Key information

Title: Cellular pressure vessel, method for fabrication and use thereof
Application number: 20210228
Case type: National
Status: 08.07.2024 Patent meddelt (B1)
Filed: 22.02.2021
Effective date: 22.02.2021
Publicly available: 23.08.2022
Next annual fee due: 28.02.2027
Applicant: Lattice International AS (NO)
Owner: LATTICE INTERNATIONAL AS (NO)
Inventor: Pål G. Bergan (NO)
Agent: BRYN AARFLOT AS (NO)
Granted: 08.07.2024
Patent number: 348049
Expiry date: 22.02.2041

Abstract and drawing

Disclaimer: This text has been machine-scanned and may contain errors – please refer to "Publications" for legally binding content.

The invention provides a pressure vessel, comprising an outer pressure shell, thermal insulation around the outer pressure shell if the tank is for cold or cryogenic operation, and at least one opening for filling and emptying fluid. The pressure vessel comprises: a plurality of identical longitudinal cellular units, from at least two longitudinal cellular units, wherein the cellular units are arranged side by side along a longitudinal direction, with a shared wall in between, each shared wall inside the outer pressure shell comprises at least one opening allowing fluid to migrate between the longitudinal cellular units and to equalize the pressure between the longitudinal cellular units, and wherein fixed ratios between dimensions and wall thicknesses provide, when external constraints and outer shell parts are excluded, a membrane stress condition without bending in the internal walls of the longitudinal cellular units. The invention also provides a method of building the pressure vessel and use of the pressure vessel.

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Date	Doc. No.	Process	Case number	In/Out	Journal description	To/from
04.09.2025	02-01	Endring av søker/innehaver	2025/09413	UT	GH Forespørsel	BRYN AARFLOT AS
02.09.2025	01-01	Endring av søker/innehaver	2025/09413	INN	Generell henvendelse	BRYN AARFLOT AS
10.07.2024	11-01	Saksbehandling	20210228(348049)	UT	PT Registreringsbrev nasjonal patent (15) (PT20210228)
26.04.2024	10-01	Saksbehandling	20210228	UT	Intention to grant	BRYN AARFLOT AS
12.10.2023	09-06	Saksbehandling	20210228	INN	Response letter	BRYN AARFLOT AS
12.10.2023	09-05	Saksbehandling	20210228	INN	Norwegian translation of claims - marked	BRYN AARFLOT AS
12.10.2023	09-04	Saksbehandling	20210228	INN	Norwegian translation of claims - clean	BRYN AARFLOT AS
12.10.2023	09-03	Saksbehandling	20210228	INN	Description and claims in English - marked	BRYN AARFLOT AS
12.10.2023	09-02	Saksbehandling	20210228	INN	Description and claims in English - clean	BRYN AARFLOT AS
12.10.2023	09-01	Saksbehandling	20210228	INN	Korrespondanse (Hovedbrev inn)	BRYN AARFLOT AS
13.07.2023	08-01	Saksbehandling	20210228	UT	Substantive examination	BRYN AARFLOT AS
05.07.2023	07-07	Saksbehandling	20210228	INN	Response letter	BRYN AARFLOT AS
05.07.2023	07-06	Saksbehandling	20210228	INN	Norwegian translation of claims	BRYN AARFLOT AS
05.07.2023	07-05	Saksbehandling	20210228	INN	Description - marked	BRYN AARFLOT AS
05.07.2023	07-04	Saksbehandling	20210228	INN	Description - clean	BRYN AARFLOT AS
05.07.2023	07-03	Saksbehandling	20210228	INN	Claims - marked	BRYN AARFLOT AS
05.07.2023	07-02	Saksbehandling	20210228	INN	Claims - clean	BRYN AARFLOT AS
05.07.2023	07-01	Saksbehandling	20210228	INN	Korrespondanse (Hovedbrev inn)	BRYN AARFLOT AS
24.04.2023	06-01	Saksbehandling	20210228	UT	Substantive examination	BRYN AARFLOT AS
03.01.2023	05-01	Saksbehandling	20210228	UT	PT Varsel om betaling av første årsavgift (3317) (PT20210228)	PROTECTOR IP AS
19.08.2022	02-01	Overdragelse av søknad/rettighet	2022/12869	UT	GH Forespørsel	PROTECTOR IP AS
15.08.2022	01-02	Overdragelse av søknad/rettighet	2022/12869	INN	Generalfullmakt NO	PROTECTOR IP AS
15.08.2022	01-01	Overdragelse av søknad/rettighet	2022/12869	INN	Generell henvendelse	PROTECTOR IP AS
04.03.2022	04-02	Saksbehandling	20210228	INN	Letter_to_NIPO	PROTECTOR IP AS
04.03.2022	04-01	Saksbehandling	20210228	INN	Korrespondanse (Hovedbrev inn)	PROTECTOR IP AS
07.09.2021	03-02	Saksbehandling	20210228	UT	PT report 03:41:42
07.09.2021	03-01	Saksbehandling	20210228	UT	Substantive examination	PROTECTOR IP AS
24.02.2021	02-01	Saksbehandling	20210228	UT	Infobrev til oppfinner	PROTECTOR IP AS
22.02.2021	01-07	Saksbehandling	20210228	INN	Statement_applicants_right_to_invention	PROTECTOR IP AS
22.02.2021	01-06	Saksbehandling	20210228	INN	PoA NO Lattice Technology	PROTECTOR IP AS
22.02.2021	01-05	Saksbehandling	20210228	INN	Figures	PROTECTOR IP AS
22.02.2021	01-04	Saksbehandling	20210228	INN	Description	PROTECTOR IP AS
22.02.2021	01-03	Saksbehandling	20210228	INN	Claims	PROTECTOR IP AS
22.02.2021	01-02	Saksbehandling	20210228	INN	Abstract	PROTECTOR IP AS
22.02.2021	01-01	Saksbehandling	20210228	INN	Søknadsskjema Patent	PROTECTOR IP AS

