NZ202711A - Profiled semipermeable membrane - Google Patents
Profiled semipermeable membraneInfo
- Publication number
- NZ202711A NZ202711A NZ202711A NZ20271182A NZ202711A NZ 202711 A NZ202711 A NZ 202711A NZ 202711 A NZ202711 A NZ 202711A NZ 20271182 A NZ20271182 A NZ 20271182A NZ 202711 A NZ202711 A NZ 202711A
- Authority
- NZ
- New Zealand
- Prior art keywords
- membrane
- film
- profile
- profiling
- imparting elements
- Prior art date
Links
- 239000012528 membrane Substances 0.000 title claims description 122
- 239000000463 material Substances 0.000 claims description 38
- 239000007788 liquid Substances 0.000 claims description 30
- 238000004519 manufacturing process Methods 0.000 claims description 18
- 230000015572 biosynthetic process Effects 0.000 claims description 9
- 239000000758 substrate Substances 0.000 claims description 9
- 238000000034 method Methods 0.000 claims description 7
- 239000000853 adhesive Substances 0.000 claims description 6
- 230000001070 adhesive effect Effects 0.000 claims description 6
- 239000012815 thermoplastic material Substances 0.000 claims description 6
- 238000005345 coagulation Methods 0.000 claims description 5
- 230000015271 coagulation Effects 0.000 claims description 5
- 230000009969 flowable effect Effects 0.000 claims description 5
- 229920001169 thermoplastic Polymers 0.000 claims description 4
- 239000004416 thermosoftening plastic Substances 0.000 claims description 4
- 238000001125 extrusion Methods 0.000 claims description 3
- 239000012530 fluid Substances 0.000 claims description 2
- 230000001788 irregular Effects 0.000 claims description 2
- 238000009987 spinning Methods 0.000 claims description 2
- 238000007711 solidification Methods 0.000 claims 1
- 230000008023 solidification Effects 0.000 claims 1
- 125000006850 spacer group Chemical group 0.000 description 9
- -1 for example Polymers 0.000 description 7
- 239000000203 mixture Substances 0.000 description 7
- 238000000614 phase inversion technique Methods 0.000 description 5
- 239000004698 Polyethylene Substances 0.000 description 3
- 238000013459 approach Methods 0.000 description 3
- 230000010287 polarization Effects 0.000 description 3
- 229920000573 polyethylene Polymers 0.000 description 3
- 239000004952 Polyamide Substances 0.000 description 2
- 239000004743 Polypropylene Substances 0.000 description 2
- 230000002745 absorbent Effects 0.000 description 2
- 239000002250 absorbent Substances 0.000 description 2
- 229920001577 copolymer Polymers 0.000 description 2
- 239000004744 fabric Substances 0.000 description 2
- 229920002647 polyamide Polymers 0.000 description 2
- 229920000642 polymer Polymers 0.000 description 2
- 229920001155 polypropylene Polymers 0.000 description 2
- 239000004627 regenerated cellulose Substances 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- NIXOWILDQLNWCW-UHFFFAOYSA-N Acrylic acid Chemical class OC(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 1
- IMROMDMJAWUWLK-UHFFFAOYSA-N Ethenol Chemical compound OC=C IMROMDMJAWUWLK-UHFFFAOYSA-N 0.000 description 1
- CERQOIWHTDAKMF-UHFFFAOYSA-N Methacrylic acid Chemical compound CC(=C)C(O)=O CERQOIWHTDAKMF-UHFFFAOYSA-N 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 229920001400 block copolymer Polymers 0.000 description 1
- 150000001720 carbohydrates Chemical class 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- 229920002301 cellulose acetate Polymers 0.000 description 1
- 229920003086 cellulose ether Polymers 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- 239000013505 freshwater Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000000499 gel Substances 0.000 description 1
- 238000003780 insertion Methods 0.000 description 1
- 230000037431 insertion Effects 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 150000002825 nitriles Chemical class 0.000 description 1
- 229920000620 organic polymer Polymers 0.000 description 1
- 239000012466 permeate Substances 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 229920002492 poly(sulfone) Polymers 0.000 description 1
- 229920000515 polycarbonate Polymers 0.000 description 1
- 239000004417 polycarbonate Substances 0.000 description 1
- 229920000728 polyester Polymers 0.000 description 1
- 229920001184 polypeptide Polymers 0.000 description 1
- 229920002635 polyurethane Polymers 0.000 description 1
- 239000004814 polyurethane Substances 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 102000004196 processed proteins & peptides Human genes 0.000 description 1
- 108090000765 processed proteins & peptides Proteins 0.000 description 1
- 102000004169 proteins and genes Human genes 0.000 description 1
