Porous membrane

1. A membrane comprising:

a sheet of expanded polytetrafluoroethylene, wherein the sheet includes a first extrudate made from a first PTFE fine powder resin mixed with processing lubricant at a first lube rate of between 14 wt-% to 17 wt-% of the processing lubricant to the first PTFE fine powder resin, wherein the sheet further includes a second extrudate made from the first PTFE fine powder resin mixed with the processing lubricant at the first lube rate, wherein each of the first and second extrudates have a predefined thickness that is based on a die configuration of an extruder;

the first extrudate forced into a portion of the second extrudate to form an integrated tape structure that is bi-axially stretched;

the sheet is porous and has a gas permeability of in the range of 0.1 CFM to 0.30 CFM according to ASTM D737; and

the sheet has an average Mullen Hydrostatic Burst pressure in the range of 135 psi to 175 psi according to ASTM D751.

2. The membrane of claim 1 wherein the sheet has a gas permeability of 0.2 CFM according to ASTM D737.

3. The membrane of claim 1 wherein the sheet has an average Mullen Hydrostatic Burst pressure in the range of 150 psi to 175 psi according to ASTM D751.

4. The membrane of claim 1 wherein the pore size is in the range of 0.01 micron to 0.25 micron.

5. The membrane of claim 1 , wherein the predefined thickness is between approximately 0.035 inches and 0.045 inches.

6. A membrane comprising:

a sheet of expanded polytetrafluoroethylene, the sheet including:

a first extrudate made from a first PTFE fine powder resin mixed with processing lubricant at a first lube rate of between 14 wt-% to 22 wt-% of the processing lubricant to the first PTFE fine powder resin, the sheet further includes;

a second extrudate made from the first PTFE fine powder resin mixed with the processing lubricant at the first lube rate, wherein each of the first and second extrudates have a predefined thickness of between approximately 0.035 inches and 0.045 inches;

the first extrudate forced into a portion of the second extrudate to form an integrated tape structure that is bi-axially stretched to have a machine direction stretch ratio of between about 1.0 and 6.0 and a transverse direction width in the range of about eight to twelve times its original transverse width dimension;

the sheet is porous and has a gas permeability in the range of 0.1 CFM to 3.0 CFM according to ASTM D737; and

the sheet has an average Mullen Hydrostatic Burst pressure in the range of 135 psi to 175 psi according to ASTM D751.

7. The membrane of claim 6 wherein the first and second extrudates are combined into the integrated tape structure by a mechanical interlocking of nodes and fibrils making up the first and second extrudates.

8. The membrane of claim 6 wherein the sheet has a gas permeability of 0.2 CFM according to ASTM D737.

9. The membrane of claim 6 wherein the sheet has an average Mullen Hydrostatic Burst pressure in the range of 150 psi to 175 psi according to ASTM D751.

10. The membrane of claim 7 wherein the pore size is in the range of 0.01 micron to 0.25 micron.

11. The membrane of claim 6 , wherein the first lube rate is between 14 wt-% to 17 wt-% of the processing lubricant to the first PTFE fine powder resin.

12. A method of making a membrane comprising the steps of:

providing a first extrudate made from a first PTFE fine powder resin mixed with processing lubricant at a first lube rate of between 14 wt-% to 17 wt-% of the processing lubricant to the first PTFE fine powder resin;

providing a second extrudate made from the first PTFE fine powder resin mixed with processing lubricant at the first lube rate, wherein each of the first and second extrudates have a predefined thickness that is based on a die configuration of an extruder;

overlying the first and second extrudates;

calendering the overlying first and second extrudates so that the first extrudate is forced into a portion of the second extrudate to form an integrated tape;

stretching the integrated tape in the machine direction; and

stretching the integrated tape in the transverse direction to provide a porous sheet that has a gas permeability in a range from 0.1 CFM to 0.30 CFM according to ASTM D737 and an average Mullen Hydrostatic Burst pressure in the range of 135 psi to 175 psi according to ASTM D751.

13. The method of claim 12 wherein the calendering step includes the step of combining the first and second extrudates into the integrated tape structure by a mechanically interlocking nodes and fibrils making up the first and second extrudates.