Spiral membrane module with controlled by-pass seal

Claim 2

In a membrane apparatus, which apparatus comprises: (a) a housing adapted to contain a spiral-membrane module, the housing having an interior wall surface; (b) a spiral-membrane module positioned within the housing, to define a generally annular clearance space between the exterior surface of the spiral membrane and the interior wall of the housing, the spiral-membrane module designed to separate a feed stream into a permeate stream and a concentrate stream; (c) means to introduce a feed stream axially of the spiral-membrane module; (d) means to withdraw a concentrate stream; and (e) means to withdraw a permeate stream, the improvement which comprises: a mesh means peripherally surrounding the spiral membrane in the annular clearance space, the mesh means in a close, partially sealing relationship between the exterior surface of the module and the interior surface of the housing, to provide for a controlled by-pass of the feed stream in the annular clearance space, thereby improving the cleanliness of the clearance space downstream of the open-mesh material, by preventing the accumulation of products in the annular clearance space.

Claim 3

The apparatus of claim 1 wherein the mesh means comprises an open-mesh, strand-type material composed of synthetic strands.

Claim 4

The apparatus of claim 1 wherein the mesh means comprises a helical wrap of the mesh material about the exterior surface of the spiral-membrane module.

Claim 5

The apparatus of claim 1 wherein the mesh means comprises a single wrap of the mesh material about the exterior surface of the membrane module, with the mesh material having abutting edges.

Claim 6

The apparatus of claim 1 wherein the mesh means comprises a thermoplastic material composed of generally uniform, open material of extruded strands.

Claim 7

The apparatus of claim 1 wherein the mesh means is a mesh material positioned peripherally and generally centrally of the spiral-membrane module within the housing and extends substantially the length of the spiral-membrane module.

Claim 8

The apparatus of claim 1 wherein the mesh means is a mesh material having the strands thereon positioned at an angle to the axial flow, and the mesh material is of a predetermined mesh-opening size to control the amount of by-pass through the mesh material.

Claim 9

The apparatus of claim 1 wherein the mesh means is a mesh material having a thickness ranging from about 5 to 100 mils in thickness.

Claim 10

The apparatus of claim 1 wherein the mesh means is selected to provide for a controlled by-pass flow of from about 4 to 12 gallons per minute.

Claim 11

The apparatus of claim 1 wherein the mesh means comprises a tubular, single-layer, thermoplastic, mesh material in a snug, close-fitting relationship about the exterior surface of the spiral-membrane module.

Claim 12

The apparatus of claim 1 wherein the spiral-membrane module is characterized by a generally smooth, resin-coated exterior surface.

Claim 13

The apparatus of claim 1 wherein the spiral-membrane module is characterized by a roughened, exterior resin surface, to provide for controlled by-pass.

Claim 14

The apparatus of claim 1 wherein the spiral-membrane module has a resin exterior surface, and the mesh means comprises a raised, molded, mesh pattern on the exterior surface of the spiral-membrane module.

Claim 15

The apparatus of claim 1 wherein the mesh material is a synthetic material composed of strands defining generally uniform, open spaces, having a thickness of from about 5 to 100 mils, and an open-space area of approximately 50% or more.

Claim 16

The apparatus of claim 1 wherein the mesh material is composed of strands disposed at an angle of from about 45 to 60 degrees to the axial flow of the feed stream through the annular clearance space, with a strand count of the material ranging from about 4×4 to 10×10.

Claim 17

The apparatus of claim 1 wherein the mesh material extends from about 1 to 4 inches from either end of the spiral-membrane module.

Claim 18

In a membrane apparatus, which apparatus comprises: (a) a housing adapted to contain a spiral-membrane module, the housing having an interior wall surface; (b) a spiral-membrane module positioned within the housing, to define a generally annular clearance space between the exterior surface of the spiral-membrane module and the interior wall surface of the housing, the spiral-membrane module designed to separate a feed stream into a permeate stream and a concentrate stream; P1 (c) means to introduce a feed stream axially of the spiral-membrane module; (d) means to withdraw a concentrate stream; and (e) means to withdraw a permeate stream, the improvement which comprises: an open-mesh, strand-type, tubular, sheet material composed of synthetic strands and peripherally surrounding the spiral-membrane module and positioned in the annular clearance space and extending substantially the length of the spiral membrane, the mesh material having a thickness ranging from about 5 to 100 mils in thickness and being in a close, partially sealing relationship between the exterior surface of the spiral-membrane module and the interior wall surface of the housing, to provide for a controlled by-pass of the feed stream in the annular clearance space, thereby improving the cleanliness of the clearance space downstream of the open-mesh material, by preventing the accumulation of products in the annular clearance space.

Claim 19

In a membrane apparatus, which apparatus comprises: (a) a housing adapted to contain a spiral-membrane module, the housing having an interior wall surface; (b) a spiral-membrane module positioned within the housing, to define a generally annular clearance space between the exterior surface of the spiral-membrane module and the interior wall surface of the housing, the spiral-membrane module designed to separate a feed stream into a permeate stream and a concentrate stream; P1 (c) means to introduce a feed stream axially of the spiral-membrane module; (d) means to withdraw a concentrate stream; and (e) means to withdraw a permeate stream, the improvement which comprises: an open-mesh, strand-type, tubular, sheet material composed of synthetic strands and peripherally surrounding the spiral-membrane module and positioned in the annular clearance space and extending substantially the length of the spiral membrane, the mesh material having a thickness ranging from about 5 to 100 mils in thickness and being in a close, partially sealing relationship between the exterior surface of the spiral-membrane module and the interior wall surface of the housing, to provide for a controlled by-pass of the feed stream in the annular clearance space, thereby improving the cleanliness of the clearance space downstream of the open-mesh material, by preventing the accumulation of products in the annular clearance space.

Claim 20

The apparatus of claim 17 wherein the mesh material comprises a thermoplastic material composed of generally uniform, open material of extruded strands, with the strands at an angle of 45 degrees or more to the axial flow in the annular space.

Claim 23

The method of claim 19 wherein the mesh material is selected to provide for a controlled by-pass flow of from about 4 to 12 gallons per minute.

Claim 24

The method of claim 19 wherein the mesh material has the strands thereon positioned at an angle to the axial flow through the annular space, and the mesh material is of a predetermined mesh-opening size to control the amount of by-pass through the mesh material.

Claim 25

The method of claim 19 wherein the mesh material is a tubular material and is positioned peripherally and generally centrally of the spiral-membrane module within the housing and extends substantially the length of the spiral-membrane module.

Claim 26

The method of claim 19 wherein the spiral-membrane module has a resin surface, and the mesh material is formed by molding a mesh pattern peripherally in and about the exterior surface of the spiral-membrane module.

Claim 27

The method of claim 19 which includes heat-softening a tubular, thermoplastic mesh material formed of strands and having a thickness of from 5 to 100 mils, and slipping the softened mesh material about the periphery of the exterior surface of the spiral-membrane module and extending substantially the length of the spiral-membrane module, to provide, on cooling of the mesh material, a snug-fitted, tubular mesh material.