The present invention pertains generally to efficient refrigeration systems for use in grocery stores and cold food storage. More particularly, the present invention pertains to an efficient method of removing condensate that collects during operation by utilizing waste heat and airflow generated by the refrigeration system. The Present invention is particularly, but not exclusively, useful as a way to reduce energy consumption of portable or self-contained refrigeration units.
Supermarket departments are typically designed and setup with remote refrigeration systems where remote refrigerated cases such as wall units and islands are installed with and controlled by central compressor banks/condensing units typically located in a back room or outside the building. In this type of installation, the condensate, which is water that condenses on the cooling coils then drips off, is drained into floor drains through permanently installed plumbing.
In some situations, it is desirable for the refrigerated cases to be of the self-contained design where the entire refrigeration system is contained within the refrigerator itself. Self-contained units may be used for adding additional refrigeration into store areas not originally designed in the store refrigeration system, for temporary or seasonal use, or for ease and low cost of department reconfiguring. Self-contained refrigerators may be permanently affixed to the floor or may be mobile thought the use of wheels or casters.
Removing condensate is of special concern where a floor drain and accompanying plumbing is not a viable option. In this situation, there are three options that are commonly used. The first is where condensate is eliminated by collecting and boiling it off in a pan having a heating element. The high electrical current draw of the heating element requires additional electrical service to the refrigerator, either by a significantly higher amperage circuit or the addition of another electrical circuit. The second option is to use the hot gas side of the refrigeration system and create a loop or coil that is immersed in a condensate collection pan. This option does not work as well as the heater pan since the condensate is often produced at a faster rate than the hot gas loop is able to remove under normal relative humidity conditions. In this case, excess condensate must be drained manually from the refrigerator. The third option requires periodic manual draining of the refrigerator.
Recently, the Department of Energy (DOE) started to implement their 2012 Energy Conservation Program, which regulates commercial refrigeration equipment. Its rules are mandatory for all manufacturers selling equipment in the United States. The program mandates maximum energy consumption dependent on the type model of the equipment. The traditional method of boiling away the condensate through the use of a heating element typically consumes more than one third of the total energy consumption requirement of prior generation refrigerators. Full-time electric heaters to boil off the condensate are no longer a viable method in terms of meeting energy consumption requirements. In response to this program, commercial manufacturers have started to address energy usage in their designs to meet the DOE 2012 program requirements.
What is now needed in the industry is a high efficiency refrigeration system that does not require periodic manual draining or emptying and does not require the additional electrical current load to support operation of a heating element thereby reducing the system's power consumption.
A condensate collection pan made sufficiently large enough to hold all of the condensate expected to be generated during operation of the refrigeration system at any given time is designed to accommodate an electric heating element, a hot gas loop, coil, or other configuration of hot gas tubing from the refrigeration system employed, and a limit switch controlled by a liquid level float or other liquid level sensing switch that turns the heating element on and off. Further, the refrigeration system defrost timer is wired so that when the condensing unit is turned off for the defrost cycle the heating element is turned on for the duration of the defrost cycle. In addition to this, the temperature controller that regulates the on-off durations of the condensing unit during the cooling cycle is also wired so that when the condensing unit is turned off for case temperature regulation, the heating element is simultaneously turned on for the same duration. In certain embodiments, the condensing unit fan is wired to continuously run so that steam generated from boiling off the condensate is removed from the refrigerator's interior. Because the high electrical current draw of the compressor is alternating with the high electrical current draw of the heating element, no additional electrical service is required for the heating element. In other embodiments, the hot gas loop from the refrigeration system is used to preheat the condensate to assist the electric heating element in order to shorten the amount of time it takes to heat the condensate to point of evaporation.
During operation of a typical system, the defrost time duration would not be long enough for the heater to eliminate the condensate faster than it is produced during normal cooling operation. Typically, the cooling cycle lasts for 4-6 hours and the defrost cycle lasts for 15 minutes. The time it takes for the water to be raised from room temperature to the point of evaporation is too long resulting in condensate remaining in the pan after the defrost cycle has ended. The hot gas loop of the present invention preheats the condensate temperature to between 150 and 200 degrees F. This results in a shortened amount of time required to evaporate the condensate verses the majority of the defrost time being utilized to bring the condensate to the point of bong only to have the defrost cycle end with condensate remaining in the condensate tray.
