US3653414A - Method of charging a thermostatic system with a condensible and a noncondensible medium - Google Patents
Method of charging a thermostatic system with a condensible and a noncondensible medium Download PDFInfo
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- US3653414A US3653414A US36312A US3653414DA US3653414A US 3653414 A US3653414 A US 3653414A US 36312 A US36312 A US 36312A US 3653414D A US3653414D A US 3653414DA US 3653414 A US3653414 A US 3653414A
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- noncondensible
- condensible
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- 238000000034 method Methods 0.000 title claims abstract description 19
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims abstract description 53
- 229910052757 nitrogen Inorganic materials 0.000 claims abstract description 27
- 238000011010 flushing procedure Methods 0.000 claims abstract description 15
- 238000012360 testing method Methods 0.000 abstract description 6
- 239000007789 gas Substances 0.000 description 12
- 239000007788 liquid Substances 0.000 description 8
- 239000000203 mixture Substances 0.000 description 3
- 229920006395 saturated elastomer Polymers 0.000 description 3
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 2
- NEHMKBQYUWJMIP-UHFFFAOYSA-N chloromethane Chemical compound ClC NEHMKBQYUWJMIP-UHFFFAOYSA-N 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- VOPWNXZWBYDODV-UHFFFAOYSA-N Chlorodifluoromethane Chemical compound FC(F)Cl VOPWNXZWBYDODV-UHFFFAOYSA-N 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 238000007710 freezing Methods 0.000 description 1
- 230000008014 freezing Effects 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 229940050176 methyl chloride Drugs 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- 150000002829 nitrogen Chemical class 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 230000002040 relaxant effect Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 235000010269 sulphur dioxide Nutrition 0.000 description 1
- 239000004291 sulphur dioxide Substances 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
- 238000003466 welding Methods 0.000 description 1
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Classifications
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01K—MEASURING TEMPERATURE; MEASURING QUANTITY OF HEAT; THERMALLY-SENSITIVE ELEMENTS NOT OTHERWISE PROVIDED FOR
- G01K5/00—Measuring temperature based on the expansion or contraction of a material
- G01K5/32—Measuring temperature based on the expansion or contraction of a material the material being a fluid contained in a hollow body having parts which are deformable or displaceable
Definitions
- Appl' 36312 The invention relates to a method and apparatus for charging a thermostatic system with condensible and noncondensible [52] U.S. Cl ..l4l/4, 141/9, 141/49, mediums such as Freon and nitrogen.
- the noncondensible 141/63, 141/104 medium is introduced first at a predetermined partial pressure [51] Int.
- the invention relates to a method of charging a thermostatic system with a condensible and a noncondensible medium, andto a charging apparatus for performing this method.
- thermostatic systems which consist for example of a temperature sensor and a working element connected thereto by way of a capillary tube
- charge materials which consist of a medium which is condensible over a working temperature range and of a medium which is not condensible over a working temperature range.
- condensible media are sulphur dioxide and halogenized hydrocarbons such as methyl chloride or the substances marketed under the trade names Freon or Frigen. Nitrogen or another inert gas is used as the noncondensible medium.
- the thermostatic system For the purpose of charging the thermostatic system, it is first evacuated, filled with the condensible medium in vapor form and then charged with the noncondensible medium to the point at which the required total pressure is reached. Surprisingly, in the majority of cases the required temperaturepressure, curves that would be expected as the result of the charged quantity of condensible medium, have not been obtained. Frequently, the curves obtained have even diverged from each other.
- the object of the invention is to provide a charging method which provides perfectly reproducible results and enables the performance of the method to be still further simplified.
- this object is achieved by first charging the noncondensible medium into the system and then the condensible medium.
- the invention is based upon the heretofore unobserved fact that the condensible medium, which is first filled into the system and is in vapor form, partially condenses under the pressure at which the noncondensible medium is charged into the system so that the condensible medium thus undergoes considerable reduction in volume. Consequently, a higher proportion of noncondensible medium is charged into the system than corresponds to the required quantitative ratio. Furthermore, the quantity of the condensate is very much dependent upon temperature. Slight changes in the charging conditions, e.g. in the room temperature, lead to clearly differing temperature-curves.
- a quantity of liquid condensate, measured in a measuring chamber can be charged into the thermostatic system.
- thermostatic system is cooled. This ensures that the condensible medium is condensed at this cooled part and passes into the thermostatic system rapidly and as completely as required.
- the flushing operation is carried out by charging the system with nitrogen at an excess pressure and then relaxing the pressure.
