CN101193978A - Transparent polymer blends containing polyesters comprising a cyclobutanediol and articles prepared therefrom - Google Patents

Transparent polymer blends containing polyesters comprising a cyclobutanediol and articles prepared therefrom Download PDF

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Publication number
CN101193978A
CN101193978A CNA2006800205594A CN200680020559A CN101193978A CN 101193978 A CN101193978 A CN 101193978A CN A2006800205594 A CNA2006800205594 A CN A2006800205594A CN 200680020559 A CN200680020559 A CN 200680020559A CN 101193978 A CN101193978 A CN 101193978A
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residue
acid
component
composition
cyclobutanediol
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Inventor
W·R·黑尔
T·J·佩科里尼
S·A·吉列姆
E·D·克劳福德
D·S·波特
G·W·康奈尔
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Eastman Chemical Co
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Eastman Chemical Co
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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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  • Compositions Of Macromolecular Compounds (AREA)
  • Polyesters Or Polycarbonates (AREA)
  • Manufacture Of Macromolecular Shaped Articles (AREA)
  • Containers Having Bodies Formed In One Piece (AREA)
  • Laminated Bodies (AREA)
  • External Artificial Organs (AREA)
  • Materials For Medical Uses (AREA)

Abstract

Disclosed are polymer compositions having high transparency and low haze comprising immiscible blends of at least one polyester comprising 2,2,4,4-tetramethyl-1,3-cyclobutanediol, and a copolyamide or a transamidized, homogeneous blend of a least two polyamides. The components of the immiscible blend have refractive indices which differ by about 0.006 to about -0.0006. The small difference in the refractive indices enable the incorporation of regrind into the polymer composition to produce transparent shaped articles. The blends of the present invention are useful in producing shaped articles such as, for example, sheeting, films, tubes, bottles, preforms and profiles. These articles may have one or more layers and can exhibit improved excellent barrier properties and good melt processability while retaining excellent mechanical properties. Metal catalysts can be incorporated into the compositions to produce oxygen-scavenging compositions.

