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Au/γ-Al_2O_3催化剂上高浓度甲醇催化消除反应的研究 被引量:1

The Study of Catalytic Elimination of High Concentration Methanol on Supported Au/γ-Al_2O_3 Catalysts
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摘要 采用沉积沉淀法制备了负载型Au/γ-Al2O3催化剂,并进行了BET、SEM等表征.对高浓度甲醇蒸汽进行催化消除反应.探讨了载体粒径、金含量和活化气体(O2、N2、H2)对催化剂性能的影响.结果表明:载体粒径不同的催化剂表面积不同,不同的活化气体对反应产物有很大影响.在O2活化的最佳催化剂Au(2.0%)/γ-Al2O3(0.4-0.5mm)上浓度为86.3g/m3的甲醇的最低全转化温度是170℃,产物中CO2和甲醚的选择性分别为99.7%和0.3%,达到国家安全排放标准.图1,表3,参16. The supported Au/γ-Al2O3 catalysts were prepared by deposition-precipitation method. Catalytic elimination of methanol vapor was carried out.The effects of the diameter of carrier, the gold contents and pretreated gases (O2, N2, H2) on activity of the catalysts were studied. Results show that the surface area of catalysts supported on different diameter of carrier is not the same value, the difference of pretreated gases has great influence on the products of methanol. Over the optimum catalyst Au (2%)/γ-Al2O3(0.4-0.5 mm) pretreated by O2, the lowest temperature at which methanol (86.3 g/m^3) has the total conversion is 170℃ , the selectivity of CO2 and methyl ether is 99.7% and 0.3% respectively, which attains the national security exhaustion standard, 1fig., 3tabs., 16refs.
出处 《湖南科技大学学报(自然科学版)》 CAS 北大核心 2006年第3期77-80,共4页 Journal of Hunan University of Science And Technology:Natural Science Edition
基金 湖南省自然科学基金资助项目(05JJ30143)
关键词 负载型Au/γ-Al2O3催化剂 甲醇 催化消除 supported Au/γ-Al2O3 catalyst methanol catalytic elimination
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  • 1[3]CORDI E M,O'NEILL P J,FALCONER J L.Transient Oxidation of Volatile Organic Compounds on a CuO/Al203 Catalyst[J].Applied Catalysis B:Environmental,1997,14:23-36.
  • 2[4]PARIDA K M,SAMAL A.Catslytic Combustion of Volatile Organic Compounds on Indian Ocean Manganese Nodules[J].Applied Catalysis A:General,1999,182:249-256.
  • 3[5]SIMONA M,SALVATORE S,CARMELO C,et al.Catalytic Combustion of Volatile Organic Compounds on Gold/Iron Oxide Catalysts[J].Applied Catalysis B:Environmental,2000,28:245-251.
  • 4[6]SALVATORE S,SIMONA M,CARMELO C,et al.Catalytic Combustion of Volatile Organic Compounds over Group IB Metal Catalysts an Fe2O3[J].Catalysis Communications,2001,2:229-232.
  • 5[7]SAMANTARAY S K,PARIDA K.Modified Ti02-Si02 Mixed Oxides 1.Fffect of Manganese Concentration and Activation Temperature towards Catalytic Combustion of Volatile Organic Compounds[J].Applied Catalysis B:Environmental,2005,57:83-91.
  • 6[8]SALVATORE S M,SIMONA M,CARMELO C,et al.Catalytic Combustion of Volatile Organic Compounds on Gold/Cerium Oxide Catalysts[J].Applied Catalysis B:Environmental,2003,40:43-49.
  • 7[9]STUART H T,CATHERINE S H,GRAHAM J H,et al.The Activity and Mechanism of Uranium Oxide Catalysts for the Oxidative Destruction of Volatile Organic Compounds[J].Catalysis Today,2000,59:249-259.
  • 8[10]HARUTA M,UEDA A,TSUBOTA S,et al.Low-temperature Catalytic Combustion of Methanol and Its Decomposed Derivatives over Supported Gold Catalysts[J].Catalysis Today,1996,29:443-447.
  • 9[11]CORDI E M,FALCONER J L.Oxidation of Volatile Organic Compounds on Al203,Pd/ Al203 and PdO/ Al203 Catalysts[J].Journal of Catalysis,1996,162:104-117.
  • 10[12]SIMONA M,SALVATORE S,CARMELO C,et al.Influence of Catalyst Pretrestments on Volatile Organic Compounds Oxidation over Cold/Iron Oxide[J].Applied Catalysis A:General,2001,34:277-285.

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