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Acetic Acid Recovery Using Membranes

Award Information
Agency: Department of Energy
Branch: N/A
Contract: DE-FG02-09ER85492
Agency Tracking Number: 90312
Amount: $999,671.00
Phase: Phase II
Program: SBIR
Solicitation Topic Code: 12 d
Solicitation Number: DE-FOA-0000350
Timeline
Solicitation Year: 2010
Award Year: 2010
Award Start Date (Proposal Award Date): N/A
Award End Date (Contract End Date): 2012-08-14
Small Business Information
1360 Willow Road Suite 103
Menlo Park, CA 94025
United States
DUNS: 942795892
HUBZone Owned: No
Woman Owned: No
Socially and Economically Disadvantaged: No
Principal Investigator
 Yu (Ivy) Huang
 Dr.
 (650) 328-2239
 ihuang@mtrinc.com
Business Contact
 Elizabeth Weiss
Title: Ms.
Phone: (650) 543-3378
Email: egweiss@mtrinc.com
Research Institution
N/A
Abstract

Recovery and recycling of acetic acid from aqueous streams is an important industrial separation that is high cost and energy intensive when performed by conventional technology. This makes acetic acid recovery a tantalizing target for a more efficient, lower cost, simpler approach such as membrane technology. However, the required separation performance, combined with the need for robust chemical and thermal stability of the membrane materials, makes the use of membrane technology for acetic acid recovery very challenging. In this project, perfluorinated polymer membranes are used to dehydrate acetic acid using two new membrane processes. The membranes are stable in hot acetic acid/water mixtures and have good selectivities for separation of water from acetic acid. The proposed membrane processes will lower energy costs by more than 50% compared to conventional separations. In Phase I, we demonstrated the feasibility of the proposed technology. Stable membranes were made that met the permeation criteria required for an economical process. A few bench-scale modules were made and successfully tested with aqueous acetic acid solutions at 90-100

* Information listed above is at the time of submission. *

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