[0001] 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.
Prior art
[0002] 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.
[0003] 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.
[0004] An alternative to the environmentally harmful substances is the gas CO
2, which has a critical point at 31.1 °C and 73.91 bars, which thus means that the
contents of CO
2 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 CO
2 condenses at an increased pressure.
[0005] It is known to fill CO
2 systems by means of a system having a process unit and a filling unit.
[0006] The drawback of these systems, however, is that they can exceed the critical point
at 31.1 °C, so that the CO
2 becomes a mixture of liquid and gas, and the metering unit used for the metering
of the CO
2 amount thus cannot meter correctly, and that, thus, the amount of gas is not recorded.
The object of the invention
[0007] 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 CO
2 in liquid form, thereby allowing the amount of CO
2 to be metered correctly.
Summary of the invention
[0008] The object stated above is achieved by a method as described in the introductory
portion of claim 1, wherein CO
2 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 CO
2 is metered by the passage through the meter and is filled into the CO
2 system through the filling valve.
[0009] This makes it possible to avoid formation of gas in the system at standstill for
an extended period of time, when the CO
2 is thereby heated by the surroundings, if the said method is followed and the system
is in continuous operation, and, moreover, the amount of CO
2 may be metered correctly.
[0010] As will appear from claim 2, 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.
[0011] 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.
[0012] 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 CO
2 is thereby heated by the surroundings, and, moreover, the amount of CO
2 may be metered correctly. In addition, the filling adapter used may be constructed
more compactly, which may be an advantage depending on the circumstances.
The drawing
[0013] 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
in which the following reference numerals and designations are used:
- 1.
- Process unit
- 2
- Container
- 3
- Pump
- 4
- Meter
- 5
- Filling adapter
- 6
- Circulation valve
- 7
- Filling valve
- 8
- Hose
- 9
- Parallel valve
Detailed description of the invention
[0014] 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.
[0015] 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.
[0016] 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.
[0017] 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.
[0018] The cooling of the process unit may take place by means of any known cooling system.
1. 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).
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), 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).