共查询到18条相似文献,搜索用时 62 毫秒
1.
2.
3.
4.
催化湿式氧化法是一种有效的处理有毒、有害、高浓度有机废水的水处理技术。文章对催化湿式氧化技术的机理、催化剂的组成、分类、特点、主要技术指标、参数及目前的应用等情况做了介绍。指出催化剂的加入能够极大的提高湿式氧化技术对有机物的降解效率,高效、稳定的催化剂的研制是降低湿式氧化反应温度与压力的有效手段。催化湿式氧化技术是较有发展前途的水处理技术。 相似文献
5.
燃煤烟气中有机污染物的排放逐渐引起重视。锰铈(MnCe)基催化剂被认为是一种低温高效、低成本的可应用于燃煤烟气污染物脱除的催化剂。本文通过浸渍法制备了MnCe基催化剂,通过物理化学表征和烟气模拟台架实验,研究了MnCe基催化剂配比、反应工况、烟气复杂组分(H2O、SO2、NH3、NO)以及典型污染物脱除过程(Hg0和NO催化转化)对催化脱除烟气中邻二甲苯行为的影响和规律。实验结果表明,Mn和Ce摩尔比为6∶4时催化剂脱除邻二甲苯效率良好。反应空速和MnCe负载量在低温下对催化脱除效率影响显著。烟气中H2O、SO2、NH3、NO等组分对催化产生抑制作用,但抑制程度与作用机理具有显著差异。MnCe基催化剂对烟气SCR脱硝与Hg0催化氧化皆具有较高效率,且受烟气中邻二甲苯影响较小;但受SCR气氛与Hg0抑制,邻二甲苯催化脱除反应效率明显降低。 相似文献
6.
锰氧化物具有活性高、毒性低、资源丰富、合成方法多样等优点,常作为许多催化反应的催化剂或载体材料。该文综述了近年来锰氧化物催化剂的研究进展,主要介绍了单一锰氧化物、掺杂改性的锰氧化物以及锰氧化物复合材料在甲醛催化氧化反应中的催化性能;讨论了形貌、晶型结构以及其他因素对催化性能的影响;并归纳了一部分甲醛催化氧化的反应机理;最后指出要发展高效、经济、环保的锰氧化物催化剂,通过构建更多的缺陷、添加助剂、掺杂改性等方法,增加活性面和活性位的数量,来提高锰氧化物的催化性能是未来的主要研究方向。 相似文献
7.
8.
采用氧化还原共沉淀法制备系列不同配比的锰铈复合氧化物,用于CO和CH4催化氧化,考察不同焙烧温度对催化剂性能的影响。研究表明,焙烧温度500℃和Mn与Ce物质的量比为5∶5的催化剂具备最优的CO和CH4催化氧化性能。催化剂在90℃时,CO转化率可达100%;对于CH4催化氧化,反应温度500℃时,CH4转化率为80%。通过N2吸附-脱附、H2-TPR和XRD等研究其物化结构性能,结果表明,在系列催化剂中,焙烧温度500℃和Mn与Ce物质的量比为5∶5的催化剂具有最高的比表面积和最活泼的晶格氧,可能是其具有优异催化活性的原因。 相似文献
9.
湿式催化氧化法废水处理中催化剂和实验条件的优选 总被引:3,自引:0,他引:3
研究了湿式催化氧化法在处理难降解有机废水中催化剂的选择和实验条件的优化。在催化剂选择实验中以分子筛为载体共制备一元催化剂、二元催化剂和三元催化剂共计 16种 ,并以之分别处理分散黄、分散蓝、分散红、活性红和活性黑 5种染料以及甲基橙 ,得出了Ce系列和Cu系列的催化剂活性最高 ,COD和浊度的去除率最高可达 90 0 %以上。在以活性红染料为处理对象进行了条件的优化实验中 ,得到了最佳的条件是每 10 0mL活性红染料废水应加入H2 O2 溶液1 0mL ,催化剂 1 0g ,处理时间为 2 0h。 相似文献
10.
以Mn-Al-O为载体,钼酸盐为活性成分的前驱体,采用共沉淀-浸渍法制备出Mo-Mn-Al-O催化剂,使用ICP-OES、BET、XRD和XPS方法对其进行表征,研究其在常温常压下催化湿式氧化阳离子型染料废水的催化活性。实验结果表明,Mo的浸渍浓度为1.5 mol·L-1、浸渍温度为55℃、焙烧时间为3 h和焙烧温度为400℃下制备出的Mo-Mn-Al-O催化剂对阳离子红GTL、阳离子红X-GRL、阳离子黄X-GL和阳离子蓝X-BL都有较好的催化性能。特别是,当催化剂投加量为2.72 g·L-1时,反应1 h后对阳离子红GTL的脱色率和TOC去除率分别达到74.8%和64.5%。 相似文献
11.
