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CATALYTIC CRACKING PROCESS FOR REDUCING SULFUR CONTENT IN GASOLINE AND THE DEVICE THEREOF

机译:降低汽油中硫含量的催化裂化工艺及其装置

摘要

The invention relates to a catalytic cracking process for reducing sulfur content in gasoline and the device thereof, which includes a fluidized bed reactor in addition of a heavy oil catalytic cracking riser, characterized in enhancing contact time of oil-gas with the catalyst, further desulfurizing and reducing olefin content and increasing octane number in gasoline; regenerating all recycling catalysts, quality of products being stable and easily operated, reducing sulfur of gasoline to a maximum limit; adding a cooling device so as to avoid coking when the catalyst contacts with oil-gas in high temperature and decrease of yield of light oil resulted by excessively high reaction temperature of gasoline upgrading, improving products distribution, being flexible to change catalyst-oil ratio and reaction temperature of catalytic cracking reaction. The invention also provides an easily operated process for FCC desulfurization with stronger desulfurizing ability, good selectivity of products and high light oil yield, which can realize 40-80% of FCC gasoline desulfurization. Furthermore, more than 80% of FCC gasoline desulfurization can be achieved if the process is applied in combination with some particular catalysts.
机译:本发明涉及一种降低汽油中硫含量的催化裂化工艺及其装置,该装置包括除重油催化裂化提升管外的流化床反应器,其特征在于增加了油气与催化剂的接触时间,进一步脱硫。降低汽油中的烯烃含量并提高辛烷值;使所有回收催化剂再生,产品质量稳定且易于操作,将汽油中的硫减少到最大极限;增加冷却装置,避免高温下催化剂与油气接触时结焦,避免汽油提质反应温度过高导致轻油收率下降,改善产品分布,灵活改变催化剂油比,催化裂化反应的反应温度。本发明还提供了一种易于操作的FCC脱硫方法,该方法具有较强的脱硫能力,良好的产品选择性和较高的轻油收率,可实现FCC汽油脱硫的40-80%。此外,如果该方法与某些特定的催化剂结合使用,则可实现超过80%的FCC汽油脱硫。

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