U.S. patent number 3,732,922 [Application Number 05/119,124] was granted by the patent office on 1973-05-15 for heat-exchanger module.
This patent grant is currently assigned to Stein Industrie. Invention is credited to Pierre Pouderoux.
United States Patent |
3,732,922 |
Pouderoux |
May 15, 1973 |
HEAT-EXCHANGER MODULE
Abstract
A tube bundle for the circulation of a first fluid is disposed
within a shell for the circulation of a second fluid. At least one
end of the tube bundle has a rectilineal portion followed by
expansion-bends for compensating differential expansions. The tubes
are subdivided in the vicinity of the rectilineal portion into two
half-bundles each disposed on a square lattice with an identical
pitch on each side of a principal lattice line along which the two
lattices are relatively displaced by one half pitch. At the level
of the expansion-bends, the two lattices are in interjacent
relation, the tubes have substantially the same cross-section and
the tubes of one row located at right angles to the principal line
retain the same cross-section as in the rectilineal portion, extend
into the other lattice in the plane of said row and pass between
the parallel rows of the other lattice.
Inventors: |
Pouderoux; Pierre (Paris,
FR) |
Assignee: |
Stein Industrie (Paris,
FR)
|
Family
ID: |
9051879 |
Appl.
No.: |
05/119,124 |
Filed: |
February 26, 1971 |
Foreign Application Priority Data
Current U.S.
Class: |
165/158; 122/32;
165/81; 165/160; 165/163 |
Current CPC
Class: |
F22B
1/1823 (20130101); F28D 7/005 (20130101) |
Current International
Class: |
F22B
1/18 (20060101); F22B 1/00 (20060101); F28D
7/00 (20060101); F28f 009/22 (); F28d 007/08 () |
Field of
Search: |
;165/158,159,160,163,81
;122/32 |
References Cited
[Referenced By]
U.S. Patent Documents
Primary Examiner: Davis, Jr.; Albert W.
Claims
What we claim is :
1. A heat-exchanger module comprising a plurality of tubes for the
circulation of a first fluid which are disposed in a bundle between
two tube-plates within a shell for the circulation of a second
fluid and provided at least at one extremity of said bundle with a
rectilineal portion followed by expansion-bends for compensating
differential expansions, wherein said tubes are subdivided at least
in said rectilineal portion in the vicinity of said tube-bundle
extremity into two half-bundles each disposed on a square lattice
with an identical pitch on each side of a principal lattice line
along which the two lattices are relatively displaced by one half
pitch and wherein said two lattices are disposed in interjacent
relation at the level of the expansion-bends and the tubes of each
row which is located at right angles to said principal line in each
lattice retain substantially the same cross-section as in the
rectilineal portion and extend into the other lattice while forming
the expansion-bends in the plane of said row and passing between
the parallel rows of the tubes of the other lattice.
2. A heat-exchanger module according to claim 1, wherein said
module comprises a pipe for the discharge or admission of said
second fluid which is located at a sufficient distance from said
tube-bundle extremity to assist the circulation of said second
fluid away from the expansion-bends.
3. A heat-exchanger module according to claim 1, wherein said shell
forms in the vicinity of said tube-bundle extremity a chamber which
has a larger diameter than the bundle itself and which encloses the
expansion-bends.
4. A heat-exchanger module according to claim 3, wherein the tube
bundle is surrounded within said chamber by a sleeve which
terminates at the level of the expansion-bends, said sleeve being
provided with at least one opening through which the second fluid
is permitted to pass.
5. A heat-exchanger module according to claim 1, said module being
employed as a steam generator for the vaporization and superheating
of said first fluid, wherein the pitch of the tube bundle is
smaller in the superheater section than in the evaporator section,
said tube bundle being surrounded at the level of the superheater
section by an inner sheath which limits the zone of circulation of
the second fluid within said shell.
Description
The invention relates to a heat-exchanger module of tubular type
which can be employed alone but is preferably intended to
constitute heat exchangers of large size as a result of
interassembly of identical modules.
