EP0000544A1 - Heat stabilized thermoplastic resins containing compounds with phosphorus to phosphorus bonds - Google Patents

Heat stabilized thermoplastic resins containing compounds with phosphorus to phosphorus bonds Download PDF

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Publication number
EP0000544A1
EP0000544A1 EP78100439A EP78100439A EP0000544A1 EP 0000544 A1 EP0000544 A1 EP 0000544A1 EP 78100439 A EP78100439 A EP 78100439A EP 78100439 A EP78100439 A EP 78100439A EP 0000544 A1 EP0000544 A1 EP 0000544A1
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Prior art keywords
phosphorus
grams
composition
stabilizer
containing compounds
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EP78100439A
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French (fr)
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EP0000544B1 (en
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Joseph Mcclendon Baggett
George Edward Ham
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Dow Chemical Co
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Dow Chemical Co
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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K5/00Use of organic ingredients
    • C08K5/49Phosphorus-containing compounds
    • C08K5/5398Phosphorus bound to sulfur
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07FACYCLIC, CARBOCYCLIC OR HETEROCYCLIC COMPOUNDS CONTAINING ELEMENTS OTHER THAN CARBON, HYDROGEN, HALOGEN, OXYGEN, NITROGEN, SULFUR, SELENIUM OR TELLURIUM
    • C07F9/00Compounds containing elements of Groups 5 or 15 of the Periodic System
    • C07F9/02Phosphorus compounds
    • C07F9/06Phosphorus compounds without P—C bonds
    • C07F9/08Esters of oxyacids of phosphorus
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07FACYCLIC, CARBOCYCLIC OR HETEROCYCLIC COMPOUNDS CONTAINING ELEMENTS OTHER THAN CARBON, HYDROGEN, HALOGEN, OXYGEN, NITROGEN, SULFUR, SELENIUM OR TELLURIUM
    • C07F9/00Compounds containing elements of Groups 5 or 15 of the Periodic System
    • C07F9/02Phosphorus compounds
    • C07F9/28Phosphorus compounds with one or more P—C bonds
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K5/00Use of organic ingredients
    • C08K5/49Phosphorus-containing compounds
    • C08K5/51Phosphorus bound to oxygen

