DE102008048727A1 - Device for filtering media e.g. lacquer/cathodic dipping lacquer, comprises membrane filter element, inlet to introduce unfiltered medium into the device, outlet to discharge filtered medium from the device, and filtrate collection chamber - Google Patents
Device for filtering media e.g. lacquer/cathodic dipping lacquer, comprises membrane filter element, inlet to introduce unfiltered medium into the device, outlet to discharge filtered medium from the device, and filtrate collection chamber Download PDFInfo
- Publication number
- DE102008048727A1 DE102008048727A1 DE102008048727A DE102008048727A DE102008048727A1 DE 102008048727 A1 DE102008048727 A1 DE 102008048727A1 DE 102008048727 A DE102008048727 A DE 102008048727A DE 102008048727 A DE102008048727 A DE 102008048727A DE 102008048727 A1 DE102008048727 A1 DE 102008048727A1
- Authority
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- Germany
- Prior art keywords
- filter device
- filter element
- membrane filter
- media flow
- flow channel
- 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.)
- Ceased
Links
- 239000012528 membrane Substances 0.000 title claims abstract description 71
- 239000000706 filtrate Substances 0.000 title claims abstract description 21
- 238000001914 filtration Methods 0.000 title claims abstract description 16
- 239000004922 lacquer Substances 0.000 title claims abstract description 7
- 238000007598 dipping method Methods 0.000 title abstract description 3
- 239000004020 conductor Substances 0.000 claims abstract description 23
- 125000006850 spacer group Chemical group 0.000 claims abstract description 15
- 238000000034 method Methods 0.000 claims abstract description 14
- 229920000642 polymer Polymers 0.000 claims abstract description 9
- 239000002184 metal Substances 0.000 claims abstract description 6
- 239000011368 organic material Substances 0.000 claims abstract description 6
- 238000004804 winding Methods 0.000 claims abstract description 5
- 238000000576 coating method Methods 0.000 claims abstract description 4
- 239000003973 paint Substances 0.000 claims description 23
- 229920002301 cellulose acetate Polymers 0.000 claims description 10
- 239000002033 PVDF binder Substances 0.000 claims description 4
- 239000004743 Polypropylene Substances 0.000 claims description 4
- 229920002492 poly(sulfone) Polymers 0.000 claims description 4
- 229920002239 polyacrylonitrile Polymers 0.000 claims description 4
- 229920001155 polypropylene Polymers 0.000 claims description 4
- 229920002981 polyvinylidene fluoride Polymers 0.000 claims description 4
- 239000004952 Polyamide Substances 0.000 claims description 3
- 235000013361 beverage Nutrition 0.000 claims description 3
- 239000000463 material Substances 0.000 claims description 3
- 229920002647 polyamide Polymers 0.000 claims description 3
- 239000002351 wastewater Substances 0.000 claims description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 3
- 229920012266 Poly(ether sulfone) PES Polymers 0.000 claims description 2
- 235000013365 dairy product Nutrition 0.000 claims description 2
- 239000004417 polycarbonate Substances 0.000 claims description 2
- 229920000515 polycarbonate Polymers 0.000 claims description 2
- -1 polypropylene Polymers 0.000 claims description 2
- 239000004627 regenerated cellulose Substances 0.000 claims description 2
- 239000006223 plastic coating Substances 0.000 claims 1
- 239000004033 plastic Substances 0.000 abstract description 3
- 229920003023 plastic Polymers 0.000 abstract description 3
- 238000007599 discharging Methods 0.000 abstract 2
- 239000011248 coating agent Substances 0.000 abstract 1
- 239000004744 fabric Substances 0.000 abstract 1
- 239000002861 polymer material Substances 0.000 abstract 1
- 239000002245 particle Substances 0.000 description 8
- 239000007788 liquid Substances 0.000 description 6
- 239000000919 ceramic Substances 0.000 description 5
- 230000000694 effects Effects 0.000 description 4
- 238000005470 impregnation Methods 0.000 description 3
- 239000000853 adhesive Substances 0.000 description 2
- 230000001070 adhesive effect Effects 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 2
- 238000009295 crossflow filtration Methods 0.000 description 2
- 229920005597 polymer membrane Polymers 0.000 description 2
- 238000007789 sealing Methods 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 230000003068 static effect Effects 0.000 description 2
- BUHVIAUBTBOHAG-FOYDDCNASA-N (2r,3r,4s,5r)-2-[6-[[2-(3,5-dimethoxyphenyl)-2-(2-methylphenyl)ethyl]amino]purin-9-yl]-5-(hydroxymethyl)oxolane-3,4-diol Chemical compound COC1=CC(OC)=CC(C(CNC=2C=3N=CN(C=3N=CN=2)[C@H]2[C@@H]([C@H](O)[C@@H](CO)O2)O)C=2C(=CC=CC=2)C)=C1 BUHVIAUBTBOHAG-FOYDDCNASA-N 0.000 description 1
- TVEXGJYMHHTVKP-UHFFFAOYSA-N 6-oxabicyclo[3.2.1]oct-3-en-7-one Chemical compound C1C2C(=O)OC1C=CC2 TVEXGJYMHHTVKP-UHFFFAOYSA-N 0.000 description 1
