Method for promoting solid catalyst to depolymerize cellulose
A solid catalyst, solid acid catalyst technology, applied in chemical instruments and methods, preparation of organic compounds, oligosaccharides, etc., can solve the problems of mass transfer and acid site contact, long ball milling pretreatment time, and high energy consumption. Overcome the effects of acid discharge, short ball milling time and simple process
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Embodiment 1
[0017] Weigh 1g of microcrystalline cellulose ( PH-101, purchased from sigma-aldrich), weighed 0.9g zirconium phosphate (solid acid catalyst), put cellulose and zirconium phosphate together in the same ball mill jar, and milled in the ball mill for 1h. After the ball milling, take out two Then mix it with 50ml of water and 0.075g of Ru / C and put it into a batch reactor with a capacity of 100ml, fill it with hydrogen to make the pressure of the reactor 6MPa, heat it to 190°C, react for 2.5 hours, take out The product was analyzed.
[0018] Control 1: traditional ball milling method
[0019] Weigh 1g of microcrystalline cellulose ( PH-101 (purchased from sigma-aldrich) and 0.9g zirconium phosphate (solid acid catalyst), put the cellulose and zirconium phosphate in different ball mill jars, and mill in the ball mill for 1h. After the ball milling, take out the cellulose and zirconium phosphate, then mixed with 50ml of water and 0.075gRu / C and added to a batch reactor with a ...
Embodiment 2
[0028] Referring to Example 1, the difference is that the ball milling time is 4h, using α-cellulose instead of microcrystalline cellulose, the results show that the traditional ball milling method makes the cellulose partially converted into sorbitol and mannitol, and the conversion rate of cellulose is 87%, The total yield of sorbitol and mannitol was 70.7%, and the selectivity of sorbitol and mannitol was 81.3%. The conversion rate of cellulose by the method of the present invention is 100%, the total yield of sorbitol and mannitol is 84%, and the selectivity of sorbitol and mannitol is 84%. Other products of cellulose conversion are small alcohols, some gaseous products, and some unidentified substances. The comparison results show that the method of the invention can promote the depolymerization of cellulose by the solid catalyst.
Embodiment 3
[0030] Referring to Example 1, the difference is that 0.9g of zirconium phosphate is replaced by 0.9gH-MOR (mordenite), and the ball milling time is 2h. The results show that the traditional ball milling method partially converts cellulose into sorbitol and mannitol, and the conversion rate of cellulose is 48%, the total yield of sorbitol and mannitol is 25%, the selectivity of sorbitol and mannitol is 52%, utilizes the transformation rate of method cellulose of the present invention 81.5%, the total yield of sorbitol and mannitol is 40%, the selectivity of sorbitol and mannitol is 49%. The comparison results show that the method of the invention can promote the depolymerization of cellulose by the solid catalyst.
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