SHELL AND TUBE HEAT EXCHANGER

Abstract: A shell and tube heat exchanger according to the present invention is used, for example, as a heat exchanger for the blood in an artificial lung. In this type of heat exchanger, a plurality of tubes are arranged in a cylindrical housing, and heads having fluid inlet and outlet are provided at both ends of this housing, a fluid being passed through these tubes. The cylindrical housing is further provided with fluid inlet and outlet so as to pass another fluid through the portion of the interior of the housing which is on the outer side of the tubes. The head in which the fluid inlet is formed is provided therein with a baffle board for stopping a flow of a fluid and generate a turbulent flow. This arrangement can prevent bubbles from residing in the head on the fluid inlet side, and enables the fluid to be distributed uniformly into the tubes and the temperature in the heat exchanger to be kept uniform.

Description: The present invention relates to the field of multitube heat exchangers. Whereas multitube heat exchangers having a rectangular housing an rectangular heads are known (DE 2 303 788), there have widely been used multitube heat exchangers having a tubular housing including heads defined by partitions in the opposite sides of the tubular housing. One of the heads has a fluid inlet port and the other head has a fluid outlet port. The housing accommodates a number of pipes juxtaposed between the heads for passing a fluid therethrough. The housing has fluid inlet and outlet holes for passing another fluid around the tubes, so that heat can be exchanged between the fluids through the walls of the tubes. If a multitube heat exchanger of this type known, for example from FR-A-1 583 744, is reduced in size for use as a heat exchanger for an artificial lung or the like, for example, the volumes of the heads are relatively large as compared with the effective heat-exchanging area of the heat exchanger. As a result, the speed of flow of the fluid in the pipes is greatly affected by the position of the pipes because of the directivity of the fluid flowing into one of the heads. Particularly, if the inlet port of the head is oriented tangentially to the tubular housing, the fluid produces a swirling motion in the head due to its directivity, thus developing a pressure difference between the central and outer circumferential regions in the head. Therefore, the speed of flow of the fluid flowing in those pipes which are located in the central region largely differs from the speed of flow of the fluid flowing in those pipes which are located in the outer circumferential region, with the result that the temperature in the heat exchanger becomes ununiform. The fluid in the central pipes does not flow, and hence a heat exchange between the fluid in the central pipes and the other fluid flowing around the central pipes is ineffective, and hence the efficiency of the entire heat exchanger is low. It is thus difficult to control the temperature of the other fluid in its entirety. Air bubbles introduced into the inlet port of the head tend to be attracted to the central lower-pressure region in the head. Consequently, these air bubbles are liable not to be discharged out through the pipes, making the temperature in the heat exchanger more uneven. In view of the aforesaid drawbacks of the conventional tube heat exchangers, it is an object of the present invention to provide a multitube heat exchanger which can remove air bubbles trapped in the central region in a head with a fluid inlet port and which prevents the speed of flow of a fluid in the pipes from flowing at different speeds depending on the position of the pipes, so that the fluid can uniformly distributed into the pipes to uniformize the temperature in the heat exchanger. As claimed the multitude heat exchanger of the present invention includes a tubular housing having partitions on opposite ends thereof which form heads respectively. One of the heads has a fluid inlet port and the other head has a fluid outlet port, and a plurality of juxtaposed pipes extend between the heads for passing a fluid therebetween. The housing has fluid inlet and outlet holes for passing another fluid around the pipes, for effecting a heat exchange between the fluids through walls of the pipes. According to the invention, Said fluid inlet port opens tangentially to said one head. A plurality of baffle plates are disposed in the head which has said fluid inlet port. The baffle plates project a certain distance in the axial direction of the head, extend radially outwardly and terminate at the inner circumferential surface of the head. The baffle plates are angularly spaced from each other for generating a turbulent flow in the fluid introduced from said