US20180250853A1 - Membrane Potting Methods - Google Patents

Membrane Potting Methods Download PDF

Info

Publication number
US20180250853A1
US20180250853A1 US15/972,852 US201815972852A US2018250853A1 US 20180250853 A1 US20180250853 A1 US 20180250853A1 US 201815972852 A US201815972852 A US 201815972852A US 2018250853 A1 US2018250853 A1 US 2018250853A1
Authority
US
United States
Prior art keywords
potting
sleeve
head
mold
potting sleeve
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Abandoned
Application number
US15/972,852
Inventor
Peter Breffni Ackland
Michael Collignon
Ying Hao Teo
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Evoqua Water Technologies LLC
Original Assignee
Evoqua Water Technologies LLC
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Priority claimed from AU2012904203A external-priority patent/AU2012904203A0/en
Application filed by Evoqua Water Technologies LLC filed Critical Evoqua Water Technologies LLC
Priority to US15/972,852 priority Critical patent/US20180250853A1/en
Publication of US20180250853A1 publication Critical patent/US20180250853A1/en
Abandoned legal-status Critical Current

Links

Images

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C39/00Shaping by casting, i.e. introducing the moulding material into a mould or between confining surfaces without significant moulding pressure; Apparatus therefor
    • B29C39/02Shaping by casting, i.e. introducing the moulding material into a mould or between confining surfaces without significant moulding pressure; Apparatus therefor for making articles of definite length, i.e. discrete articles
    • B29C39/10Shaping by casting, i.e. introducing the moulding material into a mould or between confining surfaces without significant moulding pressure; Apparatus therefor for making articles of definite length, i.e. discrete articles incorporating preformed parts or layers, e.g. casting around inserts or for coating articles
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D63/00Apparatus in general for separation processes using semi-permeable membranes
    • B01D63/02Hollow fibre modules
    • B01D63/021Manufacturing thereof
    • B01D63/022Encapsulating hollow fibres
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2313/00Details relating to membrane modules or apparatus
    • B01D2313/21Specific headers, end caps
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D63/00Apparatus in general for separation processes using semi-permeable membranes
    • B01D63/02Hollow fibre modules

Definitions

  • aspects and embodiments disclosed herein relate generally to methods and apparatus for mounting porous hollow filtration membranes in a membrane filtration system.
  • Synthetic polymeric membranes are well known in the field of ultrafiltration and microfiltration for a variety of implementations, including desalination, gas separation, filtration, and dialysis.
  • the properties of the membranes vary depending on the morphology of the membranes, for example, depending on parameters such as symmetry, pore shape, and pore size, and the chemical nature of the polymeric material used to form the membrane.
  • a large membrane surface area may be provided when a large filtrate flow is desired.
  • a large number of hollow porous membranes may be mounted together and housed in filtration modules.
  • a commonly used technique to reduce the size of the filtration apparatus is to form the hollow porous membranes in the shape of hollow porous fibers.
  • the hollow porous membranes act in parallel to filter a feed liquid, for example, water for purification. By producing a pressure differential across the membrane walls, the liquid is forced to flow through the pores of the walls of each of the hollow porous membranes while contaminants remain trapped on one side of the membranes and filtrate is withdrawn from the other side.
  • the filtrate collects inside the hollow regions, cavities or channels (known as lumens) within the porous hollow membranes and is drawn off through ends of the lumens.
  • an impenetrable barrier may be formed between the feed and the filtrate. It is desirable that the seal formed by the barrier between the feed and filtrate be maintained to avoid contamination of the filtrate with feed. It is thus desirable that such module pots be designed to withstand forces such as hydraulic pressure from fluid flow inside the filtration module which might otherwise compromise the seal between the feed and the filtrate.
  • a module pot may be designed to perform further functions including structurally supporting and mounting the membranes within a module or otherwise within a filtration system.
  • filtrate is withdrawn only from one end of the membranes and the other ends are merely sealed and supported by a potting head.
  • only one potting head is provided with the membranes being looped with both open ends located in the same potting head.
  • the porous membrane ends may be sealingly potted using a curable resin material with the porous membrane ends being positioned within the resin material in its liquid non-cured state.
  • the resin material may be allowed to cure to form a generally solid potting head.
  • the curable resin material may be surrounded by a potting sleeve.
  • the potting sleeve may be used to provide an interface between the potting head formed by the cured resin material and associated equipment such as headers and mounting apparatus.
  • curable potting materials which may be used to secure filtration membranes within a potting head disposed in a potting sleeve may shrink during the curing process. This shrinkage may result in the formation of residual tensile stress within the potting head due to resistance of the potting sleeve to such shrinkage. Residual tensile stress in potting materials has been found to not only decrease fracture strength and toughness but also to reduce the fatigue life of the materials. The residual tensile stress may cause cracking, splitting, and/or breaking of the potting head. This can result in compromising the separation between the feed liquid and the filtrate stream in a filtration system and possible undesirable contamination of filtrate.
  • a potting sleeve for use in forming a potting head having a porous hollow membrane mounted therein.
  • the potting sleeve includes a first fixed portion and a second portion which is movable relative to the first fixed portion to reduce a peripheral extent of the second portion.
  • the second portion of the potting sleeve is inwardly deformable to reduce the peripheral extent thereof.
  • the second portion of the potting sleeve may include structurally weakened regions configured to provide for the second portion of the potting sleeve to be inwardly deformable.
  • the second portion of the potting sleeve may be formed of a flexible material.
  • the potting sleeve includes one or more openings in a wall of the potting sleeve.
  • the openings may be slots.
  • a method of mounting a porous hollow membrane in a potting head of a membrane filtration apparatus comprises providing a mold for receiving potting material and positioning a potting sleeve within the mold.
  • the potting sleeve includes a first fixed portion and a second portion which is movable relative to the first fixed portion to reduce a peripheral extent of the second portion.
  • the method further comprises positioning a portion of the porous hollow membrane to be mounted in a region of the mold encompassed by the potting sleeve, introducing a curable potting material into the region to immerse the portion of the porous hollow membrane in the potting material, at least partially curing the potting material to form the potting head, and removing the potting head and the potting sleeve from the mold.
  • the second portion of the potting sleeve is inwardly deformable to reduce the peripheral extent thereof.
  • the second portion of the potting sleeve may include structurally weakened regions configured to provide for the second portion of the potting sleeve to be inwardly deformable.
  • the second portion of the potting sleeve may be formed of a flexible material.
  • the potting sleeve is provided with one or more openings in a wall of the potting sleeve.
  • the openings may be slots.
  • a method of mounting a porous hollow membrane in a support structure of a membrane filtration apparatus comprises providing a mold for receiving potting material, positioning one or more deformable members within the mold, positioning a portion of the porous hollow membrane to be mounted within the mold, introducing a curable potting material into the mold to immerse the portion of the porous hollow membrane and at least part of the one or more deformable members in the potting material, at least partially curing the potting material to form the potting head, and removing the potting head and the one or more deformable members from the mold.
  • the deformable member comprises a cylindrical plug.
  • the plug may be hollow and collapsible.
  • the plug may be expandable.
  • the deformable member is formed of a flexible material.
  • the deformable member may be formed of a material selected from the group consisting of a soft resin material and rubber.
  • an outer surface of the deformable member is provided with engagement formations.
  • the engagement formations may comprise one or more of a groove, a rib, a shoulder, and a fin.
  • the engagement formations may extend axially from a central body of the deformable member.
  • the engagement formations may extend circumferentially from a central body of the deformable member.
  • a structural element for supporting a potting head having a porous hollow membrane mounted therein and extending from a first surface of the potting head.
  • the structural element comprises a cap configured to engage with a potting sleeve of the potting head, the cap having a bearing surface which supports a second surface of the potting head opposite to the first surface of the potting head when the cap is engaged with the potting sleeve.
  • the cap is generally cylindrical and the bearing surface includes one or more radially extending ribs.
  • the structural element may extend into the second surface of the potting head.
  • a potting sleeve for use in forming a potting head having a porous hollow membrane mounted therein.
  • the potting sleeve includes at least one reinforcement member positioned between inner walls of the potting sleeve, the reinforcement member having opposed sides extending axially of the potting sleeve between a first end portion and an opposed second end portion of the reinforcement member.
  • the reinforcement member is connected to an internal wall of the potting sleeve at connection points on each of the opposed sides of the first end portion and the reinforcement member is free of engagement with the potting sleeve apart from at the connection points.
  • the reinforcement member is plate-like.
  • the reinforcement member may be located along a diameter of the potting sleeve.
  • the first end portion of the reinforcement member is spaced axially from one end of the potting sleeve.
  • the reinforcement member apart from adjacent the connection points is, in use, positioned within the potting head.
  • FIG. 1 is an elevational view of a top potting sleeve for a membrane sub-module
  • FIG. 2 is a plan view of the potting sleeve of FIG. 1 ;
  • FIG. 3A is an elevational section view of the potting sleeve of FIG. 1 taken along section B-B of FIG. 2 ;
  • FIG. 3B is a similar side elevational sectional view as FIG. 3A with the potting sleeve positioned in a potting mold;
  • FIG. 4 is a broken elevational view of a membrane sub-module according to another embodiment
  • FIG. 5 is an underside perspective view of the lower potting sleeve of the sub-module of FIG. 4 ;
  • FIG. 6 is an elevational view of the lower potting sleeve of the sub-module of FIG. 4 ;
  • FIG. 7 is an elevational view of a deformable member according to another embodiment
  • FIG. 8 is a cross-sectional elevational view of the deformable member of FIG. 7 ;
  • FIG. 9 is a top perspective view of a deformable member according to another embodiment.
  • FIG. 10A is a cross-sectional elevational view of a potting mold with the deformable member of FIG. 7 positioned in use in the potting material together with filtration membranes;
  • FIG. 10B is a similar view as FIG. 10A of the deformable member of FIG. 7 positioned in use in a potting head;
  • FIG. 11 is a top perspective view of a potting sleeve with structural extension according to another embodiment
  • FIG. 12 is a top perspective cross sectional view taken along a diameter of the potting sleeve of FIG. 11 ;
  • FIG. 13 is an exploded top perspective view of an upper portion of a membrane sub-module employing the potting sleeve according to the embodiment of FIGS. 11 and 12 ;
  • FIG. 14 is a top perspective cross sectional view taken along a diameter of the membrane sub-module of FIG. 13 in assembled form;
  • FIG. 15 is a cross sectional elevational view of the sub-module of FIG. 14 ;
  • FIG. 16 is an elevational view of an upper potting sleeve according to another embodiment
  • FIG. 17 is a top perspective cross sectional view taken along a diameter of the potting sleeve of FIG. 16 with potting resin in the potting sleeve;
  • FIG. 18 is a top perspective cross sectional view taken along a diameter of the potting sleeve of FIG. 16 without potting resin in the sleeve.
  • aspects and embodiments disclosed herein are directed to filtration modules or sub-modules and to methods of forming same. Aspects and embodiments disclosed herein provide for a reduced amount of residual stress in potting material of the potting heads of the filtration modules or sub-modules after formation of the potting heads as compared to prior known methods and apparatus. This reduction in residual stress may reduce the chances of mechanical failure of the potting head, for example, delamination of membranes from the potting material in which they are retained, delamination of the potting material from a potting sleeve in which it may be disposed, cracking of the potting material, or other forms of mechanical failure. Aspects and embodiments disclosed herein also provide for a membrane module to include a potting head having a potting material layer thickness with a strength greater than prior known potting heads having potting material layers of equivalent thicknesses.
  • a potting sleeve for use in forming a filtration membrane module may be provided with one or more features to at least partially alleviate mechanical stresses which may develop within a potting material during curing of the potting material in the potting sleeve. Many potting materials shrink upon curing, resulting in tensile stresses forming in the potting material if the potting material is constrained to maintain set dimensions during curing.
  • a potting sleeve into which a potting material may be introduced and then cured includes one or more features which provide for one or more dimensions of one or more portions of the potting sleeve to decrease during the curing of the potting material. The decrease in the one or more dimensions of the potting sleeve during curing of the potting material accommodates at least some of the shrinkage of the potting material thus reducing the tendency for tensile stresses to develop in the curing potting material.
  • one or more stress relieving features may be disposed in the curing potting material in a potting sleeve.
  • the one or more features may expand or be displaced during the curing of the potting material, relieving mechanical stresses which might otherwise develop in the curing potting material.
  • FIGS. 1 to 3 there is shown one embodiment of an upper or top potting sleeve for a membrane sub-module 4 .
  • the potting sleeve 5 is generally cylindrical though it will be appreciated that the cross-sectional shape of the potting sleeve is not critical and many suitable cross-sectional shapes may be used depending on the desired geometric shape of the potting head.
  • the potting sleeve 5 may have an elliptical, square, rectangular, or triangular cross-section.
  • the outer surface 6 of the potting sleeve 5 may be provided with a number of engagement formations.
  • the engagement formations may comprise, for example, circumferentially extending grooves, shoulders, or ribs on outer surface 6 of the potting sleeve 5 . It will be appreciated by those in the art that, depending on specific implementations, a variety of different forms and shapes of formation may be used to provide for engagement of the potting sleeve 5 and its associated potting head with other components of the membrane sub-module 4 .
  • a lower portion of the potting sleeve 5 is provided with a circumferential, outwardly extending rib 7 which, in use, is supported on a shoulder provided in the housing of the sub-module (not shown).
  • a circumferential, outwardly extending rib 7 which, in use, is supported on a shoulder provided in the housing of the sub-module (not shown).
  • two axially spaced rows of circumferentially spaced through-openings 8 and 9 are provided in the wall of the potting sleeve 5 .
  • the openings 8 , 9 are shown are circular holes but it will be appreciated the shape and size of the openings is not critical and, in embodiments where openings are desired, any suitable form of opening may be used.
  • the openings 8 , 9 may be in the form of circular holes, oval holes, slits, slots, or other shapes.
  • a pair of circumferential, outwardly extending ribs 10 and 11 form a groove 12 which, in use, accommodates a sealing O-ring (not shown).
  • a further circumferential, outwardly extending rib 13 is provided above and vertically spaced from the ribs 10 and 11 to define a supporting shoulder 13 ′.
  • the skirt portion 14 includes a circumferential groove 15 in its base portion 16 and a reduced diameter inset upper portion 17 with a further circumferential groove 18 positioned between the base portion 15 the upper extent of the inset portion 17 .
  • This groove 18 serves to form an outwardly extending lip 19 at the upper extent of the inset portion 17 .
  • the lip 19 may be used to engage with a lifting mechanism (not shown) to remove the sub-module from the filtration apparatus.
  • the skirt portion 14 forms a portion of the potting sleeve 5 which it movable relative to the fixed lower portion of the sleeve.
  • the skirt portion 14 may be utilized to reduce the peripheral extent of the movable portion of the potting sleeve 5 .
  • the skirt portion 14 may include a plurality of circumferentially spaced, vertically extending slots 20 formed therein to define deformable or flexible finger portions 21 therebetween.
  • the upper potting sleeve 5 is positioned in a potting mold 23 , together with the membranes 24 to be potted, and is filled with potting material 22 from a level just below the upper set of through-openings 9 to above the upper extent of the potting sleeve 5 .
  • the potting material 22 may include any material which may retain filtration membranes 24 within the potting sleeve 5 .
  • the potting material 22 may include, for example, urethane, resin, epoxy, or other suitable materials.
  • the membrane pot may be formed from more than a single layer of potting material, for example, as disclosed in co-pending U.S. patent application Ser. No.
  • the layers may be formed of different materials.
  • a lower layer distal from the side of the potting head from which the membranes 24 emerge may be formed of a material which strongly adheres to the membranes 24 but is relatively rigid, for example, an epoxy material.
  • a softer potting material, for example, a urethane material may form a layer above the rigid layer.
  • the membranes 24 may emerge from the softer potting material.
  • the softer potting material may flex in use providing for the membranes 24 to move slightly at the point they enter the softer potting material, which may decrease the chances for the membranes 24 to shear from the potting head.
  • the inner surface of the potting sleeve 5 may include one or more layers of material which may promote adhesion of the potting material 22 to the potting sleeve, and/or which may elastically deform to facilitate the reduction in mechanical stresses in the cured potting material 22 .
  • the one or more layers of material may include, for example, a layer of a urethane material.
  • the wall of the portion of the potting sleeve 5 defined by the flexible finger portions 21 may deform radially inward to reduce the peripheral extent of skirt portion 14 of the potting sleeve 5 and reduce or eliminate mechanical stresses which might otherwise form within the cured potting material.
  • slots 20 may be utilized in some embodiments to weaken the skirt portion 14 and provide a movable portion of the potting sleeve 5 to reduce the peripheral extent thereof by inward deformation of the sleeve wall, a variety of other configurations may be used to achieve a similar result in providing for deformability of the potting sleeve.
  • the slots 20 may be replaced by or augmented with thin flexible regions which enable the finger portions 21 to flex inwardly.
  • the potting sleeve 5 or a portion of the potting sleeve may be formed from a deformable or flexible material.
  • the flexible material may be any material which may adhere to potting material 22 which may be used to retain filtration membranes within the potting sleeve 5 and which has sufficient flexibility to contract along with the potting material 22 upon curing.
  • the flexible material may include, for example, urethane or rubber.
  • the flexible material may be urethane including a flexibilizing agent.
  • the wall of the potting sleeve or a portion thereof may be formed of a number of radial segments which move circumferentially relative to one another to produce an inwardly collapsible configuration.
  • the slots 20 are shown as extending generally vertically, it will be appreciated that they may extend at an angle to vertical, if desired.
  • the slots may extend horizontally, breaking the skirt 14 into a plurality of horizontal finger-like segments or may form a spiral in the skirt 14 .
  • the lower potting sleeve 30 is generally similar in configuration to the upper potting sleeve 5 described above and may include any one or more of the features of the upper potting sleeve 5 .
  • FIG. 4 shows a broken perspective view of a membrane sub-module 4 with an upper potting sleeve 5 and a lower potting sleeve 30 .
  • the lower potting sleeve 30 has a smooth-walled fixed upper portion 31 divided from a fixed middle portion 32 by a circumferential outwardly extending or protruding locating shoulder 33 .
  • the middle portion 32 of the lower potting sleeve wall 34 is provided with a series of vertically spaced rows of through-openings 35 .
  • the through-openings 35 in each row are circumferentially spaced from one another and formed in circumferentially spaced groups 36 consisting of a number of rows of through-openings 35 .
  • the through-openings 35 are illustrated as are rounded slots, however, it will be appreciated the form, shape, size, and number of the through-openings 35 is not critical and any suitable form or number of through-openings 35 may be employed. In use, these openings 35 provide for fluid communication with the membranes mounted in the potting head.
  • the lower extent of the middle portion 32 of the sleeve 30 is defined by a further circumferential, outwardly extending locating shoulder 37 . Adjacent and above the locating shoulder 37 , a further row of circumferentially spaced slot openings 38 are provided in the sleeve wall. It will be appreciated the form, shape, size, and number of the openings 38 is not critical and any suitable form or number of openings 38 may be employed.
  • a lower skirt 39 extends downwardly below the shoulder 37 and has a circumferential groove 40 formed therein.
  • the lower skirt 39 is movable relative to the fixed upper portion 31 and the fixed middle portion 32 of the lower porting sleeve 30 .
  • the lower skirt 39 includes a plurality of circumferentially spaced, vertically extending slots 41 formed therein to define deformable or flexible finger portions 42 therebetween. The lower skirt 39 thus forms a movable portion of the potting sleeve to reduce the peripheral extent thereof by deformation of the flexible finger portions 42 .
  • the wall 34 of the lower potting sleeve 30 defined by the flexible finger portions 42 can move radially inward to reduce the peripheral extent of skirt 39 of the potting sleeve 30 to reduce or eliminated stresses which might otherwise be formed within the cured potting head.
  • the embodiments described above include openings in the potting sleeves and a variety of engagement formations formed in the outer surfaces of the potting sleeves, it will be appreciated these features are not critical and embodiments comprising a simple plain potting sleeve without openings or particular engagement formations could be employed provided the potting sleeve includes a movable portion which enables the peripheral extent of the potting sleeve to be reduced when the potting material shrinks during curing, thus reducing the potential for mechanical stresses to develop within the potting material.
  • FIGS. 7 to 10B another embodiment of a potting head 52 is illustrated.
  • a deformable member 50 is positioned in the potting material 51 during the potting process so as to relieve stresses produced during the curing of the potting material 51 .
  • deformable member 50 may be used to achieve the desired function. Embodiments disclosed herein are not limited to the type of deformable member 50 illustrated in FIGS. 7 to 10B . Further, although a single deformable member 50 is shown in FIGS. 10A and 10B , it will be appreciated that a number of deformable members 50 may be positioned as desired throughout the potting head 52 .
  • the deformable member 50 comprises a generally cylindrical, hollow, elongate plug 55 .
  • One end of the plug 55 is formed with a conical head 56 while the other end is formed with an enlarged diameter base portion 57 .
  • the outer wall of the elongate plug 55 is provided with outwardly extending engagement formations for providing engagement with the potting material of the potting head.
  • the engagement formations may comprise longitudinally extending fins 58 spaced at 90° intervals around the circumference of the plug 55 .
  • fins 58 need not extend along the lateral extent of the deformable member 50 as illustrated, but may alternatively or additionally be in the form of rings or tabs extending from a central body of the deformable member with surfaces arranged normal to the lateral extent of the central body of the deformable member 50 or at other angles as desired. It will be appreciated that any suitable form of engagement formation may be used, for example, grooves, ribs, shoulders, dimples, or formations of other shapes.
  • FIG. 9 illustrates another form of the engagement formations.
  • the outer wall or surface of the plug is provided with a series of axially spaced circumferential grooves 59 .
  • the deformable member 55 may assume even additional shapes.
  • the central body of the deformable member need not by cylindrical as illustrated, but may rather be formed with a square, rectangular, oval, or polygonal cross section, or any other cross section as desired.
  • the cross-sectional area of the central body of the deformable member 55 may vary along its lateral extent, for example, expanding or decreasing from a base to a tip of the deformable member 55 .
  • the plug 55 may be hollow and may be made of thin molded plastic material.
  • the thin plastic material may deform due the heat released by the exothermic reaction which occurs during curing of the potting material 52 .
  • the deformable plug may be formed of pre-molded rubber which can readily adhere to the potting material.
  • the deformable plug 55 can be molded from a soft resin material, for example, urethane a short time (for example, about 30 minutes) before pre-potting of the membranes.
  • the soft urethane plug can then be located in the potting material to ensure chemical bonding between the plug and the potting material of the potting head.
  • the soft resin material provides a readily deformable plug.
  • the deformable plug 55 may be molded in a mold coated with polytetrafluoroethylene or another non-stick material to ensure the outer surface of the plug is free of mold release agent which could hinder the chemical bond between the plug 55 and the potting material of the potting head.
  • FIGS. 10A and 10B show one embodiment of the deformable plug 55 located within a potting head 52 .
  • the plug 55 is attached by means of the enlarged base portion 57 to a pre-potting dish 59 ′.
  • the plug 55 is then located within the potting mold 23 together with the membranes 24 to be potted, the potting sleeve 5 and potting material 51 introduced into the potting mold 23 .
  • the conical head 56 of the plug 55 assists deflection of the membranes 24 away from the plug 55 during the insertion of the membranes into the potting mold 23 .
  • the mold 23 may be centrifuged to facilitate correct distribution of the potting material 51 around the membranes 24 .
  • the base 57 of the plug may be sliced off leaving the plug 55 flush with the top of the potting head 52 .
  • the soft core or cores created within the potting head 52 by the deformable plug 55 will stretch or otherwise deform allowing the potting material 51 to shrink as it cures, avoiding much of the residual stress which might otherwise be produced by the shrinkage.
  • the reduction in residual stresses within the potting head 52 may lead to a reduction in stress at the membrane-potting material interface.
  • FIGS. 11 to 14 show a further embodiment of a potting head arrangement including a mechanism for mechanically reinforcing the potting head.
  • the thickness of the potting head is increased to resist fluctuating pressures within the membrane sub-module during use.
  • the increased thickness of the potting head results in excessive usage of potting material and the consequent increase in weight of the sub-module.
  • the increased thickness of the potting head may result in an undesirable lumen pressure drop in the length of the membrane as the length of the membrane operating at maximum flow may be substantially increased. Accordingly, where possible, it is desirable to minimize the thickness of the potting head while maintaining its mechanical strength.
  • deflection of the potting head and/or potting material during use when exposed to high pressures in a filtration system may be undesirably large. It has been found desirable to provide reinforcement of the potting material without producing excessive stress between the potting material and the potting sleeve during curing. Further, by providing a supporting structural element, the mechanical integrity of the potting head can be maintained while providing a potting material layer which is more resistant to deformation than a potting material layer of an equivalent thickness which is not reinforced with a supporting structural element.
  • FIGS. 11 and 12 show perspective views of an extension fitting 60 for a potting sleeve 61 .
  • the extension fitting 60 includes structural element 62 for supporting a potting head 63 having one or more porous hollow membranes (not shown) mounted therein and extending from a first surface thereof.
  • the structural element 62 comprises a cap 64 configured to engage with a potting sleeve 61 of the potting head 63 .
  • the cap 64 has a bearing surface 65 which supports a second surface 66 of the potting head 63 opposite the first surface of the potting head 63 which forms an interface with the porous hollow membranes disposed in the potting head 63 when the cap 64 is engaged with the potting sleeve 61 .
  • the bearing surface 65 may comprise the lower surfaces of a series of radially extending ribs 67 which are equally spaced around the circumference of an inner wall of the generally cylindrical cap 64 .
  • the ribs 67 extend diametrically of the cylindrical cap 64 .
  • the cylindrical cap 64 has a downwardly extending skirt portion 68 below the lower surface 65 of each rib 67 and engages with a reduced diameter stepped portion 69 of the potting sleeve 61 .
  • ribs 67 may additionally or alternatively be included in the cap 64 .
  • the ribs 67 may include one or more rings which may be disposed concentrically within the cap, and/or may include ribs which are non-equally spaced around the circumference of the inner wall of the cap 64 .
  • FIGS. 13 and 14 show the use of the extension fitting in a membrane module 70 .
  • the potting sleeve 61 and cap 64 slide into a generally cylindrical module housing 71 , although it will be appreciated that the module housing 71 , potting sleeve 61 , and cap 64 may in other embodiments have alternative cross sections, for example, square or rectangular cross sections.
  • the module cap 64 is removably engaged with the top of the module housing 71 and applies an axial support force to the surface 66 of the potting head 63 to prevent deflection thereof under fluctuating pressure from within the sub-module during use.
  • bearing surface comprising the lower surfaces of the series of radially extending ribs 67 is shown in FIGS. 11 to 14 a variety of forms of bearing surface could alternatively or additionally be used.
  • a cylinder having a generally flat bearing surface corresponding to the upper surface of the potting head could also or alternatively be used.
  • FIGS. 16 to 18 show another embodiment of a potting sleeve.
  • the overall configuration of the potting sleeve is similar in configuration to the sleeve shown in FIGS. 5 and 6 . Designations are the same for the same features in each embodiment.
  • the potting sleeve 30 includes at least one reinforcement member 80 positioned between inner walls of the potting sleeve 30 .
  • the reinforcement member 80 has opposed sides 82 and 83 extending axially of the potting sleeve 30 between a first end portion 84 and an opposed second end portion 85 of the reinforcement member 80 .
  • the reinforcement member is connected to an internal wall of the potting sleeve 30 at connection points 86 , 87 on each of the respective opposed sides 82 and 83 of the first end portion 84 .
  • the reinforcement member 80 is free of engagement with the potting sleeve 30 apart from at the connection points 86 , 87 .
  • the reinforcement member 80 is generally plate-like and the connection points 86 and 87 are outwardly extending portions at the lower ends of each opposed side 82 and 83 of the reinforcement member 80 .
  • the upper non-fixed portion of the reinforcement member 80 is embedded in the potting head material 88 .
  • the non-fixing of this portion enables the reinforcement member 80 to move during curing and shrinking of the potting material 88 and thus undue stresses between the potting head material 88 and the inner surface of the potting sleeve 30 are reduced or avoided.
  • a similar form of potting sleeve could be employed for the upper potting sleeve of the membrane sub-module.
  • the form, shape and dimensions of the reinforcement member 80 are not critical.
  • the reinforcement member 80 may in alternate embodiments include more than one plate-like member which may be parallel or which may intersect the plate-like member illustrated.
  • the reinforcement member 80 may be in a shape other than the generally rectangular shape illustrated, for example a semi-circular shape.
  • one or more apertures may be defined in the reinforcement member 80 .
  • the reinforcement members may interengage or intersect one another provided they have a portion or portions free to move relative to the potting material 88 .