Additions to the refrigeration systems may be computerized controls that receive inputs from various sensors that determine optimal on and off frequency and duration of the defrost cycle as well as control of the condensate removal system thereby further improving the energy efficiency of the system. In some embodiments, the computerized control further comprises an Early Leak Detection (ELD) system. The ELD utilizes one or more sensors configured to monitor and report the level of condensate in the condensate pan. If the sensors indicate the condensate level in the condensate pan is too high, the ELD sends a signal to the computerized control, which in turn shuts down the compressor, energizes or keeps energized the condenser fan and any condensate pan heaters, energizes audible and visual indicators, and sends a signal to a central monitoring and control system. In other embodiments, the ELD system is implemented without the use of computerized control but still is configured to shut down the compressor, energize or keep energized the condenser fan and any condensate pan heaters, and energize audible and visual indicators. Once the condensate removal system has brought the condensate level back to a normal operating level, the refrigeration system resets then returns to normal operation. However, the audible and visual indicators will remain energized until the refrigerated portions return to normal operating temperature.
Some embodiments of the present invention also comprise a moisture sensor located underneath or next to the condensate pan, or at a low point where leakage is likely to collect, to provide additional early leak detection. The moisture sensor allows for the detection of leakage from somewhere in a refrigerated case, such as from internal piping or other water boundaries associated with the case. The moisture sensor sends a signal to the control system, computerized or otherwise, causing visual and audible alarms to energize. In some embodiments, in response to a moisture alarm, the control system shuts down the compressor, energizes or keeps energized the condenser fan, and energizes the one or more condensate pan heaters. Other embodiments utilizing the moisture sensor may shut down all compressors, heaters, and fans when the sensor detects moisture but still energizes the visual and audible indicators and sends a signal to the central control system.
In some embodiments of the present invention, a high-volume pump is utilized to eliminate the condensate. The pump can pump condensate up to a 45-foot vertical rise and to a virtually unlimited horizontal run. The use of a pump allows for the use of piping or flexible tubing that can be routed through a given space to the nearest drain. The advantages of using this method are it provides the lowest possible energy consumption and it has the lowest level of regular maintenance required to operate the system. Such a system is appropriate for high humidity locations and floral applications.
In other embodiments, a wicking dissipater is used to aid in the removal of condensate. The wick is a high efficiency wicking element that remains in contact with the bottom of a condensate tray. The waste air from the condensing unit is ducted through the wicking element to evaporate the absorbed condensate. When tested, a refrigeration system using a wicking dissipater was able to eliminate all of the condensate generated by the refrigerator within a controlled test environment of 75 degrees F. and 55% relative humidity. In some embodiments that use a wicking dissipater, a heating element is also implemented to ensure that all condensate is removed during temporary “out-of-normal” operating environments. A mold and mildew inhibitor solution dispenser may be implemented to minimize or prevent the formation of mold and mildew in the wicking element and the condensate tray.
In yet other embodiments, a hot-gas loop dissipater is used to aid in the removal of condensate. This dissipater utilizes the refrigeration plumbing waste heat between the compressor and the condenser to heat the condensate in order to accelerate evaporation. The evaporation process may be amplified by creating layers of hot-gas loop plumbing within multiple levels of condensate holding trays to heat the condensate to aid in the evaporation process. The hot-gas loop dissipater may also be combined with the wicking dissipater to further accelerate the evaporation process. A heating element located in the condensate trays may also be implemented to handle temporary “out-of-normal” operating environments.
Some embodiments of the present invention combine the features of other embodiments, such as a system comprising a shroud assembly for directing air flow through the condensate area, a wicking element, one or more condensate pan heaters, a hot loop dissipater, computerized controls with networking capabilities, condensate pan level sensors, a mold and mildew inhibitor system, and an ELD system.
