CS270123B1 - Filter areal materials - Google Patents
Filter areal materials Download PDFInfo
- Publication number
- CS270123B1 CS270123B1 CS873366A CS336687A CS270123B1 CS 270123 B1 CS270123 B1 CS 270123B1 CS 873366 A CS873366 A CS 873366A CS 336687 A CS336687 A CS 336687A CS 270123 B1 CS270123 B1 CS 270123B1
- Authority
- CS
- Czechoslovakia
- Prior art keywords
- weight
- filter
- amount
- materials
- pulp
- Prior art date
Links
- 239000000463 material Substances 0.000 title claims abstract description 13
- 239000004952 Polyamide Substances 0.000 claims abstract description 4
- 229920002678 cellulose Polymers 0.000 claims abstract description 4
- 239000001913 cellulose Substances 0.000 claims abstract description 4
- 229920002647 polyamide Polymers 0.000 claims abstract description 4
- 229920000768 polyamine Polymers 0.000 claims abstract 2
- 239000002023 wood Substances 0.000 claims abstract 2
- 239000000835 fiber Substances 0.000 claims description 14
- 229920001131 Pulp (paper) Polymers 0.000 claims description 9
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 7
- 239000000203 mixture Substances 0.000 claims description 6
- 229920000742 Cotton Polymers 0.000 claims description 5
- 239000004577 thatch Substances 0.000 claims description 5
- 244000025254 Cannabis sativa Species 0.000 claims description 3
- 235000012766 Cannabis sativa ssp. sativa var. sativa Nutrition 0.000 claims description 3
- 235000012765 Cannabis sativa ssp. sativa var. spontanea Nutrition 0.000 claims description 3
- 239000004480 active ingredient Substances 0.000 claims description 3
- 235000009120 camo Nutrition 0.000 claims description 3
- 235000005607 chanvre indien Nutrition 0.000 claims description 3
- 239000011487 hemp Substances 0.000 claims description 3
- 229920005989 resin Polymers 0.000 claims description 3
- 239000011347 resin Substances 0.000 claims description 3
- BRLQWZUYTZBJKN-UHFFFAOYSA-N Epichlorohydrin Chemical compound ClCC1CO1 BRLQWZUYTZBJKN-UHFFFAOYSA-N 0.000 claims 1
- 239000004593 Epoxy Substances 0.000 claims 1
- 238000001914 filtration Methods 0.000 abstract description 8
- 235000013305 food Nutrition 0.000 abstract description 3
- 239000010426 asphalt Substances 0.000 abstract 2
- 239000013067 intermediate product Substances 0.000 abstract 1
- 239000011344 liquid material Substances 0.000 abstract 1
- 239000010425 asbestos Substances 0.000 description 4
- 229910052895 riebeckite Inorganic materials 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 239000002994 raw material Substances 0.000 description 3
- 239000003795 chemical substances by application Substances 0.000 description 2
- 239000003822 epoxy resin Substances 0.000 description 2
- 229920000647 polyepoxide Polymers 0.000 description 2
- 239000011148 porous material Substances 0.000 description 2
- 239000011122 softwood Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 241000196324 Embryophyta Species 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 1
- 125000003118 aryl group Chemical group 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000007865 diluting Methods 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 238000000265 homogenisation Methods 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 239000012633 leachable Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 229940127554 medical product Drugs 0.000 description 1
- 229940126601 medicinal product Drugs 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 238000004080 punching Methods 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- LSNNMFCWUKXFEE-UHFFFAOYSA-L sulfite Chemical compound [O-]S([O-])=O LSNNMFCWUKXFEE-UHFFFAOYSA-L 0.000 description 1
- 229910021653 sulphate ion Inorganic materials 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D39/00—Filtering material for liquid or gaseous fluids
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D39/00—Filtering material for liquid or gaseous fluids
- B01D39/14—Other self-supporting filtering material ; Other filtering material
- B01D39/16—Other self-supporting filtering material ; Other filtering material of organic material, e.g. synthetic fibres
