U.S. patent number 3,568,764 [Application Number 04/855,586] was granted by the patent office on 1971-03-09 for heat exchanger.
Invention is credited to Richard T. Britt, Louis A. Klein, Daniel J. Newman.
United States Patent |
3,568,764 |
Newman , et al. |
March 9, 1971 |
HEAT EXCHANGER
Abstract
A baffle is provided adjacent to the outlet side of the tube
sheet of a multiple tube pass heat exchanger. A portion of the
input fluid is passed between the baffle and the tube sheet, rather
than through the tubes, so that the tube sheet is maintained at a
substantially uniform temperature. Ferrules pass the outlet gas
portions from the tubes to the outlet chamber of the channel.
Inventors: |
Newman; Daniel J. (Jackson
Heights, NY), Klein; Louis A. (Flushing, NY), Britt;
Richard T. (Elmont, NY) |
Family
ID: |
25321622 |
Appl.
No.: |
04/855,586 |
Filed: |
September 5, 1969 |
Current U.S.
Class: |
165/134.1;
165/158; 165/176 |
Current CPC
Class: |
F28F
9/0282 (20130101); F28D 7/06 (20130101); F28F
9/00 (20130101) |
Current International
Class: |
F28F
27/02 (20060101); F28D 7/06 (20060101); F28F
27/00 (20060101); F28F 9/00 (20060101); F28D
7/00 (20060101); F28f 009/02 () |
Field of
Search: |
;165/134,158,176 |
References Cited
[Referenced By]
U.S. Patent Documents
Foreign Patent Documents
Primary Examiner: Davis, Jr.; Albert W.
Claims
We claim:
1. An apparatus for exchanging heat between a first fluid and a
second fluid by indirect heat exchange which comprises a heat
exchanger shell, a tube sheet extending across one end of said
shell, a channel disposed about the outer side of said tube sheet
and connected to said shell, a partition in said channel, said
partition extending to said tube sheet and dividing said channel
into a fluid inlet chamber and a fluid outlet chamber, at least one
fluid inlet tube, said inlet tube extending into said shell from
the portion of said tube sheet adjacent to said fluid inlet
chamber, at least one fluid outlet tube, said outlet tube extending
from said shell to an opening in the portion of said tube sheet
adjacent to said fluid outlet chamber, means to transfer fluid from
the discharge end of said fluid inlet tube to the fluid inlet end
of said outlet tube, means to pass said first fluid into said inlet
chamber, whereby a first portion of said first fluid flows through
said inlet tube, said fluid transfer means and said outlet tube, a
shield disposed in said fluid outlet chamber, said shield being
substantially parallel with and spaced from the portion of said
tube sheet adjacent to said fluid outlet chamber, a ferrule, said
ferrule being mounted in said shield and extending from said shield
into said fluid outlet tube and spaced from the inner tube wall,
whereby the first portion of said first fluid discharged from said
outlet tube flows through said ferrule and into said fluid outlet
chamber, at least one opening provided in said partition between
said shield and said tube sheet, whereby a second portion of said
first fluid flows through said opening and between said shield and
said tube sheet, thereby maintaining the temperature level of the
portion of said tube sheet adjacent to said fluid outlet chamber at
a temperature level approximately that of the valance of said tube
sheet, said second portion of said first fluid thereafter flowing
into said fluid outlet chamber to mix with said first portion of
said first fluid discharged from said ferrule, means to remove said
first fluid from the fluid outlet chamber of said channel, and
means to circulate said second fluid through said shell external to
said fluid inlet tube and said fluid outlet tube, whereby heat is
exchanged between said second fluid and said first portion of said
first fluid flowing through said tubes.
2. The apparatus of claim 1, in which the extension of said ferrule
within said fluid outlet tube is tapered.
3. The apparatus of claim 1, in which at least one spacer is
provided between said ferrule and said fluid outlet tube, whereby
part of said second portion of said first fluid flows between said
ferrule and said outlet tube.
4. The apparatus of claim 1, in which internal insulation is
provided on the inner surface of the portion of said channel
defining said fluid outlet chamber.
5. The apparatus of claim 1, in which internal insulation is
provided on the inner surface of all of said channel.
6. The apparatus of claim 1, in which a flange is provided on the
outer edge of said shield, said flange extending into said fluid
outlet chamber, whereby said second portion of said first fluid is
directed parallel to said channel adjacent to the outer joint
between said channel and said shell.
7. The apparatus of claim 1, in which said means to transfer fluid
from the discharge end of said fluid inlet tube to the fluid inlet
end of said outlet tube is a second channel mounted on the opposed
end of said shell.
