US4514304A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method for purifying and concentrating organic matters
Assignee: Tosoh Corp
•
Filing: 1983-09-30
•
Granted: 1985-04-30
•
Expires: 2003-09-30
Abstract
Abstract A method for purifying and concentrating organic matters by employing an amphoteric ion-exchange membrane which is made of a ternary block copolymer consisting of a macromolecule poly A - having cation-exchange group, a macromolecule poly B + having anion-exchange group and a macromolecule poly C having no ion-exchange group and allows sodium chloride to permeate at a concentration not lower than 100% of that in the starting aqueous solution when a pressure of 50 kg/cm 2 is given to the starting aqueous solution of sodium chloride of 0.01 g/dl and by allowing inorganic salts to permeate selectively from an aqueous solution of the organic compounds containing the inorganic salts with giving an increased pressure thereto.
Inventors
- 👤 Yoshiyuki Miyaki
- 👤 Yoshitaka Fujita
- 👤 Kazunori Se
- 👤 Teruo Fujimoto
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-07 20:59
CPC Classifications
B; B01; B01D; B01D61/00; B01D61/42; B01D61/44; B01D71/00; B01D71/06; B01D71/76; B01D71/80; B01D2325/00; B01D2325/18
Claims Analysis
Total Claims: 13
Claim 1
Independent Claim
135 words
In a method for purifying and concentrating organic matters containing inorganic salts, the improvement comprising (a) employing an amphoteric ion-exchange membrane which is made of a ternary block copolymer consisting of a macromolecule poly A - having cation-exchange group, a macromolecule poly B + having an ion-exchange group and a macromolecule poly C having no ion-exchange group, said amphoteric ion-exchange membrane characterized in that it allows sodium chloride to permeate at a concentration not lower than 100% of that in a starting aqueous solution when a pressure of 50 kg/cm 2 is given to a starting aqueous solution of sodium chloride of 0.01 g/dl concentration, and (b) by allowing inorganic salts to selectively permeate from an aqueous solution of the organic compounds containing the inorganic salts through the membrane by applying an increased pressure thereto.
Claim 2
Dependent Claim
135 words
In a method for purifying and concentrating organic matters containing inorganic salts, the improvement comprising (a) employing an amphoteric ion-exchange membrane which is made of a ternary block copolymer consisting of a macromolecule poly A - having cation-exchange group, a macromolecule poly B + having an ion-exchange group and a macromolecule poly C having no ion-exchange group, said amphoteric ion-exchange membrane characterized in that it allows sodium chloride to permeate at a concentration not lower than 100% of that in a starting aqueous solution when a pressure of 50 kg/cm 2 is given to a starting aqueous solution of sodium chloride of 0.01 g/dl concentration, and (b) by allowing inorganic salts to selectively permeate from an aqueous solution of the organic compounds containing the inorganic salts through the membrane by applying an increased pressure thereto.
Claim 3
Dependent Claim
64 words
The method for purifying and concentrating organic matters recited in claim 1 wherein the amphoteric ion-exchange membrane is made of the ternary block copolymer in which the macromolecule poly A - having cation exchange group and the macromolecule poly B + having anion-exchange group are linked so that they may not be adjacent each other by the macromolecule poly C being included between them.
Claim 4
Dependent Claim
74 words
The method for purifying and concentrating organic matters recited in claim 1, wherein the amphoteric ion exchange membrane is obtained by introducing cation-exchange group and anion-exchange group into an original block copolymer in which components of macromolecule consisting of a macromolecule poly A capable of introducing cation-exchange group, a macromolecule poly B capable of introducing anion-exchange group and a macromolecule poly C incapable of introducing the ion-exchange groups, are linked in a straight chain.
Claim 5
Dependent Claim
57 words
The method for purifying and concentrating organic matters recited in claim 3, wherein the macromolecule poly A capable of introducing cation-exchange group and the macromolecule poly B capable of introducing anion-exchange group are linked, being separated by the macromolecule poly C incapable of introducing the ion exchange groups so that they may not be adjacent each other.
Claim 6
Dependent Claim
32 words
The method for purifying and concentrating organic matters recited in claim 1, wherein the portion of the macromolecule poly C having no ion-exchange group in the amphoteric ion exchange membrane is cross-linked.
Claim 7
Dependent Claim
31 words
The method for purifying and concentrating organic matters recited in claim 1, wherein the portion of the macromolecule poly A - having cation-exchange group in the amphoteric ion-exchange membrane is cross-linked.
Claim 8
Dependent Claim
31 words
The method for purifying and concentrating organic matters recited in claim 1, wherein the portion of the macromolecule poly B + having anion-exchange group in the amphoteric ion-exchange membrane is cross-linked.
Claim 9
Dependent Claim
30 words
The method for purifying and concentrating organic matters recited in claim 1, wherein the amphoteric ion-exchange membrane is employed in a state of being joined on a porous supporting membrane.
Claim 10
Dependent Claim
23 words
The method for purifying and concentrating organic matters recited in claim 1, wherein the amphoteric ion-exchange membrane is 0.1 μm-5 μm in thickness.
Claim 11
Dependent Claim
56 words
The method for purifying and concentrating organic matters recited in claim 1, wherein one face of the amphoteric ion-exchange membrane is in contact with the starting solution under a high pressure and another face thereof is in contact with the permeated solution under a low pressure at the time of selective permeation of the inorganic salt.
Claim 12
Dependent Claim
68 words
The method for purifying and concentrating organic matters recited in claim 1, wherein the pressure applied to the starting liquid is higher than the pressure of π represented by the following equation: ##EQU3## mi: weight molar concentration of i-th species of organic compounds V w ° : molar volume of water R: gas constant T: absolute temperature n: number of kinds of organic compounds in aqueous solution thereof.
Claim 13
Dependent Claim
29 words
The method for purifying and concentrating organic matters recited in claim 1, wherein the organic compound is a non-electrolyte having a molecular weight of more than 10 2 g/mol.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1988-04-29 | 1988-10-29 | 1989-04-30 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1992-04-29 | 1992-10-29 | 1993-04-30 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1996-04-29 | 1996-10-29 | 1997-04-30 | $7700.00 | Window Closed / Lapsed |