- B01D39/18—Other self-supporting filtering material ; Other filtering material of organic material, e.g. synthetic fibres the material being cellulose or derivatives thereof
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H27/00—Special paper not otherwise provided for, e.g. made by multi-step processes
- D21H27/08—Filter paper
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Filtering Materials (AREA)
- Paper (AREA)
Abstract
Description
Predmetom vynálezu sú filtračně plošné materiály, zejména filtračně došky, používané na filtráciu kvapalín, najma к filtrácll potravinářských produktov, vody a medicinálnych výrobkov vo farmácii a ostatných priemyeelných produktov. k The subject of the invention is filter sheet materials, in particular filter seals, used for the filtration of liquids, in particular for the filtration of food products, water and medicinal products in pharmacy and other industrial products. to
Ooteraz sa na výrobu filtračných plošných materiálov používal vláknitý azbest v znesl 8 inými vláknitými surovinami, ako je zušlachtená buničina, bavlněný linters, připadne Salšie přísady a chemikálie. Množstvo azbestu vo filtračných materiáloch dosahovalo až 45 4 hmotnostných (ZSSR, Pat· 533 385; Filtrox-Werke A.G., St. Gallen, Schwiez: Firemně litera túra, 1976; Seitz - Werke, Bad Kreuznach, BRO: Firemně literatúra, 1974 - 1979; Euzinger Union-Werke, A.G. Mannheim, BRO: Firemně literatúra, 1974). Přítomnost’ azbestu vo filtrač ných materiěloch 1 cez jeho vynikajúce účinky je zdravotně nežiadúca, nakoTko uvolněná jemně vlákna azbeetu majú karcerogénné účinky.So far, fibrous asbestos has been used to produce filter sheet materials and has been taken up by 8 other fibrous raw materials such as refined pulp, cotton linters, or more salty ingredients and chemicals. The amount of asbestos in the filter materials was up to 45 4% by weight (USSR, Pat · 533 385; Filtrox-Werke AG, St. Gallen, Schwiez: Corporate Letter Hike, 1976; Seitz - Werke, Bad Kreuznach, BRO: Corporate Literature, 1974 - 1979 Euzinger Union-Werke, Mannheim AG, BRO: Firemne literatura, 1974). The presence of b asbestos in filter materials 1 despite its excellent effects is undesirable because the finely released asbestos fibers have carcerogenic effects.
Navrhované filtračně plošné materiály, zejmena filtračně došky, sa vyznačujú tým, že obsahujú pololétku, pozoetávajúou zo zušfaohtsných vlákien pradných rastlín (bavlněný liteře, lan, konope), v množstvo 1 až 50 4 hmotnostných; zuSIachtenů drevnú buničinu s ob sahom ^-celulózy nad 92% hmotnostných a bielanú papierenskú,buničinu v množstvo 5 - 984 hmotnostných, pričom vzájomný poměr dřevných buničín móže byť .1:1 až 4:1, áalej kalcinovanú kremelinu v množstvo 1 až 454 hmotnostných a polyamid - epoxidovú živicu, či polyamid polyamín - epichlórhydrlnovů živicu v množstvo 0,3 až 1,5 4 hmotnostných absolutné suchej (a.s) účinnej zložky.The proposed filter sheet materials, in particular filter thatch, are characterized in that they contain a half-fly, which is made from the fine fibers of the fiber plants (cotton liters, ropes, hemp), in an amount of 1 to 50% by weight; wood pulp containing? -cellulose over 92% by weight and white paper pulp in an amount of 5-984% by weight, wherein the ratio of wood pulp may be between 1: 1 to 4: 1 and calcined kieselguhr in an amount of 1 to 454% by weight and a polyamide-epoxy resin or polyamide-polyamine-epichlorohydrin resin in an amount of 0.3 to 1.5% by weight of the absolute dry (as) active ingredient.
Vláknité suroviny použitě pre filtračně došky a ostatně filtračně plošné materiály, slůžiace pre filtráciu potravinářských a medicinálnych produktov sa vyznačujú vysokou čistotou, nesmú spůsobovať farebné zákaly, chuťové, či aromatické vady· Kaloinované krsmelina sa vyznačuje vyeokou inertnosťou к filtrovaným médiám a obsah vodou vyluhovatel’ných látok je maximálně 0,34 hmotnostných.Fiber raw materials used for filtering thatch and other filtering surface materials used for filtration of food and medical products are characterized by high purity, must not cause color haze, taste or aromatic defects · Calloated kieselguhr is characterized by high inertia to filtered media and water leachable content substances is a maximum of 0.34% by weight.
