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详细介绍了GIS的预防性试验项目和试验仪器及试验要求,结合具体工程实例,通过对35 kV GIS柜进行主回路导电电阻测试和交流耐压试验,阐述了交接性试验在地铁GIS柜中的应用,指出变接性试验是检测设备潜在缺陷的重要手段。 相似文献
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针对聚丙烯装置预聚反应器轴流泵P200机械密封在装置开工投用期间发生泄漏失效的问题,根据理论计算,确定增压活塞投用与停用的环管压力的临界值;结合实际受损机械密封分析,提出完善增压活塞的投用方案,并加强轴流泵停车期间,尤其是开车前的维护工作,防止杂质进入密封腔。实际运行证明了提出的解决方案能有效避免轴流泵机械密封的失效,保证装置的开车顺利。 相似文献
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针对大压力、小压力行程的重型液压设备的结构尺寸大、油泵功率大、利用系数低、液压系统复杂等问题,提出一种压力随机可调、工作效率高、结构紧凑、性能稳定可靠的复合式高增压油缸结构。对比分析了复合缸液压机和普通单缸液压机的工作过程;论述了复合缸液压机的运行原理和设计要求;介绍了可控式增压复合油缸性能及应用。结果表明:通过增压缸将液压系统提供的压力油转换为增压油提供给主油缸,使其产生大的压力输出,可有效地减小设备主机尺寸;通过控制缸随时进行高低压转换,各阶段速度压力按需配置,实现成形工艺的最优搭配,成形周期缩短;可以提高油泵的利用系数,减小泵站装机容量;液压系统工作负荷低,性能稳定可靠,寿命长。 相似文献
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Shreenath Krishnamurthy Vemula Rama Rao Sathishkumar Guntuka Paul Sharratt Reza Haghpanah Arvind Rajendran Mohammad Amanullah Iftekhar A. Karimi Shamsuzzaman Farooq 《American Institute of Chemical Engineers》2014,60(5):1830-1842
The capture and concentration of CO2 from a dry flue gas by vacuum swing adsorption (VSA) has been experimentally demonstrated in a pilot plant. The pilot plant has the provision for using two coupled columns that are each packed with approximately 41 kg of Zeochem zeolite 13X. Breakthrough experiments were first carried out by perturbing a N2 saturated bed with 15% CO2 and 85% N2 feed, which is representative of a dry flue gas from coal‐fired power plants. The breakthrough results showed long plateaus in temperature profiles confirming a near adiabatic behavior. In the process study, a basic four‐step vacuum swing adsorption (VSA) cycle comprising the following steps: pressurization with feed, adsorption, forward blowdown, and reverse evacuation was investigated first. In the absence of any coupling among the steps, a single bed was used. With this cycle configuration, CO2 was concentrated to 95.9 ± 1% with a recovery of 86.4 ± 5.6%. To improve the process performance, a four‐step cycle with light product pressurization (LPP) using two beds was investigated. This cycle was able to achieve 94.8 ± 1% purity and 89.7 ± 5.6% recovery. The Department of Energy requirements are 95% purity and 90% recovery. The proposed underlying physics of performance improvement of the four‐step cycle with LPP has also been experimentally validated. The pilot plant results were then used for detailed validation of a one‐dimensional, nonisothermal, and nonisobaric model. Both transient profiles of various measured variables and cyclic steady state performance results were compared with the model predictions, and they were in good agreement. The energy consumptions in the pilot plant experiments were 339–583 ± 36.7 kWh tonne?1 CO2 captured and they were significantly different from the theoretical power consumptions obtained from isentropic compression calculations. The productivities were 0.87–1.4 ± 0.07 tonne CO2 m?3 adsorbent day?1. The results from our pilot plant were also compared with available results from other pilot plant studies on CO2 capture from flue gas. © 2014 American Institute of Chemical Engineers AIChE J, 60: 1830–1842, 2014 相似文献
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