EP1724000A1 - Multiple layered membrane with thin fluorine containing polymer layer - Google Patents
Multiple layered membrane with thin fluorine containing polymer layer Download PDFInfo
- Publication number
- EP1724000A1 EP1724000A1 EP06252601A EP06252601A EP1724000A1 EP 1724000 A1 EP1724000 A1 EP 1724000A1 EP 06252601 A EP06252601 A EP 06252601A EP 06252601 A EP06252601 A EP 06252601A EP 1724000 A1 EP1724000 A1 EP 1724000A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- layer
- membrane
- fluorine containing
- primer
- coating
- 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.)
- Granted
Links
- 239000012528 membrane Substances 0.000 title claims abstract description 86
- 229910052731 fluorine Inorganic materials 0.000 title claims abstract description 31
- 239000011737 fluorine Substances 0.000 title claims abstract description 31
- YCKRFDGAMUMZLT-UHFFFAOYSA-N Fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 title claims abstract description 30
- 229920000642 polymer Polymers 0.000 title claims description 13
- 239000000758 substrate Substances 0.000 claims abstract description 16
- 239000011248 coating agent Substances 0.000 claims abstract description 15
- 238000000576 coating method Methods 0.000 claims abstract description 15
- 238000000034 method Methods 0.000 claims abstract description 12
- 238000010438 heat treatment Methods 0.000 claims abstract description 10
- 238000005507 spraying Methods 0.000 claims abstract description 9
- 239000006185 dispersion Substances 0.000 claims description 17
- 229920002943 EPDM rubber Polymers 0.000 claims description 16
- ZWEHNKRNPOVVGH-UHFFFAOYSA-N 2-Butanone Chemical compound CCC(C)=O ZWEHNKRNPOVVGH-UHFFFAOYSA-N 0.000 claims description 15
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 claims description 9
- 238000004519 manufacturing process Methods 0.000 claims description 7
- 230000008569 process Effects 0.000 claims description 7
- XEKOWRVHYACXOJ-UHFFFAOYSA-N Ethyl acetate Chemical compound CCOC(C)=O XEKOWRVHYACXOJ-UHFFFAOYSA-N 0.000 claims description 6
- 239000000463 material Substances 0.000 claims description 6
- 239000007921 spray Substances 0.000 claims description 6
- 229940032007 methylethyl ketone Drugs 0.000 claims description 5
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 claims description 4
- GNDOBZLRZOCGAS-UHFFFAOYSA-N 2-isocyanatoethyl 2,6-diisocyanatohexanoate Chemical compound O=C=NCCCCC(N=C=O)C(=O)OCCN=C=O GNDOBZLRZOCGAS-UHFFFAOYSA-N 0.000 claims description 3
- SECXISVLQFMRJM-UHFFFAOYSA-N N-Methylpyrrolidone Chemical compound CN1CCCC1=O SECXISVLQFMRJM-UHFFFAOYSA-N 0.000 claims description 3
- 229920000459 Nitrile rubber Polymers 0.000 claims description 3
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 claims description 3
- 239000004962 Polyamide-imide Substances 0.000 claims description 3
- 239000006229 carbon black Substances 0.000 claims description 3
- 229920002312 polyamide-imide Polymers 0.000 claims description 3
- 229920006393 polyether sulfone Polymers 0.000 claims description 3
- 239000011347 resin Substances 0.000 claims description 3
- 229920005989 resin Polymers 0.000 claims description 3
- 239000008096 xylene Substances 0.000 claims description 3
- 239000004695 Polyether sulfone Substances 0.000 claims description 2
- 239000000440 bentonite Substances 0.000 claims description 2
- 229910000278 bentonite Inorganic materials 0.000 claims description 2
- SVPXDRXYRYOSEX-UHFFFAOYSA-N bentoquatam Chemical compound O.O=[Si]=O.O=[Al]O[Al]=O SVPXDRXYRYOSEX-UHFFFAOYSA-N 0.000 claims description 2
- 229920001084 poly(chloroprene) Polymers 0.000 claims description 2
- 239000004408 titanium dioxide Substances 0.000 claims description 2
- 238000005238 degreasing Methods 0.000 claims 2
- 125000001153 fluoro group Chemical group F* 0.000 claims 1
- 229920001973 fluoroelastomer Polymers 0.000 claims 1
- 239000010410 layer Substances 0.000 description 23
- 229920001343 polytetrafluoroethylene Polymers 0.000 description 15