- the flushing operation can be repeated several times if required. During each flushing operation parts of the unrequited gases are mixed with pure nitrogen and parts of this mixture are blown out again during the subsequent relaxation of pressure, so that the unrequired gases are reduced to a fraction of the proportion previously present each time.
- a pressure of similar magnitude can be applied to the other side of the movable part of the system, e.g. the diaphragm or bellows. This reinforces the flushing action, since a pumping action is applied to the contents of the system by the return movement of the diaphragm or of the bellows. Furthermore, the properties of the material of the diaphragm or bellows are improved by the application of pressure on both sides as compared with unilateral loading.
- a charging apparatus for performing the method of the invention is characterized by a first container for the pressurized noncondensible medium and a first pipe which extends therefrom and to which a pressure gauge is connected, in addition to a charging head, and which can be blocked by means of valves when the pressure gauge indicates a predetermined value, the apparatus also being characterized by a second container for pressurized condensible medium, from which container a second pipe, incorporating a measuring device which can be blocked by means of valves, runs to the charging head.
- the second pipe can be connected to the second container at the bottom for example, and the metering device can consist of a liquid-measuring vessel. This arrangement is particularly suitable when fairly large quantities of the condensible medium have to be filled into the system.
- the second pipe can be connected to the top of the second container and the metering device can consist of a measuring chamber with a pressure gauge connected thereto. lf superheated medium is introduced into the measuring chamber, which has a predetermined volume, until a first pressure that can be read off on the pressure gauge is reached, and is then passed into the thermostatic system until the pressure has dropped to a predetermined second value, this ensures that a precisely defined quantity of the condensible medium has passed into the thermostatic system.
- This metering device is particularly suitable for introducing small quantities of the condensible medium. This is desirable for example in the case of thermostatic systems in which it is intended to limit pressure by completely vaporizing the condensible medium at a limiting value for temperature that is somewhat beyond the working range.
- the charging operation can also be rendered automatic if the pressure gauge actuates contacts which close the inlet valve at a predetermined first pressure and, if required, open the outlet valve and, at a predetermined lower second pressure, close the outlet valve and open the inlet valve.
- a reducing valve is fitted on the output side of the second container.
- the condensible medium can be stored in the liquid state and under a relatively high pressure, and after relaxation of the pressure in the reducing valve, the medium is always available with a sufficient degree of superheat.
- a thermostatic system consists of a sensor 1, a working element 2, a capillary tube 3 connecting these two components, and a capillary charging port 4.
- the working element comprises a case 5 and a diaphragm element 6.
- the diaphragm can bear against the two halves of the case in its two end-positions.
- the sensor is connected to a charging head 9 by way of the capillary charging pipe 4.
- This head 9 is connected to a pipe 8.
- the working element controls a valve having two compartments 10 and 11. These two compartments communicate with a connecting pipe 12.
- This nitrogen container 13 is connected to each of the pipes 15 and 16 by way of a reducing valve 14.
- the pipes 15 and 16 contain magnetic valves 17 and 18, the magnetic valve 18 monitoring the connecting pipe 12.
- Fitted in the connecting pipe 12 is a further magnetic valve 19 which opens to atmosphere.
- This magnetic valve 19 is used for discharging nitrogen and air mixed therewith which is flushed from the system.
- the magnetic valve 17 communicates with the charging pipe 8 by way of a pipe 20, to which is connected a pressure gauge 21, and by way ofa magnetic valve 22.
- a container 23 is partly charged with the condensible medium.
- the vapor which corresponds to the pressure at room temperature, passes by way of a reducing valve 24 to a pipe 25, which is connected to a measuring container 27 by way of a magnetic valve 26.
- a pressure gauge 28 Connected to the measuring container 27 is a pressure gauge 28.
- the outlet of the container is connected to a pipe 30 through a magnetic valve 29.
- the container 23, the measuring container 27 and the associated parts can also be replaced by another container 31 to the base of which is connected an outlet pipe 32 which leads, by way ofa valve 33, to a measuring container 34 for fluid.
- the outlet of this container is connected to the pipe 30 through a valve 35.
- the charging pipe 8 also communicates with the atmosphere through a valve 36 and, if required, can be connected to a vacuum pump 38 by way of a further valve 37.
- the charging operation can proceed in the following way: Firstly it is assumed that the thermostatic system is connected to the charging apparatus through its charging port 4. The valves 17 and 22 are then opened. The pressure is automatically determined by the reducing valve 14; the pressure so established obtains in the pipes and thus also in the sensor 1 and in the entire thermostatic system. This pressure can be as great as 28 atmos. for example, this corresponding to the test pressure for the system. The air contained in the pressure is therefore compressed to a fraction of its original volume. The air thus mixes with the nitrogen. The valve 22 is then closed and the valve 36 opened.
