Description The present invention relates to a sorption store for storing gaseous substances, which comprises a closed container which is at least partly filled with an adsorption medium and a feed device which comprises a passage through the container wall, through which a gas can flow into the container. The invention further provides a method of charging a sorption store with a gas, wherein the sorption store comprises a closed container and a feed device which has a passage through the container wall, through which the gas can flow into the container, and the container has at least two parallel, channel-shaped subchambers which are located in its interior and are each at least partly filled with an adsorption medium and whose channel walls are coolable. To store gases for stationary and mobile applications, sorption stores are increasingly being used nowadays in addition to pressurized gas tanks. Sorption stores generally comprise an adsorption medium having a large internal surface area on which the gas is adsorbed and thereby stored. During filling of a sorption store, heat is liberated as a result of the adsorption and has to be removed from the store. Analogously, heat has to be supplied for the process of desorption when taking gas from the store. Heat management is therefore of great importance in the design of sorption stores.

The patent application US 2008/0168776 A1 describes a sorption store for hydrogen which comprises an external container which is thermally insulated from the surroundings and in the interior of which a plurality of pressure containers comprising an adsorption medium are arranged. The intermediate spaces between the pressure containers are filled with a cooling liquid in order to be able to remove the heat evolved during adsorption.

The patent application DE 10 2007 058 673 A1 describes an apparatus for storing gaseous hydrocarbons, which comprises an insulated container filled with an adsorption medium. A heating element is provided in the container and this heating element is controlled by means of a control system in such a way that a minimum pressure is maintained over an ideally long period of time when taking off gas. A disadvantage of known sorption stores is that filling with gas proceeds only slowly. Particularly in mobile applications, for example in motor vehicles, this disadvantage is particularly serious.

It is an object of the invention to provide an apparatus for storing gaseous substances which allows fast charging of gas and improved taking-off of gas. The apparatus should have a simple construction and require little electric energy during operation. A further object is to provide a method of quickly and efficiently charging the store. This object is achieved by the subject matter of the invention as described in claim 1. Further advantageous embodiments of the invention may be found in the dependent claims. Further subjects of the invention are indicated in claim 9 and the claims dependent on this. The method of the invention is carried out using a sorption store which comprises a closed container and a feed device which has a passage through the container wall, through which the gas can flow into the container. The container has at least two parallel, channel-shaped subchambers which are located in its interior and are each at least partly filled with an adsorption medium and whose channel walls are coolable. In a first step of the method of the invention, gas is fed in in such an amount that a pressure in the store of at least 30% of a predetermined final pressure is reached as quickly as possible. In a subsequent second step, the amount of gas fed in is varied in such a way that the course of the pressure in the store approximates the adsorption kinetics of the adsorption medium until the predetermined final pressure in the store is reached after a predetermined period of time.

Sorption stores as are known from the prior art are, for charging, usually connected to a pressure line from which the gas to be stored flows at constant pressure into the store until a predetermined final pressure in the store has been reached. However, it has been found that the time required for charging can be significantly reduced when charging is carried out according to the method of the invention.

In the sorption store, gas is stored both by adsorption on the adsorption medium and also in the voids between and in individual particles of the adsorption medium or in regions of the container which are not filled with adsorption medium. During the first step of the method of the invention, the voids are firstly filled with gas. The pressure in the store follows, with virtually no lag time, the pressure of the gas flowing into the container. To minimize the total time required for the charging operation, this first step should be carried out as quickly as possible, for example by introducing the gas at a pressure which corresponds to at least 30% of the predetermined final pressure right from the beginning of the charging operation.

During the first step, part of the gas is adsorbed, as a result of which the temperature of the adsorption material and thus also of the gas flowing over it increases. In the second step, the course of the pressure in the store approximates the adsorption kinetics of the adsorption medium. Methods of determining the adsorption kinetics are known to those skilled in the art, for example by means of pressure jump experiments or adsorption balances (e.g. in "Zhao, Li and Lin, Industrial & Engineering Chemistry Research, 48(22), 2009, pages 10015-10020").

