Patent Grant
8757248
This application is the National Phase of International Application no. PCT/EP2008/005484, filed 4 Jul. 2008, which claims priority to and the benefit of EP patent application number 07075587.1, filed 12 Jul. 2007, the contents of all which are incorporated by reference herein.
The present invention relates to a heat exchanger for heat exchange between fluids.
U.S. Pat. No. 3,648,768 has disclosed heat exchanger elements of plastic material consisting of a plurality of parallel pipes having connecting webs maintaining the pipes transversely spaced apart, which elements can be manufactured in one piece. It is stated in this document that the elements should be designed to have an inherent static stability for all practical purposes, more specifically sufficient bending strength to allow the elements supported at their ends to bridge a distance of several meters without bending. When multiple elements of this type are combined so as to form a larger heat exchanger block, spacing members are used whose opposite sides conform to the contours of one side of each of two adjacent heat exchanger elements. These spacing members may be e.g. glued or welded to the respective elements. Mechanical connecting means such as rivets, screws and tie rods may also be used. The elements may be connected to headers by cutting out the ends of the connecting webs so that short individual pipe ends project from the remaining main body of the connecting webs. These pipe ends may be fitted into bores of the header or anchored therein using short nipples. Due to the design this known heat exchanger having a heat exchange block comprising multiple elements of this type is a cross-flow heat exchanger.
A significant disadvantage of this known device is that although the elements are said to be thin-walled, relatively thick walls are required in heat exchangers of industrial scale, thereby severely limiting heat transfer between the fluids. Furthermore, despite the fact that the elements may be manufactured in one piece, a laborious operation whether by (physico)chemical means whether by mechanical means is needed to assemble several elements into a large heat exchange block.
Furthermore a compact countercurrent heat exchanger is for example known from US 2005/0217837. In this known heat exchanger a plurality of longitudinally extending and parallel fluid carrying tubes are arranged in thermal contact with one another. According to this publication each tube has at least one bend congruent to a bend in an immediately adjacent tube. All tubes are manufactured separately and then assembled together using for example Ag based alloy for brazing. During use a first heat exchange fluid flows through any one tube in a direction opposite to a direction of a second heat exchange fluid that flows through an immediately adjacent tube. In such a way a counter-flow heat exchange relation between the first and second heat exchange fluid is achieved. From the context of the specification it is apparent that such a compact counter-flow heat exchanger is obviously intended for use in aerospace dynamic power systems. In this known device the heat exchanger tubes are made from stainless steel.
Heat exchangers made from metal as in US 2005/0217837 are subject to fouling. Furthermore corrosion of the metal from which the heat exchanger channels are made may cause problems depending on the nature of the fluids between which heat is to be exchanged. Improvement with respect to corrosion may be achieved by using more expensive, more corrosion resistant metals or alloys such as stainless steel.
U.S. Pat. No. 4,733,718 has disclosed heat exchanger bodies or heat accumulator bodies for application according to the recuperator or regenerator principles. Such a body comprises a stack of extruded hollow chamber panels made from plastic and having plane smooth outer walls and webs that join the outer walls in a single piece. It is said that the plastic must be resistant to the media which, in use, will flow through the chambers of the hollow chamber panels. The softening temperature of the plastic should be above the highest operating temperature. The advantages claimed of this known heat exchanger body made up of a stack of individual hollow chamber panels are that the construction costs and expenses are low. The examples of individual hollow chamber panels shown in this document comprise a plastic body of one row of four adjacent hollow chambers. Several of these panels can be stacked to form the heat exchanger body. The joining of these panels in the area of the front surfaces thereof can be produced by welding, gluing or mechanically e.g. using clamping elements. Interlocking elements co-operating with elevations and/or depressions in the outer surfaces of the front surfaces of the panels are preferred. Disadvantages of this known heat exchanger relate to the double wall thickness affecting heat transfer, the square cross-section being a source of sealing problems and difficulties encountered in separately feeding the chambers. Furthermore, although the single panels can be manufactured easily, assembling multiple elements into a stacked configuration is laborious. The manufacturing process of the panels may become more complicated, if interlocking parts should be present in the panels themselves.
