US20060042274A1 - Refrigeration system and a method for reducing the charge of refrigerant there in - Google Patents
Refrigeration system and a method for reducing the charge of refrigerant there in Download PDFInfo
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- US20060042274A1 US20060042274A1 US10/928,228 US92822804A US2006042274A1 US 20060042274 A1 US20060042274 A1 US 20060042274A1 US 92822804 A US92822804 A US 92822804A US 2006042274 A1 US2006042274 A1 US 2006042274A1
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- 239000003507 refrigerant Substances 0.000 title claims abstract 21
- 238000005057 refrigeration Methods 0.000 title claims abstract 10
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- 239000012530 fluid Substances 0.000 claims abstract 10
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- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical group N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 claims 4
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Images
Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F16—ENGINEERING ELEMENTS AND UNITS; GENERAL MEASURES FOR PRODUCING AND MAINTAINING EFFECTIVE FUNCTIONING OF MACHINES OR INSTALLATIONS; THERMAL INSULATION IN GENERAL
- F16L—PIPES; JOINTS OR FITTINGS FOR PIPES; SUPPORTS FOR PIPES, CABLES OR PROTECTIVE TUBING; MEANS FOR THERMAL INSULATION IN GENERAL
- F16L9/00—Rigid pipes
- F16L9/14—Compound tubes, i.e. made of materials not wholly covered by any one of the preceding groups
- F16L9/147—Compound tubes, i.e. made of materials not wholly covered by any one of the preceding groups comprising only layers of metal and plastics with or without reinforcement
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B41/00—Fluid-circulation arrangements
- F25B41/40—Fluid line arrangements
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F13/00—Arrangements for modifying heat-transfer, e.g. increasing, decreasing
- F28F13/18—Arrangements for modifying heat-transfer, e.g. increasing, decreasing by applying coatings, e.g. radiation-absorbing, radiation-reflecting; by surface treatment, e.g. polishing
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2400/00—General features or devices for refrigeration machines, plants or systems, combined heating and refrigeration systems or heat-pump systems, i.e. not limited to a particular subgroup of F25B
- F25B2400/12—Inflammable refrigerants
Definitions
- the present invention relates to refrigeration systems and, more particularly, to methods for reducing the total charge of refrigerant in a refrigeration system.
- 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.
- the refrigerant is a combustible hydrocarbon fluid, such as propane.
- 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.
- the present invention provides a system and method for reducing the charge of refrigerant in 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.
- 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.
- 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.
- FIG. 1 is a schematic illustration of a refrigeration system in accordance with one embodiment of the present invention
- FIG. 2 is a perspective view of a section of a fluid conduit of a refrigeration system in accordance with one embodiment of the present invention.
- FIG. 3 is a cross section of the conduit of FIG. 2 taken along lines 3 - 3 .
- refrigeration system 10 of the present invention includes fluid circuit 12 through which a refrigerant circulates.
- the refrigerant may be any conventional refrigerant used in refrigeration systems, including flammable refrigerants, such as propane and ammonia.
- Fluid circuit 12 operably couples, in serial order, compressor 14 , first heat exchanger or condenser 16 , expansion device 18 and second heat exchanger or evaporator 20 .
- refrigeration system 10 may also include accumulator 22 coupled to fluid circuit 12 between evaporator 20 and compressor 14 .
- Suction line heat exchanger 24 may also be operably coupled to fluid circuit 12 .
- Suction line heat exchanger 24 includes first and second portions 24 a and 24 b , which are in a heat exchange relationship with one another.
- First portion 24 a is operably coupled to fluid circuit 12 between first heat exchanger 16 and expansion device 18 .
- Second portion 24 b is operably coupled to fluid circuit 12 between accumulator 22 and compressor 14 .
- Applications of such refrigeration systems include refrigeration, air conditioning, chillers and other cooling applications.
- 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.
