Improvement of welding heat source models for TIG-MIG hybrid welding process

Tungsten inert gas-metal inert gas (TIG-MIG) hybrid welding process is an effective way to improve welding productivity and quality due to advantages of the two processes. Mathematical analysis is crucial to fundamentally understand this synergetic welding process. In this study, based on experimental visualization of arc behaviors, some assumptions are proposed to deduce adaptive plane and volumetric heat source models separately for each involved welding method first. The influence of torch angles on distribution of temperature and geometry of weld bead are calculated and compared with experimental results. It shows that this developed algorithm of heat source can be employed to accurately predict welding process whether the electrode gun is slanted backward or forward to the direction of welding. Then TIG-MIG hybrid welding process is simulated and analyzed without considering the attractive or repulsive force of two arcs. The characteristic of TIG-MIG welding process is discussed compared to single MIG. It lays the foundation for the further research on the interaction of the two arcs during TIG-MIG hybrid welding.     

基于Tripod Beta事故模型的触电事故原因分析

应用Tripod Beta事故模型对某厂触电事故进行了深入分析,得到了事故原因,并提出预防类似事故的建议措施。     

生物吸附/MBR/硫铁自养反硝化组合工艺运行特性及蛋白质源污泥增量研究

为实现污水处理的深度脱氮除磷及蛋白质源污泥增量,进行了生物吸附/MBR/硫铁自养反硝化组合工艺处理城镇污水的试验研究.结果表明,生物吸附池可以快速富集进水中的大部分有机物,COD平均去除率为55.1%,剩余污泥采用厌氧发酵方式处理,用于生产优质碳源.通过组合工艺系统中的硝化、硫自养反硝化及铁屑除磷作用,出水氨氮、总氮和总磷分别达到1、5和0.4 mg·L~(-1)以下.优质碳源投加到MBR工艺段,碳源环境的改善使得污泥增长率从0.17 g VSS/g COD提高至0.49 g VSS/g COD,进水中总氮的同化比例从40%提高至59%.此外,污泥中蛋白质及氨基酸含量也显著增长,增长率分别为18.3%和19.7%.组合工艺在获得高排放标准水质的同时,实现了高蛋白质源污泥的增量,可为污泥资源化利用提供优质原料.     

秸秆压块与燃煤供热系统生命周期环境排放对比研究

为证明采用秸秆压块燃料替代煤炭进行供热的可持续性,对秸秆压块和燃煤供热系统的生命周期环境排放进行了对比分析.基于我国2012年投入产出表,构建了投入产出生命周期评价(IO-LCA)和过程生命周期评价(PLCA)相结合的混合生命周期评价(Hybrid-LCA)模型,核算了玉米秸秆压块和燃煤供热系统供应1 GJ热的生命周期CO2、SO2、NOx和PM2.5排放.结果显示,秸秆压块供热系统的生命周期CO2排放量为7 kg·GJ-1热,比燃煤供热排放减少121 kg.此外,秸秆压块供热系统比燃煤供热系统可以分别减少SO2排放98%、NOx排放76%和PM2.5排放58%.控制原料水分,通过减少原料收集和能源转化过程中的耗损,减少能源转化过程的电力消耗以及控制原料收集半径等可以有效改进秸秆压块供热系统环境表现.     

城市热岛效应下浅层土中混凝土的酸腐蚀试验研究

针对城市热岛效应引起城区浅层土地温场升高这一观测结果,采用室内快速模拟试验方法,对城区酸性土壤腐蚀混凝土材料的温度效应开展了试验研究.试验研究了在温度为5℃、20℃和40℃条件下,混凝土试样在酸浓度分别为0%、5%和10%的沙土介质中放置30 d、90 d后的抗压强度变化规律,并对混凝土试样在腐蚀过程中的腐蚀系数变化规...     

小麦在与水杨酸诱导的应答过程中PGIP的积累

以ＳＷ８９－２５８９小麦品系为材料,利用自制的小麦抗ＰＧＩＰ血清和ｄｏｔ－ｉｍｍｕｎｏｂｉｎｄｉｎｇ ａｓｓａｙ,并结合ＰＧＩＰ粗提液对ｅｎｄｏ－ＰＧ的抑制实验,研究了小麦内源多聚半乳糖醛酸酶抑制蛋白（ＰＧＩＰ）水平与水杨酸之间的应答关系。发现用水杨酸处理过的ＰＧＩＰ粗提液在ＮＣ膜上的显色斑点颜色均较Ｈ２Ｏ处理的ＰＧＩＰ粗提液深,而且对ｅｎ－ｄｏ－ＰＧ的抑制程度也高于未用水杨酸处理的ＰＧＩＰ粗提液     

Edible Invertebrates Among Amazonian Indians: A Critical Review of Disappearing Knowledge

