WO2003041841A1 - Liquid/gas state separating device - Google Patents

Liquid/gas state separating device Download PDF

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Publication number
WO2003041841A1
WO2003041841A1 PCT/IB2002/004735 IB0204735W WO03041841A1 WO 2003041841 A1 WO2003041841 A1 WO 2003041841A1 IB 0204735 W IB0204735 W IB 0204735W WO 03041841 A1 WO03041841 A1 WO 03041841A1
Authority
WO
WIPO (PCT)
Prior art keywords
liquid
vapour
separating device
gas state
state separating
Prior art date
Application number
PCT/IB2002/004735
Other languages
French (fr)
Inventor
Pierre Jeuch
Original Assignee
Thermagen
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Thermagen filed Critical Thermagen
Priority to DE60205770T priority Critical patent/DE60205770T2/en
Priority to US10/495,572 priority patent/US7390341B2/en
Priority to AT02781496T priority patent/ATE302640T1/en
Priority to EP02781496A priority patent/EP1448290B1/en
Publication of WO2003041841A1 publication Critical patent/WO2003041841A1/en

Links

Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B17/00—Sorption machines, plants or systems, operating intermittently, e.g. absorption or adsorption type
    • F25B17/08—Sorption machines, plants or systems, operating intermittently, e.g. absorption or adsorption type the absorbent or adsorbent being a solid, e.g. salt
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D45/00—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
    • B01D45/04—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by utilising inertia
    • B01D45/06—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by utilising inertia by reversal of direction of flow
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2400/00—General features or devices for refrigeration machines, plants or systems, combined heating and refrigeration systems or heat-pump systems, i.e. not limited to a particular subgroup of F25B
    • F25B2400/11—Drop catchers

