Method for producing synthetic gas by reforming by-product glycerin vapor of biological diesel production
A steam reforming and biodiesel technology, which is applied in the production of bulk chemicals, chemical instruments and methods, inorganic chemistry, etc., can solve the problems of unfavorable development and utilization of precious metal catalysts, and achieve the effect of convenient operation, good selectivity and simple operation
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Embodiment 1
[0015] Preparation of Nickel-Based Catalysts
[0016] Preparation process: (1) preparing a zirconium oxychloride solution with a concentration of 1.0mol / L; (2) preparing a cerium nitrate solution with a concentration of 1.0mol / L; (3) measuring cerium nitrate according to Ce / Zr=1 / 1 solution and zirconium oxychloride solution, the preparation of Ce 3+ 、Zr 4+ A mixed solution with a total ion concentration of 1.0 mol / L; for the above three solutions, use ammonia water as a precipitant, and add it dropwise for precipitation and keep stirring to control the pH of the solution to 9.5-10.5. After the precipitation was complete, it was aged for 12 h, washed with deionized water until the pH was 7 and no Cl could be detected with silver nitrate -1 , dried at 120°C for 12h, and calcined at 600-800°C for 2-5h to obtain CeO 2 , ZrO 2 and CeO 2 -ZrO 2 Powder, specific surface area 20-80m 2 / g. Weigh three parts of nickel nitrate according to the Ni mass content of 10% to 15%, respe...
Embodiment 2
[0019] Adopt the 15wt%Ni / CeO that makes by embodiment 1 method 2 Catalyst 200mg, using hydrogen volume content of 5% H 2 -N 2 The mixed gas is pre-reduced at 500°C for 2 hours, and the reaction space velocity is set at 15000 hours -1 , Glycerin aqueous solution steam water carbon ratio 3:1, reaction temperature 500 ℃, other experimental conditions are the same as Example 1. The reaction result is as follows: the glycerol conversion rate is 98%, and the molar composition of the reaction product: H 2 : 56.8%, CO: 31.9%, CO 2 : 9.8%, CH 4 : 1.5%, H 2 / CO=1.78.
Embodiment 3
[0021] Adopt the 10wt%Ni / CeO that makes by embodiment 1 method 2 -ZrO 2 Catalyst, set reaction space velocity 5000h -1 , Glycerol aqueous solution steam water carbon ratio 4:1, reaction temperature 500 ° C, catalyst reduction and other experimental conditions are the same as in Example 2. The reaction result is as follows: glycerol conversion rate 100%, reaction product molar composition: H 2 : 62.7%, CO: 25.3%, CO 2 : 10.7%, CH 4 : 1.3%, H 2 / CO=2.48.
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