汽油在西北黄土上吸附特性的研究

通过动力学和热力学吸附实验,研究了汽油在西北地区黄土上的吸附行为,同时研究了提取的天然腐植酸对汽油在黄土上吸附行为的影响.结果表明,汽油在黄土上的吸附在6h内达到平衡.无论是否加入腐植酸,汽油在黄土上的吸附动力学过程均符合Elovich方程,其热力学吸附符合Freundlich方程.腐植酸的存在使汽油在黄土上的吸附能力减小.反应温度从25℃升高到45 C,汽油在土壤上的饱和吸附量从6.300mg·g-1减小到1.365 mg·g-1,表明汽油在黄土上的吸附属于放热反应.溶液pH和土壤粒径的增大,均不利于汽油在黄土上的吸附,溶液pH和土壤粒径越大,其在黄土上的吸附量越小.另外,在室温下对吸附了汽油的土壤样品和纯汽油挥发行为的研究表明,吸附了汽油的土壤样品的汽油挥发比纯汽油慢,其挥发率与时间成对数关系.     

零价铁对脱色希瓦氏菌S12偶氮还原的促进作用

以脱色希瓦氏菌(Shewanella decolorationis)S12为实验菌株,研究了零价铁(ZVI)存在条件下微生物的厌氧偶氮还原特性及其最佳反应条件.结果表明,ZVI可显著促进菌株S12的厌氧偶氮还原速率.培养30 h后含有20 mmol.L-1微米级ZVI和S12菌的培养体系中,菌株S12对1 mmol.L-1苋菜红的脱色率达100%,比不含ZVI的S12菌培养体系和只含ZVI的体系的偶氮还原率分别提高了23.16%和94.66%;在额外含20 mmol.L-1甲酸钠的培养体系中,ZVI的存在也使S12菌对苋菜红的脱色率提高了20.54%.此外,ZVI的存在可显著提高培养体系对偶氮染料的耐受能力.在投加ZVI和菌株S12培养体系中,连续批量投加浓度为1 mmol.L-1的苋菜红可在276 h内实现11次有效脱色,而不含ZVI的S12菌培养体系中只能实现3次有效脱色.进一步的研究发现,ZVI与菌株S12协同培养体系的最适反应pH为9.0,最适ZVI投加量为60 mmol.L-1.与毫米级和纳米级ZVI颗粒相比,微米级ZVI颗粒具有更强的促进作用.本研究结果将为利用ZVI协同促进偶氮染料的生物治理效果提供科学参数.     

Synthesis and characterization of agricultural controllable humic acid superabsorbent

Humic acid superabsorbent polymer (P(AA/AM-HA)) and superabsorbent polymer (P(AA/AM)) were synthesized by aqueous solution polymerization method using acrylic acid (AA), acrylamide (AM) and humic acid (HA) as raw material. The effects of N,N'-methylenebisacrylamide (MBA) crosslinking agent, potassium peroxydisulfate (KPS) initiator, reaction temperature, HA content, ratio of AA to AM, concentration of monomer and neutralization of AA on water absorption were investigated. Absorption and desorption ratios of nitrogen fertilizer and phosphate fertilizer were also investigated by determination of absorption and desorption ratio of NH₄⁺, PO₄^3- on P(AA/AM-HA) and P(AA/AM). The P(AA/AM-HA) and P(AA/AM) were characterized by Fourier translation infrared spectroscopy, biological photomicroscope and scanning electron microscopy (SEM). The optimal conditions obtained were as follows: the weight ratio of MBA to AA and AM was 0.003; the weight ratio of KPS to AA and AM was 0.008; the weight ratio of HA to AA was 0.1; the mole ratio of AM to AA is 0.1; the mole ratio of NaOH to AA is 0.9; the reaction temperature was 60℃. P(AA/AMHA) synthesized under optimal conditions, has a good saline tolerance, its water absorbency in distilled water and 0.9 wt.% saline solution is 1180 g/g and 110 g/g, respectively. P(AA/AM-HA) achieves half saturation in 6.5 min. P(AA/AM-HA) is superior to P(AA/AM) on absorption of NH₄⁺, PO₄^3-. The SEM micrograph of P(AA/AM-HA) shows a fine alveolate structure. The biological optical microscope micrograph of P(AA/AM-HA) shows a network structure. Graft polymerization between P(AA/AM) and HA was demonstrated by infrared spectrum. The P(AA/AM-HA) superabsorbent has better absorbing ability of water and fertilizer, electrolytic tolerance and fewer cost than P(AA/AM) superabsorbent.     

