US2479848A

US2479848A - Multitemperature refrigeration apparatus and method

Info

Publication number: US2479848A
Application number: US662364A
Authority: US
Inventors: Mackey Charles Osborn; Gardiner M Rogers
Original assignee: ORANGE CRUSH Co
Current assignee: ORANGE CRUSH Co; ORANGE-CRUSH Co
Priority date: 1946-04-15
Filing date: 1946-04-15
Publication date: 1949-08-23
Anticipated expiration: 1966-08-23

Description

C. C. MACKEY ET' AL.

MULTITEMPERATURE REFRIGERATION APPARATUS AND METHOD Filed April l5, 1946 Patented Aug. 23, 1949 MULTITEMPERATURE RFRIGERATION APPARATUS AND METHOD y and Gardiner M. Rogers, ors to Orange-Crush Company, Chicago, Ill., acorporation of Illinois Application April l5, 1946, Serial No. 662,364

(Cl. (i2-125) Charles Osborn Macke Ithaca, N. Y., assign 12 Claims.

This invention relates to refrigeration, and more particularly to a multi-temperature refrigeration apparatus and method for maintaining different compartments of a refrigerator cabinet, or other segregated spaces, at different temperatures suited to the individual purposes of such compartments `or spaces. By Way of example, one of the compartments may be for freezlng food products/and storing them at low temperature and another or others of such compartments may be for storing other food products at one or more higher temperatures.

The principal object of the invention is to provide an improved refrigeration system of this character in which a thermosyphoning secondary refrigerant is employed in conjunction with a primary refrigerant or coolant and is circulated to and from the respective compartments or spaces by thermosyphonic acition resulting from changes in temperature and corresponding changes in fluid density of such secondary refrigerant. The system thus provides for circulatidn of the secondary refrigerant without mechanicai pumping and for this reason, as well as by the elimination of other commonly used devices, can be built for a much lower rst cost than can the conventional multi-temperature refrigeration system. The use of the thermosyphoning refrigerant in the manner contemplated also assures eciency in operation and the maintenance of unusually uniform temperatures in the respective refrigerated spaces.

Another factor making for economy in the system is that only one evaporator is required to maintain widely differing temperatures in two or more different parts of the system.

A further important feature of the invention is the provision of a multi-temperature refrigerating system of the general type above indicated in which condensation of water vapor on the surfaces in the high temperature compartment and the frosting of such surfaces may be prevented, thus avoiding excessive dehydration of fruits and vegetables or other products which may be stored in this compartment and eliminating the problem of defrosting.

Many other advantages and desirable characteristics of the invention will be apparent from the following description taken in connection with the accompanying drawing, in which the single ligure shows, in more or less diagrammatic form, a refrigeration system embodying -the apparatus, and adapted to carry out the method, of the invention.

In said drawing we lhave shown a primary refrigerant circuit, including a conventional condensing unit l, a liquid line 2, a thermostatic expansion valve 3, an evaporator 4 and a suction line 5. The condensing unit includes the usual motor-compressor unit 6, condenser 1 and receiver 8. From the latter the primary refrigerant, which may be Frech-12, passes through` the liquid line 2 to the expansion valve 3, or equivalent throttling device. Upon expanding through the latter, said primary refrigerant drops to a predetermined low temperature in the evaporator d, which may beof the dry expansion type and, in accordance with our invention, is positioned in a vessel v9 containing a secondary refrigerant ll which circulates through the system and serves as the cooling medium for the compartments or spaces to be refrigerated, as will later be described. The secondary refrigerant is thus in heat exchange relation with the evaporator i by which it is cooled to the desired extent, as, for example, to 15 F. The unit, comprising the evaporator li and vessel 9 (which is constantly lled with secondary refrigerant), is therefore hereinafter referred to as a heat exchanger and it will be understood that the compressor-condenser-evaporator primary refrigerating system is shown by way of example only since, for certain adaptations of the invention, some other form of primary coolant, such as an absorption refrigeration system, might be preferred.