- test pressure provides the very considerable advantage that the stresses, which may occur during the welding of a diaphragm element, are compensated by these pressure conditions. The service life of the element is extended by this compensation of the stresses.
- the partial pressure of the nitrogen in the system is then adjusted to the required value.
- the magnetic valve 18 is closed and the magnetic valve 19 opened.
- the pressure gauge 21 can be used to set the pressure if a partial pressure of the nitrogen above that of the atmosphere is required. If this pressure is to be below atmospheric pressure, then instead of the valve 36, a vacuum pump 38 can be connected by way of the magnetic valve 37, the desired reduced pressure being produced, whereafter the valve 36 or 37 and the valve 22 are closed again.
- the system can now be charged with the condensible medium. If the system is charged with a liquid condensible medium, a quantity of liquid is allowed to flow from the container 31 through the valve 33 and into the measuring container 34, the valve 35 being closed. As little as a few cm. or even fractions of a cm. can be measured in the measuring container. When a certain charge level is reached, the valve 33 is closed. Thereafter, the valve 35 is opened until the charge level has dropped to a point at which it corresponds to the required charge quantity. The condensate then flows through the charging port 9 into the sensor 1 and is there mixed with the noncondensible medium present. In certain cases it is advisable to cool the sensor or the thermostatic system in proportion to the room temperature, so that the condensible medium can also pass into the thermostatic system in a reliable manner.
- a still more advantageous method can be used in the case of small quantities of condensible medium, e.g. when pressurelimited valves are used, by measuring off superheated vapor.
- the pressure gauge 28 fitted at this point shows what is the pressure of the superheated gas at room temperature.
- the magnetic valve 26 is then closed and the magnetic valve 29 opened.
- the superheated gas can then flow from the container 27 to the thermostatic system, an at a certain drop in pressure, indicated by the pressure gauge 28, the magnetic valve 29 is closed again. In this case it is advisable to keep the sensor below room temperature, e.g. by means of a cooling device.
- This superheated gas then immediately condenses on the cooler part of the system, and it passes into the thermostatic system in a reliable manner. In this way, very small quantities can be readily determined, since the volume of the container 27 is adapted to suit the quantity of condensible medium that is to be charged into the system, and thus a measurable quantity is reached based on the known equation of state for the gases.
- this method offers the advantage that even when the required quantity is very small and almost incapable of being measured, very accurate charging can be achieved since occasionally droplets can adhere to the walls of the measuring container due, for example, to adherence of liquid to the container walls.
- a thermostatic expansion valve with a pressure limit directly at freezing point this is of considerable advantage since often only a spot of condensate will be present in the subsequently closed thermostatic system.
- the charging port 4 is clamped together by means of jaws and is then soldered up.
- the pressure in the container 27 must be higher than the pressure at the pressure gauge 21 after the noncondensible medium has been introduced.
- a very accurate charge quantity is obtained in the thermostatic system, since the volume of the system is known and is first charged only with superheated gas in the form of nitrogen. Then, the rest of the charge, which can simply be read off from the pressure-drop at the container 27, is introduced.
- the pressure gauge 28 can directly control the valves 28 and 29. If the valve 26 is opened and the valve 29 closed, the pressure in the container 27 rises until the pressure gauge reaches an upper limiting value. At this value, the valve 26 is closed. When the valve 29 is later opened for charging the thermostatic system, the pressure in the container 27 drops until, at a lower limiting value, the valve 29 is closed. When charging takes place on an assembly line, the pressure gauge 28 can also open the valve 29 at the upper limiting value and the valve 26, possibly after a time-lag, at the lower limiting value.
- a method of charging a thermostatic system with a condensible medium and a noncondensible medium comprising the steps of firstly charging the system with said noncondensible medium and secondly charging said system with said condensible medium, said noncondensible medium being charged into said system at a predetermined pressure, said condensible medium being charged into said system in a measured quantity, said noncondensible medium being nitrogen, the method including the step of flushing said system with nitrogen at least once prior to said step of charging said system with said noncondensible medium, said system including a working element having a moving part with chambers on opposite sides thereof and a sensor bulb connected with a capillary tube to one of said chambers, said method including the step of directing nitrogen to the other of said chambers subsequent to said step of flushing said system
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Abstract
The invention relates to a method and apparatus for charging a thermostatic system with condensible and noncondensible mediums such as Freon and nitrogen. The noncondensible medium is introduced first at a predetermined partial pressure followed by the introduction of a measured quantity of the condensible medium. An aspect of the invention involves a preliminary flushing of the system with nitrogen at the system testing pressure such that not only is the system purged of air but the system is tested at the same time.