Description

The transparent, oxygen-scavenging compositions that contains the polyester that comprises cyclobutanediol reaches by its goods of making
The cross reference of related application
The application is that the part of the U.S. Patent application 11/363,375 of submission on February 27th, 2006 continues, the rights and interests of 60/657,747 U.S. Provisional Application that submit to its 2,60/657,746 and 2005 on March that requires on March 2nd, 2005 to submit to.The application further requires the U.S. Provisional Application 60/691 of submission on June 17th, 2005 according to 35U.S.C. § 119 (e), 567, the U.S. Provisional Application 60/731 that on October 28th, 2005 submitted to, 454, the U.S. Provisional Application 60/731 that on October 28th, 2005 submitted to, 389, the U.S. Provisional Application 60/739 that on November 22nd, 2005 submitted to, 058, the U.S. Provisional Application 60/739 that on November 22nd, 2005 submitted to, 869, the U.S. Provisional Application 60/750 that on December 15th, 2005 submitted to, 692, the U.S. Provisional Application 60/750 that on December 15th, 2005 submitted to, 693, the U.S. Provisional Application 60/750 that on December 15th, 2005 submitted to, 682, with the U.S. Provisional Application of submitting on December 15th, 2,005 60/750,547 rights and interests, all these full contents are incorporated herein by reference thus.
Invention field
The present invention relates to comprise transparent, the immiscible polymer blend of at least two kinds of polymeric constituents.Particularly, the present invention relates to comprise and contain 2,2,4,4-tetramethyl--1, the unmixing blend of at least a polyester of 3-cyclobutanediol and the intimate blending thing of copolyamide or at least two kinds of polymeric amide, wherein there is nuance in the out of phase specific refractory power absolute value of this unmixing blend.The present invention also relates to comprise the moulded products of this unmixing blend, wherein the specific refractory power of this polymeric constituent is very approaching.
Background of invention
Many products, particularly food are to the existence of oxygen and the loss or the absorption sensitivity of water.Wrapped product with this susceptibility is apt to deteriorate owing to being exposed to oxygen or absorption moisture.Restriction oxygen is exposed to the wrapping material of food, for example, helps to keep the quality of food and reduces corrupt.The use of this separated packaging material keeps the goods longer time thus and has reduced storage cost and refuse thus again.Address this problem the trial of taking in wrapping material, to be extensive use of oxygen barrier agent and/or moisture barrier agent.Known many polymer materialss play the effect of oxygen or moisture barrier agent.For example, typical moisture barrier agent comprises polyethylene and polypropylene.Representative oxygen barrier agent comprise poly-(ethylene-vinyl alcohol) (EVOH), poly-(vinyl alcohol) (PVOH), the blend of polymeric amide (nylon) and these materials.Poly-(vinylidene chloride), vinyl chloride copolymer and vinylidene chloride-methyl acrylate copolymer also are suitable for and make moisture and oxygen barrier agent.
But these conventional obstructive material expensive and have unsettled constitutional features or other defective make that breaking away from barrier material fully prepares wrapping material difficulty or undesirable.For example, EVOH though have excellent oxygen barrier properties, is not effective moisture barrier agent.Price was surprisingly high when other barrier material was used alone as wrapping material.For fear of these problems, the general multilayered structure that adopts wherein can drop to thin layer with the consumption of expensive barrier material in the practice, and is used as structural sheet with cheap polymkeric substance on the one or both sides of this barrier layer.Adopt multilayered structure also to help to avoid damaging by structural sheet protection barrier layer.But, multilayer product manufacturing cost height.In addition, may there be the difficulty of recovery in multi-layer product, because different polymeric constituents is difficult to separate.In addition, scrappy polymkeric substance or " regrinding (regind) " that reclaims often caused unsatisfied mist degree or opacity with the original polymer blend, because starting materials and regrinding is incompatible.
The blend of use barrier polymer and another polymkeric substance also can overcome the defective of conventional obstructive polymkeric substance.Unfortunately, as implied above, the blend of many barrier polymer and other thermoplastic polymer is immiscible and is opaque or fuzzy.This blend is not satisfied for application examples that requires transparency such as beverage container.
Polyester polymers for example poly-(ethylene glycol terephthalate) (PET) is usually used in packaging application.PET has manyly makes it be suitable for the performances make wrapping material, comprises in being packaged in the bottle that contains many portions of beverages acceptable carbon dioxide barrier properties the soft drink.But, need improve the carbonic acid gas barrier of PET and improve its oxygen barrier performance for the soft drink that is packaged in the bottle more, it is not to be very suitable for packing the oxygen sensitivity product, for example, the meat of beer, citrus products, tomato based product and sterile packed.Poly-((ethylene naphthalate)) is (PEN) big 3～10 times than PET validity as barrier agent, but very expensive.
Can adopt multilayered structure to improve the gas-barrier characteristic of PET.For example, polymkeric substance and the PET combination with excellent oxygen barrier performance (being also referred to as " passive obstruct ") or removing performance (being also referred to as " initiatively intercepting ") can be made the layer structure of being made up of each polymkeric substance.But, these multilayered structure manufacturing cost costlinesses.Also adopt the blend of barrier polymer and PET to improve the oxygen barrier performance of packing, still as implied above, often have poor transparency and and be not suitable for many packaging application.The transparency of blend difference also makes it be difficult to the processing waste in the blend polymer is recycled in the original polymer.
Often expect the toughness of the bottle of copolyester film and extrusion-blown modling " EBM ", and often replace PET to be used for extrusion-blown modling and film application.These are used and often require the suitable barrier with orientation PET.But unfortunately, the barrier of copolyester is poorer than orientation PET.Can by will approach, barrier films be coextruded to thicker body structure in make multilayered structure in the heart, improve whole barrier thus.But for economy, EBM and membrane process typically require the regrinding (that is, clout and finishing material) of reprocessing high level (up to 80%).Unfortunately, typical barrier material is not with copolyester dissolves each other and the blend of these barrier polymer and polyester often shows high-caliber mist degree and poor transparency.Thus, scrappy polymkeric substance (that is, regrinding) is drawn when getting back in the initial layer, the level of haze of whole membrane structure is increased to unacceptable level.
There is a need in the art for good passive and/or initiatively barrier, economic and blend polymer that can efficient recovery.This blend should be transparent, thermoplasticity and the barrier polymer that provides the high barrier of oxygen, water and carbonic acid gas is provided, and can be used for product forming process economically, and it combines high-caliber regrinding.In addition, need to be used for preparing economically multi-layer product and the obstruct that can hold high-caliber regrinding and combinations of thermoplastic polymers with high-clarity.
Summary of the invention
Polymer composition with high-clarity and high obstructing performance can be prepared by the unmixing blend of the blend of the homogeneous of one or more thermoplastic polymers and two kinds of polymeric amide, acid amides exchange at least, and wherein the difference of the specific refractory power of polyamide component and thermoplastic polymer components is about 0.006～approximately-0.0006.Thus, the invention provides a kind of polymer composition, it comprises following unmixing blend:
(i) first component comprises at least a thermoplastic polymer that is selected from polyester, polycarbonate, polyarylester and intimate blending thing thereof; With
(ii) second component comprises the homogeneous of at least 2 kinds of polymeric amide, the blend of acid amides exchange; Wherein, this second component is about 0.006～approximately-0.0006 with difference RI (second the component)-RI (first component) of the specific refractory power of this first component (i) (ii), and the percent transmittancy of this unmixing blend is at least 75%, and mist degree is 10% or lower.
Another aspect of the present invention, first component comprise and contain terephthalate, 2,2,4,4-tetramethyl--1, the polyester of the residue of 3-cyclobutanediol and 1,4 cyclohexane dimethanol.Thus, the present invention also provides a kind of polymer composition, and it comprises following unmixing blend:
(i) first component comprises at least a polyester, and it comprises:
(a) diacid residues comprises based on the total diacid residue being the residue of the terephthalic acid of about 70～about 100mol%; At least a residue that has up to the modified aromatic dicarboxylic acid of 20 carbon atoms of 0～about 30mol%; At least a residue that has up to the modified aliphatic dicarboxylic acid of 16 carbon atoms with 0～about 10mol%; With
(b) diol residue comprises that based on the total diol residue be 2,2,4 of about 1～about 99mol%, 4-tetramethyl--1, the residue of 3-cyclobutanediol; Residue with the 1,4 cyclohexane dimethanol of about 1～about 99mol%; With
(ii) second component comprises blend homogeneous, the acid amides exchange of at least two kinds of polymeric amide;
Wherein, this second component is about 0.006～approximately-0.0006 with difference RI (second the component)-RI (first component) of the specific refractory power of this first component (i) (ii), and the percent transmittancy of this unmixing blend is at least 75%, and mist degree is 10% or lower.
First component comprises at least a thermoplastic polymer that is selected from polyester, polycarbonate, polyarylester, reaches the intimate blending thing of these polymkeric substance, and this second component comprises the blend of at least 2 kinds of polymeric amide simultaneously, and it is formed the intimate blending thing by the acid amides exchange.We find, the polymeric amide by selecting at least two kinds of aliphatics with different levels and aromatic moieties and with these polymeric amide acid amides exchanges to form the intimate blending thing, the specific refractory power of this first and second component can be very approaching.Thus, the specific refractory power that the intimate blending thing of this thermoplastic polymer and polymeric amide can be used to cut out second component and first component makes that the difference of specific refractory power is about 0.006～approximately-0.0006 in the scope of expectation.For example, polyester and the intimate blending thing that comprises the polycarbonate of dihydroxyphenyl propane can be used as first component, and comprise that the acid amides of first polymeric amide of residue of m-xylenedimaine and hexanodioic acid and second fatty polyamide exchanges, intimate blending thing and can be used as barrier polymer.When specific refractory power is complementary thus, first and second components form transparent, unmixing blend, it is applicable to that preparation can be used for the high transparent moulded products of multiple packaging application.Also can be by prepared in various methods multilayered structure as known in the art.For example, can be with first and second components by the melt coextrusion or be injected into independent layer altogether, perhaps can be individually formed layer and in subsequent process, be brought together, for example lamination.
Second component also can comprise the copolyamide with a certain proportion of aromatics and aliphatic dicarboxylic acid and diamines residue, can change this ratio so that the specific refractory power of first and second components is very approaching.Thus, another aspect of the invention is a kind of polymer composition, it comprises following unmixing blend:
(i) first component comprises at least a thermoplastic polymer that is selected from polyester, polycarbonate, polyarylester and intimate blending thing thereof; With
(ii) second component comprises copolyamide;
Wherein, this second component is about 0.006～approximately-0.0006 with difference RI (second the component)-RI (first component) of the specific refractory power of this first component (i) (ii), and the percent transmittancy of this unmixing blend is at least 75%, and mist degree is 10% or lower.In another embodiment, this first component comprises and contains terephthalate, 2,2,4,4-tetramethyl--1, the polyester of the residue of 3-cyclobutanediol and 1,4 cyclohexane dimethanol.Thus, the invention provides a kind of polymer composition, it comprises following unmixing blend:
(i) first component comprises at least a polyester, and it comprises:
(a) diacid residues comprises based on the total diacid residue being the residue of the terephthalic acid of about 70～about 100mol%; At least a residue that has up to the modified aromatic dicarboxylic acid of 20 carbon atoms of 0～about 30mol%; At least a residue that has up to the modified aliphatic dicarboxylic acid of 16 carbon atoms with 0～about 10mol%; With
(b) diol residue comprises that based on the total diol residue be 2,2,4 of about 1～about 99mol%, 4-tetramethyl--1, the residue of 3-cyclobutanediol; Residue with the 1,4 cyclohexane dimethanol of about 1～about 99mol%; With
(ii) second component comprises blend homogeneous, the acid amides exchange of at least two kinds of polymeric amide;
Wherein, this second component is about 0.006～approximately-0.0006 with difference RI (second the component)-RI (first component) of the specific refractory power of this first component (i) (ii), and the percent transmittancy of this unmixing blend is at least 75%, and mist degree is 10% or lower.
Another aspect of the invention is a kind of polymer composition by comprising that the following method of melt blending makes:
(i) first component comprises at least a thermoplastic polymer that is selected from polyester, polycarbonate, polyarylester and intimate blending thing thereof; With
(ii) second component comprises the homogeneous of at least 2 kinds of polymeric amide, the blend of acid amides exchange;
Wherein, this second component is about 0.006～approximately-0.0006 with difference RI (second the component)-RI (first component) of the specific refractory power of this first component (i) (ii), and the percent transmittancy of this unmixing blend is at least 75%, and mist degree is 10% or lower.In still another embodiment of the present invention, this first component comprises and contains terephthalate, 2,2,4,4-tetramethyl--1, the polyester of the residue of 3-cyclobutanediol and 1,4 cyclohexane dimethanol.Thus, the present invention also provides a kind of polymer composition by comprising that the following method of melt blending makes:
(i) first component comprises at least a polyester, and it comprises:
(a) diacid residues comprises based on the total diacid residue being the residue of the terephthalic acid of about 70～about 100mol%; At least a residue that has up to the modified aromatic dicarboxylic acid of 20 carbon atoms of 0～about 30mol%; At least a residue that has up to the modified aliphatic dicarboxylic acid of 16 carbon atoms with 0～about 10mol%; With
(b) diol residue comprises that based on the total diol residue be 2,2,4 of about 1～about 99mol%, 4-tetramethyl--1, the residue of 3-cyclobutanediol; Residue with the 1,4 cyclohexane dimethanol of about 1～about 99mol%; With
(ii) second component comprises blend homogeneous, the acid amides exchange of at least two kinds of polymeric amide;
Wherein, this second component is about 0.006～approximately-0.0006 with difference RI (second the component)-RI (first component) of the specific refractory power of this first component (i) (ii), and the percent transmittancy of this unmixing blend is at least 75%, and mist degree is 10% or lower.
The barrier of composition exhibiting excellence of the present invention.By with transition-metal catalyst for example cobalt, manganese, iron, ruthenium, copper, nickel, palladium and platinum introduce this blend and strengthen oxygen barrier properties, make the deoxidation composition thus.Thus, the present invention further provides a kind of deoxidation composition, it comprises:
(A) comprise following unmixing blend:
(i) first component comprises at least a thermoplastic polymer that is selected from polyester, polycarbonate, polyarylester and intimate blending thing thereof; With
(ii) second component comprises copolyamide;
Wherein, this second component is about 0.006～approximately-0.0006 with difference RI (second the component)-RI (first component) of the specific refractory power of this first component (i) (ii), and the percent transmittancy of this unmixing blend is at least 75%, and mist degree is 10% or lower;
(B) at least a metal that is selected from the periodic table of elements the 3rd～12 family the 4th～6 row.
Typical metal catalyst comprises but is not to be defined in, cobalt, manganese and iron.This unmixing blend first component can comprise and contains terephthalate, 2,2,4,4-tetramethyl--1, the polyester of the residue of 3-cyclobutanediol and 1,4 cyclohexane dimethanol.Thus, another embodiment of the present invention is a kind of deoxidation composition, and it comprises:
(A) comprise following unmixing blend:
(i) first component comprises at least a polyester, and it comprises:
(a) diacid residues comprises based on the total diacid residue being the residue of the terephthalic acid of about 70～about 100mol%; At least a residue that has up to the modified aromatic dicarboxylic acid of 20 carbon atoms of 0～about 30mol%; At least a residue that has up to the modified aliphatic dicarboxylic acid of 16 carbon atoms with 0～about 10mol%; With
(b) diol residue comprises that based on the total diol residue be 2,2,4 of about 1～about 99mol%, 4-tetramethyl--1, the residue of 3-cyclobutanediol; Residue with the 1,4 cyclohexane dimethanol of about 1～about 99mol%; With
(ii) second component comprises blend homogeneous, the acid amides exchange of at least two kinds of polymeric amide;
Wherein, this second component is about 0.006～approximately-0.0006 with difference RI (second the component)-RI (first component) of the specific refractory power of this first component (i) (ii), and the percent transmittancy of this unmixing blend is at least 75%, and mist degree is 10% or lower; With
(B) at least a metal that is selected from the periodic table of elements the 3rd～12 family the 4th～6 row.
Blend of the present invention is applicable to the transparent moulded products of preparation, and it has improved barrier property, melt processability and very good mechanical properties, and it can adopt high regrinding/original polymer ratio to prepare.These moulded products can have single or multiple layers, and have many packaging application.Thus, the present invention further provides a kind of method for preparing moulded products, it comprises:
(A) melt blending is following:
(i) first component comprises at least a thermoplastic polymer that is selected from polyester, polycarbonate, polyarylester and intimate blending thing thereof; With
(ii) second component comprises the homogeneous of copolyamide or at least two kinds of polymeric amide, the blend of acid amides exchange;
Wherein, this first component (i) and second component (ii) form the unmixing blend, the difference RI of the specific refractory power of this second component and this first component (second component)-RI (first component) is about 0.006～approximately-0.0006, and the percent transmittancy of this unmixing blend is at least 75%, and mist degree is 10% or lower;
(B) form moulded products;
(C) recovery comprises first and second components (i) of blend and scrappy polymer composition (ii);
(D) grind this scrappy polymer composition to make regrinding;
(E) randomly, should scrappy polymer composition drying; With
(F) with first and second components (i) of this polymkeric substance regrinding and step (A) with (ii) mix.In another example, this first component can comprise and contains terephthalate, 2,2,4,4-tetramethyl--1, the polyester of the residue of 3-cyclobutanediol and 1,4 cyclohexane dimethanol.Thus, the present invention also comprises a kind of method that forms moulded products, and it comprises:
(A) melt blending is following:
(i) first component comprises at least a polyester, and it comprises:
(a) diacid residues comprises based on the total diacid residue being the residue of the terephthalic acid of about 70～about 100mol%; At least a residue that has up to the modified aromatic dicarboxylic acid of 20 carbon atoms of 0～about 30mol%; At least a residue that has up to the modified aliphatic dicarboxylic acid of 16 carbon atoms with 0～about 10mol%; With
(b) diol residue comprises that based on the total diol residue be 2,2,4 of about 1～about 99mol%, 4-tetramethyl--1, the residue of 3-cyclobutanediol; Residue with the 1,4 cyclohexane dimethanol of about 1～about 99mol%; With
(ii) second component comprises blend homogeneous, the acid amides exchange of at least two kinds of polymeric amide;
Wherein, this first component (i) and second component (ii) form the unmixing blend, the difference RI of the specific refractory power of this second component and this first component (second component)-RI (first component) is about 0.006～approximately-0.0006, and the percent transmittancy of this unmixing blend is at least 75%, and mist degree is 10% or lower;
(B) form moulded products;
(C) recovery comprises first and second components (i) of blend and scrappy polymer composition (ii);
(D) grind this scrappy polymer composition to make regrinding;
(E) randomly, should scrappy polymer composition drying; With
(F) with first and second components (i) of this polymkeric substance regrinding and step (A) with (ii) mix.
The example of the moulded products that can make by method of the present invention comprises but is not to be defined in, sheet material, film, pipe, bottle or section bar.This moulded products can by extrude, calendering, thermoforming, blowing, extrusion-blown modling, injection moulding, compression moulding, casting, drawing-off, tentering or make.
This moulded products can have one or more layers that comprise the unmixing blend of this first and second component, perhaps can have the wherein multilayer of first and second components in independent layer.Thus, the present invention also provides a kind of multilayer formed article, and it comprises:
(i) the first layer comprises at least a thermoplastic polymer that is selected from polyester, polycarbonate, polyarylester and intimate blending thing thereof; With
The (ii) second layer comprises the intimate blending thing of the acid amides exchange of at least two kinds of polymeric amide;
Wherein, this second layer is about 0.006～approximately-0.0006 with difference RI (the second layer)-RI (the first layer) of the specific refractory power of this first layer (i) (ii), and the percent transmittancy of this moulded products is at least 75%, and mist degree is 10% or lower.On the other hand, the first layer can comprise and contains terephthalate, 2,2,4,4-tetramethyl--1, the polyester of the residue of 3-cyclobutanediol and 1,4 cyclohexane dimethanol.Thus, another embodiment of the present invention is a kind of multilayer formed article, and it comprises:
(i) the first layer comprises at least a polyester, and it comprises:
(a) diacid residues comprises based on the total diacid residue being the residue of the terephthalic acid of about 70～about 100mol%; At least a residue that has up to the modified aromatic dicarboxylic acid of 20 carbon atoms of 0～about 30mol%; At least a residue that has up to the modified aliphatic dicarboxylic acid of 16 carbon atoms with 0～about 10mol%; With
(b) diol residue comprises that based on the total diol residue be 2,2,4 of about 1～about 99mol%, 4-tetramethyl--1, the residue of 3-cyclobutanediol; Residue with the 1,4 cyclohexane dimethanol of about 1～about 99mol%; With
The (ii) second layer comprises blend homogeneous, the acid amides exchange of at least two kinds of polymeric amide;
Wherein, this second layer is about 0.006～approximately-0.0006 with difference RI (the second layer)-RI (the first layer) of the specific refractory power of this first layer (i) (ii), and the percent transmittancy of this moulded products is at least 75%, and mist degree is 10% or lower.
The present invention further provides a kind of method that forms multilayer formed article, it comprises:
(i) heating first component that comprises at least a thermoplastic polymer that is selected from polyester, polycarbonate, polyarylester and intimate blending thing thereof is to the temperature of about Tg+100 ℃ of this first component～about Tg+300 ℃;
Second component that (ii) heats the intimate blending thing of the acid amides exchange that comprises copolyamide or at least two kinds of polymeric amide arrives about Tg+100 ℃ of this second component～about Tg+300 ℃;
(iii) be formed on the moulded products that has this first and second component in the independent layer;
(iv) reclaim the first and second scrappy components;
(v) grind these first and second scrappy components to make regrinding;
(vi) randomly, with this regrinding drying; With
(vii) with this regrinding and step (i) and first component (ii), second component or its combined hybrid;
Wherein, step second component and difference RI (second the component)-RI (first component) of the specific refractory power of first component of step (i) (ii) is about 0.006～approximately-0.0006, and the percent transmittancy of this moulded products is at least 75%, and mist degree is 10% or lower.Among another embodiment, this first component can comprise and contains terephthalate, 2,2,4,4-tetramethyl--1, the polyester of the residue of 3-cyclobutanediol and 1,4 cyclohexane dimethanol.Thus, another aspect of the invention is a kind of method that forms multilayer formed article, it comprises:
(i) heating first component is to the temperature of about Tg+100 ℃ of this first component～about Tg+300 ℃, and this first component comprises at least a polyester, and it comprises:
(a) diacid residues comprises based on the total diacid residue being the residue of the terephthalic acid of about 70～about 100mol%; At least a residue that has up to the modified aromatic dicarboxylic acid of 20 carbon atoms of 0～about 30mol%; At least a residue that has up to the modified aliphatic dicarboxylic acid of 16 carbon atoms with 0～about 10mol%; With
(b) diol residue comprises that based on the total diol residue be 2,2,4 of about 1～about 99mol%, 4-tetramethyl--1, the residue of 3-cyclobutanediol; Residue with the 1,4 cyclohexane dimethanol of about 1～about 99mol%;
Second component that (ii) heats the intimate blending thing of the acid amides exchange that comprises copolyamide or at least two kinds of polymeric amide arrives about Tg+100 ℃ of this second component～about Tg+300 ℃;
(iii) be formed on the moulded products that has this first and second component in the independent layer;
(iv) reclaim the first and second scrappy components;
(v) grind these first and second scrappy components to make regrinding;
(vi) randomly, with this regrinding drying; With
(vii) with this regrinding and step (i) and first component (ii), second component or its combined hybrid;
Wherein, step second component and difference RI (second the component)-RI (first component) of the specific refractory power of first component of step (i) (ii) is about 0.006～approximately-0.0006, and the percent transmittancy of this moulded products is at least 75%, and mist degree is 10% or lower.This regrinding can be attached to first or the second layer in, and can be about 5～about 60wt% of these goods.
Describe in detail
Polymer composition with high-clarity and high obstructing performance can be prepared by the unmixing blend of the blend of the homogeneous of one or more thermoplastic polymers and two kinds of polymeric amide, acid amides exchange at least, and wherein the difference of the specific refractory power of polymeric amide and thermoplastic polymer is about 0.006～approximately-0.0006.The percent transmittancy of this unmixing blend is at least 75%, and mist degree is 10% or lower.In the general embodiment, the invention provides polymer composition, it comprises following unmixing blend:
(i) first component comprises at least a thermoplastic polymer that is selected from polyester, polycarbonate, polyarylester and intimate blending thing thereof; With
(ii) second component comprises the homogeneous of at least 2 kinds of polymeric amide, the blend of acid amides exchange;
Wherein, this second component is about 0.006～approximately-0.0006 with difference RI (second the component)-RI (first component) of the specific refractory power of this first component (i) (ii), and the percent transmittancy of this unmixing blend is at least 75%, and mist degree is 10% or lower.This thermoplastic polymer and polymeric amide can be selected from many polymkeric substance.For example, this first component can comprise and contains terephthalate, 2,2,4,4-tetramethyl--1, the polyester of the residue of 3-cyclobutanediol and 1,4 cyclohexane dimethanol.The selection and the ratio of polymeric amide that can be by second component, perhaps alternatively, the thermoplastic polymer by blend first component is regulated the specific refractory power of this second component and first component so that difference is about 0.006～approximately-0.0006 to form the intimate blending thing.The new composition of the present invention can be used to make the moulded products with one or more layers, for example sheet material, film, pipe, bottle or section bar.This moulded products can by extrude, calendering, thermoforming, blowing, extrusion-blown modling, injection moulding, compression moulding, casting, drawing-off, tentering or make.Can make multi-layer product, wherein this unmixing blend is present in one or more layers, and perhaps first and second components are present in the independent layer.Because the nuance of the first and second component specific refractory poweres, the moulded products that is made by composition of the present invention can and keep good transparency in conjunction with a large amount of regrindings.The transparency of these moulded products that make and barrier property make them be specially adapted to packaging application.
Unless point out on the contrary, the numeral of all expression composition consumptions, performance such as molecular weight, reaction conditions, and as this specification sheets and claim are employed, all be interpreted as in all scenario modifying by term " about ".Thus, unless point out on the contrary, the digital parameters that provides in following specification sheets and the claims is an approximation, and it can change according to the performance of the expectation that reaches out for by the present invention.At least, each digital parameters should be at least with the specific numeral of being reported for work with by adopting conventional rounding-off method to constitute.In addition, the scope of mentioning in the disclosure content and the claim is intended to comprise entire area particularly but not is end points.For example, described 0～10 scope has been intended to disclose all integers between 0 to 10, and for example 1,2,3,4 etc., all marks between 0 to 10, for example 1.5,2.3,4.57,6.1113 etc. and end points 0 and 10.In addition, the scope relevant with chemical substituting group, for example " C1～C5 hydrocarbon " is intended to comprise particularly and discloses C1 and C5 hydrocarbon and C2, C3 and C4 hydrocarbon.
Although illustrating the digital scope and the parameter of wide region of the present invention is approximation, the numerical value that provides in the specific embodiment as far as possible accurately provides.But any number contains the certain error that certainly leads in essence in the standard deviation that they are found in the experimental measurement separately.
As using in this specification sheets and the claims, singulative " (a) ", " one (an) " and " this (the) " comprise their plural indicator, unless context is clearly pointed out on the contrary.For example, mention a kind of " polymkeric substance " and a kind of " moulded products ", be intended to comprise and handle or make multiple polymers or goods.Mention and contain or comprise " a kind of " composition or " a kind of " polymkeric substance, be intended to comprise respectively other composition or other polymkeric substance, except pointed.
" comprise (comprising) " or the implication of " containing (containing) " or " comprising (including) " is, at least compound, element, particle or the method steps etc. that have indication in composition or goods or the method, but be not the existence of getting rid of other compound, catalyzer, material, particle, method steps etc., even this other compound, material, particle, method steps etc. have and the indication identical functions, unless clearly get rid of in the claim.
It should be understood that yet and mention one or more method stepss, is not the existence of eliminating other method steps before or after the described step of combination, perhaps inserts method steps between clear those steps of determining.In addition, the title letter of method steps or composition is the easy way that is used to differentiate different behaviors or composition, and can arrange described title letter with random order, unless point out on the contrary.
Term used herein " polyester " is intended to comprise homopolymerization polyester, copolyester and ternary polyester.Usually, the synthetic polymer that makes for the polycondensation by one or more difunctionalitys and/or trifunctional carboxylic acids and one or more difunctionalitys and/or trifunctional oxy-compound of polyester.Typically, this bifunctional carboxylic acid is dicarboxylic acid or hydroxycarboxylic acid, and this difunctionality oxy-compound is dihydroxy alcohol, for example glycol and glycol.In addition, polyester of the present invention can contain branched monomer, and it can contain the combination of 3 or a plurality of carboxyl, hydroxyl or carboxyl and hydroxyl.Thus, term used herein " diacid " or " dicarboxylic acid ", also being intended to comprise can be as the polyfunctional carboxylic acids of branched monomer, for example trihemellitic acid.Similarly, term used herein " glycol " or " glycol ", also being intended to comprise can be as the multifunctional hydroxy compounds of branched monomer, for example tetramethylolmethane.Among the present invention, this difunctionality or polyfunctional carboxylic acids can be aliphatics or cycloaliphatic dicarboxylic acid, for example hexanodioic acid, perhaps aromatic dicarboxylic acid, for example terephthalic acid.This difunctionality oxy-compound can be the cycloaliphatic glycol, 1,4 cyclohexane dimethanol for example, linearity or branching aliphatic diol, for example 1,4-butyleneglycol, perhaps aromatic diol, for example quinhydrones.
The polyester that uses among the present invention is typically made by dicarboxylic acid and glycol, and it reacts with the ratio that fully equates and is incorporated in the polyester polymers as they corresponding residues.Thus, the polyester derived from dicarboxylic acid and diol residue of the present invention contains the sour residue (100mol%) and the diol residue (100mol%) of the first-class molar ratio of essence, makes the total mole number of repeating unit equal 100mol%.Thus, the molar percentage that provides in the present disclosure can be based on the total mole number of sour residue, the total mole number of diol residue or the total mole number of repeating unit.For example, containing based on the total acid residue is the copolyester of the terephthalic acid of 30mol%, and implication is the copolyester that contains the 30mol% terephthalic acid residue in the acid of 100mol% altogether residue.Thus, the terephthalic acid residue who among every 100mol acid residue, has 30mol.In another example, containing based on the total diol residue is the copolyester of the 1,4 cyclohexane dimethanol of 30mol%, and implication is to contain 30mol%1 in the 100mol% diol residue altogether, the copolyester of 4-cyclohexanedimethanol residue.Thus, the 1,4 cyclohexane dimethanol residue that among every 100mol diol residue, has 30mol.Such as used in this article, terephthalic acid, ethylene glycol and 1, the copolyester of 4-cyclohexanedimethanol, when diol component is mainly ethylene glycol, can be called " PET ", when diol component is mainly 1,4 cyclohexane dimethanol, be called " PCT ", in ethylene glycol and 1, the ratio of 4-cyclohexanedimethanol is greater than being called " PETG " at 1 o'clock, and in the ratio of ethylene glycol and 1,4 cyclohexane dimethanol less than being called " PCTG " at 1 o'clock.
Term used herein " polymeric amide " is intended to comprise the synthetic polymer that polycondensation by one or more bifunctional carboxylic acids and one or more bifunctional amines or the ring-opening polymerization by lactan make, and can comprises homopolymer and multipolymer.For example, this bifunctional carboxylic acid can be dicarboxylic acid such as hexanodioic acid or m-phthalic acid, and this bifunctional amine can be diamines, for example hexamethylene-diamine or m-xylenedimaine.Term used herein " copolyamide " is interpreted as implication and is comprising in 2 the chemically polymeric amide of distinct repeating unit at least.For example, MXD6 nylon is not copolyamide, because it only contains single, chemically distinct repeating unit, it contains the residue of hexanodioic acid and m-xylenedimaine.On the contrary, poly-(the hexa-methylene adipamide-copolymerization-isophthaloyl amine) that condensation by hexamethylene-diamine and hexanodioic acid and m-phthalic acid makes, have two kinds of chemically different then repeating units, promptly, contain hexamethylene-diamine and hexanodioic acid residue repeating unit and contain hexamethylene-diamine and another repeating unit of the residue of m-phthalic acid.
Term " polycarbonate " is defined as the condensation product of carbonic ether raw material and two raw polyols herein, have carbonate component that contains the 100mol% carbonate unit and the diol component that contains the 100mol% diol units, amount to 200mol% monomeric unit or 100mol% " repeating unit ".In one embodiment of the present invention, the polycarbonate of first component partly is based on 4, and the polycarbonate of 4 '-isopropylidene diphenol is known as bisphenol-a polycarbonate.Utilizable multiple linearity or branching polycarbonate can be derived from dihydroxyphenyl propanes among the present invention, and can prepare according to operation well-known in the art, for example, as US3, in 030,335 and 3,317,466 disclosed like that.The example that can be used for the bisphenol-a polycarbonate of the present invention and commercially available acquisition comprises with trade mark LEXAN  (can obtain from General Electric Company) and the commercially available material of MAKROLON  (can be from Bayer, Inc obtains).
Term used herein " polyarylester " is interpreted as implication and is the polyester that the polycondensation by one or more difunctionality aromatic dicarboxylic acids and one or more dihydric phenol makes.For example, typical aromatic dicarboxylic acid is terephthalic acid and m-phthalic acid, and typical aromatics diphenol is dihydroxyphenyl propane and quinhydrones.
Mention the term " residue " that uses in the polymkeric substance of the present invention herein, implication is for being incorporated into any organic structure in the polymkeric substance by relating to corresponding monomeric polycondensation or ring-opening reaction.Term used herein " repeating unit ", implication are to repeat the shortest monomeric sequence found in polymkeric substance.For example, in the polyester, repeating unit is the organic structure with dicarboxylic acid residue and diol residue.In the polymeric amide, repeating unit is the structure with dicarboxylic acid and diamines residue, lactan or amino-acid residue, by the amide group bonding.
Those of ordinary skills also will be appreciated that with various polyester of the present invention, polymeric amide, residue that polycarbonate is relevant with polyarylester can be derived from any derivative of female monomeric compound itself or parent compound.For example, dicarboxylic acid of mentioning in the polymkeric substance of the present invention and amino-acid residue can be derived from dicarboxylic acid or amino acid, perhaps its relevant carboxylic acid halides, ester, salt, acid anhydrides or its mixture.Thus, term used herein " dicarboxylic acid " or " amino acid ", be intended to comprise any derivative of dicarboxylic acid and dicarboxylic acid, comprise carboxylic acid halides, ester, half ester, salt, half salt, acid anhydrides, mixed acid anhydride or its mixture that it is relevant, be applicable to and the polycondensation process of glycol, make high molecular weight polyesters, polymeric amide, polycarbonate or polyarylester thus.Term " hydroxycarboxylic acid " is intended to comprise aliphatics and cycloaliphatic hydroxycarboxylic acid and monohydroxy-monocarboxylic acid and its any derivative, comprise carboxylic acid halides, ester, cyclic ester (comprising dimer such as lactic acid lactide), salt, acid anhydrides, mixed acid anhydride or its mixture that they are relevant, be applicable to that polycondensation process or ring-opening reaction are to make high molecular weight polyesters.Similarly, " amino acid " is intended to comprise aliphatics, aromatics and cycloaliphatic amino acid and derivative thereof, comprise carboxylic acid halides, acid amides, cyclic amide (lactan), salt, acid anhydrides, mixed acid anhydride or its mixture that they are relevant, be applicable to that polycondensation process or ring-opening reaction are to make superpolyamide.In addition, term " diamines " is intended to comprise that diamines and their relevant salt, acid amides or its are applicable to any other derivative of preparation polymeric amide.
When no matter when using term " logarithmic viscosity number (I.V.) " among the application, be illustrated in the viscosity measurement that 25 ℃ of solvent 0.5g polymkeric substance that adopt every 100mL to comprise 60wt% phenol and 40wt% tetrachloroethane down carry out with being interpreted as.
Term used herein " specific refractory power " (being abbreviated as " RI " herein), the refractometry that expression obtains according to method well-known in the art.Bao Dao specific refractory power is to adopt Metricon Prism Coupler under the 633nm wavelength herein TMModel 2010 refractometers (can from Metricon Inc. obtain) are measured, and with three orthogonal directionss (extrude or stretch, laterally and thickness direction) go up the mean value report of the specific refractory power of measuring.The phrase that uses in the content of composition of the present invention, method and moulded products " specific refractory power poor " herein, often expression deducts the specific refractory power of the component (" the first layer " in so-called " first component " or the multi-layer product) that contains polyester, polycarbonate or polyarylester herein herein and the numerical value that obtains from the specific refractory power of the component (" second layer " so-called " second component " or the multi-layer product) that contains polymeric amide or copolyamide.Thus, according to the present invention, poor (" the Δ RI ") of specific refractory power should calculate according to following formula:
Δ RI=RI (second component or layer)-(first component or layer)
The difference that those skilled in the art obviously know specific refractory power can be positive number or negative.
Term used herein " % mist degree ", expression is adopted HunterAssociates Laboratory according to ASTM method D1003, Inc., the haze value that Reston, HunterLabUltraScan Sphere 8000 colorimeters that Va makes utilize Hunter ' s Universal Software (3.8 version) (% mist degree=100* diffuse transmission/total transmission) to measure.Term used herein " percent transmittancy " is with term " percent transmittance " synonym.The operation of measuring specific refractory power is provided among the embodiment.For composition of the present invention, by with the composition molding or to be cast into thickness be 1/8 inch sheet material or film and measure mist degree and percent transmittancy is determined mist degree and percent transmittancy (being the % transmission) according to the operation of describing among the embodiment.For moulded products, comprise multilayer formed article, can (promptly 1 * 1cm), thickness be 1/8 inch or littler, and measures mist degree according to described operation herein, determines mist degree and percent transmittancy thus by cut out small portion from these goods.
Term used herein " second-order transition temperature " (Tg) is represented the Tg value that adopts dsc (DSC) to measure, typically adopts the scanning speed of 20 ℃/min.The example of DSC equipment is TA equipment 2929 differential scanning calorimeters.
Composition of the present invention comprises and contains first component that one or more are selected from the thermoplastic polymer of polyester, polycarbonate, polyarylester and intimate blending thing thereof.Term used herein " thermoplastic polymer " is intended to have the general sense that those of ordinary skills understand, and, recovers the polymkeric substance of its original situation when being exposed to heat during softening and cool to room temperature that is.First component can comprise single thermoplastic polymer, perhaps can contain the blend of 2 kinds or multiple polymers, and prerequisite is that this blend is the intimate blending thing.Term used herein " intimate blending thing " and term " miscible " synonym, and be intended to represent that this blend has single, isotropic phase, shown in single, as to depend on composition Tg.For example, first polymkeric substance miscible with second polymkeric substance can be used for " plasticising " this second polymkeric substance, for example, and as US6, shown in 211,309.The intimate blending thing can pass through two or more polymkeric substance of simple blend, perhaps for example exchanges two or more polymkeric substance by transesterify or acid amides in polyester or the polymeric amide situation at polycondensate and forms.On the contrary, term used herein " immiscible " expression blend shows at least 2, random blended phase, and shows more than one Tg.Some polymkeric substance can be immiscible and still compatible with each other.Miscible and immiscible polymer blend can be at Polymer Blends volume 1 and 2 with the further general introduction about the various analytical technologies of their characteristics, and D.R.Paul and CB.Bucknall edit, and 2000, John Wiley ﹠amp; Sons finds among the Inc..
This first component can comprise that one or more are selected from the thermoplastic polymer of polyester, polycarbonate, polyarylester and intimate blending thing thereof.For example, this first component can comprise polyester, it comprises (a) diacid residues, comprise based on the total diacid residue and be selected from terephthalic acid, m-phthalic acid, naphthalic acid and 1 for 80mol% at least, at least a residue of the residue of at least a dicarboxylic acid of 4-cyclohexane cyclohexanedimethanodibasic and 0～about 20mol% with modification dicarboxylic acid of 2～20 carbon atoms; (b) diol residue, comprise based on the total diol residue and be selected from ethylene glycol, 1 for 80mol% at least, 4-cyclohexanedimethanol, neopentyl glycol, Diethylene Glycol, 1, ammediol, 1,4-butyleneglycol and 2,2,4,4-tetramethyl--1, at least a residue of the residue of at least a glycol of 3-cyclobutanediol and 0～about 20mol% with modification glycol of 3～16 carbon atoms.The ring glycol that contains cis and trans-isomer(ide) can be as the pure cis or the mixture of trans-isomer(ide) or cis and trans-isomer(ide).
For example, diacid residues can comprise that one or more are selected from the residue of the dicarboxylic acid of terephthalic acid, m-phthalic acid or its combination, and diol residue comprises that one or more are selected from 1,4-cyclohexanedimethanol, neopentyl glycol, ethylene glycol, 2,2,4,4-tetramethyl--1, the residue of the glycol of 3-cyclobutanediol and combination thereof.In a kind of embodiment, for example, this diacid residues can comprise the residue of terephthalic acid and m-phthalic acid.In the polyester terephthalic acid higher than the concentration of m-phthalic acid be useful because the polyester that obtains provides bigger shock strength to blend.For example, this diacid residues can comprise the residue of m-phthalic acid of residue and 0～about 40mol% of the terephthalic acid of about 60～about 100mol%, and this diol residue can comprise the residue of the 1,4 cyclohexane dimethanol of about 100mol%.Other example of dicarboxylic acid content comprises the residue of the m-phthalic acid of the residue of terephthalic acid of about 80～about 100mol% and 0～20mol%, the residue of the residue of the terephthalic acid of about 95～about 100mol% and the terephthalic acid of about 100mol%.
Other the representative polyester that can be used as the thermoplastic polymer of component (i) comprises and contains following polyester: the diacid residues of residue that (a) comprises the terephthalic acid of about 80～about 100mol%, diol residue with the residue of the neopentyl glycol of the residue of the 1,4 cyclohexane dimethanol that comprises about 50～about 90mol% and about 10～about 50mol%; (b) comprise the diacid residues of residue of the terephthalic acid of 100mol%, with the diol residue of the residue of the ethylene glycol of the residue of the 1,4 cyclohexane dimethanol that comprises about 10～about 40mol% and about 60～about 90mol%; (c) comprise the diacid residues of residue of the terephthalic acid of 100mol%, diol residue with the residue of the Diethylene Glycol of the residue of the ethylene glycol of residue, 0～about 90mol% of the 1,4 cyclohexane dimethanol that comprises about 10～about 99mol% and about 1～about 25mol%; (d) comprise the diacid residues of residue of the terephthalic acid of 100mol%, with the diol residue of the residue of the ethylene glycol of the residue of the 1,4 cyclohexane dimethanol that comprises about 50～about 90mol% and about 10～about 50mol%.
In another embodiment, this first component can comprise at least a terephthalic acid, 2,2,4 that contains, 4-tetramethyl--1,3-cyclobutanediol, 1, the polyester of the residue of 3-cyclobutanediol and 1,4 cyclohexane dimethanol.For example, this polyester can comprise (a) diacid residues, comprises based on the total diacid residue being the residue of the terephthalic acid of about 70～about 100mol%; At least a residue that has up to the modified aromatic dicarboxylic acid of 20 carbon atoms of 0～about 30mol%; At least a residue that has up to the modified aliphatic dicarboxylic acid of 16 carbon atoms with 0～about 10mol%; (b) diol residue comprises that based on the total diol residue be 2,2,4 of about 1～about 99mol%, 4-tetramethyl--1, the residue of 3-cyclobutanediol; Residue with the 1,4 cyclohexane dimethanol of about 1～about 99mol%.Other representative example that can be used for the polyester of this first component comprises but is not to be defined in, comprises following polyester: be the residue of the terephthalic acid of 70～about 100mol% based on the total diacid residue; At least a residue that has up to the modified aromatic dicarboxylic acid of 20 carbon atoms of 0～about 30mol%; At least a residue that has up to the modified aliphatic dicarboxylic acid of 16 carbon atoms with 0～about 10mol%; With in the following diol residue composition any: (i) 2,2,4 of about 5～about 60mol%, 4-tetramethyl--1, the residue of the 1,4 cyclohexane dimethanol of the residue of 3-cyclobutanediol and about 40～about 95mol%; 2,2,4 of (ii) about 15～about 40mol%, 4-tetramethyl--1, the residue of the 1,4 cyclohexane dimethanol of the residue of 3-cyclobutanediol and about 60～about 85mol%; 2,2,4 of (iii) about 20～about 30mol%, 4-tetramethyl--1, the residue of the 1,4 cyclohexane dimethanol of the residue of 3-cyclobutanediol and about 70～about 80mol%; 2,2,4 of (iv) about 20～about 25mol%, 4-tetramethyl--1, the residue of the 1,4 cyclohexane dimethanol of the residue of 3-cyclobutanediol and about 75～about 80mol%.
Still in another example, this dicarboxylic acid can be selected from terephthalic acid and m-phthalic acid, and this glycol can be selected from 1,4 cyclohexane dimethanol and ethylene glycol.In a kind of composition, for example, this dicarboxylic acid is that terephthalic acid and this glycol are 1,4 cyclohexane dimethanol.Still in another example, this diacid residues can comprise the residue of the terephthalic acid of 95mol% at least, and this diol residue can comprise the residue of the ethylene glycol of the residue of Diethylene Glycol of the residue of the 1,4 cyclohexane dimethanol of about 10～about 40mol%, about 1～about 25mol% and about 35～about 89mol%.
If desired, this polyester may further include 0～about 30mol% one or more have the residue of the modification diacid of 2-20 carbon atom.For example, can use other aromatic dicarboxylic acid that contains 8～about 16 carbon atoms of 0～about 30mol%, the cycloaliphatic dicarboxylic acid that contains 8～about 16 carbon atoms, the aliphatic dicarboxylic acid that contains 2～about 16 carbon atoms or its mixture.The example of modified aromatic dicarboxylic acid comprises but is not to be defined in, 4,4 '-diphenyl dicarboxylic acid, m-phthalic acid, 1,4-naphthalene dicarboxylic acids, 1,5-naphthalene dicarboxylic acids, 2,6-naphthalene dicarboxylic acids, 2,7-naphthalene dicarboxylic acids, 4,4 '-oxybenzoic acid and trans-4,4 '-in the Stilbene dicarboxylic acid one or more.The example of modified aliphatic dicarboxylic acid comprises but is not to be defined in, one or more in oxalic acid, propanedioic acid, succsinic acid, pentanedioic acid, hexanodioic acid, pimelic acid, suberic acid, nonane diacid and the sebacic acid.For example, the diacid component of this polyester can be with the residue modification up at least a modified aliphatic dicarboxylic acid of 16 carbon atoms of having of 0～about 10mol%.
In another embodiment, this polyester can comprise the residue based on the ethylene glycol of the residue of the 1,4 cyclohexane dimethanol of the about 1～about 99mol% of the total mole number of diol residue, about 99～about 1mol%.Comprise about 1～about 10mol%, about 1～about 25mol%, about 1～about 40mol%, 50mol% and above and 100mol% for the typical molar percentage of the residue of the 1,4 cyclohexane dimethanol of polyester of the present invention.Still in another embodiment, for example, this dicarboxylic acid is 1, and 4-cyclohexane dicarboxylic acid and this glycol are 1,4 cyclohexane dimethanol.In another example, this polyester can comprise the residue of 1,4 cyclohexane dimethanol unit and neopentyl glycol.Still in another example, this polyester can comprise 1,4 cyclohexane dimethanol unit and 2,2,4,4-tetramethyl--1, the residue of 3-cyclobutanediol.
The diol component of this polyester also can be with at least a modification glycol modification with 3～16 carbon atoms of 0～about 20mol%.Other scope of modification glycol comprises but is not to be defined in, 0～about 10mol% and less than 5mol%.This modification glycol can be to be selected from 1,2-propylene glycol, 1, ammediol, 1,4-butyleneglycol, 1,5-pentanediol, 1,6-hexylene glycol, 1,4-cyclohexanedimethanol, p-Xylol glycol, neopentyl glycol, polyoxyethylene glycol, polytetramethylene glycol and 2,2,4,4-tetramethyl--1, one or more of 3-cyclobutanediol.The example of polyalkylene glycol comprise poly-(tetramethylene glycol) (PTMG) and poly-(ethylene glycol) (PEG), molecular weight is up to about 2000.This diol component, for example, can be with the polyoxyethylene glycol of 0～about 10mol% or polytetramethylene glycol modification to strengthen elastic behavior.In another example, this diol residue can comprise the residue of the Diethylene Glycol of the residue of ethylene glycol of residue, 0～about 90mol% of the 1,4 cyclohexane dimethanol of about 10～about 99mol% and about 1～about 25mol%.This polyester also can contain based on total acid or diol residue for up to about 5mol%, typically about 0.01～about 2.0mol% or more typically about 0.01～about 1mol%, residue derived from the multifunctional branching agent of the compound with at least three carboxyls and/or hydroxyl forms branched polyester thus.This examples for compounds comprises trihemellitic acid, trihemellitic acid acid anhydride and pyromellitic acid dianhydride, glycerine, Sorbitol Powder, 1,2,6-hexanetriol, tetramethylolmethane, tartrate, citric acid, trimethylolethane and trimesic acid etc.It will be appreciated by those skilled in the art that by the various resins of blend or by the copolymerization of direct reaction device and can obtain final composition.The latter expects for the composition mutability is minimized, but economic necessity makes the blend cost more effective.
Another example of polyester is to contain based on the total diacid residue to be any those in the residue of the terephthalic acid of about 100mol% and the following diol residue composition, based on the total diol residue: (i) residue of the ethylene glycol of the residue of the 1,4 cyclohexane dimethanol of about 1～about 5mol% and about 99～about 95mol%; The residue of the ethylene glycol of the residue of the 1,4 cyclohexane dimethanol of (ii) about 29～about 33mol% and about 71～about 67mol%; The residue of the ethylene glycol of the residue of the 1,4 cyclohexane dimethanol of (iii) about 45～about 55mol% and about 55～about 45mol%; The residue of the ethylene glycol of the residue of the 1,4 cyclohexane dimethanol of (iv) about 60～about 65mol% and about 40～about 35mol%; (the residue of the ethylene glycol of the residue of the 1,4 cyclohexane dimethanol of v) about 79～about 83mol% and about 21～about 17mol%; (the vi) residue of the 1,4 cyclohexane dimethanol of about 100mol%; (2,2,4 of vii) about 5～about 60mol%, 4-tetramethyl--1, the residue of the 1,4 cyclohexane dimethanol of the residue of 3-cyclobutanediol and about 40～about 95mol%; (2,2,4 of viii) about 15～about 40mol%, 4-tetramethyl--1, the residue of the 1,4 cyclohexane dimethanol of the residue of 3-cyclobutanediol and about 60～about 85mol%; (ix) 2,2,4 of about 20～about 30mol%, 4-tetramethyl--1, the residue of the 1,4 cyclohexane dimethanol of the residue of 3-cyclobutanediol and about 70～about 80mol%; (x) 2,2,4 of about 20～about 25mol%, 4-tetramethyl--1, the residue of the 1,4 cyclohexane dimethanol of the residue of 3-cyclobutanediol and about 75～about 80mol%.
Believe, comprise by terephthalic acid, its ester or its mixture, 1,4-cyclohexanedimethanol and 2,2,4,4-tetramethyl--1, the 3-cyclobutanediol forms, certain composition with certain monomer composition, logarithmic viscosity number and/or second-order transition temperature, in high impact strength, stability to hydrolysis, toughness, chemical resistant properties, good color and transparency, long crystallization half-life, low ductility to the fragility excess temperature, aspect one or more of low-gravity and hot formability, be better than polyester as known in the art and polycarbonate.Think that these compositions are similar to polycarbonate aspect thermotolerance, and still can on standard industry equipment, process.
Another aspect of the present invention, for example, the Tg that is used for the polyester of composition of the present invention, method and moulded products can be at least a of following scope: 60～200 ℃; 60～190 ℃; 60～180 ℃; 60～170 ℃; 60～160 ℃; 60～155 ℃; 60～150 ℃; 60～145 ℃; 60～140 ℃; 60～138 ℃; 60～135 ℃; 60～130 ℃; 60～125 ℃; 60～120 ℃; 60～115 ℃; 60～110 ℃; 60～105 ℃; 60～100 ℃; 60～95 ℃; 60～90 ℃; 60～85 ℃; 60～80 ℃; 60～75 ℃; 65～200 ℃; 65～190 ℃; 65～180 ℃; 65～170 ℃; 65～160 ℃; 65～155 ℃; 65～150 ℃; 65～145 ℃; 65～140 ℃; 65～138 ℃; 65～135 ℃; 65～130 ℃; 65～125 ℃; 65～120 ℃; 65～115 ℃; 65～110 ℃; 65～105 ℃; 65～100 ℃; 65～95 ℃; 65～90 ℃; 65～85 ℃; 65～80 ℃; 65～75 ℃; 70～200 ℃; 70～190 ℃; 70～180 ℃; 70～170 ℃; 70～160 ℃; 70～155 ℃; 70～150 ℃; 70～145 ℃; 70～140 ℃; 70～138 ℃; 70～135 ℃; 70～130 ℃; 70～125 ℃; 70～120 ℃; 70～115 ℃; 70～110 ℃; 70～105 ℃; 70～100 ℃; 70～95 ℃; 70～90 ℃; 70～85 ℃; 70～80 ℃; 70～75 ℃; 75～200 ℃; 75～190 ℃; 75～180 ℃; 75～170 ℃; 75～160 ℃; 75～155 ℃; 75～150 ℃; 75～145 ℃; 75～140 ℃; 75～138 ℃; 75～135 ℃; 75～130 ℃; 75～125 ℃; 75～120 ℃; 75～115 ℃; 75～110 ℃; 75～105 ℃; 75～100 ℃; 75～95 ℃; 75～90 ℃; 75～85 ℃; 75～80 ℃; 80～200 ℃; 80～190 ℃; 80～180 ℃; 80～170 ℃; 80～160 ℃; 80～155 ℃; 80～150 ℃; 80～145 ℃; 80～140 ℃; 80～138 ℃; 80～135 ℃; 80～130 ℃; 80～125 ℃; 80～120 ℃; 80～115 ℃; 80～110 ℃; 80～105 ℃; 80～100 ℃; 80～95 ℃; 80～90 ℃; 80～85 ℃; 85～200 ℃; 85～190 ℃; 85～180 ℃; 85～170 ℃; 85～160 ℃; 85～155 ℃; 85～150 ℃; 85～145 ℃; 85～140 ℃; 85～138 ℃; 85～135 ℃; 85～130 ℃; 85～125 ℃; 85～120 ℃; 85～115 ℃; 85～110 ℃; 85～105 ℃; 85～100 ℃; 85～95 ℃; 85～90 ℃; 90～200 ℃; 90～190 ℃; 90～180 ℃; 90～170 ℃; 90～160 ℃; 90～155 ℃; 90～150 ℃; 90～145 ℃; 90～140 ℃; 90～138 ℃; 90～135 ℃; 90～130 ℃; 90～125 ℃; 90～120 ℃; 90～115 ℃; 90～110 ℃; 90～105 ℃; 90～100 ℃; 90～95 ℃; 95～200 ℃; 95～190 ℃; 95～180 ℃; 95～170 ℃; 95～160 ℃; 95～155 ℃; 95～150 ℃; 95～145 ℃; 95～140 ℃; 95～138 ℃; 95～135 ℃; 95～130 ℃; 95～125 ℃; 95～120 ℃; 95～115 ℃; 95～110 ℃; 95～105 ℃; 95～100 ℃; 100～200 ℃; 100～190 ℃; 100～180 ℃; 170 ℃ of 100o; 100～160 ℃; 100～155 ℃; 100～150 ℃; 100～145 ℃; 100～140 ℃; 100～138 ℃; 100～135 ℃; 100～130 ℃; 100～125 ℃; 100～120 ℃; 100～115 ℃; 100～110 ℃; 105～200 ℃; 105～190 ℃; 105～180 ℃; 105～170 ℃; 105～160 ℃; 105～155 ℃; 105～150 ℃; 105～145 ℃; 105～140 ℃; 105～138 ℃; 105～135 ℃; 105～130 ℃; 105～125 ℃; 105～120 ℃; 105～115 ℃; 105～110 ℃; 110～200 ℃; 110～190 ℃; 110～180 ℃; 110～170 ℃; 110～160 ℃; 110～155 ℃; 110～150 ℃; 110～145 ℃; 110～140 ℃; 110～138 ℃; 110～135 ℃; 110～130 ℃; 110～125 ℃; 110～120 ℃; 110～115 ℃; 115～200 ℃; 115～190 ℃; 115～180 ℃; 115～170 ℃; 115～160 ℃; 115～155 ℃; 115～150 ℃; 115～145 ℃; 115～140 ℃; 115～138 ℃; 115～135 ℃; 110～130 ℃; 115～125 ℃; 115～120 ℃; 120～200 ℃; 120～190 ℃; 120～180 ℃; 120～170 ℃; 120～160 ℃; 120～155 ℃; 120～150 ℃; 120～145 ℃; 120～140 ℃; 120～138 ℃; 120～135 ℃; 120～130 ℃; 125～200 ℃; 125～190 ℃; 125～180 ℃; 125～170 ℃; 125～165 ℃; 125～160 ℃; 125～155 ℃; 125～150 ℃; 125～145 ℃; 125～140 ℃; 125～138 ℃; 125～135 ℃; 127～200 ℃; 127～190 ℃; 127～180 ℃; 127～170 ℃; 127～160 ℃; 127～150 ℃; 127～145 ℃; 127～140 ℃; 127～138 ℃; 127～135 ℃; 130～200 ℃; 130～190 ℃; 130～180 ℃; 130～170 ℃; 130～160 ℃; 130～155 ℃; 130～150 ℃; 130～145 ℃; 130～140 ℃; 130～138 ℃; 130～135 ℃; 135～200 ℃; 135～190 ℃; 135～180 ℃; 135～170 ℃; 135～160 ℃; 135～155 ℃; 135～150 ℃; 135～145 ℃; 135～140 ℃; 140～200 ℃; 140～190 ℃; 140～180 ℃; 140～170 ℃; 140～160 ℃; 140～155 ℃; 140～150 ℃; 140～145 ℃; 148～200 ℃; 148～190 ℃; 148～180 ℃; 148～170 ℃; 148～160 ℃; 148～155 ℃; 148～150 ℃; Greater than 148～200 ℃; Greater than 148～190 ℃; Greater than 148～180 ℃; Greater than 148～170 ℃; Greater than 148～160 ℃; Greater than 148～155 ℃; 150～200 ℃; 150～190 ℃; 150～180 ℃; 150～170 ℃; 150～160; 155～190 ℃; 155～180 ℃; 155～170 ℃; With 155～165 ℃.
Others of the present invention, the diol component that is used for polyester of the present invention comprise but are not to be defined in, following combination range at least a: 2,2,4 of 1～99mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 1～99mol%; 2,2,4 of 1～95mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 5～99mol%; 2,2,4 of 1～90mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 10～99mol%; 2,2,4 of 1～85mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 15～99mol%; 2,2,4 of 1～80mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 20～99mol%, 2,2,4 of 1～75mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 25～99mol%; 2,2,4 of 1～70mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 30～99mol%; 2,2,4 of 1～65mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 35～99mol%; 2,2,4 of 1～60mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 40～99mol%; 2,2,4 of 1～55mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 45～99mol%; 2,2,4 of 1～50mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 50～99mol%; 2,2,4 of 1～45mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 55～99mol%; 2,2,4 of 1～40mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 60～99mol%; 2,2,4 of 1～35mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 65～99mol%; 2,2,4 of 1～30mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 70～99mol%; 2,2,4 of 1～25mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 75～99mol%; 2,2,4 of 1～20mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 80～99mol%; 2,2,4 of 1～15mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 85～99mol%; 2,2,4 of 1～10mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 90～99mol%; With 2,2,4 of 1～5mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 95～99mol%.