The system is shown as embodied in a cabinet comprising outer walls IZ within which there are located a low temperature freezing and storage compartment I3 and a high temperature storage compartment lli. Said compartments are surrounded by suitable insulation l5 and above them there is an insulated compartment I6 containing the heat exchanger above mentioned and other elements which will be hereinafter described.

The condensing unit l is contained within a space l1 beneath the insulated part of the cabinet and is shown as mounted upon a frame or pedestal It.

The secondary refrigerant after being cooled to, say, -15 F. in the heat exchanger 9 ows downwardly therefrom through an outlet pipe I9 and, as shown, passes through two circuits, one leading to the low temperature compartment I3 and the other to the high temperature compartment I4, the latter circuit however including a mixing chamber 2| in which the secondary refrigerant is raised to a higher temperature before being admitted to the high temperature compartment.

The mst-mentioned circuit is downwardly through a pipe 22 in which there is a solenoid valve 28 under the control of a thermal switch 24 located in the high temperature compartment i3 and connected with said solenoid valve by suitable wiring contained in a conduit 25. When the valve 23 is opened the refrigerant nows downwardly through said pipe 22 and, as it receives heat from the compartment i3, its density de creases and circulation is set up to cause return thereof through a pipe 2t to a transversely extending pipe 21 connecting with ,an intake pipe 2d leading into the top of the vessel il. Cross pipes 2d are provided between the

pipes

22 and 26 and said pipes 22, 2t and it may be contained within hollow shelves and walls ln the Storage space, or may open into such hollow shelves 'its walls which may themselves serve as conduits to provide more extensive refrigerating suriaces if this should be desired.

As above indicated, the secondary refrigerant may be at a temperature of F. upon leaving the heat exchanger and in that case may return to the heat exchanger at a temperature of. say, 5 F. The control switch dd may be set to.close the solenoid valve t2 when the tempera ture in the storage space drops to 0 F., thereby stopping circulation in this circuit. This taper:-1 ature has been found to be a suitable one for storage of frozen foods and will be automaticady maintained by the means lust described.

it may be noted in this connection that the primary refrigerant vapor is returned to the condensingunit at a proper temperature to prevent liquefactlon in the return line, and a low pressure cut-out may be used in the condensing unit so that the motor will be stopped when the suction pressure of the primary refrigerant drops to a predetermined control value.

Il'he second circuit of the secondary refriger ant mentioned above is through a pipe Si, which is preferably inclined to the horizontal, leading to the mixing chamber 2i and through a pipe d2 leading from said chamber, a downwardly errtending pipe 33, cross pipes Sli and a riser ed in the compartment it, said riser leading to an in take pipe 36 opening into the top oi said tu". chamber 2i. An air vent 3l is, or may be, vided at the top of the pipe 3e above the point of connection thereof with the pipe 35.

A solenoid valve 38 is provided in the pipe 3l and is controlled by a thermal switch 3d located in the pipe '32, or in the pipe tt adjacent the junction o said pipes as shown in the drawing, said switch being responsive to the temperature of the liquid in the pipe in which it is located. Said thermal switch 39 is connected With the valve 38 by means of wiring cond in a conduit di. n

ifA it be desired to maintain the high temperature compartment ld at a temperature of 40 F.. the control may be set so that the secondary refrigerant will leave the mixing chamber 2l at a temperature of 34 F., it being understood that the cold refrigerant from the vessel t will have been mixed with the relatively warm refrigerant returning to the mixing chamber through the pipes 35 and 3S and that the control switch'e may be set so as to close the valve 30 when the temperature of the refrigerant flowing from. the mixing chamber 2i through the

pipes

32 and 33 drops under 34 F.

When the temperature ofthe refrigerant now- 4 ing through the pipe 83. the cross pipes 34 and the riser 35 in the compartment I4 rises to about 38 F. the density of the liquid will decrease sufciently tov set up the circulation causing the return or the liquid to the chamber at about that temperature.

