The present invention relates to the field of air conditioning systems. More specifically, the present invention relates to an air conditioning system that includes an energy recovery capability.
Dependence on the natural exchange of air between the indoors and outdoors through air infiltration and exfiltration may not be satisfactory for good indoor air quality and moisture control. Accordingly, mechanical ventilation systems have been developed that use fans to maintain a flow of fresh outdoor air into a building (outside air stream) while exhausting out an equal amount of stale indoor air (exhaust air stream).
Unfortunately, these ventilation systems place additional burdens on the heating, ventilating, and air conditioning systems of a building. In particular, costly conditioned air is exhausted (along with contaminants) as the exhaust air stream, while the outside air stream must be brought in and conditioned (cooled, heated, and/or dehumidified) in order to provide a healthy environment in the building. Furthermore, these ventilation systems result in the loss of heating or cooling energy in the exhaust air. The problem of losing heating or cooling energy through the air exhausted from a building or facility has had a major impact in the form of wasted energy and high costs for heating, ventilating, and cooling buildings, institutions, and facilities.
This problem is exacerbated in commercial facilities and institutions that require nearly one hundred percent outside air at high ventilation rates. A pet store, veterinarian's office, or gymnasium represents a few of such facilities, but similar requirements are presented in other applications as well. The heating and cooling energy needed to condition this air, as well as the fan energy needed to move it, can be prohibitively costly. Moreover, with the high percentage of outdoor air mandated for commercial and institutional buildings, controlling indoor humidity levels can become a challenge.
Strategies for recovering at least a portion of this wasted energy have concentrated on separate systems and methods for recovering the lost heating or cooling energy through cross flow exchangers, run-around loops, heat wheels, heat pipes, and so forth. Each of these strategies try to scavenge the maximum amount of heating or cooling energy from the exhaust air stream and return that energy to precondition the supply air. These systems, typically referred to as energy recovery ventilators, have generally been implemented in the colder regions of the United States, Canada, Europe, and Scandinavia.
In warm areas, there is not a significant energy dollar savings from using energy recovery ventilators since they are not as effective in the cooling season and they can be quite costly. That is, the cost of the additional electricity consumed by the system fans may exceed the energy savings from not having to condition the supply air in mild climates. Nevertheless, pollutants generated in a building, facilities, or institutions can accumulate and reduce the indoor air quality to unhealthful levels. In addition, regulations governing commercial facilities and institutions that require nearly one hundred percent outside air at high ventilation rates still apply in these warm areas.
Accordingly what is needed is a system and method for ensuring a healthy indoor environment and positive moisture control for an interior space in a variety of climates. What is further needed is a system and method for energy recovery that enable a facility's heating and cooling system to be downsized through lost energy recovery.
A more complete understanding of the present invention may be derived by referring to the detailed description and claims when considered in connection with the Figures, wherein like reference numbers refer to similar items throughout the Figures, and:
An embodiment of the invention entails an air conditioning and energy recovery system. Another embodiment of the invention entails a method of controlling the air conditioning and energy recovery system so as to provide effective energy recovery in both the heating and cooling seasons. In particular, the system and methodology enable the recovery of lost energy (btu's) through the condenser cycle by using a refrigerant fluid (e.g., Freon) as the medium of energy recovery instead of conventionally utilized water or air. The incorporation of an energy recovery capability with an air conditioning system enables downsizing of the system relative to prior art heating, ventilation, and air conditioning systems. This downsizing is accomplished through a reduction in peak heating and cooling requirements. Downsizing can result in a system that is half the weight of prior art systems for rooftop mounting. Furthermore, the system and associated methodology can be readily implemented in environments that require up to one hundred percent outside air at high ventilation rates. In addition, the system is operable over a wide range of air conditions, such as from one hundred and twenty-two degrees Fahrenheit to as low as negative ten degrees Fahrenheit.
