CA2413799C

CA2413799C - Water separation from solvent

Info

Publication number: CA2413799C
Application number: CA2413799A
Authority: CA
Inventors: Robert S. Johnson
Original assignee: Individual
Current assignee: Individual
Priority date: 2000-06-29
Filing date: 2001-06-27
Publication date: 2010-08-24
Anticipated expiration: 2021-06-27
Also published as: EP1309391A1; AU2001275846A1; JP4150586B2; EP1309391A4; CA2413799A1; JP2004501756A; WO2002002211A1

Abstract

An apparatus (100) and method for separating residual water from a solvent.
The device comprises a reservoir (102) containing a solution comprising solvent containing residual water, the reservoir having an opening to allow the solution to drain from the reservoir. A membrane layer is provided comprising a first layer (104) of fluoropolymer and a second layer of fluoropolymer (105). The membrane is positioned in series with the reservoir opening. Vacuum is generated on one side of the membrane layer wherein the solvent containing water passes through the membrane therein removing water from the solvent to provide a solvent with a water level of less than or equal to 1.0 ppm.

Description

3 This application claims the benefit of copending U.S. provisional patent application 4 serial No. 60/215,055 filed June 29, 2000, the teachings of which are incorporated herein by reference.

This invention generally relates to the field of chemical laboratory equipment for 8 sample preparation and particularly to the use of a hydrophobic membrane to separate water 9 from an organic solvent, and more particularly to an apparatus and method for increasing the l0 flow rate of the solvent through the membrane without adversely affecting the performance 11 of the membrane.

13 When samples are to be analyzed for organic and/or inorganic trace compounds, the 14 samples are typically extracted with an organic solvent. The solvent extracts the compounds from the sample, due to selective chemistry.
16 Before the extract can be analyzed, all residual water should preferably be removed 17 from the extracting solvent. This is due to the adverse effect residual water can have on 18 subsequent sample preparation steps which are required to prepare and analyze the samples.
19 Current practice embodies the use of a drying agent called sodium sulfate and has 2o been the standard technique to remove the residual water from solvent extracts. Sodium 21 sulfate is a granular material that has a high binding capacity for residual water. The sodium 22 sulfate is first heated to. drive off any water that has been adsorbed into the material. This 23 typically requires heating overnight at 400C. The sodium sulfate is then placed into a glass 24 funnel containing filter paper, or a chromatography column. The funnel or column is then washed with extracting solvent to wash off any impurities, The extracting solvent is then 26 discarded. Once the sodium sulfate is clean, the solvent extract is poured on top of the 27 sodium sulfate. As the solvent drains slowly through, the residual water becomes bound to 28 the surface of the sodium sulfate. The collected solvent passing through is now dry and ready 29 for analysis.
3o The use of sodium sulfate, even though easy to use, requires many physical 31 manipulations. Sodium sulfate requires the use of glassware that must be subsequently 32 washed so as not to introduce contaminants into the samples and requires the purchase of, and 1 the disposal of, the used sodium sulfate. The labor time and the materials costs, add 2 significantly to the total cost of performing sample extractions.
3 U.S. Patent 5,268,150 assigned to Corning Incorporated, discloses the use of a 4 hydrophobic membrane in an extraction device which allows a solvent to pass therethrough, yet will not allow a significant amount of water from the sample liquid to pass therethrough.
6 The patent discloses that hydrophobic membranes incorporating polytetrafluoroethylene 7 (PTFE) have been found to be very effective in achieving the desired results of letting solvent 8 pass, while retaining the sample usually consisting of a relatively large portion of water or an 9 aqueous solution. The patent goes on to state that the typical dimensions of the membrane 1o range from 10 to 50 millimeters in diameter with a thickness ranging from 0.1 to 5.0 microns 11 with a pore size ranging from 0.2 to 5.0 microns, depending upon the sample being 12 processed.
13 Accordingly, it is an object of the invention to improve on the above referenced 14 designs and provide a more efficient technique for separation water from a given solvent.
More specifically, it is an object of the present invention to provide a method and apparatus 16 and improved membrane design to improve the purification flow rate of a solvent/water 17 mixture or emulsion through said membrane, to remove water, without adversely effecting 18 membrane performance.