Abstract

Apparatus and methods are disclosed which reduce stress formation in potting heads for porous hollow filtration membranes. In one example, there is disclosed a potting sleeve for forming a potting head which includes a first fixed portion and a second portion which is movable relative to the first fixed portion to reduce a peripheral extent thereof. In another example, a method of mounting a porous hollow membrane in a membrane filtration apparatus includes positioning a portion of porous hollow membranes within a mold and introducing a curable potting material into the mold so as to immerse the portion of the porous hollow membranes and at least part of one or more deformable members in the potting material. The method further includes at least partially curing the potting material to form a potting head and removing the potting head and the one or more deformable members from the mold.

Description

    CROSS-REFERENCE TO RELATED APPLICATIONS
  • This application is a division of and claims benefit under 35 U.S.C. § 120 to co-pending U.S. patent application Ser. No. 14/033,968, titled MEMBRANE POTTING METHODS, filed on Sep. 23, 2013, which claims foreign priority benefits under 35 U.S.C. § 119(a)-(d) or 35 U.S.C. § 365(b) from Australian application no. 2012904203, filed Sep. 26, 2012, each of which is incorporated herein by reference in its entirety for all purposes.
  • BACKGROUND 1. Technical Field
  • Aspects and embodiments disclosed herein relate generally to methods and apparatus for mounting porous hollow filtration membranes in a membrane filtration system.
  • 2. Discussion of Related Art
  • Any discussion of the prior art throughout the specification should in no way be considered as an admission that such prior art is widely known or forms part of common general knowledge in the field.
  • Synthetic polymeric membranes are well known in the field of ultrafiltration and microfiltration for a variety of implementations, including desalination, gas separation, filtration, and dialysis. The properties of the membranes vary depending on the morphology of the membranes, for example, depending on parameters such as symmetry, pore shape, and pore size, and the chemical nature of the polymeric material used to form the membrane.
  • A large membrane surface area may be provided when a large filtrate flow is desired. In commercial embodiments, a large number of hollow porous membranes may be mounted together and housed in filtration modules. A commonly used technique to reduce the size of the filtration apparatus is to form the hollow porous membranes in the shape of hollow porous fibers. The hollow porous membranes act in parallel to filter a feed liquid, for example, water for purification. By producing a pressure differential across the membrane walls, the liquid is forced to flow through the pores of the walls of each of the hollow porous membranes while contaminants remain trapped on one side of the membranes and filtrate is withdrawn from the other side. In systems where feed liquid is applied to the outer walls of the membranes (outside-in filtration), the filtrate collects inside the hollow regions, cavities or channels (known as lumens) within the porous hollow membranes and is drawn off through ends of the lumens.
  • By sealing the ends of a porous hollow membrane in a module pot an impenetrable barrier may be formed between the feed and the filtrate. It is desirable that the seal formed by the barrier between the feed and filtrate be maintained to avoid contamination of the filtrate with feed. It is thus desirable that such module pots be designed to withstand forces such as hydraulic pressure from fluid flow inside the filtration module which might otherwise compromise the seal between the feed and the filtrate.
  • In addition to sealing the ends of porous hollow membranes, a module pot may be designed to perform further functions including structurally supporting and mounting the membranes within a module or otherwise within a filtration system. In some filtration arrangements, filtrate is withdrawn only from one end of the membranes and the other ends are merely sealed and supported by a potting head. In other arrangements, only one potting head is provided with the membranes being looped with both open ends located in the same potting head.
  • In some potting arrangements, the porous membrane ends may be sealingly potted using a curable resin material with the porous membrane ends being positioned within the resin material in its liquid non-cured state. The resin material may be allowed to cure to form a generally solid potting head. The curable resin material may be surrounded by a potting sleeve. The potting sleeve may be used to provide an interface between the potting head formed by the cured resin material and associated equipment such as headers and mounting apparatus.
  • SUMMARY
  • It has been found that some curable potting materials which may be used to secure filtration membranes within a potting head disposed in a potting sleeve may shrink during the curing process. This shrinkage may result in the formation of residual tensile stress within the potting head due to resistance of the potting sleeve to such shrinkage. Residual tensile stress in potting materials has been found to not only decrease fracture strength and toughness but also to reduce the fatigue life of the materials. The residual tensile stress may cause cracking, splitting, and/or breaking of the potting head. This can result in compromising the separation between the feed liquid and the filtrate stream in a filtration system and possible undesirable contamination of filtrate.
  • It would be desirable to provide an arrangement of a potting head and potting sleeve in which the formation of residual stress within the potting head during curing of the potting material is reduced as compared to prior known methods.
  • According to one aspect, there is provided a potting sleeve for use in forming a potting head having a porous hollow membrane mounted therein. The potting sleeve includes a first fixed portion and a second portion which is movable relative to the first fixed portion to reduce a peripheral extent of the second portion.
  • In some embodiments, the second portion of the potting sleeve is inwardly deformable to reduce the peripheral extent thereof. The second portion of the potting sleeve may include structurally weakened regions configured to provide for the second portion of the potting sleeve to be inwardly deformable. The second portion of the potting sleeve may be formed of a flexible material.
  • In some embodiments, the potting sleeve includes one or more openings in a wall of the potting sleeve. The openings may be slots.
  • In accordance with another aspect, there is provided a method of mounting a porous hollow membrane in a potting head of a membrane filtration apparatus. The method comprises providing a mold for receiving potting material and positioning a potting sleeve within the mold. The potting sleeve includes a first fixed portion and a second portion which is movable relative to the first fixed portion to reduce a peripheral extent of the second portion. The method further comprises positioning a portion of the porous hollow membrane to be mounted in a region of the mold encompassed by the potting sleeve, introducing a curable potting material into the region to immerse the portion of the porous hollow membrane in the potting material, at least partially curing the potting material to form the potting head, and removing the potting head and the potting sleeve from the mold.
  • In some embodiments, the second portion of the potting sleeve is inwardly deformable to reduce the peripheral extent thereof. The second portion of the potting sleeve may include structurally weakened regions configured to provide for the second portion of the potting sleeve to be inwardly deformable. The second portion of the potting sleeve may be formed of a flexible material.
  • In some embodiments, the potting sleeve is provided with one or more openings in a wall of the potting sleeve. The openings may be slots.
  • In accordance with another aspect, there is provided a method of mounting a porous hollow membrane in a support structure of a membrane filtration apparatus. The method comprises providing a mold for receiving potting material, positioning one or more deformable members within the mold, positioning a portion of the porous hollow membrane to be mounted within the mold, introducing a curable potting material into the mold to immerse the portion of the porous hollow membrane and at least part of the one or more deformable members in the potting material, at least partially curing the potting material to form the potting head, and removing the potting head and the one or more deformable members from the mold.
  • In some embodiments, the deformable member comprises a cylindrical plug.
  • The plug may be hollow and collapsible. The plug may be expandable.
  • In some embodiments, the deformable member is formed of a flexible material. The deformable member may be formed of a material selected from the group consisting of a soft resin material and rubber.
  • In some embodiments, an outer surface of the deformable member is provided with engagement formations. The engagement formations may comprise one or more of a groove, a rib, a shoulder, and a fin. The engagement formations may extend axially from a central body of the deformable member. The engagement formations may extend circumferentially from a central body of the deformable member.
  • In accordance with another aspect, there is provided a structural element for supporting a potting head having a porous hollow membrane mounted therein and extending from a first surface of the potting head. The structural element comprises a cap configured to engage with a potting sleeve of the potting head, the cap having a bearing surface which supports a second surface of the potting head opposite to the first surface of the potting head when the cap is engaged with the potting sleeve.
  • In some embodiments, the cap is generally cylindrical and the bearing surface includes one or more radially extending ribs. The structural element may extend into the second surface of the potting head. In accordance with another aspect, there is provided a potting sleeve for use in forming a potting head having a porous hollow membrane mounted therein. The potting sleeve includes at least one reinforcement member positioned between inner walls of the potting sleeve, the reinforcement member having opposed sides extending axially of the potting sleeve between a first end portion and an opposed second end portion of the reinforcement member. The reinforcement member is connected to an internal wall of the potting sleeve at connection points on each of the opposed sides of the first end portion and the reinforcement member is free of engagement with the potting sleeve apart from at the connection points.
  • In some embodiments, the reinforcement member is plate-like. The reinforcement member may be located along a diameter of the potting sleeve.
  • In some embodiments, the first end portion of the reinforcement member is spaced axially from one end of the potting sleeve.
  • In some embodiments, the reinforcement member apart from adjacent the connection points is, in use, positioned within the potting head.
  • BRIEF DESCRIPTION OF DRAWINGS
  • The accompanying drawings are not intended to be drawn to scale. In the drawings, each identical or nearly identical component that is illustrated in various figures is represented by a like numeral. For purposes of clarity, not every component may be labeled in every drawing. In the drawings:
  • FIG. 1 is an elevational view of a top potting sleeve for a membrane sub-module;
  • FIG. 2 is a plan view of the potting sleeve of FIG. 1;
  • FIG. 3A is an elevational section view of the potting sleeve of FIG. 1 taken along section B-B of FIG. 2;
  • FIG. 3B is a similar side elevational sectional view as FIG. 3A with the potting sleeve positioned in a potting mold;
  • FIG. 4 is a broken elevational view of a membrane sub-module according to another embodiment;
  • FIG. 5 is an underside perspective view of the lower potting sleeve of the sub-module of FIG. 4;
  • FIG. 6 is an elevational view of the lower potting sleeve of the sub-module of FIG. 4;
  • FIG. 7 is an elevational view of a deformable member according to another embodiment;
  • FIG. 8 is a cross-sectional elevational view of the deformable member of FIG. 7;
  • FIG. 9 is a top perspective view of a deformable member according to another embodiment;
  • FIG. 10A is a cross-sectional elevational view of a potting mold with the deformable member of FIG. 7 positioned in use in the potting material together with filtration membranes;
  • FIG. 10B is a similar view as FIG. 10A of the deformable member of FIG. 7 positioned in use in a potting head;
  • FIG. 11 is a top perspective view of a potting sleeve with structural extension according to another embodiment;
  • FIG. 12 is a top perspective cross sectional view taken along a diameter of the potting sleeve of FIG. 11;
  • FIG. 13 is an exploded top perspective view of an upper portion of a membrane sub-module employing the potting sleeve according to the embodiment of FIGS. 11 and 12;
  • FIG. 14 is a top perspective cross sectional view taken along a diameter of the membrane sub-module of FIG. 13 in assembled form;
  • FIG. 15 is a cross sectional elevational view of the sub-module of FIG. 14;
  • FIG. 16 is an elevational view of an upper potting sleeve according to another embodiment;
  • FIG. 17 is a top perspective cross sectional view taken along a diameter of the potting sleeve of FIG. 16 with potting resin in the potting sleeve; and
  • FIG. 18 is a top perspective cross sectional view taken along a diameter of the potting sleeve of FIG. 16 without potting resin in the sleeve.
  • DETAILED DESCRIPTION
  • Aspects and embodiments disclosed herein are not limited to the details of construction and the arrangement of components set forth in the following description or illustrated in the drawings. Aspects disclosed herein are capable of other embodiments and of being practiced or of being carried out in various ways. Also, the phraseology and terminology used herein is for the purpose of description and should not be regarded as limiting. The use of “including,” “comprising,” “having,” “containing,” “involving,” and variations thereof herein is meant to encompass the items listed thereafter and equivalents thereof as well as additional items.
  • Aspects and embodiments disclosed herein are directed to filtration modules or sub-modules and to methods of forming same. Aspects and embodiments disclosed herein provide for a reduced amount of residual stress in potting material of the potting heads of the filtration modules or sub-modules after formation of the potting heads as compared to prior known methods and apparatus. This reduction in residual stress may reduce the chances of mechanical failure of the potting head, for example, delamination of membranes from the potting material in which they are retained, delamination of the potting material from a potting sleeve in which it may be disposed, cracking of the potting material, or other forms of mechanical failure. Aspects and embodiments disclosed herein also provide for a membrane module to include a potting head having a potting material layer thickness with a strength greater than prior known potting heads having potting material layers of equivalent thicknesses.
  • In some embodiments, a potting sleeve for use in forming a filtration membrane module may be provided with one or more features to at least partially alleviate mechanical stresses which may develop within a potting material during curing of the potting material in the potting sleeve. Many potting materials shrink upon curing, resulting in tensile stresses forming in the potting material if the potting material is constrained to maintain set dimensions during curing. In some embodiments disclosed herein a potting sleeve into which a potting material may be introduced and then cured includes one or more features which provide for one or more dimensions of one or more portions of the potting sleeve to decrease during the curing of the potting material. The decrease in the one or more dimensions of the potting sleeve during curing of the potting material accommodates at least some of the shrinkage of the potting material thus reducing the tendency for tensile stresses to develop in the curing potting material.
  • In other embodiments one or more stress relieving features may be disposed in the curing potting material in a potting sleeve. The one or more features may expand or be displaced during the curing of the potting material, relieving mechanical stresses which might otherwise develop in the curing potting material.
  • Referring to FIGS. 1 to 3 there is shown one embodiment of an upper or top potting sleeve for a membrane sub-module 4. The potting sleeve 5 is generally cylindrical though it will be appreciated that the cross-sectional shape of the potting sleeve is not critical and many suitable cross-sectional shapes may be used depending on the desired geometric shape of the potting head. For example, in various embodiments, the potting sleeve 5 may have an elliptical, square, rectangular, or triangular cross-section.
  • The outer surface 6 of the potting sleeve 5 may be provided with a number of engagement formations. The engagement formations may comprise, for example, circumferentially extending grooves, shoulders, or ribs on outer surface 6 of the potting sleeve 5. It will be appreciated by those in the art that, depending on specific implementations, a variety of different forms and shapes of formation may be used to provide for engagement of the potting sleeve 5 and its associated potting head with other components of the membrane sub-module 4.
  • A lower portion of the potting sleeve 5 is provided with a circumferential, outwardly extending rib 7 which, in use, is supported on a shoulder provided in the housing of the sub-module (not shown). Above the rib 7, two axially spaced rows of circumferentially spaced through-openings 8 and 9 are provided in the wall of the potting sleeve 5. The openings 8, 9 are shown are circular holes but it will be appreciated the shape and size of the openings is not critical and, in embodiments where openings are desired, any suitable form of opening may be used. For example, the openings 8, 9 may be in the form of circular holes, oval holes, slits, slots, or other shapes.
  • Above the openings 8, 9, a pair of circumferential, outwardly extending ribs 10 and 11 form a groove 12 which, in use, accommodates a sealing O-ring (not shown). A further circumferential, outwardly extending rib 13 is provided above and vertically spaced from the ribs 10 and 11 to define a supporting shoulder 13′. In some embodiments, it may be desirable to provide ribs 10, 11, and 13 in a region of the potting sleeve 5 which is substantially rigid to ensure the integrity of any mounting or sealing arrangements or structures.
  • An upwardly extending skirt portion 14 is provided above the rib 13. The skirt portion 14 includes a circumferential groove 15 in its base portion 16 and a reduced diameter inset upper portion 17 with a further circumferential groove 18 positioned between the base portion 15 the upper extent of the inset portion 17. This groove 18 serves to form an outwardly extending lip 19 at the upper extent of the inset portion 17. The lip 19 may be used to engage with a lifting mechanism (not shown) to remove the sub-module from the filtration apparatus.
  • The skirt portion 14 forms a portion of the potting sleeve 5 which it movable relative to the fixed lower portion of the sleeve. The skirt portion 14 may be utilized to reduce the peripheral extent of the movable portion of the potting sleeve 5. The skirt portion 14 may include a plurality of circumferentially spaced, vertically extending slots 20 formed therein to define deformable or flexible finger portions 21 therebetween.
  • As best shown in FIGS. 3A and 3B, in use, the upper potting sleeve 5 is positioned in a potting mold 23, together with the membranes 24 to be potted, and is filled with potting material 22 from a level just below the upper set of through-openings 9 to above the upper extent of the potting sleeve 5. The potting material 22 may include any material which may retain filtration membranes 24 within the potting sleeve 5. The potting material 22 may include, for example, urethane, resin, epoxy, or other suitable materials. In some embodiments, the membrane pot may be formed from more than a single layer of potting material, for example, as disclosed in co-pending U.S. patent application Ser. No. 13/087,548, which is incorporated herein by reference in its entirety for all purposes. When more than one layer of potting material is used the layers may be formed of different materials. For example a lower layer distal from the side of the potting head from which the membranes 24 emerge may be formed of a material which strongly adheres to the membranes 24 but is relatively rigid, for example, an epoxy material. A softer potting material, for example, a urethane material may form a layer above the rigid layer. The membranes 24 may emerge from the softer potting material. The softer potting material may flex in use providing for the membranes 24 to move slightly at the point they enter the softer potting material, which may decrease the chances for the membranes 24 to shear from the potting head.
  • In some embodiments, the inner surface of the potting sleeve 5 may include one or more layers of material which may promote adhesion of the potting material 22 to the potting sleeve, and/or which may elastically deform to facilitate the reduction in mechanical stresses in the cured potting material 22. The one or more layers of material may include, for example, a layer of a urethane material.
  • As the potting material 22 cures and contracts, the wall of the portion of the potting sleeve 5 defined by the flexible finger portions 21 may deform radially inward to reduce the peripheral extent of skirt portion 14 of the potting sleeve 5 and reduce or eliminate mechanical stresses which might otherwise form within the cured potting material.
  • It will be appreciated that although slots 20 may be utilized in some embodiments to weaken the skirt portion 14 and provide a movable portion of the potting sleeve 5 to reduce the peripheral extent thereof by inward deformation of the sleeve wall, a variety of other configurations may be used to achieve a similar result in providing for deformability of the potting sleeve. The slots 20 may be replaced by or augmented with thin flexible regions which enable the finger portions 21 to flex inwardly. Further, in some embodiments, the potting sleeve 5 or a portion of the potting sleeve may be formed from a deformable or flexible material. The flexible material may be any material which may adhere to potting material 22 which may be used to retain filtration membranes within the potting sleeve 5 and which has sufficient flexibility to contract along with the potting material 22 upon curing. The flexible material may include, for example, urethane or rubber. In some embodiments, the flexible material may be urethane including a flexibilizing agent.
  • In another embodiment, the wall of the potting sleeve or a portion thereof may be formed of a number of radial segments which move circumferentially relative to one another to produce an inwardly collapsible configuration. Further, although the slots 20 are shown as extending generally vertically, it will be appreciated that they may extend at an angle to vertical, if desired. For example, the slots may extend horizontally, breaking the skirt 14 into a plurality of horizontal finger-like segments or may form a spiral in the skirt 14.
  • Referring to FIGS. 4 to 6, there is shown an embodiment of a lower potting sleeve 30. The lower potting sleeve 30 is generally similar in configuration to the upper potting sleeve 5 described above and may include any one or more of the features of the upper potting sleeve 5.
  • FIG. 4 shows a broken perspective view of a membrane sub-module 4 with an upper potting sleeve 5 and a lower potting sleeve 30.
  • As shown in FIGS. 5 and 6, the lower potting sleeve 30 has a smooth-walled fixed upper portion 31 divided from a fixed middle portion 32 by a circumferential outwardly extending or protruding locating shoulder 33. In a similar manner to the upper potting sleeve 5, the middle portion 32 of the lower potting sleeve wall 34 is provided with a series of vertically spaced rows of through-openings 35. The through-openings 35 in each row are circumferentially spaced from one another and formed in circumferentially spaced groups 36 consisting of a number of rows of through-openings 35. The through-openings 35 are illustrated as are rounded slots, however, it will be appreciated the form, shape, size, and number of the through-openings 35 is not critical and any suitable form or number of through-openings 35 may be employed. In use, these openings 35 provide for fluid communication with the membranes mounted in the potting head.
  • The lower extent of the middle portion 32 of the sleeve 30 is defined by a further circumferential, outwardly extending locating shoulder 37. Adjacent and above the locating shoulder 37, a further row of circumferentially spaced slot openings 38 are provided in the sleeve wall. It will be appreciated the form, shape, size, and number of the openings 38 is not critical and any suitable form or number of openings 38 may be employed.
  • A lower skirt 39 extends downwardly below the shoulder 37 and has a circumferential groove 40 formed therein. In a similar manner to the skirt 14 of the upper potting sleeve 5, the lower skirt 39 is movable relative to the fixed upper portion 31 and the fixed middle portion 32 of the lower porting sleeve 30. The lower skirt 39 includes a plurality of circumferentially spaced, vertically extending slots 41 formed therein to define deformable or flexible finger portions 42 therebetween. The lower skirt 39 thus forms a movable portion of the potting sleeve to reduce the peripheral extent thereof by deformation of the flexible finger portions 42. As potting material disposed within the potting sleeve 30 cures and contracts, the wall 34 of the lower potting sleeve 30 defined by the flexible finger portions 42 can move radially inward to reduce the peripheral extent of skirt 39 of the potting sleeve 30 to reduce or eliminated stresses which might otherwise be formed within the cured potting head.
  • Although the embodiments described above include openings in the potting sleeves and a variety of engagement formations formed in the outer surfaces of the potting sleeves, it will be appreciated these features are not critical and embodiments comprising a simple plain potting sleeve without openings or particular engagement formations could be employed provided the potting sleeve includes a movable portion which enables the peripheral extent of the potting sleeve to be reduced when the potting material shrinks during curing, thus reducing the potential for mechanical stresses to develop within the potting material.
  • Referring to FIGS. 7 to 10B, another embodiment of a potting head 52 is illustrated. In this embodiment a deformable member 50 is positioned in the potting material 51 during the potting process so as to relieve stresses produced during the curing of the potting material 51.
  • As will be appreciated, a variety of different forms of deformable member 50 may be used to achieve the desired function. Embodiments disclosed herein are not limited to the type of deformable member 50 illustrated in FIGS. 7 to 10B. Further, although a single deformable member 50 is shown in FIGS. 10A and 10B, it will be appreciated that a number of deformable members 50 may be positioned as desired throughout the potting head 52.
  • One embodiment of a suitable deformable member 50 is shown in FIGS. 7 and 8. The deformable member 50 comprises a generally cylindrical, hollow, elongate plug 55. One end of the plug 55 is formed with a conical head 56 while the other end is formed with an enlarged diameter base portion 57. The outer wall of the elongate plug 55 is provided with outwardly extending engagement formations for providing engagement with the potting material of the potting head. The engagement formations may comprise longitudinally extending fins 58 spaced at 90° intervals around the circumference of the plug 55. It will be appreciated that more or fewer than four longitudinally extending fins 58 may be utilized and that these fins 58 need not be spaced at 90° intervals but may be spaced at any particular angular interval or intervals desired. Further, in some embodiments, the fins 58 need not extend along the lateral extent of the deformable member 50 as illustrated, but may alternatively or additionally be in the form of rings or tabs extending from a central body of the deformable member with surfaces arranged normal to the lateral extent of the central body of the deformable member 50 or at other angles as desired. It will be appreciated that any suitable form of engagement formation may be used, for example, grooves, ribs, shoulders, dimples, or formations of other shapes.
  • The embodiment shown in FIG. 9 illustrates another form of the engagement formations. In this embodiment the outer wall or surface of the plug is provided with a series of axially spaced circumferential grooves 59. It will be appreciated that in other embodiments, the deformable member 55 may assume even additional shapes. For example, the central body of the deformable member need not by cylindrical as illustrated, but may rather be formed with a square, rectangular, oval, or polygonal cross section, or any other cross section as desired. Further, the cross-sectional area of the central body of the deformable member 55 may vary along its lateral extent, for example, expanding or decreasing from a base to a tip of the deformable member 55.
  • The plug 55 may be hollow and may be made of thin molded plastic material. In use, the thin plastic material may deform due the heat released by the exothermic reaction which occurs during curing of the potting material 52. In other embodiments, the deformable plug may be formed of pre-molded rubber which can readily adhere to the potting material.
  • In another embodiment, the deformable plug 55 can be molded from a soft resin material, for example, urethane a short time (for example, about 30 minutes) before pre-potting of the membranes. The soft urethane plug can then be located in the potting material to ensure chemical bonding between the plug and the potting material of the potting head. The soft resin material provides a readily deformable plug.
  • The deformable plug 55 may be molded in a mold coated with polytetrafluoroethylene or another non-stick material to ensure the outer surface of the plug is free of mold release agent which could hinder the chemical bond between the plug 55 and the potting material of the potting head.
  • FIGS. 10A and 10B show one embodiment of the deformable plug 55 located within a potting head 52.
  • In use, the plug 55 is attached by means of the enlarged base portion 57 to a pre-potting dish 59′. The plug 55 is then located within the potting mold 23 together with the membranes 24 to be potted, the potting sleeve 5 and potting material 51 introduced into the potting mold 23. The conical head 56 of the plug 55 assists deflection of the membranes 24 away from the plug 55 during the insertion of the membranes into the potting mold 23. The mold 23 may be centrifuged to facilitate correct distribution of the potting material 51 around the membranes 24. Following curing of the potting material 51, the base 57 of the plug may be sliced off leaving the plug 55 flush with the top of the potting head 52.
  • The soft core or cores created within the potting head 52 by the deformable plug 55 will stretch or otherwise deform allowing the potting material 51 to shrink as it cures, avoiding much of the residual stress which might otherwise be produced by the shrinkage. The reduction in residual stresses within the potting head 52 may lead to a reduction in stress at the membrane-potting material interface.
  • FIGS. 11 to 14 show a further embodiment of a potting head arrangement including a mechanism for mechanically reinforcing the potting head. In some prior methods as the size of a potting head increases, the thickness of the potting head is increased to resist fluctuating pressures within the membrane sub-module during use. The increased thickness of the potting head results in excessive usage of potting material and the consequent increase in weight of the sub-module. Further, the increased thickness of the potting head may result in an undesirable lumen pressure drop in the length of the membrane as the length of the membrane operating at maximum flow may be substantially increased. Accordingly, where possible, it is desirable to minimize the thickness of the potting head while maintaining its mechanical strength.
  • It has been recognized that increasing the size of a potting head may increase the desirability of providing a structure to reinforce the potting head to reduce deflection of the potting material and prevent breakage and cracking of the potting material or potting head during use. Incorporating reinforcing elements such as ribs within the potting head, however, may result in a pot structure which is rigid and stiff and which may resist the shrinkage of potting material during curing, thus providing for the formation of residual mechanical stresses in the cured potting material. It has been found that where there is no connection between the reinforcing elements and the potting sleeve surrounding the potting material, a large shear stress may be produced between the internal walls of the potting sleeve and the potting material during curing. Alternatively, where no reinforcing elements are provided, deflection of the potting head and/or potting material during use when exposed to high pressures in a filtration system may be undesirably large. It has been found desirable to provide reinforcement of the potting material without producing excessive stress between the potting material and the potting sleeve during curing. Further, by providing a supporting structural element, the mechanical integrity of the potting head can be maintained while providing a potting material layer which is more resistant to deformation than a potting material layer of an equivalent thickness which is not reinforced with a supporting structural element.
  • FIGS. 11 and 12 show perspective views of an extension fitting 60 for a potting sleeve 61. The extension fitting 60 includes structural element 62 for supporting a potting head 63 having one or more porous hollow membranes (not shown) mounted therein and extending from a first surface thereof. The structural element 62 comprises a cap 64 configured to engage with a potting sleeve 61 of the potting head 63. The cap 64 has a bearing surface 65 which supports a second surface 66 of the potting head 63 opposite the first surface of the potting head 63 which forms an interface with the porous hollow membranes disposed in the potting head 63 when the cap 64 is engaged with the potting sleeve 61. The bearing surface 65 may comprise the lower surfaces of a series of radially extending ribs 67 which are equally spaced around the circumference of an inner wall of the generally cylindrical cap 64. The ribs 67 extend diametrically of the cylindrical cap 64. The cylindrical cap 64 has a downwardly extending skirt portion 68 below the lower surface 65 of each rib 67 and engages with a reduced diameter stepped portion 69 of the potting sleeve 61. It will be appreciated that other forms of ribs 67 may additionally or alternatively be included in the cap 64. For example, the ribs 67 may include one or more rings which may be disposed concentrically within the cap, and/or may include ribs which are non-equally spaced around the circumference of the inner wall of the cap 64.
  • FIGS. 13 and 14 show the use of the extension fitting in a membrane module 70. In this embodiment, the potting sleeve 61 and cap 64 slide into a generally cylindrical module housing 71, although it will be appreciated that the module housing 71, potting sleeve 61, and cap 64 may in other embodiments have alternative cross sections, for example, square or rectangular cross sections. The module cap 64 is removably engaged with the top of the module housing 71 and applies an axial support force to the surface 66 of the potting head 63 to prevent deflection thereof under fluctuating pressure from within the sub-module during use.
  • It will be appreciated that although a bearing surface comprising the lower surfaces of the series of radially extending ribs 67 is shown in FIGS. 11 to 14 a variety of forms of bearing surface could alternatively or additionally be used. For example, a cylinder having a generally flat bearing surface corresponding to the upper surface of the potting head could also or alternatively be used.
  • FIGS. 16 to 18 show another embodiment of a potting sleeve. The overall configuration of the potting sleeve is similar in configuration to the sleeve shown in FIGS. 5 and 6. Designations are the same for the same features in each embodiment.
  • The potting sleeve 30 includes at least one reinforcement member 80 positioned between inner walls of the potting sleeve 30. The reinforcement member 80 has opposed sides 82 and 83 extending axially of the potting sleeve 30 between a first end portion 84 and an opposed second end portion 85 of the reinforcement member 80. The reinforcement member is connected to an internal wall of the potting sleeve 30 at connection points 86, 87 on each of the respective opposed sides 82 and 83 of the first end portion 84. The reinforcement member 80 is free of engagement with the potting sleeve 30 apart from at the connection points 86, 87.
  • As best shown in FIG. 17 the reinforcement member 80 is generally plate-like and the connection points 86 and 87 are outwardly extending portions at the lower ends of each opposed side 82 and 83 of the reinforcement member 80. In use, the upper non-fixed portion of the reinforcement member 80 is embedded in the potting head material 88. The non-fixing of this portion enables the reinforcement member 80 to move during curing and shrinking of the potting material 88 and thus undue stresses between the potting head material 88 and the inner surface of the potting sleeve 30 are reduced or avoided. It will be appreciated that a similar form of potting sleeve could be employed for the upper potting sleeve of the membrane sub-module. The form, shape and dimensions of the reinforcement member 80 are not critical. For example, the reinforcement member 80 may in alternate embodiments include more than one plate-like member which may be parallel or which may intersect the plate-like member illustrated. The reinforcement member 80 may be in a shape other than the generally rectangular shape illustrated, for example a semi-circular shape. In some embodiments, one or more apertures may be defined in the reinforcement member 80. Further, it will be appreciated that one of more reinforcement members having the desired operational attributes could be used. The reinforcement members may interengage or intersect one another provided they have a portion or portions free to move relative to the potting material 88.
  • Having thus described several aspects of at least one embodiment, it is to be appreciated various alterations, modifications, and improvements will readily occur to those skilled in the art. For example, it is to be appreciated that any of the features of any of the embodiments disclosed herein may be combined or substituted for features of any other embodiment disclosed herein. Such alterations, modifications, and improvements are intended to be part of this disclosure, and are intended to be within the scope of the disclosure. Accordingly, the foregoing description and drawings are by way of example only.

