磷酸三丁醌（TBP）对苯酚的络合萃取

基于可逆络合反应的萃取分离方法极性有机物稀溶液具有高效性和高选择性，本文系统进行了磷酸三丁酯（ＴＢＰ）对苯酚稀溶液的络合萃取的实验研究，负载有机相的红外谱图分析表明，ＴＢＰ与苯酚通过氢键缔合形成萃合物，以ＴＢＰ－煤油为萃取剂对工业含酚废水进行了萃取平衡和错流萃取实验，讨论了其应用的可能性及开发新的有效的络合萃取剂的途径。     

磷酸三丁酯(TBP)对苯酚的络合萃取

基于可逆络合反应的萃取分离方法对极性有机物稀溶液具有高效性和高选择性.本文系统进行了磷酸三丁酯(TBP)对苯酚稀溶液的络合萃取的实验研.负载有机相的红外谱图分析表明,TBP与苯酚通过氢键缔合形成萃合物.以TBP-煤油为萃取剂对工业含酚废水进行了萃取平衡和错流萃取实验.讨论了其应用的可能性及开发新的有效的络合萃取剂的途径.     

协同—络合萃取法回收含酚废水中的酚类

在现有的各种收处理高浓度含酚废水的方法中，溶剂萃取法最为有效，但现有常用脱酚萃取剂分别存在着萃取效能低等诸多缺点，萃残液中一般尚存有几十至几百ｍｇ．ｌ＾－１的酚类，本文提出了协同－络合萃取法，并按该法原理研制ＨＣ－１－ＨＣ－４四类新型协同－络合萃取剂，其中ＨＣ－３和ＨＣ－４对苯酚稀溶液的萃取平衡常数分别为ＫＨＣ－３＝６１２．４和ＫＨＣ４＝４８３．７，单级萃取可将两组中高浓度的含酚废水中酚浓度降至１     

协同-络合萃取法回收含酚废水中的酚类

在现有的各种回收处理高浓度含酚废水的方法中,溶剂萃取法最为有效.但现有常用脱酚萃取剂分别存在着萃取效能低等诸多缺点,萃残液中一般尚存有几十至几百mg·l~(-1)的酚类,本文提出了协同-络合萃取法,并按该法原理研制了HC-1—HC-4四类新型协同-络合萃取剂.其中HC-3和HC-4对苯酚稀溶液的萃取平衡常数分别为K_((?)C-3)=612.4和K_((?)C-4)=483.7,单级萃取可将两组中高浓度的含酚废水中酚浓度降至10mg·l~(-1)以厂,脱酚率>99%.该法为一步脱酚达标提供了可能性.     

活性炭负载TiO2催化臭氧氧化去除水中酚的研究

本文采用活性炭负载TiO2作催化剂对臭氧氧化去除含酚废水进行了研究．研究了不同的酚初始浓度、pH值及臭氧浓度对苯酚去除率的影响，获得了反应动力学常数．实验结果表明：苯酚初始浓度越小，去除率越高．在本实验条件下，向150mL苯酚溶液中通入浓度为3．48mg/L、流量为0．05m^3／h的臭氧化空气反应30min去除率即可达到99％以上。     

有机磺酸类化合物的络合萃取研究

本文以三烷基胺为络合剂,正辛醇,煤油,氯仿,四氯化碳等为稀释剂,测定了络合萃取剂对于对甲基苯磺酸,磺基水杨酸稀溶液的相平衡分配系数,讨论了稀释剂,体系ＰＨ值和７３０１络合剂含量对萃取相平衡分配系数Ｄ值的影响,确定了形成的萃合物的组成。     

液膜法处理含酚废水的研究

本文研究了蓝１１３Ｂ－煤油－ＮａＯＨ液膜体系处理苯酚废水的最佳操作条件，并对高浓度含酚废水（浓度５％以上）进行了二级处理，实验结果表明，除酚效率可达９９％以上。对内相ＮａＯＨ的最佳浓度的确定也给出了估算方法。     

N1923络合萃取丙酸的研究

分别以模拟和实际丙酸发酵废水体系为研究对象,采用络合萃取法回收稀溶液中的丙酸,结果表明,对含2%丙酸的水溶液,以45%(体积比)的N1923为萃取剂,以煤油和正辛醇为稀释剂进行萃取,在油水相比1∶4的情况下,单级萃取率可达97%.对实际发酵废水中丙酸的萃取,在二级错流萃取的情况下,也能达到同样的分离效果.有机溶剂循环使用实验表明,经过10次重复利用后其萃取能力基本不变.     