For the purposes of the present invention, the term adsorption kinetics refers to the course of the adsorption of the gas on the adsorption medium over time under isothermal and isobaric conditions. This course can frequently be approximated by an exponentially decaying function which at the beginning displays a sharp rise and then becomes ever flatter as it converges toward a final value. An example of such an approximation is the function a-(1 - e ^_bt ), where a and b are positive constants. The adsorption kinetics can also be approximated by other functions, for example a concave function, a function which is constant in sections, a function which is linear in sections or a linear function which joins the initial value and the final value. The actual flow conditions in the channel-shaped subchambers of the store depend on the configuration of the channels and on the introduction of gas into the channels. In a preferred variant of sorption stores according to the invention, the channel-shaped subchambers are closed at one end. This is, for example, the case when the separation elements are joined to the interior wall of the container at one end. In this variant, the gas flowing into the container is advantageously conducted to the open ends of the channel-shaped subchambers. In the channels, part of the gas becomes adsorbed on the adsorption medium, as a result of which the adsorption medium and the surrounding gas heat up. The interior wall of the container and the at least one separation element or the plurality of separation elements optionally present are cooled, so that a radial temperature gradient is formed between the middle of the channel- shaped subchambers and their peripheries. The second step of the feed strategy of the invention in particular introduces a continual stream of gas into the container. Circulating gas flows are established internally in the channel-shaped subchambers by interaction with the radial temperature gradient and these ensure significantly better heat removal and thus lower maximum temperatures in the adsorption medium.

In a further preferred variant of energy stores according to the invention, the channel-shaped subchambers are open at both ends and are connected pairwise with one another via common spaces. In this variant, the feed device is preferably configured so that inflowing gas is directed virtually exclusively into one of the two subchambers of each channel pair. The charging strategy according to the invention with a course of the pressure in the store which

approximates the adsorption kinetics results in the flow rate of the gas in the channel-shaped subchambers being greater than the speed at which the gas is adsorbed. This results in the formation of circulating flows through the channel-shaped subchambers which ensure that the heat evolved during adsorption can be removed more quickly and lower maximum temperatures are established in the adsorption medium.

Compared to the conventional feed strategy, in which the pressure is kept constantly high over the entire charging time, the method of the invention allows, during charging, larger amounts of gas to be introduced in the same time or shorter charging times to be achieved at the same amounts of gas.

The amount of gas fed in can, for example, be varied by matching the inlet pressure appropriately to the approximation function, e.g. by means of appropriate valve connections. In an advantageous embodiment of the method of the invention, the course of the pressure in the store approximates the adsorption kinetics in the form of pressure oscillations, in particular as a result of appropriate variation of the inlet pressure. The maximum value of the oscillation preferably corresponds to the final pressure and the minimum value of the oscillation preferably approximates the course of the adsorption kinetics. This corresponds to a reduction in the oscillation amplitude over time. At the end of the predetermined period of time, the

predetermined final pressure in the store is set. The oscillation can be, for example, sinusoidal, sawtooth-shaped or alternately constant in sections. The shape of the oscillation and also its amplitude and period are preferably matched to the specific adsorption kinetics.

An example of a function which approximates the pressure oscillation of the adsorption kinetics is:

p = ρθ + Δρ ^■ f(a) ^■ (sin(2-TT k-t) - 1 ), where po is the initial pressure, p is the difference between initial pressure and final pressure, k is the frequency and f(a) is a damping function. The damping can, for example, decrease linearly or decrease exponentially. An example is the function f(a) = a / (t+a), where a is a positive number. The frequency k can be estimated via the isothermal and isobaric adsorption kinetics tkm, which is a measure of the minimum charging time. The frequency is preferably selected so that from two to ten oscillation periods are located within tkin. At a greater number of cycles, less heat can be removed per cycle, so that the energy consumption required for providing the pressure oscillations becomes uneconomical.

The time required for filling a sorption store is influenced substantially by the materials properties of the adsorption medium, in particular its adsorption kinetics. A further influencing factor is the maximum temperature to be expected during filling, which likewise depends on the materials properties, in particular the enthalpy of adsorption. The choice of the initial pressure and of the type of pressure increase are preferably matched to the respective adsorption kinetics, the enthalpy of adsorption and the heat conduction to the walls. In the case of rapid heat removal of the enthalpy of adsorption liberated, relatively high initial pressures are advantageous in order to minimize the total charging time required. Depending on the adsorption kinetics and heat removal, initial pressures in the range from 30% to 90% of the predetermined final pressure are advantageous, with an ideally high initial pressure being selected. The magnitude of the initial pressure may be limited by the temperature increase established during adsorption.

