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91.
由于膨胀机增压端后冷却器内漏,30000 m3/h空分设备在临时停车再开车时出现了主换热器增压通道阻力增大现象。采取临时停车对增压通道进行局部加温的方法未能排除故障,后启动空压机,对主换热器部位进行加温解冻才解决问题。简介主换热器增压通道冰堵后的参数变化情况,介绍堵塞通道解冻的具体过程。  相似文献   
92.
介绍气控液压滑台的工作原理及调试过程,以及在实际安装调试过程中所遇到的问题及其解决办法。  相似文献   
93.
绝热氧化法研究煤的自燃特性   总被引:13,自引:3,他引:13  
介绍了一种绝热氧化实验设备及其实验方法,利用该设备测试了3种煤样的低温氧化自热升温过程,成功实现了100g左右小煤样的煤自然发火过程模拟试验研究,获得了煤在绝热状态下的氧化升温曲线,建立了煤的绝热氧化产热量计算的数学模型,对实验过程中煤在绝热条件下的氧化产热量进行了计算,获得了不同温度段煤的绝热氧化升温速率和产热速率。  相似文献   
94.
在考虑了亚稳态流动的基础上,基于均相流模型建立了绝热毛细管内制冷剂流动特性的数学模型;针对工质为R22的制冷系统编制了计算程序,计算结果经与其他已发表的文献进行比较,表明计算结果合理.  相似文献   
95.
The location, intensity and scope of concentrated leakage must be determined in order to repair earth-Dam scoured by the leakage. In this paper, firstly, heat tracer theory and distribution laws of temperature in soil body with leakage are discussed. Then temperature tracer model is established according to stable heat conduction theory. In such model, the concentrated seepage passage is simplified into a circular pipe as a boundary condition. The location, scope and flow-velocity of the concentrated leakage are estimated via ichnography of the lowest temperature based on temperature data from detecting wells by quantitative computation and qualitative analysis. In case study, the distribution characteristic of temperature (including temperature data of water in reservoir, drainage pipes and tail pond) can be interpreted by this model. A modified model is also set up, applied for detected data at different cross-sections of the leakage passage, in which the temperature data are rectified according to distances from data locations to calculating section. Finally, the model is solved by numerical iterative method, and the possible error of this theoretical model is discussed. The permeability coefficient in leakage area is identical with that of normal soil in magnitude after anti-seepage repairing accomplished, which indicates this model is effective.  相似文献   
96.
针对当前电网线路纵联保护所采用的光纤通道类型,分析了影响通道可靠性的因素,并提出了故障查找、测试方法。  相似文献   
97.
本文对目前典型的户式中央空调水系统进行了运行分析,并在此基础上提出了改进意见。  相似文献   
98.
In this paper the impact of product market uncertainty on the optimal replacement timing of a production facility is studied. The existing production facility can be replaced by a technologically more advanced and thus more cost-effective one. We take into account strategic interactions among the firms competing in the product market by analyzing the problem in a duopolistic setting. We calculate the value of each firm and show that i) a preemptive (simultaneous) replacement occurs when the associated sunk cost is low (high), ii) despite the preemption effect uncertainty always raises the expected time to replace, and iii) the relationship between the probability of optimal replacement within a given time interval and uncertainty is decreasing for long time intervals and humped for short time intervals. Furthermore it is shown that result ii) carries over to the case where firms have to decide about starting production rather than about replacing existing facilities. Correspondence to: Grzegorz PawlinaThis research was undertaken with support from the European Union's Phare ACE Programme 1997. The content of the publication is the sole responsibility of the authors and in no way represents the views of the Commission or its services. The authors would like to thank Kuno Huisman, Enrico Pennings, two anonymous referees, and participants of the Advances in Game Theory Conference in Hilvarenbeek, EFMA 2002 in London, and the Workshop on Recent Topics in Real Options Valuation in Krems for helpful comments.G. Pawlina  相似文献   
99.
The isochoric heat capacity C V of an equimolar H2O+D2O mixture was measured in the temperature range from 391 to 655 K, at near-critical liquid and vapor densities between 274.05 and 385.36 kgm–3. A high-temperature, high-pressure, nearly constant-volume adiabatic calorimeter was used. The measurements were performed in the one- and two-phase regions including the coexistence curve. The uncertainty of the heat-capacity measurement is estimated to be ±2%. The liquid and vapor one- and two-phase isochoric heat capacities, temperatures, and densities at saturation were extracted from the experimental data for each measured isochore. The critical temperature and the critical density for the equimolar H2O+D2O mixture were obtained from isochoric heat capacity measurements using the method of quasi-static thermograms. The measurements were compared with a crossover equation of state for H2O+D2O mixtures. The near-critical isochoric heat capacity behavior for the 0.5 H2O+0.5 D2O mixture was studied using the principle of isomorphism of critical phenomena. The experimental isochoric heat capacity data for the 0.5 H2O+0.5 D2O mixture exhibit a weak singularity, like that of both pure components. The reliability of the experimental method was confirmed with measurements on pure light water, for which the isochoric heat capacity was measured on the critical isochore (321.96 kgm–3) in both the one- and two-phase regions. The result for the phase-transition temperature (the critical temperature, T C, this work=647.104±0.003 K) agreed, within experimental uncertainty, with the critical temperature (T C, IAPWS=647.096 K) adopted by IAPWS.  相似文献   
100.
莱钢2^#1000m^3,高炉自开炉以来,通过加强原燃料管理,调整布料矩阵,摸索合理的操作制度,维持足够的鼓风动能和理论燃烧温度,保证足够的炉缸温度和活跃的炉缸工作状态,达到了低硅冶炼的目的,使铁水含硅量一直控制在0.37%左右的较低水平。  相似文献   
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