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Publication numberUS3869870 A
Publication typeGrant
Publication dateMar 11, 1975
Filing dateJul 2, 1973
Priority dateJul 2, 1973
Publication numberUS 3869870 A, US 3869870A, US-A-3869870, US3869870 A, US3869870A
InventorsRichard Kuehner
Original AssigneeBorg Warner
Export CitationBiBTeX, EndNote, RefMan
External Links: USPTO, USPTO Assignment, Espacenet
Refrigeration system utilizing ice slurries
US 3869870 A
Abstract
A slurry of ice crystals in a water immiscible carrier fluid, for example, toluene, is produced and circulated to a heat exchanger for absorbing heat from a load, principally by means of the melting ice. The two liquids are then forwarded to a receiver where they separate into two phases. The liquid water from the melted ice is returned separately to the ice forming unit and at least a part of the carrier fluid is re-chilled prior to re-circulating the slurry through the system.
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United States Patent [1 1 Kuehner Mar. 11, 1975 REFRIGERATION SYSTEM UTILIZING ICE sLIJRRIEs [75] Inventor: Richard Kuehner, Mount Prospect,

Ill.

[73] Assignee: Borg-Warner Corporation, Chicago,

Ill.

[22] Filed: July 2, 1973 [2|] Appl. No.: 375,991

[52] U.S. CI 62/114, 62/333, 62/502, 165/104 [5 l] llnt. Cl. .I F25b 23/00 [58] Field of Search 62/114, 333,334,502; 165/104 [56] References Cited UNITED STATES PATENTS 3.247.678 4/1966 Mohlman 62/199 3.564.727 2/1971 Fraser 62/33'2 X 3,603,379 9/1971 Leonard, Jr. 62/333 X FOREIGN PATENTS OR APPLICATIONS l,0l L104 l965 Great Britain I65/l04 Primary Examiner-Meyer Perlin Assistant ExaminerRonald C. Capossela Attorney, Agent, or Firm-Thomas B. Hunter [57] ABSTRACT A slurry of ice crystals in a water immiscible carrier fluid, for example, toluene, is produced and circulated to a heat exchanger for absorbing heat from a load, principally by means of the melting ice. The two liquids are then forwarded to a receiver where they separate into two phases. The liquid water from the melted ice is returned separately to the ice forming unit and at least a part of the carrier fluid is re-chilled prior to re-circulating the slurry through the system.

9 Claims, 3 Drawing Figures PRIMARY REFRIGERATION EQUIPMENT REFRIGERATION SYSTEM UTILIZING ICE SLURRIES BACKGROUND AND SUMMARY OF THE INVENTION This invention relates generally to an improved refrigeration system using a slurry consisting of ice particles in a water immiscible carrier. This invention is particularly useful in air conditioning systems employing a plurality of heat exchangers located in the various zones requiring air conditioning.

Various systems have been proposed in the prior art for supplying a refrigerated liquid, usually chilled water, from a central refrigeration station. More recently, there has been described a system in which an ice-brine slurry is circulated to the various heat exchangers through supply risers and returned to the central station for reforming of the ice-brine slurry. For example, in US. Pat. No. 3,247,678 issued to J. W. Mohlman on Apr. 26, I966, an air conditioning system of the previously mentioned type utilizes a direct expansion of butane into a brine solution which is adapted to freeze ice crystals therein; and means for circulating the ice brine slurry to the heat exchange units located throughout the building.

The advantages of using an ice slurry are also recognized. A pound of ice in melting will absorb approximately 80 BTUs, whereas if the system has to rely solely on sensible heat of the chilled fluid, 1 pound of water would only be able to absorb I BTU for each degree rise in temperature of the fluid. For example, in a typical system with a F. water-temperature rise, 1 pound of recirculated water will absorb l0 BTUs of heat. On the other hand, it is possible to absorb the same l0 BTUs by melting only one-eighth of a pound of ice. Since it is possible to produce and pump a slurry containing up to 40 percent ice, the system would only be required to circulate about 0.3 lbs of slurry to achieve the same effect.

