U.S. patent application number 16/735746 was filed with the patent office on 2020-05-07 for abnormal temperature detection for fixed bed reactors.
The applicant listed for this patent is ExxonMobil Research and Engineering Company. Invention is credited to Hans G. Korsten, Dana W. Nouri, Benjamin S. Umansky.
Application Number | 20200140766 16/735746 |
Document ID | / |
Family ID | 59723979 |
Filed Date | 2020-05-07 |
![](/patent/app/20200140766/US20200140766A1-20200507-D00000.png)
![](/patent/app/20200140766/US20200140766A1-20200507-D00001.png)
![](/patent/app/20200140766/US20200140766A1-20200507-D00002.png)
![](/patent/app/20200140766/US20200140766A1-20200507-D00003.png)
United States Patent
Application |
20200140766 |
Kind Code |
A1 |
Nouri; Dana W. ; et
al. |
May 7, 2020 |
ABNORMAL TEMPERATURE DETECTION FOR FIXED BED REACTORS
Abstract
Systems and methods are provided for detecting abnormal
temperature conditions within a fixed bed reactor. In a fixed bed
reactor, a hydrocarbon (or hydrocarbon-like) feedstock can be
exposed to one or more types of catalyst particles at elevated
temperatures and/or pressures. In addition to the one or more types
of catalyst particles, a plurality of temperature-sensor structures
can be included in a catalyst bed and/or a coating including one or
more temperature-sensor structures can be provided on an interior
wall or other interior surface in the reactor. The
temperature-sensor structures can have a threshold temperature at
which the temperature-sensor structure changes to allow
introduction and/or release of a detectable substance.
Inventors: |
Nouri; Dana W.; (Beaumont,
TX) ; Korsten; Hans G.; (Naples, FL) ;
Umansky; Benjamin S.; (Fairfax, VA) |
|
Applicant: |
Name |
City |
State |
Country |
Type |
ExxonMobil Research and Engineering Company |
Annandale |
NJ |
US |
|
|
Family ID: |
59723979 |
Appl. No.: |
16/735746 |
Filed: |
January 7, 2020 |
Related U.S. Patent Documents
|
|
|
|
|
|
Application
Number |
Filing Date |
Patent Number |
|
|
15434408 |
Feb 16, 2017 |
10590352 |
|
|
16735746 |
|
|
|
|
62303038 |
Mar 3, 2016 |
|
|
|
Current U.S.
Class: |
1/1 |
Current CPC
Class: |
C10G 47/36 20130101;
C10G 47/02 20130101; B01J 8/0285 20130101; B01J 2208/025 20130101;
B01J 2208/00061 20130101; C10G 2300/4006 20130101 |
International
Class: |
C10G 47/36 20060101
C10G047/36; C10G 47/02 20060101 C10G047/02; B01J 8/02 20060101
B01J008/02 |
Claims
1-9. (canceled)
10. A method for processing a feed in a fixed bed reactor,
comprising: exposing a hydrocarbon-like feed to a catalyst in a
fixed catalyst bed in a reactor under fixed bed processing
conditions to form a reactor effluent, the fixed bed processing
conditions comprising an average catalyst bed temperature for the
fixed catalyst bed, the reactor further comprising one or more
temperature-sensor structures, the one or more temperature-sensor
structures having a threshold temperature; and detecting a
detectable substance in the reactor effluent, the detectable
substance being introduced into the reactor effluent by at least
one of the one or more temperature-sensor structures, wherein: a)
when the detectable substance is detectable prior to exposing a
temperature-sensor structure to a threshold temperature, the amount
of detectable substance detected in the reactor effluent is at
least about 1% greater than an average amount detected in the
reactor effluent at the average catalyst bed temperature; or b)
when the detectable substance is not detectable prior to exposing a
temperature-sensor structure to a threshold temperature, the amount
of detectable substance in the reactor effluent is greater than the
detection limit for the detectable substance.
11. The method of claim 10, wherein the amount of detectable
substance detected in the reactor effluent is at least about 10
times greater than the average amount detected at the average
catalyst bed temperature.
12. The method of claim 10, wherein the one or more
temperature-sensor structures have a first rate of introducing the
detectable substance into the reactor at a temperature below the
threshold temperature and a second rate of introducing the
detectable substance at a temperature above the threshold
temperature, the second introduction rate being at least about 5
times the first introduction rate.
13. The method of claim 10, wherein the average bed temperature is
at least about 20.degree. C. lower than the threshold
temperature.
14. The method of claim 10, wherein the hydrocarbon-like feed
comprises a petroleum feed, a renewable feed, a refinery feed, a
chemicals feed, or a combination thereof.
15. The method of claim 10, wherein the one or more
temperature-sensor structures comprise temperature-sensor
particles.
16. The method of claim 15, wherein the temperature-sensor
particles are distributed randomly in the catalyst bed.
17. The method of claim 10, wherein the one or more
temperature-sensor structures comprise at least a first
temperature-sensor structure having a first threshold temperature
and a second temperature-sensor structure having a second threshold
temperature.
18. The method of claim 17, wherein the first temperature-sensor
structure introduces a first detectable substance into the reactor,
the second temperature-sensor structure introduces a second
detectable substance into the reactor, and the first detectable
substance is different from the second detectable substance.
19. The method of claim 10, wherein the reactor comprises a coating
on an interior surface, the coating being at least one of the one
or more temperature-sensor structures, the coating comprising one
or more temperature-sensor particles, or a combination thereof.
20. The method of claim 10, wherein, when the detectable substance
is not detectable prior to exposing a temperature-sensor structure
to a threshold temperature, the amount of detectable substance
detected in the reactor effluent is about 1 ppb to about 1000 ppm
by weight.
Description
CROSS-REFERENCE TO RELATED APPLICATIONS
[0001] This application claims the benefit of U.S. Provisional
Application No. 62/303,038, filed on Mar. 3, 2016, the entire
contents of which are incorporated herein by reference.
FIELD
[0002] This invention is directed to systems and methods for
detection of temperature changes within a fixed bed reaction
system.
BACKGROUND
[0003] A variety of reactions related to chemical and/or petroleum
processing can be beneficially performed by exposing a feedstock to
one or more fixed beds of catalyst within a reactor.
Hydroprocessing is an example of such a process. Depending on the
nature of the feed and the desired product, hydroprocessing can be
used to remove contaminants such as sulfur and/or nitrogen; modify
the boiling range of a feed to form higher value products; modify
the properties of a feed, such as cold flow properties or viscosity
properties; and/or saturate olefins and aromatics in the feed.
Other examples of chemical and/or petroleum processing processes
can include, but are not limited to, alkylation processes and
oligomerization processes.
[0004] One potential difficulty with exposing a feedstock to one or
more beds of catalyst in a reactor is that many types of reactions
are exothermic. If a problem develops with flow within a catalyst
bed, localized heating can occur that can allow a portion of a
catalyst bed to reach an undesirable temperature, even though the
overall reaction temperature may be within a tolerance limit. This
type of temperature excursion can cause a variety of difficulties,
such as deactivation of catalyst and production of undesired side
products. Additionally, if sufficient excessive heating occurs, the
excessive heating can potentially damage the internal structure of
the reactor, or even lead to vessel failure.
[0005] German patent publication no. DE 19818693 describes a method
for detecting temperature changes in a reactor. Long tubes
containing a substance under pressure are located on the interior
of the reactor. As the temperature increases, the pressure changes
in the tubes can be detected. In some aspects, if a sufficient
pressure is built up within a tube, the substance within a tube can
cause the tube to rupture, leading to release of the pressure
within the tube. Nitrogen is provided as an example of a substance
to use within the tubes in the aspect where a tube may break open
due to increased pressure.
SUMMARY
[0006] In an aspect, a fixed bed processing system is provided. The
fixed bed processing system can include a reactor vessel having a
reactor inlet and a reactor outlet. The reactor vessel can further
include at least one fixed bed of catalyst particles within the
reactor vessel. One or more temperature-sensor structures can also
be included within the reactor vessel. Examples of
temperature-sensor structures can include, but are not limited to,
temperature-sensor particles and coatings that comprise a
temperature-sensor structure. A detector can be in fluid
communication with the reactor outlet. The detector can optionally
correspond to a spectroscopic detector, a radiation detector, a
chromatographic detector, or a combination thereof. Optionally, the
one or more temperature-sensor structures can be composed of a
material that undergoes a structural change at a threshold
temperature. The one or more temperature-sensor structures can have
a first rate of introducing a detectable substance into the reactor
at a temperature below the threshold temperature and a second rate
of introducing the detectable substance at a temperature above the
threshold temperature, the second introduction rate optionally
being at least 5 times the first introduction rate.
[0007] In another aspect, a method for processing a feed in a fixed
bed reactor is provided. The method can include exposing a
hydrocarbon-like feed to a catalyst in a fixed catalyst bed in a
reactor under fixed bed processing conditions to form a reactor
effluent. The fixed bed processing conditions can include an
average catalyst bed temperature for the fixed catalyst bed. The
reactor can include one or more temperature-sensor structures, the
one or more temperature-sensor structures having a threshold
temperature. A detectable substance can be detected in the reactor
effluent. The detectable substance can be introduced into the
reactor effluent by at least one of the one or more
temperature-sensor structures. When the detectable substance is not
detectable prior to exposing a temperature-sensor structure to a
threshold temperature, the amount of detectable substance in the
reactor effluent can be greater than the detection limit for the
detectable substance. Optionally, at least a portion of the
detectable substance can be present in the reactor effluent
separate from introduction by the one or more temperature-sensor
structures. When the detectable substance is detectable prior to
exposing a temperature-sensor structure to a threshold temperature,
the amount of detectable substance detected in the reactor effluent
can be at least about 1% greater than an average amount detected in
the reactor effluent at the average catalyst bed temperature.
