PROCESS FOR THE PRODUCTION OF A REFRIGERATING CIRCUIT COMPRISING NON-EVAPORABLE GETTER MATERIAL

Abstract: A process is described for the production of a refrigerating circuit comprising non-evaporable getter material, wherein said getter material, previously introduced into the same circuit, is heated to a temperature of at least 200 DEG C during or immediately after the circuit evacuating step, at a residual atmospheric gas pressure of not less than 10 mbar, before introduction of the mixture of cooling fluids and before the circuit sealing. Preferred for this application is the use of zirconium-based getter alloys.

Description: "PROCESS FOR THE PRODUCTION OF A REFRIGERATING CIRCUIT COMPRISING NON-EVAPORABLE GETTER MATERIAL" The present invention relates to a process for the production of a refrigerating circuit comprising non-evaporable getter material for removing gases, particularly atmospheric gases, from the fluid mixture contained in refrigerating circuits for refrigerators and cooling devices in general. It is well known that the most common cooling system is based on the physical principle of drop of temperature of a fluid during its evaporation and is employed in domestic or industrial refrigerators, freezers, automatic dispensers of perishable foodstuffs, refrigerated shop-windows, air conditioners, etc. This principle is applied by using closed circuits containing a fluid suitable to be subjected to compression and expansion cycles. The circuit, comprising a compressor, extends mainly with a very small, substantially capillary cross-section, being coil shaped in order to increase the surface available for the exchange of heat, and is normally made of copper, an excellent heat conductor. A molecular sieve filter is generally provided upstream of the coil and the tubular portion of the evaporator with a larger cross-section lies downstream thereof, before the return to the compressor. Usually this is the general configuration, apart from possible variations. The fluid is selected among those undergoing liquid-vapor phase transition caused by pressure changes in the temperature range of 0-50°C. During the expansion step, a partial evaporation of the liquid occurs, causing its temperature to drop, and heat is removed from the parts to be cooled through the closed circuit metal walls; during the compression step, the previously formed vapor condenses, thus releasing heat that is transferred outside of the system. As cooling fluids chlorofluorocarbons (CFC) were previously used, but their industrial use has been forbidden because of their reaction with ozone in the upper part of the atmosphere. Hydrogenated CFC (HCFC) are used as substitutes and the use of lower saturated hydrocarbons is spreading, such as isobutane, (CH 3 ) 3 CH. These compounds are generally used in admixture with oils, ensuring the continuous presence of a liquid phase for the compressor correct working and lubrication of the mechanical parts thereof. In the following the cooling oil-fluid mixture will be simply referred to as freezing mixture. The presence, in the pipes composing the closed refrigerating circuit, of gases other than the working fluid vapors, generally atmospheric gases, causes some problems. First, these gases are not condensable by compression at the typical compressor working temperatures (around room temperature), and as a result remain in the circuit as gases; because of their compressibility, part of the compression/expansion work made by the compressor is transformed into a simple elastic variation of their volume and does not contribute to the evaporation/condensation cycle accomplishing the heat transfer, with the net result of a decrease of the compressor energetic yield. Moreover, the presence of gases in the refrigerating circuit causes noises, annoying especially in case of domestic refrigerators. Finally, when the cooling fluid is a hydrocarbon, the presence of air involves a certain risk of explosions, that, however remote, still is not negligible. The production of refrigerating closed circuits comprises a step of evacuation of the metallic pipes by mechanical pumping, in order to remove most of the initially contained air, and the successive filling of the circuit with the oil/cooling fluid mixture. However, the normal evacuation operations carried out industrially do not allow a complete gas removal, such as to eliminate the above described difficulties. A complete evacuation would require long pumping times, unacceptable for industrial applications. Italian patent application MI 98A 000558 in the name of the same applicant aims at providing a getter system comprising a getter material held within an evacuated chamber having at least one wall contacting the freezing mixture inside the circuit. The wall is made of a material permeable to the gases but not to the fluids constituting the mixture itself. In this way the non-evaporable getter material sorbs the atmospheric gases which are present in the cooling fluids during the circuit working life, as soon as the fluid contacts the getter material, in spite of the reduced conductance values of the circuit itself. This results in long times being necessary for sorbing the gases left in the circuit as residues from the production process. The getter material is therefore used as in the high vacuum systems, but these circuits are never under a very high vacuum and the degassing problem is negligible compared to the advantage of having, already at the start of the