Description, claims and drawings

Disclaimer: This text has been machine-scanned and may contain errors – please refer to "Publications" for legally binding content.

Description

CELLULAR PRESSURE VESSEL, METHOD FOR FABRICATION AND USE THEREOF

Technical Field

The present invention relates to storage and transport of fluids under pressure. More specifically, the invention relates to a new pressure vessel design suited for efficient production of small and medium size tanks feasible for storage of fluids existing in both liquid and gaseous form within the tank during a condition of pressure and temperature consistent with fluid properties, such as by cryogenic liquefaction, and with external insulation on the tank, if required. Typical embodiments of the invention are fuel tanks in the transport sector for containment of fossil fuels, such as LNG and LPG, and for liquid hydrogen. Other application areas with containment of gases are also feasible. The invention also relates to methods for fabricating the tanks and use of the tanks.

Background Art

Storage and transport of fluids that normally exist in gaseous form at ambient temperature without applying pressure can be challenging. Clearly, storage of such fluids in unpressurized, gaseous form is normally not practically feasible simply because of the volume it takes in relation to the mass and energy content. Two main, practical approaches thus exist: (1) to keep the gas in gaseous form under high pressure at ambient temperature or (2) to cool down the gas to become liquid form at atmospheric pressure or with combined cooling and pressurization. Even with good thermal insulation a gas that is liquid at atmospheric pressure during filling, will normally turn into a two-phase state with part of the fluid being converted from liquid to gas caused by heat ingress; such boil-off will results in pressure build-up unless gas is released from the containment.

For climate and environmental reasons, there is a growing need for decarbonizing the energy sector by turning to use of low carbon or no-carbon fuels. However, low carbon usually means lighter fuels that exist in gas form under normal temperature and pressure. With less relative molecular carbon content comes lower liquefaction/boiling temperature which means that best storage efficiency will be obtained with fluids at pressurized or unpressurized condition as liquid, in cryogenic or refrigerated condition. Examples of low carbon or carbon free energy carriers normally stored at low temperature are liquified natural gas (LNG, mainly CH4) which typically liquifies at -163 °C and ammonia (NH3) which liquifies at -33.4 °C during atmospheric pressure. The “cleanest” energy carrier is hydrogen which turns into pure water during oxidation. Unfortunately, hydrogen can be one of the most difficult gases to store. It requires extremely low cryogenic conditions with -253 °C to liquefy at atmospheric pressure. Alternatively, it may be kept as gas under extremely high pressure, such as 300 to 800 bar, during ambient temperature to provide reasonable energy content per unit volume. For comparison, the energy density of liquid hydrogen is normally more than 4 times higher than that of highly compressed hydrogen. For this reason, liquid hydrogen can be much preferred over pressurized hydrogen gas when applied in the transport sector or other applications where space comes at a premium. Very large-scale storage of hydrogen is best dealt with in liquid, cryogenic form.

Containments or tanks for pressurized fluids normally have cylindrical or spherical shape. Their ability to withstand internal pressure is provided by membrane forces in the single or doubly curved shell surface. These forces are directly proportional to the pressure inside the tank as well as to the radius of curvature. This relationship implies that the required shell wall thickness grows proportionally with pressure as well as radius whereas the thickness is inversely depending on material strength. Accordingly, the practical size in terms of radius of a cylindrical will be rather limited and, hence also the size, when the pressure is high, even when using materials with extreme strength, e.g. composites with high strength fibers. Typically, a pressure vessel carries only a few kilograms of hydrogen at ambient temperature and 500 bar pressure. A consequence of such pressure is that storing a significant amount of highly pressurized gas at ambient temperature will require a very large number of cylindrical pressure vessels or flasks. Unfortunately, such solutions have poor, overall space efficiency because of the cylindrical shape with wasted space between cylinders, and large batteries of flasks require extensive piping and valve systems resulting in increased risk of leakage.