WO 2005/071339/discloses a heat exchanger for heat exchange between oil and water. An embodiment of this known device comprises rows of interconnected modules. Each module comprises a longitudinal tube having fins and two diametrically arranged connectors allowing assembling multiple modules into a linear row of modules. A separation plate is provided as a support between rows of interconnected modules. A first fluid flows through the longitudinal tubes, while a second fluid flows in the space between the modules and the housing and/or separation plates of the heat exchanger.
It is obvious that the designs and assembling processes discussed above are complicated, cumbersome, laborious, time-consuming and therefore expensive, offering a suboptimal final product with respect to its final heat transfer properties.
An object of the present invention is to eliminate one or more of these problems.
More particularly, an object is to provide a heat exchanger, preferably made from plastic material due to its favorable anti-fouling and anti-corrosion properties and despite its poor heat transfer properties, allowing an improvement of the total strength in order to keep the wall thickness low in view of heat transfer.
Another object is to provide a heat exchanger having a stable and strong configuration, wherein the stability and strength are mainly achieved by the general design and are dependent to a lesser extent from the nature of the construction materials and thickness than the general design.
Yet another object is to provide a heat exchanger, which is easy to manufacture, in particular to assemble from modular parts and to disassemble if needed.
Another object is to provide a heat exchanger having a high heat transfer area over volume ratio (m2/m3).
Yet another object is to provide an industrial scale heat exchanger allowing the use of corrosive media as heat exchanging fluids such as seawater and reducing the risk of fouling.
According to the present invention a heat exchanger for heat exchange between fluids is provided, comprising a housing having an inlet and an outlet for each fluid, the inlet and outlet for each fluid being connected to one another by a flow path, the flow path of a first fluid comprising multiple heat exchange modules comprising at least one longitudinal hollow tube, wherein the modules are arranged in a matrix configuration that comprises at least two columns of longitudinal tubes and at least two rows of longitudinal tubes, wherein a module is provided with at least one connector for connecting to a co-operating connector of an adjacent module, such that the space enclosed between adjacent modules defines a flow path for a second fluid, parallel to the flow path for the first fluid. In the heat exchanger according to the invention a plurality of modules is arranged in a housing having an inlet and an outlet for each fluid. A module comprises at least one longitudinal hollow tube. Together the tubes establish a flow path for a first fluid from the respective inlet to the co-operating outlet in fluid communication therewith. A module is also provided with at least one connector for connecting to an adjacent module that is also provided with a suitable connector co-operating with the first mentioned connector. Due to these co-operating connecting means the heat exchanger according to the invention can be manufactured easily from a plurality of modules. Furthermore easy replacement in case of malfunctioning is allowed. Advantageously each module is provided with one or more connectors, preferably integral with the longitudinal tube, for connecting to a co-operating connector of each adjacent module. In this embodiment the resulting matrix configuration is a self-supporting arrangement. In a further preferred embodiment the modules are arranged in a matrix configuration such that the outer walls of the longitudinal tubes and the connectors of two or more modules, preferably four, enclose a space extending in the direction of the longitudinal tubes of the modules. Due to the three dimensional connections between the modules in the matrix the strength and stability thereof are high. As a result the wall thickness of the longitudinal tubes can be low thereby maintaining the heat transfer properties at a favorable level, even if the modules are manufactured from a starting material having a poor heat transfer coefficient such as plastic. The co-operating connectors of different modules are partitions separating adjacent spaces forming the flow path for a second fluid. Such a flow path fluidly connects the inlet and outlet for said second fluid. As during use the same second fluid flows at different sides of the connectors under essentially the same flow conditions, these connectors do not need sealing means in the longitudinal direction. The outer walls of the longitudinal tubes form an impermeable barrier separating the first and second fluid between which heat is exchanged. Due to the design wherein a longitudinal tube for a first fluid is surrounded on all longitudinal sides by the space(s) for a second fluid a compact heat exchanger having a high heat transfer area over volume ratio (m2/m3) is obtained. Furthermore manufacturing costs may be kept at a low level compared to heat exchangers requiring a laborious method for coupling several modules.
