US3727418A - Sub-aqueous storage of liquefied gases - Google Patents
Sub-aqueous storage of liquefied gases Download PDFInfo
- Publication number
- US3727418A US3727418A US00165234A US3727418DA US3727418A US 3727418 A US3727418 A US 3727418A US 00165234 A US00165234 A US 00165234A US 3727418D A US3727418D A US 3727418DA US 3727418 A US3727418 A US 3727418A
- Authority
- US
- United States
- Prior art keywords
- container
- lng
- balancing fluid
- water
- fluid
- 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
- 239000007789 gas Substances 0.000 title description 8
- 239000003949 liquefied natural gas Substances 0.000 claims abstract description 51
- 239000012530 fluid Substances 0.000 claims abstract description 50
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 44
- 239000012528 membrane Substances 0.000 claims description 18
- 238000000638 solvent extraction Methods 0.000 claims description 12
- QWTDNUCVQCZILF-UHFFFAOYSA-N isopentane Chemical compound CCC(C)C QWTDNUCVQCZILF-UHFFFAOYSA-N 0.000 claims description 10
- 239000007787 solid Substances 0.000 claims description 5
- 239000011810 insulating material Substances 0.000 claims description 4
- 239000011148 porous material Substances 0.000 claims description 4
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 20
- 239000003345 natural gas Substances 0.000 description 8
- 239000007788 liquid Substances 0.000 description 7
- 239000000463 material Substances 0.000 description 6
- 239000006261 foam material Substances 0.000 description 4
- 238000004891 communication Methods 0.000 description 3
- 238000001816 cooling Methods 0.000 description 3
- 238000007710 freezing Methods 0.000 description 3
- 230000008014 freezing Effects 0.000 description 3
- 238000007906 compression Methods 0.000 description 2
- 230000006835 compression Effects 0.000 description 2
- AFABGHUZZDYHJO-UHFFFAOYSA-N dimethyl butane Natural products CCCC(C)C AFABGHUZZDYHJO-UHFFFAOYSA-N 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000003628 erosive effect Effects 0.000 description 2
- 239000006260 foam Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- 229920005830 Polyurethane Foam Polymers 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 239000001273 butane Substances 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 229920001971 elastomer Polymers 0.000 description 1
- -1 ethyl butane Chemical compound 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 238000005065 mining Methods 0.000 description 1
- OFBQJSOFQDEBGM-UHFFFAOYSA-N n-pentane Natural products CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- 239000011496 polyurethane foam Substances 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 230000002441 reversible effect Effects 0.000 description 1
- 239000011435 rock Substances 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
Images
Classifications
-
- 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
- F17C3/005—Underground or underwater containers or vessels
-
- 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
- F17C2201/00—Vessel construction, in particular geometry, arrangement or size
- F17C2201/01—Shape
- F17C2201/0128—Shape spherical or elliptical
-
- 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
- F17C2201/00—Vessel construction, in particular geometry, arrangement or size
- F17C2201/01—Shape
- F17C2201/0176—Shape variable
- F17C2201/0185—Shape variable with separating membrane
-
- 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
-
- 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
- F17C2203/0602—Wall structures; Special features thereof
- F17C2203/0612—Wall structures
- F17C2203/0614—Single wall
- F17C2203/0619—Single wall with two layers
-
- 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
- F17C2203/0602—Wall structures; Special features thereof
- F17C2203/0612—Wall structures
- F17C2203/0626—Multiple walls
- F17C2203/0629—Two walls
-
- 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
- F17C2205/00—Vessel construction, in particular mounting arrangements, attachments or identifications means
- F17C2205/01—Mounting arrangements
- F17C2205/0123—Mounting arrangements characterised by number of vessels
- F17C2205/013—Two or more vessels
-
- 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
-
- 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
-
- 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
-
- 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
- F17C2227/01—Propulsion of the fluid
- F17C2227/0128—Propulsion of the fluid with pumps or compressors
- F17C2227/0135—Pumps
-
- 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
- F17C2265/00—Effects achieved by gas storage or gas handling
- F17C2265/03—Treating the boil-off
- F17C2265/032—Treating the boil-off by recovery
- F17C2265/033—Treating the boil-off by recovery with cooling
- F17C2265/034—Treating the boil-off by recovery with cooling with condensing the gas phase
-
- 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
- F17C2270/0102—Applications for fluid transport or storage on or in the water
- F17C2270/0118—Offshore
- F17C2270/0128—Storage in depth
Definitions
- ABSTRACT Liquefied natural gas is stored under water in a submerged, jacketed container the interior of which is coupled to a balancing fluid in another container, the balancing fluid being in turn coupled to the water surrounding both containers.
- the containers are fastened together, and the assembly is ballasted as appropriate, or required.
- This invention relates to the storage and/or transportation of liquefied gases under water, and more particularly to an arrangement for the sub-aqueous storage of liquefied natural gas (LNG).
- LNG liquefied natural gas
- a recent development for providing underground-storage capacity for natural gas involves freezing the earth and subsequent mining, to form underground caverns.
- this technique is quite expensive, and requires scarce and valuable real estate.
- the present invention discloses the sub-aqueous storage of LNG, and has several advantages over the dry land method of storage previously mentioned.
- a large amount of unused water space is available, it being noted that there are quantities of water areas located near most large centers of population.
- water space or areas are low in cost, and may be obtained perhaps even more inexpensively by simply excavating cheap swamp land.
- water space is relatively free from safety limitations, which is to say that water space inherently provides for safety in the case of any failures such as leaks, etc.
- An object of this invention is to provide a novel apparatus for storage of liquefied gases, such as LNG.
- Another object is to provide an apparatus for the sub-aqueous storage of liquefied gases.
- a storage arrangement for liquefied gases comprises a jacketed inner container secured to another container and containing the liquefied gas (product) to be stored.
- a suitable balancing fluid is contained in the second container and is coupled to the product stored in the first container.