An alternative to cylinders is the so-called “lattice pressure vessels” (LPV) which are based on a rather different load carrying principle. In the LPV concept the pressure on the outer tank walls is carried by an internal, modular “lattice structure” which connect and balance pressure on opposite, outer walls. Major advantages by this concept are (1) the LPV pressure vessels are fully scalable in size without requiring increased outer wall thickness, and (2) the overall space efficiency is very high because the tank can have a prismatic or box-like shape fully flexible to utilize any surrounding storage space with one tank. LPVs are modular and have a great flexibility in terms of shape and size. They are normally made of moderately thin metal plates welded together, and they are typically suited for internal pressures ranging for 2 up to 50 bars. Cryogenic fluids, such as liquified natural gas and liquid hydrogen, should normally be stored in insulated LPVs at near dew point temperature to avoid excess pressures.

LPVs are in most cases made by steel plates welded together; this implies that there will be a plurality of weld seams. It may also be difficult to scale LPVs down to very small sizes due to space required for carrying out welding. LPVs have currently been installed and used as LNG fuel tanks in ships and new applications for liquid hydrogen storage are being developed and tested.

However, a demand still exists for tanks that are particularly favorable for small and medium size tanks, feasible for operation at ambient temperature of twophase fluid liquid-gas but easily adaptable for cryogenic or cold fluid operation in general, and particularly feasible for use as tanks in mobile units such as vehicles, ships, trains, planes and so on, in addition to also being feasible as storage tanks.

Summary of The Invention

The invention meets the demand by providing a pressure vessel according to claim 1, a method according to claim 8 and use according to claim 10. Some preferable embodiments are defined in dependent claims. Further preferable embodiments include features included in dependent claims and embodiments and features as described or illustrated herein, in any compatible combination.

More specifically, the pressure vessel comprises an outer pressure shell, thermal insulation around the outer pressure shell if the tank is for cold or cryogenic operation, and at least one opening for filling and emptying fluid. The pressure vessel is distinctive in that it comprises: a plurality of identical longitudinal cellular units, numbering from two longitudinal cellular units up to a larger integer, wherein the cellular units are arranged side by side along a longitudinal direction, with a shared wall in between, each shared wall inside the outer pressure shell comprises at least one opening allowing fluid to migrate between the longitudinal cellular units and to equalize the pressure between the longitudinal cellular units, and wherein fixed ratios between dimensions and wall thicknesses provide, when external constraints and outer shell parts are excluded, a membrane stress condition without bending in the internal walls of the longitudinal cellular units.

Identical longitudinal cellular units, in this context means cross section dimensions of a longitudinal cellular unit with length L in z-direction, width B in x-direction and height H in y-direction in an x-y-z orthogonal coordinate system. Thus, the x-y plane is defined as the plane of the cellular structure and the zaxis as the length direction of the cellular structure. Further, the repetitive cells are formed side-by-side in the x-direction with internal walls in y-z planes. The width of each cell in the x-direction is termed B. The height of each cell in the ydirection is termed H. The total length of the containment in the z-direction is termed L. Conveniently, the enclosing outer walls crossing the x-axis are denoted side walls, the walls crossing the y-axis are called top- and bottom walls, respectively, and the walls crossing the z-axis are called end walls.

If the person skilled in the art follow the guidance provided in this document, in accordance with the definition of claim 1; wherein each shared wall comprises at least one opening for equalizing the pressure between the longitudinal cellular units, and with fixed ratios between dimensions and wall thicknesses as prescribed in the detailed description, with external constraints and outer shell parts excluded, the technical effect is membrane stress condition without bending in the internal walls of the longitudinal cellular units. This means that at least the shared walls between the longitudinal cellular units have membrane stress without bending, in this context meaning equal tensile stress over the thickness. However, deviations from the ratios of dimensions and/or wall thickness, and/or effects by internal pressure on the outer pressure shell parts, and/or external or other constraints, can provide deviations from membrane stress.

Minor deviations still providing technical and/or economic advantage over prior art pressure vessels are allowable within the scope of protection. Pressure vessel embodiments with deviations resulting in stress condition in the internal structure deviating from pure membrane stress by 10%, 7%, 5%, 3%, 2% or 1% or less can still be beneficial over prior art pressure vessels. Such allowable deviations can be the result of deviation from fixed ratios between dimensions and/or wall thicknesses from ratios as specified in the detailed description, parts of the outer pressure shell not having pure membrane stress, different outer pressure shell design between longitudinal cellular units, deviations from orthogonal oriented internal walls, or effects at corners and/or ends. Said deviations from membrane stress can be determined by numerical simulations, and whether or not the pressure vessel still is beneficial over prior art pressure vessels, and thereby still is according to the invention, can be found by economical modeling.

As understood by the person skilled in the art, variation from the ideal stress condition with pure membrane stress is allowable to the extent as resulting from the variations as specified above and described later. Ultimately, stresses and deformation must comply with prescriptive rules of all codes applicable for the specific use intended for the containment.

The invention further provides a method of manufacturing a pressure vessel according to the invention, comprising longitudinal cellular units. The method is distinctive in that it comprises the steps:

to build in principle identical longitudinal cellular units and/or longitudinal parts of said units, by extrusion, bending of plates, deep drawing, rolling and/or other method,

unless the longitudinal cellular units are built directly as one part, to join parts of longitudinal cellular units together to form said units by fusion welding, solid state welding, brazing, gluing or other methods satisfying regulatory requirements,

to arrange at least one opening in each internal wall structure shared between cells,

to build end wall pressure shell structures,

to join said longitudinal cellular units and said outer end wall structures,

to arrange at least one inlet and/or outlet from outside the tank to inside the tank,

if for cold fluid operational temperature, to arrange adequate insulation around the tank,

if for colder operation, such as for storing liquid hydrogen, to arrange a further pressure shell and a coupling for a vacuum pump for having vacuum or near vacuum inside the insulation in operation.