Quantitative analysis of microbial biomass yield in aerobic bioreactor

We have studied the integrated model of reaction rate equations with thermal energy balance in aerobic bioreactor for food waste decomposition and showed that the integrated model has the capability both of monitoring microbial activity in real time and of analyzing biodegradation kinetics and thermal-hydrodynamic properties. On the other hand, concerning microbial metabolism, it was known that balancing catabolic reactions with anabolic reactions in terms of energy and electron flow provides stoichiometric metabolic reactions and enables the estimation of microbial biomass yield (stoichiometric reaction model). We have studied a method for estimating real-time microbial biomass yield in the bioreactor during food waste decomposition by combining the integrated model with the stoichiometric reaction model. As a result, it was found that the time course of microbial biomass yield in the bioreactor during decomposition can be evaluated using the operational data of the bioreactor (weight of input food waste and bed temperature) by the combined model. The combined model can be applied to manage a food waste decomposition not only for controlling system operation to keep microbial activity stable, but also for producing value–added products such as compost on optimum condition.     

Degradation of monofluorophenols in water irradiated with gaseous plasma

Decomposition of aqueous monofluorophenols (MFPs) was investigated by contact glow discharge electrolysis (CGDE). During CGDE, both MFPs and the corresponding total organic carbon (TOC) in water were consumed smoothly, suggesting that carbon atoms of benzene nucleus could be eventually mineralized to inorganic carbon (IC). And all the fluorine atoms in the MFPs were equally converted to fluoride ions. Based on the primary intermediates from each starting materials, it showed that aromatic hydroxylation preferentially occurred at the para- or ortho- position to the phenolic OH group of each MFPs. The disappearance of both MFPs and TOC followed the first-order rate law. The apparent rate constants for the decay of MFPs were independent from the pK_a values of MFPs.     

日本交通部门碳排放与低碳交通相关因素研究

本文就日本向低碳社会体系转型的过程中,交通部门碳排放现状、都市交通体系构成、实施对策等方面进行了分析,探讨其交通运输领域低碳交通的相关因素及发展模式,为中国低碳交通体系的构建提供参考。     

ABR反应器中COD/SO_4~(2-)值和硫酸盐负荷对SO_4~(2-)去除影响

利用厌氧折流板反应器,分别考察了反应器启动,及不同COD/SO42-比值和硫酸盐负荷对模拟废水中SO42-去除的影响。实验在(32±0.1)℃,pH为6.0⁶.5的条件下连续运行。结果表明:ABR经过约90 d的启动驯化阶段后,进水硫酸盐及COD浓度分别为1 500 mg/L和3 000 mg/L,水力停留时间为12 h条件下,硫酸盐去除率达到了92%。固定COD/SO42-比值为2.5时,随着进水SO42-浓度的增加(1 5006.5的条件下连续运行。结果表明:ABR经过约90 d的启动驯化阶段后,进水硫酸盐及COD浓度分别为1 500 mg/L和3 000 mg/L,水力停留时间为12 h条件下,硫酸盐去除率达到了92%。固定COD/SO42-比值为2.5时,随着进水SO42-浓度的增加(1 500³ 500 mg/L),SO42-去除率逐渐下降,最低为60%,相反SO42-去除速率随着硫酸盐浓度的增加而增加,最大为7.98 kg(/m3.d);维持恒定的硫酸盐浓度(1 500 mg/L),逐渐缩短水力停留时间以提高反应器中硫酸盐负荷,SO42-去除率呈现先上升后下降的复杂变化趋势,当水力停留时间为6 h时,SO42-去除率达到最大;随着COD/SO42-比值的提高,硫酸盐去除能力增强,且反应体系对硫酸盐负荷的耐受能力也逐渐增强。     

天水市二氧化硫浓度与硫酸盐化速率的相关性分析

以2001～2010年十年间天水市城区二氧化硫浓度与硫酸盐化速率的监测数据为依据,对城区二氧化硫与硫酸盐化速率的浓度水平和变化规律进行了研究,分析和探讨了二氧化硫浓度与硫酸盐化速率相关性。     

西安市再生水利用存在问题及预测分析研究

污水作为一种稳定可靠、再生利用的水资源,经深度处理后可用作工业冷却水、城市杂用水、河流景观补充水及农业灌溉等方面。合理开发和利用再生水是解决水资源缺乏的有效途径。本文通过深入调查、分析西安市再生水利用现状,找出再生水利用率低的原因,提出针对性措施,并对防治对策进行定量分析,预测2015年西安市“污水再生利用率”为30．6％,可达到20％的国家考核要求。