Unsintered expanded polytetrafluoroethylene composite membranes having dimensional stability

Patent metadata

Field	Value
Publication number	US-12201948-B2
Application number	US-201817277763-A
Country	US
Kind code	B2
Filing date	Oct 4, 2018
Priority date	Oct 4, 2018
Publication date	Jan 21, 2025
Grant date	Jan 21, 2025

Abstract

A method of forming an unsintered biaxially expanded PTFE/thermoplastic polymer composite membrane is provided. The method includes blending fibrillatable polytetrafluoroethylene (PTFE) particles and thermoplastic polymer particles where the melting point of the thermoplastic polymer particles is less than the melting point of the fibrillatable PTFE particles. The method further includes forming the blend into a tape and expanding and heating the tape in a first direction at a first temperature. The expanded tape is then expanded, either concurrently or sequentially in a second direction to form an ePTFE composite membrane. The method does not include a sintering temperature. The ePTFE particles and thermoplastic polymer particles have an average particle size of less than 1 μm. In addition, the ePTFE composite membrane has a geometric mean matrix modulus to geometric mean matrix tensile strength ratio of at least about 6 and an absolute dimensional change percentage of less than about 1.5%.

First claim

What is claimed is:

1. A method of forming an expanded composite ePTFE membrane comprising:
providing a blend including
40 wt % to 79.9 wt % of a plurality of fibrillatable polytetrafluoroethylene (PTFE) particles having a first melting point and
20.1 wt % to 60 wt % of a plurality of thermoplastic polymer particles having a second melting point that is less than the first melting point;

forming the blend into a tape;
expanding the tape in a first direction below the second melting point to form an expanded tape; and
expanding the expanded tape in a second direction above the second melting point but below the first melting point to form an ePTFE composite membrane,
wherein the expanding occurs at temperatures below the first melting point such that the ePTFE composite membrane is not sintered
wherein the membrane has a geometric mean matrix modulus to geometric mean matrix tensile strength ratio of at least about 6,

wherein the geometric mean matrix modulus to geometric mean matrix tensile strength ratio is determined by
Ratio of geometric mean matrix modulus to geometric mean matrix tensile strength=geometric mean matrix modulus/geometric mean matrix tensile strength,

wherein
the geometric mean matrix modulus is calculated as
√(longitudinal matrix modulus*transverse matrix modulus),
wherein each, the longitudinal matrix modulus and the transverse matrix modulus at a 3% strain, are calculated as
matrix modulus=(matrix tensile stress at 3% strain)/(0.03), wherein
matrix tensile stress at 3% strain=(load at 3% strain/cross-sectional area)*(density of resin/density of the membrane),
and wherein the density of resin is 2.177 g/mL as determined by Helium pycnometry, and density of the membrane is calculated according to:
ρ= m/w*l*t

wherein ρ=density (g/cc),
m=mass (g)
w=width (9.05 cm),
l=length (5.08 cm),
and t=thickness (cm).

2. The method of claim 1 , wherein the expansion steps are performed sequentially.

3. The method of claim 1 , wherein the expansion steps are performed simultaneously.

4. The method of claim 1 , wherein the thermoplastic polymer is a thermoplastic fluoropolymer.

5. The method of claim 4 , wherein the thermoplastic fluoropolymer is selected from poly(ethene-co-tetrafluoroethene) (ETFE), polyvinylidene difluoride (PVDF), polychlorotrifluoroethylene (PCTFE), fluorinated ethylene propylene (FEP), and combinations thereof.

6. The method of claim 1 , wherein the fibrillatable PTFE particles and the thermoplastic polymer particles each have an average particle size of less than 1 μm.

7. A method of forming a biaxially expanded composite ePTFE membrane comprising:
providing a blend including:
a first plurality of particles, the first plurality of particles comprising fibrillatable polytetrafluoroethylene (PTFE) particles having an average particle size of less than 1 μm;
a second plurality of particles, the second plurality of particles comprising thermoplastic polymer particles having an average particle size of less than 1 μm, wherein the melting point of the thermoplastic polymer particles is less than the melting point of the fibrillatable PTFE particles,
wherein the blend includes from 40 wt % to 79.9 wt % fibrillatable PTFE particles and from 20.1 wt % to 60 wt % thermoplastic polymer particles;