- 239000004810 polytetrafluoroethylene Substances 0.000 description 15
- 239000010865 sewage Substances 0.000 description 7
- 239000000126 substance Substances 0.000 description 7
- 239000002351 wastewater Substances 0.000 description 7
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 6
- 229910052760 oxygen Inorganic materials 0.000 description 6
- 239000001301 oxygen Substances 0.000 description 6
- 238000005273 aeration Methods 0.000 description 5
- 239000007787 solid Substances 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 239000002253 acid Substances 0.000 description 3
- 239000011247 coating layer Substances 0.000 description 3
- 229920001971 elastomer Polymers 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 239000002344 surface layer Substances 0.000 description 3
- 150000001875 compounds Chemical class 0.000 description 2
- 238000009472 formulation Methods 0.000 description 2
- 230000006872 improvement Effects 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 238000002203 pretreatment Methods 0.000 description 2
- 230000037452 priming Effects 0.000 description 2
- 238000004080 punching Methods 0.000 description 2
- 238000004065 wastewater treatment Methods 0.000 description 2
- IRBNMBNVRSUJDG-UHFFFAOYSA-N 2,6-diisocyanatohexanoic acid Chemical compound O=C=NC(C(=O)O)CCCCN=C=O IRBNMBNVRSUJDG-UHFFFAOYSA-N 0.000 description 1
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- IOVCWXUNBOPUCH-UHFFFAOYSA-M Nitrite anion Chemical compound [O-]N=O IOVCWXUNBOPUCH-UHFFFAOYSA-M 0.000 description 1
- 206010047700 Vomiting Diseases 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 238000005452 bending Methods 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000003851 corona treatment Methods 0.000 description 1
- 238000004132 cross linking Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000000806 elastomer Substances 0.000 description 1
- 239000003925 fat Substances 0.000 description 1
- 230000004907 flux Effects 0.000 description 1
- 239000010440 gypsum Substances 0.000 description 1
- 229910052602 gypsum Inorganic materials 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 238000009832 plasma treatment Methods 0.000 description 1
- -1 polytetrafluoroethylene Polymers 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- 239000002356 single layer Substances 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 238000004381 surface treatment Methods 0.000 description 1
- 239000002352 surface water Substances 0.000 description 1
- 239000010409 thin film Substances 0.000 description 1
- 230000008673 vomiting Effects 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/20—Mixing gases with liquids
- B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
- B01F23/231—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids by bubbling
- B01F23/23105—Arrangement or manipulation of the gas bubbling devices
- B01F23/2312—Diffusers
- B01F23/23124—Diffusers consisting of flexible porous or perforated material, e.g. fabric
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/20—Mixing gases with liquids
- B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
- B01F23/231—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids by bubbling
- B01F23/23105—Arrangement or manipulation of the gas bubbling devices
- B01F23/2312—Diffusers
- B01F23/23124—Diffusers consisting of flexible porous or perforated material, e.g. fabric
- B01F23/231244—Dissolving, hollow fiber membranes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/20—Mixing gases with liquids
- B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
- B01F23/231—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids by bubbling
- B01F23/23105—Arrangement or manipulation of the gas bubbling devices
- B01F23/2312—Diffusers
- B01F23/23126—Diffusers characterised by the shape of the diffuser element
- B01F23/231262—Diffusers characterised by the shape of the diffuser element having disc shape
Definitions
- the present application relates to membrane layers.