- 229920002873 Polyethylenimine Polymers 0.000 description 1
- 230000001174 ascending effect Effects 0.000 description 1
- 239000012459 cleaning agent Substances 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 238000003618 dip coating Methods 0.000 description 1
- 238000005108 dry cleaning Methods 0.000 description 1
- 239000012510 hollow fiber Substances 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 239000010954 inorganic particle Substances 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 238000001471 micro-filtration Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 238000001728 nano-filtration Methods 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 230000003472 neutralizing effect Effects 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 238000000108 ultra-filtration Methods 0.000 description 1
- 239000002966 varnish Substances 0.000 description 1
Classifications
-
- 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
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
- C02F1/442—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by nanofiltration
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
- C02F1/444—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by ultrafiltration or microfiltration
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/14—Paint wastes
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/32—Nature of the water, waste water, sewage or sludge to be treated from the food or foodstuff industry, e.g. brewery waste waters
- C02F2103/327—Nature of the water, waste water, sewage or sludge to be treated from the food or foodstuff industry, e.g. brewery waste waters from processes relating to the production of dairy products
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Organic Chemistry (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
Description
Die vorliegende Erfindung betrifft eine Filtervorrichtung gemäß dem Oberbegriff des Anspruchs 1, sowie ein Verfahren zur Filtrierung in flüssigen Medien, speziell Lacken, insbesondere kathodischen Tauchlacken, gemäß dem Oberbegriff des Anspruchs 12.The The present invention relates to a filter device according to the The preamble of claim 1, as well as a method for filtering in liquid media, especially paints, in particular cathodic dip paints, according to the preamble of claim 12.
Grundsätzlich sind Filtervorrichtungen in statische und dynamische Filter zu unterscheiden. Bei statischen Filtern werden die Membranfilterelemente komplett vom Medium durchströmt, nicht porengängige Partikel werden an der Oberfläche des Membranfilterelementes zurückgehalten. Bei dynamischen Filtern wird das Membranfilterelement tangential und turbulent vom Medium überströmt, wobei porengängige Anteile des Mediums durch das Membranfilterelement in die Filtratsammelkammer übertreten. Grundsätzlich lassen sich dynamische Membranfilterelemente in Platten-, Rohr-, Kapillar-, Hohlfaser- und Wickelmodule unterscheiden. Insbesondere bei Plattenmodulen sind neben der traditionellen plate-and-frame Ausführung mit einer einfachen Durchströmung des Membranfilterelementes weitere unterschiedliche konstruktive Verfahren zur Erreichung der oberflächennahen Turbulenz bekannt. Beispielsweise wird die Turbulenz über den Membranen durch Eigenrotation gegeneinander oder darüber feststehenden Scherelementen oder sich über den Membranen bewegenden Rotoren oder durch aufsteigende Gasblasen tangential zum Membranfilterelement erzeugt. Ferner unterscheiden sich die Systeme in der Art des angelegten Druckes. Vielfach wird das Medium durch die Filtervorrichtung mit Druck gepumpt, andere Verfahren basieren auf einem Unterdruck an der Filtratseite.in principle filter devices are to be differentiated into static and dynamic filters. With static filters, the membrane filter elements become complete flows through the medium, non-porous particles are retained on the surface of the membrane filter element. For dynamic filters, the membrane filter element becomes tangent and turbulent flowed over by the medium, with porängängige Passages of the medium through the membrane filter element in the filtrate collection chamber. in principle can dynamic membrane filter elements in plate, tube, Capillary, hollow fiber and wound modules differ. Especially for plate modules are in addition to the traditional plate-and-frame Design with a simple flow through the Membrane filter element further different constructive procedures known to achieve near-surface turbulence. For example, the turbulence over the membranes by self-rotation against each other or above fixed shear elements or over the membranes moving rotors or through ascending gas bubbles generated tangentially to the membrane filter element. Furthermore, the systems differ in the type of applied Pressure. In many cases, the medium is through the filter device with Pressure pumped, other methods are based on a negative pressure at the Filtrate side.