Definitions

  • the invention is directed to a composition
  • a is independently 0 or 1, n is 3 to 6, X is oxygen or sulfur, R 1 , R 2 and R 3 are independently dialkylamino, alkoxy, aryloxy, alkyl, aryl, alkaryl, aralkyl, R 1 and R 2 taken with the P atom represent a cyclic structure having only carbon, phosphorus and oxygen atoms in the cyclic structure.
  • a preferred species of the invention is a the mole tic polycarbonate resin containing a compound ⁇ of the formula
  • blends or compositions of this invention are thus useful to make molded parts as in the injection molding of diverse articles such as, for example, cups, glasses, valve fittings and appliance covers.
  • thermoplastic resins or polymers which can be used in the compositions of this invention are illustrated by polyalkylenes such as polyethylene, polypropylene and related copolymers; polyvinyl chloride; vinyl polymers such as polystyrene and related copolymers such as styrene-butadiene-acrylonitrile copolymers; acrylic polymers such as polyacrylonitriles and poly(methyl- methacrylates) and related copolymers; polyesters such as poly(ethylene terephthalates); and aromatic polycarbonates such as bisphenol A polycarbonate and copolycarbonates with diverse dihydroxy phenols.
  • polyalkylenes such as polyethylene, polypropylene and related copolymers
  • polyvinyl chloride vinyl polymers such as polystyrene and related copolymers such as styrene-butadiene-acrylonitrile copolymers
  • acrylic polymers such as polyacrylonitriles and poly(methyl- methacrylates) and related copoly
  • a stabilizing amount of the compounds is defined as a range from about 0.01 to about 1.0 percent by weight and preferably about 0.05 to about 0.25 based on the total weight of the polymer.
  • compositions of this invention may also be blended with other conventional additives such as ultra violet light stabilizers, antioxidants, dyes and pigments.
  • Stabilizer A bis(5,5-dimethyl-2-oxo-l,3,2--dioxaphosphorinanyl), was prepared as follows. Into a flask fitted with stirrer, nitrogen purge, feeding funnel, thermometer, and reflux condenser were charged 50 ml of dry benzene and 4.6 grams (0.1 mole) sodium:paraffin 50:50 dispersion. The mixture was stirred about 30 minutes at room temperature with a slow nitrogen purge and then a solution containing 15 grams, (0.1 mole) of 2-hydroxy-5,5-dimethyl-1,3,2-dioxaphosphorinan dissolved in 50 ml of dry benzene was fed in at such a rate that the temperature was kept below 30°C.
  • Stabilizer B was prepared as follows. Into a flask equipped with stirrer, nitrogen purge, thermometer, and reflux condenser were charged'175 ml of benzene. The flask was purged with nitrogen to remove the air and then 25 ml of benzene was distilled off to remove any trace of water. The contents were cooled to 25°C and then with stirring 35.8 grams (0.2 mole) of dichlorophenyl phosphine was added, all at once, followed by the addition in the same manner 49.6 grams (0.4 mole) of trimethyl phosphite.
  • the mixture was refluxed for three hours, cooled, and transferred to a Rinco flask where the benzene was remcved by distillation using high vacuum and 90°C temperature.
  • the resulting product was a colorless liquid, having a weight of 53 grams, and upon standing overnight began to crystallize.
  • the product was identified by Phosphorus 31 Nuclear Magnetic Resonance to be the compound having the formula:
  • Stabilizer C was prepared'as follows. 33 grams (0.15 mole) of chlorodiphenylphosphine and 18.6 grams (0.15 mole) of trimethyl phosphite was fed into a flask equipped with stirrer, thermometer, feeding funnel, nitrogen purge, and reflux condenser containing 150 ml of dry benzene. The reaction mixture was refluxed for three hours under a very slow nitrogen purge. The reactants were cooled, transferred to a rotary evaporator where the benzene was removed by distillation under vacuum. 42 grams of a slightly yellowish syrup was recovered. After standing for several days, the syrup crystallized into a composition having a paste-like consistency.
  • a copolycarbonate of phenolphthalein and Bisphenol A hereinafter known as Polycarbonate E, was prepared by condensing 112.5 pounds (51.0 kg) of Bisphenol A and 37.5 pounds (17.0 kg) of phenolphthalein with 68 pounds (31 kg) of phosgene. The reaction was carried out in a solution of 1200 pounds (544 kg) of methylene chloride and 162.5 pounds (73.7 kg) pyridine in a 200 gallon (757 liters) glass-lined Pfaudler reactor. Para tertiary butyl phenol (2.10 pounds) (0.95 kg) was added is a terminater to control molecular weight.
  • the pyridine hydrochloride formed in the reaction and any excess pyridine was remozed by contacting the polymer solution with a solution of 76 pounds (34 kg) of 12N HC1 in 30 gallons (114 liters) of distilled water. An aliquot of the polymer solution in methylene chlorie was removed and washed two additional times with 30 volume percent distilled water. The water was separated and removed after each wash. Final traces of water were removed by contacting the solution with silica gel. The polymer solution was then filtered, the polymer precipitated with hexane, and air dried.
  • the copolycarbonate was 25 weight percent phenolphthalein and had a molecular weigh of 33,000 weight average molecular weight by gel permeation chromatography.
  • Stabilizers A, B, C and D prepared as above were blended with Polycarbonate E using ethanol as the solvent.
  • Stabilizer F was tetrakis(2,4-di-t-butylphenyl)-4,4'-bis- -(phenylyldiphosphonite) available as Sandostab P-EPQ®.
  • Stabilizer G has 3,9-(di(octadecyloxy)-2,4,8,10-tetraoxa--3,9-diphosphaspiro-5,5-undecane available as Weston 618®.
  • the stabilizer level was 1000 parts per million.
  • compositions were then air dried followed by vacuum drying at 110°C for four hours.
  • One gram of each composition was weighed into a separate 13 by 100 mm test tube and purged with nitrogen.
  • the test tubes were inserted into a 1-3/4 inch (4.4 cm) deep hole in an aluminum block with the temperature being controlled at 350°C.
  • the heat cycle time was 30 minutes.
  • a nitrogen pad (a pressure of.about 3.7 mm of mercury) was maintained on the samples during the heat cycle.
  • the polyethylene composition was next subjected to a multiextrusion test employing the same extruder above, but with the temperature at 260°C. Aften each pass through the extruder, the extruded composition was determined. A decrease in the melt index signified a breaking down and crosslinking of the polymer. The best stabilizer would result in the smallest change in the melt index.
  • Comparative Run E the same polyethylene as in Example 5 was extruded twice at 260°C, the polyethylene in the comparative run net containing any stabilizer.
  • the two compositions were vacuum oven dried and then injection molded.
  • the molded samples were heat aged in a circulating air oven at 120°C. They were removed at various times and their yellow index was determined according to ASTM-1925-63T. The results of the tests are shown in Table III.