The invention also provides use of the pressure vessel of the invention, for containing fuel in mobile units, including drones, cars, trucks, lorries, buses, trains, ships, airplanes, helicopters or any other mobile unit that can consume the fuel for operation, or use as small or medium sized storage tanks and/or transport tanks.

The current invention provides tanks and a method of producing cellular tanks and pressure vessels, providing at least the following advantages:

• The invention is based on an innovative cellular structural design principle which enables high material utilization with most of the tank structure being in an ideal state of membrane stress without significant bending

• The cellular design concept is repetitive meaning that tanks of different widths can be constructed from assembly of similar, basic structural elements

• The repetitive cellular structure is the same for the full, or nearly the full, length of the tank. This means full flexibility for choosing the tank length by a cutting a long cellular member into tank sections of desired length after which closing (capping) of end sections can be applied

• The above concept lends itself to very efficient production methods for the cellular cross-section member using extrusion of the entire cellular cross-section or efficient assembly and fusion of sub-sections of the cellular components

• A series of efficient production methods may be applied in the production of the cellular structure, such as by extrusion of one or several types of cellular members in accordance with the design principle outlined herein standard or by assembly of extruded or rolled beams or bent deep drawn plates that are compatible with such principle.

• There is great flexibility in prescribing cross-sectional size and shape which can be optimized for space efficiency for the intended application

• The cross-sectional geometry can be designed to sustain high pressures (such as beyond 50 bar)

• The cross-sectional dimension of the tank can be much larger than the size of the extrusion die by fusing several extruded elements together

• Welding is significantly reduced because a tank can be assembled from profiles with complex and cellular geometry

• Multiple tanks can be placed densely together to increase storage capacity beyond that of a single tank

• Smooth outer surface of the tank or multiple of tanks highly suitable for applying air filled or vacuum insulation required for cold or cryogenic operation

These are capabilities and advantages that clearly go beyond the properties of conventional cylindrical tank technology as well as the current known LPV technology.

Clearly, the application of extrusion or rolling methods as a main operation in the fabrication of the tanks lends itself mainly to large scale production since there is significant cost associated with setting up such production method and with making specific tools or parts needed for making the desired shape of tanks components. By itself extrusion is a typical continuous or repetitive process. For these reasons mass production of tanks will be a target application for the invention. In this regard, interesting and important applications are found in the transportation sector, and most notably for pressurized and low temperature fuel tanks. Such applications are highly consistent with current drive for using more environmental and climate friendly fuels such as liquid, low carbon gas and liquid hydrogen. The possibilities for usage are wide, such as fuel tanks for various types of cars, trucks, machinery, trains and even airplanes. Tanks by the current invention are also advantageous by the fact that internal structure strongly reduces fluid sloshing during motion.

The invention is particularly well suited for small and moderate size tanks, such as fuel tanks and tanks for transport of gaseous fluids. Small scale tanks will typically be produced by continuous and repetitive production methods whereas medium size tanks can be made by conventional techniques for joining flat and curved members.

Brief description of drawings

Figures 1-4 illustrate embodiments of a tank of the invention, in cross section. Figure 5 illustrates end details, in longitudinal section, of a tank of the invention. Figure 6 illustrates a tank of the invention in which the entire end sections of the cellular tank are covered by a combined cylindrical and spherical shell.

Figure 7 illustrates an example of how closed cells of a tank are connected via multiple openings in internal cell walls in a tank of the invention.

Figure 8 illustrates two types of thermal insulation that can be included if tanks of the invention are used for cooled or cryogenic fluids.

Figure 9 illustrates the principle of material extrusion.

Figure 10 illustrates how large cell cross-sections may be composed of extruded part sections.

Figure 11 illustrates how several cell tanks of the present invention may be put together as a “cluster” or “battery pack” and thereafter thermally isolated.

Detailed description of the invention

The current invention combines a particular design concept for pressure vessels with structure allowing efficient and largely automated way of fabricating such pressure vessels. Figure 1 illustrates the design principle for a cellular pressure vessel for which deformations due to internal pressure loads do not lead to internal constraining and component bending stresses. The cross-section 101 of the pressure vessel consists of a series of internal ribs or webs or walls 104 that connect with outer cylindrical shell sections 102 with radius R to form a cellular structure enclosed with cylindrical shell sections 103 with similar radius R on each of the sides. The fluid holding volume is made of side cells 105 and internal cells 106. Note the geometrical relationship

(H/2)2 + (B/2)2 = R2 where B/2 < R (1) The key to a pure shell response without bending is that all structural parts should deform with the same deformational strain in the transverse shell direction; this means for the stresses

for the webs: σw = pB/tw (2) for the shells: σs = pR/ts (3)

where these stresses should ideally be the same and equal to the allowable design stress for the material applied. This gives a direct relationship between tw and ts depending only on the ratio B over R

tw/ts = B/R (4)

The design stress criterion also depends on the stress σz in the longitudinal zdirection through what is normally denoted equivalent or von Mises stress.