Referring to
System 20 generally includes a supply section 22, a return section 24, a first conditioning circuit 26, and a second conditioning circuit 28. Supply section 22 is configured to provide a supply air 36 to an interior space 34. In order to do this, supply section 22 recieves air and conditions the air prior to providing the conditioned supply air 36 to interior space 34. To condition the air, supply section 22 uses a first heat exchanger 54 and a third heat exchanger 60 (discussed below), stored within supply section 22, to selectively heat or cool the received air. If necessary, after initial conditioning is done, the humidity level of the air is adjusted through heat exchanger 64 (discussed below).
Return section 24 is configured to accept return air 38 from interior space 34 and release it outside of interior space 34 as exhaust. Prior to releasing return air 38, return section 24 uses a second heat exchanger 56 and a fourth heat exchanger 62 (discussed below), stored within return section 24, to selectively cool or heat return air 38.
In general, outside air 30 is received at an inlet 32 of supply section 22. Outside air 30 is conditioned within supply section 22, and provided to interior space 34 through the appropriate ducting (not shown) as supply air 36. This conditioning includes increasing or decreasing the temperature of the air as well as altering the humidity level as needed. In addition, return section 24 receives return air 38 from interior space 34. Return air 38 is conditioned in return section 24 to selectively recover heating energy or cooling energy (discussed below) prior to its discharge from an outlet 42 of return section 24 outside of interior space 34 as exhaust air 44. First and second conditioning circuits 26 and 28 carry heat transporting fluids between supply section 22 and return section 24 to condition the air in supply section 22 and recover energy from return section 24. First and second conditioning circuits 26 and 28 are discussed in further detail in connection with
System 20 is located in a housing 46, or cabinet, that may be mounted on top of, for example, the roof of a business establishment. Housing 46 may include doors 48 for access to the components of system 20. Access through doors 48 enables ready removal, replacement, and/or servicing of fans, motors, and other components of system 20. A controller 50 may be located in part or in its entirety internal to housing 46. Alternatively, controller 50 may be located remote from housing 46 for ready access by a user. Controller 50 may control the components of system 20 via a wired or wireless connection.
First conditioning circuit 26 includes a first compressor 52, first heat exchanger 54 residing in supply section 22, and a second heat exchanger 56 residing in return section 24. Likewise, second conditioning circuit 28 includes a second compressor 58, a third heat exchanger 60 residing in supply section 22, and a fourth heat exchanger 62 residing in return section 24. A fifth heat exchanger 64 additionally resides in supply section 22. Fifth heat exchanger 64 is a component of a third conditioning circuit 66 in selective fluid communication with second conditioning circuit 28 (discussed below). Supply section 22 further includes a filter 68, a supply fan 70, and an optional furnace 72. Return section 24 further includes a filter 74 and a return fan 76. In one embodiment, first 54, second 56, third 60, fourth 62 and fifth 64 heat exchangers are coils.
When system 20 is activated, supply fan 70 draws outside air 30 into supply section 22 through filter 68, which may be a 30/30 filter, for filtering contaminants from outside air 30. Outside air 30 passes through furnace 72 where air 30 may be at least partially warmed during periods of extreme cold. Outside air 30 passes over first heat exchanger 54 where it may be selectively heated or cooled in accordance with a particular heating or cooling mode control stage. Likewise, outside air 30 passes over third heat exchanger 60 where it may be selectively heated or cooled in accordance with a particular heating or cooling mode control stage. Outside air 30 then passes by fifth heat exchanger 64 of third conditioning circuit 66 where it may be heated to dry it out, i.e. dehumidify, outside air 30 prior to the provision of the conditioned supply air 36 to interior space 34.
Additionally, when system 20 is activated, return fan 76 draws return air 38 into return section 24 through filter 74, which may be a 30/30 filter for filtering contaminants from return air 38. Return air 38 passes over second heat exchanger 56 where some of the energy used to heat or cool the return air 38 may be recovered in accordance with a particular heating or cooling mode control stage via a refrigerant loop. Return air 38 then passes over fourth heat exchanger 62 where additional heating or cooling energy of return air 38 may be recovered in accordance with a particular heating or cooling mode control stage prior to its discharge from outlet 42 as exhaust air 44.
