活性炭纤维对Cu2＋吸附性能的研究

研究了pH值、吸附接触时间、铜离子的初始浓度及活性炭纤维（ACF）的投加量对活性炭纤维吸附Cu2＋的影响，并选取了最佳的实验条件。用Langmuir方程和Freundlich方程拟合活性炭纤维对Cu2＋吸附等温线，结果表明：活性炭纤维吸附Cu2＋更符合Langmuir等温式，其相关系数为0．9995，以单分子层吸附为主。对活性炭纤维改性能明显提高对Cu2＋的吸附，其中效果最佳的吸附量从4．8mg／g增加到17．32mg／g，提高了3．6倍。     

改性沸石用于饮用水除氟的试验研究

试验针对存在的氟污染饮用水问题,将天然沸石用NaOH和Al2（SO4）3溶液改性制成除氟材料.静态试验研究表明：改性沸石除氟吸附反应快,其最佳pH值范围为5～9,而且对氟离子具有较好的离子选择性能.通过动态试验研究发现,降低进水流量和原水浓度可以增大滤层的吸附容量.两种再生方式对比试验表明：用Al2（SO4）3溶液再生效果优于用NaOH和Al2（SO4）3溶液联合再生.     

水处理用活性炭改性研究

利用锆和氯化十六烷基三甲铵共同改性活性炭,制备一种新型去除污水中硝酸盐和磷酸盐的水处理吸附剂,并考察吸附剂加量、反应温度、pH值、共存阴离子等影响因素对吸附效果的影响。结果表明:锆-氯化十六烷基三甲铵改性活性炭(Zr-CTAC-AC)吸附剂适用于硝酸盐和磷酸盐浓度在100mg/L以下的污水,随着Zr-CTAC-AC加量的增加,硝酸盐、磷酸盐去除率逐渐增加,单位吸附量逐渐下降,Zr-CTAC-AC加量为8g/L时,硝酸盐去除率为79%,Zr-CTAC-AC加量为4.0g/L时,磷酸盐去除率可达91%,但应在较低的pH值范围内使用;反应温度对Zr-CTAC-AC的吸附效果影响不大;共存Cl-、HCO3^-和SO4^2-可使硝酸盐的吸附率降低,但对磷酸盐吸附率影响较小;1mol/L NaCl溶液可使吸附到Zr-CTAC-AC表面的硝酸盐90.9%左右被解吸出来,1mol/L NaOH溶液可使吸附到Zr-CTAC-AC表面的磷酸盐78.4%左右被解吸出来。Zr-CTAC-AC能够有效去除污水中硝酸盐和磷酸盐,制备方法简单,且可循环利用,处理成本低。     

针铁矿吸附去除水中锑特性研究

针铁矿是土壤和沉积物中的重要成分,能够有效地影响环境中有毒物质的迁移和转化。实验以水中Sb(V)为目标污染物,以针铁矿为吸附剂,分析吸附的影响因素和吸附动力学,探讨在不同p H、离子强度、磷酸根浓度条件下针铁矿对Sb(V)的吸附特性。结果表明,准二级动力学方程和Elovich模型能够较好地描述Sb(V)在针铁矿上的吸附动力学特性;针铁矿对Sb(V)吸附性能随p H值的增大而减小,随离子强度的升高而降低;磷酸根与Sb(V)在针铁矿表面发生竞争吸附,加速Sb(V)向水体中的迁移。实验结果表明,针铁矿吸附去除水中锑(Ⅴ)领域有实际应用的潜力。     

牛粪生物炭对水中磷的吸附特性及其影响因素研究

以牛粪生物炭为吸附剂,通过静态吸附实验研究牛粪生物炭对磷的吸附特性。研究了pH值、投加量等对牛粪生物炭吸附磷的影响。结果表明,牛粪生物炭吸附磷的最佳初始pH值为6.0;当投加量为0.1 g时,对磷的去除较为理想;通过对动力学数据进行分析,发现准二级动力学(R~2=0.999)比准一级动力学方程(R~2=0.5 886)和Elovich方程(R~2=0.927)能更好的拟合动力学数据,颗粒内扩散方程拟合结果发现牛粪生物炭对磷的吸附包括表面吸附和颗粒内扩散两个过程。吸附等温线拟合发现Langmuir吸附等温方程能很好拟合等温吸附数据,表明生物炭对磷的吸附以单分子层吸附模式为主。     

