US3750414A - Cryogenic device for cooling objects - Google Patents
Cryogenic device for cooling objects Download PDFInfo
- 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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- United States
- Prior art keywords
- chamber
- cryogenic
- passage
- valve
- liquid
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- 238000001816 cooling Methods 0.000 title description 4
- 239000007788 liquid Substances 0.000 claims abstract description 41
- 239000007789 gas Substances 0.000 description 13
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 10
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 238000009825 accumulation Methods 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000007710 freezing Methods 0.000 description 1
- 230000008014 freezing Effects 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 230000008520 organization Effects 0.000 description 1
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25D—REFRIGERATORS; COLD ROOMS; ICE-BOXES; COOLING OR FREEZING APPARATUS NOT OTHERWISE PROVIDED FOR
- F25D3/00—Devices using other cold materials; Devices using cold-storage bodies
- F25D3/10—Devices 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.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| GB4410670 | 1970-09-16 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US3750414A true US3750414A (en) | 1973-08-07 |
Family
ID=10431817
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US00181111A Expired - Lifetime US3750414A (en) | 1970-09-16 | 1971-09-16 | Cryogenic device for cooling objects |
Country Status (2)
| Country | Link |
|---|---|
| US (1) | US3750414A (en) |
| GB (1) | GB1321675A (en) |
Cited By (6)
| 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)
| 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)
| 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 |
-
1970
- 1970-09-16 GB GB4410670A patent/GB1321675A/en not_active Expired
-
1971
- 1971-09-16 US US00181111A patent/US3750414A/en not_active Expired - Lifetime
Patent Citations (4)
| 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)
| 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 |
Also Published As
| Publication number | Publication date |
|---|---|
| GB1321675A (en) | 1973-06-27 |
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