Advantageously the modules used in the heat exchanger according to the invention are made in one piece from a plastic, preferably from a thermoplastic material, more preferably by extrusion.
Here it is to be noted that typically heat exchangers made from plastic materials are used mostly in air conditioning systems, and not so often in industry for heat exchange between process streams, wherein for example a hot (product) stream is cooled by seawater. Plastic is less sensitive to fouling and scaling, which otherwise would affect heat transfer. As the connectors and the matrix configuration attribute to the strength and stability, the wall thickness of the longitudinal tubes can be kept low, thereby allowing a reasonably high heat transfer despite the fact that the heat thermal conductivity for plastics is low compared to heat conductive materials like metals. Thus a compact design of a heat exchanger is possible. Where resistance against corrosion is less important, the heat exchanger can also be manufactured from metals, metal alloys and carbon, as these kind of materials are preferred in view of heat transfer. Due to the general design of the heat exchanger as outlined above and the resulting stability and strength the wall thickness of the longitudinal tubes can be kept low for plastic materials in view of heat transfer properties, while for expensive materials like titanium the cost price of the longitudinal tubes can be reduced because the amount of material needed is low.
A longitudinal tube is part of the flow path for a first fluid. A “space” enclosed by assembled modules provides a flow path for a second fluid. For sake of convenience, the adjective “first” will be used in this specification to indicate parts of the heat exchanger intended for a first fluid during use. Similarly, the adjective “second” will be used in this specification to indicate parts of the heat exchanger intended for a second fluid during use.
In the heat exchanger the main directions of the flows of the first and second flow are parallel to each other, preferably in opposite directions such as in a countercurrent heat exchanger having a higher overall performance than a cross-flow heat exchanger or alternatingly co-current and countercurrent as in a multipass heat exchanger.
Advantageously a module is made from a plastic material thereby reducing the risk of corrosion, as well as the occurrence of fouling. These characteristics are significant, where one or more of the fluids between which heat exchange has to take place, is aggressive such as corrosive themselves, for example, when the cooling fluid for a hot stream in a chemical plant is a liquid comprising one or more salts like seawater. The modules used in the heat exchanger according to the invention can be easily manufactured by extrusion of the (metal or plastic the latter being preferred) material in a desired length. In practice, a heat exchanger on industrial scale may have a length up to 10 meters or more. Preferably a module has a suitable length corresponding to the longitudinal dimension of the housing, thereby not requiring to mount more than one module one behind the other in the lengthwise direction of the heat exchanger. When the length of a module is limited by the manufacturing technique, a number of such modules can be arranged one behind the other in the direction of a flow path using suitable coupling means.
Compared to the heat exchangers as disclosed in the prior art discussed above, the number of welds and the like in order to assemble the plurality of modules is decreased, which makes manufacturing more easy and less expensive.
In the heat exchanger according to the invention the modules are arranged in a matrix configuration comprising at least two columns of longitudinal tubes and at least two rows of longitudinal tubes. More preferably a column and a row may comprise tens to hundreds of longitudinal tubes in view of capacity and heat transfer area.
Preferably a longitudinal tube has a circular cross-section providing a high heat transfer area over volume ratio in relation to the hydraulic diameter. In addition, the ends of circular tubes are sealed easily in similar through bores and the like of header/distributor/collector panels to be discussed herein below due to the circular shape. Furthermore extension if required can be provided by (circular) tube sections having appropriate dimensions. As to the wall thickness, the thinner the better. Long but small diameter thin-walled tubes are preferred, e.g. tubes having a wall thickness in the order of magnitude of 0.1 mm typically 0.01-1 mm, but preferably less than 0.1 mm.