磁性活性炭吸附苯酚的初步研究

本文研究了磁性活性炭对苯酚的吸附性能;探讨了Cd2＋对苯酚在磁性活性炭上吸附的影响。目的是对磁性活性炭进行研究,以及为在实际废水中吸附处理苯酚提供参考。结果表明,磁性活性炭对苯酚的吸附过程符合拟二级动力学模型,R2为0.9935;与Freundlich吸附模型相比,Langmuir吸附模型能更好地描述磁性活性炭对苯酚的吸附行为;在不影响去除率的情况下,Cd2＋的存在使苯酚吸附处理最佳浓度由30 mg/L增大至50 mg/L;同时,Cd2＋对磁性活性炭和活性炭吸附苯酚分别具有促进和抑制作用。针对苯酚的吸附去除率,当无Cd2＋时,磁性活性炭的比活性炭的低10.65%～20.2%;当有Cd2＋时,磁性活性炭的比活性炭的高0.3%～7.71%。     

干旱半干旱地区湖泊沉积物对Cu2+的吸附-解吸研究

吸附-解吸是重金属在沉积物中迁移转化的重要过程。本文研究干旱半干旱地区湖泊———乌梁素海不同区域沉积物对Cu2+的吸附-解吸过程。结果表明,吸附过程中,pH值逐渐降低;沉积物TOC含量越高,其对Cu2+的吸附能力也越强;生活污水和工业废水影响的S1样点及受农田退水影响的S2样点对Cu2+的吸附量相对较低,而相对较洁净的S3和S4样点具有较高的Cu2+吸附量。4个样点吸附量能力大小为S3>S4>S2>S1。解吸实验显示,沉积物吸附的Cu2+大部分都不能被解吸。试验结果符合Langmuir和Freundlich等温吸附方程,Langmuir方程的拟合效果要好于Freundlich方程,Langmuir方程拟合的饱和吸附量分别为3.31 mg/g、4.84 mg/g、8.39 mg/g和7.75 mg/g。     

活性炭吸附法去除印染工业废水色度的试验与研究

通过试验初步研究活性炭直接吸附去除印染工业废水色度中吸附剂投加量、吸附时间等对色度去除率的影响。通过混凝沉淀法与活性炭吸附法结合、搅拌电解法与活性炭吸附法结合、脱色氧化法与活性炭吸附法结合等试验初步探讨了活性炭吸附与其它处理方法结合去除印染工业废水色度的可行性。同时，讨论了以上几种处理方法对水样中CODCr的去除、水样pH值变化等的影响。     

超声波载铁活性炭对磷的吸附研究

选用牛粪基活性炭进行负载,使用超声波协同浸渍负载铁,得到一种简单快速且成本较低的载铁活性炭制备方法。实验表明,在牛粪活性炭与铁盐在质量比1∶2,30℃下使用超声波浸渍40min为最佳的负载方法。利用扫描电子显微镜(SEM),X射线衍射(XRD),红外光谱法(IR)对优方案的载铁活性炭进行表征,发现含铁化合物均匀的分布在活性炭孔道中,无固定晶型。其中的含铁基团对磷的吸附起了重要作用。根据载铁活性炭吸附研究,所得的载铁活性炭对浓度为25mg/L的模拟含磷溶液去除率最高达96%以上。能较好的符合Freundlich热力学方程与拟二级动力学方程(R20.97),得到的最大吸附浓度达到19.723mg/g,吸附开始2min去除率即可达70%。     

膨润土颗粒吸附剂的制备及废水中铅离子的处理研究

通过振荡吸附实验,研究了膨润土颗粒吸附材料的制备方法及颗粒吸附材料在含铅离子废水中的吸附特性.结果表明,颗粒化的最佳条件为:膨润土颗粒粒径2mm,焙烧温度550℃,焙烧时间1h.在温度25℃、pH值为6、Pb2+初始浓度为50mg/L、吸附剂用量为8g/L、吸附时间为60min时,吸附剂对废水中Pb2+的吸附去除率达90%以上,吸附剂对Pb2+ 的吸附符合Langmuir吸附方程.     

