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High-yield synthesizing method of Synthetic-Natural-Gas with higher heating level in a reactor containing Fe-based catalytic bed and Ni-based catalytic bed

机译:在Fe基催化床和Ni基催化床反应器中高产合成气的高产率合成方法

摘要

The present invention is a method for producing a methane and C2-C4 paraffin-containing synthetic natural gas (SNG) of the composition exhibiting a high calorific value of 10,000 Kcal / Nm 3 ~ 13,000 Kcal / Nm 3 ; And it relates to a reactor for producing SNG used in the high calorific value SNG production method. In the reactor for producing SNG, Fischer-Tropsh (FT) synthesis reaction and methanation reaction are sequentially performed in a single reactor, and the iron-based catalyst layer for FT synthesis and the nickel-based catalyst layer for methanation reaction are stacked upstream according to the reaction sequence. Iron catalyst for FT synthesis and nickel for methanation reaction to form synthetic natural gas with high calorific value of 10,000 Kcal / Nm 3 ~ 13,000 Kcal / Nm 3 while lowering CO 2 generation to increase SNG yield. Based on the total 100 parts by weight of the catalyst, the amount of the stacked nickel-based catalyst is characterized in that it is adjusted to 10 to 50 parts by weight.
机译:本发明是制备具有高发热量10,000Kcal / Nm 3 〜13,000Kcal / Nm <的组成的含有甲烷和C2-C4链烷烃的合成天然气(SNG)的方法。 Sup> 3 ;本发明涉及一种在高热值SNG生产方法中使用的SNG生产反应器。在用于生产SNG的反应器中,费-托(FT)合成反应和甲烷化反应在单个反应器中依次进行,并且用于FT合成的铁基催化剂层和用于甲烷化反应的镍基催化剂层在上游堆叠。反应顺序。用于FT合成的铁催化剂和用于甲烷化反应的镍以形成高热值10,000 Kcal / Nm 3 〜13,000 Kcal / Nm 3 的合成天然气,同时降低CO 2 代以提高SNG产量。基于总计100重量份的催化剂,堆叠的镍基催化剂的量的特征在于将其调整为10至50重量份。

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