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Low-temperature CO oxidation over CuO-CeO_2/SiO_2 catalysts:Effect of CeO_2 content and carrier porosity 被引量:5
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作者 Jingjie Luo Wei Chu +2 位作者 Huiyuan Xu Chengfa Jiang Tao Zhang 《Journal of Natural Gas Chemistry》 EI CAS CSCD 2010年第4期355-361,共7页
The effects of CeO2 contents and silica carrier porosity with their pore diameters ranging from 5.2 nm to 12.5 nm of CuO-CeO2/SiO2 cata-lysts in CO oxidation were investigated.The catalysts were characterized by N2 ad... The effects of CeO2 contents and silica carrier porosity with their pore diameters ranging from 5.2 nm to 12.5 nm of CuO-CeO2/SiO2 cata-lysts in CO oxidation were investigated.The catalysts were characterized by N2 adsorption/desorption at low temperature,X-ray diffraction (XRD),temperature-programmed reduction by H2 (H2-TPR),oxygen temperature programmed desorption (O2-TPD) and X-ray photoelectron spectroscopy (XPS).The results suggested that,the ceria content and the porosity of SiO2 carrier possessed great impacts on the structures and catalytic performances of CuO-CeO2/SiO2 catalysts.When appropriate content of CeO2 (Ce content 8 wt%) was added,the catalytic activity was greatly enhanced.In the catalyst supported on silica carrier with larger pore diameter,higher dispersion of CuO was observed,better agglomeration-resistant capacity was displayed and more lattice oxygen could be found,thus the CuO-CeO2 supported on Si-1 showed higher catalytic activity for low-temperature CO oxidation. 展开更多
关键词 cuo-ceo2 based catalyst silica carrier porosity carbon monoxide oxidation O2-TPD
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High performance CuO-CeO_2 catalysts for selective oxidation of CO in excess hydrogen:Effect of hydrothermal preparation conditions 被引量:2
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作者 Pengfei Zhu Jing Li +3 位作者 Qinqin Huang Siming Yan Mei Liu Renxian Zhou 《Journal of Natural Gas Chemistry》 EI CAS CSCD 2009年第3期346-353,共8页
High performance CuO-CeO2 catalysts for selective oxidation of CO in excess hydrogen were prepared by a hydrothermal method under different preparation conditions and evaluated for catalytic activities and selectiviti... High performance CuO-CeO2 catalysts for selective oxidation of CO in excess hydrogen were prepared by a hydrothermal method under different preparation conditions and evaluated for catalytic activities and selectivities. By changing the ^nCTAB/^nCe ratio and hydrothermal aging time, the catalytic activity of the CuO-CeO2 catalysts increased and the operating temperature window, in which the CO conversion was higher than 99%, was widened. XRD results showed no peaks of CuOx species and Cu-Ce-O solid solution were observed. On the other hand, Cu+ species in the CuO-CeO2 catalysts, which was associated with a strong interaction between copper oxide clusters and cerium oxide and could be favorable for improving the selective oxidation performance of CO in excess H2, were detected by H2-TPR and XPS techniques. 展开更多