Assuming that all cells are sealed or capped and that the internal pressure thereby acts at the two ends, the cellular cross-section will also be subject to stressing in the longitudinal z-direction. With the assumption of “planar crosssections remain planar”, as in Navier’s hypothesis, the longitudinal stress σz will be the same across the entire cross-section 101 and, as is the case for a cylindrical shell, σz will be about half of the shell stress σs and web stress σw. This means that equation (4) also applies for the design based on equivalent stress. This applies regardless of how many cells there are in the concept of 101.

Further, the cellular topology shown in Figure 1 has no external constraint in the x direction. For this reason, the actual thickness of the shells covering the interior cells is not essential since a thicker exterior wall 102 for the cells only means less deformation in the y direction. Still, the requirement of deformational compatibility for the outer cells 105 in the y direction applies with the thickness ratio between tw and ts in accordance (4) for the enclosing shells on the sides to ensure deformational compatibility in the y direction.

Since there is no constraint in the x direction for the cellular cross-section, the exterior thickness (and strain) in the outer walls 102 for these cells becomes unimportant. This makes it possible to replace the cylindrical wall shape 102 with a smooth, planar outside as shown in Figures 2 and 3. Figure 2 shows a cross-sectional design 111 where the interior cells 117 have an arch or vault like design with flat outer surface 112. Flat outer surfaces may be advantageous for space efficiency as well as in connection with application of external thermal insulation. Due to geometry these vault sections 112 will not be in a state of pure membrane stresses but will also be subject to bending and, hence, will have to be designed for combined membrane and bending stresses. The increased thickness required results in reduced membrane deformation for 112 walls in the y-direction. As explained, this is unproblematic since there are no external constraints in the x-direction.

Figure 3 shows a very similar design as for Figure 2, with the only difference that the outer cell walls 122 are constant thickness plates rather than of vault type. Flat plates may be less efficient from a structural point of view but may otherwise be suitable for some purposes.

The cellular designs 111 and 121 in Figures 2 and 3 differ from that of Figure 1 in another important aspect beyond the geometry of the external cell walls 112 and 122: that is the geometry of the outer side cells 116 and 126 and their connecting points 118 and 128 to the interior cells 117 and 127. The half cylinder shell walls 113 and 123 the outer cells connect fully aligned with the outer cell walls 112 and 122. It is noted that there is a fixed relationship between shell radius R for the side cells given by

R = H/2 (5)

By the deformational compatibility requirement, the side shells 113 and 123 should expand equally much in the y direction during internal pressure as the adjacent web plates 114 and 124 of the interior cells and as 115 and 125 of the nearest interior cells. It is noted that the length of the effective surface which is pressurized and stretching the outer webs 115 and 125 is only B/2 as compared with B for the interior webs 114 and 124. This means that the following relationship between the thickness two of the outer webs, the thickness tw of the inner webs, and the thickness ts of the side shells should apply

two = tw /2 = ts (6)

Figure 4 indicates that it is also feasible to implement flat rather than cylindrical surfaces on the sides of the cellular tank cross-section. The interior cellular structure is similar to that of Figures 1, 2 and 3 with corresponding explanation of reference numbers. The main difference lies in cellular side sections defined by cells 136 with cellular walls 135 in the y-x plane and walls 139 in the x-z plane. The corner cells 133 have quarter-cylindrical walls with radius R. Note also the possibility for applying internal strengthening walls 140 that support the cells on the sides laterally. Figure 4 primarily describes alternative designs with 4 flat side walls being based on the current principle of compatible deformational strain for the entire tank cross-section. The actual dimensioning depends on the geometry chosen and will be determined for the specific case. The topology shown in the figure is an example and is one of several design solutions that it is feasible based on the principle described herein.

As indicated, the cellular cross-section must be completely enclosed in the front and back ends to enable holding a pressurized fluid inside to form a pressure vessel. The optimal way of doing this depends on cross-sectional geometry and tank size. Figure 5a shows longitudinal cross-section with cell 141 (corresponding to 106, 117, 127 etc.) with outer wall 142 (corresponding to 102, 112, 122) and a capping 143 applied to both ends of all cells. Figure 5 b shows a transverse view of a cell that is capped by an end plate 143. Thus, all cells are closed at both ends with end plates fitting the shape of the cell. These plates are connected to the adjacent cell walls by a suitable type of weld 144. Clearly these welds are important both for structural integrity as well as for gas tight sealing of the tank. This design results in both plate bending action and additional membrane stiffness in the plane of the end sections and such plate also constrains deformations in x and y directions at the tank ends. For this reason, the plates should preferably have moderate thickness while still being capable of carrying the internal pressure between cells. For this reason, one may choose a geometric shape for the cells with width B being significant smaller than cell height H, e.g. ¼ or smaller, to make this solution is feasible. An alternative to flat end plate is shown in figure 5c. Each cell is enclosed with a doubly curved shell 145, welded with a seam 146, and the shell has shape and thickness providing the same strain in the x-y plane as the strain that the cellular structure is subjected to. Hence, the deformational compatibility between shell capping and cellular structure in x and y directions is maintained. The doubly curved shell geometry shall ideally be a nearly perfect membrane type shell with geometry as if the cell opening would be covered by a “soap bubble” with air pressure on the internal side. A simple way of determining a perfect membrane shell geometry is to model the cell opening using a nonlinear (large displacement) finite element computer program with initially flat, extremely thin, shell elements that will deform and perform as pure membranes. By subjecting the finite element model to internal pressure, the surface will be as a perfectly deformed, pure membrane type shell geometry. The actual apex (max deformation) and shell thickness to be used for the actual design should be chosen in accordance with the strain compatibility condition with the connected pressurized cellular cross-section and satisfaction of allowable design stress requirement.

