NO120009B - - Google Patents

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Publication number
NO120009B
NO120009B NO156718A NO15671865A NO120009B NO 120009 B NO120009 B NO 120009B NO 156718 A NO156718 A NO 156718A NO 15671865 A NO15671865 A NO 15671865A NO 120009 B NO120009 B NO 120009B
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NO
Norway
Prior art keywords
polyethylene terephthalate
methanol
terephthalic acid
weight
boiling organic
Prior art date
Application number
NO156718A
Other languages
Norwegian (no)
Inventor
J Dunn
Original Assignee
Eastman Kodak Co
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Eastman Kodak Co filed Critical Eastman Kodak Co
Publication of NO120009B publication Critical patent/NO120009B/no

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    • GPHYSICS
    • G03PHOTOGRAPHY; CINEMATOGRAPHY; ANALOGOUS TECHNIQUES USING WAVES OTHER THAN OPTICAL WAVES; ELECTROGRAPHY; HOLOGRAPHY
    • G03CPHOTOSENSITIVE MATERIALS FOR PHOTOGRAPHIC PURPOSES; PHOTOGRAPHIC PROCESSES, e.g. CINE, X-RAY, COLOUR, STEREO-PHOTOGRAPHIC PROCESSES; AUXILIARY PROCESSES IN PHOTOGRAPHY
    • G03C1/00Photosensitive materials
    • G03C1/005Silver halide emulsions; Preparation thereof; Physical treatment thereof; Incorporation of additives therein
    • G03C1/06Silver halide emulsions; Preparation thereof; Physical treatment thereof; Incorporation of additives therein with non-macromolecular additives
    • G03C1/08Sensitivity-increasing substances
    • G03C1/09Noble metals or mercury; Salts or compounds thereof; Sulfur, selenium or tellurium, or compounds thereof, e.g. for chemical sensitising
    • GPHYSICS
    • G03PHOTOGRAPHY; CINEMATOGRAPHY; ANALOGOUS TECHNIQUES USING WAVES OTHER THAN OPTICAL WAVES; ELECTROGRAPHY; HOLOGRAPHY
    • G03CPHOTOSENSITIVE MATERIALS FOR PHOTOGRAPHIC PURPOSES; PHOTOGRAPHIC PROCESSES, e.g. CINE, X-RAY, COLOUR, STEREO-PHOTOGRAPHIC PROCESSES; AUXILIARY PROCESSES IN PHOTOGRAPHY
    • G03C1/00Photosensitive materials
    • G03C1/494Silver salt compositions other than silver halide emulsions; Photothermographic systems ; Thermographic systems using noble metal compounds
    • G03C1/496Binder-free compositions, e.g. evaporated
    • G03C1/4965Binder-free compositions, e.g. evaporated evaporated
    • GPHYSICS
    • G03PHOTOGRAPHY; CINEMATOGRAPHY; ANALOGOUS TECHNIQUES USING WAVES OTHER THAN OPTICAL WAVES; ELECTROGRAPHY; HOLOGRAPHY
    • G03CPHOTOSENSITIVE MATERIALS FOR PHOTOGRAPHIC PURPOSES; PHOTOGRAPHIC PROCESSES, e.g. CINE, X-RAY, COLOUR, STEREO-PHOTOGRAPHIC PROCESSES; AUXILIARY PROCESSES IN PHOTOGRAPHY
    • G03C1/00Photosensitive materials
    • G03C1/72Photosensitive compositions not covered by the groups G03C1/005 - G03C1/705
    • G03C1/725Photosensitive compositions not covered by the groups G03C1/005 - G03C1/705 containing inorganic compounds
    • GPHYSICS
    • G03PHOTOGRAPHY; CINEMATOGRAPHY; ANALOGOUS TECHNIQUES USING WAVES OTHER THAN OPTICAL WAVES; ELECTROGRAPHY; HOLOGRAPHY
    • G03CPHOTOSENSITIVE MATERIALS FOR PHOTOGRAPHIC PURPOSES; PHOTOGRAPHIC PROCESSES, e.g. CINE, X-RAY, COLOUR, STEREO-PHOTOGRAPHIC PROCESSES; AUXILIARY PROCESSES IN PHOTOGRAPHY
    • G03C1/00Photosensitive materials
    • G03C1/72Photosensitive compositions not covered by the groups G03C1/005 - G03C1/705
    • G03C1/725Photosensitive compositions not covered by the groups G03C1/005 - G03C1/705 containing inorganic compounds
