METHOD FOR OBTAINING HYDROGEN

Information

  • Patent Application
  • 20070202037
  • Publication Number
    20070202037
  • Date Filed
    February 01, 2007
    17 years ago
  • Date Published
    August 30, 2007
    16 years ago
Abstract
The present invention provides a new method for obtaining hydrogen gas that comprises the stages of providing at least one aluminium alloy; providing at least one hydride of general formula (I), where X is selected between B and Al; Y is selected from among Li, Na, K, Mg, Ca and Al; and n is an integer number from 1 to 3; and providing an aqueous medium; so that the reaction between said aluminium alloy with said hydride in said aqueous medium is carried out at a temperature between 4 and 300° C. to produce hydrogen gas and other reaction products with good yields.
Description

BRIEF DESCRIPTION OF THE FIGURES


FIG. 1 shows the evolution of hydrogen gas (volume in ml) obtained from 0.210 g of an Al/Si alloy, in which the medium is water at 75° C. (-♦-), water with 0.2 g/l of Ca(OH)2 at 75° C. (-▴-) and water with 2.0 g/l of Ca(OH)2 at 75° C. (-▪-). Said figure describes hydrogen being obtained from the state of the art prior to the present invention.



FIG. 2 shows the evolution of hydrogen gas (ml) obtained from a mixture of 0.210 g of an Al/Si alloy and 0.103 g of NaBH4 (-▪-), in which the medium is water at 75° C., when compared with the addition (-♦-) of hydrogen gas obtained using 0.210 g of an Al/Si alloy and hydrogen gas obtained using 0.103 g of NaBH4 separately.



FIG. 3 shows the evolution of hydrogen gas (ml) obtained from a mixture of 0.219 g of an Al/Si alloy and 0.107 g of NaBH4 (-▪-), in which the medium is water with 0.2 g/l of Ca(OH)2 at 75° C., when compared with the addition (-♦-) of hydrogen gas obtained using 0.219 g of an Al/Si alloy hydrogen gas obtained using 0.107 g of NaBH4 separately.



FIG. 4 shows the evolution of hydrogen gas (ml) obtained from 0.219 g of an Al/Co alloy and 0.114 g of NaBH4 (-▪-), in which the medium is water with 2.0 g/l of Ca(OH)2 at 75° C., when compared with the addition (-♦-) of hydrogen gas obtained using 0.219 g of an Al/Co alloy and hydrogen gas obtained using 0.114 g of NaBH4 separately.



FIG. 5 shows the evolution of hydrogen gas (ml) obtained from a mixture of 0.215 g of an Al/Mg alloy and 0.102 g of NaBH4 (-▪-), in which the medium is water with 2.0 g/l of Ca(OH)2 at 75° C., when compared with the addition (-♦-) of hydrogen gas obtained using 0.215 g of an Al/Mg alloy and hydrogen gas obtained using 0.102 g of NaBH4.



FIG. 6 shows the evolution of hydrogen gas (ml) obtained from a mixture of 0.210 g of an Al/Si alloy and 0.109 g of NaBH4 (-▪-), in which the medium is water with 2.0 g/l of Ca(OH)2 at 75° C., when compared with the addition (-♦-) of hydrogen gas obtained using 0.210 g of an Al/Si alloy and hydrogen gas obtained using 0.109 g of NaBH4, and both evolutions of hydrogen gas separately: Al/Si (-χ-) and NaBH4 (-▴-).


Claims
  • 1. A method for obtaining hydrogen gas, comprising the following steps: i) providing at least one aluminium alloy;ii) providing at least one hydride of general formula (I): Y[XH4]n where X is selected between B and Al; Y is selected from among Li, Na, K, Mg, Ca and Al; and n is an integer number from 1 to 3; andiii) providing an aqueous medium;so that the reaction between said aluminium alloy with said hydride in said aqueous medium is carried out at a temperature between 4 and 300° C. to produce hydrogen gas and other reaction products.
  • 2. Method according to claim 1, wherein said aluminium alloy is selected from among Al/Si, Al/Co and Al/Mg.
  • 3. Method according to claim 1, wherein said aqueous medium is water.
  • 4. Method according to claim 1, wherein said aqueous medium is prepared by dissolving a base in water.
  • 5. Method according to claim 4, wherein said base is selected from Ca(OH)2, NaOH, KOH and mixtures thereof.
  • 6. Method according to claim 5, wherein the Ca(OH)2 is in any concentration up to saturation.
  • 7. Method according to claim 5, wherein the NaOH is in a concentration of up to 5M.
  • 8. Method according to claim 5, wherein the KOH is in a concentration of up to 5M.
  • 9. Method according to claim 1, wherein the temperature is between 50 and 100° C.
  • 10. Method according to claim 1, wherein the percentage of aluminium in relation to the compounds provided in stages i) and ii) is between 10% and 95% by weight.
  • 11. Method according to claim 10, wherein the percentage of aluminium is between 20 and 70% by weight.
  • 12. Method according to claim 1, wherein the compounds provided in stages i) and ii) are in the form of powder, flakes, pellets, monoliths, granules or foils.
  • 13. Method according to claim 12, wherein the compounds provided in stage i) are in powder form.
  • 14. Method according to claim 12, wherein the compounds provided in stage ii) are in powder form.
Priority Claims (1)
Number Date Country Kind
06110007.9 Feb 2006 EP regional