WO1989000667A1 - Dispositif d'evacuation et de mise en bouteilles de fluides - Google Patents

Dispositif d'evacuation et de mise en bouteilles de fluides Download PDF

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Publication number
WO1989000667A1
WO1989000667A1 PCT/EP1988/000603 EP8800603W WO8900667A1 WO 1989000667 A1 WO1989000667 A1 WO 1989000667A1 EP 8800603 W EP8800603 W EP 8800603W WO 8900667 A1 WO8900667 A1 WO 8900667A1
Authority
WO
WIPO (PCT)
Prior art keywords
line
connection
condenser
filling device
fluid filling
Prior art date
Application number
PCT/EP1988/000603
Other languages
German (de)
English (en)
Inventor
Hans-Günter Schmidt
Original Assignee
Alfred Teves Gmbh
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 Alfred Teves Gmbh filed Critical Alfred Teves Gmbh
Publication of WO1989000667A1 publication Critical patent/WO1989000667A1/fr
Priority to FI890739A priority Critical patent/FI890739A/fi
Priority to NO891018A priority patent/NO169620C/no
Priority to DK116389A priority patent/DK116389D0/da

Links

Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C5/00—Methods or apparatus for filling containers with liquefied, solidified, or compressed gases under pressures
    • F17C5/02—Methods or apparatus for filling containers with liquefied, solidified, or compressed gases under pressures for filling with liquefied gases
    • 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
    • F25B45/00—Arrangements for charging or discharging refrigerant
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2201/00—Vessel construction, in particular geometry, arrangement or size
    • F17C2201/01—Shape
    • F17C2201/0104—Shape cylindrical
    • F17C2201/0109—Shape cylindrical with exteriorly curved end-piece
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2205/00—Vessel construction, in particular mounting arrangements, attachments or identifications means
    • F17C2205/03—Fluid connections, filters, valves, closure means or other attachments
    • F17C2205/0302—Fittings, valves, filters, or components in connection with the gas storage device
    • F17C2205/0323—Valves
    • F17C2205/0335—Check-valves or non-return valves
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2223/00—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel
    • F17C2223/01—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel characterised by the phase
    • F17C2223/0146—Two-phase
    • F17C2223/0153—Liquefied gas, e.g. LPG, GPL
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2227/00—Transfer of fluids, i.e. method or means for transferring the fluid; Heat exchange with the fluid
    • F17C2227/01—Propulsion of the fluid
    • F17C2227/0128—Propulsion of the fluid with pumps or compressors
    • F17C2227/0135—Pumps
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2227/00—Transfer of fluids, i.e. method or means for transferring the fluid; Heat exchange with the fluid
    • F17C2227/03—Heat exchange with the fluid
    • F17C2227/0337—Heat exchange with the fluid by cooling
    • 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
    • F25B2345/00—Details for charging or discharging refrigerants; Service stations therefor
    • F25B2345/002—Collecting refrigerant from a cycle

