1-[2-(2-丁氧基乙氧基)乙氧基]辛烷 | 101433-27-6

• 分子结构分类: 有机化合物 - 有机氧化合物
• 中文名称: 1-[2-(2-丁氧基乙氧基)乙氧基]辛烷
• 英文名称: 2-butoxyethyl 2-(octoxy)ethyl ether
• 英文别名: 1-(2-(2-Butoxy-ethoxy)-ethoxy)-octane；1-[2-(2-butoxyethoxy)ethoxy]octane
• CAS: 101433-27-6
• 化学式: C₁₆H₃₄O₃
• 分子量: 274.444
• InChiKey: ZRNDMQXFESPXIC-UHFFFAOYSA-N

物化性质

• 沸点：
  338.3±17.0 °C(Predicted)
• 密度：
  0.880±0.06 g/cm3(Predicted)

计算性质

• 辛醇/水分配系数(LogP)：
  4.1
• 重原子数：
  19
• 可旋转键数：
  16
• 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

反应信息

• 作为产物：
  描述：

  二乙二醇丁醚 、 正辛醛 在 palladium on activated charcoal 氢气 作用下， 反应 10.0h， 以95%的产率得到1-[2-(2-丁氧基乙氧基)乙氧基]辛烷
  参考文献：
  名称：

  一种从醇和羰基化合物合成醚的简便催化方法

  摘要：

  二烷基醚和烷基氟烷基醚是由醇和羰基化合物在Pd/C存在下，在氢气、W...

  DOI：

  10.1246/bcsj.78.456

文献信息

• Process for the preparation of cyclic esters and method for purification of the same
  申请人：——

  公开号：US20030191326A1

  公开（公告）日：2003-10-09

  The present invention provides a process for production of a cyclic ester by depolymerization of an aliphatic polyester. In the process, a mixture containing the aliphatic polyester and a specific polyalkylene glycol ether, which has a boiling point of 230-450° C. and a molecular weight of 150-450, is heated under normal or reduced pressure to a temperature at which depolymerization of the aliphatic polyester takes place. Then, a substantially homogeneous solution phase, consisting of the melt phase of the aliphatic polyester and the liquid phase of the polyalkylene glycol ether, is formed. Heating of the solution phase is continued to form the cyclic ester by depolymerization and distil out the cyclic ester together with the polyalkylene glycol ether, and then the cyclic ester is recovered from the distillate. The present invention also provides a process for purification of a crude cyclic ester by use of the specific polyalkylene glycol ether described above.

  本发明提供了一种通过脂肪族聚酯的降解来生产环酯的方法。在该过程中，将含有脂肪族聚酯和具有沸点在230-450°C和分子量在150-450之间的特定聚烷基乙二醇醚的混合物，在常压或减压下加热至脂肪族聚酯发生降解的温度。然后，形成由脂肪族聚酯的熔融相和聚烷基乙二醇醚的液相组成的基本均相溶液相。继续加热溶液相以通过降解形成环酯并与聚烷基乙二醇醚一起蒸馏出环酯，然后从馏出物中回收环酯。本发明还提供了一种利用上述特定聚烷基乙二醇醚对粗环酯进行纯化的方法。
• A Convenient Catalytic Method for the Synthesis of Ethers from Alcohols and Carbonyl Compounds
  作者：Yasuyuki Fujii、Hisakazu Furugaki、Shinji Yano、Katsumi Kita

  DOI：10.1246/cl.2000.926

  日期：2000.8

  Unsymmetrical ethers are obtained in excellent yields by the catalytic etherification of alcohols with ketones or aldehydes in the presence of Pd/C under an atmospheric pressure of hydrogen when water produced by the reaction is continuously removed by bubbling hydrogen through the reaction mixture.

  当反应产生的水通过反应混合物中的氢气鼓泡连续除去时，在 Pd/C 存在下，在氢气压力下，通过醇与酮或醛的催化醚化反应，以极好的收率获得不对称醚。
• PROCESS FOR THE PREPARATION OF CYCLIC ESTERS AND METHOD FOR PURIFICATION OF THE SAME
  申请人：KUREHA KAGAKU KOGYO KABUSHIKI KAISHA

  公开号：EP1310496A1

  公开（公告）日：2003-05-14

  The present invention provides a process for production of a cyclic ester by depolymerization of an aliphatic polyester. In the process, a mixture containing the aliphatic polyester and a specific polyalkylene glycol ether, which has a boiling point of 230-450°C and a molecular weight of 150-450, is heated under normal or reduced pressure to a temperature at which depolymerization of the aliphatic polyester takes place. Then, a substantially homogeneous solution phase, consisting of the melt phase of the aliphatic polyester and the liquid phase of the polyalkylene glycol ether, is formed. Heating of the solution phase is continued to form the cyclic ester by depolymerization and distil out the cyclic ester together with the polyalkylene glycol ether, and then the cyclic ester is recovered from the distillate. The present invention also provides a process for purification of a crude cyclic ester by use of the specific polyalkylene glycol ether described above.

  本发明提供了一种通过脂肪族聚酯解聚生产环酯的工艺。在该工艺中，将含有脂肪族聚酯和特定聚亚烷基乙二醇醚（沸点为 230-450°C，分子量为 150-450）的混合物在常压或减压下加热至脂肪族聚酯发生解聚的温度。然后形成基本均匀的溶液相，该溶液相由脂肪族聚酯的熔体相和聚亚烷基二醇醚的液相组成。继续加热溶液相，通过解聚作用形成环酯，并将环酯和聚烷基乙二醇醚一起蒸馏出来，然后从蒸馏物中回收环酯。本发明还提供了一种通过使用上述特定聚亚烷基二醇醚提纯粗环酯的工艺。
• METHOD FOR PRODUCING GLYCOLIDE
  申请人：Kureha Corporation

  公开号：EP2377858A1

  公开（公告）日：2011-10-19

  The invention provides a production process of glycolide comprising the respective steps of: Step 1 of heating a mixture containing a glycolic acid oligomer and a high boiling polar organic under normal or reduced pressure to reflux the mixture and at that time, conducting a total reflux operation in a reflux time within a range of 0.1 to 20 hours under conditions that substantially the whole amount of a distillate distilled out of a reflux system containing the mixture is refluxed into the reflux system; Step 2 of heating the mixture after the total reflux operation or a mixture obtained by adding the high boiling polar organic solvent to a glycolic acid oligomer component recovered from the mixture after the total reflux operation to conduct depolymerization; and Step 3 of collecting glycolide from a co-distillate.

  本发明提供了一种羟基乙酸的生产工艺，包括以下步骤：步骤 1 在常压或减压下加热含有羟基乙酸低聚物和高沸点极性有机物的混合物，使混合物回流，然后进行全回流操作，回流时间在 0.1至20小时的条件下，从含有该混合物的回流系统中蒸馏出的蒸馏物基本上全部回流到该回流系统中；步骤2加热全回流操作后的混合物或将高沸点极性有机溶剂加入到全回流操作后从该混合物中回收的乙醇酸低聚物组分而得到的混合物，以进行解聚；以及步骤3从共蒸馏物中收集乙二醇醚。
• Konstitution und physikalische Eigenschaften von �thern, 3. Mitt.: �ber �ther vom Typ n-C4H9-(O-CH2-CH2)n-OR und i-C4H9-(O-CH2-CH2)n-OR
  作者：R. Riemschneider、P. Gro�

  DOI：10.1007/bf00905665

  日期：——