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Publication numberUS3019937 A
Publication typeGrant
Publication dateFeb 6, 1962
Filing dateOct 25, 1957
Priority dateOct 25, 1957
Publication numberUS 3019937 A, US 3019937A, US-A-3019937, US3019937 A, US3019937A
InventorsWillard L Morrison
Original AssigneeConch Int Methane Ltd
Export CitationBiBTeX, EndNote, RefMan
External Links: USPTO, USPTO Assignment, Espacenet
Insulated tank for storage and transportation of low boiling liquefied gas
US 3019937 A
Abstract  available in
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Claims  available in
Description  (OCR text may contain errors)

Feb. 6, 1962 W. L. MORRISON INSULATED TANK FOR STORAGE AND TRANSPORTATION OF LOW BOILING LIQUEFIED GAS Filed Oct. 25, 1957 FIG 1 fire. Z a

INVENTOR. Zflzllard L. fli /7715 11 y aiiorneyfi nite This invention relates to the storage and transportation of a low boiling liquefied gas and it relates more particularly to an insulated container in which a low boiling liquefied natural gas may be housed for storage and transportation.

As used herein, the term low boiling liquefied gas is meant to include gaseous materials in a liquefied state and which can be maintained in a liquefied state at ambient temperature only by confinement of the liquid'in a container at extremely high pressures, or which can be maintained in a liquefied state at atmospheric pressure only by holding the liquid to an extremely low temperature. Included are'such gaseous materials as nitrogen which boils at about 320 F. at atmospheric pressure, liquid air which has a boilingpoint of -3 16 F, at atmospheric pressure, and oxygen which boils at -295 F. at atmospheric pressure. While the inventive concepts described herein have application to containers for the storage and transportation of liquefied gases of the type described, theprincipal object ofthis invention is to provide a means for the storage and transportation of a liquefied natural gas which is composed-mostly of meth ane and which is characterized by a boiling point temperature within the range of 250-260" F. at about attates Patent v able only at a large premium.

pheric pressure. The difficulty with a low boiling liquefied gas resides in the means by which theliquefied material'can be housed in large. volumes for safe and economical storage and transportation. Low boiling gases have been housed in pressure containers wherein the material can be maintained under high pressure for storage and transportation at or prefer'ably somewhat below atmospheric temperature. While the absorption of heat from the atmosphere is minimized because of the lesser temperature differential between the temperature or the material and the ambient temperature, thereby to minimize dependence upon insulation, it will be apparent that the extremely high pressures demand the use of high strength containers. Such con-. tainers are not only expensive from the standpoint of the cost of materials and fabrication, but, of necessity, the capacity of such containers is limited by the ability to fabricate containers of sufilcient strength with the materials available to the industry. v

Thus such pressure containers are employed chiefly where'the amount of material to be stored or transwhich can be efficiently and economically handled in pressure containers. As the capacity of the container is increased, it will become apparent'that the amount of pressure capable of being maintained will rapidly de crease to the point where containers operating under atmospheric pressure or at most slightly above atmos- 5 ice pheric pressure are the only type of container which can be employed practically for holding the amount of liquefied natural gas transported to supply the fuel requirements of an entire section of a. country for use in the generation of power or heat. 7

Thus the problem which presents itself is in the storage and transportation of a liquefied natural gas in large'volume from a source wherein the natural gas is in plentiful supply to a distant area wherein there is either a short age of an equivalent fuel or where such fuels are avail- It is conceded that the natural gas can be liquefied at the source of plentiful supply for reduction of the gas to about of its original volume for transportation of the liquid to the point of use where it can be rcconverted from the liquid stage to a gaseous form for use as a fuel thereby to make it economical and practical to transport natural gas from a source of plentiful supply to a point where a deficiency exists. The problems which characterize the storage and transportation of natural gas in large volumes will also be found to exist in'the storage and transportation of other low boiling gases, such as oxygen, nitrogen, helium, and the like. 1

In the described modification wherein a container is to be designed for'use in the storage and transportation of liquefied natural gas at atmospheric pressure, it becomes necessary to-house the liquefied gas'within the container at about 258 F. or slightly less, depending upon the amount of higher boiling hydrocarbons or arematics present in the liquefied gas. At these extremely low pressures, the differential from the ambient temperature outside the container is such that the heat will naturally migrate from the outside into the liquid tocause volatilization thereof, the amountdepending greatly upon the rate of heat flow;