Definitions

  • the invention relates to a fluid filling device according to the preamble of patent claim 1.
  • the fluids used for example, in refrigeration systems, such as air conditioning units, cooling devices, car air conditioning systems and the like, or in hydraulic systems, such as brake systems, cause environmental pollution, such as Damage to the ozone layer or groundwater if they are simply released into the atmosphere. It is therefore important that appropriate disposal is carried out when e.g. B. Refrigerant and oil can be removed from the refrigeration systems. For this purpose, it is regularly filled into transport containers, e.g. Bottles, necessary.
  • Refrigerant pumps are known, but with which only liquid refrigerant can be pumped.
  • suction devices for refrigerants are already known, with which the refrigerant can be sucked off before working on refrigeration systems.
  • These known suction devices have one Compressor open and a downstream condenser in which the hot gas leaving the compressor is subcooled and liquefied.
  • the filling operation with these suction devices is, however, relatively complicated.
  • These suction devices can only suck the refrigerant in gaseous form and the cooling oils can only be transported out to a limited extent. Furthermore, no automatic measures have been taken to prevent the transport containers from being overfilled.
  • the invention is therefore based on the object of improving a fluid filling device according to the preamble of patent claim 1 in such a way that the filling process is simplified with a simple and inexpensive construction.
  • This is achieved according to the invention by the features characterizing claim 1.
  • the solution according to the invention includes that the suction part is not in the cycle. As a result, the oil in the compressor does not have to be changed after each expiration and mixing problems are avoided.
  • the solution according to the invention can be used universally, i.e. independent of the type of refrigerant, but also independent of the fluid in the system to be disposed of. It is thus with the device according to the invention e.g. a brake system can also be disposed of.
  • An advantageous embodiment of this solution provides a bypass line which branches off in front of the condenser and is recombined with the line behind the liquid pump. Via this bypass line, the first part of the fluid mixture is advantageously transferred directly to the container at the beginning of the filling process.
  • Another solution according to the invention is characterized by the features characterizing claim 4.
  • a liquid separator which is followed by a liquid pump, is arranged in the line connecting the connections.
  • a compressor and a condenser are provided in a second line starting from the liquid separator. Both lines are brought together again before the second connection.
  • This system is particularly suitable for simultaneously extracting refrigerant gas, refrigerant liquid and oil, for example.
  • An advantageous embodiment of the invention provides that a bypass line is provided which branches off the line in front of the liquid separator and is brought back together with the line behind the liquid pump.
  • a particularly energy-saving embodiment of the invention is characterized in that a level switch is connected to the liquid separator, by means of which the liquid pump can be switched.
  • the lubricant circuit of the compressor can be connected to the liquid pump.
  • An economical embodiment of the invention provides that the line is led through the liquid separator in a region between the compressor and the condenser.
  • a gear pump is used as the liquid pump, as is provided according to another advantageous embodiment of the invention.
  • a pump with a bypass in the manner of an oil burner pump is preferably used.
  • a weighing device is advantageously provided.
  • This weighing device is connected in a suitable manner to the drives of the individual units and switches them, e.g. via end contacts, when the maximum filling quantity is reached. An overfilling of the transport container is therefore excluded.
  • Embodiments of the invention are shown in the drawing and described below using the example of a filling device for refrigerant-oil mixture.
  • FIG. 1 is a schematic representation of a first embodiment of the invention * -
  • FIG. 2 shows a schematic representation of a second embodiment of the invention ?
  • Fig. 3 is a schematic representation of a third embodiment of the invention.
  • FIG. 1 shows a first embodiment of a refrigerant-oil mixture filling device 2.
  • the refrigerant-oil mixture filling device 2 has a first line 4, at one end of which a first connection 6 is provided, for connecting the device to a (not shown) refrigeration system or container which contains the refrigerant to be filled and at the other end second connection 8 is provided for connecting filling containers 10 which receive the filled fluid.
  • a shut-off valve 12 is connected downstream of the first connection 6 and a shut-off valve 14 is connected upstream of the second connection 8.
  • a condenser 18 is arranged in the first line 4 between these valves.
  • the mixture to be extracted is condensed and supercooled in this condenser 18, for which purpose a fully hermetically closed refrigerant circuit is connected, which contains a compressor 20 and a condenser 22.
  • the liquefier 18 is followed by a liquid pump 16 which pumps out the supercooled mixture and supplies it to the container 10.
  • a bypass line 24 branches off from the line 4 and is connected again to the first line 4 before the valve 14.
  • Check valves 26, 28 and shut-off valves 30, 32 downstream thereof are provided both in line 4 and in the bypass line 24. The check valves prevent the mixture from flowing back, so that the clearly defined flows cannot be reversed.
  • a branch line 34 extends from the common line section 4a and has a connection 36 for a vacuum pump.
  • the vacuum pump serves to make the system operational by removing any liquid that may be present.
  • a negative pressure monitor is connected to the common line section 4b and initiates a switch-off process when a certain pressure is reached, ie when no more mixture flows in.
  • An overpressure monitor 39 prevents the container pressure from rising above a critical value.
  • an automatic weighing device 40 which all drives (liquid pump, compressor,
  • Condenser fan switches off automatically when the maximum charge is reached.
  • the containers 10 standing on the weighing device 40 can be connected to the connection 14 via a flexible line 42.
  • this pump 16 it appears expedient to arrange this pump 16 with the exchanger in the system at the top and the condenser 22 and the scale 10 at the bottom.
  • This also has a first line 54 with connections 56 provided at the ends for connection to a refrigerant system and 58 for connection to a filling container 10.
  • this line 54 is at this embodiment, an oil separator 68 and, downstream of this, a liquid gear pump 66 is provided.
  • the liquid separator 68 has a heat source by means of an exchanger through which the refrigerant which is at high pressure and temperature is passed (cooling or heating coil in the
  • Liquid separator 68 and the refrigerant-oil mixture, which is at low pressure and low temperature, evaporates refrigerant in the liquid separator, which is then sucked off via line 74.
  • shut-off valves 62, 64 and 80 are also provided, as well as a check valve 76 and a pressure switch 88.
  • a second line 74 opens into the liquid separator, in which a compressor 70 and a condenser 72 are arranged.
  • a check valve 78 and a shut-off valve 82 are again provided in this line.
  • a branch line 84 with a vacuum connection 86 extends from the line section 54a.
  • a pressure switch 90 is connected to this line section.
  • a weighing device 40 is provided which corresponds to the weighing device shown in FIG. 1.
  • FIG. 3 shows a further development of the filling device as described in FIG. 2. Therefore, only the additional features and their function are described below.
  • a cleaning filter 101 is provided between the connection 56 and the shut-off valve 62 in order to retain contaminants from the filling device.
  • a bypass line 102 which has an expansion nozzle 103, and is connected to the line 54 behind the shut-off valve 62.
  • the shut-off valve 62 When liquid refrigerant is disposed of, the shut-off valve 62 is closed, while it is open when gaseous refrigerant is drawn off.
  • a further bypass line 100 is connected to the line 54, which is provided with a check valve 104 and which connects to the line 54 in the vicinity of the line section 54a. Via the bypass line 100 it is possible for liquid or gas under pressure to flow directly from the connection 56 to the filling container 10.
  • the level of the liquid separator 68 is monitored by the level switch 105 connected to it, which is electrically connected to the drive motor of the liquid pump 66 and which only switches on the liquid pump when a certain amount of liquid is present in the liquid separator 68.
  • the lubricant of the compressor 70 inevitably comes into contact with the refrigerant to be compressed, it becomes contaminated over time and must also be disposed of.
  • the level of the lubricant and the degree of contamination can be in the
  • Sight glass 106 arranged in the lubricant circuit can be monitored. If necessary, via the filler valve 107 Lubricants are refilled. If the lubricant is excessively contaminated, it can be sucked off through the disposal line 108 with the shut-off valve 109 open by means of the liquid pump 66 and fed to the filling container 10. Here, the shut-off valve 110, which is arranged between the liquid separator 68 and the liquid pump 66, is closed.
  • a degassing valve 111 is arranged near the inlet of the condenser 72, the outlet of which can be connected, for example, to a further collecting container.
  • the suction valves 76, 78, 104 are designed as ball valves with a confirmation display, each of which indicates the open or closed position of the valve.