Advantageously a connector substantially extends over the whole length of a module, parallel to the longitudinal axis of a module. In this way the connectors serve as supports for other modules over the full length thereby providing a stable and strong heat exchange block. Such longitudinally extending connectors can also easily be manufactured by extrusion. Preferably a module comprising at least one tube and respective connectors is made in one piece.
Preferably a module has at least one male connector and at least one female connector. A snap fit is a suitable example of co-operating male and female connectors. A rib or fin is a suitable male connector, while two spaced apart ribs or fins establish a suitable female connector. As said herein above, sealing between adjacent spaces is not required. If necessary, the outer surface of such a rib acting as a male connector may have one or more protrusions matching corresponding recesses in the inner surfaces facing each other of the ribs acting as a female connector.
In a particular preferred embodiment a module comprises one longitudinal tube and its associated connectors. Such a module can be handled relatively easily and allows easy exchange if necessary without distortion of the other stacked and connected modules.
Advantageously the longitudinal tube is provided with at least two connectors, the angle between adjacent connectors being less than 180° C., preferably four connectors at an angle of 90° C. The latter embodiment allows for a particularly stable rectangular main matrix configuration having a high heat transfer area over volume ratio (m2/m3), while the periphery may have any shape.
In an alternative embodiment a module comprises at least two longitudinal tubes connected to each other in a side-by-side configuration by an interconnecting web of material in one piece. Such a module offers the advantage of less assembling work, and is particularly suitable for a heat exchanger designed for low to moderate operating pressures. Preferably the end tubes thereof are provided with the appropriate connectors for connecting to each adjacent module, again allowing a stable and strong matrix configuration.
The heat exchanger according to the invention advantageously comprises a distributor for connecting the inlet for a fluid to the respective flow path and a collector for connecting the respective flow path to the outlet for said fluid. This means that during use a first fluid flows from a typically single first inlet through the distributor comprising a chamber in fluid connection with the first inlet to the respective first flow path. In this way the distributor distributes the first fluid stream flowing in a first direction over the longitudinal tubes of the heat exchanger. At the other end of the modules this first fluid stream is collected in a collector comprising a collecting chamber and discharged via the respective first outlet. Similarly a distributor and collector are provided for the second fluid.
Typically in a heat exchanger of the countercurrent type the inlet for a fluid will be at one end wall of the housing, while the outlet in fluid communication with this inlet is present in a side wall section near the opposite end wall of the housing. Typically the inlets for the fluids are at opposite ends of the housing.
In a heat exchanger of the multipass type the same configuration can be applied provided that suitable fluid returning means e.g. partition plates are provided in the distributor and/or collector. Such a modification of connecting one part of tube ends and/or spaces respectively to another part of tube ends and spaces leaves the basic design of the heat exchanger according to the invention intact.
In a preferred embodiment according to the invention the inlet and outlet of the first fluid flowing through the longitudinal tubes are arranged in opposite end walls, while the inlet and outlet of the second fluid flowing through the spaces surrounding the longitudinal tubes are present in the side wall(s) of the housing. This configuration allows for a favorable mounting of the modules, as sealing is less complex.
More preferably in such an embodiment a first distributor for a first fluid comprises a distributing chamber at one end of the housing defined by an end wall of the housing, a distributor panel spaced apart from said end wall and the respective side wall sections of the housing, and wherein a first collector for the first fluid comprises a collecting chamber at the opposite end of the housing defined by the opposite end wall of the housing, a collector panel spaced apart from said opposite end wall and the respective side wall sections of the housing, and wherein the distributor panel and the collector panel are provided with a plurality of through bores corresponding to the total number and positions of the tubes defining the first flow path, the longitudinal tubes extending through the through bores of the distributor panel and collector panel in fluid communication with the distributing chamber and collector chamber. In this preferred configuration the distributor and the collector for a first fluid are positioned at the opposite ends of the heat exchanger.