Others of the present invention, the diol component that is used for polyester of the present invention comprise but are not to be defined in, following combination range at least a: 0.01～less than 2 of 5mol%, 2,4,4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 95～99.99mol%; 0.01 2,2,4 of～4.5mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 95.5～99.99mol%; 0.01 2,2,4 of～4mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 96～99.99mol%; 0.01 2,2,4 of～3.5mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 96.5～99.99mol%; 0.01 2,2,4 of～3mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 97～99.99mol%; 0.01 2,2,4 of～2.5mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 97.5～99.99mol%; 0.01 2,2,4 of～2mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 98～99.99mol%; 0.01 2,2,4 of～1.5mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 98.5～99.99mol%; 0.01 2,2,4 of～1mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 99～99.99mol%; With 2,2,4 of 0.01～0.5mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 99.5～99.99mol%.
Others of the present invention, the diol component that is used for polyester of the present invention comprise but are not to be defined in, following combination range at least a: 2,2,4 of 5～99mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 1～95mol%; 2,2,4 of 5～95mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 5～95mol%; 2,2,4 of 5～90mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 10～95mol%; 2,2,4 of 5～85mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 15～95mol%; 2,2,4 of 5～80mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 20～95mol%; 2,2,4 of 5～75mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 25～95mol%; 2,2,4 of 5～70mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 30～95mol%; 2,2,4 of 5～65mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 35～95mol%; 2,2,4 of 5～60mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 40～95mol%; 2,2,4 of 5～55mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 45～95mol%; With 2,2,4 of 5～50mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 50～95mol%.
Others of the present invention, the diol component that is used for polyester of the present invention comprise but are not to be defined in, following combination range at least a: 5～less than 2 of 50mol%, 2,4,4-tetramethyl--1,3-cyclobutanediol and greater than the 1,4 cyclohexane dimethanol of 50～95mol%; 2,2,4 of 5～45mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 55～95mol%; 2,2,4 of 5～40mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 60～95mol%; 2,2,4 of 5～35mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 65～95mol%; 5～less than 2,2,4 of 35mol%, 4-tetramethyl--1,3-cyclobutanediol and greater than the 1,4 cyclohexane dimethanol of 65～95mol%; 2,2,4 of 5～30mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 70～95mol%; 2,2,4 of 5～25mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 75～95mol%; 2,2,4 of 5～20mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 80～95mol%; 2,2,4 of 5～15mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 85～95mol%; 2,2,4 of 5～10mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 90～95mol%; Greater than 5～and less than 2,2,4 of 10mol%, 4-tetramethyl--1,3-cyclobutanediol and less than 90～greater than the 1,4 cyclohexane dimethanol of 95mol%; 2,2,4 of 5.5mol%～9.5mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 94.5mol%～90.5mol%; With 2,2,4 of 6～9mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 94～91mol%.
Others of the present invention, the diol component that is used for polyester of the present invention comprise but are not to be defined in, following combination range at least a: 2,2,4 of 10～99mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 1～90mol%; 2,2,4 of 10～95mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 5～90mol%; 2,2,4 of 10～90mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 10～90mol%; 2,2,4 of 10～85mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 15～90mol%; 2,2,4 of 10～80mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 20～90mol%; 2,2,4 of 10～75mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 25～90mol%; 2,2,4 of 10～70mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 30～90mol%; 2,2,4 of 10～65mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 35～90mol%; 2,2,4 of 10～60mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 40～90mol%; 2,2,4 of 10～55mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 45～90mol%; 2,2,4 of 10～50mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 50～90mol%; 10～less than 2,2,4 of 50mol%, 4-tetramethyl--1,3-cyclobutanediol and greater than the 1,4 cyclohexane dimethanol of 50～90mol%; 2,2,4 of 10～45mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 55～90mol%; 2,2,4 of 10～40mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 60～90mol%; 2,2,4 of 10～35mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 65～90mol%; 10～less than 2,2,4 of 35mol%, 4-tetramethyl--1,3-cyclobutanediol and, 4-cyclohexanedimethanol greater than 65～90%1; 2,2,4 of 10～30mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 70～90mol%; 2,2,4 of 10～25mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 75～90mol%; 2,2,4 of 10～20mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 80～90mol%; With 2,2,4 of 10～15mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 85～90mol%.
Others of the present invention, the diol component that is used for polyester of the present invention comprise but are not to be defined in, following combination range at least a: 2,2,4 of 14～99mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 1～86mol%; 2,2,4 of 14～95mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 5～86mol%; 2,2,4 of 14～90mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 10～86mol%; 2,2,4 of 14～85mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 15～86mol%; 2,2,4 of 14～80mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 20～86mol%; 2,2,4 of 14～75mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 25～86mol%; 2,2,4 of 14～70mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 30～86mol%; 2,2,4 of 14～65mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 35～86mol%; 2,2,4 of 14～60mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 40～86mol%; 2,2,4 of 14～55mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 45～86mol%; 2,2,4 of 14～50mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 50～86mol%; 14～less than 2,2,4 of 50mol%, 4-tetramethyl--1,3-cyclobutanediol and greater than the 1,4 cyclohexane dimethanol of 50～86mol%; 2,2,4 of 14～45mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 55～86mol%; 2,2,4 of 14～40mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 60～86mol%; 2,2,4 of 14～35mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 65～86mol%; 2,2,4 of 14～30mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 70～86mol%; 2,2,4 of 14～24mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 76～86mol%; With 2,2,4 of 14～25mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 75～86mol%.
Others of the present invention, the diol component that is used for polyester of the present invention comprise but are not to be defined in, following combination range at least a: 2,2,4 of 15～99mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 1～85mol%; 2,2,4 of 15～95mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 5～85mol%; 2,2,4 of 15～90mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 10～85mol%; 2,2,4 of 15～85mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 15～85mol%; 2,2,4 of 15～80mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 20～85mol%; 2,2,4 of 15～75mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 25～85mol%; 2,2,4 of 15～70mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 30～85mol%; 2,2,4 of 15～65mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 35～85mol%; 2,2,4 of 15～60mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 40～85mol%; 2,2,4 of 15～55mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 45～85mol%; 2,2,4 of 15～50mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 50～85mol%; 15～less than 2,2,4 of 50mol%, 4-tetramethyl--1,3-cyclobutanediol and greater than the 1,4 cyclohexane dimethanol of 50～85mol%; 2,2,4 of 15～45mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 55～85mol%; 2,2,4 of 15～40mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 60～85mol%; 2,2,4 of 15～35mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 65～85mol%; 2,2,4 of 15～30mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 70～85mol%; 2,2,4 of 15～25mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 75～85mol%; With 2,2,4 of 15～24mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 76～85mol%.
Others of the present invention, the diol component that is used for polyester of the present invention comprise but are not to be defined in, following combination range at least a: 2,2,4 of 20～99mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 1～80mol%; 2,2,4 of 20～95mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 5～80mol%; 2,2,4 of 20～90mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 10～80mol%; 2,2,4 of 20～85mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 15～80mol%; 2,2,4 of 20～80mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 20～80mol%; 2,2,4 of 20～75mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 25～80mol%; 2,2,4 of 20～70mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 30～80mol%; 2,2,4 of 20～65mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 35～80mol%; 2,2,4 of 20～60mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 40～80mol%; 2,2,4 of 20～55mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 45～80mol%; 2,2,4 of 20～50mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 50～80mol%; 20～less than 2,2,4 of 50mol%, 4-tetramethyl--1,3-cyclobutanediol and greater than the 1,4 cyclohexane dimethanol of 50～80mol%; 2,2,4 of 20～45mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 55～80mol%; 2,2,4 of 20～40mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 60～80mol%; 2,2,4 of 20～35mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 65～80mol%; 2,2,4 of 20～30mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 70～80mol%; With 2,2,4 of 20～25mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 75～80mol%.
Others of the present invention, the diol component that is used for polyester of the present invention comprise but are not to be defined in, following combination range at least a: 2,2,4 of 25～99mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 1～75mol%; 2,2,4 of 25～95mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 5～75mol%; 2,2,4 of 25～90mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 10～75mol%; 2,2,4 of 25～85mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 15～75mol%; 2,2,4 of 25～80mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 20～75mol%; 2,2,4 of 25～75mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 25～75mol%; 2,2,4 of 25～70mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 30～75mol%; 2,2,4 of 25～65mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 35～75mol%; 2,2,4 of 25～60mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 40～75mol%; 2,2,4 of 25～55mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 45～75mol%; 2,2,4 of 25～50mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 50～75mol%; 25～less than 2,2,4 of 50mol%, 4-tetramethyl--1,3-cyclobutanediol and greater than the 1,4 cyclohexane dimethanol of 50～75mol%; 2,2,4 of 25～45mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 55～75mol%; 2,2,4 of 25～40mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 60～75mol%; 2,2,4 of 25～35mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 65～75mol%; With 2,2,4 of 25～30mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 70～75mol%.
Others of the present invention, the diol component that is used for polyester of the present invention comprise but are not to be defined in, following combination range at least a: 2,2,4 of 30～99mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 1～70mol%; 2,2,4 of 30～95mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 5～70mol%; 2,2,4 of 30～90mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 10～70mol%; 2,2,4 of 30～85mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 15～70mol%; 2,2,4 of 30～80mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 20～70mol%; 2,2,4 of 30～75mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 25～70mol%; 2,2,4 of 30～70mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 30～70mol%; 2,2,4 of 30～65mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 35～70mol%; 2,2,4 of 30～60mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 40～70mol%; 2,2,4 of 30～55mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 45 to 70mol%; 2,2,4 of 30～50mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 50～70mol%; 30～less than 2,2,4 of 50mol%, 4-tetramethyl--1,3-cyclobutanediol and greater than the 1,4 cyclohexane dimethanol of 50～70mol%; 2,2,4 of 30～45mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 55～70mol%; 2,2,4 of 30～40mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 60～70mol%; 2,2,4 of 30～35mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 65～70mol%.
Others of the present invention, the diol component that is used for polyester of the present invention comprise but are not to be defined in, following combination range at least a: 2,2,4 of 35～99mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 1～65mol%; 2,2,4 of 35～95mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 5～65mol%; 2,2,4 of 35～90mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 10～65mol%; 2,2,4 of 35～85mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 15～65mol%; 2,2,4 of 35～80mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 20～65mol%; 2,2,4 of 35～75mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 25～65mol%; 2,2,4 of 35～70mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 30～65mol%; 2,2,4 of 35～65mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 35～65mol%; 2,2,4 of 35～60mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 40～65mol%; 2,2,4 of 35～55mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 45～65mol%; 2,2,4 of 35～50mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 50～65mol%; 35～less than 2,2,4 of 50mol%, 4-tetramethyl--1,3-cyclobutanediol and greater than the 1,4 cyclohexane dimethanol of 50～65mol%; 2,2,4 of 35～45mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 55～65mol%; 2,2,4 of 35～40mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 60～65mol%.
Others of the present invention, the diol component that is used for polyester of the present invention comprise but are not to be defined in, following combination range at least a: 2,2,4 of 40～99mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 1～60mol%; 2,2,4 of 40～95mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 5～60mol%; 2,2,4 of 40～90mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 10～60mol%; 2,2,4 of 40～85mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 15～60mol%; 2,2,4 of 40～80mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 20～60mol%; 2,2,4 of 40～75mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 25～60mol%; 2,2,4 of 40～70mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 30～60mol%; 2,2,4 of 40～65mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 35～60mol%; 2,2,4 of 40～60mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 40～60mol%; 2,2,4 of 40～55mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 45～60mol%; 40～less than 2,2,4 of 50mol%, 4-tetramethyl--1,3-cyclobutanediol and greater than the 1,4 cyclohexane dimethanol of 50～60mol%; 2,2,4 of 40～50mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 50～60mol%; With 2,2,4 of 40～45mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 55～60mol%.
Others of the present invention, the diol component that is used for polyester of the present invention comprise but are not to be defined in, following combination range at least a: 2,2,4 of 45～99mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 1～55mol%; 2,2,4 of 45～95mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 5～55mol%; 2,2,4 of 45～90mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 10～55mol%; 2,2,4 of 45～85mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 15～55mol%; 2,2,4 of 45～80mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 20～55mol%; 2,2,4 of 45～75mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 25～55mol%; 2,2,4 of 45～70mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 30～55mol%; 2,2,4 of 45～65mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 35～55mol%; 2,2,4 of 45～60mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 40～55mol%; Greater than 2,2,4 of 45～55mol%, 4-tetramethyl--1,3-cyclobutanediol and 45～less than the 1,4 cyclohexane dimethanol of 55mol%; 2,2,4 of 45～55mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 45～55mol%; With 2,2,4 of 45～50mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 50～60mol%.
Others of the present invention, the diol component that is used for polyester of the present invention comprise but are not to be defined in, following combination range at least a: greater than 2 of 50～99mol%, 2,4,4-tetramethyl--1,3-cyclobutanediol and 1～less than the 1,4 cyclohexane dimethanol of 50mol%; Greater than 2,2,4 of 50～95mol%, 4-tetramethyl--1,3-cyclobutanediol and 5～less than the 1,4 cyclohexane dimethanol of 50mol%; Greater than 2,2,4 of 50～90mol%, 4-tetramethyl--1,3-cyclobutanediol and 10～less than the 1,4 cyclohexane dimethanol of 50mol%; Greater than 2,2,4 of 50～85mol%, 4-tetramethyl--1,3-cyclobutanediol and 15～less than the 1,4 cyclohexane dimethanol of 50mol%; Greater than 2,2,4 of 50～80mol%, 4-tetramethyl--1,3-cyclobutanediol and 20～less than the 1,4 cyclohexane dimethanol of 50mol%; Greater than 2,2,4 of 50～75mol%, 4-tetramethyl--1,3-cyclobutanediol and 25～less than the 1,4 cyclohexane dimethanol of 50mol%; Greater than 2,2,4 of 50～70mol%, 4-tetramethyl--1,3-cyclobutanediol and 30～less than the 1,4 cyclohexane dimethanol of 50mol%; Greater than 2,2,4 of 50～65mol%, 4-tetramethyl--1,3-cyclobutanediol and 35～less than the 1,4 cyclohexane dimethanol of 50mol%; Greater than 2,2,4 of 50～60mol%, 4-tetramethyl--1,3-cyclobutanediol and 40～less than the 1,4 cyclohexane dimethanol of 50mol%.
Others of the present invention, the diol component that is used for polyester of the present invention comprise but are not to be defined in, following combination range at least a: 2,2,4 of 55～99mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 1～45mol%; 2,2,4 of 55～95mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 5～45mol%; 2,2,4 of 55～90mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 10～45mol%; 2,2,4 of 55～85mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 15～45mol%; 2,2,4 of 55～80mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 20～45mol%; 2,2,4 of 55～75mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 25～45mol%; 2,2,4 of 55～70mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 30～45mol%; 2,2,4 of 55～65mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 35～45mol%; With 2,2,4 of 55～60mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 40～45mol%.
Others of the present invention, the diol component that is used for polyester of the present invention comprise but are not to be defined in, following combination range at least a: 2,2,4 of 60～99mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 1～40mol%; 2,2,4 of 60～95mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 5～40mol%; 2,2,4 of 60～90mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 10～40mol%; 2,2,4 of 60～85mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 15～40mol%; 2,2,4 of 60～80mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 20～40mol%; 2,2,4 of 60～75mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 25～40mol%; With 2,2,4 of 60～70mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 30～40mol%.
Others of the present invention, the diol component that is used for polyester of the present invention comprise but are not to be defined in, following combination range at least a: 2,2,4 of 65～99mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 1～35mol%; 2,2,4 of 65～95mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 5～35mol%; 2,2,4 of 65～90mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 10～35mol%; 2,2,4 of 65～85mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 15～35mol%; 2,2,4 of 65～80mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 20～35mol%; 2,2,4 of 65～75mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 25～35mol%; With 2,2,4 of 65～70mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 35～40mol%.
Others of the present invention, the diol component that is used for polyester of the present invention comprise but are not to be defined in, following combination range at least a: 2,2,4 of 70～99mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 1～30mol%; 2,2,4 of 70～95mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 5～30mol%; 2,2,4 of 70～90mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 10～30mol%; 2,2,4 of 70～85mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 15～30mol%; 2,2,4 of 70～80mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 20～30mol%; 2,2,4 of 70～75mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 25～30mol%.
Others of the present invention, the diol component that is used for polyester of the present invention comprise but are not to be defined in, following combination range at least a: 2,2,4 of 75～99mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 1～25mol%; 2,2,4 of 75～95mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 5～25mol%; 2,2,4 of 75～90mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 10～25mol%; With 2,2,4 of 75～85mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 15～25mol%.
Others of the present invention, the diol component that is used for polyester of the present invention comprise but are not to be defined in, following combination range at least a: 2,2,4 of 80～99mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 1～20mol%; 2,2,4 of 80～95mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 5～20mol%; 2,2,4 of 80～90mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 10～20mol%.
Others of the present invention, the diol component that is used for polyester of the present invention comprise but are not to be defined in, following combination range at least a: 2,2,4 of 37～80mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 20～63mol%; 40～less than 2,2,4 of 45mol%, 4-tetramethyl--1,3-cyclobutanediol and greater than the 1,4 cyclohexane dimethanol of 55～60mol%; Greater than 2,2,4 of 45～55mol%, 4-tetramethyl--1,3-cyclobutanediol and 45～less than the 1,4 cyclohexane dimethanol of 55mol%; With 2,2,4 of 46～55mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 45～54mol%; With 2,2,4 of 46～65mol%, 4-tetramethyl--1, the 1,4 cyclohexane dimethanol of 3-cyclobutanediol and 35～54mol%.
Others of the present invention, wherein 2,2,4,4-tetramethyl--1, the molecular fraction that the 3-cyclobutanediol exists is 0.01～less than 5mol%, based on the molecular fraction of the diol component that equals 100mol%, and wherein randomly have CHDM, the diol component that is used for polyester of the present invention comprises but is not to be defined in, following combination range at least a: 0.01～less than 2 of 5mol%, 2,4,4-tetramethyl--1,3-cyclobutanediol residue, greater than the glycol residue of 0.01～95mol% and the 1,4 cyclohexane dimethanol of 0～99.98mol%; 0.01～less than 2,2,4 of 5mol%, 4-tetramethyl--1,3-cyclobutanediol residue, greater than the 1,4 cyclohexane dimethanol of 0.01～94.99mole%of glycol residue and 0.01～99.98mol%; 0.01～less than 2,2,4 of 5mol%, 4-tetramethyl--1,3-cyclobutanediol residue, greater than the glycol residue of 0.01～90mol% and the 1,4 cyclohexane dimethanol of 5～99.98mol%; 0.01～less than 2,2,4 of 5mol%, 4-tetramethyl--1,3-cyclobutanediol residue, greater than the glycol residue of 0.01～85mol% and the 1,4 cyclohexane dimethanol of 10～99.98mol%; 0.01～less than 2,2,4 of 5mol%, 4-tetramethyl--1,3-cyclobutanediol residue, greater than the glycol residue of 0.01～80mol% and the 1,4 cyclohexane dimethanol of 15～99.98mol%; 0.01～less than 2,2,4 of 5mol%, 4-tetramethyl--1,3-cyclobutanediol residue, greater than the glycol residue of 0.01～75mol% and the 1,4 cyclohexane dimethanol of 20～99.98mol%; 0.01～less than 2,2,4 of 5mol%, 4-tetramethyl--1,3-cyclobutanediol residue, greater than the glycol residue of 0.01～70mol% and the 1,4 cyclohexane dimethanol of 25～99.98mol%; Greater than the glycol residue of 0.01～65mol% and the 1,4 cyclohexane dimethanol of 30～99.98mol%; 0.01～less than 2,2,4 of 5mol%, 4-tetramethyl--1,3-cyclobutanediol residue, greater than the glycol residue of 0.01～60mol% and the 1,4 cyclohexane dimethanol of 35～99.98mol%; 0.01～less than 2,2,4 of 5mol%, 4-tetramethyl--1,3-cyclobutanediol residue, greater than the glycol residue of 0.01～55mol% and the 1,4 cyclohexane dimethanol of 40～99.98mol%; 0.01～less than 2,2,4 of 5mol%, 4-tetramethyl--1,3-cyclobutanediol residue, greater than the glycol residue of 0.01～50mol% and the 1,4 cyclohexane dimethanol of 45～99.98mol%; 0.01～less than 2,2,4 of 5mol%, 4-tetramethyl--1,3-cyclobutanediol residue, greater than the glycol residue of 0.01～45mol% and the 1,4 cyclohexane dimethanol of 50～99.98mol%; 0.01～less than 2,2,4 of 5mol%, 4-tetramethyl--1,3-cyclobutanediol residue, greater than the glycol residue of 0.01～40mol% and the 1,4 cyclohexane dimethanol of 55～99.98mol%; 0.01～less than 2,2,4 of 5mol%, 4-tetramethyl--1,3-cyclobutanediol residue, greater than the glycol residue of 0.01～35mol% and the 1,4 cyclohexane dimethanol of 60～99.98mol%; 0.01～less than 2,2,4 of 5mol%, 4-tetramethyl--1,3-cyclobutanediol residue, greater than the glycol residue of 0.01～30mol% and the 1,4 cyclohexane dimethanol of 65～99.98mol%; 0.01～less than 2,2,4 of 5mol%, 4-tetramethyl--1,3-cyclobutanediol residue, greater than the glycol residue of 0.01～25mol% and the 1,4 cyclohexane dimethanol of 70～99.98mol%; 0.01～less than 2,2,4 of 5mol%, 4-tetramethyl--1,3-cyclobutanediol residue, greater than the glycol residue of 0.01～20mol% and the 1,4 cyclohexane dimethanol of 75～99.98mol%; 0.01～less than 2,2,4 of 5mol%, 4-tetramethyl--1,3-cyclobutanediol residue, greater than the glycol residue of 0.01～15mol% and the 1,4 cyclohexane dimethanol of 80～99.98mol%; 0.01～less than 2,2,4 of 5mol%, 4-tetramethyl--1,3-cyclobutanediol residue, greater than the glycol residue of 0.01～10mol% and the 1,4 cyclohexane dimethanol of 85～99.98mol%; 0.01～less than 2,2,4 of 5mol%, 4-tetramethyl--1,3-cyclobutanediol residue, greater than the glycol residue of 0.01～5mol% and the 1,4 cyclohexane dimethanol of 90～99.98mol%; 0.01～less than 2,2,4 of 5mol%, 4-tetramethyl--1,3-cyclobutanediol residue and greater than the glycol residue of 0.01～5mol% and the 1,4 cyclohexane dimethanol of 90～99.98mol%.
This diol component also can contain 2,2,4 of one of following scope, 4-tetramethyl--1,3-cyclobutanediol residue: 0.01～4.5mol%; 0.01～4mol%; 0.01～3.5mol%; 0.01～3mol%; 0.01～2.5mol%; 0.01～2.0mol%; 0.01～2.5mol%; 0.01～2mol%; 0.01～1.5mol%; 0.01～1.0mol%; With 0.01～0.5mol%.The diol component of remainder can be the 1,4 cyclohexane dimethanol and/or the ethylene glycol of any amount, as long as the total amount of diol component equals 100mol%.
Except that above-mentioned glycol, the polyester that is applicable to polymer blend of the present invention can be by 1, ammediol, 1, and 4-butyleneglycol or its mixture are made.Expection is by 1, ammediol, 1, the present composition that 4-butyleneglycol or its mixture are made can have at least a described Tg scope, at least a described logarithmic viscosity number scope and/or at least a described glycol or two acid ranges herein herein herein.In addition or alternatively, by 1, ammediol, 1, the polyester that 4-butyleneglycol or its mixture are made also can be to be made by the 1,4 cyclohexane dimethanol with at least a following consumption: 0.1～99mol%; 0.1～90mol%; 0.1～80mol%; 0.1～70mol%; 0.1～60mol%; 0.1～50mol%; 0.1～40mol%; 0.1～35mol%; 0.1～30mol%; 0.1～25mol%; 0.1～20mol%; 0.1～15mol%; 0.1～10mol%; 0.1～5mol%; 1～99mol%; 1～90mol%; 1～80mol%; 1～70mol%; 1～60mol%; 1～50mol%; 1～40mol%; 1～35mol%; 1～30mol%; 1～25mol%; 1～20mol%; 1～15mol%; 1～10mol%; 1～5mol%; 5～80mol%; 5～70mol%; 5～60mol%; 5～50mol%; 5～40mol%; 5～35mol%; 5～30mol%; 5～25mol%; 5～20mol%; With 5～15mol%; 5～10mol%; 10～99mol%; 10～90mol%; 10～80mol%; 10～70mol%; 10～60mol%; 10～50mol%; 10～40mol%; 10～35mol%; 10～30mol%; 10～25mol%; 10～20mol%; 10～15mol%; 20～99mol%; 20～95mol%; 20～80mol%; 20～70mol%; 20～60mol%; 20～50mol%; 20～40mol%; 20～35mol%; 20～30mol%; With 20～25mol%.
The logarithmic viscosity number of this polyester (I.V.) is generally about 0.1dL/g～about 1.4dL/g.I.V. other example of scope comprises about 0.65dL/g～about 1.0dL/g and about 0.7dL/g～about 0.85dL/g.As previously mentioned, the solvent 0.5g polymkeric substance that adopts every 100mL to contain 60wt% phenol and 40wt% tetrachloroethane is measured logarithmic viscosity number down at 25 ℃.For embodiments of the present invention, be applicable to that polyester of the present invention can show at least a following logarithmic viscosity number, it is being measured in 60/40 (wt/wt) phenol/tetrachloroethane under 25 ℃ with 0.5g/100mL concentration: 0.10～1.2dL/g; 0.10～1.1dL/g; 0.10～1dL/g; 0.10～less than 1dL/g; 0.10～0.98dL/g; 0.10～0.95dL/g; 0.10～0.90dL/g; 0.10～0.85dL/g; 0.10～0.80dL/g; 0.10～0.75dL/g; 0.10～less than 0.75dL/g; 0.10～0.72dL/g; 0.10～0.70dL/g; 0.10～less than 0.70 dL/g; 0.10～0.68 dL/g; 0.10～less than 0.68dL/g; 0.10～0.65dL/g; 0.10～0.6dL/g; 0.10～0.55dL/g; 0.10～0.5dL/g; 0.10～0.4dL/g; 0.10～0.35dL/g; 0.20～1.2dL/g; 0.20～1.1dL/g; 0.20～1dL/g; 0.20～less than 1dL/g; 0.20～0.98dL/g; 0.20～0.95dL/g; 0.20～0.90dL/g; 0.20～0.85dL/g; 0.20～0.80dL/g; 0.20～0.75dL/g; 0.20～less than 0.75dL/g; 0.20～0.72dL/g; 0.20～0.70dL/g; 0.20～less than 0.70dL/g; 0.20～0.68 dL/g; 0.20～less than 0.68dL/g; 0.20～0.65dL/g; 0.20～0.6dL/g; 0.20～0.55dL/g; 0.20～0.5dL/g; 0.20～0.4dL/g; 0.20～0.35dL/g; 0.35～1.2dL/g; 0.35～1.1dL/g; 0.35～1dL/g; 0.35～less than 1dL/g; 0.35～0.98dL/g; 0.35～0.95dL/g; 0.35～0.90dL/g; 0.35～0.85dL/g; 0.35～0.80dL/g; 0.35～0.75dL/g; 0.35～less than 0.75dL/g; 0.35～0.72dL/g; 0.35～0.70dL/g; 0.35～less than 0.70dL/g; 0.35～0.68dL/g; 0.35～less than 0.68dL/g; 0.35～0.65dL/g; 0.40～1.2dL/g; 0.40～1.1dL/g; 0.40～1dL/g; 0.40～less than 1dL/g; 0.40～0.98dL/g; 0.40～0.95dL/g; 0.40～0.90dL/g; 0.40～0.85dL/g; 0.40～0.80dL/g; 0.40～0.75dL/g; 0.40～less than 0.75dL/g; 0.40～0.72dL/g; 0.40～0.70dL/g; 0.40～less than 0.70dL/g; 0.40～0.68dL/g; 0.40～less than 0.68dL/g; 0.40～0.65dL/g; Greater than 0.42～1.2dL/g; Greater than 0.42～1.1dl/g; Greater than 0.42～1dL/g; Greater than 0.42～less than 1dL/g; Greater than 0.42～0.98dL/g; Greater than 0.42～0.95dL/g; Greater than 0.42～0.90dL/g; Greater than 0.42～0.85dL/g; Greater than 0.42～0.80dL/g; Greater than 0.42～0.75dL/g; Greater than 0.42～less than 0.75dL/g; Greater than 0.42～0.72dL/g; Greater than 0.42～0.70dL/g; Greater than 0.42～less than 0.70dL/g; Greater than 0.42～0.68dL/g; Greater than 0.42～less than 0.68dL/g; With greater than 0.42～0.65dL/g.
For embodiments of the present invention, be applicable to that polyester of the present invention can show at least a following logarithmic viscosity number, it is being measured in 60/40 (wt/wt) phenol/tetrachloroethane under 25 ℃ with 0.5g/100mL concentration: 0.45～1.2dL/g; 0.45～1.1dL/g; 0.45～1dL/g; 0.45～0.98dL/g; 0.45～0.95dL/g; 0.45～0.90dL/g; 0.45～0.85dL/g; 0.45～0.80dL/g; 0.45～0.75dL/g; 0.45～less than 0.75dL/g; 0.45～0.72dL/g; 0.45～0.70dL/g; 0.45～less than 0.70dL/g; 0.45～0.68dL/g; 0.45～less than 0.68dL/g; 0.45～0.65dL/g; 0.50～1.2dL/g; 0.50～1.1dL/g; 0.50～1dL/g; 0.50～less than 1dL/g; 0.50～0.98dL/g; 0.50～0.95dL/g; 0.50～0.90dL/g; 0.50～0.85dL/g; 0.50～0.80dL/g; 0.50～0.75dL/g; 0.50～less than 0.75dL/g; 0.50～0.72dL/g; 0.50～0.70dL/g; 0.50～less than 0.70dL/g; 0.50～0.68dL/g; 0.50～less than 0.68dL/g; 0.50～0.65dL/g; 0.55～1.2dL/g; 0.55～1.1dL/g; 0.55～1dL/g; 0.55～less than 1dL/g; 0.55～0.98dL/g; 0.55～0.95dL/g; 0.55～0.90dL/g; 0.55～0.85dL/g; 0.55～0.80dL/g; 0.55～0.75dL/g; 0.55～less than 0.75dL/g; 0.55～0.72dL/g; 0.55～0.70dL/g; 0.55～less than 0.70dL/g; 0.55～0.68dL/g; 0.55～less than 0.68dL/g; 0.55～0.65dL/g; 0.58～1.2dL/g; 0.58～1.1dL/g; 0.58～1dL/g; 0.58～less than 1dL/g; 0.58～0.98dL/g; 0.58～0.95dL/g; 0.58～0.90dL/g; 0.58～0.85dL/g; 0.58～0.80dL/g; 0.58～0.75dL/g; 0.58～less than 0.75dL/g; 0.58～0.72dL/g; 0.58～0.70dL/g; 0.58～less than 0.70dL/g; 0.58～0.68dL/g; 0.58～less than 0.68dL/g; 0.58～0.65dL/g; 0.60～1.2dL/g; 0.60～1.1dL/g; 0.60～1dL/g; 0.60～less than 1dL/g; 0.60～0.98dL/g; 0.60～0.95dL/g; 0.60～0.90dL/g; 0.60～0.85dL/g; 0.60～0.80dL/g; 0.60～0.75dL/g; 0.60～less than 0.75dL/g; 0.60～0.72dL/g; 0.60～0.70dL/g; 0.60～less than 0.70dL/g; 0.60～0.68dL/g; 0.60～less than 0.68dL/g; 0.60～0.65dL/g; 0.65～1.2dL/g; 0.65～1.1dL/g; 0.65～1dL/g; 0.65～less than 1dL/g; 0.65～0.98dL/g; 0.65～0.95dL/g; 0.65～0.90dL/g; 0.65～0.85dL/g; 0.65～0.80dL/g; 0.65～0.75dL/g; 0.65～less than 0.75dL/g; 0.65～0.72dL/g; 0.65～0.70dL/g; 0.65～less than 0.70dL/g; 0.68～1.2dL/g; 0.68～1.1dL/g; 0.68～1dL/g; 0.68～less than 1dL/g; 0.68～0.98dL/g; 0.68～0.95dL/g; 0.68～0.90dL/g; 0.68～0.85dL/g; 0.68～0.80dL/g; 0.68～0.75dL/g; 0.68～less than 0.75dL/g; 0.68～0.72dL/g; Greater than 0.76dL/g～1.2dL/g; Greater than 0.76dL/g～1.1dL/g; Greater than 0.76dL/g～1dL/g; Greater than 0.76dL/g～less than 1dL/g; Greater than 0.76dL/g～0.98dL/g; Greater than 0.76dL/g～0.95dL/g; Greater than 0.76dL/g～0.90dL/g; Greater than 0.80dL/g～1.2dL/g; Greater than 0.80dL/g～1.1dL/g; Greater than 0.80dL/g～1dL/g; Greater than 0.80dL/g～less than 1dL/g; Greater than 0.80dL/g～1.2dL/g; Greater than 0.80dL/g～0.98dL/g; Greater than 0.80dL/g～0.95dL/g; Greater than 0.80dL/g～0.90dL/g.
For containing 2,2,4,4-tetramethyl--1, the polyester of the present invention of 3-cyclobutanediol, cis/trans 2,2,4,4-tetramethyl--1, the mol ratio of 3-cyclobutanediol can be changed by every kind pure form or its mixture.In some embodiments, cis and/or trans 2,2,4,4-tetramethyl--1, the molar percentage of 3-cyclobutanediol are greater than the cis of 50mol% and trans less than 50mol%; Perhaps greater than the cis of 55mol% and trans less than 45mol%; Perhaps the cis of 30～70mol% and 70～30% trans; Perhaps the cis of 40～60mol% and 60～40mol%'s is trans; Perhaps trans and 50～30% cis of 50～70mol%; The perhaps cis of 50～70mol% and 50～30% trans; Perhaps the cis of 60～70mol% and 30～40mol%'s is trans; Perhaps greater than the cis of 70mol% and trans less than 30mol%; Cis-and trans-2,2,4 wherein, 4-tetramethyl--1, the molar percentage summation of 3-cyclobutanediol equals 100mol%.Cis/trans 2,2,4,4-tetramethyl--1, the mol ratio of 3-cyclobutanediol can change in 50/50～0/100 scope, and for example 40/60～20/80.
Expect that composition of the present invention can have at least a described logarithmic viscosity number scope and at least a described composition monomer scope herein herein, unless point out on the contrary.Expect that also composition of the present invention can have at least a described Tg scope and at least a described composition monomer scope herein herein, unless point out on the contrary.Expect that also composition of the present invention can have at least a described logarithmic viscosity number scope, at least a described Tg scope and at least a described composition monomer scope herein herein herein, unless point out on the contrary.
In some embodiments, terephthalic acid or its ester, for example the mixture of dimethyl terephthalate (DMT) or terephthalic acid residue and its ester can constitute part or all and be used to form the dicarboxylic acid component who is applicable to polyester of the present invention.In some embodiments, the terephthalic acid residue can constitute part or all dicarboxylic acid component who is used to form polyester of the present invention, concentration is 70mol% at least, as 80mol% at least, 90mol%, 95mol%, 99mol% or even 100mol% at least at least at least.In some embodiments,, can use the terephthalic acid of higher consumption in order to make the more polyester of high impact strength.For the purpose of the disclosure content, can be used alternatingly term " terephthalic acid " and " dimethyl terephthalate (DMT) " herein.In a kind of embodiment, dimethyl terephthalate (DMT) is for partly or entirely being used to prepare the dicarboxylic acid component who is used for polyester of the present invention.In all embodiments, can use range be terephthalic acid and/or dimethyl terephthalate (DMT) and/or its mixture of 70～100mol% or 80～100mol% or 90～100mol% or 99～100mol% or 100mol%.
Except that terephthalic acid, the dicarboxylic acid component who is applicable to polyester of the present invention can comprise up to 30mol%, up to 20mol%, up to 10mol%, up to 5mol% or up to the modified aromatic dicarboxylic acid of 1mol%.Still another embodiment contains the modified aromatic dicarboxylic acid of 0mol%.Thus,, expect that the amount ranges of one or more modified aromatic dicarboxylic acid can be any aforementioned endpoint value if when existing, for example, 0.01～30mol%, 0.01～20mol%, 0.01～10mol%, 0.01～5mol% and 0.01～1mol%.In a kind of embodiment, can be used for that modified aromatic dicarboxylic acid of the present invention comprises but be not to be defined in, have up to those of 20 carbon atoms, and it can be linear, right-orientation or symmetric.The example that can be used for modified aromatic dicarboxylic acid of the present invention comprises but is not to be defined in, m-phthalic acid, 4,4 '-diphenyl dicarboxylic acid, 1,4-, 1,5-, 2,6-, 2,7-naphthalene dicarboxylic acids and trans-4,4 '-the Stilbene dicarboxylic acid, and ester.In a kind of embodiment, this modified aromatic dicarboxylic acid is a m-phthalic acid.
The carboxyl acid component that is applicable to polyester of the present invention can further be used up to 10mol%, as having the aliphatic dicarboxylic acid modification of 2～16 carbon atoms up to 5mol% or up to one or more of 1mol%, for example, toxilic acid, succsinic acid, pentanedioic acid, hexanodioic acid, pimelic acid, suberic acid, nonane diacid and dodecanedicarboxylic acid.Some embodiments can comprise 0.01 or above mol%, as 0.1 or above mol%, 1 or above mol%, 5 or above mol% or 10 or one or more modified aliphatic dicarboxylic acid of above mol%.Still another embodiment contains the modified aliphatic dicarboxylic acid of 0mol%.Thus,, expect that the amount ranges of one or more modified aliphatic dicarboxylic acid can be any aforementioned endpoint value if when existing, for example, 0.01～10mol% and 0.1～1mol%.Total mol% of dicarboxylic acid component is 100mol%.
Can use the ester of terephthalic acid and other modification dicarboxylic acid or their corresponding esters and/or salt to replace and think.The suitable example of dicarboxylic ester comprises but is not to be defined in, dimethyl, diethyl, dipropyl, di-isopropyl, dibutyl and diphenyl.In a kind of embodiment, this ester is selected from following at least a: methyl, ethyl, propyl group, sec.-propyl and phenylester.
1,4 cyclohexane dimethanol can be cis, trans or its mixture, is 60: 40～40: 60 as cis/trans ratios.In another embodiment, anti-form-1, the amount of 4-cyclohexanedimethanol can be 60～80mol%.
The diol component that is applicable to the polyester portion of polymer blend of the present invention can contain 25mol% or still less one or more are not 2,2,4,4-tetramethyl--1, the modification glycol of 3-cyclobutanediol or 1,4 cyclohexane dimethanol; In a kind of embodiment, be applicable to that polyester of the present invention can contain one or more modification glycol less than 15mol%.In another embodiment, be applicable to that polyester of the present invention can contain 10mol% or one or more modification glycol still less.In another embodiment, be applicable to that polyester of the present invention can contain 5mol% or one or more modification glycol still less.In another embodiment, be applicable to that polyester of the present invention can contain 3mol% or one or more modification glycol still less.In another embodiment, be applicable to that polyester of the present invention can contain one or more modification glycol of 0mol%.Some embodiments also can contain 0.01 or above mol%, as 0.1 or above mol%, 1 or above mol%, 5 or above mol% or 10 or one or more modification glycol of above mol%.Thus,, expect that the amount ranges of one or more modification glycol can be any aforementioned endpoint value if when existing, for example, 0.01～15mol% and 0.1～10mol%.
Be applicable to that modification glycol of the present invention represents 2,2,4,4-tetramethyl--1, the glycol outside 3-cyclobutanediol and the 1,4 cyclohexane dimethanol, and it can contain 2～16 carbon atoms.The example of suitable this row glycol comprises but is not to be defined in, ethylene glycol, 1,2-propylene glycol, 1, ammediol, neopentyl glycol, 1,4-butyleneglycol, 1,5-pentanediol, polyoxyethylene glycol, Diethylene Glycol, polytetramethylene glycol, 1,6-hexylene glycol, p-Xylol glycol or its mixture.Other modification glycol comprises but is not to be defined in, 1, and ammediol and 1,4-butyleneglycol.In another embodiment, get rid of ethylene glycol as the modification glycol.In another embodiment, get rid of 1, ammediol and 1, the 4-butyleneglycol is as ethylene glycol.In another embodiment, get rid of 2 as the modification glycol.
Be applicable to the polyester of polymer blend of the present invention and/or the residue that polycarbonate can comprise one or more branched monomers of about 0～about 10mol%, be also referred to as branching agent herein, have 3 or a plurality of carboxyl substituent, hydroxyl substituent or its combination.Other example of the molar percentage scope of the branching agent that can exist in polyester of the present invention or the polycarbonate is about 0.05～about 5mol%, about 0.01～about 1mol%, about 0.01～about 0.7mol%, about 0.01～about 0.5mol% and about 0.1～about 0.7mol%, respectively based on the glycol of polyester and/or polycarbonate or the total mole number of diacid residues.In some embodiments, can between the polymerization period of polyester, add branched monomer or reagent.Polyester of the present invention thus can be linearity or branching.Polycarbonate also can be linearity or branching.In some embodiments, can before the polymerization of polycarbonate and/or during and/or add branched monomer or reagent afterwards.
The example of branched monomer comprises but is not to be defined in, polyfunctional acid or multifunctional pure as trihemellitic acid, trihemellitic acid acid anhydride, pyromellitic acid dianhydride, TriMethylolPropane(TMP), glycerine, tetramethylolmethane, citric acid, tartrate, 3-hydroxyl pentanedioic acid, glycerine, Sorbitol Powder, 1,2,6-hexanetriol, trimethylolethane and/or trimesic acid etc.In a kind of embodiment, the branched monomer residue can comprise 0.01～1mol% one or more be selected from following at least a residue: trihemellitic acid acid anhydride, pyromellitic acid dianhydride, glycerine, Sorbitol Powder, 1,2,6-hexanetriol, trimethylolethane, tetramethylolmethane, trimethylolethane and/or trimesic acid.Branched monomer can be added in the pet reaction mixture, perhaps with enriched material form and polyester blend, for example, as US5,654,347 and 5,696, described in 176 like that.
Owing to be applicable to that polyester more of the present invention 170 ℃ of long crystallization half-lives (for example, greater than 5 minutes) that show down, can prepare container injection blow goods, injection drawing blow goods, extrusion-blown modling system film and extrude the stretch-blow goods.Polyester of the present invention can be " unbodied " or hemicrystalline.On the one hand, be applicable to that polyester more of the present invention can have than low-crystallinity.Be applicable to that polyester more of the present invention can have amorphous form in fact thus, mean that this polyester comprises unordered in fact polymer areas.
In a kind of embodiment, the crystallization half-life of " amorphous " polyester can be greater than 5 minutes under 170 ℃, perhaps under 170 ℃ greater than 10 minutes, perhaps under 170 ℃ greater than 100 minutes.In one embodiment of the present invention, this crystallization half-life under 170 ℃ greater than 1000 minutes.In another embodiment of the present invention, the crystallization half-life that is applicable to polyester of the present invention under 170 ℃ greater than 10000 minutes.The crystallization half-life of polyester used herein, can adopt the well-known method of those skilled in the art to measure.For example, the crystallization half-life of polyester, t 1/2, can determine over time by the transmittance that laser and photo-detector are measured sample on the temperature controlled hot platform.This measurement can be by being exposed to temperature with polymkeric substance, Tmax, and subsequently it is cooled to desired temperatures and carries out.Can sample be remained under the desired temperatures by hot platform subsequently, measure transmissivity simultaneously over time.At first, sample can be visually transparent, has high transmission rate, and becomes opaque along with the sample crystallization.Be that transmittance is the time of a half between initial transmittance and the final transmittance crystallization half-life.Tmax is defined as the required temperature of fusing sample crystal region (if having crystal region).Can before measuring crystallization half-life, sample be heated to Tmax to regulate this sample.Absolute Tmax temperature is different for each composition.For example, PCT can be heated to above some temperature of 290 ℃ with the fusion-crystallization zone.
Polymkeric substance of the present invention can crystallization, hypocrystalline or amorphous polymer.Term used herein " hypocrystalline " implication is that this polymkeric substance contains two phases: orderly crystallization phases and unordered amorphous phase.Polymkeric substance with hypocrystalline form shows crystalline melt temperature (Tm) and second-order transition temperature (Tg) simultaneously, and can be different from " amorphous " polymkeric substance that only shows second-order transition temperature.
Polyester of the present invention adopts typical polycondensation condition to prepare easily by suitable dicarboxylic acid, ester, acid anhydrides or salt and suitable glycol or diol mixture.As previously mentioned, the dicarboxylic acid component of polyester of the present invention can be derived from dicarboxylic acid, their corresponding esters or its mixture.The example that is applicable to the ester of dicarboxylic acid of the present invention comprises dimethyl, dipropyl, di-isopropyl, dibutyl and diphenyl etc.In a kind of embodiment, for example, terephthalic acid can be used as raw material.In another embodiment, dimethyl terephthalate (DMT) can be used as raw material.Still in another embodiment, the mixture of terephthalic acid and dimethyl terephthalate (DMT) can be used as raw material and/or intermediate materials.
Polyester of the present invention prepares by operation well known by persons skilled in the art.They can prepare by the operation of continuous, semicontinuous and intermittent mode, and can utilize multiple type of reactor.The example of suitable type of reactor comprises but is not to be defined in, steel basin, continuously stirring groove, slurry, tubular type, wiping film, falling liquid film or extrusion reaction device.The reaction of two pure and mild dicarboxylic acid can utilize traditional polyester condition or be undertaken by fusion phase technology, but have enough degree of crystallinity those can by fusion mutually and subsequently solid phase polycondensation process prepare.For example, when the mode by transesterification reaction prepares polyester, that is, by dicarboxylic acid component's ester-formin, this reaction process can comprise two steps.The first step, with diol component and dicarboxylic acid component for example dimethyl terephthalate (DMT) at high temperature, typically, about 150 ℃～about 150 ℃, reacted about 0.5～about 8 hours, pressure range is about 0.0kPa gauge pressure～about 414kPa gauge pressure (60 pounds per square inch, " psig ").Preferably, the temperature range of transesterification reaction is about 180 ℃～about 230 ℃, carries out about 1～about 4 hours, and the preferred pressure scope is about 103kPa gauge pressure (15psig)～about 276kPa (40psig) simultaneously.Thus, with reaction product reaction under high temperature and decompression, form polyester thus and eliminate glycol, it volatilizees under these conditions easily and removes from this system.Second step, perhaps condensation polymerization step, high vacuum more and usually scope be about 230 ℃～about 350 ℃, be preferably about 250 ℃～about 310 ℃, most preferably be under the about 260 ℃～about 290 ℃ temperature and proceeded about 0.1～about 6 hours or preferred about 0.2～about 2 hours, up to the polymkeric substance that acquisition has the polymerization degree of expectation, measure by logarithmic viscosity number.Condensation polymerization step can under reduced pressure be carried out, and scope is about 53kPa (400 torr)～about 0.013kPa (0.1 torr).Can adopt stirring well-known in the art or suitable hybrid technology in two stages, guarantee the abundant heat transfer and the Surface Renewal of reaction mixture thus.Suitably catalyzer can increase the speed of reaction in two stages, for example, and the salt of alkoxy titanium compound, alkali metal hydroxide and alkoxide, organic carboxyl acid, Alkyzin compound, metal oxide etc.Also can adopt and be similar to US5, the three tier structure described in 290,631 is equipped with operation, particularly when adopting the mix monomer charging of acid and ester.
Reach by transesterification reaction in order to ensure diol component and dicarboxylic acid component's reaction and to finish, expectation sometimes adopts about 1.05～about 2.5mol diol component to the 1mol dicarboxylic acid component.But, it will be appreciated by those skilled in the art that diol component and dicarboxylic acid component's ratio is decided by the DESIGN OF REACTOR of the process that wherein reacts usually.
When preparing polyester by direct esterification, that is, the sour form preparation by the dicarboxylic acid component prepares polyester with the mixture of dicarboxylic acid or dicarboxylic acid and the mixture reaction of diol component or diol component.This is reflected at about 7kPa gauge pressure (1psig)～about 1379kPa gauge pressure (200psig), preferably is about low-molecular-weight polyester product of 1.4～about 10 less than carrying out under the pressure of 689kPa (100psig), making mean polymerisation degree thus.The temperature that adopts between the direct esterification reaction period typically is about 180 ℃～about 280 ℃, more preferably about 220 ℃～about 270 ℃.Subsequently can be by polycondensation with this low-molecular weight polymer polymerization.
Thermoplastic polymer of the present invention also can comprise polyarylester.Polyarylester is that the polymkeric substance by dihydric phenol and dicarboxylic acid obtains.The case description of polyarylester that can be used for composition of the present invention, method and moulded products is in US4, in 598,130,5,034,502 and 4,374,239.The example that can be used for preparing the dihydric phenol of polyarylester is a bisphenols, as two (4-hydroxy phenyl) methane, 2, and two (4-hydroxy phenyl) propane (" bisphenol-A ") of 2-; 2, two (the 4-hydroxy-3-methyl phenyl) propane, 4 of 2-, two (4-hydroxy phenyl) heptane, 2 of 4-, two (4-hydroxyl-3, the 5-dichlorophenyl) propane of 2-; 2, two (4-hydroxyl-3, the 5-dibromo phenyl) propane of 2-; The dihydroxyl phenolic ether, for example two (4-hydroxy phenyl) ethers, two (3,5-two chloro-4-hydroxy phenyls) ether; Dihydroxybiphenyl, p for example, p '-dihydroxybiphenyl, 3,3 '-two chloro-4,4 ' dihydroxybiphenyl; The dihydroxyl aryl sulfone, for example, two (4-hydroxy phenyl) sulfone, two (3,5-dimethyl-4-hydroxy phenyl) sulfone; Dihydroxy-benzene, for example, Resorcinol, quinhydrones; The dihydroxy-benzene that halo and alkyl replace, for example, 1,4-dihydroxyl-2,5-dichlorobenzene, 1,4-dihydroxyl-3-methylbenzene; With the dihydroxybiphenyl sulfoxide, for example, two (4-hydroxy phenyl) sulfoxide, two (3,5-two bromo-4-hydroxy phenyls) sulfoxide.Also can obtain various other dihydric phenol, for example, US2, in 999,83,3,028,365 and 3,153,008 disclosed those.Also be suitable for be by above-mentioned dihydric phenol and halogen-containing dihydric phenol as 2, two (3, the 5-two chloro-4-hydroxy phenyls) propane and 2 of 2-, the 2-pair of multipolymer that (3,5-two bromo-4-hydroxy phenyls) propane copolymerization make.Also can adopt two or more different dihydric phenol, perhaps dihydric phenol and glycol, with the polyester of hydroxyl or acid blocked, with two acid basis and the multipolymer of the blend of above-mentioned materials arbitrarily.Suitable dicarboxylic acid comprises but is not to be defined in, phthalic acid, m-phthalic acid, terephthalic acid, and the o-phthalic acid, o-, m-and p-phenylene oxalic acid and polynuclear aromatic acid, for example, diphenic acid and 1,4-naphthalic acid.
Other example that can be used for polyarylester of the present invention comprises by those of the polymkeric substance acquisition of dihydroxyphenyl propane (2, two (4-hydroxy phenyl) propane of 2-) and 50: 50/terephthaldehyde acid mixture.Some polymkeric substance can trade mark " U-Polymer U-100 " commercially available (can obtain from Unitika AmericaCorporation).Other example is based on tetramethyl-dihydroxyphenyl propane, 4, the polyarylester of 4 '-dihydroxy benaophenonel and 5-tertiary butyl m-phthaloyl chloride.
Polyarylester of the present invention can form reaction by any polyester well known in the art and prepare, for example, by the solution of aromatic dicarboxylic acid dihalide in organic solvent is under agitation mixed with the alkaline aqueous solution of bis-phenol so that the interfacial polymerization of these materials reaction; By the solution polymerization that aromatic dicarboxylic acid dihalide and bis-phenol are reacted in organic solvent at de-acidying agent such as pyridine; By melt polymerization with aromatic dicarboxylic acid diphenyl and bis-phenol reaction; By melt polymerization with aromatic dicarboxylic acid, diphenyl carbonate and bis-phenol reaction; By melt polymerization with aromatic dicarboxylic acid and bisphenol diacetate reaction; With the polymerization of passing through aromatic dicarboxylic acid and bisphenol diacetate reaction.The example for preparing the method for polyarylester is disclosed in US5, in 034,502,4,321,355 and 4,374,239.Polyarylester of the present invention typically logarithmic viscosity number is about 0.5～about 1.1dL/g.
In addition, polyester, polycarbonate and polyarylester may further include following one or more: oxidation inhibitor, melt strength toughener, branching agent (for example, glycerine, trihemellitic acid and acid anhydrides), chainextender, fire retardant, filler, acid scavenger, dyestuff, tinting material, pigment, release agent, flow enhancing agent, impact modifier, static inhibitor, processing aid, demoulding additive, softening agent, slip, stablizer, wax, UV absorption agent, white dyes, lubricant, pin are connected additive, whipping agent, static inhibitor, nucleator etc.Tinting material (being called toning agent sometimes) be can add and the neutralc tint and/or the brightness of polyester expectation given.Preferably, this polymer blend can comprise one or more processing aids of 0～about 30wt%, changes the surface property of composition thus and/or increase to flow.The representative example of processing aid comprises lime carbonate, talcum, viscosity, mica, zeolite, wollastonite, kaolin, diatomite, TiO2, NH4Cl, silica, calcium oxide, sodium sulfate and calcium phosphate.Can use various pigment or fuel, for example, make the goods of showing signs of anger.Also static inhibitor or other coating can be administered on the surface of goods.
Second component of the present composition (ii) comprises the intimate blending thing of the acid amides exchange of at least two kinds of polymeric amide.Typically, this intimate blending thing comprises 2～about 10 kinds of different polymeric amide.In another example, this intimate blending thing can comprise 2～4 kinds of polymeric amide.According to the present invention, show that the polymeric amide that is lower than about 300 ℃ fusing point can be used as at least a polymeric amide.In another example, can use fusing point to be lower than about 275 ℃ and second-order transition temperature and be higher than about 25 ℃ polymeric amide.Typically, the I.V. of this polymeric amide is about 0.3dL/g～about 2.0dL/g, is preferably 0.5dL/g at least.
For composition of the present invention, valuably, find the acid amides exchange between the polymeric amide of intimate blending thing being used to prepare.Term used herein " acid amides exchange (transamidized) ", be intended to and term " amidation exchange (transmidate) " and " amidation exchange (transamidation) " synonym, and expression is with the process of the exchange of the amide group between two kinds of different polyamides.Thus, term used herein " acid amides exchange blend " is that wherein polyamide component has exchanged and is enough to make this blend to become the blend of amide group of the amount of intimate blending thing.Acid amides exchange between two or more polymeric amide can realize typically about 270 ℃～about 350 ℃ by polymeric amide is at high temperature contacted.Other example of acid amides exchange temperature is about 280 ℃～about 350 ℃ and about 290 ℃～about 340 ℃.Acid amides exchange between the polymeric amide is by existing single glass transition temperature (Tg) to represent for blend, adopt the well-known standard technique of those skilled in the art to measure by dsc (DSC), for example, as described in the ASTM method D3418.Can be with polymeric amide directly under these temperature or heating together in the presence of the thermoplastic polymer of first component (i).For example, the contact of polymeric amide and, thus, acid amides exchange can be by first and second components of melt blending during extruding, perhaps other pyroprocessing of polymer composition and its component and taking place.In another example, can with polymeric amide in independent container together the heating and subsequently with the first component melts blend.
First and second polymeric amide of this second component can be selected from the polymeric amide of wide region.For the specific refractory power of better coupling first component, desirably, but also optionally, at least a polymeric amide comprises aromatic moieties.In a kind of example, this polymeric amide can comprise partly that number-average molecular weight is 7000 or lower aromatic poly and fatty polyamide.The combination of this polymeric amide is also included within the scope of the present invention.The partially aromatic polymeric amide comprises that the acid amides between at least one aromatic ring and at least one the non-aromatics part connects.Though whole aromatic poly are liquid crystal normally, the blend that fusing point is lower than 300 ℃ this resin can be used for the present invention.When using the intimate blending thing of polymeric amide, the specific refractory power of cutting out this polyamide blend is allowed in quick acid amides exchange between aliphatics nylon and aromatics or the partially aromatic polymeric amide (acid amides-acid amides exchange), by regulating the ratio of fatty polyamide and aromatics, partially aromatic polymeric amide.The thermoplastic polymer that this technology can make the homogeneous polyamide blend and the first component for example specific refractory power of one or more polyester is complementary.The reference of acid amides exchange can wait Polymer at Y.Takeda, and 1992vol.33 finds in the 3394th page.
According to the present invention, second component can be the intimate blending thing of the acid amides exchange of 2 kinds or multiple polymeric amide, for example, select first polymeric amide and second polymeric amide to realize specific refractory power in second component, make difference RI (second the component)-RI (first component) of specific refractory power of second and first component be about 0.006～approximately-0.0006.In order to mate the specific refractory power of first component, valuably, first and second polymeric amide have the aromatics and the aliphatic residue of different amounts.For example, second component (ii) can comprise the intimate blending thing of second polymeric amide of first polymeric amide that contains aromatic moieties and fatty family residue.About the diamines and the employed term of dicarboxylic acid monomer " aliphatics " of polymeric amide of the present invention, implication is that this monomeric carboxyl or amino are not to be examined by virtue to connect herein.For example, do not contain virtue nuclear in its main chain of hexanodioic acid, that is, connect the chain of carboxylic acid group's carbon atom; Thus, it is " aliphatic ".On the contrary, term " aromatics " implication is, contains virtue nuclear in dicarboxylic acid or the diamines main chain, for example, and terephthalic acid or 1,4-m-xylene diamine.The representative example of aromatic poly for comprise 70mol% at least contain diamines (as m-xylenedimaine or comprise m-xylenedimaine and up to the dimethylphenylene diamine mixture of 30% pair-dimethylphenylene diamine) and have those polymeric amide of residue of the aliphatic dicarboxylic acid of 6～10 carbon atoms.Thus, term " aliphatic " is intended to comprise simultaneously aliphatics and cycloaliphatic structure, for example, diamines, diacid, lactan, amino alcohol and aminocarboxylic acid, it contains as the straight chain of the composition nitrogen-atoms of main chain or straight chain or circular permutation, it can be saturated or (that is, containing carbon carbon triple bond) alkane, undersaturated (that is the carbon-carbon double bond that, contains non-aromatics) or acetylene series in essence.Thus, in the content of specification sheets of the present invention and claim, aliphatics is intended to comprise linear and branched chain structure (being called " aliphatic " herein), and ring structure (being called " alicyclic " or " cycloaliphatic " herein).But term " aliphatics " does not also lie in eliminating and can be connected to any aromatic substituent on the main chain of aliphatics or cycloaliphatic glycol or diacid or hydroxycarboxylic acid.
The weight percent of first and second polymeric amide that exist in the intimate blending thing of this acid amides exchange typically can be for about 1: 50～about 50: 1, based on the gross weight of second component.Other example of weight percent is 1: 20～about 20: 1 and about 1: 10～about 10: 1.
The example that can be used for the polymeric amide of intimate blending thing of the present invention comprises and contains the polymeric amide that one or more are selected from following residue: phthalic acid, terephthalic acid, cyclohexane dicarboxylic acid, m-xylenedimaine (being also referred to as " m-dimethylphenylene diamine " herein), right-dimethylphenylene diamine (being also referred to as " p-dimethylphenylene diamine " herein), 1,3-hexanaphthene (two) methylamine, 1,4-hexanaphthene (two) methylamine, aliphatic diacid with 6～12 carbon atoms, aliphatic amino acid or lactan with 6～12 carbon atoms, aliphatie diamine with 4～12 carbon atoms.Can use other logical diacid and diamines that produces known formation polymeric amide.This polymeric amide also can contain small amount of trifunctional or four sense comonomers such as trihemellitic acid acid anhydride, pyromellitic acid dianhydride or as known in the art other and form the polyacid and the polyamines of polymeric amide.
The example of partially aromatic polymeric amide comprises but is not to be defined in: poly-(-dimethylbenzene adipamide) (being called " MXD6 " nylon herein), poly-(hexa-methylene adipamide-copolymerization-isophthaloyl amine), poly-(hexa-methylene adipamide-copolymerization-terephthalamide) and poly-(hexa-methylene isophthaloyl amine-copolymerization-terephthalamide).In a kind of embodiment, the partially aromatic polymeric amide is poly-(-dimethylbenzene adipamide).In a kind of embodiment, the number-average molecular weight of this partially aromatic polymeric amide can be 7000 or lower.The representative example of fatty polyamide comprises poly-(2-Pyrrolidone) (nylon 4,6; CAS sequence number 44,299-2); Poly-decyl amide (nylon 6; CAS sequence number 18,111-0); Poly-(2-piperidone) (nylon 5, CAS sequence number 24938-57-6); Poly-(7-aminoheptylic acid) (nylon 7; CAS sequence number 25035-01-2); Poly-(pelargonamide) (nylon 9; CAS sequence number 25748-72-5); Poly-(the amino undecanoic acid of 11-) (Ni Long11; CAS sequence number 25035-04-5); Poly-(12-aminolauric acid) (nylon 12, CAS sequence number 24937-16-4); Poly-(ethylidene adipamide) (nylon 2,6); Polytetramethylene-adipamide (nylon 4,6; CAS sequence number 50327-22-5); Polyhexamethylene-adipamide (nylon 6,6; CAS sequence number 42,917-1), (nylon 6,9; CAS sequence number 18,806-9) poly--(hexa-methylene sebacoyl amine) (nylon 6,10; CAS sequence number 9008-66-6), poly-(hexa-methylene-undecane diamide) (nylon 6,11) poly-(hexa-methylene-dodecane diamide) (nylon 6,12; CAS sequence number 24936-74-1), poly-(eight methylene radical-adipamide (nylon 8,6); Hexanodioic acid-decamethylene diamine multipolymer (nylon 10,6; CAS sequence number 26123-27-3); Poly-decamethylene-dodecane diamide (nylon 10,12); Poly-(ten dimethylenes-adipamide) (nylon 12,6); With poly-(ten dimethylenes-sebacoyl amine) (nylon 12,8).
