Cost-performance analysis of nutrient removal in a full-scale oxidation ditch process based on kinetic modeling

A full-scale oxidation ditch process for treating sewage was simulated with the ASM2d model and optimized for minimal cost with acceptable performance in terms of ammonium and phosphorus removal. A unified index was introduced by integrating operational costs (aeration energy and sludge production) with effluent violations for performance evaluation. Scenario analysis showed that,in comparison with the baseline (all of the 9 aerators activated), the strategy of activating 5 aerators could save aeration energy significantly with an ammonium violation below 10%. Sludge discharge scenario analysis showed that a sludge discharge flow of 250–300 m3/day (solid retention time (SRT), 13–15 days) was appropriate for the enhancement of phosphorus removal without excessive sludge production. The proposed optimal control strategy was: activating 5 rotating disks operated with a mode of "111100100" ( "1"represents activation and "0" represents inactivation) for aeration and sludge discharge flow of 200 m3/day (SRT, 19 days). Compared with the baseline, this strategy could achieve ammonium violation below 10% and TP violation below 30% with substantial reduction of aeration energy cost (46%) and minimal increment of sludge production (< 2%). This study provides a useful approach for the optimization of process operation and control.     

短程硝化颗粒污泥的快速培养与硝化特性研究

以城市污水处理厂剩余污泥为种泥,以2 min沉淀时间为选择压,在序批式反应器(SBR)中快速培养出好氧颗粒污泥。经过60个周期(20 d),反应器内出现砂粒状颗粒,并持续稳定运行120 d。成熟的颗粒污泥平均粒径856.56μm,具有良好的硝化性能。SBR反应器以固定曝气时间方式运行,亚硝酸盐积累率达80%以上,实现了稳定短程硝化。试验结果表明:絮体污泥(即接种污泥)与颗粒污泥的硝化过程相似但略有差异。二者差别在于,氨氮氧化结束后,继续曝气120 min,絮体污泥将亚硝酸盐完全转化为硝酸盐,而颗粒污泥仅将部分亚硝酸盐转化且过程比较缓慢。     

餐厨垃圾与污水污泥共消化产酸试验研究

研究了餐厨垃圾与污水污泥在不同混合比例、不同污泥停留时间条件下的共消化产酸效果。试验结果表明:当餐厨垃圾与污水污泥TS比为1∶3时,SRT=1 d的反应器酸化效率最高,且乙酸含量占优,产酸效果较佳;当TS之比为1∶1时,各反应器产酸量普遍高于1∶3时,其中SRT=5 d产酸反应器,最高酸化效率达5.94,产酸量最大,且乙酸含量占优,运行效果最佳。     

废弃SCR脱硝催化剂的再生及其脱硝性能研究

对废弃脱硝催化剂处理后重新加工再生,研究了添加剂对其粉体成型和再生催化剂脱硝活性的影响,探讨了反应温度、空速、n(NH3)∶n(NO)摩尔比、氧含量、H2O和SO2对再生催化剂NH3选择性催化还原(SCR)NO的影响。结果表明:最佳再生条件是使用5%羧甲基纤维素和10%无机粘结剂辅助成型;废弃催化剂再生利用率高达90%;再生催化剂抗压强度为4.73 MPa,优于商用催化剂;空速5 000 h-1、氨氮摩尔比1、氧含量6%时,脱硝活性温度窗口为310⁴50℃,350℃时活性最高为94%;350℃时,单独通入1 000×10-6SO2或10%H2O对再生催化剂活性均有一定抑制作用,最低活性分别为70%和81%,停止通入SO2或H2O后其活性逐渐恢复;同时通入1 000×10-6SO2和10%H2O,再生催化剂活性下降至63%并于1 h内保持相对稳定,停止通入SO2和H2O 2 h后,活性逐渐恢复到73%。     