Abstract

This invention relates to thermoplastic resin compositions containing an organo-phosphorus compound. The organo-phosphorus compound has one of the formulas
Figure imga0001
Figure imga0002
Figure imga0003
wherein a is independently 0 or 1, n is 3 to 6, X is oxygen or sulfur, R1; R2 and R3 are independently dialkylamino, alkoxy, aryloxy, alkyl, aryi, alkaryl, aralkyl, or R1 and R2 taken with the phosphorus atom represent a cyclic structure having only carbon, phasphorus and oxygen atoms in the cyclic structure. The thermoplastic resin compositions of this invention are resistant to discoloration.

Description

  • It has been found that compounds having a phosphorus to phosphorus bond are useful to stabilize thermoplastic polymers or resins from the effects of heat and/or oxygen during the molding of a blend containing the polymers and a compound having one or more phosphorus to phosphorus bonds.
  • The invention is directed to a composition comprising a thermoplastic polymer and a stabilizing amount of an organo-phosphorus compound having one of the formulas
    Figure imgb0001
    Figure imgb0002
    Figure imgb0003
    wherein a is independently 0 or 1, n is 3 to 6, X is oxygen or sulfur, R1, R2 and R3 are independently dialkylamino, alkoxy, aryloxy, alkyl, aryl, alkaryl, aralkyl, R1 and R2 taken with the P atom represent a cyclic structure having only carbon, phosphorus and oxygen atoms in the cyclic structure.
  • A preferred species of the invention is a the mole tic polycarbonate resin containing a compound ` of the formula
    Figure imgb0004
  • The blends or compositions of this invention are thus useful to make molded parts as in the injection molding of diverse articles such as, for example, cups, glasses, valve fittings and appliance covers.
  • The thermoplastic resins or polymers which can be used in the compositions of this invention are illustrated by polyalkylenes such as polyethylene, polypropylene and related copolymers; polyvinyl chloride; vinyl polymers such as polystyrene and related copolymers such as styrene-butadiene-acrylonitrile copolymers; acrylic polymers such as polyacrylonitriles and poly(methyl- methacrylates) and related copolymers; polyesters such as poly(ethylene terephthalates); and aromatic polycarbonates such as bisphenol A polycarbonate and copolycarbonates with diverse dihydroxy phenols.
  • The compounds having at least one phosphorus--to-phosphorus bond which can be used in the invention are illustrated by, and not limited to, the following:
    Figure imgb0005
    Figure imgb0006
    Figure imgb0007
    Figure imgb0008
    Figure imgb0009
    Figure imgb0010
    Figure imgb0011
    Figure imgb0012
    Figure imgb0013
    Figure imgb0014
    Figure imgb0015
    Figure imgb0016
    Figure imgb0017
    Figure imgb0018
    Figure imgb0019
    Figure imgb0020
    Figure imgb0021
    Figure imgb0022
    Figure imgb0023
    • wherein Ph signifies the phenyl group,
    • Me signifies the methyl group,
    • Et signifies the ethyl group, and
    • i-Pr signifies the isopropyl group.
  • For the purposes of this invention a stabilizing amount of the compounds is defined as a range from about 0.01 to about 1.0 percent by weight and preferably about 0.05 to about 0.25 based on the total weight of the polymer.
  • The compositions of this invention may also be blended with other conventional additives such as ultra violet light stabilizers, antioxidants, dyes and pigments.
  • EXAMPLES 1 THROUGH 4 AND COMPARATIVE RUNS A THROUGH D
  • Stabilizer A, bis(5,5-dimethyl-2-oxo-l,3,2--dioxaphosphorinanyl), was prepared as follows. Into a flask fitted with stirrer, nitrogen purge, feeding funnel, thermometer, and reflux condenser were charged 50 ml of dry benzene and 4.6 grams (0.1 mole) sodium:paraffin 50:50 dispersion. The mixture was stirred about 30 minutes at room temperature with a slow nitrogen purge and then a solution containing 15 grams, (0.1 mole) of 2-hydroxy-5,5-dimethyl-1,3,2-dioxaphosphorinan dissolved in 50 ml of dry benzene was fed in at such a rate that the temperature was kept below 30°C. The contents were stirred for 15 minutes at 25°C and then a solution of 12.0 grams (0.066 mole) of 2-chloro-2-oxo-5,5-dimethyl--1,3,2-dioxaphosphorinan dissolved in benzene (50 ml) was fed dropwise at 5 to 7°C. The reaction temperature was controlled by rate of addition and an ice acetone--water bath. After