It tends to be advantageous to select a greater pressure difference between initial pressure and final pressure, the slower the removal of heat. The rate at which the pressure is increased is preferably at least 1 bar per minute of charging time in order to promote the formation of a circulating flow in the channel-shaped subchambers.

In a preferred embodiment of the method of the invention, the temperature of the gas stream is measured in at least one channel-shaped subchamber and matched, if required, to the amount of gas fed into the sorption store in such a way that a predetermined maximum temperature in the channel-shaped subchamber is not exceeded. Various materials are suitable as adsorption medium. The adsorption medium preferably comprises zeolite, activated carbon or metal organic frameworks. The porosity of the adsorption medium is preferably at least 0.2. The porosity is defined as the ratio of void volume to total volume of any subvolume in the container. At a low porosity, the pressure drop on flowing through the adsorption medium increases, which has an adverse effect on the charging time. In a preferred embodiment of the invention, the adsorption medium is present as a bed of pellets and the ratio of permeability of the pellets to the smallest pellet diameter is at least 10 ^"14 m ² /m. The rate at which the gas penetrates into the pellets during charging depends on the speed at which the pressure in the interior of the pellets approaches the pressure on the outside of the pellets. The time required for this pressure equalization and thus also the loading time of the pellets increases with decreasing permeability and with increasing diameter of the pellets. This can have a limiting effect on the total process of charging and discharging.

The time required for charging can be reduced further when the gas is cooled before being introduced.

The at least one separation element or a plurality of separation elements, in particular all separation elements present, preferably have a double wall so that a heat transfer medium can flow through them. Preference is also given to all channel walls of the channel-shaped subchambers being double walls to allow a heat transfer medium to flow through them.

Depending on the arrangement of the at least one separation element or the plurality of separation elements, a section of the interior wall of the container forms a channel wall of a channel-shaped subchamber or a plurality of channel-shaped subchambers. In this case too, the container wall is preferably a double wall. In a particularly preferred embodiment, the entire container wall including the end faces is configured so as to allow a heat transfer medium to flow through it, in particular configured as a double wall.

Depending on the temperature range which is suitable for the cooling or heating of the gas in the sorption store, various heat transfer media, for example water, glycols, alcohols or mixtures thereof, are possible. Appropriate heat transfer media are known to those skilled in the art.

It has been found to be advantageous for the spacing of the channel walls in each channel- shaped subchamber to be from 2 cm to 8 cm. Here, the term spacing refers to the shortest distance between two points on opposite walls viewed in cross section perpendicular to the axis of the channel. In the case of a channel having a circular cross section, for example, the spacing corresponds to the diameter, in the case of an annular cross section it corresponds to the width of the annulus and in the case of a rectangular cross section it corresponds to the shorter distance between the parallel sides. Particularly when all channel walls are cooled or heated, the range mentioned has been found to be a good compromise between heat transfer and fill volume of the adsorption medium. At greater spacings, heat transfer between adsorption medium and wall deteriorates, and in the case of smaller spacings the fill volume of the adsorption medium at given external dimensions of the container decreases. In addition, the weight of the sorption store and its production costs increase, which is disadvantageous, in particular in the case of mobile applications.

In a preferred embodiment, the spacings of the channel walls in the channel-shaped subchambers differ by not more than 40%, particularly preferably by not more than 20%. Such a configuration aids uniform removal of heat during charging and introduction of heat during emptying of the container.

The container of the sorption store is preferably cylindrical and the at least one separation element is arranged essentially coaxially to the axis of the cylinder. Embodiments in which the longitudinal axis of the at least one separation element is inclined by a few degrees up to a maximum of 10 degrees relative to the axis of the cylinder are considered to be "essentially" coaxial. This configuration ensures that the channel cross sections vary only slightly along the axis of the cylinder, so that uniform flow over the length of the channel can be established. Depending on the space available for installation and the maximum permissible pressure in the container, various cross-sectional areas for the cylindrical container are possible, for example circular, elliptical or rectangular. Irregularly shaped cross-sectional areas are also possible, e.g. when the container is to be fitted into a hollow space of a vehicle body. Circular and elliptical cross sections are particularly suitable for high pressures above about 100 bar.