Es
ist, beispielsweise aus der Beschreibungseinleitung der
Positiv geladene Lackpartikel neigen dazu an der negativ oder positiv geladenen Membranoberfläche anzuhaften. Hierdurch werden die Membranfilterelemente mehr oder weniger schnell u. a. mit anorganischen positiv geladenen Lackinhaltsstoffen belegt, die nur bedingt bzw. nicht mehr abreinigbar sind.positive charged paint particles tend to be negatively or positively charged To adhere membrane surface. As a result, the membrane filter elements more or less fast u. a. with inorganic positively charged Lackinhaltsstoffen occupied, the only conditionally or no longer cleanable are.
Polymermembranfilterelemente, aus beispielsweise Polyvenylidenfluorid (PVDF) oder Zelluloseacetat (CA), sind negativ oder positiv geladen, wodurch der oben skizzierte Effekt hier zu beobachten ist. Keramik hat sogar noch eine deutlich stärkere negative Ladung als Polyvenylidenfluorid (PVDF) oder Zelluloseacetat (CA), wodurch die zuvor skizzierten Effekte der Anlagerung von positiv geladenen Lackpartikeln bei Membranfilterelementen auf Keramikbasis noch verstärkt zu erwarten sind.Polymeric membrane filter elements, from, for example, polyvinylidene fluoride (PVDF) or cellulose acetate (CA), are negatively or positively charged, causing the above outlined Effect can be observed here. Ceramics have even more stronger negative charge than Polyvenylidenfluorid (PVDF) or Cellulose acetate (CA), whereby the effects outlined above Addition of positively charged paint particles in membrane filter elements On ceramics basis are to be expected even more.
Zur
Abwendung dieses unerwünschten Effektes wird beispielsweise
in der bereits oben genannten
Soweit zur KTL Filtration Membranfilterelementen auf Polymerbasis eingesetzt werden, kommen aus Kostengründen überwiegend Spiralwickelmodule und Plattenmodule zum Einsatz. Aber auch hier sind die zuvor skizzierten Effekte der Anlagerung von positiv geladene Lackpartikeln zu beobachten. Auch hierzu sind einige Maßnahmen bekannt geworden, die Anlagerung von positiv geladenen Lackpartikeln zu reduzieren.So far used for KTL filtration polymer-based membrane filter elements For cost reasons, mostly spiral-wound modules are used and disk modules are used. But here are the ones outlined above To observe effects of the addition of positively charged paint particles. Also For this purpose, some measures have become known, the attachment of positively charged paint particles.
Beispielsweise
schlägt die
Die Aufgabe der vorliegenden Erfindung liegt nunmehr darin, eine Filtervorrichtung mit einem organischen Membranfilterelement, insbesondere einem Polymermembranfilterelement vorzuschlagen, bei der das Membranfilterelement eine geringere Affinität zur Anlagerung von positiv geladene Partikeln, insbesondere Lackpartikeln aufweisen, um deren wirtschaftliche Einsetzbarkeit, insbesondere bei der Reinigung von kathodischen Tauchlacken zu ermöglichen.The Object of the present invention is now in a filter device with an organic membrane filter element, in particular a polymer membrane filter element to propose, in which the membrane filter element has a lower affinity for Addition of positively charged particles, in particular paint particles to their economic feasibility, in particular to facilitate the cleaning of cathodic dipping paints.
Erfindungsgemäß wird diese Aufgabe dadurch gelöst, dass das Membranfilterelement mit einem wirksamen Erdungspfad gegen Erdmasse ausgestattet ist.According to the invention this object is achieved in that the membrane filter element equipped with an effective grounding path against earth mass.