- Spray coating methods of applying fluorine containing dispersions onto substrates such as EPDM and Nitrile rubber already exist. They are typically combined with primers such as but not limited to polyamide-imide, polyether sulfones and sprayed onto a substrate that may have been pretreated with. Methyl-ethyl Ketone, N-Methyl Pyrrolidone, plasma or corona treatment to improve adhesion of the primer to the substrate. Following surface preparation and priming, they are coated with a fluorine containing dispersion coating, and are then cured on-line or off-line in an oven. However such methods have not previously been applied to a diffuser membrane for use in water treatment plants, which is a difficult application.
- Diffuser membranes are typically made from perforated non-fluorinated elastomers or polymers, which are perforated with small slits and, when inflated, produce a plume of bubbles which are released into waste water.
- the efficacy of such diffusers is measured primarily in their ability to produce small bubbles in great quantity, such that the combined surface area of the bubbles is large. A large quantity of small bubbles transfers much more oxygen to the process than do a smaller quantity of large bubbles and oxygen mass transfer is desirable.
- diffusers typically spend a great deal of time and energy formulating elastomeric compounds that produce small bubbles, The slightest compound formulation change may result in a vastly different bubble size.
- surface contamination from foulants such as biofilm, calcium and gypsum can cause an increase in bubble size over time, just as fats, oils, greases and solvents can penetrate traditional membranes causing chemical oxidation of the rubber. This can result in either a failed part or increased bubble size.
- the coating of a non fluorine containing membrane with a smooth fluorinated layer that is specifically designed to produce small bubbles, and to withstand thousands of perforations and a constant state of flux while submerged in waste water, is a novel invention and provides a universal solution to both fouling and efficiency issues.
- aspects of the present invention apply to flexible diffuser membranes which are used in the aeration of waste water and which is spray coated with a fluorine containing surface layer.
- a diffuser membrane is produced from blended EPDM rubber, Nitrite rubber, or Neoprene rubber, the surface is roughened either through corona, plasma, or Methyl-ethyl Ketone, and a primer and fluorine containing surface layer are applied through spray coating. Alternately a blended primer and fluorine containing surface layer are applied through spray coating.
- the membrane When treated in this way, the membrane becomes significantly more resistant to surface fouling, chemical oxidation, and its oxygen transfer efficiency is acceptably high by industry standards.
- Adhesion between a spray coated fluorine containing layer and a substrate is accomplished through substrate surface treatment, priming, coating and curing.
- a substrate layer such as membrane 3 is moulded.
- a roughing agent such as corona, plasma, methyl-ethyl ketone or N-Methyl Pyrrolidone is applied to the surface to be coated as needed depending on the quality of the substrate.
- a primer layer 2 of less than 10 microns is sprayed onto the substrate surface. This primer is then heat treated at 100 degrees C for 15 minutes.
- the primer layer may contain Polyamide-Imide or Polyether Sulfone. Alternately, the primer is blended with a fluorine containing dispersion layer and this layer is sprayed onto the substrate surface, then heat treated.
- the fluorine containing dispersion layer 1 of less than 20 microns is sprayed over the cured primer, and is heat treated at 120 degrees C for 20 minutes.
- the fluorine containing dispersion layer may contain fluoride acryl resin, xylene, toluene, bentonite, titanium dioxide, carbon black, 2-lsocyanatoethyl 2, 6-diisocyanatohexanoate, 2, 6-Diisocyanatohexanoic acid 2-isocyanatoethyl ester and/or ethyl acetate.
- This invention is about the multi-layered membrane of disk typed and tube typed membrane air diffuser.
- This system can be installed in the aeration tanks of the sewage and waste water treatment system that is used to make the air, which was supplied from the blower, fine bubbles to spray them so that the oxygen in the air can be efficiently dissolved into the sewage and waste water.
- this system analyses and removes the biochemical oxygen demand and suspended solids biologically, and enables to be appropriately mixed so that the sedimentation within the aeration tank can be prevented.