The invention further provides a sorption store for storing gaseous substances, which comprises a closed container and a feed device which comprises a passage through the container wall, through which a gas can flow into the container. The container has at least one separation element which is located in its interior and is configured so that the interior of the container is divided into at least two parallel, channel-shaped subchambers which are each at least partly filled with an adsorption medium and whose channel walls are coolable. According to the invention, viewed in cross section, the contours of the interior wall of the container and the at least one separation element and optionally the plurality of separation elements is/are essentially conformal.

In this context, conformal means that the contours have the same shape, for example all circular, all elliptical or all rectangular. The expression "essentially conformal" means that small deviations from the basic shape are still encompassed by "the same shape". Examples are round corners in the case of a rectangular basic shape or deviations within manufacturing tolerances. Such a configuration allows optimal utilization of the interior space of the container with a view to a very large amount of adsorption medium combined with efficient heating management.

The above-described preferred structural features such as the double-walled separation elements, spacings of the channel walls and/or the coaxial arrangement of the separation elements in a cylindrical container also represent preferred embodiments of the sorption store of the invention.

The choice of the wall thickness of the container and of the separation elements depends on the maximum pressure to be expected in the container, the dimensions of the container, in particular its diameter, and the properties of the material used. In the case of an alloy steel container having an external diameter of 10 cm and a maximum pressure of 100 bar, the minimum wall thickness has, for example, been estimated at 2 mm (in accordance with

DIN 17458). The internal spacing of the double walls is selected so that a sufficiently large volume flow of the heat transfer medium can flow through them. It is preferably from 2 mm to 10 mm, particularly preferably from 3 mm to 6 mm.

The at least one separation element is particularly preferably configured as a tube so that the interior space of the tube forms a first channel-shaped subchamber and the space between the outer wall of the tube and the interior wall of the container or optionally between the outer wall of the tube and a further separation element forms a second, annular channel-shaped

subchamber. The contour of the tubular separation element viewed in cross section is conformal with the contour of the interior wall of the container; they are, for example, both circular or both elliptical. In a further development of this embodiment according to the invention, a plurality of separation elements are present and are all configured as tubes having various diameters and are arranged coaxially. Their contours viewed in cross section are likewise conformal with the contour of the interior wall of the container.

The feed device comprises at least one passage through the container wall, through which a gas can flow into the container. In a particular embodiment, the feed device comprises a tubular feed line whose one end is connected to the at least one passage and which branches into a plurality of ends which open into the respective channel-shaped subchambers. In an alternative embodiment, the feed device comprises a plurality of passages through the container wall which are all connected at one end to a tubular feed line whose other end opens into the channel- shaped subchambers.

In a further advantageous embodiment, the feed device comprises components which divide the gas flowing in through the at least one passage in a specific way over all subchambers, e.g. a deflection element or a distribution device. The inflowing amount of gas is particularly preferably distributed over the channel-shaped subchambers in such a way that the ratios of the individual amounts of gas to one another correspond to the ratios of the cross-sectional areas of the subchambers. The feed device can also comprise means of influencing the gas flow, for example throttle valves or regulating valves. These means can be provided within or outside the container. It is also possible for a plurality of passages to be provided in the container wall, for example in order to introduce the gas into the channel-shaped subchambers in a plurality of places or to provide different passages for filling and for taking off gas. Preference is given to using the same passage or passages for taking off gas as for filling the container.

Compared to the prior art, the sorption store of the invention makes faster heat transport from the adsorption medium or into the adsorption medium possible. This significantly decreases the time required for charging of the store with a given amount of gas. As an alternative, the store can be charged with a larger amount of gas in a given time. When taking gas from the store, the invention makes rapid and constant provision of gas possible. For this purpose, the channel walls are heated, for example in the case of the double-walled configuration a heat transfer medium whose temperature is greater than the temperature of the gas in the channel-shaped subchambers is passed through the double wall. The sorption store of the invention is simple to construct and as a result of its compact construction is particularly suitable for mobile applications, for example in motor vehicles. The embodiment with double channel walls has the additional advantage that the heat transfer medium merely has to be changed or its temperature altered appropriately to change from cooling or heating. This embodiment is therefore suitable for mobile use both during filling and in the driving mode.

