U.S. patent application number 12/258920 was filed with the patent office on 2010-04-29 for heat pump for high purity bottom product.
Invention is credited to Paul A. Sechrist, David A. Wegerer.
Application Number | 20100101273 12/258920 |
Document ID | / |
Family ID | 42116164 |
Filed Date | 2010-04-29 |
United States Patent
Application |
20100101273 |
Kind Code |
A1 |
Sechrist; Paul A. ; et
al. |
April 29, 2010 |
Heat Pump for High Purity Bottom Product
Abstract
An apparatus for reducing the energy consumption of a
distillation column is disclosed. The apparatus draws off an
intermediate vapor stream from the rectification section of the
distillation column, where the vapor stream is compressed and used
to reboil a portion of the bottoms stream. The compressed vapor
stream transfers energy to the bottoms stream, thereby condensing a
portion of the vapor stream while vaporizing the bottoms
stream.
Inventors: |
Sechrist; Paul A.; (South
Barrington, IL) ; Wegerer; David A.; (Lisle,
IL) |
Correspondence
Address: |
HONEYWELL/UOP;PATENT SERVICES
101 COLUMBIA DRIVE, P O BOX 2245 MAIL STOP AB/2B
MORRISTOWN
NJ
07962
US
|
Family ID: |
42116164 |
Appl. No.: |
12/258920 |
Filed: |
October 27, 2008 |
Current U.S.
Class: |
62/620 ;
62/335 |
Current CPC
Class: |
B01D 3/322 20130101;
B01D 3/4266 20130101 |
Class at
Publication: |
62/620 ;
62/335 |
International
Class: |
F25J 3/00 20060101
F25J003/00; F25B 7/00 20060101 F25B007/00 |
Claims
1. An apparatus for the distillation separation of a first
component from a mixture comprising: a distillation column
comprising a rectifying section having an outlet for an overhead
vapor stream, a stripping section having an outlet for a bottoms
liquid stream, and feed section having a feed inlet and disposed
between the rectifying section and the stripping section; a bottoms
reboiler section for reboiling the bottoms liquid stream entering
from the stripping section; an overhead condensing section for
condensing the overhead vapor stream from the rectifying section; a
side vapor draw from the rectifying section; a heat pump compressor
having an inlet in fluid communication with the side vapor draw,
and an outlet; and a second reboiler heat exchanger having a fluid
side in fluid communication with the bottoms stream from the
stripping section, and having a vapor side in fluid communication
with the outlet from the heat pump compressor.
2. The apparatus of claim 1 further comprising a second heat pump
compressor having an inlet in fluid communication with the overhead
vapor stream, and an outlet thereby generating an overhead
compressed vapor stream.
3. The apparatus of claim 2 wherein the bottom reboiler section
comprises a heat exchanger having fluid side in fluid communication
with the bottoms stream from the stripping section, and having a
vapor side in fluid communication with the overhead compressed
vapor stream.
4. The apparatus of claim 2 further comprising a condenser having
an inlet in fluid communication with the second heat pump outlet,
and for condensing a portion of the overhead compressed vapor
stream.
5. The apparatus of claim 4 wherein the condenser is a trim
condenser.
6. The apparatus of claim 2 further comprising a vapor-liquid
separation tank for separating having an inlet in fluid
communication with the rectifying section outlet, and an outlet in
fluid communication with the second heat pump compressor inlet.
7. The apparatus of claim 1 further comprising a third reboiler for
reboiling additional liquid from the bottoms stream.
8. The apparatus of claim 1 wherein the side vapor draw is
positioned above the lowest tray of the rectifying section.
9. The apparatus of claim 1 further comprising a side inlet to the
rectifying section and wherein the heat pump compressor outlet is
in fluid communication with the side inlet to the rectifying
section.