the feed was in, the reactants were stirred and digested at 25°C for three hours. The contents were again cooled to 5°C by an external source at which time 100 ml of an aqueous 5 percent NaHCO3 solution was added and stirred for a few minutes. The contents were transferred to a separating funnel and allowed to phase out. At the interface a solid forms. The solid was filtered off then dried. It had a melting point of 222°C. The crude product was recrystallized using CHCl3:ethyl acetate (2:1), filtered then washed with water, filtered again then dried. The white needle crystals weighed 5.15 grams and had a melting point of 255°C. The product was identified by phosphorus-31 Nuclear Magnetic Resonance; Infrared; and Mass Spectroscopy as having the formula:
    Figure imgb0024
  • Stabilizer B was prepared as follows. Into a flask equipped with stirrer, nitrogen purge, thermometer, and reflux condenser were charged'175 ml of benzene. The flask was purged with nitrogen to remove the air and then 25 ml of benzene was distilled off to remove any trace of water. The contents were cooled to 25°C and then with stirring 35.8 grams (0.2 mole) of dichlorophenyl phosphine was added, all at once, followed by the addition in the same manner 49.6 grams (0.4 mole) of trimethyl phosphite. The mixture was refluxed for three hours, cooled, and transferred to a Rinco flask where the benzene was remcved by distillation using high vacuum and 90°C temperature. The resulting product was a colorless liquid, having a weight of 53 grams, and upon standing overnight began to crystallize. The product was identified by Phosphorus 31 Nuclear Magnetic Resonance to be the compound having the formula:
    Figure imgb0025
  • Stabilizer C was prepared'as follows. 33 grams (0.15 mole) of chlorodiphenylphosphine and 18.6 grams (0.15 mole) of trimethyl phosphite was fed into a flask equipped with stirrer, thermometer, feeding funnel, nitrogen purge, and reflux condenser containing 150 ml of dry benzene. The reaction mixture was refluxed for three hours under a very slow nitrogen purge. The reactants were cooled, transferred to a rotary evaporator where the benzene was removed by distillation under vacuum. 42 grams of a slightly yellowish syrup was recovered. After standing for several days, the syrup crystallized into a composition having a paste-like consistency. After examination by phosphorus-31 NMR, the product was identified as a mixture of 20 percent of (C6H5)2-P(O)-P-(OCH3)2 and about 40 percent of (C6H5)2-P-P(C6H5)2.
  • Figure imgb0026
    was prepared as follows. 1.2 grams
    Figure imgb0027
    of magnesium was weighed into a 125 ml flask
    Figure imgb0028
    stirrer, thermometer, feeding
    Figure imgb0029
    r2 purge and reflux condenser. After purging with N2 50 ml of tetrahydrofuran was added to the magnesium. The contents were stirred while phenol dichloro- phosphine 8.9 grams (0.05 mole) was fed in dropwise with occasional external cooling with a water bath to maintain a reaction temperature of 50° to 60°C. After phosphine addition was completed the contents were stirred at 50°C for four hours. The reaction mixture was cooled to room temperature (25°C), transferred to a separating funnel and washed with 30 ml of water. The water was removed and the oil layer was allowed to evaporate in air to about 50 percent of the original volume. Then a second addition of 30 ml of water precipitated-2.1 grams of a white solid which, when recrystallized from acetonitrile, gave a product with a melting point of 150°C, consistent with reported literature results. The structure of the compound was determined to be as follows:
    Figure imgb0030
  • A copolycarbonate of phenolphthalein and Bisphenol A, hereinafter known as Polycarbonate E, was prepared by condensing 112.5 pounds (51.0 kg) of Bisphenol A and 37.5 pounds (17.0 kg) of phenolphthalein with 68 pounds (31 kg) of phosgene. The reaction was carried out in a solution of 1200 pounds (544 kg) of methylene chloride and 162.5 pounds (73.7 kg) pyridine in a 200 gallon (757 liters) glass-lined Pfaudler reactor. Para tertiary butyl phenol (2.10 pounds) (0.95 kg) was added is a terminater to control molecular weight.