From the foregoing, it is clear that the amount of piping, which represents a major cost in any air conditioning installation, can be materially reduced. Moreover, it is possible to utilize smaller heat exchangers and/or the recirculation of less air. If the latter, this would permit the use of smaller ducts and fans.

In the Mohlman system referred to above there is a rather serious problem since the presence of salt reduces the freezing point of water. The ice-brine slurry in equilibrium inherently has a temperature less than the freezing point of pure water, 32F. As the brine circulates through the heat exchanger, it is almost impossible to prevent a substantial build up of frost or ice exchanger coil. In addition, brine solutions are also very corrosive so that expensive metal alloys for the piping are required to handle a brine solution without serious problems.

Still another disadvantage of an aqueous system is the fact that ice particles will tend to agglomerate into larger particles which can plug the passages through which the slurry is pumped. For example, if the size of the particles is large enough two or more of the partieles may. attempting to move through a restricted pas sage, be forced into contact with one another and, in effect, form an impassable bridge. Moreover, it is extremely difficult to maintain a uniform suspension of the ice particles in the aqueous fluid without continuous agitation. For example, in a brine system the ice has a lower specific gravity and the particles will tend to float. In the present invention, the specific gravity of the water immiscible carrier can ccan be selected to be equal to the specific gravity of ice to maintain the ice particles in suspension. If required, the carrier fluid can be made either more or less dense than ice so that one can predict to what extent the particles will float or settle as the particular application requires. Also, the carrier fluid may be selected on the basis of its lubricating properties which protect the surface with a lubricating layer or film to prevent agglomeration and maintain the particles at the proper size and the correct degree of suspension.

In a preferred embodiment of the invention, a slush is produced by discharging water into a water immiscible liquid which has been chilled substantially below 32F. The resultant slurry is pumped through the cooling coils where the heat is absorbed from the air by the heat of fusion of the ice. As the ice melts, of course, it produces liquid water; and when all the ice is melted a two phase liquid system results. This is discharged into a separator where the two liquids, being immiscible, separate into two phases. The water is returned to the freezer for refreezing and the non-aqueous liquid used as the carrier is returned separately for rechilling and /or to raise the slurry to a temperature to prevent coil frost.

DETAILED DESCRIPTION OF THE DRAWINGS FIG. 1 is a schematic diagram illustrating a preferred embodiment of the apparatus used to carry out the present invention;

FIG. 2 is a modification of the apparatus shown in FIG. 1; and

FIG. 3 is still another modification of the apparatus shown in FIG. 1.

DETAILED DESCRIPTION OF THE INVENTION Referring now to FIG. 1, there is depicted a typical air conditioning system for use in a multi-room office, apartment or residential building which includes a plurality of terminal units 10 through which air is circulated to be cooled. Although shown as a fan coil unit wherein fan 12 blows air over the heat exchange coil 14, it is obvious that induction units or other terminal units may be used. The source for the ice slurry is connected to the various heat exchangers 14 by means of supply risers 16 and return risers l8. Slush ice is formed in a freezing tank 20 which is cooled by any conventional form of refrigeration equipment 22 wherein refrigerant is circulated through a coil 24 to cool the liquid introduced into the freezing tank. The slurry, as indicated above comprises ice and a liquid which is immiscible with water, such as for example, toluene, chlorobenzene or similar fluids. Such water immiscible liquid is sometimes referred to herein as the carrier fluid.

From the freezing tank 20 the ice containing slurry is circulated by means of a pump 25 through line 26 to the supply riser 16. In accordance with the demand for cooling existing at any given time, the slurry is diverted through heat exchange coil 14 in terminal units 10 and the air is circulated thereover by fan 12. Suitable thermostatic controls (not shown) are included to control the flow of slurry and/or the operation of blower I2. The returning slurry directed through return riser 18 consists essentially of liquid water and the carrier fluid.