For example, this second component (ii) can comprise the intimate blending thing that contains first polymeric amide (it comprises the residue of m-xylene diamine and hexanodioic acid) and second polymeric amide (it comprises the residue of at least a diacid of selecting oneself, pimelic acid, suberic acid, nonane diacid, sebacic acid, undecane diacid, dodecanedioic acid, hexanolactam, butyrolactam, the amino undecane diacid of 11-and hexamethylene-diamine).For example, this first polymeric amide can comprise MXD6 nylon, and it can be commercially available from MitsubishiCorporation.In another example, this second polymeric amide can comprise at least a polymeric amide that is selected from nylon 4, nylon 6, nylon 9, Ni Long11, nylon 12, nylon 6,6, nylon 5,10, nylon 6,12, nylon 6,11, nylon 10,12 and combination thereof.Still in another example, this second polymeric amide can comprise nylon 6, nylon 6,6 or its blend.
This second component also can comprise single copolyamide, and the composition of wherein selecting monomer residue is with the specific refractory power close-fitting specific refractory power of acquisition with first component.Thus, in another embodiment, the invention provides a kind of polymer composition, it comprises following unmixing blend:
(i) first component comprises at least a thermoplastic polymer that is selected from polyester, polycarbonate, polyarylester and intimate blending thing thereof; With
(ii) second component comprises copolyamide;
Wherein, this second component is about 0.006～approximately-0.0006 with difference RI (second the component)-RI (first component) of the specific refractory power of this first component (i) (ii), and the percent transmittancy of this unmixing blend is at least 75%, and mist degree is 10% or lower.In another embodiment, this first component comprises and contains terephthalate, 2,2,4,4-tetramethyl--1, the polyester of the residue of 3-cyclobutanediol and 1,4 cyclohexane dimethanol.Thus, another embodiment of the present invention is a kind of polymer composition, and it comprises following unmixing blend:
(i) first component comprises at least a polyester, and it comprises:
(a) diacid residues comprises based on the total diacid residue being the residue of the terephthalic acid of about 70～about 100mol%; At least a residue that has up to the modified aromatic dicarboxylic acid of 20 carbon atoms of 0～about 30mol%; At least a residue that has up to the modified aliphatic dicarboxylic acid of 16 carbon atoms with 0～about 10mol%; With
(b) diol residue comprises that based on the total diol residue be 2,2,4 of about 1～about 99mol%, 4-tetramethyl--1, the residue of 3-cyclobutanediol; Residue with the 1,4 cyclohexane dimethanol of about 1～about 99mol%; With
(ii) second component comprises blend homogeneous, the acid amides exchange of at least two kinds of polymeric amide;
Wherein, this second component is about 0.006～approximately-0.0006 with difference RI (second the component)-RI (first component) of the specific refractory power of this first component (i) (ii), and the percent transmittancy of this unmixing blend is at least 75%, and mist degree is 10% or lower.For example, this copolyamide can comprise the residue of m-xylene diamine, p-Xylol diamines or its combination; With at least a terephthalic acid, m-phthalic acid, hexanodioic acid, pimelic acid, suberic acid, nonane diacid, sebacic acid, undecane diacid, dodecanedioic acid, hexanolactam, butyrolactam, the amino undecane diacid and 1 of 11-, the residues of monomers of 6-hexamethylene-diamine of being selected from.In another example, this copolyamide can comprise the residue of the m-xylene diamine of about 15～about 100mol%, total diamines residue based on 100mol%, with the residue of the hexanodioic acid of about 15～about 85mol% and one or more pimelic acid that are selected from, suberic acid, nonane diacid, sebacic acid, undecane diacid, the dodecanedioic acid and 1 of about 85～15mol%, the residue of the aliphatics of 4-cyclohexane dicarboxylic acid or cycloaliphatic dicarboxylic acid is based on the total diacid residue of 100mol%.Will be appreciated that can be with any embodiment combination of various embodiments with the polyester of above being discussed of the intimate blending thing of the polymeric amide of indication herein and copolyamide.
Other example that can be used for the copolyamide of composition of the present invention, individually or as with the part of the intimate blending thing of another example, comprise but be not to be defined in, comprise the copolyamide of the residue of the residue (based on total diamines residue content of 100mol%) of the m-xylene diamine of about 1 5～about 100mol% and hexanodioic acid.May reside in the typical amounts of the hexanodioic acid residue in these copolyamides, based on the total mole number of diacid residues, be about 5～about 85mol%, about 20～about 80mol% and about 25～about 75mol%.Remaining dicarboxylic acid residue can comprise the residue of one or more aliphatic dicarboxylic acids with 7～12 carbon atoms, as pimelic acid, suberic acid, nonane diacid, sebacic acid, undecane diacid, dodecanedioic acid or 1,4-cyclohexane dicarboxylic acid.In another example, this polyamic acid also can comprise the residue in m-phthalic acid and the terephthalic acid.
Except that the m-xylene diamine residue, copolyamide of the present invention can also comprise other diamines or lactan residue.For example, this copolyamide can comprise 15mol% at least or at least about the residue of the m-xylene diamine of 20mol%, the diamines residue of remainder comprises the residue of one or more aliphatics or aromatic diamine.For example, this copolyamide can comprise 1 of about 80mol% or about 85mol%, and the residue of 6-hexamethylene-diamine is based on the total mole number of diamines residue.Also can use the p-Xylol diamines, 1 of different amounts, 3-hexanaphthene two (methylamine) or 1,4-hexanaphthene two (methylamine).Similarly, this copolyamide can comprise lactan such as hexanolactam, and perhaps based on the residue of the lactan of gamma-amino-butyric acid or 11-amino-undecanoic acid, consumption is about 10mol%～about 90mol%, perhaps about 10mol～about 70mol% is based on the total mole number of repeating unit.In another embodiment, copolyamide of the present invention can comprise the residue of the m-xylene diamine of about 15mol%～about 85mol%, about 20～about 80mol% or about 25～about 75mol%, total mole number based on the diamines residue, the diamines residue content of remainder comprises the residue of one or more diamines, as aliphatie diamine, particularly 1, the 6-methylene diamine.In this embodiment, this diamines residue may further include the residue of a small amount of other diamines, for example p-Xylol diamines, perhaps cycloaliphatic diamine, for example following one or more: 1,3-hexanaphthene two (methylamine) or 1,4-hexanaphthene two (methylamine).In addition, this polymeric amide can randomly comprise, replace a part of hexanodioic acid, one or more have the aliphatics of 7～12 carbon atoms or the residue of aromatic dicarboxylic acid, as pimelic acid, suberic acid, nonane diacid, sebacic acid, undecane diacid, dodecanedioic acid, 1,4-cyclohexane dicarboxylic acid or m-phthalic acid, its amount can randomly have a small amount of terephthalic acid for about 15mol%～about 85mol%.This polymeric amide also can comprise lactan such as hexanolactam, perhaps based on the residue of the lactan of gamma-amino-butyric acid or 11-amino-undecanoic acid, consumption is about 10mol%～about 90mol%, and perhaps about 10mol～about 70mol% is based on the total mole number of repeating unit.
Still in another embodiment, foundation copolyamide of the present invention comprises the residue of the hexanodioic acid of about 15mol%～about 90mol%, and the residue diacid residues comprises the residue of the m-phthalic acid of about 10～about 85mol%, based on the total mole number of dicarboxylic acid residue.Other example of hexanodioic acid and isophthalic acid residues content comprises about 20～80mol% and about 25～about 75mol%.In this embodiment, this polymeric amide can comprise randomly that a small amount of one or more have the residue of the aliphatic dicarboxylic acid of 7～12 carbon atoms, for example pimelic acid, suberic acid, nonane diacid, sebacic acid, undecane diacid, dodecanedioic acid or 1, the 4-cyclohexane dicarboxylic acid randomly has a small amount of terephthalic acid.Randomly, this polymeric amide can comprise m-xylene diamine.Randomly, this polymeric amide can comprise the m-xylene diamine residue.The example of m-xylene residue concentration comprises about 15～about 90mol%, about 20～about 85mol%, or about 25～about 80mol%.The residue residue can comprise one or more aliphatie diamines, for example, 1, the 6-hexamethylene-diamine, one or more aromatic diamines, for example, the p-Xylol diamines.Similarly, this copolyamide also can comprise lactan such as hexanolactam, and perhaps based on the residue of the lactan of gamma-amino-butyric acid or 11-amino-undecanoic acid, consumption is about 10mol%～about 90mol%, perhaps about 10mol～about 70mol% is based on the total mole number of repeating unit.
Still among another embodiment, copolyamide of the present invention can comprise the residue of one or more lactan, hexanolactam for example, perhaps based on the lactan of gamma-amino-butyric acid or 11-amino-undecanoic acid, consumption is about 10mol%～about 90mol%, perhaps about 10mol～about 70mol%, perhaps about 15mol%～about 60mol% is based on the total mole number of repeating unit.Residue with one or more aliphatic dicarboxylic acids of 7～12 carbon atoms, as pimelic acid, suberic acid, nonane diacid, sebacic acid, undecane diacid, dodecanedioic acid or 1, the 4-cyclohexane dicarboxylic acid, its amount can be for about 20mol%～about 80mol%, based on the total mole number of repeating unit.For example, this copolyamide can comprise the residue of m-phthalic acid or terephthalic acid.In this embodiment, this copolyamide can comprise the residue of the m-xylene diamine of about 15mol%～about 85mol%, based on the total mole number of diamines residue.Other example of m-xylene diamine content is about 20～about 80mol% and about 25～about 75mol%.Remainder diamines residue can comprise one or more diamines aliphatie diamines for example 1, the residue of 6-hexamethylene-diamine.In this embodiment, this diamines residue may further include the residue of a small amount of other diamines, for example p-Xylol diamines, perhaps cycloaliphatic diamine, for example following one or more: 1,3-hexanaphthene two (methylamine) or 1,4-hexanaphthene two (methylamine).Randomly, can use a small amount of following one or more: p-Xylol diamines, 1,3-hexanaphthene two (methylamine) or 1,4-hexanaphthene two (methylamine).
Another embodiment of the present invention is a kind of polymer composition, and it is made up of following unmixing blend basically:
(i) first component is made up of at least a thermoplastic polymer that is selected from polyester, polycarbonate, polyarylester and intimate blending thing thereof basically; With
(ii) second component is made up of the blend of the homogeneous acid amides exchange of 2 kinds of polymeric amide basically at least;
Wherein, this second component is about 0.006～approximately-0.0006 with difference RI (second the component)-RI (first component) of the specific refractory power of this first component (i) (ii), and the percent transmittancy of this unmixing blend is at least 75%, and mist degree is 10% or lower.In another aspect of the present invention, this first component is basically by containing terephthalate, 2,2,4,4-tetramethyl--1, the polyester composition of the residue of 3-cyclobutanediol and 1,4 cyclohexane dimethanol.Thus, the present invention also provides a kind of polymer composition, and it is made up of following unmixing blend basically:
(i) first component is made up of at least a polyester basically, and it comprises:
(a) diacid residues comprises based on the total diacid residue being the residue of the terephthalic acid of about 70～about 100mol%; At least a residue that has up to the modified aromatic dicarboxylic acid of 20 carbon atoms of 0～about 30mol%; At least a residue that has up to the modified aliphatic dicarboxylic acid of 16 carbon atoms with 0～about 10mol%; With
(b) diol residue, basically by being 2,2,4 of about 1～about 99mol% based on the total diol residue, 4-tetramethyl--1, the residue of the 1,4 cyclohexane dimethanol of the residue of 3-cyclobutanediol and about 1～about 99mol% is formed; With
(ii) second component is made up of blend homogeneous, the acid amides exchange of two kinds of polymeric amide basically at least;
Wherein, this second component is about 0.006～approximately-0.0006 with difference RI (second the component)-RI (first component) of the specific refractory power of this first component (i) (ii), and the percent transmittancy of this unmixing blend is at least 75%, and mist degree is 10% or lower.Phrase used herein " basically by ... form ", be intended to comprise it and be the composition of unmixing blend, promptly, have at least 2 with form relevant Tg (passing through dsc measurement), and its second component that has first component that contains polyester, polycarbonate, polyarylester or its intimate blending thing and contain the blend that the homogeneous acid amides of at least two kinds of polymeric amide exchanges.In this embodiment, think that said composition got rid of the arbitrary element of the fundamental property of the composition that changes this phrase indication in fact.For example, composition can comprise other component of compatibility of % mist degree, % transmittance or the unmixing blend of the specific refractory power that can not change component, unmixing blend.For example, the adding compatilizer that can change composition compatibility and specific refractory power should be got rid of from this embodiment.Similarly, should get rid of second component that comprises the copolyamide that the copolymerization by compositing monomer makes, because think that this copolyamide has the performance of the blend of the homogeneous acid amides exchange that is different from least two kinds of polymeric amide, even the molar percentage of monomer residue equates.
Be used for polymeric amide of the present invention and typically prepared by dicarboxylic acid and diamines, it is with the reaction of equal proportion in fact, the perhaps ring-opening polymerization by lactan, and be introduced in the polyamide polymer corresponding residue as them.Thus, the present invention contains the sour residue (100mol%) and the diamines residue (100mol%) of equal molar ratio example in fact derived from the polymeric amide of dicarboxylic acid and diamines residue, makes the total mole number of repeating unit equal 100mol%.Thus, the molar percentage that provides in the present disclosure can be based on the total mole number of sour residue, the total mole number of diamines residue or the total mole number of repeating unit.For example, containing based on the total acid residue is the polymeric amide or the copolyamide of the terephthalic acid of 30mol%, and implication is the copolyamide that contains the 30mol% terephthalic acid residue in the acid of 100mol% altogether residue.Thus, the terephthalic acid residue of among every 100mol acid residue, containing 30mol.In another example, the copolyamide of the p-Xylol diamines that to contain based on total diamines residue be 30mol%, implication is the copolyamide that contains 30mol% p-Xylol diamines residue in 100mol% diamines residue altogether.Thus, the p-Xylol diamines residue that among every 100mol diol residue, has 30mol.
Any means as known in the art can be used to prepare this polymeric amide.This polymeric amide is prepared by diacid-diamine complexe by melt phase polymerization usually, and this complex compound can original position or made in independent step.In arbitrary method, diacid and diamines are as raw material.Alternatively, can use the ester-formin of diacid, preferred dimethyl ester.If the use ester, reaction must be carried out under lesser temps (being generally 80～120 ℃), is converted into acid amides up to this ester.Subsequently mixture heating up is arrived polymer temperature.In the situation of polycaprolactam, hexanolactam or 6-aminocaprolc acid can be used as raw material, and can be by adding hexanodioic acid/this polymerization process of hexamethylene-diamine salt catalysis, and it obtains nylon 6/66 polymkeric substance.When using diacid-diamine complexe, with mixture heating up to fusion and stirring up to reaching balance.
By diacid-diamines ratio control molecular weight.Excessive diamines produces the terminal amino group of higher concentration.For the deoxidation composition, regulate diacid-diamines ratio valuably to produce 20mmol/kg or lower terminal amino group concentration.If prepare diacid-diamine complexe, before polymerization, add excessive diamines in independent step.This polymerization can be carried out under normal atmosphere or high pressure.
In order to show gratifying transparency and low haze, the difference of second component of this unmixing blend and the specific refractory power of first component typically is about 0.006～pact-0.0006, and promptly RI (second component)-RI (first component) is about 0.006～approximately-0.0006.Other example of the difference of specific refractory power absolute value is about 0.005～approximately-0.0006, about 0.004～approximately-0.0006, about 0.003～approximately-0.0006, about 0.005～approximately-0.0005 and about 0.004～approximately-0.0005.But, it will be understood by those skilled in the art that the difference of acceptable specific refractory power depends on blend composition, particle diameter, specific refractory power, wavelength and grain pattern, as Biangardi etc., Die Angew.Makromole.Chemie, 183,221 (1990) is described such.
Unmixing blend of the present invention has the % transmittance (measuring by ASTM method D1003) and 10% or littler mist degree of excellent transparency and at least 75%.According to this method, by % transmittance numerical evaluation % haze value.Other example of % transmittance is at least 77%, at least 80% and at least 85%.Other example of the haze value that blend of the present invention can show be 9% or littler, 7% or littler, 5% or littler and 3% or littler.For composition of the present invention, with the said composition molding or be cast into 1/8 inch of thickness or littler sheet material or film and measure its mist degree, determine this mist degree thus according to the operation of describing among the embodiment.For moulded products, comprise multilayer formed article, can (promptly 1 * 1cm), thickness be 1/8 inch or littler, and measures mist degree according to described operation herein, determines this mist degree thus by cut out small portion from these goods.
This first component also can comprise the intimate blending thing of one or more polymkeric substance.For example, this first component can comprise that first polyester and one or more are selected from the intimate blending thing of the polymkeric substance of polycarbonate, second polyester and polyarylester.This polyester can be described herein any polyester.For example, this first component can comprise the intimate blending thing of the polyester and the polycarbonate of the residue that contains dihydroxyphenyl propane.
This polycarbonate can comprise that the total mole number based on diol residue is one or more modified aliphatic glycol with 2～16 carbon atoms of residue and 0～about 10mol% of dihydroxyphenyl propane of about 90～100mol% or the residue of dihydric phenol.Representative example comprises two (4-hydroxy phenyl) methane, 2, two (4-hydroxy phenyl) propane (" bisphenol-A ") of 2-; 2, two (the 4-hydroxy-3-methyl phenyl) propane, 4 of 2-, two (4-hydroxy phenyl) heptane, 2 of 4-, two (4-hydroxyl-3, the 5-dichlorophenyl) propane of 2-; 2, two (4-hydroxyl-3, the 5-dibromo phenyl) propane of 2-; The dihydroxyl phenolic ether, for example two (4-hydroxy phenyl) ethers, two (3,5-two chloro-4-hydroxy phenyls) ether; Dihydroxybiphenyl, p for example, p '-dihydroxybiphenyl, 3,3 '-two chloro-4,4 ' dihydroxybiphenyl; The dihydroxyl aryl sulfone, for example, two (4-hydroxy phenyl) sulfone, two (3,5-dimethyl-4-hydroxy phenyl) sulfone; Dihydroxy-benzene, for example, Resorcinol, quinhydrones; The dihydroxy-benzene that halo and alkyl replace, for example, 1,4-dihydroxyl-2,5-dichlorobenzene, 1,4-dihydroxyl-3-methylbenzene; With the dihydroxybiphenyl sulfoxide, for example, two (4-hydroxy phenyl) sulfoxide, two (3,5-two bromo-4-hydroxy phenyls) sulfoxide.Also can obtain various other dihydric phenol, for example, US2, in 999,835,3,028,365 and 3,153,008 disclosed those.Also be suitable for be by above-mentioned dihydric phenol and halogen-containing dihydric phenol as 2, two (3, the 5-two chloro-4-hydroxy phenyls) propane and 2 of 2-, the 2-pair of multipolymer that (3,5-two bromo-4-hydroxy phenyls) propane copolymerization make.Also can adopt two or more different dihydric phenol, perhaps dihydric phenol and glycol, with the polyester of hydroxyl or acid blocked, with two acid basis and the multipolymer of the blend of above-mentioned materials arbitrarily.Suitable dicarboxylic acid comprises but is not to be defined in, phthalic acid, m-phthalic acid, terephthalic acid, and the o-phthalic acid, o-, m-and p-phenylene oxalic acid and polynuclear aromatic acid, for example, diphenic acid and 1,4-naphthalic acid.
The representative example of aliphatic diol comprises the dihydroxyl alkyl oxide of ethylene glycol, propylene glycol, butyleneglycol, pentanediol, hexylene glycol, heptanediol, ethohexadiol, neopentyl glycol, arylalkyl glycol such as vinylbenzene glycol, Xylene glycol, dihydric phenol such as the dihydroxy ethyl ether of dihydroxyphenyl propane etc.Other example of aliphatic diol is high-molecular weight aliphatics dihydroxy compound more, for example, and polyoxyethylene glycol, polystyrene glycol, polypropylene glycol, polytetramethylene glycol, poly-sulfo-glycol, poly-aryl alkyl ethers two pure and mild multipolymer polyether glycols.Other representative example of dihydric phenol and aliphatic diol is described in US3, in 030,335 and 3,317,466.This polycarbonate may further include the residue of one or more branching agents, for example, and four phenolic compound, three-(4-hydroxy phenyl) ethane, pentaerythritol triacrylate and other compound, as US6,160,082,6,022,941,5,262,511,4,474, in 999 and 4,286,083 disclosed those.Enumerate other suitable branching agent below herein.In another example, this polycarbonate comprises based on the total mole number of diol residue and is the residue of the dihydroxyphenyl propane of 95mol% at least.
Logarithmic viscosity number according to the polycarbonate of blend of the present invention part is preferably at least about 0.3dL/g, more preferably 0.5dL/g at least.Melt flow according to the polycarbonate of blend of the present invention part is preferably 1～20 and more preferably 2～18, according to ASTM method D1238 under 300 ℃ temperature and adopt the weight of 1.2kg to measure.
The method for preparing polycarbonate is well known in the art.Can be used for restriction or constraint that linearity of the present invention and disclosed herein or branching polycarbonate are not subjected to polycarbonate type or its production method.Usually,, use optional monofunctional compound, and trifunctional or higher functional compound are as branching or linking agent as chain terminator with dihydric phenol such as dihydroxyphenyl propane and phosgene reaction.The reactive carboxylic acid halides of simple function, difunctionality and trifunctional also can be used as in the preparation of polycarbonate and stop compound (simple function), comonomer (difunctionality) or branching agent (trifunctional or higher).
For example, the polycarbonate of this blend part can prepare in melt, in solution or by interfacial polymerization technology well known in the art.Proper method comprises step: carbonic ether raw material and glycol are reacted the time that is enough to form polycarbonate under the pressure at 0.1～760mmHg under about 0 ℃～315 ℃ temperature.The polycarbonate that can be used for commercially available acquisition of the present invention, usually by with aromatic diol and carbonic ether raw material for example phosgene, dibutyl carbonate or diphenyl carbonate reaction prepare, thus with the carbonate unit of 100mol%, be incorporated in the polycarbonate with the diol units of 100mol%.Other representative example for preparing the method for polycarbonate is described in US5, in 498,688,5,494,992 and 5,489,665.
The blend of polyester and polycarbonate can prepare by such method, and it comprises step: blend under about 25 ℃～350 ℃ temperature is enough to form the time of transparent blend composition with polycarbonate and polyester portion.Suitable conventional blending technology comprises melt process and solution manufacturing method.Other suitable blending technology comprises dry blend/or extrude.
Composition of the present invention comprises the unmixing that wherein contains and the blend of homogeneous, can prepare by any means as known in the art, and be suitable for as thermoplastic composition and form film and individual layer and multi-layer product.Except the various components of this blend of physical blending, can make the homogeneous polyester blend by the transesterify of polyester.Similarly, can get the intimate blending thing of polymeric amide by the acid amides exchange system of polyamide component.
Melt blended method be included in be enough to under the temperature of first component and the second component partial melting with polymer blending, blend is cooled to is enough to make under the temperature of transparent blends subsequently.Term used herein " fusion " comprises but is not to be defined in, only softening polymkeric substance.The case description of common known melting mixing method is in Mixing andCompounding of Polymer s (I.Mana s-Zloczower ﹠amp in the polymer arts; Z.Tadmor eds., CarlHanser Verlag publisher, N.Y.1994).
Solution manufacturing method comprises first component of suitable w/w ratio and second components dissolved in the mixture of suitable organic solvent such as methylene dichloride or 70/30 methylene dichloride and hexafluoroisopropanol, mix this solution, and blend composition is separated from solution by the precipitation blend or by evaporating solvent.The formulations prepared from solutions blend method is known usually in the polymer arts.
Melt-mixing method is the preferred method of preparation blend composition of the present invention.Melt-mixing method is more more economical and safer than solution methods (it need use volatile solvent).Melt-mixing method also more effectively provides transparent blends.Can also can prepare by of the present invention any transparent blends that solution blending makes by melting method.But, can by melting method up to blends more of the present invention, can not prepare by solution manufacturing method.Provide the blend method of transparent blends of the present invention to suit arbitrarily.Those of ordinary skills can determine to prepare the suitable blend method of transparent blends of the present invention.
First and second components of said composition can be prepared burden in melt, for example, by using single screw extrusion machine or twin screw extruder.They also can prepare by blend in solution.Also other component such as stablizer, fire retardant, tinting material, lubricant, releasing agent, impact modifier etc. can be introduced in the prescription.For example, can be by for example metal catalyst, dyestuff, toning agent, filler etc. melt extrude batching and prepare said composition with first component and second component and other composition component arbitrarily.Can by thermoplastic polymer and polyamide component each solid pellets or bead do to mix and melt-blended mixtures in suitable mixing equipment such as forcing machine, mill etc. subsequently, the formation said composition.When comprising second component (that is, in the presence of first component) of intimate blending thing of acid amides exchange of polymeric amide when the expectation in-situ preparing, handle will making under the temperature that the acid amides exchange takes place between the polymeric amide valuably.Typically, these temperature ranges are about 270 ℃～about 350 ℃.Other example of acid amides exchange temperature is about 280 ℃～about 350 ℃ and about 290 ℃～about 340 ℃.Carry out the time period that blend will produce the unmixing blend of good distribution.Those skilled in the art can easily determine this point.If desired, can and cut into bead with the said composition cooling with further processing, can be extruded into the element of film, sheet material, section bar and other shape, injection moulding or compression moulding are to form the goods of different shape, perhaps can form it into film, and randomly by method single shaft well-known in the art or biaxial stretch-formed.
The consumption of first and second components can vary widely in this unmixing blend.For example, we can comprise first component of about 5～about 99wt% and second component of about 95～about 1wt% by the new unmixing blend of forming, based on the gross weight of said composition.Other indefiniteness representative example of the weight percent of first and second components comprises first component of about 50～about 99wt% and second component of about 50～about 1wt%, first component of about 60～about 99wt% and second component of about 40～about 1wt%, first component of about 70～about 99wt% and second component of about 30～about 1wt%.
Our invention also provides a kind of composition by comprising that the following method of melt blending makes:
(i) first component comprises at least a thermoplastic polymer that is selected from polyester, polycarbonate, polyarylester and intimate blending thing thereof; With
(ii) second component comprises the homogeneous of at least 2 kinds of polymeric amide, the blend of acid amides exchange; Wherein, this second component is about 0.006～approximately-0.0006 with difference RI (second the component)-RI (first component) of the specific refractory power of this first component (i) (ii), and the percent transmittancy of said composition is at least 75%, and mist degree is 10% or lower.Of the present invention still on the other hand in, this first component comprises and contains terephthalate, 2,2,4,4-tetramethyl--1, the polyester of the residue of 3-cyclobutanediol and 1,4 cyclohexane dimethanol.Thus, the present invention also provides a kind of polymer composition by comprising that the following method of melt blending makes:
(i) first component comprises at least a polyester, and it comprises:
(a) diacid residues comprises based on the total diacid residue being the residue of the terephthalic acid of about 70～about 100mol%; At least a residue that has up to the modified aromatic dicarboxylic acid of 20 carbon atoms of 0～about 30mol%; At least a residue that has up to the modified aliphatic dicarboxylic acid of 16 carbon atoms with 0～about 10mol%; With
(b) diol residue comprises that based on the total diol residue be 2,2,4 of about 1～about 99mol%, 4-tetramethyl--1, the residue of 3-cyclobutanediol; Residue with the 1,4 cyclohexane dimethanol of about 1～about 99mol%; With
(ii) second component comprises blend homogeneous, the acid amides exchange of at least two kinds of polymeric amide;
Wherein, this second component is about 0.006～approximately-0.0006 with difference RI (second the component)-RI (first component) of the specific refractory power of this first component (i) (ii), and the percent transmittancy of this unmixing blend is at least 75%, and mist degree is 10% or lower.Said composition comprises the various embodiments and the arbitrary combination thereof of above-mentioned polyester, polycarbonate, polyarylester, intimate blending thing and polymeric amide.For example, second component of said composition can comprise the blend of the homogeneous acid amides exchange of at least two kinds of polymeric amide, wherein can realize the acid amides exchange by polymeric amide is at high temperature contacted, and typically is about 270 ℃～about 350 ℃.Other example of acid amides exchange temperature is about 280 ℃～about 350 ℃ and about 290 ℃～about 340 ℃.
Component intimate blending thing (ii) can comprise first polymeric amide that contains aromatic moieties and second polymeric amide of fatty family residue, as previously mentioned.For example, can comprise as the typical polyamides of second polymeric amide but be not to be defined in, nylon 4, nylon 6, nylon 9, Ni Long11, nylon 12, nylon 6,6, nylon 5,10, nylon 6,12, nylon 6,11, nylon 10,12, and combination.Except aforementioned polyester, this first component can comprise polyester and contain the intimate blending thing of the polycarbonate of dihydroxyphenyl propane.
Another aspect of the invention is a kind of method for preparing transparent, oxygen-scavenging compositions, comprising:
(A) select to comprise at least a first component that is selected from the thermoplastic polymer of polyester, polycarbonate, polyarylester and intimate blending thing thereof;
(B) specific refractory power (RI) of measurement first component;
(C) provide second component, it comprises:
(i) have the copolyamide of the mol ratio of aliphatics and aromatic moieties, wherein select the mol ratio of aliphatics and aromatic moieties, make second component that specific refractory power satisfies following formula thus:
0.006 〉=RI (second component)-RI (first component) 〉=-0.0006; Perhaps
The blend (ii) homogeneous of first and second polymeric amide, the acid amides exchange, at least a this polymeric amide has aromatic moieties, wherein selects the weight percent of first and second polymeric amide, makes second component that specific refractory power satisfies following formula thus:
0.006 〉=RI (second component)-RI (first component) 〉=-0.0006,
Wherein RI is a specific refractory power; With
(D) this first and second component of melt blending, make thus percent transmittancy at least 75% and mist degree be 10% or lower unmixing blend.
Of the present invention still on the other hand in, this first component comprises and contains terephthalate, 2,2,4,4-tetramethyl--1, the polyester of the residue of 3-cyclobutanediol and 1,4 cyclohexane dimethanol.Thus, the present invention also provides a kind of method for preparing transparent, oxygen-scavenging compositions, comprising:
(A) selection comprises first component of at least a polyester, and it comprises:
(a) diacid residues comprises based on the total diacid residue being the residue of the terephthalic acid of about 70～about 100mol%; At least a residue that has up to the modified aromatic dicarboxylic acid of 20 carbon atoms of 0～about 30mol%; At least a residue that has up to the modified aliphatic dicarboxylic acid of 16 carbon atoms with 0～about 10mol%; With
(b) diol residue comprises that based on the total diol residue be 2,2,4 of about 1～about 99mol%, 4-tetramethyl--1, the residue of 3-cyclobutanediol; Residue with the 1,4 cyclohexane dimethanol of about 1～about 99mol%;
(B) specific refractory power (RI) of measurement first component;
(C) provide second component, it comprises:
(i) have the copolyamide of the mol ratio of aliphatics and aromatic moieties, wherein select the mol ratio of aliphatics and aromatic moieties, make second component that specific refractory power satisfies following formula thus:
0.006 〉=RI (second component)-RI (first component) 〉=-0.0006; Perhaps
The blend (ii) homogeneous of first and second polymeric amide, the acid amides exchange, at least a polymeric amide has aromatic moieties, wherein selects the weight percent of first and second polymeric amide, makes second component that specific refractory power satisfies following formula thus:
0.006 〉=RI (second component)-RI (first component) 〉=-0.0006,
Wherein RI represents the described specific refractory power of first and second components; With
(D) melt blending first and second components, make thus percent transmittancy at least 75% and mist degree be 10% or lower unmixing blend.
Our method comprises the various embodiments and the arbitrary combination thereof of foregoing polyester, polycarbonate, polyarylester, intimate blending thing and polymeric amide.
Our method comprises selects this first component, and it can be polyester, polycarbonate, polyarylester or its intimate blending thing.Can adopt the well-known method of those skilled in the art to determine the specific refractory power of this first component.In the situation of copolyamide, pass through to select the suitable mixture of aromatics and aliphatic monomer, if the mixture of the polymeric amide of the aromatics by selecting to contain expectation when perhaps using the intimate blending thing of polymeric amide and the mixture of aliphatic residue, cut out second component of the intimate blending thing of the acid amides exchange that can comprise single copolyamide or at least two kinds of polymeric amide, thus with the specific refractory power wringing fit of first component.The selection of the monomeric suitable proportion of polymeric amide, can be definite as getting off, for example pass through repetition test, perhaps aromatic moieties and the various polymeric amide of aliphatic residue or the specific refractory power drawing of copolyamide by containing different amounts in another example, and selection will obtain the aromatics of targeted refractive index: the mol ratio of aliphatic residue or the weight percent of polymeric amide.Can be with the first and second component melts blend.When second component comprises the intimate blending thing of acid amides exchange of at least two kinds of polymeric amide, be desirably in and for the acid amides exchange process, carry out the melt blending step under the efficient temperature.Typical acid amides exchange temperature range as previously mentioned.
Also can select this thermoplastic polymer to cooperate the specific refractory power of second component.Thus, another aspect of the invention is a kind of method for preparing transparent, oxygen-scavenging compositions, it comprises:
(A) select second component, it comprises:
(i) has the copolyamide of the mol ratio of aliphatics and aromatic moieties; Perhaps
The blend (ii) homogeneous of first and second polymeric amide, the acid amides exchange, at least a this polymeric amide has aromatic moieties;
(B) specific refractory power of measurement second component;
(C) provide and comprise at least a first component that is selected from the thermoplastic polymer of polyester, polycarbonate, polyarylester and intimate blending thing thereof; Wherein, select this polyester, polycarbonate, polyarylester and intimate blending thing thereof, make first component that specific refractory power satisfies following formula:
0.006 〉=RI (second component)-RI (first component) 〉=-0.0006,
Wherein RI is a specific refractory power; With
(D) melt blending first and second components, make thus percent transmittancy at least 75% and mist degree be 10% or lower unmixing blend.As mentioned above, this first component comprises and contains terephthalate, 2,2,4,4-tetramethyl--1, the polyester of the residue of 3-cyclobutanediol and 1,4 cyclohexane dimethanol.Thus, the present invention also provides a kind of method for preparing transparent, oxygen-scavenging compositions, comprising:
(A) select second component, it comprises:
(i) has the copolyamide of the mol ratio of aliphatics and aromatic moieties; Perhaps
The blend (ii) homogeneous of first and second polymeric amide, the acid amides exchange, at least a this polymeric amide has aromatic moieties;
(B) specific refractory power of measurement second component;
(C) selection comprises first component of at least a polyester, and it comprises:
(a) diacid residues comprises based on the total diacid residue being the residue of the terephthalic acid of about 70～about 100mol%; At least a residue that has up to the modified aromatic dicarboxylic acid of 20 carbon atoms of 0～about 30mol%; At least a residue that has up to the modified aliphatic dicarboxylic acid of 16 carbon atoms with 0～about 10mol%; With
(b) diol residue comprises that based on the total diol residue be 2,2,4 of about 1～about 99mol%, 4-tetramethyl--1, the residue of 3-cyclobutanediol; Residue with the 1,4 cyclohexane dimethanol of about 1～about 99mol%; With
Wherein, select this polyester, make first component that specific refractory power satisfies following formula:
0.006 〉=RI (second component)-RI (first component) 〉=-0.0006,
Wherein, RI is a specific refractory power; With
(D) melt blending first and second components, make thus percent transmittancy at least 75% and mist degree be 10% or lower unmixing blend.
Be understood that further aforesaid method also comprises the arbitrary combination of the various embodiments of aforementioned polyester, polycarbonate, polyarylester, intimate blending thing, copolyamide, polymeric amide.
Among a kind of embodiment, can illustrate the blend of thermoplastic polymer in particular with reference to the polycarbonate/polyester blend, the difference that obtains specific refractory power thus is about 0.006～approximately second component and first component of-0.0006.For example, the thorough compatibility of the polycarbonate of dihydroxyphenyl propane and PCTG is allowed by regulating the specific refractory power (RI) that polycarbonate/PCTG ratio is come cutting polycarbonate/PCTG.By regulating the polycarbonate ratio, the specific refractory power of first component of the present invention can be matched with the specific refractory power of the blend of the homogeneous acid amides exchange that comprises copolyamide or polymeric amide within about 0.006～about-0.0006.For example, if transparent blends forms by the following: 1) with polymer-modified with contain the blend blend that is pre-existing in of polycarbonate and polyester portion, perhaps 2) by will be polymer-modified and the blend before the introducing polyester portion of polycarbonate part, perhaps 3) by will be polymer-modified with polyester portion introduce polycarbonate partly before blend, perhaps 4) polymer-modified, polycarbonate part and polyester portion all were mixed together before blend, can determine that polymkeric substance is the suitable polymer-modified of this homogeneous polyester/polycarbonate blend.
Transparent blends of the present invention still can make the performance blend thus by introducing the polymer-modified modification that comes, and it can need not to be transparent.For example, the nylon 6 of polymeric amide such as DuPont, 6, poly-(ether-imide) is as the ULTEM poly-(ether-imide) of General Electric, polyphenylene oxide is as poly-(2,6-dimethyl phenylate) or the NORYL resin of poly-(phenylate)/polystyrene blend such as GeneralElectric, polyester, polyphenylene sulfide, polyphenylene sulfide/sulfone, poly-(ester-carbonic ether) is as LEXAN 3250 poly-(ester-carbonic ether) (General Electric), polycarbonate outside the LEXAN polycarbonate of GeneralElectric, polyarylester such as ARDEL D100 polyarylester (Amoco), polysulfones, polysulfones ether, poly-(ether-ketone) or aromatic dihydroxy compound can come the modification performance or reduce flammable as blend properties-correcting agent.Some aromatic dihydroxy compounds that are used to prepare these polymkeric substance are disclosed in US3, and 030,335 and US3,317,466.
The intimate blending thing of copolyamide of the present invention or polymeric amide can be used as barrier polymer and, so, improve the barrier property of whole composition.Term used herein " barrier polymer " implication is to have the polymkeric substance of one or more following performances: (1) water permeate is 2gm-mils/100sq in/24hr or littler, measures down at 38 ℃ by ASTM method F1249; (2) oxygen permeability is 5cc (STP)-mils/100sq in/24hrs-atm or littler, measures down at 23 ℃ by ASTM method D3985; (3) carbon dioxide permeability is 25cc (STP)-mils/100sq in/24hrs atm or littler, measures down at 23 ℃ by ASTM method D1434.
By introducing the deoxidation composition of metal catalyst, can strengthen barrier property with the reaction that makes one or more polymeric amide in Catalytic Oxygen and the said composition.Thus, our method further provides a kind of deoxidation composition, and it comprises:
(A) comprise following unmixing blend:
(i) first component comprises at least a thermoplastic polymer that is selected from polyester, polycarbonate, polyarylester and intimate blending thing thereof; With
(ii) second component comprises the intimate blending thing of the acid amides exchange of at least two kinds of polymeric amide;
Wherein, this second component is about 0.006～approximately-0.0006 with difference RI (second the component)-RI (first component) of the specific refractory power of this first component (i) (ii), and the percent transmittancy of this unmixing blend is at least 75%, and mist degree is 10% or lower; With
(B) at least a metal that is selected from the periodic table of elements the 3rd～12 family the 4th～6 row.
This unmixing blend first component can comprise and contains terephthalate, 2,2,4,4-tetramethyl--1, the polyester of the residue of 3-cyclobutanediol and 1,4 cyclohexane dimethanol.Thus, another embodiment of the present invention is a kind of deoxidation composition, and it comprises:
(A) comprise following unmixing blend:
(i) first component comprises at least a polyester, and it comprises:
(a) diacid residues comprises based on the total diacid residue being the residue of the terephthalic acid of about 70～about 100mol%; At least a residue that has up to the modified aromatic dicarboxylic acid of 20 carbon atoms of 0～about 30mol%; At least a residue that has up to the modified aliphatic dicarboxylic acid of 16 carbon atoms with 0～about 10mol%; With
(b) diol residue comprises that based on the total diol residue be 2,2,4 of about 1～about 99mol%, 4-tetramethyl--1, the residue of 3-cyclobutanediol; Residue with the 1,4 cyclohexane dimethanol of about 1～about 99mol%; With
(ii) second component comprises blend homogeneous, the acid amides exchange of at least two kinds of polymeric amide;
Wherein, this second component is about 0.006～approximately-0.0006 with difference RI (second the component)-RI (first component) of the specific refractory power of this first component (i) (ii), and the percent transmittancy of this unmixing blend is at least 75%, and mist degree is 10% or lower; With
(B) at least a metal that is selected from the periodic table of elements the 3rd～12 family the 4th～6 row.
Except the intimate blending thing of one or more polymeric amide, deoxidation composition of the present invention also can comprise above about the described single copolyamide of other embodiment of the present invention.Thus, the present invention also provides a kind of deoxidation composition, and it comprises:
(A) comprise following unmixing blend:
(i) first component comprises at least a thermoplastic polymer that is selected from polyester, polycarbonate, polyarylester and intimate blending thing thereof; With
(ii) second component comprises copolyamide;
Wherein, this second component is about 0.006～approximately-0.0006 with difference RI (second the component)-RI (first component) of the specific refractory power of this first component (i) (ii), and the percent transmittancy of this unmixing blend is at least 75%, and mist degree is 10% or lower; With
(B) at least a metal that is selected from the periodic table of elements the 3rd～12 family the 4th～6 row.
As mentioned above, this unmixing blend first component can comprise and contains terephthalate, 2,2,4,4-tetramethyl--1, the polyester of the residue of 3-cyclobutanediol and 1,4 cyclohexane dimethanol.Thus, another embodiment of the present invention is a kind of deoxidation composition, and it comprises:
(A) comprise following unmixing blend:
(i) first component comprises at least a polyester, and it comprises:
(a) diacid residues comprises based on the total diacid residue being the residue of the terephthalic acid of about 70～about 100mol%; At least a residue that has up to the modified aromatic dicarboxylic acid of 20 carbon atoms of 0～about 30mol%; At least a residue that has up to the modified aliphatic dicarboxylic acid of 16 carbon atoms with 0～about 10mol%; With
(b) diol residue comprises that based on the total diol residue be 2,2,4 of about 1～about 99mol%, 4-tetramethyl--1, the residue of 3-cyclobutanediol; Residue with the 1,4 cyclohexane dimethanol of about 1～about 99mol%; With
(ii) second component comprises copolyamide;
Wherein, this second component is about 0.006～approximately-0.0006 with difference RI (second the component)-RI (first component) of the specific refractory power of this first component (i) (ii), and the percent transmittancy of this unmixing blend is at least 75%, and mist degree is 10% or lower; With
(B) at least a metal that is selected from the periodic table of elements the 3rd～12 family the 4th～6 row.
Should further be appreciated that this deoxidation composition comprises the arbitrary combination of the various embodiments of above-mentioned first and second components, polyester, polycarbonate, polyarylester, intimate blending thing, copolyamide and polymeric amide herein.
Similarly, another embodiment of the present invention is a kind of deoxidation composition, and it is made up of following basically:
(A) basically by the following unmixing blend of forming:
(i) first component is made up of at least a thermoplastic polymer that is selected from polyester, polycarbonate, polyarylester and intimate blending thing thereof basically; With
(ii) second component is made up of the intimate blending thing of the acid amides exchange of copolyamide or two kinds of polymeric amide basically at least;
Wherein, this second component is about 0.006～approximately-0.0006 with difference RI (second the component)-RI (first component) of the specific refractory power of this first component (i) (ii), and the percent transmittancy of this unmixing blend is at least 75%, and mist degree is 10% or lower; With
(B) at least a metal that is selected from the periodic table of elements the 3rd～12 family the 4th～6 row.
Wherein the difference of the specific refractory power absolute value of this first component and second component is 0.008 or littler, and the percent transmittancy of moulded products is at least 75%, and mist degree is 10% or lower.Still in another example, the invention provides a kind of deoxidation composition, it is made up of following basically:
(A) comprise following unmixing blend:
(i) first component is made up of at least a polyester basically, and it comprises:
(a) diacid residues is basically by being the residue of the terephthalic acid of about 70～about 100mol% based on the total diacid residue; At least a residue that has up to the modified aromatic dicarboxylic acid of 20 carbon atoms of 0～about 30mol%; At least a residue composition that has up to the modified aliphatic dicarboxylic acid of 16 carbon atoms with 0～about 10mol%; With
(b) diol residue, basically by being 2,2,4 of about 1～about 99mol% based on the total diol residue, 4-tetramethyl--1, the residue of 3-cyclobutanediol; Form with the residue of the 1,4 cyclohexane dimethanol of about 1～about 99mol%; With
(ii) second component is made up of the blend of the homogeneous acid amides exchange of two kinds of polymeric amide basically at least;
Wherein, this second component is about 0.006～approximately-0.0006 with difference RI (second the component)-RI (first component) of the specific refractory power of this first component (i) (ii), and the percent transmittancy of this unmixing blend is at least 75%, and mist degree is 10% or lower; With
(B) at least a metal that is selected from the periodic table of elements the 3rd～12 family the 4th～6 row.
In these embodiments, think that said composition got rid of any key element of the fundamental property of the composition that will change this phrase indication in fact, for example, the deoxidation performance of the compatibility of the % mist degree of the specific refractory power of component, unmixing blend, % transmittance, first and second components or said composition.For example, should get rid of the deoxidation component outside the acid amides exchange blend that adds copolyamide or polymeric amide, for example, the arbitrarily easy oxidizable organic compound in diene, polyethers or the claim outside the listed component.
Deoxidation composition of the present invention can comprise a kind of metal that is selected from the Internation Union of Pureand Applied Chemistry listed periodic table of elements the 3rd～12 family the 4th～6 row in 1984 editions periodictables.Typical oxide catalyst comprises the transition-metal catalyst that can easily transform mutually between at least two oxidation state.The example of operable metal comprises copper, nickel, cobalt, iron, manganese and combination thereof.Can adopt any catalytic amount of effective deoxo, still, typically, the consumption of metal is about 5ppm～about 1000ppm.Other scope of metal concentration comprises, about 50ppm～about 750ppm, and about 5ppm～about 600ppm, about 10ppm～about 500ppm, about 50ppm～about 500ppm and about 50ppm～about 300ppm is based on the gross weight of this deoxidation composition.Metal typical ground can be with metal element itself, with the metal complex that contains organic part, use with oxide compound or with metal-salt.The example that is used for the gegenion of metal-salt comprises but is not to be defined in, muriate, acetate, acetylacetonate, stearate, palmitate, 2-ethylhexoate, neodecanoate, octylate or naphthenate, and composition thereof.This metal-salt also can be an ionomer, wherein adopts the polymkeric substance gegenion.This ionomer is well known in the art.
In a kind of example, this metal catalyst is cobalt or the compound that contains cobalt, for example, and cobalt salt.Can adopt+2 and the cobalt of+3 oxidation state.Other example of metal catalyst is the rhodium of+2 oxidation state and the copper of+2 oxidation state.Can add this metal with salt form, be carboxylate salt expediently, for example, and cobalt octoate, cobaltous acetate or new cobalt decanoate.The amount of being reported is based on the weight of blend polymer and measures on metal, but not is added to the ingredients by weight in the said composition.At metal is in the cobalt situation, and typical amounts is 50ppm or 60ppm or 75ppm or 100ppm or 125ppm at least at least at least at least at least.Catalyzer pure or in carrier (as liquid or wax) can be added in the miscellaneous equipment of forcing machine or article of manufacture, perhaps can be with it with the enriched material of polyamide polymer, to add with the enriched material of polyester polymers or with enriched material with the unmixing blend.This carrier can be reactive or non-reacted to first and second components, and can adopt volatility or nonvolatile vehicle liquid.Can select and during this deoxidation preparation of compositions, add this metal catalyst a plurality of by multiple blend scheme.The approach of particularly suitable is, polymeric amide and transition metal are incorporated in the preparation of final blend composition together late, even evening in the last fusion step before forming goods, make the deoxidation activity of this polymeric amide can not cause too early.Sometimes, as when cobalt is provided as transition metal, can preferably during the blend of first and second components, add cobalt, replace for example preparing thermoplastic polymer during.
In a kind of embodiment, for example, first component of this deoxidation composition can comprise the polyester of the arbitrary combination with aforementioned monomer residue.For example, this polyester can comprise (a) diacid residues, comprise based on the total diacid residue and be selected from terephthalic acid, m-phthalic acid, naphthalic acid and 1 for 80mol% at least, at least a residue of the residue of at least a dicarboxylic acid of 4-cyclohexane cyclohexanedimethanodibasic and 0～about 20mol% with modification dicarboxylic acid of 2～20 carbon atoms; (b) diol residue, comprise based on the total diol residue and be selected from ethylene glycol, 1 for 80mol% at least, 4-cyclohexanedimethanol, neopentyl glycol, Diethylene Glycol, 1, ammediol, 1,4-butyleneglycol and 2,2,4,4-tetramethyl--1, at least a residue of the residue of at least a glycol of 3-cyclobutanediol and 0～about 20mol% with modification glycol of 3～16 carbon atoms.In another example, this diacid residues can comprise the residue of m-phthalic acid of residue and 0～about 40mol% of the terephthalic acid of about 60～100mol%, and this diol residue can comprise the residue of the 1,4 cyclohexane dimethanol of about 100mol%.In another example, this diacid residues can comprise that the total mole number based on diacid is the residue of the terephthalic acid of about 100mol%.Can comprise as other specific examples of the polyester of this first component and contain following polyester: (i) diacid residues of the residue of the terephthalic acid of about 80～about 100mol%, diol residue with the residue of the neopentyl glycol of the residue of the 1,4 cyclohexane dimethanol of about 50～about 90mol% and about 10～about 50mol%; The (ii) diacid residues of the residue of the terephthalic acid of about 100mol% is with the diol residue of the residue of the ethylene glycol of the residue of the 1,4 cyclohexane dimethanol of about 10～about 40mol% and about 60～about 90mol%; The (iii) diacid residues of the residue of the terephthalic acid of about 100mol%, diol residue with the residue of the Diethylene Glycol of the residue of the ethylene glycol of residue, 0～about 90mol% of the 1,4 cyclohexane dimethanol of about 10～about 99mol% and about 1～about 25mol%.Other example of polyester is that to comprise based on the total diacid residue be the residue of the terephthalic acid of about 70～about 100mol%; With any those in the following diol residue composition: (i) 2,2,4 of about 5～about 60mol%, 4-tetramethyl--1, the residue of the 1,4 cyclohexane dimethanol of the residue of 3-cyclobutanediol and about 40～about 95mol%; 2,2,4 of (ii) about 15～about 40mol%, 4-tetramethyl--1, the residue of the 1,4 cyclohexane dimethanol of the residue of 3-cyclobutanediol and about 60～about 85mol%; 2,2,4 of (iii) about 20～about 30mol%, 4-tetramethyl--1, the residue of the 1,4 cyclohexane dimethanol of the residue of 3-cyclobutanediol and about 70～about 80mol%; 2,2,4 of (iv) about 20～about 25mol%, 4-tetramethyl--1, the residue of the 1,4 cyclohexane dimethanol of the residue of 3-cyclobutanediol and about 75～about 80mol%.It is at least a aforesaid trihemellitic acid, trihemellitic acid acid anhydride and pyromellitic acid dianhydride, glycerine, the Sorbitol Powder, 1 of being selected from of about 0.1～about 1mol% that this polyester can further include based on the total diacid residue, 2, the branching agent of 6-hexanetriol, tetramethylolmethane, tartrate, citric acid, trimethylolethane and trimesic acid.
Other example of polyester is to comprise based on the residue of total diacid residue for the terephthalic acid of about 100mol%; With any those in the following diol residue composition: (i) residue of the ethylene glycol of the residue of the 1,4 cyclohexane dimethanol of about 1～about 5mol% and about 99～about 95mol%; The residue of the ethylene glycol of the residue of the 1,4 cyclohexane dimethanol of (ii) about 29～about 33mol% and about 71～about 67mol%; The residue of the ethylene glycol of the residue of the 1,4 cyclohexane dimethanol of (iii) about 45～about 55mol% and about 55～about 45mol%; The residue of the ethylene glycol of the residue of the 1,4 cyclohexane dimethanol of (iv) about 60～about 65mol% and about 40～about 35mol%; (the residue of the ethylene glycol of the residue of the 1,4 cyclohexane dimethanol of v) about 79～about 83mol% and about 21～about 17mol%; (the vi) residue of the 1,4 cyclohexane dimethanol of about 100mol%; (2,2,4 of vii) about 5～about 60mol%, 4-tetramethyl--1, the residue of the 1,4 cyclohexane dimethanol of the residue of 3-cyclobutanediol and about 40～about 95mol%; (2,2,4 of viii) about 15～about 40mol%, 4-tetramethyl--1, the residue of the 1,4 cyclohexane dimethanol of the residue of 3-cyclobutanediol and about 60～about 85mol%; (ix) 2,2,4 of about 20～about 30mol%, 4-tetramethyl--1, the residue of the 1,4 cyclohexane dimethanol of the residue of 3-cyclobutanediol and about 70～about 80mol%; (x) 2,2,4 of about 20～about 25mol%, 4-tetramethyl--1, the residue of the 1,4 cyclohexane dimethanol of the residue of 3-cyclobutanediol and about 75～about 80mol%.
This first component also can comprise the intimate blending thing of at least a polyester and at least a polycarbonate.The front has been described the polycarbonate that can be used in these intimate blending things.
The intimate blending thing or the copolyamide of acid amides exchange can comprise foregoing any polymeric amide, for example, and various nylon.But valuably, the intimate blending thing of the copolyamide of this deoxidation composition or polymeric amide comprises the residue of m-xylene diamine, p-Xylol diamines or its combination.For example, this second component can comprise first polymeric amide and the intimate blending thing that comprises second polymeric amide of nylon 6, nylon 6,6 or its blend of the residue that contains m-xylene diamine and hexanodioic acid.As another example, this intimate blending thing can be mixed with first component of the intimate blending thing that contains polyester and polycarbonate (residue that contains dihydroxyphenyl propane) in the unmixing blend.For the deoxidation performance of optimizing, also expectation is that the intimate blending thing of this copolyamide or polymeric amide contains 20mmol/kg or free amino group still less.Can adopt the well-known technology of those of ordinary skills for example to determine the concentration of free amino group by titration.
In another example, this deoxidation composition comprises the copolyamide of m-xylene diamine adipic acid ester.Modification m-xylene diamine adipic acid ester uses, some of some of them hexanodioic acid residue or some m-xylene diamine residues or the two, replace with other residue, with respect to the composition that only contains m-xylene diamine adipic acid ester homopolymer, can obtain to have the deoxidation composition of improved deoxidation performance.Described herein other polymeric amide barrier polymer also can be as the part of this deoxidation composition.
The composition of the invention described above can be used to make moulded products, for example, and sheet material, film, pipe, prefabrication, bottle or section bar.These goods can be made by the well-known method of those skilled in the art, for example, extrude, calendering, thermoforming, blowing, extrusion-blown modling, injection moulding, compression moulding, casting, drawing-off, tentering or blowing.
For example, can composition of the present invention be made moulded products by any technology as known in the art, for example, film.The formation of film can be by melt extruding (for example as US4, described in 880,592) or realizing by compression moulding (for example as US4, described in 427,614) or by any other proper method.For example, can make film by well-known casting films, blown film and extrusion coated technology, the latter comprises and being expressed on the matrix.This matrix also can comprise tack coat.The film that makes by fusion-cast or blowing can heat bonding or is adopted adhesive seal to matrix.Can adopt any technology as known in the art that said composition is made the single or multiple lift film.For example, can prepare the single or multiple lift film by well-known casting films, blown film and extrusion coated technology, the latter comprises and being expressed on the matrix.Representative matrix comprises film, sheet material and woven and non-woven fabrics.The single or multiple lift film that makes by fusion-cast or blowing can heat bonding or is adopted adhesive seal to matrix.