- the entire arrangement or assembly is submerged in water, and the balancing fluid is coupled to the surrounding water.
- the assembly is ballasted, as required.
- FIG. 1 is a view in vertical section of a storage arrangement according to this invention.
- FIG. 2 is a top or plan view of the arrangement of the invention, on a smaller scale.
- a metallic inner container l which may be spherical in shape as illustrated, serves as the container for the product (LNG) which is to be stored and/or transported under water.
- a flexible, impervious separator member or membrane 2 is sealed at its edges to the inner wall of container 1, in a horizontal diametrical plane thereof.
- Member 2 is flexible and durable enough, and of sufficient size (area) to conform to the inner wall of container 1, as the relative quantities of the two liquids separated by this member vary. In FIG. 1, this member 2 is illustrated in an approximate mid-position in container 1.
- Membrane 2 is preferably made from a sheet material which can withstand cryogenic or near-cryogenic temperatures.
- the connector 4 serves as a means whereby LNG (or in some cases, vaporized or gaseous natural gas) may be pumped into or out of container 1.
- Container 5 which may have the shape of a hollow prism (see FIG. 2), is fastened securely by any suitable means (not shown) to container 1.
- Container 5, for example, has a circular opening in its upper wall in which the jacket 3 sealingly fits.
- a pipe or connector 6 extends through jacket 3 at the lower portion of container 1, to provide fluid communication between the lower portion of container 1 and the interior of container 5.
- the connectors 4 and 6 communicate with container 1 on respective opposite sides of separatormember 2.
- a flexible, impervious separator member or membrane 7 (made of the same material as membrane 2, for example) is sealed at its edges to the inner wall of container 5, near the upper end thereof.
- the connector 6, it will be noted, is coupled at its lower end to the portion of container 5 above the separator member or partition member 7.
- a connector 8 which extends through one of the side walls of container 5, below the point of attachment of member 7 to this container, provides fluid communication between the surrounding water and the interior of container 5, below member 7.
- water 9 fills the space in container 5, below membrane 7.
- the upper end of connector or pipe 4 extends to a suitable pump (not shown), for pumping LNG into, and for removing LNG from, container 1.
- the LNG 10 is stored in container 1, above the membrane 2. Since methane, the principal constituent of natural gas, has a boiling point of about -lC., the storage of natural gas in liquefied form (particularly if stored at atmospheric pressure) involves very low temperature or cryogenic storage.
- the membrane 2 couples the LNG 10 to a quantity of a balancing fluid 11 which is contained between the two separator members 2 and 7 and which is adapted to flow into and out of container 1 (as dictated by the volume of fluid 10 in container 1), by way of connector 6.
- the quantity of fluid 1 l is sufficient to fill the entire volume of container 1, if necessary, and the separator member 7 is of sufficient size to follow the balancing fluid 11 as it moves into and out of container 1.
- the membrane 7 couples the balancing fluid l 1 to the water 9. Since the membranes 2 and 7 are both flexible, and both physically separate the respective adjacent pairs of liquids with no voids or air spaces, there is zero pressure gradient across each of these membranes, so they can be made from a relatively thin sheet material (film).
- the balancing fluid 1 1 should be a liquid which does not freeze at the temperature of the LNG,'which provides a negative buoyancy as compared to the LNG (that is, one which has a density greater than that of the LNG), and which has a density somewhat similar to those of hydrocarbon fluids.
- a liquid which has these characteristics is Z-m'ethyl butane, also known as isopentane, or ethyldimethylrnethane (density 621 grams per liter, as compared to the densities of liquid methane, 0.415 grams per liter, and of water, 1,000v
- LNG 10 may be pumped through connector 4 to the container 1, causing the balancing fluid 1 1 to be displaced to'the container 5 through connector 6, and displacing water 9 from container 5 through connector 8.
- the action just described takes place by way of the flexible impervious membranes 2 and 7.
- the reverse action takes place when LNG is pumped out of container 1.
- the volume of balancing fluid l 1 remains constant, but the volumes of LNG 10 and water 9 in the storage arrangement of this invention vary, depending upon the volume of LNG being stored at any particular moment.
- the flexible members 2 and 7 follow the movements of the liquids, as required by conditions.
- Suitable cooling equipment should be coupled to connector 4 to chill any natural gas that gasifies in the container 1. Such equipment is commonly used in apparatus for handling LNG.
- the connector 4 thusprovides for the removal of vaporized natural gas, for subsequent return.
- ballast 12 in the form of gravel, rock, or even sand, as appropriate,
- the insulating jacket 3 preferably comprises a porous solid insulating material (e.g., polyurethane foam) through the pores of which water may penetrate when the apparatus issubmerged.
- a porous solid insulating material e.g., polyurethane foam
- the ice strengthens the foam material to a certain extent, but more importantly, it provides additional heat insulation.
- the thickness of the jacket 3 is preferably greater than that required for a temperature reduction from the LNG temperature to the freezing point of water. For example, if a 6-foot thickness of foam or sponge material were required to reduce the temperature from the LNG temperature to the freezing point of water, then a total thickness of say 10 ft. of foam material could be utilized at 3.
- the water pressure existing at the depth whereat the assembly is submerged is applied both to the outside and inside of the container (the application to the inside being by way of the balancing fluid l 1).
- the flexible impervious membrane 7 may .not be required in some cases, except for ecological purposes or to preserve the environment; if membrane 7 is not used, the different densities of water. 9 and of the isopentane 11 may be relied upon to provide the required separation of these two fluids.
- the container 5 does not necessarily need to have a solid bottom, as illustrated, except possibly for the prevention of impacts, etc.
- a sub-aqueous storage arrangement for liquefied natural gas (LNG), comprising a first closed submersible container, means for transferring LNG to and from the interior of said container, a second submersible container secured to said first container, means providing a fluid connection between said containers, a body of a balancing fluid in said second container and adapted to flow into and out of said first container through said fluid connection, a partitioning means between the LNG in said first container and said balancing fluid, and a partitioning means between the balancing fluid in said second container and the water surrounding both of said containers.
