Microwave-assisted stripping of oil contaminated drill cuttings

The application of microwave heating technology to conventional gas stripping processes has been investigated in the remediation of contaminated drill cuttings. The technical feasibility and limitations of nitrogen and steam stripping processes are demonstrated, and it is shown that the combination of microwave heating with the stripping process offers a step change in performance. Order of magnitude improvements in processing time are shown for the microwave-assisted processes, as well as greatly improved levels of remediation. The mechanisms of contaminant removal are discussed, along with the phenomena which occur with microwave heating processes. The energy requirements of each of pure gas and microwave-assisted processes are also discussed, and the potential applications of each technology are highlighted relative to the overall remediation requirements.     

微分脉冲阴极溶出伏安法测定环境水样中的痕量硒

采用微分脉冲阴极溶出法测定环境水样中的痕量硒,以银电极为工作电极,在酸性介质0.06mol.l^-1HCl-0.07mol.l^-1HNO3溶液中于－0.35V(vs SCE)处富集20min,使Se(IV)电沉积为硒化银,然后,以40mV.s^-1的扫速,在碱性介质2．0mol.l^-1NaOH溶液中阴极溶出至－1.2V(vsSCE),硒化银被还原为银的溶出峰电位约为－0.85V(vs SCE),硒的分析校正曲直到40ng.ml^-1仍然成线性,检测下限为11.5pg.ml^-1,相关系为0.9982,灵敏度为10.93uA/ng.ml^-1,20ng.ml^-1的RSD（n=5)为1．26％,检出限（3σ为3.46pg.ml^-1,环境水样中常见离子的存在不干扰痕量硒的测定。     

吹脱-沸石吸附法处理荧光粉生产废水研究

研究了吹脱-沸石吸附法处理荧光粉生产废水.正交试验结果表明:氨吹脱工艺中影响NH3-N去除率因素的重要性顺序为:pH＞温度＞气液比.当pH=11、气液比(V/V)=100:1、温度T=40℃、吹脱时间t=120 min,吹脱工艺对荧光粉生产废水中NH3-N的去除率为74.46%.试验确定的沸石吸附单元较佳的工艺参数为:滤速0.04 m/min、接触时间14min、pH=7.5,吹脱-沸石吸附工艺总NH3-N去除率96.04%.试验结果表明再生沸石氨吸附性能稳定,适于高氨氮的荧光粉生产废水处理.     

吹脱法处理高浓度氨氮废水的研究

通过对盘锦某催化剂厂在生产催化剂过程中产生的高浓度氨氮废水静态吹脱试验，总结出水温、pH、水力停留时间、气水比、1号脱氮剂用量等相关参数对吹脱效率的影响。     

Acute and sub-lethal toxicity of landfill leachate towards two aquatic macro-invertebrates: demonstrating the remediation potential of air stripping

A specific leachate that contained 1.036 mg l(-1) of 2-chlorobiphenyl was used in the study (255 mg l(-1) COD and 133 mg l(-1) BOD5). Bench scale (20 l) air stripping trials were used to simulate on a small-scale the treatment potential of this method. Air stripping effectively reduced the leachates COD concentration. Regardless of the volume of air supplied (1-5 l of air per minute) the leachates COD reached a <50 mg l(-1) equilibrium after 96-h exposure, however, increasing the volume of air accelerated the process. In untreated leachate, the LC50 for Asellus aquaticus was 57% v/v leachate in deionised water and 5% for Gammarus pulex (96-h, static LC50 tests without nutrition and oxygen depleting conditions). After being exposed to air stripping, these values rose from 90% to below the LC50 threshold for Asellus when 1-5 l of air per minute were applied and 30-90% for Gammarus. Furthermore, in sub-lethal concentrations of air stripped leachate (leachate that had been exposed to 5-l of air per minute for 96-h) the population dynamics of both test species remained unaltered.     

