EP2051030A2 - A method for temperature control of CO2 as well as metering and filling of CO2 systems - Google Patents
A method for temperature control of CO2 as well as metering and filling of CO2 systems Download PDFInfo
- Publication number
- EP2051030A2 EP2051030A2 EP08388037A EP08388037A EP2051030A2 EP 2051030 A2 EP2051030 A2 EP 2051030A2 EP 08388037 A EP08388037 A EP 08388037A EP 08388037 A EP08388037 A EP 08388037A EP 2051030 A2 EP2051030 A2 EP 2051030A2
- Authority
- EP
- European Patent Office
- Prior art keywords
- filling
- valve
- process unit
- meter
- unit
- 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.)
- Granted
Links
- 238000000034 method Methods 0.000 title claims abstract description 33
- 238000001816 cooling Methods 0.000 claims abstract description 10
- 230000015572 biosynthetic process Effects 0.000 abstract description 4
- 239000007788 liquid Substances 0.000 description 5
- 239000003507 refrigerant Substances 0.000 description 3
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- YCKRFDGAMUMZLT-UHFFFAOYSA-N Fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 description 1
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 229910052731 fluorine Inorganic materials 0.000 description 1
- 239000011737 fluorine Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Images
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
- F25B45/00—Arrangements for charging or discharging refrigerant
-
- 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
- F25B2309/00—Gas cycle refrigeration machines
- F25B2309/06—Compression machines, plants or systems characterised by the refrigerant being carbon dioxide
-
- 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
- F25B2345/001—Charging refrigerant to a cycle
-
- 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
- F25B9/00—Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point
- F25B9/002—Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point characterised by the refrigerant
- F25B9/008—Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point characterised by the refrigerant the refrigerant being carbon dioxide
Definitions
- the present invention relates to a method for temperature control of CO 2 as well as metering and filling of CO 2 systems by means of a system having a process unit and a filling unit.
- Refrigerants e.g. R22 (contains chlorine), R134a (HFC) and R717 (naturally inorganic) typically have a critical point, which means that the contents of liquid and gas are the same at 70 - 130 °C, and, therefore, they are far from normal ambient temperatures.
- the object of the invention is to provide a method of the type stated in the opening paragraph, which makes it possible to avoid formation of gas and thereby to keep CO 2 in liquid form, thereby allowing the amount of CO 2 to be metered correctly.
- the invention also comprises an alternative method, wherein CO 2 is continuously pumped through a hose from the process unit at a temperature below 31.1 °C and comprising a container, a pump, a meter, a circulation valve and a parallel valve, through the filling unit, which comprises a filling valve, and back to the process unit again for cooling, following which the circulation valve is closed, the parallel valve and the filling valve are opened, whereby CO 2 is metered by the passage through the meter and is filled into the CO 2 system through the filling valve.
- the filling adapter used may be constructed more compactly, which may be an advantage depending on the circumstances.
- Figure 1 shows a system for temperature control of CO 2 , in which CO 2 is pumped continuously through a hose 8 from the process unit 1, which is cooled to below 31.1 °C and comprises a container 2, a pump 3 and a meter 4, through a circulation valve 6 in the filling unit 5, which comprises a circulation valve 6 and a filling valve 7, and back to the process unit again for cooling.
- Figure 2 shows the same system, now used for metering and filling of CO 2 systems, as the circulation valve 6 is closed and the filling valve 7 is opened, whereby CO 2 may be metered by the passage through the meter 4 and be filled into the CO 2 system through the filling valve 7.
- Figure 3 shows an alternative system for temperature control of CO 2 , in which CO 2 is pumped continuously through a hose 8 from the process unit 1, which is cooled to below 31.1 °C and comprises a container 2, a pump 3, a meter 4, a circulation valve 6 and a parallel valve 9, through the filling unit 5, which comprises a filling valve 7, and back to the process unit again for cooling.
- Figure 4 shows an alternative system for metering and filling of CO 2 systems, as the circulation valve 6 is closed, the parallel valve 9 and the filling valve 7 are opened, whereby CO 2 may be metered by the passage through the meter 4 and be filled into the CO 2 system through the filling valve 7.
- the cooling of the process unit may take place by means of any known cooling system.
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Filling Of Jars Or Cans And Processes For Cleaning And Sealing Jars (AREA)
- Filling Or Discharging Of Gas Storage Vessels (AREA)
Abstract
Description
- The present invention relates to a method for temperature control of CO2 as well as metering and filling of CO2 systems by means of a system having a process unit and a filling unit.
- The use of the fluorine-containing CFC refrigerants and the subsequent HCFC and HFC refrigerants are being phased out because of their damaging impact on the environment, including the ozone layer.
- Refrigerants, e.g. R22 (contains chlorine), R134a (HFC) and R717 (naturally inorganic) typically have a critical point, which means that the contents of liquid and gas are the same at 70 - 130 °C, and, therefore, they are far from normal ambient temperatures.
