EP1015832B1 - Apparatus for recovering the cooling fluid of heat exchange circuits - Google Patents
Apparatus for recovering the cooling fluid of heat exchange circuits Download PDFInfo
- Publication number
- EP1015832B1 EP1015832B1 EP97928433A EP97928433A EP1015832B1 EP 1015832 B1 EP1015832 B1 EP 1015832B1 EP 97928433 A EP97928433 A EP 97928433A EP 97928433 A EP97928433 A EP 97928433A EP 1015832 B1 EP1015832 B1 EP 1015832B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- cooling
- cooling tower
- operating fluid
- air
- condenser
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28B—STEAM OR VAPOUR CONDENSERS
- F28B1/00—Condensers in which the steam or vapour is separate from the cooling medium by walls, e.g. surface condenser
- F28B1/06—Condensers in which the steam or vapour is separate from the cooling medium by walls, e.g. surface condenser using air or other gas as the cooling medium
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D5/00—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, using the cooling effect of natural or forced evaporation
Definitions
- This invention has for object an apparatus for recovering the cooling fluid of heat exchange circuits.
- the innovation finds particular even if not exclusive application in the field of fluids recovering (oil water, etc.) of heat exchange circuits in machines of the industrial technique as for example machines for the ice-cream production or machines for the moulding of plastics material (dies cooling), etc.
- the fluids utilised for the cooling generally come out at a temperature higher than the average environmental one E.g. 35-40°C so that their effective cooling is important for a suitable recalculation obtained with minimum dimensions and suitable efficiency.
- the temperature of said fluid is lowered to a not very high level and generally a little higher than the environment air temperature.
- the temperature of the fluid can be lowered from 35-40°C to a value not lower than 20°C. or at the maximum in its inside or little less (by using the evaporative system).
- the temperature at which it is possible to recover the water cannot get lower than the temperature of the damp bulb of the utilised air.
- the temperature of the damp bulb is about 24-25°C so that the cooling is notoriously limited.
- the temperature by which it is possible to recover the water cannot get lower than the temperature of the dry bulb of the utilised air and therefore the lowering of temperature is more limited.
- the aim of this invention is to avoid the above-mentioned drawbacks by creating an apparatus that is able to supply a more cooling efficacy to the said operating fluids (heat exchange) in said main operative machines.
- Figure 1 is a schematic view of a simplified system according to the invention, in this specific case with a single condenser radiator for cooling operating water by a not-evaporative external system.
- Figure 2 is a view of a solution with double radiator of the condenser and use of evaporative external system.
- the freezing circuit inserted in the system, which innovatively places the condenser (7) or more condensers (7, 19), as inlet of the airflow, at the beginning of the cooling tower, and the evaporator (9) at the end of the cooling tower to cool further the operating fluid, by means of the connection 5 before of the discharging and recirculation in the main operating machine (6).
- the air is heated at Tm>Ta getting through the condenser means (7) drying.
- the efficiency of the heat exchanges in 7 and 8 may be improved by using an external evaporative system Eg. by water spraying (15,16).
- the tower 8 can also use an evaporative system.
- the operating fluid Before being discharged the operating fluid is made pass through the evaporator 9 of the freezing circuit, thus obtaining its further cooling at a temperature Tu ⁇ Te.
- the outlet temperature Tu in this way can reach values also extremely low with respect to the ambient temperature and get to about 0° C.
- Fig.2 the rain-like or spraying evaporative system for improving the exchange by, an intermediate collector (13) that collects the discharge of the water from rain or spray both from the condenser (19-17) and from the cooling tower (8,12), to then be made recirculate by a pump (14) respectively above the condenser (16) and over the tower (15).
- an intermediate collector (13) that collects the discharge of the water from rain or spray both from the condenser (19-17) and from the cooling tower (8,12), to then be made recirculate by a pump (14) respectively above the condenser (16) and over the tower (15).
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
- Compression-Type Refrigeration Machines With Reversible Cycles (AREA)
- Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
- Devices That Are Associated With Refrigeration Equipment (AREA)
- Heat Treatments In General, Especially Conveying And Cooling (AREA)
Abstract
Description
- This invention has for object an apparatus for recovering the cooling fluid of heat exchange circuits.
- The innovation finds particular even if not exclusive application in the field of fluids recovering (oil water, etc.) of heat exchange circuits in machines of the industrial technique as for example machines for the ice-cream production or machines for the moulding of plastics material (dies cooling), etc.
- It is known that in prior art there are many types of machines which use, fluid cooled circuits, in particular water or oil.
- The fluids utilised for the cooling generally come out at a temperature higher than the average environmental one E.g. 35-40°C so that their effective cooling is important for a suitable recalculation obtained with minimum dimensions and suitable efficiency.
- In prior art, exist already apparatuses of such type, which are built substantially as a cooling tower involving the recalculation of the operating fluid come out from the main machine subjecting it to a heat exchange by a passage through a forced air-jet, also by using the evaporative system.
