The present invention relates to a method for the exchange of heat between liquid and air.

The exchange of heat between air and liquid, espe- cially water, plays an important part in our use of ener- gy, for instance in the cooling and heating of buildings, air treatment, industrial heating processes, such as drying etc. In many energy systems using, for example, heat pumps, solar heat, waste heat or district heating, the efficiency could be improved considerably if the flow resistance in the heat exchangers employed were reduced. However, this would result in heat transmission surfaces substantially larger than is economically feas¬ ible with today's technology.

Known heat exchangers for liquid/air are designed as closed pipe systems for liquid circulation, and the outer pipe surface area which is the heat-exchanging surface towards the air, is frequently increased by finning. To ensure stability and heat conductivity, the pipes and fins are preferably made of metal. Such heat exchangers are expensive and, besides, suffer from the disadvantage that the fins cause a certain flow resistanc and that it is difficult to defrost the space between the fins. Furthermore external and internal corrosion may occur. The present invention has for its object to offer a method of effecting heat exchange between an air flow and a liquid flow by simple and inexpensive means hav¬ ing a high stability to external and internal corrosion and a very low resistance to heat conductivity. To rea- lize this object, the liquid is caused to flow by gravi¬ ty a-s a liquid film spreading under capillary action between two substantially vertically oriented membranes held together by the adhesive force in the liquid film.

and air is conducted in contact with the sid°s of the membranes- facing away from the liquid film for heat ex¬ change through said membranes.

The invention also comprises a heat exchanger in- tended for carrying the above method into effect and characterised by a heat-exchanging surface consisting of at least two vertical band-shaped membranes, the sur¬ faces of which are disposed opposite and at a slight distance away from one another and which are held to- gether by a liquid film spreading under capillary action, means for supplying and uniformly distributing the liquid flow in the upper part of the space between said mem¬ branes, means for taking up the liquid from the lower part of said space between said membranes, and means for conducting the air into contact with the surfaces of said membranes facing away from one another.

The invention will be described in more detail in the following, reference being *ad to the accompanying drawings which illustrate embodiments of the invention. Fig. 1 illustrates schematically in lateral vertical section a flow diagram during heat exchange according to the invention. Figs. 2 and 3 illustrate the heat ex¬ changing surface of the arrangement as shown in Fig. 1 in a vertical section from in front and in a horizontal section, respectively. Figs. 4 and 5 are, respectively, front and lateral sections, on a larger scale, of a prac¬ tical embodiment of a heat exchanger according to the invention.

The method of effecting heat exchange according to the invention will be described first, with reference to Figs. 1-3.

The invention utilizes as the heat-exchanging sur¬ face one or more band-shaped pairs of membranes 3 con¬ sisting of two thin membranes 4a and 4b held together by a film 5 of a liquid 1 spreading under capillary ac¬ tion. By suspending or clamping said pair of membranes 3 in vertical position and by supplying, without positive

pressure, a weak flow of the liquid 1 along the upper horizontal opening 31 of said pair of membranes, a uni¬ formly distributed downward flow of said liquid film 5 under the action of gravity and flow resistance is obtain- ed. With small flows, the adhesive forces between the membrane surfaces are substantially greater than the static liquid pressures, and uniform flow pattern is obtained along the entire vertical extent of said pair of membranes 3. Heat exchange from the liquid flow 1 spread in this manner occurs through the membrane walls to an air or gas- flow 2 propelled in narrow gaps 6 surrounding said pair of membranes 3.

The air flow 2 preferably is propelled in counter- flow to the liquid flow 1.

The membranes 4a and 4b may be made of different materials and may be of the same or different thickness. The membrane surface facing the liquid film 5 should have a low surface tension to facilitate spreading of the film, while the membrane surface facing the air gap 6 preferably is hydrophobic to facilitate the release of dirt, condensate and ice from the surface.

To reduce costs and facilitate maintenance, the material used for the membranes preferably is a plastic film, for instance a polyester film having a thickness of 50μm, which is chemically or. mechanically etched on one surface to increase wettability. With the above- mentioned membrane thickness, the resistance to heat conductivity in the membrane wall will be negligible, although the plastic material in itself is a poor heat conductor.

