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    • 2. 发明申请
    • Process for the Production of Olefins by Autothermal Cracking
    • 通过自热裂解生产烯烃的方法
    • US20080119681A1
    • 2008-05-22
    • US11795818
    • 2005-12-22
    • Andrew Lindsay BurnsIan Allan Beattie Reid
    • Andrew Lindsay BurnsIan Allan Beattie Reid
    • C07C4/04
    • C10G27/04B01J23/40B01J23/56B01J23/62B01J23/74B01J23/76B01J23/89B01J35/04C07C4/06C07C2523/42C10G11/20C10G2400/20C07C11/02
    • The present invention provides a process for the production of olefins by autothermal cracking of a liquid paraffinic hydrocarbon-containing feedstock in the presence of a molecular oxygen-containing gas, wherein said process comprises (a) providing a liquid paraffinic hydrocarbon-containing feedstock, (b) mixing said liquid paraffinic hydrocarbon-containing feedstock with a diluent comprising steam, said diluent being pre-heated to a temperature of at least 300° C., to produce a vaporised diluent liquid paraffinic hydrocarbon-containing feedstream comprising at least 20% by volume of steam, (c) subsequently mixing said vaporised diluted liquid paraffinic hydrocarbon-containing feedstream with a molecular oxygen-containing gas to produce a diluted mixed feedstream, (d) subsequently contacting said diluted mixed feedstream with a catalyst capable of supporting combustion beyond the normal fuel rich limit of flammability, to provide a hydrocarbon product stream comprising olefins.
    • 本发明提供了一种在含分子氧的气体存在下通过液体含链烷烃的原料的自热裂解生产烯烃的方法,其中所述方法包括(a)提供含液体链烷烃的原料( b)将所述液体含链烷烃的原料与包含蒸汽的稀释剂混合,将所述稀释剂预加热到至少300℃的温度,以产生蒸发的稀释液液体含链烷烃的进料流,其包含至少20% 蒸汽体积,(c)随后将所述蒸发的稀释液体含石蜡烃的进料流与含分子氧的气体混合以产生稀释的混合进料流,(d)随后使所述稀释的混合进料流与能够支持燃烧的催化剂接触, 燃料的正常燃料极限,以提供包含烯烃的烃产物流。