HEAT EXCHANGER

Abstract: A heat exchanger (1) comprises an annular vessel (10) containing a heat transfer fluid (11). Immersed in the fluid (11) is a plurality of flat spiral working tubes (15) forming part of a refrigerating circuit and also a plurality of flat spiral product tubes (20) carrying air to be cooled and thereby dried. Heat is extracted from the air in the tubes (20) by the refrigerant partly via the fluid (11) and partly via the mutual contact of adjacent alternate spirals of working and product tubes. Condensation is removed from the cooled air by a separator (28).

Description: Heat Exchanger This invention relates to heat exchangers for heating or cooling a product fluid such as air. The-invention provides a heat exchanger for heating or a product fluid, the exchanger comprising a vessel containing aheat transfer fluid, at least one generally flat spiral working tube at least partially immersed in the heat transfer fluid and having an inlet and an outlet for the passage there through of .erking fluid, and at least one generally flat spiral product tube at least partially immersed in the heat transfer fluid and having an inlet and an outlet for the passage therethrough of the product fluid, whereby heat may be transferred between the product/fluid and the working fluid through the heat transfer fluid. Where there the plurality 6f the working and/or product tubes, the working and product tubes are preferably arranged in alternate layers. The vessel may have an annular interior containing the heat transfer fluid and tubes. Preferably, the directions of flow in adjacent spirals are respectively inwardly and outwardly of the spirals, and the tubes of adjacent spirals may abut each other. Furthermore, the directions of flow in abutting tubes of adjacent spirals are preferably in opposite sense. Conveniently, each spiral is orientated substantially horizontally. Pipes connected to the inlet and outlet of the or each workingand/or product tube may typically pass through a lower wall or the bottom of the vessel. The vessel is preferably a closed container. In the case where the heat exchanger is used for cooling the product fluid, the working fluid would be a refrigerant which could be contained in a refrigerating circuit of which the or each working tube forms part. A thermostat is preferably provided which is responsive to the cooled product fluid to control the refrigerating circuit to prevent freezing of condensate in the heat exchanger. The product fluid may be air. The heat exchanger may form part of a gas dryer, the#'cproductfIuid#baing2gas to be dryed, there being a separator connected to the outlet of the or each product tube for separating condensate from the cooled gas. Such a gas dryer may have a second heat exchanger connected t#o the inlets of the or each priduct tube and to the separator for transferring heat from incoming gas to outgoing gas. An embodiment of the invention will now be described, by way of example, with reference to the accompanying drawing, which shows in diagrammatic elevation an air dryer incorporating a heat exchanger embodying the invention. A heat exchanger generally indicated 1 comprises a vessel 10 defining an annular interior containing a heat transfer fluid 11 such as glycol solution. The vessel 10 is closed by a lid 12 which can be removed to allow inspection. The lid is fitted with a plastic venting cap (not shown) to prevent build-up of pressure in the vessel, the cap having a baffle to prevent spillage of glycol during transit. When the heat -exchanger is installed, there is of course no need for the baffle. A plurality of spiral working -tdbes -15forming part' of a refrigerating circuit for cooling the fluid 11 are immersed in this fluid in the vessel 10. The tubes 15 are supplied with refrigerant through input pipes 16 from a distributor (not shown). After flowing around the tubes 15, the refrigerant is collected at the outer edges of the spirals in a collection pipe 18 which passes out through the bottom of the vessel 10 and conveys the refrigerant back to the compressor (not shown). Also immersed in the fluid 11 is a plurality of spiral product titles 20 through which the product fluid - in this case the air to be dried - is passed to be cooled. The refrigerating circuit is controlled by a thermostat (not shown) which is ideally responsive to the temperature of the air flowing from the product tires 20 to prevent condensate freezing. Conveniently, the thermostat may comprise a capillary operating switch associated with a mercury bulb attached to a, product tube 20 in a temperature well at the coldest part of the tube. The thermostat cuts the compressor sout near freezing point, for example 10C, and cuts it in at for example 300. It will be appreciated that the choice of the temperature differential between stopping and starting the compressor is a compromise between the desire to achieve close control of the temperature and tulle undesirability of a short cycle time for the compressor. The spirals are arranged horizontally in alternate abutting layers of working and product tubes; in the embodiment shown, each spiral has about four and a half turns but need only have a single overlapping turn. However, as wall be understood, the greater the number of turns, the greater the resultant heat transfer. Heat passes from the air to the refrigerant primarily through. the fluid 11 but some heat is also transferred directly from theproduct. tubes 20 to the working tubes 15 by-virtue of their mutual contact. Flow of refrigerant in the:w;o#ii#.ttte spirals ts outward whereas flow of air in the product tubes is inward. Furthermore, flow in any portion of any tube is. opposite in direction to the flow in the abutting tube portion of an adjacent layer. In this way, as the air flows along the tubes 20 it is adjacen##t progressively cooler refrigerant resulting in greater efficiency of heat transfer. The air to be dried is passed into a precooler/ reheater heat exchanger shown schematically at 21 and thence to a distribution manifold 22, any condensate being drained away through a liquid trap 23. Pipes 25 passing through the bottom of the vessel feed the air from the manifold 22 to the spiral product tubes 20 and the cooled air travels out of the vessel 11 along output pipes 26 to a collection manifold 27 and thence along a pipe 31 to an air/ condensate separator 28. Condensate from the separator drains away through a trap 29 while the dried air passes out of the separator through a conduit 30 and through the heat exchanger 21 to emerge at B. It will be appreciated that the heat exchange in the exchanger 21 between the incoming wet air and the outgoing dry air causes the former to be precooled and the latter to be reheated. All joints between the pipes 25, 26 and manifolds 22, 27 respectively, between pipe 31 and separator28 and between conduit 33 and exchanger 21 are external and screw-threaded. The above embodiment of the invention has the advantage that due to the independent tubes for refrigerant and air all immersed in the heat transfer fluid, the air tubes may have small bores and therefore all joints in the air circuit can be screw-threaded. This allows easy inspection, maintenance and replacement of components. A further advantage is that the intermediate heat transfer fluid, such as glycol, in conjunction with the thermostat allows the air drier to be cycled according to demand, thus saving power costs at partial load conditions, and stabilizes the heat transfer process to control and maintain a minimum temperature of the air with minimum risk of freezing the condensate in the tubes.