- 108090000623 proteins and genes Proteins 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000013535 sea water Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 239000001993 wax Substances 0.000 description 1
- 238000004804 winding Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
- B01D69/06—Flat membranes
- B01D69/061—Membrane bags or membrane cushions
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
- B01D69/06—Flat membranes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/22—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by diffusion
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D63/00—Apparatus in general for separation processes using semi-permeable membranes
- B01D63/08—Flat membrane modules
- B01D63/082—Flat membrane modules comprising a stack of flat membranes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D63/00—Apparatus in general for separation processes using semi-permeable membranes
- B01D63/10—Spiral-wound membrane modules
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D65/00—Accessories or auxiliary operations, in general, for separation processes or apparatus using semi-permeable membranes
- B01D65/08—Prevention of membrane fouling or of concentration polarisation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
- B01D69/10—Supported membranes; Membrane supports
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
- B01D69/10—Supported membranes; Membrane supports
- B01D69/107—Organic support material
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2313/00—Details relating to membrane modules or apparatus
- B01D2313/14—Specific spacers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2321/00—Details relating to membrane cleaning, regeneration, sterilization or to the prevention of fouling
- B01D2321/20—By influencing the flow
- B01D2321/2008—By influencing the flow statically
- B01D2321/2016—Static mixers; Turbulence generators
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2325/00—Details relating to properties of membranes
- B01D2325/08—Patterned membranes
Description
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Priori^ Oo-fes _; , , 7.'!^.'^
Complete Specification .FitediA"; 7f?~
Ctass:
Pv&lioatson Date: ... ft ?."iUk 1^.5 #,. P-& Joufftaf. No: .... JP:7.'........
N.Z. No.
NEW ZEALAND
Patents Act 1953
COMPLETE SPECIFICATION
"FILM FOR SEPARATING MULTICOMPONENT LIQUID OR GASEOUS SYSTEMS."
We, HOECHST AKTIENGESELLSCHAFT, a corporation organized under the laws of the Federal Republic of Germany,of D-6230 Frankfurt/Main 80, Federal Republic of Germany,
do hereby declare the invention, for which we pray that a Patent may be granted to us, and the ;method by which it is to be performed,to be particularly described in and by the following statement
(Followed by 1A.)
- ifi-
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FILM FOR SEPARATING MULTICOMPONENT LIQUID OK GASEOUS SYSTEMS
BACKGROUND OF THE INVENTION
The present invention relates to a film 5 which has the function of separating a component or portions of a component from solutions or other liquid or gaseous multicomponent systems.
It is already known to use semipermeable membranes for separating individual components from 10 various liquid mixtures, in particular from solutions. Thus, for example, semipermeable membranes are used for separating liquid components from a mixture of liquids, for separating gaseous components from a mixture of gases and for separating liquid solvents 15 from a mixture containing these solvents and a material dissolved therein. Such separation processes are becoming increasingly more important, especially in connection with producing fresh water from seawater and other sources of salt-containing 20 water.
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The material from which these semipermeable membranes have been made is usually an organic polymer, such as, for example, cellulose acetate. However, a membrane of such material must be constructed 5 to be very thin and therefore has only a low tensile strength. To protect the structurally weak membrane materials against deformation or damage through hydraulic pressure or mechanical action, it is therefore customary to provide these materials with a 10 carrier or support material. Examples of support materials of this type have been described in British" Patent No. 1,595,299, and they usually consist of a porous, but solid, fabric-like material.
U.S. Patent No. 3,950,255 and U.S. Patent No. 3,894,166 15 disclose additional semipermeable membranes and processes for their preparation.
