Hydrocracking and hydrotreating separate refinery streams
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United States of America Patent
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Oct 7, 2003
Issued Date -
N/A
app pub date -
Mar 14, 2001
filing date -
Jan 8, 1999
priority date (Note) -
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Abstract
This invention is directed to middle distillate production (e.g., diesel and kerosene products) by means of a reactor hydroprocessing system using two or more reactors (or a single reactor vessel having two or more stages, each stage containing one or more reaction zones). Hydrocracking is preferably performed in the initial reactor, and hydrotreating (and/or further hydrocracking) is preferably performed in the subsequent reactor vessel or stages within a single vessel. Reaction stages are effectively segregated to avoid recracking of products, to dramatically reduce hydrogen consumption in saturating the bottoms product and to carry out aromatic saturation of middle distillates in a clean low-temperature environment.
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