For example, can adopt traditional blown film equipment that said composition is formed film.This film-forming apparatus can be called " blown film " equipment in this area the sort of, and comprises the circular die that is used for said composition is therefrom promoted and forms the foaming blown film of film " bubble ".Should " bubble " last avalanche and formation film.
Said composition can be used for forming moulded products by extrusion-blown modling and injection stretch-blowing.Shooting Technique is softening in cartridge heater with copolyamide or homogeneous polyamide blend, with its injection, under high pressure be molten in the mold of sealing simultaneously, with the mold cooling to impel curing and from mold, to displace the prefabrication of molding.Moulding compound is highly suitable for the preparation of prefabrication and the final bottle shape of the performance with expectation of subsequently these prefabrication reheat being stretched-are blow molded into.The injection moulding prefabrication is heated to 100 ℃～150 ℃ suitable orientation temperature down and with back draft-blowing.A kind of technology in back by at first by mechanical means stretch in the axial direction the prefabrication (as by using the core rod insert pushing tow) of heat with after-blow high-pressure air (up to 500psi) to form encircling to stretch on the direction.In this way, make the bottle of biaxially oriented blowing.Typical expansion proportional range is 5/1～15/1.
Excellent transparency of the present invention and low haze make and can make transparent moulded products by introducing a large amount of scrappy polymkeric substance or " regrinding ".Term used herein " regrinding " thinks to have in this area the implication of accepting usually, that is, from product forming process, reclaim and be ground into more short grained scrappy polymkeric substance.Often, regrinding to be to sell for introduction into the waste material in the moulded products, and wherein to use for it be unessential to the transparency of these goods.For some moulded products, for example, be used for the bottle and the film of packaging application, low haze and high-clarity are the features of expectation.These goods, the particularly manufacturing of many one-tenth goods produce a large amount of scrappy polymkeric substance in essence, and it often can not be returned to goods and form in the technology owing to form the mist degree of unacceptable level.Because the specific refractory power wringing fit of first and second components, can make low haze, transparent moulded products by composition of the present invention, wherein comprise regrinding.
Thus, another aspect of the present invention is a kind of method that forms moulded products, and it comprises:
(A) melt blending is following:
(i) first component comprises at least a thermoplastic polymer that is selected from polyester, polycarbonate, polyarylester and intimate blending thing thereof; With
(ii) second component comprises the homogeneous of copolyamide or at least two kinds of polymeric amide, the blend of acid amides exchange;
Wherein, this first component (i) and second component (ii) form the unmixing blend, the difference RI of the specific refractory power of this second component and this first component (second component)-RI (first component) is about 0.006～approximately-0.0006, and the percent transmittancy of this unmixing blend is at least 75%, and mist degree is 10% or lower;
(B) form moulded products;
(C) recovery comprises first and second components (i) of blend and scrappy polymer composition (ii);
(D) grind this scrappy polymer composition to make regrinding;
(E) randomly, should scrappy polymer composition drying; With
(F) with first and second components (i) of this polymkeric substance regrinding and step (A) with (ii) mix.In another example, this first component can comprise and contains terephthalate, 2,2,4,4-tetramethyl--1, the polyester of the residue of 3-cyclobutanediol and 1,4 cyclohexane dimethanol.Thus, the present invention also comprises a kind of method that forms moulded products, and it comprises:
(A) melt blending is following:
(i) first component comprises at least a polyester, and it comprises:
(a) diacid residues comprises based on the total diacid residue being the residue of the terephthalic acid of about 70～about 100mol%; At least a residue that has up to the modified aromatic dicarboxylic acid of 20 carbon atoms of 0～about 30mol%; At least a residue that has up to the modified aliphatic dicarboxylic acid of 16 carbon atoms with 0～about 10mol%; With
(b) diol residue comprises that based on the total diol residue be 2,2,4 of about 1～about 99mol%, 4-tetramethyl--1, the residue of 3-cyclobutanediol; Residue with the 1,4 cyclohexane dimethanol of about 1～about 99mol%; With
(ii) second component comprises blend homogeneous, the acid amides exchange of at least two kinds of polymeric amide;
Wherein, this first component (i) and second component (ii) form the unmixing blend, the difference RI of the specific refractory power of this second component and this first component (second component)-RI (first component) is about 0.006～approximately-0.0006, and the percent transmittancy of this unmixing blend is at least 75%, and mist degree is 10% or lower;
(B) form moulded products;
(C) recovery comprises first and second components (i) of blend and scrappy polymer composition (ii);
(D) grind this scrappy polymer composition to make regrinding;
(E) randomly, should scrappy polymer composition drying; With
(F) with first and second components (i) of this polymkeric substance regrinding and step (A) with (ii) mix.
Thus, our method is allowed in the scrappy polymkeric substance regrinding introducing moulded products, is kept low haze and high-clarity simultaneously.Should further be appreciated that aforesaid method comprises aforesaid first and second components, polyester, polycarbonate, polyarylester, intimate blending thing, copolyamide, polymeric amide, the various embodiments deoxidation composition and combination.
For example, as previously mentioned, the unmixing blend that is formed by first and second components may further include at least a metal that is selected from the periodic table of elements the 3rd～12 family the 4th～6 row.The example of metal comprises but is not to be defined in, copper, nickel, cobalt, iron, manganese and combination thereof.Typically, the amount of metal is the metal of per 1,000,000 about 5～about 600 weight parts, based on the gross weight of this moulded products.Preferred metal is a cobalt.
The moulded products of the inventive method can form by any means as known in the art and aforesaid.For example, this moulded products can by extrude, calendering, thermoforming, blowing, extrusion-blown modling, injection moulding, compression moulding, casting, drawing-off, tentering or make.
Though method of the present invention can be used to prepare the random molding goods, the representative article that can prepare is sheet material, film, prefabrication, pipe and bottle.These goods can have simple layer or contain 2～about 7 layers.Regrinding can be incorporated in one or more these layers the regrinding that it typically can comprise based on this weight of one or more layers is about 50～100wt%.Other example of the regrinding level that can exist in the moulded products is about 5～about 95wt%, about 10～about 60wt%, about 15～about 50wt% and about 20～about 30wt%, based on this gross weight of one or more layers.
This moulded products can comprise that wherein one or more comprise the layer of this first and second component as the unmixing blend, perhaps first component and second component multilayer in independent layer wherein.Thus, the present invention also provides a kind of multilayer formed article, and it comprises:
(i) the first layer comprises at least a thermoplastic polymer that is selected from polyester, polycarbonate, polyarylester and intimate blending thing thereof; With
The (ii) second layer comprises the intimate blending thing of the acid amides exchange of at least two kinds of polymeric amide;
Wherein, this second layer is about 0.006～approximately-0.0006 with difference RI (the second layer)-RI (the first layer) of the specific refractory power of this first layer (i) (ii), and the percent transmittancy of this moulded products is at least 75%, and mist degree is 10% or lower.On the other hand, the first layer can comprise and contains terephthalate, 2,2,4,4-tetramethyl--1, the polyester of the residue of 3-cyclobutanediol and 1,4 cyclohexane dimethanol.Thus, another embodiment of the present invention is a kind of multilayer formed article, and it comprises:
(i) the first layer comprises at least a polyester, and it comprises:
(a) diacid residues comprises based on the total diacid residue being the residue of the terephthalic acid of about 70～about 100mol%; At least a residue that has up to the modified aromatic dicarboxylic acid of 20 carbon atoms of 0～about 30mol%; At least a residue that has up to the modified aliphatic dicarboxylic acid of 16 carbon atoms with 0～about 10mol%; With
(b) diol residue comprises that based on the total diol residue be 2,2,4 of about 1～about 99mol%, 4-tetramethyl--1, the residue of 3-cyclobutanediol; Residue with the 1,4 cyclohexane dimethanol of about 1～about 99mol%; With
The (ii) second layer comprises blend homogeneous, the acid amides exchange of at least two kinds of polymeric amide;
Wherein, this second layer is about 0.006～approximately-0.0006 with difference RI (the second layer)-RI (the first layer) of the specific refractory power of this first layer (i) (ii), and the percent transmittancy of this moulded products is at least 75%, and mist degree is 10% or lower.This moulded products can comprise aforesaid first and second components, polyester, polycarbonate, polyarylester, intimate blending thing, copolyamide, polymeric amide, the various embodiments deoxidation composition and combination.
This multilayer formed article can by extrude, calendering, thermoforming, blowing, extrusion-blown modling, injection moulding, compression moulding, casting, drawing-off, tentering or make.Because the wringing fit between this specific refractory power of first and second layers, this multi-layer product may further include the regrinding of the mixture that contains first and second layers, can be introduced into the first layer, for the second time or in the combination of first and second time.Typically, this regrinding is about 5wt%～about 60wt% of multi-layer product, based on the gross weight of these goods.Other example of the weight percent of regrinding is about 10wt%～about 40wt% and about 20wt%～about 30wt% of goods gross weight in the moulded products.
This multi-layer product can have 2～about 7 layers, according to its set application.For example, as mentioned above, this moulded products can be sheet material, film, pipe, bottle or prefabrication.Complicated layer structure also is possible.For example, this moulded products can have the layer structure shown in ABA, ABABA, ABCBA or the ACBCA, its middle level A comprise the first layer (i), layer B comprise the second layer (ii) and layer C comprise the polyester of acquisition during containing scrappy first and second layers (i) and mixture (ii), back human consumer reclaims or the regrinding of polycarbonate or its combination.The composition that depends on this regrinding, what it can be useful is, the difference RI of the specific refractory power of layer B and layer C (layer B)-RI (layer C) be about 0.006～approximately-0.0006, keeps the transparency of goods and the ability of introducing regrinding thus.
In another embodiment, layer A can comprise the second layer (ii), and layer B can comprise that the first layer (i) and layer C can comprise polyester or polycarbonate or its combination that obtains in scrappy first and second layers (i) and mixture (ii), the back human consumer's recovery.
In addition, the second layer of our new multi-layer product (ii) may further include at least a metal that is selected from the periodic table of elements the 3rd～12 family the 4th～6 row.The example of metal comprises copper, nickel, cobalt, iron, manganese and combination thereof.Typically, the amount of metal is the metal of per 1,000,000 about 10～about 500 weight parts, based on the gross weight of this moulded products.Other example of metal concentration is about 5ppm～about 600ppm and 10ppm～about 750ppm, based on the gross weight of this moulded products.Preferred metal is a cobalt.
Still in another embodiment, multilayer formed article of the present invention may further include at least one other layer, and its gross weight that comprises based on this layer is the regrinding of about 50～about 100wt%.This other layer that contains regrinding may further include at least a metal that is selected from the periodic table of elements the 3rd～12 family the 4th～6 row.The example of metal comprises copper, nickel, cobalt, iron, manganese and combination thereof.Typically, the amount of metal is the metal of per 1,000,000 about 10～about 500 weight parts, based on the gross weight of this moulded products.Other example of metal concentration is about 5ppm～about 600ppm and 10ppm～about 750ppm, based on the gross weight of this moulded products.Preferred metal is a cobalt.
As mentioned above, this multilayer formed article can comprise the various embodiments of foregoing moulded products, thermoplastic polymer, polymeric amide, unmixing blend, intimate blending thing and deoxidation composition.For example, this at least a thermoplastic polymer can comprise linearity or branched polyester, it comprises based on the total diacid residue and is selected from terephthalic acid, m-phthalic acid, naphthalic acid and 1 for 80mol% at least, at least a residue of the residue of at least a dicarboxylic acid of 4-cyclohexane cyclohexanedimethanodibasic and 0～about 20mol% with modification dicarboxylic acid of 2～2 0 carbon atoms; (b) diol residue, comprise based on the total diol residue and be selected from ethylene glycol, 1 for 80mol% at least, 4-cyclohexanedimethanol, neopentyl glycol, Diethylene Glycol, 1, ammediol, 1,4-butyleneglycol and 2,2,4,4-tetramethyl--1, at least a residue of the residue of at least a glycol of 3-cyclobutanediol and 0～about 20mol% with modification glycol of 3～16 carbon atoms; Comprise first polymeric amide of the residue that contains m-xylene diamine and hexanodioic acid and comprise the intimate blending thing of second polymeric amide of nylon 6, nylon 6,6 or its blend with these one or more barrier polymer.Other example of polyester is that to comprise based on the total diacid residue be the residue of the terephthalic acid of about 70～about 100mol%; With any those in the following diol residue composition: (i) 2,2,4 of about 5～about 60mol%, 4-tetramethyl--1, the residue of the 1,4 cyclohexane dimethanol of the residue of 3-cyclobutanediol and about 40～about 95mol%; 2,2,4 of (ii) about 15～about 40mol%, 4-tetramethyl--1, the residue of the 1,4 cyclohexane dimethanol of the residue of 3-cyclobutanediol and about 60～about 85mol%; 2,2,4 of (iii) about 20～about 30mol%, 4-tetramethyl--1, the residue of the 1,4 cyclohexane dimethanol of the residue of 3-cyclobutanediol and about 70～about 80mol%; 2,2,4 of (iv) about 20～about 25mol%, 4-tetramethyl--1, the residue of the 1,4 cyclohexane dimethanol of the residue of 3-cyclobutanediol and about 75～about 80mol%.It is at least a aforesaid trihemellitic acid, trihemellitic acid acid anhydride and pyromellitic acid dianhydride, glycerine, the Sorbitol Powder, 1 of being selected from of about 0.1～about 1mol% that this polyester can further include based on the total diacid residue, 2, the branching agent of 6-hexanetriol, tetramethylolmethane, tartrate, citric acid, trimethylolethane and trimesic acid.
For example, this thermoplastic polymer can comprise branched polyester.In another example, this thermoplastic polymer may further include the intimate blending thing of the polyester and the polycarbonate of the residue that contains dihydroxyphenyl propane.
Multilayer formed article of the present invention can prepare by the known any means of those of ordinary skills.For example, this moulded products can form by any conventional technology that is used to form film, comprises lamination, extrudes lamination, coextrusion, stretching-blowing and coextrusion blowing, and can set forth in particular with reference to the typical method for preparing multilayer film by coextrusion.For example, with first and second components, and optional layer arbitrarily, to feed in the hopper of same number of forcing machine, each forcing machine is handled the one or more material that is used for these layers.Typically, for composition of the present invention, with first and second components before extruding and during be heated to the temperature of about Tg+100 ℃～about Tg+300 ℃ separately, wherein Tg is the second-order transition temperature by first or second component of dsc measurement.Melt flow stream in each forcing machine is fed in the single manifold co-extrusion outlet mould.In the time of in this mouthful mould, the arranged side by side and combination with layer, the single multilayer film with polymer materials forms from this mouthful mould subsequently.Leave after mouthful mould, this film is cast on the casting roll of first controlled temperature, pass through around this first roller, and subsequently to the second controlled temperature roller, it is cooler than first roller usually.Mouthful mould rate of cooling of mould is afterwards left in the major control of controlled temperature roller.In the other method, this film-forming apparatus can be called blown film equipment in this area the sort of, and comprises the branch manifold circular die of the foaming blown film that is used for this film composition therefrom promoted and form the film bubble, and film steeps last avalanche and forms film.The method that coextrusion forms film and sheet material layered product is well-known.Alternatively, can be at first single layer be formed sheet material, and subsequently under heat and pressure use or impracticable intermediate adhesion layer it is laminated together.
The transparency of the present composition and low haze also make can introduce the moulded products that a large amount of scrappy polymkeric substance or " regrinding " make multi-layer transparent.Thus, our method also provides a kind of method that forms multilayer formed article, and it comprises:
(i) heating first component that comprises at least a thermoplastic polymer that is selected from polyester, polycarbonate, polyarylester and intimate blending thing thereof is to the temperature of about Tg+100 ℃ of this first component～about Tg+300 ℃;
Second component that (ii) heats the intimate blending thing of the acid amides exchange that comprises copolyamide or at least two kinds of polymeric amide arrives about Tg+100 ℃ of this second component～about Tg+300 ℃;
(iii) be formed on the moulded products that has this first and second component in the independent layer;
(iv) reclaim the first and second scrappy components;
(v) grind these first and second scrappy components to make regrinding;
(vi) randomly, with this regrinding drying; With
(vii) with this regrinding and step (i) and first component (ii), second component or its combined hybrid;
Wherein, step second component and difference RI (second the component)-RI (first component) of the specific refractory power of first component of step (i) (ii) is about 0.006～approximately-0.0006, and the percent transmittancy of this moulded products is at least 75%, and mist degree is 10% or lower.Among another embodiment, this first component can comprise and contains terephthalate, 2,2,4,4-tetramethyl--1, the polyester of the residue of 3-cyclobutanediol and 1,4 cyclohexane dimethanol.Thus, another aspect of the invention is a kind of method that forms multilayer formed article, it comprises:
(i) heating first component is to the temperature of about Tg+100 ℃ of this first component～about Tg+300 ℃, and this first component comprises at least a polyester, and it comprises:
(a) diacid residues comprises based on the total diacid residue being the residue of the terephthalic acid of about 70～about 100mol%; At least a residue that has up to the modified aromatic dicarboxylic acid of 20 carbon atoms of 0～about 30mol%; At least a residue that has up to the modified aliphatic dicarboxylic acid of 16 carbon atoms with 0～about 10mol%; With
(b) diol residue comprises that based on the total diol residue be 2,2,4 of about 1～about 99mol%, 4-tetramethyl--1, the residue of 3-cyclobutanediol; Residue with the 1,4 cyclohexane dimethanol of about 1～about 99mol%;
Second component that (ii) heats the intimate blending thing of the acid amides exchange that comprises copolyamide or at least two kinds of polymeric amide arrives about Tg+100 ℃ of this second component～about Tg+300 ℃;
(iii) be formed on the moulded products that has this first and second component in the independent layer;
(iv) reclaim the first and second scrappy components;
(v) grind these first and second scrappy components to make regrinding;
(vi) randomly, with this regrinding drying; With
(vii) with this regrinding and step (i) and first component (ii), second component or its combined hybrid;
Wherein, step second component and difference RI (second the component)-RI (first component) of the specific refractory power of first component of step (i) (ii) is about 0.006～approximately-0.0006, and the percent transmittancy of this moulded products is at least 75%, and mist degree is 10% or lower.Aforesaid method can comprise the various embodiments of the method and the arbitrary combination thereof of aforesaid first and second components, polyester, polycarbonate, polyarylester, intimate blending thing, copolyamide, polymeric amide, deoxidation composition, moulded products, formation goods.
Our method makes and a large amount of scrappy polymkeric substance regrindings can be introduced in the moulded products, keeps low haze and high-clarity simultaneously.This regrinding typically is included in the step (i) that produces with waste material during the process that forms goods and the mixture of first and second components (ii), but also can use any polymer materials, as long as its difference with the specific refractory power of second component is about 0.006～pact-0.0006.Can be with the regrinding of this process and first component, step second component (ii) or the combined hybrid of first and second components of step (i).This regrinding can be introduced first or the second layer, and about 5wt%～about 60wt% that can this moulded products, based on the gross weight of this moulded products.For the moulded products of the inventive method, other example of regrinding content is about 10wt% of moulded products～about 40wt% and about 20wt%～about 30wt%.
The multi-layer product of our method can have 2～about 7 layers, according to its set application.For example, as mentioned above, this multilayer formed article can be sheet material, film, pipe, bottle or prefabrication.Complicated layer structure also is possible.For example, this moulded products can have the layer structure shown in ABA, ABABA, ABCBA or the ACBCA, its middle level A comprise first component, the layer B of step (i) comprise step (ii) second component and layer C comprise the mixture that contains step (i) and the first and second scrappy components (ii), back human consumer reclaim in the polyester of acquisition or the regrinding of polycarbonate or its combination.The composition that depends on this regrinding, what it can be useful is, the difference RI of the specific refractory power of layer B and layer C (layer B)-RI (layer C) be about 0.006～approximately-0.0006, keeps the transparency of goods and the ability of introducing regrinding thus.
In another embodiment, layer A can comprise step second component (ii), layer B can comprise first component of step (i) and mixture, back human consumer that layer C can comprise step (i) and the first and second scrappy components (ii) reclaim in polyester or polycarbonate or its combination of acquisition.
In addition, step second component (ii) of our new multi-layer product may further include at least a metal that is selected from the periodic table of elements the 3rd～12 family the 4th～6 row.The example of metal comprises copper, nickel, cobalt, iron, manganese and combination thereof.Typically, the amount of metal is the metal of per 1,000,000 about 10～about 500 weight parts, based on the gross weight of this moulded products.Other example of metal concentration is about 5ppm～about 600ppm and 10ppm～about 750ppm, based on the gross weight of this moulded products.Preferred metal is a cobalt.When having metal, regulate diacid-diamines ratio valuably, make that terminal amino group concentration is 20mmol/kg or lower.
Still in another embodiment, the step of the inventive method (iii) may further include and forms at least one other layer, and its gross weight that comprises based on this layer is the regrinding of about 50～about 100wt%.This other layer that contains regrinding may further include at least a metal that is selected from the periodic table of elements the 3rd～12 family the 4th～6 row.The example of metal comprises copper, nickel, cobalt, iron, manganese and combination thereof.Typically, the amount of metal is the metal of per 1,000,000 about 10～about 500 weight parts, based on the gross weight of this moulded products.Other example of metal concentration is about 5ppm～about 600ppm and 10ppm～about 750ppm, based on the gross weight of this moulded products.Preferred metal is a cobalt.
As mentioned above, this multilayer formed article can comprise the various embodiments of foregoing moulded products, thermoplastic polymer, polymeric amide, unmixing blend, intimate blending thing and deoxidation composition.For example, this at least a thermoplastic polymer can comprise linearity or branched polyester, it comprises based on the total diacid residue and is selected from terephthalic acid, m-phthalic acid, naphthalic acid and 1 for 80mol% at least, at least a residue of the residue of at least a dicarboxylic acid of 4-cyclohexane cyclohexanedimethanodibasic and 0～about 20mol% with modification dicarboxylic acid of 2～20 carbon atoms; (b) diol residue, comprise based on the total diol residue and be selected from ethylene glycol, 1 for 80mol% at least, 4-cyclohexanedimethanol, neopentyl glycol, Diethylene Glycol, 1, ammediol, 1,4-butyleneglycol and 2,2,4,4-tetramethyl--1, at least a residue of the residue of at least a glycol of 3-cyclobutanediol and 0～about 20mol% with modification glycol of 3～16 carbon atoms; Comprise first polymeric amide of the residue that contains m-xylene diamine and hexanodioic acid and comprise the intimate blending thing of second polymeric amide of nylon 6, nylon 6,6 or its blend with these one or more barrier polymer.Other example of polyester is that to comprise based on the total diacid residue be the residue of the terephthalic acid of about 70～about 100mol%; 0～about 30mol% has a residue up at least a modified aromatic dicarboxylic acid of 20 carbon atoms; The residue of having with 0～about 10mol% up at least a modified aliphatic dicarboxylic acid of 16 carbon atoms; With any those in the following diol residue composition, based on the total diol residue: (i) 2,2,4 of about 5～about 60mol%, 4-tetramethyl--1, the residue of the 1,4 cyclohexane dimethanol of the residue of 3-cyclobutanediol and about 40～about 95mol%; 2,2,4 of (ii) about 15～about 40mol%, 4-tetramethyl--1, the residue of the 1,4 cyclohexane dimethanol of the residue of 3-cyclobutanediol and about 60～about 85mol%; 2,2,4 of (iii) about 20～about 30mol%, 4-tetramethyl--1, the residue of the 1,4 cyclohexane dimethanol of the residue of 3-cyclobutanediol and about 70～about 80mol%; 2,2,4 of (iv) about 20～about 25mol%, 4-tetramethyl--1, the residue of the 1,4 cyclohexane dimethanol of the residue of 3-cyclobutanediol and about 75～about 80mol%.It is at least a aforesaid trihemellitic acid, trihemellitic acid acid anhydride and pyromellitic acid dianhydride, glycerine, the Sorbitol Powder, 1 of being selected from of about 0.1～about 1mol% that this polyester can further include based on the total diacid residue, 2, the branching agent of 6-hexanetriol, tetramethylolmethane, tartrate, citric acid, trimethylolethane and trimesic acid.
For example, this thermoplastic polymer can comprise branched polyester.In another example, this thermoplastic polymer may further include the intimate blending thing of the polyester and the polycarbonate of the residue that contains dihydroxyphenyl propane.
Another embodiment of the present invention is a kind of method that forms multilayer formed article, and it comprises:
(A) heating first component is to the temperature of about Tg+100 ℃ of this first component～about Tg+300 ℃, this first component comprises (i) at least a polyester, it comprises: (a) diacid residues comprises the residue that is at least about the terephthalic acid of 95mol% based on the total diacid residue; (b) diol residue comprises the residue that is at least about at least a glycol that is selected from ethylene glycol and 1,4 cyclohexane dimethanol of 95mol% based on the total diol residue; With about 60～about 85mol% residue; The (ii) at least a polycarbonate that comprises the residue of dihydroxyphenyl propane; Perhaps (iii) its intimate blending thing;
(B) heating second component is to about 290 ℃ temperature, this second component comprises the polymeric amide that contains diamines and diacid residues and is selected from nylon 6 and nylon 6, the intimate blending thing of the acid amides exchange of 6 at least a polymeric amide, this polymeric amide comprise based on total diamines residue for the residue of the m-xylenedimaine of about 100mol% with based on the polymeric amide of total diacid residue for the residue of the hexanodioic acid of about 100mol%;
(C) be formed on the moulded products that has this first and second polymer composition in the independent layer;
(D) reclaim the first and second scrappy components;
(E) grind these first and second scrappy components to make regrinding;
(F) randomly, with this regrinding drying; With
(G) with this regrinding and step (A) and first component (B), second component or its combined hybrid;
Wherein, the difference RI (second component) of the specific refractory power of first component of second component of step (B) and step (B)-RI (first component) is about 0.006～approximately-0.0006, and the percent transmittancy of this moulded products is at least 75%, and mist degree is 10% or lower.Among another embodiment, this first component can comprise and contains terephthalate, 2,2,4,4-tetramethyl--1, the polyester of the residue of 3-cyclobutanediol and 1,4 cyclohexane dimethanol.Thus, another embodiment of the present invention is a kind of method that forms multilayer formed article, and it comprises:
A kind of method for preparing multilayer formed article comprises:
(A) heating first component is to the temperature of about Tg+100 ℃ of this first component～about Tg+300 ℃, and described first component comprises at least a polyester, and it comprises:
(a) diacid residues comprises based on the total diacid residue being the residue of the terephthalic acid of about 95～about 100mol%; With
(b) diol residue comprises that based on the total diol residue be 2,2,4 of about 15～about 40mol%, 4-tetramethyl--1, the residue of 3-cyclobutanediol; Residue with the 1,4 cyclohexane dimethanol of about 60～about 85mol%;
Wherein, the logarithmic viscosity number of this polyester is about 0.55～about 0.75dL/g;
(B) heating second component is to about 290 ℃～about 310 ℃ temperature, this second component comprise following acid amides exchange, the intimate blending thing: (a) have diamines and diacid residues and comprise based on total diamines residue being the polymeric amide of residue of the hexanodioic acid of about 100mol% for the residue of the m-xylenedimaine of about 100mol% with based on the total diacid residue; (b) be selected from least a polymeric amide of nylon 6 and nylon 6,6;
(C) be formed on the moulded products that has this first and second polymer composition in the independent layer;
(D) reclaim the first and second scrappy components;
(E) grind these first and second scrappy components to make regrinding;
(F) randomly, with this regrinding drying; With
(G) with this regrinding and step (A) and first component (B), second component or its combined hybrid;
Wherein, the difference RI of the specific refractory power of first component of second component of step (B) and step (B) (second component)-RI (first component) is about 0.006～approximately-0.0006, and the percent transmittancy of described moulded products is at least 75%, and mist degree is 10% or lower.Aforesaid method can comprise the various embodiments of the method and the arbitrary combination thereof of aforesaid first and second components, polyester, polycarbonate, polyarylester, intimate blending thing, copolyamide, polymeric amide, deoxidation composition, moulded products, formation goods.
As previously mentioned, this regrinding can comprise first and second components (i) and mixture (ii), and can be with itself and first component (i), second component (ii) or its combined hybrid.This regrinding can be for about 5wt%～about 60wt% of this moulded products, based on the gross weight of this moulded products.For the moulded products of the inventive method, other example of regrinding content is about 10wt% of moulded products～about 40wt% and about 20wt%～about 30wt%.The polyester of this method can comprise the diacid residues that contains at least about the residue of the terephthalic acid of 95mol%, and the diol combination thing that can have certain limit.For example, this polyester can comprise the diol residue of residue of the ethylene glycol of the residue of the 1,4 cyclohexane dimethanol that contains about 1～about 5mol% and about 99～about 95mol%.Other example of diol combination thing that is used for the polyester of this method comprises but is not to be defined in: the diol residue of residue that (i) contains the ethylene glycol of the residue of 1,4 cyclohexane dimethanol of about 29～about 33mol% and about 71～about 67mol%; (b) contain the diol residue of residue of the ethylene glycol of the residue of 1,4 cyclohexane dimethanol of about 45～about 55mol% and about 55～about 45mol%; The diol residue of residue that (iii) contains the ethylene glycol of the residue of 1,4 cyclohexane dimethanol of about 60～about 65mol% and about 40～about 35mol%; The diol residue of residue that (iv) contains the ethylene glycol of the residue of 1,4 cyclohexane dimethanol of about 79～about 83mol% and about 21～about 17mol%; (the diol residue of residue that v) contains the 1,4 cyclohexane dimethanol of about 100mol%.Other example of polyester is that to comprise based on the total diacid residue be the residue of the terephthalic acid of about 95～about 100mol%; With any those in the following diol residue composition, based on the total diol residue: (i) 2,2,4 of about 5～about 60mol%, 4-tetramethyl--1, the residue of the 1,4 cyclohexane dimethanol of the residue of 3-cyclobutanediol and about 40～about 95mol%; 2,2,4 of (ii) about 15～about 40mol%, 4-tetramethyl--1, the residue of the 1,4 cyclohexane dimethanol of the residue of 3-cyclobutanediol and about 60～about 85mol%; 2,2,4 of (iii) about 20～about 30mol%, 4-tetramethyl--1, the residue of the 1,4 cyclohexane dimethanol of the residue of 3-cyclobutanediol and about 70～about 80mol%; 2,2,4 of (iv) about 20～about 25mol%, 4-tetramethyl--1, the residue of the 1,4 cyclohexane dimethanol of the residue of 3-cyclobutanediol and about 75～about 80mol%.It is at least a aforesaid trihemellitic acid, trihemellitic acid acid anhydride and pyromellitic acid dianhydride, glycerine, the Sorbitol Powder, 1 of being selected from of about 0.01～1mol% that this polyester can further include based on the total diacid residue, 2, the branching agent of 6-hexanetriol, tetramethylolmethane, tartrate, citric acid, trimethylolethane and trimesic acid.
In another example, this thermoplastic polymer may further include the intimate blending thing of the polyester and the polycarbonate of the residue that contains dihydroxyphenyl propane.Every kind of polyester and polycarbonate can be linearity or branching.
In addition, step second component (ii) of our new method may further include at least a metal that is selected from the periodic table of elements the 3rd～12 family the 4th～6 row.The example of metal comprises copper, nickel, cobalt, iron, manganese and combination thereof.Typically, the amount of metal is the metal of per 1,000,000 about 10～about 500 weight parts, based on the gross weight of this moulded products.Other example of metal concentration is about 5ppm～about 600ppm and 10ppm～about 750ppm, based on the gross weight of this moulded products.Preferred metal is a cobalt.When having metal, regulate diacid-diamines ratio valuably, make that terminal amino group concentration is 20mmol/kg or lower.
Still in another embodiment, the step of the inventive method (C) may further include and forms at least one other layer, and its gross weight that comprises based on this layer is the regrinding of about 50～about 100wt%.This other layer that contains regrinding may further include at least a metal that is selected from the periodic table of elements the 3rd～12 family the 4th～6 row.The example of metal comprises copper, nickel, cobalt, iron, manganese and combination thereof.Typically, the amount of metal is the metal of per 1,000,000 about 10～about 500 weight parts, based on the gross weight of this moulded products.Other example of metal concentration is about 5ppm～about 600ppm and 10ppm～about 750ppm, based on the gross weight of this moulded products.Preferred metal is a cobalt.
Moulded products of the present invention can further be orientated by stretching, and it can improve the barrier property of goods.As previously mentioned, can be desirably with other conventional additive or polymer-modified being incorporated in the polymer composition of the present invention.For example, can add oxidation inhibitor, light and heat stablizer, dyestuff, static inhibitor, lubricant, sanitas, processing aid, surface slip agent, release agent, pigment, fire retardant, whipping agent etc.Can use more than one additive.Additive can exist with the amount of any desired, but typically with about 20wt% of being not more than the moulded products gross weight, preferably be not more than 10wt% and exist.
This polymer composition, deoxidation composition and by its moulded products that makes also can comprise up to about 30wt%, preferably less than about 20wt%, derived from some platelet particles of at least a layered silicate material, improve their barrier property thus.This platelet particles can be with at least a ammonium compound modification.The residual ash of measuring polymkeric substance-platelet particles composition when the consumption of platelet particles can be handled by foundation ASTM D5360-94 assigns to determine.The gas-barrier improvement is typically along with the concentration of platelet particles in the matrix material increases and increases.Provide improved obstruct (particularly when good distribution and time) in order though be low to moderate about 0.01% platelet particles consumption, preferably had composition, because they have shown the improvement that the gas permeability aspect is expected at least about the platelet particles of 0.5wt%.
Usually, layered silicate is the intensive aggregate of platelet particles, and its similar card ground is together tightly packed.Platelet particles of the present invention typically thickness for being about 10～about 5000nm less than about 2nm and diameter.For purposes of the present invention, measurement only refers to platelet particles and is not ammonium compound or any other dispersing auxiliary that may use and processing compound.Suitable platelet particles is derived from the layered silicate material that typically is free flowing powder, and its cation exchange capacity is about 0.3～about 1.5meq/g, and is preferably about 0.8～about 1.5meq/g.The example of suitable layered silicate material comprises mica type stratiform phyllosilicate, comprises clay, montmorillonite, na montmorillonite, sodium hectorite, wilkinite, nontronite, beidellite, volonsloite, saponite, sauconite, magadite, fibrous morphology crystals, synthetic sodium hectorite etc.This class clay can obtain from a plurality of companies, comprises Southern Clay Products and Nanocor, Inc..Most preferred platelet particles is derived from sodium hectorite or na montmorillonite.This clay obtains in the U.S. easily, is known as the polynite of Wyoming model and obtains in other area in the world, comprises the Kunipia clay, can be from KunimineIndustries, and Inc. obtains.
Typically handle layered silicate material to improve the dispersiveness in polymer composition.Known multiple useful clay treatment in this area, and these handle also can be before this layered silicate material be introduced matrix material of the present invention, afterwards or during use, do not depart from scope of the present invention.The example of useful processing comprises but is not to be defined in, and handles with silane compound, swelling agent, polymkeric substance and oligopolymer, dispersing auxiliary, organic cation salt and their combination.
Adopt the example of the useful processing of silane compound to comprise disclosed processing in the International Application No. WO 93/11190.The example of useful silane compound comprises, (3-glycidoxypropyl) Trimethoxy silane, 2-methoxyl group (poly-ethyleneoxy group) propyl group seven methyl trisiloxanes, octadecyl dimethyl (the 3-trimethoxy adds the silylation propyl group) ammonium chloride etc.
Adopt the example of the useful processing of swelling agent to comprise oligopolymer well known in the art.The representative polymer and the oligopolymer that are used to handle clay comprise US5, in 552,469 and 5,578,672 disclosed those.Multiple dispersing auxiliary is known, comprises multiple material, comprises water, alcohol, ketone, aldehyde, chlorinated solvent, hydrocarbon solvent, aromatic hydrocarbons etc. or its combination.
Embodiment
Summary:
The present invention further sets forth by the following example.Utilize the scanning speed of TA Instruments 2920 differential scanning calorimeters (DSC), measure the second-order transition temperature (Tg) of polyester, polymeric amide and blend by ASTM method D3418 with 20 ℃/min.Measure heat-drawn wire by ASTM method D648, and carry out the test of breach shock strength according to ASTM method D256.Measure flexural property according to ASTM method D790.Under 23 ℃, measure the tensile properties of blend according to ASTM method D638.In 60/40 (wt/wt) phenol/tetrachloroethane, under 25 ℃, measure the logarithmic viscosity numbers of polyester with the concentration of 0.5g/100mL.By proton magnetic resonance (PMR) spectrum ( 1H NMR) measures the glycol content of the polyester portion of these blends.Determine the compatibility of blend by the differential scanning calorimetric of press mold and moulded parts.
Utilize Hunter Associates Laboratory, Inc., Reston, VA., HunterLab UltraScan Sphere 8000 calorimeters of making, adopt Hunter ' s UniversalSoftware (3.8 version), measure haze value (% mist degree=100* diffuse transmission/total transmission) by ASTM method D1003.Carry out the calibration and the operation of this equipment according to the HunterLab User Manual.By ligh trap being placed on the opposite side of sample port integrating sphere, eliminate the light path that led directly to (straight-thru) thus, obtain diffuse transmission (% transmissivity).Only measure with light greater than 2.5 degree scatterings.Total transmission comprises measures the light that led directly to sample and by the off-axis light of sample scattering.Sample is placed the exit end of spheroid, make that the off-axis light in the whole ball inside can be used for scattering.Visually measure transparency with employing mist degree metering facility.For blend of the present invention and various composition, be 1/8 inch or littler sheet material, film or plate and above-mentioned operation measurement mist degree of foundation and percent transmittance by composition being formed thickness, determine mist degree and percent transmittance.For moulded products, comprise multilayer formed article, be that (i.e. 1 * 1cm) part goods, and measure mist degree and percent transmittance according to above-mentioned operation are determined mist degree and percent transmittance for 1/8 inch or littler sub-fraction by cutting out thickness.
Utilize Metricon Prism Coupler TMModel 2010 refractometers (can from Metricon Inc. obtain) are measured specific refractory power under 633nm, and be reported as 3 orthogonal directionss (extrude or stretch, laterally and thickness direction) go up the mean value of the specific refractory power of measuring.Go up the preparation alignment films at the long film drawing machine of TM (for manufacturers's name), the sample of its single shaft ground or the stretching compacting of twin shaft ground, blowing or extruded film.The operation of film drawing machine is based on the motion of rectangular each other two pull bars under the effect of hydrostatic transmission bar.The pull bar that the pull bar of existence and each motion is relatively fixed.These paired relative movement and fixed pull bar, four limits of membrane sample are connected in inferior, form rectangular each other two axles, sample are stretched to up to 4 or 7 times of original sizes with any stretch ratio along this, depend on the machine of use.Sample placed on the clip on the machine and before stretching be heated, if desired.Be output as the stress vs elongation data (if desired) under the temperature of test and stretched film in this equipment.
Utilize MOCON, Inc.Minneapolis, the Ox-Tran oxygen permeator that MN. makes is measured the oxygen permeability of film.By the thickness of known area, the film of film in the test, calculate oxygen permeability across the partial pressure difference of the oxygen of this film and the stable state transfer rate of measuring.In the situation of the sample that shows active deoxidation, the flux of measurement is not just very under stable state, slowly changes because transfer rate can change in time along with the efficient of deoxidation reaction.But, in these situations, often can think that the oxygen transmission is in the pseudostationary attitude during infiltration is measured.In the following example in the included active deoxidation sample, it is very little of not changing obviously to remove efficient during the measuring process, and calculates perviousness by the pseudostationary attitude transfer rate of measuring.
The comparative example 1～12
Listed copolyester in the table 1, but polyester G is made by terephthalic acid, ethylene glycol and 1,4 cyclohexane dimethanol (CHDM).Shown the amount of CHDM in the polyester in the table 1.Example F contains 100%CHDM (0% ethylene glycol), but the acid moieties of 26mol% is for replacing the m-phthalic acid of terephthalic acid.Polyester G is following making: with 21.24 lb (49.71g-mol) dimethyl terephthalate (DMT), 12.61 lb (39.77g-mol) 1,4-cyclohexanedimethanol and 6.30lb (19.88g-mol) 2,2,4, the reaction in the presence of the catalyzer butyl tin three (2-ethylhexoate) of 200ppm together of 4-tetramethyl--1,3-cyclobutanediol.2,2,4,4-tetramethyl--1, the cis/trans ratios of 3-cyclobutanediol are about 50/50.The cis/trans ratios of 1,4 cyclohexane dimethanol is about 30/70.Carry out in 18 gallons of stainless steel pressure containers that condensing tower, vacuum system and HELICONE type agitator are housed being reflected under the nitrogen purging.Stirrer moves with 25rpm, reaction mixture temperature is elevated to 250 ℃ and pressure is elevated to 20psig.Reaction mixture was remained on 250 ℃ and 20psig pressure following 2 hours.With 3psig/ minute speed pressure is reduced to 0psig subsequently.Subsequently the temperature of reaction mixture is elevated to 270 ℃ and pressure is elevated to 90mmHg.Remain on after following 1 hour of 270 ℃ and the 90mmHg, stirrer speed is reduced to 15rpm, reaction mixture temperature is elevated to 290 ℃, and pressure is reduced to less than 1mmHg.Reaction mixture is remained on 290 ℃ and less than following 12 minutes of 1mmHg.Utilize nitrogen that the pressure of pressurized vessel is increased to 1 normal atmosphere subsequently.From pressurized vessel, extrude molten polymer subsequently.Refrigerative, the polymkeric substance extruded are ground with by the 6-mm screen cloth.The logarithmic viscosity number of this polymkeric substance is that 0.590dL/g and Tg are 106 ℃.NMR analyzes demonstration, and this polymkeric substance is by 2,2,4 of the 1,4 cyclohexane dimethanol residue of 77.1mol% and 22.9mol%, 4-tetramethyl--1, and 3-cyclobutanediol residue is formed.The colour of this polymkeric substance: L*=83.27, a*=-1.34 and b*=5.08.
Table 1
Polyester CHDM in the polyester (mol%) Tg The specific refractory power of polyester
A 1.5 81 1.5708
B 31 83 1.5644
C 50 84 1.5593
D 62 86 1.5573
E 81 91 1.5547
F 100 88 1.5519
G 77 106 1.5470
With copolyester and MXD6 6121 polymeric amide (contain the m-xylene of 100mol% and the hexanodioic acid of 100mol%, can obtain) from Mitsubishi Corporation 70 ℃ of following dried overnight.Each and MXD6 of these copolyesters are mixed with 1,3 and 5% bag, and feed following temperature setting (℃) in 1.5 inches single screw extrusion machines of Sterling under 90rpm, form blend thus:
District 1 District 2 District 3 District 4 District 5
240 250 260 260 260
With blend 70 ℃ of following dried overnight, and on Toyo 90 injection moulding machines, under 270 ℃, be injection molded into 1/8 inch thick 4 subsequently " square plate.The specific refractory power of measuring MXD6 is 1.5824.The specific refractory power that has shown the haze value that obtains and nylon in the table 2 deducts the result after the specific refractory power of polyester:
Table 2
Embodiment Polyester type Polyester (wt%) MXD6 (wt％) The % mist degree Total light transmittance (%) RI (nylon)-RI (polyester)
C-1 A 99 1 5.2 82.8 0.0116
C-2 A 97 3 14.3 81.6 0.0116
C-3 A 95 5 29.8 82.0 0.0116
C-4 B 99 1 5.1 79.5 0.0180
C-5 B 97 3 22.4 70.7 0.0180
C-6 B 95 5 42.9 62.4 0.0180
Embodiment Polyester type Polyester (wt%) MXD6 (wt％) The % mist degree Total light transmittance (%) RI (nylon)-RI (polyester)
C-7 C 99 1 8.5 80.7 0.0231
C-8 C 97 3 31.0 70.4 0.0231
C-9 C 95 5 50.7 62.6 0.0231
C-10 D 99 1 11.5 77.6 0.0251
C-11 D 97 3 59.0 63.3 0.0231
C-12 D 95 5 81.6 53.5 0.0231
Embodiment 13-24,27-29,31-32,34-36,38 and comparative example 25-26,30,33,36-37 and 39
With nylon 6 (can Zytel  7335F obtain) and MXD6 (class 6 121) from DuPont 120 ℃ dry 48 hours and mix down with various ratio bags.Subsequently polymeric amide bag blend is fed following condition (℃) in 1.5 inches single screw extrusion machines of Sterling under 90rpm, form the blend of homogeneous acid amides exchange thus, exist single, relevant Tg to show this point with composition for every kind of blend.Shown the Tg value in the table 3.
District 1 District 2 District 3 District 4 District 5
250 270 300 300 300
The blend of nylon of part acid amides exchange or MXD6 120 ℃ of following dried overnight, and are injection molded into 1/8 inch thick sample subsequently on Toyo 90 injection moulding machines, perhaps under 240 ℃, are extruded into the thick film of 15mil under 240 ℃.Prepare this film by following expressing technique: employed forcing machine is traditional 2.54cm diameter Killian forcing machine, and 24: 1 L: D (length: ratio diameter), be equipped with the feed worm and the interlock maddock mixing section that possess 3: 1 compression ratios.Use traditional feed head with melt Conveying in traditional 15.24cm hanger-style die.Use the downward stack arrangement of 2 roller casting films to cool off this melt.Subsequently these films are stretched down at 95 ℃ on all directions on TM-Long 4x.The performance of these films is shown in the table 3 and the performance after stretching is shown among the table 3A before stretching.Should be pointed out that the oxygen permeability of table among the 3A is to use 100%O under 30 ℃ and 50% relative humidity 2Measure as test gas.
Film performance before table 3-stretches
Embodiment MXD6 (wt％) Nylon 6 (wt%) Tg (℃) Oxygen permeability (cc*mil/ 100in 2* day * atm) Thickness (mil) Specific refractory power
13 100 0 88 0.533 15.003 1.5824
14 95 5 87 0.440 15.000 1.5772
15 90 10 83 0.100 14.465 1.5739
16 87 13 83 0.063 14.498 1.5724
17 85 15 81 0.413 14.065 1.5717
18 75 25 77 1.266 15.260 1.5655
19 73 27 76 1.060 14.065 1.5641
20 70 30 75 1.317 14.535 1.5617
21 65 35 72 1.334 14.755 1.5599
22 62 38 72 0.740 16.385 1.5575
23 60 40 70 0.709 14.630 1.5536
24 0 100 44 1.5318
Film performance after table 3A-stretches
Embodiment MXD6 (wt％) Nylon 6 (wt%) Oxygen permeability (cc*mil/ (100in 2*day*atm) Thickness (mil)
13 100 0 0.230 0.900
14 95 5 0.238 0.930
15 90 10 0.263 0.850
16 87 13 0.340 0.860
17 85 15 0.325 0.820
18 75 25 0.499 0.900
19 73 27 1.402 0.885
20 70 30 0.622 0.880
21 65 35 0.215 0.970
22 62 38 0.847 1.095
23 60 40 0.982 0.995
24 0 100
In order to form embodiment shown in the table 4 and comparative example, blend or MXD6 dried overnight between 70～120 ℃ of the exchange of part acid amides are also prepared burden with the polyester of table 1 subsequently.With polyester dried overnight between 70～120 ℃.The blend or the MXD6 bag of the acid amides exchange of each and the selected table 3 of 10wt% of table 1 polyester are mixed, and be fed to following temperature setting (℃) in 1.5 inches single screw extrusion machines of Sterling under 90rpm, form the unmixing blend thus:
District 1 District 2 District 3 District 4 District 5
240 260 280 280 280
With blend 70 ℃ of following dried overnight, and on Toyo 90 injection moulding machines, under 270 ℃, be injection molded into 1/8 inch thick 4 subsequently " square plate.The specific refractory power that has shown the haze value that obtains and nylon in the table 4 deducts the result after the specific refractory power of polyester.
In order to form embodiment 38 and comparative example C-39, that the blend of the exchange of the acid amides among the embodiment 20 of table 3 is also mixed with the polyester A or the C bag of table 1 subsequently 70 ℃ of following dried overnight.Also with this polyester dried overnight between 70～120 ℃.Subsequently the bag blend is injection molded into 1/8 inch thick 4 on Toyo 90 injection moulding machines under 270 ℃ " square plate.The specific refractory power that has shown the haze value that obtains and MXD6 or blend of nylon in the table 4 deducts the result after the specific refractory power of polyester.
Table 4-has the polyester blend of MXD6/Nylon 6 intimate blending things
Embodiment Polyester type Embodiment in the blend table 3 CHDM in polyester (mol%) Blend MXD6 (wt%) Blend Nylon6 (wt%) Mist degree % Total light transmittance % RI (nylon)-RI (polyester)
C-25 A 13 1.5 100 0 28.1 71.1 0.0116
C-26 A 14 1.5 95 5 13.5 76.0 0.0064
27 A 15 1.5 90 10 6.3 77.8 0.0031
28 A 16 1.5 87 13 6.9 78.1 0.0016
29 A 17 1.5 85 15 7.7 77.9 0.0009
C-30 B 17 31 85 15 21.3 81.8 0.0073
31 B 18 31 75 25 5.0 86.5 0.0011
32 B 19 31 73 27 8.5 85.4 -0.0003
C-33 B 20 31 70 30 16.2 84.1 -0.0027
34 C 20 50 70 30 4.1 86.8 0.0024
36 C 21 50 65 35 8.3 84.5 0.0006
C-36 C 22 50 62 38 13.6 82.8 -0.0018
C-37 C 23 50 60 40 19.3 80.2 -0.0057
Embodiment Polyester type Embodiment in the blend table 3 CHDM in polyester (mol%) Blend MXD6 (wt%) Blend Nylon6 (wt%) Mist degree % Total light transmittance % RI (nylon)-RI (polyester)
38 C 20 50 70 30 3.7 86.3 0.0024
C-39 A 20 3.5 70 30 33.0 69.9 -0.0091
Embodiment 40:
In the embodiment of this indication, adopted the synthetic route of polymeric amide with suitable specific refractory power, replace two kinds of polymeric amide of blend in the foregoing description 13～24.Can adopt any means as known in the art to prepare these direct synthetic polymeric amide.This polymeric amide is prepared by diacid-diamine complexe by melt phase polymerization usually, and this complex compound can prepare in situ or in independent step.In the other method, diacid and diamines are as raw material.Alternatively, can use the ester-formin of diacid, preferred dimethyl ester.If the use ester, reaction must be carried out at a lower temperature, is generally 80～120 ℃, is converted into acid amides up to ester.Subsequently mixture heating up is arrived polymerization temperature.For the embodiment of this indication, institute's synthetic polymeric amide is poly-(m-xylene pimeloyl amine), and it is by diamines m-xylene diamine and diacid pimelic acid synthetic.Subsequently with the copolyester A blend in this polymeric amide and the 90wt% table 1, according to disclosed method among the embodiment 25～39.Prediction copolyester A is 0.0034 and predicts it is transparent with the difference of the specific refractory power of poly-(m-xylene pimeloyl amine).The mist degree of the blend that prediction obtains be less than 10% and transmissivity be greater than 75%.
Embodiment 42,47-49 and 56 and the unitary film and the deoxidation composition of comparative example 41,43-46 and 50-55 blend:
With top about embodiment 13～24 that discussed with table 5 in the mode of being given prepare the blend of several MXD6/N6 acid amides exchanges.With the top mode of being discussed about embodiment 13～24 listed refractive index value in the meter 5 on the 15mil film of the blend of these acid amides exchanges.The pre-blend of MXD6/N6 or several copolyester bags in MXD6 and the table 1 of these acid amides exchange of 3wt% or 5wt% are mixed, according to table 6.Subsequently these pill blends are also fed in 1.0 inches single screw extrusion machines of the Killian under 95rpm under the temperature shown in the table 6 subsequently 60 ℃～70 ℃ following dried overnight, form the thick film of nominal 30mil by this unmixing blend thus.The haze value of film that all contains pure MXD6 is greater than 10%.Wherein the film that is complementary within 0.006～-0.0006 scope of the specific refractory power of the specific refractory power of blend of nylon and corresponding polyester is transparent (mist degree≤10%).
MXD6-Nylon 6 blends of table 5-homogeneous
Nylon Form Specific refractory power Tg(℃)
W- MXD6/23wt%Nylon 6 pre-compositions of acid amides exchange 1.565 0 78
X- MXD6/30wt%Nylon 6 pre-compositions of acid amides exchange 1.5617 75
Y- MXD6/41wt%Nylon 6 pre-compositions of acid amides exchange 1.5528 70
Z- MXD6/50wt%Nylon 6 pre-compositions of acid amides exchange 1.5472 66
MXD6 MXD6 1.5824 88
In order to prepare the deoxidation composition, the enriched material that will contain new cobalt decanoate is added in two these films.Be prepared as follows this enriched material.With the independent charging of polyester type C and new cobalt decanoate, with the form of lozenge with Cobalt Ten-Cem TM22.5% (can obtain from OMG Corp.) supplied with, and is fed in the 57mm twin screw extruder and melt blending under about 235 ℃ bucket set(ting)value.The melt blended material that leaves forcing machine is about 0.08 " form of diameter thigh, with its with water cooling and cutting into about 0.125 " long pill.The ratio of polyester and polymeric amide and enriched material (weight) is 93: 5～5～1.5, and the cobalt concentration of metal makes this ratio be implemented in about 140～150ppm cobalt in the final blend film in this enriched material.The sample that contains cobalt shows excellent deoxidation capacity.These samples, 1 week was installed in it on Ox-Tran permeator after extruding, and it surpasses 6 months in one's duty average apparent perviousness under these conditions is less than 0.15cc (STP) * mil/100 inch 2/ sky/normal atmosphere.
Table 6-30mil single thin film result
Embodiment Polyester Nylon Melt temperature The % mist degree Total light transmittance (%) RI (nylon)-RI (polyester) Oxygen permeability *
C-41 B 3％MXD6 250℃ 22.72 88.1 0.0180
42 B 3％W 250℃ 1.13 90.5 0.0006
C-43 C 250℃ 0.47 90.8 n/a 25.06
C-44 C 3％MXD6 250℃ 35.90 87.8 0.0231
C-45 C 5％MXD6 280℃ 53.57 87.7 0.0231 13.62
C-46 C 5％MXD6+ Co 280℃ 34.12 86.2 0.0231 0.20
47 C 3％X 250℃ 1.00 90.7 0.0024
48 C 5％X 280℃ 0.98 90.6 0.0024 20.70
49 C 5％X+Co 280℃ 1.10 90.4 0.0024 0.09
Embodiment Polyester Nylon Melt temperature The % mist degree Total light transmittance (%) RI (nylon)-RI (polyester) Oxygen permeability *
C-50 E 3％MXD6 290℃ 27.12 85.6 0.0277
C-51 E 3％Y 290℃ 2.99 90.8 -0.0019
C-52 F 3％MXD6 250℃ 64.06 87.9 0.0305
C-53 F 3％Z 250℃ 2.28 92.3 -0.0047
C-54 G 280℃ 0.74 90.9 n/a
C-55 G 3％MXD6 280℃ 82.57 81.0 0.0354
56 G 3％Z 280℃ 2.09 90.8 0.0002
* apparent perviousness (mean values that 3 perviousness of 2 films of every kind of composition and each film are measured), be installed on the device after 15 days, under 23 ℃ and about 60～80% relative humidity, use air to measure as the upstream test gas.
Embodiment 59 and 62 and comparative example 57～58 and 60～61
The regrinding of multilayer film
By with the layer coextrusion of two 15mil polyester C around the layer of the MXD6/30wt%N6 blend " X " of thick MXD6 of 4mil or acid amides exchange, make multilayer film.It is known as " ABA " structure, and wherein " A " layer is that skin and " B " layer are internal layer.Using Killian 1 " forcing machine extrudes this skin by polyester C under 265 ℃ temperature.Using 0.75 " the Killian forcing machine extruding internal layer for MXD6 under 285 ℃ the temperature and for MXD6/30wt%N6 blend " X " under 275 ℃ temperature.In order to simulate these multilayer films, subsequently these multilayer films are ground and mix so that 50/50 ratio is dried with another polyester C pill as the utilization again of regrinding in single layer structure.To do subsequently mix thing 70 ℃ dry down and at Killian 1 " under 240 ℃ temperature, be extruded into the 20mil film on the forcing machine.Haze value is shown in the table 7.Co-extruded films all has the haze value less than 2%.But, these do not pulverize again and during with pure polyester " C " blend, this value that contains the film of C/MXD6 regrinding blend is increased to greater than 10%.This film that contains " C/X " regrinding keeps transparent.
In the same manner, by with the layer coextrusion of two 15mil polyester G around the layer of the MXD6/50wt%N6 blend " Z " of thick MXD6 of 5mil or acid amides exchange, make multilayer film.It is known as " ABA " structure, and wherein " A " layer is that skin and " B " layer are internal layer.Using Killian1 " forcing machine extrudes this skin by polyester G under 285 ℃ temperature.Using 0.75 " the Killian forcing machine extrudes the internal layer of MXD6 or MXD6/50wt%N6 blend " Z " under 285 ℃ temperature.In order to simulate these multilayer films, subsequently these multilayer films are ground and mix so that 50/50 ratio is dried with another polyester G pill as the utilization again of regrinding in single layer structure.To do subsequently mix thing 100 ℃ dry down and at Killian 1 " under 280 ℃ temperature, be extruded into the 20mil film on the forcing machine.Haze value is shown in the table 7.Co-extruded films all has the haze value less than 2.5%.But, these do not pulverize again and during with pure polyester " G " blend, this value that contains the film of G/MXD6 regrinding blend is increased to greater than 10%.This film that contains " G/Z " regrinding keeps transparent.
Table 7
30mil ABA co-extrusion film (4milB layer) The 20 mil single thin films of producing from the mixture of 50% " C " or " G " pill and 50% ground co-extrusion film
Embodiment Material Mist degree (%) Total light transmittance (%) Mist degree (%) Total light transmittance (%) RI (nylon)-RI (polyester)
C-57 C 0.12 91.5 0.09 91.5 n/a
C-58 C/MXD6/C 1.49 91.1 16.44 87.3 0.0231
59 C/X/C 0.62 91.2 0.37 91.5 0.0022
C-60 G 0.74 90.9 0.24 91.1 n/a
C-61 G/MXD6/G 2.15 91.1 87.34 82.5 0.0354
62 G/Z/G 0.74 90.9 1.88 90.6 0.0002
Embodiment 64 and comparative example 63
The stripping strength of multilayer film
By with the layer coextrusion of two 15mil polyester C around the layer of the MXD6/30wt%N6 blend " X " of thick MXD6 of 4mil or acid amides exchange, make the ABA film.The nylon 6 that uses in the blend of acid amides exchange among this embodiment is Zytel 7301.Using Killian 1 " forcing machine extrudes outside polyester C layer under 265 ℃ temperature.Using 0.75 " the Killian forcing machine squeezes under the temperature shown in the table 8 and extrudes internal layer.The MXD6/30wt%N6 blend " X " of acid amides exchange shows the stripping strength that is better than polyester C on MXD6.In addition, when the internal layer melt temperature when 280 ℃ are increased to 285 ℃, obtained the MXD6/30wt%N6 blend of acid amides exchange and the improvement stripping strength of polyester C.The MXD6 stripping strength does not show any temperature dependency.
Table 8
Embodiment Material " B " layer melt temperature Average stripping strength
C-63 C/MXD6/C 270℃ 280℃ 285℃ g/mm 1.74 1.7 1.88
64 C/X/C 270℃ 280℃ 285℃ 4.33 4.42 7.14