In the separation of liquid components from mixtures of liquids, the total surface area of the membrane which comes into contact with the 20 amount of liquid supplied is one of the operating parameters and affects the throughput quantity obtainable. In order to obtain a membrane surface area which is as large as possible per unit of volume, numerous devices have been described 25 which contain membrane stacks, membrane bags or tubes wound from membrane materials.
U.S. Patent No. 3,367,504 and U.S. Patent No. 3,397,790 describe, for example, spiral-shaped membrane separating devices. 30 However, the surface area of the membrane utilized is not the sole critical factor for the design of a membrane separating device, but in addition the type of flow over the membrane surface must be taken into consideration in this type
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of device as a second parameter. Optimally guided currents prevent deposits on the membrane which can cause blockages, lower to a minimum the concentration polarization on the active membrane layer and 5 ensure maximum permeation. In order to form current paths by which the liquid can approach the membrane, spacers are therefore introduced into layered or wound membrane separating devices. Such spacers: are described, for example, in British Patent 10 No. 2,000,694. . .
All these known designs, which are in the form of layers or are wound in the shape of spirals, have in common that they use membrane films having smooth planar surfaces and that these films are 15 combined with wide-meshed fabric-like spacers to ensure that the liquid approaches the membrane surface. In the known designs, such a spacer not only has a spacing function, but in addition it also acts as a flow breaker and turbulence promoter, 20 because it is a mesh of threads which has voids between the threads and enlargements at their points of intersection. On the one hand, the turbulences indeed reduce the tendency for deposits to build up on the membrane, but, on the other hand, 25 dead zones are formed where the flow is insufficiently high, and the entire device has a relatively high flow resistance. A uniform laminar flow, which favors the prevention of concentration polarization, can therefore not be achieved in the known combina-30 tion of smooth membranes and fabric-like spacers. The insertion of- the spacer layer also complicates the manufacture of membrane separating devices which have a spiral or layer structure, and hence increases the manufacturing costs.
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Another way of producing flow paths in layered or wound membrane separating devices is described in U.S. Patent No. 4,206,050. This document discloses a membrane unit wherein the support 5 layer and the permselective membrane applied thereon have a profile. In this device, a spacer can be dispensed with when arranging the membrane unit in layers or winding it up in the form of a-spiral, since the flow paths between the layers 10 are already predetermined by the profiling of the support material. However, these membrane units are only suitable for specific adsorption processes, for example, in medical applications, and, in addition, relatively large raised areas form in the 15 membrane units thus manufactured, which generally insufficiently reduce concentration polarization in the case of other applications.
SUMMARY OF THE INVENTION
It is therefore an object of the present 20 invention to provide an improved film for separating multicomponent liquid or gaseous systems.
Another object of the invention is to provide such a film which makes it possible to simplify the manufacture of membrane separating devices which 25 are built up in the form of layers or in a spirallike form.
It is also an object of the invention to provide such a film which omits the separate spacer layer.
A further object of the invention resides in providing such a film which simultaneously provides improved flow conditions in the interspaces
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of the membrane layers, and, in so doing, eliminates the disadvantages of support material which has already been profiled.
Another object of the invention resides in providing a process for preparing the film according to the invention.
It is also an object of the invention to provide an improved device for separating multi-component liquid or gaseous systems.
In accomplishing the foregoing objects, there has been provided in accordance with one aspect of the present invention a film suitable for separating multicomponent liquid or gaseous systems, which is comprised of a sheet-like semipermeable membrane having profiling on at least one of its surfaces, and preferably, a support layer to which the semipermeable membrane is applied, the support layer being smooth on both sides and permeable to flowable media, wherein the profiling is on the surface of the film which faces away from the smooth support layer. Most preferably, the profiling is comprised of profile-imparting elements which are firmly bonded to the surface of the membrane layer.
Broadly the invention comprises a film adapted for separating multi-component liquid or gaseous systems, which comprises; a) a sheet-like semipermeable membrane presenting profiling in cross section on at least one of its surfaces; b) means for imparting said profiling to said semipermeable membrane, comprising a plurality of flexible profile-imparting elements, each comprised of extrudable thermoplastic material; and c) a fluid media-permeable, flexible support layer presenting a first and second smooth side, said first smooth side being immediately adjacent to said semipermeable membrane.
