Patent Document

TECHNICAL FIELD 
       [0001]    This invention relates generally to transport refrigeration systems and, more particularly, to a method and apparatus for detecting an excess level of CO 2  vapor in a container and providing an indication thereof to an operator. 
       BACKGROUND OF THE INVENTION 
       [0002]    Refrigerated vehicles have longed been employed in a wide variety of applications including the storing and marketing of perishable commodities, particularly produce such as fruit and vegetables, as well as other perishable foods, including processed and frozen or chilled products such as ice cream or the like. The refrigerated vehicles contemplated by the present invention include, for example, truck trailers for road transport and piggy-back use, railroad cars and container bodies contemplated for land and sea service and the like. Accordingly, all such refrigerated containers are included within the present invention under the general designation of refrigerated containers or vehicles adapted to receive cargo in a refrigerated space. 
         [0003]    Refrigeration systems for such refrigerated containers have generally used conventional refrigerants in a closed loop system which included an evaporator for cooling the air in the container. Because of environmental concerns, hydrochloro flourocarbons (HCFCS), such as R-22 have been discontinued and hydroflourocarbons (HFCS), such as R-134a, R-410a and R-407c have taken their place. However, because of these same environmental concerns, it has been desirable to replace the use of these HFCS with a more “benign” refrigerant which does not adversely react with the atmosphere. Accordingly, the use of CO 2  has now become attractive for use in vapor compression systems for refrigerated containers. 
         [0004]    One characteristic of carbon dioxide as a refrigerant is that it has low critical temperature and therefore, most CO 2  refrigerant vapor compression systems are designed for operation in the transcritical regime. This requires that they operate at substantially higher pressure then when operating with conventional refrigerants, and special compressors are designed for that purpose. In order to accommodate these higher pressures, the other components and tubing must be robust in their design. Still, the likelihood of leakage occurring within this system is greater than when operating with a lower pressure system with conventional refrigerants. 
         [0005]    Depending on where in the system a leak may occur, the CO 2  may be released to the outside atmosphere or to the inside of the container box. If released to the inside of the container box, the carbon dioxide concentration may create a potentially hazardous atmosphere to humans that may enter the container box. While the toxicity of CO 2  is not likely to be a problem, the corresponding reduction in available oxygen may be harmful to one entering the container box. In this regard, OSHA has indicated that the lowest acceptable oxygen concentration for shift-long exposure is 19.5%, which corresponds to a carbon dioxide concentration of about 60,000 ppm (6%). 
         [0006]    The use of carbon dioxide sensors within a refrigerant container has been made, but for a different purpose and manner. That is, in so called “controlled atmosphere” refrigerated container systems, the concentration of nitrogen within the container is enhanced so as to thereby decrease the oxidization (i.e. ripening) that may occur during shipping and storage. Such a system is described in U.S. Pat. No. 5,457,963. In such a system, there are certain types of cargo (e.g. asparagus, blueberry, blackberry, cantaloupe, fresh chili pepper) where the depletion of CO 2  within the container is detrimental to the cargo. Thus, a known technique is to sense when the percentage of CO 2  reaches a predetermined lower level and then responsively injecting CO 2  into the container from a pressurized vessel that is provided for that purpose. 
         [0007]    What is needed is a method and apparatus for determining when the content of CO 2  has reached an undesirable higher level and providing notice thereof so that an operator does not enter the container under those conditions. 
       DISCLOSURE OF THE INVENTION 
       [0008]    In accordance with one aspect of the invention, a CO 2  sensor is provided in a refrigerated container for the purpose of determining when the CO 2  concentration reaches a predetermined high threshold. An indication of this condition is then provided in a display so that an operator will be aware of the condition. 
         [0009]    In the drawings as hereinafter described, one embodiment is depicted; however, various other modifications and alternate constructions can be made thereto without departing from the spirit and scope of the invention. 
     
    
     
       BRIEF DESCRIPTION OF THE DRAWINGS 
         [0010]      FIG. 1  is a schematic illustration of a container refrigeration system in accordance with the prior art. 
           [0011]      FIG. 2  is a schematic illustration of a refrigerated container in accordance with the present invention. 
           [0012]      FIG. 3  is a graphic illustration of CO 2  concentration as a function of container load status. 
           [0013]      FIG. 4  is a schematic illustration of a control and display portion thereof. 
           [0014]      FIG. 5  is a flow diagram of the sensing and display process in accordance with the present invention. 
       