Claims (77)

1. polymer composition comprises following unmixing blend:
(i) first component comprises at least a polyester, and it comprises:
(a) diacid residues comprises based on the total diacid residue being the residue of the terephthalic acid of about 70～about 100mol%; At least a residue that has up to the modified aromatic dicarboxylic acid of 20 carbon atoms of 0～about 30mol%; At least a residue that has up to the modified aliphatic dicarboxylic acid of 16 carbon atoms with 0～about 10mol%; With
(b) diol residue comprises that based on the total diol residue be 2,2,4 of about 1～about 99mol%, 4-tetramethyl--1, the residue of 3-cyclobutanediol; Residue with the 1,4 cyclohexane dimethanol of about 1～about 99mol%; With
(ii) second component comprises blend homogeneous, the acid amides exchange of at least two kinds of polymeric amide;
Wherein, described second component is about 0.006～approximately-0.0006 with difference RI (second the component)-RI (first component) of the specific refractory power of described first component (i) (ii), and the percent transmittancy of described unmixing blend is at least 75%, and mist degree is 10% or lower.
2. the composition of claim 1, blend wherein said homogeneous, the acid amides exchange are to form by described at least two kinds of polymeric amide are contacted under about 290 ℃～about 340 ℃ temperature.
3. the composition of claim 1, it described second component that comprises described first component (i) of about 5～about 99wt% and about 95～about 1wt% (ii), based on the gross weight of described composition.
4. the composition of claim 3, it described second component that comprises described first component (i) of about 50～about 99wt% and about 50～about 1wt% (ii), based on the gross weight of described composition.
5. the composition of claim 4, it described second component that comprises described first component (i) of about 70～about 99wt% and about 30～about 1wt% (ii), based on the gross weight of described composition.
6. the composition of claim 1, wherein said second component are about 0.005～approximately-0.0006 with difference RI (second the component)-RI (first component) of the specific refractory power of described first component (i) (ii).
7. the composition of claim 1, wherein said modified aromatic dicarboxylic acid be selected from 4,4 '-diphenyl dicarboxylic acid, m-phthalic acid, 1,4-naphthalene dicarboxylic acids, 1,5-naphthalene dicarboxylic acids, 2,6-naphthalene dicarboxylic acids, 2,7-naphthalene dicarboxylic acids, 4,4 '-oxybenzoic acid and trans-4,4 '-the Stilbene dicarboxylic acid; And described modified aliphatic dicarboxylic acid is selected from propanedioic acid, succsinic acid, pentanedioic acid, hexanodioic acid, pimelic acid, suberic acid, nonane diacid and dodecanedioic acid.
8. the composition of claim 1, wherein said diol residue further comprises based on the residue of total diol residue for about 25mol% or at least a modification glycol still less, this modification glycol is selected from ethylene glycol, 1,2-propylene glycol, 1, ammediol, 1,4-butyleneglycol, 1,5-pentanediol, 1,6-hexylene glycol, p-Xylol glycol, neopentyl glycol, polyoxyethylene glycol, Diethylene Glycol and polytetramethylene glycol.
9. the composition of claim 1, wherein said polyester comprises that further based on total diacid or diol residue be the residue of at least a branching agent of about 0.01～1mol%, this branching agent is selected from trihemellitic acid, trihemellitic acid acid anhydride and pyromellitic acid dianhydride, glycerine, Sorbitol Powder, 1,2,6-hexanetriol, tetramethylolmethane, tartrate, citric acid, trimethylolethane and trimesic acid.
10. the composition of claim 1, wherein said diol residue comprises 2,2,4 of about 5～about 60mol%, 4-tetramethyl--1, the residue of the 1,4 cyclohexane dimethanol of the residue of 3-cyclobutanediol and about 40～about 95mol%.
11. the composition of claim 10, wherein said diol residue comprises 2,2,4 of about 15～about 40mol%, 4-tetramethyl--1, the residue of the 1,4 cyclohexane dimethanol of the residue of 3-cyclobutanediol and about 60～about 85mol%.
12. the composition of claim 11, wherein said diol residue comprises 2,2,4 of about 20～about 30mol%, 4-tetramethyl--1, the residue of the 1,4 cyclohexane dimethanol of the residue of 3-cyclobutanediol and about 70～about 80mol%.
13. the composition of claim 1, wherein said diacid residues comprises the terephthalic acid of about 100mol%.
14. the composition of claim 13, wherein said diol residue comprises 2,2,4 of about 5～about 60mol%, 4-tetramethyl--1, the residue of the 1,4 cyclohexane dimethanol of the residue of 3-cyclobutanediol and about 40～about 95mol%.
15. the composition of claim 14, wherein said diol residue comprises 2,2,4 of about 15～about 40mol%, 4-tetramethyl--1, the residue of the 1,4 cyclohexane dimethanol of the residue of 3-cyclobutanediol and about 60～about 85mol%.
16. the composition of claim 15, wherein said diol residue comprises 2,2,4 of about 20～about 30mol%, 4-tetramethyl--1, the residue of the 1,4 cyclohexane dimethanol of the residue of 3-cyclobutanediol and about 70～about 80mol%.
17. the composition of claim 1, wherein said first component further comprise the intimate blending thing of polycarbonate of described polyester and the residue that comprises dihydroxyphenyl propane.
18. the composition of claim 17, wherein said polyester and described polycarbonate are branching.
19. a polymer composition comprises following unmixing blend:
(i) first component comprises at least a polyester, and it comprises:
(a) diacid residues comprises based on the total diacid residue being the residue of the terephthalic acid of about 70～about 100mol%; At least a residue that has up to the modified aromatic dicarboxylic acid of 20 carbon atoms of 0～about 30mol%; At least a residue that has up to the modified aliphatic dicarboxylic acid of 16 carbon atoms with 0～about 10mol%; With
(b) diol residue comprises that based on the total diol residue be 2,2,4 of about 1～about 99mol%, 4-tetramethyl--1, the residue of 3-cyclobutanediol; Residue with the 1,4 cyclohexane dimethanol of about 1～about 99mol%; With
(ii) second component comprises copolyamide;
Wherein, described second component is about 0.006～approximately-0.0006 with difference RI (second the component)-RI (first component) of the specific refractory power of described first component (i) (ii), and the percent transmittancy of described unmixing blend is at least 75%, and mist degree is 10% or lower.
20. the composition of claim 19, wherein said copolyamide comprises the residue of m-xylenedimaine, para-xylene diamines or its combination; With at least a residues of monomers, this monomer is selected from terephthalic acid, m-phthalic acid, hexanodioic acid, pimelic acid, suberic acid, nonane diacid, sebacic acid, undecane diacid, dodecanedioic acid, hexanolactam, butyrolactam, 11-amino-undecane diacid and 1,6-hexamethylene-diamine.
21. the composition of claim 20, wherein said copolyamide comprise that the total diamines residue content based on 100mol% is the residue of the m-xylenedimaine of about 15～about 10mol%; With the total diacid residue content based on 100mol% be residue and one or more aliphatics of about 85～about 15mol% or the residue of cycloaliphatic diacid of the hexanodioic acid of about 15～about 85mol%, this diacid is selected from pimelic acid, suberic acid, nonane diacid, sebacic acid, undecane diacid, dodecanedioic acid.
22. the composition of claim 19, wherein said modified aromatic dicarboxylic acid be selected from 4,4 '-diphenyl dicarboxylic acid, m-phthalic acid, 1,4-naphthalene dicarboxylic acids, 1,5-naphthalene dicarboxylic acids, 2,6-naphthalene dicarboxylic acids, 2,7-naphthalene dicarboxylic acids, 4,4 '-oxybenzoic acid and trans-4,4 '-the Stilbene dicarboxylic acid; And described modified aliphatic dicarboxylic acid is selected from propanedioic acid, succsinic acid, pentanedioic acid, hexanodioic acid, pimelic acid, suberic acid, nonane diacid and dodecanedioic acid.
23. the composition of claim 19, wherein said diol residue further comprises based on the residue of total diol residue for about 25mol% or at least a modification glycol still less, this modification glycol is selected from ethylene glycol, 1,2-propylene glycol, 1, ammediol, 1,4-butyleneglycol, 1,5-pentanediol, 1,6-hexylene glycol, p-Xylol glycol, neopentyl glycol, polyoxyethylene glycol, Diethylene Glycol and polytetramethylene glycol.
24. the composition of claim 19, it comprises that further based on total diacid or diol residue be the residue of at least a branching agent of about 0.01～1mol%, this branching agent is selected from trihemellitic acid, trihemellitic acid acid anhydride and pyromellitic acid dianhydride, glycerine, Sorbitol Powder, 1,2,6-hexanetriol, tetramethylolmethane, tartrate, citric acid, trimethylolethane and trimesic acid.
25. the composition of claim 19, wherein said diol residue comprises 2,2,4 of about 5～about 60mol%, 4-tetramethyl--1, the residue of the 1,4 cyclohexane dimethanol of the residue of 3-cyclobutanediol and about 40～about 95mol%.
26. the composition of claim 25, wherein said diol residue comprises 2,2,4 of about 15～about 40mol%, 4-tetramethyl--1, the residue of the 1,4 cyclohexane dimethanol of the residue of 3-cyclobutanediol and about 60～about 85mol%.
27. the composition of claim 26, wherein said diol residue comprises 2,2,4 of about 20～about 30mol%, 4-tetramethyl--1, the residue of the 1,4 cyclohexane dimethanol of the residue of 3-cyclobutanediol and about 70～about 80mol%.
28. the composition of claim 19, wherein said diacid residues comprises the terephthalic acid of about 100mol%.
29. the composition of claim 28, wherein said diol residue comprises 2,2,4 of about 5～about 60mol%, 4-tetramethyl--1, the residue of the 1,4 cyclohexane dimethanol of the residue of 3-cyclobutanediol and about 40～about 95mol%.
30. the composition of claim 29, wherein said diol residue comprises 2,2,4 of about 15～about 40mol%, 4-tetramethyl--1, the residue of the 1,4 cyclohexane dimethanol of the residue of 3-cyclobutanediol and about 60～about 85mol%.
31. the composition of claim 30, wherein said diol residue comprises 2,2,4 of about 20～about 30mol%, 4-tetramethyl--1, the residue of the 1,4 cyclohexane dimethanol of the residue of 3-cyclobutanediol and about 70～about 80mol%.
32. the composition of claim 19, wherein said first component further comprise the intimate blending thing of polycarbonate of described polyester and the residue that comprises dihydroxyphenyl propane.
33. the composition of claim 32, wherein said polyester and described polycarbonate are branching.
34. the composition of claim 1, wherein said second component (ii) comprise the intimate blending thing of second polymeric amide of first polymeric amide that contains aromatic moieties and fatty family residue.
35. the composition of claim 34, wherein said intimate blending thing comprises first polymeric amide of the residue that contains m-xylenedimaine and hexanodioic acid, and described second polymeric amide comprises at least a aliphatics or cycloaliphatic residues of monomers, this monomer select oneself diacid, pimelic acid, suberic acid, nonane diacid, sebacic acid, undecane diacid, dodecanedioic acid, hexanolactam, butyrolactam, 11-amino-undecane diacid and 1, the 6-hexamethylene-diamine.
36. comprising, the composition of claim 35, wherein said second polymeric amide be selected from nylon 4, nylon 6, nylon 9, Ni Long11, nylon 12, nylon 6,6, nylon 5,10, nylon 6,12, at least a polymeric amide of nylon 6,11, nylon 10,12 and combination thereof.
37. the composition of claim 36, wherein said second polymeric amide comprises nylon 6, nylon 6,6 or its blend.
38. the composition of claim 37, wherein diol residue comprises 2,2,4 of about 5～about 60mol%, 4-tetramethyl--1, the residue of the 1,4 cyclohexane dimethanol of the residue of 3-cyclobutanediol and about 40～about 95mol%.
39. the composition of claim 38, wherein said diol residue comprises 2,2,4 of about 15～about 40mol%, 4-tetramethyl--1, the residue of the 1,4 cyclohexane dimethanol of the residue of 3-cyclobutanediol and about 60～about 85mol%.
40. the composition of claim 39, wherein said diol residue comprises 2,2,4 of about 20～about 30mol%, 4-tetramethyl--1, the residue of the 1,4 cyclohexane dimethanol of the residue of 3-cyclobutanediol and about 70～about 80mol%.
41. the composition of claim 37, wherein said diacid residues comprises the terephthalic acid of about 100mol%.
42. the composition of claim 41, wherein said diol residue comprises 2,2,4 of about 5～about 60mol%, 4-tetramethyl--1, the residue of the 1,4 cyclohexane dimethanol of the residue of 3-cyclobutanediol and about 40～about 95mol%.
43. the composition of claim 42, wherein said diol residue comprises 2,2,4 of about 15～about 40mol%, 4-tetramethyl--1, the residue of the 1,4 cyclohexane dimethanol of the residue of 3-cyclobutanediol and about 60～about 85mol%.
44. the composition of claim 43, wherein said diol residue comprises 2,2,4 of about 20～about 30mol%, 4-tetramethyl--1, the residue of the 1,4 cyclohexane dimethanol of the residue of 3-cyclobutanediol and about 70～about 80mol%.
45. the composition of claim 37, wherein said first component further comprise the intimate blending thing of polycarbonate of described polyester and the residue that comprises dihydroxyphenyl propane.
46. the composition of claim 45, wherein said polyester and described polycarbonate are branching.
47. the composition of claim 46, wherein said polyester comprises that further based on total diacid or diol residue be the residue of at least a branching agent of about 0.01～1mol%, this branching agent is selected from trihemellitic acid, trihemellitic acid acid anhydride and pyromellitic acid dianhydride, glycerine, Sorbitol Powder, 1,2,6-hexanetriol, tetramethylolmethane, tartrate, citric acid, trimethylolethane and trimesic acid.
48. the composition of claim 45, wherein said diol residue comprises 2,2,4 of about 5～about 60mol%, 4-tetramethyl--1, the residue of the 1,4 cyclohexane dimethanol of the residue of 3-cyclobutanediol and about 40～about 95mol%.
49. the composition of claim 48, wherein said diol residue comprises 2,2,4 of about 15～about 40mol%, 4-tetramethyl--1, the residue of the 1,4 cyclohexane dimethanol of the residue of 3-cyclobutanediol and about 60～about 85mol%.
50. the composition of claim 49, wherein said diol residue comprises 2,2,4 of about 20～about 30mol%, 4-tetramethyl--1, the residue of the 1,4 cyclohexane dimethanol of the residue of 3-cyclobutanediol and about 70～about 80mol%.
51. the composition of claim 45, wherein said diacid residues comprises the terephthalic acid of about 100mol%.
52. the composition of claim 51, wherein said diol residue comprises 2,2,4 of about 5～about 60mol%, 4-tetramethyl--1, the residue of the 1,4 cyclohexane dimethanol of the residue of 3-cyclobutanediol and about 40～about 95mol%.
53. the composition of claim 52, wherein said diol residue comprises 2,2,4 of about 15～about 40mol%, 4-tetramethyl--1, the residue of the 1,4 cyclohexane dimethanol of the residue of 3-cyclobutanediol and about 60～about 85mol%.
54. the composition of claim 53, wherein said diol residue comprises 2,2,4 of about 20～about 30mol%, 4-tetramethyl--1, the residue of the 1,4 cyclohexane dimethanol of the residue of 3-cyclobutanediol and about 70～about 80mol%.
55. comprise the moulded products of each composition in the claim 1,11,15,17,19,30,36,43 or 53.
56. the moulded products of claim 55, its by extrude, calendering, thermoforming, blowing, extrusion-blown modling, injection moulding, compression moulding, casting, drawing-off, tentering or blowing form.
57. the moulded products of claim 56, it is sheet material, film, pipe, prefabrication or bottle.
58. the moulded products of claim 57, it is a bottle.
59. the moulded products of claim 57, it has 2～7 layers.
60. a polymer composition, it is by comprising that the following method of melt blending makes:
(i) first component comprises at least a polyester, and it comprises:
(a) diacid residues comprises based on the total diacid residue being the residue of the terephthalic acid of about 70～about 100mol%; At least a residue that has up to the modified aromatic dicarboxylic acid of 20 carbon atoms of 0～about 30mol%; At least a residue that has up to the modified aliphatic dicarboxylic acid of 16 carbon atoms with 0～about 10mol%; With
(b) diol residue comprises that based on the total diol residue be 2,2,4 of about 1～about 99mol%, 4-tetramethyl--1, the residue of 3-cyclobutanediol; Residue with the 1,4 cyclohexane dimethanol of about 1～about 99mol%; With
(ii) second component comprises blend homogeneous, the acid amides exchange of at least two kinds of polymeric amide;
Wherein, described second component is about 0.006～approximately-0.0006 with difference RI (second the component)-RI (first component) of the specific refractory power of described first component (i) (ii), and the percent transmittancy of described unmixing blend is at least 75%, and mist degree is 10% or lower.
61. the composition of claim 60, wherein said melt blending are under about 290 ℃～about 340 ℃.
62. the composition of claim 60, wherein said polyester comprises that further based on total diacid or diol residue be the residue of at least a branching agent of about 0.01～1mol%, this branching agent is selected from trihemellitic acid, trihemellitic acid acid anhydride and pyromellitic acid dianhydride, glycerine, Sorbitol Powder, 1,2,6-hexanetriol, tetramethylolmethane, tartrate, citric acid, trimethylolethane and trimesic acid.
63. the composition of claim 60, wherein said diol residue comprises 2,2,4 of about 5～about 60mol%, 4-tetramethyl--1, the residue of the 1,4 cyclohexane dimethanol of the residue of 3-cyclobutanediol and about 40～about 95mol%.
64. the composition of claim 63, wherein said diol residue comprises 2,2,4 of about 15～about 40mol%, 4-tetramethyl--1, the residue of the 1,4 cyclohexane dimethanol of the residue of 3-cyclobutanediol and about 60～about 85mol%.
65. the composition of claim 64, wherein said diol residue comprises 2,2,4 of about 20～about 30mol%, 4-tetramethyl--1, the residue of the 1,4 cyclohexane dimethanol of the residue of 3-cyclobutanediol and about 70～about 80mol%.
66. the composition of claim 60, wherein said diacid residues comprises the terephthalic acid of about 100mol%.
67. the composition of claim 66, wherein said diol residue comprises 2,2,4 of about 5～about 60mol%, 4-tetramethyl--1, the residue of the 1,4 cyclohexane dimethanol of the residue of 3-cyclobutanediol and about 40～about 95mol%.
68. the composition of claim 67, wherein said diol residue comprises 2,2,4 of about 15～about 40mol%, 4-tetramethyl--1, the residue of the 1,4 cyclohexane dimethanol of the residue of 3-cyclobutanediol and about 60～about 85mol%.
69. the composition of claim 68, wherein said diol residue comprises 2,2,4 of about 20～about 30mol%, 4-tetramethyl--1, the residue of the 1,4 cyclohexane dimethanol of the residue of 3-cyclobutanediol and about 70～about 80mol%.
70. the composition of claim 60, wherein said first component further comprise the intimate blending thing of polycarbonate of described polyester and the residue that comprises dihydroxyphenyl propane.
71. the composition of claim 70, wherein said polyester and described polycarbonate are branching.
72. a method for preparing transparent, oxygen-scavenging compositions comprises:
(A) selection comprises first component of at least a polyester, and it comprises:
(a) diacid residues comprises based on the total diacid residue being the residue of the terephthalic acid of about 70～about 100mol%; At least a residue that has up to the modified aromatic dicarboxylic acid of 20 carbon atoms of 0～about 30mol%; At least a residue that has up to the modified aliphatic dicarboxylic acid of 16 carbon atoms with 0～about 10mol%; With
(b) diol residue comprises that based on the total diol residue be 2,2,4 of about 1～about 99mol%, 4-tetramethyl--1, the residue of 3-cyclobutanediol; Residue with the 1,4 cyclohexane dimethanol of about 1～about 99mol%;
(B) specific refractory power (RI) of described first component of measurement;
(C) provide second component, it comprises:
(i) have the copolyamide of the mol ratio of aliphatics and aromatic moieties, wherein select the mol ratio of described aliphatics and aromatic moieties, make second component that specific refractory power satisfies following formula thus:
0.006 〉=RI (second component)-RI (first component) 〉=-0.0006; Perhaps
The blend (ii) homogeneous of first and second polymeric amide, the acid amides exchange, at least a described polymeric amide has aromatic moieties, wherein selects the weight percent of described first and second polymeric amide, makes second component that specific refractory power satisfies following formula thus:
0.006 〉=RI (second component)-RI (first component) 〉=-0.0006,
Wherein RI represents the described specific refractory power of described first and second components; With
(D) described first and second components of melt blending, make thus percent transmittancy at least 75% and mist degree be 10% or lower unmixing blend.
73. a method for preparing transparent, oxygen-scavenging compositions comprises:
(A) select second component, it comprises:
(i) has the copolyamide of the mol ratio of aliphatics and aromatic moieties; Perhaps
The blend (ii) homogeneous of first and second polymeric amide, the acid amides exchange, at least a described polymeric amide has aromatic moieties;
(B) specific refractory power of described second component of measurement;
(C) selection comprises first component of at least a polyester, and it comprises:
(a) diacid residues comprises based on the total diacid residue being the residue of the terephthalic acid of about 70～about 100mol%; At least a residue that has up to the modified aromatic dicarboxylic acid of 20 carbon atoms of 0～about 30mol%; At least a residue that has up to the modified aliphatic dicarboxylic acid of 16 carbon atoms with 0～about 10mol%; With
(b) diol residue comprises that based on the total diol residue be 2,2,4 of about 1～about 99mol%, 4-tetramethyl--1, the residue of 3-cyclobutanediol; Residue with the 1,4 cyclohexane dimethanol of about 1～about 99mol%;
Wherein, select described polyester, make first component that specific refractory power satisfies following formula:
0.006 〉=RI (second component)-RI (first component) 〉=-0.0006,
Wherein RI is a specific refractory power; With
(D) described first and second components of melt blending, make thus percent transmittancy at least 75% and mist degree be 10% or lower unmixing blend.
74. each composition in the claim 1,11,15,17,19,30,36,43 or 53, the logarithmic viscosity number of wherein said polyester is 0.5～0.75dL/g.
75. the composition of claim 74, wherein said logarithmic viscosity number are 0.6～0.72dL/g.
76. each composition in the claim 1,11,15,17,19,30,36,43 or 53, the second-order transition temperature of wherein said polyester are about 110 ℃～about 150 ℃.
77. the composition of claim 76, wherein said second-order transition temperature are about 120 ℃～about 135 ℃.
CNA2006800205594A 2005-06-17 2006-03-30 Transparent polymer blends containing polyesters comprising a cyclobutanediol and articles prepared therefrom Pending CN101193978A (en)