8. The apparatus of claim 1, in which said means to transfer fluid
from the discharge end of said fluid inlet tube to the fluid inlet
end of said outlet tube is a curved tube section.
9. The apparatus of claim 8, in which said inlet tube, said curved
tube section and said outlet tube define a U-tube for heat
exchange.
10. The apparatus of claim 1, in which said first fluid is
initially cooler than said second fluid, and said first fluid is
heated by indirect heat exchange with said second fluid while
flowing through said tubes.
11. The apparatus of claim 1, in which said first fluid is a
gas.
12. The apparatus of claim 11, in which said gas is the cold tail
gas from a nitric acid production process, and said second fluid is
a hot gas stream generated by the catalytic combustion of ammonia
vapor with air to form a nitrogen oxides-rich gas stream.
Description
BACKGROUND OF THE INVENTION
1. Field of the Invention
The invention relates to shell and tube heat exchangers, for
indirect heat exchange between fluid streams, one of which is
passed through the tubes while the other circulates through the
shell of the unit external to the tubes. A typical application is
the preheating of the tail gas from a high pressure nitric acid
process, prior to passing the tail gas through an expander for
power recovery, by passing the cold tail gas through the tubes of a
heat exchanger. The tail gas is heated by heat exchange with a hot
process gas stream formed by the catalytic oxidation of ammonia
vapor with air to form nitrogen oxides, for subsequent conversion
to nitric acid.
2. Description of the Prior Art
Apparatus for fluid heat exchange involving the provision of
thermal shields or the like for the formation of stagnant regions
of reduced fluid flow is shown in U.S. Pat. Nos. 1,651,875;
2,203,357; 2,252,069; 3,132,691 and 3,279,532. The provision of
heat exchange between the tail gas produced by a nitric acid
process and the hot effluent gas stream formed by catalytic ammonia
oxidation is described in U.S. Pat. application No. 409,507 filed
Nov. 6, 1964 and now U.S. Pat. No. 3,467,492, granted Sept. 16,
1969.
In multiple pass heat exchangers heating or cooling a fluid through
a large temperature range, great difficulty is experienced in
maintaining a suitable seal between the tube sheet and the shell
side fluid due to the differences in expansion resulting from the
different temperatures at the inlet and the outlet tubes. For a
typical shell and tube heat exchanger design, the tube sheet
temperature tends to approach the temperature of the tubes in the
pierced section since, unless boiling or condensing occurs on the
shell side, heat transfer coefficients inside the tubes will be
higher than on the relatively stagnant shell side face of the tube
sheet, and heat transfer surface areas contacting the tube side
fluid inside the tube sheet is normally substantially greater than
that contacting the shell side fluid on its face. In a multiple
pass unit therefore, the tube sheet tends to have substantially
different temperatures at the sections where the tube side fluid is
respectively admitted and removed. When these temperatures are
substantially different, the thermal expansion of each part will be
correspondingly different, resulting in different forces being
exerted at the opposite sides of the joint between the tube sheet
and shell. Such differing stresses will lead to a relative
loosening of part of the gasket seal at these points, or cracking
of a welded seal when provided, requiring at least the tightening
of the bolts after each heating or cooling of the unit, and
ultimately requiring replacement of the gasket after a few
cycles.
SUMMARY OF THE INVENTION
In the present invention, the difference in temperatures between,
for example, the top and bottom of the tube sheet is minimized by
providing a baffle and tube ferrules on the downstream half of the
tube sheet so as to permit some inlet fluid to bypass to the outlet
fluid side, thus making the latter half of the tube sheet
temperature more nearly approach that of the inlet half. Internal
insulation can also be provided in the channel to minimize
differences between top and bottom temperature, or these
differences relative to the new uniform tube sheet temperature
could become a problem.
The ferrules provided should be tapered or be a nonheat conductive
material, not only to facilitate assembly but also to insure
against their contacting the tube wall, which could permit transfer
of heat from the tube side fluid to the tube sheet. Alternatively,
spacers could be provided on each ferrule, to permit some of the
inlet gas to directly cool the tube wall before mixing with the
outlet gas, thus further reducing temperature variations on the
tube sheet.
The baffle or shield is supported and spaced from the outlet half
of the tube sheet on ferrules rolled lightly into each outlet tube.
