Concentric tubular membrane device and process useful in ion exchange or absorbent processes

Claim 2

A membrane separation device useful for carrying out an ion exchange or absorbent process comprising: A. a housing comprising a case and two endplates; B. a first microporous tubular membrane defining within it a volume region; C. a second microporous tubular membrane wherein the first tubular membrane is concentrically situated inside the second tubular membrane such that a first annular region between the first and second tubular membranes is formed; D. fine size ion exchange or absorbent particles having a size of between about 10 and 100 microns disposed within the first annular region formed by the first and second concentrically situated tubular membranes; D'. a second annular region defined between the interior wall of the case and the exterior convex surface of the second microporous tubular membrane; E. first opening means in fluid communication with said volume region within the first microporous tubular membrane for either introducing a feed fluid into the volume region or for withdrawing treated fluid from the volume region; E'. second opening means in fluid communication with said second annular region for either introducing a fluid feed into the second annular region or for withdrawing treated fluid from the second annular region; F. a means of sealing the first and second tubular membranes to the inside surface of the housing; and G. at least one porous spacer situated between the first and second concentrically situated tubular membranes.

Claim 3

The membrane separation device of claim 1 which further comprises: H. a means for flushing the annular region formed by the first and second concentrically situated tubular membranes.

Claim 4

The membrane separation device of claim 2 wherein the sealing means is permanent.

Claim 5

The membrane separation device of claim 3 wherein the sealing means comprises an elastomer, a thermoplastic resin, or a thermoset resin.

Claim 6

The membrane separation device of claim 2 wherein the sealing means is removable.

Claim 7

The membrane separation device of claim 5 wherein the sealing means comprises an O-ring or gasket.

Claim 8

The membrane separation device of claim 6 wherein the first and second tubular membranes possess a porosity of between about 20 and about 80 percent.

Claim 9

The membrane separation device of claim 7 wherein the first and second tubular membranes possess a pore size in the range of from about 0.1 to about 50 microns.

Claim 10

The membrane separation device of claim 8 wherein the membranes possess a water flux at about 25° C. and 10 psig of at least about 3,000 GFD.

Claim 11

The membrane separation device of claim 9 wherein the annular region spacing formed by the first and second concentrically situated tubular membranes is between about 2 and about 50 millimeters.

Claim 12

A membrane separation process for treating water containing metals, organics, or mixtures thereof comprising: A. introducing into a concentric tubular membrane device feed water containing metals, organics, or mixtures thereof via first or second opening means, wherein the concentric tubular membrane device comprises: (1) a housing comprising a case and two endplates, (2) a first microporous tubular membrane defining a volume region, (3) a second microporous tubular membrane wherein the first tubular membrane is concentrically situated inside of the second tubular membrane such that a first annular region between the first and second tubular membranes is formed, (4) fine size ion exchange or absorbent particles having a size of between about 10 and 100 microns disposed within the first annular region formed by the first and second concentrically situated tubular membranes, (5) a second annular region defined between the interior wall of the case and the convex exterior of the second microporous tubular membrane; (6) first opening means in fluid communication with said volume region within the first membrane for either introducing a feed fluid into the volume region or for withdrawing treated fluid from the volume region; (7) second opening means in fluid communication with said second annular region for either introducing fluid feed into the second annular region or for withdrawing treated fluid from the second annular region; (8) a means of sealing the first and second tubular membranes to the inside surface of the housing, and (9) at least one porous spacer situated between the first and second concentrically situated tubular membranes; B. permeating the feed water containing metals, organics, or mixtures thereof through the second or first microporous tubular membrane into the first annular region formed between the first and second tubular membranes; C. absorbing the metals, organics, or mixtures thereof into the fine size ion exchange or absorbent particles disposed within the first annular region; D. permeating water depleted in metals, organics, or mixtures thereof through first or second, respectively, microporous tubular membrane; and E. withdrawing water depleted in metals, organics, or mixtures thereof from the concentric tubular membrane device via the respective first or second opening means.

Claim 13

A membrane separation process for treating water containing metals, organics, or mixtures thereof comprising: A. introducing into a concentric tubular membrane device feed water containing metals, organics, or mixtures thereof via first or second opening means, wherein the concentric tubular membrane device comprises: (1) a housing comprising a case and two endplates, (2) a first microporous tubular membrane defining a volume region, (3) a second microporous tubular membrane wherein the first tubular membrane is concentrically situated inside of the second tubular membrane such that a first annular region between the first and second tubular membranes is formed, (4) fine size ion exchange or absorbent particles having a size of between about 10 and 100 microns disposed within the first annular region formed by the first and second concentrically situated tubular membranes, (5) a second annular region defined between the interior wall of the case and the convex exterior of the second microporous tubular membrane; (6) first opening means in fluid communication with said volume region within the first membrane for either introducing a feed fluid into the volume region or for withdrawing treated fluid from the volume region; (7) second opening means in fluid communication with said second annular region for either introducing fluid feed into the second annular region or for withdrawing treated fluid from the second annular region; (8) a means of sealing the first and second tubular membranes to the inside surface of the housing, and (9) at least one porous spacer situated between the first and second concentrically situated tubular membranes; B. permeating the feed water containing metals, organics, or mixtures thereof through the second or first microporous tubular membrane into the first annular region formed between the first and second tubular membranes; C. absorbing the metals, organics, or mixtures thereof into the fine size ion exchange or absorbent particles disposed within the first annular region; D. permeating water depleted in metals, organics, or mixtures thereof through first or second, respectively, microporous tubular membrane; and E. withdrawing water depleted in metals, organics, or mixtures thereof from the concentric tubular membrane device via the respective first or second opening means.

Claim 14

The process of claim 11 in which the concentric tubular membrane device further comprises: (10) a means for flushing the annular region formed by the first and second concentrically situated tubular membranes.

Claim 15

The process of claim 12 wherein the sealing means in the concentric tubular membrane device is permanent.

Claim 16

The process of claim 13 wherein the sealing means comprises an elastomer, a thermoplastic resin, or a thermoset resin.

Claim 17

The process of claim 12 wherein the sealing means in the concentric tubular membrane device is removable.

Claim 18

The membrane separation device of claim 15 wherein the sealing means comprises an O-ring or gasket.

Claim 19

The process of claim 16 wherein the first and second tubular membranes possess a pore size in the range of from about 0.1 to about 50 microns.

Claim 20

The process of claim 17 wherein the membranes possess a water flux through the first and second tubular membranes at about 25° C. and 10 psig of at least about 3,000 GFD.

Claim 21

The process of claim 18 wherein the annual region spacing formed by the first and second concentrically situated tubular membranes is between about 2 and 50 millimeters.

Claim 22

The process of claim 19 wherein the temperature of the feed water is between about 0° and 90° C.

Claim 23

The process of claim 20 wherein the pressure of the feed water is between about 5 and about 100 psig.

Claim 24

The process of claim 21 wherein the fine particle ion exchange or absorbent particles possess a particle size of between about 20 and about 74 microns.

Claim 25

The process of claim 22 wherein the concentric tubular membrane device removes at least about 50 weight percent of the metals and/or organics present in the feed water.