Claims (25)

What is claimed is:
1. A potting sleeve for use in forming a potting head having a porous hollow membrane mounted therein, the potting sleeve including a first fixed portion and a second portion which is movable relative to the first fixed portion to reduce a peripheral extent of the second portion.
2. The potting sleeve of claim 1, wherein the second portion of the potting sleeve is inwardly deformable to reduce the peripheral extent thereof.
3. The potting sleeve of claim 2, wherein the second portion of the potting sleeve includes structurally weakened regions configured to provide for the second portion of the potting sleeve to be inwardly deformable.
4. The potting sleeve of claim 1, wherein the potting sleeve includes one or more openings in a wall of the potting sleeve.
5. The potting sleeve of claim 4, wherein the openings are slots.
6. The potting sleeve of claim 1, wherein the second portion of the potting sleeve is formed of a flexible material.
7. A method of mounting a porous hollow membrane in a potting head of a membrane filtration apparatus, the method comprising:
providing a mold for receiving potting material;
positioning a potting sleeve within the mold, the potting sleeve including a first fixed portion and a second portion which is movable relative to the first fixed portion to reduce a peripheral extent of the second portion;
positioning a portion of the porous hollow membrane to be mounted in a region of the mold encompassed by the potting sleeve;
introducing a curable potting material into the region to immerse the portion of the porous hollow membrane in the potting material;
at least partially curing the potting material to form the potting head; and
removing the potting head and the potting sleeve from the mold.
8. The method of claim 7, wherein the second portion of the potting sleeve is inwardly deformable to reduce the peripheral extent thereof.
9. The method of claim 8, wherein the second portion of the potting sleeve includes structurally weakened regions configured to provide for the second portion of the potting sleeve to be inwardly deformable.
10. The method of claim 7, wherein the potting sleeve is provided with one or more openings in a wall of the potting sleeve.
11. The method of claim 10, wherein the openings are slots.
12. The method of claim 7, wherein the second portion of the potting sleeve is formed of a flexible material.
13. A method of mounting a porous hollow membrane in a support structure of a membrane filtration apparatus, the method comprising:
providing a mold for receiving potting material;
positioning one or more deformable members within the mold;
positioning a portion of the porous hollow membrane to be mounted within the mold;
introducing a curable potting material into the mold to immerse the portion of the porous hollow membrane and at least part of the one or more deformable members in the potting material;
at least partially curing the potting material to form the potting head; and
removing the potting head and the one or more deformable members from the mold.
14. The method of claim 13, wherein the deformable member comprises a cylindrical plug.
15. The method of claim 14, wherein the plug is hollow and collapsible.
16. The method of claim 13, wherein the deformable member is formed of a flexible material.
17. The method of claim 13, wherein the deformable member is formed of a material selected from the group consisting of a soft resin material and rubber.
18. The method of claim 13, wherein an outer surface of the deformable member is provided with engagement formations.
19. The method of claim 18, wherein the engagement formations comprise one or more of a groove, a rib, a shoulder, and a fin.
20. The method of claim 18, wherein the engagement formations extend axially from a central body of the deformable member.
21. The method of claim 18, wherein the engagement formations extend circumferentially from a central body of the deformable member.
22. A structural element for supporting a potting head having a porous hollow membrane mounted therein and extending from a first surface of the potting head, the structural element comprising a cap configured to engage with a potting sleeve of the potting head, the cap having a bearing surface which supports a second surface of the potting head opposite to the first surface of the potting head when the cap is engaged with the potting sleeve.
23. The structural element of claim 22, wherein the cap is generally cylindrical and the bearing surface includes one or more radially extending ribs.
24. The structural element of claim 22, wherein the structural element extends into the second surface of the potting head.
25.-29. (canceled)
US15/972,852 2012-09-26 2018-05-07 Membrane Potting Methods Abandoned US20180250853A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US15/972,852 US20180250853A1 (en) 2012-09-26 2018-05-07 Membrane Potting Methods

Applications Claiming Priority (6)

Application Number Priority Date Filing Date Title
AU2012904203 2012-09-26
AU2012904203A AU2012904203A0 (en) 2012-09-26 Membrane potting methods
US14/033,968 US9962865B2 (en) 2012-09-26 2013-09-23 Membrane potting methods
AU2013231145 2013-09-23
AU2013231145A AU2013231145B2 (en) 2012-09-26 2013-09-23 Membrane potting methods
US15/972,852 US20180250853A1 (en) 2012-09-26 2018-05-07 Membrane Potting Methods

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
US14/033,968 Division US9962865B2 (en) 2012-09-26 2013-09-23 Membrane potting methods

Publications (1)

Publication Number Publication Date
US20180250853A1 true US20180250853A1 (en) 2018-09-06

Family

ID=50338089

Family Applications (2)

Application Number Title Priority Date Filing Date
US14/033,968 Active 2035-09-26 US9962865B2 (en) 2012-09-26 2013-09-23 Membrane potting methods
US15/972,852 Abandoned US20180250853A1 (en) 2012-09-26 2018-05-07 Membrane Potting Methods

Family Applications Before (1)

Application Number Title Priority Date Filing Date
US14/033,968 Active 2035-09-26 US9962865B2 (en) 2012-09-26 2013-09-23 Membrane potting methods

Country Status (2)

Country Link
US (2) US9962865B2 (en)
AU (1) AU2013231145B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5494720B2 (en) * 2012-05-14 2014-05-21 Nok株式会社 Hollow fiber membrane module
CN109925553A (en) * 2017-12-18 2019-06-25 光宝电子(广州)有限公司 Haemodialyser and its manufacturing method
CN109876675A (en) * 2019-03-19 2019-06-14 星达(泰州)膜科技有限公司 A kind of modified ultrafiltration membrane and preparation method thereof

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20040178136A1 (en) * 2001-11-05 2004-09-16 Tohru Taniguchi Hollow fiber membrane module
WO2010140857A2 (en) * 2009-06-05 2010-12-09 Kolon Industries, Inc. Module case and hollow fiber membrane module using the same