- In this way the temperature of said fluid is lowered to a not very high level and generally a little higher than the environment air temperature. For example if the environment air is at 20°C the temperature of the fluid can be lowered from 35-40°C to a value not lower than 20°C. or at the maximum in its inside or little less (by using the evaporative system).
- This fact involves the drawback that the heat exchange efficacy inside of the main machine (E.g. machine from ice-cream machine of pressure-injection for plastics materials, etc.) is rather reduced.
- In the cooling towers and in the air water exchangers of the evaporative type in general, the temperature at which it is possible to recover the water cannot get lower than the temperature of the damp bulb of the utilised air.
- Normally, in the summer months, it is calculated that the temperature of the damp bulb is about 24-25°C so that the cooling is notoriously limited.
- In the water-air exchangers of the non-evaporative type (for example finned dry exchangers), the temperature by which it is possible to recover the water cannot get lower than the temperature of the dry bulb of the utilised air and therefore the lowering of temperature is more limited.
- The aim of this invention is to avoid the above-mentioned drawbacks by creating an apparatus that is able to supply a more cooling efficacy to the said operating fluids (heat exchange) in said main operative machines.
- This and other aims are reached as claimed by means of an apparatus that includes cooling tower means by air-jets, for the cooling of operating fluids circulating by heat exchange in main operative machines, of the type involving:
- at least one inlet of said operating fluid heated by the heat exchange in said main machine and
- at least one coupling for the re-inlet of said operating fluid, suitably cooled by means of said cooling tower means, in the recalculation system of said main machine, characterised in that in it is included at least one freezing circuit with evaporators means and condenser means, in which:
- said condenser means are put at the beginning of said cooling tower means for exchanging heat with the said air-low, before it covers said cooling tower means;
- said evaporators means are put at the end of said cooling tower means for exchanging heat with said operating fluid for its further cooling.
- In this way it is obtained a considerable higher yield being possible to bring the operating temperature also to extremely low and lower than the environment temperature values.
- These and other advantages will appear from the following description of two preferred embodiments, with the aid of the included drawings whose details are not to be considered as limitative but only given as an example.
- Figure 1 is a schematic view of a simplified system according to the invention, in this specific case with a single condenser radiator for cooling operating water by a not-evaporative external system.
- Figure 2 is a view of a solution with double radiator of the condenser and use of evaporative external system.
- Referring to the figures it is possible to notice that with 1, 2 and 3 is shown the flow of the cooling air, while is not shown the fan in compression or suction that determines such flow being this latter of prior art.
- With 11 is shown the equipment's container.
- With 4 and 6 are respectively shown the couplings for the operating water inlet and outlet (or other fluid) from the main machine (Eg. Machine for ice-cream not shown).
- With 8 is shown the cooling tower of prior art, for the cooling of the operating fluid 4-6.
- With 10 is shown the freezing circuit inserted in the system, which innovatively places the condenser (7) or more condensers (7, 19), as inlet of the airflow, at the beginning of the cooling tower, and the evaporator (9) at the end of the cooling tower to cool further the operating fluid, by means of the connection 5 before of the discharging and recirculation in the main operating machine (6).
- A work example results from the parameters indicated in the figure on the respective temperatures where:
- When the air gets in from the outside 1 the temperature is the environmental one Ta.
- The air is heated at Tm>Ta getting through the condenser means (7) drying.
- In the meantime when it gets in 4 the operating fluid has a temperature Te>Tm and consequently in the tower 8 this operating fluid is cooled at a certain value, while the air exits from the opposite side at a temperature TF>Tm.
- The efficiency of the heat exchanges in 7 and 8 may be improved by using an external evaporative system Eg. by water spraying (15,16). The tower 8 can also use an evaporative system.
- Before being discharged the operating fluid is made pass through the evaporator 9 of the freezing circuit, thus obtaining its further cooling at a temperature Tu<Te.
- The outlet temperature Tu in this way can reach values also extremely low with respect to the ambient temperature and get to about 0° C.
- In the solution of Fig.2 is indicated the rain-like or spraying evaporative system for improving the exchange by, an intermediate collector (13) that collects the discharge of the water from rain or spray both from the condenser (19-17) and from the cooling tower (8,12), to then be made recirculate by a pump (14) respectively above the condenser (16) and over the tower (15).
- The space 18 between the two condensers will make possible that in the condenser group there is more heat exchange efficiency as in the second condenser (19) is utilized the evaporation of the water from external wetting (16).
Claims (8)
- Apparatus that includes cooling tower means (8) by air-jet (1), for the cooling of operating fluids circulating by heat exchange in main operative machines (4), of the type involving:- at least one inlet of said operating fluid heated by the heat exchange in the said main machine (4) and- at least one coupling for the re-immission of said operating fluid, suitably cooled by means of said cooling tower means (8), in the recirculation system of said main machine (6),characterised in that in it is included at least one freezing circuit with evaporators means (9) and condenser means (7), in which:said condenser means (7) are put at the beginning of said cooling tower means (8) for exchanging heat with said air-flow (1-2), before it surrounds said cooling tower means (8) for a first cooling of the said operating fluid;said evaporators means (9) are put at the end (5) of said cooling tower means (8), for exchanging heat with said operating fluid for its further cooling (6).
