Integrated process for the sustainable and autonomous co2-emission-free production of hydrogen and related system
US-2024200017-A1 · Jun 20, 2024 · US
US9452932B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9452932-B2 |
| Application number | US-201214354854-A |
| Country | US |
| Kind code | B2 |
| Filing date | Aug 8, 2012 |
| Priority date | Oct 28, 2011 |
| Publication date | Sep 27, 2016 |
| Grant date | Sep 27, 2016 |
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The present invention relates to a hydrogen production module by an integrated reaction/separation process, and a hydrogen production reactor using the same, and more specifically, provides a hydrogen production apparatus which laminates a plurality of layered unit cells, is mounted in a pressure-resistant chamber, and can be operated at a high pressure, wherein the unit cell comprises a first modified catalyst, and a second modified catalyst opposite to a hydrogen separator. The hydrogen production module can produce hydrogen using a hydrocarbon, carbon monoxide and an alcohol as sources. Particularly, all the modified catalysts are formed into a porous metal plate form, thereby maximizing the heat transfer effect necessary for reaction. While a reaction and separation of hydrogen simultaneously occur, separated reactants permeate the first modified catalyst so as to come in contact with the same, and then pass through the gap between the hydrogen separator and the second modified catalyst opposite to each other. Therefore, it is possible to obtain a high efficiency over the equilibrium conversion rate of reaction temperature, and high purity hydrogen can be obtained.
Opening claim text (preview).
The invention claimed is: 1. A hydrogen production module comprising: a reaction gas inlet plate on which a reaction gas channel is formed on an upper surface thereof; a first reforming catalyst plate which is laminated on the reaction gas inlet plate, and includes a first reforming catalyst which is transmissive to a reaction gas and is provided in a first reforming catalyst insertion hole formed therein; a reforming gas transfer plate which is laminated on the first reforming catalyst plate, and includes a reforming gas channel formed on a lower surface thereof at a position corresponding to the first reforming catalyst; a second reforming catalyst plate which is laminated on the reforming gas transfer plate, and includes a second reforming catalyst which is non-transmissive to the reaction gas and is provided in a second reforming catalyst insertion hole formed therein; a gap holding plate which is laminated on the second reforming catalyst plate, and includes a gap flow hole formed therein at a position corresponding to the second reforming catalyst; a hydrogen separation membrane plate which is laminated on the gap holding plate, and includes a hydrogen separation membrane which is provided in a hydrogen separation membrane insertion hole formed at a position corresponding to the gap flow hole; and a hydrogen transfer plate which is laminated on the hydrogen separation membrane plate, and includes a hydrogen transfer channel formed on a lower surface thereof at a position corresponding to the hydrogen separation membrane, which are sequentially laminated in this order, wherein each of the reaction gas inlet plate, the first reforming catalyst plate, the reforming gas transfer plate, the second reforming catalyst plate, the gap holding plate, the hydrogen separation membrane plate, and the hydrogen transfer plate of a laminated structure has a hydrogen gas outlet hole, a reaction gas inlet hole, and an impermeable gas outlet hole, which are respectively formed so as to pass through the laminated plates being disposed at positions spaced apart from each other, the reaction gas inlet hole is communicated with the reaction gas channel in the reaction gas inlet plate, the reforming gas transfer plate has a reforming gas supplying hole formed therein to be communicated with the reforming gas channel, the second reforming catalyst plate and the gap holding plate have a reforming gas supplying hole formed therein to be communicated with the reforming gas supplying hole of the reforming gas transfer plate, the gap flow hole is communicated with the reforming gas supplying hole and the impermeable gas outlet hole in the gap holding plate, and the hydrogen transfer channel is communicated with the hydrogen gas outlet hole in the hydrogen transfer plate. 2. A hydrogen production reactor comprising: the hydrogen production module of claim 1 ; and an upper plate and a lower plate which cover an upper portion and a lower portion of the hydrogen production module to protect the same, wherein the reaction gas inlet hole formed in the reaction gas inlet plate which is one component of the hydrogen production module is connected with a reaction gas inlet pipe into which a reaction gas is flowed through the lower plate from an outside, the impermeable gas outlet hole formed in the reaction gas inlet plate is connected with an impermeable gas discharge pipe through the lower plate so as to discharge an impermeable gas to the outside, and the hydrogen gas outlet hole of the hydrogen transfer plate or the hydrogen gas outlet hole of the reaction gas inlet plate is connected with a hydrogen discharge pipe to discharge a hydrogen gas through the upper plate or the lower plate. 3. The hydrogen production reactor according to claim 2 , wherein the reaction gas inlet hole has a cross-sectional that is larger than a cross-sectional area of the impermeable gas outlet hole. 4. The hydrogen production reactor according to claim 2 , comprising one or more of the hydrogen production module. 5. The hydrogen production reactor according to claim 4 , wherein the hydrogen production module is installed in a pressure chamber. 6. The hydrogen production reactor according to claim 5 , wherein the reaction gas supply pipe, the impermeable gas discharge pipe, and the hydrogen discharge pipe are disposed so as to be connected to the hydrogen production module by passing through the pressure chamber. 7. The hydrogen production module according to claim 5 , wherein the pressure chamber is supplied with a pressurized gas.
Heat exchange aspects · CPC title
containing a CO-shift step, i.e. a water gas shift step · CPC title
Catalysts coated on the surface of plates or inserts · CPC title
Plates arranged in parallel · CPC title
Natural gas or methane · CPC title
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