Enhancement of Rhodobacter sphaeroides growth and carotenoid production through biostimulation

Bacillus thuringiensis/cereus L2 was added as a biostimulant to enhance the biomass accumulation and carotenoid yield of Rhodobacter sphaeroides using wastewater as the culturing medium. Results showed that biostimulation could significantly enhance the R. sphaeroides biomass production and carotenoid yield. The optimal biostimulant proportion was 40 μL(about 6.4 × 105CFU). Through the use of biostimulation, chemical oxygen demand removal, R. sphaeroides biomass production, carotenoid concentration, and carotenoid yield were improved by 178%, 67%, 214%, and 70%, respectively. Theoretical analysis revealed that there were two possible reasons for such increases. One was that biostimulation enhanced the R. sphaeroides wastewater treatment efficiency. The other was that biostimulation significantly decreased the peroxidase activity in R. sphaeroides. The results showed that the highest peroxidase activity dropped by 87% and the induction ratio of the RSP_3419 gene was 3.1 with the addition of biostimulant. The enhanced carotenoid yield in R. sphaeroides could thus be explained by a decrease in peroxidase activity.     

多环芳烃的几种理化参数与LC50的相关性研究

对多环芳烃（PAHs)4种理化参数（KOW、SW、^1X、Vg(r))与LC50的相关关系进行了研究，建立了4种一元线性回归方程。结果表明，4种参数的相关系数分别为：0.7266、0.8083、0.9488、0.9570，经r检验，后两种属高度显著相关。用所建立的一元线性回归方程对7种PAHs的LC50进行估算，估算值民实测值相比，平均相对误差分别为58.84%、32.23%、17.61%、19.8%，用^1X和Vg(r)对LC50进行估算的估算度也较高。经比较，提出用Vg(r)估算PAHs对麦穗鱼LC50的新方法。     

电除尘器气流分布数值计算方法研究

运用CFD方法对电除尘器内的气流流动进行数值计算,以相应的电除尘器气流分布模型试验为验证算例。数值计算采用多孔介质模型简化进口喇叭气流分布板,以第一电场进口断面的气流速度分布趋势及相对均方根值为评判标准,对比3种不同导流片布置方案的模型实测结果与数值计算结果。结果表明:各方案模拟结果与试验结果均吻合较好,最终布置方案的数值计算结果满足电除尘器设计要求。     

风景区环境噪声的模糊综合评价

通过对城市风景旅游公园内各不同功能的景点区进行环境噪声实测和对游人进行主观反应调查,运用模糊数学的原理,对公园环境噪声进行综合评价。在目前尚未对城市风景旅游公园建立专门的噪声标准的情况下,这一评价方法对正确评估城市风景旅游公园的声环境质量有积极的实用意义。     

Spectroscopic study on transformations of dissolved organic matter in coal-to-liquids wastewater under integrated chemical oxidation and biological treatment process

A large amount of wastewater containing various toxic organic contaminants is produced during coal-to-liquids process. In this study, several spectroscopic methods were used to monitor the transformation of organic pollutants during an integrated chemical oxidation and biological process. The results showed that the hydrophobic acid fraction increased after Fenton oxidation, which was likely due to the production of small-molecule organic acids. Soluble microbial products were generated during biological treatment processes,which were degraded after ozonation; meanwhile, the hydrophilic base and acid components increased. Ultraviolet-visible spectroscopic analysis indicated that peaks at the absorption wavelengths of 280 and 254 nm, which are associated with aromatic substances, were detected in the raw water. The aromatic substances were gradually removed, becoming undetectable after biological aeration filter(BAF) treatment. Fourier transform infrared spectroscopy analysis revealed that the functional groups of phenols;benzene, toluene, ethylbenzene, and xylene(BTEX); aromatic hydrocarbons; aliphatic acids;aldehydes; and esters were present in raw wastewater. The organic substances were oxidized into small molecules after Fenton treatment. Aromatic hydrocarbons were effectively removed through bioadsorption and biodegradation after BAF process.Biodegradable organic matter was reduced and finally became undetectable after anoxic–oxic treatment in combination with a membrane bioreactor. Four fluorescent components were fractionated and obtained via excitation–emission matrix parallel factor analysis(EEM-PARAFAC). Dissolved organic matter fractionation in conjunction with EEM-PARAFAC was able to monitor more precisely the evolution of characteristic organic contaminants.     