Other end cap designs can also be implemented for the proposed cellular cross-sections. Figure 6 shows a solution with a combined cylindrical and spherical end enclosure spanning the entire end sections. The radius for the cylindrical and spherical sections shall be the same as for the radius for the cellular sides in Figure 2, 3, or 4. The thickness of the cylindrical end sections 157 shall be the same as ts for the cylindrical side shells 153, see equations (2) and (3), and the shell will thereby be compatible with the deformational strain condition in the y-direction for the cellular cross-section corresponding to equation 6. A best deformational compatibility for the spherical corner shells 158 shall be that their thickness tss is about half of the cylindrical thickness in accordance with the strain compatibility principle; thus

tss = ½ ts = ½ two = ¼ tw or tw = 2 two = 2 ts = 4 tss (7)

It is noted that with end capping of all cells, as shown in Figure 5, the cell space become fully enclosed and without any connection which, clearly, is not compatible with being a tank to be filled with fluid. Figure 7 shows a simple way of dealing with this problem by boring holes 165 in the separating walls 161 before applying the end capping 163. Although one hole in each internal separation wall could be enough, it is will usually be preferable to apply at least 4 holes 165 in each wall as shown in the figure to allow for connections at each end of the cells and also positioned high and low to facilitate easy flow of both liquid and gaseous phases of the internal fluid.

It is quite common that fluids that are gaseous at ambient temperature and atmospheric pressure are stored in liquid form after cooling; examples are liquid petroleum gas, ammonia, liquid carbon dioxide, liquified natural gas, liquid oxygen, liquid nitrogen, liquid hydrogen and so on. Clearly, in all such cases there will be need for insulating the storage tank to reduce heat ingress from the surroundings followed by rapid pressure build-up. The present pressure vessel innovation can be designed for a suitable, operational, internal pressure and can also easily be thermally insulated. Figure 8 illustrated how thermal insulation may be applied for previously illustrated cellular cross-sections such as 101, 111, 121 and 131 from Figures 1, 2, 3 and 4, respectively. Figure 8a shows air filled insulation material 171, such as poly-urethane foam, fiber insulation or perlite surrounds the cellular tank surface. The outside of the insulation is covered by a protective cladding 172, also termed a further pressure shell. For gases that turn liquid only at deep cold, cryogenic conditions it may be preferable to apply vacuum or near vacuum condition by evacuating most of the air within the insulation space 171 while the cladding 172 must be completely airtight. Figure 8b shows a type of vacuum insulation where and an airtight, outer shell 175 capable of sustaining outside atmospheric pressure is partly connected with supports 173 to the inner tank. The air in the space 174 is evacuated before the tank is put in service with cold, liquid gas.

An effective way of manufacturing pressured vessels according to the invention is by material extrusion of the cellular structure by using a continuous, direct extrusion process. Among typical materials suitable for extrusion are aluminum, titanium, magnesium, and steel alloys for which extrusion forming is carried out at suitable temperature. For some applications plastics or composites may be extruded or formed otherwise according to the design principle prescribed herein. Figure 9 illustrates in a simplified way the principle of direct, continuous extrusion. The extrusion chamber 181 has a ram or piston that pushed on the material piece or billet 184 that is continuously through a die 183 to form the cross-sectional shape or profile of the extruded member 185. As will be the case for the current innovation the die must include an inserted mandrel 186 or the ram itself has extended part to forms cells 187 within the extruded member 185.

Limiting factors for continuous extrusion process of a given material is the maximum diameter of the die opening and the maximum force that the extrusion ram can exert. Accordingly, relatively small, cellular, tank cross-sections can be extruded as one piece. The process that follows includes cutting the extruded member into desired tank lengths, drilling holes for connection between neighboring cells, as in Figure 7, and applying end capping of cells, as in Figure 5, or capping the entire end sections, as in Figure 6.

