壳聚糖吸附处理废水的研究进展

壳聚糖吸附处理废水的研究包括其对废水吸附性能和吸附机理的研究两个方面。壳聚糖表现出了良好的吸附废水中重金属离子、染料分子和其它易引起变异物质的能力;壳聚糖对金属离子和染料的吸附机理模型研究理论意义重大,它将进一步推动壳聚糖的实际工程应用。     

利用粉煤灰处理采油废水的研究

利用电厂粉煤灰及灰场氧化塘对现河首站采油废水中的污染物进行吸附和生化处理试验。试验结果表明:粉煤灰具有类似活性炭的结构和比表面积,对废水中的石油类、COD、氨氮、挥发酚等污染物具有较强的吸附、沉降和过滤作用。     

粉煤灰—膨润土颗粒吸附材料的制备及其处理含铅离子废水的研究

通过振荡吸附实验,研究了粉煤灰-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,制备颗粒吸附剂的优化条件为:粉煤灰∶膨润土=5∶5(质量比),在600℃下焙烧2h.在温度25℃、pH值为5、Pb2+初始浓度为40mg/L、吸附剂用量为2g/L、吸附时间为1h条件下,吸附剂对废水中Pb2+的去除率可达95.27%.     

氨基改性MCM-41对阴离子染料酸性品红的吸附研究

采用3-氨丙基三甲氧基硅烷对MCM-41进行氨基功能化修饰,并以此作为吸附剂(NH2-MCM-41)来去除阴离子染料废水酸性品红(AF)。应用平衡吸附法,重点考察了溶液的p H值、吸附剂的投加量、吸附时间以及染料的初始浓度对吸附效果的影响,并采用吸附等温线和动力学模型进行吸附机理分析。实验得出:溶液的p H值对吸附效果影响较大,染料的去除率随着吸附剂质量、反应时间的增加而上升,随染料初始浓度的增加而下降。Langmuir模型对染料的等温吸附行为拟合效果最好,吸附动力学符合准二级动力学模型。解吸附研究得出NH2-MCM-41有较好的解吸附效果和重复使用率。氨基改性后的MCM-41对AF有良好的吸附效果,可以作为一种新型高效的吸附剂进一步用于阴离子染料废水治理。     

染料废水脱色的物理化学处理技术

染料废水目前主要的脱色方法有吸附、混凝、氧化还原和生化法.活性炭吸附适用于低浓度的染料废水处理.聚硅硫酸铁混凝效果与Fe/SiO4摩尔比和pH值相关.氢氧化镁可有效去除印染废水中的直接红染料.有机絮凝剂往往需要和其它药剂复配.氧化法脱色率大,但成本高昂,且受染料废水的组成、氧化性及pH值影响.还原法药剂价格低廉,但还原降解产物具有毒性,必须经过二次处理.生物法成本较低,又受制于染料的生物降解性.因此发展多种手段联合应用已是当前染料废水处理的研究方向.     

粉煤灰在重金属废水处理中的应用

粉煤灰是一种可再资源化的工业固体废弃物。利用粉煤灰对重金属废水进行处理可谓是一种以废治废、变废为宝、实现废物综合利用的有效途径。综述了粉煤灰吸附法在重金属废水处理中的国内外研究现状,展望了该方法的应用前景。     

城市剩余污泥制备吸附剂的研究及其应用

以城市污水处理厂的剩余污泥为原料,采用化学活化法制备活性碳污泥吸附剂.通过对比不同活化剂活化效果,并对影响活化产物吸附性能的因素进行了研究.结果表明以3mol/L的ZnCl2为活化剂,活化温度为550℃,固液比为1:2.5,热解时间2h,制备的活性碳吸附剂吸附碘值为317.4mg/g,活性炭吸附剂比表面积为232.526m2/g.采用制备的活性碳吸附剂处理模拟废水COD去除效果较好.     