Description
0 United States Patent [151 3,653,414
Weidner 1 51 Apr. 4, 11972 54] METHOD OF CHARGING A 3,232,324 2/1966 Sokol ..141/3 THERMOSTATIC SYSTEM WITH A 2 33%}: 3; 133g g ess CONDENSIBLE AND A 2,684,805 7/1954 McBean.... NONCQNDENSIBLE MEDIUM 2,527,136 10/1950 Kagi et a1. ..222/s7 x t i [72] lnven or Er c Weidner, Augustenborg, Denmark Primary Examiner Edward J Earls [73] Assignee: Danfoss A/S, Nordborg, Denmark Attorney-Wayne B. Easton [22] Filed: May 11, 1970 ABSTRACT [21] Appl' 36312 The invention relates to a method and apparatus for charging a thermostatic system with condensible and noncondensible [52] U.S. Cl ..l4l/4, 141/9, 141/49, mediums such as Freon and nitrogen. The noncondensible 141/63, 141/104 medium is introduced first at a predetermined partial pressure [51] Int. Cl ..B65b 31/02 followed by he introduc ion of a measured quantity of the [58] Field of Search ..73/368.2, 368.4, 368.6; n n i le medi m- An a pe of the inv ntion involves a 141/1-5, 7-9, 1 1, 18, 20, 31, 37, 39, 47, 49, 63, 61, preliminary flushing of the system with nitrogen at the system 66, 82, 104, 197; 222/3, 4, 57 testing pressure such that not only is the system purged of air but the system is tested at the same time. 56] References Cited 1 Claim, 1 Drawing Figure UNITED STATES PATENTS 2,780,899 2/1957 Benson et al ..l41/3 X Patented April 4, 1972 7 3,653,414
31 :lt 20\ Ti: 1;:
METHOD OF CHARGING A THERMOSTATIC SYSTEM WITH A CONDENSIBLE AND A NONCONDENSIBLE MEDIUM The invention relates to a method of charging a thermostatic system with a condensible and a noncondensible medium, andto a charging apparatus for performing this method.
In the case of thermostatic systems which consist for example of a temperature sensor and a working element connected thereto by way of a capillary tube, it is known to use charge materials which consist of a medium which is condensible over a working temperature range and of a medium which is not condensible over a working temperature range. Among the condensible media are sulphur dioxide and halogenized hydrocarbons such as methyl chloride or the substances marketed under the trade names Freon or Frigen. Nitrogen or another inert gas is used as the noncondensible medium.
For the purpose of charging the thermostatic system, it is first evacuated, filled with the condensible medium in vapor form and then charged with the noncondensible medium to the point at which the required total pressure is reached. Surprisingly, in the majority of cases the required temperaturepressure, curves that would be expected as the result of the charged quantity of condensible medium, have not been obtained. Frequently, the curves obtained have even diverged from each other.
The object of the invention is to provide a charging method which provides perfectly reproducible results and enables the performance of the method to be still further simplified.
According to the invention, this object is achieved by first charging the noncondensible medium into the system and then the condensible medium.
The invention is based upon the heretofore unobserved fact that the condensible medium, which is first filled into the system and is in vapor form, partially condenses under the pressure at which the noncondensible medium is charged into the system so that the condensible medium thus undergoes considerable reduction in volume. Consequently, a higher proportion of noncondensible medium is charged into the system than corresponds to the required quantitative ratio. Furthermore, the quantity of the condensate is very much dependent upon temperature. Slight changes in the charging conditions, e.g. in the room temperature, lead to clearly differing temperature-curves. If on the other hand, in accordance with the invention, the system is first charged with the noncondensible medium, this risk is no longer run, since its volume can diminish only in dependence upon the charging pressure but not as a result of condensation. Thus there arise no difficulties in filling the thermostatic system with a measured quantity of the condensible medium.
This can be done for example by charging the noncondensible medium into the system up to a partial pressure corresponding to the required mix ratio and then charging the condensible medium in a measured quantity. For example, a quantity of liquid condensate, measured in a measuring chamber, can be charged into the thermostatic system. For practical purposes it is simplest to measure the condensible medium in the superheated condition and to fill it into the system.
A particular advantage is obtained here if at least part of the thermostatic system is cooled. This ensures that the condensible medium is condensed at this cooled part and passes into the thermostatic system rapidly and as completely as required.