    
    
     DETAILED DESCRIPTION OF THE INVENTION 
       [0015]    A typical refrigerant vapor compression system using CO 2  as a refrigerant is shown generally at  10  in  FIG. 1  to include a compressor  11 , a heat rejecting heat exchanger  12 , an expansion device  13 , and a heat absorbing heat exchanger  14 , all connected in serial flow relationship in a closed loop refrigeration cycle. The vapor compression system  10  may also include a filter/drier  16  and a flash tank receiver  17  connected in serial flow relationship between the heat rejecting heat exchanger  12  and the expansion device  13 . 
         [0016]    The compressor  11  functions to compress and circulate the CO 2  refrigerant through the refrigerant circuit, and may be a single multi-stage compressor having at least a first lower pressure compression stage and a second higher pressure compression stage, such as for example, a scroll compressor or a reciprocating compressor. It may also comprise a pair of compressors such as, for example, a pair of reciprocating or scroll compressors having a refrigerant line connecting the discharge outlet to the first compressor in refrigerant flow relationship with the suction inlet port of the second compressor. In the case of the single multi-stage compressor, each compressor stage would be driven by a single motor operatively connected to drive both stages, and in the case of a pair of compressors, each compressor would be driven independently by its own dedicated motor. 
         [0017]    The refrigerant vapor compression system  10  is designed to operate in a subcritical cycle. Thus, the refrigerant heat rejecting heat exchanger  12  is designed to operate as a refrigerant condensing heat exchanger through which hot, high pressure CO 2  vapor discharge from the compressor  11  passes in heat exchange relationship with a cooling medium to condense the refrigerant passing therethrough from a refrigerant vapor to refrigerant liquid. The refrigerant condensing heat exchanger  12 , which may also be referred to herein as a condenser, may comprise a finned tube heat exchanger, such as, for example, a fin and round tube heat exchanger coil or a fin and flat minichannel tube heat exchanger. In transport refrigeration system applications, the typical cool medium is ambient air passed through the condenser  12  in heat exchange relationship with the refrigerant by means of a fan  18  operatively associated with the condenser  12 . 
         [0018]    The heat absorbing heat exchanger  14  may be referred to as an evaporator and may be a conventional finned tube heat exchanger such as, for example, a fin and round tube heat coil or a fin and minichannel flat tube heat exchanger through which expanded refrigerant having transversed the expansion device  13  passes in heat exchange relationship with the heated fluid, whereby the refrigerant is vaporized and typically superheated. The heating fluid passed in heat exchange relationship with the refrigerant in the evaporator  14  may be air passed through the evaporator  14  by means of a fan  19  operatively associated with the evaporator  14 , to be cooled and commonly also dehumidified and then supplied to the climate controlled environment  21  containing a perishable cargo such as, for example, refrigerated or frozen food items. 
         [0019]    The flash tank receiver  17  typically operates with both liquid refrigerant and vapor refrigerant disposed therein. That is, a liquid refrigerant from the condenser  12  enters the flash tank receiver  17  and settles to the bottom of the tank. Since liquid will be at saturated temperature, refrigerant vapor will fill the space in the tank not filled by liquid refrigerant. Liquid refrigerant is metered out of the tank  17  by the expansion device  13  which controls refrigerant flow to the evaporator  14 . As operating conditions of the subcritical refrigerant vapor compression system change, the charge requirements for the system will change and the liquid level in the receiver tank will rise or fall as appropriate to establish a new equilibrium liquid level. 
         [0020]    Referring now to  FIG. 2 , there is shown a cargo container  22  which is designed to contain cargo  23  that is stored in the climate controlled environment  21  for the purpose of maintaining the cargo  23  in a fresh and refrigerated conditioned. For that purpose, a refrigeration system  24  containing the vapor compression system  10 , is operatively connected to one end of the cargo container  22  as shown. Thus, as indicated by the arrows, the air in the climate controlled environment  21  passes into the refrigeration system  24  and is passed, by way of the fan  19 , through the evaporator  14  where it is cooled, after which it passes through the passage  26  back into the lower portion of the cargo container  22  and upwardly through the cargo  23  to complete the cycle. 