- the purpose of the invention is a device that sprays the air, taken from a blower, through the membrane infinitesimally for various processes that supply oxygen to the micro organisms in an aeration tank to purify waste and related processes where sewage and waste waters are biologically processed.
- the membrane used for this purpose are the ones composed of single material and single layer such as EPDM, SILICON and NITRIL.
- the membrane may be manufactured by coating the PTFE on the multi layer structure or both surfaces of the conventional EPDM or NITRIL membrane (MEMBRANE 22), so that the acid-resistance, resistance to chemical, heat resistance, and the function that can prevent foreign elements from being adhered, which are the functions not owned by EPDM and NITRIL membrane, can be provided.
- This invention coats PTFE on both surfaces of membrane whose main material is EPDM or Nitril. It adds the characteristics of PTFE based on the physical property of EPDM membrane so that the functions and durability of the membrane within the sewage and waste water can increase.
- the PTFE coating layer is likely to peel from the EPDM surface if there is no pre-treatment
- the layer was processed through a hardening process from heat treatment so that PTFE coating layer should not rise during the manufacturing process of bending the layer or punching a pore.
- the air diffuser of PTFE coating membrane of this invention has the characteristics as follows, it prevents suspended solids from being adhered under water during a process where air is sprayed within the aeration tank of the sewage and surface water treatment system. Also, it has superior acid resistances and strong resistance to chemical.
- Figs. 4 to 6 provide illustrations of a practical example according to this invention as shown below.
- the compositions of the membrane air diffuser according to this invention are represented.
- the multi layered membrane (membrane 13) is assembled into the air diffuser (Base 11) and this assemble is tightened by a retaining nut (retaining nut 12).
- the multilayered membrane (membrane 13) tightened by a retaining nut and expanded by the air supplied through the orifice of the air diffuser base and at this time many slits, which were made by punching over the effective surface of the membrane, are opened while vomiting equal fine bubbles of 1-2mm sizes.
- the air diffuser of multi layer membrane of PFTE has the following effects; it has strong resistance to chemical substances of strong corrosiveness flown into along with sewage or waste water. Also, it is safely prevented from the suspended solids such as CaC1 2 that is easily adhered to the EPDM membrane surface, and it has acid resistance.
- the membrane can be used in a number of applications and for example.
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
- Laminated Bodies (AREA)
- Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)
- Manufacture Of Macromolecular Shaped Articles (AREA)
Abstract
Description
- The present application relates to membrane layers.
- It is known to provide membrane layers and an example is given in
US Patent Application Number 10/711607 - Spray coating methods of applying fluorine containing dispersions onto substrates such as EPDM and Nitrile rubber already exist. They are typically combined with primers such as but not limited to polyamide-imide, polyether sulfones and sprayed onto a substrate that may have been pretreated with. Methyl-ethyl Ketone, N-Methyl Pyrrolidone, plasma or corona treatment to improve adhesion of the primer to the substrate. Following surface preparation and priming, they are coated with a fluorine containing dispersion coating, and are then cured on-line or off-line in an oven. However such methods have not previously been applied to a diffuser membrane for use in water treatment plants, which is a difficult application.
- This improvement is of particular importance in application of such a coating to a diffuser membrane used in the sewage and industrial wastewater treatment industries. Diffuser membranes are typically made from perforated non-fluorinated elastomers or polymers, which are perforated with small slits and, when inflated, produce a plume of bubbles which are released into waste water. The efficacy of such diffusers is measured primarily in their ability to produce small bubbles in great quantity, such that the combined surface area of the bubbles is large. A large quantity of small bubbles transfers much more oxygen to the process than do a smaller quantity of large bubbles and oxygen mass transfer is desirable. Manufacturers of diffusers typically spend a great deal of time and energy formulating elastomeric compounds that produce small bubbles, The slightest compound formulation change may result in a vastly different bubble size. Furthermore, where diffuser membranes are submerged in dirty water, surface contamination from foulants such as biofilm, calcium and gypsum can cause an increase in bubble size over time, just as fats, oils, greases and solvents can penetrate traditional membranes causing chemical oxidation of the rubber. This can result in either a failed part or increased bubble size. The coating of a non fluorine containing membrane with a smooth fluorinated layer that is specifically designed to produce small bubbles, and to withstand thousands of perforations and a constant state of flux while submerged in waste water, is a novel invention and provides a universal solution to both fouling and efficiency issues.
