Dehydrogenation reaction apparatus and system including the same
A dehydrogenation reaction apparatus and a system including the same are disclosed. The dehydrogenation reaction apparatus includes: a main housing; and a dehydrogenation reactor which is provided inside of the main housing and has a catalyst provided inside. In particular, the dehydrogenation reactor generates hydrogen from a liquid organic hydrogen carrier (LOHC). The dehydrogenation reaction apparatus further includes: a heating device provided inside of the main housing and configured to apply heat to the dehydrogenation reactor through a phase change material, where the phase change material is provided between the main housing, and the dehydrogenation reactor and the heating device.
1 . A dehydrogenation reaction apparatus comprising:
a main housing;
a dehydrogenation reactor provided inside the main housing and including a catalyst, the dehydrogenation reactor configured to generate hydrogen from a liquid organic hydrogen carrier (LOHC); and
a heating device provided inside of the main housing and configured to apply heat to the dehydrogenation reactor through a phase change material,
wherein the phase change material is provided between the main housing, the dehydrogenation reactor and the heating device.
2 . The dehydrogenation reaction apparatus of claim 1 , wherein
the liquid organic hydrogen carrier comprises decalin, decahydronaphthalene, tetralin, 1,2,3,4-tetrahydronaphthalene, cyclohexane, dicyclohexyl, methylcyclohexane (MCH), N-ethylcarbazole (NEC), perhydro-N-ethylcarbazole, dibenzyltoluene (DBT), a mixture (BPDM) of biphenyl and diphenyl methane, a mixture of bicyclohexyl and dicyclohexylmethane, perhydro-monobenzyltoluene, perhydro-dibenzyltoluene, perhydro-N-methylindole, methylpiperidine, dimethylpiperidine, methylquinoline, bipiperidine, phenylpyridine, or combinations thereof.
3 . The dehydrogenation reaction apparatus of claim 1 , wherein
the catalyst comprises Pt/Al 2 O 3 , Pt/C, Pd/Al 2 O 3 , Pd/C, Pt—Sn/Al 2 O 3 , Pt—Pd/Al 2 O 3 , Pt—Rh/Al 2 O 3 , Pt—Ru/Al 2 O 3 , Pt—Ir/Al 2 O 3 , or combinations thereof, or
the catalyst comprises a metal oxide having at least any one metal among Pt, Pd, Ru, Ni, Sn, K, Ce, Pr, Mg, Zr, Y, or S, and a supporting member comprising Al 2 O 3 , SiO 2 , or carbon.
4 . The dehydrogenation reaction apparatus of claim 1 , wherein
the phase change material comprises diphenylmethane, monobenzyltoluene, or dibenzyltoluene.
5 . The dehydrogenation reaction apparatus of claim 1 , wherein
the heating device is an electric heater.
6 . The dehydrogenation reaction apparatus of claim 1 , wherein
the heating device is a gas combustion apparatus.
7 . The dehydrogenation reaction apparatus of claim 1 , wherein the dehydrogenation reactor comprises:
an inlet through which the liquid organic hydrogen carrier is configured to inflow, and
an outlet through which the liquid organic hydrogen carrier dehydrogenated in the dehydrogenation reactor is configured to be exhausted.
8 . The dehydrogenation reaction apparatus of claim 1 , wherein
the dehydrogenation reactor and the heating device are disposed in series.
9 . The dehydrogenation reaction apparatus of claim 1 , wherein
the heating device and the dehydrogenation reactor are disposed in parallel in a vertical direction.
10 . The dehydrogenation reaction apparatus of claim 9 , wherein:
the dehydrogenation reactor has a U-shape,
an inlet through which the liquid organic hydrogen carrier is configured to inflow is positioned on a first side of the U-shaped dehydrogenation reactor, and
an outlet through which dehydrogenated liquid organic hydrogen carriers are configured to be exhausted is positioned on a second side of the U-shaped dehydrogenation reactor.
11 . The dehydrogenation reaction apparatus of claim 10 , wherein
the heating device has a shape corresponding to the dehydrogenation reactor.
12 . The dehydrogenation reaction apparatus of claim 1 , wherein:
the heating device is disposed in a center of the main housing,
the dehydrogenation reactor is disposed to surround the heating device with a central housing interposed therebetween,
the catalyst is provided between the main housing and the central housing, and
the phase change material is provided between the heating device and the central housing.
13 . The dehydrogenation reaction apparatus of claim 12 , wherein:
an inlet through which the liquid organic hydrogen carrier is configured to inflow is positioned on a first side of the main housing, and
an outlet through which the liquid organic hydrogen carrier dehydrogenated in the dehydrogenation reactor is configured to be exhausted is positioned on a second side of the main housing.
14 . The dehydrogenation reaction apparatus of claim 1 , wherein:
the dehydrogenation reactor includes a first dehydrogenation reactor and a second dehydrogenation reactor,
the heating device and the first dehydrogenation reactor having the catalyst inside are disposed in series,
the second dehydrogenation reactor is disposed to surround the heating device and the first dehydrogenation reactor with a central housing interposed therebetween,
a catalyst is provided between the main housing and the central housing, and
the phase change material is provided between the central housing, the heating device, and the first dehydrogenation reactor.
15 . The dehydrogenation reaction apparatus of claim 14 , wherein:
a first inlet through which the liquid organic hydrogen carrier is configured to inflow is positioned on a first side of the main housing,
a first outlet through which the liquid organic hydrogen carrier dehydrogenated in the second dehydrogenation reactor is configured to be exhausted is positioned on a second side of the main housing,
a second inlet, through which the liquid organic hydrogen carrier is configured to inflow, is positioned in the first dehydrogenation reactor, and
a second outlet, through which the liquid organic hydrogen carrier dehydrogenated in the first dehydrogenation reactor is configured to be exhausted, is positioned in the first dehydrogenation reactor.
16 . A dehydrogenation reaction system comprising:
a dehydrogenation reaction apparatus comprising: a main housing; a dehydrogenation reactor provided inside the main housing and including a catalyst, the dehydrogenation reactor configured to generate hydrogen from a liquid organic hydrogen carrier (LOHC); and a heating device provided inside of the main housing and configured to apply heat to the dehydrogenation reactor through a phase change material, wherein the phase change material is provided between the main housing, the dehydrogenation reactor and the heating device;
a preheater for preheating the liquid organic hydrogen carrier supplied to the dehydrogenation reaction apparatus; and
a gas-liquid separator that separates the hydrogen produced in the dehydrogenation reaction apparatus and the liquid organic hydrogen carrier.
17 . The dehydrogenation reaction system of claim 16 , wherein
the gas-liquid separator includes:
a chiller configured to cool the dehydrogenated liquid organic hydrogen carrier; and
a liquid tank configured to store the liquid organic hydrogen carrier cooled by the chiller.
18 . The dehydrogenation reaction system of claim 16 , further comprising
a buffer tank installed downstream of the gas-liquid separator and configured to store hydrogen gas separated by the gas-liquid separator.