BRIEF DESCRIPTION OF THE DRAWINGS
[0008] FIG. 1 schematically shows an example of a fixed bed reactor
suitable for use with temperature-sensor structures as described
herein.
[0009] FIG. 2 schematically shows another example of a fixed bed
reactor with temperature-sensor structure corresponding to a
coating on an interior wall of the reactor.
[0010] FIG. 3 schematically shows an example of a
temperature-sensor coating on an interior wall of a reactor.
[0011] FIG. 4 schematically shows an example of a coating that
contains temperature-sensor particles on an interior wall of a
reactor.
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS
Overview
[0012] In various aspects, systems and methods are provided for
detecting abnormal temperature conditions within a fixed bed
reactor. In a fixed bed reactor, a hydrocarbon (or
hydrocarbon-like) feedstock can be exposed to one or more types of
catalyst particles at fixed bed processing conditions including
elevated temperatures and/or pressures. In addition to the one or
more types of catalyst particles, a plurality of temperature-sensor
particles (or other temperature-sensor structure) can be included
in a catalyst bed. Alternatively, a coating including a
temperature-sensor structure can be provided on an interior wall or
other interior surface in the reactor. The temperature-sensor
particles (or other temperature-sensor structure) can have a
threshold temperature at which the structure of the particle
changes to allow introduction and/or release of a detectable
substance. Any convenient type of structural change can be used,
such as rupture of the particle shell, melting of the particle,
and/or opening due to differences in thermal expansion rates of the
particle materials. After the structural change, the
temperature-sensor particle can introduce a detectable substance
into the feedstock as it is processed in the catalyst bed. The
detectable substance can be directly introduced into the feedstock,
such as by releasing a dye or radioisotope into the feedstock.
Alternatively, the detectable substance can be indirectly
introduced. An example of indirectly introducing a substance into
the feedstock can be releasing a reagent into the feedstock for
subsequent formation of a detectable compound (such as by
decomposition). Another example can be a structural change that
exposes a catalyst to the feed/effluent in the reactor that can
catalyze formation of a detectable compound within the reaction
effluent. The substance, whether directly or indirectly introduced,
can be suitable for detection in-line or otherwise in real time
from an effluent of the reactor that contains the catalyst bed.
[0013] Many types of reactions performed using a fixed catalyst bed
can correspond to exothermic reactions performed at a desired
temperature or within a temperature window. Unfortunately, the flow
pattern within a catalyst bed can become non-uniform for a variety
of reasons. When a non-uniform (or otherwise non-ideal) flow
pattern occurs, localized heating may concomitantly occur within
portions of a catalyst bed to a greater degree than desired. This
localized heating can lead to substantial increases in temperature
beyond the expected and/or target operating temperature for the
catalyst bed, particularly for highly exothermic reactions.
[0014] An unexpected and/or abnormal temperature can cause a
variety of problems within a reactor. For some catalysts, operating
at increased temperatures can activate alternative reaction
pathways, potentially leading to undesired products, catalyst
damage, and/or even a runaway reaction. Increased temperatures can
additionally or alternatively potentially damage equipment within a
reactor and/or lead to vessel failure.
[0015] Another difficulty with non-uniform flow patterns is that
such flow patterns can be difficult to detect. Conventionally, the
temperature within a reactor can be monitored using a large
plurality of thermocouples. For example, a reactor with a diameter
of about 5 meters and including 3 catalyst beds can include
hundreds of thermocouples located at various heights and radial
locations in the reactor. In order to position thermocouples at the
large number of locations where localized heating might occur, a
reactor can include concentric rings at a plurality of elevations
to provide a support structure for mounting thermocouples. Another
option can be to have a plurality of vertical thermowells that can
house thermocouples at various elevations within a reactor. Both
the number of thermocouples and the presence of the
thermowells/other support structures for housing the thermocouples
can pose difficulties. This can include problems during
loading/unloading the catalyst bed due to the presence of the
thermowells; changes introduced into the flow pattern within
catalyst bed(s) due to the presence of the thermocouples and/or
thermowells; and/or issues related to new flow paths (i.e., leaks)
between various reactor internals due the presence of the
thermocouples and/or thermowells. Additionally or alternately, the
thermocouples/thermowells can tend to be fixed in location once a
reactor is constructed, with limited or possibly no ability to
adjust the location of thermocouples based on the reaction being
performed in a reactor.
[0016] Temperature-sensor particles (and/or other
temperature-sensor structures) can provide a more flexible solution
for detection of abnormal temperature events in a reactor. During
loading of a catalyst bed, temperature-sensor particles can be
added in any convenient manner. This can include distribution at
specific locations, random distribution throughout a bed,
distribution in a pattern throughout a catalyst bed, or
combinations thereof. Because the temperature-sensor particles can
be part of the catalyst bed, the location of the temperature-sensor
particles can be modified with each catalyst load change. Use of
temperature-sensor particles can additionally or alternatively
simplify detection of temperature changes. Rather than having to
separately connect a large plurality of thermocouples to one or
more detectors, the temperature-sensor particles can release a
substance that can be directly or indirectly detected in the
effluent from a catalyst bed and/or a reactor. This can allow one
detector or a small plurality of detectors located at one or more
convenient locations in an effluent flow path to be used for
detection of an abnormal temperature event.
[0017] In addition to or as an alternative to use of
temperature-sensor particles, temperature-sensor coatings can be
used within a reactor. This can correspond to having a coating
including embedded temperature-sensor particles. Another option can
be to have an internal coating of a material suitable for forming a
temperature-sensor structure, so that the coating itself can
undergo a structural change when an abnormal temperature event
occurs. Temperature-sensor particles and temperature-sensor
coatings can more generally be referred to as temperature-sensor
structures.
[0018] An example of a reaction system where methods for detection
of abnormal temperature events can be useful includes a
reactor/reaction system containing at least one fixed bed of an
acidic catalyst, basic catalyst, and/or a catalyst containing a
molecular sieve. Catalysts including at least one molecular sieve
and/or acidic/basic catalysts can be used to facilitate a variety
of reactions. Many types of processes can involve processing of
petroleum feeds, renewable feeds, refinery streams, chemical
production feeds, and/or other hydrocarbon-like feeds in the
presence of one or more fixed catalyst beds. In such processes, the
target process conditions can include a temperature that reduces
and/or minimizes the catalysis of undesirable reaction
pathways.
[0019] One example of an undesirable reaction pathway can be
cracking of hydrocarbons. Many acidic catalysts and/or catalysts
containing molecular sieves can have substantial cracking activity
at higher temperatures. At lower temperatures, this cracking
activity can be controlled, reduced, and/or minimized, so that
desired products can be selectively formed. However, due to the
exothermic nature of most cracking reactions, if the temperature
becomes high enough, the rate of cracking may be able to generate
sufficient additional heat generated to result in a
self-reinforcing cycle of increasing cracking and further
increasing temperature. When this occurs due to a localized "hot
spot" in a catalyst bed, it can be difficult to detect the onset of
this type of self-reinforcing condition unless the "hot spot"
happens to be near the edge of the reactor where a conventional
thermocouple can be located. The ability to distribute
temperature-sensor particles throughout a catalyst bed can
facilitate early detection of this type of event, so that a
corrective action can be taken while reducing and/or minimizing (i)
potential damage to the catalyst bed and/or (ii) the amount of
product yield loss due to unexpected processing conditions.
Temperature-Sensor Structure--Definitions
[0020] In order to clarify the description of the invention, the
following definitions are provided. The following definitions
should be applied throughout the description herein unless
otherwise specified.
[0021] A temperature-sensor structure is defined herein as a
structure (such as a particle, a coating, or a combination thereof)
exhibiting a structural change at a threshold temperature to allow
for increased introduction of a detectable substance into a feed or
effluent flow within a reactor. The threshold temperature
corresponds to a temperature at the typical and/or expected
operating pressure of the reactor/reaction system where the
temperature-sensor structure is being used. The threshold
temperature can be a high temperature threshold or a low
temperature threshold. For a temperature-sensor structure with a
high temperature threshold, the structure can exhibit a structural
change at temperatures above the threshold temperature, while a
structure with a low temperature threshold can exhibit a structural
change at temperatures below the threshold temperature. In an
aspect, a temperature-sensor structure (such as a
temperature-sensor particle or temperature-sensor coating) is
defined to be different from any thermocouples which may optionally
be present in a reactor/reaction system.
[0022] One option for characterizing the amount of a detectable
substance can be based on the rate of introduction of the
detectable substance into the feed or effluent within the reactor.
When a temperature-sensor structure is exposed to a temperature
exceeding (either high or low) the threshold temperature, a
structural change can occur in the structure resulting in an
increased rate of introduction of a detectable substance into a
reactor effluent. The increased rate of introduction can be
characterized based on a) a rate of introduction per second prior
to exposure to a temperature beyond the threshold temperature and
b) a rate of introduction per second for at least one time period
during and/or after the exposure to the temperature beyond the
threshold temperature. The increased rate of introduction can
correspond to a rate of introduction (per second) of the detectable
substance after the exposure to the abnormal temperature of at
least 5 times greater than the average rate of introduction (per
second) prior to the abnormal temperature exposure. For example,
the rate of introduction after the exposure to the abnormal
temperature exposure can be at least about 5 times greater than the
average rate of introduction prior to the abnormal temperature
exposure, for example at least about 10 times, at least about 25
times, at least about 100 times, or at least about 1000 times, such
as up to about 10.sup.10 times greater or more. The average rate of
introduction prior to the abnormal temperature can be determined
based on a convenient time scale. If there is ambiguity, the
average rate of introduction prior to the abnormal temperature
exposure can be determined for the hour prior to the abnormal
temperature exposure. If for some reason an hour is not practical,
based on the measurement technique, the average rate of
introduction can be determined for the minute prior. As an example,
a temperature-sensor particle may introduce about 0.1 .mu.g/sec (or
less) of a dye into an effluent before exposure to a temperature
above a high temperature threshold. After exposure to a temperature
above a high temperature threshold, the temperature-sensor particle
can release substantially all of the dye within the particle into
the effluent, e.g., resulting in release of about 1 mg of dye into
the effluent. If the dye release is substantially complete within 1
second, this would correspond to a release rate of about 1 mg/sec,
or about 1000 .mu.g/sec, which corresponds to a rate of
introduction of the dye into the effluent after the abnormal
temperature exposure that is a factor of about 10.sup.4 greater
than the average rate of introduction of dye prior to the abnormal
temperature exposure. For the limiting situation of an effluent
that does not have a detectable level of a substance prior to the
increase caused by a temperature-sensor material, an increase from
a non-detectable level to a detectable level is defined herein as
corresponding to the larger of a) a rate of introduction that is at
least about 10 times greater, or b) an increase in the rate of
introduction by a factor determined based on the difference between
the detection limit for the substance and the actual detected level
in the effluent.