2o A method/apparatus for separating residual water from a solvent, comprising the steps 21 of providing a reservoir containing a solution comprising solvent containing residual water, 22 the reservoir having an opening to allow the solution to drain from the reservoir, and passing 23 the solution in the reservoir through a fluoropolymer membrane supported on a 24 fluoropolymer screen. The supported membrane is positioned in series with the reservoir opening, the membrane having a first side in contact with the solution and an opposing 26 second side. Pressure is decreased on the second side of the supported membrane relative to 27 the first side of said supported membrane to thereby increase the flow rate of the solvent 28 through the membrane, wherein the fluoropolymer membrane operates to remove water from 29 the solvent.
3o BRIEF DESCRIPTION OF THE DRAWINGS
31 Figure 1 is a sectional view of a first separator apparatus in accordance with the 32 present invention, and 1 Figure 2 is a sectional view of a second separator apparatus in accordance with the 2 present invention.
3 Figure 3 is an exploded view of a preferred separator apparatus in accordance with the 4 presentinvention.
The above and other objects, feature, and advantages of the present invention will be 6 apparent in the following detailed description thereof when read in conjunction with the '7 appended drawings wherein the same reference numerals denote the same or similar parts 8 throughout the several views.

1o Referring to the drawings, there is illustrated generally a first concentrator/extractor 11 apparatus 100. The concentrator/extractor apparatus 100 comprises a column 102 and 12 fluoropolymer material layers 104 and 105. Preferably, fluoropolymer layer 104 is laminated 13 to fluoropolymer layer 105 to provide a membrane type construction. A
preferred 14 fluoropolymer for layer 104 is PTFE and a preferred fluoropolymer for layer 105 is ethylene-chlorotrifluroethylene (ECTFE).
16 A screen support layer is shown at 106, in addition to a base assembly 108, and a 17 collection vessel 110. The column 102 forms a reservoir to hold a solvent.
The column 102, 18 which may be pressed down on top of the membrane (fluoropolymer layer 104 laminated to 19 fluoropolymer layer 105) may be used to hold the membrane in place. The column 102 may 2o seal the membrane and prevent any solvent from passing around the edge of the membrane.
21 The column 102 and the collection vessel 110 are preferably made of glass.
The screen 22 support member 106 is preferably an ECTFE or ETFE fluoropolymer fabric screen with 0.5- .
23 1.0 mm openings, 0.5 -1.0 mm thick, and a 0.25-0.50 mm thread.
24 The membrane comprises layers 104 and 105 are preferably characterized as follows:
Pore Size: 0.05 to 0.2 micron;
26 Bubble Point: Individual between 24.0 psi and 34.0 psi (47 mm membrane;
27 isopropanol at 21°C) 28 WEP: 50.0 psi minimum individual 29 Gurley Number: Mean < 30.0 seconds (100 cc air through 1 in2 orifice, 4.88"
water pressure drop) 1 Thickness: Preferably 1.0 mils to 20 mils.
2 The following definitions apply to the above:
3 Gurley number: A measure of the air permeability of the fluoropolymer. The Gurley 4 number is the time in second required for 100cc of air to pass through a one square inch area of membrane, when a constant pressure of 4.88 inches of water is applied.
6 Bubble point: The minimum pressure in KG/CMZ required to force air through the 7 fluoropolymer that has been prewetted with water, isopropanol, or methanol.
8 Water entry pressure: The pressure at which water permeates through the membrane.
9 This is a visual test.
In a preferred embodiment, the PTFE layer 104 has usable diameters in the range of 11 40-100 mm. The fluoropolymer layer 104 and fabric support member 105 are positioned in 12 series between the column 102 and the collection vessel 110. In a most preferred 13 embodiment, a 3 mil thick PTFE layer 104 with a 0.1 micron pore size is supported on a 10 14 mil thick non-woven layer 105, comprised of ECTFE polymer, which ECTFE
polymer is preferably obtained from Ausimont and sold under the tradename "HALAR".
16 It is worth noting that in a preferred embodiment, a 3.0 mil PTFE layer is laminated to 17 a 10 mil ECTFE layer, and. a resulting thickness of 3-7 mils is produced for the laminate as a 18 result of the heat setting laminating process.
19 In accordance with the present invention, the screen layer 106 is preferably ethylene-trifluroethylene copolymer (ETFE). The screen layer serves to gap or space laminated layers 21 104 and 105 on the funnel surface such that it is possible to distribute the pressure differential 22 across the entire cross-sectional area of the funnel surface to achieve more efficient 23 performance. However, while it can be appreciated that screen layer 106 is a separate 24 components, it can be appreciated that screen layer 106 may actually be incorporated directly into the surface of the funnel upon which the laminated layers 104 and 106 rest. This would 26 provide the equivalent effect of spacing laminated layers 104 and 106 to evenly distribute the 27 pressure differential created~by vacuum.