Application of 'waste' wood-shaving bottom ash for adsorption of azo reactive dye

The utilization of wood-shaving bottom ash (WBA) for the removal of Red Reactive 141 (RR141), an azo reactive dye, was investigated. WBA/H(2)O and WBA/H(2)SO(4) were made by treating WBA with water and 0.1M H(2)SO(4), respectively, to increase adsorption capacity. Adsorption of RR141 from reactive dye solution (RDS) and reactive dye wastewater (RDW) by WBA/H(2)O and WBA/H(2)SO(4) involved the BET surface area and pore size diameter. Properties of adsorbents, effect of contact time, initial pH of solution, dissolved metals and elution studies indicated that the decolorisation mechanism involved both chemical adsorption and precipitation with calcium ions. In addition, the WBA/H(2)SO(4) surface might contain sulphate-cation complexes that were specific to enhancing dye adsorption from RDW. The adsorption isotherm had a best fit by the Freundlich model. Freundlich parameters showed that WBA/H(2)O used more heterogeneous surface than WBA/H(2)SO(4) and activated carbon for RDW adsorption. A thermodynamic study indicated that RDW adsorption was an endothermic process. The maximum dye adsorption capacities of WBA/H(2)O, WBA/H(2)SO(4) and activated carbon obtained from a Langmuir model at 30 degrees C were 24.3, 29.9, and 41.5mgl(-1), respectively. In addition, WBA/H(2)O and WBA/H(2)SO(4) could reduce colour and high chemical oxygen demand (COD) of real textile wastewater. According to the difficulty in the elution study, it was an environmentally safe disposal of this waste. Therefore, WBA, a waste from combustion of wood shavings, was suitable to be used as an effective adsorbent for azo reactive dye removal.     

臭氧-活性炭工艺在炼化循环排污水处理中的应用＊

针对炼化企业循环排污水中有机污染物浓度不能满足脱盐处理工艺进水水质要求的问题,开展了臭氧氧化-活性炭吸附工艺去除循环排污水中有机污染物的研究。通过对两种处理工艺进行不同组合的实验结果得知:当反应时间控制在最佳值,臭氧氧化和活性炭吸附单独处理循环排污水时,COD去除率分别约为27%和20%,处理效率偏低;当两种工艺组合后,在臭氧浓度为12 mg/L、氧化时间20 min、吸附时间为10 min时,COD去除率则达到52%,组合工艺协同作用效果明显。     

粉煤灰处理染料废水的研究

利用粉煤灰吸附性能较好、来源广泛及价格低廉等特点,对染料废水进行吸附试验研究。结果表明,粉煤灰的活化方式、粒度及用量对染料废水吸附性能有影响。160—200目30%硫酸活化粉煤灰吸附能力最强,且对染料废水的吸附过程符合Langmuir吸附等温曲线,最大吸附量为667mg/g。     

烟气脱汞技术研究进展

基于现阶段烟气汞的排放情况,介绍当前燃煤电站的几种烟气脱汞技术。主要是先将零价汞氧化为二价汞,再进行脱除。其中利用现有烟气控制设备,活性炭吸附及添加改性物质,有比较好的脱汞效率,电催化、光催化以及等离子体脱汞等新技术处于研发阶段,而烟气中多种污染物协同脱除有较好的应用前景。     

Determination of model parameters for zinc (II) ion biosorption onto powdered waste sludge (PWS) in a fed-batch system

