US3695050A - Liquid propellant storage tank - Google Patents
Liquid propellant storage tank Download PDFInfo
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- US3695050A US3695050A US37072A US3695050DA US3695050A US 3695050 A US3695050 A US 3695050A US 37072 A US37072 A US 37072A US 3695050D A US3695050D A US 3695050DA US 3695050 A US3695050 A US 3695050A
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- storage tank
- control chamber
- gas
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- low thermal
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C3/00—Vessels not under pressure
- F17C3/02—Vessels not under pressure with provision for thermal insulation
- F17C3/10—Vessels not under pressure with provision for thermal insulation by liquid-circulating or vapour-circulating jackets
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C3/00—Vessels not under pressure
- F17C3/02—Vessels not under pressure with provision for thermal insulation
- F17C3/04—Vessels not under pressure with provision for thermal insulation by insulating layers
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2203/00—Vessel construction, in particular walls or details thereof
- F17C2203/03—Thermal insulations
- F17C2203/0304—Thermal insulations by solid means
- F17C2203/0308—Radiation shield
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2203/00—Vessel construction, in particular walls or details thereof
- F17C2203/03—Thermal insulations
- F17C2203/0304—Thermal insulations by solid means
- F17C2203/0308—Radiation shield
- F17C2203/032—Multi-sheet layers
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2203/00—Vessel construction, in particular walls or details thereof
- F17C2203/03—Thermal insulations
- F17C2203/0304—Thermal insulations by solid means
- F17C2203/0329—Foam
- F17C2203/0333—Polyurethane
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2203/00—Vessel construction, in particular walls or details thereof
- F17C2203/03—Thermal insulations
- F17C2203/0375—Thermal insulations by gas
- F17C2203/0379—Inert
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2203/00—Vessel construction, in particular walls or details thereof
- F17C2203/03—Thermal insulations
- F17C2203/0391—Thermal insulations by vacuum
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2203/00—Vessel construction, in particular walls or details thereof
- F17C2203/06—Materials for walls or layers thereof; Properties or structures of walls or their materials
- F17C2203/068—Special properties of materials for vessel walls
- F17C2203/0685—Special properties of materials for vessel walls flexible
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2221/00—Handled fluid, in particular type of fluid
- F17C2221/01—Pure fluids
- F17C2221/011—Oxygen
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2221/00—Handled fluid, in particular type of fluid
- F17C2221/01—Pure fluids
- F17C2221/012—Hydrogen
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2221/00—Handled fluid, in particular type of fluid
- F17C2221/01—Pure fluids
- F17C2221/014—Nitrogen
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2221/00—Handled fluid, in particular type of fluid
- F17C2221/03—Mixtures
- F17C2221/032—Hydrocarbons
- F17C2221/033—Methane, e.g. natural gas, CNG, LNG, GNL, GNC, PLNG
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2223/00—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel
- F17C2223/01—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel characterised by the phase
- F17C2223/0146—Two-phase
- F17C2223/0153—Liquefied gas, e.g. LPG, GPL
- F17C2223/0161—Liquefied gas, e.g. LPG, GPL cryogenic, e.g. LNG, GNL, PLNG
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2223/00—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel
- F17C2223/03—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel characterised by the pressure level
- F17C2223/033—Small pressure, e.g. for liquefied gas
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2227/00—Transfer of fluids, i.e. method or means for transferring the fluid; Heat exchange with the fluid
- F17C2227/04—Methods for emptying or filling
- F17C2227/044—Methods for emptying or filling by purging
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2260/00—Purposes of gas storage and gas handling
- F17C2260/01—Improving mechanical properties or manufacturing
- F17C2260/012—Reducing weight
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2270/00—Applications
- F17C2270/01—Applications for fluid transport or storage
- F17C2270/0186—Applications for fluid transport or storage in the air or in space
- F17C2270/0194—Applications for fluid transport or storage in the air or in space for use under microgravity conditions, e.g. space
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/32—Hydrogen storage
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S220/00—Receptacles
- Y10S220/901—Liquified gas content, cryogenic
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S220/00—Receptacles
- Y10S220/902—Foam
Definitions
- the F REON diffuses out of the closed cells of the polyurethane foam and is subsequently replaced with air which has a gaseous thermal conductivity approximately twice that of F REON. This replacement process starts immediately on formation of the foam. The longer the foam is held in storage, the larger the percentage of air and the smaller the percentage of FREON becomes, with the attendant increase in thermal conductivity.