10. An apparatus for the distillation separation of a first
component from a mixture comprising: a distillation column
comprising a rectifying section having an outlet for an overhead
vapor stream, a stripping section having an outlet for a bottoms
liquid stream, and feed section having a feed inlet and disposed
between the rectifying section and the stripping section; an
overhead condensing section for condensing the overhead vapor
stream from the rectifying section; an overhead heat pump
compressor having an inlet in fluid communication with the overhead
vapor stream, and an outlet thereby generating an overhead
compressed vapor stream; a bottoms reboiler section for reboiling
the bottoms liquid stream entering from the stripping section,
wherein the bottom reboiler section comprises a heat exchanger
having fluid side in fluid communication with the bottoms stream
from the stripping section, and having a vapor side in fluid
communication with the overhead compressed vapor stream; a side
vapor draw from the rectifying section; a side inlet in the
rectifying section; a second heat pump compressor having an inlet
in fluid communication with the side vapor draw, and an outlet in
fluid communication with the side inlet to the rectifying section;
and a second reboiler heat exchanger having a fluid side in fluid
communication with the bottoms stream from the stripping section,
and having a vapor side in fluid communication with the outlet from
the second heat pump compressor.
11. The apparatus of claim 10 further comprising a trim condenser
having an inlet in fluid communication with the overhead heat pump
outlet, and for condensing a portion of the overhead compressed
vapor stream.
12. The apparatus of claim 10 further comprising a vapor-liquid
separation tank for separating having in inlet in fluid
communication with the rectifying section outlet, and an outlet in
fluid communication with the overhead heat pump compressor
inlet.
13. The apparatus of claim 10 further comprising a third reboiler
in fluid communication with the bottoms stream from the stripping
section, and having a vapor outlet in fluid communication with the
bottom of the stripping section of the distillation column.
14. An apparatus for the distillation of a first component from a
mixture comprising: a distillation column comprising a rectifying
section having an outlet for an overhead vapor stream, a stripping
section having an outlet for a bottoms liquid stream, and feed
section having a feed inlet and disposed between the rectifying
section and the stripping section; a side draw; a first bottoms
reboiler section comprising a means for reducing the pressure in
the bottoms liquid stream, a first reboiler having a liquid side in
fluid communication with the bottoms liquid stream and a vapor side
in fluid communication with the overhead vapor stream, and a first
heat pump compressor in fluid communication with the first reboiler
liquid side; and a vapor-liquid separation drum having an inlet in
fluid communication with the first reboiler vapor side and an
outlet in fluid communication with the top of the rectifying
section.
15. The apparatus of claim 14 wherein the side draw is a vapor side
draw from the rectifying section.
16. The apparatus of claim 15 further comprising a second reboiler
having a liquid side in fluid communication with the bottoms liquid
stream and a vapor side in fluid communication with the side vapor
from the side vapor draw, and a second heat pump compressor in
fluid communication with the second reboiler liquid side.
17. The apparatus of claim 14 further comprising a second means for
reducing pressure in the bottoms liquid stream.
18. The apparatus of claim 14 wherein the means for reducing
pressure is a Joule-Thompson type valve.
19. The apparatus of claim 14 wherein the side draw is a liquid
side draw from the stripping section.
20. The apparatus of claim 19 further comprising a second means for
reducing the liquid pressure from the liquid side draw, a second
reboiler having a liquid side in fluid communication with the
liquid side draw and a vapor side in fluid communication with a
portion of the overhead vapor stream, and a second heat pump
compressor in fluid communication with the second reboiler liquid
side.
Description
FIELD OF THE INVENTION
[0001] This invention relates to the separation of hydrocarbons.
Specifically, the invention relates to improving the energy usage
for the separation of hydrocarbon components that have similar
boiling points through distillation.
BACKGROUND OF THE INVENTION
[0002] The separation of hydrocarbons is a basic process in the
petroleum industry. Petroleum is a mixture of many hydrocarbon
compounds and the compounds are separated and used for different
purposes, such as fuel, lubricants, feedstock to polymer plants,
etc. One method of separation in the petroleum industry is
distillation. Distillation is a method of separation that is based
on a difference in the relative volatilities of the components in a
mixture, and therefore differences in the composition between a
liquid mixture and a vapor formed from the liquid mixture. In a
standard continuous distillation process involving multiple stages,
the differences in composition allows for partial separation at
each stage. The liquid and vapor phases are passed to different
stages, and further produce new liquid and vapor phases in each
having different compositions.
[0003] A problem exists for distillation systems in that they are
large consumers of energy and inefficient with respect to energy
usage and consumption. Improvements in design can significantly
reduce energy consumption. With increasing energy costs and with
increasing pressures to reduce CO.sub.2 emissions associated with
energy consumption, there is a compelling need for more efficient
distillation designs.