To minimize heat transfer, containers for housing a low boiling liquefied gas at about atmospheric pressure have been designed embodying the principles of a. thermos wherein use is made of an inner metal shell within an outer metal shell with the space in between either filled with an insulating material-of low heat conductivity or else sealed and evacuatedto maintainsub-atmospheric conditions. The inner metal shell isvusually intercom: nected with the outer metal shell for structural support and the inner shell is usually constructed with walls of sufiicient thickness to provide structural strength to support the liquid loadplus the staticferces' existing when positive pressure conditions are maintained-within the liquid storage tank For many applications, thermos type storage units of the character described have beenfound to be quite satisfactory but, where thematerial to-be housed within the container comprises a'low boiling liquefied-gas such as natural gas, a number of deficiencies will be found to exist. For example, there are very few metals available which are capable of desired structural strength especially at temperatures of F., let alone at temperatures aslow as -258 F. to -300 F. Structural steel plate, such as used in tank construction and in tanker construction, becomes embrittled and weak at the temperature of liquefiednaturalgas at atmospheric pressure such that cracks have been found to develop in the steel even without the application of load. This is of extreme importance to this new industry especially where the liquefied natural gas finds its greater demands in countries or in sections of the country which cannot economically be joined to the source of supply-by'pipe line or the like and thus relies upon tankers or trucks for transportation.

Further, many corrosive materials, such as acid gases, are present as impurities in the liquefied natural gas, the amount depending greatly onthe source of supply and the cleaning systems employed in the liquefaction process for the removal of moisture, the various acid gases and other impurities which might be present in the natural gas. Such acid gases and impurities corrode the surfaces of some metals which may be employed in tank construction. Corrosive attack is undesirable and, if progressive, will eventually eat away the material and require replacement or reconstruction of the tank-either of which would amount to the entire reconstruction of a ship when, as in the preferred concept, the tank is constructed as an integral part of the hold of the ship. Reconstruction for replacement of the metal shell will require the tie-up of the ship for many months and the expenditure of large sums of monies and labor.

Still further, a large number of elements are required properly to support the inner load carrying shell in the desired spaced relationship within the outer metal shell. These supporting elements, usually constructed of metallic material, provide direct pathways for the transmission of heat-from the outershell to the inner shell and to the liquefied gas contained therein thereby partially to nullify the effect of the insulation packed between the shells.

For these and for a. number of other reasons, doublewalled or thermos type tanks of the character heretofore constructed do not represent the most efiicient and econornical means for the storage and transportation of low boiling liquefied gases in large volume at about atmospheric pressure.

It is an object of this invention to produce a large capacity tank for the storage and transportation of a low boiling liquefied gas and it is a related object to produce a tank for the storage and transportation of liquefied natural gas in large volume at about atmospheric pressure.

More specifically, it is an object of this invention to produce a tank of the type described Which avoids the limitations found in thermos or double-walled insulated tanks of the type heretofore employed; which has good thermal insulating properties to minimize heat transfer from the ambient atmosphere to the cold liquefied gas resent as a content material in the tank; which makes use ofmaterials in contact with the liquefied gas that are not affected by the cold of the liquid or any of the corrosive materials which might be contained in admixture or in solution therewith; which avoids the use of materials of high heat conductivity communicating the liquefied content material with the ambient atmosphere thereby to minimize the transmission of heat from the outside to the cold boiling liquefied gas within the container, and which makes use of a material of low heat conductivity which retains its flexibility and strength under the tem perature conditions existing in the container. and which permits for a wide temperature differential without loss of the characteristics thereof as a thermal insulating material.

