Vapor Phase Separation of Water/Acetic Acid Mixtures through Mordenite Type Zeolite Membrane

Wednesday, November 11, 2009: 5:20 PM
Canal C (Gaylord Opryland Hotel)

Ken-ichi Sawamura, Applied Chemistry, Waseda University, Tokyo, Japan
Shintaro Daikohara, Applied Chemistry, Waseda University, Tokyo, Japan
Taisuke Furuhata, Applied Chemistry, Waseda University, Tokyo, Japan
Yasushi Sekine, Applied Chemistry, Waseda University, Tokyo, Japan
Eiichi Kikuchi, Applied Chemistry, Waseda University, Tokyo, Japan
Masahiko Matsukata, Applied Chemistry, Waseda University, Tokyo, Japan

The aqueous solution of acetic acid (AcOH) is by-produced in many chemical processes and reuse of AcOH requires de-watering of the AcOH aqueous solution. However, separation of water/AcOH mixtures by distillation consumes a large amount of energy due to the low relative volatility of water and AcOH. Combination of a membrane separation unit with distillation one can drastically reduce energy demand for the dehydration of acetic acid. While this system requires vapor phase separation of water/acetic acid mixture, there have so far been few studies on membrane separation under these conditions.

Mordenite is a kind of zeolites with both high stability and hydrophilic nature. In this communication, we report vapor phase separation properties of water/AcOH mixture through a mordenite type zeolite membrane.

A mordenite membranes was prepared on the outer surface of tubular porous a alumina support by a secondary-growth method, following the procedure described elsewhere [1]. Vapor permeation and separation measurements were performed using a stainless steel tube module cell. The effective membrane area was 6.28 cm2.

The mordenite membrane highly separated steam from water/AcOH mixtures. In the case of an equimolar mixture of water/AcOH (10/10 kPa), the permeances of water was 1.4 x 10-7 mol m-2 s-1 Pa-1 and the separation factor of water/AcOH exceeded 1000 at steady state at 448 K. The separation mechanism will be discussed.

[1] K. Sawamura et al., J. Chem. Eng. Jpn., 41 (2008) 870-877. >

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