The heating and cooling modes for first and second conditioning circuits 26 and 28 are discussed in connection with
A metering device 94, which may be in the form of a restrictor or an expansion valve, and a bypass line 96 are located in fluid loop 80 and are associated with first heat exchanger 54. Selection of a fluid route through metering device 94 or bypass line 96 is accomplished by actuation of a bypass valve 98. A fluid filter 100 may be in fluid communication with metering device 94. Likewise, a metering device 102 and a bypass line 104 are located in fluid loop 80 and are associated with second heat exchanger 56. Selection of a fluid route through metering device 102 or bypass line 104 is accomplished by actuation of a bypass valve 106.
In heating mode 78, reversing valve 82 is energized to enable a flow of refrigerant 108 from compressor 52 toward first heat exchanger 54 via fluid loop 80. That is, relatively high pressure refrigerant 108 is discharged in a gaseous form from compressor 52 via fluid loop 80 to first heat exchanger 54. As cool outside air 30 passes through first heat exchanger 54, outside air 30 removes heat from (i.e., cools) refrigerant 108 so that outside air 30 is warmed. The warmed outside air 30 subsequently passes through additional components of supply section 22 (discussed above) and is delivered as warm supply air 36 to space 34. The cooled refrigerant 108 continues through fluid loop 80 via bypass line 96 and passes through metering device 102.
Metering device 102 controls the pressure and flow of refrigerant 108 into second heat exchanger 56, residing in return section 24. As the warmed return air 38 passes through return section 24, the cooled refrigerant 108 in second heat exchanger 56 removes heat from (i.e., cools) return air 38 so that exhaust air 44 is cooled. Relatively low pressure refrigerant 108 returns to compressor 52 from second heat exchanger 56 via fluid loop 80 and receiver 88 where the refrigeration cycle is continued. Thus, refrigerant 108 is at least partially warmed by the heat energy in return air 38 that would normally have been wasted. This recovered heat energy enables the high pressure refrigerant 108 entering first heat exchanger 54 to be warmer relative to outside air 30 than it would have been without the exchange in heat exchanger 56 and to impart a greater transfer of heat to outside air 30.
A metering device 126, which may be in the form of a restrictor or an expansion valve, and a bypass line 128 are located in fluid loop 112 and are associated with third heat exchanger 60. Selection of a fluid route through metering device 126 or bypass line 128 is accomplished by actuation of a bypass valve 130. A fluid filter 132 may be in fluid communication with metering device 126. Likewise, a metering device 134 and a bypass line 136 are located in fluid loop 112 and are associated with fourth heat exchanger 62. Selection of a fluid route through metering device 134 or bypass line 136 is accomplished by actuation of a bypass valve 138.
In heating mode 110, reversing valve 114 is energized to enable a flow of refrigerant 140 from compressor 58 toward third heat exchanger 60 via fluid loop 112. That is, relatively high pressure refrigerant 140 is discharged in a gaseous form from compressor 58 via fluid loop 112 to third heat exchanger 60. As cooler outside air 30 passes through heat exchanger 60, outside air 30 removes heat from (i.e., cools) refrigerant 140 so that outside air 30 is warmed. The warmed outside air 30 subsequently passes through additional components of supply section 22 (discussed above) and is delivered as warm supply air 36 to space 34. The cooled refrigerant 140 continues through fluid loop 112 via bypass line 128 and passes through metering device 134.
