CZ627589A3 - Process for treating mixed plastic waste containing pvdc polymers - Google Patents
Process for treating mixed plastic waste containing pvdc polymers Download PDFInfo
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- CZ627589A3 CZ627589A3 CS896275A CS627589A CZ627589A3 CZ 627589 A3 CZ627589 A3 CZ 627589A3 CS 896275 A CS896275 A CS 896275A CS 627589 A CS627589 A CS 627589A CZ 627589 A3 CZ627589 A3 CZ 627589A3
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- CZ
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- plastic waste
- mixture
- mixed plastic
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/62—Plastics recycling; Rubber recycling
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- Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
- Extrusion Moulding Of Plastics Or The Like (AREA)
Abstract
Description
(57) Zmes plastového odpadu obsahujúceho minimálně 15 % hmot. PVDC polymérov a PP sa v bežnom aglomeračnom zariadení upravuje prídavkom 5 až 40 % hmot. zmesi obsahujúcej 0,1 až 5 % hmot. erucylamidu, 1 až 10 % hmot. solí vyšších mastných kyselin s kovmi 2-skupiny a 85 až 98,9 % uhličitanov a/alebo hydroxidov Ca, AI, Mg.(57) A mixture of plastic waste containing at least 15% by weight of plastic waste. PVDC polymers and PP are treated in a conventional sintering plant by adding 5 to 40 wt. % of a mixture containing 0.1 to 5 wt. % erucylamide, 1 to 10 wt. salts of higher fatty acids with 2-group metals and 85 to 98.9% of carbonates and / or hydroxides of Ca, Al, Mg.
Vynález sa týká způsobu úpravy zmesných plastových odpadov obsahujúcich nevyužitelné polyvinylidénchloridové (PVDC)-lakované polypropylénové (PP)-fólie v množstve minimálně 15 % hmot· PVDC-polymérov přídavkem 5 až 40 % hmot· aditivněj zmesi zloženej z 0,1 % až 5 % hmot· klzných činidiel amidového typu, 1 % až 15 % hmot· solí vyšších mastných kyselin s kovmi 2 skupiny a 80 % až 98,9 % hmot· uhličitanov Ca, Mg, Al a/alebo hydroxidov uvedených kovov.BACKGROUND OF THE INVENTION 1. Field of the Invention % of amide type glidants, 1% to 15% of higher fatty acid salts of 2-group metals and 80% to 98.9% of Ca, Mg, Al and / or hydroxides of said metals.
Je známe, že uvedené polymérne odpady sú obvzlášť ťažko spracovateZné z důvodu velmi nízkéj tepelnej stability PVDC-polymérov, ktoré sa využívá jú na zlepšenie bariérových vlastností fólií, ako aj zváratelná vrstva· Pri tepelnom namáhaní, ku kterému pri opracovaní polymérov vždy dochádza, vzniká chlorovodík, ktorý spůsobuje koroziu spraoovatelských zariadení, značné znečisťuje pracovně prostredie a výrobok připravený z polymerneho odpadu obsahujúceho PVDC má velmi zlé mechanické vlastnosti.It is known that these polymeric wastes are particularly difficult to process due to the very low thermal stability of the PVDC polymers, which are used to improve the barrier properties of the films, as well as the weldable layer. , which causes corrosion of the process equipment, significantly pollutes the working environment and the product prepared from PVDC-containing polymeric waste has very poor mechanical properties.
Z týchto důvodov nie je doteraz známy taký technologický spůsob úpravy plastových odpadov obsahujúcich PVDC pólymáry, ktorý by umožnil ich spracovanie běžnými plastikářskými technologiemi. Možný spůsob úpravy naznačuje len U.S.P. 4643 861, ktorý uvádza zlepšenie tepelných vlastností a zníženie korozie zariadení prídavkom vápna /Ca(0H)2/ a karboxilátov kovov 2 skupiny· Nedostatkom tohto postupu je zlá spracovateZnosť vyrobeného plastového aglomerátů.For these reasons, there is not yet known such a technological method of treatment of plastic wastes containing PVDC polymorphs that would enable their processing by conventional plastic technologies. Only USP 4643 861, which discloses improving thermal properties and reducing the corrosion of equipment by the addition of lime (Ca (OH) 2 ) and metal group 2 carboxilates, suggests a possible treatment method.
