The present inventions relate generally to industrial air dryers for compressed air systems.
Compressed air is commonly used in factories to power pneumatic tools and to blow air onto various surfaces for cleaning, expanding bags, moving parts, etc. Typically, factories have a centralized compressed air system installed that feeds a network of compressed air piping that supplies numerous tools or stations with compressed air. Thus, one or more centralized air compressors may be used to supply an entire factory space with compressed air.
However, it is known that air compressors which draw air from the surrounding atmosphere also introduce moisture into the compressed air from the water vapor naturally contained in atmospheric air. Moisture within compressed air used in factories can cause numerous problems. For example, in the case of power tools that use compressed air as a power source, moisture within the supplied compressed air can cause corrosion of the internal components of the tool. In addition, where compressed air is blown onto surfaces, any moisture within the compressed air will also be blown onto the surface along with the blown air. This can be particularly problematic where it is a requirement that the surface remain dry, such as food packaging operations, and can also be a problem with delicate surfaces that might be damaged by water particles within the compressed air.
Due to the problems associated with moisture within compressed air systems, various types of air drying systems may be used in industrial factories to remove moisture contained within compressed air. While such systems are useful and adequately address the potential problems associated with moisture in compressed air, such systems can be expensive to operate and maintain. Thus, it would be desirable to provide improved air drying systems for industrial factories.
A compressed air drying system is described for removing moisture from compressed air. The system includes a reservoir of liquid coolant that is shared between multiple air drying units. Liquid coolant from the reservoir flows to a heat exchanger in each of the drying units to cool compressed air flowing through each drying unit. The liquid coolant is mixed in the reservoir to ensure that warm coolant from one of the drying units does not flow directly into one of the outlets. The invention may also include any other aspect described below in the written description or in the attached drawings and any combinations thereof.
The invention may be more fully understood by reading the following description in conjunction with the drawings, in which:
Referring now to the figures, and particularly
As shown, all of the air inlets 14 of the drying units 12 may be connected to a common inlet air header 16. The inlet air header 16 is typically a metal pipe with a larger passageway than the air inlets 14 of the individual drying units 12. The inlet air header 16 is connected to a compressed air supply which typically includes one or more air compressors that draw air from the surrounding atmosphere and compresses it to a pressure between 100-200 psi. Similarly, all of the air outlets 18 of the drying units 12 may be connected to a common outlet air header 20. The outlet air header 20 is also typically a metal pipe with a larger passageway than the air outlets 18 of the individual drying units 12. The outlet air header 20 is connected to a network of tools or stations in the factory that use the compressed air for a variety of uses. It is understood that the compressed air system 10 is also likely to have various compressed air storage tanks between the compressor(s) and the air drying system 10 and/or between the air drying system 10 and the tools and/or stations where the compressed air is used. It is also understood that each drying unit 12 may be provided with a separate control panel and controller to control the various functions of the air dryer 12 or a common controller may be provided for the entire system 10.
Turning to
Referring to the first air drying unit 12 in
The precooler/re-heater 22 is a heat exchanger 22 that exchanges heat between the incoming air flow and the outgoing air flow. That is, the incoming air flow is warm relative to the outgoing air flow. As described below, the air is cooled within the dryer 12 to withdraw moisture from the air. Thus, the precooler/re-heater 22 increases efficiency by cooling the incoming air with the outgoing air prior to additional cooling that occurs thereafter. Also, it is undesirable for the outgoing air to be too cool since this would cool the compressed air piping and cause condensation of water vapor on the exterior of the piping. Thus, the precooler/re-heater 22 prevents this from happening by heating the outgoing air using the warm incoming air.
The main cooler 24 is another heat exchanger 24 that performs the primary cooling of the compressed air. As described further below, the main cooler 24 may use a liquid coolant, such as a glycol and water mixture, to cool the compressed air. The liquid coolant may be stored in a shared reservoir 28 and may be cooled by separate refrigerant cooling systems 30 in each of the drying units 12. After the compressed air has been cooled by the main cooler 24 (e.g., to below 5° C.), the moisture separator 26 withdraws moisture from the compressed air. The withdrawn moisture is then removed through a drain 32. Thus, the compressed air entering the re-heater side 22B of the precooler/re-heater 22 and exiting the dryer 12 has been dried by removing water vapor from the compressed air. It is understood that airflow through the air dryer 12 need not be separately forced or circulated therethrough, but instead may flow through the dryer 12 as air is used by the compressed air demand and replaced by the compressed air supply. That is, any compressed air that flows to the compressed air demand from the compressed air supply must first pass through the dryer 12 (or another dryer 12 in the system 10) due to the location of the dryer 12 between the supply and demand.
