Patent US4715960A successfully refreshed from Google Patents.
US4715960A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method for the modification of polycarbonate membranes, the membranes produced by such method and their use
Assignee: ExxonMobil Technology and Engineering Co
•
Filing: 1983-03-10
•
Granted: 1987-12-29
•
Expires: 2003-03-10
Abstract
Abstract Polycarbonate membranes are prepared for the selective separation of organic liquid mixtures, especially for the separation of ketone dewaxing solvents from dewaxed oil by preshrinking said membranes in presence of a class of solvents of solubility parameter values in the range of from 8.9 to 10 (cal/cm3)0.5, and which do not dissolve the membranes. Preshrunk polycarbonate membranes, prepared by the method of the present invention, can be used for the selective separation of the various components in organic liquid mixtures such as, for the separation of dewaxing solvents from dewaxed oil, preferably the separation of ketone dewaxing solvents from dewaxed oil. The separation is based on a reverse osmosis technique whereby the solvent is permeated through the membrane under an applied pressure sufficient to overcome the osmotic pressure of the system. Applied pressures can vary from 50 up to 1,500 psi, depending on solution concentration. The separation can be carried out in the temperature range -30 DEG to about +80 DEG C., preferably about -20 DEG to about +60 DEG C.
Inventors
- 👤 John A. Thompson
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-07 12:01
CPC Classifications
B; B01; B01D; B01D67/00; B01D67/0081; B01D67/0088; B01D71/00; B01D71/06; B01D71/50
Claims Analysis
Total Claims: 13
Claim 1
Independent Claim
64 words
A method to render polycarbonate membranes selective for the separation of organic liquids, said method comprising preshrinking the polycarbonate membranes by contacting said membranes with a solvent having a solubility parameter in the range of 8.9-10 (cal/cm 3 ) 0.5 said contacting being conducted for a time sufficient to result in shrinkage of the membrane but insufficient to result in dissolution of the membrane.
Claim 2
Independent Claim
64 words
A method to render polycarbonate membranes selective for the separation of organic liquids, said method comprising preshrinking the polycarbonate membranes by contacting said membranes with a solvent having a solubility parameter in the range of 8.9-10 (cal/cm 3 ) 0.5 said contacting being conducted for a time sufficient to result in shrinkage of the membrane but insufficient to result in dissolution of the membrane.
Claim 3
Dependent Claim
39 words
The method of claim 1 wherein the solvent is nitrobenzene, acetone, methyl ethyl ketone, benzene, tetrahydrofuran, ethyl acetate, toluene and mixtures thereof, either in the pure form or in combination with solvents having solubility parameters outside the prescribed range.
Claim 4
Dependent Claim
61 words
A polycarbonate membrane which is selective for the separation of ketone from oil prepared by preshrinking the polycarbonate membrane film by contacting said membrane film with a solvent having a solubility parameter in the range 8.9-10 (cal/cm 3 ) 0.5, for a time sufficient to result in shrinkage of the film but not long enough to cause dissolution of the membrane.
Claim 5
Dependent Claim
61 words
A polycarbonate membrane which is selective for the separation of ketone from oil prepared by preshrinking the polycarbonate membrane film by contacting said membrane film with a solvent having a solubility parameter in the range 8.9-10 (cal/cm 3 ) 0.5, for a time sufficient to result in shrinkage of the film but not long enough to cause dissolution of the membrane.
Claim 6
Dependent Claim
40 words
The polycarbonate membrane of claim 3 wherein the solvent is nitrobenzene, acetone, methyl ethyl ketone, benzene, tetrahydrofuran, ethyl acetate, toluene and mixtures thereof, either in the pure form or in combination with solvents having solubility parameters outside the prescribed range.
Claim 7
Independent Claim
85 words
A method for selectively separating organic liquids by the use of polycarbonate membrane prepared by the treatment method comprising contacting said membrane with a solvent having a solubility parameter in the range 8.9-10 (cal/cm 3 ) 0.5, said contacting being conducted for a time sufficient to result in shrinkage of the membrane but insufficient to result in dissolution of the membrane, wherein the organic liquids are separated by selective permeation through said polycarbonate membrane under conditions of temperature and pressure sufficient to effect said separation.
Claim 8
Independent Claim
85 words
A method for selectively separating organic liquids by the use of polycarbonate membrane prepared by the treatment method comprising contacting said membrane with a solvent having a solubility parameter in the range 8.9-10 (cal/cm 3 ) 0.5, said contacting being conducted for a time sufficient to result in shrinkage of the membrane but insufficient to result in dissolution of the membrane, wherein the organic liquids are separated by selective permeation through said polycarbonate membrane under conditions of temperature and pressure sufficient to effect said separation.
Claim 9
Dependent Claim
33 words
The method of claim 5 wherein the solvent is nitrobenzene, acetone, methyl ethyl ketone, benzene, tetrahydrofuran, ethyl acetate, toluene and mixtures thereof either in the pure form or in combination with non-solubilizing solvents.
Claim 10
Dependent Claim
22 words
The method of claim 5 or 6 wherein the organic liquids separated one from the other are dewaxing solvents from dewaxed oil.
Claim 11
Dependent Claim
23 words
The method of claim 7 wherein the dewaxing solvents separated from the dewaxed oil are ketones, and mixtures of ketones and aromatic hydrocarbons.
Claim 12
Dependent Claim
19 words
The method of claim 8 wherein the dewaxing solvents separated from the dewaxed oil are MEK, MIBK, MEK/toluene, MEK/MIBK.
Claim 13
Dependent Claim
17 words
The method of claim 5 or 6 wherein the pressure is sufficient to overcome the osmotic pressure.
References Cited (Backward Citations)
US1350532A
Cited
US3004904A
Cited
US3228876A
Cited
US3133137A
Cited
US3133132A
Cited
US3632404A
Cited
US3699038A
Cited
US3737042A
Cited
GB1395530A
Cited
US3945926A
Cited
US4048271A
Cited
US4032309A
Cited
JPS5235493A
Cited
JPS5290506A
Cited
JPS51158024U
Cited
JPS52142595A
Cited
US4080743A
Cited
US4080744A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1990-12-28 | 1991-06-29 | 1991-12-29 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1994-12-28 | 1995-06-29 | 1995-12-29 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1998-12-28 | 1999-06-29 | 1999-12-29 | $7700.00 | Window Closed / Lapsed |