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Selective conversion of cotton cellulose to glucose and 5-hydroxymethyl furfural with SO42/MxOy solid superacid catalyst

机译:SO42 / MxOy固体超强酸催化剂将棉纤维素选择性转化为葡萄糖和5-羟甲基糠醛

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This paper presented a mild hydrothermal process for degradation of cotton cellulose with solid superacid catalyst and selective conversion of cotton cellulose to glucose and 5-hydroxymethyl furfural (HMF). Five kinds of solid superacid catalyst such as SO42-/SnO2, SO42-/TiO2 SO42-/ZrO2, SO42-/Fe2O3 and SO42-/Al2O3 were prepared by impregnation method. The BET surface area of catalyst SO42-/SnO2 was up to 118.8 m(2) g(-1) when impregnation was performed with 1 mol L-1 H2SO4 of impregnating solution at 550 degrees C calcination temperature for 3 h. It made the hydrothermal temperature of cellulose degradation decrease to 190 degrees C successfully and suppressed the side reaction. The NH3-TPD profile of SO42-/SnO2 indicated there was a wide region of stronger acid sites on the catalyst surface. The depolymerization of cotton cellulose obtained 11.0% yield and 22.0% selectivity of HMF and 26.8% yield and 53.4% selectivity of glucose, respectively. The regeneration and reuse of solid superacid catalyst were also discussed in this paper. (C) 2015 Elsevier Ltd. All rights reserved.
机译:本文提出了一种温和的水热工艺,用固体超强酸催化剂降解棉纤维素,并将棉纤维素选择性转化为葡萄糖和5-羟甲基糠醛(HMF)。采用浸渍法制备了SO42- / SnO2,SO42- / TiO2,SO42- / ZrO2,SO42- / Fe2O3和SO42- / Al2O3五种固体超强酸催化剂。当用1 mol L-1 H2SO4浸渍溶液在550摄氏度的煅烧温度下进行3 h浸渍时,催化剂SO42- / SnO2的BET表面积高达118.8 m(2)g(-1)。使纤维素降解的水热温度成功降低至190℃,并抑制了副反应。 SO42- / SnO2的NH3-TPD分布图表明,催化剂表面存在较宽的强酸位区域。棉纤维素的解聚分别获得11.0%的收率和22.0%的HMF选择性和26.8%的收率和53.4%的葡萄糖选择性。本文还讨论了固体超强酸催化剂的再生和再利用。 (C)2015 Elsevier Ltd.保留所有权利。

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