In accordance with another aspect of the invention, there has been provided a process for preparing a membrane film which has profiling on its surface comprising the steps of pouring a solution which contains a material capable of membrane formation onto a profiled substrate; and converting the material by phase inversion to produce a membrane having a negative pattern of the profiled substrate on its surface.
Another process for preparing a membrane film which has profiling on its surface comprises '
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the steps of spinning into a coagulation bath a solution which contains a material capable of membrane formation through a die which contains a slot which is delimited on one side by a straight edge 5 and on the other side by an edge with profiling;
and converting the spun material in the coagulation bath by phase inversion to produce a membrane having profiling determined by the profiled die edge on its surface.
• Still another process for preparing a membrane film which has on its surface profiling which is formed by profile-imparting elements, comprises the steps of extruding a thermoplastic material into the form of the profile imparting elements? and 15 applying the profile-imparting elements in the extrusion step to the surface of a membrane in such a way as to firmly bond them to it.
In accordance with yet another aspect of the invention, there has been provided a device 20 for separating multicomponent liquid or gaseous systems, comprising a semipermeable membrane shaped in a spiral-like or layer structure, wherein the semipermeable membrane comprises a film as defined above.
Further objects, features and advantages of the present invention will become apparent to the person skilled in this art from the detailed description of preferred embodiments which follows, when considered together with the attached figures 30 of drawing.
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BRIEF DESCRIPTION OF THE DRAWINGS
In the drawings:
Figure 1 is a cross-sectional view of one embodiment of the film according to the invention;
Figure 2 is a cross-sectional view of *
another embodiment of the film according to the invention; and
Figure 3 is a cross-sectional view of still another embodiment of the film according 10 to the invention.
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DETAILED DESCRIPTION OF PREFERRED EMBODIMENTS
The invention provides a film, in particular a film for separating multicomponent liquid or gaseous systems, which is comprised of a semipermeable membrane which has profiling on its surface.
In one preferred embodiment of the invention, the semipermeable membrane has been applied to a support layer which is smooth on both sides and is permeable to flowable media, and the surface of the film which faces away from the smooth support layer has profiling.
In further particular embodiments of the invention, the profiling is generated by profile-imparting elements which are firmly bonded to the smooth surface of the membrane layer (Figure 1) or are partly embedded in the membrane layer but still project above the membrane layer (Figure 2), or are positionally fixed between the support layer and the membrane layer in such a way that they are adjacent to the support layer and are covered by the membrane layer (Figure 3).
The semipermeable membrane can be comprised of material conventionally used for such purposes, such as, for example, regenerated cellulose, cellulose esters, cellulose ethers, carbohydrate gels, polypeptides, proteins, polyamides, polysulfones, block copolymers with polycarbonate, polymers or copolymers of derivatives of acrylic acid or methacrylic acid, such as nitriles and esters, or polymers or copolymers with vinyl alcohol. The pore size of the semipermeable
-4
membrane is within a range of from about 2 x 10 to 10 ym.
The semipermeable membrane is preferably located
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on a support layer which is permeable to flowable media and which serves to absorb the permeate and to conduct it away. The support layer also serves to strengthen and support the membrane, so that the membrane can be 5 easily handled and so that membrane damage is avoided. However, the semipermeable membrane can also be used equally well without support material.
The support layer is smooth on both sides and is comprised, for example, of paper, a fabric, a web . 10 or a mesh of plastic or metal. Sheets or films made of porous or absorbent material are also suitable as the support layer. They can be comprised, for example, of sintered polyethylene, as well as of absorbent synthetic sponge material, in particular of regenerated cellulose, 15 which is known as a sponge cloth material. Smooth is understood as meaning that each surface extends in a single plane, i.e., does not have projections.