Family Cites Families (911)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US256008A (en) 1882-04-04 Posoelain and china paste boxes
US285321A (en) 1883-09-18 Pottery mold
US511995A (en) 1894-01-02 Air and water purifier
US1997074A (en) 1930-01-24 1935-04-09 John Stogdell Stokes Method of and apparatus for molding synthetic resinous articles
US2080783A (en) 1932-03-09 1937-05-18 Celluloid Corp Method of molding thermoplastic materials
US2105700A (en) 1936-07-13 1938-01-18 William D Ramage Process for purification of beverages
US2732357A (en) 1949-11-25 1956-01-24 Suspensions of polymeric chlorotri-
US2843038A (en) 1954-01-06 1958-07-15 Robert O Manspeaker Bakery apparatus and method
US2926086A (en) 1957-07-30 1960-02-23 Universal Oil Prod Co Stabilization of non-distilled alcoholic beverages and the resulting product
US3068655A (en) 1959-12-01 1962-12-18 Standard Dredging Corp Mobile pneumatic breakwater
US3183191A (en) 1960-04-19 1965-05-11 Hach Chemical Co Stain and rust removing composition
NL269380A (en) 1960-09-19
GB996195A (en) 1961-08-03 1965-06-23 Aero Hydraulics Ltd Improvements in methods and apparatus for mixing and dispersing substances and for maintaining dispersions and emulsions
US3139401A (en) 1962-01-05 1964-06-30 Hach Chemical Co Method for removing rust from water softeners
US3198636A (en) 1962-06-08 1965-08-03 Norda Essential Oil And Chemic Preservation of wine
US3246761A (en) 1962-10-30 1966-04-19 Bryan John Gordon Liquid treating apparatus
US3191674A (en) 1963-06-18 1965-06-29 Westinghouse Electric Corp Shell-and-tube type heat exchangers
NL296139A (en) 1963-08-02
US3492698A (en) 1965-12-22 1970-02-03 Du Pont Centrifugal casting apparatus for forming a cast wall member extending transversely across an elongated bundle of substantially parallel hollow filaments of a fluid permeation separation apparatus
NL136034C (en) 1965-12-22
US3462362A (en) 1966-07-26 1969-08-19 Paul Kollsman Method of reverse osmosis
DE1642833A1 (en) 1967-03-16 1971-04-29 Yves Henderyckx Method and device for separating one or more components from a solution
US3501798A (en) 1967-04-15 1970-03-24 Ennio Carraro Electric polisher for smooth vertical walls,such as window glass
SE320270B (en) 1967-11-04 1970-02-02 Inoue Michiro
US3556305A (en) 1968-03-28 1971-01-19 Amicon Corp Composite membrane and process for making same
US3472765A (en) 1968-06-10 1969-10-14 Dorr Oliver Inc Membrane separation in biological-reactor systems
US3591010A (en) 1968-06-10 1971-07-06 Pall Corp Filter having a microporous layer attached thereto
US3625827A (en) 1968-09-27 1971-12-07 Monsanto Co Water-soluble polymer-enzyme products
US3505215A (en) 1968-10-10 1970-04-07 Desalination Systems Method of treatment of liquids by reverse osmosis
US3628775A (en) 1969-02-14 1971-12-21 Atara Corp Sewage-treating system
CH511629A (en) 1969-03-27 1971-08-31 Brasco Sa Device for filtering a pressurized fluid
US3700561A (en) 1969-08-11 1972-10-24 Pabst Brewing Co Recovery of enzymes
US3592450A (en) 1969-12-03 1971-07-13 George Maxwell Rippon Fluid circulator
US3693406A (en) 1970-01-26 1972-09-26 Air Intake Renu Method for inspecting filters
US3708071A (en) 1970-08-05 1973-01-02 Abcor Inc Hollow fiber membrane device and method of fabricating same
US3700591A (en) 1970-09-24 1972-10-24 Us Interior Cleaning of used membrane with oxalic acid
US3654147A (en) 1971-03-16 1972-04-04 Biospherics Inc Nitrate removal from sewage
US3728256A (en) 1971-06-22 1973-04-17 Abcor Inc Crossflow capillary dialyzer
US3763055A (en) 1971-07-07 1973-10-02 Us Interior Microporous support for reverse osmosis membranes
GB1412983A (en) 1971-11-30 1975-11-05 Debell & Richardson Method of producing porous plastic materials
US3795609A (en) 1971-12-28 1974-03-05 Administrator Environmental Pr Reverse osmosis-neutralization process for treating mineral contaminated waters
US3791631A (en) 1972-02-17 1974-02-12 Mm Ind Inc Method and apparatus for making colored expanded foam articles
US3804258A (en) 1972-08-08 1974-04-16 V Okuniewski Filtering device
US3843809A (en) 1972-08-23 1974-10-22 E Luck Manufacture of alcoholic beverages
US3955998A (en) 1973-06-21 1976-05-11 Phillips Petroleum Company Aqueous gels for plugging fractures in subterranean formation and production of said aqueous gels
US3962095A (en) 1973-06-22 1976-06-08 Sandoz Ltd. Dialyser cartridge
FR2236537B1 (en) 1973-07-11 1977-12-23 Rhone Poulenc Ind
US3876738A (en) 1973-07-18 1975-04-08 Amf Inc Process for producing microporous films and products
US3982095A (en) 1973-10-04 1976-09-21 Searle Cardio-Pulmonary Systems Inc. Respiratory humidifier
US3992301A (en) 1973-11-19 1976-11-16 Raypak, Inc. Automatic flushing system for membrane separation machines such as reverse osmosis machines
US3912624A (en) 1974-03-26 1975-10-14 Universal Oil Prod Co Cleaning of membrane surfaces
US3968192A (en) 1974-04-19 1976-07-06 The Dow Chemical Company Method of repairing leaky hollow fiber permeability separatory devices
JPS51128880A (en) 1975-05-02 1976-11-10 Nippon Zeon Co Method of securing yarn bundle end to case
US4105731A (en) 1975-05-02 1978-08-08 Nippon Zeon Co., Ltd. Method of embedding an end of a bundle of thread-like bodies in a molding material and controlling capillary action by said material
IT1040274B (en) 1975-07-30 1979-12-20 Consiglio Nazionale Ricerche PROCEDURE FOR PREPARATION OF ANISOTROPIC MEMBRANES SUPPORTED FOR REVERSE OSMOSIS BASED ON SYNTHETIC POLYAMIDES
GB1496805A (en) 1975-09-19 1978-01-05 Unilever Ltd Dithionite composition
JPS5278677A (en) 1975-12-25 1977-07-02 Hitachi Ltd Separation of membrane
US4105556A (en) 1976-02-18 1978-08-08 Combustion Engineering, Inc. Liquid waste processing system
JPS535077A (en) 1976-07-06 1978-01-18 Nourinshiyou Shiyokuhin Sougou Membrane separation method
US4192750A (en) 1976-08-09 1980-03-11 Massey-Ferguson Inc. Stackable filter head unit
US4247498A (en) 1976-08-30 1981-01-27 Akzona Incorporated Methods for making microporous products
US4107043A (en) 1977-03-03 1978-08-15 Creative Dispensing Systems, Inc. Inlet conduit fluid filter
US4169873A (en) 1976-12-13 1979-10-02 Aero-Hydraulics Corporation Fluid circulating device
JPS53108882A (en) 1977-03-04 1978-09-22 Kuraray Co Ltd Back washing method for hollow filament membrane
US4203848A (en) 1977-05-25 1980-05-20 Millipore Corporation Processes of making a porous membrane material from polyvinylidene fluoride, and products
US4138460A (en) 1977-06-10 1979-02-06 Cordis Dow Corp. Method for forming tubesheets on hollow fiber tows and forming hollow fiber bundle assemblies containing same
US4519909A (en) 1977-07-11 1985-05-28 Akzona Incorporated Microporous products
JPS6025194B2 (en) 1977-08-04 1985-06-17 株式会社クラレ centrifugal gluing device
US4157899A (en) 1977-10-11 1979-06-12 Cea Carter-Day Company Pulsed backflush air filter
US4183890A (en) 1977-11-30 1980-01-15 Monsanto Company Method of cutting hollow filaments embedded in resinous mass
US4204961A (en) 1978-03-15 1980-05-27 Cusato John Jr Filter apparatus with cleaning function
US4193780A (en) 1978-03-20 1980-03-18 Industrial Air, Inc. Air filter construction
US4227295A (en) 1978-07-27 1980-10-14 Baxter Travenol Laboratories, Inc. Method of potting the ends of a bundle of hollow fibers positioned in a casing
IT1114714B (en) 1978-03-25 1986-01-27 Akzo Nv POLYURETHANE INCORPORATION MASS AND RELATED PRODUCTION PROCESS
DK170416B1 (en) 1978-05-15 1995-08-28 Pall Corp Microporous, hydrophilic, membrane-free, alcohol-insoluble polyamide resin membrane, process for its preparation, use of the membrane in filter elements, and resin molding solution for use in the process
US4315819A (en) 1978-06-12 1982-02-16 Monsanto Company Hollow fiber permeator apparatus
JPS54162684A (en) 1978-06-14 1979-12-24 Ebara Infilco Co Ltd Preliminary treating method for contaminated membrane
JPS5535910A (en) 1978-09-06 1980-03-13 Teijin Ltd Permselectivity composite membrane and preparation thereof
US4190419A (en) 1978-09-22 1980-02-26 Miles Laboratories, Inc. Device for detecting serum bilirubin
DE7829409U1 (en) 1978-10-02 1986-07-31 Akzo Gmbh, 5600 Wuppertal Dialysis membrane hollow thread with a larger exchange surface
US4188817A (en) 1978-10-04 1980-02-19 Standard Oil Company (Indiana) Method for detecting membrane leakage
JPS5554004A (en) 1978-10-18 1980-04-21 Teijin Ltd Selective permeable membrane and its manufacturing
US4367139A (en) 1978-11-16 1983-01-04 Monsanto Company Hollow fiber permeator
DE2964867D1 (en) 1978-12-06 1983-03-24 Abcor Inc Hydrophilic polymeric membranes, process for their preparation, their use as ultrafiltration membranes, and precursor membranes adapted to be converted thereto
US4187263A (en) 1979-01-15 1980-02-05 Aero-Hydraulics Corporation Liquid circulating device
JPS5599703A (en) 1979-01-26 1980-07-30 Matsushita Electric Ind Co Ltd Preparation of anisotropic resin magnet
BE874961A (en) 1979-03-20 1979-09-20 Studiecentrum Kernenergi PROCESS FOR PREPARING A MEMBRANE, THEREFORE PREPARED MEMBRANE, ELECTROCHEMICAL CELL WITH SUCH MEMBRANE AND USING SUCH ELECTROchemical cell
JPS55129155A (en) 1979-03-28 1980-10-06 Sakai Chem Ind Co Ltd Production of catalyst
JPS55129107A (en) 1979-03-28 1980-10-06 Nitto Electric Ind Co Ltd Washing method of selective permeable membrane
US4243525A (en) 1979-03-29 1981-01-06 Fmc Corporation Method for reducing the formation of trihalomethanes in drinking water
DE2915730A1 (en) 1979-04-19 1980-10-30 Kronsbein Dirk Gustav CARTRIDGE FILTER
US4218324A (en) 1979-05-03 1980-08-19 Textron, Inc. Filter element having removable filter media member
US4226921A (en) 1979-07-16 1980-10-07 The Dow Chemical Company Selective plugging of broken fibers in tubesheet-hollow fiber assemblies
US4248648A (en) 1979-07-18 1981-02-03 Baxter Travenol Laboratories, Inc. Method of repairing leaks in a hollow capillary fiber diffusion device
JPS5621604A (en) 1979-07-27 1981-02-28 Toray Ind Inc Separation of liquid by semipermeable composite membrane
US4271026A (en) 1979-10-09 1981-06-02 Air Products And Chemicals, Inc. Control of activated sludge wastewater treating process for enhanced phosphorous removal
CA1115433A (en) 1979-10-26 1981-12-29 David C.I. Pollock Method for protecting a bioreactor pressurized head tank against extreme surges of influent waste water
US4367140A (en) 1979-11-05 1983-01-04 Sykes Ocean Water Ltd. Reverse osmosis liquid purification apparatus
JPS5695304A (en) 1979-12-28 1981-08-01 Teijin Ltd Perm selective composite membrane and its production
US4323453A (en) 1980-01-03 1982-04-06 Monsanto Company Tube sheets for permeators
JPS5944884B2 (en) 1980-02-26 1984-11-01 株式会社クラレ Hollow fiber end sealing method and device
JPS56121685A (en) 1980-02-29 1981-09-24 Ebara Infilco Co Ltd Treatment of liquid containing iron ion and manganese ion
US4629563B1 (en) 1980-03-14 1997-06-03 Memtec North America Asymmetric membranes
US4369605A (en) 1980-07-11 1983-01-25 Monsanto Company Methods for preparing tube sheets for permeators having hollow fiber membranes
DE3026718A1 (en) 1980-07-15 1982-02-04 Akzo Gmbh, 5600 Wuppertal HOLLOW FIBER MEMBRANE FOR PLASMA SEPARATION
JPS5735907A (en) 1980-07-15 1982-02-26 Toyobo Co Ltd Fluid separating element
US4889620A (en) 1980-09-29 1989-12-26 Water Pollution Control Corporation In place gas cleaning of diffusion elements
JPS5770144A (en) 1980-10-17 1982-04-30 Asahi Glass Co Ltd Organic solution of fluorinated copolymer containing carboxyl group
US4384474A (en) 1980-10-30 1983-05-24 Amf Incorporated Method and apparatus for testing and using membrane filters in an on site of use housing
US4389363A (en) 1980-11-03 1983-06-21 Baxter Travenol Laboratories, Inc. Method of potting microporous hollow fiber bundles
JPS57102202A (en) 1980-12-18 1982-06-25 Toyobo Co Ltd Fluid separator
US4496470A (en) 1981-01-12 1985-01-29 The B. F. Goodrich Company Cleaning composition
US4545862A (en) 1981-03-17 1985-10-08 W. L. Gore & Associates, Inc. Desalination device and process
JPS57190697A (en) 1981-05-18 1982-11-24 Serupoole Kogyo Kk Air diffusion apparatus
JPS6059933B2 (en) 1981-05-22 1985-12-27 工業技術院長 Polymer membrane with maleic anhydride residues
US4371427A (en) 1981-06-16 1983-02-01 Phillips Petroleum Company Extractive distillation
JPS5888007A (en) 1981-11-20 1983-05-26 Asahi Glass Co Ltd Separation of liquid mixture
US4707266A (en) 1982-02-05 1987-11-17 Pall Corporation Polyamide membrane with controlled surface properties
US4702840A (en) 1982-02-05 1987-10-27 Pall Corporation Charge modified polyamide membrane
US4405688A (en) 1982-02-18 1983-09-20 Celanese Corporation Microporous hollow fiber and process and apparatus for preparing such fiber
US4415452A (en) 1982-03-18 1983-11-15 Heil Richard W Method and apparatus for treating organic wastewater
US4812235A (en) 1982-03-29 1989-03-14 Hr Textron, Inc. Filter element assembly replaceable mesh pack
ATE52935T1 (en) 1982-03-29 1990-06-15 Hr Textron Inc INTERCHANGEABLE SCREEN PACK FILTERS.
US4540490A (en) 1982-04-23 1985-09-10 Jgc Corporation Apparatus for filtration of a suspension
US4431545A (en) 1982-05-07 1984-02-14 Pall Corporation Microporous filter system and process
US4476112A (en) 1982-05-10 1984-10-09 Stay Fresh, Inc. Food preservative composition
WO1983003984A1 (en) 1982-05-13 1983-11-24 Gerhard Kunz Method for the treatment of a liquid phase, particularly method for desalting aqueous solutions, as well as device for its implementation
US4414172A (en) 1982-05-21 1983-11-08 Filtertek, Inc. Process and apparatus for sealing a plurality of filter elements
JPS5952507A (en) 1982-06-03 1984-03-27 デ−・エル・エム・ドクトル・ミユラ−・アクチエンゲゼルシヤフト Apparatus for continuously concentrating suspension
US4462855A (en) 1982-06-28 1984-07-31 Celanese Corporation Process for bonding polyester reinforcement elements to rubber
JPS5928971A (en) 1982-08-06 1984-02-15 川澄化学工業株式会社 Hollow yarn type mass transfer apparatus and production thereof
US4414113A (en) 1982-09-29 1983-11-08 Ecodyne Corporation Liquid purification using reverse osmosis hollow fibers
US4476015A (en) 1982-11-02 1984-10-09 V. J. Ciccone & Associates, Inc. Multiple element fluid separation device
JPS5992094A (en) 1982-11-18 1984-05-28 Agency Of Ind Science & Technol Anaerobic digestion of organic waste matter
US4467001A (en) 1982-12-27 1984-08-21 Albany International Corp. Process and device for applying, drying and curing a coating on filaments
GB2132366B (en) 1982-12-27 1987-04-08 Brunswick Corp Method and device for testing the permeability of membrane filters
CA1221645A (en) 1983-02-28 1987-05-12 Yoshihiro Okano Filtration apparatus using hollow fiber-membrane
DE3317396A1 (en) 1983-05-13 1984-11-15 Henkel KGaA, 4000 Düsseldorf USE OF COLOYERS FROM ESTERS AND AMIDES OF ACRYLIC AND / OR METHACRYLIC ACIDS AS STOCK POINTS LOW FOR PARAFFIN SOLUTIONS
GB8313635D0 (en) 1983-05-17 1983-06-22 Whatman Reeve Angel Plc Porosimeter
CH673275A5 (en) 1983-05-20 1990-02-28 Christ Ag
JPH0657302B2 (en) 1983-07-13 1994-08-03 株式会社東芝 Backwashing method for hollow fiber membrane filters
US4636296A (en) 1983-08-18 1987-01-13 Gerhard Kunz Process and apparatus for treatment of fluids, particularly desalinization of aqueous solutions
US4650586A (en) 1983-09-26 1987-03-17 Kinetico, Inc. Fluid treatment system
US4756875A (en) 1983-09-29 1988-07-12 Kabushiki Kaisha Toshiba Apparatus for filtering water containing radioactive substances in nuclear power plants
WO1985001449A1 (en) 1983-09-30 1985-04-11 Memtec Limited Cleaning of filters
AU563321B2 (en) 1983-09-30 1987-07-02 U.S. Filter Wastewater Group, Inc. Cleaning of filters
US4888115A (en) 1983-12-29 1989-12-19 Cuno, Incorporated Cross-flow filtration
JPS60206412A (en) 1984-03-28 1985-10-18 Nitto Electric Ind Co Ltd Method for repairing end surface of hollow yarn membrane separation module
US4749487A (en) 1984-04-11 1988-06-07 Syrinx Research Pty. Ltd. High flux membrane
JPS60176300U (en) 1984-04-23 1985-11-21 海洋工業株式会社 water pump
US4539940A (en) 1984-04-26 1985-09-10 Young Richard K Tube and shell heat exchanger with annular distributor
US4609465A (en) 1984-05-21 1986-09-02 Pall Corporation Filter cartridge with a connector seal
JPS60260628A (en) 1984-06-08 1985-12-23 Idemitsu Petrochem Co Ltd Thermoplastic resin molding coated with plasma polymer film
SE441236B (en) 1984-06-18 1985-09-23 Gambro Dialysatoren PROCEDURE FOR MANUFACTURING A DEVICE CONTAINING A HALFIBER BUNCH
EP0170895B1 (en) 1984-07-09 1989-03-22 Millipore Corporation Improved electrodeionization apparatus and method
JPS6125903U (en) 1984-07-24 1986-02-15 株式会社 伊藤鉄工所 filtration equipment
DE3428307A1 (en) 1984-08-01 1986-02-13 Filterwerk Mann & Hummel Gmbh, 7140 Ludwigsburg DISPLAY DEVICE FOR THE POLLUTION LEVEL OF SUCTION AIR FILTERS
JPS6197005A (en) 1984-10-18 1986-05-15 Mitsubishi Rayon Co Ltd Manufacture of hollow yarn membrane module
JPS6197006A (en) 1984-10-18 1986-05-15 Daicel Chem Ind Ltd Repairing method of hollow yarn type module
US5192478A (en) 1984-10-22 1993-03-09 The Dow Chemical Company Method of forming tubesheet for hollow fibers
JPS61107905A (en) 1984-10-30 1986-05-26 Toshiba Corp Filter
JPS6338884Y2 (en) 1984-12-15 1988-10-13
US5198162A (en) 1984-12-19 1993-03-30 Scimat Limited Microporous films
GB2168981B (en) 1984-12-27 1988-07-06 Asahi Chemical Ind Porous fluorine resin membrane and process for preparation thereof
JPS61167406A (en) 1985-01-19 1986-07-29 Sumitomo Bakelite Co Ltd Process for bundling and fixing separation membrane
JPS61167407A (en) 1985-01-19 1986-07-29 Sumitomo Bakelite Co Ltd Preparation of hollow yarn filtration membrane module
JPS61171504A (en) 1985-01-25 1986-08-02 Agency Of Ind Science & Technol Apparatus for centrifugal molding of yarn bundle
JPS61192309A (en) 1985-02-21 1986-08-26 Asahi Chem Ind Co Ltd Hollow yarn type module
AU576424B2 (en) 1985-03-05 1988-08-25 U.S. Filter Wastewater Group, Inc. Concentration of solids in a suspension
US5024762A (en) 1985-03-05 1991-06-18 Memtec Limited Concentration of solids in a suspension
EP0213157B1 (en) 1985-03-05 1992-10-28 Memtec Limited Concentration of solids in a suspension
US4642182A (en) 1985-03-07 1987-02-10 Mordeki Drori Multiple-disc type filter with extensible support
JPS61222510A (en) 1985-03-28 1986-10-03 Nitto Electric Ind Co Ltd Hollow yarn membrane module and its preparation
US4816160A (en) 1985-03-28 1989-03-28 Memtec Limited Cooling hollow fibre cross-flow separators
US4704324A (en) 1985-04-03 1987-11-03 The Dow Chemical Company Semi-permeable membranes prepared via reaction of cationic groups with nucleophilic groups
US4793932A (en) 1985-04-10 1988-12-27 Memtec Limited Variable volume filter or concentrator
JPS61242607A (en) 1985-04-22 1986-10-28 Asahi Chem Ind Co Ltd Preparation of hollow yarn type module having slit
US4610789A (en) 1985-04-22 1986-09-09 Ppg Industries, Inc. Filtration cartridge and reactor
JPS61249505A (en) 1985-04-27 1986-11-06 Toyobo Co Ltd Method for preserving fluid separator
CA1247329A (en) 1985-05-06 1988-12-28 Craig J. Brown Fluid treatment process and apparatus
JPS61257203A (en) 1985-05-10 1986-11-14 Terumo Corp Hydrophilic porous membrane and its preparation
JPS61263605A (en) 1985-05-17 1986-11-21 Toshiba Corp Hollow yarn membrane device
JPS61274709A (en) 1985-05-29 1986-12-04 Ebara Corp Hollow yarn membrane filter apparatus
US4660411A (en) 1985-05-31 1987-04-28 Reid Philip L Apparatus for measuring transmission of volatile substances through films
JPS61291007A (en) 1985-06-17 1986-12-20 Toyobo Co Ltd Hollow yarn type separation membrane element
JPS61293504A (en) 1985-06-24 1986-12-24 Kurita Water Ind Ltd Separation device utilizing hollow yarn membrane
JPS624408A (en) 1985-06-28 1987-01-10 Toshiba Corp Filtration device using hollow yarn membrane
DE3529175A1 (en) 1985-08-14 1987-02-19 Gft Ingenieurbuero DEVICE FOR SEPARATING MIXED MEANS OF THE PERVAPORATION METHOD
US4656865A (en) 1985-09-09 1987-04-14 The Dow Chemical Company System for analyzing permeation of a gas or vapor through a film or membrane
JPS6268828A (en) 1985-09-19 1987-03-28 Youbea Le-Ron Kogyo Kk Transparent cassette liner
US4908114A (en) 1985-09-27 1990-03-13 William Ayers Mobile atom insertion reaction, mobile atom transmissive membrane for carrying out the reaction, and reactor incorporating the mobile atom transmissive membrane
US4876006A (en) 1985-10-08 1989-10-24 Ebara Corporation Hollow fiber filter device
JPS62114609A (en) 1985-11-15 1987-05-26 Ebara Corp Hollow yarn membrane filter
US4824563A (en) 1985-12-04 1989-04-25 Kabushiki Kaisha Meidensha Equipment for treating waste water
US4687578A (en) 1985-12-12 1987-08-18 Monsanto Company Fluid separation membranes
JPH0613088B2 (en) 1985-12-13 1994-02-23 ダイセル化学工業株式会社 Aseptic leak detection method for hollow fiber type modules
JPS62144708A (en) 1985-12-19 1987-06-27 Daicel Chem Ind Ltd Hollow yarn mold membrane module
DE3546091A1 (en) 1985-12-24 1987-07-02 Kernforschungsz Karlsruhe CROSS-CURRENT MICROFILTER
US4686039A (en) * 1985-12-26 1987-08-11 Monsanto Company Fluid separation module
JPS62163708A (en) 1986-01-13 1987-07-20 Ebara Corp Method for backwashing hollow yarn filter
US4779448A (en) 1986-01-28 1988-10-25 Donaldson Company, Inc. Photoelectric bubble detector apparatus and method
JPH06104753B2 (en) 1986-02-04 1994-12-21 旭化成工業株式会社 Non-adsorbing hydrophilic hollow fiber porous membrane
JPH0742861B2 (en) 1986-03-10 1995-05-15 ヤマハ発動機株式会社 Internal combustion engine intake system
US4752421A (en) 1986-04-01 1988-06-21 Kaiyo Kogyo Kabushiki Kaisha Method of supplying air masses and producing jets of water
JPS62237908A (en) 1986-04-07 1987-10-17 Kurita Water Ind Ltd Filter module for hollow yarn type membrane separation equipment
JPS62250908A (en) 1986-04-24 1987-10-31 Asahi Chem Ind Co Ltd Hollow yarn type filter
US4774132A (en) 1986-05-01 1988-09-27 Pall Corporation Polyvinylidene difluoride structure
JPH0741147B2 (en) 1986-05-09 1995-05-10 株式会社東芝 Hollow fiber membrane filtration device
JPS62187606U (en) 1986-05-21 1987-11-28
DE3617724A1 (en) 1986-05-27 1987-12-03 Akzo Gmbh METHOD FOR DETERMINING THE BLOW POINT OR THE BIGGEST PORE OF MEMBRANES OR FILTER MATERIALS
FR2600265B1 (en) 1986-06-20 1991-09-06 Rhone Poulenc Rech DRY AND HYDROPHILIC SEMI-PERMEABLE MEMBRANES BASED ON VINYLIDENE POLYFLUORIDE
JPH0350974Y2 (en) 1986-06-24 1991-10-31
FR2601182B1 (en) 1986-07-07 1992-01-24 Electricite De France PROCESS FOR THE RADIOACTIVE DECONTAMINATION OF A LUBRICANT
US4670145A (en) 1986-07-08 1987-06-02 E. I. Du Pont De Nemours And Company Multiple bundle fluid separation apparatus
US4839048A (en) 1986-07-08 1989-06-13 Pall Corporation Container for pressurized fluid
ES2014516A6 (en) 1986-07-11 1990-07-16 Mentec Ltd Cleaning of filters.
AU605187B2 (en) 1986-09-04 1991-01-10 Memtec Limited Cleaning of hollow fibre filters
AU585177B2 (en) 1986-09-12 1989-06-08 U.S. Filter Wastewater Group, Inc. Hollow fibre filter cartridge and header
US5094750A (en) 1986-09-12 1992-03-10 Memtec Limited Hollow fibre filter cartridge and header
JPS6393307A (en) 1986-10-09 1988-04-23 Asahi Chem Ind Co Ltd Hollow yarn-type filter
JPH089668B2 (en) 1986-10-14 1996-01-31 東レ株式会社 Hydrophilized film and method for producing the same
DE3636583A1 (en) 1986-10-28 1988-05-05 Draegerwerk Ag METHOD FOR PRODUCING A HOLLOW FIBER FABRIC EXCHANGE MODULE AND MODULE PRODUCED BY THIS METHOD
JPS63143905A (en) 1986-12-08 1988-06-16 Toshiba Corp Hollow yarn membrane filter
US4781831A (en) 1986-12-19 1988-11-01 Goldsmith Robert L Cross-flow filtration device with filtrate flow conduits and method of forming same
US4834998A (en) 1986-12-22 1989-05-30 Heublein, Inc. Ultrafiltration of red wines
JPS63171607A (en) 1986-12-30 1988-07-15 Sumitomo Electric Ind Ltd Method for sealing end of hollow yarn membrane
EP0341309B1 (en) 1987-01-20 1996-12-27 Terumo Kabushiki Kaisha Porous polypropylene membrane and process for its production
JPS63180254A (en) 1987-01-21 1988-07-25 Matsushita Electric Ind Co Ltd Private branch exchange
CN1004400B (en) 1987-01-27 1989-06-07 东北电力学院 Filtration method by mediums and equipment thereof
GB8704142D0 (en) 1987-02-23 1987-04-01 Whitford Plastics Ltd Protective surface treatment
US4911838A (en) 1987-02-27 1990-03-27 Kabushiki Kobe Seiko Sho Pluri-tubular aerator
US4867883A (en) 1987-04-21 1989-09-19 Hampton Roads Sanitation District Of The Commonwealth Of Virginia High-rate biological waste water treatment process using activated sludge recycle
US4846970A (en) 1987-06-22 1989-07-11 Osmonics, Inc. Cross-flow filtration membrane test unit
DE3789671T2 (en) 1987-07-28 1994-11-17 Minntech Corp FILTER CARTRIDGE.
EP0343247B1 (en) 1987-07-30 1993-03-03 Toray Industries, Inc. Porous polytetrafluoroethylene membrane, separating apparatus using same, and process for their production
JPS6438197A (en) 1987-07-31 1989-02-08 Nishihara Env San Res Co Ltd Treatment of sewage
US4784771A (en) 1987-08-03 1988-11-15 Environmental Water Technology, Inc. Method and apparatus for purifying fluids
JPH0627215B2 (en) 1987-09-17 1994-04-13 テルモ株式会社 Method for producing hydrophilic polyvinylidene fluoride porous membrane
JPH01144409A (en) 1987-09-18 1989-06-06 Pennwalt Corp Hydrophylic sequence copolymer of vinylidene fluoride and n-alkylacrylamide and its production
JPH0610277B2 (en) 1987-09-28 1994-02-09 ジャパンゴアテックス株式会社 Membrane material
JPH01111494A (en) 1987-10-23 1989-04-28 Shinko Pfaudler Co Ltd Continuously connected type intermittent air water lifting cylinder
JPH01151906A (en) 1987-12-08 1989-06-14 Ube Ind Ltd Production of hollow yarn membrane module cartridge
DE3803341A1 (en) 1988-02-04 1989-08-10 Sartorius Gmbh FLUID-OPEN-ENDING SITES HAVING POROESE MEMBRANE FILTERS AND THEIR USE
US5221478A (en) 1988-02-05 1993-06-22 The Dow Chemical Company Chromatographic separation using ion-exchange resins
US5227101A (en) 1988-03-31 1993-07-13 The Dow Chemical Company Process of making microporous membranes from poly(etheretherketone)-type polymers and low melting point crystallizable polymers