inlet port, whereby the directivity of the fluid introduced from said fluid inlet port is reduced, to substantially uniformize the rate of flow of the fluid introduced into the pipes. Preferred embodiments of a multitube heat exchanger according to the present invention will be described in detail with reference to the accompanying drawings, in which : FIG 1 is a side elevational view, partly in cross section, of a heat exchanger according to the present invention; FIG. 2 is a cross-sectional view taken along line II - II of FIG. 1; FIG. 3(a) is a diagram illustrative of discharge pressures in the pipes of the heat exchanger; FIG. 3(b) is a diagram illustrative of discharge pressures in the pipes of a heat exchanger with no baffle plates employed according to a comparative example; FIG. 4 is a transverse cross-sectional view showing baffle plates according to another embodiment of the present invention; FIG. 5(a) is a diagram illustrative of discharge pressures in the pipes with the baffle plates shown in FIG. 4 being employed; FIG. 5(b) is a diagram illustrative of discharge pressures in the pipes of a heat exchanger with no baffle plates employed; and FIG. 6 is a graph showing the relationship between the rate of a blood flow and the heat-exchanging efficiency, by way of example, of a heat exchanger according still another embodiment of the invention and a conventional multitube heat exchanger. As shown in FIG. 1, a multitube heat exchanger according to the present invention includes a tubular housing 1 with partitions 2, 3 attached to its opposite open ends and heads 4, 5 mounted on the opposite ends of the housing 1. The head 4 has a fluid inlet port 6 and a plurality of projections, e.g., baffle plates 7. As shown in FIG. 2, the baffle plates 7 are spaced a certain distance from the center of the inner side surface of the head 4 and extend in the axial direction of the head 4. The baffle plates 7 also extend radially outwardly and terminate at the inner circumferential surface of the head 4. The baffle plates 7 are angularly spaced from each other by 120°. In order for the baffle plates 7 to check the flow of a fluid introduced from the inlet port 6, one of the baffle plates 7 is inclined at 60°, for example, to a radial direction normal to the direction (tangential direction) in which the inlet port 6 is oriented. The other head 5 has a fluid outlet port 8. The housing 1 accommodates therein a plurality of pipes 9 juxtaposed between the heads 4, 5 and extending through the partitions 2, 3. The fluid is introduced from the inlet port 6 of the head 4 into the heat exchanger, flows through the pipes 9, and is discharged from the outlet port 8 of the head 5. The housing 1 has inlet and outlet holes 10, 11 defined in its outer circumference for passing another fluid around the pipes 9. The inventor conducted an experiment in which a heat-exchanging medium was introduced from the inlet port 6 into the head 4 at a rate of 22 ℓ/min. In the experiment, the removal of air bubbles was observed and the discharge pressures (mmHg) at the outlet ends of the pipes were measured. The same observation and measurement were also carried out on a heat exchanger having no baffle plates 7 according to a comparative example. The results of the experiment are shown in FIGS. 3(a) and 3(b) and Table 1 below. FIG. 3(a) shows the results of the measurement of the heat exchanger of the present invention, and FIG. 3(b) shows the results of the measurement of the comparative heat exchanger. The numerical values in the pipes 9 represent discharge pressures: The Pf (Performance factor) was calculated according to the following equation: Pf = (Tbo - Tbi)/(Twi - Tbi) where Tbo: the temperature of the fluid having been subjected to a heat exchange and discharged from the heat exchanger (°C); Tbi: the temperature of the fluid entering the heat exchanger and to be subjected to a heat exchange (°C); Twi: the temperature of a heat medium (e.g., water) entering the heat exchanger (°C). The Pf indicates how the temperature varies while the fluid to be subjected to a heat exchange is passing through the heat exchanger. As can easily be understood from Table 1, the heat exchanger of the invention has a higher heat-exchanging efficiency than that of the comparative heat exchanger, and hence has a better heat-exchanging capability. According to this embodiment, the flow of the fluid introduced from the inlet port 6 is checked and converted to a turbulent flow by the baffle plates 7, thus impairing the directivity of the fluid. The fluid is therefore introduced uniformly into the pipes 9, and air bubbles are prevented from remaining in the central region in the head 4. A heat exchanger according to another embodiment of the present invention will be described