In applications requiring very compact membrane units, the support layer can also be omitted so that 20 only the membrane and the profile-imparting elements are present. The profile-imparting elements are comprised of a material which is capable of forming a permanent bond with the membrane without adversely impairing the latter in its other properties. Extrud-25 able thermoplastics, such as polyamide, polyester, polyethylene or polypropylene, are preferably used. Threads, for example, made of these materials and having a round, triangular, rectangular or polygonal cross-section can be extruded, welded, bonded or other-30 wise fixed onto "the surface of the membrane or, in other embodiments of the invention, these threads can be partially embedded into the membrane layer, or they
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can be present between the support layer and the membrane layer in a positionally fixed manner. The threads can be fixed to the substrate over their entire contact area or only within single discrete zones. The threads 5 can be applied so as to be continuous or interrupted, and the threads can also be comprised of chains of successive point-shaped elevations. Preferably these threads or point chains are arranged parallel to one another, so that when the film is layered or wound,. 10 channels can form through which the mixture to be separated can flow. However, the profile-imparting elements can also be arranged so as to form a crosslike network on the substrate, whereby, if desired, turbulences form in the current, or they can be arranged 15 like curves, or alternatively as only point-like in an irregular distribution over the surface.
The present invention also relates to processes for manufacturing films according to the invention. In a first process, a solution which contains a material 20 capable of membrane formation is poured onto a profiled substrate and converted by the phase inversion method to give the membrane. In the phase inversion method, the liquid layer which contains a material capable of membrane formation is subjected to the 25 action of a precipitation liquid, with the result that the membrane-forming material coagulates. After the liquid has been removed, the membrane is then peeled from the substrate which is provided with profiling, and the profiling is thus obtained at a negative 30 on the membrane surface. The substrate onto which the solution containing the membrane-forming material is poured is called a release material, because it can
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- li -
be used again and again. Support-free profiled membranes are thus obtained.
In a further process for preparing films according to the invention, a solution which contains a material capable of membrane formation is spun through a die having a slot which is delimited on one side by a straight edge and on the other side by an edge- with profiling. The spun profile is passed into a coagulation bath and is converted by the phase inversion method to give the membrane. In this case also, the phase inversion method is carried out in such a way that the liquid is removed after the material capable of membrane formation has coagulated, and a support-free membrane is thus obtained.
If the extrudate is applied from the die directly to a support layer permeable to flowable media and the phase inversion method is then carried out, a film is obtained which is comprised of the membrane layer, which has profiling on its surface and which is located on the support layer.
In a further process for preparing the film according to the invention, profile-imparting elements are applied and firmly bonded to the surface of the membrane which, optionally, can be bonded to a support material. This can take place, for example, in an extrusion process in which the thermoplastic material is extruded as a heat plastified melt, for example,
in the form of a thread, onto the surface of the membrane and becomes firmly bonded to the membrane material on solidifying, or the pre-extruded thermoplastic material of the profiling elements can be fixed onto the surface of the membrane by means of an adhesive. Preferably,
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thermoplastic adhesives are used as the adhesives; these thermoplastic adhesives can be, e.g., polyethylene, polypropylene, or polyurethanes, as well as other known waxes of the synthetic or natural type.
In a further process for preparing films accord ing to the invention, the profile-imparting elements are partially embedded into the still liquid or "partially liquid membrane layer, so that they project sufficiently far to the desired height above the layer, and they 10 thus enter a firm adhesive bond with the membrane layer as it solidifies. The profile-imparting elements used can be either threads or networks; the intersection points of the networks can be knot-like enlargements, so that point-shaped profile-imparting elements are 15 obtained in this manner.
In a further process for preparing films according to the invention, threads which serve as profile-imparting elements are applied directly to the support material and are fixed there, and the semipermeable 20 membrane is then applied in such a way to the resulting profiled surface of the support material that the membrane adapts to the given profiling, with the result that the outer face of the membrane becomes profiled in a corresponding manner.
The film according to the invention can be used for preparing membrane separating devices having a spiral-type or layer structure. Such devices are known in the art, but the film according to the invention has the advantage that, in the construction of known 30 membrane separating devices from this film, it is no longer necessary to incorporate a special spacer layer which enables the mixture to be separated to approach the membrane surface. This advantage is made possible by the profiling according to the invention, which is
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located on the surface of the film and by which the formation of flow channels is achieved when the film is arranged in the form of a spiral or in layers.
