Abstract:
A method of managing a refrigeration system includes transmitting energy consumption, maintenance indicator, and food condition data from the refrigeration system to a management center; analyzing the energy consumption, maintenance indicator, and food condition data at the management center; and monitoring, diagnosing and prognosing the performance of the refrigeration system in response to the analysis. The method may also include altering a configuration of the refrigeration system in response to the analysis. The refrigeration system may be located at a retail location and the management center may be located remotely to the retail location.

Description:
CROSS-REFERENCE TO RELATED APPLICATIONS 
   This application is a continuation of U.S. patent application Ser. No. 10/132,663 filed on Apr. 25, 2002, now U.S. Pat. No. 6,675,591, which claims the benefit of U.S. Provisional Application No. 60/288,551 filed on May 3, 2001. The disclosures of the above applications are incorporated herein by reference. 

   FIELD OF THE INVENTION 
   The present invention relates to managing a refrigeration system and, more particularly, to monitoring and evaluating food inventory and equipment of a food retailer. 
   BACKGROUND OF THE INVENTION 
   Produced food travels from processing plants to retailers, where the food product remains on display case shelves for extended periods of time. In general, the display case shelves are part of a refrigeration system for storing the food product. In the interest of efficiency, retailers attempt to maximize the shelf-life of the stored food product while maintaining awareness of food product quality and safety issues. 
   For improved food quality and safety, the food product should not exceed critical temperature limits while being displayed in the grocery store display cases. For uncooked food products, the product temperature should not exceed forty-one (41) degrees Fahrenheit. Above this critical temperature limit, bacteria grow at a faster rate. In order to maximize the shelf life and safety of the food product, retailers must carefully monitor the food product stored therein. In general, monitoring of the temperature of the food product enables determination of the bacterial growth rates of the food product. To achieve this, refrigeration systems of retailers typically include temperature sensors within the individual refrigeration units. These temperature sensors feed the temperature information to a refrigeration system controller. Monitoring of the food product involves information gathering and analysis. 
   The refrigeration system plays a key role in controlling the quality and safety of the food product. Thus, any breakdown in the refrigeration system or variation in performance of the refrigeration system can cause food quality and safety issues. Thus, it is important for the retailer to monitor and maintain the equipment of the refrigeration system to ensure its operation at expected levels. 
   Further, refrigeration systems generally require a significant amount of energy to operate. The energy requirements are thus a significant cost to food product retailers, especially when compounding the energy uses across multiple retail locations. As a result, it is in the best interest of food retailers to closely monitor the performance of the refrigeration systems to maximize their efficiency, thereby reducing operational costs. 
   Monitoring food product quality and safety, as well as refrigeration system performance, maintenance and energy consumption are tedious and time-consuming operations and are undesirable for retailers to perform independently. Generally speaking, retailers lack the expertise to accurately analyze time and temperature data and relate that data to food product quality and safety, as well as the expertise to monitor the refrigeration system for performance, maintenance and efficiency. Further, a typical food retailer includes a plurality of retail locations spanning a large area. Monitoring each of the retail locations on an individual basis is inefficient and often results in redundancies. 
   Therefore, it is desirable in the industry to provide a method for monitoring the food product of a plurality of remote retailers. The method should allow a user to accurately determine the quality and safety of the food product as a function of the temperature history and length of time stored. Further, the method should provide an alarming routine for signaling when the food product has crossed particular quality and safety limits. The method should also monitor the refrigeration systems of the remote retailers for performance, maintenance and efficiency. The method should monitor multiple locations for performance comparison purposes, to avoid redundancies between remote locations and to provide the expertise required to accurately analyze characteristics of individual remote locations. 
   SUMMARY OF THE INVENTION 
   Accordingly, the present invention provides a method for monitoring and managing a refrigeration system of a remote location. The method includes a communication network and a management center in communication with the remote location through the communication network. The management center receives information from the remote location regarding performance of the refrigeration system, whereby the management center analyzes and evaluates the information for altering operation of the refrigeration system thereby improving the performance. 
   A method of managing a refrigeration system generally includes transmitting energy consumption, maintenance indicator, and food condition data from the refrigeration system to a management center; analyzing the energy consumption, maintenance indicator, and food condition data at the management center; and monitoring, diagnosing and prognosing the performance of the refrigeration system in response to the analysis. The method may include altering a configuration or altering manipulation of the refrigeration system in response to the analysis. The refrigeration system may be at retail location while the management center is at a remote location. 
   Further, the analysis of the said food condition data includes calculating a food quality index or a food safety index. The method may include alarming as a function of the food quality index or the food safety index. 
   The analysis of the energy consumption data may include analyzing weather data, wherein the weather data is historical weather data or actual weather data. Analysis of the maintenance indicator data may include analyzing condenser condition data, analyzing compressor condition data, analyzing liquid refrigerant flood back data, analyzing relay output data, analyzing contactor count data, analyzing compressor run-time data, analyzing oil check data, analyzing air filter data, or analyzing light bulb change data. The method may include outputting a work order in response to the analysis. Transmitting includes transmitting through a communication gateway to said management center, and may include post-processing the data at the communication gateway. 

   
     BRIEF DESCRIPTION OF THE DRAWINGS 
     The present invention will become more fully understood from the detailed description and the accompanying drawings, wherein: 
       FIG. 1  is a schematic overview of a system for remotely monitoring and evaluating a remote location, in accordance with the principles of the present invention; 
       FIG. 2  is a schematic view of an exemplary refrigeration system according to the principles of the present invention; 
       FIG. 3  is a frontal view of a refrigeration case of the refrigeration system of  FIG. 2 ; 
       FIG. 4  is a graph displaying cyclical temperature effects on bacteria growth within the refrigeration system; 
       FIG. 5  is a graphical representation of a time-temperature method for monitoring bacteria growth within the refrigeration system; 
       FIG. 6  is a graphical representation of a degree-minute method for monitoring bacteria growth within the refrigeration system; 
       FIG. 7  is a graphical representation of a bacteria count method for monitoring bacteria growth within the refrigeration system; 
       FIG. 8  is a flowchart outlining a method of calculating a food safety index according to the principles of the present invention; 
       FIG. 9  is a flowchart outlining a method of calculating a food quality index according to the principles of the present invention; 
       FIG. 10  is a schematic view of an energy usage algorithm in according to the principles of the present invention; 
       FIG. 11  is a screen-shot of a temperature data sheet used in conjunction with the energy usage algorithm; 
       FIG. 12  is a schematic view of a temperature data routine; 
       FIG. 13  is a screen-shot of a temperature data import sheet; 
       FIG. 14  is a schematic view of an actual site data routine implemented in the energy usage algorithm; 
       FIG. 15  is a screen-shot of a store specification component of the actual site data routine; 
       FIG. 16  is a screen-shot of a new site data component of the actual site data routine; 
       FIG. 17  is a screen-shot of a core calculator implemented with the energy usage algorithm; 
       FIG. 18  is a schematic view of a power monitoring routine; 
       FIG. 19  is a schematic view of an alarming routine; 
       FIG. 20  is a screen-shot of the power monitoring routine; 
       FIG. 21  is a schematic view of a design set-up routine; 
       FIG. 22  is a screen-shot of the design set-up routine; 
       FIG. 23  is a schematic view of a design results routine; 
       FIG. 24  is a screen-shot of the design results routine; 
       FIG. 25  is a screen-shot of a temperature variation routine; 
       FIG. 26  is a screen-shot showing charts summarizing results of the energy usage algorithm; 
       FIG. 27A  is a schematic of a dirty condenser algorithm; 
       FIG. 27B  is a flowchart outlining the dirty condenser algorithm; 
       FIG. 28  is a schematic of a discharge temperature algorithm; 
       FIGS. 29A and 29B  are respective schematics of suction superheat and discharge superheat monitoring algorithms; 
       FIG. 30  is a schematic of service call algorithm; 
       FIG. 31  is a schematic diagram of energy saving algorithms implemented by the system of the present invention; 
       FIG. 32  is a graph of alarming conditions and actions in response to each; 
       FIG. 33  is a schematic view of the alarming conditions implemented by the system of the present invention; and 
       FIG. 34  is a screen-shot of a user interface of the system for monitoring a particular food storage case of a particular location. 
   

   DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS 
   The following description of the preferred embodiments is merely exemplary in nature and is in no way intended to limit the invention, its application, or uses. 
   With reference to  FIGS. 1A and 1B , the present invention provides a system  10  for remote monitoring, diagnosis and prognosis of food inventory and equipment of a retailer. The system  10  includes a management center  12  in communication with a remote location  14 , such as a food retail outlet, having food inventory and equipment, such as a refrigeration system, HVAC system, lighting and the like, therein. A communication network  16  is provided for operably interconnecting the management center  12  and the remote location  14  enabling information transfer therebetween. The communication network  16  preferably includes a dial-up network, TCP/IP, Internet or the like. It will be appreciated by those skilled in the art, that the management center  12  may be in communication with a plurality of remote locations  14  through the communication network  16 . In this manner, the management center  12  is able to monitor and analyze operation of multiple remote locations  14 . 
   The management center  12  gathers operational data from the remote location  14  to analyze performance of several aspects of the remote location  14  through post-processing routines. Initially, the management center  12  may process temperature information for calculating food safety and food quality indices (FSI and FQI, respectively), as described in further detail below. Calculated values for FSI and FQI may be used by the management center  12  to alert a remote location  14  of food safety and quality performance. In this manner, the remote location  14  is able to adjust the operation of its systems to improve performance. 
   Also, the management center  12  may gather and process energy consumption information for its energy using equipment including various components of the refrigeration system and the refrigeration system as a whole. An analysis of the energy consumption of the energy using equipment enables the management center  12  to evaluate the overall efficiency thereof and identify any problem areas therewith. Finally, the management center  12  may gather information specific to each component of the refrigeration system for evaluating the maintenance measures each component may require. Both routine and preventative maintenance may be monitored and evaluated, thereby enabling the management center  12  to alert the remote location of potential equipment malfunctions. In this manner, overall efficiency of the refrigeration system may be enhanced. 
   Additionally, the management center  12  provides a data warehouse  18  for storing historical operational data for the remote location  14 . The data warehouse  18  is preferably accessible through the communication network  16  utilizing commercially available database software such as Microsoft Access™, Microsoft SQL-Server™, ORACLE™, or any other database software. 
   The system  10  is remotely accessible through a graphical user interface  20  via a third-party computer system through the communication network. In an exemplary embodiment, a remote user may log into the system  10  through the Internet to view operational data for the remote location  14 . The third-party computer system may include any web-enabled GUI known in the art, including but not limited to a computer, a cellular phone, a hand-held portable computer (e.g., Palm Pilot™) or the like. 
   The GUI  20  provides a view into the system  10  and allows the user to see the data for the remote location  14  via a standard web browser. The GUI  20  also provides access to software modules  22 , which preferably run on one or more servers  24 . The GUI  20  can provide this access using only a standard web browser and an Internet connection. Maintenance managers will use the GUI  20  to receive alarms for a specific remote location  14 , acknowledge alarms, manually dispatch work orders based on the alarms, make changes to set points, ensure that a remote location  14  is performing as required (by monitoring case temperatures, rack pressures, etc.), and check a remote location  14  after the receipt of an alarm. 
   More specifically, the system  10  will make use of existing network infrastructure to add value to users who use the system for collecting and/or aggregating data. This value includes speeding up (and automating) the data collection process and enabling the aggregation of data to be performed automatically. The information that is retrieved from a remote location  14  resides on servers  24 . Further, the system allows the ability to add software modules  22  to the server  24  that will extract additional information from the data. Examples are analyzing trend information of pressure and compressor status over a period of time and extracting performance degradation characteristics of the compressors. 
     FIG. 1B  shows a diagram of the communications network  16 . Multiple remote locations  14  exist behind a corporate firewall  26  and that the data behind the firewall  26  must be pushed to a server  24 , which exists outside the firewall  26 . Users are able to access the information via an Internet connection in the standard browser. In general, the user should be given the impression that he/she is always going through the server  24  to retrieve information from the remote location  14 . It is possible for a user to view both real-time data generated at the site and aggregated data in a single view. Using this architecture, software modules  22  can be easily added to perform functions on the data. 
   Web-based navigation is accomplished by the GUI  20 , which will be interfaced for all of the software modules  22 . Alarm monitoring, energy analysis, food quality, and maintenance software modules  22  are described below, and each are accessible via the GUI  20 . A software module  22  may even be provided for enabling the user to completely configure a controller, as discussed in further detail below. Its primary use will be during initial configuration of the controller. A work order module provides the capability to enter and track work orders for managing the maintenance schedule of the equipment of the remote location  14 . An asset management module provides the capability to enter and track assets and view asset history. 
   The GUI  20  also offers a number of standard screens for viewing typical site data. A store summary screen is provided and lists the status of the refrigeration, building control systems and the like. A product temperature summary screen displays product temperatures throughout the store when using product temperature probes. An alarm screen enables the user to see the status of all alarms. The alarm screen provides information about particular alarms and enables the alarm to be acknowledged and reset, as discussed in further detail hereinbelow. Basic alarm viewing/notification capability is provided and includes the ability to view an alarm, acknowledge an alarm, and receive notification of the alarm. Notification is either via GUI/browser, e-mail, facsimile, page, or text message (SMS/e-mail) to a cellular telephone. Each alarm type has the capability of selecting whether notification is required and what (and to whom) the notification method will be. 
   The GUI  20  provides the capability to display historical (logged) data in a graphical format. In general, the graph should be accessible from the screen with a single click. Data is overlaid from different areas (e.g. case temperature with saturated suction temperature) on a single graph. Some historical data may be stored on a server  24 . In general, the display of this data should be seamless and the user should not know the source of the data. 
   The GUI  20  provides the capability to display aggregated remote location data, which should be displayed as aggregated values and includes the capability to display power and alarm values. These views may be selected based on user requirements. For example, the GUI  20  provides the capability to display aggregated remote location power data for an energy manager log in and aggregated alarm data for a maintenance manager log in. The GUI  20  will provide a summary-type remote location screen with power and alarms for the remote location  14  as a default. 
   The GUI  20  provides the capability to change frequently used set points directly on the appropriate screen. Access to other set points is achieved via a set point screen that can be easily navigated with one click from the GUI  20 . In general, applications on controllers have many set points, the majority of which are not used after the initial setup. 
   Returning to  FIG. 1A , the remote location  14  may further include a post-processing system  30  in communication with the components of the refrigeration system through the controller. The post-processing system  30  is preferably in communication with the controller through a dial-up, TCP/IP, or local area network (LAN) connection. The post-processing system  30  provides intermediate processing of gathered data, which is analyzed to provide lower-level, local warnings. These lower-level, local warnings are in contrast to more detailed, higher-level warnings provided by the post-processing routines of the management center  12 . The post-processing system  30  is preferably an “In-Store Information Server,” or ISIS, that also provides a web gateway functionality. The ISIS platform of the preferred embodiment is a JACE/controller/web server commercially available from Tridium, Inc., of Richmond, Va., U.S.A. 
