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US3750414A - Cryogenic device for cooling objects - Google Patents

Cryogenic device for cooling objects Download PDF

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Publication number
US3750414A
US3750414A US00181111A US3750414DA US3750414A US 3750414 A US3750414 A US 3750414A US 00181111 A US00181111 A US 00181111A US 3750414D A US3750414D A US 3750414DA US 3750414 A US3750414 A US 3750414A
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chamber
cryogenic
passage
valve
liquid
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US00181111A
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G Heftman
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Rank Organization Ltd
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Rank Organization Ltd
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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
    • F25DREFRIGERATORS; COLD ROOMS; ICE-BOXES; COOLING OR FREEZING APPARATUS NOT OTHERWISE PROVIDED FOR
    • F25D3/00Devices using other cold materials; Devices using cold-storage bodies
    • F25D3/10Devices using other cold materials; Devices using cold-storage bodies using liquefied gases, e.g. liquid air

Definitions

  • FIG. 1 of the accompanying drawings incorporates a closed liquid gas storage vessel 1, a closed cryogenic chamber 2 arranged to contain an article 3 to be cooled, a transfer passage 4 leading from near the bottom of the storage vessel 1 into the cryogenic chamber 2, a liquid level sensitive devices in the cryogenic chamber 2 constituted by a float valve 5 operative to close an exhaust passage 6 at a given level of liquid in the chamber, and a heat sink 7 in heat-exchanging relationship with the transfer passage 4.
  • 8 denotes a quantity of a cryogenic liquid in the vessel 1.
  • the storage vessel 1 is fitted with a pressure relief valve 9 set to open automatically at a predetermined pressure.
  • a quantity of a cryogenic liquid for example liquid nitrogen
  • a cryogenic liquid for example liquid nitrogen
  • the liquid absorbs heat from the surroundings and begins to boil so that the space in the vessel above the liquid becomes filled with gas.
  • the gas pressure in the vessel l rises until it reaches the pressure at which the relief valve 9 is set to open whereupon the pressure in the vessel 1 remains constant.
  • the pressure on the surface of the liquid 8 forces liquid to rise of the transfer passage 4 and to enter the heat sink 7. Here some of the liquid in the passage 4 boils.
  • gas produced in the transfer passage 4 at the heat sink 7 by boiling of liquid in the transfer passage 4 carries with it droplets of liquid into the cryogenic chamber 2 where the droplets combine to produce a liquid content in the cryogenic chamber 2.
  • the liquid level in the chamber 2 rises until the float valve 5 operates to'close the exhaust passage 6 whereupon the pressure rises in the chamber 2 until it becomes high enough to stop the further movement of liquid through the transfer passage 4.
  • a drop in liquid level in the chamber 2 causes the float valve 5 to open the exhaust passage 6 whereupon the pressure in the chamber 2 is released.
  • the pressure in the vessel 1 thereupon forces more liquid into the chamber 2. By this mechanism the liquid in the chamber 2 is maintained at the desired level while there is liquid in the vessel 1.
  • the described Liedenfrost system suffers from the disadvantage that water gradually accumulates in the chamber 2 and in sufficient quantity can impair the efficiency and effectiveness of operation of the system and even cause the chamber 2 to break by freezing therein.
  • the water is deposited by liquid gas coming over from the vessel 1.
  • the water becomes mixed with the stored liquid principally by condensing therein from the atmosphere while the storage vessel 1 is being filled.
  • there may not be a great deal of water present in each filling of the vessel 1 all the water in successive fillings of the vessel 1 is transferred-to the chamber 2 and accumulates there.
  • a cryogenic device of the type described incorporates a by-pass passage one end of which terminates in the upper part of the vessel at a point above the normal level of liquid in the vessel and the other end of which terminates at the transfer passage, and a shut-off valve intercalated in the by-pass passage.
  • the vessel is closed by a lid incorporating a plug through which the transfer passage passes, the plug being fitted with heat-absorbing tins and functioning as the heat sink.
  • the plug may incorporate the pressure relief valve, the by-pass passage and the shutoff valve.
  • the by-pass passage may be consitituted by an extenral pipe in which the shut-off valve is fitted.
  • FIG. 2 of the accompanying drawings A practical embodiment of the invention is illustrated in FIG. 2 of the accompanying drawings in which the parts already illustrated in FIG. I are indicated by the same reference numerals.
  • 10 denotes a by-pass passage connected at one end into the upper part of the vessel by way of the heat sink 7 and at the other end into the transfer passage 4.
  • 11 denotes a shut-off valve intercalated in the by-pass passage 10.
  • the shut-off valve 11 is closed and cryogenic liquid is transferred from the vessel 1 to the chamber 2 at the required rate in the manner described in connection with the known device of FIG. I.
  • the device is put outof action by opening the valve 11. This has the effect of equalizing the pressure in the vessel 1 and the transfer passage 4 and liquid is then no longer tranferred from the vessel 1 to the chamber 2.
  • the liquid level in the chamber 2 soon drops and the float valve 5 opens the exhaust passage 6. Because the valve 11 is now open gas from the upper part of the vessel ll now flows into the chamber 2 and out through the exhaust passage 6. This gas is completely dry because any water present in the vessel 1 is in condensed form in the liquid because of the low temperature of the liquid.
  • the dry gas flowing through the chamber 2 evaporates any water therein and carries the water vapour away-with it as it escapes through the exhaust pipe 6.
  • the water content of the chamber 2 is thus reduced or completely removed by the time the device is next brought into service by closing the valve ll.
  • Preferably enough liquid is put into the vessel 1 to last a period of 24 hours which includes the normal periot! in service with the remainder of the 24 hours being the drying period during which gas from the vessel 1 flows through the chamber 2.
  • a cryogenic device comprising a closed gas storage vessel for holding a supply of liquefied gas beneath a layer of gas in the gaseous state, a closed cryogenic chamber, a transfer passage leading into said cryogenic chamber from a point near the bottom of said storage vessel covered by said liquefied gas during normal operation of said device, an exhaust passage leading from the cryogenic chamber, a liquid level sensitive device in the cryogenic chamber operative to close the exhaust passage when a predetermined liquid level in said through which the transfer passage passes, the plug being arranged to function as the heat sink and incorporating a pressure relief valve, and the by-pass passage with the shut-off valve.