- the refrigerant circulates through system 10 via conduit 12 in the direction of the arrows shown in FIG. 1 . More specifically, the refrigerant is drawn by suction pressure into compressor 14 where it is compressed to a relatively high discharge pressure. The resulting high pressure refrigerant is discharged from compressor 14 and flows via conduit 12 to condenser 16 wherein thermal energy is removed from the refrigerant, thereby condensing the refrigerant. The condensed refrigerant then flows through conduit 12 to first portion 24 a of suction line heat exchanger 24 , wherein thermal energy is transferred from the refrigerant in first portion 24 a to the refrigerant in second portion 24 b .
- the refrigerant then flows from first portion 24 a of suction line heat exchanger 22 to expansion device 18 , which reduces the pressure of the refrigerant and meters the refrigerant to evaporator 20 .
- thermal energy is transferred from the medium being cooled to the refrigerant flowing in evaporator 20 , thereby cooling the ambient air and evaporating the refrigerant.
- the refrigerant then flows from evaporator 20 through circuit 12 to accumulator 22 .
- Accumulator 22 collects and stores any liquid refrigerant remaining in the refrigerant exiting evaporator 20 and releases the refrigerant at a controlled rate to compressor 14 .
- the vapor refrigerant exiting evaporator 20 flows through accumulator 22 and is discharged into fluid circuit 12 .
- the refrigerant flows, via fluid circuit 12 , to second portion 24 b of suction line heat exchanger 22 .
- second portion 24 b the refrigerant receives thermal energy from the refrigerant flowing through first portion 24 a , thereby warming the refrigerant in second portion 24 b .
- the warmed refrigerant then flows via conduit 12 to compressor 14 and the cycle is repeated.
- Fluid circuit 12 is constructed of a fluid conduit or tube.
- the fluid conduit typically has a diameter of up to about 0.500 inches (1.275 cm).
- 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).
- 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.
- 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.
- 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.
- the conduit 12 of the refrigeration system of the present invention has a reduced diameter “D” relative to the diameter of conduits in conventional systems. More specifically, diameter D is preferably reduced to between 0.375 inches (0.9525 cm) and 0.0625 inches (0.15875 cm). As a result, the volume of the conduit is reduced and the total charge of refrigerant in the system is thereby reduced. In addition, the amount of space occupied by conduit 12 is reduced as a result of the reduced diameter conduit, thereby enabling the production of a more compact system.
- 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 (h L ) due to friction.
- F represents a functional relationship that can be developed; “Re” equals the Reynolds number; “ ⁇ ” equals the index of the internal conduit roughness; and “D” equals the conduit diameter.
- Re equals the Reynolds number; “ ⁇ ” 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.
- 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.
- conduit 12 has an interior surface 26 , which is coated with a coating 28 .
- Coating 28 provides conduit 12 with a reduced surface roughness of less than 0.0001 ft., and preferably between about 5 ⁇ 10 ⁇ 5 ft. (1.524 ⁇ 10 ⁇ 3 cm) 4 ⁇ 10 ⁇ 6 ft. (1.219 ⁇ 10 ⁇ 4 cm).
- Coating 28 preferably has a thickness of less than 0.200 inches (0.508 cm).
- Coating 28 may be any composition capable of reducing the interior surface roughness of conduit 12 and capable of withstanding the temperatures and chemical properties of the refrigerant.
- Such compositions may include one or more of the following compounds: PVC(polyvinylchloride); two component epoxy COPON EP2306H.F.; polyester reinforced polyethylene; polyvinylchlor polyethylene; polypropylene; polybutylene; aluminous cement mortar; polyurethane-acrylic blends; silicone rubber; poly(di-methyl siloxane); molybdenum disulphide; teflon and teflon mixtures (e.g.
- Coating 28 may also thermally insulate conduit 12 , thereby minimizing heat transfer in conduit 12 .
- the reduction of interior surface roughness compensates for the reduction in diameter such that the Reynolds number and flow are not significantly affected.
