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Небесная энциклопедия

Космические корабли и станции, автоматические КА и методы их проектирования, бортовые комплексы управления, системы и средства жизнеобеспечения, особенности технологии производства ракетно-космических систем

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Мониторинг СМИ

Мониторинг СМИ и социальных сетей. Сканирование интернета, новостных сайтов, специализированных контентных площадок на базе мессенджеров. Гибкие настройки фильтров и первоначальных источников.

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Поддерживает ввод нескольких поисковых фраз (по одной на строку). При поиске обеспечивает поддержку морфологии русского и английского языка
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Применить Всего найдено 4032. Отображено 100.
12-01-2012 дата публикации

Process for making thermoplastic polyesters

Номер: US20120010382A1
Автор: Zahir Bashir
Принадлежит: Saudi Basic Industries Corp

The invention relates to a process for making a thermoplastic polyester, which comprises contacting at least one carboxylic acid-based compound and at least one alcohol-based compound in esterification and subsequent polycondensation reactions, in the presence of certain exfoliated inorganic nano-layered titanates acting as a catalyst.

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26-04-2012 дата публикации

Catalytic systems for immortal ring-opening polymerisation of cyclic esters and cyclic carbonates

Номер: US20120101233A1
Принадлежит: Total Petrochemicals Research Feluy SA

The present invention discloses new catalyst systems based on complexes of divalent metals supported by chelating phenoxy ligands for immortal ring-opening polymerisation of cyclic esters and cyclic carbonates.

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21-06-2012 дата публикации

Color in Titanium Catalyzed Polyesters

Номер: US20120157619A1
Принадлежит: Eastman Chemical Co

Described as one aspect of the invention are polyesters comprising (a) a dicarboxylic acid component comprising: (i) 70 to 100 mole % of terephthalic acid residues; (ii) 0 to 30 mole % of aromatic dicarboxylic acid residues having up to 20 carbon atoms; and (iii) 0 to 10 mole % of aliphatic dicarboxylic acid residues having up to 16 carbon atoms; and (b) a glycol component comprising: (i) about 10 to about 90 mole % of ethylene glycol residues; and (ii) about 90 to about 10 mole % of cyclohexanedimethanol residues; (II) residues of at least one titanium compound; and (III) at least one chelating phosphorus species, reaction products thereof, or mixtures thereof, represented by the structure: wherein: n=an integer from 1 to 4; R can be hydrogen or C 1 -C 22 -alkyl; and R1 and R2 each can be hydrogen, C 1 -C 22 -alkyl, hydroxyl, or aryl; wherein the total mole % of the dicarboxylic acid component is 100 mole %, wherein the total mole % of the glycol component is 100 mole %; and wherein the inherent viscosity of the polyester is from 0.35 to 1.2 dL/g as determined in 60/40 (wt/wt) phenol/tetrachloroethane at a concentration of 0.25 g/50 ml at 25° C.

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06-12-2012 дата публикации

Toner and toner binder

Номер: US20120308926A1
Автор: Takashi Ono, Yoko Sakurai
Принадлежит: Sanyo Chemical Industries Ltd

A polyester resin toner binder which gives a toner with good anti-blocking property at high temperature and high humidity and good low-temperature fixing ability. The present invention is directed to a toner binder for developing electrostatic charge images, which binder comprises a condensation-polymerization polyester resin, the polyester resin being a product formed in the presence of a catalyst (a) represented by the following general formula (I): Ti(—X) m (—OR) n   (I) wherein R, X, m and n are as defined herein.

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07-02-2013 дата публикации

Solid State Polymerization Process for Polyester with Phosphinic Acid Compounds

Номер: US20130035451A1
Принадлежит: BASF SE

Disclosed are phosphinic acid compounds of formula I, II or III where R 1 and R 1 ′ are for instance straight or branched C 1 -C 50 alkyl, R 2 is for instance straight or branched C 22 -C 50 alkyl, R 3 and R 3 ′ are for instance straight or branched C 1 -C 50 alkyl, R 4 is for instance straight or branched C 1 -C 50 alkylene and m is from 2 to 100. Also disclosed are polyester compositions comprising the compounds of formula I, II and III.

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21-02-2013 дата публикации

Method of preparing a polymer and compositions therefor

Номер: US20130046066A1
Принадлежит: JOHNSON MATTHEY PLC

The invention provides a method of making a polymer in the presence of a catalyst composition having an empirical formula M(glycerol) a (X) b , where M represents a metal atom selected from titanium, zirconium, hafnium or aluminium, X is a ligand derived from acetylacetone or a peroxo ion; a is a number between 1 and 2.5; b is a number in the range from 1 to 2. Reactive compositions containing the catalyst composition are also described.

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28-02-2013 дата публикации

Method for the preparation of (polybutylene-co-adipate terephthalate) through the in situ phosphorus containing titanium based catalyst

Номер: US20130053461A1
Принадлежит: SABIC INNOVATIVE PLASTICS IP BV

Biodegradable compositions containing an aliphatic-aromatic copolyester derived from aromatic polyesters. Methods of making the compositions through an in situ phosphorus containing titanium based catalyst and articles made from the compositions.

