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1,2,6-Trimethoxyhexane | 62635-56-7

中文名称
——
中文别名
——
英文名称
1,2,6-Trimethoxyhexane
英文别名
——
1,2,6-Trimethoxyhexane化学式
CAS
62635-56-7
化学式
C9H20O3
mdl
——
分子量
176.25
InChiKey
PSLCSERJPLPNKR-UHFFFAOYSA-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):
    0.9
  • 重原子数:
    12
  • 可旋转键数:
    8
  • 环数:
    0.0
  • sp3杂化的碳原子比例:
    1.0
  • 拓扑面积:
    27.7
  • 氢给体数:
    0
  • 氢受体数:
    3

文献信息

  • HETEROGENEOUS PROMOTION OF OXIRANE HYDROFORMYLATION
    申请人:Mullin Stephen Blake
    公开号:US20090163742A1
    公开(公告)日:2009-06-25
    A process for making betahydroxyaldehydes such as 3-hydroxypropanal which comprises intimately contacting (a) an oxirane, (b) carbon monoxide, (c) a reducing agent such as hydrogen, (d) from about 0.01 to about 1 weight percent, basis cobalt metal, of a cobalt hydroformylation catalyst which is optionally complexed with a tertiary phosphine ligand, and (e) a heterogeneous, preferably solid, metal promoter used at a molar ratio of 0.05, preferably 0.15, to 100 moles of heterogeneous metal relative to the moles of soluble cobalt hydroformylation catalyst.
    制备β-羟基醛的方法,例如3-羟基丙醛,包括密切接触(a)环氧烷,(b)一氧化碳,(c)还原剂,例如氢气,(d)约0.01至约1重量%,以钴金属为基础,可选择与三级膦配体形成络合物的钴羟甲酰化催化剂,以及(e)使用的非均相,优选为固体的金属促进剂,其用量为相对于可溶性钴羟甲酰化催化剂的摩尔数,0.05,优选为0.15,到100摩尔。
  • Process for the preparation of beta-hydroxy aldehydes
    申请人:SHELL INTERNATIONALE RESEARCH MAATSCHAPPIJ B.V.
    公开号:EP0478850B1
    公开(公告)日:1994-09-14
  • PROCESS FOR MAKING 1,3-DIOLS AND 3-HYDROXYALDEHYDES
    申请人:SHELL INTERNATIONALE RESEARCH MAATSCHAPPIJ B.V.
    公开号:EP0682650A1
    公开(公告)日:1995-11-22
  • LOW TEMPERATURE, LOW PRESSURE UPGRADING AND STABILIZATION OF BIO-OIL OR BIO-OIL FRACTIONS
    申请人:Iowa State University Research Foundation, Inc.
    公开号:US20150291892A1
    公开(公告)日:2015-10-15
    The present application discloses low temperature, low pressure methods (LTLP) for upgrading and/or stabilizing bio-oil or a bio-oil fraction. One method comprises providing a bio-oil or bio-oil fraction and hydrogen, which are reacted in the presence of a catalyst at a temperature of less than 150° C. and a pressure of less than 100 bar (absolute) to produce a hydrogenated liquid oil at a carbon yield of over 75%. Another method comprises providing a bio-oil or bio-oil fraction, providing oxygen reducing reaction conditions, and reacting the bio-oil or bio-oil fraction under the oxygen reducing reaction conditions at LTLP to produce an upgraded bio-oil product containing fewer carbonyls than the bio-oil or bio-oil fraction. Yet another method comprises providing a bio-oil or bio-oil fraction and a solution comprising one or more fermentation organisms and a sugar source. The solution and bio-oil or bio-oil fraction are combined to obtain a fermentation mixture, which is incubated at 15° C. to 30° C. for 16 to 72 hours to produce an upgraded bio-oil fermentation product containing fewer carbonyls than the bio-oil or bio-oil fraction.
  • US5256827A
    申请人:——
    公开号:US5256827A
    公开(公告)日:1993-10-26
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