- LNG liquefied natural gas
- first-mentioned partitioning means comprises a flexible impervious membrane mounted in said first container and physically separating said LNG from said balancing fluid.
- the second-mentioned partitioning means comprises a flexible impervious membrane mounted in said second container and physically separating said balancing fluid from said water.
- means comprises a flexible impervious member mounted in said second container and physically separating said balancing fluid from said water.
- balancing fluid is 2-methyl butane.
- jacket comprises a porous solid insulating material containing frozen water in its pores.
- a sub-aqueous storage arrangement for liquefied natural gas (LNG), comprising a first closed submersible container, means for transferring LNG to and from the interior of said container, a second submersible container secured to said first container, means providing a fluid connection between said containers, a body of a balancing fluid in said second container and adapted to flow into and out of said first container through said fluid connection, and a partitioning means between the LNG in said first container and said balancing fluid, the upper portion of said second container being secured to and sealed to said first container but the lower portion of said second container communicating with the water surrounding both of said containers.
- LNG liquefied natural gas
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Filling Or Discharging Of Gas Storage Vessels (AREA)
Abstract
Liquefied natural gas is stored under water in a submerged, jacketed container the interior of which is coupled to a balancing fluid in another container, the balancing fluid being in turn coupled to the water surrounding both containers. The containers are fastened together, and the assembly is ballasted as appropriate, or required.
Description
United States Patent [1 1 Glazier [n1 3,727,418 51 A r. 17,1973
[ SUB-AQUEOUS STORAGE OF LIQUEFIED GASES [75] Inventor: Frederick P. Glazier, Thornton, Pa.
[73] Assignee: Sun Oil Company of Pennsylvania,
Philadelphia, Pa.
[22] Filed: July 22, 1971 [21] Appl. No.: 165,234
[52] US. Cl. ..62/45, 61/05, 220/9 LG, 220/18 [51] Int. Cl. ..F17c l/00 [58] Field of Search ..62/45; 220/9 LG, 220/18; 61/05, 46; 114/05 T, 74 A; 222/3865 [56] References Cited UNITED STATES PATENTS 2,798,633 7/ 1957 Cornell et al. ..220/ 18 X 2,924,350 2/1960 Greer ..220/ l 8 X 3,396,544 8/1968 3,471,349 10/ 1969 3,518,836 7/1970 8/1971 Primary Examinefi-Meyer Perlin Assistant ExaminerRona1d C. Capossela Att0rney-George L. Church et al.
[ ABSTRACT Liquefied natural gas is stored under water in a submerged, jacketed container the interior of which is coupled to a balancing fluid in another container, the balancing fluid being in turn coupled to the water surrounding both containers. The containers are fastened together, and the assembly is ballasted as appropriate, or required.
11 Claims, 2 Drawing Figures PATENTH] AFR 1 THIS mm H Z A -A L m P. K a w D E m 2 & m 4 F y Y a elllllIlIlllllIllllll. J
SUB-AQUEOUS STORAGE OF LIQUEFIED GASES This invention relates to the storage and/or transportation of liquefied gases under water, and more particularly to an arrangement for the sub-aqueous storage of liquefied natural gas (LNG).
A need for storage facilities for natural gas exists, near the major areas of distribution (which is to say, near the major markets which exist in large metropolitan and industrial areas in the north, northeastern, Gulf Coast, and Pacific Coast regions of the United States). A recent development for providing underground-storage capacity for natural gas involves freezing the earth and subsequent mining, to form underground caverns. However, this technique is quite expensive, and requires scarce and valuable real estate.
The present invention discloses the sub-aqueous storage of LNG, and has several advantages over the dry land method of storage previously mentioned. In the first place, a large amount of unused water space is available, it being noted that there are quantities of water areas located near most large centers of population. In the next place, such water space or areas are low in cost, and may be obtained perhaps even more inexpensively by simply excavating cheap swamp land. Furthermore, water space is relatively free from safety limitations, which is to say that water space inherently provides for safety in the case of any failures such as leaks, etc.
An object of this invention is to provide a novel apparatus for storage of liquefied gases, such as LNG.
Another object is to provide an apparatus for the sub-aqueous storage of liquefied gases.
A further objectis to provide an apparatus which may be used for the underwater transportation of LNG.
A still further object'is to provide an apparatus which will accomplish the above objects in an efficient, effective, and rather inexpensive manner.
The objects of this invention are accomplished, briefly, in the following manner: A storage arrangement for liquefied gases comprises a jacketed inner container secured to another container and containing the liquefied gas (product) to be stored. A suitable balancing fluid is contained in the second container and is coupled to the product stored in the first container. The entire arrangement or assembly is submerged in water, and the balancing fluid is coupled to the surrounding water. The assembly is ballasted, as required.
A detailed description of the invention follows, taken in conjunction with the accompanying drawing, wherein:
FIG. 1 is a view in vertical section of a storage arrangement according to this invention; and
FIG. 2 is a top or plan view of the arrangement of the invention, on a smaller scale.
Referring -now to the drawing, a metallic inner container l, which may be spherical in shape as illustrated, serves as the container for the product (LNG) which is to be stored and/or transported under water. A flexible, impervious separator member or membrane 2 is sealed at its edges to the inner wall of container 1, in a horizontal diametrical plane thereof. Member 2 is flexible and durable enough, and of sufficient size (area) to conform to the inner wall of container 1, as the relative quantities of the two liquids separated by this member vary. In FIG. 1, this member 2 is illustrated in an approximate mid-position in container 1. Membrane 2 is preferably made from a sheet material which can withstand cryogenic or near-cryogenic temperatures.
A heat-insulating jacket 3, which will be described in more detail hereinafter, surrounds the container 1, and a pipe or connector 4 extends through this jacket into fluid communication (at its lower end) with the upper portion of container 1. The connector 4 serves as a means whereby LNG (or in some cases, vaporized or gaseous natural gas) may be pumped into or out of container 1.