It will be understood that, as in the case of the compartment I3.- the secondary refrigerant may be circulated through hollow walls and shelves in the compartment ll to provide more extensive cooling surfaces if this should be deaired.

It will be noted that by thus maintaining the coo surfaces in the compartment i4 above the freezing temperature of water and only slightly lower than the temperature ot the air in the compartment there will be relatively little condensation oi water vapor on the cooling surfaces andtherefore dehydration or the products stored in this com so 1aed as to amtam fruits. vegetables and like products in goed condition; also frosting of lthe cooling surfaces will be prevented and the defrosting problem. so troublesome in most refrigerating systems, will be eliminated.

I7lhere is a third circuit of the secondary reirigerant, namely, from the pipe 32 through a vertical pipe l2 and the pipes 2l and 2t to the vessel t or the 'heat exchanger. The now in the pipe "32 therefore divides ahead of the thermal switch t@ and a part oi' the relatively warm liquid is recooled in said heat exchanger. in this manner proper temperature of the portion of the secondary refrigerant used for cooling the high temperature compartment is maintained. The circulation in this circuit is due to thermosyphonic action resulting from the fact that the density of the secondary refrigerant in the conduits di and 2l is less than in the conduits i@ audit.

A contraction-and-flll tank di) is, or may be, provided at the top oi the pipe 28 to provide for a sumcient volume of secondary refrigerant to insure a um level above the level of the connection from the return line 2l. This is desirable since as the secondary refrigerant is cooled the total volume of this liquid in the system decreases. Without a reserve volume when the system is iilled at room temperature, this reduction in volume might cause the liquid level to volume the tank may be sealed from the air in order to prevent any loss of secondary refrigerant by evaporation. .although a, slight vacuum may then be created in the top of said tank d3 as the total volume of the refrigerant decreases due to cooling, the same vacuum then acts upon the dropper and riser lines and there 'will be no nte'rierence with the thermosyphoning as long as the inlet from the line 21 is not uncovered.

While we have shown only two compartments it will be understood that the principle of the invention may be extended to control the temperature of the air in more than two compartments, each at a diierent temperature, by using only one primary refrigerant heat exchanger. For example, the system is adaptable to the requirements of storage on ships of the United States Navy where three diderent storage temperatures are required, namely, 0 F. /i'or frozen foods, 33 F. for dairy products and 45 F. for

fruits and vegetables. Various other adaptations are of course within the purview of the invention.

The thermosyphoning refrigerant should be a fluid having a high coefficient of cubical expansion (or capacity for change of density with temperature), a high specific heat, high thermal conductivity, low viscosity, low freezing point and high flash and fire points. While future developments may provide more ideal fluids for this purpose than are now available we have found that a mixture of methy1 alcohol and water, with, say, two parts by volume of alcohol to one part by volume of water, is reasonably satisfactory since it has a freezing point below the lowest temperaturesneeded for refrigeration and has a considerable number of the other qualities above mentioned in reasonable measure. The new silicone oils have desirable properties for this purpose and probably will soon be available in sufficient quantities at reasonable` prices, although they have heretofore been rather expensive. Among other possible alternative substances which may be used are pure methyl alcohol, pure ethyl alcohol, ethylene glycol, glycerine and other mixtures of alcohol and water.

A desirable feature of the invention in addition to those above mentioned is that with the cooling surfaces arranged as described there is little air temperature differential from top to bottom of the storage compartments even though the latter contain shelves, where as in the common household refrigerator there is considerable air temperature variation from one shelf to another.

Another feature of our system is that the only pressure which the conduits of the secondary refrigerant circuits, which as above stated may in part be hollow walls or shelves, need withstand is the small hydrostatic head of only a few feet of secondary refrigerant. If a primary refrigerant were circulatedgthrough evaporators placed within the spaces to be refrigerated the evaporator plates would have to withstand the high pressures of the primary refrigerant at the temperature of its vaporization. 'I'his would result in y considerably greater danger ofv rupture and leakage than with our system.

