Foam metal hydrogenating catalyst and its preparing method and use
A technology of hydrogenation catalyst and metal foam, which is applied in the field of hydrogenation catalyst and its preparation, can solve the problems of low loading strength of active components, easy pollution, large amount of waste liquid, etc., and achieve good mechanical strength and thermal conductivity, and equipment investment The effect of less and higher surface area
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Embodiment 1
[0036] The preparation process of the hydrogenation catalyst of the present invention is described in detail with the noble metal active component being palladium:
[0037] 1) Preparation of aluminum foam carrier
[0038] 1. Use spray aluminum powder (industrial product) with a particle size of 200-250 mesh as raw material;
[0039] 2. Powder making: Dry NaCl powder with a particle size of 0.125 mm in an oven for 2 hours;
[0040] 3. Mixing: weigh aluminum powder, pore enhancer NaCl powder, and steel balls at a mass ratio of 2:1:10, add them to the universal ball mill and seal them, and fill them with N 2 protection, the mixing speed is 120r / m, and the mixing time is 1h to make a mixed powder;
[0041] 4. Forming and pressing: Put the mixed powder into the hydraulic press for pressing, the pressure is 300-500MPa, the pressing speed is 0.05m / s-0.02m / s, and the holding time is 3-5min;
[0042] 5. Sintering: put the pressed sample into a muffle furnace for sintering, and keep ...
Embodiment 2
[0049] The catalyst obtained in Example 1 was applied to the reaction of butynediol hydrogenation to generate butanediol. The porosity of the foam carrier is 80%, and the specific surface area is about 50m 2 / g, the catalytically active component is palladium, and the catalyst is made into a cylindrical shape of Φ5×5mm. The normal pressure activity evaluation device adopts a vertical Φ20mm bubbling reaction tube, the reaction tube is placed in a constant temperature water bath, and a flow meter is installed at the front. Start with H 2 Activate the catalyst at 120°C as the gas source, then lower it to 80°C, then add the reaction solution, and pass in H 2 , The reaction was carried out under the condition of maintaining a hydrogen pressure of 3.5 MPa. After a certain period of time, samples were taken and analyzed by gas chromatography. The results show that the single-pass conversion of butynediol reaches 80%, and the selectivity reaches 85%.
Embodiment 3
[0051] Using the method of Example 1, the aluminum foam catalyst of the present invention was prepared. The porosity of the foam carrier is 72%, the average pore diameter is 10μm, and the specific surface is about 80m 2 / g, its main active component is Pt, the content is 0.085%, and the degree of dispersion on the carrier is 48.7%, and the catalyst is made into a cylinder of Φ3×3mm;
[0052] The above catalyst is applied to the hydrogenation reaction of reformed raffinate, and the main composition of the raw material is C 5 ~C 8 , Distillation range 60~120℃, density 0.67~0.69g / cm 3 , the mass fraction of olefins is 1.5% to 5.0%, the mass fraction of aromatics is 1.0% to 3.0%, and the bromine index is 3500 to 5000 (the mg number of Br produced per 100g of oil, the same below.); Hydrogen: ordinary hydrogen grade cylinder hydrogen. Take 20ml catalyst, at operating pressure 0.2MPa, LHSV2.9h -1 , The volume ratio of hydrogen to oil is 340, and the reaction temperature is 180°C,...
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