  • After polymerization, the pyridine hydrochloride formed in the reaction and any excess pyridine was remozed by contacting the polymer solution with a solution of 76 pounds (34 kg) of 12N HC1 in 30 gallons (114 liters) of distilled water. An aliquot of the polymer solution in methylene chlorie was removed and washed two additional times with 30 volume percent distilled water. The water was separated and removed after each wash. Final traces of water were removed by contacting the solution with silica gel. The polymer solution was then filtered, the polymer precipitated with hexane, and air dried.
  • The copolycarbonate was 25 weight percent phenolphthalein and had a molecular weigh of 33,000 weight average molecular weight by gel permeation chromatography.
  • Stabilizers A, B, C and D prepared as above were blended with Polycarbonate E using ethanol as the solvent.
  • Comparative Runs A, B, C and D were made employing no stabilizers and two commercially available stabilizers. Stabilizer F was tetrakis(2,4-di-t-butylphenyl)-4,4'-bis- -(phenylyldiphosphonite) available as Sandostab P-EPQ®. Stabilizer G has 3,9-(di(octadecyloxy)-2,4,8,10-tetraoxa--3,9-diphosphaspiro-5,5-undecane available as Weston 618®. In Examples 1 through 4 and Comparative Runs C and D, the stabilizer level was 1000 parts per million.
  • The compositions were then air dried followed by vacuum drying at 110°C for four hours. One gram of each composition was weighed into a separate 13 by 100 mm test tube and purged with nitrogen. The test tubes were inserted into a 1-3/4 inch (4.4 cm) deep hole in an aluminum block with the temperature being controlled at 350°C. The heat cycle time was 30 minutes. A nitrogen pad (a pressure of.about 3.7 mm of mercury) was maintained on the samples during the heat cycle.
  • After the heat cycle, the sample was cooled. The test tube was broken and the composition was dissolved in methylene chloride. The glass particles were removed by filtration and the filtrate was diluted with more methylene chloride to make up a 100 ml solution. The color was determined on the solution by using a "Spec- tronic" Bausch and Lomb Photometer at 350 mµ and reported in Table I as percent transmittance.
    Figure imgb0031
  • EXAMPLE 5 AND COMPARATIVE RUN E
  • 15 pounds (6.8 kg) of high density polyethylene having a melt index of 5.0 and a density of 9.962 was dry blended with 0.12 ounces (3.4 grams) of Stabilizer A. The mixture was then double-pass extruded at 149°C on a 1-1/4 inch (3.2 cm) extruder with a nitrogen purge on the feed hopper of the extruder. After blending and extruding, the melt index of the polyethylene composition containing 500 parts per million of Stabilizer A was determined using ASTM Procedure D-1238.
  • The polyethylene composition was next subjected to a multiextrusion test employing the same extruder
    Figure imgb0032
    above, but with the temperature at 260°C. Aften each pass through the extruder, the
    Figure imgb0033
    extruded composition was determined. A decrease in the melt index signified a breaking down and crosslinking of the polymer. The best stabilizer would result in the smallest change in the melt index. in Comparative Run E, the same polyethylene as in Example 5 was extruded twice at 260°C, the polyethylene in the comparative run net containing any stabilizer.
  • The melt index values after extrusion are reported in Table II.
    Figure imgb0034
  • Similar results were obtained with polypropylene.
  • EXAMPLE 6 AND COMPARATIVE RUN F
  • 300 grams of Polycarbonate E was slurried with approximately 2 liters of distilled water in a Waring Blendor. While the water-polymer slurry was vigorously agitated, a solution of 1.5 grams of Stabilizer G in 15 milliliters of methylene chloride was slowly added. The polycarbonate powder was then collected on a filter and air dried.
  • This
    Figure imgb0035
    procedure was repeated adding 1.5 grams of Stabilizer A to 300 grams of Polycarbonate E to give a composition containing 5000 parts per million of Stabili-
    Figure imgb0036
    A.
  • The two compositions were vacuum oven dried and then injection molded. The molded samples were heat aged in a circulating air oven at 120°C. They were removed at various times and their yellow index was determined according to ASTM-1925-63T. The results of the tests are shown in Table III.
    Figure imgb0037
  • The data in Table III shows that the polycarbonate composition containing Stabilizer A is superior to a commercial stabilizer as far as reducing the level of color formation as determined by the yellow index.