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28-03-2013 дата публикации

METHOD FOR THE PREPARATION OF (POLYBUTYLENE-CO-ADIPATE TEREPHTHALATE) THROUGH THE IN SITU PHOSPHORUS CONTAINING TITANIUM BASED CATALYST

Номер: US20130079458A1
Принадлежит: SAUDI BASIC INDUSTRIES CORPORATION

Biodegradable compositions containing an aliphatic-aromatic copolyester derived from aromatic polyesters. Methods of making the compositions through an in situ phosphorus containing titanium based catalyst and articles made from the compositions. 1. An aliphatic-aromatic copolyester , comprising:(a) a dihydric alcohol group selected from an ethylene glycol group, 1,2-propylene glycol group, 1,3-propylene glycol group, 1,2-butanediol group, 2,3-butanediol group, 1,4-butanediol group, tetramethyl cyclobutanediol, isosorbide groups, 1,3-cyclohexanedimethanol groups, 1,4-cyclohexanedimethanol groups, hexylene glycol groups, bio-derived diol groups, and combinations thereof;(b) an aromatic dicarboxylic acid group derived from a depolymerized aromatic polyester component selected from poly(ethylene terephthalate)s, poly(butylene terephthalate)s, poly(trimethylene terephthalate)s, and combinations thereof,(c) a titanium catalyst composition comprising titanium and a color-reducing amount of a compound selected from phosphorus-containing compounds, nitrogen-containing compounds, boron-containing compounds, and combinations thereof;(d) an adipic acid group; and(e) an aromatic polyester residue selected from an isophthalic acid group, antimony-containing compounds, germanium-containing compounds, cobalt-containing compounds, tin, tin-containing compounds, titanium, titanium-containing compounds, aluminum, aluminum salts, alkaline salts, alkaline earth metal salts, phosphorus-containing compounds, sulfur-containing compounds, naphthalene dicarboxylic acid groups, epoxies, and combinations thereof,wherein the aliphatic-aromatic copolyester has a number average molecular weight of at least 20,000 Daltons and a polydispersity index from 2 to less than 6.2. The copolyester of claim 1 , wherein the dihydric alcohol group is selected from a 1 claim 1 ,4-butanediol group claim 1 , 1 claim 1 ,3-propanediol group claim 1 , ethylene glycol group claim 1 , or combinations thereof.3. The ...

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11-04-2013 дата публикации

POLYLACTIDE RESIN HAVING EXCELLENT HEAT RESISTANCE AND PREPARATION METHOD THEREOF

Номер: US20130090451A1
Принадлежит: LG CHEM, LTD.

The present invention relates to a polylactide resin having excellent heat resistance, a preparation method thereof, and a polylactide resin composition including the same. 1. A polylactide resin havinga weight average molecular weight of 100,000˜1,000,000,a content of lactide monomers generated after heat treatment at 220° C. for 1 hour in an amount of less than 0.5% by weight, anda yellow index of 30 or less.2. The polylactide resin according to claim 1 , wherein a reduction rate of weight average molecular weight after heat treatment at 220° C. for 40 minutes is −2500 g/mol·hr or less.3. The polylactide resin according to claim 2 , wherein a mass-loss rate constant k of the resin claim 2 , calculated by the following Equation 1 claim 2 , is 10 hror less claim 2 , when being isothermally heated at 260° C. for 30 minutes according to thermal gravimetric analysis (TGA):{'br': None, 'i': m', 't', 'm', 'o', 'kt, '()=()−\u2003\u2003[Equation 1]'}wherein m(o) represents the mass of the initial polylactide resin, m(t) represents the mass of the polylactide resin at the isothermal heating time (t), t represents time, and k represent a rate constant.4. The polylactide resin according to claim 1 , having an acidity of 20 meqKOH or less.5. The polylactide resin according to claim 1 , wherein the polylactide resin includes the catalyst-derived Sn metal residue in an amount of 15 ppm or less claim 1 , based on the total weight of the polylactide resin.7. A preparation method of the polylactide resin of claim 1 , comprising the step ofcarrying out ring opening polymerization with lactide monomers in the presence of an organometallic complex catalyst of the following Chemical Formula 1, {'chemistry': {'@id': 'CHEM-US-00011', '@num': '00011', 'img': {'@id': 'EMI-C00011', '@he': '14.48mm', '@wi': '69.85mm', '@file': 'US20130090451A1-20130411-C00011.TIF', '@alt': 'embedded image', '@img-content': 'chem', '@img-format': 'tif'}}, 'br': None, 'Catalytic activity=kg(polymer)/g(cat)·hr\ ...

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18-07-2013 дата публикации

Catalyst system and process for preparing of polyester resins, fibre, filaments and yarn using said catalyst system

Номер: US20130184414A1
Принадлежит: Reliance Industries Ltd

The present invention relates to a process for preparation of polyester resin in the presence of a novel catalyst system comprising an antimony compound and inorganic tin compound. The present invention also relates to a catalyst system for the preparation of polyester comprising an antimony compound and inorganic tin compound which reduces the polymerization time at all stages of polyester synthesis and reduces the generation of degradation product. This invention further relates to polyester resin with improved L color having significant importance in end-use applications.

