The present invention generally relates to air conditioning and heating systems and in particular to compressor lubrication.
In refrigeration circuits, some of the oil that lubricates the compressor is entrained in the vapor pumped by the compressor, and the oil circulates throughout the refrigerant circuit. Most refrigerant compressors require the lubricant to reduce friction and help to seal the compression cylinder or cavity. Inevitably, some of the lubricating oil is drawn into the refrigerant vapor stream and circulates throughout the refrigerant circuit and back to the compressor if nothing traps the oil along the way. In conventional refrigerant circuits, the vessel just upstream from the compressor is the “accumulator”, potentially the most likely place for oil to be trapped. But this is typically circumvented by the use of an “oil return hole” near the bottom of the tube that serves as the outlet of the accumulator. While this returns the oil to the compressor, liquid refrigerant can not be stored in the accumulator, as it also would leave by way of the oil return hole. The accumulator is an interesting misnomer in that the typical accumulator can only accumulate liquid briefly, as any liquid refrigerant quickly leaves via an oil return hole.
In circuits using an active charge control (ACC), the oil must be transported through the ACC to the compressor. In a typical ACC, at least one dimension is critical to proper oil return from the ACC to the compressor. If the dimensions within the ACC are not well matched to the size and loading of the compressor, insufficient oil transport from the ACC to the compressor can result.
By way of example, it is desirable to store all inactive liquid refrigerant in the ACC. Refrigerant arriving at the ACC is primarily vapor, but may also include liquid. In either state oil is either entrained in the vapor, or dissolved in the liquid. The vaporized refrigerant passes on through the ACC, but a significant portion of the oil clings to the ACC walls and is trapped there. Liquid arriving at the ACC is trapped there, including the oil dissolved therein.
In circuits using an active charge control (ACC), the oil must be transported through the ACC to the compressor. It has been necessary to provide means of moving oil trapped in the ACC on to the compressor. This was done with a system of splash plates and exit clearances, which caused the oil to become a fine-droplet mist or a tiny bubble consisting of oil surrounding a tiny bit of vapor. The mist and/or bubbles were then entrained in the vapor stream and carried on to the compressor. The problem with this method of oil return is that it is sensitive to the velocity of the refrigerant passing through the ACC, the area of the exit clearance, and even the type of oil used in the system. Careful matching of the compressor and the ACC was required.
As above addressed, and as is well known in the art, typical ACC dimensions are critical to proper oil return from the ACC to the compressor. If the dimensions within the ACC are not well matched to the size and loading of the compressor, insufficient oil transport from the ACC to the compressor can result.
The present invention is directed to air conditioning systems and methods. In a refrigerant circuit containing a compressor, a condenser, an evaporator, a liquid flow control, and an active charge control (ACC), an oil return mechanism operable with the compressor may comprise a heat exchanger including a primary fluid pathway and a secondary fluid pathway, a conduit placing the outlet of the condenser in fluid communication with the primary pathway of the heat exchanger to provide flow of fluid from the condenser through the primary pathway of the heat exchanger, and conduit connecting the ACC in fluid communication with the inlet of the secondary pathway of the heat exchanger and connecting the outlet of the secondary pathway in fluid communication with the compressor inlet to provide a flow of fluid from the ACC, through the secondary pathway and on to the compressor inlet, such that heat energy from the liquid flowing through the primary pathway is transmitted to the refrigerant and oil mix in the secondary pathway and evaporates the refrigerant in the secondary pathway to send refrigerant vapor and compressor oil on to the compressor inlet.
An embodiment of the oil return mechanism may include a vent tube bridging across an elevated portion of the compressor inlet tube to equalize the pressures in the compressor and ACC and to prevent transfer of the refrigerant and oil mix from the ACC to the compressor during the off-cycle of the refrigerant circuit system. The oil return mechanism may include a compressor heater to heat the compressor during the system off-cycles and to prevent refrigerant from condensing in the compressor during off-cycles and to prevent liquid refrigerant from being transferred from the ACC to the compressor during off-cycles of the refrigerant system. The oil return mechanism may include a slotted outlet tube for expediting the return of oil that may stratify and float on top of the refrigerant and oil mix in the ACC. Yet further, embodiments of the oil return mechanism may include one of or any combination of the vent tube, the compressor heater and the slotted outlet tube.