The novel features of this invention, as well as the invention itself, both as to its structure and its operation, will be best understood from the accompanying drawings, taken in conjunction with the accompanying description, in which similar reference characters refer to similar parts, and in which:
Referring initially to
Referring now to
High volume pump 54 is used to pump condensate from the condensate tray 52. Condensate is produced by the evaporator coil located in refrigerated spaces 14 and 34. The condensate tpically drips off the coils of the evaporator where it is collected and directed to condensate tray 52 through condensate drain 58. During normal operation in a high humidity location or a floral refrigeration system, the amount of condensate produced may exceed traditional methods of condensate removal, such as boiling off the condensate using a heating element. The failure to remove all produced condensate results in ongoing and routine maintenance that removes the collected condensate and may lead to the formation of mold and mildew. The use of high volume pump 54 allows the use of flexible hose or tubing 56 to direct the condensate out of refrigerated cases 10 and 30 to a location having a drain. Pump 54 provides sufficient output pressure that the condensate can be pumped up to a height above the refrigeration case then horizontally to an appropriate drain location. Since flexible hose or tubing 56 is used, the hose or tubing 56 may be routed as necessary to reach the drain location. Such an implementation allows refrigerated cases 10 and 30 to be placed a various locations in a store without the need to consider where to drain the condensate since the hose or tubing 56 is flexible and may be routed as necessary. In an alternative embodiment, refrigeration system 40 may also consist of a heating element 62 (not shown, see
Referring now to
To aid in condensate removal, the airflow generated by fan 42 is ducted by shroud 68 through condenser 41 to wick 64, where the air passes through airflow passages 65 which run horizontally through wick 64. The airflow through airflow passages 65 of wick 64 evaporates condensate absorbed by wick 64. In a preferred embodiment, the wick 64 may be made by any material known in the art to exhibit wicking properties including capillary action, including but not limited to silica, polyester, Teflon, and other synthetic materials. Also, many natural materials, such as rayon cellulose, cotton and wool, are suitable materials for acceptable wicking propeities for the present invention. Wick 64 includes air passages which run horizontally through the body of the wick 64 to facilitate the exposure of the wetted wicking material to the air as it passes through the wick 64. The particular size and shape of the wick passages 65 as shown in
The increased temperature of the airflow, resulting from the heat given off by condenser 41, increases the rate of condensate evaporation. After the airflow exits wick 64, the airflow exits the rear of refrigerated cases 10 and 30 through air outlet 16 in air outlet cover 24. In certain embodiments of the present invention, air outlet cover 24 provides a portion of shroud 68 to direct airflow to wick 64. This design also allows for quicker and easier access to the refrigeration components during maintenance. Fan 42 may be configured to operate when compressor 44 is deactivated, thereby allowing fan 42 to continue generating air flow through wick 64 to continue removing condensate.
Refrigeration system 90, similar to refrigeration system 80, utilizes heat controller 60, level sensor 63, and heating element 62. Heating element 62 can be used to supplement the condensate removal effect of wick 64. Heating element 62 also aids in the prevention of mold and mildew by periodically energizing heating element 62 to raise the temperature of any standing condensate in condensate tray 52 to an appropriate level to kill mold, mildew, and any other bacteria that may exist in the condensate. Since refrigeration system 90 utilizes waste heat to aid in the removal of condensate, the amount of time and power used by heating element 62 is greatly reduced thereby reducing the overall amount of power consumed by refrigeration system 90. Further, since the overall power requirements are reduced, standard power connections may be used to operate the systems without the need for additional power connections or high voltage connections. Such power reductions allow refrigerated cases 10 and 30 to operate within established guidelines for power consumption and efficiency.
In certain embodiments of the present invention, a dispenser 66 and dispenser tube 67 are utzed to allow for the addition of a mold and mildew inhibitor solution to the condensate. Since wick 64 will also absorb the inhibitor solution along with the condensate, mold and mildew will also be prevented within the structure of wick 64. As discussed above, heating element 62 may also be energized on a periodic basis, or as needed, to aid in the prevention of mold and mildew in condensate tray 52 and wick 64. The prevention of mold and mildew is especially critical in the grocery business due to the offensive nature of the odors produced by molds and mildews. Since refrigerated cases 10 and 30 take in and expel air, any mold or mildew smells generated within the cases 10 and 30 will be spread throughout the store.
In operation, any condensate that collects in condensate tray 52 through condensate drain 58 is heated by the waste heat transferred from hot gas tube 70, thereby increasing the rate of evaporation. Since hot gas is generated at all times during operation of compressor 44, waste heat is continually transferred to any condensate accumulated in condensate tray 52. As a result, the amount of time required for heating element 62 to operate is reduced, if not eliminated. This use of waste heat to evaporate condensate and reduced run time for heating element 62 allows refrigerated cases 10 and 30 to operate within prescribed energy consumption limits.
Also shown in
Also shown in
The presence of moisture inside refrigerated cases 10 and 30 may lead to the formation of mold and mildew, which typically produces an offensive odor. Moisture sensor 74 provides an indication that moisture has formed outside of refrigeration system 100, which may be due to an overflow condition of condensate tray 52 or a leak from another portion of refrigerated cases 10 and 30.
Referring now to
As shown in
It is to be appreciated by someone skilled in the art that different styles of refrigerated cases, such as double refrigerated case 30 (see
Referring now to
In operation, refrigerated cases 10 communicate with local server to transmit case status as well as receive operational commands, similar to system 200 discussed above. Refrigerated cases 10 having the wireless transceiver 310 allow for easier placement of refrigerated cases 10 without the need to use a hardwire connection to local network 302. An operator may interface with server 308 to program temperature set points for each refrigerated case 10 collectively, individually, or in sub-groups.
