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US2032287A - Refrigerant feed control - Google Patents

Refrigerant feed control Download PDF

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US2032287A
US2032287A US19084A US1908435A US2032287A US 2032287 A US2032287 A US 2032287A US 19084 A US19084 A US 19084A US 1908435 A US1908435 A US 1908435A US 2032287 A US2032287 A US 2032287A
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refrigerant
liquid
accumulator
evaporator
valve
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US19084A
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William R Kitzmiller
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Frick Co Inc
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Frick Co Inc
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B5/00Compression machines, plants or systems, with several evaporator circuits, e.g. for varying refrigerating capacity

Definitions

  • This invention relates to a refrigerating system employing one or more evaporators or cooling coils for producing the cooling effect, the number of evaporators in the system being dependent .upon the amount of refrigeration required.
  • a further object of the invention is to provide a system in which line adjustment of expansion valves or the like is avoided and, where the ad justment permits liquid to pass over with the gas, the system is arranged to handle the entrained refrigerant.
  • Fig. l is a diagraatic view illustrating one application of the invention.
  • FIG. 2 a similar view of a modified form.
  • compressed refrigerant is discharged from a compressor it through a pipe ii to a condenser I]? where it is liquefied.
  • Liquid refrigerant passes through pipe 40 63 to evaporator coil it where evaporation occurs and heat is absorbed thereby.
  • the refrigerant vapor is sucked back to the compressor through suction line it, accumulator ii and suction line it.
  • the above described elements are in themselves of usual or conventional construction and form no part of the present invention. Furthermore these elements may be of any desired construction other than that illustrated, for example, the coils id and it may be of double pipe construction for cooling liquids.
  • the expansion valve I9 is preferably of the adjustable type in order that it may be set as desired to permit expansion from the high to the low side of the system.
  • Liquid in the accumulator ill will drain downwardly into pipe 2E3 which is connected at its lower end to the bottom portion of the lower or secondary evaporating coil it.
  • the upper portion of the coil l5 has a connection 2!! with the suction line it so that refrigerant gas will be sucked from the coil it at the same time that it is sucked from the coil M and entrained refrigerant may also be carried into the accumulator through the pipe 2i from the coil i5.
  • Expansion valve i9 is preferably manually set to give the correct quantity or an amount slightly in excess of the correct quantity of the liquid refrigerant which will just entirely evaporate in both of the coils i l and it. Any slight excess of refrigerant withdrawn 'from the coils it and iii and. trapped out in the accumulator can be readily returned by gravity to the lower coil it because this coil is made of a length and size such that the pressure drop under the desired operating conditions, is not too great to overcome vthe gravity head of liquid from the accumulator and thereby prevent its return.
  • Fine adjustment of the expansion valve ill is not required due to the fact that if the adjustment of the valve is excessively wide it permits a greater flow than is necessary.
  • the liquid level will rise in pipe it and after the pipe 28 is filled the system will gradually become filled.
  • the valve ll closes and by so doing prevents excess refrigerant from flowing into the evaporator coils. Accordingly liquid will no longer be entrained with gas withdrawn from the evaporator coil iii to further fill up the pipe 20 or accumulator iii and with the absorption of heat the chamber 42.
  • Fig. 2 is shown a refrigerating system similar to that of Fig. 1 but modified to the extent of employing an additional evaporator coil and modified accumulator construction.
  • a compressor 25 discharges compressed refrigerant through pipe 26 into a condenser 21 where the refrigerant is liquefied.
  • the refrigerant from the condenser 21 passes through pipe 28 to an evaporator consisting of coils 29, 30 and 35 which coils like those of Fig.1 may also be of conventional construction.
  • Refrigerant vapor is withdrawn from the upper part of coils 29 and 39 through a suction line 32.and from the coil 3
  • Flow of liquid refrigerant through the liquid line 28 is controlled by an automatic valve 36 connected by pipes 31 and 38 with the accumulator and which operates responsive to liquid refrigerant level similar to valve H of Fig. 1.
  • the expansion valve 39 is preferably of the adjustable type similar to valve i9 of Fig. 1 and is capable of being manually set to permit expansion from the high to the low side of the system.
  • the accumulator 34 is provided with a partition 40 which divides the accumulator into chambers 4
  • a thermostat 44 On the low side of the system adjacent the valve 39 is located an electrically operated valve 43 controlled by a thermostat 44 from a thermostat bulb 45.