[0023] Additionally or alternatively to characterizing the rate of
introduction, for a substance not detectable prior to exposing a
temperature-sensor structure to a threshold temperature (i.e., an
abnormal temperature event), the amount of detectable substance in
the effluent after an abnormal temperature event can be greater
than the detection limit. In some aspects, the amount of detectable
substance in the effluent after an abnormal temperature event can
be at least about 10 times greater than the average amount prior to
the abnormal temperature exposure, for example at least about 10
times, at least about 25 times, at least about 100 times, or at
least about 1000 times, such as up to about 10.sup.10 times greater
or more. In this discussion, a change from having an amount of a
detectable substance in an effluent below the detection limit to
having an amount greater than the detection limit is defined herein
as a change in amount of detectable substance after an abnormal
temperature event of at least 10 times greater than the amount
prior to the abnormal temperature event.
[0024] It is noted that, in some aspects, the increase in the rate
of introduction of a detectable substance into an effluent may
correspond to an increase for only a brief period of time after
exposure to an abnormal temperature. For example, for a
temperature-sensor particle that contains a dye as a detectable
substance, substantially all of the dye in the temperature sensor
particle may be introduced into the effluent during a single (e.g.,
one second) time period after a structural change occurs for the
temperature-sensor particle. In other aspects, the rate of
introduction of the detectable substance may increase throughout
the time of exposure of a temperature-sensor structure to an
abnormal temperature, but then can return to a lower rate of
introduction when the temperature no longer exceeds the threshold
temperature. In still other aspects, the rate of introduction of
the detectable substance may be maintained even after the
temperature-sensor material is returned to a temperature below the
high temperature threshold (or alternatively above a low
temperature threshold). This may occur, for example, when the
change in the temperature-sensor structure results in exposing a
catalyst to the feed within the reactor.
[0025] Additionally or alternately, the detectable substance can be
detected in an effluent exiting from the reactor containing a fixed
bed. When detecting the detectable substance in the reactor
effluent, a suitable concentration of the detectable substance in
the reactor effluent can be an amount on the order of parts per
billion by weight to parts per million by weight. In such aspects,
the concentration of a detectable substance (after an abnormal
temperature event) in a reactor effluent, an effluent from a fixed
bed, or a combination thereof can be about 1 part per billion by
weight to about 1000 parts per million weight at the location where
the effluent (or a side stream derived from the effluent) passes
through the detector and/or at the location where the effluent is
sampled for use in the detector. For example, the concentration of
a detectable substance in an effluent when detecting an abnormal
temperature event can be (by weight) about 1 ppb to about 1000 ppm,
for example about 1 ppb to about 100 ppm, about 1 ppb to about 10
ppm, about 1 ppb to about 1 ppm, or about 1 ppb to about 100 ppb,
about 10 ppb to about 1000 ppm, about 10 ppb to about 100 ppm,
about 10 ppb to about 10 ppm, about 10 ppb to about 1 ppm, about 10
ppb to about 100 ppb, about 100 ppb to about 1000 ppm, about 100
ppb to about 100 ppm, about 100 ppb to about 10 ppm, about 100 ppb
to about 1 ppm, about 1 ppm to about 1000 ppm, about 1 ppm to about
100 ppm, about 1 ppm to about 10 ppm, about 10 ppm to about 1000
ppm, or about 10 ppm to about 100 ppm. The concentration in the
reactor effluent of the detectable substance after the abnormal
temperature event may only achieve the above concentration ranges
for a limited period of time, such as for a minute or less, or a
few seconds or less, or even a second or less. It is noted that the
concentration of detectable substance may vary widely at other
locations in a reactor after an abnormal temperature event.
[0026] Optionally, the detectable substance can be a substance
already present in the feed and/or effluent of the reactor. In such
optional aspects, the amount of increase in the concentration of
the detectable substance in an effluent (such as the effluent
exiting a reactor) can be further characterized. In some optional
aspects, the concentration of the detectable substance after
exposure of a temperature-sensor structure to an abnormal
temperature can be at least about 1% greater than the average
concentration prior to the abnormal temperature exposure, as
calculated relative to the average concentration, for example at
least about 2% greater, at least about 5% greater, at least about
10% greater, at least about 50% greater, or at least about 100%
greater, an optionally up to about 1000% greater, up to about 500%
greater, up to about 100% greater, up to about 50% greater, or up
to about 10% greater. In certain optional aspects, the substance
already present in the feed and/or effluent may be present in a
minor amount (e.g., in parts per billion or lower parts per
million), so that the concentration of the detectable substance
after an abnormal temperature event can be still higher, such as up
to about 1000% greater or more, relative to the average
concentration prior to the abnormal temperature.
[0027] In this description, introduction of a directly detectable
substance into an effluent by a temperature-sensor structure is
defined as introduction by the temperature-sensor structure of a
substance detected without further reaction in the reactor. For
example, a temperature-sensor particle/coating may contain a dye
that can be detected by a suitable spectroscopic technique in the
reactor effluent. Such a dye can be a directly detectable
substance. Another example of a directly detectable substance can
be a temperature-sensor particle/coating releasing a radioisotope,
such as based on cobalt-60. Additional or alternative options can
be a temperature-sensor particle/coating that can melt into the
reactor effluent, so that a component of the particle/coating
material itself can correspond to the detectable substance.
[0028] In this description, indirect introduction of an detectable
substance into an effluent by a temperature-sensor structure is
defined as release by the temperature-sensor structure of a
substance (or exposure of a substance) that can undergo further
reaction in the reactor, that can catalyze (or otherwise
facilitate) a reaction within the reactor, or a combination
thereof. One example of indirect introduction of a detectable
substance can include a temperature-sensor structure that can
release a reagent into a reaction effluent. The reagent can
decompose under the reactor conditions, interact with catalyst in a
catalyst bed in the reactor, react with a component of the feed
being processed, and/or undergo any other convenient reaction to
form a detectable substance. Because the reagent is not directly
detected but instead used to form the detectable substance, the
increased rate of release of the reagent is defined as indirect
introduction of a detectable substance. As another example, the
structural change for a temperature-sensor structure can result in
exposure and/or release of an additional type of catalyst into the
reaction environment. The additional type of catalyst can catalyze
(or otherwise facilitate) formation of reaction product not
otherwise present in a substantial amount in the reaction effluent.
Thus, in this type of catalyst example, the detectable substance is
not released from the temperature-sensor structure. Instead, the
indirect introduction of the detectable substance can correspond to
making an additional catalyst available, which can then catalyze
and/or otherwise result in formation of the detectable
substance.
[0029] The threshold temperature for a temperature-sensor structure
can be any convenient temperature. In various aspects, a
temperature-sensor structure can have a threshold temperature in
any of the following ranges: about 500.degree. C. to about
600.degree. C., about 500.degree. C. to about 550.degree. C., about
550.degree. C. to about 600.degree. C., about 400.degree. C. to
about 500.degree. C., about 400.degree. C. to about 450.degree. C.,
about 450.degree. C. to about 500.degree. C., about 300.degree. C.
to about 400.degree. C., about 300.degree. C. to about 350.degree.
C., about 350.degree. C. to about 400.degree. C., about 200.degree.
C. to about 300.degree. C., about 200.degree. C. to about
250.degree. C., about 250.degree. C. to about 300.degree. C., about
600.degree. C. to about 700.degree. C., about 600.degree. C. to
about 650.degree. C., or about 650.degree. C. to about 700.degree.
C. More generally, the range for a threshold temperature can be
about 200.degree. C. to about 700.degree. C., for example about
200.degree. C. to about 500.degree. C., about 300.degree. C. to
about 600.degree. C., about 400.degree. C. to about 700.degree. C.,
about 200.degree. C. to about 400.degree. C., about 300.degree. C.
to about 500.degree. C., about 400.degree. C. to about 600.degree.
C., or about 500.degree. C. to about 700.degree. C.
[0030] In this discussion, the temperature of a reaction in a
catalyst bed can be defined based on the average of the temperature
at the top of the catalyst bed and the bottom of the catalyst bed.
The top and bottom of the catalyst bed are with reference to the
direction of flow within the catalyst bed.
