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Pt/C催化剂制备方法的选择 总被引:1,自引:0,他引:1
研究了以HCl酸洗、H_2O_2、浓H_2SO_4、HNO_3氧化处理后的活性炭为载体,用不同方法制备了Pt担载量为3%的担载型Pt/C催化剂。TEM统计结果表明,HCl酸洗、HNO_3氧化活性炭为载体,甲醛还原法制备的催化剂分散度最高,平均粒径最小为2.2nm。FT-IR结果表明,HNO_3氧化处理活性炭,活性炭表面含氧基团明显增加。 相似文献
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为研究水蒸气处理后热处理对炭黑表面特性的影响,提高DMFC阳极催化剂的催化活性,利用先水蒸气处理后热处理的Vnlcan XC-72炭黑为载体制备Pt-Ru/C催化剂,与水蒸气处理的和未经处理的炭载体制备Pt-Ru/C催化剂的性能进行比较.采用XPS和BET测试了处理后的炭粉表面的含氧浓度和比表面,结果表明:水蒸气处理后,炭载体比表面积增大,含氧浓度降低;水蒸气处理后热处理,炭载体比表面积进一步减小,含氧浓度增加.用XRD对催化剂的结构进行了表征,结果表明:水蒸气处理后热处理的炭黑为载体制备Pt-Ru/C催化剂结晶状态良好,催化剂颗粒较小.在0.5mol/L CH3OH和0.5mol/L H2SO4混合溶液中,利用玻炭电极测试了循环伏安曲线和阶跃电位曲线,结果表明:用先水蒸气处理后热处理的炭粉为载体制备的催化剂比仅水蒸气处理和未经处理的炭粉为载体制备的催化剂的活性最高. 相似文献
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通过活性炭负载铂制备了一种硅氢加成反应用多相催化剂(Pt/C),考察了活性炭处理、还原pH值、催化剂铂负载量、反应时间对Pt/C催化苯乙烯与三乙氧基硅烷加成反应催化性能的影响.结果表明:用15%硝酸处理活性炭载体,pH值为8.5环境下还原的负载量为5%的Pt/C催化剂具有最好的催化效果,苯乙烯转换率为100%,β-加成产物选择性为94.9%. 相似文献
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以邻氯硝基苯为原料,在碱性环境中以Pt/C为催化剂,进行加氢还原生成2,2'-二氯氢化偶氮苯。考察溶剂、反应压力、反应温度及氢氧化钠浓度等对加氢反应的影响,确定了最佳的工艺条件,在氢氧化钠浓度20%、甲苯/氢氧化钠溶液作溶剂、反应温度80℃和反应压力0.8 MPa条件下,2,2'-二氯氢化偶氮苯收率超过88%。与传统硫化碱还原或铁粉还原工艺相比,催化加氢法在减少废水和降低成本等方面优势较大。 相似文献
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The influence of the acid treatment on cyclohexanone selectivity of phenol hydrogenation over Pd on active carbon was studied in liquid phase reaction and by temperature-programmed desorption. Acid treatment of activated carbon led to an increased cyclohexanone/cyclohexanol ratio. Acid modification of the carbon support enriched the electron density of Pd, and enhanced the desorption of the phenoxy species, which resulted in improved cyclohexanone selectivity in phenol hydrogenation. 相似文献
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硝基苯催化加氢合成对氨基苯酚工艺研究 总被引:1,自引:0,他引:1
采用Pt/C作为催化剂对硝基苯选择加氢合成对氨基苯酚进行了研究,考察了温度、酸度、反应时间、压力、催化剂等因素对反应的影响,确定了反应的优化条件。在反应温度75℃、压力2.45kPa、硫酸浓度13%、反应时间4h的条件下,用2%Pt/C催化加氢还原硝基苯可获得较高质量的产物对氨基苯酚。 相似文献
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Effects of carbonization temperature and time during carbon riveting process on the stability of Pt/C catalysts have been investigated systematically. X‐ray diffraction, transmission electron microscopy, cyclic voltammograms, and accelerated potential cycling tests have been performed to characterize the catalysts. The experimental results show that the activity of the riveted Pt/C catalyst decreases with the increasing of the heat‐treated temperature and the extension of heat‐treated time due to sintering of Pt nanoparticles. The stability of the carbon riveted Pt/C catalysts exhibits the increasing trend with the increase of the carbonization time and temperature. Considering both of the activity and stability of the riveted Pt/C catalysts, the optimized carbonization temperature and time are 400 °C and 60 min for a Pt/VulcanXC‐72 catalyst with starting particle size before carbonization of 2.2 nm and 20 wt% platinum loading, respectively. 相似文献
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采用沉积-沉淀法制备了4% Pd/C催化剂(Pd质量分数4%),分别以硝酸、盐酸、双氧水和氨水4种溶剂对Pd/C的载体活性炭进行改性,并对载体活性炭的比表面积和孔结构、零电荷点(PZC)以及活性组分Pd的分散度进行了表征,研究了活性炭改性对Pd催化剂在松香歧化反应中催化性能的影响。结果表明:经氨水改性后活性炭比表面积孔径增大且活性炭PZC值升高,有利于活性组分Pd在载体表面的分散,以氨水改性活性炭为载体制备得到的Pd/C催化剂活性最高,在催化剂投料量为0.03%,280℃反应2 h条件下,脱氢枞酸质量分数高达81.7%。 相似文献
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The kinetics of catalytic hydrogenation of ortho-nitrochlorobenzene to 2,2'-dichloroazoxybenzene on platinum/carbon catalyst is investigated in a slurry reactor with the temperature range of 313-343 K, and ortho-chloroaniline is formed as a byproduct. Models based on Rideal-Eley and Langmuir-Hinshelwood mechanism have been proposed based on the rate data and the kinetic regime. The former model can be used to fit the experimental data better. Reaction controlling steps are physical adsorption of hydrogen and adsorbed ortho-nitrochlorobenzene reacted on the surface of catalyst. 相似文献
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The kinetics of catalytic hydrogenation of ortho-nitrochlorobenzene to 2,2‘-dichloroazoxybenzene on platinum/carbon catalyst is investigated in a slurry reactor with the temperature range of 313--343 K, and orthochloroaniline is formed as a byproduct. Models based on Rideal-Eley and Langmuir-Hinshelwood mechanism have been proposed based on the rate data and the kinetic regime. The former model can be used to fit the experimental data better. Reaction controlling steps are physical adsorption of hydrogen and adsorbed ortho-nitrochlorobenzene reacted on the surface of catalyst. 相似文献
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