HOLLOW FIBER MEMBRANE MODULE INCLUDING CONCENTRATE DISTRIBUTOR
20180229187 ยท 2018-08-16
Assignee
Inventors
Cpc classification
B01D63/031
PERFORMING OPERATIONS; TRANSPORTING
International classification
Abstract
A filter module (10) including: a housing (12) extending between an opposing first (14) and second end (16) and defining an inner chamber (18), a plurality of hollow fiber membranes (20) located within the inner chamber, a tubesheet (26) including the ends (24) of the hollow fibers encased but open within a block of potting material, an end cap (30) secured to the end of the housing and including: a permeate fluid outlet (32) in fluid communication with the ends of the hollow fibers, and a concentrate fluid outlet (34) in fluid communication with the inner chamber, wherein the permeate and concentrate fluid outlets are axially aligned, and a concentrate distributor (36) including: an annular ring (38) located adjacent to the second end of the housing, at least one aperture (40) in fluid communication with the inner chamber, and an annular concentrate passageway (42) extending from the aperture and concentrically about the permeate tubesheet to the concentrate fluid outlet of the permeate end cap.
Claims
1. A filter module (10) comprising: i) a tubular-shaped housing (12) extending along an axis (X) between an opposing first (14) and second end (16) and defining an inner chamber (18); ii) a plurality of hollow fiber membranes (20) located within the inner chamber (18) and having first ends (22) located adjacent to the first end (14) of the housing (12) and second ends (24) located adjacent to the second end (16) of the housing (12); iii) a permeate tubesheet (26) comprising the second ends (24) of the hollow fiber membranes (20) encased but open within a block of potting material having a configuration corresponding to the inner periphery of the housing (12) which forms a fluid seal therewith such that fluid passage through the permeate tubesheet (26) is limited to the second ends (24) of the hollow fiber membranes (20); iv) a feed fluid inlet (28) in fluid communication with the inner chamber (18) of the module; v) an end cap (30) secured to the second end (16) of the housing (12) and comprising: a) a permeate fluid outlet (32) in fluid communication with the second ends (24) of the hollow fiber membranes (20), and b) a concentrate fluid outlet (34) in fluid communication with the inner chamber (18), wherein the permeate and concentrate fluid outlets (32, 34) are axially aligned to direct fluid axially from the module (10); and vi) a concentrate distributor (36) comprising: a) an annular ring (38) located adjacent to the second end (16) of the housing (12), b) at least one aperture (40) in fluid communication with the inner chamber (18), and c) an annular concentrate passageway (42) extending from the aperture (40) and concentrically about the permeate tubesheet (26) to the concentrate fluid outlet (34) of the end cap (30).
2. The module of claim 1 wherein the concentrate distributor (36) comprises a plurality of apertures (40, 40) spaced about the periphery of annular ring (38).
3. The module of claim 1 wherein the concentrate distributor (36) further comprises a base assembly (44) secured concentrically about the second end (16) of the housing (12) and including radially extending threads (46) adapted for securing the end cap (30) to the housing (12).
4. The module of claim 1 further including a permeate cap (58) secured to the concentrate distributor (36) and defining a permeate chamber (54) in fluid communication with the permeate fluid outlet (32) and the second ends (24) of the hollow fiber membranes (20).
5. The module of claim 1 further comprising a feed tubesheet (48) comprising the first ends (22) of the hollow fiber membranes (20) encased and sealed within a block of potting material having a configuration corresponding to an inner periphery of the housing (12) and further including at least one feed fluid passageway (50).
Description
BRIEF DESCRIPTION OF THE DRAWINGS
[0018] The invention and various embodiments may be better understood by reference to the detailed description and accompanying figures. The Figures are provided to facilitate description and are not necessarily to scale. Within these sections, like reference numerals refer to like elements.
[0019]
[0020]
DETAILED DESCRIPTION
[0021] In further reference to the Figures, during operation pressurized feed fluid (e.g. untreated water) enters the inner chamber (18) by way of fed fluid inlet (28) and flows along the length of the hollow fiber membranes (20). A portion of the feed fluid passes through the walls of membranes (permeate) and flows along their lumen to a permeate chamber (54) located within the end cap (30) and where it ultimately exits the module (10) by way of the permeate fluid outlet (32). Fluid that is unable to pass through the membranes (concentrate) flows radially outward through the aperture(s) (40, 40) of the concentrate distributor (36) and concentrically about the permeate tubesheet (26) via the annular concentrate passageway (42) to a concentrate chamber (56) located within the end cap (30). The concentrate ultimately exits the module (10) by way of the concentrate fluid outlet (34). Fluid flow patterns are as generally shown by arrows. The concentrate distributor (36) allows the concentrate to bypass around rather than through the permeate tubesheet (26). As a consequence, the tubesheet may include a higher fiber packing density. Additionally, the use of a plurality of spaced apertures (40, 40) evenly distributes concentrate fluid such that stagnate fluid areas are reduced.
