管材压扁的回弹分析

应用材料力学中的单位力法求回弹值的新理论，对管材压扁工艺的回弹量进行了分析计算，理论得出的结果与实际相符，可用于管材压扁中回弹量的计算预报。     

CB125T手把管的弯管机弯曲模具设计

介绍了CB125T摩托车手把管的弯管机弯曲工艺及模具,并以该件为例介绍了CNC弯管机弯模设计中的几何尺寸计算方法。     

轿车后轴纵臂内高压成形研究

用400MPa内高压成形机对轿车后轴纵臂进行内高压成形试验研究,设计了合理的模具结构,包括分模面和冲头密封形式。分析了矩形截面圆角成形特点和所需成形压力计算公式,制定出合理的内高压工艺和参数,成功地试制出轿车后轴纵臂,经检测尺寸满足设计要求。     

轴压外翻管通用模

此文介绍了通用翻管模的结构和翻管变形方法,这是一种最基本的翻管模,利用锥头将管坯变形翻卷。通过实验研究,提出了翻管模锥角α这一重要模具参数及其确定方法,论述了影响翻管系数K的主要因素;提出了进行顺利翻管的主要工艺参数,最后介绍了翻管制件和翻管工艺的主要用途。     

锥管件无模拉伸数学模型的研究

此文分析了锥形管件无模拉伸的变形机制,提出了锥管形件无模拉伸速度、冷热源移动速度的变化规律,对锥形管壁厚的变化也提出了相应的数学模型,并通过实验研究证明,本文提出的速度模型,较好地表达了锥形管件无模拉伸冷热源速度变化的规律.     

金属材料的超声塑性加工

此文介绍了超声振动在金属塑性加工领域的应用,讨论了超声塑性加工的理论机制和工艺特点,论述了超声场中的材料性能和粘塑性本构关系。     

内凸筋口琴管连续挤压模具

内凸筋口琴管,是汽车空调的一种新型散热管.具有散热效果好、单位面积小、重.量轻等优点.此文介绍了连续挤压内凸筋口琴管模具的设计方法及其模具芯头的冷挤压加工.     

Monitoring of atrazine in milk using a rapid tube-based ELISA and validation with HPLC

Although atrazine has been banned in the European Union since 2007 it still persists in soil from where it can enter the food chain. Milk-producing animals accumulate atrazine from contaminated feed and water and since large quantities of milk and milk products are consumed its quality should be constantly monitored. The objective of this investigation was to develop a simple tube ELISA procedure suitable for use in non-specialised laboratories and in the field. A polyclonal antibody raised in sheep and the hapten-gelatine conjugate was immobilised onto polystyrene tubes. This enables the colour produced to be read on a basic spectrophotometer. Milk samples were collected from three farms in different regions of Poland and diluted before immunoassay was performed. Samples were extracted with hexane-acetone for HPLC analysis. The amount of fat in the milk samples interferes with the dose response so it essential that the standards are prepared in the same samples matrix. A good correlation between 1% and 2% was found between the two methods in the analysis of real samples. However the ELISA procedure was more sensitive that the HPLC method since atrazine was detected in some samples by the ELISA but was not confirmed by the HPLC method. The study demonstrated that the simple antigen-coated tube assay provides a cost effective and valuable screening test that can be easily modified for direct use as a screening tool in the field.     

Importance of accounting for the piping system and boundary conditions in determining the maximum surge pressure following heat-exchanger tube-rupture

Shell-tube type heat exchangers are often used to exchange heat between a high-pressure fluid and a low-pressure fluid, and the pressure difference between the two fluids could be significantly high. If the difference in the design pressure between the low-pressure (LP) and high-pressure sides is greater than that covered by American Petroleum Institute (API 520 and 521) 10/13^th rule, dynamic analysis is required to ascertain that the maximum surge pressure that could be reached does not compromise the integrity of the LP side of the exchanger. API guidelines also notes that attention should also be given not only to the shell-side of the heat exchanger under evaluation, but also to the “upstream and downstream systems” This paper offers further insight into the importance of including the surrounding piping systems around the subject heat-exchanger where a tube-rupture scenario is considered, and also directs attention to the importance of correctly specifying the appropriate boundary conditions (B.C.) at the far ends of both the upstream and downstream piping systems. It demonstrates the effects of specifying different B.C. on the maximum pressure surge via a case study of a hot separator vapour condenser in a bitumen hydrotreating unit, where the process fluid on the tube-side is a vapour–liquid mixture at 9660 kPa(g). The vapour mass fraction of the process fluid is approximately 0.5, and is mostly hydrogen. The fluid on the LP side is cooling water connected to the plant supply and return cooling systems as well as another adjacent low pressure condenser. The design pressure for the cooling water piping system and the adjacent condenser is 1380 kPa(g).     

长时间服役的进口锅炉T91炉管失效行为研究

针对某进口亚临界锅炉三级过热器T91炉管失效事件,通过对其进行硬度、金相组织和SEM扫描电镜分析找出导致爆管的原因,并根据高温氧化皮厚度对其进行蠕变剩余寿命评估,结果表明该段T91管材爆管类型为典型长期过热爆管,炉管长期处于较高温度运行导致组织老化严重,力学性能下降,引起材料蠕变损伤,导致长期过热爆管,经计算其蠕变剩余寿命已达到寿命极限。本文对该锅炉防止类似事故具有重要作用,并对国内其他同在二十世纪90年代开始服役的T9彳炉管具有重大的参考价值和借鉴意义。