Through the thermostatic controls above described very close control of the air temperature in the freezing and low temperature storage compartment may be maintained. This is important for there is now some evidence that large temperature fluctuations in the storage of frozen products may cause more loss of quality in the products while in storage than would be caused by an improper storage temperature.

As above indicated, there is a considerable saving in equipment and thus a lower first cost when our system is employed than is involved in the conventional refrigeration system for a multitemperature cabinet. When designed for a twotemperature cabinet the conventional system requires two evaporators with two thermostatic expansion valves, two air sensitive thermal switches operating two solenoid valves in the respective liquid lines, and-one suction pressure control valve in the suction gas line leaving the high ltemperature cabinet to prevent, or seek to prevent, frosting and consequent drying of stored foods. With our system one of said evaporators and one thermostatic expansion valve is eliminated as is the suction pressure valve. It will be evident that even further savings may be effected when more than two different temperature compartments or spaces are employed.

Another feature of the present system which is of practical importance is that the volume of 6 the secondary refrigerant employed in the system is sufficiently large to obtain two beneficial results. First, the condensing unit will not shortcycle for when it starts at the cut-in point of the age of apples or like low pressure control, the temperature of a large volume of the secondary refrigerant must be reduced to the cut-out control point before the motor will be stopped. There is no need for a surge drum, or other devices, in the primary refrigerant circuit to prevent short-cycling. Second, in the event of a, power failure, the rate of temperature rise of the air in the storage compartments of this unit is extremely slow because of the large heat capacity of the volume of secondary refrigerant in the system. For common durations of power failure, the tempertaure rise in this unit would not be sufficient to permit frozen products to defrost nor sumcient to cause food spoilage in the high temperature storage compartment.

It has been previously mentioned that the primary refrigerating system is illustrated only by way of example and that other primary coolants might be employed. It is even possible that for certain uses no source of mechanical energy would be required and that the outdoor air could be used as the primary coolant when it is at lower temperature than the desired temperature of storage. The primary heat exchanger could then be located out of doors at an elevation higher than that of the storage compartments. The secondary refrigerant would be cooled by the outdoor air and would then drop to the storage compartment or compartments where it would absorb heat and then through thermosyphoning action rise and return to the heat exchanger. Low temperatures of the outdoor air could thus be utilized to maintain higher but controlled temperatures in indoor storage compartments. For example, when the temperature of the outdoor air is fluctuating between limits of -,10 F.'and 30 F. a compartment storage temperature could be held substantially constant at 40 F. This would be particularly important for winter storproducts in certain of the northern states. f

While the mixing chamber 2| is shown as in the upper compartment I 6 it may be found desirable to locate it elsewhere, as, for example', in

the upper part of the compartment I4 in which case its surface would constitute a part of the cooling' surface within that compartment.

Other modifications which do not depart from the spirit or scope of the invention may suggest themselves to those skilled in the art.

vThe foregoing detailed description has been given for clearness of understanding only, and no unnecessary limitations should be understood therefrom, but the appended claims should be construed as broadly as permissible in view of the prior art.

We claim:

l. A refrigerating apparatus comprising a cabinet having a plurality of compartments therein to be refrigerated to different degrees; a primary refrigerating ysystem including a compressor, a

condenser and an evaporator; and a secondary refrigerating system including means for bringing a secondary refrigerant into heat exchange relation to said evaporator, means for circulating said secondary refrigerant through said Acompartments by thermosyphonic action resulting from changes of temperature thereof, and thermally-controlled devices for regulating the admission of said secondary refrigerant to the different 'i compartments and the refrigerating effect thereof, whereby each compartment may be maintained at a different temperature.

