1-Butyl-2-methylpyridinium trifluoromethanesulfonate | 1770850-20-8

• 分子结构分类: 有机化合物 - 有机酸及其衍生物 - 有机磺酸及其衍生物
• 英文名称: 1-Butyl-2-methylpyridinium trifluoromethanesulfonate
• 英文别名: 1-butyl-2-methylpyridin-1-ium;trifluoromethanesulfonate
• CAS: 1770850-20-8
• 化学式: C11H16F3NO3S
• 分子量: 299.31
• InChiKey: MLOOVQAZYDNHIQ-UHFFFAOYSA-M

计算性质

• 辛醇/水分配系数(LogP)：
  2.13
• 重原子数：
  19
• 可旋转键数：
  3
• 环数：
  1.0
• sp3杂化的碳原子比例：
  0.55
• 拓扑面积：
  69.5
• 氢给体数：
  0
• 氢受体数：
  6

文献信息

• Separations with ionic liquid solvents
  申请人：Chevron Phillips Chemical Company LP

  公开号：US10227274B2

  公开（公告）日：2019-03-12

  Disclosed are systems and methods which provide a process stream comprising a gaseous component, capture the gaseous component from the process stream by an ionic liquid solvent of a separator, and recover a captured gaseous component from the ionic liquid solvent in a regenerator. A second gaseous component from the process stream may be captured by the ionic liquid solvent of the separator, and the second gaseous component may be recovered from the ionic liquid solvent in the regenerator. Alternatively, the second gaseous component from the process stream may be uncaptured by the ionic liquid solvent, and the uncaptured second gaseous component may be recovered from a membrane unit.

  所公开的系统和方法可提供包含气态成分的工艺流，通过分离器的离子液体溶剂从工艺流中捕获气态成分，并在再生器中从离子液体溶剂回收捕获的气态成分。分离器的离子液体溶剂可捕获工艺流中的第二种气体成分，并在再生器中从离子液体溶剂回收第二种气体成分。或者，工艺流中的第二气态成分可能未被离子液体溶剂捕获，未被捕获的第二气态成分可从膜装置中回收。
• Separations With Ionic Liquid Solvents
  申请人：Chevron Phillips Chemical Company LP

  公开号：US20150133711A1

  公开（公告）日：2015-05-14

  Disclosed are systems and methods which provide a process stream comprising a gaseous component, capture the gaseous component from the process stream by an ionic liquid solvent of a separator, and recover a captured gaseous component from the ionic liquid solvent in a regenerator. A second gaseous component from the process stream may be captured by the ionic liquid solvent of the separator, and the second gaseous component may be recovered from the ionic liquid solvent in the regenerator. Alternatively, the second gaseous component from the process stream may be uncaptured by the ionic liquid solvent, and the uncaptured second gaseous component may be recovered from a membrane unit.