Metering device 134 controls the pressure and flow of refrigerant 140 into fourth heat exchanger 62, residing in return section 24 (
Third conditioning circuit 66 is also in communication with second conditioning circuit 28 via a fluid loop 142. Third conditioning circuit 66 includes a reheat valve 144, a compressor 146, and fifth heat exchanger 64 in fluid communication via fluid loop 142. Reheat valve 144 may be selectively enabled to allow a flow of fluid though fluid loop 142 into compressor 146 and fifth heat exchanger 64 and return that fluid to fluid loop 112 of second conditioning circuit 28 when the dehumidification of outside air 30 is required. A dehumidification mode is discussed in connection with
At second heat exchanger 56, refrigerant 108 is condensed and cooled by the action of the cooler return air 38 flowing through second heat exchanger 56. That is, refrigerant cools in response to return air 38 to recover energy previously expended in cooling interior space 34. Refrigerant flows via bypass line 104 and fluid loop 80 to metering device 94. Metering device 94 controls the pressure and flow of refrigerant 108 into first heat exchanger 54. As warm outside air 30 passes through first heat exchanger 54, refrigerant 108 in first heat exchanger 54 removes heat (i.e., cools) outside air 30. The cooled outside air 30 subsequently passes through additional components of supply section 22 (discussed above) and is delivered as cool supply air 36 to space 34. Warmed refrigerant 108 exits first heat exchanger 54 and is returned via fluid loop 80 to compressor 52 where the refrigeration cycle is continued.
At fourth heat exchanger 62, refrigerant 140 is condensed and cooled by the action of the cooler return air 38, flowing through fourth heat exchanger 62. That is, refrigerant cools in response to return air 38 to recover energy previously expended in cooling interior space 34. Refrigerant 140 flows via bypass line 136 and fluid loop 112 to metering device 126. Metering device 126 controls the pressure and flow of refrigerant 140 into third heat exchanger 60. As warm outside air 30 passes through third heat exchanger 60, refrigerant 140 in third heat exchanger 60 removes heat (i.e., cools) outside air 30. The cooled outside air 30 subsequently passes through additional components of supply section 22 (discussed above) and is delivered as cool supply air 36 to space 34. Warmed refrigerant 140 exits third heat exchanger 60 and is returned via fluid loop 112 to compressor 58 where the refrigeration cycle is continued. The activation of first conditioning circuit 26 (
When outside air 30 is to be dehumidified in connection with either of cooling modes 148 and 150, reheat valve 144 is enabled to allow a flow of warm, high pressure refrigerant 140 into fluid loop 142. Refrigerant passes through compressor 146 and into fifth heat exchanger 64 residing in supply section 22 (
System control process begins with a task 156. At task 156, temperature and humidity of interior space 34 (
In response to tasks 156 and 158, controller 50 determines whether system 20 should be placed in a heating mode, for example, when the temperature (either sensible or wet bulb) of outside air 30 (
At query task 164, controller 50 determines whether system 20 should be placed in a cooling mode, for example, when outside temperature (either sensible or wet bulb) rises above a predetermined cooling threshold. When a determination is made that system 20 should go into a cooling mode, control process 154 proceeds to a task 166. At task 166, system 20 enters a cooling mode subprocess, discussed in connection with
At query task 164, when a determination is made that system 20 should not be placed in a cooling mode, control process 154 proceeds to a task 168. At task 168, the temperature and humidity of outside air 30 are such that it does not require heating, cooling, or dehumidification. As such, system 20 can go into a free cooling state with just ventilation being provided through the activation of supply fan 70 (
Following any of tasks 162, 166, and 168, process control loops back to task 156 to continue monitoring indoor and outdoor temperatures and to control heating, cooling, and dehumidification as required.
Heating mode subprocess 170 begins with a task 172. At task 172, controller 50 (
A task 174 is performed in cooperation with task 172. At task 176, controller 50 selects and initiates execution of a heating mode stage.
In an exemplary configuration, controller 50 selects a desired heating mode stage from one of four operational stages—Stage 1: low heat requirement 176, Stage 2: moderate heat requirement 178, Stage 3: moderate-to-high heat requirement 180, and Stage 4: high heat requirement 182. In this example, each progressively higher numerical “stage” represents conditions in which the temperature of outdoor air 30 is progressively lower (i.e., colder), thus requiring progressively greater work from first and/or second conditioning circuits 26 and 28 to achieve and maintain a desired set point in interior space 34 (
Following the initiation of any of stages 176, 178, 180, and 182, at task 174 the desired “stage” of heating will continue in response to the temperature of space 34, as well as the temperature of outdoor air 30. When heating is no longer required, heating mode subprocess 170 exits. Each of stages 176, 178, 180, and 182 is discussed briefly below.