- FIG. 1 is a cryogenic storage tank constructed in accordance with the principles of the present invention.
- FIG. 2 is another embodiment of the storage tank with a multilayer radiation shield surrounding the cryogenic storage tank.
- the cryogenic storage container 10 shown in FIGS. 1 and 2 has an inner wall 12 surrounded by a FREON expanded polyurethane foam 14 to reduce the transfer of heat by convection to the inner wall 12 from an environmental source.
- a single layer of metalized material 13 such as MYLAR is wrapped on the external surface of the foam layer to reduce the absorption of radiation in the outer surface of the foam.
- a plastic flexible membrane or bag 16 encases the foam covered inner wall 12 forming a control chamber 18.
- the plastic membrance 16 has a suitable control valve 21 for regulating fluid through inlet port 22 to control chamber 18 and a suitable outlet valve 24 adjacent port 26, attached to purging means 28 for evacuating control chamber 18 in response to an operator command.
- control chamber 18 is maintained during storage after curing under a low thermal conductive gas atmosphere having relatively high liquidus and solidus temperatures.
- control chamber 18 has been evacuated of air by purge means 28, either FREON or carbon dioxide gas is supplied to the control chamber 18 through control valve 21 which will retain the FREON expanded foam in an inert condition.
- the permeation or diffusion coefficient for CO of the FREON expanded polyurethane foam should be between that for FREON and that for air, that is greater than that for FREON but less than that for air. In this way the foam will always have FREON or a mixture of FREON and carbon dioxide contained in its cells. Thus, the thermal conductivity of the foam will be maintained relatively as low as when first formed and its degradation with time should be eliminated.
- the low thermal conductive gas is removed from control chamber 18 by purging means 28.
- Helium gas is now scheduled through control valve 21 to the control chamber 18.
- both valves 21 and 24 should be closed trapping a slight positive pressure, above atmospheric, of helium gas in the control chamber 18.
- the helium gas will not condense into a liquid or a solid at the charging temperature of the cryogen as would either the FREON or carbon dioxide gas and being dry, it will prevent the formation of frost due to the presence of water vapor in the atmosphere.
- the thermal conductivity of helium is approximately to l 1 times that of either FREON or carbon dioxide.
- the thermal conductivity of the mixture of carbon dioxide or FREON and helium will be only slightly more than that of the carbon dioxide and FREON either alone or as a mixture of the two. As the temperature in the foam falls to the liquification or solidification point of either FREON or carbon dioxide their vapor pressure is reduced and consequently the contribution to gaseous conduction from this source is also reduced.
- multi-layer radiation shields 34 are wrapped around the FREON expanded polyurethane foam.
- the multi-layer radiation shields have a reflective metallic material plated 36 on a backing member such as MYLAR 38.
- a storage unit comprising:
- foam insulating member surrounding said vessel, said foam insulating member having gaseous cells formed by a low thermal conductive gas for reducing the transfer of heat to said vessel by gaseous convection;
- a plastic bag encasing said foam insulating member forming a control chamber around said vessel, said bag having an inlet port and an outlet port;
- control means regulating the flow of said low thermal conductive gas having a relatively high liquidus and solidus temperature, through said inlet port to said air evacuated control chamber for preventing diffusion of said low thermal gas from said cells after curing during the storage period prior to said charging of the vessel.