These and other objects and advantages of this invention will hereinafter appear and for purposes of illustration, but-not of limitation, an embodiment of the invention is shown in the accompanying drawings in which FIG. 1 is a schematic diagram of a portion of a tank wall illustrating the practice of this invention;

FIG. 1a is a schematic diagram of a modification in the construction as illustrated in FIG. 1;

FIG. 2 is a schematic diagram in section of a portion of a tank wall embodying a construction diflerent from that of FIG. 1 but which further illustrates the concepts of this invention;

FIG. 3 is a schematic sectional elevational view of a container embodying the construction of FIG. 1;

FIG. 4 is a schematic sectional elevational view of a container embodying the construction of'FIG. 2;

FIG. 5 is a schematic sectionalelevational view of a container embodying a modification in the construction ofFIG. 3, and

FIG. 6 is a schematic sectional view of a container embodying a modification of the construction in FIG. 4.

In the construction and operation of a tank embodying the features of this invention, an entirely new concept has been developed. The inventive concept depends for its operation upon the characteristics of the low boiling liquefied gas to vaporize upon the absorption of heat and the ability to control the rate of escape of the vapors to prevent the escape at a rate greater than their rate of generation whereby the low boiling liquefied gas is held back by the vapors to avoid contact with the fluid impervious walls of the tank to provide an insulating space of low heat conductivity to insulate the liquefied gas from the ambient atmosphere.

The inventive concept can perhaps best be described by reference to the diagrammatic sketch of FIG..1 wherein the tank wall of a structurally strong, fluid and preferably vapor impervious material is represented by the numeral 10. The numeral 12 represents a means lining the inner Wall of the tank having a plurality of separated pores 14 or pockets and the numeral 16 represents the low boiling liquefied gas housed within the container in direct contact with the lining means 12.

The heat which penetrates through the :wall of the tank from the ambient atmosphere is transmitted to the liquefied gas at the interface to cause some vaporization thereof. Such vapors 20 as are formed at the interface will enter the pockets to become entrapped therein. In accordance with the concepts of this invention, the pockets are constructed to prevent the escape of the vapors entrapped therein at a rate greater than the rate of introduction of vapors into the pockets, as by vaporization at the interface or by transmission through the walls from adjacent pockets or pores thereby to build up a cushion of vapor in the pockets which prevents deep penetration or entrance of the liquefied gas into the lining. In general, such vapors as are introduced into each pocket in excess of that capable of escaping from the outer portions of the pockets beyond the liquid interface are forced to be released from the pockets from the open end at the interior thereof to force back the liquid in the pockets to uncover the release openings for the excess.

Theoretically, the inventive concept resides in a container formed of an impervious outer shell "having a lining on the inside of the container and in direct contact with the liquid wherein the escape of vapor by transmission through the pores is less than the rate of introduction of vapor into the pores whereby the entrapped vapors build up a back pressure suflicient to limit'undue penetration of the liquefied gas into. the porous lining thereby to provide and maintain an insulated space between the liquid and the wall of the container.

When openings are present in the insulating layer, such as in the form ofpores, cracks, or voids, they should be so oriented or of such. size as to build up the back pressure and not spill or release the pressurized vapor exerting the back pressure. It will be apparent that a number of characteristics are demanded in a material capable of use as a lining employed in the practice of this invention. For example, the lining material should be a material having low heat conductivity with pores running generally in a horizontal direction, as illustrated in FIG. 1, and preferably with the horizontally disposed pores running generally in a direction parallel with the Walls of the container, as illustrated in FIG. 1a. The pores can extend horizontally endwise and perpendicular to the container, but preferably at a slight upward tilt from the inner edge outward- 1y toward the wall of the container. The desirability for an upward tilt will depend greatly on the cross-sectional dimension of the pores; the larger the pores, the greater the preference for an upward incline to build up the pocket eflect for blocking penetration of the liquid. The lining material should possess mass integrity and structural strength to avoid deformation or deterioration under the load conditions existing. It should be relatively unaffectedfrom the standpoint of. strengthand' flexibility under the extremely low temperatures of the materials to which it will be exposed, and it should retain a substantial proportion of its flexibility under such condition for use under the wide temperature differential which will exist from the inside out to the wall. It should be capable of retaining the vapors within its pores or pockets under sufficient pressure to hold back the liquid so as to block the flow of liquid through the pores into engagement with the outer wall. Finally, it should be free of attack by the liquefied gas or the acid gases or impurities admixed or dissolved therein.

