Apparatuses and methods for energy efficient separations including refining of fuel products

Patent metadata

Field	Value
Publication number	US-9868911-B2
Application number	US-201415027983-A
Country	US
Kind code	B2
Filing date	Oct 8, 2014
Priority date	Oct 9, 2013
Publication date	Jan 16, 2018
Grant date	Jan 16, 2018

Abstract

In various aspects, methods and apparatuses for liquid-liquid extraction are provided. In certain aspects, an emulsion can be formed by combining a feed stream, an extractant, and a surfactant. The feed stream comprises a plurality of distinct components including a first component to be removed therefrom. The feed stream may be selected from a group consisting of: a hydrocarbon feed stream and an azeotrope. Then, a portion of the first component is extracted from the feed stream (or emulsion) by contact with a superoleophobic and hygroscopic membrane filter that facilitates passage of the first component and extractant through the superoleophobic and hygroscopic membrane filter. A purified product is collected having the portion of the first component removed. Such methods are particularly useful for refining fuels and oils and separating azeotropes and other miscible component systems. Energy-efficient, continuous single unit operation apparatuses for conducting such separation techniques are also provided.

First claim

What is claimed is:

1. A method of liquid-liquid extraction comprising:
creating an emulsion by combining a feed stream, an extractant, and a surfactant, wherein the feed stream comprises a first component that is a contaminant or impurity present at an initial amount and the feed stream is selected from a group consisting of: a hydrocarbon feed stream and an azeotrope comprising a hydrocarbon;
removing a portion of the first component from the emulsion by contacting the emulsion with a first side of a superoleophobic and hygroscopic membrane filter to facilitate passage of the first component and the extractant through the superoleophobic and hygroscopic membrane filter to a second side of the superoleophobic and hygroscopic membrane filter; and
collecting a purified product having the portion of the first component removed.

2. The method of claim 1 , wherein the removing the portion of the first component by contacting includes gravity-feeding the emulsion to the first side of the superoleophobic and hygroscopic membrane filter at ambient conditions.

3. The method of claim 1 , wherein the feed stream comprises a plurality of distinct components including the first component and a second component, wherein the first component and the second component are miscible with one another.

4. The method of claim 1 , wherein the feed stream comprises a plurality of distinct components including the first component and a second component, wherein the first component comprises a polar molecule and the second component comprises a non-polar molecule.

5. The method of claim 4 , wherein the hydrocarbon feed stream comprises a plurality of distinct components and is a fuel feedstock, wherein the first component is a contaminant and a remainder of the plurality of distinct components are fuel components, so that the removing of the portion of the first component by contacting the emulsion with the superoleophobic and hygroscopic membrane filter separates the first component from the fuel components so that the purified product is a refined fuel.

6. The method of claim 1 , wherein the superoleophobic and hygroscopic membrane filter is coated with a cross-linked material formed from a hydrophilic polymer comprising poly(ethylene glycol) diacrylate (PEDGA), a low surface energy material comprising 1H, 1H, 2H, 2H-heptadecafluorodecyl polyhedral oligomeric silsequioxane (F-POSS), and a cross-linker comprising 2-hydroxy-2-methyl propiophenone.

7. The method of claim 1 , wherein the superoleophobic and hygroscopic membrane filter is coated with a perfluoroalkoxy silane.

8. The method of claim 1 , wherein the portion of the first component removed from the purified product is about 99.99 weight % of the initial amount of the first component in the feed stream.

9. The method of claim 1 , wherein the removing is continuously conducted in a single unit operation of a separator device, wherein the emulsion is gravity fed from the first side to the second side of the superoleophobic and hygroscopic membrane filter to continuously separate the first component and the extractant from the emulsion.

10. The method of claim 9 , wherein the separator device further comprises:
a second membrane filter that is oleophilic and hydrophobic in fluid contact with the emulsion that continuously removes a remainder of the feed stream from the emulsion.

11. The method of claim 10 , wherein the second membrane filter is positioned above the superoleophobic and hygroscopic membrane filter with respect to a direction the emulsion is gravity fed from the first side to the second side of the superoleophobic and hygroscopic membrane filter.

