Catalyst and treatment method for upgrading tar by using catalyst
A treatment method and catalyst technology, which is applied in chemical instruments and methods, physical/chemical process catalysts, tar extraction and processing through chemical methods, etc., can solve problems in the laboratory research stage, reduce oxygen atom content, and low catalyst activity. Achieve high-efficiency aromatic etherification catalytic conversion, increase solubility, and high catalytic activity
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Embodiment 1
[0040] Catalyst preparation: 30ml concentration is 11.8wt% K 2 CO 3 Add the aqueous solution dropwise to 20g of γ-Al with a particle size of 1-2mm 2 o 3 On the granules, the dropwise addition is completed and dried naturally for 24 hours, then dried at 120°C for 12 hours, then transferred to a muffle furnace for 700°C roasting for 8 hours, and cooled in a desiccator to obtain γ-Al 2 o 3 potassium salt catalyst.
[0041] Phenol-alcohol high-temperature gas-phase etherification conversion: the creosote oil obtained by atmospheric distillation of wood tar and methanol are mixed according to a mass ratio of 1:1, and 20g of catalyst is placed in the middle of a fixed-bed tubular reactor, and then the reaction mixture is passed through a peristaltic The pump is sent in from the inlet of the fixed bed tubular reactor, and the reactant system flows through the catalyst bed placed in the fixed bed and undergoes conversion reaction. The gas phase product obtained flows out from the ...
Embodiment 2
[0043] Catalyst preparation: 30ml concentration is the K of 12.1wt% 3 PO 4 Add the aqueous solution dropwise to 20g of γ-Al with a particle size of 1-2mm 2 o 3 On the granules, the dropwise addition is completed and dried naturally for 24 hours, then dried at 120°C for 12 hours, then transferred to a muffle furnace for 700°C roasting for 8 hours, and cooled in a desiccator to obtain γ-Al 2 o 3 potassium salt catalyst.
[0044] Phenol-alcohol high-temperature vapor-phase etherification conversion: wood tar and methanol are stirred and mixed according to a mass ratio of 1:1, and 20g of catalyst is placed in the middle of the fixed-bed tubular reactor, and then the reaction mixture is transferred from the fixed-bed tubular reactor through a peristaltic pump. The reactant system flows through the catalyst bed placed in the fixed bed and undergoes a conversion reaction. The gas phase product obtained flows out from the outlet of the tubular reactor and enters the condensation s...
Embodiment 3
[0046] Catalyst preparation: 30ml concentration is the K of 28wt% 3 PO 4 Add the aqueous solution dropwise to 20g of γ-Al with a particle size of 1-2mm 2 o 3 On the granules, the dropwise addition is completed and dried naturally for 12 hours, then dried at 140°C for 8 hours, then transferred to a muffle furnace for 800°C roasting for 9 hours, and cooled in a desiccator to obtain γ-Al 2 o 3 potassium salt catalyst.
[0047] Phenol-alcohol high-temperature gas-phase etherification conversion: Stir and mix coal tar and methanol at a mass ratio of 1:3, and place 20g of catalyst in the middle of a fixed-bed tubular reactor, and then transfer the reaction mixture from the fixed-bed tubular reactor through a peristaltic pump The reactant system flows through the catalyst bed placed in the fixed bed and undergoes a conversion reaction. The gas phase product obtained flows out from the outlet of the tubular reactor and enters the condensation system, and is cooled to become a liqu...
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