Claims: CLAIMS 1. A heat exchanger for heating or cooling a product fluid, the exchanger comprising a vessel containing a heat transfer fluid, at least one generally flat spiral working tube at least partially immersed in the heat transfer fluid and having an inlet and an outlet for the passage therethrough of working fluid, and at least one generally flat spiral product tube at least partially immersed in the heat transfer fluid and having an inlet and an outlet for the passage therethrough of the product fluid, whereby heat may be transferred between the product fluid and the working fluid through the heat transfer fluid. 2. A heat exchanger as claimed in Claim 1 wherein there is a plurality of the working and/or product tubes and wherein the working and product tubes are arranged in alternate layers. 3. A heat exchanger as claimed in either Claim 1 or Claim 2 wherein the vessel has an annular interior containing the heat transfer fluid and tubes. 4. A heat exchanger as claimed in any preceding claim wherein the directions of flow in adjacent spirals are respectively inwardly and outwardly of the spirals. 5. A heat exchanger as claimed in any preceding claim wherein the tubes of adjacent spirals abut each other. 6. A heat exchanger as claimed in Claim 5 wherein the directions of flow in abutting tubes of adjacent spirals are in opposite sence. 7. A heat exchanger as claimed in any preceding claim wherein each spiral is orientated substantially horizontally. 8. A heat exchanger as claimed in any preceding claim further comprising pipes connected to the inlet and outlet of the or each working and/or product tube, which pipes pass through a lower wall or the bottom of the vessel. 9. A heat exchanger as claimed in Claim 8 wherein the vessel is a closed container. 10. A heat exchanger as claimed in any preceding claim for cooling the product fluid wherein the working fluid is a refrigerant contained in a refrigerating circuit of which the or each working tube forms part. 11. A heat exchanger as claimed in Calim 10 further comprising a thermostat responsive to the temperature of the cooled product fluid to control the refrigerating circuit to prevent freezing of condensate in the heat exchanger. 12. A heat exchanger as claimed in any preceding claim wherein the product fluid is air. 13. A gas dryer comprising a heat exchanger as claimed in Claim 11 or Claim 12, the product fluid being gas to be dryed, and a separator connected to the outlet of the or each product tube for separating condensate from the cooled gas. 14. A gas dryer as claimed in Claim 13 further comprising a second heat exchanger connected to the inlet of the or each product tube and to the separator for transferring heat from incoming gas to outgoing gas.

Inventors: PARRY, DAVID COLSTON, VERCAUTEREN, FRANCOIS-THEO
Applicants: RUSSELL FINEX LIMITED
Application year: 1982
Main classification: F28D7
IPC codes: B01D53, F25B39, F28D7