- An alternative to the environmentally harmful substances is the gas CO2, which has a critical point at 31.1 °C and 73.91 bars, which thus means that the contents of CO2 in liquid gas and gas form are the same here, and that, accordingly, no distinction can be made between these two forms. At temperatures above 31.1 °C, liquid cannot be formed merely by increasing the pressure, which is the case at temperatures below 31.1 °C, where CO2 condenses at an increased pressure.
- It is known to fill CO2 systems by means of a system having a process unit and a filling unit.
- The drawback of these systems, however, is that they can exceed the critical point at 31.1 °C, so that the CO2 becomes a mixture of liquid and gas, and the metering unit used for the metering of the CO2 amount thus cannot meter correctly, and that, thus, the amount of gas is not recorded.
- Accordingly, the object of the invention is to provide a method of the type stated in the opening paragraph, which makes it possible to avoid formation of gas and thereby to keep CO2 in liquid form, thereby allowing the amount of CO2 to be metered correctly.
- The object stated above is achieved by a method as described in the introductory portion of claim 1, wherein CO2 is pumped continuously through a hose from the process unit at a temperature below 31.1 °C and comprising a container, a pump and a meter, through a circulation valve in the filling unit, which comprises a circulation valve and a filling valve, and back to the process unit again for cooling, following which the circulation valve is closed and the filling valve is opened, whereby CO2 is metered by the passage through the meter and is filled into the CO2 system through the filling valve.
- This makes it possible to avoid formation of gas in the system at standstill for an extended period of time, when the CO2 is thereby heated by the surroundings, if the said method is followed and the system is in continuous operation, and, moreover, the amount of CO2 may be metered correctly.
- As will appear from
claim 2, the invention also comprises an alternative method, wherein CO2 is continuously pumped through a hose from the process unit at a temperature below 31.1 °C and comprising a container, a pump, a meter, a circulation valve and a parallel valve, through the filling unit, which comprises a filling valve, and back to the process unit again for cooling, following which the circulation valve is closed, the parallel valve and the filling valve are opened, whereby CO2 is metered by the passage through the meter and is filled into the CO2 system through the filling valve. - That the parallel valve is opened and the filling thereby takes place through both hoses, is necessary, as a closed parallel valve will have as a result that a relative negative pressure is generated in the hose which serves as a return hose during the cooling.
- If the said method is followed and the system is in constant operation, it is likewise possible to avoid formation of gas in the system at a standstill for an extended period of time, when the CO2 is thereby heated by the surroundings, and, moreover, the amount of CO2 may be metered correctly. In addition, the filling adapter used may be constructed more compactly, which may be an advantage depending on the circumstances.
- Exemplary embodiments of the invention will be described more fully below with reference to the drawing, in which
- fig. 1
- shows a system for temperature control of CO2, and
- fig. 2
- shows a system for metering and filling of CO2 systems, and
- fig. 3
- shows an alternative system for temperature control of CO2, and
- fig. 4
- shows an alternative system for metering and filling of CO2 systems, and
- 1.
- Process unit
- 2
- Container
- 3
- Pump
- 4
- Meter
- 5
- Filling adapter
- 6
- Circulation valve
- 7
- Filling valve
- 8
- Hose
- 9
- Parallel valve
-
Figure 1 shows a system for temperature control of CO2, in which CO2 is pumped continuously through ahose 8 from the process unit 1, which is cooled to below 31.1 °C and comprises acontainer 2, a pump 3 and ameter 4, through acirculation valve 6 in thefilling unit 5, which comprises acirculation valve 6 and afilling valve 7, and back to the process unit again for cooling. -
Figure 2 shows the same system, now used for metering and filling of CO2 systems, as thecirculation valve 6 is closed and thefilling valve 7 is opened, whereby CO2 may be metered by the passage through themeter 4 and be filled into the CO2 system through thefilling valve 7. -
Figure 3 shows an alternative system for temperature control of CO2, in which CO2 is pumped continuously through ahose 8 from the process unit 1, which is cooled to below 31.1 °C and comprises acontainer 2, a pump 3, ameter 4, acirculation valve 6 and aparallel valve 9, through thefilling unit 5, which comprises afilling valve 7, and back to the process unit again for cooling. -
Figure 4 shows an alternative system for metering and filling of CO2 systems, as thecirculation valve 6 is closed, theparallel valve 9 and thefilling valve 7 are opened, whereby CO2 may be metered by the passage through themeter 4 and be filled into the CO2 system through thefilling valve 7. - The cooling of the process unit may take place by means of any known cooling system.
Claims (2)
- A method for temperature control of CO2 as well as metering and filling of CO2 systems by means of a system having a process unit and a filling unit, characterized in that CO2 is pumped continuously through a hose (8) from the process unit (1) at a temperature below 31.1 °C and comprising a container (2), a pump (3) and a meter (4), through a circulation valve (6) in the filling unit (5), which comprises a circulation valve (6) and a filling valve (7), and back to the process unit again for cooling, following which the circulation valve (6) is closed and the filling valve (7) is opened, whereby CO2 is metered by the passage through the meter (4) and is filled into the CO2 system through the filling valve (7).