Another container 5, which may have the shape of a hollow prism (see FIG. 2), is fastened securely by any suitable means (not shown) to container 1. Container 5, for example, has a circular opening in its upper wall in which the jacket 3 sealingly fits. A pipe or connector 6 extends through jacket 3 at the lower portion of container 1, to provide fluid communication between the lower portion of container 1 and the interior of container 5. The connectors 4 and 6 communicate with container 1 on respective opposite sides of separatormember 2.
A flexible, impervious separator member or membrane 7 (made of the same material as membrane 2, for example) is sealed at its edges to the inner wall of container 5, near the upper end thereof. The connector 6, it will be noted, is coupled at its lower end to the portion of container 5 above the separator member or partition member 7.
The two-container assembly of this invention, when in use, is entirely submerged in water. A connector 8, which extends through one of the side walls of container 5, below the point of attachment of member 7 to this container, provides fluid communication between the surrounding water and the interior of container 5, below member 7. Thus, when the assembly of the invention is in use (and is therefore submerged), water 9 fills the space in container 5, below membrane 7. I
The upper end of connector or pipe 4 extends to a suitable pump (not shown), for pumping LNG into, and for removing LNG from, container 1. The LNG 10 is stored in container 1, above the membrane 2. Since methane, the principal constituent of natural gas, has a boiling point of about -lC., the storage of natural gas in liquefied form (particularly if stored at atmospheric pressure) involves very low temperature or cryogenic storage.
The membrane 2 couples the LNG 10 to a quantity of a balancing fluid 11 which is contained between the two separator members 2 and 7 and which is adapted to flow into and out of container 1 (as dictated by the volume of fluid 10 in container 1), by way of connector 6. The quantity of fluid 1 l is sufficient to fill the entire volume of container 1, if necessary, and the separator member 7 is of sufficient size to follow the balancing fluid 11 as it moves into and out of container 1. The membrane 7 couples the balancing fluid l 1 to the water 9. Since the membranes 2 and 7 are both flexible, and both physically separate the respective adjacent pairs of liquids with no voids or air spaces, there is zero pressure gradient across each of these membranes, so they can be made from a relatively thin sheet material (film).
The balancing fluid 1 1 should be a liquid which does not freeze at the temperature of the LNG,'which provides a negative buoyancy as compared to the LNG (that is, one which has a density greater than that of the LNG), and which has a density somewhat similar to those of hydrocarbon fluids. A liquid which has these characteristics is Z-m'ethyl butane, also known as isopentane, or ethyldimethylrnethane (density 621 grams per liter, as compared to the densities of liquid methane, 0.415 grams per liter, and of water, 1,000v
grams per liter; melting point about 160C).
As an example, LNG 10 may be pumped through connector 4 to the container 1, causing the balancing fluid 1 1 to be displaced to'the container 5 through connector 6, and displacing water 9 from container 5 through connector 8. The action just described takes place by way of the flexible impervious membranes 2 and 7. The reverse action takes place when LNG is pumped out of container 1. Thus, .the volume of balancing fluid l 1 remains constant, but the volumes of LNG 10 and water 9 in the storage arrangement of this invention vary, depending upon the volume of LNG being stored at any particular moment. The flexible members 2 and 7 follow the movements of the liquids, as required by conditions.
It is desirable, for purposes of LNG. storage, that there be no ullage space in container 1, to avoid the extra buoyancy which such space could entail. Suitable cooling equipment should be coupled to connector 4 to chill any natural gas that gasifies in the container 1. Such equipment is commonly used in apparatus for handling LNG. The connector 4 thusprovides for the removal of vaporized natural gas, for subsequent return.
Although the balancing fluid 11 has a much higher density than that of the LNG, both it and the LNG have densities less than that of water, so that they themselves provide a positive buoyancy effect when submerged in water. The weight of the various containers does of course provide a negative buoyancy effect, but in order to make sure that the assembly remains safely submerged even when there is a maximum of LNG 10 (and a minimum of water 9) in the apparatus, ballast 12 (in the form of gravel, rock, or even sand), as appropriate,
' or as required, is provided in a compartment mounted at the periphery of container 5.
it will be appreciated that the apparatus described utilizes an essentially balanced pressure approach, which keeps compressive or tensile forces lowin fact, practically non-existent.
The insulating jacket 3 preferably comprises a porous solid insulating material (e.g., polyurethane foam) through the pores of which water may penetrate when the apparatus issubmerged. At the temperature of the LNG (about -1 60C.), this water freezes, resulting in frozen water (ice) intermixed with the resilient compressible foam type material. The ice strengthens the foam material to a certain extent, but more importantly, it provides additional heat insulation. The thickness of the jacket 3 is preferably greater than that required for a temperature reduction from the LNG temperature to the freezing point of water. For example, if a 6-foot thickness of foam or sponge material were required to reduce the temperature from the LNG temperature to the freezing point of water, then a total thickness of say 10 ft. of foam material could be utilized at 3. The extra 4 feet of foam material on the outside (beyond the 6 feet mentioned) would then prevent erosion of the ice by water action. Alternatively, instead of this extra thickness of foam material, a substantially impervious flexible skin (such as a rubber cover), with holes to permit the flow of water in either direction through the skin (but at much reduced veloci ties), could be added on the outside of the foam-ice jacket, to prevent erosion of the icy material.
It would be possible to utilize the two-container assembly previously described for the underwater transportation of LNG. For this, the connector 4 would be removed, and a controlled ullage space (operating through a cooling or compression cycle, as required) would be established in the top of container 1, to pro vide nearly zero buoyancy at all times. The transporting submarine and the weight of its equipment would be designed quite accurately to provide near zero buoyancy at all times. The difference in lift or buoyancy (as the volume of LNG in container'l varies) between the water and natural gas would need to be taken into account (the relative quantities of these two liquids in the assembly varying as the volume of LNG varies, the volume of balancing fluid remaining constant, as previously mentioned). By an arrangement of buoyant tanks, with cooling and compression equipment, a near zero buoyancy could be maintained for the LNG submarine.
the water pressure existing at the depth whereat the assembly is submerged is applied both to the outside and inside of the container (the application to the inside being by way of the balancing fluid l 1).