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US69156705P 2005-06-17 2005-06-17
US60/691,567 2005-06-17
US60/731,454 2005-10-28
US60/731,389 2005-10-28
US60/739,058 2005-11-22
US60/738,869 2005-11-22
US60/750,693 2005-12-15
US60/750,547 2005-12-15
US60/750,692 2005-12-15
US60/750,682 2005-12-15
US11/363,481 2006-02-27
US11/363,374 2006-02-27
US11/363,417 2006-02-27
US11/363,418 2006-02-27
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CNA2006800205823A Pending CN101193733A (en) 2005-06-17 2006-03-30 Transparent, multilayered article containing polyesters comprising a cyclobutanediol and its preparing method
CNA2006800205838A Pending CN101193945A (en) 2005-06-17 2006-03-30 LCD films or sheets comprising polyester compositions formed from 2,2,4,4-tetramethyl-1,3-cyclobutanediol and 1,4-cyclohexanedimethanol
CNA2006800205397A Pending CN101193934A (en) 2005-06-17 2006-03-30 Container comprising polyester compositions which comprise cyclobutanediol
CNA2006800205448A Pending CN101203542A (en) 2005-06-17 2006-03-30 Optical mediam comprising polyester compositions formed from 2,2,4,4-tetramethyl-1,3-cyclobutanediol and 1,4-cyclohexanedimethanol
CNA2006800205518A Pending CN101193941A (en) 2005-06-17 2006-03-30 Glass laminates comprising polyester compositions formed from 2,2,4,4-tetramethyl-1,3-cyclobutanediol and 1,4-cyclohexanedimethanol
CNA2006800206489A Pending CN101213239A (en) 2005-06-17 2006-03-30 Thermoformed sheet(s) comprising polyester compositions which comprise cyclobutanediol
CN200680020542.9A Active CN101193936B (en) 2005-06-17 2006-03-30 Polyester compositions comprising a cyclobutanediol and articles prepared therefrom
CNA2006800205804A Pending CN101193668A (en) 2005-06-17 2006-03-30 Dialysis filter shell comprising polyester compositions formed from 2,2,4,4-tetramethyl-1,3-cyclobutanediol and 1,4-cyclohexanedimethanol
CN200680020540XA Active CN101193935B (en) 2005-06-17 2006-03-30 Feeder comprising polyester compositions which comprise cyclobutanediol
CN2006800205626A Active CN101193943B (en) 2005-06-17 2006-03-30 Film(s) and/or sheet(s) comprising polyester compositions which comprise cyclobutanediol and have a certain combination of inherent viscosity and moderate glass transition temperature
CNA2006800205594A Pending CN101193978A (en) 2005-06-17 2006-03-30 Transparent polymer blends containing polyesters comprising a cyclobutanediol and articles prepared therefrom
CNA2006800205819A Pending CN101193944A (en) 2005-06-17 2006-03-30 Anti-protein articles comprising cyclobutanediol
CNA200680020572XA Pending CN101193721A (en) 2005-06-17 2006-03-30 Preparation of transparent, shaped articles containing polyesters comprising a cyclobutanediol
CN2006800206544A Active CN101203543B (en) 2005-06-17 2006-03-30 Polyester compositions which comprise cyclobutanediol having certain cis/trans ratios
CNA2006800205895A Pending CN101193980A (en) 2005-06-17 2006-03-30 Methods for preparing transparent formed articles comprising polymer containing a cyclobutanediol
CNA2006800205236A Pending CN101193977A (en) 2005-06-17 2006-03-30 Intravenous components comprising polyester compositions formed from 2,2,4,4-tetramethyl-1,3-cyclobutanediol and 1,4-cyclohexanedimethanol
CNA2006800205452A Pending CN101193938A (en) 2005-06-17 2006-03-30 Polyester compositions containing high amounts of cyclobutanediol and articles made therefrom
CN2006800205611A Active CN101193932B (en) 2005-06-17 2006-03-30 Polyester compositions which comprise cyclobutanediol and have a certain combination of inherent viscosity and moderate glass transition temperature and articles made therefrom
CN2006800205378A Active CN101193933B (en) 2005-06-17 2006-03-30 Film(s) and/or sheet(s) comprising polyester compositions which comprise cyclobutanediol and have a certain combination of inherent viscosity and moderate glass transition temperature
CNA2006800207458A Pending CN101193946A (en) 2005-06-17 2006-03-30 Film(s) and/or sheet(s) comprising polyester compositions which comprise cyclobutanediol
CN2006800205058A Active CN101203541B (en) 2005-06-17 2006-03-30 Polyester compositions which comprise cyclobutanediol and have a certain combination of inherent viscosity and high glass transition temperature and product made therefrom
CN2006800207443A Active CN101203544B (en) 2005-06-17 2006-03-30 Thermoplastic articles comprising cyclobutanediol having a decorative material embedded therein
CNA2006800205700A Pending CN101193979A (en) 2005-06-17 2006-03-30 Transparent deoxidizing compositions comprising polymer containing a cyclobutanediol and articles prepared therefrom
CN2006800205433A Active CN101193937B (en) 2005-06-17 2006-03-30 Bottle comprising polyester compositions which comprise cyclobutanediol
CN2006800205607A Active CN101193942B (en) 2005-06-17 2006-03-30 Film(s) and/or sheet(s) comprising polyester compositions which comprise cyclobutanediol and articles made therefrom
CNA2006800205490A Pending CN101193940A (en) 2005-06-17 2006-03-30 Outdoor signs comprising polyester compositions formed from 2,2,4,4-tetramethyl-1,3-cyclobutanediol and 1,4-cyclohexanedimethanol
CNA2006800205255A Pending CN101203540A (en) 2005-06-17 2006-03-30 Eye device comprising polyester compositions formed from 2,2,4,4-tetramethyl-1,3- cyclobutanediol and 1,4-cyclohexanedimethanol
CNA2006800205467A Pending CN101193939A (en) 2005-06-17 2006-03-30 Polyester compositions containing cyclobutanediol and articles made therefrom

