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METHOD AND INSTALLATION FOR HEATING AND PARTIAL OXIDATION OF MIXTURE OF STEAM AND NATURAL GAS AFTER THE PRIMARY REFORMER

机译:主重整器后加热蒸汽和天然气混合气并部分氧化的方法和安装

摘要

1. A method of heating and partial oxidation of an unheated pre-reformed mixture of steam and natural gas for syngas, wherein energy is supplied to the gas stream (raw syngas) in the flow direction after the primary reformer, characterized in that the energy is supplied after the primary reformer directly through at least one porous burner located in the gas outlet channel of the primary reformer. ! 2. A method according to claim 1, characterized in that the energy is supplied through a plurality of porous burners located in the gas outlet channels of the primary reformer forming the flow path. ! 3. A method according to claim 1 or 2, characterized in that, in addition to supplying energy to it by means of a combustible gas and supplying an oxidizing agent, for example oxygen, nitrogen is also supplied to the gas stream in order to make the synthesis gas suitable for use in an ammonia plant. ! 4. The method according to claim 1, characterized in that CO2 and / or steam is additionally supplied to the gas stream. ! 5. A method according to claim 1 or 2, characterized in that the porous burner is used with a pre-reformed mixture of steam and natural gas in a sub-stoichiometric mode or when feeding a combustible gas in a super-stoichiometric mode. ! 6. A method according to claim 1 or 2, characterized in that the gas flow becomes vortex under the influence of a stationary mixer coated with a steam reformer catalyst. ! 7. The method according to claim 1 or 2, characterized in that the gas flow acquires a vortex character under the influence of a stationary mixer placed downstream of the corresponding burner, and the mixer is coated with
机译:1.一种加热和部分氧化未加热的蒸汽和天然气用于合成气的预重整混合物的方法,其中,在一次重整器之后,在流动方向上向气流(原始合成气)提供能量,其特征在于,所述能量直接在初级重整器之后通过位于初级重整器的气体出口通道中的至少一个多孔燃烧器供应气体。 ! 2.根据权利要求1所述的方法,其特征在于,通过位于形成所述流路的所述初级重整器的气体出口通道中的多个多孔燃烧器供应能量。 ! 3.根据权利要求1或2所述的方法,其特征在于,除了通过可燃气体向其供应能量并供应氧化剂(例如氧气)之外,还向所述气流中供应氮气。适用于氨厂的合成气。 ! 4.根据权利要求1所述的方法,其特征在于,将CO 2和/或蒸汽另外供应至所述气流。 ! 5.根据权利要求1或2所述的方法,其特征在于,所述多孔燃烧器以亚化学计量比或以超化学计量比供入可燃气体时与蒸汽和天然气的预重整混合物一起使用。 ! 6.根据权利要求1或2所述的方法,其特征在于,在涂覆有蒸汽重整催化剂的固定混合器的影响下,所述气流变成涡流。 ! 7.根据权利要求1或2所述的方法,其特征在于,在放置在相应燃烧器下游的固定混合器的影响下,所述气流获得涡旋特性,并且所述混合器涂覆有

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