- a storage unit as recited in claim 1, wherein said evacuating means purges said control chamber of said low thermal conductive gas and said control means regulates the flow of helium to said control chamber in response to an operator signal for preventing condensation of the low thermal conductivity gas and water vapor on the outer surface of said vessel during charging of said vessel with said liquid propellant.
- a storage unit as recited in claim 2, including:
- a reflective metallic material plated on a backing member to form a radiation shield said radiation shield being wrapped on the outer surface of said foam insulating member for reducing the transfer of heat to said vessel by radiation from an environmental source.
- a method of reducing the transfer of heat between and external surface of a cryogenic storage tank and the environment comprising the steps of:
- means for reducing the transfer of heat to the external surface of a storage tank comprising:
- purging means operatively connected to said inlet port and said outlet port for removing air from said control chamber and for introducing a gas to said control chamber having a relatively low thermal conductivity as compared to that of air and having high liquidus and solidus temperatures relative to the usual cryogens for maintaining said FREON expanded polyurethane in an inert condition.
- purging means replaces said gas in said control chamber with helium prior to charging said storage tank with cryogen for preventing consensation of water vapor or purge gas on the outside of said storage tank.
- cryogenic storage system as defined in claim 6, including:
- cryogenic storage system as defined in claim 7, including:
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- Engineering & Computer Science (AREA)
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- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Filling Or Discharging Of Gas Storage Vessels (AREA)
Abstract
A multi-layer insulated tank for storing a liquid propellant. A tank is coated with a low thermal conductive gas expanded foam. The foam coated tank is encased in a plastic bag and is maintained under a low thermal conductive gas until just before the tank is charged with the liquid propellant. Just prior to charging the tank with cryogen, the low thermal conductive gas is replaced by helium or nitrogen depending upon the cryogen to prevent condensation of water vapor and/or purge gas on the outer surface of the tank.
Description
United States Patent Bancroft [54] LIQUID PROPELLANT STORAGE TANK [72] Inventor: George H. Bancroft, Davenport,
Iowa
[73] Assignee: The Bendix Corporation [22] Filed: May 14, 1970 [21] Appl. No.: 37,072
[ 51 Oct. 3, 1972 11/1961 Match ..220/9 LG l/l962 Hnilicka, Jr. ..220/10 Primary Examiner-William F. ODea Assistant ExaminerRonald C. Capossela Attorney-William N. Antonis and Flame, Hartz, Smith and Thompson ABSTRACT 8 Claims, 2 Draiving Figures 521 U.S.,Cl. ..62/45, 220/9 LG, 200/9 F 51 Int. Cl. ..F17c 13/00 581 Field of Search ..62/45, 54,61 1; 220/9 L/G, 220/10, 9 F
[56] References Cited UNITED STATES PATENTS 3,321,159 5/1967 Jackson ..62/45 X 3,170,310 2/1965 Croneld ..62/DIG. 13
PUEGING NEH/VS 2 s 70 fl/E L f SUPPLY PATENTED w 3 I972 PURGING NEHNS FIG.
pueanvs r NEH/V5 28 T0 FUEL INVENTOR FIG. 2 BY PM,
ATTORNEY LIQUID PROPELLANT STORAGE TANK BACKGROUND OF THE INVENTION other. In the case of space boosters and particularly for large storage tanks, the second tank wall represents a large weight penalty on the payload of the booster. Once the tank reaches space, even with a single walled tank, the vacuum is no problem since it is the atmosphere of space thereby eliminating the transfer of heat by conduction. However, in space the transfer of heat by radiation affects the cryogens in the storage tank. In order to reduce the transfer of heat by radiation which is not affected by the gas pressure in the annulus between the double tanks, discreet radiation shields or multi-layer insulation is introduced into the annular space.
