热电池失效分析及等效加速贮存试验技术

目的建立基于实测环境载荷的热电池等效加速贮存试验技术,掌握其在环境载荷作用下的性能退化规律。方法在分析热电池组成和所受环境载荷情况的基础上,分析热电池的主要失效模式,设计基于实测环境数据的等效加速贮存试验,开展热电池等效加速贮存试验,分析热电池性能和热图像的变化情况,利用粒子滤波算法对电池剩余电容量进行预测。结果随加速循环次数(时间)的增加,热电池的电容量下降。热图像表明,热电池经过等效加速贮存试验后,其放电过程表面温度要高于初始放电表面温度。粒子滤波算法能够有效模拟电容量的退化过程,电池剩余电容量预测结果与试验结果误差在10%以内。结论等效加速贮存试验得到了热电池的性能退化规律,从而为热电池的贮存试验提供一种解决方案。     

低成本高效慢速烤燃试验方法研究

目的研究低成本高效慢速烤燃试验方法。方法利用自主研发的一套慢速烤燃试验装置,以1℃/min和3.3℃/h升温程序作为对比试验,设置几种三阶段升温程序,对JBO-9013和JH-14炸药进行慢速烤燃试验,以此获得不同升温程序下试样的响应温度和响应等级。结果 1℃/min、3.3℃/h、三阶段(100/150/193℃)升温程序下,JBO-9013响应温度分别为243.1、199.5、199.8、201.4、193.0℃,响应等级均为燃烧反应;JH-14响应温度分别为211.0、186.0、191.7℃,响应等级均为爆轰反应。结论升温程序对JBO-9013和JH-14响应温度和响应剧烈程度均有影响。与GJB8018—2013中1℃/min升温程序相比,三阶段升温程序与MIL-STD-2105D和STANAG 4439中3.3℃/h烤燃试验结果吻合度较高。因此,三阶段升温程序具有缩短试验周期、提高试验效率和降低试验成本的作用。     

The performance of RAMS in representing the convective boundary layer structure in a very steep valley

Data from a comprehensive field study in the Riviera Valley of Southern Switzerland are used to investigate convective boundary layer structure in a steep valley and to evaluate wind and temperature fields, convective boundary layer height, and surface sensible heat fluxes as predicted by the mesoscale model RAMS. Current parameterizations of surface and boundary layer processes in RAMS, as well as in other mesoscale models, are based on scaling laws strictly valid only for flat topography and uniform land cover. Model evaluation is required to investigate whether this limits the applicability of RAMS in steep, inhomogeneous terrain. One clear-sky day with light synoptic winds is selected from the field study. Observed temperature structure across and along the valley is nearly homogeneous while wind structure is complex with a wind speed maximum on one side of the valley. Upvalley flows are not purely thermally driven and mechanical effects near the valley entrance also affect the wind structure. RAMS captured many of the observed boundary layer characteristics within the steep valley. The wind field, temperature structure, and convective boundary layer height in the valley are qualitatively simulated by RAMS, but the horizontal temperature structure across and along the valley is less homogeneous in the model than in the observations. The model reproduced the observed net radiation, except around sunset and sunrise when RAMS does not take into account the shadows cast by the surrounding topography. The observed sensible heat fluxes fall within the range of simulated values at grid points surrounding the measurement sites. Some of the scatter between observed and simulated turbulent sensible heat fluxes are due to sub-grid scale effects related to local topography.     

大气汞形态测定中吸附剂的选择及性能

本文选择了上试-402树脂作为常温高效选择性吸附氯化甲基汞的吸附剂,改进了Cbromosorb W-SE30-HCl吸附剂管的制备方法,并同时组装了一套由微孔纤维滤膜与Chromosorb W-SE30-HCl、402树脂、螺旋银丝、镀金细砂等四种吸附管串联组成的采样系统,由小型采样机抽气采样,于常温下同时依次富集颗粒汞、氯化汞、氯化甲基汞、单质汞及二甲基汞,系统小型轻便,适于野外采样。采样后,四种吸附剂分别采用高低两种温度脱汞。上述五种形态汞均由装有高温石英原子化器的AAs定量测定。     

热活化过硫酸盐氧化降解水体中泛影酸钠的研究

利用热活化过硫酸盐氧化降解水体中的泛影酸钠,主要研究了体系反应温度、氧化剂浓度、溶液初始pH、底物浓度及自然水体组分对降解效果的影响.结果表明,热活化过硫酸盐降解泛影酸钠符合准一级反应动力学模型及遵循阿伦尼乌斯模型,计算得到反应活化能为105.57 kJ·mol~(-1).增加过硫酸盐初始浓度或提高反应温度及降低泛影酸钠初始浓度可以增大泛影酸钠的降解速率常数k(k=0.0062×[K_2S_2O_8]_0,R~2=0.98,[K_2S_2O_8]_0=2～8 mmol·L~(-1);lnk=-12698×1/T+34.91,R~2=0.98,T=325～345 K;k=-1.54×[泛影酸钠]_0+0.064,R~2=0.98).泛影酸钠的降解速率常数k受溶液初始pH影响较小.溶液中Cl~-、HCO~-_3和HA的存在均会抑制泛影酸钠的降解.较低的TOC去除率和产物的检测表明,泛影酸钠降解过程中仅发生苯环侧链的破坏.泛影酸钠的降解途径主要有酰胺键断裂、氨基氧化和脱羧基羟基化.     

