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FOR REFORMING OF METHANE AND CARBON DIOXIDE, PREPARATION OF COBALT BASED CATALYSTS AND PRODUCTION METHOD OF SYNTHESIS GAS

机译:甲烷和二氧化碳的重整,钴基催化剂的制备及合成气的生产方法

摘要

Purpose: the manufacturing method of synthesis gas includes being arranged to than existing nickel reforming catalyst with excellent reaction activity using identical and hydrogen the cobalt-base catalyst for methane and carbon dioxide reform and carbon monoxide, has improved the service life by low-temperature carbonization reaction. Construction: cobalt-base catalyst is reformed for methane and carbon dioxide indicates (X)-b (company)-c (Y)/Z. in chemical formula XIt is Pt, Pd, Rh, Ir or Ru and Y be Zr or La carriers Z is SiO2 or aluminium oxide. In 100 parts by weight of carrier Z, first is that 0.1~10.0, b is 5.0~30.0, c is 1. by weight0~30.0 component. The manufacturing method of synthesis gas includes that carbon monoxide and hydrogen manufacture synthesis gas under the exhaust gas of 1 molar ratio: 0.5~2.0 CO/H2 is by using catalyst. Manufacture is carried out under the temperature of 600~800 C, and 0.The pressure of 01~1 MPa and 500~100,000 space velocities ml/g cathr.
机译:目的:合成气的制备方法包括与现有的具有相同反应活性的镍重整催化剂相比,采用与氢相同的甲烷,二氧化碳重整和一氧化碳钴基催化剂,通过低温碳化提高了使用寿命反应。结构:将钴基催化剂重整成甲烷,二氧化碳表示(X)-b(公司)-c(Y)/ Z。在化学式X中,它是Pt,Pd,Rh,Ir或Ru,Y是Zr或La载体Z是SiO2或氧化铝。在100重量份的载体Z中,首先是0.1〜10.0,b是5.0〜30.0,c是1。按重量计0〜30.0成分。合成气的制造方法包括一氧化碳和氢气在1摩尔比的排气下合成气:0.5〜2.0 CO / H2是通过使用催化剂。制造在600〜800 C的温度和0的温度下进行。压力为01〜1 MPa,空速为500〜100,000毫升/克·时。

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