The normal use of nitrogen as the noncondensible medium offers particular advantages. The system can then be flushed with nitrogen before being charged with the required quantity of nitrogen. This avoids the need for the considerably more expensive evacuation of the thermostatic system. Flushing does not need to be carried out with very great intensity, since the air previously filling the system will have already had a nitrogen content of approximately 78 percent.
It is for example sufficient if the flushing operation is carried out by charging the system with nitrogen at an excess pressure and then relaxing the pressure. The flushing operation can be repeated several times if required. During each flushing operation parts of the unrequited gases are mixed with pure nitrogen and parts of this mixture are blown out again during the subsequent relaxation of pressure, so that the unrequired gases are reduced to a fraction of the proportion previously present each time.
If the flushing pressure is raised to the test pressure for the system, not only is a particularly good flushing effect achieved, but the compressive strength of the system is tested at the same time.
After at least one flushing operation, a pressure of similar magnitude can be applied to the other side of the movable part of the system, e.g. the diaphragm or bellows. This reinforces the flushing action, since a pumping action is applied to the contents of the system by the return movement of the diaphragm or of the bellows. Furthermore, the properties of the material of the diaphragm or bellows are improved by the application of pressure on both sides as compared with unilateral loading.
A charging apparatus for performing the method of the invention is characterized by a first container for the pressurized noncondensible medium and a first pipe which extends therefrom and to which a pressure gauge is connected, in addition to a charging head, and which can be blocked by means of valves when the pressure gauge indicates a predetermined value, the apparatus also being characterized by a second container for pressurized condensible medium, from which container a second pipe, incorporating a measuring device which can be blocked by means of valves, runs to the charging head. By actuating the valves in the first pipe in dependence upon the value indicated by the pressure gauge, the noncondensible medium can be charged into the thermostatic system through the charging head at a predetermined pressure. Actuation of the valves in the second pipe enables the system, with the help of the metering device, then to be charged with the required quantity of condensible medium.
The second pipe can be connected to the second container at the bottom for example, and the metering device can consist of a liquid-measuring vessel. This arrangement is particularly suitable when fairly large quantities of the condensible medium have to be filled into the system. In an alternative arrangement, the second pipe can be connected to the top of the second container and the metering device can consist of a measuring chamber with a pressure gauge connected thereto. lf superheated medium is introduced into the measuring chamber, which has a predetermined volume, until a first pressure that can be read off on the pressure gauge is reached, and is then passed into the thermostatic system until the pressure has dropped to a predetermined second value, this ensures that a precisely defined quantity of the condensible medium has passed into the thermostatic system. This metering device is particularly suitable for introducing small quantities of the condensible medium. This is desirable for example in the case of thermostatic systems in which it is intended to limit pressure by completely vaporizing the condensible medium at a limiting value for temperature that is somewhat beyond the working range.
The charging operation can also be rendered automatic if the pressure gauge actuates contacts which close the inlet valve at a predetermined first pressure and, if required, open the outlet valve and, at a predetermined lower second pressure, close the outlet valve and open the inlet valve.
Expediently, a reducing valve is fitted on the output side of the second container. In this way the condensible medium can be stored in the liquid state and under a relatively high pressure, and after relaxation of the pressure in the reducing valve, the medium is always available with a sufficient degree of superheat.
The invention will now be described in more detail by reference to equipment suitable for the charging method. This equipment is illustrated schematically in the drawing.
A thermostatic system consists of a sensor 1, a working element 2, a capillary tube 3 connecting these two components, and a capillary charging port 4. The working element comprises a case 5 and a diaphragm element 6. The diaphragm can bear against the two halves of the case in its two end-positions. For charging purposes, the sensor is connected to a charging head 9 by way of the capillary charging pipe 4. This head 9 is connected to a pipe 8. The working element controls a valve having two compartments 10 and 11. These two compartments communicate with a connecting pipe 12.
Nitrogen under very high pressure, and in particular the test pressure for the thermostatic system, is present in the container 13. This nitrogen container 13 is connected to each of the pipes 15 and 16 by way ofa reducing valve 14. The pipes 15 and 16 contain magnetic valves 17 and 18, the magnetic valve 18 monitoring the connecting pipe 12. Fitted in the connecting pipe 12 is a further magnetic valve 19 which opens to atmosphere. This magnetic valve 19 is used for discharging nitrogen and air mixed therewith which is flushed from the system. The magnetic valve 17 communicates with the charging pipe 8 by way of a pipe 20, to which is connected a pressure gauge 21, and by way ofa magnetic valve 22.