  • Refrigerant gas and entrained liquids are withdrawn from the evaporator 29 through pipe 32 to chamber 4
  • the baffle 40 in the accumulator terminates near the bottom of the accumulator and refrigerant in the chamber 4
  • a thermostatically operated valve 49 controls.
  • valve 49 being controlled from any desired point in the circuit by a thermostat 59 having a bulb 5
  • valves which can be operated in accordance with temperature conditions may be employed.
  • valve 49 will reopen to permit equalization of refrigerating levels in chambers 4
  • valve 49 When the valve 49 is closed, forcing liquid from chamber 42 of the accumulator into chamber 4
  • Expansion valve 39 similarly to expansion valve i9 in Fig. 1 above, is set to supply refrigerant sufficient or somewhat in excess of that required to be evaporated in all the coils of the cooler and therefore a mixture of gaseous and liquid refrigerants is withdrawn from each of the coils Gaseous refrigerant and entrained liquid withdrawn from the coils 29 and 30 is separated in chamber M of the accumulator, the gaseous refrigerant passing to the suction line and the liquid refrigerant draining down to the line 46.
  • is discharged into chamber 42 of the accumulator, the gaseous refrigerant passing through pipe 48 into suction line 35 and the liq-' uid refrigerant draining through pipe 41. If an excess of liquid refrigerant is fed through the valve 39 the level of liquid refrigerant will rise in the accumulator 34 until the valve 36 closes, shutting off the supply. Thereafter liquid refrigerant passing from the accumulator through pipes 46 and 41 will pagtially evaporate due to heat absorption and the level in the accumulator since no liquid is flowing in will be reduced, until the liquid level in the accumulator has decreased sufiiciently to cause the opening up of valve 36.
  • the valves 43 and 49 may be controlled from different points suchas points 45 and 5
  • Thermostats which control these valves are preferably set at slightly difierent temperature levels.
  • a method of refrigeration comprising supplying liquid refrigerant, evaporating a portion of said liquid refrigerant, withdrawing the vaporous and entrained liquid from the place of evaporation, separating liquid from the vapor, evaporating a portion of the separated liquid, withdrawing the vaporous and entrained liquid from the second place of evaporation, separating liquid from the vapor, equalizing the liquid level between the two separated liquids, and utilizing part of the entrained liquid from the second separation for a subsequent evaporation.
  • a method of refrigeration comprising supplying liquid refrigerant, evaporating a portion of said liquid refrigerant, withdrawing the vaporous and entrained liquid from the place of evaporation, separating liquid from the vapor, evaporating a portion of the separated liquid, withdrawing the vaporous and entrained liquid from the second place of evaporation, separating liquid from the vapor, equalizing the liquid level between the separated liquids, utilizing part of the entrainedliquid from the second separation for a subsequent evaporation and utilizing liquid refrigerant from the second separation to out off the supply for the final evaporation.
  • a refrigerating system comprising an evaporator formed of a plurality of sections and an accumulator having a plurality of sections for separating entrained liquid refrigerant from gaseous refrigerant, means for supplying liquid refrigerant to one section of the evaporator, means for returning some of the separated liquid to another section of the evaporator, equalizing the liquid level between two sections of the accumulator, and means for cutting off one section of the evaporator.
  • a refrigerating system comprising an evapotor having a plurality of sections and an accumulator having at least two sections, means for supplying liquid refrigerant to one of said evaporator sections in excess of the amount that may be evaporated therein, separating the excess liquid from the gaseous refrigerant drawn from the evaporator in one section of the accumulator, returning a portion of the separatedliquid to another section of the evaporator, equalizing the liquid level between the sections of the accumulator, and feeding part of the liquid from the'second section of the accumulator to a third evaporator section.
  • a refrigerating system comprising an evaporator having a plurality of sections and an accumulator having at least two sections, means for supplying liquid refrigerant to one of said evaporator sections in excess of the amount that may be evaporated therein, separating the excess liquid from the gaseous refrigerant drawn from the evaporator in one section of the accumulator, returning a portion of the separated liquid to another section of the evaporator, equalizing the liquid level between the sections of the accumulator, feeding part of the liquid from the second section of the accumulator to a third evaporator section, and means for forcing liquid refrigerant from the second section of the accumulator in a manner to cut off the liquid supply to the third section of the evaporator.
  • a refrigerating system .of connected elements including an evaporator composed of sections,an accumulator,means for supplying refrig-' 'erant deposited in the accumulator from one evaporator section into another evaporator section, means responsive to accumulator liquid level for altering the refrigerant supplied to the evaporator, and means between said last mentioned means and an evaporator section for restricting the refrigerant supply thereto.
