Method for catalytic activation of alkali lignin by Pd/SO4<2->/ZrO2
An alkali lignin, catalytic activation technology, applied in chemical instruments and methods, physical/chemical process catalysts, chemical/physical processes, etc. The effect of enhancing activity and increasing content
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specific Embodiment approach 1
[0009] Specific implementation mode one: this implementation mode is a kind of Pd / SO 4 2- / ZrO 2 The method for catalyzing and activating alkali lignin in papermaking black liquor is specifically completed according to the following steps:
[0010] One, the preparation of catalyst: ZrOCl 2 ·8H 2 O was added to distilled water to prepare ZrOCl with a mass concentration of 10% to 20%. 2 ·8H 2 O solution, to the ZrOCl 2 ·8H 2 Add concentrated ammonia water drop by drop to the O solution, stir, adjust the pH to 9-11, filter with suction after aging for 24 hours, wash the filter cake with water until there is no Cl, and obtain Zr(OH) 4 filter cake, the Zr(OH) 4 The filter cake is soaked in 1mol / L sulfuric acid solution for 12h, then suction filtered, dried at 110°C for 12h, pre-calcined at 200°C to 300°C for 0.5h, and calcined at 500°C to 600°C for 3h to obtain SO 4 2- / ZrO 2 , the SO 4 2- / ZrO 2 Add distilled water and stir, heat to 80°C, add PdCl dropwise 2 Hydroch...
specific Embodiment approach 2
[0020] Specific embodiment 2: The difference between this embodiment and specific embodiment 1 is: wash the catalyst separated after 2h-6h of reaction in step 3 of specific embodiment 1, and put the separated catalyst at 200°C-300°C Calcined for 0.5h to obtain a catalytic reaction Pd / SO 4 2- / ZrO 2 Catalyst, use 0.25g~1g of said catalytic reaction Pd / SO 4 2- / ZrO 2 The catalyst replaces the Pd / SO described in step 1 in the specific embodiment 1 4 2- / ZrO 2 Catalyst 0.25g~1g, that is, use 0.25g~1g of the catalyst to react Pd / SO once 4 2- / ZrO 2 The catalyst replaces the Pd / SO described in step 3 in the specific embodiment 1 4 2- / ZrO 2 Catalyst 0.25g~1g, after the reaction is finished, the catalyst is separated. Others are the same as the first embodiment.
specific Embodiment approach 3
[0021] Specific embodiment 3: The difference between this embodiment and specific embodiments 1 to 2 is: wash the separated catalyst with water after the reaction described in specific embodiment 2, and roast the separated catalyst at 200°C to 300°C for 0.5h , to obtain the catalytic reaction secondary Pd / SO 4 2- / ZrO 2 Catalyst, using 0.25g~1g of said catalytic reaction secondary Pd / SO 4 2- / ZrO 2 The catalyst replaces the Pd / SO described in step 1 in the specific embodiment 1 4 2- / ZrO 2 Catalyst 0.25g ~ 1g, that is, use 0.25g ~ 1g of the catalytic reaction of the secondary Pd / SO 4 2- / ZrO 2 The catalyst replaces the Pd / SO described in step 3 in the specific embodiment 1 4 2- / ZrO 2 Catalyst 0.25g~1g, after the reaction is finished, the catalyst is separated. Others are the same as the specific embodiment 1 to 2.
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