Types of Temperature-Sensor Structures
[0031] Examples of temperature-sensor materials can include
particles and/or coatings. Temperature-sensor particles can
correspond to particles having any convenient size and/or shape
suitable for incorporation into a catalyst bed. For example, many
types of catalyst particles can range from about 1 mm to about 6 mm
in diameter, most commonly in the range of about 1.3 mm to about 3
mm. In some aspects, the diameter of the temperature-sensor
particle can be about 0.25 times to about 4.0 times the diameter of
the catalyst particles of the bed in which the capsules are
intended to be loaded, for example about 0.25 times to 3.0 times
the diameter, about 0.25 times to about 2.0 times, about 0.25 times
to about 1.0 times, about 0.5 times to about 4.0 times, about 0.5
times to about 3.0 times, about 0.5 times to about 2.0 time, about
0.5 times to about 1.0 times, about 1.0 times to about 4.0 times,
about 1.0 times to about 3.0 times, about 1.0 times to about 2.0
times, or about 2.0 times to about 4.0 times. It is noted that a
temperature-sensor particle smaller than about 20% of the catalyst
diameter of the catalyst particles in a bed may be susceptible to
being washed away during processing of a feed. Additionally or
alternately, a temperature-sensor particle can have a diameter of
about 0.1 mm to about 25 mm, for example about 0.1 mm to about 10
mm, about 0.1 mm to about 6.0 mm, about 0.1 mm to about 3.0 mm,
about 0.1 mm to about 2.0 mm, about 0.1 mm to about 1.0 mm, about
0.3 mm to about 25 mm, about 0.3 mm to about 10 mm, about 0.3 mm to
about 6.0 mm, about 0.3 mm to about 3.0 mm, about 0.3 mm to about
2.0 mm, about 0.3 mm to about 1.0 mm, about 0.5 mm to about 25 mm,
about 0.5 mm to about 10 mm, about 0.5 mm to about 6.0 mm, about
0.5 mm to about 3.0 mm, about 0.5 mm to about 2.0 mm, about 0.5 mm
to about 1.0 mm, about 1.0 mm to about 25 mm, about 1.0 mm to about
10 mm, about 1.0 mm to about 6.0 mm, or about 1.0 mm to about 3.0
mm.
[0032] Some shapes can correspond to 3-dimension solid shapes
suitable for acting as containers for another substance, such as a
spherical particle, cylindrical or rod-like particle, ovoid
particle, or any other convenient shape. Other suitable shapes can
correspond to any convenient shape that can be conventionally used
as a shape for a catalyst particle, including shapes formed by
extrusion methods. Common suitable catalyst shapes for a
temperature-sensor particle can include, but are not necessarily
limited to, sphere, cylinder, trilobe, and quadrulobe. One option
for forming a temperature-sensor coating can be to form a coating
including temperature-sensor particles in the coating. Additionally
or alternately, the coating itself can correspond to a
temperature-sensor material.
[0033] In some aspects, a temperature-sensor structure can
correspond to a container that holds another substance. A
structural change in the temperature-sensor structure can then
introduce and/or expose the substance originally contained within
the temperature-sensor material to the reaction environment.
Additionally or alternately, a structural change in a
temperature-sensor structure can cause the temperature-sensor
structure to melt or otherwise be introduced into the effluent in
the reaction environment, so that the temperature-sensor structure
directly or indirectly becomes the detectable substance.
[0034] An example of a temperature-sensor structure is a
temperature-sensor particle that contains another substance that
can be introduced and/or exposed to the reaction environment in a
reactor. The substance in the temperature-sensor particle can be a
fluid under the conditions in the reaction environment and/or can
be soluble in the fluid flow passing through the reaction
environment. Optionally, for a substance corresponding to a
catalyst, the catalyst can a) become part of the fluid flow in the
reactor (such as a liquid catalyst and/or a catalyst with a
particle size substantially smaller than other catalyst particles
in the catalyst bed); b) be introduced into and become part of the
catalyst bed; and/or c) be retained in the temperature-sensor
particle.
[0035] One option for a temperature-sensor particle can be a
particle composed of a material having a melting point in a desired
temperature range. In this type of aspect, as the temperature
approaches the melting point of the material used to form the
temperature-sensor particle, the particle can undergo a structural
change (such as melting and/or flow) allowing a substance within
the particle to be released into the reaction environment. In this
type of aspect, the threshold temperature of the temperature-sensor
particle may not necessarily correspond exactly to the melting
temperature of the particle material, as simply approaching the
melting temperature may cause sufficient structural change to allow
release of a substance contained within a particle.
[0036] A wide variety of metals and alloys are known that have
melting points within different temperature ranges. A
temperature-sensor particle can be composed of any convenient
metal, metal alloy, and/or other metal-based compound a) having an
appropriate threshold temperature for a given application and b)
not otherwise reacting with the reaction environment in a manner
that can lead to release of the substance within the
temperature-sensor particle at temperatures below the threshold
temperature. For example, many hydroprocessing environments can
include a combination of H.sub.2S, CO.sub.2, NH.sub.3, and/or water
at elevated temperature and pressure. The temperature-sensor
particle can be selected to not degrade under the selected
hydroprocessing environment conditions. One of skill in the art can
use chemical equilibrium calculations based on thermochemical
properties when selecting a suitable material for a
temperature-sensor particle.
[0037] Table 1 shows examples of various metals and alloys suitable
for forming temperature-sensor particles (and/or other
temperature-sensor structures), depending the specific reaction
conditions within a fixed-bed processing environment.
TABLE-US-00001 TABLE 1 Metal and Alloy Melting Points Melting
Points deg C. deg F. Aluminum alloys ~463-~671 ~865-~1240 Babbitt
~249 ~480 Lead ~328 ~621 Magnesium alloys ~349-~649 ~660-~1200 Tin
~232 ~449 Zinc ~420 ~787
[0038] Another option for forming a temperature-sensor particle can
be to form a particle containing a condensed phase substance that
converts to a gas as the temperature increases. Based on the
quantity of the substance inside the particle, the particle can be
designed to undergo a structural change when the pressure inside
the particle is sufficient to rupture/burst the particle.
[0039] Still another option can be to form the particle from two or
more different materials, such as two different metals and/or
alloys. The different materials can be selected to have different
thermal expansion properties so the differing thermal expansion
properties cause the particle to open when a threshold temperature
is achieved.
[0040] The content of the temperature-sensor particles can vary
depending on the desired type of detectable substance. Examples of
directly detectable substances can include various types of dyes
suitable for spectroscopic identification. This can include dyes
readily detectable using fluorescence spectroscopy,
ultraviolet-visible (UV-VIS) spectroscopy, and/or other
spectroscopic techniques. Radioactive isotopes are another example
of a directly detectable substance. Cobalt-60 is an example of a
readily detectable radioactive isotope suitable for use in various
hydroprocessing or other fixed bed reaction environments. An
example of the content for a temperature-sensor particle for an
indirectly detectable substance can be a catalyst particle
catalyzing formation of a detectable substance within the reaction
environment.
[0041] The type (or types) of detection methods used for detection
of the detectable substance can be selected based on the nature of
the detectable substance. Suitable types of detection methods can
include, but are not limited to, electromagnetic spectrometers
(e.g., fluorescence spectrometers, UV-VIS spectrometers, FTIR
spectrometers), radiation detectors, gas chromatographs, mass
spectrometers, and/or any other convenient type of detector. Some
properties can be detected substantially continuously in real time,
such as refractive index and/or infrared absorption, allowing for
an alarm or other indicator to be triggered when the measured
property exceeds a threshold value. For other types of detection,
such as gas chromatography, measurement can typically occur on a
slower (typically periodic) time scale, such as once per minute.
For slower types of detection, the introduction of the detectable
substance into the effluent can be a method of introduction
allowing for detection on longer time scales. In some aspects,
detection of a detectable substance can be performed in-line on the
reactor effluent. Additionally or alternatively, a slip stream/side
stream can be formed from the reactor effluent and passed into the
detector. Further additionally or alternatively, depending on the
detection method, a portion of the reaction effluent can be
withdrawn from the fluid flow and passed into the detector.
[0042] The considerations for a temperature-sensor coating can be
similar to those for a temperature-sensor particle. The same types
of materials can be used for the coating, as well as the same types
of (directly or indirectly) detectable substances.
Fixed Bed Processing Conditions
[0043] The systems and methods described herein for detection of an
abnormal or unexpected temperature in a fixed bed processing
environment can be used with any convenient type of process for
processing of a (mineral) petroleum-based feed, a renewable feed, a
refinery feed, a chemicals feed, and/or another type of
hydrocarbonaceous or hydrocarbon-like feed (such as a feed
including hydrocarbon-like compounds optionally containing
heteroatoms other than carbon and hydrogen). Hydrocarbon and
hydrocarbon-like feeds are defined herein to include synthetically
formed hydrocarbon and hydrocarbon-like feeds, such as feeds based
on compounds formed using a Fischer-Tropsch type process.
Petroleum-based feeds can include, but are not limited to,
whole/reduced crudes, fractions of such crudes, and/or feeds
derived from processing of such crudes and crude fractions.
[0044] Fixed bed reactors are defined herein to include any
convenient reactor configuration including a bed of catalyst
particles remaining within a reactor during processing of a
catalyst. This can include trickle-bed reactors, fixed bed downflow
reactors and upflow reactors, co-current and counter-current
reactors, reactors operating in gas phase, liquid phase, and/or
mixed phase, and combinations thereof. Optionally, the systems and
methods described herein could be used to provide
temperature-sensor coatings for reactors including ebullating beds
of catalyst, moving beds of catalyst, slurries of catalyst and
feed, and/or other types of reactor configurations where at least a
portion of the catalyst from a catalyst bed can be withdrawn from a
reactor during operation.
[0045] Fixed bed reactors can be suitable for performing various
types of reactions on petroleum, renewable, refinery, chemical
and/or other hydrocarbon-like feedstreams. Examples of suitable
types of reactions can include, but are not limited to,
hydroprocessing reactions, reforming reactions, oligomerization
reactions (including polymerization), alkylation reactions,
transalkylation reactions, dealkylation reactions, and synthesis
reactions such as Fischer-Tropsch and/or aromatic synthesis.