- A method for temperature control of CO2 as well as metering and filling of CO2 systems by means of a system having a process unit and a filling unit, characterized in that CO2 is pumped continuously through a hose (8) from the process unit (1) at a temperature below 31.1 °C and comprising a container (2), a pump (3), a meter (4), a circulation valve (6) and a parallel valve (9), through the filling unit (5), which comprises a filling valve (7), and back to the process unit again for cooling, following which the circulation valve (6) is closed, the parallel valve (9) and the filling valve (7) are opened, whereby CO2 is metered by the passage through the meter (4) and is filled into the CO2 system through the filling valve (7).
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DKPA200701483 | 2007-10-15 |
Publications (3)
Publication Number | Publication Date |
---|---|
EP2051030A2 true EP2051030A2 (en) | 2009-04-22 |
EP2051030A3 EP2051030A3 (en) | 2010-02-24 |
EP2051030B1 EP2051030B1 (en) | 2013-01-23 |
Family
ID=40239775
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP08388037A Active EP2051030B1 (en) | 2007-10-15 | 2008-10-14 | A method for temperature control of CO2 as well as metering and filling of CO2 systems |
Country Status (1)
Country | Link |
---|---|
EP (1) | EP2051030B1 (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2009132836A1 (en) * | 2008-04-29 | 2009-11-05 | Vulkan Lokring-Rohrverbindungen Gmbh & Co. Kg | Filling cooling circuits with liquid refrigerant |
DE102014011051A1 (en) * | 2014-07-22 | 2016-01-28 | Dürr Somac GmbH | Device for filling vehicle air conditioning systems with refrigerant R744 |
ITUA20163839A1 (en) * | 2016-05-26 | 2017-11-26 | Texa Spa | MAINTENANCE EQUIPMENT OF A CARBON DIOXIDE AIR CONDITIONING SYSTEM FOR A MOTOR VEHICLE AND ITS OPERATING METHOD |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1999002928A1 (en) * | 1997-07-11 | 1999-01-21 | Zexel Corporation | Freezer |
EP1143213A1 (en) * | 2000-03-30 | 2001-10-10 | Behr GmbH & Co. | Filling apparatus for motor vehicle air-conditioning systems |
JP2004163037A (en) * | 2002-11-14 | 2004-06-10 | Osaka Gas Co Ltd | Compression type heat pump system |
WO2006066580A1 (en) * | 2004-12-14 | 2006-06-29 | Agramkow Fluid Systems A/S | A method and a system for filling a refrigeration system with refrigerant |
-
2008
- 2008-10-14 EP EP08388037A patent/EP2051030B1/en active Active
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1999002928A1 (en) * | 1997-07-11 | 1999-01-21 | Zexel Corporation | Freezer |
EP1143213A1 (en) * | 2000-03-30 | 2001-10-10 | Behr GmbH & Co. | Filling apparatus for motor vehicle air-conditioning systems |
JP2004163037A (en) * | 2002-11-14 | 2004-06-10 | Osaka Gas Co Ltd | Compression type heat pump system |
WO2006066580A1 (en) * | 2004-12-14 | 2006-06-29 | Agramkow Fluid Systems A/S | A method and a system for filling a refrigeration system with refrigerant |
Non-Patent Citations (1)
Title |
---|
"FILLING IN WORKSHOP AND PRODUCTION AGRAMKOW - THE SAFE CHOICE" VDA ALTERNATE REFRIGERANT WINTER MEETING, XX, XX, 13 February 2003 (2003-02-13), pages 1-34, XP001172663 * |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2009132836A1 (en) * | 2008-04-29 | 2009-11-05 | Vulkan Lokring-Rohrverbindungen Gmbh & Co. Kg | Filling cooling circuits with liquid refrigerant |
DE102014011051A1 (en) * | 2014-07-22 | 2016-01-28 | Dürr Somac GmbH | Device for filling vehicle air conditioning systems with refrigerant R744 |
ITUA20163839A1 (en) * | 2016-05-26 | 2017-11-26 | Texa Spa | MAINTENANCE EQUIPMENT OF A CARBON DIOXIDE AIR CONDITIONING SYSTEM FOR A MOTOR VEHICLE AND ITS OPERATING METHOD |
WO2017203481A1 (en) * | 2016-05-26 | 2017-11-30 | Texa S.P.A. | Apparatus for maintaining a motor vehicle air conditioning system provided with carbon dioxide and operating method thereof |
US11149998B2 (en) | 2016-05-26 | 2021-10-19 | Texa S.P.A. | Apparatus for maintaining a motor vehicle air conditioning system provided with carbon dioxide and operating method thereof |
Also Published As
Publication number | Publication date |
---|---|
EP2051030A3 (en) | 2010-02-24 |
EP2051030B1 (en) | 2013-01-23 |
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