茄子秸杆活性炭对染料废水的吸附性能研究

以茄子秸秆为原料，ZnCl2为活化剂制备粉末状活性炭，主要研究了活性炭对染料废水的吸附性能；以活性红X-3B和酸性蓝RL为模型染料，考察了染料初始浓度、pH值、活性炭投加量和吸附时间等对染料脱色率的影响。结果表明，染料初始浓度和活性炭投加量对染料脱色率影响较大。初始浓度为300mg／L时，活性炭的最佳投加量分别为1g／L和1．4g／L；在最佳工艺条件下，脱色率分别在93％和98％以上，COD去除率分别为94．5％和86．4％，出水水质达到国家一级《纺织染整工业水污染物排放标准》（GB 4287—1992）。     

壳聚糖对酸性染料的吸附性能

在不同的壳聚糖浓度、pH和温度条件下，采用分光光度法测得吸附后的染料浓度，得到了壳聚糖对酸性染料的最佳吸附条件，即在固定染料浓度和体积的情况下，壳聚糖的投入量在500mg、pH值为6、温度为室温、吸附时间为2h左右条件下吸附最佳，其结果将为利用壳聚糖处理印染废水提供一定的理论根据。     

染料废水物理化学处理技术的现状与进展

本文按吸附、膜滤、混凝、氧化刑、离子交换、Fenton试剂、光催化氧化、湿式氧化、电化学等方法分别论述了染料废水物理化学处理技术的现状和发展趋势。     

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.     

Implementation of sulfate adsorption in the SAFE model

An SO4(2-) adsorption submodel has been implemented in the dynamic soil chemistry model SAFE. The submodel calculates pH-dependent SO4(2-) and H+ adsorption to the soil, as well as the net surface charge development due to uneven adsorption of SO4(2-) and H+, using the empirical equations derived from an electrostatic model (Extended Constant Capacitance Model, ECCM) of SO4(2-) adsorption. The resulting new SAFE model was applied on a roof experiment plot in the Norway spruce [Picea abies (L.) H. Karst.] stand at Solling, Germany, where atmospheric S and N deposition was artificially reduced by the roof construction. The model performance was compared with the previous versions that used a pH-independent Freudlich model of SO4(2-) adsorption or assumed no SO4(2-) adsorption. With the ECCM-based SO4(2-) adsorption submodel, SAFE simulated soil solution SO4(2-) concentration and base saturation better, in comparison with measured data, than with the previous SO4(2-) adsorption formulations. Through the model application, also, need of additional improvement was suggested, such as calibration of mass transfer coefficients.     

电化学反应器吸附去除氟离子的研究

采用改性活性炭粉末对用纯净水加氟化钠配制而成的含氟水溶液进行动态电吸附去除实验.研究不同电压、电吸附时间,以及Cl-和SO2-4对氟离子去除的影响,并探讨吸附动力学和吸附方程.实验结果表明:活性炭对氟离子的吸附等温方程符合Freundlich方程,吸附动力学符合一级动力学方程;活性炭对氟离子去除与所施加的电位、吸附时间等因素有关,施加的电位越大,去除效果越好;随着吸附去除时间的延长,氟离子浓度下降趋缓;Cl-对氟离子去除影响很小,而SO2-4对氟离子去除有显著的不利影响.     

Preparation of novel activated carbons from H2SO4-pretreated corncob hulls with KOH activation for quick adsorption of dye and 4-chlorophenol

Corncob hull was immersed in 25 wt% H(2)SO(4) and was carbonized in an oven at 290 °C for 2h to obtain the char. The char was then activated for 1h at 780 °C by KOH at weight ratio of KOH/char of 2.5, 3.0, and 3.5. SEM photos of the carbons revealed that the cell wall of corncob hull was etched into thin film structure. It was shown that the adsorption isotherms of methylene blue and 4-chlorophenol on the carbons were well fitted by the Langmuir equation. Moreover, the adsorption kinetics could be satisfactorily described by the Elovich equation. The normalized standard deviations are less than 2.8%. The high fraction of adsorption amount adsorbed within 1 min to that at saturation demonstrated the advantage of the prepared activated carbons. The fraction of adsorption amount within 1 min to that at saturation (q(1)/q(mon)) for the adsorption of 4-CP is high up to 0.807. Such quick adsorption behavior was mainly attributed to the presence of the thin film structure of carbons.     