SUMMARY OF THE INVENTION
[0004] The present invention provides for a more efficient energy
usage in the distillation of a mixture. The distillation
improvement provides for increasing the purity of the bottoms
product while reducing the amount of external energy added to
reboil the bottoms stream to create the vapor for stripping the
lighter components from the bottoms stream.
[0005] The apparatus of the present invention includes a
distillation column, an overhead reflux condenser, and a bottoms
reboiler. The distillation column has a rectifying section with an
access port for drawing of an intermediate vapor stream. The
apparatus further includes a heat pump compressor for compressing
an intermediate vapor stream and a second reboiler heat exchanger.
The second reboiler heat exchanger vaporizes a portion of the
bottoms stream while cooling the compressed intermediate vapor
stream. The cooled compressed intermediate stream is passed back to
the rectifying section of the column, and the vaporized bottoms
stream is passed back to the bottom of the stripping section of the
distillation column.
[0006] Other objects, advantages and applications of the present
invention will become apparent to those skilled in the art from the
following detailed description and drawings.
BRIEF DESCRIPTION OF THE DRAWINGS
[0007] FIG. 1 shows a diagram of an embodiment of the
invention;
[0008] FIG. 2 shows a diagram of an embodiment with an additional
heat pump compressor for compressing the overhead vapor stream;
[0009] FIG. 3 shows a diagram for an alternate embodiment with
flashing of the bottoms liquid; and
[0010] FIG. 4 shows an alternate diagram for the embodiment with
flashing of the bottoms liquid.
DETAILED DESCRIPTION OF THE INVENTION
[0011] The separation of fluids is well known in art, and
separation by distillation is a common means for separating two or
more liquids. A distillation process operates on the principle of
different liquid components in a mixture have different
volatilities, and therefore will develop an equilibrium where for
the more volatile component, the vapor phase has a higher
concentration relative to that components concentration in the
liquid phase.
[0012] In a continuous distillation process, the basic equipment
comprises a distillation column having a plurality of plates, an
overhead condenser, and a bottoms reboiler. In general the
distillation column is a vertically oriented, cylindrical vessel
and comprises an inlet for inlet for admitting the fluid to be
separated, a rectifying section that is above the inlet, and a
stripping section that is below the fluid. The plates are typically
sieve trays or bubble cap trays, or other trays that allow the
liquid to flow across and the vapor to percolate upward through the
tray.
[0013] During the distillation process there is a vapor phase that
moves up the column and a liquid phase that moves down the column.
The liquid flows across the plates and down to subsequent plates
while the vapor passes through the plates to contact the liquid.
This provides a shift in the equilibrium, and therefore composition
in the phases as one moves up or down the column. At the bottom of
the column, the liquid is partially reboiled to create the vapor
stream that continuously moves up through the column, with the
remainder drawn off as a bottoms product stream. At the top of the
column the vapor is condensed and a portion is directed back into
the column to provide a continuous liquid stream passing down
through the column, with the remainder drawn off as condensate, or
distillate.
[0014] However, distillation can be energy intensive, and can
require many stages, or plates, depending on the properties of the
components in the mixture to be separated. This is important for
mixtures of liquids that have close boiling points, due to
increasing the number of stages to effect a desired separation.
[0015] When the bottoms product has a high purity requirement,
energy can be saved by compressing intermediate vapors streams from
the rectifying section to reboil the bottoms stream. The present
invention provides for an efficient reboiling of the bottoms
stream. The apparatus for a distillation separation of the present
invention is shown in FIG. 1. The apparatus includes a distillation
column 10 with a feed inlet 12, a rectifying section 20 disposed
above the feed inlet 12 and having an outlet 22 for an overhead
vapor stream, and a stripping section 30 disposed below the feed
inlet 12 and having an outlet 32 for a bottoms liquid stream. The
apparatus further includes a bottoms reboiler 40 for reboiling the
bottoms liquid stream, and an overhead condensing section 50 for
condensing the overhead vapor stream. The apparatus further
includes a side vapor draw 60 from the rectifying section 20. The
side vapor draw 60 is passed to heat pump compressor 62, where the
vapor from the side vapor draw 60 is compressed. The compressed
vapor is passed to the vapor side of a second reboiler heat
exchanger 64. A portion of the bottoms liquid is passed to the
liquid side of the second reboiler heat exchanger 64. The bottoms
liquid is reboiled to produce a vapor and fed to the bottom of the
stripping section 30 of the distillation column 10. The compressed
vapor will be preferably condensed, and the condensed vapor from
the reboiler heat exchanger 64 is directed to an inlet in the
rectifying section 20 of the distillation column 10.