Effect of carbon source and nitrate concentration on denitrifying phosphorus removal by DPB sludge

Effect of added carbon source and nitrate concentration on the denitrifying phosphorus removal by DPB sludge was systematically studied using batch experiments, at the same time the variation of ORP was investigated.Results showed that the denitrifying and phosphorus uptake rate in anoxic phase increased with the high initial anaerobic carbon source addition. However once the initial COD concentration reached a certain level, which was in excess to the PHB saturation of poly-P bacteria, residual COD carried over to anoxic phase inhibited the subsequent denitrifying phosphorus uptake. Simultaneously, phosphate uptake continued until all nitrate was removed, following a slow endogenous release of phosphate. High nitrate concentration in anoxic phase increased the initial denitrffying phosphorus rate. Once the nitrate was exhausted, phosphate uptake changed to release. Moreover, the time of this turning point occurred later with the higher nitrate addition. On the other hand, through on-line monitoring the variation of the ORP with different initial COD concentration, it was found ORP could be used as a control parameter for phosphorus release, but it is impossible to utilize ORP for controlling the denitrificaion and anoxic phosphorus uptake operations.     

高压电晕与臭氧联用对不同结构染料脱色效果的比较研究

比较研究了高压电晕与臭氧联用对活性艳红X-3B(单偶氮)、活性艳蓝X-BR(蒽醌)、活性黑KN-GRRC(双偶氮)、酸性红ARL(单偶氮)、酸性蓝BRL(蒽醌)、酸性橙AGT(双偶氮)和分散蓝2BLN(蒽醌)7种染料模拟废水的脱色效果.结果显示,酸性橙AGT模拟废水的脱色速度较慢,而其他6种染料在15 min内都能完全脱色,这表明染料结构本身的差异决定了脱色效果;活性染料模拟废水的脱色效果优于酸性染料;蒽醌染料和单偶氮染料模拟废水的脱色效果明显好于双偶氮染料.     

UV/H2O2工艺降解水中双酚A影响因素的研究

研究了UV/H2O2工艺对双酚A(BPA)的降解效果及影响田素.结果表明,UV/H2O2工艺可以有效降解水体中BPA,降解过程符合一级反应动力学模型;紫外光强对BPA的降解速度影响较小;H2O2浓度对BPA的降解具有促进和抑制的双重作用;BPA初始浓度对BPA降解没有影响;在酸性条件下,有利于BPA降解;NO-3、Cl-、HCO-3对BPA降解有抑制作用;当HCO-3、NO-3、Cl-摩尔浓度均为5mmol/L时,对BPA降解的抑制程度为HCO-3>NO-3>Cl-.腐殖酸在低浓度时,促进BPA降解反应进行;在高浓度时,BPA的降解受到抑制.     

基于甲烷氧化菌的城镇污水厂尾水极限脱氮系统构建及机制

好氧甲烷耦合反硝化(AME-D)在城镇污水厂尾水深度脱氮方面具有巨大的应用潜力,研究采用改良型反硝化生物滤池,利用低浓度甲烷构建出AME-D极限脱氮系统.研究发现该系统在间歇式运行方式下,出水中总氮和氨氮的平均浓度能达到1.05 mg·L^-1和0.54 mg·L^-1,其平均去除率分别为94.77%和93.30%.拉曼光谱分析结果显示,由NO^-₃对称伸缩引起的峰明显消失,由醇COH面外弯曲或C—H面外弯曲振动吸收引起峰明显增强,甲烷被氧化形成的中间产物可能主要为醇类物质. 16S rRNA基因测序结果表明,系统中的甲烷氧化菌主要为Methylocystis(0.27%)、Methylosarcina(0.10%)和Methyloparacoccus(0.12%),反硝化菌主要为Pseudomonas(56.92%)、Paenibacillus(3.52%)和Lysinibacillus(3.00%),硝化菌主要为Nitrospira(0.1%),说明AME-D极限脱氮系统的脱氮功能是由好氧甲烷氧化菌、...     

预缺氧池配水比对Johannesburg工艺脱氮除磷效果的影响

以处理城市污水的中试规模Johannesburg工艺为对象,探讨不同配水比对预缺氧池的反硝化及Johannesburg工艺脱氮除磷效果的影响。在总HRT为12.86 h,预缺氧池HRT为0.6 h的条件下,当配水比分别为0%、10%、20%和30%时,预缺氧池硝酸盐去除率分别为37.67%、78.95%、87.62%和94.95%,对应的厌氧池磷酸盐浓度分别为8.72、19.37、16.1和12.99 mg/L。预缺氧池最佳配水比为10%,此时厌氧段释磷速率、好氧吸磷速率和缺氧吸磷速率分别为6.94、3.17和2.12 mg/(g MLSS·h),厌氧池中磷的最大浓度和污泥中的磷最大含量可达到19.37 mg/L和25.7 mg TP/g MLSS。出水COD、NH3-N、TN和TP等各项水质指标有80%以上的概率达到《城镇污水处理厂污染物排放标准(GB18918-2002)》一级A标准。