U.S. patent number 3,568,765 [Application Number 04/776,428] was granted by the patent office on 1971-03-09 for plate-type heat exchanger.
This patent grant is currently assigned to Badische Anilin- & Soda-Fabrik Aktiengesellschaft. Invention is credited to Otto Konrad.
United States Patent |
3,568,765 |
Konrad |
March 9, 1971 |
PLATE-TYPE HEAT EXCHANGER
Abstract
A plate-type heat exchanger for fluids, comprising a deck of
separate plates with sealing means between adjacent plates which is
compressed by two end pieces, each of these end pieces having the
form of a short cylindrical shell with a domed end and the
compressive forces being applied to the deck of plates by means of
an end plate arranged in one of the end pieces and hydraulically
movable in the direction of the longitudinal axis of the deck of
plates.
Inventors: |
Konrad; Otto (Schriesheim,
DT) |
Assignee: |
Badische Anilin- & Soda-Fabrik
Aktiengesellschaft (Ludwigshafen/Rhine, DT)
|
Family
ID: |
25107351 |
Appl.
No.: |
04/776,428 |
Filed: |
November 18, 1968 |
Current U.S.
Class: |
165/166 |
Current CPC
Class: |
F28F
3/083 (20130101) |
Current International
Class: |
F28F
3/08 (20060101); F28f 003/00 () |
Field of
Search: |
;165/75,81,157,158,167,174,175,166 |
References Cited
[Referenced By]
U.S. Patent Documents
Primary Examiner: O'Leary; Robert A.
Assistant Examiner: Streule; Theophil W.
Claims
I claim:
1. A plate-type heat exchanger for liquids or gases comprising a
deck of individual, heat exchange plates and interposed gasket
means, a first, domed, end member at one end of said deck, a
second, domed, end member at the other end of said deck, conduit
means for introduction and discharge of heat-exchange fluids on
said first domed member into and from said heat exchanger, an end
plate interposed between said deck and said second, end member with
its peripheral edge slidably disposed inside said second, end
member for pistonlike movement of said end plate in the direction
of the longitudinal axis of said heat exchanger, aligned apertures
in said heat-exchange plates, said gasket means being interposed
between contiguous plates and defining, with respective aligned
apertures, a plurality of longitudinally extending passages for
flow of fluids axially through said heat exchanger, means in said
second, domed, end member for communicating pairs of passages to
reverse fluid flow from one passage and return it through another
passage, and means providing a substantially pressure tight seal
between said end plate and said second, domed end member whereby
fluid pressure in the latter member moves said end plate toward
said deck to compress said deck.
2. A plate-type heat exchanger as claimed in claim 1 wherein the
dome portion of said second member contains displacement bodies
which reduce the fluid capacity of said domed portion.
3. A plate-type heat exchanger as claimed in claim 1 wherein said
heat-exchange plates are circular plates with said apertures
comprising four symmetrically arranged openings near the periphery
of each heat-exchange plate for supplying and withdrawing the
heat-exchange fluids to and from the spaces between the
heat-transfer surfaces of neighboring plates, the outer edge of
each of these openings extending for less than a quarter arc of the
circumference of each plate, and each of the four areas situated
between two adjacent openings are provided with an aperture, these
apertures serving, in pairs, to convey the heat-exchange fluids
from the fixed end piece to the detachable end piece and vice versa
while bypassing the spaces between the heat-transfer surfaces of
the plates.
4. A plate-type heat exchanger as claimed in claim 1 wherein said
plates are circular plates, the external diameter of said end plate
being greater than the external diameters of said heat-exchange
plates.
5. A plate-type heat exchanger as claimed in claim 1 wherein said
plates are circular plates, the external diameter of said end plate
being at least equal to the external diameters of said
heat-exchange plates, and means for providing in said second,
domed, end member a fluid pressure greater than the fluid pressure
of said heat-exchange fluids.
Description
This invention relates to an improved plate-type heat exchanger for
liquids or gases.
Known plate-type heat exchangers consist of a deck of rectangular
or circular plates compressed between two end pieces. The plates
are corrugated on the surface and are provided with holes for
supplying and withdrawing the fluids to and from the spaces between
the plates. The end pieces have the form of flat plates and are
provided with connections for the admission and discharge of the
heat-exchanging fluids. Between adjacent plates there are arranged
sealing means which seal the spaces between the heat-exchange
surfaces and the ducts for the fluids when the deck of plates is
compressed by means of tie bolts arranged at the periphery of the
plates.
A drawback of these plate heat exchangers is that only plates
having a relatively small diameter or side length can be used in
their construction, because the high compressive forces which must
be applied to the deck of plates via the tie bolts for sealing
cause bending of the plates, which becomes more and more marked as
the diameter or side length of the plates in increased and readily
results in leaks.
It is an object of this invention to provide a plate-type heat
exchanger in which the compressive forces are distributed over the
whole area of the plates as uniformly as possible in order to avoid
bending of the individual plates even if the plates are relatively
large. Another object of this invention is to provide a plate-type
heat exchanger having all connections for the admission and the
discharge of the fluids arranged on the stationary end piece in
which, even in the case of large plates, the ducts for conveying
the fluids from the fixed end piece to the movable end piece and
vice versa can be arranged as holes in the plates without risk of
leakage.