改性凹凸棒土吸附地下水中硝基苯的实验研究

从凹凸棒土(以下简称凹土)的有机改性入手,研究凹土的十六烷基三甲基溴化铵(CTAB)、十八烷基三甲基氯化铵(OTAC)改性及吸附模拟硝基苯(nitrobenzene,NB)污染地下水的影响因素及性能。结果表明:采用超声改性法制得的CTAB、OTAC改性凹土对地下水中NB具有较强的吸附能力,每100g凹土改性剂最佳用量为30 mmol。在NB浓度为20mg/L、投加量为4%、吸附时间30 min的条件下,NB吸附去除率分别达45.68%、55.40%;改性凹土的静态吸附行为符合Langmuir吸附等温方程。     

悬浮膜(CFM)分离技术在油田废水处理中的应用

应用微电解等技术对油田废水进行预处理,然后用悬浮膜进行分离,使其中的油、微生物和固体物与水相分离,使其达到回注用水要求。重点对CFM分离设备的结构及原理加以介绍,以期推进过滤技术的进步,提高油田废水的处理水平。     

基于臭氧溶胞的活性污泥减量化技术

目前常见的活性污泥减量技术主要包括解偶联技术、微生物的捕食作用以及隐性生长三种方法。基于臭氧氧化溶胞作用从而强化细菌隐性生长的污泥减量技术具有较好的处理效果及良好的应用前景。着重探讨了臭氧溶胞作用的机理及溶胞过程的影响因素。考虑到污泥减量技术在实际污水处理系统中的应用,探讨了臭氧溶胞对污水生物处理系统的影响。     

含铬废水的处理技术及机理简述

介绍了废水中六价铬的来源及存在形态,以及处理含铬废水的物理、物化、化学及生物等各种工艺,并对各种工艺的机理和优缺点进行分析,展望含铬废水的治理前景。     

Biodegradation of 2-methylquinoline by Enterobacter aerogenes TJ-D isolated from activated sludge

Bacterial strain Enterobacter aerogenes TJ-D capable of utilizing 2-methylquinoline as the sole carbon and energy source was isolated from acclimated activated sludge under denitrifying conditions. The ability to degrade 2-methylquinoline by E. aerogenes TJ-D was investigated under denitrifying conditions. Under optimal conditions of temperature (35℃) and initial pH 7, 2-methylquinoline of 100 mg/L was degraded within 176 hr. The degradation of 2-methylquinoline by E. aerogenes TJ-D could be well described by the Haldane model (R² > 0.91). During the degradation period of 2-methylquinoline (initial concentration 100 mg/L), nitrate was almost completely consumed (the removal efficiency was 98.5%), while nitrite remained at low concentration (< 0.62 mg/L) during the whole denitrification period. 1,2,3,4-Tetrahydro-2-methylquinoline, 4-ethyl-benzenamine, N-butyl-benzenamine, N-ethyl-benzenamine and 2,6-diethyl-benzenamine were metabolites produced during the degradation. The degradation pathway of 2-methylquinoline by E. aerogenes TJ-D was proposed. 2-Methylquinoline is initially hydroxylated at C-4 to form 2-methyl-4-hydroxy-quinoline, and then forms 2-methyl-4-quinolinol as a result of tautomerism. Hydrogenation of the heterocyclic ring at positions 2 and 3 produces 2,3-dihydro-2-methyl-4-quinolinol. The carbon-carbon bond at position 2 and 3 in the heterocyclic ring may cleave and form 2-ethyl-N-ethyl-benzenamine. Tautomerism may result in the formation of 2,6-diethyl-benzenamine and N-butyl-benzenamine. 4-Ethyl-benzenamine and N-ethyl-benzenamine were produced as a result of losing one ethyl group from the above molecules.     

烟气脱硫装置增容改造技术探讨

国内大量石灰石-石膏湿法烟气脱硫装置需进行增容改造,介绍了增容改造的主要方案及各方案的应用案例,分析了方案选择的影响因素,总结了增容改造的主要特点,提出了改造项目的建议,为火电机组的脱硫增容改造提供借鉴。