1. Field of the Invention
The present invention relates to refrigeration systems and, more particularly, to methods for reducing the total charge of refrigerant in a refrigeration system.
2. Description of the Related Art
Refrigeration systems for refrigeration, air conditioning and other cooling applications typically include a fluid circuit that operably connects the components of the system and through which the refrigerant flows through the system. The fluid circuit is typically constructed of a set of tubes connecting the components. At any given time, a substantial amount of the refrigerant flowing through the system is contained within these tubes. In some systems, the refrigerant is a combustible hydrocarbon fluid, such as propane. Unfortunately, hydrocarbon refrigerants have a low Flammability Limit. The Flammability Limit refers to the concentration level that may be sufficient to trigger an explosion in the presence of oxygen and a flame or spark. It is desirable to minimize the total change or volume of refrigerant in the system to thereby reduce the likelihood that the concentration of hydrocarbon refrigerant in the ambient air will exceed the Flammability Limit in the event of a leak. This may be particularly desirable in compact refrigeration systems wherein the volume of ambient air is minimized due to circumstances, such as ventilation and elevation of the system from floor/support surface. Therefore, a need remains for a system having a reduced refrigerant charge without reducing the performance and capacity of the system.
The present invention provides a system and method for reducing the charge of refrigerant in refrigeration system. In one form, in a given design of a refrigeration system, the present invention provides a method for reducing the charge of the refrigerant flowing through the refrigeration system. The refrigeration system includes a fluid conduit through which a flammable refrigerant circulates. The fluid conduit couples, in serial order, a compressor, a first heat exchanger, an expansion device, and a second heat exchanger. The conduit defines an interior diameter, an interior surface, and a given friction factor range. The method includes the steps of reducing the interior diameter of the conduit to thereby reduce the system design refrigerant charge, and coating the interior surface of the reduced diameter conduit with a coating composition to thereby reduce the surface roughness of the interior surface and provide a friction factor for the reduced diameter conduit that is substantially within the given friction factor range.
In a given design of a refrigeration system the present invention provides another method for reducing the charge of the refrigerant flowing through the refrigeration system. The refrigeration system comprises a fluid conduit through which a combustible refrigerant circulates, the fluid conduit coupling, in serial order, a compressor, a first heat exchanger, an expansion device, and a second heat exchanger. The conduit defines an interior diameter and an interior surface. The flow of refrigerant in the conduit has a given Reynolds number range. The method includes the steps of reducing the interior diameter of the conduit to thereby reduce the system design refrigerant charge, and coating the interior surface of the reduced diameter conduit with a coating composition to thereby reduce the surface roughness of the interior surface and provide a Reynolds number for the flow of refrigerant in the reduced diameter conduit that is substantially within the given Reynolds number range.
In still another form, the present invention provides a vapor compression system for use with a refrigerant. The system includes a fluid circuit coupling, in serial order, a compressor, a first heat exchanger, an expansion device, and a second heat exchanger. The fluid circuit comprises a refrigerant conduit through which the refrigerant flows. The flow of refrigerant defines a Reynolds number (Re) of greater than 2000. The fluid circuit defines an interior surface coated with a composition, which provides the interior surface with a wall roughness of less than about 0.0001 ft.
The above-mentioned and other features and objects of this invention, and the manner of attaining them, will become more apparent and the invention itself will be better understood by reference to the following description of embodiments of the invention taken in conjunction with the accompanying drawings, wherein:
The embodiments hereinafter disclosed are not intended to be exhaustive or limit the invention to the precise forms disclosed in the following description. Rather the embodiments are chosen and described so that others skilled in the art may utilize its teachings.
Referring first to
Compressor 14 may be any known compressor suitable for compressing a refrigerant fluid, such as a combustible hydrocarbon. Such suitable compressors may include single or multi-stage compressors having one or more rotary vane mechanisms, reciprocating piston mechanisms, orbiting scroll mechanisms, centrifugal mechanisms and/or other conventional compressor mechanisms. First and second heat exchangers 16, 20 may be of any conventional condenser/evaporator design. Accumulator 22, expansion device 18 and suction line heat exchanger 24 may also be of conventional types.