研究了阿布拉霉素废水的湿式空气氧化和混凝-酸解预处理技术。分析了COD、阿布拉霉素、NH4+浓度、BOD5/COD。监测了废水的色度和味。在1L反应器中,于200℃和4 MPa条件下,对阿布拉霉素废水进行了无催化剂、RuO2/Al2O3和RuO2/CeO2/Al2O3的湿式空气氧化。结果表明在湿式空气氧化法中,使用催化剂RuO2/Al2O3和RuO2/CeO2/Al2O3反应150 min后,阿布拉霉素的去除率分别达到50.2%和55.0%,COD去除率达到40.0%和46.0%,BOD5/COD增加到0.49和0.54。使用混凝-酸解法预处理,COD和阿布拉霉素去除率轻微下降,BOD5/COD增加到0.45,污水不适合生物处理。在WAO中,废水的色度和味被有效控制,反应时间明显缩短。在阿布拉霉素废水的湿式空气氧化中,HO2.可以促进有机化合物氧化。CeO2的加入能够促进阿布拉霉素废水的湿式空气氧化中催化剂RuO2/Al2O3的活性和稳定性。 相似文献
12.
Catalytic wet air oxidation (CWAO) was investigated in laboratory-scale experiments for the treatment of o-chlorophenol in wastewater. Experimental results showed that wet air oxidation (WAO) process in the absence of catalyst was also effective for o-chlorophenol in wastewater treatment. Up to 80% of the initial CODCr was removed by wet air oxidation at 270℃ with twice amount of the required stoichiometric oxygen supply. At temperature of 150℃, the removal rate of CODCr was only 30%. Fe2(SO4)3, CuSO4, Cu(NO3)2 and MnSO4 exhibited high catalytic activity. Higher removal rate of CODCr was obtained by CWAO. More than 96% of the initial CODCr was removed at 270℃ and 84.6%-93.6% of the initial CODCr was removed at 150℃. Mixed catalysts had better catalytic activity for the degradation of o-chlorophenol in wastewater. 相似文献
13.
Catalytic wet air oxidation (CWAO) was investigated in laboratory-scale experiments for the treatment of o-chlorophenol in wastewater. Experimental results showed that wet air oxidation (WAO) process in the absence of catalyst was also effective for o-chlorophenol in wastewater treatment. Up to 80% of the initial CODcr was removed by wet air oxidation at 270℃ with twice amount of the required stoichiometric oxygen supply. At temperature of 150℃, the removal rate of CODCr was only 30%. Fe2(SO4)3, CuSO4, Cu(NO3)2 and MnSO4 exhibited high catalytic activity. Higher removal rate of CODcr was obtained by CWAO. More than 96% of the initial CODcr was removed at 270℃ and 84.6%-93.6% of the initial COD Cr was removed at 150℃. Mixed catalysts had better catalytic activity for the degradation of o-chlorophenol in wastewater. 相似文献
14.
郑育元 《化学反应工程与工艺》2017,33(2)
以纳米TiO_2为载体,通过优化制备方法,合成了高活性的Ru/TiO_2贵金属催化剂,采用X射线衍射(XRD)、N_2物理吸附、程序升温还原(H_2-TPR)和透射电镜(TEM)等手段对催化剂进行表征,并将制备的催化剂应用到湿式氧化处理3种有机酸模拟废水中。研究表明,氢气还原有助于Ru在TiO_2表面的分散,由此制备的催化剂氧化活性较高。在200℃,初始氧压3 MPa的条件下反应2 h,Ru/TiO_2在湿式氧化处理丙烯酸、丁二酸和乙酸有机酸模拟废水时,化学需氧量(COD)去除率分别达到95.3%,91.6%和70.1%。 相似文献
15.
16.
Alicia Rubalcaba María Eugenia Surez-Ojeda Julin Carrera Josep Font Frank Stüber Christophe Bengoa Agustí Fortuny Azael Fabregat 《Catalysis Today》2007,124(3-4):191-197
The aim of this work is to study the viability of the H2O2 Promoted Catalytic Wet Air Oxidation (PP-CWAO) process, using activated carbon (AC) as catalyst, to increase the biodegradability of phenolic aqueous solutions. Seventy-two hours experiments were performed in a trickle bed reactor at 140 °C and 2 bar of oxygen partial pressure. Feed concentrations, in terms of theoretical chemical oxygen demand (ThCOD), were 11.8 g COD l−1 for phenol, 12.6 g COD l−1 for o-cresol and 8.0 g COD l−1 for p-nitrophenol. Air was used as main oxidant and 20% of the stoichiometric amount of H2O2 needed for pollutant complete mineralisation was added as oxidation promoter. Adding H2O2 to the CWAO process not only increases pollutant removal but also leads to higher mineralisation of the remaining oxidation products. For instance, removal of phenol, o-cresol and p-nitrophenol increase from 45, 33 and 15% in the CWAO process to 64, 64 and 49% in the PP-CWAO process. In addition, the PP-CWAO process leads to better biodegradability enhancements, when compared to CWAO, as demonstrated by the respirometric tests. However, it is still necessary to improve the oxidation step in order to assure more biodegradable effluents that could be combined with a subsequent biological wastewater plant. 相似文献
17.