Reactor for releasing hydrogen from a liquid compound
US-2016136610-A1 · May 19, 2016 · US
US10710877B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10710877-B2 |
| Application number | US-201515326118-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jan 27, 2015 |
| Priority date | Jul 18, 2014 |
| Publication date | Jul 14, 2020 |
| Grant date | Jul 14, 2020 |
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The present invention provides a hydrogen generating apparatus and a hydrogen generating method, wherein the hydrogen generating apparatus generates hydrogen by dehydrating formic acid, and comprises: a reactor for containing water and a heterogeneous catalyst; a formic acid feeder for feeding formic acid into the reactor; and a moisture remover for removing moisture generated from the reactor.
Opening claim text (preview).
The invention claimed is: 1. An apparatus for generating hydrogen by dehydrogenation of a formic acid, comprising: a reactor containing a heterogeneous catalyst, wherein the reactor has an opening within the reactor capable of feeding water to the reactor; a syringe pummp connected to the reactor configured to supply a formic acid into the reactor; a moisture remover connected to the reactor configured to remove moisture generated at the reactor; and a cold trap bath configured to condense the moisture removed by the moisture remover and supply the condensed moisture as in a form of water to the reactor, wherein the cold trap bath is connected to the reactor to supply the water to the reactor via the opening, wherein the heterogeneous catalyst comprises a metal heterogeneous catalyst and a catalyst support, wherein the metal heterogeneous catalyst is at least one selected from the group consisting of Pt, Rh, Ru, Au, Ag, Pd, Ni, Co, Cu, and Fe. 2. The apparatus for generating hydrogen according to claim 1 , wherein the heterogeneous catalyst is a solid catalyst. 3. The apparatus for generating hydrogen according to claim 1 , wherein the formic acid supplied to the reactor by the syringe pump is an aqueous formic acid solution with a concentration of 70 to 99.9 wt %. 4. The apparatus for generating hydrogen according to claim 1 , wherein the syringe pump supplies the formic acid to the reactor at a feed rate of 0.1 mL to 2.2 L per minute. 5. The apparatus for generating hydrogen according to claim 1 , wherein the water contained in the reactor and the formic acid supplied to the reactor by the syringe pump are mixed at the reactor to form an aqueous formic acid solution with a concentration of 20 to 90 wt %. 6. The apparatus for generating hydrogen according to claim 1 , wherein the catalyst support is at least one selected from the group consisting of a metal foam, a carbon support, and a porous support. 7. The apparatus for generating hydrogen according to claim 6 , wherein the carbon support is any one of any one of a carbon sheet, a carbon felt, a carbon black, and a carbon nanotube. 8. The apparatus for generating hydrogen according to claim 6 , wherein the porous support is any one of Al2O3, ZrO2, TiO2, and CeO2. 9. The apparatus for generating hydrogen according to claim 1 , wherein the metal heterogeneous catalyst is Pd/meso porous g-C3N4 (Pd/mpg-C3N4). 10. A method for generating hydrogen by dehydrogenation of a formic acidly by utilizing the apparatus of claim 1 , comprising, adding a formic acid to a mixture of water and a heterogeneous catalyst to perform a dehydrogenation reaction. 11. The method for generating hydrogen according to claim 10 , further comprising: removing a moisture generated at the dehydrogenation reaction. 12. The method for generating hydrogen according to claim 11 , further comprising: condensing the moisture removed in the moisture removing step and using the condensed moisture as water for the dehydrogenation reaction. 13. The method for generating hydrogen according to claim 10 , wherein the formic acid is an aqueous formic acid solution with a concentration of 70 to 99.9 wt %. 14. The method for generating hydrogen according to claim 10 , wherein the formic acid is added at a feed rate of 0.1 mL to 2.2 L per minute. 15. The method for generating hydrogen according to claim 10 , wherein the water and the formic acid are mixed to form an aqueous formic acid solution with a concentration of 20 to 90 wt %.
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