    • G03C1/7253Lead salts
    • GPHYSICS
    • G03PHOTOGRAPHY; CINEMATOGRAPHY; ANALOGOUS TECHNIQUES USING WAVES OTHER THAN OPTICAL WAVES; ELECTROGRAPHY; HOLOGRAPHY
    • G03CPHOTOSENSITIVE MATERIALS FOR PHOTOGRAPHIC PURPOSES; PHOTOGRAPHIC PROCESSES, e.g. CINE, X-RAY, COLOUR, STEREO-PHOTOGRAPHIC PROCESSES; AUXILIARY PROCESSES IN PHOTOGRAPHY
    • G03C1/00Photosensitive materials
    • G03C1/005Silver halide emulsions; Preparation thereof; Physical treatment thereof; Incorporation of additives therein
    • G03C1/06Silver halide emulsions; Preparation thereof; Physical treatment thereof; Incorporation of additives therein with non-macromolecular additives
    • G03C1/08Sensitivity-increasing substances
    • G03C1/09Noble metals or mercury; Salts or compounds thereof; Sulfur, selenium or tellurium, or compounds thereof, e.g. for chemical sensitising
    • G03C2001/091Gold
    • GPHYSICS
    • G03PHOTOGRAPHY; CINEMATOGRAPHY; ANALOGOUS TECHNIQUES USING WAVES OTHER THAN OPTICAL WAVES; ELECTROGRAPHY; HOLOGRAPHY
    • G03CPHOTOSENSITIVE MATERIALS FOR PHOTOGRAPHIC PURPOSES; PHOTOGRAPHIC PROCESSES, e.g. CINE, X-RAY, COLOUR, STEREO-PHOTOGRAPHIC PROCESSES; AUXILIARY PROCESSES IN PHOTOGRAPHY
    • G03C1/00Photosensitive materials
    • G03C1/005Silver halide emulsions; Preparation thereof; Physical treatment thereof; Incorporation of additives therein
    • G03C1/06Silver halide emulsions; Preparation thereof; Physical treatment thereof; Incorporation of additives therein with non-macromolecular additives
    • G03C1/08Sensitivity-increasing substances
    • G03C1/09Noble metals or mercury; Salts or compounds thereof; Sulfur, selenium or tellurium, or compounds thereof, e.g. for chemical sensitising
    • G03C2001/095Disulfide or dichalcogenide compound
    • GPHYSICS
    • G03PHOTOGRAPHY; CINEMATOGRAPHY; ANALOGOUS TECHNIQUES USING WAVES OTHER THAN OPTICAL WAVES; ELECTROGRAPHY; HOLOGRAPHY
    • G03CPHOTOSENSITIVE MATERIALS FOR PHOTOGRAPHIC PURPOSES; PHOTOGRAPHIC PROCESSES, e.g. CINE, X-RAY, COLOUR, STEREO-PHOTOGRAPHIC PROCESSES; AUXILIARY PROCESSES IN PHOTOGRAPHY
    • G03C1/00Photosensitive materials
    • G03C1/005Silver halide emulsions; Preparation thereof; Physical treatment thereof; Incorporation of additives therein
    • G03C1/06Silver halide emulsions; Preparation thereof; Physical treatment thereof; Incorporation of additives therein with non-macromolecular additives
    • G03C1/08Sensitivity-increasing substances
    • G03C1/09Noble metals or mercury; Salts or compounds thereof; Sulfur, selenium or tellurium, or compounds thereof, e.g. for chemical sensitising
    • G03C2001/097Selenium

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  • Chemical & Material Sciences (AREA)
  • Physics & Mathematics (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • General Physics & Mathematics (AREA)
  • Inorganic Chemistry (AREA)
  • Spectroscopy & Molecular Physics (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Non-Silver Salt Photosensitive Materials And Non-Silver Salt Photography (AREA)
  • Silver Salt Photography Or Processing Solution Therefor (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Description

Fremgangsmåte til avbygging av polyetylentereftalat til tereftalsyredimetylester. Process for breaking down polyethylene terephthalate into terephthalic acid dimethyl ester.

