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Poly (block-phosphonato-ester) and poly (block-phosphonato-carbonate) and methods of making same

A polyphosphonate and phosphonooxy technology, applied in the fields of poly and poly and its preparation, can solve the problems of reduced optical transparency, no control of polyphosphonate block size, darkening of color and the like

Inactive Publication Date: 2012-09-19
FRX POLYMERS LLC
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Neutral catalysts are expensive and do not provide control over polyphosphonate block size in block polymers
Additionally, where the neutral catalyst remains in the final polymer product, it can lead to problems such as increased turbidity, reduced hydrolytic stability, reduced optical clarity, darker color and may catalyze thermal degradation of the polymer when used at elevated temperatures

Method used

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  • Poly (block-phosphonato-ester) and poly (block-phosphonato-carbonate) and methods of making same
  • Poly (block-phosphonato-ester) and poly (block-phosphonato-carbonate) and methods of making same
  • Poly (block-phosphonato-ester) and poly (block-phosphonato-carbonate) and methods of making same

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0073] 10 g low molecular weight oligomeric phosphonate (with 1190 g bisphenol A, 18.5 mole percent excess phosphonic acid diester (1595.5 g, methyl diphenoxy-phosphine oxide), 0.6 mole percent low carbon branched compound 1, 1,1-tris(4-hydroxyphenyl)ethane (9.2 g) and sodium phenoxide catalyst (150 mg) dried overnight at 40 °C at 2 mbar were prepared by a melt transesterification process with a T of 90 °C. g and η of 110 rel ) and 30 g of high viscosity polycarbonate (bisphenol A based) (such as Makraolon 3103 from Bayer) and 12 mg of tetraphenylphosphonium phenol transesterification catalyst were combined in a vessel under reduced pressure at 300 °C for 2 hours to remove volatile reactions product. Films of the product cast from dichloromethane solutions after drying were characterized and determined to have a T of 133-134°C g , η of 1.28-1.29 rel and a phosphorus content of approximately 2.72%.

Embodiment 2

[0075] 9.2 g of low molecular weight oligomeric phosphonates (by adding 207.9 g of methyl diphenoxy-phosphine oxide and 177.2 g of bisphenol A, 21.4 g of trisphenol phosphate (trisphenol phosphate) and 0.054 g of phosphonium phenolate catalyst under heating and Under vacuum for 7 hours, 191.4 grams of T with 70°C were generated g and an η of 1.09 rel The product phosphonate oligomers to prepare low M w Phosphonate oligomer) was mixed with 30.8 g of Makrolon 3103 dried under reduced pressure at 80°C overnight and 12 mg of tetraphenylphosphonium phenolate catalyst, and heated at 300°C under vacuum for 2 hours to remove by-products formed. The resulting product was 39.8 g with a T of 140 °C g , η of 1.29 rel ; Infrared (IR) P-O_C peak at 935cm -1 and a poly(phosphonooxycarbonate) with a phosphorus content (measured) of 1.98%.

Embodiment 3

[0077] 10g low molecular weight oligomeric phosphonate (by 75.9 gram methyl diphenoxy-phosphine oxides and 32.2g resorcinol, 0.92g trisphenol phosphate and 24mg phenol tetraphenyl phosphonium catalysts are reacted under heating and reducing The first day under pressure (66.5 g of by-product removed) and the second day of reaction with 24 mg of phosphonium phenolate catalyst under heat and reduced pressure (5.8 g of by-product removed) yielded 35 g of T g and an η of 1.05 rel The low M w Resorcinol phosphonate oligomer) was mixed with 30 g of Makrolon 3103 dried overnight at 80° C. under reduced pressure and 12 mg of phosphonium phenolate catalyst, and heated at 300° C. under vacuum for 4 hours to remove by-products formed. The resulting is a T with a T of 109°C g , η of 1.27 rel , and a phosphorus content (measured) of 4.31% of a slightly yellowish poly(phosphonooxycarbonate).

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Abstract

Compositions including poly(block-phophonato-esters) or poly(block-phosphonato-carbonate) and a process for making them from oligomeric phosphonates and / or polyphosphonates and polyester and / or polycarbonates are disclosed. The compositions provide tough flame retardant materials and coatings.

Description

[0001] This application is a Chinese patent application submitted on August 11, 2006 with the title of "poly(block-phosphonooxy-ester) and poly(block-phosphonooxy-carbonate) and their preparation method" Divisional application No. 200680029380.5, which is a Chinese national phase application of PCT international application PCT / US2006 / 031505 that entered China on February 13, 2008. [0002] Cross references to related applications: This application claims U.S. Provisional Application No. 60 / 707,304, filed August 11, 2005, entitled "Polymers Including Polyphosphonates and Polyesters, and Methods of Making," and filed August 11, 2005, entitled " Priority of U.S. Provisional Application No. 60 / 707,323 to "Polymers Including Polyphosphonates and Polyesters and Methods of Making." technical field [0003] This application relates to poly(block-phosphonooxy-esters) and poly(block-phosphonooxy-carbonates) and methods for their preparation. Background technique [0004] Random pol...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C08G64/18C08G79/04C08G63/692C08L85/02C08L69/00C08L67/00
CPCC08G64/0258C08G64/083C08G2261/126C08L69/00C08J3/005C08G63/692C08L67/00C08J2385/02C08G64/18C08L2666/02
Inventor 迪特尔·弗赖塔格
Owner FRX POLYMERS LLC
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