Biosorption of zinc (II) ions onto pre-treated powdered waste sludge (PWS) was investigated using a completely mixed tank operating in fed-batch mode instead of an adsorption column. Experiments with variable feed flow rate (0.05-0.5 L h(-1)), feed Zn(II) ion concentrations (37.5-275 mg L(-1)) and amount of adsorbent (1-6 g PWS) were performed using fed-batch operation at pH 5 and room temperature (20-25 degrees C). Break-through curves describing variations of aqueous (effluent) zinc ion concentrations with time were determined for different operating conditions. Percent zinc removal from the aqueous phase decreased, but the biosorbed (solid phase) zinc ion concentration increased with increasing feed flow rate and zinc concentration. A modified Bohart-Adams equation was used to determine the biosorption capacity of PWS (q'(s)) and the rate constant (K) for zinc ion biosorption. Biosorption capacity (q'(s)=57.7 g Zn kg(-1) PWS) of PWS in fed-batch operation was found to be comparable with powdered activated carbon (PAC) in column operations. However, the adsorption rate constant (K=9.17 m(3) kg(-1) h(-1)) in fed-batch operation was an order of magnitude larger than those obtained in adsorption columns because of elimination of mass transfer limitations encountered in the column operations. Therefore, a completely mixed tank operated in fed-batch mode was proven to be more advantageous as compared to adsorption columns due to better contact between the phases yielding faster adsorption rates.     

不同造孔剂负载金属活性炭的制备及其脱硫性能初步研究

以糠醛渣、酚醛树脂和一定的造孔剂为原料制备球形活性炭，考察其碘吸附值和负载金属的性能，结果表明，较好的造孔剂为CMC。同时，通过浸泡方式在活性炭上负载铜、钒以及铜钒复合物，在不同温度下考察各活性炭的脱硫性能，结果表明，负载钒的活性炭在437K下对SO2的转化有明显的催化作用，而铜、钒负载量的适当增加有利于活性炭吸附性能的提高。     

酸改性活性炭在重金属与氨氮废水处理中的应用

重金属以及氨氮是造成水体污染的重要物质,在对水体重金属以及氨氮的去除方法中,活性炭吸附法有一定的进展.本文参照常见的酸类物质如硝酸、盐酸、硫酸、磷酸、柠檬酸和其他酸性物质对活性炭改性去除重金属和氨氮的研究,综述了各种酸改性的机理和对活性炭的影响,定性地比较了活性炭在各种酸改性后的去除能力.总结了对酸性改性活性炭在去除重金属和氨氮应用中的发展方向和前景,对于日后用酸性废水改性活性炭以达到以废治废的功效有着指导、借鉴作用.     

水处理用活性炭改性研究

研究了锆（Zr）和十六烷基三甲基氯化铵（CTAC）联合改性活性炭的制备，并考察Zr-CTAC改性活性炭对水中硝酸盐和磷酸盐的吸附作用及相关吸附机制，着重论述了锆（Zr）和十六烷基三甲基氯化铵联合改性活性炭（Zr-CTAC-AC）对水中硝酸盐和磷酸盐的吸附去除作用，结果表明Zr-CTAC-AC对水中硝酸盐和磷酸盐均具备较好的吸附去除能力。     

Adsorption of phenol and its derivatives from water using synthetic resins and low-cost natural adsorbents: a review

In this article, the technical feasibility of the use of activated carbon, synthetic resins, and various low-cost natural adsorbents for the removal of phenol and its derivatives from contaminated water has been reviewed. Instead of using commercial activated carbon and synthetic resins, researchers have worked on inexpensive materials such as coal fly ash, sludge, biomass, zeolites, and other adsorbents, which have high adsorption capacity and are locally available. The comparison of their removal performance with that of activated carbon and synthetic resins is presented in this study. From our survey of about 100 papers, low-cost adsorbents have demonstrated outstanding removal capabilities for phenol and its derivatives compared to activated carbons. Adsorbents that stand out for high adsorption capacities are coal-reject, residual coal treated with H3PO4, dried activated sludge, red mud, and cetyltrimethylammonium bromide-modified montmorillonite. Of these synthetic resins, HiSiv 1000 and IRA-420 display high adsorption capacity of phenol and XAD-4 has good adsorption capability for 2-nitrophenol. These polymeric adsorbents are suitable for industrial effluents containing phenol and its derivatives as mentioned previously. It should be noted that the adsorption capacities of the adsorbents presented here vary significantly depending on the characteristics of the individual adsorbent, the extent of chemical modifications, and the concentrations of solutes.