However, during the filling process and holding time on the ground, an uninsulated tank would experience high heat transfer and consequent loss of fluid due not only to the gaseous conduction and radiation, but also a very substantial heat loss from the action of gaseous convection. To reduce the heat loss from such gaseous convection in large liquid propellant storage tanks used in space boosters for the storage, primarily of cryogens such as liquid oxygen, liquid hydrogen and liquid methane, foam insulation is used as one member of the insulation system. It has been observed that initially following the curing period, the thermal conductivity of a FREON expanded foam is lower than after standing for a few months exposed to air. It has been proposed that, the F REON diffuses out of the closed cells of the polyurethane foam and is subsequently replaced with air which has a gaseous thermal conductivity approximately twice that of F REON. This replacement process starts immediately on formation of the foam. The longer the foam is held in storage, the larger the percentage of air and the smaller the percentage of FREON becomes, with the attendant increase in thermal conductivity.
SUMMARY OF THE INVENTION The transfer of heat by gaseous convection to the storage tank will be the greatest at the surface of the earth. In my invention, I place a plastic membrance around the FREON expanded foam coated storage tank to form a control chamber therein. By maintaining a low thermal conductive gas which has relatively high liquidus and solidus temperatures in the control chamber during storage of the tank after fabrication,
the maximum effectiveness of the foam coating in reducing heat loss will be obtained.
In addition by using a plastic membrance as the second tank wall, a substantial reduction in weight of the storage tank will be produced. Once the storage tank reaches space, the plastic membrane can be jetisoned or destroyed since the atmosphere of space is a vacuum.
It is therefore an object of this invention to provide a means forreducing thermal conduction between a storage tank and an environmental source.
BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a cryogenic storage tank constructed in accordance with the principles of the present invention.
FIG. 2 is another embodiment of the storage tank with a multilayer radiation shield surrounding the cryogenic storage tank.
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS In the drawings, like members represent the same element in each embodiment.
The cryogenic storage container 10 shown in FIGS. 1 and 2 has an inner wall 12 surrounded by a FREON expanded polyurethane foam 14 to reduce the transfer of heat by convection to the inner wall 12 from an environmental source. A single layer of metalized material 13 such as MYLAR is wrapped on the external surface of the foam layer to reduce the absorption of radiation in the outer surface of the foam. A plastic flexible membrane or bag 16 encases the foam covered inner wall 12 forming a control chamber 18. The plastic membrance 16 has a suitable control valve 21 for regulating fluid through inlet port 22 to control chamber 18 and a suitable outlet valve 24 adjacent port 26, attached to purging means 28 for evacuating control chamber 18 in response to an operator command.
To obtain the maximum effectiveness of the FREON expanded polyurethane foam, the control chamber 18 is maintained during storage after curing under a low thermal conductive gas atmosphere having relatively high liquidus and solidus temperatures. After control chamber 18 has been evacuated of air by purge means 28, either FREON or carbon dioxide gas is supplied to the control chamber 18 through control valve 21 which will retain the FREON expanded foam in an inert condition.
This is because carbon dioxide has approximately the same gaseous thermal conductivity as the FREON which is of the order of 0.005 BTU per hour per sq. ft. per degree rankine while air has a thermal conductivity approximately 0.0100 twice that of FREON or CO On the basis of molecular size, the permeation or diffusion coefficient for CO of the FREON expanded polyurethane foam should be between that for FREON and that for air, that is greater than that for FREON but less than that for air. In this way the foam will always have FREON or a mixture of FREON and carbon dioxide contained in its cells. Thus, the thermal conductivity of the foam will be maintained relatively as low as when first formed and its degradation with time should be eliminated.
Upon charging chamber 30 with a cryogen through connecting means 32 having a valve 20 controlled by an operator, the low thermal conductive gas is removed from control chamber 18 by purging means 28. Helium gas is now scheduled through control valve 21 to the control chamber 18. Just prior to launch both valves 21 and 24 should be closed trapping a slight positive pressure, above atmospheric, of helium gas in the control chamber 18. The helium gas will not condense into a liquid or a solid at the charging temperature of the cryogen as would either the FREON or carbon dioxide gas and being dry, it will prevent the formation of frost due to the presence of water vapor in the atmosphere. The thermal conductivity of helium is approximately to l 1 times that of either FREON or carbon dioxide. Although after an extended period of time, the helium will diffuse into the foam, during the normal hold time, the build-up of the partial pressure of helium in the foam cells would be expected to be negligibly small, much less than a small fraction of one atmosphere. The thermal conductivity of the mixture of carbon dioxide or FREON and helium will be only slightly more than that of the carbon dioxide and FREON either alone or as a mixture of the two. As the temperature in the foam falls to the liquification or solidification point of either FREON or carbon dioxide their vapor pressure is reduced and consequently the contribution to gaseous conduction from this source is also reduced.