Holes provided in the channel partition plate permit the bypassing
of sufficient inlet fluid to flow behind the shield and ferrules,
and generally between the shield and the tube sheet, to hold the
entire sheet at close to the inlet fluid temperature. When the tube
sheet is held to a more nearly constant temperature by the shield,
the external leakage problem may be transferred to some extent to
the channel flange joint. In order to further obviate such transfer
of the temperature differential and leakage problem, internal
insulation may be provided in at least the top half of the head in
order to further minimize temperature differences. In an
alternative embodiment, the outer edge of the shield is flanged in
order to direct sufficient cooler fluid across the body flange from
the space between the shield and the tube sheet, in order to
minimize the temperature differences on the body flange without
providing internal insulation.
The primary advantage of the invention is that leakage problems due
to differential thermal expansion of the tube sheet in shell and
tube heat exchangers are prevented. Another advantage is that the
apparatus is relatively simple to fabricate and install. A further
advantage is that temperature differences between the shell and
head or channel are effectively prevented.
It is an object of the present invention to provide an improvement
in fluid heat exchangers.
Another object is to provide an improved shell and tube heat
exchanger.
A further object is to provide a shell and a tube heat exchanger in
which a portion of the input tube side fluid is bypassed and
utilized to minimize temperature differentials in the tube
sheet.
An additional object is to prevent differential thermal expansion
of members in a shell and tube heat exchanger.
Still another object is to contact the tube outlet side of the tube
sheet of a shell and tube heat exchanger with a portion of the
inlet fluid to prevent differential thermal expansion and
leakage.
These and other objects and advantages of the present invention
will become evident from the description which follows.
DESCRIPTION OF THE DRAWINGS AND PREFERRED EMBODIMENTS
Referring now to the drawings, FIG. 1 is a sectional elevation view
of one embodiment of the invention, as applied to a U-tube heat
exchanger,
FIG. 3 is an enlarged view of a portion of the apparatus of FIG. 1,
showing structural details,
FIG. 3 is a sectional elevation view of FIG. 2, taken on section
3-3,
FIG. 4 is a sectional elevation view of an alternative embodiment
of the invention, as applied to one conventional type of shell and
tube heat exchanger,
FIG. 5 is an enlarged view of a portion of the apparatus of FIG. 4,
showing structural details,
FIG. 6 is a sectional elevation view of FIG. 5, taken on section
6-6, and
FIG. 7 is a sectional elevation view of another alternative
embodiment of the invention.
Referring now to FIG. 1, stream 1 is typically the cold tail gas
from a high pressure nitric acid process, however stream 1 may in
practice consist of any cold fluid which is to be heated, or any
hot fluid which is to be cooled. For purposes of clarity, stream 1
will be described as a cold nitric acid process tail gas. The cold
gas stream 1 passes via nozzle 2 into the channel 3, which consists
of a heat exchanger head. An internal insulation layer 4 is
provided over the entire inner surface of channel 3, and a
partition 5 divides the channel 3 into a lower cold gas inlet
section and an upper heated gas outlet section. The cold gas flows
from the lower section of channel 3 below partition 5 into the
inlet section 6 of heat exchange U-tube which are mounted in tube
sheet 7. One tube is shown in the FIG. The tube sheet 7 is mounted
between channel 3 and the heat exchanger shell or body 8. A hot
fluid stream 9, which in the case of a nitric acid production
facility may consist of the hot gas mixture formed by catalytic
ammonia oxidation to nitrogen oxides, is passed via nozzle 10 into
shell 8, and stream 9 flows downwards external to the heat
exchanger U-tube and thereby becomes cooled by indirect heat
exchange with the cold tail gas flowing within the U-tube. The
resulting cooled gas stream is removed from shell 8 via lower
nozzle 11 as stream 12, which is now passed to further heat
exchange or process usage.
The heat exchanger U-tube is defined by the straight inlet section
6, the curved or semicircular return section 13, and the straight
outlet section 14. A tapered ferrule 15 is lightly rolled into the
outlet end of tube 14, and the ferrule 15 is mounted on the baffle
or shield 16 which extends upwards from partition 5 adjacent to and
spaced from the tube sheet 7. The baffle 16 is generally disposed
substantially parallel with the tube sheet 7. The heated tail gas
flowing through tube section 14 passes through ferrule 15 and is
discharged into the upper heated gas outlet section of channel 3
beyond baffle 16, so that the heated tail gas does not contact or
heat the tube sheet 7.
In accordance with the present invention, one or a series of
openings 17 is provided in the section of the partition 5 between
tube sheet 7 and shield 16. A portion of the cold inlet gas stream
1 flows from the lower cold gas inlet section of channel 3 through
the opening 17, and thereafter the cold gas portion flows upwards
between tube sheet 7 and shield 16, thus serving to cool the tube
sheet 7 and maintain tube sheet 7 at a substantially uniform
temperature. The cold gas portion next flows, around the upper end
of shield 16, which is spaced from channel 3, and the cold gas
portion then joins the main heated gas stream in the upper heated
gas outlet portion of channel 3. The heated tail gas is removed
from channel 3 via nozzle 18 as stream 19, which is not at high
pressure and elevated temperature and is suitable for passage to
expansion and power recovery in a suitable gas turbine, expander or
the like.
