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作 者:ZHU Lihua XU Feng BI Yewu SHEN Bin
机构地区:[1]Heilongjiang University of Science and Technology
出 处:《Chinese Journal Of Geochemistry》2014年第2期183-186,共4页中国地球化学学报
基 金:supported jointly by the National Natural Science Foundation of China(No.51004045);Scientific Research Fund of Education Department of Heilongjiang Province,China(No.12511481)
摘 要:The influencing factors for liquid phase catalytic oxidation of mine gas to methanol(in form of CH3COOCH3) are studied using the self-established experimental apparatus. The results show that CH3COOCH3(target product) is obtained by using CH3COOH as reaction solvent, and the yield of target product increases with the increasing of reaction temperature, gas pressure and reaction time. In the mine gas-Pd(OAc)2-CH3COOH system, the yield of CH3COOCH3 increases with the increasing of addition of Pd(OAc)2 which is redox catalyst for mine gas conversion. The yield of CH3COOCH3 will be greatly improved by composite additional oxidant which is obtained by equimolar mix of p-benzoquinone with NO2.The influencing factors for liquid phase catalytic oxidation of mine gas to methanol (in form of CHaCOOCH3) are studied using the self-established experimental apparatus. The results show that CH3COOCH3 (target product) is obtained by using CH3COOH as reaction solvent, and the yield of target product increases with the increasing of reaction temperature, gas pressure and reaction time. In the mine gas-Pd(OAc)2-CHaCOOH system, the yield of CHaCOOCH3 increases with the increasing of addition of Pd(OAc)2 which is redox catalyst for mine gas conversion. The yield of CH3COOCH3 will be greatly improved by composite additional oxidant which is obtained by equimolar mix of p-benzoquinone with NO2.
关 键 词:液相催化氧化 矿井瓦斯 影响因素 甲醇 还原催化剂 实验装置 反应溶剂 反应温度
分 类 号:TD712[矿业工程—矿井通风与安全]
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