the present invention relates to the use of supercritical fluids ( scfs ) as a medium to effect the hydrogenation of aluminum , thereby forming alane . over the past decade , scfs have developed from laboratory curiosities to occupy an important role in synthetic chemistry and industry . scfs combine the most desirable properties of a liquid with those of a gas : these include the ability to dissolve solids and total miscibility with permanent gases . for example , supercritical ( sc ) co 2 has found a wide range of applications in homogeneous catalysis , including such processes as hydrogenation , hydroformylation and olefin metathesis . heterogeneous catalyses carried out in scco 2 includes fischer - tropsch synthesis and hydrogenation . furthermore , sch 2 o has also found wide utility in enhancing organic reactions . alane is a very attractive system for hydrogen storage , being a simple binary hydride containing 10 . 1 wt % hydrogen with a theoretical h density of 148 g / l , and possessing a higher volumetric hydrogen capacity than liquid hydrogen . the material is marginally stable at room temperature , releasing h 2 between 60 and 140 ° c . aluminum is cheap , safe and plentiful and is widely used in 21 st century technologies . alane thus clearly satisfies four of the five doe criteria . according to the understanding prior to this invention , the major drawback is its lack of reversibility : direct combination of al and h 2 requires draconian pressures — in excess of 25 kbar . the thermodynamic properties of alh 3 vitiate conventional gas - solid synthesis : alh 3 is thermochemically on the cusp with respect to decomposition to al and h 2 ( the α -, β - and γ - phases of alh 3 have δh dehyd values of ca . + 6 , − 4 and + 1 kj mol − 1 , respectively ). thus , even at very high pressures of h 2 , the modest thermal input needed to overcome the activation barrier will place the system thermodynamically in favor of the elements ( i . e . to the left of eq . 3 ). scfs have unique properties that allow us to overcome this antagonistic interplay between the kinetic and thermodynamic properties of the system . the total miscibility of h 2 with a scf is a distinct advantage in this respect , allowing effective concentrations of hydrogen equivalent to hundreds of bar to be attained easily and efficiently , and favoring the thermodynamics of alh 3 over the elements . in addition , conventional solvents may be added to the scf medium to enhance the solubility of reactants and / or products , allowing one to alter the kinetic and / or thermodynamic profile of the reaction ( q . v .). this is particularly important for a system like alh 3 that is thermally fragile . furthermore , the high diffusivity of permanent gases in scf media encourages favorable kinetics to be established close to room temperature . examples of supercritical fluid systems and reaction conditions that can be used to produce alane by direct hydrogenation of aluminum include , but are not limited to : co 2 ( 75 bar ), h 2 ( 30 - 50 bar ) 50 - 60 ° c ., 2 - 4 h ; dimethyl ether ( 8 bar ), h 2 ( 30 - 40 bar ), 125 ° c ., 2 - 4 h ; ethane ( 65 bar ), h 2 ( 30 - 40 bar ), 90 ° c ., 2 - 4 h ; and ternary mixtures of me 2 o , co 2 and h 2 . fig1 is a schematic diagram of the apparatus used to regenerate alane from a dehydrogenated sample of the material . in fig1 , there is shown a high pressure reaction vessel 1 , which is in fluid communication by way of piping and valves with a me 2 o cylinder 2 , a co 2 cylinder 3 , a co 2 pump 4 and a h 2 cylinder 5 . customary symbols for valves are shown in the lines connecting the various components of the apparatus . a sample of alane prepared by conventional methods was doped with ticl 3 ( 2 mol %) in order to facilitate h 2 evolution and absorption , then the material was dehydrogenated , giving a light gray powder . a powder x - ray diffraction pattern of the resulting material showed only peaks arising from al . the material was then introduced into a 100 ml stainless - steel pressure reactor 1 under a blanket of inert gas . examples of inert gases that are suitable for use in the systems and methods of the invention include helium , argon and nitrogen . nitrogen having negligible oxygen content can be obtained as the boil - off gas from liquid nitrogen , or by gettering nitrogen over metal shavings heated to elevated temperatures ( e . g ., iron heated to 800 ° c .). see for example , j . b . milstein and l . f . saunders , “ gettering of gases for high purity applications ,” j . crystal growth 89 , 124 ( 1988 ). a small amount of me 2 o was admitted from tank 2 to vessel 1 as a vapor ( 50 psi ) under its own head pressure . liquid co 2 ( 890 psi ) was next admitted to vessel 1 from tank 3 with the aid of pump 4 , and finally h 2 , ( 500 psi was added from tank 5 to vessel 1 . the reaction mixture in 1 was then heated to 60 ° c ., thereby forcing the co 2 / h 2 mixture into a supercritical phase , and the contents were stirred at 150 rpm for 1 h . preferably , a temperature below 100 ° c . is employed . suitable stirring apparatus can include any of a mechanical stirrer and a magnetic stirrer . at this point , vessel 1 was cooled to room temperature and all volatile material was removed by venting and pumping , for 1 h . reaction vessel 1 was then disconnected from the other components in fig1 , transported into an inert atmosphere glove box , and opened revealing a gray powder , albeit slightly different in color and appearance to the starting material . in fig1 features such as heating and cooling apparatus , vents to allow components or reagents to be removed from the system and controllers to operate the heating apparatus , the cooling apparatus and the valves are not shown . conventional pressure sensing equipment that provides an electrical signal indicative of a pressure can be used to sense and to control pressures in the