28 Furthermore, in the context of the present invention it should be appreciated that the 29 removal of water from a given solvent containing, e.g., some analyte to be evaluated by 1 techniques such as gas-chromatography/mass spectrometry (GC/MS), is such that the 2 removal of water is highly efficient and allows for the generation of a GC/MS analysis that is 3 not compromised by the presence of water. In that regard, it has been found that the present 4 invention allows for removal of water down to a level at or below 1.0 ppm.
Expanding upon the above, it will be appreciated that with respect to the removal of 6 water herein, it has been found that by reference to the generation of a GC/MS analysis that is 7 not compromised by the presence of water, it should also be understood that this is reference 8 to the fact that the water removal herein is sufficient to reduce the water levels to that level 9 wherein the possibility of contamination of the GC column by a water soluble inorganic acid 1o is removed or attenuated. In addition, the possibility of any degradation of the GC column 11 due to the presence of water soluble inorganic salts is also equally attenuated or removed, and 12 GC/MS can proceed without such problems.
13 Additionally, it is worth noting that the invention herein is preferably applied to a 14 water/solvent mixture wherein the solvent is denser than water. However, in broad context the invention herein is not so limited.
16 As shown in Figure 2, there is illustrated generally a second concentrator/extractor 17 apparatus 200. The concentrator/extractor apparatus 200 comprises a column 202, a 18 fluoropolymer layer 204 (PTFE) and a fluoropolymer layer 205 (ECTFE) that, as noted 19 above, are preferably laminated to one another. In addition, a support screen member 206 is shown, a base assembly 20~, and a collection vessel 210. The apparatus 200 can be coupled 21 to an external low-level vacuum 216. A low level vacuum is one that preferably creates a 22 pressure drop of less than 6" Hg. Alternatively, the assembly 200 could include a vacuum 23 generator device that uses a compressed gas source to create a pressure differential. This 24 assembly 200 could be manufactured as a unit and could sit in a hood, directly underneath a separatory funnel. Once the gas source is set, the operator may select one of a plurality of 26 vacuum levels on a vacuum level selector panel 214. The vacuum selector panel 214 controls 27 the pressure drop across the membrane. These levels may include: off, low, medium, and 28 high. Alternatively, the vacuum level may be continuously variable. Being able to select 29 from a variety of different vacuum levels has shown to be useful, as samples which create a significant emulsion can be quite easily broken if no vacuum is used. Once the emulsion has 31 broken, then the vacuum setting can be increased to significantly reduce the sample process 1 time. For example, lOml of methylene chloride may take about 4 minutes to flow through 2 with a 5"Hg vacuum, but the same sample through the same membrane may only take 15-20 3 second at 6"Hg. This is a significant time savings.
4 A controller 212 coupled to the vacuum 216 can be added that will vary the pressure drop across the membrane as a function of time. For example, the controller 212 can be 6 programmed to have an initial predetermined period of time during which no vacuum or a 7 very low first predetermined vacuum level is applied and a second predetermined period of 8 time during which an increased second predetermined vacuum level is applied.
The 9 controller 212 can also be programmed to turn off the vacuum after a third predetermined to period of time to prevent the apparatus from pulling residual water through the membrane.
11 Given sufficient time, approximately 6 - 12 hours, any residual water on the surface of the 12 membrane may "wet" the membrane and flow through with the organic solvent.
Therefore, 13 there is a limited time window for allowing water to reside on the membrane, but this time is 14 not a problem for the application that this device will be used for.
In addition, testing has shown that draining the emulsion directly into the membrane 16 , reservoir aids with the breaking of emulsions. Once the emulsion has broken, if the analyst 17 desires, after each drying step, the retained water and emulsion can be poured back into the 18 separatory funnel for additional extractions. This could possibly significantly increase 19 recovery values.
As noted, Figure 3 is an exploded view of a preferred separator apparatus in 21 accordance with the present invention. More specifically, as shown therein there can be seen 22 locking ring 310, wave spring 312, thrust ring 314, reservoir 316, base 318 for membrane and 23 screen (not shown), stopcock 322, shut-off connectors 324 and 326 (through which vacuum 24 may be applied), bracket 328 and support rod 330.
It should be understood that, while the present invention has been described in detail 26 herein, the invention can be embodied otherwise without departing from the principles 27 thereof, and such other embodiments are meant to come within the scope of the present 28 invention as def ned in the following claims.