- Aspects of the present invention apply to flexible diffuser membranes which are used in the aeration of waste water and which is spray coated with a fluorine containing surface layer.
- A diffuser membrane is produced from blended EPDM rubber, Nitrite rubber, or Neoprene rubber, the surface is roughened either through corona, plasma, or Methyl-ethyl Ketone, and a primer and fluorine containing surface layer are applied through spray coating. Alternately a blended primer and fluorine containing surface layer are applied through spray coating.
- When treated in this way, the membrane becomes significantly more resistant to surface fouling, chemical oxidation, and its oxygen transfer efficiency is acceptably high by industry standards.
- Embodiments of the present invention are described by way of example and with reference to the attached drawings wherein:
- Fig. 1 is a cross-sectional view of a multi layered disc membrane;
- Fig. 2 is a cross-sectional view of a membrane onto which layers have been applied;
- Fig. 3 is a cutaway view of a multi layered tube membrane;
- Fig. 4 is a cross-section of an air diffuser assembly;
- Fig. 5 is a cross-section of a membrane; and,
- Fig. 6 is a schematic illustration of a manufacturing process.
- Adhesion between a spray coated fluorine containing layer and a substrate is accomplished through substrate surface treatment, priming, coating and curing.
- Firstly, a substrate layer such as
membrane 3 is moulded. - Secondly, a roughing agent such as corona, plasma, methyl-ethyl ketone or N-Methyl Pyrrolidone is applied to the surface to be coated as needed depending on the quality of the substrate.
- Thirdly, a
primer layer 2 of less than 10 microns is sprayed onto the substrate surface. This primer is then heat treated at 100 degrees C for 15 minutes. The primer layer may contain Polyamide-Imide or Polyether Sulfone. Alternately, the primer is blended with a fluorine containing dispersion layer and this layer is sprayed onto the substrate surface, then heat treated. - Fourthly, if using separate primer and fluorine containing dispersion layers, the fluorine containing dispersion layer 1 of less than 20 microns is sprayed over the cured primer, and is heat treated at 120 degrees C for 20 minutes. The fluorine containing dispersion layer may contain fluoride acryl resin, xylene, toluene, bentonite, titanium dioxide, carbon black, 2-
lsocyanatoethyl 2, 6-diisocyanatohexanoate, 2, 6-Diisocyanatohexanoic acid 2-isocyanatoethyl ester and/or ethyl acetate. - From the foregoing it will be seen that this invention is one well adapted to attain all ends and objectives hereinabove set forth together with the other advantages which are obvious and which are inherent to the structure.
- It will be understood that certain features and subcombinations are of utility and may be employed without reference to other features and subcombinations. This is contemplated by and is within the scope of the claims.
- Since many possible embodiments may be made of the invention without departing from the scope thereof, it is to be understood that all matter herein set forth or shown in the accompanying drawings is to be interpreted as illustrative, and not in a limiting sense.
- This invention is about the multi-layered membrane of disk typed and tube typed membrane air diffuser. This system can be installed in the aeration tanks of the sewage and waste water treatment system that is used to make the air, which was supplied from the blower, fine bubbles to spray them so that the oxygen in the air can be efficiently dissolved into the sewage and waste water. By doing it, this system analyses and removes the biochemical oxygen demand and suspended solids biologically, and enables to be appropriately mixed so that the sedimentation within the aeration tank can be prevented.
