Application of electrochemical reactor divided by cellulosic membrane for optimized simultaneous removal of phenols,chromium, and ammonia from tannery effluents

The post treatment of simulated tannery wastewater was evaluated in an electrochemical oxidation process under galvanostatic conditions. A continuous flow reactor divided by a cellulosic membrane consisted of Ti/SnO₂–Sb anodes and iron cathodes was used. Central composite design and response surface methodology (RSM) were applied to investigate the effects of six operational parameters, namely initial concentration of total phenols (TPh), total chromium (TCr), total ammonia nitrogen (TAN), flow rate (Q), current intensity (I), and electrode surface area (A). Effectiveness of the innovative cellulosic membrane was proven by considerable pH variations in the anolyte and catholyte chambers. A faster removal rate was observed for TPh and TAN, followed by TCr. The treatment level was very sensitive to Q and I in the studied ranges. RSM showed the removal efficiencies of 78.14%, 63.42%, and 86.09% for TPh, TCr, and TAN, respectively, are achieved under optimal conditions with consumption of only 9.03 kWh m^?3 electrical energy. Chlorinated compounds such as chloroform, 2,4-dichlorophenol, and chlorobenzene were detected as the degradation intermediates. According to the obtained results, electrolysis in the divided cell with cellulosic membrane is a practical, cost-effective method for advanced treatment of tannery effluents.     

Residues of 14C‐γ‐HCH in paddy after dusting,and the fate of γ‐HCH during refining process of rice bran oil

Paddy (rice) plants were dusted with 10% HCH containing ¹⁴C‐Γ‐HCH, at the rate of 2.5 kg a.i./ha and ¹⁴C‐residues were determined in different fractions of rice. Rice bran (0.187 ppm) had more of ¹⁴C‐residues than grain (0.026 ppm) and husk (0.042 ppm). The rice bran oil contained 0.129 ppm HCH residues. While degumming, dewaxing, alkali refining and bleaching had no effect, deodorisation alone eliminated 99.5% of added ¹⁴C‐residues in rice bran the oil during refining process.     

湖泊沉积物中氨氧化微生物的amoA基因数量

采用定量PCR方法测定了4个湖泊沉积物中氨氧化微生物的amoA基因数量,并分析了其与环境因子之间的关系. 结果表明:小南湖AOA(氨氧化古菌)和AOB(氨氧化细菌)的amoA基因数量最多,分别达2.1×104和2.8×103copies/g(以干质量计,下同);梁子湖仅检测到了AOA amoA基因的存在,平均值为4.9×103copies/g. 东湖和汤逊湖的AOA amoA基因数量比较接近,约为3.0×103copies/g,然而AOB的amoA基因数量在这2个湖泊中仅分别为37和86copies/g;在这些采样点中,AOA的amoA基因数量是AOB的3~278倍. 统计分析发现,随着湖泊营养水平和间隙水中ρ(NH₄+)的上升,AOA和AOB的amoA基因数量均呈增加趋势,但ρ(NH₄+)增加对AOB的促进作用要大于AOA,导致AOA和AOB的amoA基因数量比值与间隙水中ρ(NH₄+)呈显著负相关. pH上升对2类氨氧化微生物的抑制作用则与ρ(NH₄+)增加对它们的促进作用相反. 沉积物中amoA基因数量与间隙水中ρ(NO₂-)无显著相关性,但与ρ(NO₃-)呈显著正相关. 由于ρ(NH₄+)与ρ(DO)之间呈显著负相关,因此认为ρ(DO)与氨氧化微生物amoA基因数量之间的显著负相关可能更多的是对ρ(NH₄+)与氨氧化微生物amoA基因数量之间紧密关系的一种间接反应.      

洱海表层沉积物中总氮含量及氨氮的释放特征

通过现场调查和室内模拟试验,对洱海具有代表性的9个表层沉积物样品中w(TN)的分布特征以及沉积物中NH₄+-N释放动力学特征进行了研究. 结果表明,洱海表层沉积物中w(TN)在2.0844～6.5153g/kg之间,平均值为3.5378g/kg,北部西岸为高值区,南部(靠近大理市)为次高值区. 一级动力学模型可很好地拟合洱海表层沉积物NH₄+-N释放动力学特征,NH₄+-N最大释放量在0.1209～0.2810g/kg之间;释放主要集中在0~5min内,约占最大释放量的68%~83%;随后释放速率逐渐放缓,到120min后基本达到释放平衡.运用无限稀释法对沉积物NH₄+-N释放潜能进行测定表明,洱海沉积物NH₄+-N释放潜能在1.7001~3.5879 g/kg之间,在水土质量比约为2500时,NH₄+-N释放量达到最大,随后释放逐渐趋于平衡. 洱海沉积物NH₄+-N释放潜能及最大释放量均与其w(TN)呈显著正相关. 洱海沉积物中w(TN)与NH₄+-N释放潜能和最大释放量均高于长江中下游湖泊,具有较大的氮释放风险.      