Durch diese Maßnahme kann sichergestellt werden, dass scher- bzw. ladungsempfindliche Moleküle in einer Flüssigkeit am Entstehungsort ihrer temporären molekularen Ladungsstörung ein sofortiger Potentialausgleich in Form eines sicheren Erdungspfades zur Verfügung gestellt wird, wodurch ihr neutraler Charakter erhalten bleibt und die Gefahr der elektrostatischen Bindung an einer negativ oder positiv oder neutrale geladene organischen Membranoberfläche, insbesondere einer Polymermembran, d. h. einer Kunststoffmembran, verhindert wird.By this measure can ensure that or charge-sensitive molecules in a liquid at the site of their temporary molecular charge disorder an immediate potential equalization in the form of a safe grounding path is provided, thereby neutralizing their character preserves and the danger of electrostatic binding a negatively or positively or neutrally charged organic membrane surface, in particular a polymer membrane, d. H. a plastic membrane, is prevented.
Ferner kann durch die erfindungsgemäß vorgeschlagene Maßnahme sichergestellt werden, dass die Filterleistungswerte im Rahmen der bisher erreichten Filterleistungswerte nach Inbetriebnahme liegen, aber eine deutlich längere Langzeitstabilität bzw. eine niedrigere Belagsrate positiv geladener Moleküle auf dem Membranfilterelement erreicht wird. Durch die erfindungsgemäße Ausgestaltung eines Erdungspfades für das mindestens eine Membranfilterelement kann eine Standzeitverlängerung bzw. eine Fouling-Verhinderung des Membranfilterelements erreicht werden. Mit der vorgeschlagenen Filtervorrichtung können hohe Filtratmengen produziert werden, welche in aller Regel für Folgeprozesse, wie z. B. Spülvorgänge, verwendet werden. Entweder kommen hohe Funktionsleistungen (Filtratleistungen) den Folgeprozessen in qualitativer Hinsicht zugute, oder Filtervorrichtungen können kleiner und damit kostengünstiger dimensioniert werden. Diese Aspekte in Kombination mit deutlich verlängerten Standzeiten erlauben bislang nicht erreichbare Kostensenkungspotentiale für die gattungsgemäßen Filtervorrichtungen zu erschließen.Further can by the invention proposed Measure ensure that the filter performance values are within the previously achieved filter performance values after commissioning, but a significantly longer long-term stability or a lower deposition rate of positively charged molecules the membrane filter element is achieved. By the invention Design of a grounding path for the at least one Membrane filter element can be a life extension or a fouling prevention of the membrane filter element can be achieved. With the proposed filter device can high Filtratmengen which are usually used for follow-up processes, such as B. rinses are used. Either High functional performances (filtrate performances) come to follow-up processes in qualitative terms, or filter devices may smaller and thus cost-effective dimensions. These aspects in combination with significantly longer service life allow previously unattainable cost reduction potential for to develop the generic filter devices.
Weitere vorteilhafte Ausgestaltungen der vorgeschlagenen Erfindung ergeben sich aus den Merkmalen der Unteransprüche.Further yield advantageous embodiments of the proposed invention from the features of the subclaims.
Eine weitere Aufgabe der vorliegenden Erfindung liegt darin, ein Verfahren zur Filtrierung von Lacken, insbesondere kathodischen Tauchlacken, vorzuschlagen, welches eine besonders wirtschaftliche Filterung von Lacken, insbesondere kathodischen Tauchlacken, ermöglicht.A Another object of the present invention is to provide a method for the filtration of paints, in particular cathodic dip paints, to propose, which is a particularly economical filtering of paints, especially cathodic dip paints allows.