The attached drawings are intended to illustrate the invention in more detail. In Figure 1, which is a sectional view of one embodiment of the film according to the invention, the profile-imparting elements 1 are firmly bonded to the surface of the smooth membrane layer 2, which is bonded to a support layer 3. Figure 2 illustrates a sectional view of another embodiment of the film according to the invention, in which the profile-imparting elements 1 are partially embedded in the membrane layer 2 and are firmly bonded to the latter. Finally, Figure 3 is a sectional view of still another embodiment of the film according to the invention, in which the profile-imparting elements 1 are positionally fixed in such a way between the support layer 3 and the membrane layer 2 that they are adjacent to the support layer..
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Claims (21)
1. A film adapted for separating multicomponent liquid or gaseous systems, which comprises; a) a sheet-like semipermeable membrane presenting profiling in cross section on at least one of its surfaces; b) means for imparting said profiling to said semipermeable membrane, comprising a plurality of flexible profile-imparting elements, each comprised of extrudable thermoplastic material; and c) a fluid media-permeable, flexible support layer presenting a first and second smooth side, said first smooth side being immediately adjacent to said semipermeable membrane.
2. A film as claimed in claim 1, wherein the profiling is comprised of said profile-imparting elements which are firmly bonded to the surface of the membrane layer which faces away from said first smooth side.
3. A film as claimed in claim 1, wherein the profiling is comprised of profile-imparting elements which are partially embedded in the membrane layer and are firmly bonded thereto.
4. A film as claimed in claim 1, wherein the profiling is comprised of profile-imparting elements which are positionally fixed in such a way between the support layer and the membrane layer that they are adjacent to the support layer.
5. A film as claimed in claim 2, wherein the profile-imparting elements are comprised of threads which have a round or polygonal cross-section and which are arranged parallel to one another.
6. A film as claimed in claim 5, wherein the threads serving as profile-imparting elements are arranged parallel to the direction of flow of the liquid or gas. 202711
7. A film as claimed in claim 6, wherein the threads serving as profile-imparting elements are firmly bonded to the semipermeable membrane over the entire length of their support areas.
8. A film as claimed in claim 6, wherein the threads serving as profile-imparting elements are firmly bonded to the semipermeable membrane only within single discrete zones of their support area.
9. A film as claimed in claim 6, wherein the threads serving as profile-imparting elements are interrupted at regular intervals,
10. A film as claimed in claim 2, wherein the profiling is formed by series of points which run parallel to one another.
11. A film as claimed in claim 10, wherein the series of points serving as profiling are arranged parallel to the direction of flow of the liquid or gas.
12. A film as claimed in claim 2, wherein the profiling is comprised of a plurality of point-shaped elevations which are distributed in irregular fashion over the entire film surface.
13. A process for preparing a membrane film which has profiling on its surface comprising the steps of: pouring a solution which contains a material capable of membrane formation onto a profiled substrate; and converting the material by phase inversion to produce a membrane having a negative pattern of the profiled substrate on its surface.
*;14. A process for preparing a membrane film which has profiling on its surface comprising the steps of:;spinning into a coagulation bath a solution which contains a material capable of membrane formation through a die which contains a slot which is delimited on one side by a straight edge and on the other side by an edge with profiling; and;- 16 -;202-711;converting the spun material in the coagulation bath by phase inversion to produce a membrane having profiling determined by the profiled die edge on its surface.;
15. A process as claimed in claim 14, wherein the material exiting from the die is applied onto a support layer permeable to flowable media.;
16. A process for preparing a membrane film which has on its surface profiling which is formed by profile-imparting elements, comprising the steps of:;extruding a thermoplastic material into the form of the profile-imparting elements; and applying the profile-imparting elements in the extrusion step to the surface of a membrane in such a way as to firmly bond them to it.;
17. A process for preparing a membrane film as claimed in claim 16, further comprising the step of bonding the profile-imparting elements to the surface of the membrane by means of a thermoplastic adhesive.;
18. A process for preparing a membrane film as claimed in claim 16, wherein the membrane is still in liquid form and the profile-imparting elements are partially embedded in the still liquid membrane and become firmly bonded to the membrane upon solidification of the membrane.;
19. A process for preparing a membrane film as claimed in claim 16, which comprises extruding the profile-imparting elements onto a support layer and thereafter applying the membrane to the side of the support layer to which the profile-imparting elements have been applied.;•N \;13 MAR 1985 r];* - 17 - pf.Q7-f 1 ivUig I _jl JL
20. A device for separating multicomponent liquid or gaseous systems, comprising a semipermeable membrane shaped in a spiral-like or layer structure, wherein the semipermeable membrane comprises a film as defined by claim 1.
