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5-Nonadecen-1-ol

中文名称
——
中文别名
——
英文名称
5-Nonadecen-1-ol
英文别名
(E)-nonadec-5-en-1-ol
5-Nonadecen-1-ol化学式
CAS
——
化学式
C19H38O
mdl
——
分子量
282.5
InChiKey
BTJASUXQNVKCMG-CCEZHUSRSA-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):
    8
  • 重原子数:
    20
  • 可旋转键数:
    16
  • 环数:
    0.0
  • sp3杂化的碳原子比例:
    0.89
  • 拓扑面积:
    20.2
  • 氢给体数:
    1
  • 氢受体数:
    1

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。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。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的超临界压力。本文还包括其他实施例。
  • Coating compositions for use in golf balls
    申请人:Hogge F. Matthew
    公开号:US20060089419A1
    公开(公告)日:2006-04-27
    A golf ball comprising a core, a cover encasing the core, at least one coating layer encasing the cover, and at least one indicia layer immediate adjacent to the coating layer is provided. At least one of the indicia and coating layers comprises at least one two-part, reactive composition comprising at least one radiation-curable iso(thio)cyanate and at least one isocyanate-reactive chemical.
    一种高尔夫球包括一个球芯、一个包裹球芯的盖子、至少一个包裹盖子的涂层和至少一个紧邻涂层的指示层。指示层和涂层中至少有一层包含至少一种双组分反应性组合物,该组合物由至少一种辐射固化异(氰酸酯和至少一种异氰酸酯反应性化学品组成。
  • 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.
  • US7247697B2
    申请人:——
    公开号:US7247697B2
    公开(公告)日:2007-07-24
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