IP Library › Granted Patent US 11,569,523
Granted Patent B2
US 11,569,523 · App. 16/859,712 · Granted Jan 31, 2023

Polymer electrolyte membrane for medium and high temperature, preparation method thereof and high temperature polymer electrolyte membrane fuel cell comprising the same

Inventors: So Young Lee (Seoul, KR); Seung Ju Lee (Seoul, KR); Min Jae Lee (Seoul, KR); Hyun Seo Park (Seoul, KR); Jong Hyun Jang (Seoul, KR); Hyoung-Juhn Kim (Seoul, KR); Suk Woo Nam (Seoul, KR); Young Suk Jo (Seoul, KR); Yeong Cheon Kim (Seoul, KR)
Assignee: Korea Institute of Science and Technology
H01M8/1051H01M8/103H01M8/1011H01M8/1013H01M8/1048H01M8/1072H01M8/1081H01M8/1088H01M8/1009H01M2008/1095H01M2250/20H01M2300/0068H01M2300/0082H01M2300/0091
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Quick Facts
Patent No.
US 11,569,523
App. No.
16/859,712
Granted
Jan 31, 2023
Kind
B2
Abstract

The present disclosure relates to a polymer electrolyte membrane for medium and high temperature, a preparation method thereof and a high-temperature polymer electrolyte membrane fuel cell including the same, more particularly to a technology of preparing a composite membrane including an inorganic phosphate nanofiber incorporated into a phosphoric acid-doped polybenzimidazole (PBI) polymer membrane by adding an inorganic precursor capable of forming a nanofiber in a phosphoric acid solution when preparing phosphoric acid-doped polybenzimidazole and using the same as a high-temperature polymer electrolyte membrane which is thermally stable even at high temperatures of 200-300° C. without degradation of phosphoric acid and has high ion conductivity.

Claims (31)

1. A high-temperature polymer electrolyte membrane which is thermally stable at high temperatures of 200-300° C. without degradation of phosphoric acid, comprising a composite membrane comprising:

a phosphoric acid-doped polybenzimidazole (PBI) polymer membrane; and

a cerium phosphate nanofiber incorporated into the polymer membrane.

2. A membrane electrode assembly for a fuel cell, comprising the high-temperature polymer electrolyte membrane according to claim 1 .

3. A fuel cell system comprising the membrane electrode assembly according to claim 2 .

4. The fuel cell system according to claim 3 , wherein the fuel cell is a direct liquid organic hydrogen carrier (LOHC) fuel cell.

5. The fuel cell system according to claim 4 , wherein the liquid organic hydrogen carrier is one or more selected from: a C 1 -C 3 organic compound comprising methanol (CH 3 OH), dimethyl ether (C 2 H 6 O) and 2-propanol (C 3 H 8 O); a C 4 or higher organic compound comprising N-ethylcarbazole (NEC), biphenyl, diphenylmethane, methylcyclohexane (MCH) and dibenzyltoluene (DBT); and an inorganic compound comprising ammonia (NH 3 ), nitrohydrazine (N 2 H 4 ), hydrazine borane (N 2 H 4 BH 3 ) and ammonia borane (NH 3 BH 3 ).

6. An electrical device comprising the fuel cell system according to claim 4 , wherein the electrical device is one or more selected from an electric vehicle, a hybrid electric vehicle, a plug-in hybrid electric vehicle, an electric boat, electric train, an aircraft, an unmanned aircraft, an electric power motor, a stationary power generator, a mobile power generator and a power storage device.

7. A method for preparing the composite membrane according to claim 1 , comprising:

(a) mixing a phosphoric acid-doped PBI polymer solution and a precursor solution of a cerium precursor dissolved in phosphoric acid; and

(b) forming the resulting mixture into a membrane.

8. The method for preparing a composite membrane according to claim 7 , wherein the phosphoric acid-doped PBI polymer solution is synthesized by reacting 3,3′-diaminobenzidine, terephthalic acid and polyphosphoric acid at 100-400° C. under inert gas atmosphere and adding phosphoric acid when the reaction solution becomes viscous.

9. The method for preparing a composite membrane according to claim 7 , wherein

the precursor solution is a cerium precursor solution dissolved in phosphoric acid, and,

in the cerium precursor solution dissolved in phosphoric acid, the phosphoric acid and the cerium precursor are mixed weight ratio of 1:0.01-0.09.

10. The method for preparing a composite membrane according to claim 7 , wherein 1-99 wt % of the inorganic precursor is mixed based on the phosphoric acid-doped PBI polymer.

11. The method for preparing a composite membrane according to claim 7 , wherein, the mixing in (a) is performed at 150-300° C.

12. The method for preparing a composite membrane according to claim 7 , wherein, in (b), a composite membrane is formed by casting the mixture of (a) onto a substrate and then hydrolyzing the cast membrane under humidified condition.

13. The method for preparing a composite membrane according to claim 12 , wherein the hydrolysis in (b) is performed at 30-100° C. under relative humidity of 50-100% RH for 10-48 hours.

14. The method for preparing a composite membrane according to claim 7 , wherein

the PBI polymer solution is synthesized by reacting 3,3′-diaminobenzidine, terephthalic acid and polyphosphoric acid at 100-400° C. under inert gas atmosphere and adding phosphoric acid when the reaction solution becomes viscous,

the 3,3′-diaminobenzidine, the terephthalic acid, the polyphosphoric acid and the phosphoric acid are mixed at a weight ratio of 1:0.4-1:35-50:10-20,

the inert gas is argon gas,

the reaction is conducted by (i) stirring for 10-30 hours at a first heat-treating temperature of 100-190° C. and (ii) stirring for 20-100 minutes at a second heat-treating temperature of 195-300° C.,

the precursor solution is a cerium precursor solution dissolved in phosphoric acid,

in the cerium precursor solution dissolved in phosphoric acid, the phosphoric acid and the cerium precursor are mixed at a weight ratio of 1:0.01-0.09,

the cerium precursor is cerium sulfate tetrahydrate,

the cerium precursor is mixed in an amount of 10-90 wt % based on the PBI,

(a) is performed by mixing at 150-300° C.,

in (b), a composite membrane is formed by casting the mixture of (a) onto a substrate and then hydrolyzing the cast membrane under humidified condition, and

the hydrolysis in (b) is performed at 30-100° C. under relative humidity of 50-100% RH for 10-48 hours.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Apr 27, 2020
From: LEE, SO YOUNG; LEE, SEUNG JU; LEE, MIN JAE; PARK, HYUN SEO; JANG, JONG HYUN; KIM, HYOUNG-JUHN; NAM, SUK WOO; JO, YOUNG SUK; KIM, YEONG CHEON
To: KOREA INSTITUTE OF SCIENCE AND TECHNOLOGY
Reel/Frame 052505/0492 →
Priority Claims (2)
KR 10-2019-0128609 · Oct 16, 2019 · national
KR 10-2019-0173763 · Dec 24, 2019 · national
Continuity (1)
Related Publication 20210119237A1 · Apr 22, 2021