The flexible impervious membrane 7 may .not be required in some cases, except for ecological purposes or to preserve the environment; if membrane 7 is not used, the different densities of water. 9 and of the isopentane 11 may be relied upon to provide the required separation of these two fluids.
Also, the container 5 does not necessarily need to have a solid bottom, as illustrated, except possibly for the prevention of impacts, etc.
The invention claimed is:
l. A sub-aqueous storage arrangement for liquefied natural gas (LNG), comprising a first closed submersible container, means for transferring LNG to and from the interior of said container, a second submersible container secured to said first container, means providing a fluid connection between said containers, a body of a balancing fluid in said second container and adapted to flow into and out of said first container through said fluid connection, a partitioning means between the LNG in said first container and said balancing fluid, and a partitioning means between the balancing fluid in said second container and the water surrounding both of said containers. t
2. Arrangement according to claim 1, wherein the first-mentioned partitioning means comprises a flexible impervious membrane mounted in said first container and physically separating said LNG from said balancing fluid.
3. Arrangement according to claim 1, wherein the second-mentioned partitioning means comprises a flexible impervious membrane mounted in said second container and physically separating said balancing fluid from said water.
means comprises a flexible impervious member mounted in said second container and physically separating said balancing fluid from said water.
8. Arrangement defined in claim 7, wherein balancing fluid is 2-methyl butane.
9. Arrangement of claim 7, including also a heat-insulating jacket on said first container.
said
l0. Arrangement defined in claim 9, wherein said jacket comprises a porous solid insulating material containing frozen water in its pores.
11. A sub-aqueous storage arrangement for liquefied natural gas (LNG), comprising a first closed submersible container, means for transferring LNG to and from the interior of said container, a second submersible container secured to said first container, means providing a fluid connection between said containers, a body of a balancing fluid in said second container and adapted to flow into and out of said first container through said fluid connection, and a partitioning means between the LNG in said first container and said balancing fluid, the upper portion of said second container being secured to and sealed to said first container but the lower portion of said second container communicating with the water surrounding both of said containers. I
Claims (11)
1. A sub-aqueous storage arrangement for liquefied natural gas (LNG), comprising a first closed submersible container, means for transferring LNG to and from the interior of said container, a second submersible container secured to said first container, means providing a fluid connection between said containers, a body of a balancing fluid in said second container and adapted to flow into and out of said first container through said fluid connection, a partitioning means between the LNG in said first container and said balancing fluid, and a partitioning means between the balancing fluid in said second container and the water surrounding both of said containers.
2. Arrangement according to claim 1, wherein the first-mentioned partitioning means comprises a flexible impervious membrane mounted in said first container and physically separating said LNG from said balancing fluid.
3. Arrangement according to claim 1, wherein the second-mentioned partitioning means comprises a flexible impervious membrane mounted in said second container and physically separating said balancing fluid from said water.
4. Arrangement defined in claim 1, wherein said balancing fluid is 2-methyl butane.
5. Arrangement of claim 1, including also a heat-insulating jacket on said first container.
6. Arrangement defined in claim 5, wherein said jacket comprises a porous solid insulating material containing frozen water in its pores.
7. Arrangement according to claim 1, wherein the first-mentioned partitioning means comprises a flexible impervious membrane mounted in said first container and physically separating said LNG from said balancing fluid; and wherein the second-mentioned partitioning means comprises a flexible impervious member mounted in said second container and physically separating said balancing fluid from said water.
8. Arrangement defined in claim 7, wherein said balancing fluid is 2-methyl butane.
9. Arrangement of claim 7, including also a heat-insulating jacket on said first container.
10. Arrangement defined in claim 9, wherein said jacket comprises a porous solid insulating material containing frozen water in its pores.
11. A sub-aqueous storage arrangement for liquefied natural gas (LNG), comprising a first closed submersible container, means for transferring LNG to and from the interior of said container, a second submersible container secured to said first container, means providing a fluid connection between said containers, a body of a balancing fluid in said second container and adapted to flow into and out of said first container through said fluid connection, and a partitioning means between the LNG in said first container and said balancing fluid, the upper portion of said second container being secured to and sealed to said fiRst container but the lower portion of said second container communicating with the water surrounding both of said containers.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US16523471A | 1971-07-22 | 1971-07-22 |
