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Catalytic upgrading of lignite pyrolysis volatiles over modified HY zeolites

机译:改性HY沸石对褐煤热解挥发物的催化提质

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HY zeolite is modified by hydrothermal and HNO3 treatment and used as the catalyst to upgrade Baiyinghua pyrolysis volatiles on a fixed-bed reactor at 600 degrees C. The results show that hydrothermal and acid treatment obviously affect zeolite structure and upgrading of pyrolysis volatiles. The dealumination of HY increases with hydrothermal temperature, resulting in the decrease of total surface area and acid amount and the formation of larger pores. However, the content and yield of light tar are enhanced over modified HY, and the cracking of volatiles into gas is retarded. Acid treatment of hydrothermal modified HY at 650 degrees C removes extra-framework Al, improves surface area and the volatiles cracking. But high acid concentration leads to the destruction of zeolite structure, and is unfavorable to the upgrading. Modified HY by treatment at 650 degrees C and 0.8 mol/L HNO3 shows the best performance in catalytic volatiles upgrading. About 81.5 wt% light tar content and 61.1% light aromatic hydrocarbons content can be obtained. Especially, the yields of naphthalene and methylnaphthalene are increased by 8.9 and 6.8 times. The content of oxygenated PAHs is reduced by 4.3 times. The improved performance is mainly due to high surface area, large pore diameter and suitable acidity.
机译:HY沸石经过水热和HNO3处理后改性,并作为催化剂在600摄氏度的固定床反应器上对白英华热解挥发物进行升级。结果表明,水热和酸处理明显影响沸石的结构和热解挥发物的升级。 HY的脱铝作用随水热温度的升高而增加,导致总表面积和酸量减少,并形成较大的孔。但是,与改性的HY相比,轻质焦油的含量和收率得到提高,并且挥发物向气体的裂化得到了抑制。在650摄氏度下对水热改性HY进行酸处理可去除多余的Al,改善表面积和挥发物裂解。但是高浓度的酸会导致沸石结构的破坏,不利于提质。通过在650摄氏度和0.8 mol / L的HNO3中处理改性的HY在催化挥发物的提质方面显示出最佳性能。可获得约81.5重量%的轻焦油含量和61.1%的轻质芳烃含量。尤其是,萘和甲基萘的产率分别提高了8.9和6.8倍。含氧多环芳烃的含量减少了4.3倍。性能的提高主要归因于高表面积,大孔径和合适的酸度。

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