Oppfinnelsen angår en fremgangsmåte til avbygging av polyetylentereftalat til tereftalsyredimetylester under trykk og ved temperaturer opp til 210° C i nærvær av metanol samt høytkokende organiske forbindelser og omestreringskatalysatorer. The invention relates to a method for breaking down polyethylene terephthalate to terephthalic acid dimethyl ester under pressure and at temperatures up to 210° C in the presence of methanol as well as high-boiling organic compounds and transesterification catalysts.

Avbygging av polyetylentereftalat fore-tas når misfarget og forurenset avfall i Decomposition of polyethylene terephthalate is carried out when discolored and contaminated waste i

form av tråder, fibre eller bånd- eller også kompakte masser skal anvendes om igjen av økonomiske grunner. Man har foreslått å avbyggge disse avfall ved omsetning med kokende glykol. De derved erholdte teref-talsyrediglykolestere er sterkt forurenset in the form of threads, fibers or ribbons or compact masses must be reused for economic reasons. It has been proposed to break down these wastes by treatment with boiling glycol. The terephthalic acid diglycol esters thus obtained are heavily contaminated

og lar seg erfaringsmessig bare meget vans-kelig rense. Det er videre blitt foreslått å avbygge polyetylentereftalat med konsen-trerte syrer til det dannes tereftalsyre. Denne omstendige fremgangsmåte betyr ikke noe særlig fremskritt fordi tereftal-syren likeledes fåes i forurenset tilstand, og først må forestres hvis man skal an-vende den til en ny polykondensasjon. Etter et annet forslag lykkes avbygging av polyetylentereftalat hvis man oppheter polyesteren i nærvær av katalysatorer som f. eks. metafosforsyre og i nærvær av over-hetet metanoldamp uten anvendelse av trykk til 220—245° C. and, according to experience, is only very difficult to clean. It has also been proposed to break down polyethylene terephthalate with concentrated acids until terephthalic acid is formed. This elaborate procedure does not mean any particular progress because the terephthalic acid is likewise obtained in a contaminated state, and must first be esterified if it is to be used for a new polycondensation. According to another proposal, the decomposition of polyethylene terephthalate is successful if the polyester is heated in the presence of catalysts such as e.g. metaphosphoric acid and in the presence of superheated methanol steam without the application of pressure to 220-245° C.

Oppfinnerne har funnet at avbygging av polyetylentereftalat til tereftalsyredimetylester oppnås med meget godt utbytte og meget rent produkt hvis man oppheter polyesteren i nærvær av metanol samt av høytkokende organiske forbindelser som difenyl, difenyloksyd, difenylmetan, a- og The inventors have found that the breakdown of polyethylene terephthalate to terephthalic acid dimethyl ester is achieved with a very good yield and a very pure product if the polyester is heated in the presence of methanol and of high-boiling organic compounds such as diphenyl, diphenyl oxide, diphenylmethane, a- and

p-metylnaftalin og omestringskatalysa- p-methylnaphthalene and transesterification catalysis

