0.88 MPa时,2种灭火管系统降温冷却效果相差不大,但充压1.81 MPa时Novec 1230灭火管系统对环境温度的降温冷却作用更强。     

Antepartum rupture of the intertwin-dividing membrane in monochorionic diamniotic twins: a case report and review of the literature

We report a case of monochorionic diamniotic twin gestation confirmed by ultrasound visualization of the thin intertwin-dividing membrane at 32 weeks' gestation. Ultrasound at 36 weeks failed to demonstrate the thin dividing membrane. The pregnancy ended a few days later with spontaneous vaginal delivery of the first twin. The second twin was in transverse lie with no membranes that could be felt around. Severe fetal heart rate deceleration developed, prompting delivery by emergency caesarean section. Cord entanglement was noted at the time of delivery, which resulted in severe perinatal morbidity of the second twin. The antepartum rupture of the dividing membrane must have happened some time between 32 and 36 weeks. The etiology for this intrauterine disruption is unknown. A review of the literature about the antepartum rupture of the intertwin-dividing membrane is described, along with its possible causes and complications. In addition, we discuss possible causes of incorrect amnionicity determination, and thus how to minimize these pitfalls. We conclude that antepartum disruption of the intertwin-dividing membrane is more common than previously thought. Moreover, prenatal ultrasonographic visualization of a dividing membrane in a diamniotic twin pregnancy does not rule out future change in this environment to a monoamniotic one, with all its perinatal morbidity and mortality complications, which result mainly from cord entanglement. This suggests a modification in the method and frequency of the prenatal fetal well-being follow-up, as well as the time and mode of delivery. Copyright © 2005 John Wiley & Sons, Ltd.     

超临界锅炉过（再）热器氧化皮剥落分析

目前,我国新投产的火力发电机组容量大、参数高,超,瞄界和超超,瞄界机组已经成为我国的主力发电机组。随着机组参数的提高,锅炉过（再）热器管蒸汽侧氧化成为影响发电机组安全经济运行的主要因素之一。本文研究了超临界电站锅炉过（再）热器管氧化皮的形成原理和规律,分析了氧化皮的剥落模式及机理,探讨了氧化皮剥落的影响因素,并提出了控制氧化皮形成和剥落的对策,研究结果可对电厂氧化皮剥落问题提供指导作用。