When the foam insulated tank is projected into space, the primary heat transfer is through radiation. To reduce the effect of radiation from an environmental source, multi-layer radiation shields 34 (see FIG. 2) are wrapped around the FREON expanded polyurethane foam. The multi-layer radiation shields have a reflective metallic material plated 36 on a backing member such as MYLAR 38.
Since a slightly positive pressure of helium was established in the control chamber 18 on the ground, once the storage tank has been projected into space, the helium gas will expand causing the plastic membrance to rupture due to the increased differential pressure. Upon rupturing, the foam covered storage tank will then be in the absolute vacuum of space wherein the transfer of heat by convection is eliminated and the multi-layer radiation shield 34 is the primary source of thermal energy control.
Iclaim:
l. A storage unit, comprising:
a vessel;
means for charging said vessel with a liquid propellant;
a foam insulating member surrounding said vessel, said foam insulating member having gaseous cells formed by a low thermal conductive gas for reducing the transfer of heat to said vessel by gaseous convection;
a plastic bag encasing said foam insulating member forming a control chamber around said vessel, said bag having an inlet port and an outlet port;
evacuation means connected to said outlet port for removing the air from said control chamber; and
control means regulating the flow of said low thermal conductive gas having a relatively high liquidus and solidus temperature, through said inlet port to said air evacuated control chamber for preventing diffusion of said low thermal gas from said cells after curing during the storage period prior to said charging of the vessel.
2. A storage unit, as recited in claim 1, wherein said evacuating means purges said control chamber of said low thermal conductive gas and said control means regulates the flow of helium to said control chamber in response to an operator signal for preventing condensation of the low thermal conductivity gas and water vapor on the outer surface of said vessel during charging of said vessel with said liquid propellant.
3. A storage unit, as recited in claim 2, including:
a reflective metallic material plated on a backing member to form a radiation shield, said radiation shield being wrapped on the outer surface of said foam insulating member for reducing the transfer of heat to said vessel by radiation from an environmental source.
4. A method of reducing the transfer of heat between and external surface of a cryogenic storage tank and the environment, comprising the steps of:
coating said external surface with a FREON expanded polyurethane foam;
surrounding said surface with a membrance to form a control chamber therein;
purging said control chamber of air;
introducing a gas into said control chamber having a relatively low thermal conductivity and relatively high liquidus and solidus temperatures as compared to those of air for insulating said cryogenic storage tank;
wrapping said external surface of said layer of foam on the external surface of said storage tank with a reflective metallic material applied to a backing member to form an initial radiation shield; and
changing said gas to helium gas prior to charging said storage tank with a cryogen for preventing condensation of the said low thermal conductivity gas and water vapor on the outside of said storage tank.
5. In a cryogenic storage system, means for reducing the transfer of heat to the external surface of a storage tank, comprising:
a foam coating of FREON expanded polyurethane secured to the external surface of said storage tank;
a flexible membrance surrounding said coating having an inlet port and an outlet port, said flexible membrane and coating forming a control chamber therebetween; and
purging means operatively connected to said inlet port and said outlet port for removing air from said control chamber and for introducing a gas to said control chamber having a relatively low thermal conductivity as compared to that of air and having high liquidus and solidus temperatures relative to the usual cryogens for maintaining said FREON expanded polyurethane in an inert condition.