- Referring to Figs. 4 to 6 of the drawings in which:-
- Fig. 4 represents the cross section of an assembled air diffuser according to this invention.
- Fig. 5 is a cross section illustrating a membrane with the PTFE, which was prepared for both surfaces of membrane for air diffuser according to this invention.
- Fig. 6 represents a process where the PTFE is coated on the membrane for air diffusers according to this invention.
- Within these drawings the following reference numeration is used:
- 11 : Base
- 12 : Retaining unit
- 13 : Multi layered membrane
- 21 : EPDM membrane
- 22 : Primer
- 23 : PTFE (polytetrafluoroethylene) coating layer
- The purpose of the invention is a device that sprays the air, taken from a blower, through the membrane infinitesimally for various processes that supply oxygen to the micro organisms in an aeration tank to purify waste and related processes where sewage and waste waters are biologically processed. The membrane used for this purpose are the ones composed of single material and single layer such as EPDM, SILICON and NITRIL.
- In this invention, the membrane may be manufactured by coating the PTFE on the multi layer structure or both surfaces of the conventional EPDM or NITRIL membrane (MEMBRANE 22), so that the acid-resistance, resistance to chemical, heat resistance, and the function that can prevent foreign elements from being adhered, which are the functions not owned by EPDM and NITRIL membrane, can be provided.
- The invention for achieving the above purposes has the following characteristics:
- This invention coats PTFE on both surfaces of membrane whose main material is EPDM or Nitril. It adds the characteristics of PTFE based on the physical property of EPDM membrane so that the functions and durability of the membrane within the sewage and waste water can increase.
- Generally, in case of the multi-layered membrane with coating of EPDM and PTFE, the PTFE coating layer is likely to peel from the EPDM surface if there is no pre-treatment In aspects of PTFE layer coated after pre-treatment, the layer was processed through a hardening process from heat treatment so that PTFE coating layer should not rise during the manufacturing process of bending the layer or punching a pore.
- The air diffuser of PTFE coating membrane of this invention has the characteristics as follows, it prevents suspended solids from being adhered under water during a process where air is sprayed within the aeration tank of the sewage and surface water treatment system. Also, it has superior acid resistances and strong resistance to chemical.
- Figs. 4 to 6 provide illustrations of a practical example according to this invention as shown below.
- The compositions of the membrane air diffuser according to this invention are represented. The multi layered membrane (membrane 13) is assembled into the air diffuser (Base 11) and this assemble is tightened by a retaining nut (retaining nut 12). As for the function of the membrane air diffuser, the multilayered membrane (membrane 13) tightened by a retaining nut and expanded by the air supplied through the orifice of the air diffuser base and at this time many slits, which were made by punching over the effective surface of the membrane, are opened while vomiting equal fine bubbles of 1-2mm sizes.
- The manufacturing process of a membrane in which PTFE has been coated is described with reference to Fig. 6, wash and dry both surfaces of EPDM or NITRIL membrane (21) and press them by (primer 22) and then heat them for about thirty minutes in a heat treatment furnace,.
- Afterwards, coat a membrane which was cooled off, with PTFE and plasticize it in the heat treatment furnace for over 20 minutes at over 100 degrees for plasticity of the membrane.
- As described above in detail, the air diffuser of multi layer membrane of PFTE according to this invention has the following effects; it has strong resistance to chemical substances of strong corrosiveness flown into along with sewage or waste water. Also, it is safely prevented from the suspended solids such as CaC12 that is easily adhered to the EPDM membrane surface, and it has acid resistance.
- The membrane can be used in a number of applications and for example.
- a) a disc typed membrane for air diffusers that prevents the suspended solids from being adhered under water by coating PTFE in the multi layer structural on both surfaces of EPDM or NITRIL membranes and that has acid resistance, resistance to chemical, and heat resistance.
- b) related to application 1m the multi layered tube type membrane for air diffusers whose membrane is made in a tube form.
