Multilayer Porous Membrane and Process of Manufacture
a porous membrane, multi-layer technology, applied in the field of porous membranes, to achieve the effect of reducing the collapse of the microporous structur
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example 1
Materials
[0103]Ultra-high molecular weight polyethylene (UHMW-PE) (240SU, Mitsui Chemical)
Mineral oil (MO) (Britol 35 USP, Witco Corp.)
[0104]Dibutyl sebacate (DBS) (A0167-R, BrandNu Lab)
Halogenated hydrocarbon solvent mixture (AccuFlush II, MicroCare Corp.)
Membrane Preparation:
[0105]A double-layer microporous UHMW-PE membrane was prepared by co-extruding two UHMW-PE solution streams (1 and 2) of different formulations simultaneously from two separate twin-screw extrusion lines. The two extrusion lines were connected by an extrusion feed block and flat sheet die such that the two solution layers are combined as one before being extruded and quenched.
Solution Stream 1
[0106]A slurry mixture consisting of 14 wt. % UHMW-PE powder, 21.5 wt. % DBS and 64.5 wt. % MO was prepared at room temperature. This mixture was stirred and metered via a FMI pump (Fluid Metering, model V200) into a twin-screw compounding extruder (Brabender, model D6 / 2) equipped with a pair of counter-rotating screw (L / ...
example 2
[0113]A double layer UHMW-PE membranes were prepared by the co-extrusion method as described in Example 1 except for the following differences:
Solution Stream 1
[0114]Slurry mixture used consists of 17 wt. % UHMW-PE powder, 41.5 wt. % DBS and 41.5 wt. % MO. Gear pump speed used was 8 rpm
Solution Stream 2
[0115]Slurry mixture used consists of 15 wt. % UHMW-PE powder, 72.2 wt. % DBS and 12.8 wt. % MO. Gear pump speed used was 40 rpm.
[0116]The chill roll temperature used for quenching the co-extruded structure was at 50 C. The properties of this membrane are given in Table 2
example 3
[0117]A double layer UHMW-PE membrane was prepared as in Example 2 except the chill roll temperature used for quenching the co-extruded structure was at 31 C. The properties of this membrane are given in the Table below.
TABLEThicknessMean IPA Bubble Point*IPA Flow Rate**Membrane(μ)(psi)(ml / min / cm2)Example 166464.1Comparative60433.1Example 1Example 246642.0Example 344821.2*by air-flow porosimetry method (ASTM method F316-80)**at 21° C. and 14 psi Δp
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