永安火电厂人为继电保护不正确动作事故分析及预防对策

通过历年来永安火电厂继电保护人为不正确动作事故情况,进行原因分析,并采取一系列措施,取得了较好效果。     

油田采油注入水处理技术

介绍了中原油田注入水水质特点,以前采用的处理工艺和存在的问题,并分析了问题的根源在于产出水的“四高一低”,原处理工艺难以去除。针对这一情况,中原油田与江汉石油学院合作开发研制了三组分水质调整剂,分别调整ｐＨ,破坏液体的稳定性并去除液体中的金属离子;他们对三种组分的加入时间和投加量进行了试验,结果表明：三种组分应按顺序加入,其中Ａ、Ｂ剂应有足够的间隔,加入量根据不同水质由试验确定。通过中原油田水处理站的运行试验得出结论：该工艺简单,投资小,处理效果好,适合中原油田的水质特性;处理后的水水质稳定,有效控制了腐蚀,减少了穿孔损失和污染损失,取得了显著的社会效益和环境效益     

流动系统内生物膜的形成及控制

应用辐射流动室（Ｒａｄｉｃａｌ Ｆｌｏｗ Ｃｈａｍｂｅｒ,ＲＦＣ）技术宣地研究水力剪切力对硝化细菌在聚苯乙烯（ＰＳ）载体表面固定的。发现水力剪切力直接影响硝化细菌的固定。当作用于ＰＳ表面的水力剪切力大于８．０Ｎ／ｍ＾２时,硝化细菌基本不能在ＰＳ表面险境着;水力剪切力小于８．０Ｎ／ｍ＾２时,硝化细菌的固定程度随剪切力的减小而加强,直至达到最大,实验表明辐射液动室技术为定量研究生物膜形成及控制与水力剪     

天津地区土壤中萘的生态风险分析

以天津地区表土188个样点的实测萘浓度以及萘对10种代表性土壤生物的半致死浓度为基础资料,尝试用3种方式评价了该地区土壤中萘的生态风险.并进行了方法学比较.研究结果发现,暴露浓度和毒性效应概率密度函数的重叠面积与联合概率曲线一致地反映出很低的生态风险,准确计算的暴露浓度超过LC50的概率仅为1.67%.结果说明该地区土壤萘的生态风险极低,仅严重污染的局部地区可能发生最敏感生物种受害.用于进行风险评价的3种方法各有利弊.     

新能源场群连锁故障路径的仿真预测方法

新能源场站的大规模集群化接入不仅增加了连锁故障的发生概率,也恶化了故障发生后的电网运行状态。为适应电网运行分析的新要求,以新能源机组和无功补偿装置实际运行工况为依据,研究了一种用于预测新能源场群连锁故障路径的仿真计算方法。通过基于大电网数据的仿真算例分析,得到了某新能源场群在典型约束条件下的详细连锁故障路径。结果表明:基于新能源场站机组实际情况建立的仿真模型更适宜于连锁脱网路径的仿真预测。     

人工神经网络和专家系统在污水生物处理系统中的应用

对近年来国内外污水生物处理系统中人工神经网络和专家系统的应用进行了简要的回顾。分析了废水生物处理工艺难于控制的原因及人工神经网络和专家系统的结构和特点。结果表明．国外智能控制发展迅速,并且应用领域遍及污水生物处理的各个方面,国内尚处于起步阶段。简要探讨了废水生物处理智能控制今后应深入研究的问题及方向。     

电化学降解与声电化降解苯胺溶液的对比实验研究

采用电化学和声电化两种方法处理苯胺溶液．考察了处理时间、苯胺浓度、pH、电解质浓度、电解电压等因素对苯胺降解率的影响,并对两种方法处理的溶液分别进行紫外分析。实验结果表明．在其他条件相同的情况下．声电化降解所得苯胺降解率远远大于采用电化学方法所得降解率。     

饮用水中硝酸根的催化还原研究进展

由于化肥的过度使用 ,造成地下水中硝酸盐的污染日益严重。饮用水中高浓度的硝酸盐对人类健康会产生极大的威胁。本文综述了催化还原脱除水中硝酸根的研究进展和现状 ,并对其发展趋势进行了简单的论述。     

Influence of H2S and NH3 on biogas dry reforming using Ni catalyst: a study on single and synergetic effect

● NH₃ in biogas had a slight inhibitory effect on dry reforming. ● Coexistence of H₂S and NH₃ led to faster decline of biogas conversion. ● Regeneration was effective for catalysts deactivated under synergetic effect. Biogas is a renewable biomass energy source mainly composed of CH₄ and CO₂. Dry reforming is a promising technology for the high-value utilization of biogas. Some impurity gases in biogas can not be completely removed after pretreatment, which may affect the performance of dry reforming. In this study, the influence of typical impurities H₂S and NH₃ on dry reforming was studied using Ni/MgO catalyst. The results showed that low concentration of H₂S in biogas could cause serious deactivation of catalyst. Characterization results including EDS, XPS and TOF-SIMS confirmed the adsorption of sulfur on the catalyst surface, which was the cause of catalyst poisoning. We used air calcination method to regenerate the sulfur-poisoned catalysts and found that the regeneration temperature higher than 500 °C could help catalyst recover the original activity. NH₃ in the concentration range of 50–10000 ppm showed a slight inhibitory effect on biogas dry reforming. The decline rate of biogas conversion efficiency increased with the increase of NH₃ concentration. This was related to the reduction of oxygen activity on catalyst surface caused by NH₃. The synergetic effect of H₂S and NH₃ in biogas was investigated. The results showed that biogas conversion decreased faster under the coexistence of H₂S and NH₃ than under the effect of H₂S alone, so as the surface oxygen activity of catalyst. Air calcination regeneration could also recover the activity of the deactivated catalyst under the synergetic effect of H₂S and NH₃.