高浓度制药废水处理技术的研发及应用

制药废水组成复杂,污染物浓度高,污水CODcr浓度达10000mg/l,含有大量有毒、有害物质。本中采用催化氧化预处理+水解酸化+UASB+接触氧化+炭滤吸附的工艺流程,通过改善细部参数及改良配套设备设计,提高了各单元去除效率,降低了能耗及处理成本,出水CODcr浓度达到污水综合排放标准.     

零价铁还原和吸附去除水中污染物的研究进展

近年来,零价铁以其低毒、廉价、易操作且对环境不会产生二次污染等优点,在水污染治理中受到重视。文章介绍了零价铁处理污水的机理,对利用零价铁的还原和吸附作用去除污水中的氯代有机物、硝基芳香族化合物、偶氮染料、重金属、高氯酸盐、硝酸盐等的研究情况进行了综述,指出了零价铁废水处理技术的研究方向。     

铁阳极电解脱色直接黄11染料模拟废水

研究采用铁为阳极电化学法处理直接黄11染料模拟废水脱色性能的影响进行研究。影响因素包括:电流密度、pH值、染料浓度和电解质浓度。研究结果表明,电流密度大有利于染料废水脱色,但能耗消耗大;初始溶液在中性条件下不仅取得很好的处理效果,而且脱色能耗较低;随着染料初始浓度增加脱色率和脱色能耗降低的趋势;随着电解质浓度升高染料脱色率下降的趋势,脱色能耗先减少,然后缓慢增大。在染料初始浓度50 mg/L、pH值为7.11、电流密度2.083 mA/cm2、电解质Na2SO4浓度0.01 mol/L、温度20℃、搅拌速度600 r/min、电解时间60min条件下,脱色率达到92.2%,脱色能耗1.709 kW.h/kg染料。     

城镇生活污水厂实行清洁生产途径分析

结合企业清洁生产理论,根据污水处理厂实际情况,从“节能、降耗、减排、增效”出发,详细阐述了污水厂实行清洁生产的途径。指出节约电能、新鲜水、药剂,减少污染物排放是污水处理厂清洁生产的主要出发点。并进行实例分析。     

生物沸石对吡啶、喹啉的降解与吸附作用

探讨了通过生物沸石的降解及吸附作用,解决吡啶、喹啉及转化产物NH 4+-N的污染问题.结果表明,生物沸石中的吡啶降解菌Shinella zoogloeoides BC026及喹啉降解菌Pseudomonas sp.BW003能有效去除吡啶、喹啉,同时转化后的NH 4+-N也能被天然沸石或改性沸石所吸附.尽管改性沸石吸附能力不如天然沸石,但其表面能更有效附着微生物,在实际工程应用上更具前景.     

沼液复合型杀虫剂的田间应用试验研究

通过沼液复合型杀虫剂的田间应用试验,对各种沼液复合型杀虫剂的抗病防虫性能进行了深入研究.在大田应用条件下测试了沼液复合型杀虫剂的杀虫效果.结果表明,该沼液复合型杀虫剂对蚜虫的毒杀作用均比较明显.为了推进沼液复合型杀虫剂的商业化进程,提出便于其田间应用的各种最佳配比浓度,即BP01号、BP02号、BP03号、BP04号、BP05号沼液复合型杀虫剂抗病防虫性能最佳的配比分别为9 500倍液、26000倍液、11 667倍液、22 000倍液和13 333倍液.     

有机化改性海泡石对六六六吸附性能的探讨

分别采用阴阳离子表面活性剂对海泡石进行有机化改性处理,并对改性海泡石进行了吸附六六六实验.结果表明,未经有机化改性的海泡石对六六六各异构体去除能力由小到大依次为:γ-六六六(12.66%)、δ-六六六(12.79%)、α六六六(17.35%)、β-六六六(33.57%).经DOSO3Na有机化改性的海泡石对六六六各异构体的去除能力由小到大依次为:β-六六六、γ δ-六六六、α-六六六.经CTMAB有机化改性的海泡石对六六六各异构体的去除能力由小到大依次为:β-六六六、α-六六六、γ δ-六六六.有机化改性海泡石使体系中β-六六六大幅度增加,可能为有机化海泡石催化α、γ、δ各异构体向β异构体转化.     