12. The method of claim 1 , wherein the feed stream is a fuel feed stream selected from a group consisting of: a diesel fuel, a jet fuel, gasoline, kerosene, a liquid petroleum gas, a low sulfur fuel, a coal-derived liquid fuel, a synthetic fuel, an ether, an alcohol, a biofuel, a biodiesel, a biodiesel-derived fuel, a synthetic diesel, and combinations thereof and the combining of the fuel feed stream with the extractant further comprises introducing the fuel feed stream into a contacting vessel fluidically coupled to the first side of the superoleophobic and hygroscopic membrane filter, wherein the contacting vessel contains a continuous phase of the extractant, and the selectively removing further comprises:
selectively removing the extractant from the contacting vessel through the superoleophobic and hygroscopic membrane filter;
coalescing the fuel feed stream within the contacting vessel; and
collecting the coalesced fuel as the refined fuel, wherein the refined fuel has less than or equal to about 1,000 parts per million of the first component.

13. The method of claim 12 , further comprising: filtering the selectively extracted extraction fluid through a selective stationary absorbent.

14. The method of claim 1 , wherein the first component that is a contaminant or impurity in the feed stream comprises one or more of a sulfur-containing compound, a nitrogen-containing compound, or an aromatic compound.

15. A method of liquid-liquid extraction comprising:
mixing together an extractant, a surfactant, and a feed stream that comprises a first component that is a contaminant or impurity present at an initial amount so as to form an emulsion, wherein the feed stream is selected from a group consisting of: a hydrocarbon feed stream and an azeotrope comprising a hydrocarbon;
removing a portion of the first component from the emulsion by contacting the emulsion with a first side of a superoleophobic and hygroscopic membrane filter to facilitate passage of the first component and the extractant through the superoleophobic and hygroscopic membrane filter to a second side of the superoleophobic and hygroscopic membrane filter;
collecting an extracted stream comprising the first component and extractant after it passes through the superoleophobic and hygroscopic membrane filter;
adsorbing at least a portion of the first component in the extracted stream by contacting the extracted stream with an adsorbent and separating the first component from the extractant; and
collecting a purified product having the portion of the first component removed.

16. The method of claim 15 , further comprising recycling the extractant after the adsorbing by mixing recycled extractant with the surfactant and the feed stream.

17. The method of claim 15 , wherein the portion of the first component removed from the purified product is about 99.99 weight % of the initial amount of the first component in the feed stream.

18. The method of claim 15 , wherein the removing is continuously conducted in a single unit operation of a separator device, wherein the emulsion is gravity fed from the first side to the second side of the superoleophobic and hygroscopic membrane filter to continuously separate the first component and the extractant from the emulsion to form the extracted stream and the separator device further comprises:
a second membrane filter that is oleophilic and hydrophobic in fluid contact with the emulsion that continuously removes a remainder of the feed stream from the emulsion to form the purified product; and
the adsorbent disposed downstream of the second side of the superoleophobic and hygroscopic membrane filter to continuously adsorb at least a portion of the first component from the extractant.

19. The method of claim 15 , wherein the mixing comprises introducing the feed stream into a vessel by a first spray nozzle and introducing the extractant and the surf

Assignees

• Univ Michigan Regents
• Us Air Force
• Us Air Force

Inventors

• Reams Josiah T
• Guenthner Andrew
• Mabry Joseph
• Lamison Kevin
• Tuteja Anish
• Kota Arun K
• Kwon Gibum

Classifications

• C10L1/026

  for compression ignition · CPC title

• C10G2300/202

  Heteroatoms content, i.e. S, N, O, P · CPC title

• C02F1/44

  by dialysis, osmosis or reverse osmosis {(general membrane separation processes B01D61/00, membrane modules B01D63/00, electrodialysis C02F1/4693, combination of membrane modules and bioreactors C02F3/1268)} · CPC title

• C10L2270/04

  for turbines, planes, power generation · CPC title

• C07C29/86

  by liquid-liquid treatment · CPC title