响应面法优化超临界水氧化处理农药废水

在间歇式超临界水氧化系统中对草甘膦农药废水进行降解实验。选取温度、反应时间、过氧量3个量为因素量，总有机碳(TOC)去除率为响应量进行中心组合设计（CCD）。在实验的基础上，利用响应面分析法（RSM）对实验结果进行分析及参数优化：建立了TOC去除率与各个因素关系的二次多项式数学模型；分析了各个因素单独的及相互作用对TOC去除率的影响；优化结果表明，在温度483℃、反应时间29.2 min、过氧量148.4%的条件下，达到了最佳效果，此时TOC的去除率为100%。     

废椰壳制备活性炭负载CuO处理活性艳红X-3B废水的工艺优化

为了综合利用废椰壳,进行了废椰壳制备活性炭并负载氧化铜处理活性艳红X-3B废水的研究。采用正交实验法,以COD和色度去除率为目标函数确定了活性炭的最佳制备工艺条件为：磷酸浓度65%（质量百分数）,m（磷酸）/m（椰壳）比3∶1,活化时间2.5 h,活化温度500℃。在该活性炭上负载氧化铜处理活性艳红X-3B染料废水,其COD和色度去除率分别为83.70%和99.72%。用扫描电镜（SEM）和X衍射仪（XRD）对裸活性炭和载铜活性炭样品表面形貌和结构进行了表征和分析。通过单因素实验法确定了废水处理的最佳工艺条件为：pH值5,曝气时间4 h和催化剂用量0.55 g,在此条件下,COD和色度去除率分别为86.70%和99.75%,相应的出水指标为75 mg/L和32稀释倍数。     

三维电极法处理钻井废水影响因素分析

采取电化学法处理某钻井废水,考察了三维电极系统处理钻井废水时,废水浓度、电流密度、处理时间、电解质浓度和pH值对废水COD降解率的影响,实验结果表明,三维电极法处理钻井废水效果显著;增大电流密度、提高电解质浓度和延长处理时间能使COD去除率提高;最佳pH值为9。正交实验得到最优水平组合为A2B3C2D3E4,在此条件下COD去除率为86.56%。     

生物质材料预处理餐饮废水

采用4种廉价的生物质材料（水葫芦、柚子皮、木屑、核桃壳）用于餐饮废水的预处理。通过静态烧杯实验，研究了各生物质材料预处理废水的效果及最佳处理条件。结果表明，生物质材料对废水中COD的去除率均在45％以上，油脂吸附量为4～16mg／g，最优吸附材料为水葫芦，COD去除率达65％，油脂吸附量为16mg／g；水葫芦和柚子皮的最佳处理条件为：粒径〈0．2mm，投加量为20g／L，废水pH为4，处理时间为2h，温度为20℃；木屑和核桃壳的最佳实验条件为：粒径〈0．2mm，投加量为28g／L，pH为2，处理时间为2．5h，温度为20℃。生物质对餐饮废水的预处理，为废水中大量有机物和废弃油脂的去除提供了新思路和途径。     

基于中心组合设计的电解预处理含酚废水工艺优化

针对含酚废水不宜直接进行生化处理的问题,采用电解法预处理含酚废水,通过中心组合设计优化初始p H、电压、极板间距、电解质浓度和苯酚初始浓度对苯酚去除率的影响。结果表明,5个因素的影响为电压电解质浓度极板间距初始p H苯酚初始浓度。优化后的最佳条件如下:初始p H为6.56、电压为24.93 V、极板间距为20.05 mm、电解质质量浓度为2.46 g/L、苯酚初始质量浓度为368.87 mg/L。在优化条件下,苯酚初始质量浓度为300.00~500.00 mg/L时,出水质量浓度计算值为12.60~51.60mg/L,实验值为17.40~55.40 mg/L,去除率计算值为89.68%~96.47%,实验值为88.90%~95.40%,计算值与实验值接近,说明模型可靠。     