         [0021]    Considering now that the vapor compression system  10  as shown in  FIG. 1  contains CO 2  vapor in that portion of the circuit between the expansion device  13  and the condenser  12 , with the vapor being at relatively high pressures up to 2250 psi (15.5 MPa), the possibility of leakage from that portion of the circuit must be recognized. Depending on where that leakage occurs, the CO 2  vapor may be released to the atmosphere, as would occur if it flowed from the left side of the refrigeration system  24  in  FIG. 2 , or to the climate controlled environment  21 , if it were to flow to the right side of the refrigeration system  24 . If it flows to the atmosphere, the adverse effects are minimal except for possible need to replenish the lost refrigerant. However, if the flow of CO 2  vapor is into the climate controlled environment  21  it may create an unsafe condition for the entry of a person within the container  22  since infusion of the CO 2  will necessarily deplete the associated concentration of oxygen in the space. This is particularly true as the amount of cargo in the space is increased. 
         [0022]    Referring now to  FIG. 3 , there is shown a graphical representation of the relationship between the percentage of a full load (i.e. a filled container) and the percentage of concentration of CO 2  in the container. That is, if a leakage of a certain amount of CO 2  vapor enters the cargo container  22  in an empty condition, it will have the full volume of the container into which it will be dissipated, and the overall effect will be substantially less then when a load is included in the cargo container  22 . On the other hand, when there is a substantial load of cargo  23  in the cargo container  22 , as shown in  FIG. 2 , then the amount of space into which the leaked CO 2  may be dissipated is substantially reduced, and therefore the effect is substantially greater. The data in  FIG. 3  therefore shows that the level of carbon dioxide concentration will vary from less than 4% if the container box is empty to over 40% carbon dioxide concentration if the container box is fully loaded. 
         [0023]    Referring again to  FIG. 2 , it will be seen that, in accordance with the present invention, a CO 2  sensor  27  is installed within the refrigeration system  24  at a point where the return air from the cargo container  22  enters the refrigeration system  24 . Sensor  27  is in a position to sample the air returning from the cargo container  22  to determine the concentration of CO 2  therein. 
         [0024]    The sensor  27  may be of a conventional type such as, for example, an infrared analyzer which is available from Texas Instruments. The manner in which the sensor  27  is electronically connected to related components is shown in  FIG. 4 . 
         [0025]    The sensor  27  generates an analog signal representative of the concentration of CO 2  in the container  22 . That analog signal is sent along line  28  to an analog-to-digital converter  29  with the representative digital signal being sent along line  30  to a controller  31 . The controller  31  then sends a signal along line  32  to a display console  33  which, in turn, sends a signal along line  34  to generate a representative visual display at  35  so as to thereby alert an outside person of a potential hazardous atmosphere inside the container  22 . 
         [0026]    Shown in  FIG. 5  is a logic flow diagram to indicate the manner in which the controller  32  operates to provide an appropriate display at the display console  33 . In block  30 , the controller  32  reads the CO 2  sensor  27  every second while the unit is under power. A representative signal is then sent to a comparator  36  and compared with a predetermined threshold, such as 3%, for example. So long as the CO 2  concentration is indicated as being below a predetermined level, as indicated by the block  40 , a signal is sent to the display console  33  and an appropriate indicator  37  is visually displayed at  35  to show that the condition in the cargo container  22  is “all clear” for entry of a person therein. However, when the controller  32  indicates that the level of CO 2  concentration in the cargo container  22  is above a predetermined level, such as three percent, for example, as indicated at block  38 , then a signal will be sent to the display console  33  and an appropriate “High CO 2 ” visual display will be shown at  35  to indicate to an operator that a hazardous condition exists within the cargo container  22  and that it should not be entered until appropriate action has been taken, such as, for example, the cargo container  22  is vented by opening the doors and allowing for the escape of CO 2  gases that are trapped therein. 
         [0027]    As part of the operating protocol, an operator will be instructed by appropriate notices posted on the unit, by operating manuals, and possibly by appropriate instructions provided on the display console  33 , that, in order to avoid a hazardous condition, the operator should check the display console to ensure that the hazardous condition does not exist at the time. 
         [0028]    Although the present invention has been particularly shown and described with reference to one embodiment as illustrated by the drawings, it will be understood by one skilled in the art that various changes in detail may be made thereto without departing from the spirit and scope of the invention as defined by the claims.

Technology Category: g