This mixture is delivered to separation tank 28 wherein the two liquids separate by gravity into two homogeneous liquid phases. It will be assumed that the carrier fluid A, toluene for example, in this case would have a specific gravity lower than that of water. In this case, the upper body of liquid A would comprise substantially 100 percent carrier fluid while the lower body B consists of essentially 100 percent water which is usually liquid, but may include some unmelted ice. Water is delivered to freezing tank 20 through line 29. Carrier fluid is drawn-off through line 30 and may be divided into two streams under the control of mixing valve 31 which may be manually or automatically controlled. The one stream 32 is returned to the freezing tank 20 and the other stream is passed through line 34 to control the percentage of carrier fluid in the slurry stream going to the supply riser 16. In this way the temperature of the slurry can be controlled at about 32F.

Various modifications may be made to the system just described to achieve substantially the same results. For example, a direct contact system may be utilized in which a refrigerant is introduced directly into the receiver containing the mixture of water and the carrier fluid. Also, it is possible to manufacture a slurry of ice and introduce it directly into a body of carrier fluid for circulation to the load.

FIG. 2 illustrates a first modification showing that portion of the system which is designed to make up the slurry for distribution to the risers 16 and 18. Where this system employs features of construction in common with FIG. 1, the same reference numerals are used to designate corresponding elements.

The mixture of carrier fluid and essentially liquid water is returned from the load via return riser l8 and delivered to tank 28 where the water and carrier fluid separate into two distinct liquid phases. The water B is withdrawn through line 29 while the carrier fluid (which is the upper layer of liquid within the tank 28) is conducted to vessel 20 through line 32. A separate branch line 34 for the carrier fluid connects with conduit 26 leading to the suction side of the pump for distribution to the load, and is under the control of mixing valve 31 in the same manner as the FIG. 1 embodiment.

The foregoing system is commonly referred to as a direct contact system and utilizes a refrigerant which may be a halocarbon refrigerant or a hydrocarbon such as butane. Compressor 44 compresses the refrigerant and directs it through line 45 to a condenser 46 to liquefy the hot gas by heat exchange with air or water. The high pressure liquid refrigerant then passes through expansion device 48 in line 47 where it is mixed with water flowing through line 29 and enters chamber 20. The refrigerant evaporates in chamber 20 and by abstracting the heat from the water causes a slurry of ice to form. The suction gas is then returned through line 50 to the suction side of compressor 44.

In FIG. 3 there is shown a system which utilizes suitable means for manufacturing finely divided ice particles and is adapted to introduce such ice particles directly into a body of carrier fluid for circulation to the system. As in the other embodiments the water and carrier fluid separate into two phases in receiver 28 and the water B is conducted via line 29 to an ice maker unit designated at 60. This unit which may be of any conventional design is illustrated as being of the type described in US. Pat. No. 2,575,374 issued to E. C. Walsh on Nov. 20, l95l which is intended to be incorporated by reference herein. Water is frozen on the walls of a drum 62 and removed therefrom by scraper elements 64 driven by motor 65 for discharge through a chute 66 into the mixing vessel 20. The ice maker is refrigerated by a vapor cycle circuit including a compressor 70, condenser 72, expansion device 74 and an evaporator chamber 76 which is in direct communication with the walls of the drum 62. In this system the temperature of the fluid in chamber 20 is never below 32 F., so it is not necessary to use a mixing control from the separation chamber 28. All of the carrier fluid may be conducted to mixing chamber 20 to receive the ice discharged from the ice maker.

It is, of course, not necessary to use the ice-water change of state in the present invention. All that is required is that two substances be provided which are capable of existing both in liquid and solid phases and providedfurther that the two substances in liquid phase be immiscible. Naturally, one substance should have a freezing point low enough to abstract heat efficiently from air used in human comfort air conditioning applications, i.e., at least as low as about F., and the other substances must have a freezing point substantially below that of the first substance.