A container 23 is partly charged with the condensible medium. The vapor which corresponds to the pressure at room temperature, passes by way of a reducing valve 24 to a pipe 25, which is connected to a measuring container 27 by way of a magnetic valve 26. Connected to the measuring container 27 is a pressure gauge 28. The outlet of the container is connected to a pipe 30 through a magnetic valve 29. The container 23, the measuring container 27 and the associated parts can also be replaced by another container 31 to the base of which is connected an outlet pipe 32 which leads, by way ofa valve 33, to a measuring container 34 for fluid. The outlet of this container is connected to the pipe 30 through a valve 35. The charging pipe 8 also communicates with the atmosphere through a valve 36 and, if required, can be connected to a vacuum pump 38 by way of a further valve 37. The charging operation can proceed in the following way: Firstly it is assumed that the thermostatic system is connected to the charging apparatus through its charging port 4. The valves 17 and 22 are then opened. The pressure is automatically determined by the reducing valve 14; the pressure so established obtains in the pipes and thus also in the sensor 1 and in the entire thermostatic system. This pressure can be as great as 28 atmos. for example, this corresponding to the test pressure for the system. The air contained in the pressure is therefore compressed to a fraction of its original volume. The air thus mixes with the nitrogen. The valve 22 is then closed and the valve 36 opened. Part of the nitrogen-air mixture can escape therethrough, and the pressures drops to that of the atmosphere. At this moment only about one-thirtieth of the unrequired atmospheric air is contained in the charge gas. Where nitrogen is used as the charge gas, the proportion of gases other than nitrogen is less than 1 percent. This quantity is generally permissible. On the other hand however the proportion of foreign gases can be still further reduced by a further similar flushing operation. At the same time the magnetic valve 18 is opened, nitrogen flowing at the same pressure into the compartments l0 and 11 by way of the pipe 12. This pressure is maintained while the valve 36 is opened. In this way this pressure reinforces the emptying of the diaphragm case by way of the sensor and magnetic valve 36. Here, it is of particular advantage for this to take place in the diaphragm casing from which, in the normal way, atmospheric air is most difficult to remove.
These high pressures also enable a simultaneous check to be carried out to determine whether the system is fluid-tight. If the case 5 is loaded with the same pressure on both sides, then by simply immersing the entire valve body in a liquid, it is possible to ascertain whether leaking elements are present, since gas bubbles will occur if they are. Furthermore, the test pressure provides the very considerable advantage that the stresses, which may occur during the welding of a diaphragm element, are compensated by these pressure conditions. The service life of the element is extended by this compensation of the stresses.
The partial pressure of the nitrogen in the system is then adjusted to the required value. For this purpose, the magnetic valve 18 is closed and the magnetic valve 19 opened. If the thermostatic system is now under excess pressure and the magnetic valve 17 is closed, the pressure gauge 21 can be used to set the pressure if a partial pressure of the nitrogen above that of the atmosphere is required. If this pressure is to be below atmospheric pressure, then instead of the valve 36, a vacuum pump 38 can be connected by way of the magnetic valve 37, the desired reduced pressure being produced, whereafter the valve 36 or 37 and the valve 22 are closed again.
The system can now be charged with the condensible medium. If the system is charged with a liquid condensible medium, a quantity of liquid is allowed to flow from the container 31 through the valve 33 and into the measuring container 34, the valve 35 being closed. As little as a few cm. or even fractions of a cm. can be measured in the measuring container. When a certain charge level is reached, the valve 33 is closed. Thereafter, the valve 35 is opened until the charge level has dropped to a point at which it corresponds to the required charge quantity. The condensate then flows through the charging port 9 into the sensor 1 and is there mixed with the noncondensible medium present. In certain cases it is advisable to cool the sensor or the thermostatic system in proportion to the room temperature, so that the condensible medium can also pass into the thermostatic system in a reliable manner.
A still more advantageous method can be used in the case of small quantities of condensible medium, e.g. when pressurelimited valves are used, by measuring off superheated vapor. This takes places in the following manner: a liquid condensible medium is present in the container 23 at room temperature. Saturated vapor is formed above this medium and the pressure thereof corresponds to the room temperature. This saturated vapor can now flow into the pipe 25 through an automaticallyoperating pressure-reducing valve, the saturated vapors becoming superheated and passing through the open magnetic valve 26 into the measuring container 27. The pressure gauge 28 fitted at this point shows what is the pressure of the superheated gas at room temperature. The magnetic valve 26 is then closed and the magnetic valve 29 opened. The superheated gas can then flow from the container 27 to the thermostatic system, an at a certain drop in pressure, indicated by the pressure gauge 28, the magnetic valve 29 is closed again. In this case it is advisable to keep the sensor below room temperature, e.g. by means of a cooling device. This superheated gas then immediately condenses on the cooler part of the system, and it passes into the thermostatic system in a reliable manner. In this way, very small quantities can be readily determined, since the volume of the container 27 is adapted to suit the quantity of condensible medium that is to be charged into the system, and thus a measurable quantity is reached based on the known equation of state for the gases. Compared with direct charging with the liquid medium, this method offers the advantage that even when the required quantity is very small and almost incapable of being measured, very accurate charging can be achieved since occasionally droplets can adhere to the walls of the measuring container due, for example, to adherence of liquid to the container walls. In the case of a thermostatic expansion valve with a pressure limit directly at freezing point, this is of considerable advantage since often only a spot of condensate will be present in the subsequently closed thermostatic system.