[0046] Hydroprocessing reactions provide a convenient example of a
type of reaction that can benefit from the methods described
herein. Hydroprocessing as described herein can generally refer to
treating or upgrading a feedstock (such as a hydrocarbonaceous
feed) in the presence of a catalyst and hydrogen at elevated
temperature and pressure. Hydroprocessing can particularly refer to
any process carried out in the presence of hydrogen, including, but
not limited to, hydroconversion, hydrocracking (which includes
selective hydrocracking), hydrogenation, hydrotreating,
hydrodesulfurization, hydrodenitrogenation, hydrodemetallation,
hydrodearomatization, hydroisomerization, hydrodewaxing or
catalytic dewaxing, hydrofinishing, and/or aromatic saturation. The
hydroprocessing reaction can be carried out in a vessel or a
hydroprocessing zone in which a feed can be exposed to a
hydroprocessing catalyst in the presence of hydrogen. Conditions
that can be specified for exposing a feed to a bed of
hydroprocessing catalyst can include, but are not limited to,
temperature, pressure, hydrogen flow, hydrocarbon (or
hydrocarbon-like) feed flow, or combinations thereof.
[0047] Hydroprocessing can be carried out in the presence of
hydrogen. A hydrogen stream can be fed/injected into a vessel or
reaction/hydroprocessing zone in which the hydroprocessing catalyst
is located. Hydrogen, which is contained in a hydrogen "treat gas,"
can be provided to the reaction zone. Treat gas, as referred to
herein, can be either pure hydrogen or a hydrogen-containing gas,
which is a gas stream containing hydrogen in an amount sufficient
for the intended reaction(s), optionally including one or more
other gases (e.g., nitrogen and light hydrocarbons such as
methane), and which should not adversely interfere with or affect
either the reactions or the products. Impurities, such as H.sub.2S
and NH.sub.3, may be undesirable and can be at least partially
removed from the treat gas before being conducted to the reactor.
The treat gas stream introduced into a reaction stage can
advantageously contain at least about 50 vol % or at least about 75
vol % hydrogen.
[0048] During fixed bed hydroprocessing, hydrogen can be supplied
at a rate of from about 50 SCF/B (standard cubic feet of hydrogen
per barrel of total feed) (.about.5-10 Sm.sup.3/m.sup.3) to about
50000 SCF/B (.about.9000-10000 Sm.sup.3/m.sup.3). Hydrogen can be
supplied co-currently with the hydrocarbon (or hydrocarbon-like)
feed, counter-currently, or separately via a separate gas conduit
to the hydroprocessing zone. The contact of the feed with the
hydroprocessing catalyst and the hydrogen can produce a total
product including a liquid hydroprocessed effluent, a gaseous
hydroprocessed effluent, or a combination thereof.
[0049] With regard to other fixed bed hydroprocessing conditions,
the temperature in the contacting zone (e.g., the average catalyst
bed temperature) can be about 300.degree. F. (.about.149.degree.
C.) to about 1000.degree. F. (.about.538.degree. C.), depending on
the nature of the hydroprocessing. Total pressure in the contacting
zone can range from about 50 psig (.about.350 kPag) to about 3000
psig (.about.21 MPag) or more. The hydrogen partial pressure during
hydroprocessing can be from about 50 psia (.about.350 kPaa) to
about 3000 psia (.about.21 MPaa). Liquid hourly space velocity
(LHSV) of the feed relative to the catalyst can generally range
from about 0.01 to about 30 h.sup.-1, for example from about 0.05
h.sup.-1 to about 30 h.sup.-1, from about 0.05 h.sup.-1 to about 20
h.sup.-1, from about 0.05 h.sup.-1 to about 10 h.sup.-1, from about
0.1 h.sup.-1 to about 20 h.sup.-1, or from about 0.1 to about 10
h.sup.-1.
[0050] Depending on the aspect, the threshold temperature for a
temperature-sensor structure can be at least about 20.degree. C.
greater than the average catalyst bed temperature when an abnormal
temperature event occurs, for example at least about 30.degree. C.
greater, at least about 40.degree. C. greater, or at least about
50.degree. C. greater. Additionally or alternately, the threshold
temperature for a temperature-sensor structure (such as a particle
or coating) can be selected based on a temperature associated with
and/or characteristic of the reactor vessel. For example, many
types of reactor vessels can have a design window of suitable
operating temperatures. The threshold for a temperature-sensor
structure can be selected to be at least about 20.degree. C. lower
than the maximum design operating temperature, for example at least
about 30.degree. C. lower.
[0051] A reactor can contain any convenient number of fixed beds of
catalysts. Some common reaction configurations can include 1 to 5
catalyst beds containing catalyst particles, but larger numbers of
catalyst beds can also be suitable.
[0052] Any convenient type of hydroprocessing catalyst can be used.
This can include bulk catalysts and supported catalysts, and/or
bound catalysts and binderless catalysts. Some types of
hydroprocessing catalysts can include molecular sieves and/or other
acidic or basic catalysts that facilitate a variety of types of
reactions. The relative selectivity of a catalyst that can catalyze
multiple types of reactions can be dependent on the temperature in
the reaction environment. Detection of an abnormal temperature can
be useful for fixed bed processing using such hydroprocessing
catalysts, so that unexpected increases in temperature can be
identified in a controlled manner.
[0053] In some aspects, at least one catalyst in a reactor
containing a fixed bed of catalyst can include a molecular sieve,
such as a catalyst that includes a zeolite. Optionally, a catalyst
including a zeolite and/or another type of molecular sieve can
further include one or more supported metals from Groups 6-14 of
the IUPAC periodic table. Examples of suitable metals can include
noble metals such as Pt, Pd; other Group 6 and Group 8-10 metals,
and combinations thereof. Depending on the nature of the molecular
sieve, catalysts comprising molecular sieves can be used for a
variety of hydroprocessing reactions, such as hydrocracking,
catalytic dewaxing, and aromatic saturation. Depending on the
nature of the molecular sieve, catalysts comprising molecular
sieves can further be suitable for other types of reactions, such
as alkylation, transalkylation, dealkylation, oligomerization,
and/or aromatics formation. The molecular sieves can correspond to
zeolites (silicoaluminates), or the framework of the molecular
sieve can include heteroatoms different from silicon and aluminum,
or the framework of the molecular sieve can be substantially
composed of atoms other than silicon and aluminum. Examples of
suitable molecular sieves can include, but are not limited to,
molecular sieves having a 10-member ring or 12-member ring pore
size as the largest pore channel size of the molecular sieve.
Examples of molecular sieve frameworks having a 10-member ring or
12-member ring pore channel as the largest pore channel include
*MRE, MTT, EUO, AEL, AFO, SFF, STF, MFI, FAU (including zeolite X
and Y), EMT, TON, OSI, ATO, GON, MTW, SFE, SSY, MWW, MOR, *BEA,
CON, MSE, ISV, IWR, IWV, and/or VET. Other examples of non-zeolitic
molecular sieves can include, but are not limited to, molecular
sieves having the M41S framework.
[0054] More generally, a variety of chemical conversion processes
can be performed in a fixed bed reactor environment. For each of
the exemplary processes listed below, the fixed bed processing
conditions for operation of a fixed bed reactor when performing the
corresponding process are provided. Examples of chemical conversion
processes that can be performed under fixed bed processing
conditions in a fixed bed reactor can include, but are not limited
to:
[0055] (a) alkylation of aromatics with short chain
(C.sub.2-C.sub.6) olefins, e.g., alkylation of ethylene or
propylene with benzene to produce ethylbenzene or cumene
respectively, in the gas or liquid phase, with reaction conditions
optionally including one or more of an average catalyst bed
temperature from about 10.degree. C. to about 250.degree. C., a
pressure from about 0 psig to about 500 psig (about 3.5 MPag), a
total weight hourly space velocity (WHSV) from about 0.5 hr.sup.-1
to about 100 hr.sup.-1, and an aromatic/olefin mole ratio from
about 0.1 to about 50;
[0056] (b) alkylation of aromatics with long chain
(C.sub.10-C.sub.20) olefins, in the gas or liquid phase, with
reaction conditions optionally including one or more of an average
catalyst bed temperature from about 250.degree. C. to about
500.degree. C., a pressure from about 0 psig to 500 psig (about 3.5
MPag), a total WHSV from about 0.5 hr.sup.-1 to about 50 hr.sup.-1,
and an aromatic/olefin mole ratio from about 1 to about 50;
[0057] (c) transalkylation of aromatics, in gas or liquid phase,
e.g., transalkylation of polyethylbenzenes and/or
polyisopropylbenzenes with benzene to produce ethylbenzene and/or
cumene respectively, with reaction conditions optionally including
one or more of an average catalyst bed temperature from about
100.degree. C. to about 500.degree. C., a pressure from about 1
psig (about 7 kPag) to about 500 psig (about 3.5 MPag), and a WHSV
from about 1 hr.sup.-1 to about 10,000 hr.sup.-1;
[0058] (d) disproportionation of alkylaromatics, e.g.,
disproportionation of toluene to produce xylenes, with reaction
conditions optionally including one or more of an average catalyst
bed temperature from about 200.degree. C. to about 760.degree. C.,
a pressure from about 1 atm (about 0 psig) to about 60 atm (about
5.9 MPag), a WHSV from about 0.1 hr.sup.-1 to about 20 hr.sup.-1,
and a hydrogen/hydrocarbon mole ratio from 0 (no added hydrogen) to
about 50;
[0059] (e) dealkylation of alkylaromatics, e.g., deethylation of
ethylbenzene, with reaction conditions optionally including one or
more of an average catalyst bed temperature from about 200.degree.