below . In this second embodiment, baffle plates 7a (see FIG 4) are disposed in the head 4 of the heat exchanger shown in FIG. 1. The baffle plates 7a are of substantially the same construction as that of the baffle plates 7 described above, except that the baffle plates 7a have ends terminate short of the inner circumferential surface of the head 4. As with the first embodiment, a fluid was introduced from the inlet port 6 of the head 4, and discharge pressures (mmHg) at the outlet ends of the pipes 9 were measured. The same measurement was also effected on a heat exchanger having no baffle plates 7a according to a comparative example. The results of the experiment are shown in FIGS. 5(a) and 5(b). FIG. 5(a) shows the results of the measurement of the heat exchanger of the present invention, and FIG. 5(b) shows the results of the measurement of the comparative heat exchanger. The numerical values in the pipes 9 represent discharge pressures (mmHg). As with the first embodiment, the fluid flows substantially uniformly through the pipes 9 of the heat exchanger according to the second embodiment. However, no fluid at all flowed through the pipes 9 in the central region in the comparative heat exchanger. The baffle plates 7a are effective in reducing the pressure loss, making it possible to reduce the resistance and assuring a smooth fluid flow. The total rate of flow and the pressure loss of the comparative and inventive heat exchangers when the heat-exchanging medium is introduced using pumps of the same capacity are given in following Table 2: In Table 2, Q represents the rate of flow of the medium (ℓ/min). Using the same heat exchanger as that of the second embodiment and the comparative heat exchanger, the heat-exchange efficiencies of the heat exchangers were measured when cow blood having a hemoglobin concentration of 12 g/dℓ was employed and water flowed at a rate of 15 ℓ/min. The results are shown in FIG. 6, which indicates that the heat-exchanging efficiency of the heat exchanger of the present invention is better than that of the comparative heat exchanger. The baffle plates 7, 7a are normally made of the same material as, or a material similar to, the housing 1. However, the material of the baffle plates 7, 7a is not limited to those materials. The configuration and number of the baffle plates 7, 7a may be varied insofar as the introduced fluid flows into the pipes 9 uniformly at a constant rate. The direction in which the baffle plates 7, 7a installed is not limited; they may be attached at any angle insofar as they can generate a turbulent fluid flow. When the heat exchanger of the invention is in use, a heat medium flows through or around the pipes 9. However, if the heat exchanger is used as a heat exchanger associated with an artificial lung, it is preferable that blood flow around the pipes 9 and heat medium (cold water) flow through the pipes 9. With the present invention, as described above, the baffle plates for producing a turbulent fluid flow are disposed in the head with the inlet port. No air bubbles remain trapped in the head, and the discharge pressures under which the fluid is discharged from the pipes are prevented from being fluctuated. The heat exchanger of the invention has a high heat-exchanging efficiency.

Claims: A multitube heat exchanger including a tubular housing (1) having partitions (2, 3) on opposite ends thereof which form heads (4,5), respectively, one of the heads (4) having a fluid inlet port (6) and the other head (5) having a fluid outlet port (8), and a plurality of juxtaposed pipes (9) extending between said heads for passing a fluid through said pipes, said housing having fluid inlet (10) and outlet (11) holes for passing another fluid around said pipes (9) for effecting a heat exchange between the fluids through walls of the pipes, characterized by the fact that said fluid inlet port (6) opens tangentially to said one head (4) and by the fact that it includes a plurality of baffle plates disposed in the head which has said fluid inlet port, said baffle plates projecting certain distance in the axial direction of the head, extending radially outwardly and terminating at the inner circumferential surface of the head, and being angularly spaced from each other for generating a turbulent flow in the fluid introduced from said fluid inlet port, whereby the directivity of the fluid introduced from said fluid inlet port is reduced, to substantially uniformize the rate of flow of the fluid introduced into the pipes.

Inventors: NOGAWA, ATSUHIKO TERUMO KABUSHIKI KAISHA, OSHIYAMA, HIROAKI TERUMO KABUSHIKI KAISHA, SAKAI, SATORU TERUMO KABUSHIKI KAISHA
Applicants: TERUMO KABUSHIKI KAISHA
Application year: 1988
Main classification: F28D7
IPC codes: F28F13, A61M1, F28D7, A61M5, F28F9