[0016] For efficiency, when the apparatus is for producing a
bottoms product having a high purity requirement, the rectifying
section 20 can be reduced in size by withdrawing vapor through the
side vapor draw 60, and the side vapor draw 60 can be positioned
above the lowest tray in the rectifying section 20. The feed is
allowed to separate into liquid and vapor from the feed, and
drawing a portion of the vapor flowing through the rectification
section 20, reduces the volume flow of vapor and liquid through the
rectifying section 20 above the side vapor draw. By drawing off an
intermediate stream for compression, the compression ratio is
reduced and saves energy through operation of a compressor at lower
severity.
[0017] Through the use of compressing intermediate vapor streams to
reboil the bottoms, there will be a significant decrease in the
external energy required for a distillation column. Compressing the
intermediate vapor streams will reduce the compression ratio, and
provide energy savings from reduced utilities. For vapor streams
from the top of the column, the composition will differ and there
will be a greater compression ratio. This invention will be
especially useful for separation of similar components having close
boiling points. For example, in the separation of a
propane/propylene mixture, the distillation is carried out at
elevated pressures and due to the similar properties, a high degree
of separation would require a large number of stages, or trays, in
a distillation column. The use of compressing intermediate streams
drawn off from the rectifying section can provide a significant
amount of energy for reboiling of the bottoms stream. If only a
propane stream needs to be purified, the rectifying section can be
smaller and compressed streams drawn off from the rectifying
section will have heat sufficient to reboil a portion of the
bottoms.
[0018] In another embodiment, as shown in FIG. 2, the apparatus
further includes a second heat pump compressor 52 for compressing
the overhead vapor stream. The overhead vapor stream passes to a
vapor-liquid separator 54, where the vapor is directed to the
compressor 52. A portion of the liquid from the vapor-liquid
separator is directed to product, while a second portion is
directed to liquid reflux in the column 10. In this embodiment, the
bottoms reboiler 40 is a reboiler heat exchanger, the compressed
overhead vapor stream passes on the vapor side of the heat
exchanger, and a portion of the bottoms liquid passes on the the
liquid side of the heat exchanger reboiler 40. The compressed vapor
is at least partly condensed, and redirected to the top of the
column 10. The condensed liquid is under pressure, and passes
through a pressure reducing valve where upon entry to the top of
the rectifying section 20 of the column 10, the liquid partially
flashes. The condensed liquid can enter a separate port at the top
of the rectifying section, or can enter through the reflux entry
port. The vapor exits the outlet 22 of the rectifying section 20
and the liquid is used as a reflux for the rectifying section 20.
Excess condensed liquid from the vapor-liquid separator 54 is
pumped via a pump 58 to storage, or other operational units within
a petrochemical plant.
[0019] The apparatus further includes a third reboiler 42, also
known as a trim reboiler. The third reboiler 42 provides additional
heat when there is insufficient heat from the first reboiler heat
exchanger 40 and the second reboiler heat exchanger 64.
[0020] A portion of the compressed overhead vapor stream can be
passed through a trim condenser 56. This portion is condensed and
passed to the vapor-liquid separator after passing through a
pressure reducing valve to the lower pressure of the vapor-liquid
separator. The condensed liquid will partially flash and the
remaining liquid will contribute to the reflux in the column
10.
[0021] The use of a trim condenser 56 will depend on the amount of
compressed overhead vapor that is not needed to be passed to the
reboiler 40. This is determined by the heat load requirements of
the reboiler 40 and the amount of compressed overhead vapor to be
condensed.
