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CN105377750A 在基于氧气输送膜的转化系统内生产合成气的方法和系统 无效 - 驳回

在基于氧气输送膜的转化系统内生产合成气的方法和系统
摘要：
用于在基于氧气输送膜的转化系统内生产合成气的方法和系统，其使用具有在约1.6和3.0之间的汽碳比并且具有在约500℃和750℃之间的温度的合并的进料流（200），其中所述基于氧输送膜的转化系统和相关的合成生产工艺设备大体上没有碳形成和金属尘化腐蚀。所述合并的进料流包括预转化的烃类进料（195）、过热蒸汽（180）和反应产物流（198），所述反应产物流（198）通过与位于氧输送膜元件（120）的渗透侧的渗透氧反应的含氢气流（163）的反应产生。
摘要（英）：

A method and system for producing a synthesis gas in an oxygen transport membrane based reforming system that utilizes a combined feed stream (200) having a steam to carbon ratio between about 1.6 and 3.0 and a temperature between about 500 DEG C and 750 DEG C wherein the oxygen transport membrane based reforming system and associated synthesis production process equipment are substantially free of carbon formation and metal dusting corrosion. The combined feed stream is comprised a pre-reformed hydrocarbon feed (195), superheated steam (180), and a reaction product stream (198) created by the reaction of a hydrogen containing stream (163) reacted with the permeated oxygen at the permeate side of the oxygen transport membrane elements (120).

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