- Whilst endeavouring in the foregoing specification to draw attention to those features of the invention believed to be of particular importance it should be understood that the Applicant claims protection in respect of any patentable feature or combination of features hereinbefore referred to and/or shown in the drawings whether or not particular emphasis has been placed thereon.
Claims (22)
- A multi-layer membrane comprising:a first layer comprising a polymer layer on a membrane and a second layer over said first layer comprising a dispersion layer wherein said dispersion layer is a fluorine containing dispersion layer.
- A multi-layer membrane as claimed in claim 1, wherein said first layer comprises a fluoroelastomer.
- A multi-layer membrane as claimed in claim 1 or claim 2 wherein said dispersion layer further includes a primer and a fluorine containing dispersion.
- A multi-layer membrane as claimed in claims 1 to 3, wherein said first layer further includes material selected from a group consisting of neoprene rubber, ethylene propylene diene monomer (EPDM) and nitrile rubber.
- A multi-layer membrane as claimed in any preceding claim, wherein said first layer further includes a primer layer and wherein said primer layer is less than 10 microns.
- A multi-layer membrane as claimed in any preceding claim, wherein said membrane is selected from a group consisting of a tubular shaped membrane, a disc shaped membrane and a panel shaped membrane.
- A multi-layer membrane as claimed in claim 5, wherein said primer layer comprises material selected from a group consisting of Polyamide-Imide and Polyether Sulfone.
- A multi-layer membrane as claimed in any preceding claim, wherein said second layer is less than 20 microns.
- A multi-layer membrane as claimed in any preceding claim, wherein said second layer is less than 20 microns and said second layer is heat treated at a temperature of greater than 120 degrees C.
- A multi-layer membrane as claimed in any preceding claim, wherein said second layer further comprises material selected from a group consisting of fluoride acryl resin, xylene, toluene, bentonite, titanium dioxide, carbon black, 2-Isocyanatoethyl 2,6-diisocyanatohexanoate. 2,6-Diisocyanatohexanoic acid 2-isocyanatoethyl ester and ethyl acetate.
- A multi-layer membrane as claimed in any preceding claim, wherein said first layer is a non-fluarinated polymer.
- A mulfi-layer membrane as claimed in any preceding claim, wherein a primer and said fluorine containing dispersion is applied onto said first layer in a single application.
- A multi-layer membrane as claimed in any preceding, wherein said second layer is applied through a spray, and is cured using a method selected from a group consisting of an on-line and an off-line oven.
- A multi-layer membrane as claimed in any preceding claim, wherein said first layer further includes materials selected from a group consisting of fluoride acryl resin, methyl-ethyl ketone, xylene, toluene and carbon black.
- A multi-layer membrane as claimed in any preceding claim, wherein said membrane is pretreated with plasma, corona, N-Methyl Pyrrolidone or methyl-ethyl ketone prior to coating of said first layer.
- A multi-layer membrane as claimed in any preceding claim, wherein said membrane is pretreated prior to coating of said first layer.
- A multi-layer membrane as claimed in any preceding claim wherein the dispersion layer is polytetrafluorothene (PTFE).
- A process for preparing a multi layer membrane wherein said membrane comprises a polymer layer consisting of a fluorine containing polymer, a substrate, wherein a bond between said first layer and said second layer is formed first via a degreasing step, followed by a primer, heat treatment of said primer, spray coating of a fluorine containing dispersion, and finally heat treatment of said coating,
- A process for preparing a multi layer membrane wherein said membrane comprises a polymer layer consisting of a fluorine containing polymer, a substrate, wherein a bond between said first layer and said second layer is formed first via a degreasing step, followed by a spray coating of combined primer and fluorine containing dispersion, and finally heat treatment of said combined primer and said coating.
- A process for preparing a multi layer membrane wherein said membrane comprises a polymer layer consisting of a fluorine containing polymer, a substrate, wherein a bond between said first layer and said second layer is formed via a spray coating of combined primer and fluorine containing dispersion, and finally heat treatment of said combined primer and said coating.
