Multiple bundle permeator

Claim 2

A hollow-fiber membrane separation apparatus which comprises: a pressure container composed of a shell and end plates; a plurality of hollow-fiber bundles, each comprising a cross-section bundle of hollow fibers having one end mounted in a tubesheet, which are longitudinally aligned and placed in the pressure container, said hollow-fibers having selective permeability to fluid, and being further aligned so as to form a first space between the outside of the bundles and the inside of the pressure container; an elongated feed member through which fluid to be treated can flow radially into and through one or more of the hollow-fiber bundles; a second space situate in between adjacent hollow-fiber bundles, said space being defined by the facing ends of adjacent hollow-fiber bundles and being in communication with the first space between the outside of the bundles and the pressure container; a first opening in the pressure container which is in communication with the elongated feed member through which the fluid to be treated is fed; a second opening or openings in the pressure container in communication with the open ends of the hollow fibers through which the permeate is discharged; an elongated discharge member housed inside said elongated feed member, said elongated discharge member being in communication with said second space; and a third opening in the pressure container in communication with the elongated discharge member through which the residue fluid is discharged.

Claim 3

A hollow-fiber membrane separation apparatus of claim 1 in which the pressure container is an elongated cylinder.

Claim 4

A hollow-fiber membrane separation apparatus of claim 2 in which the first space is an annular space.

Claim 5

A hollow-fiber membrane separation apparatus of claim 2 in which the two hollow-fibers are substantially identical in size and configuration.

Claim 6

A hollow-fiber membrane separation apparatus of claim 1 containing two hollow-fiber bundles.

Claim 7

A hollow-fiber membrane separation apparatus of claim 1 in which the hollow-fiber membranes in each hollow-fiber bundle has an inner diameter of about 20 microns to about 200 microns and a hollow ratio of about 10% to about 50%.

Claim 8

A hollow-fiber membrane separation apparatus of claim 1 in which the hollow-fiber membranes have an inner diameter of about 40 microns and a hollow ratio of about 20%.

Claim 9

A hollow-fiber membrane separation apparatus of claim 1 in which the elongated discharge member is concentrically housed within the elongated feed member.

Claim 10

A process for selectively separating fluids comprising a hollow-fiber membrane fluid-separation apparatus in which the hollow-fiber membrane separation apparatus comprises: a pressure container composed of a shell and end plates; a plurality of hollow-fiber bundles, each comprising a cross-section bundle of hollow fibers having one end mounted in a tubesheet, which are longitudinally aligned and placed in the pressure container, said hollow-fibers having selective permeability to fluid, and being further aligned so as to form a first space between the outside of the bundles and the inside of the pressure container; an elongated feed member through which fluid to be treated can flow radially into and through one or more of the hollow-fiber bundles; a second space situate in between adjacent hollow-fiber bundles, said space being defined by the facing ends of adjacent hollow-fiber bundles and being in communication with the first space between the outside of the bundles and the pressure container; a first opening in the pressure container which is in communication with the elongated feed member through which the fluid to be treated is fed; a second opening or openings in the pressure container in communication with the open end of hollow fibers through which the permeate is discharged; an elongated discharge member concentrically housed inside said elongated feed member, said elongated discharge member being in communication with said second space; and a third opening in the pressure container in communication with the elongated discharge member through which the residue fluid is discharged; wherein the feed fluid passes into the fluid separation apparatus through the first opening; the feed fluid is simultaneously distributed radially to two or more hollow-fiber bundles through the elongated feed tube; the feed fluid selectively permeates the hollow-fiber membranes and the permeate flows through the hollow fibers to the tubesheets at the end of each bundle and then being discharged from the pressure container through the second opening; the residue fluid flows radially through the hollow-fiber bundles and is collected in the first space between each hollow-fiber bundle and the pressure container; thereafter, the residue fluid from all hollow-fiber bundles flows into the elongated discharge member and is discharged through the third opening in the pressure container.

Claim 11

A process for selectively separating fluids comprising a hollow-fiber membrane fluid-separation apparatus in which the hollow-fiber membrane separation apparatus comprises: a pressure container composed of a shell and end plates; a plurality of hollow-fiber bundles, each comprising a cross-section bundle of hollow fibers having one end mounted in a tubesheet, which are longitudinally aligned and placed in the pressure container, said hollow-fibers having selective permeability to fluid, and being further aligned so as to form a first space between the outside of the bundles and the inside of the pressure container; an elongated feed member through which fluid to be treated can flow radially into and through one or more of the hollow-fiber bundles; a second space situate in between adjacent hollow-fiber bundles, said space being defined by the facing ends of adjacent hollow-fiber bundles and being in communication with the first space between the outside of the bundles and the pressure container; a first opening in the pressure container which is in communication with the elongated feed member through which the fluid to be treated is fed; a second opening or openings in the pressure container in communication with the open end of hollow fibers through which the permeate is discharged; an elongated discharge member concentrically housed inside said elongated feed member, said elongated discharge member being in communication with said second space; and a third opening in the pressure container in communication with the elongated discharge member through which the residue fluid is discharged; wherein the feed fluid passes into the fluid separation apparatus through the first opening; the feed fluid is simultaneously distributed radially to two or more hollow-fiber bundles through the elongated feed tube; the feed fluid selectively permeates the hollow-fiber membranes and the permeate flows through the hollow fibers to the tubesheets at the end of each bundle and then being discharged from the pressure container through the second opening; the residue fluid flows radially through the hollow-fiber bundles and is collected in the first space between each hollow-fiber bundle and the pressure container; thereafter, the residue fluid from all hollow-fiber bundles flows into the elongated discharge member and is discharged through the third opening in the pressure container.