In accordance with this invention, these objects are achieved by a
plate-type heat exchanger incorporating a deck of separate plates
with sealing means between adjacent plates which is arranged
between a fixed end piece and an end piece detachably connected
with the fixed end piece via tie bolts (hereinafter called
"detachable end piece"), the connections for the admission and the
discharge of the heat-exchange fluids being provided on the fixed
end piece and means for reversing the flow of the fluids being
provided at the other end of the deck of plates, wherein each of
the two end pieces has the form of a short flanged cylindrical
shell with a domed end and wherein an end plate is arranged inside
the detachable end piece in such a way that it is movable in the
manner of a piston in the direction of the longitudinal axis of the
heat exchanger, the deck of plates between the end plate and the
fixed end piece being capable of being compressed hydraulically by
means of the end plate by introducing a pressure fluid between the
end plate and the detachable end piece. If the pressure fluid is
not one of the heat-exchange fluids, the size of the end plate
should be at least equal to that of the plates arranged between the
end plate and the fixed end piece. If one of the heat-exchange
fluids is used as the pressure medium, the end plate should be
larger than the plates arranged between the end plate and the fixed
end piece. In order to ensure that the ducts for conveying the
heat-exchange fluids from the fixed end piece to the detachable end
piece and vice versa can be arranged as openings in the plates, it
is advisable for the plates to be circular in shape, the actual
heat-transfer surface of each plate being surrounded by four
uniformly spaced openings at the periphery of the plate for
supplying and withdrawing the heat-exchange fluids to and from the
spaces between the heat-transfer surfaces of neighboring plates,
the outer edge of each of these openings extending for less than a
quarter arc of the circumference of the plate, and each of the four
areas situated between two neighboring openings being provided with
an aperture, these apertures serving, in pairs, to convey the
heat-exchange fluids from the fixed end piece to the detachable end
piece and vice versa while bypassing the spaces between the
heat-transfer surfaces of the plates.
One embodiment of a plate-type heat exchanger according to the
invention will now be described, by way of example, with reference
to the accompanying drawing, in which:
FIG. 1 is a schematic longitudinal section of the heat exchanger
according to this invention;
FIG. 2 is a plan view of a single plate of the heat exchanger
without gaskets;
FIG. 3 is a plan view of a single plate of the heat exchanger with
gaskets; and
FIG. 4 is an exploded perspective view of a part of the heat
exchanger body .
Referring to FIG. 1 the plate-type heat exchanger illustrated
comprises a fixed end piece 10 containing pipe connections 18 for
the supply and withdrawal of the heat-exchange fluids, a detachable
end piece 11 provided with displacement bodies 17, circular plates
12 arranged between the two end pieces, a fixed end plate 13
located in the end piece 10, an end plate 14 provided with a seal
15 and movably arranged inside the end piece 11, and a plurality of
tie bolts 16 which hold the end pieces 10 and 11 together. FIG. 2
shows a circular plate 12 in which the actual heat-transfer surface
25 is surrounded by openings 20, 21, 28 and 29 for the supply and
withdrawal of the heat-exchange fluids to and from the spaces
between the plates. Since the connections for the admission and
discharge of the fluids to and from the heat exchanger are arranged
in the fixed end piece 10, ducts must be provided in the heat
exchanger for conveying the heat-exchange fluids from the end piece
10 to the other end of the deck of plates and vice versa while
bypassing the heat-transfer surfaces 25 of the plates. Therefore,
the openings 20, 21, 28 and 29 are arranged in such a way that
their outer edges extend for less than a quarter arc of the
circumference of the plate. The four areas situated between the
said openings are provided with apertures 22 and 23 which, in
pairs, serve to convey the heat-exchange fluids from the end piece
10 to the other end of the deck of plates and vice versa while
bypassing the heat-transfer surfaces 25 of the plates 12.
FIG. 3 shows the plate 12 according to FIG. 2 with gaskets, which
separate the openings 20, 21, 22, 23, 28 and 29 from each other and
cause the openings 20 and 28 to communicate with the space above
the heat-transfer surface 25. If plates with gaskets placed on them
in accordance with FIG. 3 are arranged to form a stack in which
adjacent plates are arranged at 90.degree. in relation to each
other, a heat exchanger body is formed (an exploded perspective
view of which is given in FIG. 4) in which the spaces between
neighboring heat-exchange surfaces alternately communicate with the
openings 20 and 28 and the openings 21 and 29. For the sake of
simplicity, only a limited number of plates 12 and gaskets 24 are
shown in FIG. 4. The fixed end piece 10 is followed by the end
plate 13, which in turn is followed by alternating gaskets 24 and
plates 12, the end of the heat exchanger being formed by the
movable end plate 14 and the end piece 11. The paths of the
heat-exchange fluids are marked by arrows; the paths of the fluids
through the spaces between the heat-exchange surfaces 25 of two
neighboring plates 12 are shown by arrows in the plane of the
intermediate gasket.