The invention is illustrated below with the aid of the drawings; the drawings are to be interpreted as in-principle depictions. They do not restrict the invention, for example in respect of specific dimensions or configurational variants of components. In the interest of clarity, they are generally not to scale, especially in respect of length and width ratios. The drawings show:

Fig. 1 : Embodiment of a sorption store according to the invention having a flow equalizer for inflowing gas

Fig. 2: Embodiment of a sorption store according to the invention having double channel walls, an elliptical cross-sectional area of the container and a plurality of passages

Fig. 3: Embodiment of a sorption store according to the invention having a rectangular cross section of the container

Fig. 4: Example of a flow diagram for determining the initial pressure for charging according to the invention of a sorption store

Fig. 5: Comparison of charging strategy according to the invention with conventional charging strategy List of reference numerals used

10 . . Container

1 1 . . Container wall

15 . . Separation element

16 . . Separation element

17 . . Separation element

21 . . Passage

22 . . Covering plate

30 . First subchamber

31 . . Second subchamber

32 . . Third subchamber

33 . . Fourth subchamber

40 . . Adsorption medium

5x . Process steps for determining the initial pressure

Figures 1 to 3 show schematic sections through sorption stores according to the invention. The illustrative sorption stores have an essentially cylindrical container 10. The upper drawings in each case depict longitudinal sections through the axis of the cylinder, and the drawings underneath each of these show corresponding cross sections perpendicular to the axis of the cylinder.

Fig. 1 shows a first preferred embodiment of a sorption store according to the invention. The container 10 has a circular cross section and at its end faces has a passage 21 through the container wall. A separation element 15 which is configured as a tube having a circular cross section and is arranged coaxially to the axis of the cylinder is located in the interior of the container 10. The interior space of the tube forms a first channel-shaped subchamber 30. The space between the outer wall of the tube and the interior wall of the container forms a second, annular channel-shaped subchamber 31. The separation element 15 has a spacing from the inlet-end end face; at the opposite end it extends to the end face of the container. In the example shown, the two subchambers 30, 31 are completely filled with an adsorption medium 40. At the end facing the passage 21 , the subchambers 30, 31 are bounded by a covering plate 22 which extends over the entire cross section of the container. In the example shown, five openings through which gas can flow into the subchambers are present in the covering plate 22. The covering plate functions as flow equalizer which ensures uniform flow of gas into the subchambers 30, 31. The openings shown are by way of example; they can also have another configuration. For example, annular or interrupted annular openings can be provided in the outer region which connects the passage 21 to the second subchamber 31 .

The broken-line arrows symbolize the gas flow within the container. Inflowing gas firstly goes into the space which is not filled with adsorption medium between the passage 21 and the covering plate 22 and becomes uniformly uniform distributed there. The gas flows through the openings in the covering plate into the two subchambers 30, 31 where it is adsorbed on the adsorption medium. The adsorption medium and the surrounding gas heat up as a result of the adsorption. The interior wall of the container 10 and the separation element 15 are cooled so that a radial temperature gradient is established between the middle of the channel-shaped subchambers and their peripheries. The second step of the feed strategy according to the invention, in particular, brings about continual gas flow into the container. Interaction of this with the radial temperature gradient results in circulating gas flows which ensure significantly better heat removal and thus lower maximum temperatures in the adsorption medium being established internally in the channel-shaped subchambers 30, 31. As a result, the container can be loaded with the same amount of gas in a shorter time than in the case of the conventional feed strategy in which the pressure is kept constantly high over the entire charging time.

Fig. 2 shows a further preferred embodiment of a sorption store according to the invention. The container 10 has an elliptical cross section and a tubular separation element 15 which likewise has an elliptical cross section is arranged coaxially to the axis of the cylinder in the interior of the container. As in the previous example, the interior space of the tubular separation element 15 forms a first channel-shaped subchamber 30 and the space between the outer wall of the tube and the interior wall of the container forms a second, annular channel-shaped subchamber 31. The channel walls of the channel-shaped subchambers 30 and 31 , which are formed by the container wall 1 1 and the separation element 15, have double walls so that a heat transfer medium can flow through the walls. Corresponding feed connections and discharge connections for a heat transfer medium are provided but are not shown in the figure. In this example, the entire interior volume of the container is filled with adsorption medium 40. The feed device comprises five passages 21 through the container wall, through which gas can flow into the interior of the container. The passages 21 are located at one end face of the container 10, are configured as tubes and are arranged uniformly around the circumference in the region of the annular, outer subchamber 31 and also centrally in the middle of the end face as inlet into the interior subchamber 30. In this embodiment, the separation element 15 extends at both ends to the respective end face of the container.