   With reference to  FIGS. 2 and 3 , an exemplary refrigeration system  100  of the remote location  14  preferably includes a plurality of refrigerated food storage cases  102 . The refrigeration system  100  includes a plurality of compressors  104  piped together with a common suction manifold  106  and a discharge header  108  all positioned within a compressor rack  110 . A discharge output  112  of each compressor  102  includes a respective temperature sensor  114 . An input  116  to the suction manifold  106  includes both a pressure sensor  118  and a temperature sensor  120 . Further, a discharge outlet  122  of the discharge header  108  includes an associated pressure sensor  124 . As described in further detail hereinbelow, the various sensors are implemented for evaluating maintenance requirements. 
   The compressor rack  110  compresses refrigerant vapor that is delivered to a condenser  126  where the refrigerant vapor is liquefied at high pressure. The condenser  126  includes an associated ambient temperature sensor  128  and an outlet pressure sensor  130 . This high-pressure liquid refrigerant is delivered to a plurality of refrigeration cases  102  by way of piping  132 . Each refrigeration case  102  is arranged in separate circuits consisting of a plurality of refrigeration cases  102  that operate within a certain temperature range.  FIG. 2  illustrates four (4) circuits labeled circuit A, circuit B, circuit C and circuit D. Each circuit is shown consisting of four (4) refrigeration cases  102 . However, those skilled in the art will recognize that any number of circuits, as well as any number of refrigeration cases  102  may be employed within a circuit. As indicated, each circuit will generally operate within a certain temperature range. For example, circuit A may be for frozen food, circuit B may be for dairy, circuit C may be for meat, etc. 
   Because the temperature requirement is different for each circuit, each circuit includes a pressure regulator  134  that acts to control the evaporator pressure and, hence, the temperature of the refrigerated space in the refrigeration cases  102 . The pressure regulators  134  can be electronically or mechanically controlled. Each refrigeration case  102  also includes its own evaporator  136  and its own expansion valve  138  that may be either a mechanical or an electronic valve for controlling the superheat of the refrigerant. In this regard, refrigerant is delivered by piping to the evaporator  136  in each refrigeration case  102 . The refrigerant passes through the expansion valve  138  where a pressure drop causes the high pressure liquid refrigerant to achieve a lower pressure combination of liquid and vapor. As hot air from the refrigeration case  102  moves across the evaporator  136 , the low pressure liquid turns into gas. This low pressure gas is delivered to the pressure regulator  134  associated with that particular circuit. At the pressure regulator  134 , the pressure is dropped as the gas returns to the compressor rack  110 . At the compressor rack  110 , the low pressure gas is again compressed to a high pressure gas, which is delivered to the condenser  126 , which creates a high pressure liquid to supply to the expansion valve  138  and start the refrigeration cycle again. 
   A main refrigeration controller  140  is used and configured or programmed to control the operation of the refrigeration system  100 . The refrigeration controller  140  is preferably an Einstein Area Controller offered by CPC, Inc. of Atlanta, Ga., U.S.A., or any other type of programmable controller that may be programmed, as discussed herein. The refrigeration controller  140  controls the bank of compressors  104  in the compressor rack  110 , via an input/output module  142 . The input/output module  142  has relay switches to turn the compressors  104  on an off to provide the desired suction pressure. A separate case controller (not shown), such as a CC-100 case controller, also offered by CPC, Inc. of Atlanta, Ga., U.S.A., may be used to control the superheat of the refrigerant to each refrigeration case  102 , via an electronic expansion valve in each refrigeration case  102  by way of a communication network or bus. Alternatively, a mechanical expansion valve may be used in place of the separate case controller. Should separate case controllers be utilized, the main refrigeration controller  140  may be used to configure each separate case controller, also via the communication bus. The communication bus may either be a RS-485 communication bus or a LonWorks Echelon bus that enables the main refrigeration controller  140  and the separate case controllers to receive information from each refrigeration case  102 . 
   Each refrigeration case  102  may have a temperature sensor  146  associated therewith, as shown for circuit B. The temperature sensor  146  can be electronically or wirelessly connected to the controller  140  or the expansion valve for the refrigeration case  102 . Each refrigeration case  102  in the circuit B may have a separate temperature sensor  146  to take average/min/max temperatures or a single temperature sensor  146  in one refrigeration case  102  within circuit B may be used to control each refrigeration case  102  in circuit B because all of the refrigeration cases  102  in a given circuit operate at substantially the same temperature range. These temperature inputs are preferably provided to the analog input board  142 , which returns the information to the main refrigeration controller  140  via the communication bus. 
   Additionally, further sensors are provided and correspond with each component of the refrigeration system and are in communication with the refrigeration controller. Energy sensors  150  are associated with the compressors  104  and condenser  126  of the refrigeration system  100 . The energy sensors  150  monitor energy consumption of their respective components and relay that information to the controller  140 . 
   Circuits and refrigeration cases  102  of the refrigeration system  100  include a screen  152  illustrating the type and status of the refrigeration case  102  or circuit. Temperatures are displayed via graphical means (e.g. a thermometer) with an indication of set point and alarm values. The screen  152  supports a display of case temperatures (i.e. return, discharge, defrost termination, coil in, coil out, and product temperatures) and the status of any digital inputs (i.e. cleaning, termination, etc.). The screen  152  also displays a defrost schedule and the type of termination (i.e. time, digital, temperature) for the last defrost. In general, all information related to a refrigeration case  102  or circuit will be displayed on or accessible through the screen  152 . 
   A screen  154  is also provided to graphically display the status of each configured suction group. Discharge and suction pressures are displayed as gauges intended to be similar to the gauge set a refrigeration mechanic would use. The corresponding saturated suction temperature will be displayed as well. In general, suction groups are displayed graphically with icons that represent each compressor  104 . The status of the compressors  104  is shown graphically, as well as the status of any configured unloaders. In general, all status information for a suction group is displayed on the screen  154 . 
   A screen  156  is also provided to graphically display the status of each configured condenser  126 . The suction and discharge pressure of the condenser  126  are displayed as gauges intended to be similar to a gauge set a refrigeration mechanic would use. The corresponding condensing temperature will be displayed as well. In general, the condenser  126  should be displayed graphically with icons that represent each fan of the condenser  126 . A status of the fans is shown graphically. In general, all status information for a condenser  126  will be displayed on the screen  156 . 
   A screen (not shown) will also be provided for roof top units (not shown), the detailed description of which is foregone. The status of the roof top unit will be shown with animated graphics (fan, airflow, cooling, heating, as animated pieces). The screen will also show the space temperature, supply temperature, etc. The set point and alarm values are shown for the space temperature. Humidity and humidity control may also be shown if configured. 
   It will be appreciated that the hereindescribed refrigeration system is merely exemplary in nature. The refrigeration system of the remote location may vary as particular design requirements of the location dictate. 
   Remote locations  14  having refrigeration systems  100  typically include food-product retailers and the like. The food-product retailers are concerned with both the safety and the aesthetic quality of the food products they sell. Generally, bacteria that pose a threat to human health are referred to as “pathogen” bacteria and grow quickly when the temperature of their host product rises above a certain threshold temperature. For example, forty-one (41) degrees Fahrenheit is recognized industry-wide as the temperature below which most pathogens grow slowly and below which perishable food products should be stored. Bacteria that diminish the quality (color, smell, etc.) of a food product are referred to as “spoiler” bacteria and have growth rates that vary from product to product. Spoiler bacteria generally grow more quickly than pathogen bacteria. Thus, a food product&#39;s quality may appear to be of poor color or smell but still safe for human consumption. Bacteria populations and disease risk are a function of both the frequency and severity of over-temperature product conditions. Biological growth rates increase non-linearly, as a product warms past about forty-one (41) degrees Fahrenheit. For example, a product at about fifty-one (51) degrees Fahrenheit is more likely to host large colonies of toxic bacteria than a product at about forty-four (44) degrees Fahrenheit. However, there may be as much risk from having the product in a case at about forty-four (44) degrees Fahrenheit for a longer period of time than in a single case at about fifty-one (51) degrees Fahrenheit for a shorter period of time. 