  • a refrigerating system of connected elements including an evaporator formed of sections, an accumulator for trapping out liquid entrained with gaseous refrigerant as it is drawn from the evaporator, means for supplying refrigerant deposited in the accumulator into an evaporator section, means responsive to accumulator liquid level for altering the refrigerant supply to the evaporator, and means between said last mentioned means and an evaporator section for restricting the refrigerant supply.
  • the method of refrigeration comprising the stages of supplying refrigerant to a first place of evaporation, evaporating a portion of said refrigerant, passing evaporated refrigerant and entrained liquid refrigerant to a place of separation, separating the liquid refrigerant from the' gaseous refrigerant, passing said separated liquid refrigerant to a second place of evaporation, con,- trolling the supply of refrigerant to the first place of evaporation in accordance with the quantity of refrigerant fluid passed from the first place of evaporation, and further restricting said supply to the first place of evaporation to thereby maintain a. supply of refrigerant in both places of evaporation.
  • a refrigerating system of connected elements including an evaporator composed of sections, an accumulator, means for supplying refrigerant deposited in the accumulator from one evaporator section into another evaporator section, means for altering the refrigerant supplied to the evaporator, responsive to an excess of refrigerant supplied thereto, and means between said last mentioned means and an evaporator section for restricting the refrigerant supply thereto.
  • a refrigerating system of connected elements including an evaporator formed of sections, means for supplying'refrigerant to a first evaporator section, means for supplying refrigerant from said first evaporator section to a second evaporator section, a valve for shutting off the supply of refrigerant to the first evaporator section responsive to an excess of refrigerant supplied thereto, and a second valve between the first valve and the first evaporator section for restricting the supply of refrigerant.

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  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Mechanical Engineering (AREA)
  • Thermal Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Devices That Are Associated With Refrigeration Equipment (AREA)

Description

Patented Feb. 25, 1936 ITED STATES PATENT OFFICE REFRIGERANT FEED CONTBQL Application April 30,
10 Claims.
This invention relates to a refrigerating system employing one or more evaporators or cooling coils for producing the cooling effect, the number of evaporators in the system being dependent .upon the amount of refrigeration required.
Heretofore certain types of evaporators, especially those formed of relatively long lengths of tubing and carrying heavy refrigerating loads,
have been found difiicult to flood and if operated flooded, large quantities of entrained liquids are carried over with the suction gas which entrained liquid has been found difficult to provide for.
It is an object of the present invention to provide a refrigerating system having means for automatically controlling the supply of refrigerant from the condenser, for automatically controlling the circulation of the refrigerant in the cooling coils to produce the desired refrigerant effect, for automatically maintaining the fluid or other substance refrigerated at a definite temperature, and for securing a flooded condition in the coils.
A further object of the invention is to provide a system in which line adjustment of expansion valves or the like is avoided and, where the ad justment permits liquid to pass over with the gas, the system is arranged to handle the entrained refrigerant.
Other objects and advantages will be apparent from the following description taken in connection with the accompanying drawing wherein,
Fig. l is a diagraatic view illustrating one application of the invention.
Fig. 2, a similar view of a modified form.
Referring to Fig. l of the drawing, compressed refrigerant is discharged from a compressor it through a pipe ii to a condenser I]? where it is liquefied. Liquid refrigerant passes through pipe 40 63 to evaporator coil it where evaporation occurs and heat is absorbed thereby.
The refrigerant vapor is sucked back to the compressor through suction line it, accumulator ii and suction line it. The above described elements are in themselves of usual or conventional construction and form no part of the present invention. Furthermore these elements may be of any desired construction other than that illustrated, for example, the coils id and it may be of double pipe construction for cooling liquids.
The flow of liquid refrigerant through pipe it is controlled by an automatic valve ll, connected by pipes 22 and 23 respectively with the upper portion of the accumulator and a depending liquid receiving pipe it, operates responsive to 1935, Serial No. 19,084
liquid level. The liquid refrigerant passing the valve ll flows through pipe I 3' and expansion valve is into the lowermost turn of the cooling coil Hi.
The expansion valve I9 is preferably of the adjustable type in order that it may be set as desired to permit expansion from the high to the low side of the system.
From the upper portion of the coil ill into which the refrigerant has been admitted from the pipe l3 through expansion valve it the gaseous refrigerant, after having performed its refrigerating function and absorbed heat, is sucked back to the compressor through pipe i5, accumulator ll and suction line it. Along with this gaseous refrigerant a quantity of entrained liquid will be carried and the entrained liquid will be separated by gravity from the gaseous refrigerant and deposited in the accumulator ll.
