Method for carrying out adsorption desulfurization on cracked gasoline

The invention discloses a method for carrying out adsorption desulfurization on catalytically cracked gasoline. Catalytic gasoline subjected to selective hydrodesulfurization is taken as a raw material (with sulfur content being less than 150 micrograms/gram) and firstly is subjected to cutting frac...

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Hauptverfasser: DONG BINGLI, MA YINGHAI, GAO XIONGHOU, ZHANG SONGXIAN, REN HAIOU, LI CHANGMING, SONG BANGYONG, NI YAN, ZHOU JINBO, CHENG ZHONGKE, CHENG LIANGLIANG, TIAN LIANG, LI JICHUN, GOU WENJIA, YANG LIBIN, WANG YANFEI
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creator DONG BINGLI
MA YINGHAI
GAO XIONGHOU
ZHANG SONGXIAN
REN HAIOU
LI CHANGMING
SONG BANGYONG
NI YAN
ZHOU JINBO
CHENG ZHONGKE
CHENG LIANGLIANG
TIAN LIANG
LI JICHUN
GOU WENJIA
YANG LIBIN
WANG YANFEI
description The invention discloses a method for carrying out adsorption desulfurization on catalytically cracked gasoline. Catalytic gasoline subjected to selective hydrodesulfurization is taken as a raw material (with sulfur content being less than 150 micrograms/gram) and firstly is subjected to cutting fractionation through a fractionating tower to obtain light gasoline and heavy gasoline; then, the light gasoline enters a fixed bed reactor for non-hydroforming physical adsorption desulfurization, wherein the non-hydroforming physical adsorption desulfurization can not reduce the olefin content, so that the octane value of a product cannot be lost; and the heavy gasoline enters the fixed bed reactor for hydroforming adsorption desulfurization, and the reaction product and a light gasoline physical adsorption desulfurization product are blended to obtain a clean gasoline product which meets the requirement of Euro V sulfur index. The method disclosed by the invention can be combined with the traditional selective hydrodesulfurization process to produce the clean gasoline which meets the requirement of Euro V sulfur index and has the advantages of small equipment investment, convenience in adsorbent filling operation, easy operation and low octane value loss.
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Catalytic gasoline subjected to selective hydrodesulfurization is taken as a raw material (with sulfur content being less than 150 micrograms/gram) and firstly is subjected to cutting fractionation through a fractionating tower to obtain light gasoline and heavy gasoline; then, the light gasoline enters a fixed bed reactor for non-hydroforming physical adsorption desulfurization, wherein the non-hydroforming physical adsorption desulfurization can not reduce the olefin content, so that the octane value of a product cannot be lost; and the heavy gasoline enters the fixed bed reactor for hydroforming adsorption desulfurization, and the reaction product and a light gasoline physical adsorption desulfurization product are blended to obtain a clean gasoline product which meets the requirement of Euro V sulfur index. 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subjects CHEMISTRY
CRACKING HYDROCARBON OILS
FUELS
LUBRICANTS
METALLURGY
MINERAL WAXES
PEAT
PETROLEUM, GAS OR COKE INDUSTRIES
PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVEHYDROGENATION, OLIGOMERISATION, POLYMERISATION
RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, ORGASES
REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS
REFORMING OF NAPHTHA
TECHNICAL GASES CONTAINING CARBON MONOXIDE
title Method for carrying out adsorption desulfurization on cracked gasoline
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