Publications (1)
Publication Number | Publication Date |
---|---|
US3727418A true US3727418A (en) | 1973-04-17 |
Family
ID=22598031
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US00165234A Expired - Lifetime US3727418A (en) | 1971-07-22 | 1971-07-22 | Sub-aqueous storage of liquefied gases |
Country Status (1)
Country | Link |
---|---|
US (1) | US3727418A (en) |
Cited By (39)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3798919A (en) * | 1972-11-14 | 1974-03-26 | Us Navy | Deep submergence ambient pressure cryogenic storage apparatus |
US3828565A (en) * | 1973-02-16 | 1974-08-13 | Chicago Bridge & Iron Co | Offshore liquid storage facility |
US3898846A (en) * | 1974-02-19 | 1975-08-12 | Chicago Bridge & Iron Co | Offshore storage tank |
US3961488A (en) * | 1974-11-19 | 1976-06-08 | A/S Akers Mek. Verksted | Method for filling and emptying of cassions |
US3981701A (en) * | 1973-08-10 | 1976-09-21 | H.W. Andersen Products Inc. | Method and apparatus for controlling a volatile substance |
US4059065A (en) * | 1977-02-07 | 1977-11-22 | Mobil Oil Corporation | Semisubmersible loading mooring and storage facility |
US4068480A (en) * | 1975-11-13 | 1978-01-17 | Kenneth Winans Lefever | Liquid storage systems |
US4136997A (en) * | 1976-11-08 | 1979-01-30 | Chapman Marcus R | Floating wall oil container |
US4141377A (en) * | 1976-08-30 | 1979-02-27 | Brown & Root, Inc. | Underwater storage assembly |
US4190072A (en) * | 1976-08-30 | 1980-02-26 | Brown & Root, Inc. | Underwater storage assembly |
US4209271A (en) * | 1978-08-10 | 1980-06-24 | Chicago Bridge & Iron Company | Storage tank with liquid insulator for storing cryogenic fluids using water displacement |
US4232983A (en) * | 1978-12-07 | 1980-11-11 | Sidney F. Cook | Offshore submarine storage facility for highly chilled liquified gases |
US4302130A (en) * | 1978-03-30 | 1981-11-24 | Olav Mo | Gas platform |
US4365576A (en) * | 1980-07-21 | 1982-12-28 | Cook, Stolowitz And Frame | Offshore submarine storage facility for highly chilled liquified gases |
US4402632A (en) * | 1980-08-25 | 1983-09-06 | Cook, Stolowitz & Frame | Seabed supported submarine pressure transfer storage facility for liquified gases |
US4662386A (en) * | 1986-04-03 | 1987-05-05 | Sofec, Inc. | Subsea petroleum products storage system |
US5293751A (en) * | 1989-07-19 | 1994-03-15 | Mitsubishi Jukogyo Kabushiki Kaisha | Method and system for throwing carbon dioxide into the deep sea |
US5778679A (en) * | 1996-10-28 | 1998-07-14 | Amtrol Inc. | Method and apparatus for increasing acceptance and adjusting the rate of pressure variations within a prespecified range in precharged fluid storage systems |
US6260501B1 (en) * | 2000-03-17 | 2001-07-17 | Arthur Patrick Agnew | Submersible apparatus for transporting compressed gas |
US6490881B1 (en) * | 1998-07-14 | 2002-12-10 | Csir | Generating displacement and theroacoustic refrigerator |
US6718900B2 (en) | 2002-06-11 | 2004-04-13 | Gregory James Carter | Variable storage vessel and method |
US20050120723A1 (en) * | 2004-02-11 | 2005-06-09 | Mustang Engineering, L.P. | Methods and Apparatus For Processing, Transporting And/Or Storing Cryogenic Fluids |
NO320112B1 (en) * | 2002-10-23 | 2005-10-24 | Navion Asa | Seabed storage |
US20080041068A1 (en) * | 2006-08-19 | 2008-02-21 | Horton Edward E | Liquefied natural gas re-gasification and storage unit |
US20080041291A1 (en) * | 2006-08-19 | 2008-02-21 | Horton Edward E | Deep water gas storage system |
US20080083246A1 (en) * | 2006-10-06 | 2008-04-10 | Aker Kvaerner, Inc. | Gas Conditioning Method and Apparatus for the Recovery of LPG/NGL(C2+) From LNG |
US20080210305A1 (en) * | 2004-09-21 | 2008-09-04 | Aker Kvaerner, Inc. | Liquified Natural Gas Sump For a Gravity Based Structure |
WO2009133563A2 (en) * | 2008-05-01 | 2009-11-05 | Seagen Systems Ltd. | Underwater storage system |
US20110146803A1 (en) * | 2008-09-05 | 2011-06-23 | Zhirong Wu | Multifunctional offshore base with liquid displacement system |
US20120291688A1 (en) * | 2010-01-19 | 2012-11-22 | John Arthur Dawes | Subsea Pressure Compensation System |
US20120305411A1 (en) * | 2010-02-15 | 2012-12-06 | Ron Elazari-Volcani | Underwater energy storage system and power station powered therewith |
US20140341657A1 (en) * | 2013-04-06 | 2014-11-20 | Safe Marine Transfer, LLC | Large subsea package deployment methods and devices |
US20150020541A1 (en) * | 2013-07-18 | 2015-01-22 | S.G.B.D. Technologies Ltd. | Methods and systems for underwater gas pressurization and liquefaction |
US9045209B2 (en) | 2013-03-14 | 2015-06-02 | Sanko Tekstil Isletmeleri Sanayi Ve Ticaret A.S. | Active volume energy level large scale sub-sea energy fluids storage methods and apparatus for power generation and integration of renewable energy sources |
US9079639B2 (en) | 2013-04-06 | 2015-07-14 | Safe Marine Transfer, LLC | Large volume subsea chemical storage and metering system |
US9470365B1 (en) * | 2015-07-13 | 2016-10-18 | Chevron U.S.A. Inc. | Apparatus, methods, and systems for storing and managing liquids in an offshore environment |
US9540169B1 (en) * | 2015-01-13 | 2017-01-10 | Daniel A. Krohn | Subsea storage tank for bulk storage of fluids subsea |
