非热平衡等离子体协同催化脱除挥发性有机化合物的研究进展

单纯运用非热平衡等离子体(NTP)技术脱除挥发性有机化合物(VOCs)的效率和能量利用率并不高,而且在降解过程中可能会产生某些有害副产物。为了克服NTP技术在VOCs治理方面的缺陷,可将NTP和化学催化方法组合运用,结合两者的优势使系统的VOCs脱除率、能量利用率和CO2选择率显著提高。从催化反应器结构、NTP与催化剂协同作用的原理等方面总结了近年来NTP协同催化技术在VOCs脱除方面的应用状况。最后指出,NTP协同催化技术在VOCs脱除方面有良好的应用前景,但要真正实现其工程应用,仍有很多问题亟待研究和解决。     

Al-MnO2/SBA-15催化剂的制备 及其催化燃烧甲醛的性能

以介孔分子筛SBA - 15为载体,分别浸渍Mn、Al等催化活性组分,制备了MnO2/SBA-15催化剂和Al-MnO2/SBA-15催化剂.采用X射线衍射、N2吸附-脱附对催化剂的结构进行了表征,在微型固定床反应器上对催化剂的低浓度甲醛催化燃烧性能进行了评价.实验结果表明:MnO2/SBA-15系列催化剂均具有SBA...     

微波催化氧化处理正丁酸废水Ni-Co-Ce-O催化剂的制备及表征

采用微波催化氧化处理正丁酸模拟废水,以COD去除率为评价指标,对固相-焙烧法制备的3个系列共45种催化剂进行筛选,通过正交实验对催化剂制备工艺进行优化,并对优选出的催化剂进行XRD和SEM表征。结果表明,NiO+Co₂O₃+CeO₂（Ni∶Co=1∶1、NiO+Co₂O₃/CeO₂=1∶4）为筛选出的最优催化剂;Ni-Co-Ce-O催化剂最优制备条件为Ni：Co摩尔比1∶2、（NiO+Co₂O₃）/CeO₂质量比5%、研磨时间40 min、焙烧温度450℃、焙烧时间3 h,此条件下制备的催化剂催化效能最高,COD去除率达67%。     

The Role of Catalyst Properties on Methanol Oxidation over V2O5–TiO2 Using Ozone

Oxidation of methanol over V₂O₅ catalysts supported on anatase TiO₂ that were prepared using sol-gel formation and impregnation procedures were investigated. The effects of incorporating Mg in sol-gel to influence the properties of the catalyst were also studied. The process provides an alternative low temperature reaction pathway for reducing emissions of hazardous air pollutant (HAPs) such as methanol and total reduced sulfur compounds (TRS) from pulp and paper mills. The bulk and surface composition of the catalysts were determined by XRD and SEM-EDAX, respectively. The X-ray diffraction patterns of the vanadia–titania catalysts showed mainly the anatase phase of TiO₂. Temperature programmed desorption of methanol from the different catalyst showed that the α and β peaks differ significantly with V content and addition of Mg. The combination of gas phase and surface reactions on the V/TiO₂ catalysts reduced the amount of ozone required for high degradation of methanol to mainly CO _x with small quantities of methyl formate. In the absence of ozone the catalysts showed very low activity. It is hypothesized that the ozone is directly influencing the V⁴⁺ and V⁵⁺ redox cycle of the catalyst. Oxidation of methanol is influenced by the operation variables and catalyst properties. The results of this study revealed that the V content has significant influence on the catalyst activity, and the optimum vanadia loading of about 6 wt%. Higher turnover frequencies were observed over sol-gel catalysts than with catalysts prepared by the impregnation method.     

Effect of spent engine oil on the growth parameters and chlorophyll content of <Emphasis Type="Italic">Corchorus olitorius</Emphasis> Linn

The effect of spent engine oil on the height, leaf number, leaf area, stem girth, chlorophyll, and moisture contents of Corchorus olitorius grown on 0, 0.2%, 0.4%, 0.6%, 0.8%, 1.0%, 2.0%, and 3.0% (v/w oil/soil) oil-contaminated soil was investigated. The engine oil at all concentrations delayed the germination of C. olitorius by 2 days (compared to control) and there was a general significant reduction in all the growth parameters in plants grown on contaminated soil compared to control plants. The highest leaf area of 26.8 cm² was found in the control plant and least was found in the 0.6% soil (0.11 cm²) after 3 weeks while no values were recorded on the 0.8–3.0% engine-oil-contaminated soil after 5 weeks of experiment. The highest chlorophyll content was also found in the control plant (11.5 mg/l). This showed that spent engine oil has an adverse effect on the growth of C. olitorius plant.     