NaOH溶液对有机相苯酚反萃取的研究

本文系统进行了ＮａＯＨ溶液对负载苯酚的ＴＢＰ＋煤油溶剂的反萃取平衡实验。考虑苯酚的支萃取平衡和解离平衡,建立了反萃取的计算模式,并证明了模型的可行性。本文还讨论了ＮａＯＨ溶液浓度,油水相比,萃取平衡分配系数,溶剂中的负载苯酚浓度和ＮａＯＨ溶液中初始酚含量对反萃取率的影响。     

催化湿式氧化法预处理显影废水的研究

考察了催化湿式氧化法对医院显影废水进行预处理的可行性.紫外扫描结果表明,对甲氨基苯酚硫酸盐、对苯二酚等特征污染物被降解为小分子物质,在催化剂Ru/TiO2存在下,催化湿式氧化法与湿式氧化相比,有机物的降解更加彻底.通过考察催化剂用量、温度、压力及pH值等条件对CODCr去除率的影响,确定适宜的反应条件为:催化剂用量为2g·l-1,温度为220℃,压力为1.5MPa,pH为8.9.在上述反应条件下,CODCr去除率达62.5%,色度去除率达98%,BOD5/CODCr值由原来的0.07提高到0.45.     

乳化液膜法提取苯酚的动力学研究

研究了以双丁二烯亚胺－煤油作膜相,ＮａＯＨ溶液为内水相的乳化液膜提取苯的动力学特性,测定了膜相与内外水相组成,搅拌速度,温度对提取速率的影响,得出了提取速率规律。     

广州城市水体沉积物中重金属形态分布研究

选取广州城市水体中的４ 个污染沉积物样品,采用连续提取法研究沉积物中重金属元素（ Ｐｂ 、 Ｚｎ 、 Ｃｕ 、 Ｎｉ 、 Ｃｒ 、 Ｍｎ） 的形态分布,结果表明：重金属元素主要以残渣态、有机结合态和氧化铁结合态存在,其中 Ｐｂ 、 Ｎｉ、 Ｍｎ 以残渣态和氧化铁结合为主, Ｚｎ 以残渣态和有机结合态为主, Ｃｕ 以有机态和氧化铁结合态为主, Ｃｒ 以氧化铁结合态为主。沉积物中固相组分对重金属的富集能力为：无定型氧化锰＞ ＞ 碳酸盐＞ 氧化铁＞ 有机质,而富集量则是后两者大于前两者。     

二(2-乙基己基)磷酸络合萃取邻氨基苯酚的研究

以二(2-乙基己基)磷酸(D2EHPA)为萃取剂,研究稀释剂种类、萃取剂浓度、溶液的初始pH值、溶液中甲(乙)醇等因素对邻氨基酚(OAP)稀溶液分配比(D)的影响.结果表明:溶液的初始pH值在7左右时,D有最大值;D值随二(2-乙基己基)磷酸浓度的增大而提高,且在极性环境要优于惰性环境;甲(乙)醇是影响萃取结果的主要因素.     

Determination of cobalt by air-assisted liquid–liquid microextraction

Abstract

A rapid and selective technique for extraction, preconcentration and determination of trace amounts of cobalt in water and pharmaceutical samples by air-assisted liquid–liquid microextraction combined with flame atomic absorption spectrometry is proposed. 1-Nitroso-2-naphthol is used as a complexing agent and 1-octanol as an extraction solvent. Parameters relevant for analytical effectivity, i.e. pH of sample solution, concentration of complexing agent, volume of extraction solvent, and number of extraction cycles are optimized using a Box–Behnken design. At optimum conditions, a dynamic linear range of 5–600?µg L^?1 is obtained, with a limit of detection of 1.2?µg L^?1. The method is used for determination of Co(II) in environmental water and pharmaceutical samples.     

Sequential anaerobic and aerobic treatment of pulp and paper mill effluent in pilot scale bioreactor

In the present study sequential anaerobic and aerobic treatment in two step bioreactor was performed for removal of colour in the pulp and paper mill effluent. In anaerobic treatment, colour 50%, lignin 62%, COD 29%, absordable organic halides (AOX) 25% and phenol 29% were reduced in eight days. The anaerobically treated effluent was separately applied in bioreactor in presence of fungal strain, Paecilomyces sp., and bacterial strain, Microbrevis luteum. Data of study indicated reduction in colour 80%, AOX 74%, lignin 81%, COD 93% and phenol 76 per cent by Paecilomyces sp. where as Microbrevis luteum showed removal in colour 59%, lignin 71%, COD 86%, AOX 84% and phenol 88% by day third when 7 days anaerobically treated effluent was further treated by aerobic microorganisms. Change in pH of the effluent and increase in biomass of microorganism's substantiated results of the study, which was concomitant to the treatment method.     