关键词 selective oxidation CO excess hydrogen cuo-ceo2 catalyst HYDROTHERMAL preparation condition
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Low CO content hydrogen production from oxidative steam reforming of ethanol over CuO-CeO_2 catalysts at low-temperature 被引量:1
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作者 Xue Han Yunbo Yu +1 位作者 Hong He Jiaojiao Zhao 《Journal of Energy Chemistry》 SCIE EI CAS CSCD 2013年第6期861-868,共8页
CuO-CeO2 catalysts were prepared by a urea precipitation method for the oxidative steam reforming of ethanol at low-temperature.The catalytic performance was evaluated and the catalysts were characterized by inductive... CuO-CeO2 catalysts were prepared by a urea precipitation method for the oxidative steam reforming of ethanol at low-temperature.The catalytic performance was evaluated and the catalysts were characterized by inductively coupled plasma atomic emission spectroscopy,X-ray diffraction,temperature-programmed reduction,field emission scanning electron microscopy and thermo-gravimetric analysis.Over CuOCeO2 catalysts,H2 with low CO content was produced in the whole tested temperature range of 250–450 C.The non-noble metal catalyst 20CuCe showed higher H2production rate than 1%Rh/CeO2 catalyst at 300–400 C and the advantage was more obvious after 20 h testing at400 C.These results further confirmed that CuO-CeO2 catalysts may be suitable candidates for low temperature hydrogen production from ethanol. 展开更多
关键词 cuo-ceo2 catalyst hydrogen production oxidative steam reforming LOW-TEMPERATURE
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Effects of CuO-CeO<sub>2</sub>Addition on Structure and Catalytic Properties of Three Way Catalysts
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作者 Nguyen The Luong Nguyen Duy Tien +2 位作者 Eiji Yamasue Hideyuki Okumura Keiichi N. Ishihara 《Journal of Materials Science and Chemical Engineering》 2017年第12期28-39,共12页
The noble metals (Pt, Pd, Rh) supported on Cu-Ce mixed oxides with γ-Al2O3 washcoat/FeCrAl substrate were investigated as catalytic performance of Three Way Catalysts (TWC) under simulated automotive exhaust feed gas... The noble metals (Pt, Pd, Rh) supported on Cu-Ce mixed oxides with γ-Al2O3 washcoat/FeCrAl substrate were investigated as catalytic performance of Three Way Catalysts (TWC) under simulated automotive exhaust feed gas. The structural, morphological features and catalytic activity were observed by X-ray diffractometry (XRD), scanning electron microscopy (SEM), Brunauer-Emmett-Teller (BET), X-ray photoelectron spectroscopy (XPS) and GC-TCD (Varian CP-4900). The catalytic performance of noble metals (Pt, Rh, Pd) supported on Cu-Ce mixed oxides with γ-Al2O3 washcoat/FeCrAl substrate was be compared with noble metals (Pt, Rh, Pd) supported on Ce-Zr mixed oxides with γ-Al2O3 washcoat/FeCrAl substrate and only γ-Al2O3 washcoat/FeCrAl substrate at various stoichiometric ratio of oxygen. The results showed that the addition of Cu-Ce mixed oxides improved CO oxidation reaction at lower temperature during stable lambda of 1, the highest CO conversion of 99% is observed for the noble metals (Pt, Pd, Rh) support on Cu-Ce with γ-Al2O3 washcoat/FeCrAl substrate. The results also showed that, the addition of Cu-Ce mixed oxides promoted released oxygen, thus it improved strongly CO and C3H8 conversion at lean oxygen stoichiometric operation. 展开更多
