U.S. patent number 3,640,340 [Application Number 05/091,477] was granted by the patent office on 1972-02-08 for heat exchange device with convoluted heat transfer wall.
This patent grant is currently assigned to Baxter Laboratories, Inc.. Invention is credited to Fred Michael Cohen, Ronald James Leonard.
United States Patent |
3,640,340 |
Leonard , et al. |
February 8, 1972 |
HEAT EXCHANGE DEVICE WITH CONVOLUTED HEAT TRANSFER WALL
Abstract
A heat exchanger device with a convoluted heat transfer wall to
define a first and second set of flow channel defining pockets
having oppositely opening mouths. Each set of pocket mouths
communicates with a separate fluid inlet and fluid outlet means
disposed adjacent opposite ends of the pocket mouths. Sets of
continuous ridges fit into the pocket mouths between each fluid
inlet and outlet to provide flow channels of unvarying width by
preventing transverse movement of the convolutions of the heat
transfer wall, as well as to seal the pocket mouths between each
fluid inlet and outlet.
Inventors: |
Leonard; Ronald James (Elk
Grove Village, IL), Cohen; Fred Michael (Chicago, IL) |
Assignee: |
Baxter Laboratories, Inc.
(Morton Grove, IL)
|
Family
ID: |
22227990 |
Appl.
No.: |
05/091,477 |
Filed: |
November 20, 1970 |
Current U.S.
Class: |
165/166;
165/DIG.399; 162/165; 607/106 |
Current CPC
Class: |
A61M
5/44 (20130101); F28D 9/0025 (20130101); A61M
2205/366 (20130101); Y10S 165/399 (20130101) |
Current International
Class: |
A61M
5/44 (20060101); F28D 9/00 (20060101); F28b
003/00 () |
Field of
Search: |
;165/164-169,46 ;113/118
;128/400,399 |
References Cited
[Referenced By]
U.S. Patent Documents
Primary Examiner: Matteson; Frederick L.
Assistant Examiner: Streule; Theophil W.
Claims
That which is claimed is:
1. A heat exchanger device which defines a heat transfer wall of
convoluted shape to define a first set and a second set of flow
channel defining pockets, the mouths of the pockets of the first
set opening in a direction opposite to the mouths of the pockets of
the second set, a fluid inlet and a fluid outlet disposed adjacent
opposite ends of the pocket mouths of each of said first and second
sets, and sets of continuous sealing ridges fitting into said
pocket mouths between each said fluid inlet and outlet to provide
flow channels of unvarying width by preventing transverse movement
of the convolutions of said heat transfer wall, and to seal said
pocket mouths between each said fluid inlet and outlet.
2. The device of claim 1 in which each fluid inlet, fluid outlet,
and set of continuous ridges communicating with a single set of
pocket mouths are defined by a unitary, elastomeric manifold
fitting over each set of pockets.
3. The device of claim 2 in which the ends of said convoluted heat
transfer wall are potted with sealant to prevent fluid leakage from
the ends of said pockets.
4. The device of claim 3 in which each said manifold has separate
ridge extensions at the ends thereof for sealing fit into said
pockets, said ridge extensions being beveled outwardly to receive
said sealant.
5. The device of claim 4 in which the outer lateral walls of said
manifolds are sealed to said convoluted heat transfer wall with
beads of sealant which are spaced from each other to expose
portions of said heat transfer wall between said sealant beads to
the exterior.
Description
BACKGROUND OF THE INVENTION
The growing art of organ perfusion requires compact apparatus for
heat exchange between separate fluids, and particularly for heat
exchange between blood and a heat transfer fluid. The same heat
exchange equipment is also useful for warming or cooling the blood
of a patient during surgical operations and the like.
In Transactions--American Society for Artificial Internal Organs,
Vol. 6, pp. 360-369, Esmond et al. discloses a disposable stainless
steel blood heat exchanger which uses a convoluted heat transfer
wall for defining two separate sets of oppositely opening pockets.
Each set of pockets forms a multiple path flow conduit for a
separate fluid which interleaves with the other multiple path flow
conduit, providing abundant surface area for heat exchange in a
very small space.
