Method for producing hydrogen through fluidized-bed methane steam reforming
A technology for producing hydrogen from methane steam and reforming, which is applied in chemical instruments and methods, hydrogen, chemical recovery, etc., can solve problems such as different operating rules, simplify the process, reduce system energy consumption, and avoid oxidation and sintering deactivation. Effect
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Embodiment 1
[0071] Example 1 illustrates the effect of using the method provided by the present invention to enhance hydrogen production by steam reforming of methane.
[0072] Reforming catalyst preparation:
[0073] Pseudoboehmite, kaolin, nickel nitrate aqueous solution and decationized water are mixed and beaten according to the proportion, hydrochloric acid is added to adjust the pH value, the obtained colloid is spray-dried and formed into particles with a size of 90-130 microns, and then roasted at 550 ° C for 2 hours to obtain The microspherical carrier has a NiO content of 37wt%, a kaolin content of 33wt%, and an alumina content of 30wt% after sintering. After calcination, the reforming catalyst is reduced at 350°C in a hydrogen atmosphere to reduce nickel oxide to metal Ni, which is designated as ReAT-1. ReAT-1 has an average particle size of 110 microns and a bulk density of 1.0kg / cm3.
[0074] Adsorption catalyst preparation:
[0075] 5.6Kg of decationized water, 2.0kg of pse...
Embodiment 2
[0078] Example 2 illustrates the effect of using the method provided by the present invention to enhance hydrogen production by steam reforming of methane.
[0079] The reaction device used, the adsorption catalyst used, the reforming catalyst, and the specific steps are the same as in Example 1. The difference is that in the reaction operating conditions, the raw material gas-water-carbon ratio is 4, the reaction temperature is 650 ° C, and the reaction pressure is 0.1 MPa, the regenerator temperature is 700°C, the stripper gas linear velocity is 0.8m / s, and the feed gas flow rate is 4.5m / s. The experimental results are shown in Table 1.
Embodiment 3
[0081] Example 3 illustrates the effect of using the method provided by the present invention to enhance hydrogen production by steam reforming of methane.
[0082] The reaction device used, the adsorption catalyst used, the reforming catalyst, and the specific steps are the same as in Example 1. The difference is that in the reaction operating conditions, the raw material gas-water-carbon ratio is 8, the reaction temperature is 700 ° C, and the reaction pressure is 0.5 MPa, the regenerator temperature is 750°C, and the stripper gas line velocity is 1.1m / s. The experimental results are shown in Table 1.
[0083] Table 1
[0084] example
[0085] As can be seen from Table 1, the method for hydrogen production by steam reforming of methane provided by the present invention not only simplifies the flow process, but also has higher hydrogen content in the obtained hydrogen product, and CO and CO 2 The content is lower. By adopting the method provided by the invention,...
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