Fluid emulsion purification processes using microporous materials having filtration and adsorption properties

Patent metadata

Field	Value
Publication number	US-9546326-B2
Application number	US-201414193902-A
Country	US
Kind code	B2
Filing date	Feb 28, 2014
Priority date	Nov 4, 2011
Publication date	Jan 17, 2017
Grant date	Jan 17, 2017

Abstract

The present invention is directed to methods of separating a fluid emulsion stream into a hydrocarbon stream and an aqueous stream, by contacting the stream with a microporous membrane to yield a hydrocarbon product stream and an aqueous product stream. The membrane comprises a substantially hydrophobic, polymeric matrix, and substantially hydrophilic, finely divided, particulate, substantially water-insoluble filler distributed throughout the matrix. The polymeric matrix has a mean pore size less than 1.0 micron, and the purities of the product streams are independent of the flux rate of the aqueous product stream and the pore size of the membrane.

First claim

What is claimed is:

1. A method of separating a fluid emulsion stream having a continuous aqueous phase into a hydrocarbon stream and an aqueous stream, comprising passing the fluid emulsion stream through a microporous membrane to yield a hydrocarbon product stream and an aqueous product stream, wherein the membrane comprises a substantially hydrophobic, polymeric matrix and substantially hydrophilic, finely divided, particulate precipitated silica filler distributed throughout said matrix, wherein the polymeric matrix has pores with a volume average diameter less than 1.0 micron, and wherein the membrane demonstrates a hydrocarbon retention rate of at least 90% that is independent of flux rate of the aqueous product stream and the pore size of the membrane.

2. The method of claim 1 , wherein the membrane comprises at least 35 percent by volume of a network of interconnecting pores communicating throughout the membrane.

3. The method of claim 2 wherein the polymeric matrix has pores with a volume average diameter ranging from 0.02 to 1.0 microns.

4. The method of claim 1 , wherein the membrane is in the form of a sheet.

5. The method of claim 1 , wherein the polymeric matrix comprises polyolefin.

6. The method of claim 1 , wherein the filler has been surface modified with functional groups that react with or adsorb one or more materials in the fluid stream.

7. The method of claim 6 , wherein the filler has been surface modified with hydrophilic functional groups.

8. The method of claim 1 , wherein the fluid emulsion stream comprises 2 to 50 percent by weight hydrocarbon.

9. The method of claim 1 , wherein said membrane is housed in a filter assembly.

10. The method of claim 9 , wherein the filter assembly is selected from the group consisting of a pleated filter and a spiral filter.

11. A method of separating a fluid emulsion stream having a continuous hydrocarbon phase into hydrocarbon stream and an aqueous stream, comprising contacting the fluid emulsion stream with a microporous membrane, wherein the membrane comprises a substantially hydrophobic polymeric matrix and substantially hydrophilic, finely divided, particulate precipitated silica filler distributed throughout said matrix, wherein the polymeric matrix has pores with a volume average diameter of less than 1.0 microns, and wherein the hydrocarbon product stream has a water content of less than 10 percent by weight, that is independent of the of flux rate of the aqueous product stream and the pore size of the membrane.

12. A method of separating a fluid emulsion stream into a hydrocarbon stream and an aqueous stream, comprising contacting the fluid emulsion stream with a microporous membrane to yield a hydrocarbon product stream and an aqueous product stream, wherein the membrane comprises a microporous material, said microporous material comprising:
(a) a polyolefin matrix present in an amount of at least 2 percent by weight,
(b) finely divided, particulate, substantially water-insoluble hydrophilic precipitated silica filler distributed throughout said matrix, said filler constituting from about 10 percent to about 90 percent by weight of said microporous material wherein the weight ratio of filler to polyolefin is greater than 0.3, and
(c) at least 35 percent by volume of a network of interconnecting pores communicating throughout the microporous material; wherein said microporous material is prepared by the following steps:
(i) mixing the polyolefin matrix (a), silica (b), and a processing plasticizer until a substantially uniform mixture is obtained;
(ii) introducing the mixture, optionally with additional processing plasticizer, into a heated barrel of a screw extruder and extruding the mixture through a sheeting die to form a continuous sheet;
(iii) forwarding the continuous sheet formed by the die to a pair of heated calender rolls acting cooperatively to form continuous sheet of lesser thickness than the continuous sheet exiting from the die;
(iv) optionally stretching the continuous sheet in at least one stretching direction above the elastic limit, wherein the stretching occurs during or immediately after step (ii) and/or step (iii) but prior to step (v);
(v) passing the sheet to a first extraction zone where the processing plasticizer is substantially removed by extraction with an organic liquid;
(vi) passing the continuous sheet to a second extraction zone where residual organic extraction liquid is substantially removed by steam and/or water;
(vii) passing the continuous sheet through a dryer for substantial removal of residual water and remaining residual organic extraction liquid; and
(viii) optionally stretching the continuous sheet in at least one stretching direction above the elastic limit, wherein the stretching occurs during or after step (v), step (vi), and/or step (vii) to form a microporous material.

13. The method of claim 12 , wherein the fluid emulsion stream is passed through the microfiltration membrane at a flux rate of 0.05 to 20 Gallons/(ft 2 ×psi×day).

14. The method of claim 12 , wherein the fluid emulsion stream comprises crude oil well effluent.

15. The method of claim 12 wherein the fluid emulsion stream does not undergo any separation processes prior to contacting the microfiltration membrane.

16. The method of claim 12 , wherein the hydrocarbon product stream contains less than 10 percent by weight water.

17. The method of claim 12 , wherein the aqueous product stream contains less than 5 percent by weight hydrocarbon.

18. The method of claim 12 wherein the hydrocarbon product stream is recirculated through the microfiltration membrane at least once.

19. The method of claim 12 wherein the fluid emulsion stream passes through a plurality of microfiltration membranes oriented in parallel to provide a total flow rate of at least 125 gal/min.

20. The method of claim 12 wherein the polymeric matrix has pores with a volume average diameter ranging from 0.02 to 1.0 microns.

21. The method of claim 12 wherein the microporous material is in the form of a sheet and has a thickness ranging from 0.5 mil to 18 mil (12.7 to 457.2 microns).

22. The method of claim 12 , wherein the silica (b) has been surface modified with functional groups that react with or adsorb one or more materials in the fluid stream.

Assignees

• Ppg Ind Ohio Inc

Inventors

• Guo Qunhui
• Knox Carol L
• Wilt Truman
• Votruba-Drzal Peter
• Kahle Charles F
• Mccollum Gregory J

Classifications

• C08L23/06

  Polyethylene · CPC title

• B01D17/085

  with membranes · CPC title

• C08K3/34

  Silicon-containing compounds · CPC title

• B01D67/003

  by selective elimination of components, e.g. by leaching · CPC title

• B01D2323/06

  Specific viscosities of materials involved · CPC title