Uvedené nedostatky odstraňuje spůsob úpravy zmesných plastových odpadov obsahujúcich PVDC-polyméry a polypropy2 prídavkom 0,1 až 5 % hmot· klzných činidiel amidového typu v zmesi β 1 až 15 % hmot· solí vyšších mastných kyselin s kov mi 2 skupiny a 80 až 98,9 % hmot· uhličitanmi Ca, AI, Mg a/alebo hydroxidmi uvedených kovov v množstve 5 až 40 % hmot* na celkovú hmotnost zmesi plastového odpadu·The above drawbacks are eliminated by the treatment of mixed plastic wastes containing PVDC-polymers and polypropy2 by the addition of 0.1 to 5% by weight of an amide type glidant in a mixture of 1 to 15% by weight of higher fatty acid salts of metals of 2 groups and 80 to 98, 9% by weight · Ca, Al, Mg carbonates and / or hydroxides of said metals in an amount of 5 to 40% by weight * based on the total weight of the plastic waste mixture ·
Uvedená aditívna zmes sa přidá do rozdrveného zmesného plastového odpadu pri aglomeraci! vo vodnéj suspenzi! pri bežnom postupe aglomerovania plastov, ktorá sa vykoná na běžných aglomeračných zariadeniach. Výhody spočívajú v tom, že takto vyrobený aglomerát Je možné využit ako vhodnú surovinu pře výrobky vyrábané vytláčením, vstrekovaním připadne lisováním·The additive mixture is added to the crushed mixed plastic waste during agglomeration! in an aqueous suspension! in a conventional plastic agglomeration process carried out on conventional agglomeration equipment. The advantage lies in the fact that the agglomerate thus produced can be used as a suitable raw material for extruded, injection molded or molded products.
Příklad 1.Example 1.
Zmesný plastový odpad vznikajúcl pri výrobě biaxiálně orientovaných polypropylénových folií PVDC-disperíami s obsahem 40 % hmot· PVDC-polymárov bol aglomerovaný běžným sposobom. Aglomerát bol testovaný na plastografe Brabender pri teplote 180 °C s cielom určit indukčnú periodu· Daná vzorka sa pri tejto teplote spontánně rozkládala a nebolo možná vzorku vyhodnotit·The mixed plastic waste resulting from the production of biaxially oriented polypropylene films by PVDC dispersions containing 40% by weight of PVDC polymers was agglomerated in a conventional manner. The agglomerate was tested on a Brabender plastograph at 180 ° C to determine the induction period. · The sample spontaneously decomposed at this temperature and the sample could not be evaluated
Příklad 2.Example 2.
Aglomerát připravený podlá příkladu 1 bol aditivovaný zmesou 90 % hmot· vápna a 10 % hmot· stearátu vápenatého o množstve 20 % hmot· v pomere k aglomerátů podlá U.S.P 4,643,861· Pri testovaní na plastografe Brabender vzorka pri teplote 180 °C degradovala do 10 min· s tým, že tmavnutie vzorky bolo pozorované už v priebehu 2 minút. Uvedená zmes bola skúšobne vytláčaná na dutý profil na zariadení BU 0 32 pri teplotách Jednotlivých pásiem 160 °C, 170 °C,The agglomerate prepared according to Example 1 was additivated with a mixture of 90% by weight lime and 10% by weight calcium stearate in an amount of 20% by weight relative to the USP 4,643,861 agglomerates. except that darkening of the sample was observed within 2 minutes. Said mixture was extruded to a hollow profile on a BU 0 32 at single band temperatures of 160 ° C, 170 ° C,
180 °C. Pri uvedených podmienkach nebolo možné vyrobit pov w žadovaný výrobok, kedže zmes pěnila, V dalšom bola s uvede3 nou zmesou odskúšaná technológla lisovania pri nasledovných podmienkach:Mp 180 ° C. Under the above conditions, it was not possible to produce the desired product as the mixture foamed. In the following, the molding technology was tested with the mixture under the following conditions:
teplota - 180 °Ctemperature - 180 ° C
Vyrobený výlisok bol celkom zdegradovaný a unikajúci chlorovodík značné znepříjemňoval pracovně prostredie.The molded part was completely degraded and the escaping hydrogen chloride made the work environment unpleasant.
Příklad 3.Example 3.