various portions of the equipment . electrically or pneumatically operated valves can be used to control the timing and the flow rates as gases and fluids are moved from one container to another , or are held in a container , or are vented . conventional electrical heaters and conventional fluid based ( e . g ., water ) thermal exchange systems can be used to heat and cool the reaction vessel to the moderate temperatures required . conventional thermal controllers , using sensors such as thermocouples , and feedback circuits that sense temperature and compare the temperature to a set point can be employed . in some embodiments , conventional general purpose programmable computers can be used to implement the control functions for thermal control and for pumping , mass flow , and pressure control . in some cases , a person is permitted to control the valves and the operation of the apparatus . it is anticipated that higher yields of alane may be obtained . in particular , several factors could cause a reduction of the amount of alane measured as compared to the amount of alane produced in the process . first , the pressure of the system has to be reduced to remove the alane , thereby reducing the partial pressure of hydrogen available for equilibrium with the product , which might permit the product to decompose to some unknown extent . in addition , the specimen to be examined is removed from the vessel 1 , and may be exposed to both oxygen and water vapor in the air ambient that is present during the analysis , even though the specimen is intended to be protected from reactive environments during the analysis . fig2 is an image of a commercially available reactor for carrying out reactions using supercritical fluids . this reactor , and similar high pressure , compact laboratory reactors , are available from parr instrument company , 211 fifty third street , moline , ill . 61265 - 9984 , or from several other sources . these reactors can be obtained with controllers that are used to monitor , control , datalog and archive various parameters , including temperature control , stirring speed control , monitor pressure , log data , control gas and liquid feeds and handle the product produced . in some instances a pc user interface is used to control one or more reactors . fig3 and 4 are pressure - composition - temperature ( pct ) graphs that illustrate the progress of a dehydrogenation process for a specimen of aluminum with titanium hydrogenated under conditions similar to those described with respect to fig1 . fig5 is a gas chromatograph ( gc ) plot that illustrates the release of hydrogen from a sample of aluminum with titanium hydrogenated using scco 2 (˜ 70 bar )/ h 2 (· 35 bar ), for 20 hours at a temperature of 60 ° c ., in which the lower curve represents a control plot of the nitrogen carrier gas , and the upper curve represents the gas desorbed by heating the hydrogenated sample of aluminum with titanium in the presence of the nitrogen carrier gas . in a second method we expect that a doped supercritical co 2 reaction medium can be used to prepare alane . we also expect that one can use a completely different supercritical fluid , to create a better thermodynamic environment . it is expected that one can form an intermediate molecular alane adduct , l . alh 3 , whose enthalpy of complex formation ( δhc ) is more favorable than that of naked alh 3 , and which can then be heated to temperatures close to ambient to remove the donor l and produce the desired polymeric ( alh 3 ) x material . we believe that the likelihood of this procedure working is high , as a similar two - stage process is employed to stabilize alane and then decomplex it in the so - called ‘ organometallic route ’ that is currently the only method of making the material . it is expected that the donor molecule l , can be any one of a range of materials including ethers ( such as me 2 o and et 2 o ) and amines ( such as me 3 n and et 3 n ). we expect that either or both of the 1 : 1 and 2 : 1 l . alh 3 complexes may serve as useful stabilized intermediates in the formation of alane . we expect that the addition of molecular hydrogen transfer catalysts ( e . g . wilkinson &# 39 ; s catalyst ) to the scf reaction mixture may also be effective , in addition to the solid - state catalysts ( e . g . ti ) incorporated in the al substrate . as we have already explained , the marginal thermodynamic stability of alane has thwarted its direct preparation from al and h 2 according to the reaction shown in eq . 3 given above , except under conditions of extreme temperature and pressure . we expect that the use of alternative scf media and mixtures with donor solvent or co - solvent capability , along with the use of hydrogen transfer catalysts , will allow the stabilizing of a molecular adduct of nl . alh 3 intermediate ( with n = 1 or n = 2 ), while subsequent removal of the donor l and transformation to the polymeric binary hydride ( eqs . 4 and 5 ). it has already been demonstrated that triethylenediamine ( teda ) can stabilize alh 3 sufficiently to permit direct reaction between al and h 2 in conventional hydrocarbon solvents to form polymeric alh 3 . teda . however , the strongly - bound teda ligand is not removable from the alh 3 in this product , therefore rendering the adduct ineffective for preparation of pure alane . see “ the direct synthesis of amine alanes .” e . c . ashby , journal of the american chemical society , 1964 , vol . 86 , p . 