IP Library Granted Patent US 8,486,579
Granted Patent B2
US 8,486,579 · App. 12/821,961 · Granted Jul 16, 2013

Polymer blend proton exchange membrane and method for manufacturing the same

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Quick Facts
Patent No.
US 8,486,579
App. No.
12/821,961
Granted
Jul 16, 2013
Kind
B2
Abstract

The present invention relates to a polymer blend proton exchange membrane comprising a soluble polymer and a sulfonated polymer, wherein the soluble polymer is at least one polymer selected from the group consisting of polysulfone, polyethersulfone and polyvinylidene fluoride, the sulfonated polymer is at least one polymer selected from the group consisting of sulfonated poly(ether-ether-ketone), sulfonated poly(ether-ketone-ether-ketone-ketone), sulfonated poly(phthalazinone ether ketone), sulfonated phenolphthalein poly (ether sulfone), sulfonated polyimides, sulfonated polyphosphazene and sulfonated polybenzimidazole, and wherein the degree of sulfonation of the sulfonated polymer is in the range of 96% to 118%. The present invention further relates to a method for manufacturing the polymer blend proton exchange membrane.

Claims (15)

1. A method for manufacturing a polymer blend proton exchange membrane comprising the following steps:

a) dissolving a soluble polymer in an organic solvent and obtaining a uniform solution, wherein the soluble polymer is at least one polymer selected from the group consisting of polysulfone, polyethersulfone and polyvinylidene fluoride;

b) dissolving a sulfonated polymer in the solution obtained in step a) and obtaining a polymer blend membrane forming solution,

wherein the sulfonated polymer is at least one polymer selected from the group consisting of sulfonated poly(ether-ether-ketone), sulfonated poly(ether-ketone-ether-ketone-ketone), sulfonated poly(phthalazinone ether ketone), sulfonated phenolphthalein poly (ether sulfone), sulfonated polyimide, sulfonated polyphosphazene and sulfonated polybenzimidazole,

wherein the sulfonated polymer is prepared by directly dissolving an unsulfonated polymer in concentrated sulfuric acid, Nordhausen acid, or chlorosulfonic acid and sulfonating the unsulfonated polymer,

wherein the sulfonated polymer is prepared by two steps: the first step is to carry out reaction for 3 to 5 hours at 20 to 40° C.; the second step is to carry out reaction for 1 to 4 hours at 70 to 100° C., and

wherein the degree of sulfonation of the sulfonated polymer is in the range of 96% to 118%; and

c) forming a polymer blend proton exchange membrane by tape casting the polymer blend membrane forming solution, then removing the polymer blend proton exchange membrane after being dried and heat-treated.

2. The method according to claim 1 , wherein the method further includes a step: d) immersing the polymer blend proton exchange membrane in sulfuric acid aqueous solution for a whole day and taking out the membrane for later use.

3. The method according to claim 1 , wherein the degree of sulfonation of the sulfonated polymer is 98 to 116%, preferably 100 to 114%, more preferably 106 to 110%.

4. The method according to claim 1 , wherein the sulfonated polymer is made from an unsulfonated polymer with melt viscosity of 100 to 550 centipoise, preferably 300 to 450 centipoise, more preferably 350 to 400 centipoise, at 300 to 500° C.

5. The method according to claim 1 , wherein the resulting sulfonated polymer is shaped through a water-cooling process, preferably through a process in which the resulting sulfonated polymer slurry is poured into a screen with 1 to 4 mm mesh size and flows into deionized water beneath the screen and a strip-like sulfonated polymer is obtained after stirring.

6. The method according to claim 5 , wherein the resulting strip-shaped sulfonated polymer is washed to remove remaining sulfuric acid, then is dried at a temperature of 100 to 120° C. for at least 1 hour, preferably at least 4 hours.

7. The method according to claim 1 , wherein the weight-average molecular weight of the soluble polymer is in the range of 35000 to 65000, preferably 45000 to 55000, more preferably 48000 to 52000.

8. The method according to claim 1 , wherein the content of the soluble polymer is 10% to 50%, preferably 13% to 38%, more preferably 18% to 35%, most preferably 22% to 32%, based on the total weight of the membrane.

Assignments (8)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Oct 10, 2024
From: BEIJING PU NENG CENTURY SCI. & TECH. CO., LTD.
To: VRB ENERGY INC.
Reel/Frame 068868/0800 →
CORRECTIVE ASSIGNMENT TO CORRECT THE NATURE OF CONVEYANCE PREVIOUSLY RECORDED AT REEL: 048175 FRAME: 0806. ASSIGNOR(S) HEREBY CONFIRMS THE CHANGE OF NAME. Recorded Jan 31, 2019
From: JD HOLING INC.
To: VRB ENERY INC.
Reel/Frame 048203/0459 →
CORRECTIVE ASSIGNMENT TO CORRECT APPLICATION NUMBERS 12/810,950 AND 13/934,046 PREVIOUSLY RECORD ON REEL 048175 FRAME 0806 HEREBY CONFIRMS CHANGE OF NAME Recorded Jan 7, 2019
From: JD HOLDING INC.
To: VRB ENERGY INC.
Reel/Frame 048175/0806 →
CHANGE OF NAME Recorded Aug 22, 2018
From: JD HOLDING INC.
To: VRB ENERGY INC.
Reel/Frame 046913/0407 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Dec 15, 2017
From: PRUDENT ENERGY, INC.
To: BEIJING PU NENG CENTURY SCI. & TECH. CO. LTD.
Reel/Frame 044408/0046 →
CORRECTIVE ASSIGNMENT TO CORRECT THE ASSIGNEE'S ADDRESS TO READ "ROOM 102, RESEARCH BUILDING B" INSTEAD OF "B-102, RESEARCH BUILDING B" PREVIOUSLY RECORDED ON REEL 030105 FRAME 0370. ASSIGNOR(S) HEREBY CONFIRMS THE CONVEYANCE TO PRUDENT ENERGY INC.. Recorded May 6, 2013
From: BEIJING PRUDENT CENTURY TECHNOLOGY CO., LTD.
To: PRUDENT ENERGY INC.
Reel/Frame 030359/0195 →
CHANGE OF NAME Recorded Mar 28, 2013
From: BEIJING PRUDENT CENTURY TECHNOLOGY CO., LTD.
To: PRUDENT ENERGY INC.
Reel/Frame 030105/0370 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jun 23, 2010
From: HUANG, MIANYAN; ZHAO, YANLING; LI, LINLIN
To: BEIJING PRUDENT CENTURY TECHNOLOGY CO., LTD.
Reel/Frame 024583/0831 →