In general operation, the refrigerant circulates through system 10 via conduit 12 in the direction of the arrows shown in
Fluid circuit 12 is constructed of a fluid conduit or tube. In conventional refrigeration systems the fluid conduit typically has a diameter of up to about 0.500 inches (1.275 cm). In such systems the percentage of refrigerant residing in the fluid conduit is typically between 18% and 29% of the total refrigerant in the system (not including the refrigerant in the compressor). For example, Table 1 shows how the refrigerant charge is distributed among components of a particular compact refrigeration system. This particular system has a microchannel type condenser and evaporator. The compressor is a reciprocating compressor, which has low pressure refrigerant gas in the housing and is lubricated with mineral oil.
As illustrated in Table I, the fluid conduit including the discharge line, the liquid line and the suction line, of a refrigeration system may hold over 18% of the total refrigerant (not including the refrigerant in the compressor) at any given time.
In another example, the total refrigerant charge in the system has been reduced by plugging every other microchannel in the heat exchanger, thereby reducing the amount of refrigerant in the heat exchanger. Table II shows the distribution of refrigerant among the components of such a system. By reducing the refrigerant charge in the heat exchanger, the percentage of refrigerant residing in connecting lines is increased from 18% to 29%.
These figures demonstrate that, at any given time, a substantial amount of refrigerant charge may reside in the fluid conduit.
Referring now to
However, the reduction of the diameter of conduit 12 is not a simple means for reducing the total refrigerant charge of the system. A reduction in the diameter of conduit 12 results in an increase in pressure loss or head loss (hL) due to friction. The head loss (hL) due to a flow of refrigerant through a segment of a pipe or conduit, such as conduit 12, may be calculated using the well-known Darcy-Weisbach formula below.
In the Darcy-Weisbach equation, “hL” equals head loss; “f” equals the friction factor; “L” equals the length of the conduit; “V” equals average fluid velocity; “D” equals the diameter of the conduit; and “g” equals the acceleration of gravity. As is demonstrated by the Darcy-Weisbach equation, head loss increases directly as the diameter decreases. This result is exacerbated by the friction factor, which also increases as the diameter decreases. The friction factor (f) is a function of the velocity, density and viscosity of the fluid, as well as the diameter and internal roughness of the conduit. The Darcy-Weisbach friction factor, “f”, may be calculated using the equation below.
In this equation, “F” represents a functional relationship that can be developed; “Re” equals the Reynolds number; “ε” equals the index of the internal conduit roughness; and “D” equals the conduit diameter. The Darcy-Weisbach friction factor equation demonstrates that the friction factor is increased when the diameter is decreased. An increase in the friction factor results in a further increase in heat loss.
The Reynolds number is an expression of the fluid velocity, density, viscosity and conduit size. The Reynolds number equation is found below.
In the Reynolds number equation “Q” equals the conduit line flow rate; “ν” equals the viscosity of the fluid; and “D” equals the diameter of the conduit. This equation illustrates that the Reynolds number also increases with a decrease in diameter. An increased Reynolds number yields an increased friction factor which, in turn, further increases the head loss.
As is demonstrated by these equations, a decrease in the diameter of the conduit directly increases the head loss in the Darcy-Weisbach equation and further increases the head loss through the friction factor and Reynolds number in the Darcy-Weisbach equation. An increase in head loss may reduce the efficiency and efficacy of the refrigeration system. Consequently, simply reducing the diameter of conduit 12 is not an efficient, effective means for reducing the total refrigerant charge of the system 10.
To compensate, at least in part, for the effect the reduction in diameter has on the head loss, the conduit 12 of the present system also has a reduced interior surface roughness. Conventional conduits typically are constructed of steel and/or copper and have an interior surface of about 0.003 ft. Referring to
The present invention reduces the total charge of refrigerant by reducing the volume of the conduit, while minimizing head loss due to the reduction in diameter by reducing the surface roughness. As a result, the present invention reduces the total charge of refrigerant in the system, thereby minimizing the risks associated with flammable refrigerants. The reduced total refrigerant charge permits the system to be used in smaller areas with reduced ambient circumstances such as ventilation, elevation from the floor, and ambient air/space surrounding the system.
While this invention has been described as having an exemplary design, the present invention may be further modified within the spirit and scope of this disclosure. This application is therefore intended to cover any variations, uses, or adaptations of the invention using its general principles. Further, this application is intended to cover such departures from the present disclosure as come within known or customary practice in the art to which this invention pertains.