   The temperature of a host food product, as mentioned above, significantly influences the rate at which bacteria, whether spoiler or pathogen, grows. Generally, conventional refrigeration systems function using a cyclical temperature strategy. According to the cyclical temperature strategy, low and high temperature set points are predetermined. The refrigeration system operates to cool the products until the low temperature set point is achieved. Once achieving the low-temperature set point, the refrigeration system ceases cooling the food product and the temperature is allowed to rise until meeting the high-temperature set point. Once the high-temperature set point is achieved, cooling resumes until meeting the low-temperature set point. 
   With particular reference to  FIG. 4 , cyclical temperature control and its effects on bacterial growth will be discussed in detail. An increase in temperature increases the rate at which bacteria grows. Time period A of the chart of  FIG. 4  shows an exemplary increase in temperature from approximately thirty (30) degrees Fahrenheit to approximately fifty (50) degrees Fahrenheit. An increase in bacteria count is associated with the rise in temperature. The bacteria count of time period A rises from approximately ten thousand (10,000) counts/gm to approximately forty thousand (40,000) counts/gm. Time period B shows an exemplary decrease in temperature from the fifty (50) degrees Fahrenheit achieved at the end of time period A, to approximately thirty (30) degrees Fahrenheit. A decrease in the rate at which the bacteria grows is associated with the decrease in temperature. It is important to note, however, that the bacteria count still increases and only slows significantly when the temperature cools to about thirty (30) degrees Fahrenheit. The exemplary increase in bacteria count rises from approximately forty thousand (40,000) counts/gm to approximately seventy thousand (70,000) counts/gm. The first half of time period B reflects a significant rate of growth of bacteria while a decrease in the rate is not achieved until the latter half of time period B. Thus, re-chilling or re-freezing of food products does not kill or reduce the bacteria-count, but simply reduces the growth rate of the bacteria. 
   The system of the present invention implements a variety of monitoring and alarming routines provided in the form of software. Components of these routines include product temperature monitoring and alarming. To achieve this, the routines include a time/temperature alarming routine, a degree/minutes alarming routine and a bacteria-count alarming routine. While each of these routines is described in detail hereinbelow, it should be noted that in terms of food safety and quality they are listed in order of increasing effectiveness. In other words, the time/temperature alarming routine provides a good means of monitoring product temperature while the bacteria-count alarming routine provides the most effective means. 
   With reference to  FIG. 5 , the time/temperature alarming routine will be described in detail. Initially, both time and temperature set points are provided. In the exemplary embodiment of  FIG. 5 , the time set point is sixty (60) minutes and the temperature set point is about forty (40) degrees Fahrenheit. The time and temperature set points are combined to provide an alarming point. In the exemplary case, the alarming point would be the point at which the product has been at a temperature greater than forty (40) degrees Fahrenheit for longer than sixty (60) minutes. With reference to alarm scenario R 1  of  FIG. 5 , the product temperature passes forty (40) degrees Fahrenheit at point P 1 . Thus, the sixty (60) minute clock begins running at point P 1 . If the product temperature has not fallen back below about forty (40) degrees Fahrenheit within the sixty (60) minute timeframe then an alarm is signaled. Point M 1  represents the point at which sixty (60) minutes have passed and the temperature has remained over about forty (40) degrees Fahrenheit. Therefore, in accordance with the time/temperature routine, an alarm would be signaled at point M 1 . 
   Although the above-described time/temperature routine is a good method of monitoring product temperature, it retains specific disadvantages. One disadvantage is that bacteria count is not considered. This is best illustrated with reference to alarm scenario R 2 . As can be seen, the product temperature of alarm scenario R 2  increases, approaching the about forty (40) degrees Fahrenheit temperature set point without ever crossing it. As discussed above, with respect to  FIG. 4 , increases in temperature, even though below the about forty (40) degrees Fahrenheit temperature set point, results in increased rate of bacteria growth. Thus, although the time/temperature routine would not signal an alarm in alarm scenario R 2 , bacteria growth would continue, approaching undesired levels of bacteria count over time. 
   With reference to  FIG. 6 , the degree/minutes alarming routine will be described in detail. Initially, a degree/minutes set point is determined. In the exemplary case, the degree/minutes set point is about eight hundred (800). This value is provided as an average value determined from historical data and scientific testing and analysis of bacteria growth. In this manner, bacteria growth is considered when determining whether an alarm is signaled. With reference to alarm scenarios R 1  and R 2  of  FIG. 6 , the degree/minute alarming routine integrates the ideal product temperature curve (i.e., area above “ideal temp” line) with respect to time. If the integration results in a value of about eight hundred (800) or greater, an alarm is signaled. In the exemplary case both alarm scenarios R 1 , R 2  would result in an alarm. Alarm scenario R 1  would most likely signal an alarm prior to alarm scenario R 2 . This is because the bacteria growth rate would be significantly higher for alarm scenario R 1 . An alarm would be signaled in alarm scenario R 2  because, although the product temperature of alarm scenario R 2  never rises above an accepted temperature (i.e., about forty (40) degrees Fahrenheit), the borderline temperature of alarm scenario R 2  results in a high enough bacteria growth rate that undesired bacteria levels would be achieved in time. 
   With reference to  FIG. 7 , the bacteria-count alarming routine will be described in detail. Initially, an alarm set point is determined according to the maximum acceptable bacteria count for the product. In the exemplary case, the alarm set point is approximately one hundred twenty thousand (120,000) counts/gm.  FIG. 7 , similarly to  FIG. 4 , shows a cyclical-temperature curve and a bacteria-count curve. The bacteria-count routine periodically calculates the bacteria count for a given temperature at a given time, thereby producing the bacteria-count curve. Given the cyclical temperature of the exemplary case of  FIG. 7 , neither of the aforementioned alarming routines would signal an alarm. However, once the bacteria count is greater than the approximately one hundred twenty thousand (120,000) counts/gm alarm set point, an alarm is signaled. As noted previously, the bacteria count alarming routine is the most effective of those described herein. The effectiveness of the bacteria count alarming routine is a result of the direct relation to an actual bacteria count of the product. 
   Bacteria count is calculated for each type of bacteria (i.e., pathogen, spoiler), and is a function of a base bacteria count, time, product type, and temperature. Initially, base bacteria counts (N o ) are provided for each type of bacteria. As provided by the present invention, an exemplary base bacteria count for pathogen bacteria is about one hundred (100) counts/gram and for spoiler bacteria is about ten thousand (10,000) counts/gram. These values have been determined through experiment and analysis of the bacteria types. Both the product type and temperature determines the rate at which a particular type of bacteria will grow. The present invention further provides initial temperatures for both pathogen and spoiler bacteria, at which, their respective growth is effectively stopped. In an exemplary embodiment, the initial temperature for pathogens is twenty-nine (29) degrees Fahrenheit and for spoilers is eighteen and one-half (18.5) degrees Fahrenheit. Similarly to the initial bacteria count values, these values have been determined through experiment and analysis of the bacteria types. In general, experimental bacteria counts for both pathogens and spoilers were plotted with respect to temperature. A line was interpolated for each and extrapolated to find their respective y-intercepts, or temperature values for zero growth. 
   Algorithms are provided in the form of software modules that can reside either in software module twenty-two (22) or post-processing system thirty (30) (ISIS). Both spoiler and pathogen bacteria are calculated based on time and temperature measured by an infrared temperature gun two hundred (200) or a food product simulator two hundred two (202). A food quality alarm is generated when the spoiler bacteria multiplies ten (10) times and food safety alarm is generated when pathogen bacteria multiplies five (5) times. Additionally, index calculation, namely FQI and FSI, is done to rate the performance of a fixture, department or store within a chain. As a result the FSI determination uses worst-case values to provide a conservative valuation of food safety risk and to minimize the possibility of an undetected food safety problem. The FQI enables monitoring of the aesthetic quality of products, thereby enabling the remote location to increase the shelf life of perishable products resulting in increased customer satisfaction and cost savings. 
   With reference to  FIG. 8 , the algorithm for calculating the FSI will be described in detail. The FSI of the present invention corresponds to bacterial risk levels and provides a method for relative-risk evaluation. Initially, at step  800 , the temperature of a product sample from each of the product groups (P 1 , P 2 , . . . , P j ) will be measured in each of the cases (C 1 , C 2 , . . . , C i ) (see  FIG. 3 ). Thus, a temperature matrix is formed accounting for a sample of each of the products in each of the cases: 
   
