PATENT
Process
For Converting A Hydrocarbon Feed And Apparatus Relating Thereto
United States Patent Application 20130079572
Inventors:
Haizmann, Robert (Rolling Meadows, IL, US)
Application Number:
13/244083
Publication Date:
03/28/2013
Filing Date:
09/23/2011
Assignee:
UOP, LLC (Des Plaines, IL, US)
Abstract:
The
embodiments disclosed herein can provide a process for converting a hydrocarbon
feed. The process may include hydrocracking the hydrocarbon feed slurried with
a particulate catalyst in a presence of hydrogen in a hydrocracking reaction
zone to produce a hydrocracked stream, separating at least a portion of the
hydrocracked stream, and passing the at least the portion of the hydrocracked
stream through a thermal cracking heating zone at conditions effective for
thermally cracking the at least the portion of the hydrocracked stream.
FIELD OF THE INVENTION
This invention generally relates to a process for converting a hydrocarbon
feed, and an apparatus related thereto.
DESCRIPTION OF THE RELATED ART
Generally, slurry hydrocracking is a useful process and can obtain a very high
conversion of various heavy hydrocarbons, such as a vacuum residue, to desired
products that may be further processed to gasoline and/or diesel. However,
slurry hydrocracking has a shortcoming, namely an inadequate conversion of
certain heavy hydrocarbons, such as a vacuum gas oil. Usually, refineries
require a low capital cost solution to maximize production of gasoline and
diesel from lower value VGO and VR. As a consequence, there is desire to modify
a slurry hydrocracking process for converting VGO economically and efficiently.
SUMMARY OF THE INVENTION
The embodiments disclosed herein can provide a process for converting a
hydrocarbon feed. The process may include hydrocracking the hydrocarbon feed
slurried with a particulate catalyst in a presence of hydrogen in a
hydrocracking reaction zone to produce a hydrocracked stream, separating at
least a portion of the hydrocracked stream, and passing the at least the
portion of the hydrocracked stream through a thermal cracking heating zone at
conditions effective for thermally cracking the at least the portion of the
hydrocracked stream.
Another exemplary embodiment may be a process for converting a hydrocarbon
feed. The process can include hydrocracking the hydrocarbon feed slurried with
a particulate catalyst in a presence of hydrogen in a hydrocracking reactor to
produce a hydrocracked stream, separating at least a portion of the
hydrocracked stream in an atmospheric fractionation column to obtain a one or
more C20-C50 hydrocarbons stream and a vacuum fractionation column to obtain a
one or more C20-C40 hydrocarbons stream, and passing the one or more C20-C40
hydrocarbons stream through a thermal cracking heater at conditions effective
for thermally cracking the at least the portion of the hydrocracked stream and
providing at least a portion of a product stream to the atmospheric
fractionation column.
A further exemplary embodiment can be an apparatus for thermal cracking one or
more hydrocarbons. The apparatus can include a slurry hydrocracking zone for
receiving a hydrocarbon feed and a particulate catalyst, a first fractionation
zone for receiving a hydrocracked stream from the slurry hydrocracking zone, a
second fractionation zone for receiving a one or more C20-C50 hydrocarbons
stream from the first fractionation zone, and a thermal cracking heating zone
for receiving a one or more C20-C40 hydrocarbons stream. Typically, the second
fractionation zone produces the one or more C20-C40 hydrocarbons stream.
The embodiments disclosed herein provide an efficient and economical mechanism
for an improved conversion process. Particularly, a thermal cracking heater can
process at least a portion of product from a slurry hydrocracking apparatus. By
thermally cracking a recovered LVGO and optionally an HVGO stream, these
materials can be converted to gasoline and diesel. Hence, the overall operation
of an apparatus can be improved greatly.
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