US4904426A (en) 1988-03-31 1990-02-27 The Dow Chemical Company Process for the production of fibers from poly(etheretherketone)-type polymers
GB8807825D0 (en) 1988-03-31 1988-05-05 Romicon Inc Multiple membrane filtration systems
DE3824359A1 (en) 1988-04-07 1989-10-19 Bayer Ag COMPOSITE MEMBRANES, METHOD FOR THEIR PRODUCTION AND THEIR USE
US4800019A (en) 1988-04-22 1989-01-24 Union Carbide Corporation Tubesheet for semipermeable membrane devices
US5147553A (en) 1988-05-04 1992-09-15 Ionics, Incorporated Selectively permeable barriers
US4966699A (en) 1988-05-25 1990-10-30 Terumo Kabushiki Kaisha Hollow fiber membrane fluid processor
US4886601A (en) 1988-05-31 1989-12-12 Japan Organo Co., Ltd. Column filter using bundles of long fibers
JP2527462B2 (en) 1988-06-03 1996-08-21 ダイセル化学工業株式会社 Hollow fiber ultrafiltration membrane module automatic leak detection and alarm system
JPH0217924A (en) 1988-07-04 1990-01-22 Toshiba Corp Method for backwashing hollow yarn membrane filter apparatus
JPH0217925A (en) 1988-07-07 1990-01-22 Toshiba Corp Method for backwashing hollow yarn membrane filter apparatus
GB8816216D0 (en) 1988-07-07 1988-08-10 Fairey Arlon Ltd Filters
JP2830080B2 (en) 1988-07-08 1998-12-02 株式会社デンソー Filter element and manufacturing method thereof
JPH0226625A (en) 1988-07-14 1990-01-29 Toshiba Corp Back washing method of hollow fiber membrane filter
JPH0760197B2 (en) 1988-07-21 1995-06-28 株式会社荏原製作所 Backwashing method for hollow fiber membrane filters
JPH0240296A (en) 1988-07-30 1990-02-09 Nippon Sharyo Seizo Kaisha Ltd Apparatus and method for treating waste water
US5075065A (en) 1988-08-01 1991-12-24 Chemical Fabrics Corporation Method for manufacturing of cast films at high productivity
US5043113A (en) 1988-08-05 1991-08-27 Hoechst Celanese Corp. Process for formation of halogenated polymeric microporous membranes having improved strength properties
DE3829766A1 (en) 1988-09-01 1990-03-22 Akzo Gmbh METHOD FOR PRODUCING MEMBRANES
US4963304A (en) 1988-09-26 1990-10-16 The Dow Chemical Company Process for preparing microporous membranes
JP2529726B2 (en) 1988-10-14 1996-09-04 ダイセル化学工業株式会社 Hollow fiber type membrane module
JPH02126922A (en) 1988-11-04 1990-05-15 Mitsui Eng & Shipbuild Co Ltd Back washing method of separating membrane
FR2639248B1 (en) 1988-11-21 1990-12-28 Lyonnaise Eaux HOUSING FOR FILTER MODULES WITH FIBER BEAMS
JPH02144132A (en) 1988-11-25 1990-06-01 Mitsubishi Rayon Co Ltd Porous polyolefin film
JPH0671540B2 (en) 1988-12-20 1994-09-14 株式会社東芝 Cleaning method of hollow fiber membrane filter
JPH0657304B2 (en) 1988-12-27 1994-08-03 三浦工業株式会社 Membrane modular water treatment system
US4919815A (en) 1989-02-06 1990-04-24 Zimpro/Passavant Inc. Two-stage anaerobic/aerobic treatment process
US4999038A (en) 1989-02-07 1991-03-12 Lundberg Bo E H Filter unit
DE3904544A1 (en) 1989-02-15 1990-08-16 Fraunhofer Ges Forschung POLYMINE MEMBRANES BASED ON POLYVINYLIDENE FLUORIDE, METHOD FOR THE PRODUCTION AND USE THEREOF
US4952317A (en) 1989-03-10 1990-08-28 Bradley Culkin Device and method for filtering a colloidal suspension
JPH02241523A (en) 1989-03-16 1990-09-26 Sumitomo Bakelite Co Ltd Hollow yarn membrane module
JP2856763B2 (en) 1989-04-20 1999-02-10 株式会社東芝 Backwashing device for hollow fiber membrane filter
JP2773231B2 (en) 1989-04-25 1998-07-09 東洋紡績株式会社 Leak test method for hydrophobic hollow fiber type porous membrane
NL8901090A (en) 1989-04-28 1990-11-16 X Flow Bv METHOD FOR MANUFACTURING A MICROPOROUS MEMBRANE AND SUCH MEMBRANE
US4988444A (en) 1989-05-12 1991-01-29 E. I. Du Pont De Nemours And Company Prevention of biofouling of reverse osmosis membranes
US5005430A (en) 1989-05-16 1991-04-09 Electric Power Research Institute, Inc. Automated membrane filter sampler
DE3916511A1 (en) 1989-05-20 1990-12-13 Seitz Filter Werke MEMBRANE FILTER DEVICE FOR MICRO AND ULTRAFILTRATION OF FLUIDS IN THE CROSSFLOW PROCESS
JPH0318373A (en) 1989-06-16 1991-01-25 Terumo Corp Method and device for detecting leak of hollow fiber membrane type liquid processor
JPH0736039B2 (en) 1989-06-27 1995-04-19 株式会社荏原製作所 Method for removing suspended impurities from condensate by mixed bed condensate desalination system
US5138870A (en) 1989-07-10 1992-08-18 Lyssy Georges H Apparatus for measuring water vapor permeability through sheet materials
DE3923128A1 (en) 1989-07-13 1991-01-24 Akzo Gmbh FLAX OR CAPILLARY MEMBRANE BASED ON A HOMOGENEOUS MIXTURE OF POLYVINYLIDE FLUORIDE AND OF A SECOND, BY CHEMICAL IMPROVEMENT, HYDROPHILIBLABLE POLYMERS
US5015275A (en) 1989-07-14 1991-05-14 The Dow Chemical Company Isotropic microporous syndiotactic polystyrene membranes and processes for preparing the same
DE3926059C2 (en) 1989-08-07 1998-01-29 Basf Ag Phosphonomethylated polyvinylamines, process for their preparation and their use
JPH0645185B2 (en) 1989-08-30 1994-06-15 ユニチカ株式会社 Porous composite sheet and method for producing the same
US5080770A (en) 1989-09-11 1992-01-14 Culkin Joseph B Apparatus and method for separating particles
JPH03110445A (en) 1989-09-25 1991-05-10 Fuji Photo Film Co Ltd Completeness testing method
EP0447513B1 (en) 1989-09-29 1997-01-29 Memtec Limited Filter cartridge manifold
US5059317A (en) 1989-10-02 1991-10-22 Dietrich Marius Transportable apparatus for producing drinking water
US5227063A (en) 1989-10-03 1993-07-13 Zenon Environmental Inc. Tubular membrane module
CN1016735B (en) 1989-10-05 1992-05-20 中国石油化工总公司一坪化工厂 Miniature coulomb titrimeter for measuring nitrogen content
EP0519132A1 (en) 1989-10-18 1992-12-23 Exxon Research And Engineering Company Hollow fiber module
US5079272A (en) 1989-11-30 1992-01-07 Millipore Corporation Porous membrane formed from interpenetrating polymer network having hydrophilic surface
US5158721A (en) 1989-11-30 1992-10-27 Millipore Corporation Porous membrane formed from interpenetrating polymer network having hydrophilic surface
FR2655642B1 (en) 1989-12-11 1992-02-28 Anjou Rech WATER TREATMENT PLANT BY A TANGENTIAL FILTER LOOP.
DE3943249C2 (en) 1989-12-29 1993-11-18 Seitz Filter Werke Closed filter element
DE4000978A1 (en) 1990-01-16 1991-07-18 Basf Ag METHOD FOR REMOVING HEAVY METALIONS FROM WINE AND WINE-BASED BEVERAGES
ES2064083T4 (en) 1990-01-23 2007-04-01 Anoxkaldnes As METHOD AND REACTOR FOR WATER PURIFICATION.
US5066375A (en) 1990-03-19 1991-11-19 Ionics, Incorporated Introducing and removing ion-exchange and other particulates from an assembled electrodeionization stack
WO1991016124A1 (en) 1990-04-20 1991-10-31 Memtec Limited Modular microporous filter assemblies
US5364527A (en) 1990-06-20 1994-11-15 Heinz Zimmermann Apparatus and process for treating water
IT1242864B (en) 1990-06-26 1994-05-18 Perdomini Spa AUTOMATIC CONTROL AND OPTIMIZATION SYSTEM OF ULTRAFILTRATION PROCEDURES IN INDUSTRIAL FOOD AND / OR CHEMICAL AND / OR CHEMICAL-PHARMACEUTICAL PLANTS AND ULTRAFILTRATION PROCEDURE USING SUCH SYSTEM.
DE4117281C2 (en) 1990-06-29 1996-02-22 Gore Enterprise Holdings Inc Hydrophilized, microporous membrane made of polytetrafluoroethylene and process for its production
US5104546A (en) 1990-07-03 1992-04-14 Aluminum Company Of America Pyrogens separations by ceramic ultrafiltration
US5639373A (en) 1995-08-11 1997-06-17 Zenon Environmental Inc. Vertical skein of hollow fiber membranes and method of maintaining clean fiber surfaces while filtering a substrate to withdraw a permeate
US5104535A (en) 1990-08-17 1992-04-14 Zenon Environmental, Inc. Frameless array of hollow fiber membranes and module containing a stack of arrays
US5248424A (en) 1990-08-17 1993-09-28 Zenon Environmental Inc. Frameless array of hollow fiber membranes and method of maintaining clean fiber surfaces while filtering a substrate to withdraw a permeate
US5182019A (en) 1990-08-17 1993-01-26 Zenon Environmental Inc. Cartridge of hybrid frameless arrays of hollow fiber membranes and module containing an assembly of cartridges
FR2666245B1 (en) 1990-08-31 1992-10-23 Lyonnaise Eaux METHOD FOR CONTROLLING THE OPERATING MODES OF AN AUTOMATIC WATER FILTRATION APPARATUS ON TUBULAR MEMBRANES.
JP2904564B2 (en) 1990-08-31 1999-06-14 オルガノ株式会社 Method of scrubbing filtration tower using hollow fiber membrane
JP2858913B2 (en) 1990-09-26 1999-02-17 オルガノ株式会社 Filtration method using hollow fiber membrane
US5102550A (en) 1990-11-01 1992-04-07 The United States Of America As Represented By The Secretary Of The Navy Apparatus and process for desalination of seawater
USH1045H (en) 1990-11-19 1992-05-05 The United States Of America As Represented By The Secretary Of The Army Air bubble leak detection test device
JPH04187224A (en) 1990-11-20 1992-07-03 Mitsubishi Rayon Co Ltd Production of fluorine-based porous hollow yarn membrane
JPH0815597B2 (en) 1990-11-22 1996-02-21 株式会社クボタ Operating method of sewage treatment equipment
US5176953A (en) 1990-12-21 1993-01-05 Amoco Corporation Oriented polymeric microporous films
JPH04250898A (en) 1990-12-28 1992-09-07 Yanmar Diesel Engine Co Ltd Batch-wise waste water treating device
US5069065A (en) 1991-01-16 1991-12-03 Mobil Oil Corporation Method for measuring wettability of porous rock
JP2706853B2 (en) 1991-01-16 1998-01-28 ハウス食品株式会社 Membrane filter integrity inspection method and inspection device
JPH04256425A (en) 1991-02-05 1992-09-11 Nippon Millipore Kogyo Kk Back washing device for filtration
JPH04256424A (en) 1991-02-06 1992-09-11 Nitto Denko Corp Hollow fiber membrane module
GB2253572B (en) 1991-02-11 1994-12-14 Aljac Engineering Limited Flow device in fluid circuits
US5677360A (en) 1991-02-13 1997-10-14 Mitsubishi Rayon Co., Ltd. Hydrophilic polymer alloy, fiber and porous membrane comprising this polymer alloy, and methods for preparing them
JPH084722B2 (en) 1991-02-20 1996-01-24 株式会社荏原製作所 Membrane separation device
DE69205198T2 (en) 1991-03-07 1996-03-07 Kubota Kk Device for treating activated sludge.
JP3115624B2 (en) 1991-03-20 2000-12-11 ダイセル化学工業株式会社 Hollow fiber membrane module and method of manufacturing the same
FR2674448B1 (en) 1991-03-26 1994-03-25 Dumez Lyonnaise Eaux METHOD FOR CLEANING MESOPOROUS TUBULAR MEMBRANES OF ULTRAFILTRATION.
JP3093811B2 (en) 1991-04-08 2000-10-03 旭化成工業株式会社 Polyvinylidene fluoride resin film and method for producing the same
EP0509152A1 (en) 1991-04-17 1992-10-21 Ecotechniek B.V. Method and apparatus for processing manure
JPH04317793A (en) 1991-04-17 1992-11-09 Kubota Corp Water treatment apparatus
DE4113420A1 (en) 1991-04-25 1992-10-29 Bayer Ag Hollow polyacrylonitrile fibres, useful for membrane processes - mfd. by dry-wet or wet spinning from special spinning solns. contg. PAN and non-solvent etc., with simultaneous extrusion of core fluid
CA2109436C (en) 1991-05-01 2002-02-05 Level Valley Dairy Company Wastewater treatment system
JPH04334530A (en) 1991-05-10 1992-11-20 Kubota Corp Filter apparatus
DE4117422C1 (en) 1991-05-28 1992-11-12 Willi Prof. Dr.-Ing. 7432 Bad Urach De Dettinger Monitoring contamination level of filter, partic. for hydraulic fluids - in which signal is produced which correlates with quotient of two pressure differences and evaluating device produces signal to change filter when quotient reaches given value
DE4119040C2 (en) 1991-06-10 1997-01-02 Pall Corp Method and device for testing the operating state of filter elements
US5211823A (en) 1991-06-19 1993-05-18 Millipore Corporation Process for purifying resins utilizing bipolar interface
US5156738A (en) 1991-06-21 1992-10-20 Johnson Filtration Systems Inc. Apparatus for uniformly distributing gas and/or liquid in an underdrain lateral system
JP2659475B2 (en) 1991-06-27 1997-09-30 株式会社クボタ Solid-liquid separator
JP3200095B2 (en) 1991-07-24 2001-08-20 旭化成株式会社 Hydrophilic heat-resistant film and method for producing the same
AU671803B2 (en) 1991-08-07 1996-09-12 Siemens Industry, Inc. Concentration of solids in a suspension using hollow fibre membranes
US5186821A (en) 1991-09-03 1993-02-16 D. Thomas Murphy Wastewater treatment process with cooperating velocity equalization, aeration and decanting means
JP2622044B2 (en) 1991-10-04 1997-06-18 東レ株式会社 Hollow fiber membrane module and method of using the same
US5135663A (en) 1991-10-18 1992-08-04 Loctite Corporation Method of treating (meth)acrylic monomer-containing wastewater
US5137631A (en) 1991-10-22 1992-08-11 E. I. Du Pont De Nemours And Company Multiple bundle permeator
US5180407A (en) 1991-11-14 1993-01-19 Demarco Thomas M Vacuum loader with vaned and short tangential separator
JPH05137977A (en) 1991-11-15 1993-06-01 Kubota Corp Detection of separation membrane breakage for membrane filter
US5192442A (en) 1991-12-02 1993-03-09 Zimpro Passavant Environmental Systems, Inc. Multiple zone batch treatment process
JP3111101B2 (en) 1991-12-03 2000-11-20 旭化成工業株式会社 Leak inspection method for membrane separation equipment
TW207964B (en) 1991-12-16 1993-06-21 Permea Inc
JPH05161831A (en) 1991-12-16 1993-06-29 Mitsubishi Kasei Corp Hollow yarn membrane module and separation method using the same
WO1993013489A1 (en) 1991-12-24 1993-07-08 Sierra Semiconductor Corporation An anti-aliasing method for polynomial curves using integer arithmetics
JPH05184884A (en) 1992-01-08 1993-07-27 Mitsubishi Rayon Co Ltd Method for backwashing hollow fiber membrane module
US5269919A (en) 1992-01-17 1993-12-14 Von Medlin Wallace Self-contained water treatment system
US5556591A (en) 1992-01-21 1996-09-17 Millipore S.A. Membrane sealing techniques using thermoplastic polymers
US5203405A (en) 1992-02-03 1993-04-20 Phillips Petroleum Company Two pass shell and tube heat exchanger with return annular distributor
US5198116A (en) 1992-02-10 1993-03-30 D.W. Walker & Associates Method and apparatus for measuring the fouling potential of membrane system feeds
WO1993015827A1 (en) 1992-02-12 1993-08-19 Mitsubishi Rayon Co., Ltd. Hollow yarn membrane module
FR2697446B1 (en) 1992-11-03 1994-12-02 Aquasource Process for the treatment of a fluid containing suspended and dissolved materials, using separation membranes.
US5411663A (en) 1992-03-20 1995-05-02 Micron Separations, Inc. Alcohol-insoluble nylon microporous membranes
JPH05279447A (en) 1992-03-31 1993-10-26 Mitsubishi Rayon Co Ltd Silicon-based block copolymer and membrane made thereof
JPH05285348A (en) 1992-04-04 1993-11-02 Nitto Denko Corp Vertical type hollow fiber membrane module
JPH05305221A (en) 1992-04-28 1993-11-19 Toshiba Corp Membrane separation water treatment apparatus
DE69313574T2 (en) 1992-05-01 1998-01-08 Memtec Japan Ltd Device for checking the integrity of membrane filters
EP0641247B1 (en) 1992-05-18 1996-10-30 Minntech Corporation Hollow fiber filter cartridge and method of manufacture
JPH0627215A (en) 1992-07-08 1994-02-04 Matsushita Electric Ind Co Ltd Portable gps receiver
CA2100643A1 (en) 1992-08-14 1994-02-15 Guido Sartori Fluorinated polyolefin membranes for aromatics/saturates separation
JPH0671120A (en) 1992-08-27 1994-03-15 Akai Electric Co Ltd Method for detecting blinding of filter
US5633163A (en) 1992-09-14 1997-05-27 Dowmus Pty Ltd Method for treating wastewater and solid organic waste
JP3250274B2 (en) 1992-10-08 2002-01-28 東レ株式会社 Filter
US5244579A (en) 1992-10-09 1993-09-14 Zenon Environmental Inc. Transportable reverse osmosis water purification unit
US5275766A (en) 1992-10-30 1994-01-04 Corning Incorporate Method for making semi-permeable polymer membranes
AU663022B2 (en) 1992-11-02 1995-09-21 Siemens Industry, Inc. Fibre monitoring system
US5320760A (en) 1992-12-07 1994-06-14 E. I. Du Pont De Nemours And Company Method of determining filter pluggage by measuring pressures
JPH06170364A (en) 1992-12-07 1994-06-21 Suido Kiko Kk Filter device using permeation membrane
FR2699424B1 (en) 1992-12-21 1995-02-03 Dumez Lyonnaise Eaux Hollow fiber filtration module and its manufacturing process.
JPH06190250A (en) 1992-12-25 1994-07-12 Mitsubishi Rayon Co Ltd Washing method for membrane module
US5262054A (en) 1992-12-30 1993-11-16 E. I. Du Pont De Nemours And Company Process for opening reverse osmosis membranes
US5401401A (en) 1993-01-13 1995-03-28 Aquaria Inc. Hang on tank canister filter
US5316671A (en) 1993-01-21 1994-05-31 Murphy D Thomas Submersible aeration train and aeration apparatus for biological purification of sewage
US5374353A (en) 1993-01-21 1994-12-20 Murphy; D. Thomas Aeration train and aeration apparatus for biological purification of wastewater
JP3010951B2 (en) 1993-01-25 2000-02-21 株式会社クボタ Immersion filtration device
JPH06238273A (en) 1993-02-17 1994-08-30 Mitsubishi Rayon Eng Co Ltd Membrane separation-type water purification
US5468397A (en) 1993-03-16 1995-11-21 Memtec America Corporation Gas backwash of pleated filters
JP3289376B2 (en) 1993-03-26 2002-06-04 栗田工業株式会社 Membrane separation device
US5389260A (en) 1993-04-02 1995-02-14 Clack Corporation Brine seal for tubular filter
JPH06285496A (en) 1993-04-07 1994-10-11 Ebara Infilco Co Ltd Hollow fiber membrane separation biological treatment and device for organic drainage
JPH06292820A (en) 1993-04-09 1994-10-21 Kurita Water Ind Ltd Membrane separation device
US5514278A (en) 1993-04-12 1996-05-07 Khudenko; Boris M. Counterflow microbiological processes
US5361625A (en) 1993-04-29 1994-11-08 Ylvisaker Jon A Method and device for the measurement of barrier properties of films against gases
US5297420A (en) 1993-05-19 1994-03-29 Mobil Oil Corporation Apparatus and method for measuring relative permeability and capillary pressure of porous rock
US5401405A (en) 1993-05-24 1995-03-28 Davis Water & Waste Industries, Inc. Combined air/water backwash in a travelling bridge filter
FR2705734B1 (en) 1993-05-25 1995-06-30 Snecma Method and device for improving the safety of fluid filters.
IL105875A (en) 1993-06-01 1998-04-05 Aga Ab Selective clogging of failed fibers
JPH09220569A (en) 1993-06-02 1997-08-26 Kubota Corp Solid-liquid separator
JPH06343837A (en) 1993-06-02 1994-12-20 Ebara Infilco Co Ltd Hollow fiber membrane module
US5425415A (en) 1993-06-15 1995-06-20 Abb Lummus Crest Inc. Vertical heat exchanger
JP3273665B2 (en) 1993-06-17 2002-04-08 株式会社東芝 Hollow fiber membrane filtration device and cleaning method thereof
JP2946072B2 (en) 1993-07-09 1999-09-06 三菱レイヨン株式会社 Filtration method
US5415490A (en) * 1993-07-13 1995-05-16 Flory; John F. Rope termination with constant-cross-section, divided-cavity potted socket
JP3306794B2 (en) 1993-07-30 2002-07-24 冨士ダイス株式会社 Frame member and method of manufacturing the same
DE4326603C2 (en) 1993-08-07 1995-11-02 Kummer Karl Dankwart Dipl Ing Sewage treatment plant with aeration tank, process for wastewater treatment
US5358732A (en) 1993-08-10 1994-10-25 Albert Einstein College Of Medicine Of Yeshiva University Method and system for removing impurities from aliments
JPH07112185A (en) 1993-08-26 1995-05-02 Nitto Denko Corp Waste water treating device and washing method therefor
JP2721787B2 (en) 1993-09-06 1998-03-04 日本メムテック株式会社 Backwashing method for hollow fiber membrane module
JP3342928B2 (en) 1993-09-13 2002-11-11 オルガノ株式会社 Hanging equipment for filtration equipment using hollow fiber modules
US5419816A (en) 1993-10-27 1995-05-30 Halox Technologies Corporation Electrolytic process and apparatus for the controlled oxidation of inorganic and organic species in aqueous solutions
EP0725669B1 (en) 1993-10-27 1998-09-30 Memtec Limited Method and apparatus for recovering water from a sewer main
JP3453173B2 (en) 1993-11-12 2003-10-06 三菱レイヨン株式会社 Hollow fiber membrane module with diffuser
JPH07136471A (en) 1993-11-15 1995-05-30 Toray Ind Inc Hollow yarn membrane module
FR2713220B1 (en) 1993-11-30 1996-03-08 Omnium Traitement Valorisa Installation of water purification with submerged filter membranes.
JPH07155758A (en) 1993-12-07 1995-06-20 Mitsubishi Rayon Co Ltd Waste water treating device
JPH07155564A (en) 1993-12-10 1995-06-20 Mitsubishi Rayon Co Ltd Hollow yarn membrane module and its production
US5403479A (en) 1993-12-20 1995-04-04 Zenon Environmental Inc. In situ cleaning system for fouled membranes
JP3160140B2 (en) 1993-12-22 2001-04-23 オルガノ株式会社 Filtration device using hollow fiber module
JP2763262B2 (en) 1993-12-24 1998-06-11 日本碍子株式会社 Backwashing method of ceramic membrane
JP3341428B2 (en) 1993-12-24 2002-11-05 栗田工業株式会社 Operating method of immersion membrane device
JP3341427B2 (en) 1993-12-24 2002-11-05 栗田工業株式会社 Immersion membrane equipment
JP3289457B2 (en) 1993-12-28 2002-06-04 栗田工業株式会社 Immersion membrane equipment
JPH07185268A (en) 1993-12-28 1995-07-25 Toray Ind Inc Hollow fiber filter membrane element and module
TW255835B (en) 1994-01-07 1995-09-01 Kubota Kk Filtration membrane module
JPH07204635A (en) 1994-01-21 1995-08-08 I B Ii:Kk Water purifier
JPH07251043A (en) 1994-01-28 1995-10-03 Toto Ltd Filtering method and filter device
US6036030A (en) 1994-02-02 2000-03-14 Bechtel Bwxt Idaho Llc Method for producing a selectively permeable separation module
JPH07236819A (en) 1994-02-25 1995-09-12 Nok Corp Air bubble disperser
DK175061B1 (en) 1994-03-02 2004-05-10 Apv Pasilac As Membrane filtration Event
DE4406952A1 (en) 1994-03-03 1995-09-07 Bayer Ag Process for concentrating paint overspray
US5501798A (en) 1994-04-06 1996-03-26 Zenon Environmental, Inc. Microfiltration enhanced reverse osmosis for water treatment
JP3486451B2 (en) 1994-04-12 2004-01-13 三菱レイヨン株式会社 Hollow fiber membrane module
JPH07289860A (en) 1994-04-25 1995-11-07 Toray Ind Inc Cleaning method of hollow fiber membrane module
US5556541A (en) 1994-04-26 1996-09-17 Filtertek, Inc. Process for making hermetically sealed filter units and filters made thereby
JPH07303895A (en) 1994-05-16 1995-11-21 Kubota Corp Water treatment apparatus
JP3396085B2 (en) 1994-05-24 2003-04-14 テルモ株式会社 Hollow fiber membrane type blood processor
JP3697719B2 (en) 1994-05-26 2005-09-21 松下電工株式会社 Water purifier and method for cleaning porous filtration membrane in water purifier
JPH07313850A (en) 1994-05-30 1995-12-05 Kubota Corp Method for backward washing immersion-type ceramic membrane separator
US5491023A (en) 1994-06-10 1996-02-13 Mobil Oil Corporation Film composition
JP3094407B2 (en) 1994-06-29 2000-10-03 株式会社石垣 Concentrator using hollow fiber membrane
CN2204898Y (en) 1994-06-29 1995-08-09 鹿乔 Proportional flow controlling valve
US5531900A (en) 1994-07-07 1996-07-02 University Of Arizona Modification of polyvinylidene fluoride membrane and method of filtering
US5846425A (en) 1994-07-22 1998-12-08 Whiteman; George R. Methods for treatment of waste streams
ATE198996T1 (en) 1994-07-28 2001-02-15 Millipore Corp POROUS COMPOSITE MEMBRANE AND METHOD
JPH0839089A (en) 1994-08-02 1996-02-13 Toto Ltd Purifying tank and operation thereof
US5451317A (en) 1994-09-08 1995-09-19 Kubota Corporation Solid-liquid separator
AUPM800694A0 (en) 1994-09-09 1994-10-06 Memtec Limited Cleaning of hollow fibre membranes
US5470469A (en) 1994-09-16 1995-11-28 E. I. Du Pont De Nemours And Company Hollow fiber cartridge
FR2726568B1 (en) 1994-11-08 1996-12-06 Atochem Elf Sa POLYMER MIXTURES COMPRISING A HALOGEN POLYMER AND COMPATIBILIZED BY A GRAFT ALIPHATIC POLYESTER
AUPM957194A0 (en) 1994-11-18 1994-12-15 Act Electricity & Water Wastewater treatment method and plant
CN2236049Y (en) 1994-12-01 1996-09-25 张利军 Three-way stop valve
JP3194684B2 (en) 1995-01-27 2001-07-30 ダイセル化学工業株式会社 Natural water membrane purification method
DE19503060A1 (en) 1995-02-01 1996-08-08 Henkel Ecolab Gmbh & Co Ohg Cleaning procedure for membrane filters
EP1655066B1 (en) 1995-03-15 2009-10-07 Siemens Water Technologies Corp. Filtration monitoring and control system
CN1094066C (en) 1995-03-22 2002-11-13 株式会社机械化学研究所 Method of desalinating saline water and apparatus thereof
TW283657B (en) 1995-03-31 1996-08-21 Mitsui Eng & Shipbuilding Co Membrane device and its processing device
AU2348695A (en) 1995-04-14 1996-10-30 Aquasource Method for operating and controlling a bank of filtration me mbrane modules, and bank of modules therefor
US5597732A (en) 1995-04-14 1997-01-28 Bryan-Brown; Michael Composting apparatus
JP3446399B2 (en) 1995-05-31 2003-09-16 日立プラント建設株式会社 Immersion type membrane separation device and membrane separation method using the same
JPH08332357A (en) 1995-06-06 1996-12-17 Toray Ind Inc Method and apparatus for regenerating filter module
WO1996039993A1 (en) 1995-06-07 1996-12-19 Gore Hybrid Technologies, Inc. An implantable containment apparatus for a therapeutical device and method for loading and reloading the device therein
GB9511842D0 (en) 1995-06-10 1995-08-09 North West Water Group Plc Filter
JPH09890A (en) 1995-06-21 1997-01-07 Mitsubishi Kakoki Kaisha Ltd Flat membrane separation device
US5906742A (en) 1995-07-05 1999-05-25 Usf Filtration And Separations Group Inc. Microfiltration membranes having high pore density and mixed isotropic and anisotropic structure
JP3349015B2 (en) 1995-07-25 2002-11-20 株式会社日立製作所 Filtration device
JPH0938648A (en) 1995-08-02 1997-02-10 Japan Organo Co Ltd Treatment of blow water of power plant
US5670053A (en) 1995-08-07 1997-09-23 Zenon Environmental, Inc. Purification of gases from water using reverse osmosis
US5766479A (en) 1995-08-07 1998-06-16 Zenon Environmental Inc. Production of high purity water using reverse osmosis
US5944997A (en) 1995-08-11 1999-08-31 Zenon Environmental Inc. System for maintaining a clean skein of hollow fibers while filtering suspended solids
US6863823B2 (en) 2001-03-23 2005-03-08 Zenon Environmental Inc. Inverted air box aerator and aeration method for immersed membrane
US7087173B2 (en) 1995-08-11 2006-08-08 Zenon Environmental Inc. Inverted cavity aerator for membrane module
US6193890B1 (en) 1995-08-11 2001-02-27 Zenon Environmental Inc. System for maintaining a clean skein of hollow fibers while filtering suspended solids
US6656356B2 (en) 1998-10-09 2003-12-02 Zenon Environmental Inc. Aerated immersed membrane system