C. to about 760.degree. C., a pressure from about 1 atm (about 0
psig) to about 60 atm (about 5.9 MPag), a WHSV from about 0.1
hr.sup.-1 to about 20 hr.sup.-1, and a hydrogen to hydrocarbon mole
ratio from 0 (no added hydrogen) to about 50;
[0060] (f) isomerization of alkylaromatics, such as xylenes, with
reaction conditions optionally including one or more of an average
catalyst bed temperature from about 200.degree. C. to about
540.degree. C., a pressure from about 100 kPaa to about 7 MPaa, a
WHSV from about 0.1 hr.sup.-1 to about 50 hr.sup.-1, and a
hydrogen/hydrocarbon mole ratio from 0 (no added hydrogen) to about
10;
[0061] (g) reaction of paraffins with aromatics, e.g., to form
alkylaromatics and light gases, with reaction conditions optionally
including one or more of an average catalyst bed temperature from
about 260.degree. C. to about 375.degree. C., a pressure from about
0 psig to about 1000 psig (about 6.9 MPag), a WHSV from about 0.5
hr.sup.-1 to about 10 hr.sup.-1, and a hydrogen/hydrocarbon mole
ratio from 0 (no added hydrogen) to about 10;
[0062] (h) paraffin isomerization to provide branched paraffins
with reaction conditions optionally including one or more of an
average catalyst bed temperature from about 200.degree. C. to about
315.degree. C., a pressure from about 100 psig (about 690 kPag) to
about 1000 psig (about 6.9 MPag), a WHSV from about 0.5 hr.sup.-1
to about 10 hr.sup.-1, and a hydrogen to hydrocarbon mole ratio
from about 0.5 to about 10;
[0063] (i) alkylation of iso-paraffins, such as isobutane, with
olefins, with reaction conditions optionally including one or more
of an average catalyst bed temperature from about -20.degree. C. to
about 350.degree. C., a pressure from about 0 psig to about 700
psig (about 4.9 MPag), and a total olefin WHSV from about 0.02
hr.sup.-1 to about 10 hr.sup.-1;
[0064] (j) dewaxing of paraffinic feeds with reaction conditions
optionally including one or more of an average catalyst bed
temperature from about 200.degree. C. to about 450.degree. C., a
pressure from about 0 psig to about 1000 psig (about 6.9 MPag), a
WHSV from about 0.2 hr.sup.-1 to about 10 hr.sup.-1, and a
hydrogen/hydrocarbon mole ratio from about 0.5 to about 10;
[0065] (k) cracking of hydrocarbons with reaction conditions
optionally including one or more of an average catalyst bed
temperature from about 300.degree. C. to about 700.degree. C., a
pressure from about 0.1 atm (about 10 kPag) to about 30 atm (about
3 MPag), and a WHSV from about 0.1 hr.sup.-1 to about 20 hr.sup.-1;
and/or
[0066] (l) isomerization of olefins with reaction conditions
optionally including one or more of an average catalyst bed
temperature from about 250.degree. C. to about 750.degree. C., an
olefin partial pressure from about 30 kPa to about 300 kPa, and a
WHSV from about 0.5 hr.sup.-1 to about 500 hr.sup.-1.
Examples of System Configurations
[0067] FIG. 1 schematically shows an example of a reactor 100
containing a fixed bed including both catalyst particles and
temperature-sensor particles. In FIG. 1, reactor 100 can include a
catalyst bed 110 shown as containing particles, which can represent
both catalyst particles and temperature-sensor particles. The
catalyst particles can be loaded into catalyst bed 110 in any
convenient manner. One option for loading temperature-sensor
particles can be to distribute the temperature-sensor particles
throughout the bed. This can correspond to a random distribution; a
distribution corresponding to a pattern, such as distribution
according to a grid pattern or radial pattern; a random
distribution along one axis while following a pattern along a
second axis; or distribution in selected areas of a catalyst bed,
such as preferentially distributing the catalyst near the walls of
the reactor and/or near other structural features of the catalyst
bed.
[0068] The reactor depicted in FIG. 1 can correspond to a down-flow
fixed bed and/or trickle bed reactor. During operation, a feed (or
multiple feeds) can be introduced into reactor 100 using one or
more reactor inlets 120. Optionally, additional reactor inlets 120
can be used to introduce treat gases (such as hydrogen) into the
reactor 100, or treat gases can be introduced using the same
inlet(s) as the feed. The feedstock can contact the catalyst in
catalyst bed 110, and the resulting effluent can exit from one (or
more) reactor outlet(s) 130. A detector 135 can directly monitor
the flow in a single or primary reactor outlet 130, or
alternatively detector 135 can be located to monitor a portion of a
reactor outlet 130 corresponding to a side stream or slip stream of
the primary outlet flow. In other aspects, reactor inlet(s) 110 and
outlet(s) 130 can be provided to allow for other convenient modes
of operation, such as upflow, co-current, and/or counter-current
operation.
[0069] FIG. 2 schematically shows another example of a reactor 200
with a temperature-sensor coating for detection of abnormal
temperature events. In FIG. 2, a coating 242 can be located on at
least portions of interior wall 240 of reactor 200. The locations
of coating 242 on the interior wall 240 of reactor 200 can
correspond to any convenient design. For example, the coating 242
can correspond to the entire surface of interior walls 240 for the
entire depth of catalyst bed 210, or even beyond the extent of
catalyst bed 210. Alternatively, coating 242 can be applied as a
series of coating strips on interior wall 240, such as coating
strips spaced in a regular pattern around the interior wall 240.
Alternatively, coating 242 can be located on less than the full
depth of the catalyst bed, in continuous horizontal strips around
the interior wall 240, in vertical strips that have a depth less
than the catalyst bed, and/or in any other convenient pattern.
Similar to FIG. 1, the reactor configuration shown in FIG. 2 can
correspond to a downflow configuration, where a feed (and/or
multiple feeds and/or treat gas) can be introduced into reactor 200
using reactor inlet(s) 220, while the effluent formed by contacting
the feed with the catalyst in catalyst bed 210 can exit reactor 200
using reactor outlet(s) 230. Also similar to FIG. 1, detector 235
can be located at reactor outlet 230 for detection of the
detectable substance.
[0070] When a temperature-sensor structure is provided as a coating
on the interior wall 340 within a reactor, at least two types of
configurations can be used. FIG. 3 shows a coating configuration
where the coating 342 can be the temperature-sensor structure. The
arrow in FIG. 3 indicates the direction of flow of effluent
relative to the reactor wall. In this type of aspect, the coating
342 can undergo a structural change when a threshold temperature is
exceeded (i.e., an abnormal temperature) in proximity to the
coating, such as at a hot spot 360. In this type of configuration,
the material 356 of the coating 342 can correspond to the
detectable substance, either directly or indirectly, or a dye 358
(or another detectable substance) can be mixed with the coating 342
and/or trapped behind the coating 342, so that the dye 358 can be
introduced into the effluent in catalyst bed 310 when an abnormal
temperature event occurs.
[0071] FIG. 4 shows an alternative configuration where the coating
442 can provide support for maintaining the position of
temperature-sensor particles 454 within the coating 442. In this
type of configuration, a temperature-sensor particle 454 can
undergo a structural change when exposed to an abnormal
temperature. In such a configuration, the coating 442 supporting
the particles 454 may not undergo a structural change, so that only
the temperature-sensor particles 454 can have a structural change
when exposed to the abnormal temperature. Similar to the
configuration in FIG. 3, the presence of an abnormal temperature,
such as due to hot spot 460, can allow a detectable substance to be
released into the effluent in catalyst bed 410.
Use of Multiple Temperature-Sensor Materials with Different
Temperature Thresholds
[0072] In some aspects, more than one type of temperature sensor
structure can be used for detection of abnormal temperature events.
The different types of temperature-sensor structures can be
selected in order to provide additional information regarding the
nature of an abnormal temperature event.
[0073] One option can be to use a plurality of temperature-sensor
structures containing different (directly or indirectly) detectable
substances. This can be useful for providing additional information
regarding the location of an abnormal temperature event. For
example, the volume of a catalyst bed can be divided into an
arbitrary number of regions. The temperature-sensor particles
introduced into a given region can be selected based on the nature
of the detectable substance introduced into the reactor effluent by
the particle. When an abnormal temperature event occurs, the region
of the catalyst bed where the abnormal temperature occurred can be
identified based on the detectable substance that was detected at
the reactor outlet. As another variation, one type of detectable
substance can be used for a temperature-sensor coating while
another type of detectable substance can be used for
temperature-sensor particles distributed in the catalyst bed. This
can provide information regarding whether an abnormal temperature
event occurred near a reactor wall versus an interior portion of a
catalyst bed.
[0074] Still other convenient combinations of using multiple
temperature-sensor structures with different detectable substances
can additionally or alternatively be used. As another example,
temperature-sensor structures with different threshold temperatures
can be introduced into a catalyst bed and/or placed in a coating.
In this type of example, when an abnormal temperature occurs, there
can be a period of time where the abnormal temperature can exceed a
first temperature threshold but can be lower than a second
temperature threshold. The resulting detectable substance
introduced into the reactor effluent can allow the operator to
identify a range for the abnormal temperature in the reactor. If
the temperature continues to increase, a second (or possibly more)
temperature threshold(s) can be exceeded, resulting in release of
additional detectable substances. Having temperature-sensor
structures with multiple thresholds can provide information, for
example, regarding the severity of an abnormal temperature event.
If multiple temperature thresholds are exceeded during a relatively
short period of time, this may indicate a more serious event
requiring a greater response, such as entirely shutting down a
reactor versus simply reducing a flow rate of feed into a
reactor.