For the indigenous populations of Amazonia, invertebrates constitute an important component of the diet. We have information on entomophagy for 39 ethnic groups, about 21,4 per cent of the 182 groups known in the Amazon Basin, but the use of this non conventional food resource is probably much more widespread. We present here a data-base of all the information available for each ethnic group regarding the species included in the diet, the scientific and the ethno name if known, the stage of life-cycle consumed, the manner of preparation and, when known, the host plant. This data-base lists 115 species scientifically identified and 131 ethno names. In addition, we have information about other 384 ethno names, with unsecure link to the Linnean taxonomy suggesting that local knowledge is very extensive. The data-base represents not only an easy to consult resource, but also a support for further research. The knowledge of the relations between indigenous populations and ecosystem is indeed the base for the natural and cultural biodiversity preservation.     

Comparative study on performances of a heat-pipe PV/T system and a heat-pipe solar water heating system

The heat-pipe solar water heating (HP-SWH) system and the heat-pipe photovoltaic/thermal (HP-PV/T) system are two practical solar systems, both of which use heat pipes to transfer heat. By selecting appropriate working fluid of the heat-pipes, these systems can be used in the cold region without being frozen. However, performances of these two solar systems are different because the HP-PV/T system can simultaneously provide electricity and heat, whereas the HP-SWH system provides heat only. In order to understand these two systems, this work presents a mathematical model for each system to study their one-day and annual performances. One-day simulation results showed that the HP-SWH system obtained more thermal energy and total energy than the HP-PV/T system while the HP-PV/T system achieved higher exergy efficiency than the HP-SWH system. Annual simulation results indicated that the HP-SWH system can heat the water to the available temperature (45°C) solely by solar energy for more than 121 days per year in typical climate regions of China, Hong Kong, Lhasa, and Beijing, while the HP-PV/T system can only work for not more than 102 days. The HP-PV/T system, however, can provide an additional electricity output of 73.019 kWh/m², 129.472 kWh/m², and 90.309 kWh/m² per unit collector area in the three regions, respectively.     

A real-time simulating non-isothermal mathematical model for the passive feed direct methanol fuel cell

In order to understand the complex transport phenomena in a passive direct methanol fuel cell (DMFC), a theoretical model is essential. The analytical model provides a computationally efficient framework with a clear physical meaning. For this, a non-isothermal, analytical model for the passive DMFC has been developed in this study. The model considers the coupled heat and mass transport along with electrochemical reactions. The model is successfully validated with the experimental data. The model accurately describes the various species transport phenomena including methanol crossover and water crossover, heat transport phenomena, and efficiencies related to the passive DMFC. It suggests that the maximum real efficiency can be achieved by running the cell at low methanol feed concentration and moderate current density. The model also accurately predicts the effect of various operating and geometrical parameters on the cell performance such as methanol feed concentration, surrounding temperature, and polymer electrolyte membrane thickness. The model predictions are in accordance with the findings of the other researchers. The model is rapidly implementable and can be used in real-time simulation and control of the passive DMFC. This comprehensive model can be used for diagnostic purpose as well.     

The determination and matching analysis of pinch point temperature difference in evaporator and condenser of organic rankine cycle for mixed working fluid

Exergo-economic analysis of the pinch point temperature difference (PPTD) in both evaporator and condenser of sub-critical organic Rankine cycle system (ORCs) are performed based on the first and second laws of thermodynamics. Taking mixture R13I1/R601a as a working fluid and the annual total cost per net output power Z as exergo-economic performance evaluation criterion, the effects of PPTD in evaporator ΔT_e, and the PPTD ratio of condenser to evaporator y, on the exergo-economic performance of ORCs are analyzed. Moreover, how some other parameters influence the optimal PPTD in evaporator ΔT_e,opt and the optimal PPTD ratio of condenser to evaporator y_opt are also discussed. It has been found that the exergo-economic performance of ORCs is remarkably influenced by ΔT_e and y, and there exists ΔT_e,opt and y_opt. In addition, ΔT_e,opt and y_opt are affected by heat transfer coefficient ratio of condenser to evaporator ß, the temperature of working fluid at dew point in condenser T_1a, and composition of R13I1/R601a: larger ß and T_1a lead to lower ΔT_e,opt and y_opt; by contraries, larger mass fraction of R13I1 makes ΔT_e,opt and y_opt increase, and y_opt increases linearly. The effects of the temperature of working fluid at bubble point in evaporator T_3a, mass flow rate of exhaust flue gas m_g, and inlet temperature of exhaust flue gas T_gi on ΔT_e,opt and y_opt are very slight. For comparison, three additional working fluids, namely R601a, R245fa, and 0.32R245fa/0.68R601a, are also taken into account.