At Stage 1: low heat requirement 176, supply and return fans 70 and 76, respectively, (
At Stage 2: moderate heat requirement 178, supply and return fans 70 and 76, respectively, are set to a desired fan speed. For example, supply fan 70 may be set to 4200 cubic-feet-per-minute (cfm) and return fan 76 may be set to 5000 cfm. In addition, first conditioning circuit, circuit B, 28 (
At Stage 3: moderate-to-high heat requirement 180, supply and return fans 70 and 76, respectively, are set to a desired fan speed. For example, supply fan 70 may be set to 4200 cubic-feet-per-minute (cfm) and return fan 76 may be set to 5000 cfm. In addition, first conditioning circuit, circuit A, 26 (
At Stage 4: high heat requirement 182, supply and return fans 70 and 76, respectively, are set to a desired fan speed. For example, supply fan 70 may be set to 4200 cubic-feet-per-minute (cfm) and return fan 76 may be set to 5000 cfm. In addition, first conditioning circuit, circuit A, 26 (
Cooling mode subprocess 184 begins with a task 186. At task 186, controller 50 (
In an exemplary configuration, controller 50 selects a desired cooling mode stage from one of six operational stages—Stage 1: low cool/dehumidification requirement 190, Stage 2: low cool no dehumidification requirement 192, Stage 3: moderate cool no dehumidification requirement 194, Stage 4: moderate-to-high cool no dehumidification requirement 196, Stage 5: high cool/dehumidification requirement 198, and Stage 6: high cool no dehumidification requirement 200. In this example, each progressively higher numerical “stage” represents conditions in which the temperature of outdoor air 30 is progressively higher (i.e., colder) and/or more humid, thus requiring progressively greater work from first and/or second conditioning circuits 26 and 28 to achieve and maintain a desired set point in interior space 34 (
Following the initiation of any of stages 190, 192, 194, 196, 198, and 200, at task 188 the desired “stage” of cooling will continue in response to the temperature of space 34, as well as the temperature of outdoor air 30. When cooling is no longer required, cooling mode subprocess 184 exits. Each of stages 190, 192, 194, 196, 198, and 200 is discussed briefly below. Although not expressly stated below, it should be understood that since the following stages 190, 192, 194, 196, 198, and 200 are related to cooling, furnace 72 (
At Stage 1: low cool/dehumidification requirement 190, supply and return fans 70 and 76, respectively, (
At Stage 2: low cool no dehumidification requirement 192, supply and return fans 70 and 76, respectively, (
At Stage 3: moderate cool no dehumidification requirement 194, supply and return fans 70 and 76, respectively, (
At Stage 4: moderate-to-high cool no dehumidification requirement 196, supply and return fans 70 and 76, respectively, (
At Stage 5: high cool/dehumidification requirement 198, supply and return fans 70 and 76, respectively, (
At Stage 6: high cool no dehumidification requirement 200, supply and return fans 70 and 76, respectively, (
Dehumidification mode subprocess 202 begins with a task 204. At task 204, controller 50 (
In an exemplary configuration, controller 50 selects a desired dehumidification mode stage from one of three operational stages—Stage 1: first dehumidification requirement 208, Stage 2: second dehumidification requirement 210, and Stage 3: third dehumidification requirement 212. Following the initiation of any of stages 208, 210, and 212, at task 206 the desired “stage” of dehumidification will continue in response to the humidity of space 34, as well as the humidity of outdoor air 30. When dehumidification is no longer required, dehumidification mode subprocess 202 exits. Each of stages 208, 210, and 212 is discussed briefly below.
Stage 1: dehumidification requirement 208, supply and return fans 70 and 76, respectively, (
Stage 2: dehumidification requirement 210, supply and return fans 70 and 76, respectively, (
At Stage 3: dehumidification requirement 212, supply and return fans 70 and 76, respectively, (
Cooling section 214 is an air cooler that pre-conditions the temperature of outside air 30 that enters supply section 22. This pre-conditioning reduces the temperature of the air that enters supply section 22, thus reducing the energy needed to bring the temperature and humidity of outside air 30 to user required humidity and temperature of supply air 36. The temperature reduction in cooling section 214 is done using only the heat in outside air 30, and so will reduce the temperature without increasing energy costs. Although cooling section 214 would be effective when outside air 30 is being cooled before being supplied to inside space 34, it should not be used when outside air 30 must be heated.
