Refrigeration sub-cooler and air conditioning dehumidifier

Information

  • Patent Grant
  • 6338254
  • Patent Number
    6,338,254
  • Date Filed
    Friday, December 1, 2000
    24 years ago
  • Date Issued
    Tuesday, January 15, 2002
    22 years ago
Abstract
An efficient method and system for dehumidifying an environment and refrigerating a second environment with a closed loop refrigeration system consisting of compressing refrigerant with a refrigeration compressor (10) to a high temperature and pressure, condensing the high pressure refrigerant to a liquid at a high temperature, circulating high pressure refrigerant through a heat exchanger (60) which is used to transfer energy from the liquid to an environment which is being air conditioned at a higher efficiency which contains the refrigerated environment (200). The liquid is then evaporated to a gas at a low pressure in a refrigeration evaporator coil (220).
Description




BACKGROUND OF THE INVENTION




1. Field of the Invention




This invention pertains to a novel method of dehumidifying an environment, which includes a refrigeration system and an air conditioning system while reducing the operational cost.




2. Description of the Related Art




Prior art systems have used refrigeration systems condensers to reheat the environment. This approach utilizes the heat which would normally be rejected to the outside environment to heat the inside environment. The Hy-Dry system sold by DTE Energy utilizes the liquid line from an air conditioning system to heat the air after it has passed over the cooling coil and air conditioning system's liquid is sub-cooled in the process. This allows the unit to discharge air at a higher temperature causing a lower net ejected humidity. Although, in this situation dehumidification may or may not take place there is no change in the coefficient of performance of the over all system other than that which is due to enlarging the heat transfer surface. That is, the same effect could be generated by simply increasing the cooling coil surface. While other prior art systems have used desiccant wheels or they have operated the reheat, which in turn causes the air conditioning to turn on and remove the moisture. In the later cases the net result is at an added operational cost.




OBJECTIVES AND ADVANTAGES OF THE INVENTION




Table of Functions, Purposes, Objectives, Goals, Tasks
















OBJECTIVE




SOLUTION











REFRIGERATION LIQUID IS




PASS AIR FROM THE CONDI-






SUB-COOLED




TIONED ENVIRONMENT OVER







THE SUB-COOLING COIL OR PASS







A SECONDARY FLUID OVER THE







LIQUID AND THEN THROUGH THE







CONDITIONED ENVIRONMENTS







AND FURTHER SUB-COOL THE







LIQUID WITH A HEAT EX-







CHANGER ON THE AIR







CONDITIONER






LOWER ENERGY COST OF




SUB-COOL THE LIQUID WITH A






THE REFRIGERATION




COMPRESSOR OPERATING AT AIR






SYSTEM IS ACHIEVED BY




CONDITIONING EFFICIENCY THE






REMOVING PART OF THE




LATENT LOAD ON THE REFRIG-






ENERGY AT LESS COST




ERATION SYSTEM IS REDUCED







DUE TO THE LOWER HUMIDITY IN







THE REFRIGERATED







ENVIORNMENT






DEHUMIDIFICATION IS




BY HEATING CONDITIONED






ACHIEVED




ENVIRONMENT AIR WITH THE







WARM LIQUID AND CAUSING THE







AIR CONDITIONING COMPRESSOR







TO OPERATE






LOWER HUMIDITY IN THE




PASS AIR OVER THE A/C COIL






DISCHARGE AIR DUCT




FIRST AND THEN PASS THE AIR






WHICH RESULTS IN LESS




OVER THE SUB-COOLING HEAT






FAVORABLE ENVIRON-




FOR EXCHANGER






MENT FUNGUS GROWTH





















BRIEF DESCRIPTION OF THE DRAWING FIGURES





FIG. 1

is a schematic of a dehumidification sub-cooling system utilizing the current invention.





FIG. 2

is a schematic of a dehumidification sub-cooling system utilizing the current invention in which the refrigeration system has parallel piped evaporators.





FIG. 3

is a schematic of a dehumidification sub-cooling system utilizing the current invention utilizing an additional heat exchanger on the air conditioning system to further sub-cool the refrigeration liquid.





FIG. 4

is a schematic of a dehumidification sub-cooling system utilizing the current invention in which energy in refrigeration liquid is transferred to a secondary fluid prior to being discharged into the air conditioned space.





FIG. 5

is a schematic of a dehumidification sub-cooling system utilizing the current invention which includes piping for using conventional reheat.





FIG. 6

is a schematic of a conventional refrigeration system used for dehumidification.











SUMMARY OF THE INVENTION




The current invention is an efficient method for dehumidifying an environment and refrigerating a second environment with a closed loop refrigeration system consisting of compressing refrigerant with a refrigeration compressor to a high temperature and pressure, condensing the high pressure refrigerant to a liquid at a high temperature, circulating high pressure liquid refrigerant through a heat exchanger which is used to transfer energy from the liquid to an environment which is being air conditioned at a higher efficiency and which may contain the refrigerated environment. The liquid is then evaporated to a gas at a low pressure in a refrigeration evaporator coil.




