生物法处理含油钻井废水的影响因素研究

以含油钻井废水原浆为处理对象,研究了生物法处理过程中的相关影响因素.实验结果表明,氮、磷源是影响钻井废水中石油烃降解的重要因素,最佳氮、磷源及其加入量分别为(NH4)2SO4100 mg/L和KH2PO460 mg/L.在30～36℃,接种量15%,pH=6～8条件下处理72 h后可使钻井废水中的石油烃含量由805.6 mg/L下降到17.6 mg/L.     

腐殖酸、细颗粒泥沙对粉末活性炭吸附苯酚特性影响的研究

通过一系列实验,探讨了粉末活性炭吸附水中苯酚时,腐殖酸(HA)浓度和细颗粒泥沙用量对苯酚吸附量和去除率的影响.实验结果表明:在中性条件下,随着HA浓度的增加,粉末活性炭对苯酚的吸附量减少;在不同质量细颗粒泥沙的影响下,苯酚的去除率基本不变;在未加HA时,粉末活性炭对苯酚的吸附行为用Langmuir吸附等温式拟合效果最好,对苯酚的最大吸附量为150.60 mg/g,而在有HA存在时,粉末活性炭对苯酚的吸附行为用Freundlich吸附等温式拟合效果最好,对苯酚的最大吸附量为28.49 mg/g.     

沸石用于去除废水中的氨氮

天然沸石及改性沸石对氨氮有很强的选择性吸附能力。介绍了沸石去除废水中氨氮的应用研究,包括在O/A生物处理系统、二级氧化塘处理系统、土地处理系统、湿地系统和堆肥系统等中的应用。分析了氨氮在沸石上发生吸附和离子交换的主要影响因素和规律。为开拓沸石在废水处理中的应用提供科学与技术基础。     

不同类型电镀液中阴离子的离子色谱法检测

采用抑制型电导离子色谱法检测电镀液中的常见阴离子.色谱条件是: IonPac AS11-HC阴离子交换色谱柱,淋洗液自动发生装置在线产生KOH梯度淋洗,抑制型电导检测.检测限(S/N=3)在0.29-15.3 μg·l-1,阴离子F-,Cl-,MSA-,NO-3,SO2-4,PO3-4和CrO2-4的线性范围均在两个数量级以上,RSD在5%以下,回收率为92%-110%,具有灵敏度高,选择性好,重现性佳等特点,用于实际样品的检测,结果令人满意.     

水溶液中活性成分对壬基酚聚氧乙烯醚光降解的影响

采用长波紫外灯(UV365)和模拟日光灯研究光化学活性成分对水溶液中壬基酚聚氧乙烯醚(NPEOs)光降解效率的影响,并讨论了光降解导致NPEOs成分分布的变化.研究表明,在UV365辐射下,亚硝酸根,Fe(Ⅲ),H2O2和腐殖酸(HA)等的存在对NPEOs96h的降解效率有较明显的促进作用;在模拟日光下,Mn(Ⅱ),Fe(Ⅲ),H2O2等对NPEOs的光降解也有一定的促进,而此条件下HA的存在则表现为对光降解的抑制作用.此外,还考察了NPEOs在不同比例的Fe(Ⅲ)-HA和Fe(Ⅲ)-H2O2复合体系中的光降解效率.除了导致光降解效率的提高外,活性成分的存在也会导致降解后NPEOs成分分布的变化.以在UV365辐射下为例,H2O2(1000 μmol·l-1)或Fe(Ⅲ)(10和100 μmol·l-1)的加入使反应后短链NPEOs所占比例从初始的22.52%明显提高至29.75%,29.89%和51.89%.这种成分分布的变化可能是由于长链NPEOs在降解过程中发生EO链衰减,从而使短链NPEOs成为其降解中间产物;或是由于长链NPEOs比其短链同系物具有更高的敏化降解速率所导致的.     

