Catalytic hydrogen supply system based on organic liquid and hydrogen supply method thereof
A technology of organic liquid and catalyst carrier, applied in the field of hydrogen energy, can solve the problems of poor mechanical properties of graphene carrier, difficulty in long-term industrial application, high catalyst cost, etc., and achieve low catalyst cost, low raw material cost, and hydrogen supply purity high effect
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Embodiment 1
[0060] This embodiment provides a hydrogen supply method for a catalytic hydrogen supply system based on an organic liquid, comprising the following steps:
[0061] S1. Select organic liquid hydrogen supply material: the hydrogen supply material A is a mixture of octadehydrobenzyltoluene and dodecahydrobenzyltoluene, wherein the mass ratio of octadehydrobenzyltoluene to dodecahydrobenzyltoluene The hydrogen supply raw material B is 2-methyldecalin, and the mass ratio of the hydrogen supply raw material A to the hydrogen supply raw material B is 3:1.
[0062] S2. Select a supported hydrogen-donating reaction catalyst: alumina-supported palladium-copper catalyst, denoted as Pd-Cu / Al 2 o 3, wherein the mass content of Pd is 1.8wt%, the mass content of Cu is 10.0wt%, the particle size of the catalyst is 20-60 mesh, and the specific surface area of the catalyst is 182m 2 / g.
[0063] Hydrogen Donation Reaction Catalyst Pd-Cu / Al 2 o 3 Prepared by impregnation as follows:
[...
Embodiment 2
[0069] A hydrogen supply method based on an organic liquid catalytic hydrogen supply system, comprising the following steps:
[0070] S1. Select the organic liquid hydrogen supply material: the hydrogen supply material A is a mixture of octadehydrobenzyltoluene and dodecahydrobenzyltoluene, wherein the mass ratio of octadehydrobenzyltoluene and dodecahydrobenzyltoluene is The ratio is 4:1, the hydrogen supply raw material B is 2-methyldecalin, and the mass ratio of the hydrogen supply raw material A to the hydrogen supply raw material B is 0.5:1.
[0071] S2. Select supported hydrogen-donating reaction catalyst Pt-Cu / Al 2 o 3 -SiO 2 , wherein the mass content of Pt is 2wt%, the mass content of Cu is 28wt%, the particle size of the catalyst is 10-100 mesh, and the specific surface area of the catalyst is 10m 2 / g.
[0072] Hydrogen Donation Reaction Catalyst Pt-Cu / Al 2 o 3 -SiO 2 Prepared by impregnation as follows:
[0073] Firstly, Cu(NO 3 ) 3 As the precursor of ...
Embodiment 3
[0078] This embodiment provides a hydrogen supply method for a catalytic hydrogen supply system based on an organic liquid, comprising the following steps:
[0079] S1. Select the organic liquid hydrogen supply material: the hydrogen supply material A is a mixture of octadehydrobenzyltoluene and dodecahydrobenzyltoluene, wherein the mass ratio of octadehydrobenzyltoluene and dodecahydrobenzyltoluene is The ratio is 1:2, the hydrogen supply raw material B is 1-methyldecalin, and the mass ratio of the hydrogen supply raw material A to the hydrogen supply raw material B is 1.9:1.
[0080] S2. Select supported hydrogen-donating reaction catalyst Pt-Cu / Al 2 o 3 , wherein the mass content of Pt is 0.9wt%, the mass content of Cu is 8.0wt%, the particle size of the catalyst is 200-240 mesh, and the specific surface area of the catalyst is 190m 2 / g.
[0081] Hydrogen Donation Reaction Catalyst Pt-Cu / Al 2 o 3 Prepared by impregnation as follows:
[0082] Firstly, Cu(NO 3 ) 3 ...
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