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15-08-2013 дата публикации

PROCESS FOR THE PREPARATION OF POLYETHERESTER POLYOLS

Номер: US20130211041A1
Принадлежит: BASF SE

Disclosed is a process for the preparation of polyetherester polyols prepared with hybrid catalysts, the polyether esters obtained from the process and the use of such materials in polyurethane applications. The hybrid catalysts used in this invention comprise double metal cyanide complex catalysts (DMC) and at least one co-catalyst. 2. The process according to claim 1 , wherein X is C═O.5. The process according to claim 1 , wherein X is CR1R2.6. The process according to claim 5 , wherein R1 and R2 are each hydrogen claim 5 , and Y is —(CR3R4)m- claim 5 ,wherein m is 3 or 5, andR3 and R4 are each hydrogen.7. (canceled)8. The process according to claim 1 , wherein the co-catalyst is a compound catalyzing an esterification reaction claim 1 , a compound catalyzing a transesterification reaction claim 1 , or both.9. (canceled)10. The process according to claim 1 , wherein the co-catalyst is a titanium alkoxide.11. The process according to claim 1 , wherein the double metal cyanide complex catalyst is present in an amount of from 5 to 2000 ppm claim 1 , and the co-catalyst is present in an amount of from 1 to 1000 ppm claim 1 , each with respect to a total mass of the polyetherester polyol.1215-. (canceled)16. The process according to claim 1 , wherein the double metal cyanide complex catalyst comprises at least one selected from the group consisting of Co—Zn claim 1 , Fe—Zn claim 1 , and Ni—Zn.17. The process according to claim 16 , wherein the double metal cyanide complex catalyst comprises Co—Zn having formula Zn[Co(CN)].18. The process according to claim 11 , wherein the double metal cyanide complex catalyst is present in an amount of from 20 to 250 ppm claim 11 , and the co-catalyst is present in an amount of from 1 to 100 ppm.19. The process according to claim 11 , wherein the double metal cyanide complex catalyst is present in an amount of from 50 to 150 ppm claim 11 , and the co-catalyst is present in an amount of from 1 to 60 ppm.20. The process according to ...

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19-09-2013 дата публикации

POLYESTER POLYMERIZATION PROCESS

Номер: US20130243984A1
Принадлежит: INVISTA North America S.ar.I.

The present invention relates to a process for producing PET based on titanium catalyst having acceptable properties for resin used in the production of bottles for beverages. More particularly the invention relates to a process in which the incoming pre-polymer temperature is higher than the final outlet temperature in the final melt phase polycondensation reactor. 1. A method for the production of solid polyester polymer resin comprising:a) esterifying the diacids and diols to form an oligomer mixture with a DP of less than 20; andb) polycondensing the oligomer mixture in the presence of a polycondensation catalyst composition comprising titanium species at a temperature of greater than 284° C. to an IV of about 0.4 dl/g; andc) completing the polycondensation by increasing the IV by at least 0.2 dl/g and cooling the polymer melt temperature to less than 282° C.; andd) solidifying and cutting the molten polyester polymer composition into solid polyester polymer particles; and optionallye) solid state polymerizing the solid polyester polymer particles to increase the IV by more than 0.05 dl/g.2. The method of claim 1 , wherein step a) esterifies the diester of the said diacids.3. The method of claim 1 , wherein the mole ratio of said diol to said diacid is less than about 1.15.4. The method of or claim 1 , wherein the said diacids comprise at least 80 weight % of terephthalic acid or 2 claim 1 ,6-naphthalene dicarboxylic acid.5. The method of claim 4 , wherein said diols comprise at least 80 weight % of ethylene glycol.6. The method of the above claims claim 4 , wherein said titanium species is at an amount of about 5 to about 25 ppm.7. The method of the above claims wherein a reheat additive claim 4 , toners and other additives are added during said steps a) or b).8. The polyester resin by the method of any of the above claims.9. An article made from the said polyester resin of .10. The article of wherein said article is an extrusion blow molded or injection ...

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17-10-2013 дата публикации

Catalyst composition

Номер: US20130274092A1

The disclosure provides a catalyst composition, including: a metal or metal compound; and an organic diacid metal salt. The metal includes titanium (Ti), stibium (Sb) or combinations thereof and the metal compound includes antimony oxide (Sb 2 O 3 ) or tetra-n-butoxy titanium (TBT). The catalyst composition includes about 0.3-6 wt % of the metal or metal compound and about 94-99.7 wt % of the organic diacid metal salt.

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24-10-2013 дата публикации

N-Heterocyclic Carbene Based Zirconium Complexes For Use In Lactones Ring Opening Polymerization