     
       
             
             
             
             
             
           
         
             
                 
             
           
           
             
               C 1 : 
               T 11   
               T 12   
               . . .  
               T 1j   
             
             
               C 2 : 
               T 21   
               T 22   
               . . .  
               T 2j   
             
             
               C i : 
               T i1   
               T i2   
               . . .  
               T ij   
             
             
                 
             
           
        
       
     
   
   After the product temperatures are measured, the maximum product temperature is determined for each case (C 1 , C 2 , . . . , C i ), at step  810 , as follows:
 
MAX ( T   11   , T   12   , . . . , T   1j )= T   1MAX 
 
MAX ( T   21   , T   22   , . . . , T   2j )= T   2MAX 
 
MAX ( T   i1   , T   i2   , . . . , T   ij )= T   iMAX 
 
   Each food product (P 1 , P 2 , . . . , P j ) has an associated expected shelf life rating (S 1 , S 2 , . . . , S j ). The shelf life ratings (S 1 , S 2 , . . . , S j ), designated at step  820 , are based on scientifically developed and experimentally confirmed micro-organism growth equations. At step  830 , the maximum shelf life rating (S 1MAX , S 2MAX , . . . , S jMAX ) for the products (P 1 , P 2 , . . . , P j ) within each case (C 1 , C 2 , . . . , C i ) is determined as follows:
 
MAX ( S   11   , S   12   , . . . , S   1j )= S   1MAX 
 
MAX ( S   21   , S   22   , . . . , S   2j )= S   2MAX 
 
MAX ( S   i1   , S   i2   , . . . , S   ij )= S   iMAX 
 
   Each food product (P 1 , P 2 , . . . , P j ) further has an associated base bacteria count (N o1 , N o2 , . . . , N oj ). At step  840 , the maximum base bacteria count (N o1 , N o2 , . . . , N oj ) for the products (P 1 , P 2 , . . . , P j ) within each case (C 1 , C 2 , . . . , C i ) is determined as follows:
 
MAX ( N   o11   , N   o12   , . . . , N   o1j )= N   o1MAX 
 
MAX ( N   o21   , N   o22   , . . . , N   o2j )= N   o2MAX 
 
MAX ( N   oi1   , N   oi2   , . . . , N   oij )= N   oiMAX 
 
   Having determined the maximum temperature, the maximum shelf-life rating and the maximum base bacteria count for the products (P 1 , P 2 , . . . , P j ) in each case (C 1 , C 2 , . . . , C i ), a bacteria count (N 1t , N 2t , . . . , N it ) is calculated for a specific time (t) for each case (C 1 , C 2 , . . . , C i ) at step  850 . The bacteria count (N 1t , N 2t , . . . , N it ) is a function of the maximum product temperature, the maximum base bacteria count, and the maximum shelf-life rating, as determined above, with respect to the type of bacteria concerned. The bacteria count is provided as:
 
 N   it   =N   oimax ×2 gi 
 
where  g   i =shelf life×[ m×T   p   +c]   2 
 
   In the case of food safety, the concerned bacteria are pathogens. Thus, the values m and c are the slope and intercept for the model generated for pathogen bacteria, discussed above. 
   Having determined the bacteria counts (N 1t , N 2t , . . . , N it ) and the threshold maximum base bacteria counts (N o1MAX , N o2MAX , . . . , N ojMAX ), the food safety index (FSI) for each case (C 1 , C 2 , . . . , C i ) is calculated at step  870 . The calculation of the FSI for each case is determined by the following equation:
 
 FSI   i =100×[1−[In( N   it   /N   oiMAX )/In 2]×0.2]
 
   As a result, FSI values for each case are calculated. 
   Bacteria populations and disease risk are a function of both the frequency and severity of over-temperature product conditions. Biological growth rates increase non-linearly, as a product warms past forty-one (41) degrees Fahrenheit. For example, a product at fifty-one (51) degrees Fahrenheit is more likely to host large colonies of toxic bacteria than a product at forty-four (44) degrees Fahrenheit. However, there may be as much risk from having the product in a case at forty-four (44) degrees Fahrenheit for a longer period of time than in a single case at fifty-one (51) degrees Fahrenheit for a shorter period of time. To account for this variation, an average safety factor FSI AVG  is used. 
   Having determined a FSI for each case of the refrigeration system, secondary parameters B and R are subsequently calculated at step  875 . The secondary parameter B is equal to the number of cases and R is equal to the sum of all of the FSIs for the cases that has potentially hazardous food (PHF). At step  880 , secondary parameters B and R are used to calculate the average FSI, as follows:
 
 FSI   AVG   =R/B 
 
   Thus, the FSI for a department or store is provided as FSI AVG . 
   With particular reference to  FIG. 9 , the algorithm for calculating the FQI will be described in detail. Initially, at step  900 , the temperature of each of the product groups (P 1 , P 2 , . . . , P j ) will be measured in each of the cases (C 1 , C 2 , . . . , C i ) (see  FIG. 2 ). Thus, a temperature matrix is formed accounting for all of the products in all of the cases: 
   
     
       
             
             
             
             
             
           
         
             
                 
             
           
           
             
               C 1 : 
               T 11   
               T 12   
               . . .  
               T 1j   
             
             
               C 2 : 
               T 21   
               T 22   
               . . .  
               T 2j   
             
             
               C i : 
               T i1   
               T i2   
               . . .  
               T ij   
             
             
                 
             
           
        
       
     
   
   After the product temperatures are measured, the average temperature for each product group P within each case C is determined at step  910 .
 
 T   1AVG =AVG( T   11   , T   12   , . . . , T   1j )
 
 T   2AVG =AVG ( T   21   , T   22   , . . . , T   2j )
 
 T   iAVG =AVG( T   i1   , T   i2   , . . . , T   ij )
 
   As discussed above with respect to the FSI, each food product has an associated shelf-life rating (S 1 , S 2 , . . . , S i ). At step  920  of the FQI calculation, the average shelf-life rating (S 1AVG , S 2AVG , . . . , S jAVG ) for the products (P 1 , P 2 , . . . , P j ) within each case (C 1 , C 2 , . . . , C i ) is determined as follows:
 
AVG ( S   11   , S   12   , . . . , S   1j )= S   1AVG 
 
AVG ( S   21   , S   22   , . . . , S   2j )= S   2AVG 
 
AVG ( S   i1   , S   i2   , . . . , S   ij )= S   iAVG 
 
   As further discussed above, each food product (P 1 , P 2 , . . . , P j ) has an associated base bacteria count (N o1 , N o2 , . . . , N oj ). At step  930 , the average base bacteria count (N o1AVG , N o2AVG , . . . , N ojAVG ) for the products (P 1 , P 2 , . . . , P j ) within each case (C 1 , C 2 , . . . , C i ) is determined as follows:
 