Erfindungsgemäß wird
diese Aufgabe durch ein Verfahren mit den kennzeichnenden Merkmalen des
Anspruchs 12 gelöst. Dadurch, dass der Lack mit einer Filtervorrichtung
- 11
- Filtrat Sammelrohrfiltrate manifold
- 1a1a
- Filtrat Sammelrohrperforationfiltrate Sammelrohrperforation
- 22
- Filtermembran als Sandwichfilter membrane as a sandwich
- 33
- Spannbänderstraps
- 44
- Abstandshalter (spacer)spacer (Spacer)
- 55
- AntitelskopiersternAntitelskopierstern
- 66
- Medieneingang (Einlass)media input (Inlet)
- 6a6a
- Filtratfiltrate
- 6b6b
- Medienausgang/Auslass (Konzentrat)Media output / outlet (Concentrate)
- 6c6c
- MedienströmungskanalMedia flow channel
- 77
- Filtratsammelkammerfiltrate
- 88th
- Dichtungsringsealing ring
- 99
- Sandwich Klebenahtsandwich adhesive seam
- 1010
- Leiterladder
- 1111
- Membranfilterelement als WickelmodulMembrane filter element as a winding module
- 1212
- Filtergehäusefilter housing
- 1313
- Filtervorrichtungfilter means
- 1414
- MedienströmungskanalleiterMedia flow channel manager
Eine
erfindungsgemäß Filtervorrichtung
Bei
dem Membranfilterelement
Bei
dem Membranfilterelement
Das
Membranfilterelement
Die
Funktionsweise bzw. das Filterverfahren und weitere Details der
in
Das
zu filtrierende Medium wird der Filtervorrichtung über
einen Einlass
Erfindungsgemäß ist
vorgesehen, dass das mindestens teilweise aus einem organischen
Material bestehende Membranfilterelement
Ferner
sind in
Der
Erdungspfad umfasst im Wesentlichen mindestens einen Medienströmungskanalleiter
Der
Medienströmungskanalleiter
Es
kann ebenfalls vorgesehen sein, dass die Medienströmungskanalleiter
Die
Anordnung von Medienströmungskanalleitern
Die
vorgeschlagene Filtervorrichtung
ZITATE ENTHALTEN IN DER BESCHREIBUNGQUOTES INCLUDE IN THE DESCRIPTION
Diese Liste der vom Anmelder aufgeführten Dokumente wurde automatisiert erzeugt und ist ausschließlich zur besseren Information des Lesers aufgenommen. Die Liste ist nicht Bestandteil der deutschen Patent- bzw. Gebrauchsmusteranmeldung. Das DPMA übernimmt keinerlei Haftung für etwaige Fehler oder Auslassungen.This list The documents listed by the applicant have been automated generated and is solely for better information recorded by the reader. The list is not part of the German Patent or utility model application. The DPMA takes over no liability for any errors or omissions.
Zitierte PatentliteraturCited patent literature
- - EP 1138370 A2 [0003, 0006] - EP 1138370 A2 [0003, 0006]
- - US 5391426 [0008] - US 5391426 [0008]
- - US 4849106 [0008] - US 4849106 [0008]
Claims (12)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE102008048727A DE102008048727A1 (en) | 2008-09-24 | 2008-09-24 | Device for filtering media e.g. lacquer/cathodic dipping lacquer, comprises membrane filter element, inlet to introduce unfiltered medium into the device, outlet to discharge filtered medium from the device, and filtrate collection chamber |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE102008048727A DE102008048727A1 (en) | 2008-09-24 | 2008-09-24 | Device for filtering media e.g. lacquer/cathodic dipping lacquer, comprises membrane filter element, inlet to introduce unfiltered medium into the device, outlet to discharge filtered medium from the device, and filtrate collection chamber |
Publications (1)
Publication Number | Publication Date |
---|---|
DE102008048727A1 true DE102008048727A1 (en) | 2010-03-25 |
Family
ID=41693888
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DE102008048727A Ceased DE102008048727A1 (en) | 2008-09-24 | 2008-09-24 | Device for filtering media e.g. lacquer/cathodic dipping lacquer, comprises membrane filter element, inlet to introduce unfiltered medium into the device, outlet to discharge filtered medium from the device, and filtrate collection chamber |
Country Status (1)
Country | Link |
---|---|