Liquid in the accumulator ill will drain downwardly into pipe 2E3 which is connected at its lower end to the bottom portion of the lower or secondary evaporating coil it. The upper portion of the coil l5 has a connection 2!! with the suction line it so that refrigerant gas will be sucked from the coil it at the same time that it is sucked from the coil M and entrained refrigerant may also be carried into the accumulator through the pipe 2i from the coil i5.
Expansion valve i9 is preferably manually set to give the correct quantity or an amount slightly in excess of the correct quantity of the liquid refrigerant which will just entirely evaporate in both of the coils i l and it. Any slight excess of refrigerant withdrawn 'from the coils it and iii and. trapped out in the accumulator can be readily returned by gravity to the lower coil it because this coil is made of a length and size such that the pressure drop under the desired operating conditions, is not too great to overcome vthe gravity head of liquid from the accumulator and thereby prevent its return.
Fine adjustment of the expansion valve ill is not required due to the fact that if the adjustment of the valve is excessively wide it permits a greater flow than is necessary. The liquid level will rise in pipe it and after the pipe 28 is filled the system will gradually become filled. When the liquid level has risen above a predetermined point the valve ll closes and by so doing prevents excess refrigerant from flowing into the evaporator coils. Accordingly liquid will no longer be entrained with gas withdrawn from the evaporator coil iii to further fill up the pipe 20 or accumulator iii and with the absorption of heat the chamber 42.
the supply of liquid refrigerant in the evaporator coil l5, pipe 29, and accumulator l1, will be evaporized or boiled off and the vapor sucked back to the compressor until the quantity of liquid refrigerant is reduced sumciently to cause reopening of the automatic valve H.
In Fig. 2 is shown a refrigerating system similar to that of Fig. 1 but modified to the extent of employing an additional evaporator coil and modified accumulator construction. According to the construction of Fig. 2 a compressor 25 discharges compressed refrigerant through pipe 26 into a condenser 21 where the refrigerant is liquefied. The refrigerant from the condenser 21 passes through pipe 28 to an evaporator consisting of coils 29, 30 and 35 which coils like those of Fig.1 may also be of conventional construction. Refrigerant vapor is withdrawn from the upper part of coils 29 and 39 through a suction line 32.and from the coil 3| through a suction line 33, both lines 32 and 33 discharging into an accumulator 34 from whence refrigerant vapor is sucked through pipe 35 back to the compressor.
Flow of liquid refrigerant through the liquid line 28 is controlled by an automatic valve 36 connected by pipes 31 and 38 with the accumulator and which operates responsive to liquid refrigerant level similar to valve H of Fig. 1. When the automatic valve 36 is open refrigerant flows past the expansion valve 39 into the bottom of the upper coil 29. The expansion valve 39 is preferably of the adjustable type similar to valve i9 of Fig. 1 and is capable of being manually set to permit expansion from the high to the low side of the system. I Y
The accumulator 34 is provided with a partition 40 which divides the accumulator into chambers 4| and 42, the automatic valve 36 being adapted to close when the liquid level in the chamber 4| reached a predetermined height. On the low side of the system adjacent the valve 39 is located an electrically operated valve 43 controlled by a thermostat 44 from a thermostat bulb 45.
Refrigerant gas and entrained liquids are withdrawn from the evaporator 29 through pipe 32 to chamber 4| of the accumulator where liquid and gas are separated, the gaseous refrigerant being sucked through pipe 35 to the compressor and the liquid refrigerant draining by gravity through pipe 46 into the bottom of the second or intermediate evaporator coil 39 from which refrigerant vapor and entrained liquid are drawn through pipe 32 into the accumulator.
The baffle 40 in the accumulator terminates near the bottom of the accumulator and refrigerant in the chamber 4| fiows past the baflie into Liquid refrigerant from the chamber 42 flows downwardly through pipe 41" into the bottom of the evaporator coil 3| from which gaseous refrigerant and any. entrained liquid is carried through the pipe 33 into the chamber 42 of the accumulator. Vapor from the chamber 42 of the accumulator is withdrawn through pipe 48 into the suction line 35 extending to the compressor.