Experimental investigation of the e ect of flow turbulence and sediment transport patterns on the adsorption of cadmium ions onto sediment particles

The mechanism of flow turbulence,sediment supply conditions,and sediment transport patterns that affect the adsorption of cadmiumions onto sediment particles in natural waters are experimentally simulated and studied both in batch reactors and in a turbulencesimulation tank.By changing the agitation conditions,the sediment transport in batch reactors can be categorized into bottom sediment-dominated sediment and suspended sediment-dominated sediment.It is found that the adsorption rate of bottom sediment is much lessthan that of suspended sediment,but the sediment transport pattern does not affect the final(equilibrium)concentration of dissolvedcadmium.This result indicates that the parameters of an adsorption isotherm are the same regardless of the sediment transport pattern.Inthe turbulence simulation tank,the turbulence is generated by harmonic grid-stirred motions,and the turbulence intensity is quantifiedin terms of eddy diffusivity,which is equal to 9.84F(F is the harmonic vibration frequency)and is comparable to natural surfacewater conditions.When the turbulence intensity of flow is low and sediment particles stay as bottom sediment,the adsorption rateis significantly low,and the adsorption quantity compared with that of suspended sediment is negligible in the 6 h duration of theexperiment.This result greatly favors the simplification of the numerical modeling of heavy metal pollutant transformation in naturalrivers.When the turbulence intensity is high but bottom sediment persists,the rate and extent of descent of the dissolved cadmiumconcentration in the tank noticeably increase,and the time that is required to reach adsorption equilibrium also increases considerablydue to the continuous exchange that occurs between the suspended sediment and the bottom sediment.A comparison of the results ofthe experiments in the batch reactor and those in the turbulence simulation tank reveals that the adsorption ability of the sediment,andin particular the adsorption rate,is greatly over-estimated in the batch reactor.     

Kinetics of selective catalytic reduction of NO by NH3 on Fe-Mo/ZSM-5 catalyst

The catalyst of Fe-Mo/ZSM-5 has been found to be more active than Fe-ZSM-5 and Mo/ZSM-5 separately for selective catalytic reduction (SCR) of nitric oxide (NO) with NH3. The kinetics of the SCR reaction in the presence of O2 was studied in this work. The results show that the observed reaction orders were 0.74-0.99, 0.01-0.13, and 0 for NO, O2 and NH3, respectively, at 350-450℃. And the apparent activation energy of the SCR was 65 kJ/mol on the Fe-Mo/ZSM-5 catalyst. The SCR mechanism was also deduced. Adsorbed NO species can react directly with adsorbed ammonia species on the active sites to form N2 and H2O. Gaseous O2 might serve as a reoxidizing agent for the active sites that have undergone reduction in the SCR process. It is also important to note that a certain amount of NO was decomposed directly over the Fe-Mo/ZSM-5 catalyst in the absence of NH3.     

铅在棉秆基活性炭上的吸附动力学与热力学

以棉秆与棉秆纤维为原料,利用磷酸活化法制备了低成本的高比表面微孔棉秆基活性炭,通过静态实验研究了活性炭对水溶液中铅的吸附特性,测定了溶液pH值、吸附时间、溶液温度对吸附的影响,探讨了吸附动力学、热力学及吸附机制.根据低温液氮(N2/77K)吸附测定数据,以BET方程、BJH法及H-K法对活性炭孔结构进行了表征,以Boehm滴定、FTIR、零电荷点pHPZC测定及元素分析定量表征活性炭表面含氧官能团.结果表明,以棉秆和棉秆纤维为原料制备的活性炭的比表面积分别为1570和1731m2·g-1,含氧酸官能团含量分别为1.43和0.83mmol·g-1,均高于商业活性炭ST1300.静态吸附实验表明,棉秆基活性炭对铅有较大的吸附容量和吸附效率,最大吸附量超过120mg·g-1,溶液pH对吸附有较大的影响,吸附量随时间增大而增大,在5min内可达饱和吸附量的80%;吸附动力学数据符合假二级方程,Freundlich方程能更好地描述等温吸附行为;热力学研究表明,吸附吉布斯自由能(ΔG0)0,而焓变(ΔH0)0,说明吸附为吸热的自发反应过程,升温有利于吸附,离子交换可能在吸附过程中起了重要作用.