Additional Embodiments
Embodiment 1
[0075] A method for processing a feed in a fixed bed reactor,
comprising: exposing a hydrocarbon-like feed to a catalyst in a
fixed catalyst bed in a reactor under fixed bed processing
conditions to form a reactor effluent, the fixed bed processing
conditions comprising an average catalyst bed temperature for the
fixed catalyst bed, the reactor further comprising one or more
temperature-sensor structures, the one or more temperature-sensor
structures having a threshold temperature; and detecting a
detectable substance in the reactor effluent, the detectable
substance being introduced into the reactor effluent by at least
one of the one or more temperature-sensor structures, wherein: a)
when the detectable substance is detectable prior to exposing a
temperature-sensor structure to the threshold temperature, the
amount of detectable substance detected in the reactor effluent is
at least about 1% greater (for example at least about 2% greater,
at least about 5% greater, at least about 10% greater, or at least
about 100% greater) than an average amount detected in the reactor
effluent at the average catalyst bed temperature; or b) when the
detectable substance is not detectable prior to exposing a
temperature-sensor structure to a threshold temperature, the amount
of detectable substance in the reactor effluent is greater than the
detection limit for the detectable substance.
Embodiment 2
[0076] A fixed bed processing system, comprising: a reactor vessel
having a reactor inlet and a reactor outlet; at least one fixed bed
of catalyst particles within the reactor vessel; one or more
temperature-sensor structures within the reactor vessel; a detector
in fluid communication with the reactor outlet, the detector
optionally comprising a spectroscopic detector, a radiation
detector, a chromatographic detector, or a combination thereof,
wherein the one or more temperature-sensor structures are composed
of a material that undergoes a structural change at a threshold
temperature, and wherein the one or more temperature-sensor
structures have a first rate of introducing a detectable substance
into the reactor at a temperature below the threshold temperature
and a second rate of introducing the detectable substance at a
temperature above the threshold temperature, the second
introduction rate being at least about 5 times (e.g., at least
about 10 times, at least about 25 times, at least about 100 times,
or at least about 1000 times) the first introduction rate.
Embodiment 3
[0077] The method of Embodiment 1, wherein the amount of detectable
substance detected in the reactor effluent is at least about 10
times greater (for example at least about 25 times greater, at
least about 100 times greater, or at least about 1000 times
greater) than the average amount detected at the average catalyst
bed temperature.
Embodiment 4
[0078] The method of Embodiment 1 or 3, wherein the one or more
temperature-sensor structures have a first rate of introducing the
detectable substance into the reactor at a temperature below the
threshold temperature and a second rate of introducing the
detectable substance at a temperature above the threshold
temperature, the second introduction rate being at least about 5
times the first introduction rate.
Embodiment 5
[0079] The method of any of Embodiments 1 and 3-4, wherein the
average bed temperature is at least about 20.degree. C. lower than
the threshold temperature, or at least about 30.degree. C. lower,
or at least about 40.degree. C. lower.
Embodiment 6
[0080] The method of any of embodiments 1 and 3-5, wherein the
hydrocarbon-like feed comprises a petroleum feed, a renewable feed,
a refinery feed, a chemicals feed, or a combination thereof.
Embodiment 7
[0081] The system or method of any of the above Embodiments,
wherein the one or more temperature-sensor structures are composed
of a material, the detectable substance being directly or
indirectly formed from the material.
Embodiment 8
[0082] The system or method of any of the above Embodiments,
wherein the one or more temperature-sensor structures comprise
temperature-sensor particles, the temperature-sensor particles
optionally having a diameter that is about 0.25 times to about 4
times the diameter of an average catalyst particle diameter in the
catalyst bed.
Embodiment 9
[0083] The system or method of Embodiment 8, wherein the
temperature-sensor particles are distributed randomly in the
catalyst bed, wherein the temperature-sensor particles further
comprise a catalyst, or a combination thereof.
Embodiment 10
[0084] The system or method of any of Embodiments 1-7, wherein at
least a portion of the temperature-sensor structures are
distributed randomly in the catalyst bed, wherein at least a
portion of the temperature-sensor structures further comprise a
catalyst, or a combination thereof.
Embodiment 11
[0085] The system or method of any of the above Embodiments,
wherein the one or more temperature-sensor structures comprise at
least a first temperature-sensor structure having a first threshold
temperature and a second temperature-sensor structure having a
second threshold temperature.
Embodiment 12
[0086] The system or method of any of the above Embodiments,
wherein a first temperature-sensor structure introduces a first
detectable substance into the reactor, a second temperature-sensor
structure introduces a second detectable substance into the
reactor, and the first detectable substance is different from the
second detectable substance.
Embodiment 13
[0087] The system or method of any of the above Embodiments,
wherein the reactor comprises a coating on an interior surface, the
coating a) being at least one of the one or more temperature-sensor
structures; b) comprising one or more temperature-sensor particles;
or c) a combination thereof.
Embodiment 14
[0088] The system or method of any of the above Embodiments,
wherein the detectable substance is an indirectly detectable
substance.
Embodiment 15
[0089] The method of any of Embodiments 1 and 3-14, wherein, when
the detectable substance is not detectable prior to exposing a
temperature-sensor structure to a threshold temperature, the amount
of detectable substance detected in the reactor effluent is about 1
ppb to about 1000 ppm by weight.
Embodiment 16
[0090] The method of any of Embodiments 1 and 3-15, wherein the
fixed bed processing conditions comprise fixed bed hydroprocessing
conditions, which optionally comprise a treat gas rate from about
50 SCF/B (.about.5-10 Sm.sup.3/m.sup.3) to about 50000 SCF/B
(.about.9000-10000 Sm.sup.3/m.sup.3), an average catalyst bed
temperature from about 300.degree. F. (.about.149.degree. C.) to
about 1000.degree. F. (.about.538.degree. C.), a total pressure
from about 50 psig (.about.350 kPag) to about 3000 psig (.about.21
MPag), a hydrogen partial pressure from about 50 psia (.about.350
kPaa) to about 3000 psia (.about.21 MPaa), and a liquid hourly
space velocity (LHSV) of the feed relative to the catalyst from
about 0.01 h.sup.-1 to about 30 h.sup.-1.
EXAMPLE
Application of Inventive Concept to Hydroprocessing for Lubricant
Base Stock Production
[0091] Catalytic methods for formation of lubricant base stocks
often involve exposing a feed having a boiling range of about
650.degree. F. (.about.343.degree. C.) to about 1050.degree. F.
(.about.566.degree. C.) to a series of catalysts under selected
hydroprocessing conditions. Exposing the feed and/or the resulting
intermediate effluents to the catalysts can be conveniently
performed using fixed catalyst beds.
[0092] As shown below, fixed bed hydrocracking conditions can often
involve catalyst bed temperatures of about 300.degree. C. to about
450.degree. C. Catalytic dewaxing can involve catalyst bed
temperatures of about 250.degree. C. to about 430.degree. C. The
specific temperature ranges can depend on the nature of the feed
and the nature of the catalyst. While hydrocracking and dewaxing
reactions can be well-controlled in the desired temperature ranges,
exposing a feed to a hydrocracking and/or dewaxing catalyst at
higher temperatures can potentially lead to undesirable increases
in activity for alternative reaction pathways and/or undesirable
increases in cracking activity. This can result in localized
heating and temperature increases in a catalyst bed, leading to
still higher reaction rates and further heating and temperature
increases. The temperature-sensor structures described herein can
be used to detect temperatures above a desired or target
temperature range within a catalyst bed. Based on the temperatures
of operation for hydrocracking and catalytic dewaxing, suitable
choices of a material for a temperature-sensor particle or coating
can be zinc (melting point .about.420.degree. C.) or magnesium
alloys (melting point .about.349.degree. C.-649.degree. C.). When a
temperature-sensor particle or coating made from zinc or a
magnesium alloy melts, a substance contained within the particle or
coating can be introduced into the reactor effluent and
detected.
[0093] One type of catalytic processing during lubricant base stock
production can be hydrocracking. During lubricant base stock
production, hydrocracking can be used for removal of heteroatom
contaminants and/or for producing an upgraded effluent with an
improved viscosity index.
[0094] Hydrocracking catalysts typically contain sulfided base
metals on acidic supports, such as amorphous silica alumina,
cracking zeolites such as USY, or acidified alumina. Often these
acidic supports are mixed or bound with other metal oxides such as
alumina, titania or silica. Examples of suitable acidic supports
include acidic molecular sieves, such as zeolites or
silicoaluminophophates. One example of suitable zeolite is USY,
such as a USY zeolite with cell size of .about.24.30 Angstroms or
less. Additionally or alternately, the catalyst can be a low
acidity molecular sieve, such as a USY zeolite with a Si to Al
ratio of at least about 20, and preferably at least about 40 or at
least about 50. ZSM-48, such as ZSM-48 with a SiO.sub.2 to
Al.sub.2O.sub.3 ratio of about 110 or less (such as about 100 or
less, about 90 or less, from about 40 to about 100, or from about
40 to about 90) is another example of a potentially suitable
hydrocracking catalyst. Still another option is to use a
combination of USY and ZSM-48. Still other options include using
one or more of zeolite Beta, ZSM-5, ZSM-35, or ZSM-23, either alone
or in combination with a USY catalyst. Non-limiting examples of
metals for hydrocracking catalysts include metals or combinations
of metals that include at least one Group VIII metal, such as
nickel, nickel-cobalt-molybdenum, cobalt-molybdenum,
nickel-tungsten, nickel-molybdenum, and/or
nickel-molybdenum-tungsten. Additionally or alternately,
hydrocracking catalysts with noble metals can also be used.
Non-limiting examples of noble metal catalysts include those based
on platinum and/or palladium. Support materials which may be used
for both the noble and non-noble metal catalysts can comprise a
refractory oxide material such as alumina, silica, alumina-silica,
kieselguhr, diatomaceous earth, magnesia, zirconia, or combinations
thereof, with alumina, silica, alumina-silica being the most common
(and preferred, in an embodiment).