Filtračně došky a ostatně filtračně plošné materiály připravené z vyššie uvedených surovin premenlivého zloženia. vláknitých komponent, granulometrického zloženia kremellny, jej množstva vo filtri, sa vyznačujú tým, že majú Sirokú účinnost a filtračný výkon. Podl’a priemyselného použitia slúžia na priamu filtráciu hrubších a jemnějších disperzi! až koloidných roztokov. Vyrábajů sa obvyklými papierenskými postupmi. Připravená papierovina podlá vyznačenej zanášky sa stvárňuje na site papierenského stroja, Sálej sa upravuje lisováním na potrebnú hrůbku a vo valcovej a teplovzdušnej sušiarni sa vysuší na konečnú sušinu 944 + 24, - 14.Filter-thatch and other filter-surface materials prepared from the aforementioned raw materials of variable composition. The fiber components, the granulometric composition of the silica, the amount thereof in the filter, are characterized by having a wide efficiency and filtration performance. According to industrial use, they are used for direct filtration of thicker and finer dispersions! to colloidal solutions. They are produced by conventional papermaking processes. The prepared pulp according to the marked furnish is rendered on a paper machine sieve, the sale is treated by pressing to the necessary depth and dried in a cylindrical and hot-air dryer to the final dry matter 944 + 24, - 14.
Přikladl , .Example,.
Z bavlněného llnterau vymletého na 20°SR, zuéfachtenej blelenej eulflnovéj ihllčnatej buničiny a bielenej papiersnskej ihličnatej buničiny v pomere 2:1 spoločne vymletých v zmesl no 22°8R aa připraví papierovina, pričom poměr zložlek bavlněného lintereu o zmesi zušTachteňej ,a papierenekej buničiny je 3:1. Na hmotu vlákien a.s. sa přidá kalcinovaná kremelina v množstva 804 hmotnostných, papierovina sa v holendri zhomogenizuje a potom sa přidá 14 hmotnostných polyamid - polyamín - epichlorhydrinová živica, počítaná na a.s. účinně zložku. Po zriedení bielou papierenskou vodou na koncentráciu 0,84 sa papierovina sformujé na pozdlžnom site papierenského stroja, tento sa Sálej upravuje lisováním za mokra a nakoniec sa vyauší na konečnú sušinu 944. Po vysušení sa na vyaekávaoom stroji pripravia’ hárky požadovaných rozmerov. Vyrobené filtračně plošně materiály majú plošnú hmotnost 1 300 g/m2, hrůbku 3,5 mm s priemernů velkost pórov do 2,2^um.From cotton lintter milled to 20 ° SR, scooped bleached eulfine softwood pulp and bleached softwood pulp in a ratio of 2: 1 co-milled in a mixture of no 22 ° 8R aa to prepare pulp, the ratio of cotton linters to 3 : first To the mass of the fibers, calcined diatomaceous earth is added in an amount of 804 wt. After diluting with white papermaking water to a concentration of 0.84, the papermaking is formed on the longitudinal sieve of the papermaking machine, the papermaking is wet-pressed and finally dried to a final dry weight of 944. After drying, sheets of the desired dimensions are prepared. The filter sheet materials produced have a basis weight of 1300 g / m 2 , a depth of 3.5 mm with a pore diameter of up to 2.2 µm.