Номер: US20130281653A1
Принадлежит: CLARIANT FINANCE (BVI) LIMITED

This invention is reporting new N-heterocyclic carbene based zirconium (or hafnium) complexes and their uses as catalysts for the lactones ring opening polymerization. These new catalysts are robust and versatile and exert control over polymer molecular weight and/or stereochemistry and exhibit high reactivity (cf. for low temperature applications). In particular the new catalysts show both enhanced activity and at the same time a better selectivity than the catalysts employed by the prior art. 2. A N-heterocyclic carbene according to claim 1 , whereinM is Zr,{'sub': 3', '4, 'R1 is Cl, Br, C-Calkoxy or aryloxy,'}R2 is optional and is a coordinative solvent,{'sub': 3', '4', '4', '5, 'X is Cl, Br, C-Calkoxy, aryloxy, benzyloxy, C-Calkyl or benzyl,'}{'sub': 3', '2', '5', '3', '7', '4', '9, 'R3 and R4 are independently from each other selected from the group consisting of hydrogen, CH, CH, CHand CH,'}{'sub': 3', '2', '5', '3', '7', '4', '9, 'R5 and R6 are independently from each other selected from the group consisting of hydrogen, CH, CH, CHand CH,'}R5 and R6 are optionally linked together to form an unsaturated or saturated 6 membered ring, when saturated, this cycle optionally has two chiral centers.{'sub': 1', '10', '5', '10, 'R7 and R8 are independently from each other selected from the group consisting of C-Calkyl, and C-Ccycloalkyl.'}4. A process according to claim 3 , wherein the solvent is selected from the group consisting of C-Calcohols claim 3 , dialkyletheroxides claim 3 , alkylnitriles claim 3 , aromatics claim 3 , dimethylformamide claim 3 , N-methylpyrolidone and mixtures thereof.5. A N-heterocyclic carbine according to claim 1 , wherein the coordinative solvent is tetrahydrofurane claim 1 , diethylether claim 1 , water claim 1 , acetonitrile or dimethylamine.6. A N-heterocyclic carbine according to claim 1 , wherein the X is Cl claim 1 , Br claim 1 , F or I.7. A N-heterocyclic carbine according to claim 1 , wherein at least one of R3 and R4 is ...

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16-01-2014 дата публикации

POLYLACTIDE RESIN AND PREPARATION METHOD THEREOF

Номер: US20140018515A1
Принадлежит: LG CHEM, LTD.

The present invention is directed to an organometallic complex and a catalyst composition capable of producing polylactide resins with improved properties at a higher conversion rate, a method of producing the organometallic complex, polylactide resins having enhanced hydrolysis resistance and heat resistance together with superior mechanical properties, a preparation process therefore, and polylactide resin compositions including the same. 2. The polylactide resin according to claim 1 , which has acidity of 3 to 10 meq/kg and a weight average molecular weight of 200 claim 1 ,000 to 1 claim 1 ,000 claim 1 ,000.3. The polylactide resin according to claim 1 , wherein the amount of the catalyst residue is no more than 15 ppm.48. The polylactide resin according to claim claim 1 , which shows a weight loss of less than 20 wt % when heated from room temperature to 300° C. during thermal gravimetric analysis (TGA). The present application is a divisional of U.S. patent application Ser. No. 13/148,367, filed on Aug. 8, 2011, which is a national phase entry under 35 U.S.C. §371 of International Application No. PCT/KR2010/000793, filed Feb. 9, 2010, published in Korean, which claims the benefit of Korean Patent Application Nos. 10-2009-0010182, filed Feb. 9, 2009; 10-2009-0040123, filed May 8, 2009; and 10-2009-0072140, filed Aug. 5, 2009. The disclosures of said applications are incorporated by reference herein.(a) Field of the InventionThe present invention relates to polylactide resins with improved properties, and a preparation process therefore. More specifically, the present invention is directed to an organometallic complex and a catalyst composition capable of producing polylactide resins with improved properties at a higher conversion rate, a method of producing the organometallic complex, polylactide resins having enhanced hydrolysis resistance and heat resistance together with superior mechanical properties, a preparation process therefore, and polylactide resin ...

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16-01-2014 дата публикации

POLYLACTIDE RESIN AND PREPARATION METHOD THEREOF

Номер: US20140018516A1
Принадлежит: LG CHEM, LTD.

The present invention is directed to an organometallic complex and a catalyst composition capable of producing polylactide resins with improved properties at a higher conversion rate, a method of producing the organometallic complex, polylactide resins having enhanced hydrolysis resistance and heat resistance together with superior mechanical properties, a preparation process therefor, and polylactide resin compositions including the same. 2. The process for preparing a polylactide resin according to claim 1 , wherein the MXYis tin(II) 2-ethylhexanoate (Sn(Oct)).3. The process for preparing a polylactide resin according to claim 1 , wherein Ris a monovalent phenyl group substituted with a C1 to C10 alkyl group or a C3 to C10 alkyl group or cycloalkyl group claim 1 , and Ris a divalent phenylene group substituted with a C1 to C10 alkyl group claim 1 , or a C3 to C10 alkylene group or cycloalkylene group.4. The process for preparing a polylactide resin according to claim 1 , wherein the compounds of Chemical Formula 2 and Chemical Formula 3 are added at a ratio of 0.001 to 0.1 moles with respect to 100 moles of the lactide monomers claim 1 , respectively.5. The process for preparing a polylactide resin according to claim 1 , wherein the ring opening polymerization is carried out in the presence of an initiator comprising a compound with a hydroxy group.6. The process for preparing a polylactide resin according to claim 5 , wherein the compound with a hydroxy group has 8 or more carbon atoms.7. The process for preparing a polylactide resin according to claim 5 , wherein the initiator is added at a ratio of 0.001 to 1 mole with respect to 100 moles of the lactide monomers.8. The process for preparing a polylactide resin according to claim 1 , wherein the ring opening polymerization is carried out in a manner of a bulk polymerization.9. The process for preparing a polylactide resin according to claim 1 , wherein the ring opening polymerization is carried out at a ...