KR20050046718A (en) 1995-08-11 2005-05-18 제논 인바이런멘탈 인코포레이티드 Vertical skein of hollow fiber membranes and method of maintaining clean fiber surfaces
US6685832B2 (en) 1995-08-11 2004-02-03 Zenon Environmental Inc. Method of potting hollow fiber membranes
JP3137568B2 (en) 1995-09-07 2001-02-26 オルガノ株式会社 Method of scrubbing filtration tower using hollow fiber membrane
JPH0975682A (en) 1995-09-13 1997-03-25 Kanegafuchi Chem Ind Co Ltd Hollow fiber membrane integrated module
JP3294979B2 (en) 1995-09-14 2002-06-24 株式会社精工技研 Optical fiber ferrule assembly with angle index indicating direction of polarization plane of optical fiber
JP3583201B2 (en) 1995-09-14 2004-11-04 三菱レイヨン株式会社 Cleaning method for separation membrane module
CN1102425C (en) 1995-09-21 2003-03-05 旭化成株式会社 Hollow fiber membrane module
JP3671473B2 (en) 1995-10-05 2005-07-13 栗田工業株式会社 Immersion membrane separator
JP3671477B2 (en) 1995-10-12 2005-07-13 栗田工業株式会社 Cleaning method for submerged membrane separator
JPH09103655A (en) 1995-10-13 1997-04-22 Kanegafuchi Chem Ind Co Ltd Hollow fiber membrane filter
RU2119817C1 (en) 1995-10-23 1998-10-10 Акционерное общество открытого типа "Полимерсинтез" Porous fluorocarbon membrane, method of its preparation, and cartridge filter based on this membrane
JPH09117647A (en) 1995-10-24 1997-05-06 Kubota Corp Operation of air diffusion device
JPH09187628A (en) 1995-10-31 1997-07-22 Nikkiso Co Ltd Hollow fiber type module and its production
US5626755A (en) 1995-11-08 1997-05-06 Micronair, Inc. Method and apparatus for waste digestion using multiple biological processes
JPH09138298A (en) 1995-11-16 1997-05-27 Hitachi Ltd Filter using hollow-fiber membrane and method for backwashing it
JPH09141063A (en) 1995-11-21 1997-06-03 Mitsubishi Rayon Co Ltd Hollow fiber membrane module
FR2741280B1 (en) 1995-11-22 1997-12-19 Omnium Traitement Valorisa METHOD FOR CLEANING A FILTER SYSTEM OF THE SUBMERSIBLE MEMBRANE TYPE
US5744037A (en) 1995-11-28 1998-04-28 Ebara Corporation Method of treating foul water
JPH09155345A (en) 1995-12-01 1997-06-17 Hitachi Plant Eng & Constr Co Ltd Filtration method for hollow fiber membrane module
JPH09192458A (en) 1996-01-22 1997-07-29 Nok Corp Hollow yarn membrane module
US6074718A (en) 1996-02-06 2000-06-13 Koch Membrane Systems, Inc. Self supporting hollow fiber membrane and method of construction
US5895570A (en) 1996-02-09 1999-04-20 United States Filter Corporation Modular filtering system
US6077435A (en) 1996-03-15 2000-06-20 Usf Filtration And Separations Group Inc. Filtration monitoring and control system
JPH09271641A (en) 1996-04-04 1997-10-21 Kanegafuchi Chem Ind Co Ltd Production of hollow yarn membrane module
JPH09313902A (en) 1996-05-28 1997-12-09 Kubota Corp Chemical cleaning method for immersion type ceramic membrane separation device
JPH09324067A (en) 1996-06-05 1997-12-16 Shin Etsu Polymer Co Ltd Production of porous fluororesin
EP0814116A1 (en) 1996-06-19 1997-12-29 Hüls Aktiengesellschaft Hydrophilic coating of polymeric substrate surfaces
US5989428A (en) 1996-06-21 1999-11-23 Goronszy; Mervyn Charles Controlling wastewater treatment by monitoring oxygen utilization rates
EP0813897A3 (en) 1996-06-21 1998-06-24 Japan Pionics Co., Ltd. Dust removing apparatus and dust removing method
JP3198923B2 (en) 1996-07-04 2001-08-13 栗田工業株式会社 Cleaning method of membrane
US5958243A (en) 1996-07-11 1999-09-28 Zenon Environmental Inc. Apparatus and method for membrane filtration with enhanced net flux
JP3248611B2 (en) 1996-07-12 2002-01-21 日立プラント建設株式会社 Solid-liquid separation device
JPH1033955A (en) 1996-07-23 1998-02-10 Hitachi Zosen Corp Membrane separation apparatus
JP3278577B2 (en) 1996-07-31 2002-04-30 セイコーインスツルメンツ株式会社 Adhesive for optical connector and ferrule and optical connector using the same
US5814234A (en) 1996-08-14 1998-09-29 Prosys Corporation Integrated soil and fluid decontamination system
US5866001A (en) 1996-08-21 1999-02-02 Essef Corporation Filament wound housing for a reverse osmosis filter cartridge
JPH10110657A (en) 1996-08-22 1998-04-28 Stanadyne Automot Corp Filter assembly having matching cartridge support structure
JPH1066972A (en) 1996-08-28 1998-03-10 Nomura Micro Sci Co Ltd Cleaning and regenerating method of separation membrane for water treatment
JPH1076264A (en) 1996-09-05 1998-03-24 Kubota Corp Sewage treatment apparatus using immersion type membrane separator
JPH1076144A (en) 1996-09-05 1998-03-24 Kurita Water Ind Ltd Membrane separator by hollow tubular membranes
JPH1085566A (en) 1996-09-11 1998-04-07 Hitachi Ltd Pleated type filter
US5888401A (en) 1996-09-16 1999-03-30 Union Camp Corporation Method and apparatus for reducing membrane fouling
JPH1085562A (en) 1996-09-17 1998-04-07 Asahi Chem Ind Co Ltd Union restricting orifice and filtration device
JPH1085565A (en) 1996-09-19 1998-04-07 Yamada Kogyo Kk Membrane separator
JP3686918B2 (en) 1996-10-16 2005-08-24 森村興産株式会社 Filtration device for solid-liquid separation of sewage, wastewater, etc.
USD396046S (en) 1996-10-24 1998-07-14 Allen Scheel Steer device for an outboard motor
AUPO377796A0 (en) 1996-11-21 1996-12-19 Memtec America Corporation Microporous membrane filtration and backwashing process
JP3436026B2 (en) 1996-12-02 2003-08-11 エヌオーケー株式会社 Hollow fiber membrane module
EP1010457A4 (en) 1996-12-10 2006-03-22 Asahi Chemical Ind Porous polyvinylidene fluoride resin film and process for producing the same
AUPO412596A0 (en) 1996-12-10 1997-01-09 Memtec America Corporation Improved microporous membrane filtration assembly
AT407291B (en) 1996-12-12 2001-02-26 Andreas Weissenbacher THREE-WAY VALVE
US6045899A (en) 1996-12-12 2000-04-04 Usf Filtration & Separations Group, Inc. Highly assymetric, hydrophilic, microfiltration membranes having large pore diameters
CA2551202C (en) 1996-12-20 2010-10-26 Usf Filtration And Separations Group, Inc. Scouring method
US20040232076A1 (en) 1996-12-20 2004-11-25 Fufang Zha Scouring method
WO1998028064A1 (en) 1996-12-21 1998-07-02 Akzo Nobel Nv Membrane module with hollow fibre membranes arranged in layers
JPH10180048A (en) 1996-12-27 1998-07-07 Kurita Water Ind Ltd Immersion type membrane separator
DE19700493A1 (en) 1997-01-09 1998-07-16 Bayer Ag Methods for cleaning surfaces
US6146747A (en) 1997-01-22 2000-11-14 Usf Filtration And Separations Group Inc. Highly porous polyvinylidene difluoride membranes
USD396726S (en) 1997-02-06 1998-08-04 Abc Group Combined air intake manifold and filter
JP3887072B2 (en) 1997-02-12 2007-02-28 株式会社クラレ Method for cleaning hollow fiber membrane module and filtration device used in the method
JPH10225685A (en) 1997-02-17 1998-08-25 Hitachi Ltd Water purifying treatment device
JPH10235168A (en) 1997-02-24 1998-09-08 Mitsubishi Rayon Co Ltd Filter cleaning method
US6120688A (en) 1997-02-25 2000-09-19 Zenon Environmental, Inc. Portable reverse osmosis unit for producing drinking water
US6007712A (en) 1997-02-28 1999-12-28 Kuraray Co., Ltd. Waste water treatment apparatus
US6048454A (en) 1997-03-18 2000-04-11 Jenkins; Dan Oil filter pack and assembly
JPH10249171A (en) 1997-03-18 1998-09-22 Kanegafuchi Chem Ind Co Ltd Hollow yarn membrane module
US5733456A (en) 1997-03-31 1998-03-31 Okey; Robert W. Environmental control for biological nutrient removal in water/wastewater treatment
FR2762834B1 (en) 1997-05-05 1999-06-04 Ete Europ De Traitement Des Ea PROCESS AND PLANT FOR THE TREATMENT OF WASTEWATER AND THEIR APPLICATION TO WINE EFFLUENTS
JP2945894B2 (en) 1997-05-16 1999-09-06 日本碍子株式会社 How to remove cleaning chemicals
JPH10328538A (en) 1997-05-29 1998-12-15 Japan Organo Co Ltd Method for cleaning hollow yarn membrane filtration tower
AUPO709797A0 (en) 1997-05-30 1997-06-26 Usf Filtration And Separations Group Inc. Predicting logarithmic reduction values
JP3859816B2 (en) 1997-06-16 2006-12-20 三菱レイヨン株式会社 Hollow fiber membrane filtration device
NL1006390C2 (en) 1997-06-25 1998-12-29 Triqua B V Cross=flow filtration process
US6354444B1 (en) 1997-07-01 2002-03-12 Zenon Environmental Inc. Hollow fiber membrane and braided tubular support therefor
US5914039A (en) 1997-07-01 1999-06-22 Zenon Environmental Inc. Filtration membrane with calcined α-alumina particles therein
JPH1128467A (en) 1997-07-08 1999-02-02 Nkk Corp Immersion type membrane separation device
JPH1131025A (en) 1997-07-11 1999-02-02 Ricoh Co Ltd Pc card slot
JPH1133365A (en) 1997-07-17 1999-02-09 Asahi Chem Ind Co Ltd Method and apparatus for two-layer centrifugal bonding of hollow yarn membrane module
JPH1133367A (en) 1997-07-24 1999-02-09 Mitsubishi Rayon Co Ltd Hollow yarn membrane module
UA61961C2 (en) 1997-07-29 2003-12-15 A non-biocidal method for inhibiting biogenic sulfide generation
US5997745A (en) 1998-04-08 1999-12-07 Zenon Environmental Inc. Method for producing high purity water using triple pass reverse osmosis (TPRO)
JPH1176769A (en) 1997-09-01 1999-03-23 Daicel Chem Ind Ltd Cleaning method of filter membrane module
JPH1176770A (en) 1997-09-03 1999-03-23 Kanegafuchi Chem Ind Co Ltd Operation of hollow yarn membrane module
JPH1190189A (en) 1997-09-19 1999-04-06 Inax Corp Method for cleaning membrane with liquid chemical
US6641733B2 (en) 1998-09-25 2003-11-04 U. S. Filter Wastewater Group, Inc. Apparatus and method for cleaning membrane filtration modules
US6017451A (en) 1997-10-01 2000-01-25 Kopf; Henry B. Spider fitting for multi-module filter system, and motive cart assembly comprising same
US6039872A (en) 1997-10-27 2000-03-21 Pall Corporation Hydrophilic membrane
US6083393A (en) 1997-10-27 2000-07-04 Pall Corporation Hydrophilic membrane
US6723758B2 (en) 1997-11-12 2004-04-20 Ballard Power Systems Inc. Graft polymeric membranes and ion-exchange membranes formed therefrom
JPH11156360A (en) 1997-11-25 1999-06-15 Kubota Corp Method for operation of water treatment plant
JPH11156166A (en) 1997-11-28 1999-06-15 Mitsubishi Heavy Ind Ltd Cleaning method for hollow fiber membrane module
USD400890S (en) 1997-12-03 1998-11-10 Gambardella C Bruce Automotive manifold
US6290756B1 (en) 1997-12-03 2001-09-18 Praxair Technology, Inc. Hollow fiber membrane tubesheets of variable epoxy composition and hardness
JPH11165200A (en) 1997-12-05 1999-06-22 Mitsubishi Rayon Co Ltd Method for treating sludge
JP3866399B2 (en) 1997-12-16 2007-01-10 住友重機械工業株式会社 Membrane filtration device and operation method thereof
JPH11179171A (en) 1997-12-25 1999-07-06 Toshiba Eng Co Ltd Hollow fiber membrane filter and its operation method
JPH11300177A (en) 1998-02-23 1999-11-02 Kubota Corp Membrane separator
EP0937494A3 (en) 1998-02-23 2000-03-01 Kubota Corporation Membrane separation system
US6066401A (en) 1998-02-25 2000-05-23 National Research Council Of Canada Wide-band two-layer antireflection coating for optical surfaces
CA2321990A1 (en) 1998-02-27 1999-09-02 Masanori Itakura Crude oil processing apparatus and crude oil processing method
US6126819A (en) 1998-03-13 2000-10-03 Rochem Ro-Wasserbehandlung Gmbh Apparatus for the treatment of liquids contaminated by foreign substances
DE19811945A1 (en) 1998-03-13 1999-09-16 Rochem Ro Wasserbehandlung Gmbh Cross-flow membrane filter for municipal water treatment plant
US5951878A (en) 1998-03-20 1999-09-14 Aqua-Aerobic Systems, Inc. Method and apparatus for cleaning filter material in a filter apparatus utilizing a suction generating nozzle
DE69928237T2 (en) 1998-03-31 2006-08-03 Samsung Engineering Co., Ltd. METHOD OF TREATING WASTEWATER FOR REMOVING ORGANIC SUBSTANCES AND NITROGEN,
JP3682897B2 (en) 1998-04-24 2005-08-17 東洋濾紙株式会社 High strength hydrophilic polyvinylidene fluoride porous membrane and method for producing the same
DE29906389U1 (en) 1998-04-30 1999-06-17 Cramer Weberei Heek Nienborg G Multi-layer textile building material
JPH11309351A (en) 1998-04-30 1999-11-09 Kuraray Co Ltd Washing of hollow fiber membrane module
US6074551A (en) 1998-04-30 2000-06-13 Culligan Water Conditioning Of Fairfield County Automatic cleaning system for a reverse osmosis unit in a high purity water treatment system
JPH11319501A (en) 1998-05-08 1999-11-24 Toray Ind Inc Hollow fiber membrane module and use applications thereof
JPH11319507A (en) 1998-05-22 1999-11-24 Toray Ind Inc Hollow fiber membrane module
JPH11333265A (en) 1998-05-26 1999-12-07 Nitto Denko Corp Membrane module
JP3924926B2 (en) 1998-06-15 2007-06-06 東レ株式会社 Hollow fiber membrane filtration membrane module
JP2000079390A (en) 1998-06-30 2000-03-21 Kikai Kagaku Kenkyusho:Kk Purified water production
FR2781168B1 (en) 1998-07-17 2000-09-15 Polymem WATER TREATMENT PROCESS AND INSTALLATION
ES2300149T3 (en) 1998-07-21 2008-06-01 Toray Industries, Inc. PROCEDURE FOR THE INHIBITION OF THE DEVELOPMENT OF BACTERIA IN THE NEIGHBORHOOD OF A MEMBRANE OF SEPARATION AND STERILIZATION TECHNIQUE OF THIS.
US6113782A (en) 1998-07-28 2000-09-05 Terumo Cardiovascular Systems Corporation Potting of tubular bundles in housing
JP2000051669A (en) 1998-08-05 2000-02-22 Hitachi Ltd Hollow fiber membrane module fitted with lower cap
JP4230569B2 (en) 1998-08-07 2009-02-25 三菱レイヨン株式会社 Hollow fiber membrane module
US6280626B1 (en) 1998-08-12 2001-08-28 Mitsubishi Rayon Co., Ltd. Membrane separator assembly and method of cleaning the assembly utilizing gas diffuser underneath the assembly
US6217770B1 (en) 1998-08-14 2001-04-17 Atp International Apparatus and method for treatment of water
US6096213A (en) 1998-08-14 2000-08-01 3M Innovative Properties Company Puncture-resistant polyolefin membranes
JP2000061466A (en) 1998-08-20 2000-02-29 Nkk Corp Device for treating membrane-filtration waste water and its operation
JP2000070684A (en) 1998-08-27 2000-03-07 Japan Organo Co Ltd Backwashing of pleated membrane filter
US5968357A (en) 1998-08-27 1999-10-19 Voith Sulzer Paper Technology North America, Inc. Screen basket having a removable and replaceable cylindrical mesh liner
US6071404A (en) 1998-08-31 2000-06-06 Tsui; Tommy Water treating device
UA72220C2 (en) 1998-09-08 2005-02-15 Байоенджініерінг Рісорсиз, Інк. Water-immiscible mixture solvent/cosolvent for extracting acetic acid, a method for producing acetic acid (variants), a method for anaerobic microbial fermentation for obtaining acetic acid (variants), modified solvent and a method for obtaining thereof
TWI222895B (en) 1998-09-25 2004-11-01 Usf Filtration & Separations Apparatus and method for cleaning membrane filtration modules
MXPA01003215A (en) 1998-09-28 2005-07-25 D Lindbo Glen Wastewater treatment tank with influent gates and pre-react zone with an outwardly flared lower portion.
JP4069226B2 (en) 1998-09-28 2008-04-02 旭化成ケミカルズ株式会社 Method for fixing cartridge type module and tank type filtration device
US7014173B2 (en) 1998-10-09 2006-03-21 Zenon Environmental Inc. Cyclic aeration system for submerged membrane modules
US6550747B2 (en) 1998-10-09 2003-04-22 Zenon Environmental Inc. Cyclic aeration system for submerged membrane modules
ES2220113T3 (en) 1998-10-09 2004-12-01 Zenon Environmental Inc. CYCLE AERATION SYSTEM FOR SUBMERSED MEMBRANE MODULES.
US6319411B1 (en) 1998-10-09 2001-11-20 Zenon Environmental Inc. Method of maintaining clean vertical skeins of hollow fiber membranes and system therefor
US6706189B2 (en) 1998-10-09 2004-03-16 Zenon Environmental Inc. Cyclic aeration system for submerged membrane modules
NL1010544C2 (en) 1998-11-13 2000-05-16 Stork Friesland Bv Method and device for removing suspended matter and salts from a liquid by means of membrane filtration.
WO2000030742A1 (en) 1998-11-23 2000-06-02 Zenon Environmental Inc. Water filtration using immersed membranes
CA2290053C (en) 1999-11-18 2009-10-20 Zenon Environmental Inc. Immersed membrane module and process
WO2001036075A1 (en) 1999-11-18 2001-05-25 Zenon Environmental Inc. Immersed membrane filtration system and overflow process
JP4107453B2 (en) 1998-11-26 2008-06-25 旭化成ケミカルズ株式会社 Hollow fiber membrane cartridge
JP2000157845A (en) 1998-11-26 2000-06-13 Asahi Chem Ind Co Ltd Hollow fiber membrane cartridge and its fixing structure
JP2000157850A (en) 1998-11-27 2000-06-13 Nitto Denko Corp Separating membrane preservation liquid and separating membrane module
GB9826575D0 (en) 1998-12-04 1999-01-27 Oladpa Tox
US6162020A (en) 1998-12-04 2000-12-19 Nca2Bioprocess, Inc. Airlift pump apparatus and method
US6156200A (en) 1998-12-08 2000-12-05 Usf Filtration & Separations Group, Inc. Gas-scrubbed hollow fiber membrane module
JP4012640B2 (en) 1998-12-24 2007-11-21 旭化成ケミカルズ株式会社 Hollow fiber membrane module
JP2000189958A (en) 1998-12-28 2000-07-11 Maezawa Ind Inc Immersion type membrane filter device
DE19959916A1 (en) 1998-12-30 2000-07-20 Henkel Chile Sa Aqueous polymer dispersion, useful for adhesives and coatings, contains organic and/or inorganic filler particles and organic polymer particles that are formed in presence of at least one filler
US6432310B1 (en) 1999-01-22 2002-08-13 Nitto Denko Corporation Methods of running and washing spiral wound membrane module
JP2000233020A (en) 1999-02-15 2000-08-29 Nikkiso Co Ltd Washing method and washing device for blood treating device
JP2000237548A (en) 1999-02-17 2000-09-05 Tokyo Denki Komusho Co Ltd Hollow fiber membrane type heat storage tank water purifying device
JP4200576B2 (en) 1999-02-23 2008-12-24 トヨタ自動車株式会社 Fuel cell system
JP2000254459A (en) 1999-03-05 2000-09-19 Sumitomo Heavy Ind Ltd Method for washing solid-liquid separation element and solid-liquid separator
US6149817A (en) 1999-03-08 2000-11-21 Celgard Inc. Shell-less hollow fiber membrane fluid contactor
WO2000058038A1 (en) 1999-03-26 2000-10-05 Sumitomo Heavy Industries, Ltd. Method apparatus for disposal of chlorine-containing organic compound
US6770202B1 (en) 1999-04-14 2004-08-03 Pall Corporation Porous membrane
AU762091B2 (en) 1999-04-20 2003-06-19 Evoqua Water Technologies Llc Membrane filtration manifold system
US6322703B1 (en) 1999-04-20 2001-11-27 Asahi Kasei Kabushiki Kaisha Method for purifying aqueous suspension
AUPP985099A0 (en) 1999-04-20 1999-05-13 Usf Filtration And Separations Group Inc. Membrane filtration manifold system
JP3572992B2 (en) 1999-04-21 2004-10-06 日立プラント建設株式会社 Operating method of membrane filtration device
JP2000317276A (en) 1999-05-12 2000-11-21 Zenken:Kk Filtering device
JP2000334276A (en) 1999-05-25 2000-12-05 Mitsubishi Rayon Co Ltd Operation of filtration device
US6221247B1 (en) 1999-06-03 2001-04-24 Cms Technology Holdings, Inc. Dioxole coated membrane module for ultrafiltration or microfiltration of aqueous suspensions
JP2000342932A (en) 1999-06-04 2000-12-12 Mitsubishi Rayon Co Ltd Potting method for separation membrane
US6627082B2 (en) 1999-06-10 2003-09-30 Envirogen, Inc. System and method for withdrawing permeate through a filter and for cleaning the filter in situ
US6277512B1 (en) 1999-06-18 2001-08-21 3M Innovative Properties Company Polymer electrolyte membranes from mixed dispersions
US6755970B1 (en) 1999-06-22 2004-06-29 Trisep Corporation Back-flushable spiral wound filter and methods of making and using same
JP3617378B2 (en) 1999-06-25 2005-02-02 日立プラント建設株式会社 Immersion flat membrane filtration device
GB9914854D0 (en) 1999-06-25 1999-08-25 Wilkes Ian P Self cleaning membrane device for filtration used in submerged operation
US6485645B1 (en) 1999-07-20 2002-11-26 Zenon Environmental Inc Biological process for removing phosphorus involving a membrane filter
AU6144600A (en) 1999-07-20 2001-02-05 Zenon Environmental Inc. Biological process for removing phosphorus involving a membrane filter
US6303035B1 (en) 1999-07-30 2001-10-16 Zenon Environmental Inc. Immersed membrane filtration process
AU6257000A (en) 1999-07-29 2001-02-19 Zenon Environmental Inc. Chemical cleaning backwash for immersed filtering membranes
US20010052494A1 (en) 1999-10-25 2001-12-20 Pierre Cote Chemical cleaning backwash for normally immersed membranes
US20040007525A1 (en) 1999-07-30 2004-01-15 Rabie Hamid R. Maintenance cleaning for membranes
FR2797198B1 (en) 1999-08-04 2002-05-03 Tami Ind MEMBRANE FOR TANGENTIAL FILTRATION AND ITS MANUFACTURING METHOD
DE19940994B4 (en) 1999-08-28 2004-02-26 Clausthaler Umwelttechnikinstitut Gmbh, (Cutec-Institut) Process for the removal of sewage sludge
US6214231B1 (en) 1999-08-27 2001-04-10 Zenon Environmental Inc. System for operation of multiple membrane filtration assemblies
JP2001070967A (en) 1999-09-02 2001-03-21 Asahi Kasei Corp Cleaning system for laundry waste water
JP2001079366A (en) 1999-09-10 2001-03-27 Asahi Kasei Corp Method for washing membrane
JP3603692B2 (en) 1999-09-14 2004-12-22 日立プラント建設株式会社 Membrane separation method and apparatus
US6468472B1 (en) 1999-09-16 2002-10-22 Metrex Research Corporation Cleaning and decontaminating dialyzers by per-compound solutions
US6589426B1 (en) 1999-09-29 2003-07-08 Zenon Environmental Inc. Ultrafiltration and microfiltration module and system
US6361695B1 (en) 1999-10-02 2002-03-26 Zenon Environmental Inc. Shipboard wastewater treatment system
JP2001104760A (en) 1999-10-05 2001-04-17 Mitsubishi Heavy Ind Ltd Immersion type membrane filtration apparatus and method for washing filtration membrane
JP4384310B2 (en) 1999-10-22 2009-12-16 メタウォーター株式会社 Membrane cleaning method
NL1013465C2 (en) 1999-11-02 2001-05-03 Stork Friesland Bv Membrane filtration element with sleeve element and sleeve members.
US6623643B2 (en) 1999-11-19 2003-09-23 Microtek Medical Holdings, Inc. Process for treatment of aqueous environments containing a water soluble polymer
US6861001B2 (en) 1999-12-02 2005-03-01 The General Hospital Corporation Methods for removal, purification, and concentration of viruses, and methods of therapy based thereupon
US6423784B1 (en) 1999-12-15 2002-07-23 3M Innovative Properties Company Acid functional fluoropolymer membranes and method of manufacture
FR2802444B1 (en) 1999-12-16 2002-06-14 Polymen HOLLOW FIBER WATER FILTRATION MODULE
ES2236027T3 (en) 1999-12-17 2005-07-16 Millipore Corporation ENCAPSULATED OF HOLLOW FIBERS WRAPPED IN SPIRAL.
US6324898B1 (en) 1999-12-21 2001-12-04 Zenon Environmental Inc. Method and apparatus for testing the integrity of filtering membranes
JP2001179060A (en) 1999-12-27 2001-07-03 Maezawa Ind Inc Internal pressure type membrane treatment device
JP2001179059A (en) 1999-12-27 2001-07-03 Japan Organo Co Ltd Filter of pathogenic microorganism
JP3729130B2 (en) 1999-12-28 2005-12-21 等 金澤 Method for modifying polymer material and use thereof
US6315895B1 (en) 1999-12-30 2001-11-13 Nephros, Inc. Dual-stage hemodiafiltration cartridge
US6635179B1 (en) 1999-12-30 2003-10-21 Nephros, Inc. Sterile fluid filtration cartridge and method for using same
JP2001190937A (en) 2000-01-06 2001-07-17 Sumitomo Heavy Ind Ltd Water purification equipment and method of cleaning membrane element
JP2001190938A (en) 2000-01-11 2001-07-17 Miura Co Ltd Method of detecting breakage of water treating membrane
JP2001205055A (en) 2000-01-31 2001-07-31 Daicel Chem Ind Ltd Method for operating membrane separation apparatus and apparatus therefor
JP2001212587A (en) 2000-02-04 2001-08-07 Kubota Corp Method and apparatus for diffusing air of membrane separation activated sludge method
JP2001232160A (en) 2000-02-21 2001-08-28 Hitachi Plant Eng & Constr Co Ltd Membrane filter
USD478913S1 (en) 2000-02-24 2003-08-26 Usf Filtration And Separations Group, Inc. Manifold header
GB0004921D0 (en) 2000-03-02 2000-04-19 Waterleau Global Water Technol System for sustainable treatment of municipal and industrial wastewater
US6440303B2 (en) 2000-03-02 2002-08-27 Chapin Manufacturing, Inc. Fluid filter
US6926829B2 (en) 2000-03-06 2005-08-09 Kvaerner Process Systems A.S. Apparatus and method for separating fluids through a membrane
EP1423338B1 (en) 2000-03-08 2007-01-24 Zenon Technology Partnership Reaktor with membrane module for gas transfer and membrane supported biofilm process
US6875357B1 (en) 2000-03-15 2005-04-05 Aqua-Aerobic Systems, Inc. Process and apparatus for treatment of waste water
US6299775B1 (en) 2000-03-17 2001-10-09 Clint R. Elston Waste and wastewater treatment and recycling system
JP4527232B2 (en) 2000-03-28 2010-08-18 旭化成ケミカルズ株式会社 Rack type filter
AUPQ680100A0 (en) 2000-04-10 2000-05-11 Usf Filtration And Separations Group Inc. Hollow fibre restraining system
US6337018B1 (en) 2000-04-17 2002-01-08 The Dow Chemical Company Composite membrane and method for making the same
US6936085B2 (en) 2000-05-10 2005-08-30 Demarco Maxvac Corporation Vacuum loader
EP1156015A1 (en) 2000-05-15 2001-11-21 VA TECH WABAG ESMIL GmbH Process and plant for filtrate generation from the stream of recycled sludge
AU142387S (en) 2000-05-31 2000-11-27 Evoqua Water Tech Llc Manifold header cap
EP1166871A1 (en) 2000-06-21 2002-01-02 Fuji Photo Film B.V. Photocalytic sheet of film and its manufacturing process
JP2002011472A (en) 2000-06-28 2002-01-15 Nishihara Environ Sanit Res Corp Immersed membrane separation apparatus
EP1299170B1 (en) 2000-06-29 2010-08-11 BioGasol IPR ApS Method for withdrawing and filtering partial volumes of process fluid
CA2415580C (en) 2000-07-10 2006-07-04 Asahi Kasei Kabushiki Kaisha Hollow thread film cartridge, hollow thread film module using the cartridge, and tank type filter
EP1174177A3 (en) 2000-07-18 2002-12-04 Nitto Denko Corporation Spiral wound membrane element, spiral wound membrane module and treatment system employing the same as well as running method and washing method therefor
US6517723B1 (en) 2000-07-27 2003-02-11 Ch2M Hill, Inc. Method and apparatus for treating wastewater using membrane filters
US20030038075A1 (en) 2000-08-02 2003-02-27 Tatsuo Akimoto Hollow yarn membrane module, hollow yarn membrane module unit, and method of producing hollow yarn membrane modules
JP2002058968A (en) 2000-08-18 2002-02-26 Suehiro Tadashi Filter
JP2002143849A (en) 2000-08-31 2002-05-21 Toray Ind Inc Method for producing water
DE10045227C1 (en) 2000-09-13 2002-02-07 Vosenkaul Klaus Membrane filter for water treatment uses capillary membrane fibre bundle projecting into untreated water and fitting into permeate collection space at opposite end
