Green energy generation through PEHF – a blueprint of alternate energy harvesting

In this work, an attempt has been made to harvest green energy from piezoelectric material using fluid flow in a conduit. Piezoelectric Energy Harvesting using Fluid Flow (PEHF) experimental model has been designed and the outputs obtained are compared with results obtained from simulations using ANSYS (computational fluid dynamics) and also with the mathematical modeling. The PEHF model has been utilized to analyze the effect of flow rate of water with reference to energy extracted. The full wave bridge rectifier and voltage doubler circuits have been used to obtain the direct current (DC) from the PEHF model. It is observed that the output obtained using experiments holds good in agreement with the results retrieved through simulations and mathematical results. The increase in flow rate of fluid leads to initially increase and then decrease in output of PEHF model as the maximum energy generated when flow rates (external force) matches with the frequency of excitation of the systems, i.e., at its resonance. The maximum energy output is generated at its resonance frequencies. It is observed that the full wave bridge rectifier circuit gives greater output as compared to a voltage doubler circuit.     

Dynamic contact angle effects on gas-liquid behaviors in the cathode of proton exchange membrane fuel cell with stirred tank reactor design

Liquid water management is still a critical issue in the improvement of proton exchange membrane fuel cell (PEMFC) performance. In this work, for the first time, the liquid water behavior and transport inside the cathode of a PEMFC with a stirred tank reactor (STR) design, rather than the conventional PEMFC flow channel design, are numerically studied. The dynamic contact angle (DCA) is applied to multiple wall boundaries in the numerical model through a user-defined-function (UDF) code, i.e., STR-DCA model. Another numerical model with the static contact angle (SCA) and same operating conditions, i.e., STR-SCA model, is also developed for comparison. The volume of fluid (VOF) method is employed in the simulation to track the gas-liquid interface. The results show that the liquid water distribution and transport are significantly different between these two models, indicating the remarkable effects of DCA on the simulation results. It is also verified the capability of STR-PEMFC to reduce the liquid water flooding, showing the potential of this channel-less type fuel cell in the further development.     

生物酶破胶水基压裂液影响因素的试验研究

与其他压裂液破胶剂相比,生物酶破胶剂能很好地保护环境,而影响生物酶破胶水基压裂液效果的因素主要是底物的浓度、酶的加量、pH值以及破胶温度.本文采用正交试验设计,分析了各因素对生物酶破胶水基压裂液效果的影响程度,并分析了各因素不同水平对压裂液黏度的影响趋势,结果表明调整各因素的不同水平可以实现不同的压裂液黏度和破胶时间,...     

双提升管催化裂化装置隔离汽油沉降器后的风险分析及对策

分析了双提升管催化裂化装置隔离汽油沉降器的方法及隔离后存在的风险,根据分析结果提出相应对策。     

超临界水氧化偏二甲肼废水的研究

用超临界水氧化法对偏二甲肼废水进行了试验研究,结果表明：以02为氧化剂采用该法能有效地氧化分解废水中的偏二甲肼。反应温度、压力和停留时间是影响废水中偏二甲肼分解去除的主要因素,升高温度、压力和延长停留时间都会显著地提高偏二甲肼的去除率。在氧气过量的情况下,改变氧气浓度对废水的COD去除率没有明显影响。当反应温度为550℃、反应压力为30MPa、反应时间大于90 s时,废水的COD去除率高达99．8％。     

废水中氨氮湿式空气氧化和超临界水氧化研究进展

湿式空气氧化法(WAO)和超临界水氧化法（SCWO)废水处理技术近年已有广泛研究。当催化剂存在于氧化体系时,不仅能降低反应温度、压力,而且可提高废水中有害物质的降解效率。介绍了氨的湿式空气氧化和超临界水氧化催化剂应用的研究进展、各种催化剂在超临界水中的稳定性能及氨的催化超临界水氧化情况。     

某些剧毒有机废料在高温至超临界水中的处理实验

为了探索毒害有机废料的处理条件和反应机制,用二氨基乙二肟,氨基氰和蜜胺作初始试料,在温度１５０－４００℃,压力１００－７００×１０＾５Ｐａ的条件下进行了水热实验研究,部分密胺实验还添加了Ｈ２Ｏ２,实验结构表明,在水热条件下,尤其在超临界水中,二氨基乙二肟和氨基氰既可以通过热解作用而聚合成较高分子量的氮杂环混合物,进而水解转化成ＣＯ２和ＮＨ３,也可以直接发生水解作用,生成ＣＯ２和ＮＨ３,添加氧化剂可     

超临界态二氧化碳再生活性炭法治理甲苯废气

制鞋业产生的含甲苯、苯和二甲苯废气的治理大多采用活性炭吸附法。该课题提出以压缩二氧化碳为脱附剂,采用超临界流体萃取技术再生活性炭及回收甲苯工艺。实验表明,以液态或超临界态的压缩二氧化碳作萃取剂,采用萃取法可完全再生活性炭,其采用液态优于超临界态;压缩二氧化碳对活性炭具有扩孔作用,可增加活性炭的吸附容量,多次再生的活性炭吸附容量几乎不变;萃取剂的用量和密度显著影响着活性炭的再生效率;活性炭捆包填充在脱附塔中,不会显著增加脱附的阻力。      

超临界水氧化去除含酚废水TOC的动力学研究

本文利用自行设计的一套连续式超临界水氧化实验装置,以过氧化氢为氧化剂,处理实验室模拟含酚废水。在超临界条件下(P=30MPa,T=400℃,440℃,480℃,520℃)进行超临界水氧化实验。结果表明,TOC去除速率在氧化剂过量10倍的情况下,对TOC是2.15级反应。速率常数与温度的关系符合阿仑尼乌斯公式。反应的实验活化能为171.7kJ/mol,前置因子A为2.99×1011。     

钻井废液的固液分离工艺与设备

影响钻井废液固液分离的因素包括钻井废液的稀释比例、脱稳处理药剂的种类和加量、固液分离设备。文章介绍了钻井废液处理的基本流程,分析了钻井废液pH值对固液分离效果的影响,论述了卧式螺旋卸料沉降离心机的基本结构、设备参数和操作参数对固液分离效果的影响。