2. A refrigerating apparatus comprising a cabinet having a plurality of compartments therein to be refrigerated to dinerent degrees: a primary rcfrigerating system including a compressor, a .condenser and an evaporator; and a secondary refrigerating system including means for bringing a secondary refrigerant into heat exchange relation to said evaporator, means for vcirculating said secondary refrigerant through said compartments by thermosyphonic action resulting from changes of temperature thereof, thermallycontrolled devices for regulating the admissionl oi said secondary refrigerant to the different compartments and the refrigerating effect thereof, whereby each compartment may be maintained at a different temperature, and means for raising the temperature of a portion of said secondary refrigerant which is to be used for refrigerating a compartment to be maintained at relatively high temperature before admission thereof to said compartment.

3. A refrigerating apparatus comprising a cabinet having a plurality of compartments therein to be refrigerated to different degrees;.a primary refrigerating system including a compressor, a condenser and an evaporator; and a secondary refrigerating system including means for bringing a secondary refrigerant into heat exchange relation to said evaporator, means for circulating said secondary refrigerant through said compartments by thermosyphonic action resulting from changes-of temperature thereof, thermallycontrolled devices for regulating the admission of said secondary refrigerant to'the different compartments and the refrigerating effect thereof,

whereby each compartment may be maintained at a different temperature, and means for raising the temperature of a portion of said secondary refrigerant which is to be used for refrigerating a compartment to be maintained at relatively high temperature before admission thereof to said compartment, said last-mentioned means comprising a mixing chamber in which cold secondary refrigerant coming from the vicinity of said evaporator is mixed with relatively warm secondary refrigerant returned from said hightemperature compartment to raise the temperature of said cold refrigerant before it is admitted to the latter compartment.

4. A refrigerating apparatus comprising a cabinet having a freezing compartment to be maintained at a sub-freezing temperature and a storage compartment to be maintained at a temperature above freezing; a primary refrigerating element adapted to be maintained at a low subfreezing temperature; and a secondary refrigerating system including means for bringing a secondary refrigerant into heat exchange relation to said primary refrigerating element, means for circulating portions of said secondary refrigerant through the respective compartments aforesaid by thermosyphonic action resulting from changes in temperature of said refrigerant, and thermally-controlled devices for regulating the admission of said portions of the secondary refrigerant to said compartments and the refrigerating effect thereof, whereby said compartments may be maintained at the respective temperatures suited to the aforesaid functions thereof.

5. A refrigeration system comprising a cabinet having a plurality of compartments to be refrigerated and maintained at different temperatures;

a primary refrigerant circuit including an evaporator and means for controlling the flow of primary refrigerant to and from said evaporator to maintain a predetermined low temperature therein; a' secondary refrigerant circuit including a cooler in heat exchange relation with said evaporator, and means for controlling the Bow of secondary refrigerant through said compartments byv thermosyphonic action to separately regulate the temperature maintained by said secondary refrigerant in each compartment, 'whereby said compartments may be maintained at different temperatures. v

6. A refrigeration system comprising a cabinet having a plurality of compartments to be refrigerated and maintained at different temperatures; a primary refrigerant circuit including an evaporator and means for controlling the ow of primary refrigerant to and from said evaporator to maintain a predetermined low temperature therein; a secondary refrigerant circuit including a cooler in heat exchange relation with said evaporator, and means for controlling the ilow of secondary refrigerant through said compartments by thermosyphonic action to separately regulate the temperature maintained by said secondary refrigerant in each compartment, whereby said compartments may be maintained at different temperatures, said last mentioned means including thermally-controlled valves for controlling the flow of the secondary refrigerant to said compartments.'