FR2814454B1 (en) 2000-09-27 2002-12-20 Degremont PROCESS FOR THE PURIFICATION OF WASTEWATER FOR THE ELIMINATION OF NITROGEN AND PHOSPHATE POLLUTIONS
AT408955B (en) 2000-09-28 2002-04-25 Va Tech Wabag Gmbh MEMBRANE FILTER SYSTEM AND METHOD FOR FILTERING
US6555002B2 (en) 2000-10-06 2003-04-29 Premier Wastwater International, Llc Apparatus and method for wastewater treatment with enhanced solids reduction (ESR)
AUPR064800A0 (en) 2000-10-09 2000-11-02 Usf Filtration And Separations Group Inc. Improved membrane filtration system
AUPR094600A0 (en) 2000-10-23 2000-11-16 Usf Filtration And Separations Group Inc. Fibre membrane arrangement
AUPR143400A0 (en) 2000-11-13 2000-12-07 Usf Filtration And Separations Group Inc. Modified membranes
FR2816851B1 (en) 2000-11-20 2003-09-26 Aquasource IMPROVEMENTS IN PROCESSES FOR REPAIRING THE BLOCKED FIBERS OF THE MEMBRANES, IN PARTICULAR OF ULTRA-, NANO- AND HYPER-FILTRATION
US6525064B1 (en) 2000-12-08 2003-02-25 3M Innovative Properties Company Sulfonamido substituted imidazopyridines
FR2817768B1 (en) 2000-12-13 2003-08-29 Lyonnaise Eaux Eclairage METHOD FOR REGULATING A MEMBRANE FILTRATION SYSTEM
JP4382275B2 (en) 2000-12-15 2009-12-09 前澤工業株式会社 Membrane module cleaning method
NO318619B1 (en) 2000-12-29 2005-04-18 Norsk Hydro As Device for combustion of a carbonaceous fuel, a method for operating said device, and use of said device.
GB0100647D0 (en) 2001-01-10 2001-02-21 Walker Filtration Ltd Filter unit
CA2434940A1 (en) 2001-01-23 2002-08-01 Attila Herczeg Asymmetric hollow fiber membranes
KR20020067227A (en) 2001-02-16 2002-08-22 (주)경동이엔씨 Air lifting pipe and waste or polluted water disposal plant
KR200232145Y1 (en) 2001-02-16 2001-07-19 (주)경동이엔씨 Air lifting pipe and waste or polluted water disposal plant
EP1363857A2 (en) 2001-02-23 2003-11-26 V.A.I. Ltd. Methods and apparatus for biological treatment of waste waters
ITMI20010421A1 (en) 2001-03-01 2002-09-02 Ausimont Spa SEMI-PERMEABLE SEMI-CRYSTALLINE FLUOROPOLYMER Porous MEMBRANES
JP3561690B2 (en) 2001-03-05 2004-09-02 三洋電機株式会社 Filtration system
EP1281432A4 (en) 2001-03-08 2005-07-27 Toray Industries Hollow fiber membrane, hollow fiber membrane module, and water purifier
AUPR421501A0 (en) 2001-04-04 2001-05-03 U.S. Filter Wastewater Group, Inc. Potting method
KR20040020053A (en) 2001-04-18 2004-03-06 버디 돈 그레이 Method and apparatus for a recirculating tangential separation system
US6757059B2 (en) 2001-04-30 2004-06-29 Therma-Wave, Inc. Wafer chuck with integrated reference sample
JP4689074B2 (en) 2001-05-17 2011-05-25 オルガノ株式会社 Filtration device
US6805806B2 (en) 2001-06-12 2004-10-19 Hydrotreat, Inc. Method and apparatus for treatment of wastewater employing membrane bioreactors
AUPR584301A0 (en) 2001-06-20 2001-07-12 U.S. Filter Wastewater Group, Inc. Membrane polymer compositions
CA2351272C (en) 2001-06-22 2009-09-15 Petro Sep International Ltd. Membrane-assisted fluid separation apparatus and method
FR2827360B1 (en) 2001-07-11 2005-10-28 Valeo Thermique Moteur Sa CONTROL VALVE FOR A FLUID CIRCUIT CIRCUIT, ESPECIALLY FOR A COOLING CIRCUIT OF AN ENGINE
JP2003024751A (en) 2001-07-11 2003-01-28 Asahi Kasei Corp Hollow fiber membrane cartridge
US6702561B2 (en) 2001-07-12 2004-03-09 Nxstage Medical, Inc. Devices for potting a filter for blood processing
JP4360057B2 (en) 2001-08-06 2009-11-11 株式会社ジーエス・ユアサコーポレーション Immersion membrane filtration apparatus and immersion membrane filtration method
JP4860843B2 (en) 2001-08-09 2012-01-25 旭化成ケミカルズ株式会社 External pressure type hollow fiber membrane module
AUPR692401A0 (en) 2001-08-09 2001-08-30 U.S. Filter Wastewater Group, Inc. Method of cleaning membrane modules
JP2003053160A (en) 2001-08-14 2003-02-25 Mitsubishi Rayon Co Ltd Cleaning method for separating membrane and membrane filtrater
JP2003062436A (en) 2001-08-23 2003-03-04 Toray Ind Inc Method for manufacturing hollow fiber membrane module
US6592762B2 (en) 2001-08-29 2003-07-15 United States Filter Corporation Process for treating BOD-containing wastewater
JP3548736B2 (en) 2001-09-03 2004-07-28 住友重機械工業株式会社 Backwashing method of separation membrane
TW536424B (en) 2001-09-05 2003-06-11 Mitsubishi Rayon Co Water-clean cartridge, water-cleaner, and washing method of water-cleaner
AUPR774201A0 (en) 2001-09-18 2001-10-11 U.S. Filter Wastewater Group, Inc. High solids module
US6721529B2 (en) 2001-09-21 2004-04-13 Nexpress Solutions Llc Release agent donor member having fluorocarbon thermoplastic random copolymer overcoat
US6673210B2 (en) 2001-09-27 2004-01-06 Voith Paper Patent Gmbh Cleaning a semipermeable membrane in a papermaking machine
KR100441208B1 (en) 2001-10-24 2004-07-22 삼성엔지니어링 주식회사 Batch style waste water treatment apparatus using biological filtering process and waste water treatment method using the same
KR20030033812A (en) 2001-10-25 2003-05-01 주식회사 제오텍 A Treatment Process For Livestock Wastewater
JP3908939B2 (en) 2001-11-02 2007-04-25 三菱レイヨン株式会社 Method for producing hollow fiber membrane module
EP1312408B1 (en) 2001-11-16 2006-07-19 US Filter Wastewater Group, Inc. Method of cleaning membranes
US6761826B2 (en) 2001-11-30 2004-07-13 New Star Lasers, Inc. Pulsed blackbody radiation flux enhancement
US6790912B2 (en) 2001-12-11 2004-09-14 3M Innovative Properties Company Extrudable fluoropolymer blends
DE10161095C1 (en) 2001-12-12 2002-11-07 Klaus Vosenkaul Process for membrane filtration of liquids e.g. water, uses fiber bundle of capillary membranes having one end cast in headpiece open to permeate collecting chamber of the headpiece and a freely moving closed end
JP2003181247A (en) 2001-12-17 2003-07-02 Nitto Denko Corp Treatment system having spiral membrane element and its operating method
JP2003190976A (en) 2001-12-27 2003-07-08 Toray Ind Inc Apparatus and method for treating wastewater
CA2472490A1 (en) 2002-01-02 2003-07-24 Triple I Module with self-supporting sheet membranes
ATE508988T1 (en) 2002-01-07 2011-05-15 Berliner Wasserbetr E BIOLOGICAL WATER TREATMENT WHICH INCLUDES POST-DENITRIFICATION AND A MEMBRANE FILTER
EP1463578B1 (en) 2002-01-09 2011-09-28 Hydranautics Method for cleaning a filtration membrane module with hollow fiber membranes
KR100419259B1 (en) 2002-01-10 2004-02-21 주식회사 제닉스엔지니어링 Wastewater Treatment Method Using Membrane Bioreactor With Reduced Sludge Production
US6712970B1 (en) 2002-01-11 2004-03-30 Enviroquip, Inc. Sewage treatment process with phosphorus removal
US6890435B2 (en) 2002-01-28 2005-05-10 Koch Membrane Systems Hollow fiber microfiltration membranes and a method of making these membranes
KR100459986B1 (en) 2002-02-05 2004-12-04 강용태 Advanced Step Aeration with Media(ASA, SFC-Biofilter)
US7247238B2 (en) 2002-02-12 2007-07-24 Siemens Water Technologies Corp. Poly(ethylene chlorotrifluoroethylene) membranes
AUPS046602A0 (en) 2002-02-12 2002-03-07 U.S. Filter Wastewater Group, Inc. Halar membranes
DE10209170C1 (en) 2002-03-01 2003-08-07 Horst Chmiel Mechanically cleaning hollow fiber membranes comprises forming hollow fibers into bundles, vertically joining together on their opposite-lying ends, and grasping in center to set at angle
JP4173969B2 (en) 2002-03-14 2008-10-29 旭化成クラレメディカル株式会社 Hemodialysis filter and hemodiafiltration device
JP2003266072A (en) 2002-03-18 2003-09-24 Japan Organo Co Ltd Membrane filtration method
JP2003275759A (en) 2002-03-20 2003-09-30 Hitachi Plant Eng & Constr Co Ltd Water treatment device
JP3744447B2 (en) 2002-03-20 2006-02-08 日立プラント建設株式会社 Membrane separator
US6811696B2 (en) 2002-04-12 2004-11-02 Pall Corporation Hydrophobic membrane materials for filter venting applications
US7186344B2 (en) 2002-04-17 2007-03-06 Water Visions International, Inc. Membrane based fluid treatment systems
NL1020491C2 (en) 2002-04-26 2003-10-28 Norit Membraan Tech Bv Measuring integrity of filter membrane, comprises creating volume of gas on filtrate side, increasing pressure on feed side to create pressure drop and measuring increase in pressure on filtrate side
US8668779B2 (en) 2002-04-30 2014-03-11 Nalco Company Method of simultaneously cleaning and disinfecting industrial water systems
US6869534B2 (en) 2002-05-05 2005-03-22 Brentwood Industries, Inc. Sludge digestion methods and apparatus
US6706185B2 (en) 2002-05-22 2004-03-16 Kurita Water Industries Ltd. Biological method of phosphorus removal and biological phosphorus-removing apparatus
JP2003340250A (en) 2002-05-27 2003-12-02 Kurita Water Ind Ltd Membrane separation device
JP4530245B2 (en) 2002-06-10 2010-08-25 旭化成ケミカルズ株式会社 Membrane separator
US6863816B2 (en) 2002-06-17 2005-03-08 Dharma Living Systems, Inc. Tidal vertical flow wastewater treatment system and method
US6743362B1 (en) 2002-06-17 2004-06-01 Enviroquip Inc. Sewage treatment process
AUPS300602A0 (en) 2002-06-18 2002-07-11 U.S. Filter Wastewater Group, Inc. Methods of minimising the effect of integrity loss in hollow fibre membrane modules
KR100471419B1 (en) 2002-06-19 2005-02-21 김석기 Apparatus for treating sewage
US6994867B1 (en) 2002-06-21 2006-02-07 Advanced Cardiovascular Systems, Inc. Biocompatible carrier containing L-arginine
AU2003247229B2 (en) 2002-06-28 2009-04-30 Nederlandse Organisatie Voor Toegepast-Natuurwetenschappelijk Onderzoek Tno Process for cleaning filters
KR200295350Y1 (en) 2002-08-07 2002-11-21 서봉리사이클링(주) Sludge discharger using lumped air
JP2004073950A (en) 2002-08-13 2004-03-11 Asahi Kasei Chemicals Corp Membrane washing method
AU2002950934A0 (en) 2002-08-21 2002-09-12 U. S. Filter Wastewater Group, Inc. Aeration method
US20040035770A1 (en) 2002-08-26 2004-02-26 Edwards Haskell L. Dynamically responsive aerobic to anoxic inter-zone flow control system for single vessel multi-zone bioreactor wastewater treatment plants
WO2004024304A2 (en) 2002-09-13 2004-03-25 Pall Corporation Systems and methods for cleaning hollow fiber membranes
EP1551535B1 (en) 2002-10-10 2012-01-25 Siemens Industry, Inc. Membrane filter and backwash method for it
KR100412330B1 (en) 2002-10-25 2004-01-07 주식회사 진우환경기술연구소 Membrane Coupled Activated Sludge Method Operating Anoxic/Anaerobic Zone alternatively for Removal of Nitrogen and Phosphorus
FR2847572B1 (en) 2002-11-22 2006-04-21 Omnium Traitement Valorisa METHOD OF TREATING WATER USING INORGANIC HIGH SPECIFIC SURFACE PULVERULENT REAGENT INCLUDING A RECYCLING STAGE OF SAID REAGENT
US6863817B2 (en) 2002-12-05 2005-03-08 Zenon Environmental Inc. Membrane bioreactor, process and aerator
AU2002953111A0 (en) 2002-12-05 2002-12-19 U. S. Filter Wastewater Group, Inc. Mixing chamber
US7531042B2 (en) 2002-12-19 2009-05-12 Hydranautics Methods for cleaning and maintaining membrane surface during filtration
JP4211400B2 (en) 2003-01-14 2009-01-21 三浦工業株式会社 Operation method of hollow fiber membrane filtration device
FR2850297B1 (en) 2003-01-29 2005-04-15 Aquasource METHOD FOR MANUFACTURING MEMBRANES FOR FILTRATION MODULES, IN PARTICULAR FOR THE TREATMENT OF WATER
JP2004230280A (en) 2003-01-30 2004-08-19 Toray Ind Inc Production method for hydrophilic polyvinylidene fluoride-based resin porous membrane
JP4042967B2 (en) 2003-01-30 2008-02-06 オルガノ株式会社 Filtration device backwash method
CA2417945A1 (en) 2003-01-31 2004-07-31 Pall Corporation Methods and system for purifying fluids and regenerating purification media
US7014763B2 (en) 2003-02-03 2006-03-21 Aqua-Aerobic Systems, Inc. Multiple barrier biological treatment systems
JP2004249168A (en) 2003-02-18 2004-09-09 Fuji Electric Systems Co Ltd Operation method for water treatment device
EP1452571B1 (en) 2003-02-28 2005-08-17 3M Innovative Properties Company Fluoropolymer dispersion containing no or little low molecular weight fluorinated surfactant
US7087172B2 (en) 2003-03-05 2006-08-08 Usfilter Corporation Methods for reducing nitrate demands in the reduction of dissolved and/or atmospheric sulfides in wastewater
EP1603659A2 (en) 2003-03-14 2005-12-14 Zenon Environmental Inc. Nanofiltration system for water softening with internally staged spiral wound modules
EP1466658A1 (en) 2003-04-11 2004-10-13 UTISOL Technologies AG Device and method for aeration of membrane filters
KR100535301B1 (en) 2003-05-13 2005-12-08 연세대학교 산학협력단 Hollow fiber membrane module and Method for making thereof
JP2004337730A (en) 2003-05-15 2004-12-02 Suido Kiko Kaisha Ltd Method for washing membrane
WO2005005028A1 (en) 2003-07-04 2005-01-20 Akzo Nobel N.V. Cleaning of filtration membranes with peroxides
AU2003903507A0 (en) 2003-07-08 2003-07-24 U. S. Filter Wastewater Group, Inc. Membrane post-treatment
US6946073B2 (en) 2003-09-02 2005-09-20 Ch2M Hill, Inc. Method for treating wastewater in a membrane bioreactor to produce a low phosphorus effluent
EP1663461A4 (en) 2003-07-30 2009-01-14 Phase Inc Filtration system with enhanced cleaning and dynamic fluid separation
FR2858609B1 (en) 2003-08-04 2006-10-13 Otv Sa METHOD AND INSTALLATION FOR BIOLOGICAL TREATMENT OF ACTIVATED SLUDGE WATER WITH AERATION CONTROL
JP4034705B2 (en) 2003-08-27 2008-01-16 株式会社神鋼環境ソリューション Novel microorganism and method for treating organic solid using the microorganism
US8268176B2 (en) 2003-08-29 2012-09-18 Siemens Industry, Inc. Backwash
JP2005087887A (en) 2003-09-17 2005-04-07 Fuji Electric Systems Co Ltd Membrane washing method
SG119706A1 (en) 2003-09-19 2006-03-28 Us Filter Wastewater Group Inc Improved methods of cleaning membrane modules
WO2005028086A1 (en) 2003-09-22 2005-03-31 U.S. Filter Wastewater Group, Inc. Backwash and cleaning method
US7282147B2 (en) 2003-10-07 2007-10-16 Phase Inc. Cleaning hollow core membrane fibers using vibration
WO2005037414A1 (en) 2003-10-20 2005-04-28 Krishnamurthi Rao C H Novel device for submerged ultrafiltration
US20050115899A1 (en) 2003-10-21 2005-06-02 Minggang Liu Membrane bioreactor having single header membrane module
US7879229B2 (en) 2003-10-29 2011-02-01 Zenon Technology Partnership Water treatment plant with immersed membranes
US20070095741A1 (en) * 2003-10-31 2007-05-03 Berends Hendrik Johan F Filter module
CN1235668C (en) 2003-11-06 2006-01-11 上海交通大学 E-Fenton oxidation technique of dirty blocking agent in reverse osmosis concentrating liquid
US7022233B2 (en) 2003-11-07 2006-04-04 Severn Trent Services, Water Purification Solutions, Inc. Biologically active reactor system and method for treating wastewater
US7083733B2 (en) 2003-11-13 2006-08-01 Usfilter Corporation Water treatment system and method
JP2005144291A (en) 2003-11-13 2005-06-09 Ngk Insulators Ltd Method for controlling aeration quantity
CN100421772C (en) 2003-11-14 2008-10-01 西门子水技术公司 Improved module cleaning method
EP1533325B1 (en) 2003-11-17 2011-10-19 3M Innovative Properties Company Aqueous dispersions of polytetrafluoroethylene having a low amount of fluorinated surfactant
JP4533618B2 (en) 2003-11-25 2010-09-01 アムテック株式会社 Disinfectant cleaning composition
US7279215B2 (en) 2003-12-03 2007-10-09 3M Innovative Properties Company Membrane modules and integrated membrane cassettes
KR100558510B1 (en) 2003-12-22 2006-03-07 주식회사 포스코건설 Advanced wastewater treatment apparatus by submerged membrane
WO2005070524A1 (en) 2004-01-09 2005-08-04 Trisep Corporation Filtration with low-fouling, high-flow, low-energy spiral wound membrane cartridges
WO2005073134A1 (en) 2004-02-02 2005-08-11 Kurita Water Industries Ltd. Process for biological treatment of organic waste water and apparatus therefor
US20070056905A1 (en) 2004-02-18 2007-03-15 Beck Thomas W Continuous pressure decay test
US7220358B2 (en) 2004-02-23 2007-05-22 Ecolab Inc. Methods for treating membranes and separation facilities and membrane treatment composition
US20070051679A1 (en) 2004-02-27 2007-03-08 Adams Nicholas W H Water filtration using immersed membranes
WO2005082498A1 (en) 2004-02-27 2005-09-09 Zenon Environmental Inc. Water filtration using immersed membranes
CA2482517A1 (en) 2004-09-24 2006-03-24 Zenon Environmental Inc. Membrane filter cleansing process
US20050194315A1 (en) 2004-02-27 2005-09-08 Adams Nicholas W.H. Membrane batch filtration process
US7311833B2 (en) 2004-03-03 2007-12-25 Kazuo Yamamoto Zero excess sludge membrane bioreactor
US7264725B2 (en) 2004-03-04 2007-09-04 Celgard Inc. Hollow fiber membrane contactor and method of making same
WO2005092799A1 (en) 2004-03-26 2005-10-06 U.S. Filter Wastewater Group, Inc. Process and apparatus for purifying impure water using microfiltration or ultrafiltration in combination with reverse osmosis
JP4508694B2 (en) 2004-03-30 2010-07-21 株式会社クボタ Water treatment method and apparatus
EP2380854A3 (en) 2004-04-22 2012-07-04 Siemens Industry, Inc. Filtration apparatus comprising a membrane bioreactor and a treatment vessel for digesting organic materials
US7122121B1 (en) 2004-05-28 2006-10-17 Jiang Ji Advanced submerged membrane modules, systems and processes
WO2005118117A1 (en) 2004-05-28 2005-12-15 Siemens Water Technologies Corp. Retractable cantilever rack support
WO2006002469A1 (en) 2004-07-02 2006-01-12 U.S. Filter Wastewater Group, Inc Gas transfer membrane
JP3807423B2 (en) 2004-08-12 2006-08-09 栗田工業株式会社 Immersion membrane separator
DE202004012693U1 (en) 2004-08-13 2004-10-14 Enviro-Chemie Gmbh Coupling system for a filter module for filtering liquids by reverse osmosis, microfiltration and ultra- and nano-filtration comprises a connection between a filter module and a tubular system using a tubular coupling on an end region
CA2577137C (en) 2004-08-20 2014-04-22 Siemens Water Technologies Corp. Membrane modules with gas and filtrate conduits and racks formed therefrom
CA2579168C (en) 2004-09-07 2015-06-23 Siemens Water Technologies Corp. Membrane filtration with reduced volume cleaning step
EP1799334B1 (en) 2004-09-14 2013-12-11 Siemens Water Technologies LLC Methods and apparatus for removing solids from a membrane module
CN100548452C (en) 2004-09-15 2009-10-14 西门子水技术公司 The method of incrustation in a kind of membrane filtration system and the control membrane filtration system
US7172699B1 (en) 2004-10-13 2007-02-06 Eimco Water Technologies Llc Energy efficient wastewater treatment for nitrogen and phosphorus removal
US20060081533A1 (en) 2004-10-16 2006-04-20 Khudenko Boris M Batch-continuous process and reactor
JP2006116495A (en) 2004-10-25 2006-05-11 Sumitomo Electric Fine Polymer Inc Filter device
CA2585861A1 (en) 2004-11-02 2006-05-11 Siemens Water Technologies Corp. Membrane filtration module with fluid retaining means
US7591950B2 (en) 2004-11-02 2009-09-22 Siemens Water Technologies Corp. Submerged cross-flow filtration
US7329344B2 (en) 2004-12-22 2008-02-12 Siemens Water Technologies Corp. Grease and scum removal in a filtration apparatus comprising a membrane bioreactor and a treatment vessel for digesting organic materials
WO2006066350A1 (en) 2004-12-24 2006-06-29 Siemens Water Technologies Corp. Simple gas scouring method and apparatus
US8496828B2 (en) 2004-12-24 2013-07-30 Siemens Industry, Inc. Cleaning in membrane filtration systems
NZ556400A (en) 2005-01-14 2011-05-27 Siemens Water Tech Corp Cleaning of membrane filtration system
US7279100B2 (en) 2005-01-31 2007-10-09 Ashbrook Simon-Hartley Operations, Lp Methods and apparatus for treating wastewater employing a high rate clarifier and a membrane
US7501062B2 (en) 2005-02-22 2009-03-10 Shell Oil Company Process for permeation enhanced reactive extraction of levulinic acid
US7507274B2 (en) 2005-03-02 2009-03-24 Velocys, Inc. Separation process using microchannel technology
US7396453B1 (en) 2005-04-19 2008-07-08 Procorp Enterprises, Llc Hydraulically integrated solids/liquid separation system for wastewater treatment
JP2008539054A (en) 2005-04-29 2008-11-13 シーメンス・ウォーター・テクノロジーズ・コーポレイション Chemical cleaning for membrane filters
US7326343B2 (en) 2005-05-03 2008-02-05 University Of Western Ontario Canada Treatment of wastewater containing phosphorous and nitrogen
US7147777B1 (en) 2005-05-09 2006-12-12 Eimco Water Technologies Llc Wastewater treatment system with membrane separators and provision for storm flow conditions
KR101214439B1 (en) 2005-05-25 2012-12-21 에치투엘 주식회사 Immersed hollow fiber membrane module
US20060273038A1 (en) 2005-06-02 2006-12-07 Syed Murtuza A Chemical cleaning for membranes
EP3189885A1 (en) 2005-07-12 2017-07-12 Zenon Technology Partnership Process control for an immersed membrane system
US7850851B2 (en) 2005-08-12 2010-12-14 Siemens Water Technologies Corp. Biological phosphorus removal
EP1945333B1 (en) 2005-08-22 2011-06-08 Siemens Industry, Inc. An assembly for water filtration to minimise backwash volume
US20070045183A1 (en) 2005-08-26 2007-03-01 Murphy Dee T Purified water reclamation process
WO2007044442A2 (en) 2005-10-05 2007-04-19 Siemens Water Technologies Corp. Method and system for treating wastewater
WO2007044415A2 (en) 2005-10-05 2007-04-19 Siemens Water Technologies Corp. Method and apparatus for treating wastewater
US7563363B2 (en) 2005-10-05 2009-07-21 Siemens Water Technologies Corp. System for treating wastewater
US20070095754A1 (en) 2005-10-28 2007-05-03 Dennis Livingston Efficient MBR operation in wastewater treatment
CA2626941A1 (en) 2005-11-08 2007-05-18 Siemens Water Technologies Corp. Combination membrane/biolytic filtration
US7314563B2 (en) 2005-11-14 2008-01-01 Korea Institute Of Science And Technology Membrane coupled activated sludge method and apparatus operating anoxic/anaerobic process alternately for removal of nitrogen and phosphorous
JP4993901B2 (en) * 2005-11-29 2012-08-08 水ing株式会社 Hollow fiber membrane module
CA2629709A1 (en) 2005-12-09 2007-06-14 Siemens Water Technologies Corp. Reduced backwash volume process
WO2007065956A1 (en) 2005-12-09 2007-06-14 Aquafin N.V. Process and installation for treating wastewater
KR100656294B1 (en) 2005-12-19 2006-12-11 연세대학교 산학협력단 Hollow fiber membrane module and method for making thereof
US7147778B1 (en) 2006-01-05 2006-12-12 I. Kruger Inc. Method and system for nitrifying and denitrifying wastewater
US20090001018A1 (en) 2006-01-12 2009-01-01 Fufang Zha Operating Strategies in Filtration Processes
US7455765B2 (en) 2006-01-25 2008-11-25 Siemens Water Technologies Corp. Wastewater treatment system and method
US20100025320A1 (en) 2006-03-22 2010-02-04 Warren Thomas Johnson Backwash and cleaning method
US7510655B2 (en) 2006-04-11 2009-03-31 Siemens Water Technologies Corp. Process to improve the efficiency of a membrane filter activated sludge system
US7481933B2 (en) 2006-04-11 2009-01-27 Siemens Water Technologies Corporation Process to improve the efficiency of a membrane filter activated sludge system
US7713413B2 (en) 2006-04-11 2010-05-11 Siemens Water Technologies Corp. Aerated anoxic membrane bioreactor
FR2901488B1 (en) 2006-05-23 2008-08-15 Otv Sa AERATION DEVICE FOR IMMERSION MEMBRANE-BASED WATER FILTRATION SYSTEM INCLUDING FLOOR WITH GAS INJECTION MEANS AND AT LEAST ONE PRESSURE BALANCING SYSTEM
US7761826B1 (en) 2006-07-24 2010-07-20 Cadence Design Systems, Inc. Method and system for crosstalk analysis
CN101511455B (en) 2006-08-31 2013-07-03 西门子工业公司 Low pressure backwash
DE102006044624B4 (en) 2006-09-19 2008-07-10 Koch Membrane Systems Gmbh Apparatus for fumigating a liquid
FR2909902B1 (en) 2006-12-13 2009-12-25 Otv Sa ULTRAFILTRATION OR MICRO-FILTRATION INSTALLATION AND METHOD OF MAINTAINING SUCH A INSTALLATION
US20100012585A1 (en) 2007-02-16 2010-01-21 Fufang Zha Membrane filtration process and design
US8318028B2 (en) 2007-04-02 2012-11-27 Siemens Industry, Inc. Infiltration/inflow control for membrane bioreactor
CN101652169A (en) 2007-04-04 2010-02-17 西门子水处理技术公司 Membrane module protection
US7459083B1 (en) 2007-05-07 2008-12-02 I. Kruger Inc. Method for controlling fouling of a membrane filter
AU2008251556A1 (en) 2007-05-11 2008-11-20 Zenon Technology Partnership Membrane module with multiple bottom headers and filtration process
US20120285885A1 (en) 2007-05-29 2012-11-15 Siemens Industry, Inc. Membrane cleaning with pulsed gas slugs
DE202008018516U1 (en) 2007-05-29 2015-01-09 Evoqua Water Technologies Llc Membrane cleaning with a pulsed air lift pump
US20100170847A1 (en) 2007-05-29 2010-07-08 Fufang Zha Membrane cleaning using an airlift pump
WO2009000035A1 (en) 2007-06-28 2008-12-31 Siemens Water Technologies Corp. Cleaning method for simple filtration systems
DE102007041991A1 (en) 2007-09-05 2009-03-12 Fülling, Rainer, Dr. Process for the purification of substrates by oxidants and reducing agents and the use of oxidizing agents for the oxidation of extracellular polymeric substances
JP5362343B2 (en) 2008-01-11 2013-12-11 旭化成ケミカルズ株式会社 Membrane separation unit
US7540957B1 (en) 2008-03-21 2009-06-02 Pentair Filtration, Inc. Modular drinking water filtration system with bottom load cartridges with grip-enhanced end rings and color coding
JP5359872B2 (en) * 2008-07-01 2013-12-04 東レ株式会社 Immersion type hollow fiber membrane module
CN106064021B (en) 2008-07-24 2019-06-04 懿华水处理技术有限责任公司 Frame system for film filter module
EP2313172A4 (en) 2008-08-14 2013-03-13 Siemens Industry Inc Block configuration for large scale membrane distillation
AU2009282912B2 (en) 2008-08-20 2014-11-27 Evoqua Water Technologies Llc Improved membrane system backwash energy efficiency
EP2437870A1 (en) 2009-06-02 2012-04-11 Siemens Industry, Inc. Membrane cleaning with pulsed gas slugs and global aeration
AU2010257526A1 (en) 2009-06-11 2012-01-12 Siemens Industry, Inc Methods for cleaning a porous polymeric membrane and a kit for cleaning a porous polymeric membrane
US20110049048A1 (en) 2009-09-03 2011-03-03 General Electric Company Water purification system
US9358505B2 (en) 2009-09-03 2016-06-07 General Electric Company Gas sparger for an immersed membrane
HUE045642T2 (en) 2010-04-30 2020-01-28 Evoqua Water Tech Llc Fluid flow distribution device
WO2012040412A1 (en) 2010-09-24 2012-03-29 Siemens Industry, Inc. Fluid control manifold for membrane filtration system
US9364805B2 (en) 2010-10-15 2016-06-14 General Electric Company Integrated gas sparger for an immersed membrane