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Physics & Mathematics (AREA)
  • Mechanical Engineering (AREA)
  • Thermal Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Filling Or Discharging Of Gas Storage Vessels (AREA)

Abstract

A cryogenic device incorporates a liquid storage vessel from near the bottom of which a transfer passage leads to a closed cryogenic chamber having an exhaust passage closable by a liquid level sensitive device in the closed chamber. A heat sink is in heat-exchanging relation with the transfer passage. A by-pass pipe in which a shut-off valve is intercalated connects the upper part of the liquid storage vessel to the transfer passage.

Description

United States Patent [1 1 [111 3,750,414 Heftman [4 1 Aug. 7, 1973 1 CRYOGENIC DEVICE FOR COOLING 3,418,822 12/1968 Massey 62/52 OBJECTS 3,126,711 3/1964 Miller 62/52 [75] Inventor: George Hettman, Hatch End,
England [73] Assignee: The Rank Organization Limited,
London, England [22] Filed: Sept. 16, 1971 [2!] Appl. No.: 181,111
[30] Foreign Application Priority Data Sept. 16, 1970 Great Britain 44,106/70 [52] US. Cl. 62/55, 62/514 [51] Int. Cl. Fl7c 7/02 [58] Field of Search 62/514, 50, 52, 54, 62/55 [56] References Cited UNITED STATES PATENTS 3,440,829 4/1969 Davis-White 62/55 FOREIGN PATENTS OR APPLICATIONS 929,795 1/1960 Great Britain 62/52 Primary Examiner-Meyer Perlin Assistant Examiner-Paul Devinsky Attorney-Holcombe, Wetherill & Brisebois [57] ABSTRACT A cryogenic device incorporates a liquid storage vessel from near the bottom of which a transfer passage leads to a closed cryogenic chamber having an exhaust passage closable by a liquid level sensitive device in the closed chamber. A heat sink is in heat-exchanging relation with the transfer passage. A by-pass pipe in which a shut-off valve is intercalated connects the upper part of the liquid storage vessel to the transfer passage.
3 Claims, 2 Drawing Figures PATENTEUAUB H973 SHEET 1 BF 2 PAIENTEWn H975 SHEEI 2 BF 2 1 CRYOGENIC DEVICE FOR COOLING OBJECTS This invention relates to cryogenic devices and particularly to devices for cooling instruments which perform best at very low temperatures. As an example it may be remarked that infrared detectors for certain purposes require to be cooled to the temperature of liquid notrogen.
Such a known device referred to as a Liedenfrost system and illustrated diagrammatically in FIG. 1 of the accompanying drawings incorporates a closed liquid gas storage vessel 1, a closed cryogenic chamber 2 arranged to contain an article 3 to be cooled, a transfer passage 4 leading from near the bottom of the storage vessel 1 into the cryogenic chamber 2, a liquid level sensitive devices in the cryogenic chamber 2 constituted by a float valve 5 operative to close an exhaust passage 6 at a given level of liquid in the chamber, and a heat sink 7 in heat-exchanging relationship with the transfer passage 4. 8 denotes a quantity of a cryogenic liquid in the vessel 1. Usually the storage vessel 1 is fitted with a pressure relief valve 9 set to open automatically at a predetermined pressure.
In operation of the Liedenfrost system as described and illustrated a quantity of a cryogenic liquid, for example liquid nitrogen, is put into the storage vessel. The liquid absorbs heat from the surroundings and begins to boil so that the space in the vessel above the liquid becomes filled with gas. The gas pressure in the vessel l rises until it reaches the pressure at which the relief valve 9 is set to open whereupon the pressure in the vessel 1 remains constant. The pressure on the surface of the liquid 8 forces liquid to rise of the transfer passage 4 and to enter the heat sink 7. Here some of the liquid in the passage 4 boils. With a properly chosen setting of the relief valve 9, the correct setting being determined mainly by the dimensions of the storage vessel 1 and the transfer pipe 4 and the ambient temperature, gas produced in the transfer passage 4 at the heat sink 7 by boiling of liquid in the transfer passage 4 carries with it droplets of liquid into the cryogenic chamber 2 where the droplets combine to produce a liquid content in the cryogenic chamber 2. The liquid level in the chamber 2 rises until the float valve 5 operates to'close the exhaust passage 6 whereupon the pressure rises in the chamber 2 until it becomes high enough to stop the further movement of liquid through the transfer passage 4. A drop in liquid level in the chamber 2 causes the float valve 5 to open the exhaust passage 6 whereupon the pressure in the chamber 2 is released. The pressure in the vessel 1 thereupon forces more liquid into the chamber 2. By this mechanism the liquid in the chamber 2 is maintained at the desired level while there is liquid in the vessel 1.