Ce改性Fe-Mn/TiO2低温SCR脱硝催化剂硫中毒机理

以Ce改性Fe-Mn/TiO_2低温选择性催化还原(SCR)脱硝催化剂为研究对象,通过活性测试和一系列表征技术对其低温抗硫性能及中毒机理进行探究。实验结果表明:当烟气中通入SO_2体积分数在0.02%以下时,Fe_(0.1)Ce_(0.07)Mn_(0.4)/TiO_2催化剂呈现出良好的抗硫性,且停止通入SO_2时催化剂的脱硝活性可恢复至初始水平;当通入SO_2的体积分数增加至0.04%时,催化剂会发生不可逆失活。表征结果显示:(NH_4)_2SO_4在催化剂表面的沉积和活性组分锰氧化物的硫酸化(生成MnSO_4)是催化剂硫中毒的主要原因;中毒后的催化剂比表面积显著降低,氧化还原能力减弱;催化剂Lewis酸的酸性大幅度减弱是催化剂活性降低的重要原因。     

废弃SCR催化剂中钒和钨的浸出及回收

采用NaOH溶液一次性浸出废弃SCR催化剂中的钒和钨,并用硫酸对浸出液进行除杂,再利用NH4Cl和硫酸分步对浸出液中的钒和钨进行沉淀回收。在NaOH质量分数40%、液固比8、浸出时间4 h、浸出温度90℃的最佳碱浸条件下,钒和钨的浸出率分别达到90.44%和84.49%。除杂过程的铝去除率达到100%,硅去除率达到77.56%。在沉钒pH为8.0、n(NH_4~+)∶n(V)为4的最佳沉钒条件下,钒回收率达到82.79%。在n(SO_4~(2-))∶n(W)为2的最佳沉钨条件下,钨回收率达到76.41%。     

整体式催化剂选择性催化氧化硫化氢

在堇青石蜂窝陶瓷基体上分两步涂覆了SiO₂和TiO₂两种涂层,再通过浸渍法制备了V₂O₅/TiO₂-SiO₂/堇青石整体式催化剂。采用BET、XRD、XRF、SEM和H₂-TPR等方法对催化剂进行了表征,并对催化剂的H₂S选择性催化氧化活性进行了评价。结果表明：V₂O₅负载量为20%（w）时,催化剂的活性最好;在反应温度180 ℃、空速3 000 h^-1、V（O₂）∶V（H₂S）=0.5的条件下,转化率达96.94%,硫产率达95.41%。在40 h的稳定性试验过程中,转化率稳定在96%左右,硫产率稳定在94%左右,催化剂的稳定性较好。与传统颗粒状催化剂相比,该整体式催化剂更具工业应用前景。     

固态反应法制备FeHY催化剂及其催化降解活性艳蓝的性能研究

分别以NaY、NH4Y和HY沸石为载体,以乙酰丙酮铁为铁源,采用固态反应法制备了铁负载量均为10%（w）的FeNaY-10、FeNH4Y-10和FeHY-10催化剂。考察了各催化剂对活性艳蓝（KN-R）的降解效果,其中FeHY-10的催化降解效果最佳。采用XRD和FTIR技术对FeHY-10催化剂进行表征。表征结果显示,FeHY催化剂晶体结构仍然保持了Y分子筛特有的孔道结构,铁物种在Y 分子筛表面高度分散。催化降解实验表明,催化降解KN-R的最佳工艺条件为KN-R溶液（质量浓度为300 mg/L）加入量为50 mL、溶液pH为2、催化剂FeHY-25（铁负载量为25%（w））加入量为0.281 3 g、H2O2质量浓度为6.356 g/L、降解温度为35 ℃、降解时间为140 min,在此工艺条件下FeHY催化剂对KN-R的降解率为97.4%。     

Studies on process optimization of biodiesel production from waste cooking and palm oil

This work investigated the optimisation of biodiesel production from waste cooking oil (WCO) and palm oil using a two-step transesterification process for WCO and base catalysed transesterification for palm oil. Transesterification reactions were carried out to investigate the effects of prepared catalyst CaO, methanol/WCO and methanol/palm oil ratio and temperature on the yield of biodiesel. A series of experiments were conducted to determine the best conditions for biodiesel production, using methanol/oil ratio between 4:1 and 11:1 and contact time varying between 2 and 4 h. Biodiesel yield of around 90 and 70% was obtained for palm and waste cooking oil at the methanol/oil ratios of 6:1 and 8:1 at temperature of 60 °C for reaction time of 4 h using prepared CaO as catalyst. The physicochemical properties of palm and WCO biodiesel were carried out using standard methods, while the fatty acid profile was determined using gas chromatography. The investigation concludes that biodiesel obtained from palm and waste cooking oil was within the specified limit.