Method for preparing hydrogen from cellulose
A cellulose and hydrogen technology, applied in chemical instruments and methods, hydrogen, non-metallic elements, etc., can solve the problems of catalyst deactivation, low hydrogen yield, etc., to avoid side reactions, high conversion efficiency, high hydrogen selectivity and yield effect
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Embodiment 1
[0024] Embodiment 1: the preparation of catalyst
[0025] Catalyst carrier of the present invention adopts powdered activated carbon, and its characteristics are as follows:
[0026] Specific surface: 873.4m 2 / g; average pore diameter 2.15nm.
[0027] Wash with deionized water several times and dry in an oven at 110°C before use.
[0028] Catalysts No. 1 to No. 5 were prepared by HCHO reduction method. Dissolve soluble metal salts in water to prepare a solution containing a certain amount of metal elements, and slowly add it into the activated carbon slurry under stirring. Then add NaOH solution and HCHO solution and heat to near boiling. Cool to room temperature, filter and wash with deionized water, and then dry at 110°C to prepare single-metal supported catalysts with different components (Table 1 is the prepared catalysts containing different metal components).
[0029] Specifically as the preparation of No. 1 catalyst: prepare the required amount of H 2 PtCl 6 Aqu...
Embodiment 2-8
[0035] Embodiment 2-8: the activity evaluation of catalyst
[0036] In the following examples, the following general method is used to carry out the hydrogen production reaction by hydrothermal reforming of cellulose with the reforming catalyst of Example 1.
[0037] The hydrothermal reforming hydrogen production reaction of cellulose was carried out in a 300mL autoclave, the amount of cellulose added was 2g, the amount of water added was 90g, the amount of catalyst added was 1g, the reaction temperature was 260°C, and the reaction time was 4h. The product was analyzed by gas chromatography.
[0038] The conversion rate of cellulose is calculated by the mass change of cellulose before and after the reaction:
[0039] Cellulose conversion rate (%)=(1-residual cellulose amount after reaction / added cellulose amount)×100, wherein the amount of residual cellulose after reaction is measured by the residual solid removal catalyst after reaction.
[0040] The gasification rate of reac...
Embodiment 9-13
[0056] Examples 9-13: Influence of reaction temperature on hydrogen production by hydrothermal reforming of cellulose
[0057] The effect of reaction temperature on cellulose-catalyzed hydrogen production was studied. The number of the reforming catalyst was 1. The other reaction processes were similar to those in Examples 2-8, except that the reaction temperature was different. The test results are as follows.
[0058] Table 3 Effect of reaction temperature on hydrogen production results of cellulose reforming
[0059]
[0060] As can be seen from Table 3, the yield of hydrogen increases significantly with the increase of temperature, while the selectivity of hydrogen decreases slightly.
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