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1-heptoxy-3-methylimidazolium bis(trifluoromethanesulfonyl)imide | 1422952-76-8

中文名称
——
中文别名
——
英文名称
1-heptoxy-3-methylimidazolium bis(trifluoromethanesulfonyl)imide
英文别名
1-heptyloxy-3-methylimidazolium bis(trifluoromethanesulfonyl)imide
1-heptoxy-3-methylimidazolium bis(trifluoromethanesulfonyl)imide化学式
CAS
1422952-76-8
化学式
C2F6NO4S2*C11H21N2O
mdl
——
分子量
477.449
InChiKey
CMROJKAYSUREEB-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

反应信息

  • 作为产物:
    描述:
    1-methyl-3-heptoxyimidazolium bromide 、 bis(trifluoromethane)sulfonimide lithium 为溶剂, 反应 2.0h, 生成 1-heptoxy-3-methylimidazolium bis(trifluoromethanesulfonyl)imide
    参考文献:
    名称:
    Isoamyl acetate synthesis in imidazolium-based ionic liquids using packed bed enzyme microreactor
    摘要:
    The acylation of isoamyl alcohol with acetic anhydride catalyzed by immobilized Candida antarctica lipase B was studied in ionic liquids (ILs) based on quaternary imidazolium cations with alkyl, alkenyl, alkynyl, benzyl, alkoxyl or N-aminopropyl side chains. Among the tested ILs, the highest enzyme activity together with the highest isoamyl acetate yield were obtained in [C(7)mmim][Tf2N].No loss of lipase B activity was observed during one-month incubation in this hydrophobic IL without the presence of substrates. Isoamyl acetate synthesis using [C(7)mmim][Tf2N] as solvent was further studied in a continuously operated miniaturized enzymatic packed bed reactor at various flow rates and temperatures. Up to 92% isoamyl acetate yield could be obtained within 15 min by using 0.5 M acetic anhydride and 1.5 M isoamyl alcohol inlet concentrations at 55 degrees C, corresponding to the volumetric productivity of 61 mmol l(-1) min(-1), which to the best of our knowledge is the highest reported so far for this reaction. No decrease in productivity was experienced during the subsequent runs of continuous microbioreactor operation performed within 14 consecutive days. The benefits of reactor miniaturization along with the green solvent application were therefore successfully exploited for the development of a sustainable flavour ester production. (C) 2012 Elsevier Ltd. All rights reserved.
    DOI:
    10.1016/j.procbio.2012.04.028
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