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R-(-)-carveol

中文名称
——
中文别名
——
英文名称
R-(-)-carveol
英文别名
(1R)-2-methyl-5-prop-1-en-2-ylcyclohex-2-en-1-ol
R-(-)-carveol化学式
CAS
——
化学式
C10H16O
mdl
——
分子量
152.236
InChiKey
BAVONGHXFVOKBV-QVDQXJPCSA-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):
    2.1
  • 重原子数:
    11
  • 可旋转键数:
    1
  • 环数:
    1.0
  • sp3杂化的碳原子比例:
    0.6
  • 拓扑面积:
    20.2
  • 氢给体数:
    1
  • 氢受体数:
    1

反应信息

  • 作为反应物:
    描述:
    R-(-)-carveol叔丁基过氧化氢 、 Λ-(+)-tris(acetylacetonato)chromium(III) 作用下, 以 氯苯 为溶剂, 反应 5.0h, 生成 香芹酮
    参考文献:
    名称:
    Metal-Catalyzed Oxidations with Pinane Hydroperoxide:  A Mechanistic Probe To Distinguish between Oxometal and Peroxometal Pathways
    摘要:
    The relative reactivities of tert-butyl hydroperoxide (TBHP) and pinane hydroperoxide (PHP) in metal (Cr, Mo, Ru, Se, V, and Zr)-catalyzed oxidations were compared. When these oxidations involve rate-limiting oxygen transfer from a peroxometal species to the substrate huge differences between TBHP and PHP were observed, e.g., molybdenum-catalyzed epoxidation of cyclohexene with TBHP gave a 98% yield while PHP gave 0%. When the reaction involves reaction of an oxometal species with the substrate as the rate-limiting step, little or no difference is observed, e.g., the selenium-catalyzed allylic oxidation of beta-pinene gave a 96% and 99% yield with TBHP and PHP, respectively. Small but significant differences are observed when reoxidation of the catalyst by the hydroperoxide to the active oxometal species is the rate-limiting step; e.g., the chromium-catalyzed oxidation of carveol gave carvone in 89% and 24% yield with TBHP and PHP, respectively. Hence, the effect of RO2H structure on rate is dependent on the rate-limiting step.
    DOI:
    10.1021/jo971270b
  • 作为产物:
    描述:
    R-(+)-1,2-limonene epoxide 、 zinc 2-ethylhexanoate 、 2-氨基苯酚 生成 R-(-)-carveol
    参考文献:
    名称:
    Catalyst system and process for rearrangement of epoxides to allylic alcohols
    摘要:
    一种催化剂系统可用于实现(a)通过重排相应环氧化物制备烯丙基醇,当烯丙基醇是所需的产物时;(b)随后的反应,例如选择性氧化,将在步骤(a)中获得的烯丙基醇转化为所需的产物,例如α,β-不饱和羰基化合物;和/或(c)能够在一个锅中进行步骤a)和b)。在一个实施例中,该催化剂系统包括(i)至少包括一个初级催化剂的催化剂包括一个或多个均相或异相的、无机的、有机的或复杂的含金属化合物,以及(ii)至少包括一种苯酚化合物的活化剂/改性剂。
    公开号:
    US20030065230A1
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文献信息

  • Metal-Catalyzed Oxidations with Pinane Hydroperoxide:  A Mechanistic Probe To Distinguish between Oxometal and Peroxometal Pathways
    作者:H. E. B. Lempers、A. Ripollès i Garcia、R. A. Sheldon
    DOI:10.1021/jo971270b
    日期:1998.3.1
    The relative reactivities of tert-butyl hydroperoxide (TBHP) and pinane hydroperoxide (PHP) in metal (Cr, Mo, Ru, Se, V, and Zr)-catalyzed oxidations were compared. When these oxidations involve rate-limiting oxygen transfer from a peroxometal species to the substrate huge differences between TBHP and PHP were observed, e.g., molybdenum-catalyzed epoxidation of cyclohexene with TBHP gave a 98% yield while PHP gave 0%. When the reaction involves reaction of an oxometal species with the substrate as the rate-limiting step, little or no difference is observed, e.g., the selenium-catalyzed allylic oxidation of beta-pinene gave a 96% and 99% yield with TBHP and PHP, respectively. Small but significant differences are observed when reoxidation of the catalyst by the hydroperoxide to the active oxometal species is the rate-limiting step; e.g., the chromium-catalyzed oxidation of carveol gave carvone in 89% and 24% yield with TBHP and PHP, respectively. Hence, the effect of RO2H structure on rate is dependent on the rate-limiting step.
  • Catalyst system and process for rearrangement of epoxides to allylic alcohols
    申请人:——
    公开号:US20030065230A1
    公开(公告)日:2003-04-03
    A catalyst system that can be used to achieve (a) preparation of allylic alcohols by rearrangement of the corresponding epoxide, when the allylic alcohol is a desired product; (b) subsequent reaction, e.g., selective oxidation, of the allylic alcohols obtained in step (a) to afford a desired product, e.g., alpha, beta-unsaturated carbonyl compounds; and/or (c) the ability to perform steps a) and b) in a one-pot process. In one embodiment, the catalyst system includes (i) at least one primary catalyst includes one or more homogeneous or heterogeneous, inorganic, organic or complex metal-containing compound, and (ii) at least one activator/modifier comprising at least one phenolic compound.
    一种催化剂系统可用于实现(a)通过重排相应环氧化物制备烯丙基醇,当烯丙基醇是所需的产物时;(b)随后的反应,例如选择性氧化,将在步骤(a)中获得的烯丙基醇转化为所需的产物,例如α,β-不饱和羰基化合物;和/或(c)能够在一个锅中进行步骤a)和b)。在一个实施例中,该催化剂系统包括(i)至少包括一个初级催化剂的催化剂包括一个或多个均相或异相的、无机的、有机的或复杂的含金属化合物,以及(ii)至少包括一种苯酚化合物的活化剂/改性剂。
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