Thereafter, the charging port 4 is clamped together by means of jaws and is then soldered up. In this system there is no need to check whether the correct quantity has in fact entered, since it is not possible for the noncondensible medium now to compress the superheated vapor of the condensible medium and thus for an uncontrolled quantity of noncondensible medium to be charged into the system. It is obvious that the pressure in the container 27 must be higher than the pressure at the pressure gauge 21 after the noncondensible medium has been introduced. Thus a very accurate charge quantity is obtained in the thermostatic system, since the volume of the system is known and is first charged only with superheated gas in the form of nitrogen. Then, the rest of the charge, which can simply be read off from the pressure-drop at the container 27, is introduced.
If the pressure gauge 28 is provided with contacts, it can directly control the valves 28 and 29. If the valve 26 is opened and the valve 29 closed, the pressure in the container 27 rises until the pressure gauge reaches an upper limiting value. At this value, the valve 26 is closed. When the valve 29 is later opened for charging the thermostatic system, the pressure in the container 27 drops until, at a lower limiting value, the valve 29 is closed. When charging takes place on an assembly line, the pressure gauge 28 can also open the valve 29 at the upper limiting value and the valve 26, possibly after a time-lag, at the lower limiting value.
lclaim:
1. A method of charging a thermostatic system with a condensible medium and a noncondensible medium comprising the steps of firstly charging the system with said noncondensible medium and secondly charging said system with said condensible medium, said noncondensible medium being charged into said system at a predetermined pressure, said condensible medium being charged into said system in a measured quantity, said noncondensible medium being nitrogen, the method including the step of flushing said system with nitrogen at least once prior to said step of charging said system with said noncondensible medium, said system including a working element having a moving part with chambers on opposite sides thereof and a sensor bulb connected with a capillary tube to one of said chambers, said method including the step of directing nitrogen to the other of said chambers subsequent to said step of flushing said system
Claims (1)
1. A method of charging a thermostatic system with a condensible medium and a noncondensible medium comprising the steps of firstly charging the system with said noncondensible medium and secondly charging said system with said condensible medium, said noncondensible medium being charged into said system at a predetermined pressure, said condensible medium being charged into said system in a measured quantity, said noncondensible medium being nitrogen, the method including the step of flushing said system with nitrogen at least once prior to said step of charging said system with said noncondensible medium, said system including a working element having a moving part with chambers on opposite sides thereof and a sensor bulb connected with a capillary tube to one of said chambers, said method including the step of directing nitrogen to the other of said chambers subsequent to said step of flushing said system.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US3631270A | 1970-05-11 | 1970-05-11 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US3653414A true US3653414A (en) | 1972-04-04 |
Family
ID=21887881
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US36312A Expired - Lifetime US3653414A (en) | 1970-05-11 | 1970-05-11 | Method of charging a thermostatic system with a condensible and a noncondensible medium |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US3653414A (en) |
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3762450A (en) * | 1971-07-29 | 1973-10-02 | Union Oil Co | Ecological handling of volatile liquids |
| US3789888A (en) * | 1969-12-29 | 1974-02-05 | Hayssen Mfg Co | Gas flushing system for vertical form, fill and seal machines |
| EP0142866A3 (en) * | 1983-11-22 | 1986-12-10 | Consolidated Controls Corporation | Compact implantable medication infusion unit and method of filling and sealing the pressure stabilizing chamber thereof |
| US4667855A (en) * | 1980-11-25 | 1987-05-26 | W. R. Grace & Co. | Method of reducing failure of pressurized container valves |