However, certain disadvantages arise with the convoluted heat
exchange devices of the prior art. In particular, the individual
convolutions of such a convoluted heat transfer wall are quite
flexible and springy, and they are easily moved laterally back and
forth in the manner of an accordion bellows. The result of this is
that the flow channels within the pockets defined by the
convolutions may easily vary in thickness, especially when there is
a difference in the pressure of the two fluids in the separate flow
channels. Hence it is difficult in the prior art devices to keep
the flow channels at a desired optimum thickness for the best heat
transfer and flow efficiency because of the high flexibility of the
convoluted heat transfer wall. Even if support studs are
intermittently provided in the pockets in the manner of U.S. Pat.
No. 2,953,110, a substantial variation in the thickness of the
various flow paths can still take place through accordionlike
flexing, as well as through bowing of the walls between the studs
when a differential pressure is present in the two flow paths.
Differential pressures of up to about 10 p.s.i. are typically used
in the devices for heat exchange between blood and another
fluid.
Furthermore, in the prior art devices, the blood is free to migrate
out of the mouths of the pockets in substantial quantity, passing
into low-flow areas adjacent the pocket mouths, where it can
stagnate and clot. The presence of such a large amount of clotting
blood can result in the relatively rapid spread of blood clotting,
and pieces of clotted blood passing downstream along with the fresh
blood.
DESCRIPTION OF THE INVENTION
The heat exchange device of this invention utilizes a convoluted
heat transfer wall to define first and second sets of oppositely
opening pockets, with a separate fluid inlet and fluid outlet
disposed adjacent opposite ends of each set of pocket mouths. Sets
of continuous sealing ridges are disposed to fit into each pocket
mouth between each fluid inlet and outlet. This greatly reduces
transverse movement of the convolutions of the heat transfer wall,
providing flow channels of unvarying width, even in the presence of
the relatively high differential pressures of 10 p.s.i. or more
between fluids flowing in the separate sets of pockets.
Furthermore, the sealing ridges greatly reduce the migration of
fluid, and most importantly blood, out of the main flow path within
the pockets into stagnant areas adjacent the mouths of the pockets,
thus greatly reducing the possibility of substantial amounts of
blood clotting taking place in the heat exchange device.
An added advantage of the device of this invention is that it
operates with a constant volume in its flow channels irrespective
of moderate changes in pressure in the flow channels. This is
important in surgical operations, so that the amount of blood
present in the heat exchange system can be readily determined
without calculation.
In the drawings,
FIG. 1 is a plan view of the heat exchange device of this
invention, showing one manifold thereof.
FIG. 2 is an elevational view of the heat exchange device of this
invention, showing both manifolds and a portion of the convoluted
heat transfer wall.
FIG. 3 is a vertical sectional view of FIG. 2 showing details of
the convoluted heat transfer wall and the general pattern of flow
of separate fluids through the heat exchanger device.
FIG. 4 is a bottom plan view as indicated by line 4--4 of FIG. 3 of
one manifold used in the device of this invention, showing the
internal side of the manifold which presses against and secures
convolutions of the heat transfer wall.
FIG. 5 is a transverse section taken along line 5--5 of FIGS. 2 and
3.
Referring to the drawings, a heat exchange device is shown in which
a pair of manifolds 10, 12 bracket and sealingly secure
convolutions 14 of a heat transfer wall 16. Manifolds 10, 12 can be
molded from an elastomeric material, typically silicone rubber or
another antithrombogenic material such as suitable formulations of
polyurethane or other thermoplastic or cross-linked elastomeric
materials.
Each manifold 10, 12 comprises an inlet 18, 18a, and an outlet 20,
20a, as well as a plurality of continuous sealing ridges 22, 22a,
to fit into the mouths of oppositely opening pockets 24, 24a
defined by convoluted heat transfer wall 16. Ridges 22, 22a provide
anchoring to the individual convolutions 14 of heat transfer wall
16, preventing their lateral movement, with the resultant benefits
described above. The ridges 22, 22a also are desirably proportioned
and sufficiently elastomeric to provide a generally fluidtight seal
at the mouth of each of pockets 24, 24a to prevent fluid, and
particularly blood, from passing out of the mouths of the pockets
into stagnant areas 26, 26a, in which flow through the device is
substantially reduced and blood clotting may take place.