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23-01-2014 дата публикации

TITANIUM-BASED CATALYST SHOWING EXCELLENT ACTIVITY AND SELECTIVITY IN POLYCONDENSATION REACTIONS

Номер: US20140024798A1
Принадлежит: EQUIPOLYMERS GMBH

A polycondensation reaction mixture is disclosed which includes a catalyst, acyclic esters, ethylene glycol, and water. The catalyst is a titanium atrane. The polycondensation reaction mixture is prepared by the steps of (a) contacting a solution comprising a titanium (IV) alkoxide compound and a first solvent with an organic acid; (b) contacting the solution formed in step (a) with a substituted or unsubstituted trialkanolamine to form an impure catalyst; (c) purifying the impure catalyst to form the titanium atrane catalyst; and (d) bringing the catalyst into contact with the acyclic esters under conditions that produce the ethylene glycol and water. 2. A method for making the polycondensation reaction mixture according to comprising: (a) contacting a solution comprising a titanium (IV) alkoxide compound and a first solvent with an organic acid; (b) contacting the solution formed in step (a) with a substituted or unsubstituted trialkanolamine to form an impure catalyst; (c) purifying the impure catalyst to form the titanium atrane catalyst; and (d) bringing the catalyst into contact with the acyclic esters under conditions that produce the ethylene glycol and water.3. The method according to claim 2 , wherein the titanium (IV) alkoxide compound is titanium n-butylate claim 2 , titanium isopropylate claim 2 , titanium n-propylate claim 2 , titanium t-buylate claim 2 , or titanium ethylate.4. The method according to claim 3 , wherein the first solvent is a primary alcohol claim 3 , a secondary alcohol claim 3 , or a tertiary alcohol.5. The method according to claim 4 , wherein the organic acid is a carboxylic acid.6. The method according to claim 5 , wherein the organic acid is acetic acid or propionic acid.7. The method according to claim 6 , wherein the trialkanolamine is triethanolamine claim 6 , triisopropanolamine claim 6 , or a substituted triethanolamine.8. The method according to claim 2 , wherein step (c) further comprises: c1) evaporating the first solvent ...

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30-01-2014 дата публикации

METHOD FOR THE PREPARATION OF POLYALKYLENE TEREPHTHALATE RESIN COMPOSITIONS EMPLOYING TITANIUM-CONTAINING CATALYST COMPLEX

Номер: US20140027945A1
Принадлежит: SABIC INNOVATIVE PLASTICS IP B.V.

A process of preparing a polyalkylene terephthalate comprising reacting an alkylene diol and an aromatic dicarboxy compound that is an aromatic dicarboxylic acid, aromatic dicarboxylic (C-C)alkyl ester, or a combination thereof, wherein ester interchange and polymerization occurs in the presence of a catalyst complex formed by the reaction of tetraisopropyl titanate and a boron, phosphorous or nitrogen-containing complexing agent, which catalyst can be synthesized in situ prior to ester interchange and introduced to a mixture of the alkylene diol and the aromatic dicarboxy compound prior to ester interchange. 1. A process of preparing a polyalkylene terephthalate comprising reacting a alkylene diol and a dicarboxy aromatic compound selected from the group aromatic dicarboxylic acids , aromatic dicarboxylic (C-C)alkyl esters , and combinations thereof , wherein the process comprises:{'sub': 1', '8, 'forming a catalyst that consists of the reaction product of tetra(C-Calkyl) titanate and a complexing agent selected from the group phosphorus-containing compounds, a nitrogen-containing compounds, a boron-containing compound, and combinations thereof;'}obtaining ester interchange by combining the catalyst with the alkylene diol and the aromatic dicarboxy compound; andpolymerizing the product of ester interchange, in the continued presence of the catalyst, yielding polyalkylene terephthalate.2. The process of claim 1 , wherein the catalyst is prepared in situ by combining the tetra(C-Calkyl) titanate claim 1 , complexing agent claim 1 , and the alkylene diol prior to ester interchange between the alkylene diol and dicarboxy aromatic compound.3. The process of claim 1 , wherein the aromatic dicarboxy compound is virgin terephthalic acid or dimethyl terephthalate or produced by depolymerizing recycled polyethylene terephthalate.4. The process of claim 1 , wherein the alkylene diol is produced from biomass.5. The process of claim 1 , wherein the alkylene diol is selected ...

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30-01-2014 дата публикации

METHOD FOR THE PREPARATION OF MODIFIED POLY(ALKYLENE TEREPHTHALATE) EMPLOYING IN SITU TITANIUM-CONTAINING CATALYST

Номер: US20140031440A1
Принадлежит:

