螺旋钢管盘制成形的一种新方法

对如何在三辊卷板机上进行盘制螺旋钢管、盘管所用模具及成形工艺作了介绍.     

Assessing the Leakage Rates from Punctured Submerged Vessels

The leakage of fluid leaving a puncture in a pressurized vessel immersed in a quiescent, miscible medium is studied under steady flow conditions. This problem has engineering applications in submerged pipelines and hazardous gas lines. The leakage rate for the puncture is characterized as functions of various hydrodynamic and geometric conditions. Dimensional analysis shows that the leakage percent, Q*, is a function of the Reynolds number, the pressure ratio between the center of the tube and the external hydrostatic pressure, P^*, and the hole-to-main tube diameter ratio, D^*. The effect of puncture shape is also examined, rectangular and circular. A 3-D finite volume computational model is constructed for laminar flow of a Newtonian fluid under steady conditions and validated with supporting experiments. The results show that the fractional leakage rate Q* increases with P^* and approaches a constant value at high P^* for a fixed Reynolds number. In addition, it is found that the leakage rate increases with decreasing Reynolds number at a fixed pressure ratio. The geometric effect of the diameter ratio is shown to have a more pronounced effect near a pressure ratio of two with more fluid exiting the puncture for larger diameter ratios. The results of the shape analysis show that the circular puncture has the largest fractional leakage when compared to a rectangle with an equivalent cross-sectional area.     

大口径薄壁无缝铝管变薄旋压工艺

介绍采用离心铸坯——变薄旋压方法制作大口径薄壁铝管的工艺.包括简要工艺流程、特点、适用范围等.该工艺为解决国内大口径薄壁无缝铝管提供了新的途径.     

Hydroforming of locally heat treated tubes

In tube hydroforming, the process chain can be very long as it may involve several pre-forming operations (e.g. bending, crushing, end forming, etc.) which are usually followed by an intermediate annealing stage. Conventional annealing is performed in batches and it is often perceived as a long, relatively expensive and non-environmentally friendly operation. For this reason, in this paper local intermediate heat treatment is proposed as a promising alternative solution, in order to reduce the throughput process time. The study has been carried out on a real tubular motorcycle part, by performing both experiments and numerical simulations, in order to verify whether local annealing can be an effective substitute of conventional global annealing. Several alternative ways of locally heat treating an Al6060 tube right before hydroforming have been investigated. The results demonstrate that a feasible solution can be found, with local heat treatment of relatively small portions of the tube.     

Consequence analysis by means of characteristic curves to determine the damage to buildings from bursting spherical vessels

Since the damage suffered by buildings as a consequence of explosions usually affect the people inside them, it is important to take it into account when performing consequence analysis. The aim of this paper is to provide a methodology to estimate consequences to buildings from pressure waves produced by spherical vessel burst. This is done by combining characteristic overpressure–impulse–distance curves [González Ferradás, E., Diaz Alonso, F., Sanchez Perez, J.F., Miñana Aznar, A., Ruiz Gimeno, J. and Martinez Alonso, J., 2006, Characteristic overpressure–impulse–distance curves for vessel burst, Process Safety Progress, 25(3): 250–254] with PROBIT equations. The main advantage of this methodology is that it allows an overview of all the magnitudes involved, as damage is shown in the same graph as the overpressure, impulse and distance. In this paper diagrams and equations are presented to determine minor damage to buildings (broken windows, displacement of doors and window frames, tile displacement, etc.), major structural damage (cracks in walls, collapse of some walls) and collapse (the damage is so extensive that the building is partially or totally demolished).     

双侧破裂模型对地震动空间相关性影响的远场分析

根据震源理论,将由双侧破裂模型计算得到的场地Fourier谱,等价表述为从初始破裂点沿两个相反方向破裂的单侧破裂模型独立计算到的相同场地Fourier谱,以相对长度为权重的线性组合。据此,在远场假定下,得到了双侧破裂模型刻画地震动场分布的两个重要复变参数α1和α2,以及由它们确定场的孔径的解析表达式。最后,以一次地震为例,计算了α1和α2的实部和虚部,以及孔径随震中距、方位角和频率变化的三维图像。     

复杂人机系统班组人误模型与量化分析

讨论一个班组人员行为模型,即包括:任务模型、事件模型、班组模型和人-机交互模型4个模块,并用其模拟和分析事故状态下的运行班组对异常事故的响应过程;利用班组认知过程流程图模型表征事件发展过程中班组成员对事故的征兆识别、决策、计划和行动执行的响应过程;采用CREAM的量化分析技术,对核电站的蒸汽发生器管道破管事故的班组认知失误事件进行量化分析。     

土工管袋技术在湖库底泥脱水中的应用研究

为掌握土工管袋充填过程的变化规律及脱水效果,在疏浚船舶和絮凝剂的配合下,通过对土工管袋首次充填过程及后续充填过程进行实验研究,筛选出了最佳的管袋种类、获得了充填过程管袋高度变化曲线、管袋利用效率、底泥脱水后含水率变化曲线以及充填施工过程中的控制方法等技术指标,为土工管袋的工程化提供了指导,为管袋技术的大规模应用和技术集成化奠定了一定的基础。     

天然气管路导气球阀失效分析

目的分析西部某气田天然气管路球阀发生开裂泄漏事故的原因。方法对球阀的化学成分、断口、金相组织等进行检测分析。结果球阀裂纹起源于阀体内表面,裂纹沿晶界扩展,晶界未发现贫铬现象,不存在晶间腐蚀;阀体材料存在沿晶铸造缺陷和枝晶露头,水淬激冷过程中形成沿晶微裂纹,承压状态下裂纹沿晶扩展;球阀螺纹根部最薄且应力集中,裂纹由内向外扩展,最终沿螺纹根部环向断裂,断口形貌为沿晶断裂。结论导气球阀失效原因是螺纹根部存在应力集中和铸造阀体存在缺陷。在两者共同作用下,导致阀体承压状态下沿晶脆性断裂。     

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.