物探螺旋钻机钻杆液压夹紧机构的设计计算

利用ANSYS大型有限元分析软件,对新设计的物探螺旋钻机钻杆液压夹紧机构进行了数值模拟分析计算。分析计算结果表明,当钻杆液压夹紧机构的钳体材料选择ZG310-570,所用液压马达的排量为390 mL/r时,该系统在最小驱动压力4.82 MPa、最大驱动压力7.30 MPa时才能正常工作。这种数值模拟分析为进一步改善钻杆液压夹紧机构的受力,改进机构的设计提供了依据。     

利用Excel表格进行供暖系统计算

利用Excel表格进行供暖工程设计计算，可以减少工作量，提高工作效率。介绍了房间热负荷和供暖管道水力计算方法。     

First-principles study of the tensile and fracture of the Al/TiN interface

Employing the density functional theory, we investigate the tensile and fracture processes of the Al/TiN(0 0 1) interface. The simulation presents directly the strain–stress relationship, the ideal tensile strength and the process of bond breaking of the system. Through the analysis of deformation, we find that the softer Al layers deform larger than the harder TiN layers during the tensile process. And fracture occurs between the interface and the sub-interface Al layers. In addition, the results show that during the tensile process, the ripple of the interfacial TiN layer decreases gradually with the increment of the strain. Charge transfer was detected from the Al to TiN layers near the interface area during the tensile process by means of charge density and density of states analyses. The charge transfer affects the fracture process. Compared to our previous study of the Al/TiN(1 1 1) interface, the Al/TiN(0 0 1) interface has smaller work of adhesion and larger tensile strength than the Al/TiN(1 1 1) interface. Our investigation shows that the fractures of the Al/TiN(0 0 1) and (1 1 1) interface systems both happen in the Al layers near the interface.     

翻领成型器领口曲线的程序计算展开法

根据翻领成型器领口曲线的数学模型，介绍一种利用计算器复杂公式存贮的特殊功能，预编程序计算相关参数。然后画领口曲线展开图的方法。     

可行性研究财务评价中利息的计算

介绍了可行性研究财务评价中利息计算的内容和方法。     

Prediction of evaporation heat transfer coefficient and pressure drop of refrigerant mixtures

A study on the prediction of heat transfer coefficient (HTC) and pressure drop of refrigerant mixtures is reported. HTCs and pressure drops of prospective mixtures to replace R12 and R22 are predicted on the same cooling capacity basis. Results indicate that nucleate boiling is suppressed at qualities greater than 20.0% for all mixtures and evaporation becomes the main heat transfer mechanism. For the same capacity, some mixtures containing R32 and R152a show 8.0–10.0% increase in HTCs. Some mixtures with large volatility difference exhibit as much as 55.0% reduction compared with R12 and R22, caused by mass transfer resistance and property degradation due to mixing (32.0%) and reduced mass flow rates (23.0%). Other mixtures with moderate volatility difference exhibit 20.0–30.0% degradation due mainly to reduced mass flow rates. The overall impact of heat transfer degradation, however, is insignificant if major heat transfer resistance exists in the heat transfer fluid side (air system). If the resistance in the heat transfer fluid side is of the same order of magnitude as that on the refrigerant side (water system), considerable reduction in overall HTC of up to 20% is expected. A study of the effect of uncertainties in transport properties on heat transfer shows that transport properties of liquid affect heat transfer more than other properties. Uncertainty of 10.0% in transport properties causes a change of less than 6% in heat transfer prediction.     

基于Ansys的电化学加工辅助阴极设计

根据电化学加工极间间隙电势分布的拉普拉斯方程，提出了一种阴极设计算法－误差调整法。该算法的实现主要采用了Ansys有限元计算软件。计算结果表明：该法计算迭代次数较为适当，对于精度要求不高的电化学加工阴极设计，基于Ansys的辅助阴极设计有效可行。     

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通过对J.J.Arps方程的推导,提出了油气藏产量递减曲线分析的最佳拟合法。用该法可直接求出递减指数N、初始递减率D1及油气递减前的稳定产量Qi,避免了使用试差法的大量运算过程,大大提高了油气藏工程中指标预测的精度。     

曲率圆弧段代替切线段的数值计算方法

为了确保安全,核工业和其它一些工业要求某些参数的计算值只能取正的相对误差且不大于5×10-3,这是它们对数值计算的基本要求.例如,反应堆带功率运行时,功率增长总是随时间上升,功率曲线是向下凹的.传统的龙格-库塔法计算值总是小于真实值,并且随着时间的增加,计算值越来越小于真实值.按计算值分析,反应堆是安全的,但实际上反应堆是不安全的.这对反应堆的安全极为不利.为此,本文开拓了一个全新的数值计算方法.与龙格-库塔法相比,该方法计算工作量小,与预测一校正法相比,该方法没有启动问题.更值得指出的是计算值高于真实值,这样,反应堆计算结果总是偏于安全的.