Paraffin hydrorefining catalyst and its prepn process
A hydrofining and catalyst technology, which is applied in the refining of petroleum wax, can solve the problems of inability to produce food-grade paraffin with qualified color and insufficient removal performance of colored substances in paraffin, so as to improve the activity of paraffin hydrofining and decolorization performance, Super paraffin wax decolorization performance, the effect of high dispersion state
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Embodiment 1
[0035] (1).B 2 o 3 -Al 2 o 3 Preparation of vector
[0036] Weigh 200g of alumina monohydrate dry rubber powder (containing 2w% alumina trihydrate), add 6.5g B 2 o 3 , 150ml 3wt% HNO 3 and 5ml H 2 O. Mix well, knead into a plastic shape and extrude into clover strips. After air drying overnight, dry at 110°C for 2 hours.
[0037] Place the dried sample in a high-temperature furnace, raise the temperature to 200°C at a rate of 3°C per minute, and roast at this temperature for 1.0 hour. Then, the temperature was raised to 460° C. at a rate of 3° C. per minute, and was roasted at a constant temperature at this temperature for 2.0 hours, and then the temperature was raised to 650° C. at a rate of 3° C. per minute, and roasted at a constant temperature at this temperature for 2.0 hours.
[0038] (2). Preparation of Mo-Ni-P solution
[0039] Dissolve 14ml of phosphoric acid (concentration: 85v%) in 600ml of water. The solution was added to 80 g of molybdenum oxide with s...
Embodiment 2
[0043] (1).B 2 o 3 -Al 2 o 3 Preparation of vector
[0044] Same as embodiment 1 (1) step, but B 2 o 3 The addition amount is changed to 9.5g.
[0045] (2) Preparation of Mo-Ni-P solution
[0046] The steps are the same as in Example 1 (2).
[0047] (3).Mo-Ni-P / B 2 o 3 -Al 2 o 3 Catalyst preparation
[0048] Same as the steps in Example 1(3).
Embodiment 3
[0050] (1).B 2 o 3 -Al 2 o 3 Preparation of vector
[0051] Same as embodiment 1 (1) step, but B 2 o 3 Change to BF 3 . BF 3 Addition amount is 23.5g.
[0052] (2). Preparation of Mo-Ni-P solution
[0053] Same step as Example 1(2), but the filtrate was concentrated to 260ml.
[0054] (3).Mo-Ni-P / B 2 o 3 -Al 2 o 3 Catalyst preparation
[0055] The same as in Example 1 (3), but the third stage of the calcination temperature is changed to 390 ° C.
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