- the Reynolds number preferably remains between 2300 and 50000.
- 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.
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Abstract
Description
- 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:
-
FIG. 1 is a schematic illustration of a refrigeration system in accordance with one embodiment of the present invention; -
FIG. 2 is a perspective view of a section of a fluid conduit of a refrigeration system in accordance with one embodiment of the present invention; and -
FIG. 3 is a cross section of the conduit ofFIG. 2 taken along lines 3-3. - 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
FIG. 1 , refrigeration system 10 of the present invention includesfluid circuit 12 through which a refrigerant circulates. The refrigerant may be any conventional refrigerant used in refrigeration systems, including flammable refrigerants, such as propane and ammonia.Fluid circuit 12 operably couples, in serial order,compressor 14, first heat exchanger orcondenser 16,expansion device 18 and second heat exchanger orevaporator 20. As illustrated inFIG. 1 , refrigeration system 10 may also includeaccumulator 22 coupled tofluid circuit 12 betweenevaporator 20 andcompressor 14. Suctionline heat exchanger 24 may also be operably coupled tofluid circuit 12. Suctionline heat exchanger 24 includes first andsecond portions First portion 24 a is operably coupled tofluid circuit 12 betweenfirst heat exchanger 16 andexpansion device 18.Second portion 24 b is operably coupled tofluid circuit 12 betweenaccumulator 22 andcompressor 14. Applications of such refrigeration systems include refrigeration, air conditioning, chillers and other cooling applications. -
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 andsecond heat exchangers Accumulator 22,expansion device 18 and suctionline 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 inFIG. 1 . More specifically, the refrigerant is drawn by suction pressure intocompressor 14 where it is compressed to a relatively high discharge pressure. The resulting high pressure refrigerant is discharged fromcompressor 14 and flows viaconduit 12 to condenser 16 wherein thermal energy is removed from the refrigerant, thereby condensing the refrigerant. The condensed refrigerant then flows throughconduit 12 tofirst portion 24 a of suctionline heat exchanger 24, wherein thermal energy is transferred from the refrigerant infirst portion 24 a to the refrigerant insecond portion 24 b. The refrigerant then flows fromfirst portion 24 a of suctionline heat exchanger 22 toexpansion device 18, which reduces the pressure of the refrigerant and meters the refrigerant toevaporator 20. Inevaporator 20 thermal energy is transferred from the medium being cooled to the refrigerant flowing inevaporator 20, thereby cooling the ambient air and evaporating the refrigerant. The refrigerant then flows fromevaporator 20 throughcircuit 12 toaccumulator 22. Accumulator 22 collects and stores any liquid refrigerant remaining in therefrigerant exiting evaporator 20 and releases the refrigerant at a controlled rate tocompressor 14. The vaporrefrigerant exiting evaporator 20 flows throughaccumulator 22 and is discharged intofluid circuit 12. Fromaccumulator 22, the refrigerant flows, viafluid circuit 12, tosecond portion 24 b of suctionline heat exchanger 22. Insecond portion 24 b the refrigerant receives thermal energy from the refrigerant flowing throughfirst portion 24 a, thereby warming the refrigerant insecond portion 24 b. The warmed refrigerant then flows viaconduit 12 tocompressor 14 and the cycle is repeated. -
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.TABLE I Refrigerant Component Charge, grams Dis Line 0.292 Cond sup head 0.602 Cond Superheat 0.210 Cond 2ph 5.678 Cond 2ph head 0.939 Cond Subcooled 2.615 Cond sub head 0.939 Liq Line 4.002 Evap 2ph head 0.245 Evaporator 8.277 Evap sup head 0.031 Suction Line 0.129 Charge in compressor 30.000 Total out of compressor 23.960 Total in lines 4.423 Total in lines, % 18.460 - 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%.