US9664019B2 (en) | 2013-07-18 | 2017-05-30 | S.G.B.D. Technologies Ltd. | Underwater gas field development methods and systems |
US20200003365A1 (en) * | 2018-06-28 | 2020-01-02 | Toyota Jidosha Kabushiki Kaisha | Hydrogen gas compressing system and hydrogen gas compression method |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2798633A (en) * | 1954-03-02 | 1957-07-09 | Gulf Oil Corp | Storage apparatus |
US2924350A (en) * | 1957-04-23 | 1960-02-09 | David M Greer | Storage tanks for liquids |
US3396544A (en) * | 1966-11-07 | 1968-08-13 | Mobil Oil Corp | Storage tank fixed on the ocean bottom and method of installation |
US3471349A (en) * | 1966-09-06 | 1969-10-07 | Bendix Corp | Method of constructing a positive expulsion tank |
US3518836A (en) * | 1968-02-14 | 1970-07-07 | Hideo Itokawa | Underwater oil tank |
US3599590A (en) * | 1969-06-10 | 1971-08-17 | Jose Dominguez Rego | Floating oil-recovery sump |
-
1971
- 1971-07-22 US US00165234A patent/US3727418A/en not_active Expired - Lifetime
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2798633A (en) * | 1954-03-02 | 1957-07-09 | Gulf Oil Corp | Storage apparatus |
US2924350A (en) * | 1957-04-23 | 1960-02-09 | David M Greer | Storage tanks for liquids |
US3471349A (en) * | 1966-09-06 | 1969-10-07 | Bendix Corp | Method of constructing a positive expulsion tank |
US3396544A (en) * | 1966-11-07 | 1968-08-13 | Mobil Oil Corp | Storage tank fixed on the ocean bottom and method of installation |
US3518836A (en) * | 1968-02-14 | 1970-07-07 | Hideo Itokawa | Underwater oil tank |
US3599590A (en) * | 1969-06-10 | 1971-08-17 | Jose Dominguez Rego | Floating oil-recovery sump |
Cited By (58)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3798919A (en) * | 1972-11-14 | 1974-03-26 | Us Navy | Deep submergence ambient pressure cryogenic storage apparatus |
US3828565A (en) * | 1973-02-16 | 1974-08-13 | Chicago Bridge & Iron Co | Offshore liquid storage facility |
US3981701A (en) * | 1973-08-10 | 1976-09-21 | H.W. Andersen Products Inc. | Method and apparatus for controlling a volatile substance |
US3898846A (en) * | 1974-02-19 | 1975-08-12 | Chicago Bridge & Iron Co | Offshore storage tank |
US3961488A (en) * | 1974-11-19 | 1976-06-08 | A/S Akers Mek. Verksted | Method for filling and emptying of cassions |
US4068480A (en) * | 1975-11-13 | 1978-01-17 | Kenneth Winans Lefever | Liquid storage systems |
US4141377A (en) * | 1976-08-30 | 1979-02-27 | Brown & Root, Inc. | Underwater storage assembly |
US4190072A (en) * | 1976-08-30 | 1980-02-26 | Brown & Root, Inc. | Underwater storage assembly |
US4136997A (en) * | 1976-11-08 | 1979-01-30 | Chapman Marcus R | Floating wall oil container |
US4059065A (en) * | 1977-02-07 | 1977-11-22 | Mobil Oil Corporation | Semisubmersible loading mooring and storage facility |
US4302130A (en) * | 1978-03-30 | 1981-11-24 | Olav Mo | Gas platform |
US4209271A (en) * | 1978-08-10 | 1980-06-24 | Chicago Bridge & Iron Company | Storage tank with liquid insulator for storing cryogenic fluids using water displacement |
US4232983A (en) * | 1978-12-07 | 1980-11-11 | Sidney F. Cook | Offshore submarine storage facility for highly chilled liquified gases |
FR2478260A1 (en) * | 1978-12-07 | 1981-09-18 | Cook Sidney | UNDERWATER FACILITY FOR WIDE-RANGE STORAGE FOR HIGHLY COOLED LIQUEFIED GASES |
US4365576A (en) * | 1980-07-21 | 1982-12-28 | Cook, Stolowitz And Frame | Offshore submarine storage facility for highly chilled liquified gases |
US4402632A (en) * | 1980-08-25 | 1983-09-06 | Cook, Stolowitz & Frame | Seabed supported submarine pressure transfer storage facility for liquified gases |
US4662386A (en) * | 1986-04-03 | 1987-05-05 | Sofec, Inc. | Subsea petroleum products storage system |
US5293751A (en) * | 1989-07-19 | 1994-03-15 | Mitsubishi Jukogyo Kabushiki Kaisha | Method and system for throwing carbon dioxide into the deep sea |
US5778679A (en) * | 1996-10-28 | 1998-07-14 | Amtrol Inc. | Method and apparatus for increasing acceptance and adjusting the rate of pressure variations within a prespecified range in precharged fluid storage systems |
US6490881B1 (en) * | 1998-07-14 | 2002-12-10 | Csir | Generating displacement and theroacoustic refrigerator |
US6260501B1 (en) * | 2000-03-17 | 2001-07-17 | Arthur Patrick Agnew | Submersible apparatus for transporting compressed gas |
US6718900B2 (en) | 2002-06-11 | 2004-04-13 | Gregory James Carter | Variable storage vessel and method |
NO320112B1 (en) * | 2002-10-23 | 2005-10-24 | Navion Asa | Seabed storage |
US20060225633A1 (en) * | 2002-10-23 | 2006-10-12 | Arild Samuelsen | Seabed located storage |
US7448404B2 (en) | 2002-10-23 | 2008-11-11 | Navion Asa | Seabed located storage |
US20050120723A1 (en) * | 2004-02-11 | 2005-06-09 | Mustang Engineering, L.P. | Methods and Apparatus For Processing, Transporting And/Or Storing Cryogenic Fluids |
US7293417B2 (en) | 2004-02-11 | 2007-11-13 | Mustang Engineering, L.P. | Methods and apparatus for processing, transporting and/or storing cryogenic fluids |
US20080210305A1 (en) * | 2004-09-21 | 2008-09-04 | Aker Kvaerner, Inc. | Liquified Natural Gas Sump For a Gravity Based Structure |
WO2008024652A2 (en) * | 2006-08-19 | 2008-02-28 | Agr Deepwater Development Systems, Inc. | Liquefied natural gas re-gasification and storage unit |
US7654279B2 (en) * | 2006-08-19 | 2010-02-02 | Agr Deepwater Development Systems, Inc. | Deep water gas storage system |
US20080041291A1 (en) * | 2006-08-19 | 2008-02-21 | Horton Edward E | Deep water gas storage system |
