N-甲基咪唑配体络合金属Cu(Ⅰ)催化剂对水中2,4-二甲氧基溴苯还原脱溴

合成了以N-甲基咪唑为配体,Cu为活性中心的络合金属多相催化剂Cu(Ⅰ)-NHC-SBA-15.通过1H-NMR、13C-NMR、有机元素分析和FTIR对各步合成反应产物结构经行了鉴定;用SEM、N2吸附脱附等方法对催化剂进行了表征;用ICP测定了催化剂Cu含量.对催化剂催化2,4-二甲氧基溴苯还原脱溴活性进行了测试.在反应时间为24 h,通过正交实验和单因素实验,考察了催化剂用量、反应温度、还原剂用量等因素对脱溴率的影响,并确定了最佳反应条件:催化剂用量为0.05 g、水合肼用量为2 mL、反应温度为80℃,脱溴效果较好,脱溴率达到98.5％.对催化剂重复使用进行了初步研究.对催化反应动力学进行了初步研究,结果表明,该多相催化反应是由表面反应速度控制,并符合一级动力学反应.对反应机理进行了初步探讨.     

不同温度对SBBR同步短程硝化反硝化处理炼油催化剂废水的影响

采用SBBR在溶解氧1.0 mg/L条件下考察了不同温度对实际炼油催化剂废水脱氮系统效能的影响.结果表明,SBBR容积负荷及同步硝化反硝化(SND)三氮去除率与进水氨氮浓度正相关.不同进水浓度下,反应器SND三氮去除率最高可达40％左右.33、30及28℃条件下,反应器亚硝积累率均可稳定保持在90％以上.不同温度下短程硝化反硝化pH值及ORP变化趋势基本一致,结合在线监控pH值及ORP变化规律调控反应时间,最大限度保证短程硝化的稳定性.     

Production of bio-oil from algal biomass and its upgradation to biodiesel using CaO-based heterogeneous catalysts

The present article deals with the production of bio-oil from algal biomass as well as the preparation and characterization of noble CaO-based heterogeneous catalyst for upgradation of bio-oil to biodiesel. The bio-oil has been extracted from algal biomass using hexane as solvent in soxhlet apparatus and upgraded to biodiesel by transesterification using noble CaO-based heterogeneous catalysts. Catalyst with TiO₂:CaO molar ratio of 0.25 and calcination temperature of 700°C has been found to be most suitable among all the catalysts developed. Characterization of the catalysts has been done by using X-ray diffraction (XRD), scanning electron microscope (SEM), and thermo-gravimetric analysis (TGA). The input--output model has been developed to correlate experimental and predicted value of biodiesel yield. Optimization of process parameters has been done using response surface methodology. Various properties and elemental composition of algal bio-oil and biodiesel have been determined and compared with biodiesel.     

纳米α-MnO2催化臭氧氧化降解水中双酚A

采用水热法制备了纳米α-MnO₂催化剂,并通过XRD和SEM技术对催化剂的成分和形貌进行了表征。采用纳米α-MnO₂催化剂催化臭氧氧化降解水中的双酚A（BPA）,考察了初始溶液pH、催化剂加入量和反应温度对BPA去除率的影响。实验结果表明,纳米α-MnO₂催化剂催化臭氧氧化降解BPA的最佳工艺条件为：催化剂加入量100 mg/L,初始溶液pH 8.5,反应温度18 ℃。在此最佳条件下处理质量浓度为10 μg/mL的BPA溶液120 min,BPA去除率为96.4%。回收洗涤后第二次使用的催化剂的BPA去除率为80.5%,第三次使用的催化剂的BPA去除率为74.1%,催化剂的活性随重复使用次数的增加而缓慢降低,活性较稳定。     

电石法聚氯乙烯生产行业的汞污染防治

结合我国电石法聚氯乙烯生产行业的发展现状,提出了采用低汞触媒替代高汞触媒以降低汞消耗、开发高效除汞器以提高脱汞效率、深度解吸废盐酸以解决汞转移问题、深度处理含汞废水以实现综合利用、优化工艺控制以降低汞触媒消耗、改善防护措施以减轻汞扩散等汞污染防治工作的要点。     

用含锌废催化剂制备纳米氧化锌

以含锌废催化剂为原料,经酸浸、除杂、锌粉置换、合成等工艺制得碱式碳酸锌,再经过滤、洗涤、干燥、煅烧制备纳米氧化锌。考察了酸浸工艺硫酸溶液含量和液固比（硫酸与含锌废催化剂的质量比）对锌浸出率的影响,以及煅烧温度对纳米氧化锌质量的影响。实验结果表明：在硫酸质量分数为30%、液固比为5的最佳酸浸工艺条件下,锌浸出率为92%;在最佳煅烧温度为400 ℃的条件下,氧化锌质量分数大于95%,比表面积大于50 m²/g;纳米氧化锌颗粒大小均匀,平均粒径小于50 nm。     