[0095] When only one hydrogenation metal is present on a
hydrocracking catalyst, the amount of that hydrogenation metal can
be at least about 0.1 wt % based on the total weight of the
catalyst, for example at least about 0.5 wt % or at least about 0.6
wt %. Additionally or alternately when only one hydrogenation metal
is present, the amount of that hydrogenation metal can be about 5.0
wt % or less based on the total weight of the catalyst, for example
about 3.5 wt % or less, about 2.5 wt % or less, about 1.5 wt % or
less, about 1.0 wt % or less, about 0.9 wt % or less, about 0.75 wt
% or less, or about 0.6 wt % or less. Further additionally or
alternately when more than one hydrogenation metal is present, the
collective amount of hydrogenation metals can be at least about 0.1
wt % based on the total weight of the catalyst, for example at
least about 0.25 wt %, at least about 0.5 wt %, at least about 0.6
wt %, at least about 0.75 wt %, or at least about 1 wt %. Still
further additionally or alternately when more than one
hydrogenation metal is present, the collective amount of
hydrogenation metals can be about 35 wt % or less based on the
total weight of the catalyst, for example about 30 wt % or less,
about 25 wt % or less, about 20 wt % or less, about 15 wt % or
less, about 10 wt % or less, or about 5 wt % or less. In
embodiments wherein the supported metal comprises a noble metal,
the amount of noble metal(s) is typically less than about 2 wt %,
for example less than about 1 wt %, about 0.9 wt % or less, about
0.75 wt % or less, or about 0.6 wt % or less. It is noted that
hydrocracking under sour conditions is typically performed using a
base metal (or metals) as the hydrogenation metal.
[0096] A hydrocracking process can be carried out at temperatures
of about 550.degree. F. (.about.288.degree. C.) to about
840.degree. F. (.about.449.degree. C.), hydrogen partial pressures
of from about 1500 psig to about 5000 psig (.about.10.3 MPag to
.about.34.6 MPag), liquid hourly space velocities from about 0.05
h.sup.-1 to 10 h.sup.-1, and hydrogen treat gas rates from about
35.6 m.sup.3/m.sup.3 to about 1781 m.sup.3/m.sup.3 (.about.200
SCF/B to .about.10000 SCF/B). In other embodiments, the conditions
can include temperatures in the range of about 600.degree. F.
(343.degree. C.) to about 815.degree. F. (435.degree. C.), hydrogen
partial pressures of from about 1500 psig to about 3000 psig (10.3
MPag-20.9 MPag), and hydrogen treat gas rates of from about 213
m.sup.3/m.sup.3 to about 1070 m.sup.3/m.sup.3 (.about.1200 SCF/B to
6000 SCF/B). The LHSV can be from about 0.25 h.sup.-1 to about 50
h.sup.-1 or from about 0.5 h.sup.-1 to about 20 h.sup.-1, for
example from about 1.0 h.sup.-1 to about 4.0 h.sup.-1.
[0097] In some aspects, a portion of the hydrocracking catalyst can
be contained in a second reactor stage. In such aspects, a first
reaction stage of the hydroprocessing reaction system can include
one or more hydrotreating and/or hydrocracking catalysts. The
conditions in the first reaction stage can be suitable for reducing
the sulfur and/or nitrogen content of the feedstock. A separator
can then be used in between the first and second stages of the
reaction system to remove gas phase sulfur and nitrogen
contaminants. One option for the separator can be to simply perform
a gas-liquid separation to remove contaminant. Another option can
be to use a separator such as a flash separator that can perform a
separation at a higher temperature. Such a high temperature
separator can be used, for example, to separate the feed into a
portion boiling below a temperature cut point, such as about
350.degree. F. (.about.177.degree. C.) or about 400.degree. F.
(.about.204.degree. C.), and a portion boiling above the
temperature cut point. In this type of separation, the naphtha
boiling range portion of the effluent from the first reaction stage
can be removed, thus reducing the volume of effluent processed in
the second or other subsequent stages. Of course, any low boiling
contaminants in the effluent from the first stage could be
separated into the portion boiling below the temperature cut point.
If sufficient contaminant removal is performed in the first stage,
the second stage can be operated as a "sweet" or low contaminant
stage.
[0098] Still another option can be to use a separator between the
first and second stages of the hydroprocessing reaction system that
can perform at least a partial fractionation of the effluent from
the first stage. In this type of aspect, the effluent from the
first hydroprocessing stage can be separated into at least a
portion boiling below the distillate (such as diesel) fuel range, a
portion boiling in the distillate fuel range, and a portion boiling
above the distillate fuel range. The distillate fuel range can be
defined based on a conventional diesel boiling range, such as
having a lower end cut point temperature of at least about
350.degree. F. (.about.177.degree. C.) or at least about
400.degree. F. .about.(204.degree. C.) to having an upper end cut
point temperature of about 700.degree. F. (.about.371.degree. C.)
or less or about 650.degree. F. (.about.343.degree. C.) or less.
Optionally, the distillate fuel range can be extended to include
additional kerosene, such as by selecting a lower end cut point
temperature of at least about 300.degree. F. (.about.149.degree.
C.).
[0099] In aspects where the inter-stage separator is also used to
produce a distillate fuel fraction, the portion boiling below the
distillate fuel fraction includes, naphtha boiling range molecules,
light ends, and contaminants such as H.sub.2S. These different
products can be separated from each other in any convenient manner.
Similarly, one or more distillate fuel fractions can be formed, if
desired, from the distillate boiling range fraction. The portion
boiling above the distillate fuel range represents the potential
lubricant base stocks. In such aspects, the portion boiling above
the distillate fuel range is subjected to further hydroprocessing
in a second hydroprocessing stage. Optionally, the lighter lube
fractions can be distilled and operated in the catalyst dewaxing
sections in a blocked operation where the conditions are adjusted
to maximize the yield and properties of each lube cut.
[0100] Prior to, during, and/or after exposing a feed (including an
intermediate effluent) to a hydrocracking catalyst, a feed can also
be exposed to a dewaxing catalyst to improve cold flow properties
of the resulting product. For catalytic dewaxing, suitable dewaxing
catalysts can include molecular sieves such as crystalline
aluminosilicates (zeolites). In an embodiment, the molecular sieve
can comprise, consist essentially of, or be ZSM-22, ZSM-23, ZSM-48.
Optionally but preferably, molecular sieves that are selective for
dewaxing by isomerization as opposed to cracking can be used, such
as ZSM-48, ZSM-23, or a combination thereof. Additionally or
alternately, the molecular sieve can comprise, consist essentially
of, or be a 10-member ring 1-D molecular sieve, such as EU-2,
EU-11, ZBM-30, ZSM-48, or ZSM-23. ZSM-48 is most preferred. Note
that a zeolite having the ZSM-23 structure with a silica to alumina
ratio of from about 20:1 to about 40:1 can sometimes be referred to
as SSZ-32. Optionally but preferably, the dewaxing catalyst can
include a binder for the molecular sieve, such as alumina, titania,
silica, silica-alumina, zirconia, or a combination thereof, for
example alumina and/or titania or silica and/or zirconia and/or
titania.
[0101] Preferably, the dewaxing catalysts used in processes
according to the invention are catalysts with a low ratio of silica
to alumina. For example, for ZSM-48, the ratio of silica to alumina
in the zeolite can be about 100:1 or less, such as about 90:1 or
less, or about 75:1 or less, or about 70:1 or less. Additionally or
alternately, the ratio of silica to alumina in the ZSM-48 can be at
least about 50:1, such as at least about 60:1, or at least about
65:1.
[0102] In various embodiments, the catalysts according to the
invention further include a metal hydrogenation component. The
metal hydrogenation component is typically a Group VI and/or a
Group VIII metal. Preferably, the metal hydrogenation component can
be a combination of a non-noble Group VIII metal with a Group VI
metal. Suitable combinations can include Ni, Co, or Fe with Mo
and/or W, advantageously in some embodiments Ni with Mo and/or
W.
[0103] The amount of metal in the catalyst can be at least about
0.1 wt % based on catalyst, for example at least about 0.5 wt %, at
least about 1.0 wt %, at least about 2.5 wt %, or at least about
5.0 wt %, based on catalyst. Additionally or alternatively, the
amount of metal in the catalyst can be 20 wt % or less based on
catalyst, for example about 10 wt % or less, about 5 wt % or less,
about 2.5 wt % or less, or about 1 wt % or less. For embodiments
where the metal is a combination of a non-noble Group VIII metal
with a Group VI metal, the combined amount of metal can be from
about 0.5 wt % to about 20 wt %, for example from about 1 wt % to
about 15 wt % or from about 2.5 wt % to about 10 wt %.
[0104] Fixed bed processing conditions for catalytic dewaxing of a
feedstock in the presence of a dewaxing catalyst can include a
temperature from about 300.degree. C. to about 450.degree. C.,
e.g., from about 343.degree. C. to about 435.degree. C., a hydrogen
partial pressure from about 3.5 MPag to about 34.5 MPag (.about.500
psig to 5000 psig), e.g., from about 4.8 MPag to about 21 MPag
(.about.700 psig to .about.3000 psig), and a hydrogen circulation
rate from about 180 m.sup.3/m.sup.3 (.about.1000 SCF/B) to 1800
m.sup.3/m.sup.3 (.about.10000 SCF/B), e.g., from about 210
m.sup.3/m.sup.3 (.about.1200 SCF/B) to about 1100 m.sup.3/m.sup.3
(.about.6000 SCF/B). The LHSV can be from about 0.2 h.sup.-1 to
about 10 h.sup.-1, such as from about 0.5 h.sup.-1 to about 5
h.sup.-1 or from about 1 h.sup.-1 to about 4 h.sup.-1.
[0105] The principles and modes of operation of this invention have
been described above with reference to various exemplary and
preferred embodiments. As understood by those of skill in the art,
the overall invention, as defined by the claims, encompasses other
preferred embodiments not specifically enumerated herein.
* * * * *