Making porous membranes and the membrane products

Claim 2

In a process for making a polymeric membrane that is either a microporous membrane or a skinned, asymmetric, semipermeable membrane, that has at least 60% of its volume taken up by pores, by casting a solution of the polymer in a solvent for the polymer onto the surface of a travelling backing belt in the form of a thin, continuous layer of the polymer solution, then passing the belt and thus carrying the layer into and through a formation bath comprising a liquid that is not a solvent for the polymer but that is miscible with the solvent, to form the layer into a porous membrane, with a consequent migration of the solvent liquid from the layer into the formation bath and an enrichment of the composition of the formation bath in the solvent, and thereafter removing the solvent from the porous membrane, and drying it, the improvement wherein the same liquid material that is used as the solvent component of the casting solution is used as a component of the formation bath, the balance of the formation bath consisting of a liquid that is not a solvent for the polymer, and wherein the process includes the following continuous process steps: withdrawing from the formation bath solvent-enriched formation bath liquid, monitoring the composition of the withdrawn liquid and adding any necessary non-solvent liquid to adjust the composition to within the desired operating range of composition for the formation bath, then returning the composition-adjusted liquid to the bath, the amount of composition adjustment and the rates of withdrawal and return respectively being such as to limit the deviation in composition of the bath between the point of withdrawal and return respectively to not more than about 10%.

Claim 3

In a process for making a polymeric membrane that is either a microporous membrane or a skinned, asymmetric, semipermeable membrane, and that has at least 60% of its volume taken up by pores, by casting a solution of the polymer in a solvent for the polymer onto the surface of a travelling backing belt in the form of a thin, continuous layer of the polymer solution, then passing the belt and thus carrying the layer into a formulation bath comprising a liquid that is not a solvent for the polymer but that is miscible with the solvent, to form the layer into a porous membrane, removing the solvent from the porous membrane, and drying, the improvement wherein the same liquid material that is used as the solvent component of the casting solution is used as a component of the formation bath, the balance of the formation bath consisting essentially of the non-solvent liquid, and wherein the process includes the following steps practised for the continuous production of the membrane: passing the belt and cast layer through an elongate formation bath and through an elongate path therein from the point of entry of the belt and layer into the formation bath to the point of departure therefrom, withdrawing formation bath liquid from the bath adjacent the entry point of the belt into the bath, monitoring the composition of the withdrawn formation bath liquid and adding any necessary non-solvent liquid to maintain the composition within a desired operating range, so that it is recirculable liquid, then returning the recirculable liquid to the formation bath adjacent the departure point of the belt from the bath, thereby establishing a flow of liquid through the formation bath in a direction opposite to the direction of travel of the belt and cast layer.

Claim 4

In a process for making a polymeric membrane that is either a microporous membrane or a skinned, asymmetric, semipermeable membrane, and that has at least 60% of its volume taken up by pores, by casting a solution of the polymer in a solvent for the polymer onto the surface of a travelling backing belt in the form of a thin, continuous layer of the polymer solution, then passing the belt and thus carrying the layer into a formulation bath comprising a liquid that is not a solvent for the polymer but that is miscible with the solvent, to form the layer into a porous membrane, removing the solvent from the porous membrane, and drying, the improvement wherein the same liquid material that is used as the solvent component of the casting solution is used as a component of the formation bath, the balance of the formation bath consisting essentially of the non-solvent liquid, and wherein the process includes the following steps practised for the continuous production of the membrane: passing the belt and cast layer through an elongate formation bath and through an elongate path therein from the point of entry of the belt and layer into the formation bath to the point of departure therefrom, withdrawing formation bath liquid from the bath adjacent the entry point of the belt into the bath, monitoring the composition of the withdrawn formation bath liquid and adding any necessary non-solvent liquid to maintain the composition within a desired operating range, so that it is recirculable liquid, then returning the recirculable liquid to the formation bath adjacent the departure point of the belt from the bath, thereby establishing a flow of liquid through the formation bath in a direction opposite to the direction of travel of the belt and cast layer.

Claim 5

The process of claim 2 wherein the rates of withdrawal of formation bath liquid and return of recirculable liquid respectively are such as to limit any deviation in the composition of the bath between the points of withdrawal and return respectively to not more than about 10%.

Claim 6

The process of claim 1 wherein the rates of withdrawal of formation bath liquid and return of recirculable liquid respectively are such that an equilibrium is established and the deviation from the equilibrium composition is not more than about 2% at most.

Claim 7

The process of claim 1, wherein the solvent for the polymer in the casting solution is a single liquid solvent material.

Claim 8

The process of claim 1 wherein the solvent for the polymer in the casting solution is a mixture of solvent liquids.

Claim 9

The process of claim 2, wherein the drying of the membrane product is conducted with physical restraint of the membrane against shrinkage, so as to prevent distortion of the membrane due to surface tension effects.

Claim 10

The process of claim 2 wherein the speed of entry of the belt carrying the layer of polymer solution into the formation bath is at least 5 cm/sec.

Claim 11

The process of claim 1, for making a microporous membrane having intercommunicating capillary pores having an average size below about 14 micrometers, wherein the formation bath is an elongate, shallow body of liquid of which the solvent liquid for the polymer forms a major amount and is present in sufficient quantity to cause the porous structure to be that of a microporous membrane, and wherein the immersion of the polymer layer is maintained until the microporous structure is essentially fully formed.

Claim 12

A microporous membrane produced by the continuous process of claim 9.

Claim 13

A continuous process for making a skinned, asymmetric, semi-permeable membrane in accordance with claim 2, wherein the liquid that is not a solvent for the polymer is present in a sufficient concentration in the formation bath to cause skin formation upon immersion of the layer of polymer solution in the bath, and including the step of maintaining the layer immersed in the bath until the porous structure of the semi-permeable membrane has been essentially fully formed.

Claim 14

A semi-permeable membrane produced by the continuous process of claim 11.