亚临界水技术处理厨余垃圾的比较研究

在亚临界实验条件下，以淀粉、纤维素类物质为模型化合物，H₂O₂为氧化剂，研究了厨余垃圾（大米、白菜）在亚临界水中部分氧化获取小分子有机酸的过程中处理时间、处理温度、加氧量对有机酸（甲酸、乙酸）生成的影响。以碳转化率为评价指标，确定反应最佳条件。实验结果表明：淀粉和纤维素分别在处理时间1～1.5 min，加氧量70%～100%，温度280℃；处理时间1～2 min，加氧量70%～100%，温度280～300℃条件下，生成有机酸浓度最大，达到最佳工艺条件。     

温度对复合厌氧折流板膜生物反应器处理生活污水效能的影响简

将新型CAMBR反应器（厌氧折流板反应器（ABR）与膜生物反应器（MBR）优化组合）用于处理生活污水，研究温度对该反应器处理效能的影响。实验水力停留时间7.5 h，混合液回流比设置为200%，pH值为6.5~8.5，溶解氧3 mg/L左右。控制3个温度梯度：高温（32~37℃），中温（20~25℃），低温（5~10℃），每个温度运行35 d。结果表明，在高温条件下，系统出水COD、NH₄⁺-N、TN和TP平均浓度分别为25、0.5、12.5和0.7 mg/L。在中温条件下，系统出水COD、NH₄⁺-N、TN和TP浓度分别30、1.2、12.5和0.4 mg/L。在低温条件下，COD和TP分别经过15 d和20 d调整适应，出水可恢复至35 mg/L和1 mg/L。由于低温（10℃以下）对硝化细菌产生强烈抑制，出水NH₄⁺-N去除率最终稳定在35%，TN去除率为40%。低温条件下，该反应器应用于污水处理中需注意适当保温，以保证出水水质。     

响应面法优化Fenton预处理干法腈纶废水

采用Fenton法预处理难降解干法腈纶废水,选取H2O2用量、Fe2+用量、初始pH和反应温度4个因素为变量,COD去除率为响应值进行中心组合设计。利用响应面法对实验结果进行分析,建立了以COD去除率为响应值的二次多项式模型并进行了显著性检验,分析了各因素单独及交互作用对COD去除率的影响,确定了最佳反应条件,并考察了最佳条件下处理前后废水可生化性和毒性变化。结果表明,所选取的4个因素影响COD去除率的主次顺序依次为:H2O2用量、Fe2+用量、初始pH和反应温度;在H2O2浓度为90.0 mmol/L、Fe2+浓度为23.9 mmol/L、初始pH值为3.4、温度为38.5℃的最佳条件下,COD去除率为53.8%,与模型预测值51.9%吻合度较高,偏差仅为3.66%;最佳条件下处理后废水可生化性显著提高,生物毒性明显降低,适宜于后续的生化处理。     

电Fenton法预处理餐饮废水

分析采用电Fenton法处理某高校食堂餐饮废水,为城市餐饮废水预处理提供了新途径。实验考察了p H、极板距、反应时间及电压等因素对餐饮废水COD、SS去除率的影响。通过正交实验确定的最佳实验条件为:电压27 V,电解时间40 min,p H为4,极板距1 cm。在此最佳条件下,COD去除率为66.1%,SS去除率为85.4%。     

电催化氧化处理变性木薯淀粉生产综合废水研究

采用DSA电极电催化处理变性木薯淀粉生产综合废水,研究了槽电压,电流密度,支持电解质,pH值,电解时间等因素对其中COD去除率的影响.在选定的实验条件下,槽电压8 V,电流密度为40 mA/cm2,支持电解质为0.1g/L的NaCl,pH值为8.5～9.0,电解2 h,废水中COD的去除率达88.3%.     