Screening zur Mobilisierbarkeit von Kupfer aus Böden und Schlämmen

In the presented paper, the pHstat-procedure is compared with four simple extraction procedures. These procedures make use of the following extraction solutions: distilled water (based on DIN 38414 part 4, DIN-S4), 1 mol/L ammonium nitrate, 1 mol/L ammonium acetate at pH 7.0 and 1 mol/L sodium acetate at pH 5.0, respectively. The extraction procedures were applied to 10 different soil samples and 2 sludges. The DIN-S4-procedure shows the lowest amounts of mobilized copper. The highest parts are extracted by sodium acetate solution. For the procedures investigated, the mobilized amounts extracted by ammonium acetate solution are most comparable with those of the pHstat-procedure. The simple sodium acetate procedure is useful for screening to select significant samples from a large number of soils. Thus, the high effort caused by the pHstat-procedure can be reduced to a minimum through the application of this screening procedure. The application of this screening, however, is difficult for samples containing large parts of organic compounds, e.g. sewage sludge. These samples show a different extracting behaviour.     

Removal of toxic chromium(VI) from aqueous solution by activated carbon using Casuarina equisetifolia

Highly activated carbon from the seed husk of Casuarina Casuarinas equisetifolia, a worldwide famous plant, have been prepared and tested for the removal of toxic Cr(VI) from its aqueous solution. The adsorbent was investigated for influences of initial chromium concentration (75, 100, 125, and 150 mg l^-1), pH, contact time, and quantity of carbon on removal of Cr(VI) from aqueous solution at room temperature (25±2 °C). The adsorption kinetic of Cr(VI) was studied, and the rates of sorption were found to conform to pseudo-second-order kinetics with a good correlation (R²≥0.99). The Langmuir and Freundlich models fit the isotherm data well. Furthermore, the Gibbs free energy was obtained for each system and was found to be-5.29 kJ mol^-1 for removal of Cr(IV). The negative value of Δ G° indicates the feasibility and spontaneous nature of adsorption. The results indicate that acidic pH (1.05) supported the adsorption of Cr(IV) on activated carbon. The maximum adsorption capacity of Cr(VI) on activated carbon was about 172.4 mg g^-1 at pH 1.05.     

不同进水有机物浓度下移动床生物膜反应器(SBMBBR)脱氮除磷特性

考察了不同进水有机物浓度下厌氧/好氧序批式移动床生物膜反应器（SBMBBR）污染物去除特性,实验结果表明,SBMBBR能够实现低碳源污水中氮和磷的同步去除,在进水TN和TP浓度分别为116.7 mg.L-1和11.5 mg.L-1、COD浓度为456 mg.L-1的条件下,TN和TP去除率分别达到94.3%和92.2%以上.反应器除磷是基于常规生物除磷和反硝化除磷过程实现的,脱氮主要是基于好氧段发生的同时硝化反硝化（SND）作用而完成.由于生物膜内部存在的DO扩散梯度,在好氧阶段混合液DO浓度不断提高的条件下反应器内具有良好SND反应的发生.进水COD浓度由149 mg.L-1提高至456 mg.L-1的过程中,反应器硝化效果不变,反硝化和除磷效果改善.反应器在好氧阶段pH值基本维持在7.0—7.1之间,为各类菌群的生长创造了条件.碱度变化较pH值更能反映硝化和反硝化反应发生的程度.反应器中微生物相丰富,生物膜以丝状菌为骨架,其上附着大量的球状菌和杆状菌,而悬浮活性污泥中丝状菌较少,形成了由细菌、真菌到原生动物和后生动物的复杂的生态体系,为系统取得稳定的污水处理效果提供了有效的保证.     

Microwave and Fenton's reagent oxidation of wastewater

We compared two H₂O₂ oxidation methods for the treatment of industrial wastewater: oxidation using Fenton's reagent [H₂O₂/Fe(II)] and microwave irradiation. Both methods were applied to the treatment of synthetic phenol solutions (100 mg L⁻¹) and of an industrial effluent containing a mixture of ionic and non-ionic surfactants at high load (20 g L⁻¹ of COD). The effects of initial pH, initial H₂O₂ concentration, Fenton catalyst amount and irradiation time were assessed. According to the oxidation of phenol, it has been found that the oxidation by Fenton's reagent is dependent on the pH, contrary to the microwave system, which is not influenced by this parameter. For both systems, a limiting amount of oxidant has been found; above this point the oxidation of phenol is not improved by a further addition of peroxide. The oxidation of the industrial surfactant effluent has only been successful with the Fenton's reagent. In this case, large amounts of ferrous ions are necessary for the precipitation of the ionic surfactants of the effluent, followed by the oxidation of the non-ionic constituents of the solution. Electronic Publication