Claims (4)

1. A composition comprising a thermoplastic polymer and a stabilizing amount of an argano-
Figure imgb0038
compound having one of the formulas
Figure imgb0039
Figure imgb0040
Figure imgb0041
wherein a is independently 0 or l, n is 3 to 6, X is oxygen or sulfur, R1, R2 and R3 are independently dialkylamino, alkoxy, aryloxy, alkyl, aryl, alkaryl, aralkyl, or R1 and R2 taken with the phosphorus atom represent a cyclic structure having only carbon, phosphorus and oxygen atoms in the cyclic structure.
2. The composition as in Claim 1 wherein the organo-phosphorus compound has the formula
Figure imgb0042
3. The composition as in Claim 1 wherein the thermoplastic polymer is a polycarbonate.
4. The composition as in Claim 1 wherein the organo-phosphorus compound is present from 0.01 to 1.0 percent by weight based on the total weight of the polymer.
EP78100439A 1977-07-20 1978-07-19 Heat stabilized thermoplastic resins containing compounds with phosphorus to phosphorus bonds Expired EP0000544B1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US05/817,326 US4111899A (en) 1977-07-20 1977-07-20 Heat stabilized thermoplastic resins containing compounds with phosphorus to phosphorus bonds
US817326 1986-01-09

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EP0000544A1 true EP0000544A1 (en) 1979-02-07
EP0000544B1 EP0000544B1 (en) 1982-08-04

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EP (1) EP0000544B1 (en)
JP (1) JPS5422447A (en)
CA (1) CA1085542A (en)
DE (1) DE2861986D1 (en)
IT (1) IT1156872B (en)

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US6369157B1 (en) 2000-01-21 2002-04-09 Cyclics Corporation Blend material including macrocyclic polyester oligomers and processes for polymerizing the same
US6420048B1 (en) 2001-06-05 2002-07-16 Cyclics Corporation High molecular weight copolyesters from macrocyclic oligoesters and cyclic esters
US6420047B2 (en) 2000-01-21 2002-07-16 Cyclics Corporation Macrocyclic polyester oligomers and processes for polymerizing the same
US6436548B1 (en) 2000-09-12 2002-08-20 Cyclics Corporation Species modification in macrocyclic polyester oligomers, and compositions prepared thereby
US6436549B1 (en) 2001-07-16 2002-08-20 Cyclics Corporation Block copolymers from macrocyclic oligoesters and dihydroxyl-functionalized polymers
US6525164B2 (en) 2000-09-01 2003-02-25 Cyclics Corporation Methods for converting linear polyesters to macrocyclic oligoester compositions and macrocyclic oligoesters
US8283437B2 (en) 2000-09-01 2012-10-09 Cyclics Corporation Preparation of low-acid polyalkylene terephthalate and preparation of macrocyclic polyester oligomer therefrom

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US7750109B2 (en) 2000-09-01 2010-07-06 Cyclics Corporation Use of a residual oligomer recyclate in the production of macrocyclic polyester oligomer
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US6787632B2 (en) 2001-10-09 2004-09-07 Cyclics Corporation Organo-titanate catalysts for preparing pure macrocyclic oligoesters
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US8519035B2 (en) * 2007-09-04 2013-08-27 Basf Se Cyclic phosphines as flame retardants
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US8759411B2 (en) * 2010-02-01 2014-06-24 Basf Se Derivatives of diphosphines as flame retardants for polyurethanes
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US10414985B2 (en) * 2014-03-27 2019-09-17 Basf Se Heptaphosphorus-derived compounds as flame retardants

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US6420047B2 (en) 2000-01-21 2002-07-16 Cyclics Corporation Macrocyclic polyester oligomers and processes for polymerizing the same
US6639009B2 (en) 2000-01-21 2003-10-28 Cyclis Corporation Macrocyclic polyester oligomers and processes for polymerizing the same
US6525164B2 (en) 2000-09-01 2003-02-25 Cyclics Corporation Methods for converting linear polyesters to macrocyclic oligoester compositions and macrocyclic oligoesters
US8283437B2 (en) 2000-09-01 2012-10-09 Cyclics Corporation Preparation of low-acid polyalkylene terephthalate and preparation of macrocyclic polyester oligomer therefrom
US6436548B1 (en) 2000-09-12 2002-08-20 Cyclics Corporation Species modification in macrocyclic polyester oligomers, and compositions prepared thereby
US6420048B1 (en) 2001-06-05 2002-07-16 Cyclics Corporation High molecular weight copolyesters from macrocyclic oligoesters and cyclic esters
US6436549B1 (en) 2001-07-16 2002-08-20 Cyclics Corporation Block copolymers from macrocyclic oligoesters and dihydroxyl-functionalized polymers

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CA1085542A (en) 1980-09-09
US4111899A (en) 1978-09-05
EP0000544B1 (en) 1982-08-04
JPS5422447A (en) 1979-02-20
IT1156872B (en) 1987-02-04
DE2861986D1 (en) 1982-09-30
IT7850385A0 (en) 1978-07-20

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