TABLE II Dis Line 0.28816 Cond sup head 0.59306 Cond Superheat 0.10841 Cond 2ph 3.04814 Cond 2ph head 0.98704 Cond Subcooled 0.00288 Cond sub head 0.98704 Liq Line 4.01242 Evap 2ph head 0.12291 Evaporator 4.82839 Evap sup head 0.01626 Suction Line 0.12650 Charge in oil (g) 30.00000 Total out of compressor 15.12119 Total in lines 4.42707 Total lines, % 29.27729 - These figures demonstrate that, at any given time, a substantial amount of refrigerant charge may reside in the fluid conduit.
- Referring now to
FIGS. 2 and 3 , to reduce the total charge of refrigerant in system 10, theconduit 12 of the refrigeration system of the present invention has a reduced diameter “D” relative to the diameter of conduits in conventional systems. More specifically, diameter D is preferably reduced to between 0.375 inches (0.9525 cm) and 0.0625 inches (0.15875 cm). As a result, the volume of the conduit is reduced and the total charge of refrigerant in the system is thereby reduced. In addition, the amount of space occupied byconduit 12 is reduced as a result of the reduced diameter conduit, thereby enabling the production of a more compact system. - 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 ofconduit 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 asconduit 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 toFIGS. 2 and 3 ,conduit 12 has aninterior surface 26, which is coated with acoating 28.Coating 28 providesconduit 12 with a reduced surface roughness of less than 0.0001 ft., and preferably between about 5×10−5 ft. (1.524×10−3 cm) 4×10−6 ft. (1.219×10−4 cm).Coating 28 preferably has a thickness of less than 0.200 inches (0.508 cm).Coating 28 may be any composition capable of reducing the interior surface roughness ofconduit 12 and capable of withstanding the temperatures and chemical properties of the refrigerant. Such compositions may include one or more of the following compounds: PVC(polyvinylchloride); two component epoxy COPON EP2306H.F.; polyester reinforced polyethylene; polyvinylchlor polyethylene; polypropylene; polybutylene; aluminous cement mortar; polyurethane-acrylic blends; silicone rubber; poly(di-methyl siloxane); molybdenum disulphide; teflon and teflon mixtures (e.g. HiFlon); graphite; ANL-NFC (Argonne Laboratory developed amorphous carbon coating); ceramic/polymer mixtures (e.g. Series 100 Infused Matrix Endura coating); octadecyltrichlorosilane; 1H,1H,2H,2H-perflourodecyltrichlorosilane; unsaturated hydrosable resin (e.g. Fluiglide); poly(vinylpyrrolidone); polyester acrylic co-polymer (e.g. Polyglass HA); vinyl ester/acrylic copolymer (e.g. Polyglass VE); bisphenol ‘A’ polyester resin; polyester/polyurethane polymer alloy (e.g. HN4); polyurethane resin; and carbon based PVD coatings (e.g. Genocoa).Coating 28 may also thermally insulateconduit 12, thereby minimizing heat transfer inconduit 12. The reduction of interior surface roughness compensates for the reduction in diameter such that the Reynolds number and flow are not significantly affected. The Reynolds number preferably remains between 2300 and 50000. - 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.
