轻钢-尾砂微晶发泡板组合墙平面外受力性能试验

本文提出了一种轻钢-尾砂微晶发泡板组合墙,是由内部嵌入钢筋的尾砂微晶发泡板与轻钢龙骨组合而成。为研究其风吸或风压作用下弹性变形性能以及平面外受弯破坏全过程,进行了8个轻钢-尾砂微晶发泡板组合墙足尺试件的单向加载试验。试件参数包括组合墙高度、发泡板强度、嵌入发泡板的钢筋直径、发泡板是否带釉面、发泡板是否复合轻质砌块。每个试件均进行3个工况的加载,前两个工况模拟风吸作用,加载至试件外表面产生裂缝;第三个工况模拟风压作用,加载至试件破坏。采用门式加载架,悬吊试件实现简支,通过简支分配梁将集中荷载分成与试件八点接触加载,各加载点设置球铰支座。研究表明:轻钢龙骨与发泡板有良好的平面外共同工作性能;采取增大组合墙截面高度、提高发泡板材料强度、发泡板设置釉面层、发泡板复合粉煤灰砌块的构造措施,均可提高组合墙的平面外受力性能,复合粉煤灰砌块对提高试件平面外承载能力效果最为显著;利用截面换算方式对组合墙板平面外极限承载力进行计算,计算结果与试验符合较好。结合试验数据及外围护墙板的风荷载计算公式,计算出组合墙的极限风荷载值,为该组合墙的设计及工程应用提供了参考。     

湍流模型和壁面函数对有障碍半开口空间氢气燃烧模拟的影响

为了进一步验证有障碍半开口空间内氢气燃烧数值模拟的准确性，使用对比验证的方法对FLUENT软件湍流模型和壁面函数数值模拟结果的准确性进行了研究。研究结果表明:可实现k-ε湍流模型和非平衡壁面函数使燃烧压力和火焰形状与实验结果相比偏差较大，RNG k-ε湍流模型和可伸缩壁面函数可更准确地预测燃烧压力变化及火焰传播行为。     

SO_2与CeO_2超细颗粒非均相反应产物的细胞毒性效应

大气二次细颗粒物(secondary fine particulate matters,SFPMs)是我国城市大气PM_(2.5)的主要组成部分。然而由于PM_(2.5)组成成份复杂,其毒性产生的来源并不明确。在本研究中,我们以二氧化铈(CeO_2)超细颗粒物(UFPs)为大气细矿物质颗粒模型,研究了SO_2气体在模拟大气环境中,如湿度(RH)、紫外光照(UV)和NO_2存在条件下,在CeO_2UFPs界面经多相反应生成的二次无机细颗粒物的性质及与细胞毒性的构效关系。实验通过实时高通量细胞分析系统,实时观察了CeO_2-SFPMs暴露对小鼠单核巨噬细胞(RAW264.7)增殖的影响;并进一步检测了CeO_2-SFPMs对细胞膜通透性和细胞凋亡的影响。结果表明,SO_2与CeO_2UFPs作用后可转化为硫酸盐,在有NO_2存在下转化更为明显。CeO_2-SFPMs对细胞毒性效应与其生成的环境条件相关,并具有时间效应性。RAW264.7细胞暴露于CeO_2-SFPMs 8 h,细胞增殖无明显变化;暴露8~25 h后,CeO_2-SFPMs对细胞增殖的抑制率随CeO_2@CeO_2+SO_2@CeO_2+SO_2+RH≈@CeO_2+SO_2+RH+UV@CeO_2+SO_2+RH+NO_2的顺序显著升高。CeO_2-SFPMs对Raw264.7细胞膜通透性和细胞凋亡的影响研究也证明CeO_2-SFPMs@CeO_2+SO_2+RH+NO_2产生的细胞毒性最明显。     

3种石油烃降解菌对石油烃的降解效果及其细胞表面疏水性

选取3种石油烃降解菌:假单胞菌(Pseudomonas sp.,DS-1)、铜绿色假单胞菌(Pseudomonas aeruginosa,DS-2)和无色杆菌(Achromobacter sp.,DS-3),研究其对石油烃的降解效果及其细胞表面疏水性。结果表明,经过6d的降解,3种石油烃降解菌对石油烃的降解率分别为99.08%、79.75%、84.34%。石油烃的黏附性测试和盐析聚集测试结果表明,3种石油烃降解菌均表现出较高的细胞表面疏水性,其规律为DS-1DS-3DS-2。其中DS-1的细胞表面疏水性最高,达65.90%。DS-1、DS-2和DS-3菌株发生盐析聚集所需最小(NH4)2SO4摩尔浓度分别为2.0、2.8、2.4 mol/L。菌株的细胞表面疏水性和降解有机物的能力有着较高的相关性。     

一体式MFC-好氧MBR运行效果及膜污染特性

膜生物反应器（MBR）是一种高效的污水处理工艺，而微生物燃料电池（MFC）能利用N0i作为电子受体进行脱氮。为解决膜生物反应器（MBR）脱氮效率低和膜污染问题，建立了一套能够进行脱氮、有效抑制膜污染的一体式MFC-好氧MBR新工艺。以开路MFC—MBR反应器为对照，对耦合系统中污水处理效果、膜污染情况进行研究。研究表明，2套系统的COD去除率均超过88％，对NH4-N的去除均达到99％。闭路MFC—MBR系统TN去除率达到69．4％，高于开路系统的55．3％。混合液的MLVSS／MLSS稳定在88％左右，同时耦合系统能够改善污泥混合液的性质，zeta电位的绝对值和粘度较开路系统有所减少，污泥颗粒平均体积粒径（233．482μm）较开路系统（94．877μm）有明显增加，膜清洗周期延长了41．17％。     