Elements and Functions




Table of Element and Numbers and Figures


















#





ELEMENT DESCRIPTION




FIGURES


























10





REFRIGERATION COMPRESSOR




1,2,3,4,5,6






10




B




AIR CONDITIONING SYSTEM




1








COMPRESSOR






15





COMPRESSOR SUCTION




1,2,3,4,5,6






15




B




AIR CONDITIONING COMPRESSOR




1,2








SUCTION






20





COMPRESSOR DISCHARGE




1,2,3,4,5,6






20




B




AIR CONDITIONING COMPRESSOR




1








DISCHARGE






30





CONDENSER




1,2,3,4,5,6






30




B




AIR CONDITIONING SYSTEM CONDENSER




1






40





THREE WAY VALVE




5,6






60





REHEAT COIL




1,2,3,4,5,6






70





RECEIVER




1,2,3,4,5,6






70




B




AIR CONDITIONING SYSTEM RECEIVER




1






75





LIQUID REFRIGERANT




1,2,3,4,5,6






75




B




AIR CONDITIONING SYSTEM LIQUID




1








REFRIGERANT






80





CHECK VALVE




5






81





CHECK VALVE




5






105





REFRIGERATION CONDENSER FAN




1,2,3,4,5,6






105




B




CONDENSER FAN AIR CONDITIONING




1








SYSTEM






150





THREE WAY VALVE




5,6






180





LIQUID EVACUATION SOLENOID




5,6






200





REFRIGERATED AREA




1,2,3,4,5,6






200




B




AIR CONDITIONED SYSTEM AIR HANDLER




1,2,3,4,5,6






200




C




REFRIGERATED AREA C




1,2,3,4,5,6






220





EVAPORATOR




1,2,3,4,5,6






220




B




AIR CONDITIONING EVAPORATOR




1,2






220




C




PARALLEL PIPED EVAPORATOR C




2,3,4,5,6






225





EXPANSION VALVE




1,2,3,4,5,6






225




B




AIR CONDITIONING SYSTEM EXPANSION




1








VALVE






225




C




REFRIGERATION SECOND EVAPORATOR




2,3,4,5,6








EXPANSION VALVE






226





EVAPORATOR FAN FOR EVAPORATOR 220




1,2,3,4,5,6






226




B




AIR CONDITIONING EVAPORATOR FAN




1,2,3,4,5,6








FOR EVAPORATOR 220B






226




C




AIR CONDITIONING EVAPORATOR FAN




1,2,3,4,5,6








FOR EVAPORATOR 220C






302





303 AIR CONDITIONING SUCTION OUTLET




3






303





AIR CONDITIONING SUCTION -




3








REFRIGERATION LIQUID HEAT LIQUID








HEAT EXCHANGER






304





303 AIR CONDITIONING SUCTION INLET




3






306





AIR CONDITIONING LIQUID LINE




1,2,3,4,5,6






310





AIR FLOW




1,2,3,4,5,6






500





SECONDARY FLUID CIRCULATING PUMP




4






502





SECONDARY FLUID HEAT EXCHANGER




4








REFRIGERANT FLUID PATH






503





SECONDARY FLUID HEAT EXCHANGER




4














Further objectives and advantages of the invention will become apparent from a consideration of the drawings and ensuing description.




DESCRIPTION OF THE PREFERRED EMBODIMENTS




Description of FIG.


1


:




In

FIG. 1

a refrigeration system ejects energy from its liquid into a coil 60 located in air conditioning system air handler


200




b.


A refrigeration compressor


10


compresses a refrigerant to a high pressure and temperature discharges it through pipe


20


to condenser


30


. Air is blown across condenser


30


causing the gas to condense into a liquid. Liquid


75


is accumulated in receiver tank


70


. Liquid is then routed to liquid cooling coil


60


where it gives up energy and as a consequence the liquid temperature going into coil


60


is higher than the liquid temperature leaving. The refrigerant is then routed to an evaporator


200


where it is expanded through an expansion valve


225


. The expanded refrigerant is warmed by air blown across evaporator


220


by fan


226


. The expanded gas is routed back to compressor suction


15


where compressor


10


starts the cycle over.




The air conditioning system performs the same function of removing energy from an evaporator area


220




b


and discharging it through a condenser


30




b


at a lower compression ratio. It however does this with a higher efficiency since the level to which it must raise the compression is less than that of the refrigeration system. It also means that the cost of running the refrigeration system is less, for many reasons as will be described herein. The adding of heat to the air conditioning system has the added benefit of causing additional air conditioning operation resulting in dehumidification of the air conditioned environment. Which has cascaded benefits of producing a lower humidity in the environment of air conditioned space and the refrigeration space. This produces less latent heat load on the refrigeration systems.