For continuous operation, the heat-exchanging sur¬ face 3 described above is incorporated in a flow circuit as shown in Fig. 1. A flow of a liquid 1 is supplied to the upper opening 31 of the pair of membranes 3 via an open supply vessel 7 and a flow-distributing throttle 8 and then flows over the membrane surface in heat-ex-

changing relation with the air flow 2. The liquid is dis¬ charged through-the lower opening 32 of said pair of membranes 3 and is collected in a collecting vessel 9a and conducted, through an inclined conduit 10, to a supply tank 11 from where the liquid flows through a liquid heat exchanger 12 connected to an outer cooling or heat¬ ing source 13 and continue to a circulation pump 14 which finally, via a riser pipe 15 and a flow-controlling valve 16, opens into the supply vessel 7. By circulation of the liquid 1, heat exchange is effected between the cooling/heating source 13 and the air- flow 2 in the gaps 6.

When, during operation, the air in the gaps 6 is cooled to a temperature below the freezing point, and frost or coatings of ice are formed on the upper part of said pair of membranes 3, such coatings are readily released and caused to fall out by periodically supply¬ ing, in accordance with the invention, liquid of higher temperature between said pair of membranes 3. To this end, there is connected to the flow circuit a vessel

17 which communicates with the supply tank 11 via a con¬ duit 18 and which is partly filled with liquid la which is heated by means of a heating coil 19. The suction side of the pump 14.is connected by means of a solenoid valve 20 to the tank 11 and, by means of a solenoid valve 21, to the vessel 17. By periodically closing the valve 20 and opening the valve 21, heated liquid la is intro¬ duced into the upper part of the pair of membranes 3. The lower opening 32 of the pair of membranes 3 is provided with a deflector 22 so that condensate and released coatings of ice will not be mixed with the li¬ quid which, in the above-mentioned case of operation, is an aqueous solution with, for example, calcium chlo¬ ride or monopropylene glycol. A practical embodiment of a heat exchanger for air/liquid will now be described with reference to Figs. 4 and 5.

The heat exchanger comprises a number of identical band-shaped membranes 4a, 4b of, for example, polyester film which has a width of 1.0 m and a thickness of 50uπι and which is chemically matted on one side. The membranes 4a are in the form of endless loops which are hung each over one liquid-distributing apertured pipe 40, while the membranes 4b which also are ^" in the form of endless loops, are strung between supporting rods 41 within the loops of the membranes 4a, whereby the two loops will form two pairs of membranes. The cross-sectional dimen¬ sions of the pipes 40 and the supporting rods are approxi¬ mately the same so that the membranes will contact one another with their matted surfaces. The supporting rods are carried by a structure 43 which is fixedly secured, and the loops are slightly compressed at a distance from their ends by means of rods 42 extending in parallel with the pipes 40 and the supporting rods 44. The ends of the outer loops with the membranes 4a are obliquely cut off and welded together so that, -when the loops are hung from the pipes 40, the free lower end will incline in one direction, as shown at 44 in Fig. 4. In the embodi¬ ment according to Fig. 5, four outer loops with membranes 4a are hung adjacent one another each from one tube 40 and each contain one inner loop with a membrane 4b, and the entire arrangement is accommodated by a casing 45 carrying the pipes 40, the structure 43 with the support¬ ing rods 41, and the rods 42. The casing 45 has a bottom 49 which is inclined in the same manner as the inclined lower ends of the outer loops, as shown in Fig. 4, and an outlet pipe 50 in its lowermost portion. Lower pipe sockets 46 for the supply of air are also secured to the casing, and upper apertures are provided for the discharge of air.

If liquid is supplied to the pipes 40 from a distri- buting pipe 48, it will be uniformly distributed over all of the pairs of membranes 4a, 4b and, furthermore, will be uniformly supplied over the entire width of each

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pair of membranes. As has previously been mentioned, the liquid flows dovmwards through the pairs of membranes 4a, 4b in the form of a film 6 spreading under capillary action, while heat exchange is effected with an air flow 2 supplied via the pipe sockets 46 and moving upwardly in the gaps between the pairs of membranes. The liquid ^• is d _* eflected along the oblique lower edge of the outer loop with the membrane 4b and the outlet pipe 50, while the upwardly moving air is discharged via the apertures 47.

The heat exchange described above can be adapted to many different types of operation by variation of such parameters as width and height, the number of pairs of membranes, the width of the air gap, and the flow rates of air and liquid. The h-eat exchanger can be provid¬ ed at low cost with very large heat-exchanging surfaces since the membrane material included therein is very inexpensive.