Retention of gases by hexadecyltrimethylammonium-montmorillonite clays

Intercalated montmorillonite clays with different amounts of organic hexadecyltrimethylammonium (HDTMA) cations were studied to analyse their CO, CH(4), and SO(2) gas retentions. Equilibrium adsorption was measured by using a standard volumetric apparatus at 25 degrees C and 0.1 MPa. The solids were characterised by X-ray diffraction. The levels of adsorption of SO(2) by organo-montmorillonites (0.3595-1.6403 mmol/g) were higher than those of CO (up to 0.0202 mmol/g) and CH(4) (up to 0.0273 mmol/g) gases. HDTMA montmorillonites may be effective adsorbents for removing SO(2) and for its potential separation in the presence of CO and/or CH(4) molecules, which can be present in contaminated air.     

炭法烟气脱硫机理的研究现状

炭法烟气脱硫技术是一种污染治理与资源回收利用相结合的脱硫技术，本文在对活性炭吸附催化转化SO2过程、H2O和O2的存在对脱硫过程的影响，以及改性活性炭脱硫性能提高影响因素等方面分析基础上，论述了炭法脱硫机理研究现状，并提出了以后的发展方向。     

不同前处理方法对活性炭吸附一氧化碳的影响

本文采用颗粒状活性炭（GH-A)作吸附剂，通过不同的前处理方法，以一氧化碳CO与空气的混合物为分离测定对象，用气固色谱法测定被活性炭充分吸附前、后的混合气体中CO的含量，对比评价几种前处理方法。结果表明，对CO的吸附量显著提高的前处理方法分别是研磨筛分至32—38目、酸洗、添加改性剂So而水洗则降低了活性炭吸附CO的能力。     

饮用矿泉水中微量钡的测定方法

采用硫酸钡比浊法测定饮用矿泉水中微量的钡。结果如下：１＋１０硫酸用量以５ｍＬ为最佳;标准曲线相关系数达极显著水准;回收率９５—１０７％;变异系数６４８％;最佳比浊时间为停止搅拌后３０ｍｉｎ内     

废钻井液脱稳与ξ电位关系的研究

为了寻求钻井液脱稳剂H2SO4的最佳用量,采用JS94B型微电泳仪对钻井液体系的ξ电位进行了研究。实验中测定了钻井液在不同稀释倍数下ξ电位的变化情况,研究了脱稳剂H2SO4加量与钻井液临界ξ电位的关系,从而得出H2SO4加入量以045mL/100g废钻井液为宜,其临界ξ电位为-752997mV。     

Gas dynamics in eutrophic lake sediments affected by oxygen, nitrate, and sulfate

In many freshwater ecosystems, the contents of NO3- and SO4(2-) have increased, whereas O2 has been depleted due to the increased acid and nutrient loads. These changes may affect carbon turnover and the dynamics of the major greenhouse gases CO2, CH4, and N2O. We studied the effects of O2, NO3-, and SO4(2-) availability on carbon mineralization, and fluxes of CO2, CH4, and N2O in the sediments of hyper-eutrophic Lake Kev?t?n, Finland. Undisturbed sediment cores from the deep (9 m) and shallow (4 m) profundal were incubated in a laboratory microcosm with oxic and anoxic water flows with NO3- or SO4(2-) concentrations of 0, 30, 100, 300, and 2000 microM. The carbon mineralization rate (i.e., the sum of released CO2-C and CH4-C) was not affected by the oxidants. However, the oxidants did change the pathways of carbon degradation and the release of CH4. All of the oxidants depressed CH4 fluxes in the shallow profundal sediments, which had low organic matter content. In the deep profundal sediments rich in organic matter, the CH4 release was reduced by O2 but was not affected by SO4(2-) (the effect of NO3- was not studied). There was an increase in N2O release as the overlying water NO3- concentration increased. Anoxia and highly elevated NO3- concentrations, associated with eutrophication, increased drastically the global warming potential (GWP) of the sedimentary gases in contrast to the SO4(2-) load, which had only minor effects on the GWP.