The described Liedenfrost system suffers from the disadvantage that water gradually accumulates in the chamber 2 and in sufficient quantity can impair the efficiency and effectiveness of operation of the system and even cause the chamber 2 to break by freezing therein. The water is deposited by liquid gas coming over from the vessel 1. The water becomes mixed with the stored liquid principally by condensing therein from the atmosphere while the storage vessel 1 is being filled. Although there may not be a great deal of water present in each filling of the vessel 1 all the water in successive fillings of the vessel 1 is transferred-to the chamber 2 and accumulates there.
It is an object of the present invention to provide an improved device which is arranged to operate on the Liedenfrost principle but which is free from the trouble of water accumulation in the cryogenic vessel.
According to the invention a cryogenic device of the type described incorporates a by-pass passage one end of which terminates in the upper part of the vessel at a point above the normal level of liquid in the vessel and the other end of which terminates at the transfer passage, and a shut-off valve intercalated in the by-pass passage.
Conveniently the vessel is closed by a lid incorporating a plug through which the transfer passage passes, the plug being fitted with heat-absorbing tins and functioning as the heat sink. The plug may incorporate the pressure relief valve, the by-pass passage and the shutoff valve.
Alternatively the by-pass passage may be consitituted by an extenral pipe in which the shut-off valve is fitted.
A practical embodiment of the invention is illustrated in FIG. 2 of the accompanying drawings in which the parts already illustrated in FIG. I are indicated by the same reference numerals.
In FIG. 2, 10 denotes a by-pass passage connected at one end into the upper part of the vessel by way of the heat sink 7 and at the other end into the transfer passage 4. 11 denotes a shut-off valve intercalated in the by-pass passage 10.
In normal operation of the device according to the invention the shut-off valve 11 is closed and cryogenic liquid is transferred from the vessel 1 to the chamber 2 at the required rate in the manner described in connection with the known device of FIG. I. At the end of each period of use the device is put outof action by opening the valve 11. This has the effect of equalizing the pressure in the vessel 1 and the transfer passage 4 and liquid is then no longer tranferred from the vessel 1 to the chamber 2. The liquid level in the chamber 2 soon drops and the float valve 5 opens the exhaust passage 6. Because the valve 11 is now open gas from the upper part of the vessel ll now flows into the chamber 2 and out through the exhaust passage 6. This gas is completely dry because any water present in the vessel 1 is in condensed form in the liquid because of the low temperature of the liquid. The dry gas flowing through the chamber 2 evaporates any water therein and carries the water vapour away-with it as it escapes through the exhaust pipe 6. The water content of the chamber 2 is thus reduced or completely removed by the time the device is next brought into service by closing the valve ll.
Preferably enough liquid is put into the vessel 1 to last a period of 24 hours which includes the normal periot! in service with the remainder of the 24 hours being the drying period during which gas from the vessel 1 flows through the chamber 2.
What is claimed is:
1. In a cryogenic device comprising a closed gas storage vessel for holding a supply of liquefied gas beneath a layer of gas in the gaseous state, a closed cryogenic chamber, a transfer passage leading into said cryogenic chamber from a point near the bottom of said storage vessel covered by said liquefied gas during normal operation of said device, an exhaust passage leading from the cryogenic chamber, a liquid level sensitive device in the cryogenic chamber operative to close the exhaust passage when a predetermined liquid level in said through which the transfer passage passes, the plug being arranged to function as the heat sink and incorporating a pressure relief valve, and the by-pass passage with the shut-off valve.
3. A device as claimed in claim 1 in which the by-pass passage is constituted by an external pipe in which the shut-off valve is fitted.
i i i i l

