{"title":"Conversion of Glucose to 5-Hydroxymethylfurfural (5-HMF) Over Sulfated Zinc Oxide Catalyst","authors":"Richa Tomer, Somshubhra Maity, Prakash Biswas","doi":"10.2139/ssrn.3721524","DOIUrl":null,"url":null,"abstract":"Zinc oxide and sulfated zinc oxide catalysts prepared by precipitation and wetness impregnation methods, respectively, and characterized by various sophisticated techniques like XRD, FE-SEM, EDX, TGA, NH3-TPD and N2 adsorption-desorption. These catalysts tested for glucose dehydration to 5-hydroxymethylfurfural (5-HMF) formation and the influence of several reaction constraints as reaction temperature, reaction time, catalyst amount, and sulfation loading on ZnO were evaluated in terms of glucose conversion and 5-HMF Yield. Catalytic activity results demonstrated a maximum of 15.8 % 5-HMF yield with complete conversion of glucose over 2.5M SO42-/ZnO catalyst at 220°C after a reaction time of 6 h in the presence of dimethyl sulfoxide (DMSO) reaction solvent. The formation of other unidentified side reaction products restricted the higher yield of HMF. Reaction parameter study suggested that higher reaction temperature (> 220oC), higher substrate to catalyst ratio (> 0.5) was not beneficial for higher yield of HMF. Longer reaction time has not affected the yield of HMF. The results obtained also suggested that the acidic nature of catalyst was responsible for the high conversion of glucose.","PeriodicalId":18731,"journal":{"name":"Materials Processing & Manufacturing eJournal","volume":"60 1","pages":""},"PeriodicalIF":0.0000,"publicationDate":"2020-02-05","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Materials Processing & Manufacturing eJournal","FirstCategoryId":"1085","ListUrlMain":"https://doi.org/10.2139/ssrn.3721524","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"","JCRName":"","Score":null,"Total":0}
引用次数: 0
Abstract
Zinc oxide and sulfated zinc oxide catalysts prepared by precipitation and wetness impregnation methods, respectively, and characterized by various sophisticated techniques like XRD, FE-SEM, EDX, TGA, NH3-TPD and N2 adsorption-desorption. These catalysts tested for glucose dehydration to 5-hydroxymethylfurfural (5-HMF) formation and the influence of several reaction constraints as reaction temperature, reaction time, catalyst amount, and sulfation loading on ZnO were evaluated in terms of glucose conversion and 5-HMF Yield. Catalytic activity results demonstrated a maximum of 15.8 % 5-HMF yield with complete conversion of glucose over 2.5M SO42-/ZnO catalyst at 220°C after a reaction time of 6 h in the presence of dimethyl sulfoxide (DMSO) reaction solvent. The formation of other unidentified side reaction products restricted the higher yield of HMF. Reaction parameter study suggested that higher reaction temperature (> 220oC), higher substrate to catalyst ratio (> 0.5) was not beneficial for higher yield of HMF. Longer reaction time has not affected the yield of HMF. The results obtained also suggested that the acidic nature of catalyst was responsible for the high conversion of glucose.
采用沉淀法和湿浸渍法分别制备了氧化锌和硫酸氧化锌催化剂,并采用XRD、FE-SEM、EDX、TGA、NH3-TPD和N2吸附-脱附等复杂技术对催化剂进行了表征。对葡萄糖脱水生成5-羟甲基糠醛(5-HMF)的催化剂进行了测试,并从葡萄糖转化率和5-HMF产率方面评价了反应温度、反应时间、催化剂用量和硫酸锌负载等几种限制条件对反应的影响。催化活性结果表明,在250 m SO42-/ZnO催化剂上,在220℃下,在二甲亚砜(DMSO)溶剂存在下,反应时间为6 h,葡萄糖完全转化,5-HMF收率最高为15.8%。其他未知副反应产物的生成限制了HMF的高产率。反应参数研究表明,较高的反应温度(>220℃),更高的底物与催化剂比(>0.5)不利于提高HMF产量。较长的反应时间对HMF的收率没有影响。结果还表明,催化剂的酸性是葡萄糖高转化率的原因。