Selective phenol removal membranes and valorization of olive oil waste streams
AssigneeB.G. Negev Technologies and Applications Ltd., At Ben-Gurion University
InventorsJack GILRON, Charles LINDER, Zeev WIESMAN
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Abstract
The present invention discloses stable composite membranes comprising a porous support having one or more thin selective layers coated on a top surface thereof, whereas at least one of said thin selective layers comprises a crosslinked fluorinated silicone polymer, and further wherein the total thickness of said one or more thin selective layers ranges between 0.1 to 10 microns. The use of these membranes in the process of olive oil wastewater treatment and the valorization of polyphenol-rich by-products, are also disclosed.
Claims24
1-33. (canceled)
A stable composite membrane comprising a porous support having one or more thin selective layers coated on a top surface thereof, whereas at least one of said thin selective layers comprises a crosslinked fluorinated silicone polymer, and further wherein the total thickness of said one or more thin selective layers ranges between 0.1 to 10 microns.
A process for obtaining a polyphenol rich concentrate of an olive oil mill wastewater stream, said process comprising:
- a. Contacting an olive oil mill wastewater stream with an acid, to obtain an acidified olive oil mill wastewater stream at a pH ranging from 2 to 2.5;
- b. Feeding said acidified olive oil mill wastewater stream into a holding tank, and phase separating from said olive oil mill wastewater:
- i. a bottom layer stream rich in suspended solids,
- ii. a top layer stream rich in olive oil
- iii. a middle layer stream, that is largely devoid of suspended solids and of olive oil;
- c. Feeding said middle layer stream into an ultrafiltration unit (UF), thereby separating said middle layer stream into a UF permeate and a UF concentrate;
- d. Feeding said UF permeate into a nanofiltration unit (NF), thereby separating said UF permeate into a NF concentrate rich in polyphenols and a NF permeate largely free of polyphenols;
- e. Separately feeding each of said UF concentrate and said NF concentrate into a selective side of a membrane contactor unit comprising the composite membrane of claim 1, and circulating said concentrate next to a selective side of said membrane, further whereas a high pH strip solution is circulated next to a porous side of said membrane, to obtain a polyphenol rich permeate stream at the porous side of the contactor membrane unit;
- f. passing said polyphenol rich permeate stream through a second nanofiltration unit (NF2), thereby obtaining a concentrate which is a polyphenol rich product, and a caustic solution permeate.
Dependencies are inferred from the claim text.