铬渣中Cr(Ⅵ)的浸出及强化研究

采用ICP-OES,XRD,SEM,EDX和电导率在线监测等手段分析铬渣浸取前后的变化及各种元素浸出量随pH值的变化,考察了添加化学悬浮剂、浸取体系和超声处理对铬渣中Cr（Ⅵ）浸出行为的强化作用.结果表明,浸取过程基本不改变铬渣的结构;pH为5-7,使用合适的浸取介质有利于Cr（Ⅵ）的溶出,通过添加化学悬浮剂APG650可提高浸取效率3倍,超声处理可提高浸取效率70多倍.     

Zinc removal from synthetic waters using magnetite/graphene oxide composites

The removal of heavy metals from wastewater has become a global challenge, which demands the continuous study of efficient and low-cost treatment alternatives such as adsorption. In this research, the removal of zinc was evaluated using batch adsorption processes with nonconventional materials such as graphene oxide (GO), magnetite (MG), and their composites (GO:MG), formulated with three weight ratios (2:1, 1:1, and 1:2). Graphene was synthesized by the modified Marcano method, using pencil lead graphite as a precursor. MG and the composites were synthesized by chemical coprecipitation of ferrous sulfate and ferric chloride. The materials were characterized by Raman and Fourier transform infrared spectroscopies, scanning electron microscopy, X-ray diffraction, and the Brunauer–Emmett–Teller method to determine the functional groups, microstructural and morphological characteristics, and specific surface area. Batch adsorption tests were carried out to optimize the adsorbent dose and contact time with zinc solutions of 10 ppm. Zinc adsorption reached equilibrium at 2 h, with an optimal dose between 0.25 and 1.0 g/L. The maximum zinc removal efficiencies/adsorption capacities were 98.6%/165.6, 83.4%/47.6, 83.5%/21.9, 72.8%/19.9, and 82.2%/9.25 mg/g using GO, 2GO:1MG, 1GO:1MG, 1GO:2MG, and MG, respectively. Furthermore, the analysis of the isotherm and adsorption kinetics models determined that the adsorption processes using MG and the composites fit the Sips and pseudo-second-order models.     

用次氯酸钠法处理选矿废水

采用次氯酸钠法处理铅锌硫化矿选矿废水,考察了废水初始pH、NaClO加入量及反应时间对选矿废水COD去除率的影响。在废水pH为4、NaClO加入量为100g/L、反应时间为30min的条件下,选矿废水的COD去除率可达到98．3％;当pH为11、反应时间为10min、NaClO加入量为1g/L时,选矿废水的COD去除率为39．4％。     

流化催化裂化烟气脱硫助剂的制备及其脱硫活性

采用溶胶-凝胶法制备锌铝助剂,该助剂于700℃焙烧后与流化催化裂化（FCC）催化剂进行机械混合,制得混合催化剂;在FCC烟气工业模拟装置上考察混合催化剂的脱硫活性,用混合催化剂的脱硫活性来反映锌铝助剂的脱硫性能。实验结果表明,氧化锌质量分数为10％的锌铝助剂的脱硫活性最佳,脱硫率达62．5％。采用红外光谱和X射线衍射（XRD）对锌铝助剂的脱硫机理进行了研究,红外分析结果表明,弱的L酸中心有利于锌铝助剂脱硫,XRD分析结果表明,锌铝助剂在锌铝尖晶石结构尚未完全形成时,存在较多的晶格缺陷,能够有效地吸附烟气中的SOx,将其转化为H2S。     

Carbonization of waste PVC to develop porous carbon material without further activation

Efficient removal of chlorine from PVC achieved by two-stage heat-treatment (280 and 410 degrees C) provided chlorine-free isotropic pitch containing additive. The pitch was stabilized and carbonized into porous carbons with surface areas of approximately 300 m2/g. Resultant porous carbons showed three pore structures of supermicropore, micropore and mesopore. The generation of CO2 from the decomposition of the CaCO3 additive in waste PVC is responsible for the development of porous structures. The surface area of the carbonized product increased after the removal of CaO.