It is known in particular that heat exchangers which are
constructed by interassembling standard units having smaller
dimensions are employed in particular for heat transfer processes
between two fluids which are liable to give rise to violent
reactions with each other in the event of leakage. This problem
arises in particular in heat exchangers which are employed as steam
generators in conjunction with nuclear reactors of the fast-neutron
type ; the fluids between which the transfer takes place are in
that case water which vaporizes and a liquid metal such as
sodium.
In this case, the design concept of unit construction has the
effect of facilitating the location of any leakage which may occur
and the possibility of isolating each module individually often
avoids the need for complete outage of the heat exchanger in the
event of leakage ; moreover, a leak which develops in any
particular tube is less liable to result in damage to a large
number of adjacent tubes.
The present invention proposes a heat-exchanger module which meets
these different requirements more effectively than the structures
which have been adopted up to the present time. More particularly,
the invention is intended to achieve a further increase in
operational safety, especially by solving the problems of
differential thermal expansions and vibrations, as well as to
permit the construction of a module which has a substantially
uniform and compact external geometry and which can readily be
assembled with other identical modules in order to constitute a
heat exchanger having a high output and small overall space
requirements while ensuring a high degree of operational
safety.
The heat-exchanger module in accordance with the invention
comprises a plurality of tubes for the circulation of a first fluid
which are disposed in a bundle between two tube-plates within a
shell for the circulation of a second fluid and is provided at
least at one extremity of said bundle with a rectilineal portion
followed by expansion-bends for compensating differential
expansions. The heat-exchanger module is characterized in that said
tubes are subdivided at least in said rectilineal portion in the
vicinity of said tube-bundle extremity into two half-bundles each
disposed on a square lattice with an identical pitch on each side
of a principal lattice line along which the two lattices are
relatively displaced by 1/2 pitch. At the level of the
expansion-bends, the two lattices are disposed in interjacent
relation and the tubes of each row which is located at right angles
to said principal line in each lattice retain substantially the
same cross-section as in the rectilineal portion, extend into the
other lattice while forming the expansion-bends in the plane of
said row and pass between the parallel rows of the tubes of the
other lattice.
In accordance with further characteristic features, the
heat-exchanger module is characterized in that it comprises a pipe
for the discharge or admission of said second fluid which is
located at a sufficient distance from said tube-bundle extremity to
assist the circulation of said second fluid away from the
expansion-bends, that said shell forms in the vicinity of said
tube-bundle extremity a chamber which has a larger diameter than
the bundle itself and which encloses the expansion-bends and/or the
tube bundle is surrounded within said chamber by a sleeve which
terminates at the level of the expansion-bends, said sleeve being
provided with at least one opening through which the second fluid
is permitted to pass.
A particular embodiment which has been chosen by way of example in
order to provide an explanatory illustration of the invention will
now be described with reference to the accompanying drawings, in
which :
FIG. 1 is a vertical sectional view of a heat-exchanger module in
accordance with the invention ;
FIG. 2 is a diagrammatic sectional view of the same module taken
along line A--A of FIG. 1.
FIG. 3 is a sectional view through the module of FIG. 1 to show the
distribution of the tubes therein.
The heat-exchanger module as illustrated in these figures is a
unitary module which is intended to be assembled together with
other similar modules disposed in parallel so as to constitute a
complete heat exchanger.
In the particular case under consideration, said heat exchanger is
in fact the steam generator of a nuclear power station in which a
breeder reactor is cooled by liquid sodium or another liquid alkali
metal. During operation, heat is transferred by means of said heat
exchanger between the hot sodium which is cooled and the water
which is vaporized.