AVG ( N   o11   , N   o12   , . . . N   o1j )= N   o1AVG 
 
AVG ( N   o21   , N   o22   , . . . , N   o2j )= N   o2AVG 
 
AVG ( N   oi1   , N   oi2   , . . . , N   oij )= N   oiAVG 
 
   Furthermore, an ideal storage temperature TI is associated with each product P. The product mixes for each case C are determined at step  940  and are generally given as follows:
 
C i [P 1 %, P 2 %, . . . , P j %]
 
   Using the product mix values, a weighted average is determined for the ideal temperature TI, at step  950 , as follows:
         Ideal Temperature TI:
 
 TI   1AVG   =TI   1   P   1 %+ TI   2   P   2 %+ . . . + TI   j   P   j %
 
 TI   2AVG   =TI   1   P   1 %+ TI   2   P   2 %+ . . . + TI   j   P   j %
 
 TI   iAVG   =TI   1   P   1 %+ TI   2   P   2 %+ . . . + TI   j   P   j %
       

   Having determined the average temperature, the average shelf-life rating and the average base bacteria count for the products (P 1 , P 2 , . . . , P j ) in each case (C 1 , C 2 , . . . , C i ), a bacteria count (N 1t , N 2t , . . . , N it ) is calculated for a specific time (t) for each case (C 1 , C 2 , . . . , C i ). The bacteria count (N 1t , N 2t , . . . , N it ) is a function of the average product temperature, the average base bacteria count, and the average shelf-life rating, as determined above, with respect to the type of bacteria concerned. In the case of food quality, the concerned bacteria are spoiler. The bacteria count is calculated as previously discussed hereinabove. 
   Having determined the bacteria counts (N 1t , N 2t , . . . , N it ) and the average base bacteria counts (N o1AVG , N o2AVG , . . . , N oiAVG ), the food quality index (FQI) for each case (C 1 , C 2 , . . . , C i ) is calculated at step  970 . The calculation of the FQI for each case is determined by the following equation:
 
 FQI   i =100×[1−[In( N   it   /N   oiAVG )/In 2]×0.1]
 
   As a result, FQIs are calculated for each case C. 
   Having determined the FQI for each case C of the refrigeration system, secondary parameters B and R are subsequently calculated at step  975 . As before, secondary parameter B is equal to the number of cases and R is equal to the sum of all of the quality factors. At step  980 , secondary parameters B and R are used to calculate the average quality factor FQI AVG , as follows:
 