The described characteristics are available in combina tion in very few materials. Best results have been secured by the use of a material in the form of a highly porous wood having structural strength sufficient to maintain the loads existing and which is capable of being formed into a composite structure, such as insulating panels which can be mounted onto the walls in substantial sealing relation therewith to provide the desired porosity wherein the desired back pressure principle can be developed. Woody materials having the described porosity and low heat conductivity are relatively unaffected from the standpoint of strength and flexibility underthe' extremely low temperature conditions of the liquefied gas and, for the most part, theyvare relatively free from attack by the liquefied gas and other gases or impurities admixed or otherwise contained therein. 1

Thus use can be made of panels formed of wood, such as balsa, or quippo, having mass integrity and strength and which are capable of being formed into a continuous composite layer from the inside out to the container wall and which are capable of supporting the load under the temperature conditions existing. Such woods are to be distinguished from other materials used as thermal insulation, as represented by cork, wool or glass fibers, asbestos fibers, exfoliated mica, and the like. When use is made of balsa wood or quippo or other similar low density, good insulating woody material having structural strength, the grain of the wood should be arranged horizontally in the-built-up layer of insulation and it should preferably run horizontally in a direction parallel to the wall to which it is attached.

, While not equivalent, use can be made of other inor ganic, thermally insulating materials, such as foamed glass and foamed plastics which are not embrittled by the low temperature conditions existing and which are not affected by the components present in the liquefied gas.

The described pocket structure capable of development of the back pressure of vapors generated from the liquid at the interface of the pores or pockets to maintain a vaprous phase between the liquid and'the wall of the container can also be secured by the structure represented diagrammatically in FIG. 2 of the drawings.

In this modification, the wall 30 of fluid and preferably vapor impervious material provides the support for a plurality of vertically spaced apart, downwardly and inwardly inclined baflie plates 32 which extend continuously about the walls as a lining with the space between the baffies forming the described pockets 34. The liquefied natural gas 36 fills the area between the baflies in the tank and as much of the pockets as permissible. The vapors introduced into the pockets are incapable of escape at the rate of introduction so that the liquefied gas is forced back to a level, as represented by the line 36, which is horizontal with the inner edge of the upper bafiie forming the pocket to enable the excess vapor to escape from the pocket through the interior of the tank. To eflect the desired sealing relation of the pockets formed by the adjacent tiers of baflde plates, it is essential for the upper baffle plates to overlap the lower baffle plates for a substantial distance beyond the plane horizontal with the inner edge of the baflle. In the preferred modification, it is desirable to have the baflie plates dimensioned to have a length and to extend downwardly at an angle to provide for the described overlap with two or more of the underlying baffle-plates so as to insure the development of a vaporous phase notwithstanding the possible failure of one or more plates in the system.

It is not essential for the upper edges of the battle plates to be secured in sealing relationship with the Walls of the tank and it is not essential for the baffle plates to be formed of a fluid and vapor impervious material. It will be suflicient if the permeability to the transmission of vapor at the points of attachment to the wall and through the plates is such as to prevent the escape of vapors from the pockets at a rate greater than the introduction of vapor therein. It will be evident that the vapor introduced into any one pocket will comprise-not only the amount of vapor generated in the liquid at the interface 36 but will also include the amount of vapor which enters the pocket from the underlying or overlying pockets by transmission through the plates or about the edges of the plates at the point of attachment to the wall; If the plates are formed of a fluid and vapor impervious material, then reliance is had almost exclusively on the amount of vapor generated at the liquid interface 36 which, of necessity, will'be greater than the amount capable of'escaping from the pockets other than about the inner edge of the plates, unless openings are provided in the inner ends of the baffle plates forming the top walls of the pockets to enable the escape of vapor from the pockets at a point spaced inwardly frornthe end of the overlying pockets. When such openings are provided in theinner portions of the plates,- it'will be apparent that the vapors escaping from the pockets beneath will be introduced into the interior of the pockets above to become entrapped therein and thereby further to increase the amount of vapor introduced therein.