The broken-line arrows symbolize the gas flow within the container. In this example, the inflowing gas is distributed directly over the adsorption medium through the five passages 21. The formation of a temperature gradient and the gas flow circulating internally in the subchambers 30, 31 occurs analogously to the example described above for fig. 1.

Fig. 3 shows a further preferred embodiment of a sorption store according to the invention. The container has a cylindrical shape and an essentially rectangular cross section. The corners are rounded, and the container wall 1 1 is a double wall to allow a heat transfer medium to flow through it. The interior of the container is divided by three separation elements 15, 16, 17 into four channel-shaped subchambers 30 to 33. The separation elements are uniformly distributed in the longitudinal direction of the container, so that the subchambers likewise have rectangular cross sections with essentially identical internal areas. In the example shown, the cross sections of the subchambers are square with rounded corners. The separation elements are configured as double-walled plates and in the longitudinal direction run coaxially to the axis of the cylinder and in the transverse direction parallel to the interior container wall of the container opposite or parallel to the adjacent separation elements. The contours of the interior wall of the container and the separation elements viewed in cross section are thus conformal. In the axial direction and in the transverse direction, the separation elements each extend to the interior wall of the container and are joined thereto, so that four completely separate subchambers are obtained in the container.

A passage 21 through which gas can flow into the container is provided through an end face of the wall of the container for each subchamber 30, 31 , 32, 33. The passages 21 are tubular and extend into the respective subchamber. All channel-shaped subchambers are filled with an adsorption medium.

In this figure, too, the broken-line arrows symbolize the gas flow in the container. In a manner analogous to the embodiment of fig. 2, the inflowing gas is distributed over the adsorption medium directly through the passages 21. Owing to the cooling of the channel walls, a temperature gradient from the middle of the channel to the channel walls when viewed in cross section is established. As described in respect of fig. 1 , the feed strategy according to the invention brings about a continual gas flow into the container and in combination with the temperature gradient results in gas flows circulating internally in the channel-shaped subchambers 30, 31 , 32, 33, giving the above-described advantages.

To improve heat transfer, further components for transferring heat, e.g. a central tube in each subchamber 30, 31 , 32, 33 running along the axis of the cylinder in each case, can also be provided. Of course, such measures can also be advantageous in embodiments other than that shown in fig. 3.

Fig. 4 shows, by way of example, a flow diagram for determining the initial pressure po for the charging according to the invention of a sorption store. After the beginning 51 a starting value for the initial pressure po, for example 50% of the final pressure to be reached, is firstly selected in the initialization phase 52. Furthermore, an upper limit for the temperature T _ma x permissible in the store and also the desired end time t _e of filling, e.g. five minutes, are set down.

Step 53 comprises the actual carrying out of the experiment. An empty sorption store is charged with gas whose pressure at the inlet to the store is a constant po from the starting point in time to the point in time to which is, for example, set at one minute. Over the period of time from to to the end time t _e , the pressure at the inlet of the store is increased according to a predetermined function which approximates the course of the adsorption kinetics of the adsorption medium used. The maximum temperature reached during the loading operation in step 54 is compared with the predetermined upper limit T _ma x. If the upper limit is exceeded, the initial pressure po is reduced, for example by a predetermined value, a predetermined percentage or as interval nesting, in step 55. However, the pressure should not go below the minimum pressure amounting to 30% of the final pressure. A renewed experiment (step 53) using the reduced initial pressure is subsequently carried out.

However, if the predetermined upper temperature limit T _ma x is not reached, a check is carried out in the next step 56 as to whether the total loading of the store with gas is satisfactory at the end time t _e . The criterion can, for example, be a total loading of at least 95% of the maximum uptake capacity. If the loading is still not satisfactory, a further iteration in which the initial pressure po is increased in step 57 is carried out. The pressure can be increased, for example, by a predetermined value, a predetermined percentage or as interval nesting. A renewed experiment (step 53) using the increased initial pressure is subsequently carried out.