SDA脱硫工艺在烧结烟气脱硫中的应用

介绍了沙钢集团4号360 m2烧结机全烟气脱硫项目的工艺选择、脱硫原理、工艺流程及投产后生产情况,通过对生产后运行分析,认为旋转喷雾干燥法(SDA)作为一种新型的脱硫工艺,适合作为烧结烟气脱硫的主工艺进行推广。     

A comprehensive model to estimate the simultaneous release of acidic and basic gaseous pollutants from swine slurry under different scenarios

Swine slurry is a source of atmospheric pollutants. Emissions of basic and acidic compounds from slurry are largely dependent on the surface pH. In a storage system, the pH at the surface layers changes over time due to the volatilisation of ammonia (NH₃), carbon dioxide (CO₂) and acetic acid (HAc). In this article, a comprehensive gas emission–pH (GE–pH) coupled model is proposed to describe the simultaneous release of acidic and basic gaseous pollutants from swine slurry. The model was applied to describe the release of NH₃, CO₂, HAc and hydrogen sulphide (H₂S) from standard slurries stored in animal houses, outside storage tanks and lagoons. The modelled results agreed well with values reported in the literature and could be reasonably interpreted. The key parameters affecting the release of gases were: initial pH, initial concentration of total ammonium nitrogen and inorganic carbon, slurry temperature and air velocity. This study suggests that future modelling studies on gas emissions from animal slurry should consider the concentration of inorganic carbon and the frequency in which the slurry surface is mixed or altered, because they affect the surface pH and the release of gaseous pollutants from slurry.     

气浮-A~2/O~2工艺处理焦化废水

以玉田县古玉煤焦化工有限公司焦化废水处理站工程为例,介绍气浮-A2/O2工艺处理高浓度焦化废水的运行效果及工艺参数。运行结果表明:气浮-A2/O2工艺对焦化废水具有理想的处理效果,当进水ρ(COD)<3 500 mg/L、ρ(酚)<700 mg/L、ρ(氰化物)<20 mg/L、ρ(NH3-N)<300 mg/L时,出水ρ(COD)<100 mg/L、ρ(酚)<0.5mg/L、ρ(氰化物)<0.5 mg/L、ρ(NH3-N)<15 mg/L,各项指标均达设计要求,满足熄焦工段的用水要求和排放标准。     

A/O法处理水产品加工废水

采用A/O工艺处理水产品加工废水,处理量为500 t/d,运行两年来,效果稳定,处理结果表明:对COD、BOD5和氨氮的去除率分别为94.7%、98.1%和86.4%,出水达到GB 8978—1996《污水综合排放标准》中的一级排放标准,且该工艺具有运行费用低、处理效果好、操作管理方便等一系列优点。     

厌氧氨氧化工艺的抑制现象

厌氧氨氧化(Anammox)工艺因其高效低耗优势,在废水生物脱氮领域中具有广阔的应用前景.然而,基质、有机物、盐度、重金属、磷酸盐及硫化物等物质对Anammox工艺产生的抑制作用制约了工艺的推广应用.基质主要通过游离氨和游离亚硝酸对Anammox产生抑制,而温度和pH是基质抑制的重要调控参数.非致毒性有机物对Anammox的作用因其种类跟浓度而异.在较低的浓度条件下对Anammox的抑制作用不显著,而高于抑制阈值将严重抑制Anammox.其抑制机制尚无定论.部分研究证明致毒性有机物(醇、醛、酚及抗生素等)对Anammox具有抑制作用,但研究有待拓展深化.超过抑制阈值的盐度会抑制Anammox活性,但合适的盐度(3~15 g L-1NaCl)却能够促进Anammox生物颗粒的形成.重金属对Anammox的抑制报道较少.因试验条件及菌种等的差异使得磷酸盐及硫化物对Anammox的抑制在不同试验中存在很大差异.Anammox抑制是可控的,通过pH和温度调节、基质浓度及负荷控制、污泥驯化以及添加辅助剂等方法可解除或缓解抑制.建议今后在特种废水的Anammox脱氮、复合抑制以及Anammox抑制的分子生态学机理等方面开展深入研究.     

浅析混凝沉降实验研究与实际工艺的差异

介绍混凝沉降实验与实际沉降工艺各自的特点和存在的问题,从相似理论的角度出发,指出了玻璃量筒沉降实验和实际沉降工艺存在着几何尺寸、初始条件、运动条件三方面的不相似,较好地解释了两者的沉降速度和沉降效果的差异;并提出今后的混凝沉降实验应该进一步符合相似理论,从而更加合理地模拟实际沉降工艺.