It is of course readily seen that one of the manifolds, the one
which does not seal the blood flow path, is not required to perform
its pocket mouth sealing function with the same urgency as the
manifold sealing the blood flow path, but it is generally
convenient to manufacture the two manifolds out of the same
material and in the same mold.
Each manifold has outer walls 28, 28a to grip the convolutions of
the heat transfer wall for both fluidtight sealing and holding the
convolutions in position.
Referring to FIG. 3, a typical flow pattern of two separate fluids
in two oppositely facing pockets 24, 24a is shown. One fluid,
typically blood, passes into the heat exchange device through fluid
inlet 18 and is spread out by plenum 30 to permit blood to flow to
every pocket 24 in communication with plenum 30. Blood flow path 32
is shown in which the blood passes into each pocket 24, moves
horizontally through the length of each pocket 24, being prevented
from passing out of the mouths of each pocket by continuous sealing
ridge 22, and then is collected in plenum 34 and passes out of
fluid outlet 20.
In similar manner, a second fluid, typically a heat exchange fluid
such as saline solution, enters a second fluid inlet 18a, which
communicates with each of pockets 24a. Fluid flow path 36 is shown
in dotted line, being behind convoluted heat transfer wall 16, with
the exception of where a portion of wall 16 is broken away to
expose a portion of pocket 24a to direct view. The heat transfer
fluid flow path 36 runs in a similar manner through the length of
each pocket 24a, and exits through fluid outlet 20a.
Each pocket 24 is in close contact with at least one and usually
two pockets 24a. Thus, as the blood passes through pocket 24 and
heat exchange fluid through pockets 24a, there is a heat transfer
from one fluid to the other through the convoluted wall 16 without
any mixing of the two fluids.
Generally, the heat transfer fluid is brought from a large fluid
source in which the temperature is externally controlled as
desired, and the two fluid flow rates controlled so that the blood
has achieved the desired temperature by the time it reaches fluid
outlet 20.
The ends of convoluted heat transfer wall 16 are potted with
sealant 35 to prevent fluid leakage from the ends of pockets 24,
24a. Such sealant is typically an organosilicon room temperature
vulcanizing elastomer of a type which is readily commercially
available. The areas between outer lateral walls 28, 28a of each
manifold and convoluted heat transfer wall 16 are also potted with
linear beads 37 of sealant to prevent fluid leakage. However, a gap
is left between sealant beads 37, exposing part of convoluted wall
16 to the exterior, to further reduce the possibility of seepage of
fluid from one flow path to the other.
To provide additional anchoring of the convolutions of wall 16, and
also to accommodate the receiving and holding of sealant 35, ridge
extensions 38 are provided for sealing fit into the ends of the
mouths of pockets 24, 24a. Ridge extensions 38 are beveled
outwardly as shown in FIG. 3 to receive the sealant. The ridge
extensions and sealant 35 firmly seal the ends of manifolds 10, 12
to the ends of wall 16, preventing any undesirable lateral "play"
between them, and preventing accidental removal of the
manifolds.
The flow of the two fluids through the heat exchanger device of
this invention is shown to be countercurrent in nature, which is
the preferred technique, but it is contemplated that cocurrent flow
can also be used, in which the two fluids flow in the same
direction, if desired.
Each inlet 18, 18a and outlet 20, 20a has a flange 40 defined about
its end. This permits connection with another flanged tube in order
to connect the heat exchange device of this invention with organ
perfusion equipment, a heat exchange fluid source, blood conduits,
or any other apparatus as desired. Flanges 40 permit the connection
to another flanged tube by any connector device desired, such as
the device defined in U.S. Pat. No. 3,456,965.
The face of convoluted wall 16 which is intended for contact with
blood is typically coated with a thin silicone resin or elastomer
coating, to render wall 16 antithrombogenic.
The above disclosure is for illustrative purposes only, and not for
purposes of limitation, the invention of this application being
defined in the claims below.
* * * * *