Yet further, the oil return mechanism may include relocating the ACC evaporator tube external to the ACC vessel to further simplify the ACC function and reduce the cost of production of the refrigerant system, and may include the oil return mechanism having one of or any combination of the vent tube, the compressor heater, and the slotted outlet tube. In a refrigerant circuit containing a compressor, a condenser, an evaporator, a liquid flow control, and an active charge control (ACC), an oil return mechanism may comprise a pathway from the near-bottom of the ACC to the compressor inlet with a method aspect of the invention that may include placing a small liquid outlet near a bottom portion of the ACC outlet in fluid communication with the compressor inlet, using a conduit sized to allow approximately 1% to 3% of the refrigerant arriving at the ACC from the system evaporator to flow from the near-bottom of the ACC through the pathway to the compressor, placing the conduit, or secondary pathway of the heat exchanger in thermal contact with a heat source sufficient to completely evaporate all the refrigerant passing through the pathway, such that refrigerant vapor and compressor oil will be delivered to the compressor inlet. Yet further, the method may comprise at least one of the condenser and the evaporator having at least one earth loop conduit extending down into the earth in a loop borehole, trench or pit, the earth loop extending into the borehole comprising at least two tubes joined in fluid communication at their distal ends.
The oil return mechanism (ORM) of the present invention is desirably less sensitive to the typical variables presented in the art as addressed above. Embodiments of the invention operate on a principle of physically removing oil from the ACC by constantly draining a small portion of the liquid and oil mix in the ACC and sending it on to the compressor by way of a heat exchanger, which heat exchanger serves to evaporate the refrigerant in the drained mix, and send the vapor and separated oil on to the compressor. By sending the liquid/oil mix through the heat exchanger, sending liquid refrigerant directly into the compressor is desirably avoided.
By way of example, the amount of the drained mix is approximately 1 to 3 percent of the total refrigerant circulating through the system. If the system is circulating, say, 500 pounds per hour of refrigerant, the oil return mix might be on the order of 6 or 7 pounds per hour. The amount of mix normally in the ACC might be on the order of about 8 or 9 pounds, thus the mix in the ACC gets it's oil removed about every hour or two. The ACC, by its very nature, demands that a small amount of liquid, same as the amount drained by the ORM, is constantly trapped by the ACC.
A motivating force that moves the oil return mix is first the “vertical head” of the liquid in the ACC, as the mix is drawn from near the bottom of the ACC, and the ACC normally operates about half full of liquid. At the other end, a Venturi serves to “suck” the oil and vapor into the entrance pipe of the compressor, just upstream from the compressor. The compressor entrance tube may be shaped to be close to a floor at a point where it is penetrated by a Venturi for the ORM.
For a fuller understanding of the invention, reference is made to the following detailed description, taken in connection with the accompanying drawings illustrating various embodiments of the present invention, in which:
The present invention will now be described more fully with reference to the accompanying drawings and photos in which alternate embodiments of the invention are shown and described. It is to be understood that the invention may be embodied in many different forms and should not be construed as limited to the illustrated embodiments set forth herein. Rather, these embodiments are provided so that this disclosure may be thorough and complete, and will convey the scope of the invention to those skilled in the art.
It will be appreciated that embodiments of the invention comprise oil return mechanisms differing from the typical ACC, and are effective over a much wider range of compressor sizes and loadings. Additionally with the oil return mechanisms of the present invention, the ACC is a much simpler mechanism and thus more commercially desirable.
With reference initially to
As illustrated by way of example with reference to
With continued reference to
With continued reference to
As illustrated with continued reference to
With continued reference to
Optionally, a heater 60 may be operable with the compressor 12 for heating the compressor at least during a system off-cycle, thus preventing refrigerant from condensing in the compressor during the off-cycle and to prevent liquid refrigerant from being transferred from the ACC 18 to the compressor during the off-cycle of the system 10.
With further regard for the ACC 18, and with continued reference to
In one embodiment as further illustrated with reference to
With reference to
In one embodiment of the invention, illustrated with reference now to
With continued reference to
With continued reference to
By way of example, the restrictor 44 may be sized such that a small amount of the liquid refrigerant, less than 5% (and likely only about 1% to 3%). traversing the system evaporator 38 is returned to the compressor 12 by way of the secondary pathway 32 and the heat exchanger 28. By constantly removing a small portion of the concentrated refrigerant/oil mix, the concentration of oil in the mix is constantly reduced until equilibration is reached and the level of oil in the compressor is stabilized at a desired level. In effect, the liquid/oil mix in the ACC 18 is changed out about once every one or two hours, depending on compressor size and loading and on the size of the ACC vessel. Therefore, the relative small amount of liquid refrigerant that passes through the secondary pathway 32 is vaporized by the heat exchanger 28 and is entered into the system at the compressor inlet 14.