In the preferred practice of this invention, the baflie plates 32 can be formed of wooden shingles or shingles formed of other structural elements which are not harmfully affected by the cold or liquefied gas and which have relatively low heat conductivity. Members of higher heat conductivity may be used, such for example as metal strips, but, under such circumstances, it is desirable to make use of as thin strips as possible and to employ maximum space between the strips to minimize heat transfer through the metal members. When the space between the tiers of baffles is substantially filled with an insulating material, as previously described, the barrier elements can be in the form of very thin films or sheet stock. When a metal is employed, it is preferred to make use of aluminum, or alloys of aluminum, or stainless steels which have been found capable of use without excessive strength loss or corrosion while in direct'contact with the cold boiling liquefied gas.

When the build-up of pockets is achieved by the techniques which employ bafile plates, the bottom wall of the tank can be constructed with a metal pan 40 resting upon a thick layer of insulating material with the side edges 42 of the pan extending angularly upwardly into the space between baflle plates spaced from the bottom to be sandwiched therebetween to provide the described pocket structure in cooperation with the pan and to build up the insulating vapor space in between, as illustrated in FIG. 4.

FIG. 3 diagrammatically illustrates a container embodying the concepts of constructionrepresented by FIG. 1 wherein the liquefied gas 16 is housed within the open space between the thick layer 12 of porous insulating material provided as a lining on the inner face of the wall 10. The enclosure can be covered by a top plate 22 having a thick layer 24 of insulating material on the underside thereof to effect a thermal sea] at the open end of the container. The insulation material in the layer 24 need not embody the complete concepts de scribed because liquid will not have as great a tendency to flow therethrough to the cover plate, but it is more desirable to embody some of the concepts of the described 7 insulation layers in the cover to avoid difliculties when the ship lists or otherwise rolls or tosses to bring the liquid'into substantial contactwith the tank roof. An access opening is provided in the cover for the introduction of liquefied gas and for the removal of liquefied gas and vapors generated in the container.

If the pores of the insulating layer 12 are disconnected or extend horizontally in a direction parallel with the walls of the tank, as demonstrated by the arrangement in FIG. 1a, it will be apparent that the membranes separating the pores may still be vapor and fluid permeable to enable inflow of the liquid partially through the insulation until resisted by the vapor pressures extending beyond the liquid interface to the wall of the tank.

The modification illustrated in FIG. 4 embodies the concepts described. in FIG. 2 wherein use is made of a plurality of vertically spaced apart tiers of shelves or baffie plates 32 extending downwardly angularly from the inner face of the wall 30 to separate the liquefied gas 36 from the wall upon the development of theback pressure principle by the vapors which are released by evaporation from the liquid. Each tier may also be subdivided by vertical partitions to prevent flow of vapor from one side for concentration on another and thereby relieve pressures which would enable the liquid to flow a greater distance into the pockets.

The ability to confine the fluid within the tank in spaced relationship with the walls to provide an insulated space in between enables the use of tank structures of the type described by way of a second line of defense where use is made of an inner shell for housing the liquid. Thus in the event of failure of the. inner shell, the insulating layer of porous material becomes effective to hold back the liquefied gas from contact with the wall of the tank thereby to save the ship, the tanker, or the tank itself.

The foregoing modification is diagrammatically illustrated in PEG. wherein the numeral 50 represents the inner shell for housing the liquefied gasSZ. When this construction is employed, it is preferable to make use of the modification illustrated in FIGS. 1 and 3 because then the insulating layer 54 can also be allowed to function as a load carrying member to support the inner shell 5%} without the use of additional supports of heat conductive material. When an inner shell 60 is employed in the modification of FIGS. 2 and -4, it is preferred to provide a downturned flap 62 on the inner ends of the shelves to provide more surface for support of the shell, particularly when formed of a thin foil incapable of self-support.

Under such circumstances, the inner shell can be formed of fluid and vapor impervious material having insufficient stre'ngthto support theload and which under load will deform. sufiiciently to rest upon the inner face of the insulating layer 54 for its support. For such purposes, Use can be made of relatively thin films of metal, such as aluminum, alloys of aluminum or stainless steel. In the alternative, and more desirable from a commercial standpoint, the inner shell 50 can be formed of a structural material capable by itself of maintaining the load and which rests upon the lining of insulating material by way of support. In the event of failure, the concepts described and which embody the features of this invention are available for operation as an insulated tank to confine the liquefied gas within the tank in spaced relationship with the outer walls 56.