关键词 Three-Way catalysts (TWCs) NOBLE Metals γ-Al2O3 WASHCOAT cuo-ceo2 CEO2-ZRO2
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钒钛系脱硝催化剂抗SO_(2)和H_(2)O中毒性能研究进展 被引量:7
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作者 张鹏 贾媛媛 +4 位作者 唐中华 刘兴誉 刘军强 刘光利 巫树锋 《现代化工》 CAS CSCD 北大核心 2021年第4期67-71,共5页
综述了SO_(2)和H2O造成钒钛系SCR催化剂中毒失活的机理,总结了金属氧化物和非金属氧化物掺杂提高催化剂抗硫抗水性能的研究进展。针对当前存在的问题,提出今后的研究重点是深入分析催化剂SO_(2)和H_(2)O中毒反应的微观过程,进一步考察... 综述了SO_(2)和H2O造成钒钛系SCR催化剂中毒失活的机理,总结了金属氧化物和非金属氧化物掺杂提高催化剂抗硫抗水性能的研究进展。针对当前存在的问题,提出今后的研究重点是深入分析催化剂SO_(2)和H_(2)O中毒反应的微观过程,进一步考察改性催化剂的成型工艺及工业应用效果,开发出温度窗口宽、抗硫抗水性能稳定且同时具备工业生产和应用条件的脱硝催化剂。 展开更多
关键词 钒钛系 SCR催化剂 SO_(2) H_(2)O 改性
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2-氨基-1,3-苯二甲酸二甲酯的合成及其路线优化
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作者 张齐 侯春燕 +1 位作者 王其宝 王鹏 《广州化工》 CAS 2020年第7期39-41,共3页
对2-氨基-1,3-苯二甲酸二甲酯的实验室量产合成进行优化,获得了最佳成本的路线:以低成本的1,3-二甲基-2-硝基苯为初始原料,选定氧化、串联酯化、催化加氢三个步骤进行合成。通过对路线中前两步的合成步骤进行优化,获得最佳合成工艺参数... 对2-氨基-1,3-苯二甲酸二甲酯的实验室量产合成进行优化,获得了最佳成本的路线:以低成本的1,3-二甲基-2-硝基苯为初始原料,选定氧化、串联酯化、催化加氢三个步骤进行合成。通过对路线中前两步的合成步骤进行优化,获得最佳合成工艺参数,解决了小量合成此化合物时间成本高的问题。在百克级别的合成中,以1,3-二甲基-2-硝基苯为初始原料计算的总产率49.8%,纯度99%以上。 展开更多
关键词 2-氨基-1 3-苯二甲酸二甲酯 相转移催化剂 高锰酸钾氧化 串联酯化反应
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LS系列催化剂在湛江东兴硫磺回收装置工业应用总结 被引量:3
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作者 吴潮汉 《炼油技术与工程》 CAS 2022年第2期50-54,共5页
介绍了LS系列催化剂在中国石化湛江东兴石油化工有限公司20 kt/a硫磺回收装置上的工业应用情况。2021年3月进行了工业标定,标定期间硫磺回收装置整体运行良好。标定结果表明:在100%运行负荷下,装置各项操作参数均处于技术指标范围内;吸... 介绍了LS系列催化剂在中国石化湛江东兴石油化工有限公司20 kt/a硫磺回收装置上的工业应用情况。2021年3月进行了工业标定,标定期间硫磺回收装置整体运行良好。标定结果表明:在100%运行负荷下,装置各项操作参数均处于技术指标范围内;吸收塔顶净化气中H_(2)S和COS质量浓度均小于20 mg/m^(3);LS系列催化剂活性高,级配合理,克劳斯单元单程总硫转化率均大于97%,总硫回收率达99.99%;所得液体硫磺产品各项指标均满足GB/T 2449.2—2015《工业硫磺第2部分:液体产品》中优等品的指标要求;碱洗前烟气中SO_(2)排放浓度均低于50 mg/m^(3),碱洗后烟气中SO_(2)排放浓度小于10 mg/m^(3),均满足GB 31570—2015《石油炼制工业污染物排放标准》大气污染物特别排放限值的要求。 展开更多
关键词 LS系列催化剂 硫磺回收装置 单程总硫转化率 总硫收率 SO_(2)排放浓度
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SDJF系列催化剂在硫回收装置中的应用
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作者 符昌焕 林金安 《硫酸工业》 CAS 2022年第11期40-44,共5页
介绍了山东骏飞环保科技有限公司SDJF系列催化剂在海南炼化公司80 kt/a硫回收装置中的工业应用情况。运行结果表明,在实际运行工况下,装置各项操作参数均处于技术指标范围内;吸收塔顶净化气中H2S和COS质量浓度均小于20 mg/m^(3);SDJF系... 介绍了山东骏飞环保科技有限公司SDJF系列催化剂在海南炼化公司80 kt/a硫回收装置中的工业应用情况。运行结果表明,在实际运行工况下,装置各项操作参数均处于技术指标范围内;吸收塔顶净化气中H2S和COS质量浓度均小于20 mg/m^(3);SDJF系列催化剂活性高,级配合理,克劳斯单元总硫回收率达99.99%;所得固体硫黄产品各项指标满足GB/T 2449.1—2021《工业硫磺第1部分:固体产品》中A级的技术指标要求;装置运行期间,尾气炉排放烟气中SO_(2)质量浓度小于30 mg/m^(3),满足GB 31570—2015《石油炼制工业污染物排放标准》大气污染物特别排放限值的要求。 展开更多
关键词 硫回收 SDJF系列催化剂 总硫收率 SO_(2) 排放浓度
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