In selecting the carrier fluid, various criteria should be considered. First of all the fluid must be a liquid over the entire operating range, including shut down conditions. The specific gravity of the cooling liquid should also be preferably the same as ice at the temperatures at which the ice is frozen and circulated but different when both exist as liquids. The immiscibility of the carrier fluid in water has previously been discussed and it should be mentioned further that this property must be maintained throughout the entire temperature range at which the system is operable. Other considerations include non-toxicity, low viscosity, stability and reasonable cost. In addition to the materials mentioned earlier, satisfactory fluid would include kerosene and light fuel oil.

While this invention has been described in connection with a certain specific embodiment thereof, this is by way of illustration and not by way of limitation; and the scope of the appended claims should be construed as broadly as the prior art will permit.

What is claimed is:

l. A system comprising a first substance capable of existing in both liquid and solid phases and having a freezing point below about 60F; a second substance capable of existing in both liquid and solid phases and having a freezing point substantially below the freezing point of said first substance and being immiscible with said first substance when both are in the liquid phase; means for chilling said first substance to a temperature below its freezing point to effect a change of state from liquid to solid; means for mixing the resulting solid first substance with said second substance in liquid phase; means for circulating the resulting mixture to a refrigeration load to abstract heat therefrom by the change of state from solid to liquid of said first substance; and means for separating said first and second substances.

2. A system as defined in claim 1 including a primary refrigeration system for chilling said second substance to a temperature below the freezing point of said first substance, but above its own freezing point; and means for introducing said first substance, in liquid phase, into said chilled second substance.

3. A system as defined in claim 1 including a direct contact refrigeration system; and means for introducing a refrigerant from said direct contact refrigeration system into intimate contact with a non-homogeneous mixture of said first and second substances.

4. A system as defined in claim 1 including a refrigeration system for chilling said first substance per se below its freezing point to effect a change of state from liquid to solid; and means for mixing the resulting solid first substance with said second substance in the liquid state.

5. A system as defined in claim 1 wherein said first substance is water.

6. A method of refrigerating a thermal load compris ing the steps of forming a slurry consisting essentially of ice in a water immiscible carrier fluid; circulating the slurry to said load and bringing said slurry into heat exchange relation therewith whereby heat is abstracted by the melting of the ice in the slurry; returning the two phase stream to a separator for separating the two phases consisting essentially of water and the water immiscible carrier fluid; separating the water and said carrier fluid; re-freezing the water; and re-forming the slurry for recirculation to said thermal load.

7. A method as defined in claim 6 wherein said liquid water and water immiscible carrier fluid are mixed together and then brought into direct contact with a refrigerant to freeze the ice into a slurry.

8. A method as defined in claim 6 wherein liquid water per se is frozen and then mixed with said water immiscible carrier fluid.

9. A method as defined in claim 6 wherein said water immiscible carrier fluid is chilled to a temperature below the freezing point of water but above its own freezing point by indirect contact with a refrigerant; and liquid water is introduced into the resulting chilled carrier fluid to form a slurry.

Patent Citations
Cited PatentFiling datePublication dateApplicantTitle
US3247678 *Oct 2, 1963Apr 26, 1966John W MohlmanAir conditioning with ice-brine slurry
US3564727 *Mar 3, 1969Feb 23, 1971Virtis Co IncFreeze dryer using an expendable refrigerant
US3603379 *Apr 8, 1969Sep 7, 1971Carrier CorpHeating and cooling system
Referenced by
Citing PatentFiling datePublication dateApplicantTitle
US4283925 *Nov 15, 1979Aug 18, 1981Robert WildfeuerSystem for cooling
US4334412 *Nov 15, 1979Jun 15, 1982Robert WildfeuerCooling system
US4400286 *Jan 15, 1981Aug 23, 1983Peter SchaperHeat storage materials suitable in particular for indoor air cooling
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Classifications
U.S. Classification62/114, 165/104.31, 62/333, 165/104.17, 165/104.18, 165/104.13, 62/502
International ClassificationF25D16/00, F25D17/02, F25C1/14
Cooperative ClassificationF25C2301/002, F25D17/02, F25C1/145, F25D16/00
European ClassificationF25D16/00, F25C1/14C, F25D17/02