Claims

What is claimed is:

1. A method for separating residual water from a solvent, comprising the steps of:
providing a reservoir containing a solution comprising solvent containing residual water, the reservoir having an opening to allow the solution to drain from the reservoir, resisting the flow of the solution from the reservoir with a membrane layer comprising a first layer of fluoropolymer and a second layer of fluoropolymer, said membrane positioned in the series with the reservoir opening, decreasing the pressure on the second side of said supported membrane relative to the first side of said supported membrane to thereby increase the flow rate of the solvent through the membrane;
therein removing said water from said solvent to provide a solvent with a water level of less than or equal to 1.0 ppm.

2. The method of claim 1 wherein said first layer of fluoropolymer comprises PTFE.

3. The method of claim 1 wherein said second layer of fluoropolymer comprises ECTFE.

4. The method of claim 2 wherein said first layer comprising PTFE has a thickness of about 1-5 mils.

5. The method of claim 3 wherein said second layer of ECTFE has a thickness of about 5-15 mils.

6. The method of claim 1 wherein said membrane is characterized with a Gurley Number of ~ 30.0 seconds and a pore size of 0.05 - 2.0 microns.

7. The method of claim 1 wherein said membrane has a pore size is about 0.05 -2.0 micron.

8. The method of claim 1 wherein the step of decreasing the pressure on the second side of the membrane relative to the first side of the membrane is done by applying a vacuum

9. The method of claim 8 wherein the vacuum is varied.

10. The method of claim 8 wherein the vacuum ranges from about 1-15" Hg.

11. The method of claim 8 wherein the vacuum ranges from about 1-5" Hg.

12. The method of claim 1 wherein the decreasing of the pressure is delayed a selected period of time.

13. A method for separating residual water from a solvent, comprising the steps of:
providing a reservoir containing a solution comprising solvent containing residual water, the reservoir having an opening to allow the solution to drain from the reservoir, resisting the flow of the solution from the reservoir with a membrane layer comprising a first layer of polytetrafluroethylene (PTFE) and a second layer of ethylene-chlorotrifluroethylene (ECTFE) layer, said membrane positioned in the series with the reservoir opening, the membrane having said first layer in contact with the solution, and decreasing the pressure on the second side of said supported membrane relative to the first side of said supported membrane to thereby increase the flow rate of the solvent through the membrane.

14. The method of claim 13 wherein said membrane itself is further characterized with a Gurley Number of ~ 25.0 seconds and a pore size of 0.05 - 2.0 microns.

15. The method of claim 14 wherein said pore size is about 0.1 micron.

16. The method of claim 13 wherein said PTFE layer has a thickness of about 1-mils and said ECTFE layer has a thickness of about 5-15 mils.

17. The method of claim 13 wherein the step of decreasing the pressure on the second side of the membrane relative to the first side of the membrane is done by applying a vacuum

18. The method of claim 17 wherein the vacuum is varied.

19. The method of claim 17 wherein the vacuum ranges from about 1-15" Hg.

20. The method of claim 19 wherein the vacuum ranges from about 1-5" Hg.

21. The method of claim 1 wherein the decreasing of the pressure is delayed a selected period of time.

22. A method for separating residual water from a solvent, comprising the steps of:
providing a reservoir containing a solution comprising solvent containing residual water, the reservoir having an opening to allow the solution to drain from the reservoir, resisting the flow of the solution from the reservoir with a membrane layer comprising a first layer of fluoropolymer and a second layer of fluoropolymer, said membrane positioned in the series with the reservoir opening, said membrane supported on a screen layer, decreasing the pressure on the second side of said supported membrane relative to the first side of said supported membrane to thereby increase the flow rate of the solvent through the membrane;
therein removing said water from said solvent to provide a solvent with a water level of less than or equal to 1.0 ppm.

23. The method of claim 22 wherein said screen layer comprises a fluoropolymer polymer.

24. The method of claim 23 wherein said fluoropolymer comprises ETFE.

25. An apparatus for separating residual water from a solvent, comprising:
a reservoir containing a solution comprising solvent containing residual water, the reservoir having an opening to allow the solution to drain from the reservoir, a membrane layer comprising a first layer of fluoropolymer and a second layer of fluoropolymer, said membrane positioned in the series with the reservoir opening, a device for generating vacuum on said second layer of fluoropolymer, wherein said solvent containing water passes through said membrane layer therein removing water from said solvent to provide a solvent with a water level of less than or equal to 1.0 ppm.