In a further preferred embodiment thereof a second distributor for a second fluid comprises a distributing chamber at said opposite end of the housing defined by the collector panel, the connector sections of the modules facing the collector panel and the respective side wall sections of the housing and a second collector for the second fluid comprises a collector chamber at said first end of the housing defined by the distributor panel, the connector sections of the modules facing the distributor panel and the respective side wall sections of the housing, these second distributor and second collector being in fluid communication via the space enclosed between adjacent modules defining the flow path for the second fluid. The collector and distributor for a second fluid are positioned longitudinally adjacent to the distributor and collector for the first fluid respectively, while the tubes in which during use the first fluid flows extend through the distributing and collecting chamber of the second fluid. In order to effectively separate adjacent chambers in the heat exchanger the tubes are sealed in the distributor and collector panel respectively.
Usually a collector panel supporting the ends of the modules, in particular the ends of the longitudinal tubes thereof will be present. This panel has a plurality of through bores corresponding to the total number and positions of the tubes defining the first flow path. As the cross-section of a space has a rather complicated shape compared to the preferred circular cross-section of the longitudinal tubes, it is easier to have the same kind of arrangement at the opposite end of the housing. In other words, the inlet and outlet of the first fluid are in opposite end walls of the housing, while the inlet and outlet for the second fluid are provided in the side wall sections near the respective ends of the housing. Then only in the distributor and collector of the second fluid some kind of cross-flow heat exchange will occur. However, the major heat exchange will occur in a counter flow arrangement as defined above.
If necessary, a longitudinal tube may have an extension. In a preferred embodiment thereof a longitudinal tube is provided with an extension part comprising a tube section having a rejuvenated end inserted in the open end of the longitudinal tube. The rejuvenated end provides a sealing fit inhibiting any leakage of fluids.
In another embodiment the connectors are absent or removed at one or both ends at the longitudinal tube.
The other end of the tube section advantageously extends through the through bore in the respective panel in a sealing manner. Preferably a seal such as an O ring is provided between the outer wall of the tube section and the wall part of the respective panel defining the through bore. Other types of sealing are welding and gluing.
The type of material from which the heat exchanger modules are made depends on the nature of the heat exchanging fluids as explained herein above. Metals, ceramics, carbon and plastic may be suitable starting materials, of which plastic is preferred.
As plastic material is a poor heat conductor compared to for example metals like copper, brass and stainless steel and carbon, the thickness of the walls between adjacent chambers is kept low taking into account the physical requirements that are to be met by the construction.
In order to increase the heat transfer the plastic material from which the modules are made, may comprise a heat conduction enhancing filler like carbon particles and the like. In order to increase the strength fiber-reinforced plastics may be used.
The preferred starting material from which the modules are made, is an extrudable material like plastic, for example polyethylene, polypropylene, polystyrene, polyvinylchloride and poly(meth)acrylate, fluor containing polymers like PTFEX and biopolymers. Other plastic materials allowing higher operating temperatures for example over 100° C. to about 120° C. are polycarbonate and polysulfon. Polyvinyleen oxides, polyetherimides, polyethersulfons and especially fluor containing polymers allow for even higher operating temperatures.
According to a second aspect the invention also resides in a heat exchanger module, obviously intended for assembling a heat exchanger according to the invention, said module comprising at least one longitudinal hollow tube, the module being provided with at least one connector for connecting to a co-operating connector of another module. The preferred embodiments specified above for the heat exchanger according to the invention equally apply to the module according to the invention.
The invention will be further explained by reference to the attached drawing, wherein:
It will be obvious to the skilled persons that many deviations and modifications from the embodiments shown in the drawings can be easily manufactured. These modifications and deviations are within the scope of the attached claims.
| Number | Date | Country | Kind |
|---|---|---|---|
| 07075587 | Jul 2007 | EP | regional |
| Filing Document | Filing Date | Country | Kind | 371c Date |
|---|---|---|---|---|
| PCT/EP2008/005484 | 7/4/2008 | WO | 00 | 4/27/2010 |
| Publishing Document | Publishing Date | Country | Kind |
|---|---|---|---|
| WO2009/007065 | 1/15/2009 | WO | A |
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| Number | Date | Country | |
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| 20100200203 A1 | Aug 2010 | US |