Claims (3)

1. In a cryogenic device comprising a closed gas storage vessel for holding a supply of liquefied gas beneath a layer of gas in the gaseous state, a closed cryogenic chamber, a transfer passage leading into said cryogenic chamber from a point near the bottom of said storage vessel covered by said liquefied gas during normal operation of said device, an exhaust passage leading from the cryogenic chamber, a liquid level sensitive device in the cryogenic chamber operative to close the exhaust passage when a predetermined liquid level in said chamber is attained, and a heat sink in heat-exchanging relationship with the transfer passage, the improvement which comprises a by-pasS passage leading to said transfer passage from a point in the upper part of said vessel which is located above said supply of liquefied gas during normal operation of said device, and a shut-off valve in said by-pass passage.
2. A device as claimed in claim 1 in which the liquid gas storage vessel is closed by a lid incorporating a plug through which the transfer passage passes, the plug being arranged to function as the heat sink and incorporating a pressure relief valve, and the by-pass passage with the shut-off valve.
3. A device as claimed in claim 1 in which the by-pass passage is constituted by an external pipe in which the shut-off valve is fitted.
US00181111A 1970-09-16 1971-09-16 Cryogenic device for cooling objects Expired - Lifetime US3750414A (en)

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Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3878690A (en) * 1972-05-30 1975-04-22 Barr & Stroud Ltd Liquid transfer system
US4726194A (en) * 1985-12-05 1988-02-23 Fern Developments Limited Transfer system
US5373701A (en) * 1993-07-07 1994-12-20 The Boc Group, Inc. Cryogenic station
US5488831A (en) * 1994-10-06 1996-02-06 Griswold; Thomas A. Liquid cryogen withdrawal device
US20140111806A1 (en) * 2012-10-22 2014-04-24 Korea Institute Of Geoscience And Mineral Resources Apparatus for monitoring hot waste water discharged from power plant by using airborne multispectral scanner system
WO2019046707A1 (en) * 2017-08-31 2019-03-07 Savsu Technologies Llc Cryogenic storage container closure

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2538516A1 (en) * 1982-12-28 1984-06-29 Commissariat Energie Atomique METHOD AND APPARATUS FOR LOWING TEMPERATURE OF A DEVICE, IN PARTICULAR ABOUT 4K

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB929795A (en) * 1960-01-29 1963-06-26 British Oxygen Co Ltd Bulk storage and supply tank for liquefied gases
US3126711A (en) * 1960-04-29 1964-03-31 E miller
US3418822A (en) * 1967-06-27 1968-12-31 Firewel Company Inc Apparatus for transporting a stream of cryogenic liquified gas
US3440829A (en) * 1963-12-11 1969-04-29 Lab For Electronics Inc Liquified gas delivery system

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB929795A (en) * 1960-01-29 1963-06-26 British Oxygen Co Ltd Bulk storage and supply tank for liquefied gases
US3126711A (en) * 1960-04-29 1964-03-31 E miller
US3440829A (en) * 1963-12-11 1969-04-29 Lab For Electronics Inc Liquified gas delivery system
US3418822A (en) * 1967-06-27 1968-12-31 Firewel Company Inc Apparatus for transporting a stream of cryogenic liquified gas

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3878690A (en) * 1972-05-30 1975-04-22 Barr & Stroud Ltd Liquid transfer system
US4726194A (en) * 1985-12-05 1988-02-23 Fern Developments Limited Transfer system
US5373701A (en) * 1993-07-07 1994-12-20 The Boc Group, Inc. Cryogenic station
US5488831A (en) * 1994-10-06 1996-02-06 Griswold; Thomas A. Liquid cryogen withdrawal device
US20140111806A1 (en) * 2012-10-22 2014-04-24 Korea Institute Of Geoscience And Mineral Resources Apparatus for monitoring hot waste water discharged from power plant by using airborne multispectral scanner system
US9335166B2 (en) * 2012-10-22 2016-05-10 Korea Institute Of Geoscience And Mineral Resources Apparatus for monitoring hot waste water discharged from power plant by using airborne multispectral scanner system
WO2019046707A1 (en) * 2017-08-31 2019-03-07 Savsu Technologies Llc Cryogenic storage container closure
CN111480030A (en) * 2017-08-31 2020-07-31 萨瓦苏科技有限公司 Cryogenic Storage Container Closures
US11892124B2 (en) 2017-08-31 2024-02-06 Savsu Technologies Llc Cryogenic storage container closure
US20240159364A1 (en) * 2017-08-31 2024-05-16 Savsu Technologies Llc Cryogenic storage container closure

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