Recovery of Ni(II) from real electroplating wastewater using fixed-bed resin adsorption and subsequent electrodeposition

Resin adsorption and subsequent electrodeposition were used for nickel recovery. Treated wastewater can meet the Electroplating Pollutant Discharge Standard. The spent resin is completely regenerated by 3 BV of 4% HCl solution. 95.6% of nickel in concentrated eluent was recovered by electrodeposition. Effective recovery of high-value heavy metals from electroplating wastewater is of great significance, but recovering nickel ions from real electroplating wastewater as nickel sheet has not been reported. In this study, the pilot-scale fixed-bed resin adsorption was conducted to recover Ni(II) ions from real nickel plating wastewater, and then the concentrated Ni(II) ions in the regenerated solution were reduced to nickel sheet via electrodeposition. A commercial cation-exchange resin was selected and the optimal resin adsorption and regeneration conditions were investigated. The resin exhibited an adsorption capacity of 63 mg/g for Ni(II) ions, and the average amount of treated water was 84.6 bed volumes (BV) in the pilot-scale experiments. After the adsorption by two ion-exchange resin columns in series and one chelating resin column, the concentrations of Ni(II) in the treated wastewater were below 0.1 mg/L. After the regeneration of the spent resin using 3 BV of 4% (w/w) HCl solution, 1.5 BV of concentrated neutral nickel solution (>30 g/L) was obtained and used in the subsequent electrodeposition process. Using the aeration method, alkali and water required in resin activation process were greatly reduced to 2 BV and 3 BV, respectively. Under the optimal electrodeposition conditions, 95.6% of Ni(II) in desorption eluent could be recovered as the elemental nickel on the cathode. The total treatment cost for the resin adsorption and regeneration as well as the electrodeposition was calculated.     

Reconsideration on the effect of nitrogen on mixed culture polyhydroxyalkanoate production toward high organic loading enrichment history

Effect of nitrogen on mixed culture PHA production was reconsidered. Enrichment history of PHA accumulating culture was discussed. Higher PHA content and biomass growth were achieved in presence of nitrogen. Enrichment strategy toward higher PHA accumulation was investigated. Microbial community succession in PHA accumulation phase was investigated. In most of the operating strategies for mixed microbial cultures polyhydroxyalkanoate (PHA) production, moderate organic loads and low nitrogen concentrations are used, however, the real waste streams contain variable concentrations of carbon and nitrogen. To evaluate the effect of enrichment history on PHA producer and production the various carbon and nitrogen levels were utilized during the accumulation phase. Different operating strategies were applied in three sequencing batch reactors (SBRs) subjected to aerobic dynamic feeding. The maximum PHA production of the enriched cultures under nutrient excess, limitation and starvation (Cmol/Nmol ratio of 8, 40 and ∞, respectively) was evaluated in batch assays. A higher PHA content and biomass growth were achieved in the nutrients presence in comparison to the nutrient starvation condition. The cultures from the SBR treated under short sludge retention time, high organic loading rate, short cycle length (SBR#3) and nutrient excess reached the maximum PHA content (54.9%) and biomass increase (38.9%). Under nutrient limitation, the negative biomass growth was observed under nutrient starvation because of the sampling loss. The succession of microbial communities in SBRs and batch assays was analyzed using terminal restriction fragment length polymorphism. The SBR#3 had the best overall PHA production performance considering its high PHA content and productivity in all nutrient content, it indicates that nitrogen has a substantial impact on PHA yield especially when high organic loading rate enrichment history is involved.     

Effects of intercropping with floricultural accumulator plants on cadmium accumulation in grapevine

Environmental Science and Pollution Research - Grapevine (Vitis vinifera L.) intercropping with floricultural cadmium (Cd) accumulator plants (Helianthus annuus L., Cosmos sulphureus Cav., Cosmos...     