It willbe appreciated that slight penetration of liquefied gas into the insulating layer will take place until the temperature conditions existing cause an amount of vapor to be generated at a rate in excess of that capable of escaping from the pockets or pores in the outer portions of the insulation. Thus, for the development of a suitable insulating space, it is desirable to make use of a rela tively thick insulating layer, such for example as a layer at least 3 and preferably 8 to 24 inches in thickness. It is desirable to avoid vertical channels in the insulation through which the vapors are capable of rapid escape though an occasional channel is not fatal if spaced inwardly a sufiicient distance from the wall. Thus, in the use of panels of a porous wood, it is best to jointhe panels to form a composite structure substantially free of open, vertical spaces or channels in between. The insulation lining may be built up of a preformed plank of balsa or the likewood built up to the desired thickness and secured in substantial sealing relationship to the wall of the tank or it may be fabricated of separate panels ofsmaller dimension which are bonded one to the other in building up an insulated layer of the desired thickness with the outermost panels being bonded to the inner face of the tank wall.

This application is a continuation-in-part of my copending application Ser. No. 354,216, filed May 11, 1953, and now abandoned, which is a continuation-in-part of the then copending application Ser. No. 288,214, filed May 16, 1952, and now abandoned, and it is a continuation-inpart of my copending application Ser. No. 408,220, and now Patent No. 2,889,953, filed February 4, 1954,

It will be understood that changes may be made in the details of construction, arrangement and operation without departing from the spirit of the invention, especially as defined in the following claims.

I claim: I

1.. A container for the storage and transportation of a low boiling liquefied gas in large volume at about atmospheric pressure comprising an outer fluid and substantially vapor impervious wall of a structurally strong material, a relatively thick layer of a porous insulating material formed of a highly porous wood of low density lining the inner face of the container Wall and having its inner surfaces in direct contact with the liquid content material, the pores of the insulating lining having permeability controlled to prevent the escape of vapors at a rate greater than the introduction of vapors therein from the liquid and from adjacent pores whereby a back pressure is built up withinthe pores to block deep penetration of the liquid into the porous insulation lining thereby to maintain a spaced relationship between the liquid and the outer wall of the container to define a vapor filled insulation space therebetween which is free of liquid.

2. A. container, as claimed in claim 1 in Which the porous wood lining is in the form of a composite panel secured in substantially sealing relationship to the wall of the container.- I

References Cited in the file of this patent UNITED STATES PATENTS ii i l l i

Patent Citations
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US2321777 *Jul 9, 1940Jun 15, 1943American Hard Rubber CoHard rubber lining for receptacles
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Referenced by
Citing PatentFiling datePublication dateApplicantTitle
US3208621 *Aug 16, 1963Sep 28, 1965North American Aviation IncInsulated tank for liquids boiling below ambient temperatures
US3325037 *Nov 12, 1963Jun 13, 1967Kohn JeanCryogenic structural insulating panels
US3362559 *Nov 6, 1964Jan 9, 1968Kohring WalterFluid storage tanks
US3389823 *Jun 3, 1966Jun 25, 1968EuratomContainer for the storage and/or transportation of liquefied gases
US3668880 *Oct 16, 1970Jun 13, 1972Martin Marietta CorpCapillary insulation
US3675809 *Jun 9, 1970Jul 11, 1972Martin Marietta CorpCapillary insulation
US3693367 *Apr 24, 1970Sep 26, 1972Leonard J Di PeriThermodynamic control device
US3777501 *Mar 12, 1971Dec 11, 1973Martin Marietta CorpCapillary insulation
US5765586 *Nov 28, 1994Jun 16, 1998Powermass CorporationReduction of heat transfer between a body and its environment
US6311710Jun 5, 1998Nov 6, 2001Powermass CorporationReduction of heat transfer between a body and its environment
US7971744 *Jun 19, 2006Jul 5, 2011Jonathan D SpearFoam vessel for cryogenic fluid storage
WO2010086491A1 *Jan 14, 2010Aug 5, 2010Tom SommardalContainer
Classifications
U.S. Classification220/560.12, 220/901
International ClassificationF17C3/06
Cooperative ClassificationY10S220/901, F17C3/06
European ClassificationF17C3/06