Description of FIG.


2


:




In

FIG. 2

an additional refrigeration area


200




c


is shown which exists in parallel with refrigeration area


200


. The refrigeration piping of this evaporative cooling coil system is paralleled with that of


200


. The operation of the remainder of the system is identical to area


200


in FIG.


1


.




Description of FIG.


3


:




In FIG.


3


and additional heat exchanger


303


has been added to further cool the refrigeration liquid with the efficiency of the air conditioning system. The refrigerant expanded by expansion valve


225




b


is passed through the heat exchanger


303


. The liquid from the refrigeration system is passed through the heat exchanger and is lowered closer to the air conditioner suction temperature. The additional energy removed from the refrigeration system liquid is now removed by the air conditioning system which is more efficient than the refrigeration system.




Description of FIG.


4


:




In

FIG. 4

a secondary fluid heat exchanger


503


is utilized to transfer energy from the refrigeration liquid to the air conditioning environment. Refrigeration liquid


75


is circulated through the secondary fluid heat exchanger


503


where energy is transferred to the secondary fluid. Secondary fluid pump circulates the fluid to air reheat exchanger


60


where the energy is transferred to the air conditioned space


200




b


for removal by the air conditioning system. It should be noted that exchanger


60


in all the figures only needs to be located in the air conditioned space to be effective. One convenient and advantageous location would be underneath one of the open (lacking doors) refrigeration fixture.




Description of FIG.


5


:




In

FIG. 5

a refrigeration circuit is shown which allows for conventional hot gas reheat of the air conditioned space


200




b


in addition to the liquid cooler dehumidification system disclosed herein. When liquid cooling is required the liquid is circulated through reheat coil


60


by switching 3 way valves


40


and


150


into the appropriate positions. When full heat is required the discharge gas is circulated through reheat coil


60


positioning valves


40


and


150


into the appropriate positions.




Someone skilled in the art would be aware after reading the information contained herein that multiple refrigeration systems could have the energy from the liquid lines injected into the air conditioning system. Any refrigeration system with an efficiency which is less than the air conditioning system would produce a net efficiency gain.




While the previous description contains many specificities, these should not be construed as limitations on the scope of the invention, but rather as an exemplification of one preferred embodiment thereof. Many other variations are possible. The scope of the invention should be determined not by the embodiment(s) illustrated, but by the appended claims and their legal equivalents.




Description of FIG.


6


:




A prior art system is show in

FIG. 6

which allows for conventional hot gas reheat of the air conditioned space


200




b.





Claims
  • 1. A method for dehumidifying an environment and refrigerating a second environment with a closed loop refrigeration system consisting of:compressing refrigerant with a refrigeration compressor to a high temperature and pressure condensing the high pressure refrigerant to a liquid at a high temperature circulating the high pressure liquid refrigerant through a coil located in an air duct which contains an air conditioning coil which is refrigerated with an air conditioning compressor which has a higher coefficient of performance than the refrigeration compressor sub-cooling the liquid by exchanging energy from the coil located in the air duct and the air circulating in the air duct evaporating the liquid refrigerant to a gas at a low pressure and temperature.
  • 2. A method for dehumidifying an environment and refrigerating a second environment with a closed loop refrigeration system consisting of:compressing refrigerant with a refrigeration compressor to a high temperature and pressure condensing the high pressure refrigerant to a liquid at a high temperature sub-cooling the high pressure liquid by discharging a portion of the energy contained in the high pressure liquid into a space which is air conditioned by an air conditioning system operating at a higher efficiency than the refrigeration system and removing the energy added to the air conditioned space with the air conditioning system.
RELATED APPLICATIONS

The present application claims the benefit of U.S. provisional application Ser. 60/168,336 filed Dec. 1, 1999.

US Referenced Citations (5)
Number Name Date Kind
3165903 Roc et al. Jan 1965 A
4819444 Meckler Apr 1989 A
5105633 Briggs Apr 1992 A
5686579 Vaynberg Nov 1997 A
5953926 Dressler et al. Sep 1999 A
Non-Patent Literature Citations (4)
Entry
Item 001A Product Brief Hy-Dry System Introduction and Summary of Test Results.
Item 001B Effect of the Hy-Dry System on a DX Air-Conditioning Economic Analysis and Conclusions.
Item 002 Service Session Humidity Removal in Supermarkets by John Tomczyk, Reprinted from Refrigeration Service & Contracting copyright 1996.
Item 003 Leaving Humidity Hy-Dry.
Provisional Applications (1)
Number Date Country
60/168336 Dec 1999 US