7. A refrigeration system comprising a cabinet having a. plurality of compartments to be refrigerated and maintained at different temperatures; a primary refrigerant circuit including an evapol rator and means for controlling the flow of primary refrigerant to and from said evaporator to maintain a predetermined low temperature therein; a secondaryvirefrigerant circuit includins a cooler in heat exchange relation with said evaporator, means for controlling the ow of secondary refrigerant through said compartments by thermosyphonic action to separately l regulate the temperature maintained by said secondary refrigerant in each compartment, whereby said compartments may be maintained at different temperatures, said last mentioned means including thermally-controlled valves for controlling the ilow of the secondary refrigerant to said compartments, a mixing chamber in which relatively warm secondary refrigerant returning from a compartment which is maintained at a relatively high temperature is mixed with cold secondary refrigerant from said cooler to raise the temperature of the latterf and means for conducting the mixed refrigerant to saidlastmentioned compartment.

8. A refrigeration system comprising a cabinet having a plurality of compartments to be refileerated and maintained at different temperatures; a primary refrigerant circuit including an evaporator and means for controlling the flow of primary refrigerant to and from said evaporator to maintain a predetermined low temperature therein: a secondary refrigerant circuit including a cooler in heat exhange relation with said evaporator, means for controlling the dow of secondary refrigerant through said compartments by thermosyphonic action to separatelycontrolling the flow of the secondary refrigerant to said compartments, a mixing chamber in which relatively warm secondary refrigerant is mixed with cold secondary refrigerant from said cooler to raise the temperature of the latter, and means for conducting the mixed refrigerant to a compartment which is to be maintained at relatively high temperature.

9. In the operation of a multi-temperature refrigeration system the method which consists in circulating by thermosyphonic action a secondary refrigerant, having a high co-emcient of cubical expansion or of change in density with changes in temperature, into heat exchange relationship with a primary refrigerating element. to reduce the temperature of said secondary refrigerant to the minimum point necessary to enable it to refrigerate the coldest of a plurality of refrigerating compartments to be maintained at different temperatures, thereafter directing portions of said secondary refrigerant to the respective compartments, and regulating the amount of refrigeration of each of said compartments by the secondary refrigerant directed thereto, whereby each compartment may be maintained at a desired individual temperature.

n 10. In the operation of a multi-temperature refrigeration system the method which consists in circulating by thermosyphonic action a secondary refrigerant, having a high co-efiicient of cubical expansion or of change in density with changes in temperature, into heat exchange relationship with a primary refrigerating element. to reduce the temperature of said secondary refrigerant to the minimum point necessary to enable it to refrigerate the coldest of a plurality of refrigerating compartments to be maintained at different temperatures. thereafter directing portions o1' said secondary refrigerant to the respective compartments. and regulating the amount of refrigeration of each of said compartments by the secondary refrigerant directed thereto by varying the temperature of the refrigerant directed to the different compartments and thermally-controlling the admission of refrigerant to each compartment, whereby each compartment may be maintained at a desired individuai temperature.

primary coolant; and a secondary refrlgerating` system including means for bringing a secondary refrigerant into heat exchange relation to said primary coolant, means for circulating said secondary refrigerant through said compartments by thermospyhonic action resulting from changes of temperature thereof, and thermally-controlled devices for regulating the admission of said secondary refrigerant to the different compartments and the refrigerating effect thereof, whereby each compartment may be maintained at a different temperature.

12. A refrigerating apparatus comprising a cabinet having a plurality of compartments therein to be refrigerated to different degrees: a primary refrigerating element; and a secondary refrigerating system including means for bringing a secondary refrigerant into heat exchange relation to said primary refrigerating element, means for circulating said secondary refrigerant through said compartments by thermosyphonic action resulting from changes of temperature thereof, thermally-controlled devices for regulating the admission of said secondary refrigerant to the different compartments and the refrigerating effect thereof, whereby each compartment may be maintained at a. different temperature, and means for raising the temperature of a portion of said secondary refrigerant which is used for refrigerating a compartment to be maintained at relatively high temperature before admission thereof to said compartment.

CHARLES OSBORN MACKEY. GARDINER M. ROGERS.

REFERENCES CITED The following references are of record in the le of this patent:

UNITED STATES PA'IENTS