21. A film according to claim 1 substantially as herein described with reference to the accompanying drawings. HOECHST AKTIENGESELLSCHAFT By Their Attorneys HENRY HUGHES LIMITED
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19813148312 DE3148312A1 (en) | 1981-12-07 | 1981-12-07 | FILM FOR SEPARATING LIQUID OR GASEOUS MULTI-COMPONENT SYSTEMS |
Publications (1)
Publication Number | Publication Date |
---|---|
NZ202711A true NZ202711A (en) | 1985-07-12 |
Family
ID=6148054
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
NZ202711A NZ202711A (en) | 1981-12-07 | 1982-12-06 | Profiled semipermeable membrane |
Country Status (10)
Country | Link |
---|---|
EP (1) | EP0081182B1 (en) |
JP (1) | JPS58104604A (en) |
AU (1) | AU555429B2 (en) |
CA (1) | CA1214114A (en) |
DE (2) | DE3148312A1 (en) |
DK (1) | DK539382A (en) |
ES (1) | ES517965A0 (en) |
FI (1) | FI71493C (en) |
NO (1) | NO823916L (en) |
NZ (1) | NZ202711A (en) |
Families Citing this family (25)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS58163405A (en) * | 1982-03-24 | 1983-09-28 | Daicel Chem Ind Ltd | Semi-permeable membrane having selective permeability membrane, preparation thereof and filter type artificial kidney |
GB8522847D0 (en) * | 1985-09-16 | 1985-10-23 | Shell Int Research | Supported membrane |
WO1988009200A1 (en) * | 1987-05-29 | 1988-12-01 | Terumo Kabushiki Kaisha | Flat film permeative membrane having protrusions, its production , and bodily fluid filter |
EP0350252B1 (en) * | 1988-07-06 | 1994-03-23 | Eastman Kodak Company | The separation of elements defining a fluid flow path |
DE4133300C2 (en) * | 1991-10-08 | 1996-07-11 | Fraunhofer Ges Forschung | Method and device for determining strippable substances from liquids |
WO2006012920A1 (en) * | 2004-07-29 | 2006-02-09 | Inge Ag | Filtration membrane and method for producing the same |
US7465335B2 (en) * | 2005-02-02 | 2008-12-16 | United Technologies Corporation | Fuel deoxygenation system with textured oxygen permeable membrane |
US7465336B2 (en) * | 2005-06-09 | 2008-12-16 | United Technologies Corporation | Fuel deoxygenation system with non-planar plate members |
US7582137B2 (en) * | 2006-01-18 | 2009-09-01 | United Technologies Corporation | Fuel deoxygenator with non-planar fuel channel and oxygen permeable membrane |
EP2366449A4 (en) * | 2008-11-11 | 2012-05-30 | Snu R&Db Foundation | Membrane with a patterned surface, method for manufacturing same, and water treatment process using same |
CN102333582B (en) | 2009-02-25 | 2014-08-06 | 普拉特及惠特尼火箭达因公司 | Fluid separation system with reduced fouling |
KR101819090B1 (en) * | 2010-10-26 | 2018-01-16 | 도레이 카부시키가이샤 | Separation membrane, separation membrane element and separation membrane production method |
CN103596666A (en) * | 2011-04-13 | 2014-02-19 | Gfd纺织公司 | Filter element for fluid filtration system |
EP2730331B1 (en) * | 2011-07-07 | 2021-01-20 | Toray Industries, Inc. | Separation membrane element |
TW201325704A (en) * | 2011-09-29 | 2013-07-01 | Toray Industries | Separation membrane and separation membrane element |