Cooling section 214 generally includes a cooling inlet 216, a cooling circuit 218, an indirect exchanger 220, a media exchanger 222, a sump 224 and a cooling outlet 226. Indirect exchanger 220 accepts outside air 30 and directs outside air 30 to cooling outlet 226. While passing through indirect exchanger 220, outside air 30 is cooled by cooling fluid 238 that flows through cooling circuit 218. There is no direct contact between the air flowing through indirect exchanger 220 and outside air 30. In one embodiment, media exchanger 222 is above indirect exchanger 220, isolating the flows of outside air 30 through media exchanger 222 and indirect exchanger 220. Cooling inlet 216 includes a first air path 228 and a second air path 230. First air path 228 passes through media exchanger 222 to a fan 232 and is released out of cooling section 214 to the atmosphere. Second air path 230 passes through indirect exchanger 220.
Cooling circuit 218 includes a pump 236, which pumps cooling fluid 238 from sump 224 through cooling circuit 218 to indirect exchanger 220. In a preferred embodiment, cooling fluid 238 is water, however those skilled in the art will recognize that other heat transporting fluids may be used. Indirect exchanger 220 is a heat exchanger that transfers heat between the air in second air path 230 and cooling fluid 238 to alter the temperature of the air in second air path 230. Indirect exchanger 220 has a cooling fluid input 250 and a cooling fluid output 252. There is no contact between cooling fluid 238 and the air in second air path 230 while the air passes through indirect exchanger 220, thus the air in second air path 230 is indirectly cooled by cooling fluid 238.
From indirect exchanger 222220, cooling fluid 238 flows within cooling circuit 218 to media exchanger 220222. Media exchanger 220222 is a heat exchanger that transfers heat between cooling fluid 238 and the air in first air path 228 to alter the temperature of cooling fluid 238. Cooling fluid 238 enters media exchanger 220222 at a media exchanger input 254. There is direct contact between cooling fluid 238 and the air in first air path 228 while heat is transferred in media exchanger 220222. This direct contact reduces the temperature of cooling fluid 238 to within 3 degrees of wet bulb temperature. It is the wet bulb temperature of the air that permits air in first air path 228, having the same temperature as air in second air path 230, to reduce the temperature of cooling fluid 238, while the air in second air path 230 heats cooling fluid 238 in indirect exchanger 222220. From media exchanger 220222, cooling fluid 238 returns to sump 224. In one embodiment, cooling fluid 238 is returned to sump 224 through a return pipe 240.
In one embodiment, second air path 230 passes through a direct exchanger 234 after passing through indirect exchanger 220. Direct exchanger 234 is a heat exchanger that transfers heat between the air in second air path 230 and cooling fluid 238 to further alter the temperature of the air in second air path 230. Unlike in indirect exchanger 220, there is contact between cooling fluid 238 and the air in second air path 230 while the air passes through direct exchanger 234, thus altering the humidity level of the air in second air path 230. When direct exchanger 234 is in use, return pipe 240 is removed, and cooling fluid 238 flows from media exchanger 222 to direct exchanger 234 before returning to sump 224. By using direct exchanger 234, the temperature of the air in second air path 230 is brought to a lower level than the temperature was after indirect exchanger 220. However, the humidity level of the air in second air path 230 is increased when the air passes through direct exchanger 234, as the air comes in direct contact with cooling fluid 238.