- Apparatus according to claim 1., characterised in that said condensers means are at least in number of two (7,19), placed in parallel and crossed by said cooling air flow (1,2,3).
- Apparatus according to any one of the previous claims, characterised in that said operating fluid (4) is let fall or sprayed in said cooling tower and covered by said air-flow (2,3) for being subjected to evaporation.
- Apparatus according to any one of the previous claims, characterised in that said cooling tower means involve a canalization of said operating fluid.
- Apparatus according to any one of the previous claims, characterised in that at least one of said condenser means (7,19) is subjected to water rain or spraying during the covering by the cooling air-flow (1,2).
- Apparatus according to the previous claim, characterised in that the condenser means subjected to wetting is a second condenser means (19) placed at the end of a first dry one (7) in parallel.
- Apparatus according to any one of the previous claims, characterised in that said cooling tower means (8) are subjected to water rain-like or spraying during the covering by the cooling air-flow (2,3).
- Apparatus according to any one of the previous claims, characterised in that with the system is associated a rain-like or spraying wetting circuit that includes a collector (13) from condenser means (17) and from tower means (12) and recirculation means (14) for wetting again (16,15) said condensers means (19) and for exchanging heat of said tower (8).
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
IT96UD000197A IT1289004B1 (en) | 1996-10-16 | 1996-10-16 | APPARATUS FOR THE RECOVERY OF COOLING FLUID FROM HEAT EXCHANGE CIRCUITS |
ITUD960197 | 1996-10-16 | ||
PCT/IT1997/000144 WO1998016785A1 (en) | 1996-10-16 | 1997-06-20 | Apparatus for recovering the cooling fluid of heat exchange circuits |
Publications (2)
Publication Number | Publication Date |
---|---|
EP1015832A1 EP1015832A1 (en) | 2000-07-05 |
EP1015832B1 true EP1015832B1 (en) | 2001-09-19 |
Family
ID=11422210
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP97928433A Expired - Lifetime EP1015832B1 (en) | 1996-10-16 | 1997-06-20 | Apparatus for recovering the cooling fluid of heat exchange circuits |
Country Status (7)
Country | Link |
---|---|
EP (1) | EP1015832B1 (en) |
JP (1) | JP2001502410A (en) |
AT (1) | ATE205935T1 (en) |
AU (1) | AU3273297A (en) |
DE (1) | DE69706892T2 (en) |
IT (1) | IT1289004B1 (en) |
WO (1) | WO1998016785A1 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US9476648B2 (en) | 2014-01-21 | 2016-10-25 | Drexel University | Systems and methods of using phase change material in power plants |
US10890383B2 (en) | 2014-01-21 | 2021-01-12 | Drexel University | Systems and methods of using phase change material in power plants |
Family Cites Families (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2353233A (en) * | 1941-06-04 | 1944-07-11 | Curtis Mfg Co | Heat exchanger |
FR2370859A1 (en) * | 1976-11-12 | 1978-06-09 | Terrier Andre | Closed circuit cooling system for electric generator - has water injected into cooling air to increase heat transfer |
JPH02290484A (en) * | 1989-07-20 | 1990-11-30 | Hitachi Metals Ltd | Operating method of cooling apparatus |
JPH0763457A (en) * | 1993-08-24 | 1995-03-10 | Hitachi Metals Ltd | Cooling apparatus |
DE9313290U1 (en) * | 1993-09-03 | 1993-11-18 | Hans Güntner GmbH, 82256 Fürstenfeldbruck | Liquid recooler |
-
1996
- 1996-10-16 IT IT96UD000197A patent/IT1289004B1/en active IP Right Grant
-
1997
- 1997-06-20 AT AT97928433T patent/ATE205935T1/en not_active IP Right Cessation
- 1997-06-20 EP EP97928433A patent/EP1015832B1/en not_active Expired - Lifetime
- 1997-06-20 DE DE69706892T patent/DE69706892T2/en not_active Expired - Lifetime
- 1997-06-20 AU AU32732/97A patent/AU3273297A/en not_active Abandoned
- 1997-06-20 JP JP10518155A patent/JP2001502410A/en active Pending
- 1997-06-20 WO PCT/IT1997/000144 patent/WO1998016785A1/en active IP Right Grant
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US9476648B2 (en) | 2014-01-21 | 2016-10-25 | Drexel University | Systems and methods of using phase change material in power plants |
US10890383B2 (en) | 2014-01-21 | 2021-01-12 | Drexel University | Systems and methods of using phase change material in power plants |
Also Published As
Publication number | Publication date |
---|---|
EP1015832A1 (en) | 2000-07-05 |
ATE205935T1 (en) | 2001-10-15 |
DE69706892D1 (en) | 2001-10-25 |
JP2001502410A (en) | 2001-02-20 |
AU3273297A (en) | 1998-05-11 |
DE69706892T2 (en) | 2002-04-25 |
ITUD960197A1 (en) | 1998-04-16 |
WO1998016785A1 (en) | 1998-04-23 |
IT1289004B1 (en) | 1998-09-25 |
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