[0022] The invention also provides for a process of separating a
less volatile component in a mixture when the bottoms product has a
high purity requirement. By using a heat pump compressor,
intermediate vapor streams can be used to provide the heat to
reboil the bottoms stream for the distillation column. The process
comprises passing a mixture to a feed section of a distillation
column, having a rectifying section above the feed section and a
stripping section below the feed section. The process generates an
overhead vapor stream and a bottoms stream. A portion of the
overhead vapor stream is condensed, thereby created a condensed
overhead stream. A portion of the condensed overhead stream is
passed to the top of the rectifying section as reflux for the
distillation process. A portion of the bottoms stream is is passed
to a first reboiler where the stream is at least partially
vaporized and the vaporized bottoms stream is passed to the bottom
of the stripping section.
[0023] The process further comprises drawing of a side vapor stream
from an intermediate stage of the rectifying section, and passing
the side vapor stream to a heat pump compressor where the vapor
stream is compressed to form a compressed side vapor stream. The
compressed side vapor stream is passed to the vapor side of a
second reboiler heat exchanger, and is used to reboil a portion of
the bottoms stream which is passed to the liquid side of the second
heat exchanger. The bottoms stream is reboiled to produce a vapor
stream and passed to the bottom of the stripping section. The
compressed side vapor stream is cooled and partially or wholly
condensed, and passed to an inlet port in the rectifying section of
the column. The condensed compressed side vapor stream passes
through a pressure reducing valve and partially flashes as it is
passed to the distillation column, thereby creating a side feed
stream that is partially liquid and partially vapor.
[0024] In an alternative embodiment of the process, the overhead
vapor stream is passed to a vapor-liquid separator, thereby
creating a vapor stream and a liquid stream for use as reflux. The
vapor stream is passed to an overhead heat pump compressor creating
a compressed overhead vapor stream. The compressed overhead vapor
stream is heated as a result of the compression and is used for
reboiling a portion of the bottoms stream. In this embodiment, the
first reboiler is a heat exchanger where the compressed overhead
vapor stream is passed to the vapor side of the heat exchanger. A
portion of the bottoms stream is passed to the liquid side of the
first reboiler and a portion of the bottoms stream is vaporized to
create a bottoms vapor stream. The bottoms vapor stream is then
passed to the bottom of the stripping section. The compressed
overhead vapor stream is cooled and a portion of the stream
condenses. Preferably, the first reboiler is sized and operated at
conditions to condense all of the compressed overhead vapor
stream.
[0025] The condensed overhead vapor stream is at an elevated
pressure and passes through a pressure reducing valve before
passing to the top of the rectifying section of the column. The
condensed stream will flash as it is passed to the column and a
portion of the liquid from the flash will provide a reflux stream
for the rectifying section. The vapor that is generated from the
flashed condensed stream is passed to the vapor-liquid
separator.
[0026] In an alternate embodiment, the improved purification of the
bottoms stream involves the reducing of the pressure of the bottoms
stream and reboiling the reduced pressure bottoms stream to produce
a bottoms vapor stream. As shown in FIG. 3, the apparatus comprises
a distillation column 10 having a rectifying section 20 with an
outlet 22 for an overhead vapor stream, a stripping section 30 with
an outlet 32 for a bottoms liquid stream, and a feed section with a
feed inlet 12 disposed between the rectifying section 20 and the
stripping section 30. The apparatus further includes a reboiler
section, where the reboiler section includes a means 46 for
reducing the pressure of the liquid bottoms stream, a first
reboiler 40 having a liquid side in fluid communication with the
reduced pressure bottoms stream, and a vapor side in fluid
communication with the overhead vapor stream, and a first heat pump
compressor 70 in fluid communication with the first reboiler liquid
side. The overhead vapor stream which is condensed in the first
reboiler 40 is passed to a vapor-liquid separation drum and is in
fluid communication with the top of the rectifying section 20.
[0027] The apparatus further includes a side draw 60 for drawing
off a vapor stream from the rectifying section 20. The side vapor
draw is in fluid communication with the vapor side of a second
reboiler 64. The liquid side of the second reboiler 64 is in fluid
communication with a reduced pressure liquid bottoms stream. The
reduced pressure liquid bottoms stream can be drawn from the
already reduced pressure liquid bottoms stream passing through the
pressure reducing means 46, or can be a separate portion of the
liquid bottoms stream that is passed through a second pressure
reducing means (not shown). A second heat pump compressor 72 is in
fluid communication with the reboiled bottoms stream, and generates
a compressed bottoms vapor stream that is passed to the bottom of
the stripping section 30.