A process of preparing a modified polyalkylene terephthalate by melt polycondensation comprising reacting an alkylene diol and polyethylene terephthalate, wherein polymerization occurs in the presence of a catalyst complex formed by reaction of tetra(alkyl) titanate and a compound selected from phosphorus-containing compounds, nitrogen-containing compounds, boron-containing compounds, and combinations thereof. 1. A process of preparing a modified polyalkylene terephthalate from recycled polyethylene terephthalate , the process comprising:{'sub': 1', '8', '1', '8, 'forming a catalyst consisting of the reaction product of tetra(C-Calkyl) titanate and a complexing agent selected from the group phosphorus-containing compounds, nitrogen-containing compounds, boron-containing compounds, and combinations thereof, wherein the molar ratio of the complexing agent to the tetra(C-Calkyl) titanate is from 0.05 to less than or equal to 2:1;'}{'sub': 2', '20, 'depolymerizing the polyethylene terephthalate by combining the polyethylene terephthalate, in the presence of the catalyst, with a dihydric alcohol selected from the group C-Calkylene diols to obtain a molten mixture; and'}{'sub': 3', '20, 'polymerizing the molten mixture in the continued presence of the catalyst and C-Calkylene diol, which alkylene diol is added during or after depolymerisation such that the same or different alkylene diol can be present during depolymerization and polymerization, to yield modified polyalkylene terephthalate.'}2. The process of claim 1 , wherein the catalyst is made prior to depolymerisation.3. The process of claim 1 , wherein the catalyst is synthesized in situ claim 1 , prior to depolymerization of the polyethylene terephthalate claim 1 , by combining the tetra(C-Calkyl) titanate and complexing agent in the dihydric alcohol used to depolymerize the polyethylene terephthalate.4. The process of claim 1 , wherein the molar ratio of the phosphorus-containing compound:titanate is from 0.1:1 to ...

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30-01-2014 дата публикации

Process for the Preparation of Modified Poly(Alkylene Terephthalate) Employing an In-Situ Titanium-Containing Catalyst

Номер: US20140031441A1
Принадлежит: SABIC INNOVATIVE PLASTICS IP BV

Disclosed is an improved process for preparing a modified polyalkylene terephthalate by melt polycondensation followed optionally by solid state condensation comprising reacting an alkylene diol and polyethylene terephthalate, wherein polymerization occurs in the presence of a catalyst complex formed by reaction of tetra(alkyl) titanate and a compound selected from phosphorus-containing compounds, nitrogen-containing compounds, boron-containing compounds, and combinations thereof.

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30-01-2014 дата публикации

Process for the preparation of poly(alkylene terephthalate) employing an in-situ titanium-containing catalyst and compositions derived therefrom

Номер: US20140031454A1
Принадлежит: SABIC INNOVATIVE PLASTICS IP BV

Disclosed is a process for the manufacture of a polyalkylene terephthalate such as polybutylene terephthalate. In particular, the process comprises employing a titanium-containing catalyst formed by the reaction product of tetraalkyl titanate and a complexing agent comprising a phosphorous, nitrogen or boron atom. The process is used to prepare polyalkylene terephthalates characterized by improved hydrostability, as well as compositions derived therefrom.

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30-01-2014 дата публикации

Process for the preparation of poly(alkylene terephthalate) employing in situ titanium-containing catalyst and compositions derived therefrom

Номер: US20140031457A1
Принадлежит: SABIC INNOVATIVE PLASTICS IP BV

Disclosed is a process for the manufacture of a polyalkylene terephthalate such as polybutylene terephthalate. In particular, the process comprises employing a titanium-containing catalyst formed by the reaction product of tctraalkyl titanate and a complexing agent comprising a phosphorous, nitrogen or boron atom. The process is used to prepare polyalkylene terephthalates characterized by improved hydrostability, as well as compositions derived therefrom.

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30-01-2014 дата публикации

GLYCEROL BASED UNSATURATED POLYESTER RESINS AND RAW MATERIALS THEREFOR

Номер: US20140031490A1
Принадлежит:

The invention relates to a mixture of glycerol, mono-, di- and triacetylglycerolester in which the amount of tri-ester is less than 15 mol %, the amount of glycerol is less than 25 mol %, the amount of monoester is about 20 mol % or more, more preferred about 30 mol % or more and the amount of diester is about 20 mol % or more preferred about 40 mol % or more. The invention further relates to methods to prepare such glycerolacetylester mixtures, and to the use thereof in the preparation of unsaturated polyesters. Polyesters comprising said glycerolacetylester mixtures are made from a higher amount of raw materials than obtainable from renewable resources. 1. A process for the preparation of glycerolacetylesters , in which acetic acid and glycerol having a molar ratio of less than 2.5 , are reacted in the presence of a stannous catalyst to produce a mixture of glycerol , mono- , di- and triacetylglycerolester.2. The process according to claim 1 , wherein the resulting amount of triester relative to the resulting amounts of glycerol claim 1 , monoester and diester is less than 15 mol %.3. The process according to claim 1 , wherein the resulting amount of glycerol relative to the resulting amounts of claim 1 , monoester claim 1 , diester and triester is less than 25 mol %.4. The process according to claim 1 , wherein the resulting amount of mono-ester relative to the resulting amounts of glycerol claim 1 , diester and triester is about 20 mol % or more and wherein the resulting amount of mono-ester relative to the resulting amounts of glycerol claim 1 , diester and triester is about 50 wt % or less.5. The process according to claim 1 , wherein the resulting amount of di-ester relative to the resulting amounts of glycerol claim 1 , monoester and triester is about 20 mol % or more claim 1 , and wherein the resulting amount of di-ester relative to the resulting amounts of glycerol claim 1 , monoester and triester is about 60 wt % or less.6. The process according to claim ...

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13-03-2014 дата публикации

POLYCONDENSATION CATALYST FOR PRODUCING POLYESTER AND PRODUCTION OF POLYESTER USING THE POLYCONDENSATION CATALYST

Номер: US20140073758A1
Принадлежит: SAKAI CHEMICAL INDUSTRY CO., LTD.

