Catalyst for preparing C5 hydrogenated petroleum resin, and its preparing method
A hydrogenation petroleum resin, hydrogenation catalyst technology, applied in the field of catalyst and its preparation, can solve the problems of catalyst activity and service life adverse effects, complexity, etc.
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Embodiment 1
[0024] 1. Preparation of carrier: take 100 grams of specific surface area of 80-150m 2 / g, alumina balls with a diameter of 2 mm, soaked in 0.5 g of 0.01M cerium nitrate as cerium for 12 hours, dried at 110°C, and then calcined at 600°C for 4 hours to obtain a rare earth treated catalyst carrier.
[0025] 2. Preparation of mixed solution of catalyst active components and additives:
[0026] 1. 1 gram of tin chloride in terms of tin is mixed with a stable solution, and the concentration is 0.1M, which is called A solution; 2. In the palladium chloride aqueous solution containing 0.8 gram of metal palladium, 0.2 gram of copper chloride in terms of copper is added, Stir well and call it B solution.
[0027] 3. Loading of active components: Put the catalyst carrier prepared above into a porcelain evaporating dish and heat it, spray the above-mentioned solution A at a temperature of 120° C. on the constantly vibrating catalyst carrier, Then under the same conditions, all the a...
Embodiment 2
[0031] According to the above method, a single-component hydrogenation catalyst with a palladium content of 1.0% was prepared by using an aqueous solution of palladium chloride containing 1.0 g of metal palladium. Pack into fixed-bed reactor and carry out hydrogenation reaction, reaction condition is the same as embodiment 1, product softening point 108 ℃, bromine value 1.6gBr 2 / 100g, Gardner (Gardner) hue is No. 3 color.
Embodiment 3
[0033] The palladium content 0.8% that embodiment 1 prepares, copper content 0.2%, cerium content 0.5%, the hydrogenation catalyst of the palladium content 1.0% of the palladium content 1.0% that the embodiment 2 prepares is packed into two In the same fixed-bed reactor, the same C5 petroleum resin was used as raw material, and the reaction temperature was 160 ° C, and the pressure was 13 MPa. The former liquid space velocity was 1.0 h. -1 , the latter liquid space velocity is 0.5h -1 , the bromine value of the former product is 1.5gBr 2 / 100g, the latter is 1.8gBr 2 / 100g.
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