WO2008024652A3 (en) * | 2006-08-19 | 2008-10-09 | Agr Deepwater Dev Systems Inc | Liquefied natural gas re-gasification and storage unit |
US20080041068A1 (en) * | 2006-08-19 | 2008-02-21 | Horton Edward E | Liquefied natural gas re-gasification and storage unit |
US20090010717A1 (en) * | 2006-08-19 | 2009-01-08 | Agr Deepwater Development Systems, Inc. | Methods for Storing Gas |
US7735506B2 (en) * | 2006-08-19 | 2010-06-15 | Horton Wison Deepwater, Inc. | Methods for storing gas |
US20080083246A1 (en) * | 2006-10-06 | 2008-04-10 | Aker Kvaerner, Inc. | Gas Conditioning Method and Apparatus for the Recovery of LPG/NGL(C2+) From LNG |
US8499581B2 (en) | 2006-10-06 | 2013-08-06 | Ihi E&C International Corporation | Gas conditioning method and apparatus for the recovery of LPG/NGL(C2+) from LNG |
WO2009133563A3 (en) * | 2008-05-01 | 2010-03-18 | Seagen Systems Ltd. | Underwater storage system |
WO2009133563A2 (en) * | 2008-05-01 | 2009-11-05 | Seagen Systems Ltd. | Underwater storage system |
US20110146803A1 (en) * | 2008-09-05 | 2011-06-23 | Zhirong Wu | Multifunctional offshore base with liquid displacement system |
US8678711B2 (en) * | 2008-09-05 | 2014-03-25 | Zhirong Wu | Multifunctional offshore base with liquid displacement system |
US20120291688A1 (en) * | 2010-01-19 | 2012-11-22 | John Arthur Dawes | Subsea Pressure Compensation System |
US9084358B2 (en) * | 2010-01-19 | 2015-07-14 | Siemens Oil And Gas Offshore As | Subsea pressure compensation system |
US8801332B2 (en) * | 2010-02-15 | 2014-08-12 | Arothron Ltd. | Underwater energy storage system and power station powered therewith |
US20120305411A1 (en) * | 2010-02-15 | 2012-12-06 | Ron Elazari-Volcani | Underwater energy storage system and power station powered therewith |
US10894660B2 (en) | 2010-02-15 | 2021-01-19 | Yehuda Kahane Ltd | Underwater energy storage system and power station powered therewith |
US9309046B2 (en) | 2010-02-15 | 2016-04-12 | Arothron Ltd. | Underwater energy storage system and power station powered therewith |
US9045209B2 (en) | 2013-03-14 | 2015-06-02 | Sanko Tekstil Isletmeleri Sanayi Ve Ticaret A.S. | Active volume energy level large scale sub-sea energy fluids storage methods and apparatus for power generation and integration of renewable energy sources |
US9079639B2 (en) | 2013-04-06 | 2015-07-14 | Safe Marine Transfer, LLC | Large volume subsea chemical storage and metering system |
US9156609B2 (en) * | 2013-04-06 | 2015-10-13 | Safe Marine Transfer, LLC | Large subsea package deployment methods and devices |
US20140341657A1 (en) * | 2013-04-06 | 2014-11-20 | Safe Marine Transfer, LLC | Large subsea package deployment methods and devices |
US9664441B2 (en) * | 2013-07-18 | 2017-05-30 | S.G.B.D. Technologies Ltd. | Methods and systems for underwater gas pressurization and liquefaction |
US9664019B2 (en) | 2013-07-18 | 2017-05-30 | S.G.B.D. Technologies Ltd. | Underwater gas field development methods and systems |
US20150020541A1 (en) * | 2013-07-18 | 2015-01-22 | S.G.B.D. Technologies Ltd. | Methods and systems for underwater gas pressurization and liquefaction |
US9540169B1 (en) * | 2015-01-13 | 2017-01-10 | Daniel A. Krohn | Subsea storage tank for bulk storage of fluids subsea |
US9470365B1 (en) * | 2015-07-13 | 2016-10-18 | Chevron U.S.A. Inc. | Apparatus, methods, and systems for storing and managing liquids in an offshore environment |
US20200003365A1 (en) * | 2018-06-28 | 2020-01-02 | Toyota Jidosha Kabushiki Kaisha | Hydrogen gas compressing system and hydrogen gas compression method |
CN110657345A (en) * | 2018-06-28 | 2020-01-07 | 丰田自动车株式会社 | Hydrogen compression system and hydrogen compression method |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US3727418A (en) | Sub-aqueous storage of liquefied gases | |
US2731168A (en) | System for gathering and loading oil from underwater oil wells | |
US4209271A (en) | Storage tank with liquid insulator for storing cryogenic fluids using water displacement | |
US4232983A (en) | Offshore submarine storage facility for highly chilled liquified gases | |
US4188157A (en) | Marine structure | |
US5036904A (en) | Latent heat storage tank | |
US3376588A (en) | Buoy with buoyancy produced by liquefied gas vaporization | |
US3766583A (en) | Offshore liquefied gas terminal | |
US3110157A (en) | Transportation of cold liquids and safety means | |
CA1152761A (en) | Seabed supported submarine pressure transfer storage facility for liquified gases | |
US2963873A (en) | Method and apparatus for storing liquefied gases | |
GB2585758A (en) | Underwater vehicle for transporting cargo | |
US20100294192A1 (en) | Buoyancy system for an underwater device and associated methods for operating the same | |
GB2609952A (en) | An underwater vehicle for transporting fluid | |
US3422779A (en) | Tankship for the transportation of low-temperature liquefied gases | |
US3136135A (en) | Shipping liquefied gases | |
US3855803A (en) | Method of submerging a hollow structure | |
US3159005A (en) | Insulation system for low temperature service | |
RU2505740C2 (en) | Method for production, storage and decomposition of natural gas hydrates | |
US3537415A (en) | Container for liquefied gases | |
US3675427A (en) | Underwater storage device | |
US3229473A (en) | Vessel for transporting low temperature liquids | |
US3379012A (en) | Sealing means for ground reservoirs | |
US3283512A (en) | Earthen storage for volatile liquids and method of constructing the same | |
FI63356C (en) | ANALYZING VIDEO FILLING FOR THREADED GASKETS |