Oil quality using a microporous hollow fiber membrane

Patent metadata

Field	Value
Publication number	US-9688921-B2
Application number	US-201314052516-A
Country	US
Kind code	B2
Filing date	Oct 11, 2013
Priority date	Feb 26, 2013
Publication date	Jun 27, 2017
Grant date	Jun 27, 2017

Abstract

The present invention includes methods and systems for improving oil quality of a contaminated oil mixture by removing contaminants from a contaminated oil comprising the steps of: pretreating a membrane contactor system having a first and a second surface with an hydrophobic liquid, wherein the hydrophobic liquid is contacted to at least one of the first and second surfaces; obtaining a contaminated oil that comprises oil and lipophobic contaminants; contacting the contaminated oil onto a first surface of one or more membrane contactors to coalesce the oil on the first surface; and collecting the coalesced oil from the contaminated oil on the second surface of the membrane contactor.

First claim

What is claimed is:

1. A method for removing contaminants from a contaminated oil comprising the steps of:
washing a hydrophobic hollow fiber membrane of a membrane contactor system, wherein the hydrophobic hollow fiber membrane has a first surface and a second surface, and wherein washing includes:
washing at least one of the first surface, the second surface, or both the first and second surfaces with an alcohol,
washing at least one of the first surface, the second surface, or both the first and second surfaces with a caustic,
washing at least one of the first surface, the second surface, or both the first and second surfaces with an acid, and
drying the hydrophobic hollow fiber membrane using an inert gas;

pretreating the hydrophobic hollow fiber membrane with a hydrophobic liquid by soaking the hydrophobic hollow fiber membrane in the hydrophobic liquid or circulating the hydrophobic liquid in the hydrophobic hollow fiber membrane, wherein the hydrophobic liquid is contacted to at least one of the first and second surfaces;
obtaining a contaminated oil that comprises oil and lipophobic contaminants;
contacting the contaminated oil onto the first surface of the hydrophobic hollow fiber membrane to coalesce the oil on the first surface; and
collecting the coalesced oil on the second surface of the hydrophobic hollow fiber membrane.

2. The method of claim 1 , further comprising filtering an oil and water mixture using a solid removal system for removing small, medium and large solids from the oil and water mixture to form a stream of the contaminated oil containing only solids smaller than 30 microns, wherein the small, medium or large solids are removed with at least one of a sand filter, a rock filter, a porous ceramic material, a centrifuge, a mesh, a particulate filter, a sieve, a strainer, or gravity.

3. The method of claim 1 , wherein the contaminated oil is at least one of an oil-rich stream, crude oil, transportation fuel, heating oil, refined petroleum products, petrochemicals, bio-oils, renewable oils, vegetable oils, reclaimed oils, waste oils, oil industry liquid streams, oil contaminated water or brine, drilling mud, produced water and oil sands tailings.

4. The method of claim 1 , wherein the contaminated oil is at least one of: not subjected to gravity separation prior to contacting the first surface of the hydrophobic hollow fiber membrane, subjected to gravity separation prior to contacting the first surface of the hydrophobic hollow fiber membrane, or subjected to centrifugation prior to contacting the first surface of the hydrophobic hollow fiber membrane.

5. The method of claim 1 , wherein the contaminated oil is contacted to the first surface of the hydrophobic hollow fiber membrane within 1, 2, 4, 6, 8, 12, 24, 26, 48 or 72 hours from removal of large solids.

6. The method of claim 1 , wherein the membrane contactor system comprises hollow fiber microporous membranes.

7. The method of claim 1 , wherein the hydrophobic hollow fiber membrane comprises polyethylene, polypropylene, polyolefins, polyvinyl chloride (PVC), amorphous polyethylene terephthalate (PET), polyolefin copolymers, poly(etheretherketone) type polymers, surface modified polymers, mixtures or combinations thereof, or a surface modified polymer that comprises polymers modified chemically at one or more halogen groups by corona discharge or by ion embedding techniques.

8. The method of claim 1 , wherein the collected oil is contacted with a counterflowing fluid at the second surface, wherein the counterflowing fluid is selected from the group consisting of a non-polar fluid, an alkane, hexane, an aromatic fluid, benzene, toluene, an ether, diethyl ether, a halogenated fluid, chloroform, dichloromethane, an ester and ethyl acetate.

9. The method of claim 1 , wherein the second surface is in contact with a counterflowing fluid that comprises an oil previously recovered using a hollow fiber contactor.

10. The method of claim 1 , further comprising cleaning a clog in the membrane contactor system using a membrane cleaning system that removes debris that clogs the membrane contactor system.

11. The method of claim 1 , wherein the hydrophobic liquid is selected from at least one of mineral oil, vegetable oil, diesel fuel or oil, kerosene, naphtha, petroleum, or aromatic or aliphatic hydrocarbons containing four or greater carbon atoms.

12. The method of claim 1 , wherein the hydrophobic liquid is an isoparaffinic hydrocarbon selected from at least one of isopar L, isopar C, isopar E, isopar G, isopar H, isopar K, isopar M, or isopar V, or any synthetic thereof.

13. The method of claim 1 , wherein soaking the hydrophobic hollow fiber membrane in the hydrophobic liquid is for at least 0.1, 0.2, 0.3, 0.5, 1, 2, 3, 4, 5, 6, 7, 10, 14, 18, 20, 25, or 30 days.

14. The method of claim 1 , wherein when a flux rate of oil through the hydrophobic hollow fiber membrane degrades, the washing and the pretreating are repeated, thereby increasing the flux rate by at least 10%.

15. The method of claim 1 , wherein pretreating the hydrophobic hollow fiber membrane increases a flux rate of oil through the hydrophobic hollow fiber membrane by at least 10, 11, 12, 13, 14, 15, 20, 25, 30, 35, 40, 50, 60, 70, or 75%.

16. The method of claim 1 , wherein the hydrophobic liquid comprises a same oil as the coalesced oil.

Assignees

• Univ Texas
• Organic Fuels Algae Tech Llc

Inventors

• Seibert Frank
• Briggs Stephen William
• Truscott Stacy S
• Kipp Peter B

Classifications

• B01D2311/04

  Specific process operations in the feed stream; Feed pretreatment · CPC title

• B01D2323/04

  Hydrophobization · CPC title

• B01D2311/2649

  Filtration · CPC title

• B01D61/00

  Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor (separation of gases or vapours by diffusion B01D53/22) · CPC title

• B01D63/02

  Hollow fibre modules · CPC title