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Loading And Unloading Of Fuel Tanks Or Ships (AREA)

Abstract

Un dispositif d'évacuation et de mise en bouteilles de fluides comprend un premier branchement (6) pour le raccordement à une installation contenant des fluides, un deuxième branchement (8) pour le raccordement à des récipients d'embouteillage ou de transport (10) et un condenseur (18) agencé entre le premier et le deuxième branchement. Afin de simplifier le processus d'évacuation et de mise en bouteilles, une pompe à fluide (16) est agencée en aval du condenseur (18) dans la conduite (4) qui s'étend entre les deux branchements (6, 8).
PCT/EP1988/000603 1987-07-11 1988-07-06 Dispositif d'evacuation et de mise en bouteilles de fluides WO1989000667A1 (fr)

Priority Applications (3)

Application Number Priority Date Filing Date Title
FI890739A FI890739A (fi) 1987-07-11 1989-02-16 Toemningsanordning foer fluider.
NO891018A NO169620C (no) 1987-07-11 1989-03-09 Fluidum-tappeinnretning.
DK116389A DK116389D0 (da) 1987-07-11 1989-03-10 Apparatur til aftapning af et fluidum

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
DEP3722987.7 1987-07-11
DE3722987 1987-07-11
DEP3805832.4 1988-02-25
DE19883805832 DE3805832A1 (de) 1987-07-11 1988-02-25 Fluid-abfuellvorrichtung

Publications (1)