paste extruding the blend in a lubricant to form a calendared tape;
drying the calendared tape to remove the lubricant to produce a dried calendared tape;
expanding the dried calendared tape in a first direction at a temperature below the melting point of the thermoplastic polymer to form a uniaxially expanded ePTFE composite membrane;
heating the uniaxially expanded porous membrane to a temperature greater than the melting point of the thermoplastic polymer and less than the melting point of the fibrillatable PTFE; and,
expanding the uniaxially expanded porous membrane in a second direction, wherein the second direction is different from the first direction, to form a biaxially expanded ePTFE composite membrane,
wherein the biaxially expanded ePTFE composite membrane is not sintered, and wherein the membrane has a geometric mean matrix modulus to geometric mean matrix tensile strength ratio of at least about 6,

wherein the geometric mean matrix modulus to geometric mean matrix tensile strength ratio is determined by
Ratio of geometric mean matrix modulus to geometric mean matrix tensile strength=geometric mean matrix modulus/geometric mean matrix tensile strength,

wherein
the geometric mean matrix modulus is calculated as
√(longitudinal matrix modulus*transverse matrix modulus),
wherein each, the longitudinal matrix modulus and the transverse matrix modulus at a 3% strain, are calculated as
matrix modulus=(matrix tensile stress at 3% strain)/(0.03), wherein
matrix tensile stress at 3% strain=(load at 3% strain/cross-sectional area)*(density of resin/density of the membrane),
and wherein the density of resin is 2.177 g/mL as determined by Helium pycnometry, and density of the membrane is calculated according to:
ρ= m/w*l*t

wherein ρ=density (g/cc),
m=mass (g),
w=width (9.05 cm),
l=length (5.08 cm),
and t=thickness (cm).

8. The method of claim 7 , wherein the expansion steps are performed sequentially.

9. The method of claim 7 , wherein the expansion steps are performed simultaneously.

10. An unsintered biaxially ePTFE composite membrane comprising:
from 40 wt % to 79.9 wt % fibrillatable polytetrafluoroethylene (PTFE) particles;
from 20.1 wt % to 60 wt % thermoplastic polymer particles;
a plurality of nodes interconnected by fibrils,
wherein the fibrils include ePTFE and the nodes include a higher thermoplastic polymer content than the total thermoplastic polymer content of the ePTFE composite membrane; and

a geometric mean matrix modulus to geometric mean matrix tensile strength ratio of at least about 6,

wherein the geometric mean matrix modulus to geometric mean matrix tensile strength ratio is determined by
Ratio of geometric mean matrix modulus to geometric mean matrix tensile strength=geometric mean matrix modulus/geometric mean matrix tensile strength,

wherein
the geometric mean matrix modulus is calculated as
√(longitudinal matrix modulus*transverse matrix modulus),
wherein each, the longitudinal matrix modulus and the transverse matrix modulus at a 3% strain, are calculated as
matrix modulus=(matrix tensile stress at 3% strain)/(0.03), wherein
matrix tensile stress at 3% strain=(load at 3% strain/cross-sectional area)*(density of resin/density of the membrane),
and wherein the density of resin is 2.177 g/mL as determined by Helium pycnometry, and density of the membrane is calculated according to:
ρ= m/w*l*t

wherein ρ=density (g/cc),
m=mass (g),
w=width (9.05 cm),
l=length (5.08 cm),
and t=thickness (cm).

11. The membrane of claim 10 , wherein the fibrils comprise at least about 85% of the ePTFE.

12. The membrane of claim 10 , wherein the nodes comprise at least about 51 wt % of the thermoplastic polymer.

13. The membrane of claim 10 , wherein the ePTFE composite membrane has a dimensional change of less than 1.5% as measured by dynamic mechanical analysis (DMA) upon heating from 25° C. to 200° C. at a rate of 5° C./min and upon holding at 200° C. for 5 minutes.

14. The membrane of claim 10 , wherein the thermoplastic polymer is selected from the group consisting of: poly(ethylene-co-tetrafluoroethene) (ETFE), polyvinylidene difluoride (PVDF), polychlorotrifluoroethylene (PCTFE), fluorinated ethylene propylene (FEP) perfluoroalkoxy (PFA) and co

Assignees

• Gore & Ass

Inventors

• Ebata Yuri
• Sayler Todd S

Classifications

• B01D69/06

  Flat membranes · CPC title

• B01D2325/24

  Mechanical properties, e.g. strength · CPC title

• B01D2323/12

  Specific ratios of components used · CPC title

• B01D2323/08

  Specific temperatures applied · CPC title

• B01D71/36

  Polytetrafluoroethylene · CPC title