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还原温度对溶胶法制备Pd/C催化剂性能与微观结构的影响 被引量:1

INFLUENCE OF REDUCTION TEMPERATURE ON CATALYTIC ACTIVITY AND MICROSTRUCTURE OF Pd/C CATALYSTS PREPARED BY COLLOIDAL METHOD
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摘要 采用钯溶胶法制备对苯二甲酸加氢精制用 Pd/C 催化剂,考察了还原温度对 Pd/C 催化剂活性的影响。通过 SEM、TEM、能谱、物理吸附、化学吸附等手段对 Pd/C 催化剂结构进行表征。结果表明:随着还原温度的升高,催化剂活性和分散度快速下降,当还原温度为10℃时,对羧基苯甲醛转化率接近100%,同时分散度也达到最高,所得催化剂 Pd 晶粒细小均匀,平均粒径为6.45 nm;30℃下制备的催化剂载体表面存在明显的团聚现象,Pd 晶粒平均粒径为15~20 nm,30℃下制备催化剂表面 Pd 含量约为10℃时的5倍;随着温度升高,聚氧乙烯基与水之间的氢键断裂,其增溶能力大幅下降,同时胶体中的 Pd 颗粒碰撞几率增加,造成胶体钯中 Pd 颗粒长大聚集,催化活性降低。 A series of Pd/C catalysts for hydropurification of terephthalic acid were prepared using sol-gel process. The effect of reduction temperature on the microstructure and activity of the catalysts were investigated by means of SEM,TEM,EDS,physisorption,chemisorption and HPLC. The results show that the activity and dispersion of Pd sharply decreases with the increase of reduction temperature.The conversion ratio of 4-CBA is close to 100% at reduction temperature of 10 ℃ and the dispersion of Pd also reaches the highest. The Pd particles at this condition are fine and equally distributed with aver-age size of about 6.45 nm. However,a lot of larger particles with size of 15-20 nm gather at the sur-face at reduction temperature of 30 ℃. The amount of Pd on the catalyst surface reduced at 30 ℃ is about five times the amounts of Pd on the surface reduced at 10 ℃. Higher temperature generally causes the breaking of hydrogen bond between polyoxyethylene group and water,leading to a great reduction of solubilization capacity,which further results in the growth of Pd grain and the decrease of activity of Pd/C catalysts because of increased collision probability of Pd colloids.
出处 《石油炼制与化工》 CAS CSCD 北大核心 2014年第9期47-51,共5页 Petroleum Processing and Petrochemicals
基金 国家自然科学基金项目(50904023) 河南省教育厅自然科学研究基金项目(2010B450001)
关键词 Pd C 催化剂 还原温度 溶胶法 微观结构 精对苯二甲酸 Pd/C catalyst reduction temperature sol-gel process microstructure purified tereph-thalic acid
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  • 1Azarpour A,Zahedi G.Performance analysis of crude tereph-thalic acid hydropurification in an industrial trickle-bed reac-tor experiencing catalyst deactivation[J].Chemical Engineer-ing Journal,2012,209:180-193.
  • 2Pellegrini R,Agostini G,Groppo E,et al.0.5 % Pd/C Cata-lyst for purification of terephthalic acid:Irreversible deactiva-tion in industrial plant[J].Journal of Catalysis,2011,280(2):150-160.
  • 3Pernicone N,Cerboni M,Prelazzi G,et al.An investigation on Pd/C industrial catalysts for the purification of terephthalic acid[J].Catalysis Today,1998,44(1/2/3/4):129-135.
  • 4Harada T,Ikeda S,Miyazaki M,et al.A simple method for preparing highly active palladium catalysts loaded on various carbon supports for liquid-phase oxidation and hydrogenation reaetions[J].Journal of Molecular Catalysis A:Chemical,2007,268(112):59-64.
  • 5陈祥,周立进,顾沛国,曾崇余.制备方法对钯碳催化剂表面性质及其加氢性能影响[J].南京工业大学学报(自然科学版),2005,27(5):93-96. 被引量:16
  • 6Marinella M,Luigi C,Carlo R.Hydrogenation catalysts:The United States,US 6066589[P].2000-05-23.
  • 7任中亮,盛丁杰.PTA加氢精制Pd/C催化剂活性降低原因及处理[J].聚酯工业,2011,24(3):25-29. 被引量:2
  • 8Li Kuo-Tseng,Hsu Ming-Hao,Wang Ikai.Palladium core-porous silica shell-nanoparticles for catalyzing the hydrogena-tion of 4-carboxybenzaldehyde [J ].Catalysis Communica-tions,2008,9(13):2257-2260.
  • 9堵文斌,王继元,朱庆奋,陈韶辉.pH值对粗对苯二甲酸加氢精制Pd/C催化剂性能的影响[J].石油炼制与化工,2011,42(3):38-41. 被引量:5
  • 10Romanenko A V,Tyschishin E A,Moroz E M,et al.Influ-ence of ruthenium addition on sintering of carbon-supportedpalladium[J].Applied Catalysis A:General,2002,227(1/2)117-123.

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