Publication Number Publication Date
WO1989000667A1 true WO1989000667A1 (fr) 1989-01-26

Family

ID=25857494

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/EP1988/000603 WO1989000667A1 (fr) 1987-07-11 1988-07-06 Dispositif d'evacuation et de mise en bouteilles de fluides

Country Status (5)

Country Link
EP (1) EP0326591A1 (fr)
DE (1) DE3805832A1 (fr)
DK (1) DK116389D0 (fr)
FI (1) FI890739A (fr)
WO (1) WO1989000667A1 (fr)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1991000485A1 (fr) * 1989-06-27 1991-01-10 Ashland Oil, Inc. Systeme de recuperation et de reconstitution de refrigerant a condensation directe

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2645948B1 (fr) * 1989-04-14 1994-12-09 Mathieu Christian Installation de recuperation d'un fluide frigorigene, notamment chlorofluorocarbone
JPH03286977A (ja) * 1990-04-04 1991-12-17 Sanden Corp 多種冷媒回収装置
DE4216046A1 (de) * 1992-05-15 1993-11-18 Hans Rudolf Prof Dr Engelhorn Verfahren und Vorrichtung zum Entfernen von tiefsiedenden Kältemitteln aus Kälteanlagen
FR2784737A1 (fr) * 1998-10-15 2000-04-21 Matra Marconi Space France Remplissage d'un gaz sous pression dans un reservoir et depressurisation d'un fluide dans un reservoir
JP4366245B2 (ja) * 2004-05-24 2009-11-18 アイシン精機株式会社 冷媒供給装置
CN101504222B (zh) * 2009-02-19 2011-07-27 艾默生网络能源有限公司 一种空调

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3282305A (en) * 1964-02-20 1966-11-01 Gen Dynamics Corp Cylinder filling apparatus
US4646527A (en) * 1985-10-22 1987-03-03 Taylor Shelton E Refrigerant recovery and purification system
DE8708522U1 (fr) * 1987-06-19 1987-07-30 Christof Fischer Gmbh, 7000 Stuttgart, De
DE3616591A1 (de) * 1986-05-16 1987-11-19 Weiss Umwelttechnik Gmbh Verfahren und vorrichtung zur ueberfuehrung von kaeltemittel aus einem kaeltekreislauf in einen kaeltemittelspeicher

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2388762A1 (fr) * 1977-04-25 1978-11-24 Calgon Corp Installation de retour des vapeurs de combustible
US4261178A (en) * 1979-01-19 1981-04-14 Robinair Manufacturing Corporation Environmental protection refrigeration disposal and charging system
DE3045112C2 (de) * 1980-11-29 1985-09-19 Daimler-Benz Ag, 7000 Stuttgart Abgassystem für eine Brennkraftmaschine mit einem die Abgaszusammensetzung erkennenden Meßfühler
DD209511A1 (de) * 1982-09-14 1984-05-09 Horst Haentzschel Anordnung zur reinigung und rueckgewinnung von fluor-chlor-kohlenwasserstoff kaeltemitteln
DE3300297C2 (de) * 1983-01-07 1986-07-10 Danfoss A/S, Nordborg Vorrichtung zum Fördern von Flüssiggas

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3282305A (en) * 1964-02-20 1966-11-01 Gen Dynamics Corp Cylinder filling apparatus
US4646527A (en) * 1985-10-22 1987-03-03 Taylor Shelton E Refrigerant recovery and purification system
DE3616591A1 (de) * 1986-05-16 1987-11-19 Weiss Umwelttechnik Gmbh Verfahren und vorrichtung zur ueberfuehrung von kaeltemittel aus einem kaeltekreislauf in einen kaeltemittelspeicher
DE8708522U1 (fr) * 1987-06-19 1987-07-30 Christof Fischer Gmbh, 7000 Stuttgart, De

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1991000485A1 (fr) * 1989-06-27 1991-01-10 Ashland Oil, Inc. Systeme de recuperation et de reconstitution de refrigerant a condensation directe

Also Published As

Publication number Publication date
DK116389A (da) 1989-03-10
EP0326591A1 (fr) 1989-08-09
FI890739A0 (fi) 1989-02-16
FI890739A (fi) 1989-02-16
DK116389D0 (da) 1989-03-10
DE3805832A1 (de) 1989-01-19

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