 FQI   AVG   =R/B 
 
   Thus, the FQI for a department or store is provided as FQI AVG . 
   The system further provides a method for estimating the shelf life of products within a specific case as a function of historical temperature data and any occurrences (e.g. power outages and the like) at a particular location. The shelf life estimation method is case based. A new counter is started for each day and has a maximum length of five (5) days. Generally, food product turnover is less than five (5) days, however, the maximum length of days may vary. For each day, bacteria count is determined, as described above, using the particular temperatures experienced by the case for that day. In this manner, the growth of bacteria for the given case can be monitored and evaluated to determine how much longer products put into the case on a particular day may safely remain in the case. For example, the shelf life of a product that has been put into a case one day ago is a function of the temperatures experienced over the first day. At the same time, however, the shelf life of a product that has been in the case for three days will be determined as a function of the temperatures experienced over those three days. 
   In a first preferred embodiment, the temperature measurements for either the FSI or FQI calculation are achieved using a hand-held infrared temperature sensor measurement device such as an infrared temperature gun  200  (see  FIG. 3 ) commonly known in the art during an “audit” process. It is anticipated that the gun  200  will measure the temperatures of a sample of each product group and determine the average, minimum and maximum temperature values. In this manner, only one audit process is required to calculate both FSI and FQI. The audit process preferably occurs regularly (i.e., yearly, monthly, weekly, daily, etc.). 
   It is also anticipated that continuous food product temperature measurement is achieved real-time, as opposed to an audit process. For example, a food product simulator  202  (see  FIG. 3 ) may be disposed in each refrigerator case (C i ) for each food product group (P j ) within the refrigerator case (C i ). A detailed description of the food product simulator is provided in co-pending application Ser. No. 09/564,173, filed on May 3, 2000, with the United States Patent and Trademark Office, entitled “Wireless Method And Apparatus For Monitoring And Controlling Food Temperature,” hereby incorporated by reference. The product group temperature samples are read by the controller  140  and are continuously monitored during a “monitor” process. It is anticipated that at least one simulator  202  will be present for each product group (P j ) in a particular case (C i ). The monitor process may record temperature values at a predetermined rate (i.e., every minute, 10 minutes, etc.) that is operator programmable into the controller  140 , or real-time. The implementation of a food product simulator  202  is exemplary in nature and it is anticipated that other products and methods can be used to achieve real-time or periodic sampling within the scope of the invention. 
   As discussed previously, the present invention provides a method for gathering and processing energy consumption information for various equipment within a food retailer. Of particular importance is the energy consumption of the refrigeration system  100 . To monitor the energy consumption performance of the refrigeration system  100 , a software module  22  is provided that runs the hereindescribed algorithms and routines required. In the present embodiment, the software is provided as a Microsoft™ Excel™ workbook implementing the Visual Basic programming language. It is anticipated, however, that the software may be provided in any one of a number of formats or programmed using any one of a number of programming languages commonly known in the art. 
   With reference to  FIG. 10 , a schematic overview of the present method and supporting software is shown. In general, the method of the present invention operates around a core calculator  210  that receives information from an input block  212  and provides outputs to both an efficiency block  214  and a design block  216 . The input block  212  includes three main components. The first component is weather data  218  provided as a look-up table, based on information from the American Society of Heating, Refrigerating and Air Conditioning Engineers, Inc. (ASHRAE) of Atlanta, Ga., U.S.A. The ASHRAE look-up table includes general climate information for several cities throughout the United States and Canada, as averages over a ten-year period. With reference to  FIG. 11 , a screen-shot is provided displaying the ASHRAE data as it would appear in an Excel™ workbook and  FIG. 12  provides a schematic layout of the ASHRAE component. The ASHRAE data includes both wet and dry bulb temperature data for the remote location  14  during particular months. As seen in  FIG. 11 , temperature information is provided for specific cities based upon month and a bin temperature. The bin temperatures range from a maximum of one hundred twenty-six and one-half (126.5) degrees Fahrenheit and step down by increments of seven (7) degrees Fahrenheit. Reading  FIG. 11 , the number of hours a particular city experiences a particular temperature in the particular month, is provided. For example, during the month of January, Edmonton, Alberta, Canada experiences a dry bulb temperature of thirty-five (35) degrees Fahrenheit for a total of eight (8) hours that month. Current ASHRAE data may be imported, as shown in  FIG. 13 , thereby ensuring the most current data for the dependent calculations. The ASHRAE component provides output information for use by the core calculator. 
   The second component includes actual site data  220 , which comprises both store specification and new site data components  222 , 224 , respectively, as shown schematically in  FIG. 14 . The store specification component  222  accounts for the various refrigeration components operating at a specific remote location  14 . With reference to  FIG. 15 , a screen-shot is provided displaying an exemplary remote location  14  and its related refrigeration components, as it would appear in an Excel™ workbook. A standard component list is provided and only the information for equipment actually on-site is listed in the corresponding cells. This information includes: system name, size line-up and load (BTU/hr). The information is provided per a rack type (i.e., low temperature rack, medium temperature rack, etc.). Particular information from the store specification component  222  is also provided to the design block  216 , as described in further detail hereinbelow. 
   With reference to  FIG. 16 , a screen-shot is provided displaying exemplary data from a food retailer, as provided by the new site data component. The new site data component  224  is an import sheet that imports actual retailer data by month, date and hour. This data includes ambient temperature and power usage per rack type. 
   Again referencing  FIG. 10 , the third component of the input block includes a database  226  of information regarding actual operational parameters for specific equipment types and manufacturers. This information would be provided by CPC, Inc. of Atlanta, Ga., U.S.A. It is anticipated that this information be employed to evaluate a particular component&#39;s performance to other component&#39;s in the industry as a whole. 
   The core calculator  210  calculates the projected energy use per rack type. The calculations are provided per ambient temperature and are calculated using information from the input block  212  and the design block  216  as described in more detail below. With particular reference to  FIG. 17 , a screen-shot is provided displaying a portion of the core calculator  210 . As shown, a range of ambient temperatures is provided in the left-most column. It is important to note that these temperatures are not bin temperatures, as described above, but are provided as actual ambient temperatures. The core calculator  210  calculates the total annual energy consumption for both the compressor and condenser of a particular type of rack. These values are shown in the right-most columns of  FIG. 17 . For example, given an ambient temperature of zero (0) degrees Fahrenheit, the total theoretical compressor energy usage is 29.34 kWh, as based upon individual suction temperatures, and the total theoretical condenser energy usage is 0.5 kWh. 
   The efficiency block output includes two main tools: a power monitoring tool  230  and an alarming tool  232 , shown schematically in  FIGS. 18 and 19 , respectively. The power monitoring tool  230  provides an evaluation of the equipment power usage as compared between a calculated value, from the core calculator  210 , and the actual power usage, imported from actual site data. The power monitoring tool  230  receives inputs from the core calculator  210 , actual site data  220 , new site data  224  and its output is a function of operator selectable date, time and location. With reference to  FIG. 20 , a screen-shot is provided for the power monitoring tool  230 . The input received from the core calculator  210  includes a value for the projected use, as referenced by ambient temperature. The actual site data  226  provides the power monitoring tool  230  with the ambient temperature for each hour of the particular day. The new site data  224  provides actual use information, which is manipulated by the power monitoring  230  tool to be summarized by hour, day and month. Using this information, the power monitoring tool  230  provides a summary per rack type, whereby the actual usage is compared to the projected usage and a difference is given. In this manner, the performance of the refrigeration system  100  of a particular remote location  14  may be evaluated for efficiency. 
   The alarming tool  232  is shown schematically in  FIG. 19  and includes alarm limits for alerting a remote location  14  when equipment efficiencies fall below a particular limit. The alarming tool  232  may be implemented on-site, thereby readily providing an efficiency alert to initiate a quick correction action, as well as being implemented at the management center  12 . 
   With further reference to  FIG. 10 , the design block output provides energy usage calculations based upon specific design scenarios and includes two components: a design set-up component  234  and a design results component  236 . The design set-up component  234  interacts with the core calculator  210 , providing the core calculator  210  with input information and receiving calculations therefrom. With reference to  FIGS. 21 and 22 , a screen-shot and a schematic view are respectively provided for the design set-up component  234 . A user may input various design scenario information and is provided with a theoretical annual energy usage calculation. 
   The design set-up component  234  enables a user to input specific component and operation environment variables to evaluate any one of a number of possible operational scenarios. Each of these scenarios may be saved, deleted and retrieved, as a user desires. The user must input specification information for components such as a compressor, evaporator, sub-cooler, condenser and the like. With respect to the compressor and evaporator, inputs such as refrigerant type, superheat temperature and condenser cut-out pressure are required. The sub-cooler inputs include whether a sub-cooler is present, the dropleg cut-out temperature and fluid out temperature. The condenser inputs include the condenser capacity (BTU/hr—F), fan power (hp), actual fanpower (%), temperature difference type, whether fan cycling or variable speed, condenser temperature difference, ambient sub-cooling and HP capacity. The design set-up component  232  uses the horsepower capacity to determine a % horsepower. 
   Suction information is also provided per rack type. This information includes cut-in pressure, cut-out pressure and efficiency. Further, the store specification component  222  provides the design set-up component  232  with the total load (BTU/hr) for each rack type of the specific location. 
   The design set-up component  232  provides a summary table, briefly summarizing the energy usage per rack type. The design set-up component  232  further calculates a minimum condenser temperature, and suction calculations including cut-in temperature, cut-out temperature and average suction temperature. 
   The design results component  234  provides a more detailed breakdown of the power usage. With reference to  FIGS. 23 and 24 , a screen-shot and a schematic view are respectively provided for the design results component  234 . The design results component  234  provides output information as a function of whether temperature is measured by dry or wet bulb for the given remote location  14 . The output information includes projected use in kWh for both the compressor and condenser. This information is further compiled into total use, by month, and displayed graphically. 
   Because many of the calculations are based upon the provided ASHRAE data, it is important to consider the actual temperatures experienced at a particular location versus the average temperature provided by the ASHRAE data. With reference to  FIG. 25 , a screen-shot is provided displaying a comparison between the actual average temperatures for a particular month versus typical (i.e., ASHRAE) average temperatures for the particular month. Considering this information, deviations between the projected energy usage and actual energy usage may be more thoroughly evaluated, thereby providing a better analysis of the operation of the refrigeration system  100 . 
   With reference to  FIG. 26 , energy usage characteristics are summarized in tabular form. The total actual and projected energy usage for all rack types is provided on a daily basis for a particular month. Other tables breakdown the total by rack type. In this manner, energy usage performance may be quickly and easily summarized and evaluated for determining future operational activity. 
   As discussed above, the system  10  of the present invention provides control and evaluation algorithms, in the form of software modules  22 , for predicting maintenance requirements for the various components in the remote location  14 . In the preferred embodiment, described hereinbelow, predictive maintenance algorithms will be described with respect to the refrigeration system  100 . 
   A first control algorithm is provided for controlling the temperature difference between the refrigerant of the condenser  126  and the ambient air surrounding the condenser  126 . The ambient air sensor  128  and the pressure sensor  130  of the condenser  126  are implemented to provide the inputs for the temperature difference control strategy. The pressure sensor  130  measures the refrigerant pressure exiting the condenser  126  and determines a saturation temperature (T SAT ) from a look-up table, as a function of the type of refrigerant used. The ambient air sensor  128  measures the temperature of the ambient air (T AMB ). The temperature differential (TD) is then calculated as the difference between the two, according to the following equation:
 
 TD=T   SAT   −T   AMB 
 
   The temperature difference algorithm further implements the following configuration parameters: condenser type (i.e., differential), control type (i.e., pressure), refrigerant type (e.g., R22, R404a), fast recovery, temperature difference set point and minimum temperature set point. In the exemplary embodiment, the temperature difference set point is ten (10) degrees Fahrenheit and the minimum temperature set point (T MIN ) is seventy (70) degrees Fahrenheit. The minimum temperature set point is the T SAT  corresponding to the lowest allowable condenser pressure. 
   A first maintenance algorithm is provided for determining whether the condenser  126  is dirty, as shown in  FIGS. 27A and 27B . Predicting the status of the condenser  126  is achieved by measuring the temperature difference for the condenser  126  over a specified period of time. To achieve this, a fan (not shown) associated with the condenser  126  is turned on for a specified period of time (e.g., half hour) and the temperature difference (TD) is calculated, as described above, approximately every five (5) seconds. The average of the TD calculations is determined and stored into memory. An increase in the average TD indicates that the condenser  126  is dirty and requires cleaning. In this case an alarm is signaled. It should be noted, however, that the TD value is only meaningful if T AMB  is at least ten (10) degrees Fahrenheit lower than T MIN . If the condenser  126  has been cleaned, the dirty condenser algorithm of the controller must be reset for recording a new series of TDs. 
   The present invention further provides an alternative algorithm for detecting a dirty condenser situation. Specifically, the heat rejection (Q) of the condenser  126  is evaluated. The heat rejection is a function of an overall heat transfer coefficient (U), a heat transfer area (A) and a log mean temperature difference (LMTD), and is calculated by the following equation:
 