南海莺琼盆地沉积环境中厌氧纤维素分解菌的分布与作用

在严格厌氧条件下，研究了驾琼盆地东方１－１－１井垂直剖面不同沉积层地质样品中的厌氧纤维素分解菌．结果表明：厌氧纤维素分解菌在各样品中都存在，但其分布有很大随机性，与样品埋藏深度无相关性，与样品中一些有机物含量，如纤维素、半纤维素也无相关性，厌氧纤维素分解菌数量高的样品，其在生物模拟产甲烷实验中的单位有机质产气量也较高，有显著的相关性．菌体形态主要为杆菌和球菌．     

絮凝浮选剂PS-01的研究

为了提高油田采油（气）污水处理能力,胜利油田开发研制出新型絮凝浮选剂ＰＳ－０１,以聚合铝为主,配以常用的助凝剂二氧化硅气溶胶,工业用硫酸镁等,按比例混合在一起配置而成。在试验中将它们与油田内广泛使用的絮凝浮选剂ＳＧ－０１,ＪＸ－０１,ＮＡ－１等进行比较。结果表明：ＰＳ－０１絮凝浮选剂的原料来源广泛,合成工艺简单,易于操作;对采油（气）污水处理效果好,加药量少,处理成本低;应用的ｐＨ范围较宽,反应迅速,可缩短混合反应时间;适用性强,低温时效果不受影响;对投药设备的腐蚀性小,性质稳定,无沉淀产生;同时各种原料的不同配比对絮凝浮选效果影响很大,要控制好比例。     

分光光度法测定COD_(Cr)的试验条件选择

用分光光度法测定水中化学需氧量ＣＯＤＣｒ,通过正交试验选择氧化的最佳选择。试验结果表明对ＣＯＤＣｒ值为５０～１０００ｍｇ／Ｌ的水样：氧化剂Ｋ２Ｃｒ２Ｏ７用量为０．２０～０．４０ｍｏｌ／Ｌ,催化剂Ａｇ２ＳＯ４用量为１０ｇ／ＬＨ２ＳＯ４,消解时间１０ｍｉｎ,加热温度１８０℃。用ＣＯＤＣｒ为１３８ｍｇ／Ｌ的质控标样进行验证试验,其绝对误差为０．５～３．０ｍｇ／Ｌ。与标准方法相比用分光光度法测定ＣＯＤＣｒ具有分析误差小,省时、省力,节约药剂的特点。     

MB1870型球磨机噪声治理

球磨机运转时噪声很大,不仅生产操作时工人难以承受,而且对周围居民的生活环境造成严重污染.我们采用约束型粘弹阻尼结构减震,并结合吸声、隔声和消声技术进行综合治理,取得了良好的降噪效果.     

危机管理体制构建与政府职能转变--后非典时期对于突发公共灾害处置的思考

本文以公共卫生危机和社会突发事件为个案,以政府面对这些危机所面临的挑战和取得的经验为研究对象,分析公共危机产生的原因和基本特征,提出了面对公共危机时应建立政府危机管理的预警系统,建立快速反应机制,动员社会参与危机救治,加强信息流通,加强公共危机的法制化建设.     

废水的生物脱氮除磷新工艺的设想

结合废水生物脱氮除磷机理和影响因素，在对几种典型脱氮除磷工艺氮、磷去除率进行比较的基础上，解析了一些典型工艺除氮除磷不足之处。根据重庆城市污水水质实际情况和地形的特点，设想一种新的生物脱 氮除磷工艺，从而弥补传统工艺的不足。可望提高系统的脱氮和除磷效率，达到更好的脱氮除磷的目的，减少对水体的污染。     

超临界水氧化有机废水动力学分析

根据推流式超临界水氧化 (SCWO)反应器处理有机废水的动力学方程式 ,结合近年来超临界水氧化降解各种有机废水的实验研究情况 ,对超临界水氧化有机废水的反应动力学影响因素进行了综合分析 ,同时指出了该技术在有机废水处理中的应用优势和存在问题。