CA2866749C (en) | 2012-03-12 | 2021-06-15 | Nanotheta Co, Ltd. | Ultra-thin polymer film and porous ultra-thin polymer film |
WO2014003171A1 (en) * | 2012-06-28 | 2014-01-03 | 東レ株式会社 | Separation membrane and separation membrane element |
LU92051B1 (en) * | 2012-07-25 | 2014-01-27 | Univ Luxembourg | Membrane assembly |
US20150298064A1 (en) * | 2012-07-31 | 2015-10-22 | Toray Industries, Inc. | Separation membrane and separation membrane element |
MX2015011098A (en) * | 2013-02-28 | 2016-04-06 | Aqua Membranes Llc | Improved spiral wound element construction. |
NL2012109C2 (en) | 2014-01-20 | 2015-07-21 | X Flow Bv | A tubular membrane with a helical ridge, as well as a method and apparatus for producing such a tubular membrane. |
EP2902094A1 (en) * | 2014-01-30 | 2015-08-05 | Amer-Sil S.A. | Filtration membrane |
EP3377199A1 (en) * | 2015-11-19 | 2018-09-26 | Entegris, Inc. | Features on a porous membrane |
EP3507000A4 (en) * | 2016-09-04 | 2020-04-29 | Ariel Scientific Innovations Ltd. | Selectively-permeable membrane |
EP3613495A1 (en) * | 2018-08-23 | 2020-02-26 | MMM Innovations BVBA | Porous composite structures with touch fastener |
Family Cites Families (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR587077A (en) * | 1924-10-09 | 1925-04-10 | Manufacturing process for ultrafilter membranes | |
US2944017A (en) * | 1956-12-17 | 1960-07-05 | Millipore Filter Corp | Filter medium |
US3445321A (en) * | 1967-05-01 | 1969-05-20 | Gen Electric | Thin,reinforced permselective films |
US3721596A (en) * | 1969-11-24 | 1973-03-20 | G Drake | Fluid separation and method and apparatus for forming same |
DE2722025A1 (en) * | 1977-05-16 | 1978-11-30 | Hoechst Ag | MEMBRANE UNIT, DEVICE WITH MEMBRANE UNIT, AND METHOD OF BLOOD PURIFICATION |
-
1981
- 1981-12-07 DE DE19813148312 patent/DE3148312A1/en not_active Withdrawn
-
1982
- 1982-11-23 NO NO823916A patent/NO823916L/en unknown
- 1982-11-29 AU AU90947/82A patent/AU555429B2/en not_active Ceased
- 1982-11-30 DE DE8282111042T patent/DE3272379D1/en not_active Expired
- 1982-11-30 CA CA000416705A patent/CA1214114A/en not_active Expired
- 1982-11-30 EP EP82111042A patent/EP0081182B1/en not_active Expired
- 1982-12-03 FI FI824184A patent/FI71493C/en not_active IP Right Cessation
- 1982-12-06 ES ES517965A patent/ES517965A0/en active Granted
- 1982-12-06 JP JP57212829A patent/JPS58104604A/en active Pending
- 1982-12-06 DK DK539382A patent/DK539382A/en unknown
- 1982-12-06 NZ NZ202711A patent/NZ202711A/en unknown
Also Published As
Publication number | Publication date |
---|---|
AU9094782A (en) | 1983-06-16 |
DE3148312A1 (en) | 1983-06-09 |
FI824184L (en) | 1983-06-08 |
DE3272379D1 (en) | 1986-09-04 |
EP0081182B1 (en) | 1986-07-30 |
ES8404865A1 (en) | 1984-05-16 |
JPS58104604A (en) | 1983-06-22 |
ES517965A0 (en) | 1984-05-16 |
DK539382A (en) | 1983-06-08 |
FI824184A0 (en) | 1982-12-03 |
AU555429B2 (en) | 1986-09-25 |
CA1214114A (en) | 1986-11-18 |
NO823916L (en) | 1983-06-08 |
EP0081182A3 (en) | 1983-08-17 |
FI71493C (en) | 1987-01-19 |
EP0081182A2 (en) | 1983-06-15 |
FI71493B (en) | 1986-10-10 |
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