6. In a cryogenic storage system, as defined in claim 5, wherein purging means replaces said gas in said control chamber with helium prior to charging said storage tank with cryogen for preventing consensation of water vapor or purge gas on the outside of said storage tank.
7. In a cryogenic storage system, as defined in claim 6, including:
a reflective metallic material located on said external surface of the said foam coating to form an inner radiation shield.
8. In a cryogenic storage system, as defined in claim 7, including:
' a multi-layer insulation shield located on the outside of said foam coating to form an outer radiation shield around said storage tank. 5
Claims (7)
- 2. A storage unit, as recited in claim 1, wherein said evacuating means purges said control chamber of said low thermal conductive gas and said control means regulates the flow of helium to said control chamber in response to an operator signal for preventing condensation of the low thermal conductivity gas and water vapor on the outer surface of said vessel during charging of said vessel with said liquid propellant.
- 3. A storage unit, as recited in claim 2, including: a reflective metallic material plated on a backing member to form a radiation shield, said radiation shield being wrapped on the outer surface of said foam insulating member for reducing the transfer of heat to said vessel by radiation from an environmental source.
- 4. A method of reducing the transfer of heat between and external surface of a cryogenic storage tank and the environment, comprising the steps of: coating said external surface with a FREON expanded polyurethane foam; surrounding said surface with a membrance to form a control chamber therein; purging said control chamber of air; introducing a gas into said control chamber having a relatively low thermal conductivity and relatively high liquidus and solidus temperatures as compared to those of air for insulating said cryogenic storage tank; wrapping said external surface of said layer of foam on the external surface of said storage tank with a reflective metAllic material applied to a backing member to form an initial radiation shield; and changing said gas to helium gas prior to charging said storage tank with a cryogen for preventing condensation of the said low thermal conductivity gas and water vapor on the outside of said storage tank.
- 5. In a cryogenic storage system, means for reducing the transfer of heat to the external surface of a storage tank, comprising: a foam coating of FREON expanded polyurethane secured to the external surface of said storage tank; a flexible membrance surrounding said coating having an inlet port and an outlet port, said flexible membrane and coating forming a control chamber therebetween; and purging means operatively connected to said inlet port and said outlet port for removing air from said control chamber and for introducing a gas to said control chamber having a relatively low thermal conductivity as compared to that of air and having high liquidus and solidus temperatures relative to the usual cryogens for maintaining said FREON expanded polyurethane in an inert condition.
- 6. In a cryogenic storage system, as defined in claim 5, wherein purging means replaces said gas in said control chamber with helium prior to charging said storage tank with cryogen for preventing consensation of water vapor or purge gas on the outside of said storage tank.
- 7. In a cryogenic storage system, as defined in claim 6, including: a reflective metallic material located on said external surface of the said foam coating to form an inner radiation shield.
- 8. In a cryogenic storage system, as defined in claim 7, including: a multi-layer insulation shield located on the outside of said foam coating to form an outer radiation shield around said storage tank.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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US3707270A | 1970-05-14 | 1970-05-14 |
Publications (1)
Publication Number | Publication Date |
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US3695050A true US3695050A (en) | 1972-10-03 |
Family
ID=21892286