[0022] The subject filter module may be used in a wide range of applications including but not limited to microfiltration (MF), ultrafiltration (UF), nanofiltration (NF) and reverse osmosis (RO) and pervaporation. Similarly, a wide variety of feed fluids may be treated with the subject filter module, e.g. produced water from secondary oil recovery, waste water from industrial processes, municipal waste water, water for potable use, recycled water from washing/rinsing procedures, water requiring pre-treatment prior to subsequent treatment (e.g. via RO, ion exchange, carbon filtration, etc.), water from food, beverage and dairy processes, etc.
[0023] In a preferred embodiment the filter module includes a tubular-shaped (e.g. an elongated shell having a length greater than its width), housing extending along an axis between an opposing first and second end and defining an inner chamber. In one preferred embodiment, the outer periphery of the filter module is cylindrically-shaped having a circular cross-section. In an alternative embodiment, the housing may have a polygonal cross-section. The housing may be constructed from a wide variety of materials, e.g. plastics, ceramics, metals, etc., however, in one set of preferred embodiments the housing is made from an injection moldable plastic such as polyvinyl chloride (PVC) or acrylonitrile butadiene styrene (ABS).
[0024] The module includes a plurality (e.g. hundreds) of semi-permeable hollow fiber membranes (fibers) located within the inner chamber. The fibers include a semi-permeable wall surrounding a lumen which extends between an opposing first and second end. The fibers are preferably axially aligned with their first ends located adjacent to a first end of the housing and their second ends located adjacent to the second end of the housing. In an alternative embodiment, both ends of the fibers are located at a common end of the housing with the bulk of the fiber extending between the opposing ends of the housing in a classic U shaped configuration. Representative semi-permeable hollow fiber membranes include those made from: polysulfones, polyether sulfones, polyvinylidene fluoride, polyamides, polyacrylonitrile, polypropylene, etc.
[0025] One or both of the opposing ends of the fibers may be sealed from the inner chamber as part of a tubesheet. The tubesheet may be formed by well-known potting techniques (e.g. using epoxy, polyurethane, silicone, etc.) wherein one or both ends of the hollow fibers remain open and in fluid communication with one or more outer chambers formed within an end cap assembly. See for example U.S. Pat. No. 8,506,808 and the references cited therein. In an alternative embodiment, one end of the fibers forms part of a tubesheet with the opposing fiber ends are individually sealed in a manner that allows individual fibers to be free to move relative to another. In yet another embodiment, both ends of the fibers are sealed within a common tubesheet with the bulk of the fiber extending between the opposing ends of the housing in a classic U shaped configuration.
[0026] The fluid ports are preferably included as part of permeate and feed end caps which are secured to the opposing ends of the module. However, the module may include side or radial ports located between the ends of the module, and which provide direct access to the inner chamber.
[0027] End cap assemblies are preferably concentrically disposed about the end of the housing. In preferred embodiments, the end cap assemblies include a base having inner periphery with a matching or complementary configuration with that of the outer periphery of the end of the housing such that the base can be slid, tightly fitted and preferably sealed about the end of the housing. Depending upon the materials of construction, the base may be secured to the housing via mechanical means, e.g. pressure fit, clamps, matching threads, etc., or may be adhered such as by way of ultrasonic welding, spin welding, adhesive, etc., or combinations of such techniques. The end caps may be constructed from a wide variety of materials, e.g. plastics, ceramics, metals, etc., however, in a preferred set of embodiments the housing is made from an injection moldable plastic such as polyvinyl chloride (PVC) or acrylonitrile butadiene styrene (ABS). The end caps may include additional fluid inlets and outlets of various orientations. In a preferred embodiment, the end cap assembly includes fluid port(s) extending axially outward from the base.
[0028] While described as operating outside-in mode (i.e. feed liquid contacting the outside of the hollow fiber membranes), the module may alternatively be operated in inside-out mode wherein feed fluid is introduced inside the lumen portion of the hollow fibers. While feed fluid is typically introduced into the module under pressure, the module may alternatively be operated by applying negative pressure to the permeate side of the semi-permeable membrane, or a combination of both positive and negative pressure.
[0029] Many embodiments of the invention have been described and in some instances certain embodiments, selections, ranges, constituents, or other features have been characterized as being preferred. The designation of a feature as being preferred should not be interpreted as deeming such features as an essential or critical aspect of the invention. While shown as including an end cap assembly at both ends of the housing, the subject module includes embodiments which include only one end cap assembly.