Aglomerát připravený podlá příkladu 1 bol aditivovaný zmesou obsahujúcou 4 % erucylamidu, 16 % Ca-stearátu a 80 % CaCO^ v laboratornej miešačke v celkovom množstve 20 % hmot. v přepočte na aglomerát. Zmes bola tepelne namáhaná na plastografe Brabender pri teplote 180 °C. Za uvedených podmienok nebolo možné namerať indukčnú periodu vzhladom k malým změnám v krútiacom momente. Pri sledovaní změny sfarbenia uvede ná vzorka měnila farbu až v priebehu 20 min. Uvedená zmes bola skúšobne vytláčená na dutý profil podlá příkladu 2.The agglomerate prepared according to Example 1 was additivated with a mixture containing 4% erucylamide, 16% Ca stearate and 80% CaCO 2 in a laboratory mixer in a total amount of 20% by weight. calculated in agglomerate. The mixture was thermally stressed on a Brabender plastograph at 180 ° C. Under these conditions it was not possible to measure the induction period due to small torque changes. When monitoring the change in color, the sample changed color within 20 min. The mixture was tested by extrusion to the hollow profile of Example 2.
Bol vyrobený profil, ktorý spíňal podmienky ako opora v záhradkách. Zmes bola v ďalsom lisovaná podlá příkladu 2. Výlisok nejavil známky ďegradácie a spinal podmienky pre využitie v stavebníctve ako tepelná a zvuková izolácia.A profile was made to support the conditions as a support in the gardens. The blend was further pressed according to Example 2. The molding showed no signs of degradation and spinal conditions for use in the building industry as thermal and acoustic insulation.
Příklad 4.Example 4.
Aglomerát připravený podlá příkladu 1 bol aditivovaný zmesou obsahujúcou 4 % hmot. erucylamidu, 6 % hmot. Ca-stearátu a 90 % hmot. Mg(0H)2 v množstve 30 % hmot. v přepočte na aglomerát. Zmes bola testovaná na laboratornom hnetiči Brabender pri teplote 180 °C. Pokles krútiaceho momentu nastal po 35 min. a změna farby (sčernenie vzorky) v priebehu 20 min. Zmes bola skúšobne vytláčaná na dutý profil podlá příkladu 2. Vyrobený profil splňal podmienky potřebná na opo ru v zahrádkách. Zmes bola lisovaná podlá podmienok příkladu 2. Výliaok nejavll známky degradácie a spinal podmienky pre využitie v stavebníctve ako tepelná a zvuková izolácia.The agglomerate prepared according to Example 1 was additivated with a mixture containing 4 wt. % erucylamide, 6 wt. Ca stearate and 90 wt. Mg (OH) 2 in an amount of 30 wt. calculated in agglomerate. The mixture was tested on a Brabender laboratory kneader at 180 ° C. Torque drop occurred after 35 min. and color change (sample blackening) within 20 min. The mixture was tested by extrusion on a hollow profile according to Example 2. The profile produced met the conditions required for support in the gardens. The mixture was molded according to the conditions of Example 2. The casting showed no sign of degradation and spinal conditions for use in the building industry as thermal and acoustic insulation.
Claims (1)
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SK6275-89A SK627589A3 (en) | 1989-11-06 | 1989-11-06 | Treatment method of mixtured plastic waste containing polyvinylidene chloride polymers |
CS19896275A CZ286277B6 (en) | 1989-11-06 | 1989-11-06 | Process of treating mixed plastic waste based on polypropylene and polyvinylidene chloride |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CS19896275A CZ286277B6 (en) | 1989-11-06 | 1989-11-06 | Process of treating mixed plastic waste based on polypropylene and polyvinylidene chloride |
Publications (2)
Publication Number | Publication Date |
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CZ627589A3 true CZ627589A3 (en) | 1994-01-19 |
CZ286277B6 CZ286277B6 (en) | 2000-03-15 |
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Application Number | Title | Priority Date | Filing Date |
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CS19896275A CZ286277B6 (en) | 1989-11-06 | 1989-11-06 | Process of treating mixed plastic waste based on polypropylene and polyvinylidene chloride |
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CZ (1) | CZ286277B6 (en) |
SK (1) | SK627589A3 (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
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DE19625110A1 (en) * | 1996-06-17 | 1997-12-18 | Finacor Anstalt | Plastic recycling process and process for the production of plastic materials |
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1989
- 1989-11-06 CZ CS19896275A patent/CZ286277B6/en not_active IP Right Cessation
- 1989-11-06 SK SK6275-89A patent/SK627589A3/en unknown
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Publication number | Publication date |
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SK627589A3 (en) | 1997-11-05 |
CZ286277B6 (en) | 2000-03-15 |
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Date | Code | Title | Description |
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IF00 | In force as of 2000-06-30 in czech republic | ||
MM4A | Patent lapsed due to non-payment of fee |
Effective date: 19891106 |