Evaluation of Mass-Transfer Coefficient of Free Fall – Cascade-Aerator

The mass-transfer coefficient of a free-fall cascade-aeratorunit of 15 million litres per day was evaluated for its efficiency in the removal of a class of volatile organics, the trihalomethanes(THMs). These compounds are carcinogenic and occur as a resultof chlorination of natural waters. Due to the volatile nature ofthe THMs, the efficiency of aeration as a potential techniquefor their removal has been studied. The principle behindaeration is gas-transfer, according to which the gas-liquidinterface is hypothesized to consist of a gas and liquid filmthrough which gas is transferred by molecular diffusion untilequilibrium is attained. The overall mass transfer coefficient(K _L) of the aerator considering oxygen as the reference compound, was found to be29.3 hr^-1 for THMs.     

PCB企业退焊锡废液治理再生研究

该文提出用巯基沉淀剂来沉淀硝酸型退铅锡废水中的重金属离子(Cu,Fe,Pb,Sn),实验结果表明,适宜的沉淀条件为:在搅拌下将巯基沉淀剂P按理论量加入,同时按每升废液通入还原性添加剂二氧化硫12 g和3～5 mL,1%(W/W)PAM(分子量为400 000)絮凝剂,沉淀过滤后其退锡速度和退锡容量等性能与原退锡液无异,该工艺可使PCB企业的退铅锡废水实现循环使用。      

浅析露天矿土地复恳中应注意的几个问题

通过分析我国露天矿土地复垦现状,本文着重进行了问题探讨,从复垦技术,综合利用及经济补偿等方面提出一些新措施,以促进土地复垦,使生态、经济和社会三效益统一。     

气流与第三方物质交互解吸高浓度氨氮废水的研究

利用填料塔作为吹脱解吸设备,结合表面活性剂增强传质的特点,选取表面活性剂作为第三方物质,以空气作为气流吹脱解吸废水中的高浓度氨氮。实验研究了废水温度T、pH值、气液比n、表面活性剂种类和投加量ρ等条件变化对氨氮解吸效率η的影响。结果表明:加入表面活性剂X后,氨氮脱除效率提高2%;影响解吸效率因素的主次顺序为pH>T>n>ρ;最佳操作条件为T=80℃、pH=11.0、ρ=15 mg/L、n=650:1。在最佳的操作条件下,处理氨氮含量为2 159.0 mg/L和3 680.5 mg/L的废水时,解吸效率分别达到95.28%和94.69%,即废水最终的氨氮浓度为102.0 mg/L和195.5 mg/L,低于废水后续生化处理进水指标中对氨氮含量的要求。     

微电解-电/Fenton-曝气池工艺预处理高浓度亚麻废水

高浓度亚麻废水不宜直接进行生化处理。试验采用"Fe-C柱微电解-电/Fenton-曝气池"工艺对其进行预处理,即先采用Fe/C微电解,然后基于Fe2+的生成几乎同步引入电/Fenton反应,之后再调节流出液pH至碱性并鼓入空气以除去部分NH3-N。相应优化工艺条件为:Fe/C柱微电解时mFe/mC为2:1,废水停留时间为1.5 h;电/Fenton时双氧水(30%)滴加速度为0.025 mL/min;调节水样pH10并在空气流速为1.5 L/min的条件下空气吹脱1.5 h。采用该工艺预处理高浓度亚麻废水后,出水几乎为无色;固体悬浮物的去除率可达94.2%,NH3-N去除率可达71.4%,COD去除率可达51.8%,BOD5去除率可达28.3%,为后续生化深度处理创造了有利条件;BOD5/COD值由原来的0.12上升至0.19,废水的可生化性得到较明显的改善。电/Fenton反应的处理效果好于普通的Fenton反应,其原因可能是由于电/Fenton既有"原位"的均相/非均相Fenton反应发生,又有在微电解电场协助下的"电催化Fenton"反应发生。