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Study on Methanol Synthesis with the Analog Components of Bluecoke Furnace Gas by Rich Oxygen Carbonization

机译:用富氧碳化与蓝康炉气体模拟成分的甲醇合成研究

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According to the components of bluecoke furnace gas by rich oxygen carbonization, the methane conversion and methanol synthesis processes with simulation mix gas were separately researched using the self-made catalysts. The results show that the conversion rate of methane could achieve about 95% under the conditions of temperature of 800°C, space velocity of 9000h~(-1) and the ratio of water to hydrocarbon of about 3.0 with self-made Ni/γ-Al_2O_3 catalyst. For synthesis of methanol with self-made CuO-ZnO-Al_2O_3 catalyst in fixed reactor from the reformed gas, the space time yield and selectivity of coarse methanol respectively reached 1.5451g·g~(-1)·h~(-1) and 99.6143% under the conditions of temperature of 240°C, pressure of 5.5MPa and space velocity of 12000h~(-1).
机译:根据通过富氧碳化的BlueCoke炉气体的组分,使用自制催化剂分别研究了具有模拟混合气体的甲烷转化和甲醇合成方法。结果表明,甲烷的转化率可以在800°C的温度条件下达到约95%,空间速度为9000h〜(-1)的条件和约3.0的水与自制Ni /γ的比率。 -al_2O_3催化剂。对于从重整气体的固定反应器中具有自制作CuO-ZnO-Al_2O_3催化剂的甲醇,空间时间产率和粗甲醇的选择性分别达到1.5451g·g〜(-1)·h〜(-1)和99.6143%在温度为240°C的条件下,压力为5.5MPa和4000h〜(-1)的空速。

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