The heat exchanger is of the tubular type. As shown in FIG. 1, each
module is essentially constituted by a shell 1 which is normally
vertical and by a bundle of straight tubes 2 which are enclosed
within said shell. The ends of said tubes are welded to a bottom
tube-plate 4 and a top tube-plate 5, both tube-plates being located
within the shell 1 respectively at each end of this latter. The
tubes are thus disposed in parallel relation on the flow path of a
first heat-transfer fluid which consists in this case of water in
the form of either liquid or steam. The second fluid which consists
of liquid sodium circulates in contact with said tubes within the
shell 1. In order that the circulation should take place in a
predetermined flow pattern, an inlet pipe 6 is provided for the
admission of sodium into the upper portion of the module and an
outlet pipe 7 is provided for the discharge of the sodium at the
lower end whilst the water circulates within the tubes in the
upward direction from a supply pipe 8 to a discharge pipe 9.
The vaporized water in fact passes out of the module in the state
of superheated steam. The module therefore has an upper section
forming a superheater above a lower section which constitutes an
economizer-evaporator. Moreover, the module is so designed that the
superheater section can be placed in parallel with a resuperheater
constituted by another module which may be of a different type. To
this end, the module as herein described is provided between the
superheater section and the economizer-evaporator section with an
additional sodium inlet 10 through which the sodium passes from the
resuperheater and joins the hot sodium stream from the superheater
section at the inlet of the economizer-evaporator section.
At the level of each sodium inlet or outlet, the shell 1 is
enclosed by a spaced wall to form chambers 11 having a larger
diameter than the cylindrical portions of shell 1 which surrounds
the tube bundle. However, the cylindrical portions of shell 1 are
extended respectively within the interior of each chamber 11 by
means of extensions 12, 13, 14, respectively, which protect the
tubes from direct impact of the sodium but are nevertheless
provided with one or a number of openings 15 through which the
sodium is permitted to pass.
Moreover, the different tubes of the bundle are more closely spaced
within the superheater section than within the
economizer-evaporator section. In order that the same overall size
of the shell 1 should nevertheless be maintained in both sections,
provision is made inside said shell and within the superheater
section for an inner sheath 16 which surrounds the tube bundle,
which is welded to the shell at the upper end of this latter and
which limits the zone of sodium circulation.
In order to permit compensation for differential expansions during
operation, the configuration of each tube of the bundle forms an
expansion-bend 18 near the lower end of the module above the bottom
tube-plate 4.
The sleeve 12 which is provided around the tube bundle within the
lower sodium-outlet chamber stops short of said expansion-bends and
these latter can thus take up the entire available cross-sectional
space within said chamber. Moreover, the result thereby achieved is
to assist the circulation of sodium away from said extension-bends
which are thus located in a calm zone.
In this zone in which the tubes consequently have no further
function in the heat transfer process, a compact arrangement is
obtained by virtue of an original distribution of the bundle tubes
and by virtue of the arrangement of interjacent expansion-bends
which is thus made possible.
In the rectilineal portion which precedes the expansion-bends in
the vicinity of the lower end of the tube bundle, the different
tubes are subdivided into two half-bundles each disposed on a
square lattice with an identical pitch on each side of a main
lattice line along a diameter of the module. The geometry which is
imposed at this end of the tube bundle is not necessarily retained
in the remainder of the module.
As shown in FIG. 2, the two lattices conform to the same square
configuration and pitch but are relatively displaced by one-half
pitch along the principal line of separation. The expansion-bends
formed by the tubes of one lattice which form part of a same row at
right-angles to said principal line can thus penetrate into the
space of the other lattice while remaining in said plane and while
passing between two parallel rows of tubes of the other lattice. It
should be pointed out that, at the level of the expansion-bends,
the tubes still have substantially the same cross-section as in the
preceding rectilineal portion.
The module as hereinabove described thus makes it possible to
ensure effective compensation for differential expansions by means
of the expansion-bends which are provided at the lower extremity
but which nevertheless do not call for any increase in overall size
of the module. Positioning of said expansion-bends away from the
normal sodium flow prevents vibrations.
The invention is naturally not limited in any sense to the
particular embodiment which has been described in the foregoing but
extends to all alternative forms.
* * * * *