Definitions

  • the present invention relates to a liquid/gas state separating device capable of separating molecules of vapour of a liquid from drops of said liquid.
  • Such a separator is intended to be used in a heat exchanger for implementing cooling of a beverage by an evaporation and adsorption method.
  • the principle of such a cooling method consists of evaporating a liquid under the effect of a partial vacuum maintained by adsorption of the vapours of said liquid.
  • a refrigerant liquid contained in a heat exchanger is evaporated under vacuum. This evaporation is initiated by a partial vacuum brought about in the exchanger by activation of means of putting the heat exchanger into communication with pumping means, and then this partial vacuum is maintained by pumping the vapours of said liquid.
  • the molecules of vapour of the refrigerant liquid are pumped and drops of said liquid can be carried along by the vapour.
  • the pumping force can be such that drops of liquid L can be carried along to the pump and thus prejudice its correct operation.
  • An evaporator 12 contains a liquid 18 evaporated by pumping by means of desiccants contained in a chamber 20.
  • a mixture of vapour and liquid is thus drawn into a collector and liquid/gas state separator 34 of conventional design which separates the liquid carried along by the pumped vapours.
  • the collector and state separator 34 has a outlet pipe 38 which returns the drops of liquid to the evaporator 12 and a conduit 28 which opens a way for the vapour to the desiccant chamber 20.
  • the present invention proposes a miniaturised liquid/gas state separating device capable of being inserted into a heat exchanger disposed in a beverage package, such as a standardised can for example. More particularly, the invention relates to a liquid/gas state separating device capable of separating the molecules of vapour of a liquid evaporating under the effect of a partial vacuum maintained by pumping means from drops of said liquid carried along by the flow of vapour, characterised in that it comprises a vapour deflector and a drop collector, the vapour deflector imposing at least one sudden change of direction on the flow of vapour.
  • the drop collector comprises at least one outlet pipe for the drops of length greater than or equal to the pressure loss of the vapour in the deflector.
  • a sudden change of direction of the flow of vapour is an upward movement.
  • the total volume of said device is less than or equal to 20 cm 3 .
  • the drop collector comprises a funnel, the solid angle of which includes the partial vacuum source and the vapour deflector.
  • the vapour deflector comprises at least one wall forming a zigzag, said wall being disposed around the partial vacuum source and inside the solid angle formed by the drop collector.
  • the funnel constitutes a zigzag wall of the vapour deflector.
  • the device also comprises protection from direct splashes of drops, said protection being disposed opposite the partial vacuum source.
  • the device is made of plastic or metal.
  • the device is disposed in a heat exchanger containing a refrigerant liquid capable of evaporating under the effect of a partial vacuum maintained by pumping means associated with said exchanger.
  • the pumping means are chosen from amongst the means constituted by an adsorbent material packed under air vacuum, a mechanical vacuum pump, and a cryogenic vacuum pump.
  • - Figure 1 already described, is a diagram of a known self-cooling device for beverages of the prior art; - Figure 2 illustrates schematically the state separating device according to the invention.
  • This device comprises a vapour deflector 50 and a drop collector 60.
  • This device can be integrated into a heat exchanger 2 containing a refrigerant liquid L capable of evaporating under the effect of a partial vacuum 31 maintained by pumping means 3.
  • the pumping means are associated with the heat exchanger 2 and can consist, according to application, of a mechanical vacuum pump, or cryogenic pumping means such as cold traps which condense the water vapours, or else an evacuated cartridge containing reagents (desiccants) capable of activating and maintaining the adsorption of the refrigerant liquid L.
  • a mechanical vacuum pump or cryogenic pumping means such as cold traps which condense the water vapours, or else an evacuated cartridge containing reagents (desiccants) capable of activating and maintaining the adsorption of the refrigerant liquid L.
  • the state separating device has a vapour deflector 50 which consists of at least one wall forming a zigzag 51 imposing one or more sudden changes of direction on the flow of vapour V, preferably from the downward direction to the upward direction.
  • the vapour molecules have a very small mean free path, of the order of a micrometre, which means they can change direction very quickly.
  • the drops of liquid have a mass such that they are carried along by their inertia and thus separated from the gaseous flow. This mechanism advantageously allows liquid/gas separation without significant slowing down of the flow of vapour V and therefore does not require the occupation of a large volume.
  • the state separating device also has, in addition, a drop collector 60 making it possible to take the drops of liquid L separated from the gaseous flow of vapour V back to the bottom of the cavity of the evaporator 2.
  • the collector 60 comprises- a funnel 61 and at least one outlet pipe 62 for the drops.
  • the funnel 61 can advantageously contribute towards forming the zigzag 51 of the vapour deflector 50.
  • the vapour deflector 50 is advantageously disposed around the partial vacuum source 31 and the funnel 61 of the drop collector
  • 60 defines a solid angle which includes the partial vacuum source 31 and the vapour deflector 50.
  • the collector 60 can be connected to the wall of the heat exchanger 2 by webs for example which constitute thin partitions allowing passage of the vapour V while holding the piece of the funnel 61 in position.
  • the collector can also be held immovably attached to the zigzag 51.
  • the funnel 61 then extends as far as the wall of the heat exchanger 2 containing the partial vacuum source 31 and has louvres allowing passage of the vapour V to the pumping means 3.
  • the outlet pipe for the drops 62 has a length greater than or equal to the pressure loss of the vapour V in the zigzag 51 in order to avoid the splashing of drops L through said outlet pipe 62.
  • This pressure loss is advantageously measured as a water volume height. If, for example, a pressure loss of the vapour V of 1 mb (corresponding to 1 cm water column height) is considered, the pipe will be at least 1 cm long.
  • the state separating device also comprises protection 55 from direct splashes of drops which completes the vapour deflector 50.
  • This protection 55 is disposed opposite the partial vacuum source 31 in order to avoid direct contamination of the pumping means 3 in particular upon initiation of the adsorption reaction.
  • the liquid/gas state separating device according to the invention makes it possible to achieve the miniaturisation constraints required for applications to beverage packages in that the total volume of said device is less than or equal to 20 cm 3 .
  • the state separating device according to the invention can be constituted in plastic material, by moulding, which allows great freedom of shape, or in metal of the same kind as the heat exchanger in which it is disposed, such as aluminium or steel for example, in order to facilitate recycling of the package.

Abstract

The invention relates to a liquid/gas state separating device capable of separating the molecules of vapour (V) of a liquid evaporating under the effect of a partial vacuum (31) maintained by pumping means from drops (L) of said liquid carried along by the flow of vapour (V), characterised in that it comprises a vapour deflector (50) and a drop collector (60), the vapour deflector (50) imposing at least one sudden change of direction on the flow of vapour (V).