A thermostatically operated valve 49 controls.
the suction of the refrigerant gas through the pipe 43 from the chamber 42 to the compressor 25, the valve 49 being controlled from any desired point in the circuit by a thermostat 59 having a bulb 5| in thermal contact with fluid or other substance being cooled and the thermostat being set to operate the valve-when the temperature drops below a predetermined value. It is to be 29, 30 and 3| without damage.
understood that other types of valves which can be operated in accordance with temperature conditions may be employed.
When the valve 49 is closed, due to heat absorption in the evaporator coil 3|, refrigerant in the coil 3| is evaporated which can no longer be returned to the compressor and therefore the pressure in the chamber 42 of the accumulator increases above the pressure in the chamber 4|. This causes liquid refrigerant to flow through the opening beneath the baiiie 40 from the chamber 42 into the chamber 4|. Since the pipe 41 projects upwardly into the chamber 42 of the accumulator slightly above the bottom of the same as shown, passage of liquid refrigerant from the chambe 42 into the chamber 4| will uncover the upper end of the pipe 41 and prevent further passage of liquid refrigerant into pipe 41 thereby cutting off the supply of liquid refrigerant to the coil 3|. As no further cooling will be accomplished in this coil the capacity of the system will be reduced. If the fluid being cooled by the coils 29, 39 and 3| rises in temperature due to insufiicient cooling, the valve 49 will reopen to permit equalization of refrigerating levels in chambers 4| and 42 of the accumulator and liquid refrigerant will again be supplied through the pipe 4'5 to refrigerating coil 3|.
When the valve 49 is closed, forcing liquid from chamber 42 of the accumulator into chamber 4| the liquid level in chamber-4| may rise sufliciently to close the valve 36 which will further reduce the capacity of the system. However this condition is only temporary for as soonlas the liquid level drops in chamber 4|, valve 36 will reopen, restoring the feeding of liquid refrigerant. If the temperature-of the liquid being cooled drops to a predetermined point, valve 43 will close cutting off the supply of refrigerant from the condenser to all of the coils until such time as the temperature of the fluid being cooled, rises to open the valve 43. Upon a still further rise in temperature the valve 49 will be reopened causing coil 3| also to be put into operation.
Expansion valve 39 similarly to expansion valve i9 in Fig. 1 above, is set to supply refrigerant sufficient or somewhat in excess of that required to be evaporated in all the coils of the cooler and therefore a mixture of gaseous and liquid refrigerants is withdrawn from each of the coils Gaseous refrigerant and entrained liquid withdrawn from the coils 29 and 30 is separated in chamber M of the accumulator, the gaseous refrigerant passing to the suction line and the liquid refrigerant draining down to the line 46. The gaseous refrigerant with entrained liquid withdrawn from the coil 3| is discharged into chamber 42 of the accumulator, the gaseous refrigerant passing through pipe 48 into suction line 35 and the liq-' uid refrigerant draining through pipe 41. If an excess of liquid refrigerant is fed through the valve 39 the level of liquid refrigerant will rise in the accumulator 34 until the valve 36 closes, shutting off the supply. Thereafter liquid refrigerant passing from the accumulator through pipes 46 and 41 will pagtially evaporate due to heat absorption and the level in the accumulator since no liquid is flowing in will be reduced, until the liquid level in the accumulator has decreased sufiiciently to cause the opening up of valve 36.
The valves 43 and 49 may be controlled from different points suchas points 45 and 5| so that a combination of their location and temperaturesetting will cause the desired results or if desired the more logical method is to control both these two valves from the outlet temperatures of the liquid being cooled. Thermostats which control these valves are preferably set at slightly difierent temperature levels.
It will be obvious to those skilled in the art that various other changes may be made in the construction and arrangement of parts without departing from the spirit of the invention and therefore the invention is not limited to what is shown on the drawing and described in the specification but only as indicated in the appended claims.
I claim:
1. A method of refrigeration comprising supplying liquid refrigerant, evaporating a portion of said liquid refrigerant, withdrawing the vaporous and entrained liquid from the place of evaporation, separating liquid from the vapor, evaporating a portion of the separated liquid, withdrawing the vaporous and entrained liquid from the second place of evaporation, separating liquid from the vapor, equalizing the liquid level between the two separated liquids, and utilizing part of the entrained liquid from the second separation for a subsequent evaporation.
2. A method of refrigeration comprising supplying liquid refrigerant, evaporating a portion of said liquid refrigerant, withdrawing the vaporous and entrained liquid from the place of evaporation, separating liquid from the vapor, evaporating a portion of the separated liquid, withdrawing the vaporous and entrained liquid from the second place of evaporation, separating liquid from the vapor, equalizing the liquid level between the separated liquids, utilizing part of the entrainedliquid from the second separation for a subsequent evaporation and utilizing liquid refrigerant from the second separation to out off the supply for the final evaporation.
