苯酚
异丙苯
分解
催化作用
化学
tar(计算)
产量(工程)
选择性
有机化学
苯
核化学
材料科学
计算机科学
冶金
程序设计语言
作者
Changjun Zou,Pinwen Zhao,Ju Ge,LI Jianxiu,Linchao Yu,Qiu Jun,Rangong Sun
标识
DOI:10.1016/j.psep.2012.08.005
摘要
The base catalyst LZ-2, which was the mixture of CaO and Na–NaOH/Al2O3·3H2O, was chosen for the decomposition of phenol tar to generate valuable chemicals. The selectivity of LZ-2 for dimethyl phenyl carbinol, α-methyl styrene dimer and cumenyl phenol was 100%, 100% and 98%, respectively. Under the optimum operating conditions of catalyst 2.5 wt%, operating temperature 603.15 K and decomposition time 3.5 h, decomposition ratios of cumenyl phenol and dimethyl phenyl carbinol were 98.7% and 99.97%, respectively. In addition, the experimental repeatability demonstrated that the total yield of valuable chemicals still reached 90.1% after the catalyst being used five times. Mass and energy balance indicated that the catalytic decomposition was a high potential for the recycling of chemicals from phenol tar.
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