torer under trykk til høyst 210° C. Som omestringskatalysatorer kan det herunder anvendes alle hertil kjente katalysatorer. Særlig virksomme er sink, sinkoksyd, sink-acetat, blyoksyd, blyacetat, magnesium, magnesiumoksyd og jern. Det anvendte trykk kan utgjøre ca. 10 til 19 ato. For avbygging kommer særlig slike polyestere på tale i form av tråder, børster eller fargede og forurensede tekstilprodukter skal anvendes om igjen. Det er overraskende at den ved fremgangsmåten i henhold til oppfinnelsen erholdte dimetylester fås med godt utbytte og stor renhet ennskjønt man går ut fra misfarget avfall. De høytkok-ende organiske forbindelser anvendes i en mengde av 1—10 vektsprosent beregnet på vekten av polyesteren. Den for utførelsen av fremgangsmåten gunstige temperatur utgjør når det samtidig anvendes trykk 140—160° C. Ved disse temperaturer be-virker de nevnte høytkokende forbindelser at polyesteren begynner å svelle, resp. løse seg opp, hvoretter den i nærvær av metanol og omestringskatalysator avbygges til den ønskede tereftalsyredimetylester. tor under pressure to a maximum of 210° C. All known catalysts can be used below as transesterification catalysts. Particularly effective are zinc, zinc oxide, zinc acetate, lead oxide, lead acetate, magnesium, magnesium oxide and iron. The applied pressure can amount to approx. 10 to 19 ato. For decommissioning, such polyesters in particular come into question in the form of threads, brushes or colored and contaminated textile products that must be reused. It is surprising that the dimethyl ester obtained by the method according to the invention is obtained with a good yield and great purity, even though the starting point is discolored waste. The high-boiling organic compounds are used in an amount of 1-10 percent by weight calculated on the weight of the polyester. The temperature favorable for carrying out the method is, when pressure is used at the same time, 140-160° C. At these temperatures, the aforementioned high-boiling compounds cause the polyester to begin to swell, resp. dissolve, after which it is broken down in the presence of methanol and transesterification catalyst to the desired terephthalic acid dimethyl ester.

Ved et sammenligningsforsøk kunne man fastslå at en avbygging av polyesteren under de samme forsøksbetingelser men uten tilsetning av de nevnte høytkokende organiske forbindelser bare foregår ufull-stendig. Det oppnås herved bare en ufull-stendig avbygging spesielt betinget av dannelsen av en blandingsester av tereftalsyre, metanol og etylenglykol. I nærvær av de nevnte høytkokende organiske forbindelser derimot foregår det en fullstendig avbygging av reaksjonsproduktet, hvorved det dannes over 90 pst. av den ønskede dimetylester. De for utførelsen av reaksjonen nødvendige omestringskatalysatorer befin-ner seg i reaksjonsblandingen i fast form og kan lett fjernes ved filtrering. In a comparison test, it could be determined that a breakdown of the polyester under the same test conditions but without the addition of the aforementioned high-boiling organic compounds only takes place incompletely. Hereby only an incomplete decomposition is achieved, particularly due to the formation of a mixed ester of terephthalic acid, methanol and ethylene glycol. In the presence of the aforementioned high-boiling organic compounds, on the other hand, a complete breakdown of the reaction product takes place, whereby more than 90 per cent of the desired dimethyl ester is formed. The transesterification catalysts required for carrying out the reaction are in the reaction mixture in solid form and can be easily removed by filtration.

Eksempel 1. Example 1.

I en autoklav innfører man 4 kg polyetylentereftalatavfall i form av fibre resp. tråder og tilsetter 4,8 liter metanol samt 400 gr a-metylnaftalin og 40 gr sinkstøv. Under opprettholdelse av et trykk på 18 ato opphetes autoklaven ved 130—140° C i 4 timer. I dette tidsrom blir reaksjons-mas.sen stadig omrørt. Etter avkjøling får man råesteren i form av en kompakt hvitgrå krystallmasse som utrøres med 1,5 liter metanol for å muliggjøre en bedre filtrering. Råesteren blir deretter ved avsuging befridd for glykol og a-metylnaftalin og fås deretter ved omkrystallisering fra metanol, under samtidig utskillelse av kata-lysatoren sink, i ren form og med et utbytte på 90 pst. 4 kg of polyethylene terephthalate waste in the form of fibers or threads and add 4.8 liters of methanol as well as 400 gr a-methylnaphthalene and 40 gr zinc dust. While maintaining a pressure of 18 ato, the autoclave is heated at 130-140° C for 4 hours. During this time, the reaction mass is constantly stirred. After cooling, the crude ester is obtained in the form of a compact white-grey crystal mass which is stirred with 1.5 liters of methanol to enable better filtration. The crude ester is then freed from glycol and α-methylnaphthalene by suction and is then obtained by recrystallization from methanol, with simultaneous separation of the catalyst zinc, in pure form and with a yield of 90 per cent.

Eksem- pel 2. Example 2.