3. In a refrigerating system comprising an evaporator formed of a plurality of sections and an accumulator having a plurality of sections for separating entrained liquid refrigerant from gaseous refrigerant, means for supplying liquid refrigerant to one section of the evaporator, means for returning some of the separated liquid to another section of the evaporator, equalizing the liquid level between two sections of the accumulator, and means for cutting off one section of the evaporator.
4. A refrigerating system comprising an evapotor having a plurality of sections and an accumulator having at least two sections, means for supplying liquid refrigerant to one of said evaporator sections in excess of the amount that may be evaporated therein, separating the excess liquid from the gaseous refrigerant drawn from the evaporator in one section of the accumulator, returning a portion of the separatedliquid to another section of the evaporator, equalizing the liquid level between the sections of the accumulator, and feeding part of the liquid from the'second section of the accumulator to a third evaporator section.
5. A refrigerating system comprising an evaporator having a plurality of sections and an accumulator having at least two sections, means for supplying liquid refrigerant to one of said evaporator sections in excess of the amount that may be evaporated therein, separating the excess liquid from the gaseous refrigerant drawn from the evaporator in one section of the accumulator, returning a portion of the separated liquid to another section of the evaporator, equalizing the liquid level between the sections of the accumulator, feeding part of the liquid from the second section of the accumulator to a third evaporator section, and means for forcing liquid refrigerant from the second section of the accumulator in a manner to cut off the liquid supply to the third section of the evaporator.
6. A refrigerating system .of connected elements including an evaporator composed of sections,an accumulator,means for supplying refrig-' 'erant deposited in the accumulator from one evaporator section into another evaporator section, means responsive to accumulator liquid level for altering the refrigerant supplied to the evaporator, and means between said last mentioned means and an evaporator section for restricting the refrigerant supply thereto.
'7. A refrigerating system of connected elements including an evaporator formed of sections, an accumulator for trapping out liquid entrained with gaseous refrigerant as it is drawn from the evaporator, means for supplying refrigerant deposited in the accumulator into an evaporator section, means responsive to accumulator liquid level for altering the refrigerant supply to the evaporator, and means between said last mentioned means and an evaporator section for restricting the refrigerant supply.
8. The method of refrigeration comprising the stages of supplying refrigerant to a first place of evaporation, evaporating a portion of said refrigerant, passing evaporated refrigerant and entrained liquid refrigerant to a place of separation, separating the liquid refrigerant from the' gaseous refrigerant, passing said separated liquid refrigerant to a second place of evaporation, con,- trolling the supply of refrigerant to the first place of evaporation in accordance with the quantity of refrigerant fluid passed from the first place of evaporation, and further restricting said supply to the first place of evaporation to thereby maintain a. supply of refrigerant in both places of evaporation.
9. A refrigerating system of connected elements including an evaporator composed of sections, an accumulator, means for supplying refrigerant deposited in the accumulator from one evaporator section into another evaporator section, means for altering the refrigerant supplied to the evaporator, responsive to an excess of refrigerant supplied thereto, and means between said last mentioned means and an evaporator section for restricting the refrigerant supply thereto.
10. A refrigerating system of connected elements including an evaporator formed of sections, means for supplying'refrigerant to a first evaporator section, means for supplying refrigerant from said first evaporator section to a second evaporator section, a valve for shutting off the supply of refrigerant to the first evaporator section responsive to an excess of refrigerant supplied thereto, and a second valve between the first valve and the first evaporator section for restricting the supply of refrigerant.
W'IILIAM R.
US19084A 1935-04-30 1935-04-30 Refrigerant feed control Expired - Lifetime US2032287A (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2947798A (en) * 1957-08-20 1960-08-02 Gen Electric Cooling arrangement for electric apparatus
US3470707A (en) * 1968-02-12 1969-10-07 Andrew F Lofgreen Refrigeration system
US4233818A (en) * 1978-06-23 1980-11-18 Lastinger William R Heat exchange interface apparatus

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2947798A (en) * 1957-08-20 1960-08-02 Gen Electric Cooling arrangement for electric apparatus
US3470707A (en) * 1968-02-12 1969-10-07 Andrew F Lofgreen Refrigeration system
US4233818A (en) * 1978-06-23 1980-11-18 Lastinger William R Heat exchange interface apparatus

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