Family Applications Before (10)

Application Number Title Priority Date Filing Date
CNA2006800205823A Pending CN101193733A (en) 2005-06-17 2006-03-30 Transparent, multilayered article containing polyesters comprising a cyclobutanediol and its preparing method
CNA2006800205838A Pending CN101193945A (en) 2005-06-17 2006-03-30 LCD films or sheets comprising polyester compositions formed from 2,2,4,4-tetramethyl-1,3-cyclobutanediol and 1,4-cyclohexanedimethanol
CNA2006800205397A Pending CN101193934A (en) 2005-06-17 2006-03-30 Container comprising polyester compositions which comprise cyclobutanediol
CNA2006800205448A Pending CN101203542A (en) 2005-06-17 2006-03-30 Optical mediam comprising polyester compositions formed from 2,2,4,4-tetramethyl-1,3-cyclobutanediol and 1,4-cyclohexanedimethanol
CNA2006800205518A Pending CN101193941A (en) 2005-06-17 2006-03-30 Glass laminates comprising polyester compositions formed from 2,2,4,4-tetramethyl-1,3-cyclobutanediol and 1,4-cyclohexanedimethanol
CNA2006800206489A Pending CN101213239A (en) 2005-06-17 2006-03-30 Thermoformed sheet(s) comprising polyester compositions which comprise cyclobutanediol
CN200680020542.9A Active CN101193936B (en) 2005-06-17 2006-03-30 Polyester compositions comprising a cyclobutanediol and articles prepared therefrom
CNA2006800205804A Pending CN101193668A (en) 2005-06-17 2006-03-30 Dialysis filter shell comprising polyester compositions formed from 2,2,4,4-tetramethyl-1,3-cyclobutanediol and 1,4-cyclohexanedimethanol
CN200680020540XA Active CN101193935B (en) 2005-06-17 2006-03-30 Feeder comprising polyester compositions which comprise cyclobutanediol
CN2006800205626A Active CN101193943B (en) 2005-06-17 2006-03-30 Film(s) and/or sheet(s) comprising polyester compositions which comprise cyclobutanediol and have a certain combination of inherent viscosity and moderate glass transition temperature

Family Applications After (17)

Application Number Title Priority Date Filing Date
CNA2006800205819A Pending CN101193944A (en) 2005-06-17 2006-03-30 Anti-protein articles comprising cyclobutanediol
CNA200680020572XA Pending CN101193721A (en) 2005-06-17 2006-03-30 Preparation of transparent, shaped articles containing polyesters comprising a cyclobutanediol
CN2006800206544A Active CN101203543B (en) 2005-06-17 2006-03-30 Polyester compositions which comprise cyclobutanediol having certain cis/trans ratios
CNA2006800205895A Pending CN101193980A (en) 2005-06-17 2006-03-30 Methods for preparing transparent formed articles comprising polymer containing a cyclobutanediol
CNA2006800205236A Pending CN101193977A (en) 2005-06-17 2006-03-30 Intravenous components comprising polyester compositions formed from 2,2,4,4-tetramethyl-1,3-cyclobutanediol and 1,4-cyclohexanedimethanol
CNA2006800205452A Pending CN101193938A (en) 2005-06-17 2006-03-30 Polyester compositions containing high amounts of cyclobutanediol and articles made therefrom
CN2006800205611A Active CN101193932B (en) 2005-06-17 2006-03-30 Polyester compositions which comprise cyclobutanediol and have a certain combination of inherent viscosity and moderate glass transition temperature and articles made therefrom
CN2006800205378A Active CN101193933B (en) 2005-06-17 2006-03-30 Film(s) and/or sheet(s) comprising polyester compositions which comprise cyclobutanediol and have a certain combination of inherent viscosity and moderate glass transition temperature
CNA2006800207458A Pending CN101193946A (en) 2005-06-17 2006-03-30 Film(s) and/or sheet(s) comprising polyester compositions which comprise cyclobutanediol
CN2006800205058A Active CN101203541B (en) 2005-06-17 2006-03-30 Polyester compositions which comprise cyclobutanediol and have a certain combination of inherent viscosity and high glass transition temperature and product made therefrom
CN2006800207443A Active CN101203544B (en) 2005-06-17 2006-03-30 Thermoplastic articles comprising cyclobutanediol having a decorative material embedded therein
CNA2006800205700A Pending CN101193979A (en) 2005-06-17 2006-03-30 Transparent deoxidizing compositions comprising polymer containing a cyclobutanediol and articles prepared therefrom
CN2006800205433A Active CN101193937B (en) 2005-06-17 2006-03-30 Bottle comprising polyester compositions which comprise cyclobutanediol
CN2006800205607A Active CN101193942B (en) 2005-06-17 2006-03-30 Film(s) and/or sheet(s) comprising polyester compositions which comprise cyclobutanediol and articles made therefrom
CNA2006800205490A Pending CN101193940A (en) 2005-06-17 2006-03-30 Outdoor signs comprising polyester compositions formed from 2,2,4,4-tetramethyl-1,3-cyclobutanediol and 1,4-cyclohexanedimethanol
CNA2006800205255A Pending CN101203540A (en) 2005-06-17 2006-03-30 Eye device comprising polyester compositions formed from 2,2,4,4-tetramethyl-1,3- cyclobutanediol and 1,4-cyclohexanedimethanol
CNA2006800205467A Pending CN101193939A (en) 2005-06-17 2006-03-30 Polyester compositions containing cyclobutanediol and articles made therefrom

Country Status (1)

Country Link
CN (28) CN101193733A (en)

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CN106189118A (en) * 2016-08-11 2016-12-07 苏州柯创电子材料有限公司 There is insulation film and the manufacture method thereof of vapor water barriers function
CN106220834A (en) * 2016-08-11 2016-12-14 苏州柯创电子材料有限公司 It is applicable to insulation film and the manufacture method thereof of high steam environment
CN114423803A (en) * 2019-07-29 2022-04-29 伊士曼化工公司 Process for preparing polyesters with recycled monomers from pyrolysis and methanolysis

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CN104769037B (en) * 2012-10-15 2018-10-23 旭化成株式会社 Thermoplastic resin composition and its formed body
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CN106220834A (en) * 2016-08-11 2016-12-14 苏州柯创电子材料有限公司 It is applicable to insulation film and the manufacture method thereof of high steam environment
CN114423803A (en) * 2019-07-29 2022-04-29 伊士曼化工公司 Process for preparing polyesters with recycled monomers from pyrolysis and methanolysis

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CN101203543B (en) 2012-02-01
CN101193940A (en) 2008-06-04
CN101193932B (en) 2012-08-08
CN101193939A (en) 2008-06-04
CN101193935B (en) 2013-01-02
CN101193946A (en) 2008-06-04
CN101203544A (en) 2008-06-18
CN101193938A (en) 2008-06-04
CN101193932A (en) 2008-06-04
CN101193937A (en) 2008-06-04
CN101193668A (en) 2008-06-04
CN101193721A (en) 2008-06-04
CN101203543A (en) 2008-06-18
CN101193942A (en) 2008-06-04
CN101193980A (en) 2008-06-04
CN101193979A (en) 2008-06-04
CN101193936B (en) 2014-04-23
CN101193944A (en) 2008-06-04
CN101213239A (en) 2008-07-02
CN101193936A (en) 2008-06-04
CN101193942B (en) 2012-09-05
CN101203540A (en) 2008-06-18
CN101193934A (en) 2008-06-04
CN101193933B (en) 2012-07-04
CN101193935A (en) 2008-06-04
CN101193945A (en) 2008-06-04
CN101193941A (en) 2008-06-04
CN101203541B (en) 2012-10-10
CN101193937B (en) 2012-04-25
CN101193977A (en) 2008-06-04
CN101203544B (en) 2013-07-17
CN101203542A (en) 2008-06-18
CN101193733A (en) 2008-06-04
CN101193943B (en) 2012-09-05
CN101193933A (en) 2008-06-04
CN101203541A (en) 2008-06-18
CN101193943A (en) 2008-06-04

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