Referring now to FIG. 2, a modified version of a portion of the
structure of FIG. 1 is shown in enlarged sectional detail. The
ferrule 15 extends between shield 16 and tube sheet 7 and into tube
section 14, and only the portion of ferrule 15 within tube 14 is
tapered. Ferrule 15 is joined to shield 16 by outer continuous weld
20, and tube 14 is joined to tube sheet 7 by outer continuous weld
21. The welds 20 and 21 provide a sealing effect against gas flow
at the respective joints. The tapered portion of ferrule 15 is
centrally oriented within and spaced from tube 14 by the provision
of a plurality of projecting shoulders or nubs 22, which are
staggered about the inner periphery of tube 14, or the outer
periphery of ferrule 15, so as to permit a portion of the cold gas
flowing between shield 16 and tube 7 to flow into tube 14 through
the annular passage between ferrule 15 and tube 14, and thereby
provide a further cooling effect with respect to tube sheet 7. Tube
14 may be rolled onto tube sheet 7 by the provision of spaced
ridges 23.
FIG. 3 is a sectional view of FIG. 2, and shows the central ferrule
15, the tube 14 and the weld 21 in concentric coaxial alignment.
The four spacers or nubs 22 extending inwards from tube 14 to
contact with ferrule 15 are also shown.
Referring now to FIG. 4, an alternative embodiment of the invention
is illustrated in sectional elevation view. Cold tail gas stream 24
flows via nozzle 25 into the lower cold gas inlet section of
channel 26, which is divided into a lower section and an upper
heated gas outlet section by partition 27. The lower section of
channel 26 is not provided with an internal layer of insulation.
The cold gas flows from the lower section of channel 26 into the
plurality of tubes 28, the inlet ends of tubes 28 being mounted in
tube sheet 29. The gas outlet ends of the linear tubes 28 are
mounted in tube sheet 30, which is provided with a floating head 31
for gas return to the plurality of linear tubes 32, with the tubes
28 and 32 being generally parallel and disposed within heat
exchange shell 33 provided with head 34.
A hot fluid stream 35, which is typically a hot nitric acid process
gas stream similar to stream 9 described supra, is passed via
nozzle 36 into shell 33, and stream 35 flows upwards between tube
sheet 29 and central baffle or partition 37 and external to tubes
28 and 32, thus heating the cold tail gas within tubes 28 and 32.
The hot gas next flows above baffle 37 and downwards between baffle
37 and tube sheet 30, and external to tubes 32 and 28, thus further
heating the cold gas within tubes 32 and 28. The resulting cooled
gas is removed from shell 33 via nozzle 38 as stream 39, which is
passed to process usage.
The heated tail gas flowing from tubes 32 next flows through
ferrules 40, which are mounted in baffle or shield 41 and extend
into tubes 32. The baffle 41 extends upwards from partition 27 and
is generally substantially parallel with tube sheet 29, and is
spaced from tube sheet 29. In accordance with the present
invention, one or a plurality of openings 42 is provided in
partition 27, in the section of partition 27 between baffle 41 and
tube sheet 29. A portion of the cold gas flows from the lower inlet
section of channel 26 through opening 42 and upwards between baffle
41 and tube sheet 29, and external to the ferrules 40, thus cooling
the upper portion of the tube sheet 29 and maintaining element 29
at a substantially uniform temperature. The cold gas portion next
flows upwards and around the upper end of baffle 41, and joins the
main stream of warmed gas discharged into the upper outlet section
of channel 26 via ferrules 40. The upper warmed gas outlet section
of channel or head 26 is provided with an internal layer of
insulation 43. The warmed tail gas is removed from the upper
section of channel 26 via nozzle 44 as stream 45, which is now
passed to a suitable gas turbine, expander or the like.