1882 . see also “ the direct and reversible synthesis of the alh 3 adduct of triethylenediamine ( teda ) starting with activated al and hydrogen ,” james joseph reilly , jason graetz , james wegryzn , yusuf celibi , john johnson and wei - min zhou , mrs fall meeting , boston , 2007 . examples of adducts that can be prepared ( or that are believed to be capable of being prepared ) include adducts using molecular oxygen donor ligands such as dimethyl ether ( me 2 o ), diethyl ether ( et 2 o ), dioxane , ethylmethyl ether ( meoet ), tetrahydrofuran ( thf ), and molecular nitrogen donor ligands such as pyridine , quinuclidine , trimethylamine ( me 3 n ), triethylamine ( et 3 n ), and triethylenediamine ( teda ). representative dft - calculated energies of complex formation ( δhc ) are given in table i for oxygen donor ligands , and in table ii for nitrogen donor ligands , for the gas phase reactions described in eqs . 6 and 7 . fig6 through 9 are diagrams of illustrative conceptual diagrams of various one - and two - ligand adducts taken from the contents of tables i and ii . fig6 is an illustrative conceptual diagram of the 1 : 1 oxygen donor ligand adduct alh 3 . et 2 o . fig7 is an illustrative conceptual diagram of the 1 : 2 oxygen donor ligand adduct alh 3 . thf . fig8 is an illustrative conceptual diagram of the 1 : 1 nitrogen donor ligand adduct alh 3 . me 3 n . fig9 is an illustrative conceptual diagram of the 1 : 2 nitrogen donor ligand adduct alh 3 . 2teda . various uses for alane material can be suggested , including hydrogen storage , provision of hydrogen recovered from alane , and use of alane fuses in solid fuels for booster rockets . general purpose programmable computers useful for controlling instrumentation , recording signals and analyzing signals or data according to the present description can be any of a personal computer ( pc ), a microprocessor based computer , a portable computer , or other type of processing device . the general purpose programmable computer typically comprises a central processing unit , a storage or memory unit that can record and read information and programs using machine - readable storage media , a communication terminal such as a wired communication device or a wireless communication device , an output device such as a display terminal , and an input device such as a keyboard . the display terminal can be a touch screen display , in which case it can function as both a display device and an input device . different and / or additional input devices can be present such as a pointing device , such as a mouse or a joystick , and different or additional output devices can be present such as an enunciator , for example a speaker , a second display , or a printer . the computer can run any one of a variety of operating systems , such as for example , any one of several versions of windows , or of macos , or of unix , or of linux . in operation , a general purpose programmable computer is programmed with instructions in the form of software or firmware . the instructions control the operation of the general purpose programmable computer / the general purpose programmable computer can perform a variety of manipulations of data , such as mathematical operations ( e . g ., calculations ), logical operations ( e . g ., comparisons , or logical deductions following defined rules ), and processing of textual or graphical data ( e . g ., word processing , or image processing ). data can be provided to the general purpose programmable computer as recorded data or as real - time data . the result of any computation or processing operation is recorded in a machine - readable medium or memory for immediate use or for future use . for example , in micro - processor based analysis modules , data can be recorded in a register in a microprocessor , in a cache memory in the microprocessor , in local memory such as semiconductor memory ( e . g ., sram , dram , rom , eprom ), magnetic memory ( e . g ., floppy disc or hard disc ) and / or optical memory ( e . g ., cd - rom , dvd , hd - dvd ), or in a remote memory such as a central database . future use of data recorded in a machine - readable medium can include displaying , printing , or otherwise communicating the data to a user , using the data in a further calculation or manipulation , or communicating the data to another computer or computer - based device . machine - readable storage media that can be used in the invention include electronic , magnetic and / or optical storage media , such as magnetic floppy disks and hard disks ; a dvd drive , a cd drive that in some embodiments can employ dvd disks , any of cd - rom disks ( i . e ., read - only optical storage disks ), cd - r disks ( i . e ., write - once , read - many optical storage disks ), and cd - rw disks ( i . e ., rewriteable optical storage disks ); and electronic storage media , such as ram , rom , eprom , compact flash cards , pcmcia cards , or alternatively sd or sdio memory ; and the electronic components ( e . g ., floppy disk drive , dvd drive , cd / cd - r / cd - rw drive , or compact flash / pcmcia / sd adapter ) that accommodate and read from and / or write to the storage media . as is known to those of skill in the machine - readable storage media arts , new media and formats for data storage are continually being devised , and any convenient , commercially available storage medium and corresponding read / write device that may become available in the future is likely to be appropriate for use , especially if it provides any of a greater storage capacity , a higher access speed , a smaller size , and a lower cost per bit of stored information . well known older machine - readable media are also available for use under certain conditions , such as punched paper tape or cards , magnetic recording on tape or wire , optical or magnetic reading of printed characters ( e . g ., ocr and magnetically encoded symbols ) and machine - readable symbols such as one and two dimensional bar codes . while the present invention has been particularly shown and described with reference to the structure and methods disclosed herein and as illustrated in the drawings , it is not confined to the details set forth and this invention is intended to cover any modifications and changes as may come within the scope and spirit of the following claims .