In the embodiment according to FIG. 4, which operates on the
countercurrent principle, the fluid 26 enters the heat exchanger
through one of the connections 18 and passes through the hole 27 in
the fixed end plate 13 into the openings 20. In the plane of the
first and every second following gasket 24 part of the fluid 26 is
passed through the space between the neighboring plates 12 in the
direction of the arrow for heat-exchange. These partial streams
leave the spaces via openings 28 and are then collected to form the
stream 45 which flows parallel to the stream 26. After the two
fluid streams 26 and 45 have reached the end of the deck of plates,
they are reversed and then returned to the fixed end plate 13
through the ducts 22, thus bypassing the heat-exchange surfaces 25
of the plates 12; they pass through the holes 30 and 31 and are
combined into one stream 26 + 45, which is discharged through one
of the connections 18.
The second heat-exchange fluid 32 + 33 enters the heat exchanger
through another of the connections 18. It is divided into two
partial streams 32 and 33, which are passed through the holes 34
and 35 in the end plate 13 into the ducts 23. When the two streams
have reached the space between the last plate 12 and the end plate
14, they are reversed and then returned as stream 36 through the
openings 21 to the end piece 10. In the plane of the gasket 24
arranged immediately ahead of the end plate 14 and in the plane of
every second of the following gaskets 24 part of the stream 36 is
passed in the direction of the arrow through the spaces through
which the first heat-exchange liquid 26 does not flow; these
partial streams are collected in the openings 29 to form the stream
37 which flows parallel to the stream 36. After passing through the
holes 38 and 39 in the end plate 13, the streams 36 and 37 are
combined into one stream 36 + 37, which is discharged from the heat
exchanger through one of the connections 18.
Sealing of the ducts 22 and 23 and of the openings 20, 21, 28 and
29 is effected by allowing a pressure medium to act upon that side
of the movable end plate 14 which faces the end piece 11 so that
the end plate is moved toward the fixed end piece 10, thus
compressing the deck of plates and gaskets. In the embodiment
according to FIG. 4, the streams 26 and 45 of one of the
heat-exchange fluids are used as the pressure medium, the end plate
14 having a larger external diameter than the plates 12. For this
purpose, the streams 26 and 45 pass through the holes 40, 41, 42
and 43 in the end plate 14 and fill the space between the end plate
14 and the end piece 11. Since a larger area of the end plate 14 is
acted upon by fluid on the side facing the end piece 11 than on the
other side, a thrust toward the end piece 10 is produced which
exerts the necessary sealing force on the gaskets 24. In order to
keep the liquid-filled volume of the end piece 11 small, the latter
may be provided with displacement bodies 17 forming channels 19 of
much smaller fluid capacity. The fixed end piece 10 and the
detachable end piece 11 with their domed ends are capable of taking
up much higher pressures than the disc-shaped end pieces of
conventional heat exchangers.
The pressure medium to be introduced between the end plate 14 and
the end piece 11 may be a fluid other than the heat-exchange fluids
(hereinafter called "extraneous pressure medium"), which would have
to be introduced into the end piece 11 through a pipe connection
(not shown in FIG. 4). When the extraneous pressure medium is under
a higher pressure than the heat-exchange fluids, the end plate 14
may have the same external diameter as the plates 12. When an
extraneous pressure medium is used, reversing the flow of one of
the heat-exchange fluids can only be carried out in the end piece
11 by providing in the latter fluidtight ducts for the purpose (not
shown in FIG. 4). In any case, the end plate 14 is so arranged in
the end piece 11 that it is axially movable, the joint between the
end plate 14 and the end piece 11 being sealed by a gasket 15. The
flanges of the end pieces 10 and 11 are connected by tie bolts 16
(cf. FIG. 1), which pass through holes 44 in the flanges.
During operation of the heat exchanger, the end plate 14 is
mechanically stressed only by the pressure difference existing
between the heat-exchange fluids, on the one hand, and the
extraneous pressure medium in the end piece 11, on the other; when
one of the heat-exchange fluids is used as the pressure medium,
part of the end plate 14 is not stressed at all. The end plate 14
therefore need not be very thick and can be made from a material
which need not satisfy any particular requirements regarding
strength. When shutdowns are necessary, the pressure on the end
plate 14 and the gaskets between the plates 12 can be released in a
very simple manner by draining the pressure medium from the end
piece 11, which favorably affects the life of the gasket. The
compressive forces required for sealing the deck of plates are
uniformly distributed over the whole diameter of the latter by the
end plate 14 movably arranged in the end piece 11 so that when
large compressive forces are applied or when plates of large
diameter are used there is no risk of the plates being deformed and
leaks occurring, as may easily be the case with conventional heat
exchangers in which large compressive forces are applied to the
edges of the plates by means of tie bolts. The tie bolts 16 shown
in the drawing (FIG. 1) serve merely to firmly connect the two end
pieces 10 and 11 with each other but not to apply the compressive
forces to the plates 12.
In some cases it may be advantageous for the end plate 13 to be
arranged in the end piece 10 in such a way that it is axially
movable, as is the end plate 14 in the end piece 11.
* * * * *