Description

LIQUID/GAS STATE SEPARATING DEVICE
The present invention relates to a liquid/gas state separating device capable of separating molecules of vapour of a liquid from drops of said liquid.
Such a separator is intended to be used in a heat exchanger for implementing cooling of a beverage by an evaporation and adsorption method. The principle of such a cooling method consists of evaporating a liquid under the effect of a partial vacuum maintained by adsorption of the vapours of said liquid.
The implementation of this method of cooling by evaporation and adsorption is known and has been the subject of much research in the prior art. Many devices have been proposed, associating a heat exchanger
(evaporator) containing a refrigerant liquid to be evaporated and a reservoir containing an adsorbent, in particular for applications to self-cooling beverage packages. According to the physical principle implemented, a refrigerant liquid contained in a heat exchanger is evaporated under vacuum. This evaporation is initiated by a partial vacuum brought about in the exchanger by activation of means of putting the heat exchanger into communication with pumping means, and then this partial vacuum is maintained by pumping the vapours of said liquid. Thus, the molecules of vapour of the refrigerant liquid are pumped and drops of said liquid can be carried along by the vapour. In fact, the pumping force can be such that drops of liquid L can be carried along to the pump and thus prejudice its correct operation. It is not impossible for the vapour molecules pumped by the partial vacuum to reach a speed of 1000 km/h. It is therefore necessary to provide a liquid/gas state separator which allows passage of the vapour of the refrigerant liquid to be pumped and which returns the drops of liquid into the evaporator of the heat exchanger.
The problem of separation between the vapours and the drops of refrigerant liquid has clearly been identified within the context of applications to self- cooling packages, in particular in the patent US 5 018 368, an illustration of which is given in Figure 1. An evaporator 12 contains a liquid 18 evaporated by pumping by means of desiccants contained in a chamber 20. A mixture of vapour and liquid is thus drawn into a collector and liquid/gas state separator 34 of conventional design which separates the liquid carried along by the pumped vapours. The collector and state separator 34 has a outlet pipe 38 which returns the drops of liquid to the evaporator 12 and a conduit 28 which opens a way for the vapour to the desiccant chamber 20.
This patent clearly identifies the problem of separation of the vapours and drops of the refrigerant liquid, but the solution proposed is a conventional solution known to any chemist confronted with a similar problem. In fact, the solution described in this patent uses an intermediate receptacle of significant volume in which the pumped vapour is considerably slowed down. The drops of refrigerant liquid which would have been carried along by the vapour are thus separated from the vapour molecules by the effect of gravity since the speed of flow of the vapour is no longer sufficient to carry them along against the force of gravity. The liquid thus collected is taken back into the cavity of the evaporator by the outlet pipe 38. The implementation of this solution requires a non- negligible volume. However, such a conventional solution is not directly applicable to a self-cooling beverage package having standardised shapes and dimensions, of a beverage can for example. This is because the miniaturisation of a state separating device is difficult to obtain on account of the conventional solutions being based on the use of a relatively large volume which allows a natural separation of the drops drawn by gravitational force from the gas molecules drawn by the partial vacuum. The subsequent developments originating from the mentioned patent US 5 018 368 have furthermore shown that persons skilled in the art had turned towards an evaporator containing a refrigerant gel for applications to packages of small dimensions, as for example described in the patents WO 00/50824 and WO 01/10738 concerning respectively a method of producing the gel and the use of such a gel for developing a heat exchanger.
The objective of the present invention is to resolve the drawbacks of the prior art. To that end, the present invention proposes a miniaturised liquid/gas state separating device capable of being inserted into a heat exchanger disposed in a beverage package, such as a standardised can for example. More particularly, the invention relates to a liquid/gas state separating device capable of separating the molecules of vapour of a liquid evaporating under the effect of a partial vacuum maintained by pumping means from drops of said liquid carried along by the flow of vapour, characterised in that it comprises a vapour deflector and a drop collector, the vapour deflector imposing at least one sudden change of direction on the flow of vapour.
According to one characteristic, the drop collector comprises at least one outlet pipe for the drops of length greater than or equal to the pressure loss of the vapour in the deflector.
According to one characteristic, a sudden change of direction of the flow of vapour is an upward movement. According to one advantageous characteristic, the total volume of said device is less than or equal to 20 cm3.
