气浮-水解酸化-SBR工艺在屠宰废水处理中的应用研究

屠宰废水具有有机物含量高、可生化性较好等特点,因此生化处理是屠宰废水的主要工艺。某公司对屠宰废水采用"气浮-水解酸化-SBR"工艺进行处理,废水处理结果表明,当废水进水SS、COD cr、BOD5、NH3-N平均浓度分别为580 mg/L、1 900 mg/L、1 140 mg/L、54 mg/L时,出水SS、COD cr、BOD5、NH3-N平均浓度分别为45 mg/L、55 mg/L、15 mg/L、10 mg/L,出水水质指标满足《肉类加工工业水污染物排放标准》(GB 13457-92)的一级排放标准要求,废水中SS、COD cr、BOD5、NH3-N平均去除率分别为92%、97%、98.5%、72%。     

水解酸化/生物膜法SBR处理印染废水实验研究

针对印染废水污染物浓度高、种类多、色度高、可生化降解性差等特点,对印染废水采用水解酸化/生物膜法SBR进行处理,结果表明,该处理工艺处理效果较好,出水COD、色度、BOD5、NH3-N浓度分别为60~100 mg/L、50~70倍、20~24 mg/L、5~10 mg/L,平均去除率分别达到92.1%、86.5%、95%、90%。     

污泥和餐厨垃圾联合干法中温厌氧消化性能研究

采用完全混合式反应器R1～R5(进料脱水污泥与餐厨垃圾的湿重混合比分别为1:0、4:1、3:2、2:3和0:1),在半连续运行的状态下,考察了停留时间(solid retention time,SRT)为20 d时脱水污泥和餐厨垃圾混合干法厌氧消化的产气性能、有机质降解性能和系统稳定性.结果表明,随着进料中餐厨垃圾所占比例的增大,系统的产气率和甲烷产率呈上升趋势,产气中甲烷含量呈下降趋势,污泥中添加餐厨垃圾有助于在利用原有消化罐容积的前提下显著提高有机负荷和体积产气率.餐厨垃圾比例越大,混合物料的水解速率常数越大,有机质降解率越高,R1～R4中有机质水解速率常数分别为0.25、0.61、1.09和1.56 d-1,有机质降解率分别为37.4%、50.6%、60.7%和68.2%,水解速率差异是导致VS降解率不同的主要原因.随着餐厨垃圾比例的增大,系统内pH、总碱度(total alkalinity,TA)、总氨氮(total ammonia nitrogen,TAN)和游离氨氮(free ammonianitrogen,FAN)呈下降趋势,当污泥中添加的餐厨垃圾提高60%时,系统内pH、总碱度、总氨氮和游离氨氮分别下降6%、16%、22%和75%.游离氨和Na+分别是影响污泥和餐厨垃圾单独干法消化稳定性的重要因素,污泥和餐厨垃圾混合消化可降低潜在抑制性物质的浓度,显著提高系统稳定性.     

复合人工湿地系统强化处理单元的运行特性与效果

针对目前人工湿地运行中的水流分布不均、易堵塞、溶解氧不足导致NH4+-N硝化不充分及除磷率低下等问题,研究了作为复合人工湿地系统组成要素的高负荷水解酸化池、自然复氧/沉淀一体化装置、强化除磷脱氮槽等强化处理单元的运行特性及对全系统处理效果的影响.结果表明,高负荷水解酸化池对COD、SS有较强的去除作用,分别占系统总去除率的38.05%和34.82%;一体化装置对SS的去除占系统总去除率的22.01%,并使DO提高到2.5 mg·L-1以上;经两段强化除磷脱氮槽的强化处理,TP综合去除率提高8%以上,并使湿地出水各类污染物全面达到GB 18918-2002一级A标准.     

Abiotic degradation of four phthalic acid esters in aqueous phase under natural sunlight irradiation

Abiotic degradability of four phthalic acid esters (PAEs) in the aquatic phase was evaluated over a wide pH range 5–9. The PAE solutions in glass test tubes were placed either in the dark and under the natural sunlight irradiation for evaluating the degradation rate via hydrolysis or photolysis plus hydrolysis, respectively, at ambient temperature for 140 d from autumn to winter in Osaka, Japan. The e ciency of abiotic degradation of the PAEs with relatively short alkyl chains, such as butylbenzyl phthalate (BBP) and di-nbutyl phthalate (DBP), at neutral pH was significantly lower than that in the acidic or alkaline condition. Photolysis was considered to contribute mainly to the total abiotic degradation at all pH. Neither hydrolysis nor photolysis of di-ethylhexyl phthalate (DEHP) proceeded significantly at any pH, especially hydrolysis at neutral pH was negligible. On the other hand, the degradation rate of diisononyl phthalate (DINP) catalyzed mainly by photolysis was much higher than those of the other PAEs, and was almost completely removed during the experimental period at pH 5 and 9. As a whole, according to the half-life (t1=2) obtained in the experiments, the abiotic degradability of the PAEs was in the sequence: DINP (32–140 d) > DBP (50–360 d), BBP (58–480 d) > DEHP (390–1600 d) under sunlight irradiation (via photolysis plus hydrolysis). Although the abiotic degradation rates for BBP, DBP, and DEHP are much lower than the biodegradation rates reported, the photolysis rate for DINP is comparable to its biodegradation rate in the acidic or alkaline condition.     