| US4745953A (en) * | 1985-11-26 | 1988-05-24 | Dai Nippon Insatsu Kabushiki Kaisha | Device and method for controlling the concentration of aqueous solution of alcohol |
| US4976295A (en) * | 1987-05-22 | 1990-12-11 | Seitz Enzinger Noll Maschinenbau Aktiengesellschaft | Apparatus for filling containers with carbonated liquids under counterpressure as dispensed having different filling characteristics by adjusting pressure differential without changing flow control mechanism |
| US5339875A (en) * | 1992-02-08 | 1994-08-23 | Eastman Kodak Company | Liquid preparation method |
| US5353848A (en) * | 1993-04-27 | 1994-10-11 | The Boc Group, Inc. | Method of filling gas cylinders |
| US5445193A (en) * | 1992-04-01 | 1995-08-29 | Agfa-Gevaert Aktiengesellschaft | Apparatus for preparing and dispensing liquids for the treatment of photosensitive material |
| US5642761A (en) * | 1996-02-21 | 1997-07-01 | Fountain Fresh, Inc. | Liquid proportioning apparatus and method |
| US5992478A (en) * | 1996-07-08 | 1999-11-30 | The Boc Group, Inc. | Method and apparatus for filling containers with gas mixtures |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2475317A (en) * | 1945-01-30 | 1949-07-05 | Honeywell Regulator Co | Thermometer filling system |
| US2527136A (en) * | 1946-08-16 | 1950-10-24 | Western Electric Co | Fluid mixing apparatus |
| US2684805A (en) * | 1950-08-09 | 1954-07-27 | Carter Prod Inc | Method for charging liquid products and volatile propellants into pressure-tight containers |
| US2780899A (en) * | 1951-12-19 | 1957-02-12 | Process Engineering Inc | Apparatus for filling a fire extinguisher |
| US2846118A (en) * | 1955-03-14 | 1958-08-05 | Dale Products Inc | Gas flow control system |
| US3232324A (en) * | 1963-01-18 | 1966-02-01 | American Lecithin Co | Method and apparatus for filling aerosol dispensers |
-
1970
- 1970-05-11 US US36312A patent/US3653414A/en not_active Expired - Lifetime
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2475317A (en) * | 1945-01-30 | 1949-07-05 | Honeywell Regulator Co | Thermometer filling system |
| US2527136A (en) * | 1946-08-16 | 1950-10-24 | Western Electric Co | Fluid mixing apparatus |
| US2684805A (en) * | 1950-08-09 | 1954-07-27 | Carter Prod Inc | Method for charging liquid products and volatile propellants into pressure-tight containers |
| US2780899A (en) * | 1951-12-19 | 1957-02-12 | Process Engineering Inc | Apparatus for filling a fire extinguisher |
| US2846118A (en) * | 1955-03-14 | 1958-08-05 | Dale Products Inc | Gas flow control system |
| US3232324A (en) * | 1963-01-18 | 1966-02-01 | American Lecithin Co | Method and apparatus for filling aerosol dispensers |
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3789888A (en) * | 1969-12-29 | 1974-02-05 | Hayssen Mfg Co | Gas flushing system for vertical form, fill and seal machines |
| US3762450A (en) * | 1971-07-29 | 1973-10-02 | Union Oil Co | Ecological handling of volatile liquids |
| US4667855A (en) * | 1980-11-25 | 1987-05-26 | W. R. Grace & Co. | Method of reducing failure of pressurized container valves |
| EP0142866A3 (en) * | 1983-11-22 | 1986-12-10 | Consolidated Controls Corporation | Compact implantable medication infusion unit and method of filling and sealing the pressure stabilizing chamber thereof |
| US4745953A (en) * | 1985-11-26 | 1988-05-24 | Dai Nippon Insatsu Kabushiki Kaisha | Device and method for controlling the concentration of aqueous solution of alcohol |
| US4976295A (en) * | 1987-05-22 | 1990-12-11 | Seitz Enzinger Noll Maschinenbau Aktiengesellschaft | Apparatus for filling containers with carbonated liquids under counterpressure as dispensed having different filling characteristics by adjusting pressure differential without changing flow control mechanism |
| US5339875A (en) * | 1992-02-08 | 1994-08-23 | Eastman Kodak Company | Liquid preparation method |
| US5445193A (en) * | 1992-04-01 | 1995-08-29 | Agfa-Gevaert Aktiengesellschaft | Apparatus for preparing and dispensing liquids for the treatment of photosensitive material |
| US5353848A (en) * | 1993-04-27 | 1994-10-11 | The Boc Group, Inc. | Method of filling gas cylinders |
| US5642761A (en) * | 1996-02-21 | 1997-07-01 | Fountain Fresh, Inc. | Liquid proportioning apparatus and method |
| US5992478A (en) * | 1996-07-08 | 1999-11-30 | The Boc Group, Inc. | Method and apparatus for filling containers with gas mixtures |
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