4 kg polyetylentereftalatavfall i form av fargede og forurensede kompakte masser anbringes i en autoklav og det tilsettes 420 gr difenyloksyd og 30 gr magnesium samt 5 liter metanol. Under opprettholdelse av et trykk av 16 ato holdes autoklaven på en temperatur av 135° C i 4 timer. Her- 4 kg of polyethylene terephthalate waste in the form of colored and contaminated compact masses is placed in an autoclave and 420 gr of diphenyl oxide and 30 gr of magnesium and 5 liters of methanol are added. While maintaining a pressure of 16 ato, the autoclave is kept at a temperature of 135° C. for 4 hours. Here-

under blir reaksjonsmassen omrørt. Etter avkjøling får man råesteren i form av en kompakt hvitgrå krystallmasse som tilsettes 1,5 liter metanol for å oppnå bedre filtrering. Den ved avsuging rensede rå-ester gir deretter ved omkrystallisering fra metanol tereftalsyredimetylester i ren form og med et utbytte på 91 pst. during which the reaction mass is stirred. After cooling, the crude ester is obtained in the form of a compact white-grey crystal mass to which 1.5 liters of methanol is added to achieve better filtration. The crude ester purified by suction then gives, by recrystallization from methanol, terephthalic acid dimethyl ester in pure form and with a yield of 91 per cent.

Claims (3)

1. Fremgangsmåte til avbygging av polyetylentereftalat til tereftalsyredimetylester ved opphetning av polyetylentereftalat med metanol i nærvær av omestringskatalysatorer, karakterisert ved at avbyg-gingen foregår i nærvær av en høytkok-ende organisk forbindelse som difenyloksyd, eller a-metylnaftalin under trykk, fortrinsvis 16—18 atm. og ved temperatur på høyst 210° C.1. Process for decomposing polyethylene terephthalate to terephthalic acid dimethyl ester by heating polyethylene terephthalate with methanol in the presence of transesterification catalysts, characterized in that the decomposing takes place in the presence of a high-boiling organic compound such as diphenyl oxide, or α-methylnaphthalene under pressure, preferably 16-18 atm. and at a temperature of no more than 210° C. 2. Fremgangsmåte ifølge påstand 1, karakterisert ved at de høytkokende organiske forbindelser anvendes i en mengde av 1—10 vektprosent, fortrinsvis 5 vektprosent, beregnet på vekten av polyetylentereftalat.2. Method according to claim 1, characterized in that the high-boiling organic compounds are used in an amount of 1-10 percent by weight, preferably 5 percent by weight, calculated on the weight of polyethylene terephthalate. 3. Fremgangsmåte ifølge påstand 1 og 2, karakterisert ved at reaksjonen utføres ved en temperatur av fortrinsvis 140 til 160° C.3. Method according to claims 1 and 2, characterized in that the reaction is carried out at a temperature of preferably 140 to 160°C.
NO156718A 1964-02-10 1965-02-10 NO120009B (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US34345664A 1964-02-10 1964-02-10
US468972A US3297446A (en) 1964-02-10 1965-07-01 Synergistic sensitization of photographic systems with labile selenium and a noble metal

Publications (1)

Publication Number Publication Date
NO120009B true NO120009B (en) 1970-08-10

Family

ID=26993479

Family Applications (1)

Application Number Title Priority Date Filing Date
NO156718A NO120009B (en) 1964-02-10 1965-02-10

Country Status (9)

Country Link
US (1) US3297446A (en)
BE (1) BE659479A (en)
CH (1) CH441997A (en)
DE (1) DE1472818A1 (en)
DK (1) DK130897B (en)
GB (2) GB1098466A (en)
NL (1) NL144403B (en)
NO (1) NO120009B (en)
SE (1) SE333096B (en)

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Also Published As

Publication number Publication date
US3297446A (en) 1967-01-10
GB1150573A (en) 1969-04-30
DE1472818A1 (en) 1969-12-04
DK130897B (en) 1975-04-28
NL144403B (en) 1974-12-16
GB1098466A (en) 1968-01-10
NL6501562A (en) 1965-08-11
BE659479A (en) 1965-05-28
SE333096B (en) 1971-03-01
CH441997A (en) 1967-08-15
DK130897C (en) 1975-09-29

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