The reaction characteristics of phenolic hydroxyl group were studied under the conditions of direct coal liquefaction. 2-naphthol was used as a coal model compound in this study. Under the conditions of with and without catalysts, a series of experiments were conducted at different temperatures, pressures and reaction time. Gas chromatography-mass spectrometry and gas chromatography were used to identify and quantify the reactants and products respectively. The conversion of 2-naphthol rises with the increase of reaction temperature, initial pressure and catalyst amount. The results indicated that tem- perature had a significant effect on 2-naphthol conversion, which promoted the dehydroxylation reaction. However, initial pressure had an important influence on the hydrogenation of 2-naphthol and naphthalene. The iron catalyst plays a significant role of cracking instead of hydrogenation. It is concluded that the harsh reaction conditions of high temperature, high pressure, and more catalyst are conducive to promoting dehydroxylation of 2-naphthol. The reaction mechanism was put forward based the experimental results, in which 2-tetralone was an intermediate.
Bo-Wen MAXiao-Su ZHUWen-Bo LIXiao-Jing ZHANGShu-Feng DU
为了研究艾丁褐煤液化反应动力学,通过对煤液化产物进行分级处理,得到SO2-4/Fe2O3催化艾丁褐煤温和液化动力学模型,通过origin软件回归出各反应速率常数及相应的表观活化能和指前因子,最后对褐煤温和液化分级反应工艺提出初步设想。结果表明,模型能够较好地模拟动力学试验结果;液化反应中沥青质向酚转化的活化能为267.62 k J/mol,该过程对温度较敏感;反应组分的主要转化为油和沥青质,分别占48%和37%;随反应时间的延长,由沥青质转化得到的油和酚的量逐渐增加,由反应组分转化得到的油和酚的量先增加后趋于恒定,在一定时间内,反应组分是直接转化成油和酚的主要来源;沥青质向油的转化是油增加的速率控制步骤,沥青质向酚的转化是酚增加的速率控制步骤,在煤液化工艺流程中,实行分级加氢液化有利于控制、提高油和酚产率。
