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INTERFACE ENERGY
INTERFACE
ENERGY
For a better understanding of the process, the types of crude oil refineries are given in the table below.
TOPPING MODEL CRUDE OIL REFINERY
Produck sulfur leveels same as crude fraction sülfür levels
Product yields and quality determined solely by crude properties
Gasoline haas low octane
/// CRUDE DISTILATION
HYDROSKIMMING MODEL CRUDE OIL REFINERY
Product sulfur levels controllable by hydrotreating.
Some capability to improve product yields and quality
Gasoline octane improved by reforming
/// CRUDE DISTILATION
/// REFORMING
/// HYDROTREATING
CONVERSION MODEL CRUDE OIL REFINERY
/// CRUDE DISTILATION
Product sulfur levels controllable by hydotreating
Substantial capability for yield and quality improvement
/// REFORMING
/// ALKYLATION & OTHER UPGRADING
/// FCC -- HYDRORCRACKİNG
/// HYDROTREATING
DEEP CONVERSION MODEL CRUDE OIL REFINERY
/// CRUDE DISTILATION
Product sulfur levels controllable by hydotreating.
Maximum yields of high of high – value refined products
Maximum capabillity for quallity improvement
Essentially all residual oil “ destroyed “
/// REFORMING
/// ALKYLATION & OTHER UPGRADING
/// COKING
/// HYDROTREATING
/// FCC -- HYDRORCRACKİNG
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