FIG. 5 is an enlarged view of a portion of the apparatus FIG. 4,
and shows an embodiment of the invention in which ferrule 4 is
spaced from the tube 32 and within tube 32 by the provision of
outer linear wires or rods on the outer surface of ferrule 40. The
ferrule 40 is attached to baffle 41 by outer seal weld 46, and the
tube 32 is rolled into tube sheet 29 by ridges 47 and attached to
tube sheet 29 by outer seal weld 48. The longitudinal or linear
wires 49 are attached to the outer surface of the portion of
ferrule 40 within tube 32, and wires 49 are usually parallel to the
axis of ferrule 40. Elements 49 may consist of bars or rods in
practice, and one or a plurality of elements 49 may be provided in
suitable instances. A portion of the cold gas stream, which is
flowing upwards between baffle 41 and tube sheet 29, flows into
tubes 32 via the annular passage between ferrule 40 and tube 32
maintained by the spacer wires 49. The inward flow of cold gas
between ferrule 40 and tube 32 further serves to maintain the tube
sheet 29 at a substantially uniform temperature, by cooling the end
of tube 32 which is in contact with tube sheet 29.
FIG. 6 is a sectional view of FIG. 5, taken on section 6-6, and
shows the concentric and coaxial arrangement of ferrule 40, tube 32
and weld 48, as well as three spacer wires 49 disposed between
ferrule 40 and tube 32.
Referring now to FIG. 7, an alternative embodiment of the invention
is shown, which obviates any need or requirement for the provision
of an internal layer of insulation on the inner surface of the
channel. Cold gas stream 50 flows via nozzle 51 into the lower cold
gas inlet section of the channel or head 52, which is divided by
partition 53 into a lower inlet section and an upper warmed gas
outlet section. The cold gas flows from the lower section of
channels 52 into tubes 54 which are mounted in tube sheets 55,
which is mounted between head or channel 52 and shell 56. A hot
fluid is circulated in shell 56 external to tubes 54 and return
tubes 57, which receive warmed gas from the discharge end of tubes
54 by suitable gas return means, not shown. The tubes 57 discharge
the warmed gas into ferrules 58, which are mounted in baffle 59. In
accordance with the present invention, the baffle 59 is spaced
adjacent to and usually substantially parallel with tube sheet 55,
and baffle 59 is disposed in the upper warmed gas outlet section of
channel 52. One or a plurality of openings 60 is provided in
partition 53, at the section of partition 53 between baffle 59 and
tube sheet 55. A portion of the cold inlet gas flows from the lower
inlet section of channel 52 through opening 60 and upwards between
baffle 59 and tube sheet 55 and external to ferrules 58, thus
cooling the tube sheet 55 and maintaining all of tube sheet 55 at a
substantially uniform temperature. A flange 61 extends inwards and
into the warmed gas outlet section of channel 52 from the upper end
of baffle 59, and flange 61 is disposed adjacent to channel 52, so
that the cold gas portion discharged upwards from between baffle 59
and tube sheet 55 is diverted laterally and adjacent to channel 52
by flange 61. Thus, the portion of channel 52 adjacent to and
connected with the upper portions of tube sheet 55 and shell 56 is
also cooled by the cold gas portion admitted via opening 60. The
warmed gas discharged from ferrules 58 into the upper warmed gas
outlet section of channel 52 combines adjacent to the terminus of
flange 61 with the cold gas portion employed for cooling, and the
warmed gas is then removed from the upper section of channel 52 via
nozzle 62 as stream 63.
Numerous alternatives within the scope of the present invention,
besides those mentioned supra, will occur to those skilled in the
art. The invention is generally applicable to any type of shell and
tube heat exchanger, and to the indirect heat exchange between any
two fluids, either of which may be gaseous or liquid, and either of
which may be warmed or cooled. Thus, the streams 1, 24 or 50 may be
a hot fluid which is to be cooled in the heat exchanger apparatus,
in which case the improvement of the present invention will serve
to maintain the respective tube sheet 7, 29 or 55 at a
substantially uniform elevated temperature. The portions of this
ferrules within the tubes will generally be spaced from the tube
walls as described supra, in order to allow for inwards flow of a
cold gas portion in the annular passage between the ferrule and the
tube end as described supra. However, the ferrules may
alternatively be lightly rolled into the tubes, as shown in FIG. 1,
in which case such gas flow would be restricted. The heat exchanger
may be operated in practice in a vertical, horizontal or inclined
position, depending on process conditions, and the apparatus of the
present invention is generally applicable to any process or
facility requiring indirect heat exchange between a cold fluid and
a hot fluid. In instances when one of the fluids is a gas or vapor,
partial or total condensation of this fluid to the liquid state may
occur in the apparatus. In instances when one of the fluids is a
liquid, partial or total vaporization of this fluid to the gaseous
or vapor state may occur in the apparatus. The apparatus is also
applicable to instances when one or both of the fluids is a
gas-liquid mixture, such as a gas stream containing entrained
liquid droplets.
* * * * *