According to one characteristic, the drop collector comprises a funnel, the solid angle of which includes the partial vacuum source and the vapour deflector.
According to one characteristic, the vapour deflector comprises at least one wall forming a zigzag, said wall being disposed around the partial vacuum source and inside the solid angle formed by the drop collector. According to one advantageous embodiment, the funnel constitutes a zigzag wall of the vapour deflector.
According to one embodiment, the device also comprises protection from direct splashes of drops, said protection being disposed opposite the partial vacuum source.
According to embodiment, the device is made of plastic or metal.
According to one application, the device is disposed in a heat exchanger containing a refrigerant liquid capable of evaporating under the effect of a partial vacuum maintained by pumping means associated with said exchanger.
According to embodiment, the pumping means are chosen from amongst the means constituted by an adsorbent material packed under air vacuum, a mechanical vacuum pump, and a cryogenic vacuum pump.
Other features and advantages of the present invention will emerge in the course of the following description given by way of an illustrative and non- limitative example, and produced with reference to the figures in which:
- Figure 1, already described, is a diagram of a known self-cooling device for beverages of the prior art; - Figure 2 illustrates schematically the state separating device according to the invention.
The liquid/gas state separating device according to the invention, illustrated schematically in Figure
2, comprises a vapour deflector 50 and a drop collector 60. This device can be integrated into a heat exchanger 2 containing a refrigerant liquid L capable of evaporating under the effect of a partial vacuum 31 maintained by pumping means 3.
The pumping means are associated with the heat exchanger 2 and can consist, according to application, of a mechanical vacuum pump, or cryogenic pumping means such as cold traps which condense the water vapours, or else an evacuated cartridge containing reagents (desiccants) capable of activating and maintaining the adsorption of the refrigerant liquid L.
The state separating device according to the invention has a vapour deflector 50 which consists of at least one wall forming a zigzag 51 imposing one or more sudden changes of direction on the flow of vapour V, preferably from the downward direction to the upward direction. The vapour molecules have a very small mean free path, of the order of a micrometre, which means they can change direction very quickly. On the other hand, the drops of liquid have a mass such that they are carried along by their inertia and thus separated from the gaseous flow. This mechanism advantageously allows liquid/gas separation without significant slowing down of the flow of vapour V and therefore does not require the occupation of a large volume. The state separating device according to the invention also has, in addition, a drop collector 60 making it possible to take the drops of liquid L separated from the gaseous flow of vapour V back to the bottom of the cavity of the evaporator 2. The collector 60 comprises- a funnel 61 and at least one outlet pipe 62 for the drops. The funnel 61 can advantageously contribute towards forming the zigzag 51 of the vapour deflector 50.
According to one advantageous embodiment, the vapour deflector 50 is advantageously disposed around the partial vacuum source 31 and the funnel 61 of the drop collector
60 defines a solid angle which includes the partial vacuum source 31 and the vapour deflector 50.
The collector 60 can be connected to the wall of the heat exchanger 2 by webs for example which constitute thin partitions allowing passage of the vapour V while holding the piece of the funnel 61 in position. The collector can also be held immovably attached to the zigzag 51. The funnel 61 then extends as far as the wall of the heat exchanger 2 containing the partial vacuum source 31 and has louvres allowing passage of the vapour V to the pumping means 3.
Preferentially, the outlet pipe for the drops 62 has a length greater than or equal to the pressure loss of the vapour V in the zigzag 51 in order to avoid the splashing of drops L through said outlet pipe 62. This pressure loss is advantageously measured as a water volume height. If, for example, a pressure loss of the vapour V of 1 mb (corresponding to 1 cm water column height) is considered, the pipe will be at least 1 cm long.
According to one advantageous feature, the state separating device according to the invention also comprises protection 55 from direct splashes of drops which completes the vapour deflector 50. This protection 55 is disposed opposite the partial vacuum source 31 in order to avoid direct contamination of the pumping means 3 in particular upon initiation of the adsorption reaction.
The liquid/gas state separating device according to the invention makes it possible to achieve the miniaturisation constraints required for applications to beverage packages in that the total volume of said device is less than or equal to 20 cm3.
In the case of an application to self-cooling beverage packages, the state separating device according to the invention can be constituted in plastic material, by moulding, which allows great freedom of shape, or in metal of the same kind as the heat exchanger in which it is disposed, such as aluminium or steel for example, in order to facilitate recycling of the package.