operation, the greatest reduction of unwanted gases present in the circuit. This is made possible because a non-evaporable getter, before inserting the fluid mixture into the circuit, therefore in the presence of air, once heated to a temperature of at least 200°C, undergoes a self-feeding exothermic reaction causing in a very short time the almost complete sorption of the present air. The result is an almost complete combustion of the getter material, which is virtually "burned", and then remains inactive for all the refrigerating circuit life, having fulfilled its task, thus being certain that already from the very beginning of the circuit operation, the uncondensable gases therein have been notably reduced. These purposes are obtained according to the present invention by a process for the production of a refrigerating circuit comprising the working steps set forth in claim 1. Object of the invention is also a refrigerating circuit made by this process as well as any apparatus containing such a circuit. These and other objects, advantages and features of the process according to the present invention will be clearer from the following detailed description of an embodiment thereof with reference to the accompanying drawing, the only Figure 1 of which is a schematic view of a refrigerating circuit suitable to be produced according to the process of the present invention. With reference to the drawing, a refrigerating circuit is shown suitable to be used, in the generally shown structure, in any cooling apparatus among those above mentioned. It comprises a compressor 1 whose delivery is connected, through a tubular portion 2 called condenser and a filter 3 made of zeolites or molecular sieves, to a portion 4 extending mainly lengthwise, having a reduced, almost capillary, cross-section with a diameter of about 0.5 mm, and preferably forming volutes as a pipe coil. Portion 4 is followed by a circuit portion 5 having a much larger cross-section, acting as an evaporator. The circuit closes at the compressor through a runback 6 or heat exchanger, normally finned, to achieve a better heat exchange with the environment to be cooled. A conventional process for the preparation of such a circuit is known, by which, before its closure, the circuit is evacuated by connecting to an external rotary pump an auxiliary pipe 7 provided at the outlet of compressor 1 , by which it is connected to the runback 6, so that it sucks most of the air remained in the circuit, before introduction of the cooling fluid mixture and before final sealing. Though, because the circuit conductances are relatively low upstream of evaporator 5, in the portion with capillary cross-section 4 and in the condenser 2, also resistant to the evacuation because of filter 3, an amount of atmospheric gases which is not negligible is still trapped and can involve the difficulties mentioned at the beginning of this description. According to the present invention a getter device G with non-evaporable getter material is previously introduced in the circuit, in series, in parallel or as a branch from this, which, at the end of the evaporation step or even before its completion, but anyway before the cooling fluid introduction, is heated at a temperature of at least 200°C, enough to start the exothermic reaction occurring in the presence of air, exerting on this the violent sorption due to the getter. Then the cooling fluid is inserted (isobutane or other) and the auxiliary pipe 7 is closed for example by an operation called "pinch-off". The refrigerating circuit can therefore start working with a negligible amount of air inside, because all the atmospheric gases present in the portion less affected by the removing action exerted by the evacuation pump owing to the reduced system conductance, have been removed by the getter action. The atmospheric gas partial pressure requested to start the exothermic reaction is of at least 10 mbar, and preferably the heating to trigger such a reaction takes place when pressure is not higher than 500 mbar. At pressures lower than 10 mbar the reaction heat is not enough for the self-feeding of the gas-sorption reaction, while at pressures higher than 500 mbar the getter is consumed before it can carry out its function of reducing the residual pressure in the circuit. The possibility of working in such a wide pressure range makes versatile the process of the invention, that may be carried out either during the circuit evacuation step or just thereafter, at relatively high pressures, or, after the circuit sealing by pinch-off when the gas has spread back into the circuit itself thus leveling the pressure, at the lower values in the above indicated range. A non-evaporable getter device heated at such values of residual pressure that, however reduced, do not correspond to the operating conditions of a high vacuum getter (pressure less than 1 mbar), causes an exothermic reaction of sorption of the present air, progressively increasing its temperature until it namely burns, so ending its gettering action. The resulting temperature can be so high that in certain cases it is advisable to use special materials for the circuit portions near to the getter device, because copper, which is normally used, could be damaged by these temperatures. The following examples are provided with the purely explanatory purpose to teach those who are skilled in the art the best way to put the present invention into practice, without limiting in any way the scope