The current invention can also be produced by extrusion when larger crosssection than what is practically feasible in one cross-sectional piece. In such case the tank cross-section can be produced as an assembly of extruded member components as shown in Figure 10. Figure 10 a1, a2, and a3 illustrates cellular parts with 1, 2 or 3 webs. The figure corresponds to the design shown in Figure 1 whereas the same principle also applies to cross-sectional designs of Figure 2 and 3. Figure 10 a1 can also serve as an illustration of that the current innovation is made from standard I-shape profiles for aluminum or other types of beams. Figure 10 b1, b2 and b3 shows similar extruded sections whereas a main difference is that the joining between extruded parts will be at web intersections with outer walls rather than at the midpoint between webs. Figure 10 c1 and c2 shows cylindrical side sections that also may be extruded and connected with the cellular part in accordance with Figures 1, 2 and 3.

When a cellular cross-section is made by several extruded parts, as illustrated in Figure 10, it will be necessary to join these together to form complete tank sections such as shown in Figures 1, 2, 3 and 4. It will normally be most efficient and practical to carry out this fusion process directly on the full length of the extruded components. The process that follows thereafter will then consist of cutting the assembly into the desired lengths and thereafter apply drilling of holes and application of end caps.

Other extrusion methods may also be applied for the present innovation. One such forming method is a type of extrusion in which a billet of suitable size for the object to be formed is kept in a container with shape of the outer surface is moved against a stamp or ram with form of the open cells is pressed together to shape the end structure making half of what will be the complete tank. Two such halves will thus be fused together to form a complete, cellular tank.

Alternatively, the two halves of the tank may be fabricated by way of metal or composite casting and fused together. Austenitic stainless-steel can be applied for deep drawing or plate bending, as well as being feasible for cryogenic and cold operation. Material printing is another way of producing a tank of the current invention.

There are several alternative ways of fusing or joining sections together such as by handheld or automated welding, friction stir welding, application of frictional movement and pressure, welding with electrical clamps or rollers, heating, solid state welding, gluing etc. The current invention assumes that the appropriate way of fusing parts together is used in view of material type, tank size, reliability and quality of method, cost, etc.

There are limits to how large tanks may be produced using extrusion according to the present innovation due to die size and pressure capacity of available production facilities. The same applies to other production methods such as casting. Despite this it will still be possible to increase the overall volumetric capacity by packing several tanks together into a “cluster” or “battery”. Clearly, the possibility for putting rather flat tanks next to each other will be a preferred solution. Figure 11 shows a series of cellular tanks 201 assembled next to each other with a common outer layer of insulation 202 to form a tank cluster 203. Clearly there are piping systems, connections, valves and instruments between tanks not shown in the figure. In this way tank systems with large storage capacities may be obtained. Also, the battery pack may be configured with very little wasted space between individual tanks and with very good space utilization of the room in which the tank cluster is located. Other embodiments of the tank cluster of Figure 11 include orienting the tanks vertically, with shared walls, typically flat walls with at least one opening between vertically coupled longitudinal cellular units. Sides can be curved, or vaulted or flat pressure walls, while upper and lower pressure shell segments between shared walls can be vaulted, curved or flat pressure walls.

Aluminum is widely used for extrusion and many aluminum alloys are feasible for extrusion. In addition to “hollow” or “closed” quadratic, rectangular or hexagonal beams, and numerous open structures, extrusion can produce longitudinal cellular units, from aluminum or other metals such as Nickel steel, austenitic steels, titanium alloys, magnesium alloys, nickel based alloys and cobalt based alloys. An extendable piston included in the extrusion ram may represent a preferable tool for extrusion. An ideal welding technique, in theory at least, for welding longitudinal parts and other parts of aluminum, is solid state welding, cf WO 03/043775 A1 and other publications, since full strength can be retained. When identical, ”closed” longitudinal cellular units are joined, when combining two walls of longitudinal cellular units to a shared wall, it is essential that no leakage way for fluid is left between the two original walls, whereby quality welding around the openings provided in shared walls can be essential. However, no forces, in theory, bring the two walls of the shared wall apart, and gluing or external brazing may be sufficient.

Claims

Pressure vessel, comprising an outer pressure shell, thermal insulation around the outer pressure shell if the tank is for cold or cryogenic operation, and at least one opening for filling and emptying fluid, c h a r a c t e r i s e d i n that the pressure vessel comprises: a plurality of identical longitudinal cellular units, from at least two longitudinal cellular units, wherein the cellular units are arranged side by side along a longitudinal direction, with a shared wall in between, each shared wall inside the outer pressure shell comprises at least one opening allowing fluid to migrate between the longitudinal cellular units and to equalize the pressure between the longitudinal cellular units, and wherein fixed ratios between dimensions and wall thicknesses provide, when external constraints and outer shell parts are excluded, a membrane stress condition without bending in the internal walls of the longitudinal cellular units.

