To provide a device for separating an azeotropic mixture, with simple composition and processes, and low cost, reducing the amount of energy to be applied to achieve high energy-saving effect, and obtaining components of high purity; and to provide a method for separating an azeotropic mixture.
An azeotropic mixture is distilled in a distillation column 2 to obtain distillate steam and bottoms, and the distillate steam thus obtained is separated into steam as a heat source for a reboiler and steam for pulling out products. The compressed and heated distillate steam A is supplied, as the heat source, to the reboiler 5, and the compressed and heated distillate steam B passes through a steam-permeable membrane 6 to be separated into a non-permeable component and a permeable component. Then, the non-permeable component is recovered after heating the azeotropic mixture. The composition of the device and the processes are simple to reduce equipment cost and achieve high energy-saving effect, and the components are separated by using the steam-permeable membrane 6. Consequently, the device 1 for separating an azeotropic mixture and the method for separating an azeotropic mixture are provided, the device and method obtaining the components of high purity.
MIKURIYA TOMOYUKI
MIMURA KENICHI
KIMURA NOBUHIRO
MATSUKATA MASAHIKO
JX NIPPON OIL & ENERGY CORP
UNIV WASEDA
| JPS60202705A | 1985-10-14 | |||
| JPH07227517A | 1995-08-29 | |||
| JP2006263561A | 2006-10-05 | |||
| JP2007275690A | 2007-10-25 | |||
| JP2010036057A | 2010-02-18 | |||
| JP2010036059A | 2010-02-18 | |||
| JPS60202705A | 1985-10-14 | |||
| JPH07227517A | 1995-08-29 | |||
| JP2006263561A | 2006-10-05 | |||
| JP2007275690A | 2007-10-25 | |||
| JP2010036057A | 2010-02-18 | |||
| JP2010036059A | 2010-02-18 |