of the invention itself. EXAMPLE 1 This example refers to a test carried out at the following conditions. As a non-evaporable getter, in the form of fragments, a sintered product of zirconium powder with powder of an alloy having a weight percent composition Zr 70%-N 24.6%-Fe 5.4%, produced and sold by the applicant with the name St 707, is used. The above mentioned sintered product, as used in this example, on the contrary is produced and sold by the applicant with the name St 172. More than 10 fragments of such a sintered product, for a total weight of 0.6 g of getter material are introduced in a test chamber formed as a steel bulb having an internal volume of 52 cm 3 , connected to a vacuum line and to a manometer. This volume is smaller than the typical internal volume of the coil of a refrigerating circuit, which is about 90 cm 3 , but this is not considered to have any influence on the test validity as a simulation of the real process, because at most a greater amount of getter material would be required. Before starting the test the bulb was evacuated to a residual pressure of 500 mbar measured at room temperature. Then the metallic bulb was heated from outside to a temperature of about 350°C and the heating maintained for 5 minutes, then the bulb was cooled to room temperature, and the residual pressure was measured, which was of 145 mbar, thus indicating a percentage of removed air of about 71.3%. This test result, like for all the other examples, is reported in the following table. EXAMPLE 2 Another test is carried out with the same material and in the same way of example 1 , but the number of fragments of the St 172 material is more than 20 for a total weight of 0.5 g. EXAMPLE 3 The test of the previous examples is repeated but using as getter material 4 fragments of the alloy St 707 for a total weight of 0.6 g. EXAMPLES 4-7 The tests of example 3 are again repeated with the same material St 707, but changing every time (except for examples 6 and 7 which were carried out at identical conditions) the number of the fragments of material. EXAMPLE 8 The test of example 1 is repeated, but using a test chamber with a volume of 64 cm 2 and as a getter material an alloy, produced and sold by the applicant with the name St 787, with a weight percent composition Zr 80.8%-Co 14.2%- mischmetal 5.0%; the used mischmetal has a weight percent composition of about 50% cerium, 30% lanthanum, 15%) neodymium, and the remainder 5% other rare earths. EXAMPLE 9 This test is an example of the functioning of the invention process at low starting pressures. The test of example 1 is repeated, operating however in a chamber of volume 1.1 1, and using a tablet of 0.6 g of St 707 as a getter material. The initial pressure in the bulb was 13 mbar. The results of all the tests are reported in the following table: The results indicated in the table show that, as expected, the greater is the amount of getter material (compare tests 6 and 7 with tests 3-5) and the thinner are the particles (compare test 2 with test 1 and test 4 with tests 3 and 5), the more effective is the removal. In all cases it is evident that the sorption level is extremely good in some cases approaching 100% (examples 2, 4, 6, and 7). As stated above, it is an object of the present invention also a refrigerating circuit produced through the above described process, as well as any cooling, air-conditioning etc. device containing such a circuit.

Claims: CLAIMS 1. A process for the production of a refrigerating circuit, comprising the step of introducing non-evaporable getter material thereinto and a step of evacuation by pumping, characterized in that said getter material is heated at a temperature of at least 200°C during evacuation or in an immediately subsequent step. 2. A process according to claim 1, characterized in that said non-evaporable getter material is positioned, in series, in parallel or as a branch, in a zone of reduced conductance, upstream of a bortlenecked portion of the refrigerating circuit, where the residual pressure of the present atmospheric gases is in the range from 10 to 500 mbar. 3. A process according to claim 1 or 2, wherein, after introducing the non-evaporable getter into the circuit, a cooling fluid mixture is introduced before final sealing. 4. A process according to anyone of the previous claims, characterized in that said non-evaporable getter material comprises a zirconium-based alloy. 5. A process according to claim 4, wherein the non-evaporable getter material is a ternary Zr-V-Fe alloy. 6. A process according to claim 5, wherein said ternary alloy has a weight percent composition of Zr 70%-V 24.6%-Fe 5.4%. 7. A process according to claim 4, wherein said getter material is formed of a sintered product of zirconium powder with powder of a ternary Zr-V-Fe alloy. 8. A process according to claim 4, wherein the non-evaporable getter material is a Zr-Co-mischmetal alloy. 9. A refrigerating circuit produced according to the process of claim 1. 10. An apparatus comprising the refrigerating circuit according to claim 9.

Inventors: BOFFITO CLAUDIO, CORAZZA ALESSIO, GALLITOGNOTTA ALESSANDRO, MANINI PAOLO, BOFFITO, CLAUDIO, CORAZZA, ALESSIO, GALLITOGNOTTA, ALESSANDRO, MANINI, PAOLO
Applicants: BOFFITO CLAUDIO, CORAZZA ALESSIO, GALLITOGNOTTA ALESSANDRO, GETTERS SPA, MANINI PAOLO, BOFFITO, CLAUDIO, CORAZZA, ALESSIO, GALLITOGNOTTA, ALESSANDRO, MANINI, PAOLO, SAES GETTERS S.P.A.
Application year: 1999
Main classification: F25B43
IPC codes: F25B43