As shown in
Preferably, the liquid coolant is cooled in each of the drying units 12 by a separate refrigerant cooling system 30 in each unit 12. Thus, each of the drying units 12 has a refrigerant heat exchanger 44. The portion of liquid coolant flowing to a respective drying unit 12 may then flow through one side of the refrigerant heat exchanger 44 as the liquid coolant flows back from the main cooler 24 to the reservoir 28. A refrigerant flows through the other side of the refrigerant heat exchanger 44 to cool the liquid coolant. The refrigerant side of the refrigerant heat exchanger 44 may be considered to be an evaporator where the refrigerant evaporates and absorbs heat from the liquid coolant side of the refrigerant heat exchanger 44. The refrigerant vapor is then compressed to a higher pressure (and higher temperature) by a refrigerant compressor 46. The refrigerant then passes through a refrigerant condenser 48 that cools and liquefies the refrigerant. The condenser 48 is another heat exchanger 48 with a fan 50 that blows ambient air across the condenser 48 to dissipate heat from the refrigerant. An expansion valve 52 then reduces the pressure and temperature of the liquid refrigerant (e.g., to convert the refrigerant to a vapor). The low pressure, low temperature refrigerant then absorbs heat from the liquid coolant within the refrigerant heat exchanger 44, which results in lowering the temperature of the liquid coolant.
Thus, cooling of the liquid coolant is distributed between the refrigerant cooling systems 30 of the air drying units 12. That is, each of the refrigerant cooling systems 30 cools the portion of liquid coolant that flows through the respective air drying unit 12. As a result, the liquid coolant in the shared reservoir 28 is cooled by a combination of multiple refrigeration systems 30, and the average temperature of the liquid coolant in the reservoir 28 is determined by the cooling contributed by the multiple refrigeration systems 30 together. This allows the refrigeration systems 30 of the multiple drying units 12 to operate independently of each other. For instance, the refrigeration system 30 of one of the drying units 12 may be turned off while one or more of the refrigeration systems 30 in the other drying units 12 continues to operate. This may be useful to improve energy efficiency of the air drying system 10 by shutting down one or more of the refrigeration systems 30 when compressed air demand is low.
When the refrigeration system 30 of a drying unit 12 is off, the respective drying unit 12 may continue to cool compressed air with the liquid coolant. However, the drying unit 12 with a refrigeration system 30 that has been shut off does not contribute to cooling the liquid coolant. In this case, the liquid coolant acts as a heat sink and stores cold energy that has been contributed by the other drying units 12 with refrigeration systems 30 that are running. Thus, all of the drying units 12 can continue to cool compressed air but with less overall energy needed since not all of the refrigeration systems 30 may be running if compressed air demand is low. Although
Although an air drying unit 12 with a refrigeration system 30 that has been turned off may continue to cool compressed air as described above by relying upon cold energy contributed to the liquid coolant by the other refrigeration systems 30, the liquid coolant returning to the reservoir 28 from a drying unit 12 with a disabled refrigeration system 30 will be warmer than the liquid coolant returning from drying units 12 with operating refrigeration systems 30. This may result in an uneven temperature of the liquid coolant in the reservoir 28, and as a result, liquid coolant with different temperatures may be sent to different drying units 12 through the outlets 36. For example, as shown in
Therefore, it is desirable to provide an arrangement in the reservoir 28 that mixes the incoming liquid coolant portions before the liquid coolant exits through the outlets 36. One such arrangement is shown in
Another arrangement is shown in
As shown in
While preferred embodiments of the inventions have been described, it should be understood that the inventions are not so limited, and modifications may be made without departing from the inventions herein. While each embodiment described herein may refer only to certain features and may not specifically refer to every feature described with respect to other embodiments, it should be recognized that the features described herein are interchangeable unless described otherwise, even where no reference is made to a specific feature. It should also be understood that the advantages described above are not necessarily the only advantages of the inventions, and it is not necessarily expected that all of the described advantages will be achieved with every embodiment of the inventions. The scope of the inventions is defined by the appended claims, and all devices and methods that come within the meaning of the claims, either literally or by equivalence, are intended to be embraced therein.