光电催化降解苯胺的研究——单槽与双槽光反应器对比

以直接热氧化制备的TiO2为催化剂，采用单双槽光反应器，研究了水中苯胺的光电催化降解行为，结果表明：氧的还原反应不是光电催化反应的速率控制步骤，但氧的还原和还原产物能加快苯胺的光电催化降解速率，单槽光电反应器中，当pH由4．38升至10．30，苯胺降解反应速率是逐渐增大。当pH大于10．30后，反应速率迅速下降，使用双槽反应器，阳极室鼓氮气时，苯胺的反应速率始终随pH的升高而下降，而不阳极室鼓空气时，苯胺反应速率在pH9.0左右时最大，在相同的气氛条件下，苯胺在单槽的光电催化反应速率大于双槽的速率，利用光电流的大小可判断反应速率的快慢，但光电流的利用效率与溶液pH，氧和电压有关。     

Effects of thermally pretreated temperature on bio-hydrogen production from sewage sludge

Hydrogen can be obtained by anaerobic fermentation of sewage sludge. Therefore, in this paper the effects of thermally pretreated temperatures on hydrogen production from sewage sludge were investigated under different pre-treatment conditions. In the thermal pretreatment, some microbial matters of sludge were converted into soluble matters from insoluble ones. As a result, the suspended solid（SS） and volatile suspended solid（VSS） of sludge decreased and the concentration of soluble COD（SCOD） increased, including soluble carbohydrates and proteins. The experimental results showed that all of those pretreated sludge could produce hydrogen by anaerobic fermentation and the hydrogen yields under the temperatures of 121℃ and 50℃ were 12.23 ml/g VS（most） and 1.17 ml/g VS （least）, respectively. It illuminated that the hydrogen yield of sludge was affected by the thermally pretreated temperatures. Additionally, the endurance of high hydrogen yield depended on the translation of microbial matters and inhibition of methanogens in the sludge. The temperatures of 100℃ and 121℃ （treated time, 30 min） could kill or inhibit completely the methanogens while the others could not. To produce hydrogen and save energy, 100℃ was chosen as the optimal temperature for thermal pretrcatment. The composition changes in liquid phase in the fermentation process were also discussed. The SCOD of sludge increased, which was affected by the pretreatment temperature. The production of volatile fatty acids in the anaerobic fermentation increased with the pretreatment temperature.     

Linking desorption kinetics to phenanthrene biodegradation in soil

The desorption of polycyclic aromatic hydrocarbons (PAHs) often exhibits a biphasic profile similar to that observed for biodegradation whereby an initial rapid phase of degradation or desorption is followed by a phase of much slower transformation or release. Most investigations to-date have utilised a polymeric sorbent, such as Tenax, to characterise desorption, which is methodologically unsuitable for the analysis of soil. In this study, desorption kinetics of ¹⁴C-phenanthrene were measured by consecutive extraction using aqueous solutions of hydroxypropyl-β-cyclodextrin (HPCD). The data indicate that the fraction extracted after 24 h generally approximated the linearly sorbed, rapidly desorbing fraction (F_rap), calculated using a three-compartment model. A good linear correlation between phenanthrene mineralised and F_rap was observed (r² = 0.89; gradient = 0.85; intercept = 8.20). Hence HPCD extraction (24 h) and first-order three-compartment modelling appear to provide an operationally straightforward tool for estimating mass-transfer limited biodegradation in soil.     

Numerical studies on the thermal regimes of the horizontal tube falling film evaporation under varying feeder height

ABSTRACT

This paper discusses about the effect of feeder height and heat flux on the heat transfer characteristics of horizontal tube falling film evaporation in the thermal regimes. In order to investigate this, a two- dimensional CFD model was developed to perform simulation and results were compared and validated with published data available in the literature. Heat transfer co-efficients in the thermal regimes were determined from the CFD simulation and the results were recorded, analyzed and validated with the mathematical models available in the literature. The novelty of the current study is to predict the commencement of the fully developed thermal region over the tube from the simulation model under varying feeder height and heat flux. An effort was also made to measure the liquid film thickness around the tube from the CFD model in the thermal regimes. It is observed that angle of thermally developing region contracts and fully developed thermal region extends with the increase of the feeder height and heat flux. It is observed from the study that increase of heat flux by 10 kW/m² resulted in increase of heat transfer co-efficient value by 10–12% average in thermally developing region and 12–15% average in fully developed region. Thinnest liquid film thickness observed between 85 and 127°angle. Shifting of thinnest region of liquid film upward from the mid tube with the increase of the feeder height and heat flux is noted.     

Gear oil formulation designed to meet bio-preferred criteria as well as give high performance

A bio-based gear oil was developed from soybean oil (SBO). The SBO was first thermally polymerised and then mixed with additives and diluents. The effect of pour point depressants, co-base oils, antioxidants and anti-wear additives is reported. Lubricity, viscosity index and oxidation stability of the final formulation of the bio-based gear oil are compared with commercially available gear oils. The final formulation of bio-based gear oil gives test results: viscosity index 165, four-ball wear scar 0.375 mm. These numbers are comparable to or better than the commercially available gear oils tested for comparison. The oxidation onset temperature of the bio-based gear oil, 220°C, is lower than the evaluated commercial products, but still at an acceptable range for gear oil.