Claims (30)
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
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US10/928,228 US20060042274A1 (en) | 2004-08-27 | 2004-08-27 | Refrigeration system and a method for reducing the charge of refrigerant there in |
CA002516746A CA2516746A1 (en) | 2004-08-27 | 2005-08-19 | A refrigeration system and a method for reducing the charge of refrigerant therein |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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US10/928,228 US20060042274A1 (en) | 2004-08-27 | 2004-08-27 | Refrigeration system and a method for reducing the charge of refrigerant there in |
Publications (1)
Publication Number | Publication Date |
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US20060042274A1 true US20060042274A1 (en) | 2006-03-02 |
Family
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Family Applications (1)
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US10/928,228 Abandoned US20060042274A1 (en) | 2004-08-27 | 2004-08-27 | Refrigeration system and a method for reducing the charge of refrigerant there in |
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US (1) | US20060042274A1 (en) |
CA (1) | CA2516746A1 (en) |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
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US7958738B2 (en) * | 2008-06-06 | 2011-06-14 | Colmac Coil Mfg., Inc. | Direct expansion ammonia refrigeration system and a method of direct expansion ammonia refrigeration |
US8291719B2 (en) * | 2007-10-09 | 2012-10-23 | Be Aerospace, Inc. | Thermal control system and method |
US20130145780A1 (en) * | 2011-06-17 | 2013-06-13 | Ice Energy, Inc. | System and method for liquid-suction heat exchange thermal energy storage |
WO2013106725A1 (en) * | 2012-01-13 | 2013-07-18 | Manitowoc Foodservice Companies, Llc | Low refrigerant volume condenser for hydrocarbon refrigerant and ice making machine using same |
US20140027100A1 (en) * | 2011-04-03 | 2014-01-30 | Nec Corporation | Piping structure of cooling device, method for making the same, and method for connecting pipes |
JP2015055455A (en) * | 2013-09-13 | 2015-03-23 | 三菱電機株式会社 | Outdoor unit and air conditioner |
WO2015151238A1 (en) * | 2014-04-02 | 2015-10-08 | 三菱電機株式会社 | Air-conditioning device and installation method thereof |
US9303925B2 (en) | 2012-02-17 | 2016-04-05 | Hussmann Corporation | Microchannel suction line heat exchanger |
US11506431B2 (en) * | 2018-05-17 | 2022-11-22 | Mitsubishi Electric Corporation | Refrigeration cycle apparatus |
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Cited By (15)
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US8291719B2 (en) * | 2007-10-09 | 2012-10-23 | Be Aerospace, Inc. | Thermal control system and method |
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US7958738B2 (en) * | 2008-06-06 | 2011-06-14 | Colmac Coil Mfg., Inc. | Direct expansion ammonia refrigeration system and a method of direct expansion ammonia refrigeration |
US8474276B2 (en) | 2008-06-06 | 2013-07-02 | Colmac Coil Mfg., Inc. | Direct expansion ammonia refrigeration system and a method of direct expansion ammonia refrigeration |
US20140027100A1 (en) * | 2011-04-03 | 2014-01-30 | Nec Corporation | Piping structure of cooling device, method for making the same, and method for connecting pipes |
US20130145780A1 (en) * | 2011-06-17 | 2013-06-13 | Ice Energy, Inc. | System and method for liquid-suction heat exchange thermal energy storage |
US9212834B2 (en) * | 2011-06-17 | 2015-12-15 | Greener-Ice Spv, L.L.C. | System and method for liquid-suction heat exchange thermal energy storage |
WO2013106725A1 (en) * | 2012-01-13 | 2013-07-18 | Manitowoc Foodservice Companies, Llc | Low refrigerant volume condenser for hydrocarbon refrigerant and ice making machine using same |
US9052130B2 (en) | 2012-01-13 | 2015-06-09 | Manitowoc Foodservice Companies, Llc | Low refrigerant volume condenser for hydrocarbon refrigerant and ice making machine using same |
US9303925B2 (en) | 2012-02-17 | 2016-04-05 | Hussmann Corporation | Microchannel suction line heat exchanger |
US10514189B2 (en) | 2012-02-17 | 2019-12-24 | Hussmann Corporation | Microchannel suction line heat exchanger |
JP2015055455A (en) * | 2013-09-13 | 2015-03-23 | 三菱電機株式会社 | Outdoor unit and air conditioner |
WO2015151238A1 (en) * | 2014-04-02 | 2015-10-08 | 三菱電機株式会社 | Air-conditioning device and installation method thereof |
US11506431B2 (en) * | 2018-05-17 | 2022-11-22 | Mitsubishi Electric Corporation | Refrigeration cycle apparatus |
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