含铜废催化剂中铜的回收

采用热解—氨浸工艺处理含铜废催化剂（w（Cu）为23.6%）,优化了工艺条件,并通过蒸氨还原法制备出Cu₂O产品。实验结果表明：热解工段中,控制管式热解炉的空气流量为3.0 m³/min,在升温速率20 ℃/min、热解终温600 ℃、终温保持时间90 min的优化条件下,含铜废催化剂中的有机物热解完全;氨浸工段中,以NH₄Cl-NH₃-H₂O溶液为氨浸液,控制氨浸温度为40 ℃,在烧成料研磨时间90 min（粒径29.43 μm）、氨浸液总氨浓度4 mol/L、氨浸时间80 min的优化条件下,铜浸出率达到98%;经蒸氨还原法制得的Cu₂O产品的质量符合HG/T 2961—2010《工业氧化亚铜》中的一等品标准,产率为24%。     

制备条件对Mn-Fe/TiO2催化剂低温脱硝性能的影响

通过浸渍法制备了一系列Mn-Fe/TiO2催化剂,并采用XRD技术对其进行了表征,考察了锰前体种类、负载量（活性组分质量占载体质量的百分比）、Fe含量（Fe物质的量占活性组分物质的量的百分比）、焙烧温度等因素对催化剂低温选择性催化还原NO性能的影响。实验结果表明：以乙酸锰为前体制备的催化剂的脱硝活性明显高于以硝酸锰为前体制备的催化剂;负载量的增加有利于脱硝活性的提高,而Fe的添加对提高催化剂的活性有重要作用,但Fe含量超过15%后,对催化剂脱硝性能的影响并不明显;焙烧温度超过650 ℃时会使活性组分的结晶度提高,导致脱硝活性的降低。在锰前体为乙酸锰、负载量为15%、Fe含量为15%、焙烧温度为500 ℃、焙烧时间为6 h、反应温度为200 ℃的条件下,Mn-Fe/TiO2催化剂的NO转化率约为95%。     

Co-composting of spent coffee ground with olive mill wastewater sludge and poultry manure and effect of Trametes versicolor inoculation on the compost maturity

The co-composting of spent coffee grounds, olive mill wastewater sludge and poultry manure was investigated on a semi-industrial scale. In order to reduce the toxicity of the phenolic fraction and to improve the degree of composting humification, composts were inoculated with the white-rot fungus Trametes versicolor in the early stages of the maturation phase.During composting, a range of physico-chemical parameters (temperature and both organic matter and C/N reduction), total organic carbon, total nitrogen, elemental composition, lignin degradation and spectroscopic characteristics of the humic acids (HAs) were determined; impacts of the composting process on germination index of Hordeum vulgare and Lactuca sativa were assessed. The coffee waste proved to be a highly compostable feedstock, resulting in mature final compost with a germination index of 120% in less than 5 months composting. In addition, inoculation with T. versicolor led to a greater degree of aromatization of HA than in the control pile. Moreover, in the inoculated mixture, lignin degradation was three times greater and HA increased by 30% (P < 0.05), compared to the control pile. In the T. versicolor inoculated mixture, the averages of C and N were significantly enhanced in the HA molecules (P < 0.05), by 26% and 22%, respectively. This improvement in the degree of humification was confirmed by the ratio of optical densities of HA solutions at 465 and 665 nm which was lower for HA from the treated mixture (4.5) than that from the control pile (5.4).     

Magnetite/mesocellular carbon foam as a magnetically recoverable fenton catalyst for removal of phenol and arsenic

A magnetite-loaded mesocellular carbonaceous material, Fe₃O₄/MSU-F-C, exhibited superior activity as both a Fenton catalyst and an adsorbent for removal of phenol and arsenic, and strong magnetic property rendering it separable by simply applying magnetic field. In the presence of hydrogen peroxide, the catalytic process by Fe₃O₄/MSU-F-C completely oxidized phenol and As(III) under the conditions where commercial iron oxides showed negligible effects. Notably, the decomposition of H₂O₂ by Fe₃O₄/MSU-F-C was not faster than those by commercial iron oxides, indicating that hydroxyl radical produced via the catalytic process by Fe₃O₄/MSU-F-C was used more efficiently for the oxidation of target contaminants compared to the other iron oxides. The homogeneous Fenton reaction by the dissolved iron species eluted from Fe₃O₄/MSU-F-C was insignificant. At relatively high doses of Fe₃O₄/MSU-F-C, total concentration of arsenic decreased to a significant extent due to the adsorption of arsenic on the catalyst surface. The removal of arsenic by adsorption was found to proceed via preoxidation of As(III) into As(V) and the subsequent adsorption of As(V) onto the catalyst.