If the temperature criterion (step 54) is adhered to and the total loading is also satisfactory, the experimental program is ended (step 58). In this way, an optimal value for the initial pressure can be determined in a few, targeted experiments. The experiments are easy to carry out and are required only once for design of an actual sorption store. In an analogous way, or in combination with the above-described sequence, the feed strategy can be set down or optimized from the initial pressure to the final pressure.

Example

Results of simulation calculations carried out using the program OpenFOAM (from ENGYS) are shown below. The calculations are based on the following assumptions: - The bed of pellets can be regarded as a porous medium and as a homogeneous phase separate from the gas phase. It is thus not necessary for each individual pellet to be numerically resolved.

All pellets have the same properties in respect of size, permeability, density, heat capacity, conductivity, enthalpy of adsorption and adsorption kinetics.

- The flow effects in respect of the heat conduction of the bed can be described by known correlations.

The calculations are based on a cylindrical container having a circular cross section, an internal length extension of 100 cm and an internal diameter of 17 cm. In the interior of the container, a tube having a circular cross section is installed as separation element concentrically to the axis of the cylinder. It has a double wall and an internal diameter of 5 cm. Its wall thickness is a total of 1 cm, and the gap width between the walls of the double wall is 3 mm. The configuration corresponds to that of the example as per fig. 2 but with a circular cross section. The interior of the container is thus divided into two parallel, channel-shaped subchambers which are completely separate from one another. The spacings of the channel walls are 5 cm in both subchambers. The container wall is likewise a double wall having a wall thickness of a total of 1 cm, and the gap width between the walls of the double wall is 3 mm. The tubes connected to the passages 21 project 8 cm into the container.

The container has a fill volume of 19 liters and is filled with pellets of a metal organic framework (MOF) of the type 177 as adsorption medium. The MOF type 177 comprises zinc clusters which are joined via 1 ,3,5-tris(4-carboxyphenyl)benzene as organic linker molecule. The specific surface area (Langmuir) of the MOF is in the range from 4000 to 5000 m ² /g. Further information on this type may be found in US 7,652,132 B2. The pellets have a cylindrical shape with a length of 3 mm and a diameter of 3 mm. Their permeability is 3-10 ^-16 m ² . The ratio of permeability to smallest pellet diameter is thus 10 ^"13 m ² /m. The porosity of the bed is 0.47.

The filling of the container with pure methane, which is fed in with a temperature of 27°C, is examined. The predetermined final pressure is 90 bar absolute. A heat transfer medium flows through the container wall and the respective separation elements in such a way that a constant wall temperature of 27°C is established. Under these conditions, the container can be filled with a maximum of 2 kg of methane.

The lower graph in fig. 5 shows the results of two scenarios. In the comparative scenario (solid curve), the gas is fed into the above-described container at a constant pressure of 90 bar from the beginning. The final pressure of 90 bar is reached in the container within the first minute. After about 32 minutes, 0.9 kg of methane has been adsorbed (time ti in fig. 5). At this point in time, the voids of the bed of pellets have been filled with a further kilogram of methane, so that the container is loaded to an extent of 95% with methane.

In the scenario according to the invention (broken curve), the same container configuration as in the comparative scenario is used as a basis. However, the gas is fed in at only 80 bar for a time of one minute at the beginning until the internal pressure in the container has risen to 80 bar. The inlet pressure of the methane fed in is subsequently increased over a time of 30 minutes to the final pressure of 90 bar according to a function matched to the adsorption kinetics:

p(t) = po + Δρ ^■ (1 - e- ^{k t} ) where p ₀ = 80 bar, Δρ = 10 bar and k = 0.0025 s ^"1 .

The course of the pressure over time is shown in the upper graph in fig. 8. In the case of the tank under consideration, the simulated MOF type displays heat removal which is fast relative to the adsorption kinetics, and a value of about 90% of the final pressure is therefore selected as initial pressure. A major part of the methane to be adsorbed is adsorbed within the first minutes. This results in a sharp rise in the temperature of the adsorption medium. The simulation results demonstrate that a flow circulating internally in the channel-shaped subchambers is induced by means of this mode of operation according to the invention. As a result of the flow, the heat evolved in the adsorption medium as a result of the adsorption is removed more quickly at the cooled walls. This in turn leads to the adsorption occurring more quickly and the container being loaded to an extent of 95% with methane after only about 26 minutes (time t.2 in the lower graph in fig. 5).