首页|氧化物负载磷钨酸催化甘露醇脱水反应的研究

氧化物负载磷钨酸催化甘露醇脱水反应的研究

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分别以SiO2,TiO2,ZrO2和Al2O3为载体,采用浸渍法负载Keggin型磷钨酸,制备了一系列不同负载量的催化剂.通过红外光谱(FT-IR)、X射线衍射(XRD)、扫描电镜(SEM)和程序升温脱附(NH3-TPD)等表征手段分析催化剂.在无溶剂、减压条件下,使用制得的催化剂,研究了催化剂催化甘露醇脱水反应的性能,考察了催化剂载体种类、磷钨酸负载量、反应时间、反应温度和催化剂用量对甘露醇转化率和脱水产物的影响.结果表明,以 30%PW/SiO2为催化剂,催化反应性能较好,较佳的工艺条件是催化剂与甘露醇质量比为0.03,反应温度为170℃,反应时间为2 h,反应体系真空度为 0.09 MPa,在此条件下甘露醇的转化率为 100.0%,2,5-脱水山梨醇收率为 55.7%,1,4-脱水甘露醇收率为 9.7%,异甘露醇收率为 25.9%,副产物收率为8.5%.
Dehydration of Mannitol Catalyzed by Oxide Supported Phosphotungstic Acid
A series of supported catalysts with different loading amounts were prepared by impregnating Keggin-type phosphotungstic acid onto SiO2,TiO2,ZrO2,and Al2O3 carriers.Characterization methods such as infrared spectroscopy(FT-IR),X-ray diffraction(XRD),scanning electron microscopy(SEM),and temperature programmed desorption(NH3-TPD)were used to analyze the catalyst.The performance of the prepared catalysts in the dehydration of mannitol was studied under solvent-free and depressurized conditions.The effects of catalyst carrier type,phosphotungstic acid loading,reaction time,reaction temperature,and catalyst dosage on the conversion of mannitol and dehydration products were investigated.The results showed that the 30%PW/SiO2 catalyst exhibited superior catalytic performance.The optimal process conditions were a catalyst to mannitol mass ratio of 0.03,a reaction temperature of 170℃,a reaction time of 2 h,and a vacuum degree of 0.09 MPa.Under these conditions,the conversion of mannitol was 100.0%,the yield of 2,5-sorbitan was 55.7%,the yield of 1,4-mannitan was 9.7%,the yield of isomannide was 25.9%,and the yield of other components was 8.5%.

dehydration of mannitolcatalystsupported phosphotungstic acidreaction conditionsmetal oxides

陈涵铭、莫学坤、郑燕春、徐冰冰、侯铭轩、葛峻逍、朱明乔

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浙江大学化学工程与生物工程学院,浙江 杭州 310058

浙江大学衢州研究院,浙江 衢州 324000

浙江江正和流体科技股份有限公司,浙江 杭州 310014

衢州巨化锦纶有限责任公司,浙江 衢州 324000

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甘露醇脱水 催化剂 负载型磷钨酸 反应条件 金属氧化物

浙江大学衢州研究院科技计划项目衢州市科技计划项目衢州市科技计划项目浙江省生产制造方式转型示范项目

IZQ2022KJ30112022K052021F0122207-330851-04-02-952183

2024

化学反应工程与工艺
联合化学反应工程研究所 ,中石化上海石油化工研究院

化学反应工程与工艺

CSTPCD
影响因子:0.392
ISSN:1001-7631
年,卷(期):2024.40(4)
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