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20040178136A1 (en) * 2001-11-05 2004-09-16 Tohru Taniguchi Hollow fiber membrane module
WO2010140857A2 (en) * 2009-06-05 2010-12-09 Kolon Industries, Inc. Module case and hollow fiber membrane module using the same

Also Published As

Publication number Publication date
AU2013231145B2 (en) 2017-08-17
US20140084511A1 (en) 2014-03-27
AU2013231145A1 (en) 2014-04-10
US9962865B2 (en) 2018-05-08

Similar Documents

Publication Publication Date Title
US10207226B2 (en) Cartridge-type hollow fiber membrane module and method for manufacturing cartridge-type hollow fiber membrane module
KR102164846B1 (en) Cartridge type hollow fiber membrane module
US20180250853A1 (en) Membrane Potting Methods
US8679337B2 (en) Hollow fiber membrane module with covered membrane outer periphery
WO2011105495A1 (en) Header member, membrane module, and method for manufacturing membrane module
US5472601A (en) Hollow fiber filter
US10350549B2 (en) Hollow fiber membrane module and method for manufacturing hollow fiber membrane module
KR102551102B1 (en) Hollow fiber membrane module and manufacturing method of the hollow fiber membrane module
CN103842058A (en) Method for hydrophilizing hollow-fiber membrane module
US11364469B2 (en) Hollow fiber membrane module and filtering method
CA2101829A1 (en) Hollow fiber permeator with tubesheet preform
KR101790974B1 (en) Method for potting hollow fiber membrane using expandable device
CN112469495B (en) Hollow fiber membrane module and method for manufacturing hollow fiber membrane module
JP5385523B2 (en) Method for manufacturing separation membrane module
JP2019025420A (en) Hollow fiber membrane module and production method of hollow fiber membrane module
JP2011161313A (en) Method for manufacturing hollow fiber membrane module

Legal Events

Date Code Title Description
STPP Information on status: patent application and granting procedure in general

Free format text: DOCKETED NEW CASE - READY FOR EXAMINATION

STPP Information on status: patent application and granting procedure in general

Free format text: NON FINAL ACTION MAILED

STPP Information on status: patent application and granting procedure in general

Free format text: NON FINAL ACTION MAILED

STCB Information on status: application discontinuation

Free format text: ABANDONED -- FAILURE TO RESPOND TO AN OFFICE ACTION