Claims

1. A liquid/gas state separating device capable of separating the molecules of vapour (V) of a liquid evaporating under the effect of a partial vacuum (31) maintained by pumping means from drops (L) of said liquid carried along by the flow of vapour (V) , characterised in that it comprises a vapour deflector (50) and a drop collector (60), the vapour deflector (50) imposing at least one sudden change of direction on the flow of vapour (V) .
2. A liquid/gas state separating device according to Claim 1, characterised in that the drop collector (60) comprises at least one outlet pipe for the drops (62) of length greater than or equal to the pressure loss of the vapour (V) in the deflector (50) .
3. A liquid/gas state separating device according to one of the preceding claims, characterised in that a sudden change of direction of the flow of vapour (V) is an upward movement.
4. A liquid/gas state separating device according to one of the preceding claims, characterised in that the total volume of said device is less than or equal to 20 cm3.
5. A liquid/gas state separating device according to one of the preceding claims, characterised in that the drop collector (60) comprises a funnel (61) , the solid angle of which includes the partial vacuum source (31) and the vapour deflector (50) .
6. A liquid/gas state separating device according to one of the preceding claims, characterised in that the vapour deflector (50) comprises at least one wall forming a zigzag (51), said wall (51) being disposed around the partial vacuum source (31) and inside the solid angle formed by the drop collector (60) .
7. A liquid/gas state separating device according to Claims 5 and 6, characterised in that the funnel
(61) constitutes a zigzag wall (51) of the vapour deflector (50) .
8. A liquid/gas state separating device according to one of the preceding claims, characterised in that it also comprises protection (55) from direct splashes of drops (L) , said protection (55) being disposed opposite the partial vacuum source (31) .
9. A liquid/gas state separating device according to one of Claims 1 to 8, characterised in that it is made of plastic.
10. A liquid/gas state separating device according to one of Claims 1 to 8, characterised in that it is made of metal.
11. A liquid/gas state separating device according to one of the preceding claims, characterised in that it is disposed in a heat exchanger (2) containing a refrigerant liquid (L) capable of evaporating under the effect of a partial vacuum (31) maintained by pumping means associated with said exchanger.
12. A liquid/gas state separating device according to one of the preceding claims, characterised in that the pumping means are chosen from amongst the means constituted by an adsorbent material packed under air vacuum, a mechanical vacuum pump, and a cryogenic vacuum pump.
PCT/IB2002/004735 2001-11-16 2002-11-13 Liquid/gas state separating device WO2003041841A1 (en)

Priority Applications (4)

Application Number Priority Date Filing Date Title
DE60205770T DE60205770T2 (en) 2001-11-16 2002-11-13 EVAPORATOR WITH LIQUID / GAS DISCONNECTOR
US10/495,572 US7390341B2 (en) 2001-11-16 2002-11-13 Liquid/gas state separating device
AT02781496T ATE302640T1 (en) 2001-11-16 2002-11-13 EVAPORATOR WITH LIQUID/GASE SEPARATOR
EP02781496A EP1448290B1 (en) 2001-11-16 2002-11-13 Evaporator with liquid/gas state separating device

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FR01/14853 2001-11-16
FR0114853A FR2832325B1 (en) 2001-11-16 2001-11-16 LIQUID-GAS STATE SEPARATOR

Publications (1)

Publication Number Publication Date
WO2003041841A1 true WO2003041841A1 (en) 2003-05-22

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Family Applications (1)

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PCT/IB2002/004735 WO2003041841A1 (en) 2001-11-16 2002-11-13 Liquid/gas state separating device

Country Status (6)

Country Link
US (1) US7390341B2 (en)
EP (1) EP1448290B1 (en)
AT (1) ATE302640T1 (en)
DE (1) DE60205770T2 (en)
FR (1) FR2832325B1 (en)
WO (1) WO2003041841A1 (en)

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EP1448290A1 (en) 2004-08-25
FR2832325A1 (en) 2003-05-23
ATE302640T1 (en) 2005-09-15
DE60205770T2 (en) 2006-05-18
US7390341B2 (en) 2008-06-24
DE60205770D1 (en) 2005-09-29
EP1448290B1 (en) 2005-08-24
US20040261380A1 (en) 2004-12-30
FR2832325B1 (en) 2004-09-10

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