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US37072A Expired - Lifetime US3695050A (en) | 1970-05-14 | 1970-05-14 | Liquid propellant storage tank |
Country Status (1)
Country | Link |
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US (1) | US3695050A (en) |
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US4498304A (en) * | 1982-08-03 | 1985-02-12 | Gaz De France | Storage tank for cryogenic liquefied gas |
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US6398057B1 (en) * | 1998-01-28 | 2002-06-04 | Xerxes Corporation | Triple walled underground storage tank |
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US20050269333A1 (en) * | 2004-06-04 | 2005-12-08 | Ti Group Automotive Systems, L.L.C. | Fuel tank and method for reducing vapor permeation through a fuel tank |
US20080048047A1 (en) * | 2006-08-28 | 2008-02-28 | Air Products And Chemicals, Inc. | Cryogenic Nozzle |
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US20100187237A1 (en) * | 2008-09-23 | 2010-07-29 | Alec Nelson Brooks | Cryogenic Liquid Tank |
CN104279421A (en) * | 2014-09-29 | 2015-01-14 | 中国海洋石油总公司 | Nitrogen displacement system for LNG (Liquefied Natural Gas) storage tank |
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GB2584443A (en) * | 2019-06-03 | 2020-12-09 | Linde Kryotechnik Ag | Vacuum insulated equipment |
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US3984994A (en) * | 1972-12-05 | 1976-10-12 | Messer Griesheim Gmbh | Process and device for filling multilayer pressure containers |
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US7810669B2 (en) * | 2004-03-05 | 2010-10-12 | Airbus Deutschland Gmbh | Replaceable cartridge for liquid hydrogen |
US20050224514A1 (en) * | 2004-03-05 | 2005-10-13 | Airbus Deutschland Gmbh | Replaceable cartridge for liquid hydrogen |
US20110041307A1 (en) * | 2004-03-05 | 2011-02-24 | Airbus Deutschland Gmbh | Replaceable cartridge for liquid hydrogen |
US20050269333A1 (en) * | 2004-06-04 | 2005-12-08 | Ti Group Automotive Systems, L.L.C. | Fuel tank and method for reducing vapor permeation through a fuel tank |
US8381928B2 (en) * | 2004-06-04 | 2013-02-26 | Ti Group Automotive Systems, L.L.C. | Multilayer fuel tank with a seam having an overlay for reducing vapor permeation |
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US9200356B2 (en) | 2006-08-28 | 2015-12-01 | Air Products And Chemicals, Inc. | Apparatus and method for regulating cryogenic spraying |
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US20100275620A1 (en) * | 2007-08-28 | 2010-11-04 | Air Products And Chemicals, Inc. | Apparatus and method for providing condensation- and frost-free surfaces on cryogenic components |
WO2009032688A1 (en) * | 2007-08-28 | 2009-03-12 | Air Products And Chemicals, Inc. | Apparatus and method for providing condensation-and frost-free surfaces on cryogenic components |
US11346501B2 (en) | 2008-09-23 | 2022-05-31 | Aerovironment, Inc. | Cryogenic liquid tank |
US8960482B2 (en) | 2008-09-23 | 2015-02-24 | Aerovironment Inc. | Cryogenic liquid tank |
US20100187237A1 (en) * | 2008-09-23 | 2010-07-29 | Alec Nelson Brooks | Cryogenic Liquid Tank |
US9829155B2 (en) | 2008-09-23 | 2017-11-28 | Aerovironment, Inc. | Cryogenic liquid tank |
US10584828B2 (en) | 2008-09-23 | 2020-03-10 | Aerovironment, Inc. | Cryogenic liquid tank |
WO2016022334A1 (en) * | 2014-08-04 | 2016-02-11 | Washington State University | Vapor cooled shielding liner for cryogenic storage in composite pressure vessels |
CN104279421A (en) * | 2014-09-29 | 2015-01-14 | 中国海洋石油总公司 | Nitrogen displacement system for LNG (Liquefied Natural Gas) storage tank |
GB2584443A (en) * | 2019-06-03 | 2020-12-09 | Linde Kryotechnik Ag | Vacuum insulated equipment |
WO2023198843A1 (en) * | 2022-04-15 | 2023-10-19 | Gaztransport Et Technigaz | Leaktight and thermally insulating vessel, and associated method for placing under vacuum |
FR3134616A1 (en) * | 2022-04-15 | 2023-10-20 | Gaztransport Et Technigaz | Waterproof and thermally insulating tank and associated vacuum process |
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Owner name: LITTON SYSTEMS, INC., 360 N. CRESCENT DRIVE, BEVER Free format text: ASSIGNMENT OF ASSIGNORS INTEREST.;ASSIGNOR:BENDIX CORPORATION THE;REEL/FRAME:004076/0866 Effective date: 19821129 |