胞外多聚物在厌氧污泥颗粒化成核过程中的特性

以模拟啤酒废水为底物在IC反应器中进行厌氧污泥颗粒化培养,并对污泥颗粒化过程中胞外多聚物(EPS)的主要成分变化及其与细胞表面疏水性和Zeta电位之间的相互关系进行分析,以此来阐述EPS对污泥颗粒化成核的作用。研究结果表明,好氧剩余污泥在经过56 d的培养后,平均粒径由接种时的54.72μm增长到103.46μm,实现了厌氧污泥颗粒化成核过程;EPS蛋白质含量(PN)在颗粒化过程中逐渐由接种时的18.1 mg/g增至54.3 mg/g,而EPS多糖含量(PS)则无明显变化;此外,PN/PS与污泥平均粒径、细胞表面疏水性(RH)以及Zeta电位之间呈正相关关系,相关系数分别为0.9727、0.9593和0.9274。由此可推测:厌氧污泥颗粒化成核过程的主要作用成分为胞外蛋白质,其可以改变污泥细胞表面疏水性和Zeta电位,从而在厌氧污泥颗粒化过程中有着重要的促进作用。     

Biogas upgrading and utilization from ICEs towards stationary molten carbonate fuel cell systems

Biogas production from anaerobic digestion has increased rapidly in the last years, in many parts of the world, mainly due to its local scale disposition and to its potential on greenhouse gases (GHG) emissions mitigation. Biogas can be used as fuel for combined heat and power systems (CHP), in particular for internal combustion engines (ICEs). In recent investigations, fuel cells have been considered as alternative CHP systems. In the present article, two different energy conversion systems are compared: a 1.4 MW class MCFC system, running on pipeline natural gas, and an in situ ICE, running on biogas. In the first case, biogas is considered as a source fuel to obtain upgraded gas to be injected in the natural gas grid. In such scenario, the location of the fuel cell power plant is no longer strictly connected to the anaerobic digester site. Several energy balances are evaluated, considering different upgrading techniques and different biogas methane/carbon dioxide ratios.     

Power performance characterization of multi-crystalline silicon solar cells and its module at outdoor exposure

Outdoor power performance measurements of silicon (Si) solar cells and its assembled module were carried out at the coastal site of geographical location of 12.0107° Latitude and 79.856° Longitude, of Puducherry, India. Measurements were analyzed in comparison with the daily solar illumination data obtained by an optical pyranometer deployed with global measurement condition. It was found that the module required ~3 times more illumination to stabilize in its output voltage than the requirement of an individual cell and exhibited 11.35% loss in its efficiency compared to its STC value. Proposed operation of 5.30 hours was found resulting in an output rating fixed at ~40% from its 100% full capacity.     

Metabolism of the14C-labeled herbicide clodinafop-propargyl in plant cell cultures of wheat and tobacco

The metabolism of ¹⁴C-clodinafop-propargyl (CfP) was examined in cell cultures of wheat (Triticum aestivum L. cv. ‘Heines Koga II’) and tobacco (Nicotiana tabacum L.). Besides the non-transgenic tobacco culture, cultures transformed separately with cDNA of human cytochrome P450-monooxygenases (P450s) CYP1A1, CYP1A2, CYP3A4, CYP2B6 and CYP2C19 were examined. Experiments with wheat were executed in the presence and absence of safener cloquintocet-mexyl (CqM). After 48 h of incubation, only about 10% of applied ¹⁴C was found in media (both tobacco and wheat). Non-extractable residues of ¹⁴C-CfP in wheat cells were 16.54% (without CqM) and 30.87% (with CqM). In all tobacco cultures, 82.41–92.46% of applied radioactivity was recovered in cell extracts. In contrast to wheat, non-extractable residues amounted only to 1.50–2.82%. As determined by radio-thin layer chromatography (TLC) and -high-performance liquid chromatography (HPLC), the parent CfP was not found in the cell extracts of wheat; in tobacco cell extracts, only traces of CfP were detected. After a hydrolysis of assumed carbohydrate conjugates of CfP derived polar ¹⁴C-labeled compounds, TLC and HPLC analysis showed that in wheat, a more complex pattern of metabolites of CfP were observed as compared to all tobacco cultures. In hydrolysates resulting from wheat, the identity of three primary products was confirmed by means of GC-EI-MS: free acid clodinafop (Cf), hydroxy-Cf hydroxylated at the pyridinyl moiety, and 4-(5-chloro-3-fluoropyridin-2-yloxy)phenol. In hydrolysates derived from all tobacco cultures, main metabolite was Cf besides only traces of further unidentified products. Differences among the different tobacco cultures (non-transgenic, transgenic) did not emerge. According to kinetics of disappearance of primary metabolite Cf as well as formation of polar soluble products and non-extractable residues, metabolization of CfP proceeded at a noticeably higher rate in wheat cells treated with safener CqM than in cells without CqM treatment. Thus, these results indicated a stimulation of CfP's metabolism by CqM, although metabolic profiles observed in CqM treated and non-treated cells (after hydrolysis) were qualitatively similar. The findings obtained from all tobacco cultures suggested that with the exception of ester cleavage to Cf, CfP cannot be metabolized by tobacco itself or by the human P450s examined.