 Q=U×A ×( LMTD )
 
   The LMTD can be approximated as the TD measurements, described above. A value for Q can be approximated from the percentage output of the compressors  102  operating with the condenser  126 . Further, the above equation can be rearranged to solve for U:
 
 U=Q/A×TD 
 
   Thus, U can be consistently monitored for the condenser  126 . An increase in the calculated value of U is indicative of a dirty condenser situation. 
   A second maintenance algorithm is provided as a discharge temperature monitoring algorithm, shown in  FIG. 28 , usable to detect compressor malfunctioning. For a given suction pressure and refrigerant type, there is a corresponding discharge temperature for the compressor  102 . The discharge temperature monitoring algorithm compares actual discharge temperature (T DIS     —     ACT ) to a calculated discharge temperature (T DIS     —     THR ). T DIS     —     ACT  is measured by the temperature sensors  114  associated with the discharge of each compressor  102 . Measurements are taken at approximately 10 second intervals while the compressors  102  are running. T DIS     —     THR  is calculated as a function of the refrigerant type, discharge pressure (P DIS ), suction pressure (P SUC ) and suction temperature (T SUC ), each of which are measured by the associated sensors described hereinabove. An alarm value (A) and time delay (t) are also provided as presets and may be user selected. An alarm is signaled if the difference between the actual and calculated discharge temperature is greater than the alarm value for a time period longer than the time delay. This is governed by the following logic:
 
If ( T   DIS     —     ACT   −T   DIS     —     THR )&gt; A  and time&gt; t , then alarm
 
   A third maintenance algorithm is provided as a compressor superheat monitoring algorithm, shown schematically in  FIGS. 29A and 29B , usable to detect liquid refrigerant flood back. The superheat is measured at both the compressor suction manifold  106  and discharge header  108 . The basis of the compressor superheat monitoring algorithm is that when liquid refrigerant migrates to the compressor  102 , superheat values decrease dramatically. The present algorithm detects sudden decreases in superheat values at the suction manifold  106  and discharge header  108  for providing an alarm. 
   With particular reference to  FIG. 29A , the superheat monitoring at the suction manifold  106  will be described in detail. Initially, T SUC  and P SUC  are measured by the suction temperature and pressure sensors  120 , 118  and it is further determined whether all of the compressors  102  are on. A saturation temperature (T SAT ) is determined by referencing a look-up table using P SUC  and the refrigerant type. An alarm value (A) and time delay (t) are also provided as presets and may be user selected. An exemplary alarm value is fifteen (15) degrees Fahrenheit. The suction superheat (SH SUC ) is determined by the difference between T SUC  and T SAT . An alarm will be signaled if SH SUC  is greater than the alarm value for a time period longer than the time delay. This is governed by the following logic:
 
If SH SUC &gt;A and time&gt;t, then alarm
 
   With particular reference to  FIG. 29B , the superheat monitoring at the discharge header  108  will be described in detail. Initially, discharge temperature (T DIS ) and discharge pressure (P DIS ) are measured by the discharge temperature and pressure sensors  114 , 124 . It is also determined whether the particular compressor  102  is on. A saturation temperature (T SAT ) is determined by referencing a look-up table using PDIS and the refrigerant type. An alarm value (A) and time delay (t) are also provided as presets and may be user selected. An exemplary alarm value is fifteen (15) degrees Fahrenheit. The discharge superheat (SH DIS ) is determined by the difference between T DIS  and T SAT . An alarm is signaled if SH DIS  is greater than the alarm value for a time period longer than the time delay. This is governed by the following logic:
 
If SH SUC &gt;A and time&gt;t, then alarm
 
   A severe flood back alarm is also provided. A severe flood back occurs when both a suction flood back state and a discharge flood back state are determined. In the event that both the suction flood back alarm and the discharge flood back alarm are signaled, as described above, the severe flood back alarm is signaled. 
   A fourth maintenance algorithm is provided as a relay output monitoring algorithm, shown schematically in  FIG. 30 , usable to initiate an electrical contractor service call. In general, the relay output monitoring algorithm counts the number of on/off transition states for a given relay. The number of counts is provided to a service block that is preset with a service count value. If the number of counts is greater than the service count value then a service call is automatically placed to an electrical contractor. 
   More specifically, the algorithm initially sets an old relay state to OFF if a counter reset has been signaled or the algorithm is running for the first time. Next, the algorithm retrieves a new relay state value (i.e., ON or OFF). The algorithm then compares the new relay state value to the old relay state value. If they are unequal, the number counter is increased by a single increment. 
   Other maintenance algorithms include: contactor count, compressor run-time, oil checks, dirty air filter and light bulb change. The contactor count algorithm counts the number of times a compressor  102  cycles (i.e., turned ON/OFF). A contactor count limit is provided, whereby once the number of cycles surpasses the count limit, a work order is automatically issued by the system for signaling preventative maintenance. Similarly, the compressor run-time algorithm monitors the amount of time a compressor  102  has run. A run-time limit is provided, whereby once the run-time surpasses the run-time limit, a work order is automatically issued by the system for signaling routine maintenance. 
   As discussed in detail above, the system  10  of the present invention provides a method of monitoring and evaluating energy consumption for various components of the refrigeration system  100 . It is further anticipated, however, that the present system  10  includes additional algorithms for optimizing energy efficiency of all energy using devices within a location. To this end, power meters are provided for significant energy components of the location, including but not limited to: refrigeration circuits and condensers, HVAC, lighting, etc. With reference to  FIG. 31 , it is anticipated that the system  10  provides energy saving algorithms for each of the identified areas, including: the VSD compressor, optimum humidity control, optimum head pressure control, load management, defrost management, suction float and head pressure float. 
   The system  10  of the present invention further provides an alarming system for alerting the management center  12  or intermediate processing center of particular situations. The graph provided in  FIG. 32  outlines ten main alarming conditions and the corresponding operator action. These alarming conditions include: discharge air temperature sensor failure, product temperature sensor failure, discharge air temperature exceeded, discharge air degree-minute exceeded, product time-temperature exceeded, product degree-minute exceeded, product FDA time-temperature exceeded, spoiler count exceeded, pathogen count exceeded and product temperature cycling. As shown schematically in  FIG. 33 , the first six alarming conditions relate to equipment failure that would potentially lead to food quality and safety problems. The last four alarming conditions relate directly to food quality and safety. 
   As described in detail above, the system  10  provides a web-based operator interface for monitoring the conditions of a remote location  14 . With reference to  FIG. 34 , a screen-shot is provided detailing an exemplary user interface for monitoring the status of a particular fixture within a particular remote location  14 . The centrally disposed graph  300  provides real-time output of both the discharge air temperature and the product temperature, as provided by the product simulators, described above. Further provided are discharge air temperature and product probe temperature thermometers  302 , 304  for representing current temperature conditions. Disposed immediately below the real-time graph  300  is a notifications board  306  displaying each of the ten alarming conditions described above. Immediately below the notifications board  306  is a shelf-life estimation board  308  that shows the number of shelf-life hours remaining per the number of days a particular product has been stored within a particular case. The shelf-life estimation is calculated as described in detail above. 
   The description of the invention is merely exemplary in nature and, thus, variations that do not depart from the gist of the invention are intended to be within the scope of the invention. Such variations are not to be regarded as a departure from the spirit and scope of the invention.