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cis-Cyclonon-4-enon | 24959-49-7

中文名称
——
中文别名
——
英文名称
cis-Cyclonon-4-enon
英文别名
4-Cyclononen-1-one;(4Z)-cyclonon-4-en-1-one
cis-Cyclonon-4-enon化学式
CAS
24959-49-7
化学式
C9H14O
mdl
——
分子量
138.21
InChiKey
OLVNHMDMFVMIMY-IWQZZHSRSA-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
  • 重原子数:
    10
  • 可旋转键数:
    0
  • 环数:
    1.0
  • sp3杂化的碳原子比例:
    0.67
  • 拓扑面积:
    17.1
  • 氢给体数:
    0
  • 氢受体数:
    1

反应信息

  • 作为产物:
    描述:
    参考文献:
    名称:
    2-环丙基环己酮的光解:三碳光化学扩环
    摘要:
    辐照2-环丙基环己酮可得到顺式和反式-环酮-4-烯酮的混合物,这是主要的光化学产物。
    DOI:
    10.1039/c2969001049b
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文献信息

  • [EN] HYDROCARBON SYNTHESIS METHODS, APPARATUS, AND SYSTEMS<br/>[FR] PROCÉDÉS, APPAREIL ET SYSTÈMES DE SYNTHÈSE D'HYDROCARBURES
    申请人:MCNEFF CLAYTON V
    公开号:WO2014008355A1
    公开(公告)日:2014-01-09
    Embodiments of the invention include apparatus and systems for hydrocarbon synthesis and methods regarding the same. In an embodiment, the invention includes a process for creating a hydrocarbon product stream comprising reacting a reaction mixture in the presence of a catalyst inside of a reaction vessel to form a product mixture, the reaction mixture comprising a carbon source and water. The temperature inside the reaction vessel can be between 450 degrees Celsius and 600 degrees Celsius and the pressure inside the reaction vessel can be above supercritical pressure for water. In an embodiment, the invention includes an extrusion reactor system for creating a hydrocarbon product stream. The temperature inside the extrusion reactor housing between 450 degrees Celsius and 600 degrees Celsius. Pressure inside the reaction vessel can be above supercritical pressure for water. Other embodiments are also included herein.
    本发明的实施例包括用于合成碳氢化合物的设备和系统以及相关方法。在一种实施例中,本发明包括一种用于创建碳氢化合物产品流的过程,其中在反应容器内,在催化剂的存在下,反应混合物以形成产物混合物,反应混合物包括碳源和水。反应容器内的温度可在450摄氏度至600摄氏度之间,反应容器内的压力可高于水的超临界压力。在一种实施例中,本发明包括一种挤出反应器系统,用于创建碳氢化合物产品流。挤出反应器壳体内的温度在450摄氏度至600摄氏度之间。反应容器内的压力可高于水的超临界压力。本发明还包括其他实施例。
  • Hydrocarbon synthesis methods, apparatus, and systems
    申请人:SarTec Corporation
    公开号:US10144879B2
    公开(公告)日:2018-12-04
    Embodiments of the invention include apparatus and systems for hydrocarbon synthesis and methods regarding the same. In an embodiment, the invention includes a method for creating a hydrocarbon product stream comprising reacting a reaction mixture in the presence of a catalyst inside of a reaction vessel to form a product mixture, the reaction mixture comprising a carbon source and water. The temperature inside the reaction vessel can be between 450 degrees Celsius and 600 degrees Celsius and the pressure inside the reaction vessel can be above supercritical pressure for water. In an embodiment, the invention includes an extrusion reactor system for creating a hydrocarbon product stream. The temperature inside the extrusion reactor housing between 450 degrees Celsius and 600 degrees Celsius. Pressure inside the reaction vessel can be above supercritical pressure for water. Other embodiments are also included herein.
    本发明的实施例包括用于碳氢化合物合成的装置和系统以及有关方法。在一个实施方案中,本发明包括一种生成碳氢化合物产品流的方法,该方法包括在反应容器内催化剂存在的情况下使反应混合物发生反应以形成产品混合物,反应混合物包括碳源和水。反应容器内的温度可以在 450 摄氏度到 600 摄氏度之间,反应容器内的压力可以高于水的超临界压力。在一个实施方案中,本发明包括一个用于产生碳氢化合物产品流的挤压反应器系统。挤压反应器外壳内的温度在 450 摄氏度到 600 摄氏度之间。反应容器内的压力可高于水的超临界压力。本文还包括其他实施例。
  • HYDROCARBON SYNTHESIS METHODS, APPARATUS, AND SYSTEMS
    申请人:SarTec Corporation
    公开号:US20140046104A1
    公开(公告)日:2014-02-13
    Embodiments of the invention include apparatus and systems for hydrocarbon synthesis and methods regarding the same. In an embodiment, the invention includes a process for creating a hydrocarbon product stream comprising reacting a reaction mixture in the presence of a catalyst inside of a reaction vessel to form a product mixture, the reaction mixture comprising a carbon source and water. The temperature inside the reaction vessel can be between 450 degrees Celsius and 600 degrees Celsius and the pressure inside the reaction vessel can be above supercritical pressure for water. In an embodiment, the invention includes an extrusion reactor system for creating a hydrocarbon product stream. The temperature inside the extrusion reactor housing between 450 degrees Celsius and 600 degrees Celsius. Pressure inside the reaction vessel can be above supercritical pressure for water. Other embodiments are also included herein.
  • US9388345B2
    申请人:——
    公开号:US9388345B2
    公开(公告)日:2016-07-12
  • US9382491B2
    申请人:——
    公开号:US9382491B2
    公开(公告)日:2016-07-05
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