Chemical identification and acute biotoxicity assessment of gaseous chlorobenzene photodegradation products

In order to evaluate the ecological safety and feasibility of UV photodegradation processes for the treatment of halogenated aromatic hydrocarbons, the chemical composition and acute biotoxicity of gaseous chlorobenzene photodegradation products were investigated. Results showed that the main products of chlorobenzene photodegradation included hydrochloric acid, acetic acid, formic acid, phenol and chlorophenol. Roughly 64% of the removed chlorobenzene was converted into phenol, making it the most significant product formed. The types of byproducts suggested that two distinct reaction pathways might compete during the photodegradation process. Interestingly, it appeared that one of these pathways did not involve the direct photocatalytic oxidation of chlorobenzene. An acute biotoxicity assay measuring the inhibition of bioluminescence indicated that gaseous exhaust with overall higher toxicity was emitted after UV irradiation. The acute toxicity of the UV reactor exhaust gas was as high as EC(50)=13.5mg-Zn(2+)m(-3-)-gas. The increased toxicity mainly resulted from the conversion of chlorobenzene to more soluble toxic products and ozone production during the photodegradation process.     

紫外光降解气态氯苯的影响因素及其动力学研究

紫外光降解挥发性有机物(VOCs)是一种新型的废气处理技术.采用主波长为365 nm的500 W高压汞灯为光源,重点考察了空塔停留时间、氯苯初始浓度、反应介质等对氯苯光降解效果的影响.结果表明,在氯苯初始浓度较低时.氯苯去除率随着空塔停留时间的延长而呈线性升高.最大去除率达87%;而氯苯初始浓度过高时会使单位分子接受的光子和活性基团数量下降,引起氯苯去除率降低,空气介质中的O2和H2O在光照下可转化为活性基团.进而增强了光降解效果;而在氮气介质下光降解氯苯的效率大大降低,最大去除率仅为61%.在氯苯为0.36～8.64 mg/L时,紫外光降解氯苯遵循二级反应动力学方程.     

SBR处理模拟氯苯废水

在SBR中利用光合细菌球形红细菌污泥颗粒进行模拟氯苯废水处理的初步研究,结果表明,采用球形红细菌污泥颗粒处理模拟氯苯废水的SBR系统是可行的,其降解氯苯过程符合Monod一级反应动力学方程。当进水氯苯浓度在125～187.5 mg/L变化时,处理效率都能稳定在90.5%～95.6%之间;其最佳工艺条件为反应时间6 h、DO 4.75～5.0 mg/L、沉淀时间1.5 h、污泥颗粒浓度4 000～6 000 mg/L。在污泥颗粒浓度4 000 mg/L、DO 5.0 mg/L、反应时间6 h的最佳条件下,当进水COD为748.1 mg/L、氯苯浓度100 mg/L时,COD的去除率达90.9%,处理后出水COD满足国家一级排放标准要求。     

尿素/三乙醇胺吸收烟气NO_x的实验研究

以尿素作为吸收液,与NOx反应生成N2和CO2,脱除烟气中的氮氧化物。以一套双级串连的填料塔为主体反应器,分别对气速、液气比、反应物浓度、添加剂浓度和反应温度等参数对尿素溶液吸收NOx反应的影响进行了实验研究,获得了优化实验工况,研究结果显示,在气速为0.1 m/s、液气比为16 L/m3、三乙醇胺为0.01%（质量比）、尿素浓度为13%（质量比）工况下,反应温度为30~70℃,脱硝总效率可达50%以上,且随着NOx体积分数增加而提高。     

Formation and decomposition of chloroaromatic compounds in chlorine-containing benzene/oxygen flames