Pressure vessel according to claim 1, wherein each internal, longitudinal cellular unit, in an orthogonal coordinate system with x in horizontal direction and y in vertical direction, has width B in x-direction, the shared wall has height H in ydirection and thickness tw, the pressure vessel further comprising an outer longitudinal cell on either side of the numerous in principle identical longitudinal cellular units arranged side by side, the outer longitudinal cell has a curved outer pressure wall with curvature defined by a radius R and thickness ts, and, the following geometric relationships apply:

A. if the outer longitudinal cell has width R B/2 and B/2 < R, the following ratios apply:

(H/2)2 + (B/2)2 = R2 where B/2 < R (1)

tw/ts = B/R (4) if curved pressure shells on top and bottom of radius R are arranged between shared walls, the thickness of said curved pressure shells are ts

B. if the outer longitudinal cell has width R, and the shared wall between the outer longitudinal cell and the neighbor longitudinal cellular unit has thickness two, the following ratios apply:

R = H/2 (5) two = tw /2 = ts (6)

C. if other structural design of the sides, the wall structure and thicknesses thereof have a design criterion of strain in y-direction by pressure equal to the strain in y-direction for the in principle identical longitudinal cellular units, or should aim at minimizing any difference in strain in y-direction.

Pressure vessel according to claim 1 or 2, comprising upper and/or a lower pressure walls between upper sides and/or lower sides of shared walls of the longitudinal cellular units, in the form of curved surfaces with radius R and width B and thickness ts, and/or with flat outer surface and curved inner surface, and/or flat pressure walls, wherein said pressure walls are parts of the outer pressure shell.

Pressure vessel according to any one of claim 1-3, comprising outer pressure shell side structure and/or outer pressure shell corner structure, preferably with thickness ts = tw/2 for curved side wall structure and thickness tss = tw/4 for double curved side-end corner structure, and/or otherwise adapted for equal or near equal strains in y-direction and x-direction as for the longitudinal cellular units.

Pressure vessel according to any one of claim 1-4, wherein the longitudinal cellular units comprise closing end outer pressure shell structures, such as curved end structure with curvature of radius R = H/2 and thickness te = two=tw/2, or vaulted or flat end structures.

Pressure vessel according to any one of claim 1-5, wherein two or more pressure vessels of the invention are stacked or arranged side by-side, with the longitudinal cellular direction horizontal or vertical, with internal fluid coupled as one pressure vessel, groups of pressure vessels or individual pressure vessels.

Pressure vessel according to any one of claim 1-6, comprising insulation, for example polyurethane foam or glass bubbles, and a further pressure shell outside the insulation, wherein the insulation has sufficiently open void-structure for allowing vacuum or near vacuum formation and compressive strength for withstanding 1 bar pressure and accidental loads from the further pressure shell, further comprising a connection for a vacuum pump through the further pressure shell, for providing vacuum or near vacuum in the insulation during operation, for improved insulation.

Method of building a pressure vessel according to any one of claim 1-7, comprising longitudinal cellular units, c h a r a c t e r i s e d i n that the method comprises the steps:

to build in principle identical longitudinal cellular units and/or longitudinal parts of said units, by extrusion, bending of plates, deep drawing, rolling and/or other method,

to arrange at least one opening in each structure to become a shared wall structure,

to build outer pressure shell structures,

to join said longitudinal cellular units and said outer pressure shell structures,

to arrange at least one inlet and/or outlet from outside the tank to inside the tank,

if for cold fluid operational temperature, to arrange insulation around the tank,

if for colder operation, to arrange a further pressure shell and a coupling for a vacuum pump for allowing to have vacuum or near vacuum inside the insulation in operation.

Method according to claim 8, comprising:

to extrude identical longitudinal cellular units, such as from a feasible aluminium alloy, wherein the identical longitudinal cellular units are rectangular or quadratic in cross section,

to arrange the identical longitudinal cellular units and joining them by fusing, welding, brazing, gluing or other method, whereby shared walls will have double thickness compared to outer walls,

to fabricate and join sides and ends, preferably comprising fabricating and joining/welding curved longitudinal sections of radius R = H/2 to the half thickness two outer walls of the longitudinal cellular units, with thickness ts = two, optionally likewise for the ends, optionally with double curved corners with thickness tss = ts/2.

10.

Use of the tanks of any one of claim 1-7, for containing fuel in mobile units, including drones, cars, trucks, lorries, buses, trains, ships, airplanes, helicopters and any other mobile unit that can consume the fuel for operation, or use as small or medium sized storage tanks and/or transport tanks.

Drawings

Priority

No priority

Patent classes

IPC classes

F17C 13/00

B65D 90/02

CPC classes

F17C 13/002

B65D 90/02

F17C 2209/219

Y02E 60/32

Citations

EP 3421863 A1 (A1)

NO 323091 B1 (B1)

Applicants, owners and inventors

Owners

LATTICE INTERNATIONAL AS

Strandveien 15

1366 LYSAKER

NO (BÆRUM Municipality, Akershus county)

Org. number: 926628690

Inventors

Pål G. Bergan

Ridder Flemmings vei 38

1397 NESØYA

NO (ASKER Municipality, Akershus county)

Agent

BRYN AARFLOT AS

Stortingsgata 8

0161 OSLO

NO (OSLO Municipality, Oslo county)

Org. number: 979993269

Reference: P6287NO00

Status history

Payment history

Oppositions and appeals

No oppositions or appeals

Administrative limitation

No administrative limitation

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No liens or licenses registered

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Only events from 2024.03.04 and onwards are shown.

Cellular pressure vessel, method for fabrication and use thereof