With continued reference to
In operation, the liquid in the ACC 18 is colder than the liquid coming out of the condenser 12. Therefore, there is a temperature differential between the primary pathway 30 and the secondary pathway 32 of the heat exchanger 28. Because of the pressure differential and temperature differential, the liquid refrigerant mixed with compressor oil leaves the ACC 18, enters the secondary pathway space within the heat exchanger 28, and evaporates as it moves toward the raised end 74 of the heat exchanger. Heat energy in primary pathway 30 is transferred to the secondary pathway 32 to evaporate the liquid refrigerant in the secondary pathway 32 within the heat exchanger 28. When the liquid refrigerant completes evaporation in the heat exchanger 28, at varying levels 94, illustrated with reference again to
With continued reference to
When the refrigerant circuit is shut down, the liquid mix 92 traverses through the strainer, restrictor, heat exchanger, connecting tubes and inlet port, and fills the lower portion of the compressor inlet tube until the liquid levels in the tube are at the same elevation as the liquid level in the ACC. As the off-cycle continues, the ACC and its contents warm up and the pressure in the ACC increases. At the same time, the compressor cools off and the pressure in the compressor decreases. In systems that have a long off-cycle, it is possible that this increasing pressure differential causes an excess of liquid mix to be transferred into the compressor during the off cycle. As above described with reference to
With reference now to
As above described with reference to
With reference to
As above described with reference to embodiments of the invention, by way of example to
Many modifications and other embodiments of the invention will come to the mind of one skilled in the art having the benefit of the teachings presented in the foregoing descriptions and the associated drawings and photos. Therefore, it is to be understood that the invention is not to be limited to the specific embodiments disclosed, and that modifications and alternate embodiments are intended to be included within the scope of the claims supported by this specification.
This application claims the benefit of and priority to Provisional Application Ser. No. 61/150,815 having filing date of Feb. 9, 2009 for “Oil Return Mechanism For Active Charge Control In An Air Conditioning System, the disclosure of which is incorporated herein by reference in its entirety, and commonly owned.
Number | Name | Date | Kind |
---|---|---|---|
1899378 | Zouck | Feb 1933 | A |
2223882 | Beline | Dec 1940 | A |
2299811 | Feicht | Oct 1942 | A |
2461342 | Obreiter, Jr. | Feb 1949 | A |
2476044 | Kals | Jul 1949 | A |
2617265 | Ruff | Nov 1952 | A |
2721728 | Higgins | Oct 1955 | A |
2859596 | Evans | Nov 1958 | A |
2901894 | Zearfoss, Jr. | Sep 1959 | A |
2977773 | De Kanter | Apr 1961 | A |
3012414 | La Porte | Dec 1961 | A |
3491544 | Webber | Jan 1970 | A |
3600904 | Tilney | Aug 1971 | A |
3714028 | Hallman | Jan 1973 | A |
3785169 | Gylland, Jr. | Jan 1974 | A |
4006602 | Fanberg | Feb 1977 | A |
4030315 | Harnish | Jun 1977 | A |
4066869 | Apaloo | Jan 1978 | A |
4187695 | Schumacher | Feb 1980 | A |
4299098 | Derosier | Nov 1981 | A |
4798058 | Gregory | Jan 1989 | A |
5042271 | Manz | Aug 1991 | A |
5265437 | Saperstein et al. | Nov 1993 | A |
5461876 | Dressler | Oct 1995 | A |
5561985 | Cochran | Oct 1996 | A |
5613368 | Marohl et al. | Mar 1997 | A |
5622055 | Mei et al. | Apr 1997 | A |
2887444 | Toyoshima et al. | Mar 1999 | A |
5887441 | Spauschus et al. | Mar 1999 | A |
6343486 | Mizukami | Feb 2002 | B1 |
6457325 | Vetter | Oct 2002 | B1 |
6467300 | Noble | Oct 2002 | B1 |
6694766 | Johnson, Jr. et al. | Feb 2004 | B1 |
7080524 | Wiggs | Jul 2006 | B2 |
7086240 | Zugibe et al. | Aug 2006 | B1 |
7111472 | Cloud | Sep 2006 | B1 |
7578140 | Wiggs | Aug 2009 | B1 |
20050262873 | Hirota | Dec 2005 | A1 |
20060075775 | Boiarski et al. | Apr 2006 | A1 |
20080223073 | Fralick | Sep 2008 | A1 |
20080282713 | Anderson et al. | Nov 2008 | A1 |
20090120120 | Wiggs | May 2009 | A1 |
20110120154 | Woolley | May 2011 | A1 |
Number | Date | Country |
---|---|---|
2574832 | Jan 1997 | JP |
10141813 | May 1998 | JP |
2008193759 | Aug 2008 | JP |
Number | Date | Country | |
---|---|---|---|
20100218522 A1 | Sep 2010 | US |
Number | Date | Country | |
---|---|---|---|
61150815 | Feb 2009 | US |