Premixed chlorine-containing, fuel-rich, low-pressure benzene/oxygen flames were analysed for the formation of (oxygenated) chloroaromatic compounds and their radicals by means of the condensation/radical-scavenging method (Hausmann, M., Homann, K.-H., 1995. Ber. Busenges. Phys. Chem. 99, 853-862). Several chlorinated organic compounds (methyl chloride, t-butyl chloride, chlorobenzene, chloroform) were used as additives within a maximum concentration of 10% of total fuel. Product identification and quantification were performed by GC/MS. The extent of formation of chloroaromatic compounds in these flames was largest in the cases of chlorobenzene and chloroform as additives. For chlorobenzene, 12 different chloroaromatics could be analysed in between C7H7Cl and C12H9Cl. Their formation is mainly due to conversion of initial chlorobenzene into substituted or oxidised derivatives, or growth products. Additional chlorination of aromatics is shown to be of minor importance in chlorobenzene-containing flames. Three isomeric (o/m/p) scavenging products could be identified for the chlorophenyl radical. In the chloroform case, 15 chloroaromatics could be analysed in between C6H5Cl and C14H9Cl. The weak C-Cl bond in chloroform is responsible for the high extent of chloroaromatics formation, either by Cl abstraction from the additive or by chlorination reactions via Cl radicals. Additionally, specific pathways to (di)chloroaromatics and chlorinated fulvene-type structures are outlined via CHCl2 and CCl2 radicals.     

改性CMC聚合物吸附酸法地浸废水中的铀

在温度为70～80℃、单体质量浓度为30%～35%、羧甲基纤维素∶丙烯酸(质量比)为10∶2.5、反应时间为3.5～4 h条件下对CMC进行改性,接枝率可达68%以上。以改性前后的CMC为吸附剂,对模拟酸法地浸含铀废水进行了对比吸附实验研究。结果表明:改性CMC对铀吸附效果最佳的实验条件为:改性CMC质量浓度为0.10 g/L,温度为25℃,pH为5.0,吸附时间100 min,此时铀去除率达到了97.1%,比CMC改性后对铀的吸附率平均提高了近21%。影响吸附效果程度由强到弱的顺序为:改性CMC投加量、pH、吸附时间、温度。     

Simultaneous sorption of lead and chlorobenzene by organobentonite

Clays or organoclays have been used as a barrier to prevent the transport of hazardous contaminants in landfills. However, clays are known to effectively sorb mostly inorganic contaminants, while organoclays are mainly used for organic contaminants. Since the organoclays are basically clay particles modified with cationic surfactants, there might exist an optimal coverage of cationic surfactant on the clay particles to sorb both inorganic and organic contaminants. In order to determine the optimal mass of cationic surfactants on the bentonites, sodium bentonites were treated with various ratios of hexadecyltrimethylammonium (HDTMA) to bentonites. Chlorobenzene and lead were selected as representative contaminants. When either chlorobenzene or lead exists as a single contaminant, chlorobenzene sorption increased with increasing HDTMA to bentonite ratios, and lead sorption decreased with increasing HDTMA to bentonite ratios. Sorption of chlorobenzene was a function of HDTMA coverage on the bentonites, while lead sorption was much more influenced by the initial lead concentration rather than the mass of HDTMA added to the bentonites.     

Sorption and cosorption of organic contaminant on surfactant-modified soils

Three kinds of soils were modified with the cationic surfactants, hexadecyltrimethylammonium (HDTMA) bromide and tetramethylammonium (TMA) bromide to increase their sorptive capabilities. Sorption of chlorobenzene in simulated groundwater by these soils was investigated. HDTMA-modified soil has a higher ability to sorb chlorobenzene from simulated groundwater than unmodified soil. TMA-modified soil did not show the superiority. HDTMA thus can be used to modify soil to improve its sorption capability. Cosorption of chlorobenzene in simulated groundwater in the absence or presence of nitrobenzene and dichloromethane on HDTMA-modified soil was also investigated. Nitrobenzene facilitated sorption of chlorobenzene on all HDTMA-modified soil. Dichloromethane did not influence the sorption of chlorobenzene by HDTMA-modified soil. The results suggest that HDTMA-modified soil is a highly effective sorbent for chlorobenzene and multiple organic compounds did not impede the uptake of chlorobenzene.     