DE (1) | DE102008048727A1 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102012006320A1 (en) * | 2012-03-28 | 2013-10-02 | Manfred Völker | Membrane for reverse osmosis |
Citations (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3030097A1 (en) * | 1979-08-14 | 1981-03-26 | Nitto Electric Industrial Co., Ltd., Ibaraki, Osaka | TUBULAR MEMBRANE COMPONENT WITH SELECTIVE PERMEABILITY FOR TREATING ORGANIC SOLUTIONS |
JPS59173106A (en) * | 1983-03-23 | 1984-10-01 | Nitto Electric Ind Co Ltd | Tubular membrane separation module |
JPS59199003A (en) * | 1983-04-26 | 1984-11-12 | Asahi Chem Ind Co Ltd | Membraneous separation module for filtering oil |
JPS63302906A (en) * | 1987-06-03 | 1988-12-09 | Asahi Chem Ind Co Ltd | Hollow yarn type filter for treating condensate |
JPS6490004A (en) * | 1987-09-30 | 1989-04-05 | Hitachi Ltd | Hollow yarn membrane filter |
US4849106A (en) | 1983-06-06 | 1989-07-18 | Koch Membrane Systems, Inc. | Positive-charged ultrafiltration membrane for the separation of cathodic electrodeposition paint compositions |
DE3839985C2 (en) * | 1988-11-26 | 1992-06-11 | Daimler-Benz Aktiengesellschaft, 7000 Stuttgart, De | |
DE4223181A1 (en) * | 1992-07-15 | 1994-01-20 | Herberts Gmbh | Process for the reprocessing of electrocoating baths |
US5391426A (en) | 1992-03-11 | 1995-02-21 | W. L. Gore & Associates, Inc. | Polyalkyleneimine coated material |
DE19931261A1 (en) * | 1999-07-07 | 2001-01-18 | Roland Damm | Microfiltration process |
EP1138370A2 (en) | 2000-03-31 | 2001-10-04 | Atech Innovations GmbH | Filtering device for microfiltration and/or ultrafiltration |
EP1204464B1 (en) * | 1999-08-17 | 2003-04-09 | E.I. Du Pont De Nemours And Company | Cleaning agent and method for cleaning ultrafiltration membranes in electrophoretic dip coating installations |
-
2008
- 2008-09-24 DE DE102008048727A patent/DE102008048727A1/en not_active Ceased
Patent Citations (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3030097A1 (en) * | 1979-08-14 | 1981-03-26 | Nitto Electric Industrial Co., Ltd., Ibaraki, Osaka | TUBULAR MEMBRANE COMPONENT WITH SELECTIVE PERMEABILITY FOR TREATING ORGANIC SOLUTIONS |
JPS59173106A (en) * | 1983-03-23 | 1984-10-01 | Nitto Electric Ind Co Ltd | Tubular membrane separation module |
JPS59199003A (en) * | 1983-04-26 | 1984-11-12 | Asahi Chem Ind Co Ltd | Membraneous separation module for filtering oil |
US4849106A (en) | 1983-06-06 | 1989-07-18 | Koch Membrane Systems, Inc. | Positive-charged ultrafiltration membrane for the separation of cathodic electrodeposition paint compositions |
JPS63302906A (en) * | 1987-06-03 | 1988-12-09 | Asahi Chem Ind Co Ltd | Hollow yarn type filter for treating condensate |
JPS6490004A (en) * | 1987-09-30 | 1989-04-05 | Hitachi Ltd | Hollow yarn membrane filter |
DE3839985C2 (en) * | 1988-11-26 | 1992-06-11 | Daimler-Benz Aktiengesellschaft, 7000 Stuttgart, De | |
US5391426A (en) | 1992-03-11 | 1995-02-21 | W. L. Gore & Associates, Inc. | Polyalkyleneimine coated material |
DE4223181A1 (en) * | 1992-07-15 | 1994-01-20 | Herberts Gmbh | Process for the reprocessing of electrocoating baths |
DE19931261A1 (en) * | 1999-07-07 | 2001-01-18 | Roland Damm | Microfiltration process |
EP1204464B1 (en) * | 1999-08-17 | 2003-04-09 | E.I. Du Pont De Nemours And Company | Cleaning agent and method for cleaning ultrafiltration membranes in electrophoretic dip coating installations |
EP1138370A2 (en) | 2000-03-31 | 2001-10-04 | Atech Innovations GmbH | Filtering device for microfiltration and/or ultrafiltration |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102012006320A1 (en) * | 2012-03-28 | 2013-10-02 | Manfred Völker | Membrane for reverse osmosis |
RU2555037C2 (en) * | 2012-03-28 | 2015-07-10 | Манфред ФЁЛЬКЕР | Membrane for reverse osmosis |
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