Příklad 2Example 2
Pololátka připravená z lanových, či konopných vlákien sa rozvlákni a predomelie v ho lendri na 2O°SR. Ďalej sa přidá zušlachtená sulfitová dlhovláknitá buničina, zušlachtená sulfátová krátkovláknitá buničina a bislená dlhovláknitá papierenská buničina, pričom poměr dřevných buničín je 3:1:1 a celá zmes vlákisn sa zomelie na 24°SR, pričom sa к uvedenej zmesi vlákien přidá 0,8¾ hmotnostných polyamid - epoxidovej Živice a.s. účinnej zložky, po dókladnom rozmiešaní živice na vlákna sa přidá 65¾ hmotnostných kalcinovanej kremeliny a po dĎkladnej homogenizácii sa papierovina riedi papierenskou vodou na koncentráclu 0,4¾ a táto sa stvárftuje na okrúhlom site papierenského stroja na nekonečný pás, ktorý sa upravuje lisováním a sušením a teplovzdušnom kanále na sušinu 95¾. Při výstupe zo sušiarne sa na vysekávacom stroji pripravia došky požadovaných rozmerov. Plošná hmotnost filtračnej došky je 1 150 g/m , hrůbky 3,5 mm a priemerná velkost porov je 4,5 £jm.Semi-fabric prepared from rope or hemp fibers is pulled and pre-grinded to 20 ° SR in January. Refined sulphite long fiber pulp, refined sulphate short fiber pulp and bisected long pulp paper pulp are added, the wood pulp ratio being 3: 1: 1 and the whole fiber mixture is ground to 24 ° SR, 0.8µ by weight is added to said fiber mixture. polyamide - epoxy resin as of the active ingredient, after thoroughly mixing the resin into fibers, 65% by weight of calcined diatomaceous earth is added and after thorough homogenization, the paper is diluted with papermaking water to a 0.4¾ concentrate and formed on a round sieve of a paper machine to a continuous belt. dry matter channels 95¾. When leaving the dryer, the desired size is prepared on a punching machine. The basis weight of the filter thatch is 1,150 g / m @ 2, the thickness is 3.5 mm, and the average pore size is 4.5 .mu.m.
Claims (2)
Priority Applications (7)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CS873366A CS270123B1 (en) | 1987-05-12 | 1987-05-12 | Filter areal materials |
| BG8316788A BG50869A1 (en) | 1987-05-12 | 1988-03-01 | Filtration surface materials |
| YU90388A YU46543B (en) | 1987-05-12 | 1988-05-10 | PROCEDURE FOR THE PRODUCTION OF PLATE AND FLAT FILTER MATERIALS |
| FR8806378A FR2615119B3 (en) | 1987-05-12 | 1988-05-11 | FILTER PLATES AND FILTER MATERIALS PLANS |
| HU882367A HU202138B (en) | 1987-05-12 | 1988-05-11 | Composition and method for producing filtering sheet and flatlike filtering material |
| ES8801962A ES2006997A6 (en) | 1987-05-12 | 1988-05-12 | Filter plates and flat filter materials |
| PL27242288A PL272422A1 (en) | 1987-05-12 | 1988-05-12 | Filtration plates and planar filtrating materials |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CS873366A CS270123B1 (en) | 1987-05-12 | 1987-05-12 | Filter areal materials |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CS336687A1 CS336687A1 (en) | 1989-10-13 |
| CS270123B1 true CS270123B1 (en) | 1990-06-13 |
Family
ID=5373482
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CS873366A CS270123B1 (en) | 1987-05-12 | 1987-05-12 | Filter areal materials |
Country Status (7)
| Country | Link |
|---|---|
| BG (1) | BG50869A1 (en) |
| CS (1) | CS270123B1 (en) |
| ES (1) | ES2006997A6 (en) |
| FR (1) | FR2615119B3 (en) |
| HU (1) | HU202138B (en) |
| PL (1) | PL272422A1 (en) |
| YU (1) | YU46543B (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0741821A4 (en) * | 1993-12-28 | 1997-10-22 | Little Rapids Corp | Disposable filters and manufacturing process |
| US5554288A (en) * | 1993-12-28 | 1996-09-10 | Little Rapids Corporation | Disposable filters and manufacturing process |
-
1987
- 1987-05-12 CS CS873366A patent/CS270123B1/en unknown
-
1988
- 1988-03-01 BG BG8316788A patent/BG50869A1/en unknown
- 1988-05-10 YU YU90388A patent/YU46543B/en unknown
- 1988-05-11 HU HU882367A patent/HU202138B/en not_active IP Right Cessation
- 1988-05-11 FR FR8806378A patent/FR2615119B3/en not_active Expired
- 1988-05-12 PL PL27242288A patent/PL272422A1/en unknown
- 1988-05-12 ES ES8801962A patent/ES2006997A6/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| HU202138B (en) | 1991-02-28 |
| YU46543B (en) | 1993-11-16 |
| FR2615119A3 (en) | 1988-11-18 |
| YU90388A (en) | 1989-08-31 |
| HUT50066A (en) | 1989-12-28 |
| ES2006997A6 (en) | 1989-05-16 |
| CS336687A1 (en) | 1989-10-13 |
| BG50869A1 (en) | 1992-12-15 |
| PL272422A1 (en) | 1989-03-20 |
| FR2615119B3 (en) | 1989-07-07 |
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