A flush line 244 directs the flow of cooling fluid 238 from cooling circuit 218 directly to sump 224. Flush line 244 travels along the top of media exchanger 222, directly contacting the surface of media exchanger 222. This permits cooling fluid 238 that flows through flush line 244 to flush out any debris that may be collected along the top surface of media exchanger 222. A flush valve 242 is placed on flush line 244 to regulate when cooling fluid 238 flows through flush line 244. Periodically, flush valve 242 is opened, cooling fluid 238 flows through flush line 244, and the surface of media exchanger 222 is cleared of debris. Cooling fluid 238 that flows through flush line 244 aids in removing any debris that may obstruct the flow through media exchanger 222. Flush line 244 empties into sump 224, returning cooling fluid 238 to be recirculated through cooling circuit 218. In one embodiment, flush valve 242 is opened every hour. However, those skilled in the art will recognize that the rate of opening flush valve 242 may be altered to effectively remove debris as needed.
Cooling circuit 218 also has two flow control valves. A first flow control valve 246 controls the flow of cooling fluid 238 from indirect exchanger 220 to media exchanger 222. As cooling fluid 238 flows through indirect exchanger 220, cooling fluid 238 is heated by air through second air path 230. The flow of this heated cooling fluid 238 to media exchanger 222 is regulated by first flow control valve 246, thus partially regulating the level of flow and temperature of cooling fluid 238 that enters media exchanger 222. A second flow control valve 248 controls the flow of cooling fluid 238 directly from sump 224. Cooling circuit 218 is configured to permit cooling fluid 238 to flow either indirectly to media exchanger 222, through indirect exchanger 220, or directly to media exchanger 222. Second flow control valve 248 regulates the flow of cooling fluid 238 flowing directly to media exchanger 222.
By controlling the flow through both first and second flow control valves 246 and 248, cooling fluid 238 from indirect exchanger 220 is mixed with cooling fluid 238 directly from sump 224 as cooling fluid 238 enters media exchanger 222 for further heat exchange. By changing the flow through first or second flow control valves 246 or 248, the temperature of cooling fluid 238 that enters media exchanger 222 can be altered. Also, by regulating the amount of cooling fluid 238 that flows into media exchanger 222, first and second flow control valves 246 and 248 affect the temperature of cooling fluid 238 in sump 224. This is because the temperature of cooling fluid 238 in sump 224 will decrease if a larger amount of cooled cooling fluid 238 enters sump 224. Regulating the temperature of cooling fluid 238 this way also regulates the temperature of cooling fluid 238 that enters indirect exchanger 220, thus regulating the amount of heat energy that must be transferred in indirect exchanger 220 to ultimately regulate the air in second air path 230.
In summary, the present invention teaches an air conditioning and energy recovery system and a method of controlling the air conditioning and energy recovery system so as to provide effective energy recovery in both the heating and cooling seasons over a full range of temperature (e.g., from one hundred and twenty-two degrees Fahrenheit down to negative ten degrees Fahrenheit). The energy recovery capability is integral to the air conditioning system to enable downsizing of the system relative to prior art heating, ventilation, and air conditioning systems. This downsizing is accomplished through a reduction in peak heating and cooling requirements. Furthermore, the system and associated methodology can be readily implemented in environments that require one hundred percent outside air at high ventilation rates.
Although the preferred embodiments of the invention have been illustrated and described in detail, it will be readily apparent to those skilled in the art that various modifications may be made therein without departing from the spirit of the invention or from the scope of the appended claims. For example, the system can be adapted to include more or less stages of heating mode, cooling mode, and dehumidification mode then that which was described. In addition, various mathematical and intuitive techniques can be used for determining which stage of cooling, heating, and/or dehumidification may be implemented in response to temperature and humidity requirements.
The present invention claims priority under 35 U.S.C. §119(e) to: “Indirect/Direct Evaporative Cooling Unit,” U.S. Provisional Application Ser. No. 61/040,013, filed 27 Mar. 2008, which is incorporated by reference herein. The present invention is a continuation in part (CIP) of “Air Conditioning and Energy Recovery System and Method of Operation,” U.S. patent application Ser. No. 12/203,498, filed 3 Sep. 2008, which is incorporated by reference herein.
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20090241564 A1 | Oct 2009 | US |
Number | Date | Country | |
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61040013 | Mar 2008 | US |
Number | Date | Country | |
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Parent | 12203498 | Sep 2008 | US |
Child | 12411283 | US |