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7-hydroperoxy-5,6-E-dehydro-6,7-dihydronerol

中文名称
——
中文别名
——
英文名称
7-hydroperoxy-5,6-E-dehydro-6,7-dihydronerol
英文别名
(2Z,5E)-7-hydroperoxy-3,7-dimethylocta-2,5-dien-1-ol
7-hydroperoxy-5,6-E-dehydro-6,7-dihydronerol化学式
CAS
——
化学式
C10H18O3
mdl
——
分子量
186.251
InChiKey
UYFVWWJTLUHGLJ-DMDUXHFBSA-N
BEILSTEIN
——
EINECS
——
  • 物化性质
  • 计算性质
  • ADMET
  • 安全信息
  • SDS
  • 制备方法与用途
  • 上下游信息
  • 反应信息
  • 文献信息
  • 表征谱图
  • 同类化合物
  • 相关功能分类
  • 相关结构分类

计算性质

  • 辛醇/水分配系数(LogP):
    1.4
  • 重原子数:
    13
  • 可旋转键数:
    5
  • 环数:
    0.0
  • sp3杂化的碳原子比例:
    0.6
  • 拓扑面积:
    49.7
  • 氢给体数:
    2
  • 氢受体数:
    3

反应信息

  • 作为产物:
    描述:
    橙花醇双氧水 作用下, 以 甲醇 为溶剂, 反应 11.25h, 生成 、 7-hydroperoxy-5,6-E-dehydro-6,7-dihydronerol
    参考文献:
    名称:
    Kinetics of the Oxygenation of Unsaturated Organics with Singlet Oxygen Generated from H2O2 by a Heterogeneous Molybdenum Catalyst
    摘要:
    A heterogeneous catalyst containing MoO42- exchanged on layered double hydroxides (Mo-LDHs) is used to produce O-1(2) from H2O2, and with this dark O-1(2), unsaturated hydrocarbons are oxidized in allylic peroxides. The oxidation kinetics are studied in detail and are compared with the kinetics of oxidation by O-1(2), formed from H2O2 by a homogeneous catalyst. A model is proposed for the heterogeneously catalyzed O-1(2) generation and peroxide formation. The model divides the reaction suspension in two compartments: (1) the intralamellar and intragranular zones of the LDH catalyst; (2) the bulk solution. The 2-compartment model correctly predicts the oxidant efficiency and peroxide yield for a series of olefin peroxidation reactions. O-1(2) is generated at a high rate by the heterogeneous catalyst, but somewhat more O-1(2) is lost by quenching with the heterogeneous catalyst than using the homogeneous catalyst. Quenching occurs mainly as a result of collision with the LDH hydroxyl surface, as is evidenced by using LDH supports containing strong O-1(2) deactivators such as Ni2+. A total of 15 organic substrates were peroxidized on a preparative scale using the best Mo-LDH catalyst under optimal conditions.
    DOI:
    10.1021/ja065849f
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