The invention provides a polycondensation catalyst for producing polyester by an esterification reaction or a transesterification reaction between a dicarboxylic acid or an ester-forming derivative thereof and a glycol, wherein the polycondensation catalyst comprises particles of a solid base having on the surfaces an inner coating layer of titanic acid in an amount of from 0.1 to 50 parts by weight in terms of TiOper 100 parts by weight of the solid base, and an outer coating layer either of an oxide of at least one element selected from aluminum, zirconium and silicon, or of a composite oxide of at least two elements selected from aluminum, zirconium and silicon on the surface of the inner coating layer in an amount of from 1 to 50 parts by weight per 100 parts by weight of the solid base. 1. A polycondensation catalyst for producing polyester by an esterification reaction or a transesterification reaction between a dicarboxylic acid or an ester-forming derivative thereof and a glycol , wherein the polycondensation catalyst comprises particles of a solid base having on the surfaces an inner coating layer of titanic acid in an amount of from 0.1 to 50 parts by weight in terms of TiOper 100 parts by weight of the solid base , and an outer coating layer either of an oxide of at least one element selected from aluminum , zirconium and silicon , or of a composite oxide of at least two elements selected from aluminum , zirconium and silicon on the surface of the inner coating layer in an amount of from 1 to 50 parts by weight per 100 parts by weight of the solid base.2. The polycondensation catalyst according to claim 1 , wherein the solid base is magnesium hydroxide.3. The polycondensation catalyst according to claim 1 , wherein the solid base is hydrotalcite.4. A method for producing a polycondensation catalyst for producing polyester by an esterification reaction or a transesterification reaction between a dicarboxylic acid or an ester-forming derivative thereof and ...

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06-01-2022 дата публикации

Conductive Polymer Composition

Номер: US20220002475A1
Принадлежит: PPG Industries Ohio, Inc.

An electrically or thermally conductive polymer composition, includes: a polyester polymer having a backbone including at least 12 consecutive carbon atoms between ester linkages; and conductive particles dispersed in the polyester polymer. A component including an electrically or thermally conductive polymer composition is also disclosed. A method for self-regulating a temperature of a component is also disclosed. 1. An electrically or thermally conductive polymer composition , comprising:a polyester polymer having a backbone comprising at least 12 consecutive carbon atoms between ester linkages; andconductive particles dispersed in the polyester polymer.2. The conductive polymer composition of claim 1 , wherein the conductive polymer composition exhibits a trip temperature in a range between 20° C. and 120° C. claim 1 , wherein the trip temperature is a temperature at which a maximum slope is exhibited in a graph of normalized resistance over temperature for the conductive polymer composition.3. The conductive polymer composition of claim 1 , wherein the backbone comprises at least 18 consecutive carbon atoms.4. The conductive polymer composition of claim 1 , wherein the polyester polymer comprises at least 10 weight percent of solids of the conductive polymer composition.5. The conductive polymer composition of claim 1 , wherein the polyester polymer has a linear structure.6. The conductive polymer composition of claim 1 , wherein the polyester polymer comprises a non-aromatic polyester.7. The conductive polymer composition of claim 1 , wherein the polyester polymer comprises a saturated polyester.8. The conductive polymer composition of claim 1 , wherein the polyester polymer comprises a semi-crystalline polyester.9. The conductive polymer composition of claim 1 , wherein the polyester polymer comprises a polyester polyol polymer or a polyester polyacid polymer.10. The conductive polymer composition of claim 1 , wherein the polyester polymer is a reaction ...

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07-01-2016 дата публикации

A Process to Prepare a Polyester Polymer Composition Comprising a Polyester Polymer Having Furanic Units and a Polyester Polymer Composition Obtainable Thereby and the use Thereof

Номер: US20160002397A1
Принадлежит: SULZER CHEMTECH AG

A process to prepare a polyester polymer composition comprising a polyester polymer having furanic units is disclosed. The process comprises the step of reacting a cyclic polyester oligomer in the presence of a catalyst in a ring-opening polymerization step under conditions of a reaction temperature and reaction time sufficient to yield a polyester polymer having furanic units. The invention further relates to a polyester polymer composition obtainable by said process, wherein the polyester polymer composition comprises a polyester polymer having furanic units and a cyclic polyester oligomer comprising either structure Yor Y, preferably in a concentration of less than 5 wt %, more preferably less than 1, more preferably less than 0.5 in the composition. The present invention further relates also to the use of said polyester polymer composition in extrusion, injection molding, or blow molding. 115-. (canceled)17. The process of claim 16 , wherein the reaction temperature is from 25 to 350° C. claim 16 , and wherein the reaction time is from 10 to 300 minutes.18. The process of claim 16 , wherein the catalyst is selected from a base claim 16 , or a Lewis acid catalyst.19. The process of claim 18 , wherein the ring-opening polymerization step takes place in the presence of an initiator having at least one or more hydroxyl groups.20. The process of claim 18 , wherein the catalyst is a Lewis acid catalyst claim 18 , and wherein the initiator is present and it is selected from the group consisting of water claim 18 , 1-octanol claim 18 , 2-ethylhexanol claim 18 , 1-decanol claim 18 , isodecyl alcohol claim 18 , 1-undecanol claim 18 , 1-dodecanol claim 18 , 2-methyl-2-propanol claim 18 , 4-phenyl-2-butanol claim 18 , 1 claim 18 ,3-propandiol claim 18 , and pentaerytrol.21. The process of claim 20 , wherein the Lewis acid catalyst is tin octoate and the initiator is either 1-octanol or 2-ethylhexanol.22. The process of claim 18 , wherein the initiator is present in an ...