[0028] The pressure reducing means 46 can be a Joule-Thompson
valve, or any other means for reducing the pressure of the bottoms
liquid stream. Other means includes passing the liquid through a
turbine to drive a motor and recover some of the energy expended in
the process of reducing the pressure.
[0029] The process for this embodiment comprises passing a mixture
to the feed section of the distillation column 10. The distillation
column 10 is operated to create a vapor stream flowing up through
the column 10 and a liquid stream flowing down through the column,
with an overhead vapor stream leaving the outlet 22 of the
rectifying section 20 and a bottoms liquid stream leaving the
outlet 32 of the stripping section 30. A portion of the liquid
bottoms stream is passed through a pressure reducing means 46 and
creating a reduced pressure bottoms stream. The reduced pressure
bottoms stream is passed to a first reboiler 40 on the liquid side
of the reboiler. The overhead vapor stream is passed to the vapor
side of the first reboiler 40. The overhead vapor stream condenses
thereby generating a condensed stream, and the reduced pressure
bottoms stream vaporizes thereby creating a bottoms vapor stream.
The condensed overhead stream is passed to the top of the
rectifying section 20 as reflux.
[0030] The reduced pressure bottoms stream is reboiled in the
reboiler 40, and generates a bottoms vapor stream. Any liquid from
the reduced pressure bottoms stream not reboiled is separated and
collected and redirected back to the bottom of the stripping
section 30. Since the liquid is at a reduced pressure, the liquid
pressure is increased by a pump 74 to a pressure sufficient to
deliver the liquid to the stripping section 30. Liquid-vapor
separation of the reboiled liquid is to prevent liquid from going
to the heat pump compressors 70, 72. The bottoms vapor stream is
compressed with a heat pump compressor 70, thereby creating a
compressed bottoms vapor stream. The bottoms vapor stream is passed
to the bottom of the stripping section 30 to provide heat and vapor
to strip out more volatile components from the fluid flowing down
the distillation column 10.
[0031] A second portion of the liquid bottoms stream is passed
through a means for reducing the pressure of the liquid. The second
portion can have a separate pressure reducing means, such as a
separate valve, or can be drawn off from the first portion of the
bottoms liquid after the first portion has passed through the means
for reducing pressure. A second pressure reducing means provides
for control of the temperature driving force needed to transfer
heat and thereby reboil the second portion of the liquid bottoms
stream. The second portion passes through a second reboiler 64
where the second portion is vaporized to form a second bottoms
vapor stream. Any of the second portion of the liquid bottoms
stream that is not vaporized is separated and collected, and pumped
back to the bottom of the stripping section 30 through a pump 74.
The second bottoms vapor stream is compressed by a second heat pump
compressor 72, thereby creating a second compressed bottoms vapor
stream. The second compressed bottoms vapor stream is then passed
to the bottom of the stripping section 30 to add additional vapor
for the distillation process. The remainder of the liquid bottoms
stream is a bottoms product that has a higher purity.
[0032] A vapor side stream is drawn from a side port 60 in the
distillation column 10 and is passed through the vapor side of the
second reboiler 64, where the vapor side stream condenses. The
condensed side stream is then passed to the distillation column 10
as a side liquid feed. It is preferred that the vapor side stream
is drawn near the bottom of the rectifying section 10.
[0033] Another variation of this embodiment is shown in FIG. 4. The
apparatus comprises the distillation column 10 having a rectifying
section 20 and a stripping section 30. The apparatus further
comprises a first means 46 for reducing the pressure of the liquid
bottoms stream, and a first reboiler 40 having a liquid side in
fluid communication with the reduced pressure liquid bottoms
stream. A portion of the overhead vapor stream is passed to the
vapor side of the first reboiler 40, where the overhead vapor
stream condenses and the liquid bottoms stream is vaporized. Any of
the liquid bottoms stream not vaporized is separated and collected,
and pumped back to the bottom of the stripping section 30. A pump
74 increases the liquid pressure to at least the pressure of the
bottom of the stripping section 30 for unvaporized liquid collected
from the first reboiler 40. The vaporized bottoms stream is
compressed with a heat pump compressor 70, thereby generating a
compressed vapor stream and is passed to the bottom of the
stripping section 30. The condensed overhead vapor stream is passed
to the top of the rectifying section 20 as reflux. Preferably, the
condensed overhead vapor stream is first passed to a vapor-liquid
separation tank 54. The tank 54 collects the liquid and sends a
portion out as overhead distillate, while returning the remainder
to the top of the rectifying section 20.