- A process for preparing a multi layer membrane wherein said membrane comprises a polymer layer consisting of a fluorine containing polymer, a substrate, wherein a bond between said first layer and said second layer is formed via a spray coating of a primer, heat treatment of said primer, spray coating of fluorine containing dispersion, and finally heat treatment of said coating.
- A process as claimed in any of claims 10 to 21 wherein the fluorine containing polymer is polytetrafluorethene (PTFE)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
KR1020050041410A KR100666937B1 (en) | 2005-05-18 | 2005-05-18 | Multi layered membrane for air diffuser |
US11/164,729 US7674514B2 (en) | 2005-12-02 | 2005-12-02 | Multiple layered membrane with thin fluorine containing polymer layer |
Publications (2)
Publication Number | Publication Date |
---|---|
EP1724000A1 true EP1724000A1 (en) | 2006-11-22 |
EP1724000B1 EP1724000B1 (en) | 2011-03-16 |
Family
ID=36930236
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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EP06252601A Active EP1724000B1 (en) | 2005-05-18 | 2006-05-18 | Method for producing a composite membrane with thin fluorine containing polymer layer |
Country Status (3)
Country | Link |
---|---|
EP (1) | EP1724000B1 (en) |
AT (1) | ATE501783T1 (en) |
DE (1) | DE602006020656D1 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2011127914A1 (en) * | 2010-04-15 | 2011-10-20 | Ott Friederike | Gassing device for introducing a gas into a liquid |
CN104707496A (en) * | 2010-08-18 | 2015-06-17 | 三菱日立电力***株式会社 | Aeration device and system for flue-gas desulfurization with seawater which is equipped with same |
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US6410084B1 (en) * | 1999-02-12 | 2002-06-25 | Bha Technologies, Inc. | Porous membrane structure and method |
US20030207118A1 (en) * | 2002-04-18 | 2003-11-06 | 3M Innovative Properties Company | Adhesion and bonding of multi-layer articles including a fluoropolymer layer |
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US20050003204A1 (en) * | 2004-09-28 | 2005-01-06 | Thomas Frankel | Mutiple layered membrane with fluorine containing polymer layer |
-
2006
- 2006-05-18 EP EP06252601A patent/EP1724000B1/en active Active
- 2006-05-18 DE DE602006020656T patent/DE602006020656D1/en active Active
- 2006-05-18 AT AT06252601T patent/ATE501783T1/en not_active IP Right Cessation
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GB2051091A (en) * | 1979-02-16 | 1981-01-14 | Fluorocoat Ltd | Fluorocarbon Polymer Compositions and Method of Spray-coating |
US5238471A (en) * | 1992-10-14 | 1993-08-24 | E. I. Du Pont De Nemours And Company | Spray-applied fluoropolymer films for gas separation membranes |
US6648147B1 (en) * | 1998-05-23 | 2003-11-18 | Madison Filter 981 Limited | Phase-separation member |
US6410084B1 (en) * | 1999-02-12 | 2002-06-25 | Bha Technologies, Inc. | Porous membrane structure and method |
US20030207118A1 (en) * | 2002-04-18 | 2003-11-06 | 3M Innovative Properties Company | Adhesion and bonding of multi-layer articles including a fluoropolymer layer |
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WO2011127914A1 (en) * | 2010-04-15 | 2011-10-20 | Ott Friederike | Gassing device for introducing a gas into a liquid |
CN104707496A (en) * | 2010-08-18 | 2015-06-17 | 三菱日立电力***株式会社 | Aeration device and system for flue-gas desulfurization with seawater which is equipped with same |
Also Published As
Publication number | Publication date |
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EP1724000B1 (en) | 2011-03-16 |
DE602006020656D1 (en) | 2011-04-28 |
ATE501783T1 (en) | 2011-04-15 |
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