Moving now to
Each server 410 connects to the internet/cloud 402 through communication link 408, which may be any type of connection including WAN, cellular, Ethernet, Frame Relay, Fiber Optic, or any other communication protocol known in the industry. Also connected to internet cloud 402 is remote computer 404, which connects to internet/cloud 402 through a communication link 406, which is any communication protocol known in the industry, similar to servers 410. An operator of remote computer 404 accesses each server 410 through internet/cloud 402 to receive status information and send operational commands, such as raising and lowering temperature set points for each refrigerated case 10.
Alternatively, a remote control and monitoring server 414 (shown in dashed ones) may be located in the internet/cloud 402, which communicates directly with local servers 410. In this configuration, remote server continually communicates with local servers 410 to send and receive status information and operational commands. The remote computer 404 then connects with remote server 414 to monitor status information and adjust desired set points or other features of system 400. In this alternative configuration, remote computer 404 may also connect directly to each local server 410 to send and receive status information and operational commands.
Local networks 206, 302, and 412 may be any type of networking topology known in the industry, such as Ethernet, RS232/422/485, wireless, or other point-to-point or multi-drop technology.
It is to be appreciated by someone skilled in the art that various portions of the various embodiments described above may be combined to create a more efficient system. For example but without limitation, refrigeration system 100 may also incorporate wick 64 and shroud 68 to create a system capable of operation in a high temperature and high humidity environment without the need for additional power connections, drains or the routing of tubing through the grocery space. Another example is dispenser 66 and dispenser tube 67 may be used with refrigeration systems 40, 80, and 100 without departing from the scope and spirit of the present invention. Further, since the above discussed systems are designed to remove condensate at an increased rate, maintenance requirements are minimized since accumulated condensate will not need to be removed manually.
While there have been shown what are presently considered to be preferred embodiments of the present invention, it will be apparent to those skilled in the art that various changes and modifications can be made herein without departing from the scope and spirit of the invention.
The application claims the benefit of priority to U.S. Provisional Patent Application Ser. No. 62/127,400 entitled “Energy Efficient Refrigeration System”, filed on Mar. 3, 2015, and currently co-pending.
Number | Name | Date | Kind |
---|---|---|---|
3759059 | Kenyon | Sep 1973 | A |
4608835 | Kooy | Sep 1986 | A |
5678421 | Maynard | Oct 1997 | A |
6487867 | Herren | Dec 2002 | B1 |
8539783 | Bunch | Sep 2013 | B1 |
9327874 | Hawley, III | May 2016 | B2 |
20030121275 | Erisgen | Jul 2003 | A1 |
20050217297 | Wilson | Oct 2005 | A1 |
20050229614 | Ansted | Oct 2005 | A1 |
20070000273 | Sanders | Jan 2007 | A1 |
20080115920 | Uchida | May 2008 | A1 |
20080256974 | Verma | Oct 2008 | A1 |
20080283440 | Hartsfield, Jr. | Nov 2008 | A1 |
20090077992 | Anderson | Mar 2009 | A1 |
20100058787 | Iguchi | Mar 2010 | A1 |
20100058788 | Iguchi | Mar 2010 | A1 |
20100281896 | Al Watban | Nov 2010 | A1 |
20120023983 | Glaros | Feb 2012 | A1 |
20120303311 | Rowe, Jr. | Nov 2012 | A1 |
20120324914 | Bartoletto | Dec 2012 | A1 |
20130098091 | Stephens | Apr 2013 | A1 |
20130125575 | Szprengiel | May 2013 | A1 |
20130160475 | Vinz | Jun 2013 | A1 |
20140096545 | Zangari | Apr 2014 | A1 |
20140341710 | Creamer | Nov 2014 | A1 |
20150245721 | Nugroho | Sep 2015 | A1 |
20150330699 | Hawley, III | Nov 2015 | A1 |
20150342371 | Leong | Dec 2015 | A1 |
20150374143 | Takayama | Dec 2015 | A1 |
20150376874 | Breedlove | Dec 2015 | A1 |
Number | Date | Country |
---|---|---|
2621045 | Aug 2008 | CA |
102011085155 | Apr 2013 | DE |
2373200 | May 2012 | EP |
2198220 | Jun 1988 | GB |
2005098627 | Apr 2005 | JP |
2005274088 | Oct 2005 | JP |
Entry |
---|
JP2005098627A ENG Translation. |
Number | Date | Country | |
---|---|---|---|
20170020305 A1 | Jan 2017 | US |
Number | Date | Country | |
---|---|---|---|
62127400 | Mar 2015 | US |