[0034] The apparatus further includes a port 60 for drawing off an
intermediate liquid stream from the column 10. Preferably, the port
60 is in the stripping section 30 of the column. The intermediate
liquid stream is passed through a second pressure reducing means 66
and generating a reduced pressure intermediate liquid stream. The
reduced pressure intermediate liquid stream is in fluid
communication with the liquid side of a second reboiler 64, where
at least a portion of the liquid is vaporized. Any of the
intermediate liquid stream that is not vaporized is separated and
collected and returned to the stripping section 30. The liquid
portion from the second reboiler 64 that is not vaporized is passed
through a second pump 76 to a pressure sufficient to return the
liquid to the column 10. The liquid portion not vaporized can be
returned to the stripping section at or below the liquid draw off
port 60. In one embodiment, it is returned with the liquid
recovered from the first reboiler. A second portion of the overhead
vapor stream is passed to the vapor side of the second reboiler 64,
where the second portion is at least partially condensed. The
vaporized intermediate stream is compressed with a second heat pump
compressor 72, and the compressed intermediate vapor is returned to
the column 10. Preferably, the vapor is returned to a position in
the column 10 above the tray where the intermediate liquid stream
is drawn from the port 60. The condensed overhead vapor stream is
in fluid communication with the top of the rectifying section,
where the condensed stream will be returned as reflux.
[0035] The process comprises using the overhead vapor stream to
reboil the liquid bottoms stream and an intermediate liquid stream.
The liquid streams are passed through pressure reducing means and
will vaporize at lower temperatures. The vaporized streams are then
compressed, where the vapor is heated through the compression. The
heated and compressed vapor is then passed back to the distillation
column to provide the upflowing vapor for stripping the downflowing
liquid.
[0036] In this embodiment, a mixture is passed to the feed section
of the distillation column. The distillation column has an outlet
at the top of the rectifying section 20 for an overhead vapor
stream, and an outlet at the bottom of the stripping section 30 for
a liquid bottoms stream. A portion of the bottoms stream is passed
through a pressure reducing valve 46 to a first reboiler 40, where
it exchanges heat with a portion of the overhead vapor stream. The
bottoms stream is vaporized and the overhead vapor stream is
condensed. The vaporized bottoms stream is compressed with a heat
pump compressor 70, creating a compressed and heated bottoms vapor
stream. The bottoms vapor stream is passed to the bottom of the
stripping section 30 for providing heat to strip out components
from liquid flowing down through the column 10. The condensed
overhead vapor stream is passed to the top of the rectifying
section 20 as reflux.
[0037] The process further comprises drawing off a liquid stream
from an intermediate port 60 in the column 10 and passing the
intermediate liquid stream through a pressure reducing valve 66 to
produce a reduced pressure intermediate liquid stream, which is
passed to a second reboiler 64. The reduced pressure liquid stream
is heat exchanged with a second portion of the overhead vapor
stream, where the reduced pressure liquid stream is vaporized and
the overhead vapor stream is condensed.
[0038] The reboiled intermediate vapor stream is compressed with a
second heat pump compressor 72 and passed to an intermediate inlet
port in the column 10. Preferably, the vapor is passed to above the
tray where the intermediate liquid is drawn out of the port 60 in
the column. The second condensed portion of the overhead vapor
stream is passed to the top of the rectifying section 20 as
additional reflux.
[0039] By using the heat from the compressed intermediate stream,
energy is more efficiently used in the distillation process, and
this can further reduce the size of the distillation column below
the intermediate draw as there is lower vapor and liquid flow
through the stripping section below the intermediate draw.
[0040] While the invention has been described with what are
presently considered the preferred embodiments, it is to be
understood that the invention is not limited to the disclosed
embodiments, but it is intended to cover various modifications and
equivalent arrangements included within the scope of the appended
claims.
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