Gaseous pollutants emitted from a mechanical biological treatment plant for municipal solid waste: Odor assessment and photochemical reactivity

The concentrations and chromatographic profiles of gaseous pollutants emitted from a municipal solid waste (MSW) biological treatment plant were investigated to identify the major odor substances and atmospheric photochemical reactive species (PRS). Four methods were used to measure different gaseous pollutants in this study, including colorimetric tubes, gas chromatography with mass spectrometry/flame ionization detection/pulsed flame photometric detection (GC-MS/FID/PFPD) preceded by cold trap concentration, GC-FID preceded by solid-phase microextraction (SPME), and high-performance liquid chromatography (HPLC) after derivation by 2,4-dinitrophenylhydrazine (DNPH). Seventy-five gaseous compounds belonging to nine groups (nitrogen compounds, sulfur compounds, alkanes, alkenes, aromatics, terpenes, alcohols, carbonyls, and volatile fatty acids [VFAs]) were identified. In the pre-biotreatment facility, the total concentration of the gaseous pollutants reached the maximum value on day 7 (317 ppm). During the post-biotreatment process, the total concentration of gaseous pollutants decreased from 331 ppm at the beginning to 162 ppm in the end. The group with the greatest decrease was carbonyls, from 64 to 7.4 ppm, followed by alcohols, from 40 to 4.5 ppm, which were both oxygenated compounds. The proportion of aromatics was notably high in the pre-mechanical treatment facility, accounting for 50.6% of the total, revealing the xenobiotic compounds disseminated by stirring and agitating the waste in the initial stage. The proportions of nitrogen compounds were lower in the pre- and post-mechanical treatment facilities (1.5% and 6.9%) than in the pre- and post-biotreatment facilities (11.9% and 13.8%), suggesting that their generation was closely associated with waste degradation. The major odor compounds in the facilities were acetic acid, butyric acid, valeric acid, isovaleric acid, and dimethyl sulfide. The major PRS in the facilities were aromatics, acetaldehyde, butyraldehyde, hexanal, isopentyl aldehyde, alcohol, α-pinene, limonene, and terpinene. Outside the facilities, VFAs and aromatics were the most important compounds causing an environmental impact.

Implications: The aim of this work is to assess the gaseous environmental impacts of mechanical biological treatment technology. The emission of gaseous pollutants greatly affects the living quality of nearby residents and odor complaints are becoming a major problem now. In this study, the authors utilized various pretreatment and analytical methods to obtain integrated emission information of gaseous pollutants. The results showed the transformation and fate of the gas pollutants during the treatment processes, which would help to improve the processes and to mitigate gaseous pollution.

Supplemental Materials: Supplemental materials are available for this paper. Go to the publisher's online edition of the Journal of the Air & Waste Management Association for information on the concentrations of the nine compound families at different sampling locations in the plant.     

An experimental and numerical study of the thermal oxidation of chlorobenzene

A combustion-driven flow reactor was used to examine the formation of chlorinated and non-chlorinated species from the thermal oxidation of chlorobenzene under post-flame conditions. Temperature varied from 725 to 1000 K, while the equivalence ratio was held constant at 0.5. Significant quantities of chlorinated intermediates, vinyl chloride and chlorophenol, were measured. A dominant C-Cl scission destruction pathway seen in pyrolytic studies was not observed. Instead, hydrogen-abstraction reactions prevailed, leading to high concentrations of chlorinated byproducts. The thermal oxidation of benzene was also investigated for comparison. Chemical kinetic modeling of benzene and chlorobenzene was used to explore reaction pathways. Two chlorobenzene models were developed to test the hypothesis that chlorobenzene oxidation follows a CO-expulsion breakdown pathway similar to that of benzene. For the temperatures and equivalence ratio studied, hydrogen abstraction by hydroxyl radicals dominates the initial destruction of both benzene and chlorobenzene. Chlorinated byproducts (i.e., chlorophenol and vinyl chloride) were formed from chlorobenzene oxidation in similar quantities and at similar temperatures to their respective analogue formed during benzene oxidation (i.e., phenol and ethylene).