کد مقاله | کد نشریه | سال انتشار | مقاله انگلیسی | نسخه تمام متن |
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148406 | 456411 | 2013 | 9 صفحه PDF | دانلود رایگان |
![عکس صفحه اول مقاله: A comparative investigation on the catalytic activity of H-Al-MCM-48 and H-Zr-MCM-48 mesoporous molecular sieve on alkylation of phenol with tert-butyl alcohol A comparative investigation on the catalytic activity of H-Al-MCM-48 and H-Zr-MCM-48 mesoporous molecular sieve on alkylation of phenol with tert-butyl alcohol](/preview/png/148406.png)
• Several H-Al-MCM-48 and H-Zr-MCM-48 solid acid catalysts were prepared via wet impregnation method.
• Activities of catalysts were evaluated by alkylation reaction of phenol and tert-butyl alcohol.
• H-Al-MCM-48-25 catalyst exhibits much high catalytic activity as compared with the others catalysts.
• Under the optimum reaction conditions, H-Al-MCM-48-25 catalyst gives a maximum phenol conversion of 98.9%.
Mesoporous H-Al (or Zr)-MCM-48 solid acid catalysts were prepared by wet impregnation method through using Al (or Zr)-MCM-48 mesoporous molecular sieves derived from conventional hydrothermal method as starting materials. These solid acid catalysts were characterized by XRD, TEM, NH3-TPD and N2 physical adsorption, respectively. The alkylation of phenol with tert-butyl alcohol was carried out over these solid acid catalysts. The effect of various factors including reactant molar ratio, weight hour space velocity (WHSV), reaction time and temperature on phenol conversion and product selectivity was investigated and the results were discussed. Experimental results reveal that the resulting solid acid catalysts still retained a typical cubic mesoporous framework of MCM-48. Under comparable conditions, the H-Al-MCM-48-25 catalyst exhibits much high catalytic activity and gives a maximum phenol conversion of 98.9% with 70.3% selectivity to 4-t-butyl phenol (4-TBP). The optimum reaction conditions over these solid acid catalysts are the following: WHSV = 5 h−1, time = 2 h, temperature = 140 °C, the molar ratio of tert-butyl alcohol:phenol = 2:1.
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Journal: Chemical Engineering Journal - Volume 230, 15 August 2013, Pages 124–132