Kinetic analysis of waste activated sludge hydrolysis and short-chain fatty acids production at pH 10

The accumulation of short-chain fatty acids (SCFAs), a preferred carbon source for enhanced biological phosphorus removal microbes, was significantly improved when waste activated sludge (WAS) was fermented at pH 10. The kinetics of WAS hydrolysis and SCFAs production at pH 10 were investigated. It was observed that during WAS anaerobic fermentation at pH 10 the accumulation of SCFAs was limited by the hydrolysis process, and both the hydrolysis of WAS particulate COD and the accumulation of SCFAs followed first-order kinetics. The hydrolysis and SCFAs accumulation rate constants increased with a increasing of temperature from 10 to 35℃, which could be described by the Arrhenius equation. The kinetic data further indicated that SCFAs production at pH 10 was a biological process. Compared with the experiment of pH uncontrolled (blank test), both the rate constants of WAS hydrolysis and SCFAs accumulation at 20℃ were significantly improved when WAS was fermented at pH 10.     

Enzymatic treatment of estrogens and estrogen glucuronide

Natural and synthetic estrogens from sewage treatment systems are suspected to influence the reproductive health of the animals in the rivers.In this article we investigated the enzymatic treatment of three estrogens (estrone,17β-estradiol,and 17α-ethynyletstradiol) by a fungal laccase which oxidize phenolic compounds with dissolved oxygen.The elimination of the estrogenic activities by enzymatic oxidation was demonstrated by medaka vitellogenin assay.In addition,we developed an enzymatic treatment system comprised of β-D-glucuronidase and the laccase for 17β-estradiol 3-(β-D-glucuronide) degradation.The two enzymes eliminated 17β-estradiol 3-(β-D-glucuronide) and the intermediate,17β-estradiol,efficiently.     

Combination eect of pH and acetate on enzymatic cellulose hydrolysis

The productivity and eciency of cellulase are significant in cellulose hydrolysis. With the accumulation of volatile fatty acids (VFAs), the pH value in anaerobic digestion system is reduced. Therefore, this study will find out how the pH and the amount of acetate inuence the enzymatic hydrolysis of cellulose. The eects of pH and acetate on cellulase produced from Bacillus coagulans were studied at various pH 5-8, and acetate concentrations (0-60 mmol/L). A batch kinetic model for enzymatic cellulose hydrol...     

混凝过程中铝盐水解聚合反应平衡的流体动力学控制

为了明确混凝过程中搅拌剪切等动力学因素对铝盐水解聚合反应平衡的影响,采用配制模拟水样作为混凝水系,用Ferron逐时络合比色法对水解产物形态进行表征,并将获取结果与用去离子水组成的纯净水系获取的结果进行对比分析.同时,研究了模拟混凝水系中搅拌剪切条件对铝盐水解反应产物形态分布的影响,考查了铝盐的碱化度和模拟混凝水系的pH值对混凝体系中搅拌剪切条件作用于铝盐水解产物形态分布的影响,并提出了体系搅拌剪切条件影响混凝水系中铝盐水解反应平衡的作用机理.结果表明,混凝过程中的铝盐水解产物形态分布明显受到体系搅拌剪切条件的影响,并且随着混凝水系中铝盐水解程度的增大和转化率的提高,铝盐的水解产物形态分布受到反应体系中搅拌剪切条件的影响加大.     

DO对水解酸化池与好氧MBR组合工艺运行效果的影响研究

针对溶解氧（DO）、气水比对水解酸化池与好氧MBR组合工艺处理污水效果的影响和能耗问题．从气水比对DO的影响,DO对COD与色度去除效果的影响等方面来讨论气水比,溶解氧以及污水处理效果之间的最佳运行点。试验结果表明。在P（MLSS）分别为5．81、4．25、2．19g／L的运行条件下,MBR的最佳气水比为39：1、28．1.18：1;DO变化速率随污泥浓度的下降而升高;DO的变化对COD、色度的去除效果影响并不显著。