Hydroxymethyl Furfural Oxidation Methods
    5.
    发明申请
    Hydroxymethyl Furfural Oxidation Methods 有权
    羟甲基糠醛氧化法

    公开(公告)号:US20080103318A1

    公开(公告)日:2008-05-01

    申请号:US11932436

    申请日:2007-10-31

    CPC分类号: C07D307/48 C07D307/44

    摘要: A method of oxidizing hydroxymethylfurfural (HMF) includes providing a starting material which includes HMF in a solvent comprising water into a reactor. At least one of air and O2 is provided into the reactor. The starting material is contacted with the catalyst comprising Pt on a support material where the contacting is conducted at a reactor temperature of from about 50° C. to about 200° C. A method of producing an oxidation catalyst where ZrO2 is provided and is calcined. The ZrO2 is mixed with platinum (II) acetylacetonate to form a mixture. The mixture is subjected to rotary evaporation to form a product. The product is calcined and reduced under hydrogen to form an activated product. The activated product is passivated under a flow of 2% O2.

    摘要翻译: 氧化羟甲基糠醛(HMF)的方法包括在包含水的溶剂中将包含HMF的原料提供到反应器中。 将空气和O 2 2中的至少一个提供到反应器中。 使起始材料与包含Pt的催化剂在载体材料上接触,其中在约50℃至约200℃的反应器温度下进行接触。一种制备氧化催化剂的方法,其中ZrO 2 / SUB>并被煅烧。 将ZrO 2 2与乙酰丙酮酸铂(II)混合以形成混合物。 将混合物进行旋转蒸发以形成产物。 将产物在氢气下煅烧和还原以形成活化产物。 活化产物在2%O 2 2的流下被钝化。

    Hydroxymethyl Furfural Oxidation Methods

    公开(公告)号:US20100152470A1

    公开(公告)日:2010-06-17

    申请号:US12712100

    申请日:2010-02-24

    IPC分类号: C07D307/46

    CPC分类号: C07D307/48 C07D307/44

    摘要: A method of oxidizing hydroxymethylfurfural (HMF) includes providing a starting material which includes HMF in a solvent comprising water into a reactor. At least one of air and O2 is provided into the reactor. The starting material is contacted with the catalyst comprising Pt on a support material where the contacting is conducted at a reactor temperature of from about 50° C. to about 200° C. A method of producing an oxidation catalyst where ZrO2 is provided and is calcined. The ZrO2 is mixed with platinum (II) acetylacetonate to form a mixture. The mixture is subjected to rotary evaporation to form a product. The product is calcined and reduced under hydrogen to form an activated product. The activated product is passivated under a flow of 2% O2.