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02-01-2020 дата публикации

SYNTHESIS OF POLYGLYCOLIC ACID WITH HIGH MOLECULAR WEIGHT AND HIGH SOLUBILITY AT LOW COST

Номер: US20200002469A1
Принадлежит: TUBITAK

The invention relates to the synthesis method of polyglycolic acid (PGA) obtained by removing the excessive water and monomer formed subsequent to condensation by means of an organic solvent and using azeotropic distillation method in the presence of a catalyst. The invention is a synthesis method of polyglycolic acid with high molecular weight and high solubility, characterized by comprising the steps of placing the glycolic acid in reaction medium with a catalyst; using hydrophilic organic solvents for removing the excessive water and monomer formed during condensation; mixing and boiling the mixture; stabilizing the amount of solvent in reaction medium and distilling the water off by means of Dean stark apparatus and/or a similar apparatus; refluxing the solid polymer obtained at the end of the reaction with ethyl acetate and removing the same from monomer residue and catalyst. 1. A synthesis method of polyglycolic acid , characterized in that it comprises the steps of:placing the glycolic acid in reaction medium with a catalyst,using hydrophilic organic solvents for removing the excessive water and monomer formed during condensation,mixing and boiling the mixture,stabilizing the amount of solvent in reaction medium and distilling the water off by means of Dean stark apparatus and/or a similar apparatus,refluxing the solid polymer obtained at the end of the reaction with ethyl acetate and removing the same from monomer residue and catalyst, andmeasuring the molecular weight of the resulting aliphatic polyester by gel permeation chromatography (GPC).2. A synthesis method of polyglycolic acid according to claim 1 , characterized in that the molecular weight of the obtained aliphatic polyester is between 5000 and 60000 Da.3. A synthesis method of polyglycolic acid according to by using hydrophilic organic solvents for removing the excessive water and monomer formed during condensation such as methanol claim 1 , ethanol claim 1 , acetone claim 1 , methyl ethyl ketone ...

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02-01-2020 дата публикации

PROCESS FOR PREPARING POLY(ALKYLENE FURANDICARBOXYLATE)

Номер: US20200002471A1
Принадлежит:

A process to prepare poly(alkylene furandicarboxylate) polymer is disclosed herein. In one embodiment, the process comprises a) contacting a mixture comprising furandicarboxylic acid dialkyl ester, a diol comprising ethylene glycol, 1,3-propanediol, 1,4-butanediol, 1,4-cyclohexanedimethanol, or mixtures thereof, and a metal catalyst at a temperature in the range of from about 140° C. to about 220° C. to form prepolymer, 2. The process of claim 1 , wherein the furandicarboxylic acid dialkyl ester is 2 claim 1 ,5-furandicarboxylate dimethyl ester.3. The process of claim 1 , wherein the diol is 1 claim 1 ,3-propanediol and the poly(alkylene furandicarboxylate) polymer is poly(trimethylene furandicarboxylate).4. The process of claim 1 , wherein the diol is ethylene glycol and the poly(alkylene furandicarboxylate) polymer is poly(ethylene furandicarboxylate).5. The process of claim 1 , wherein the diol is 1 claim 1 ,4-butanediol and the poly(alkylene furandicarboxylate) polymer is poly(butylene furandicarboxylate).6. The process of claim 1 , wherein the metal catalyst comprises at least one titanium claim 1 , bismuth claim 1 , zirconium claim 1 , tin claim 1 , antimony claim 1 , germanium claim 1 , aluminum claim 1 , cobalt claim 1 , magnesium claim 1 , or manganese compound.7. The process of claim 1 , wherein the metal catalyst is present in the mixture in a concentration in the range of from about 20 ppm to about 300 ppm claim 1 , based on the total weight of the polymer.8. The process of claim 1 , wherein the anthraquinone compound is present in the mixture in a concentration in the range of from about 1 ppm to about 20 ppm claim 1 , based on the total weight of the polymer.9. The process of claim 1 , wherein the anthraquinone compound is present in the prepolymer in a concentration in the range of from about 1 ppm to about 20 ppm claim 1 , based on the total weight of the polymer.10. The process of claim 1 , wherein the anthraquinone compound is 1 claim 1 ,4-bis[(2 ...

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02-01-2020 дата публикации

Degradable hyperbranched epoxy resin and preparation method thereof

Номер: US20200002481A1

Degradable hyperbranched epoxy resin and a preparation method thereof, wherein the preparation method comprises carrying out a reaction between a cyclotriazine compound and a carboxyl-sourced compound to prepare a carboxyl-terminated or hydroxy-terminated hyperbranched polymer; then reacting with epoxy chloropropane to obtain a degradable hyperbranched epoxy resin of which the molecular weight is about 1,900-22,000 g/mol. After the degradable hyperbranched epoxy resin is cured, a cyclotriazine structure can be completely degraded within 2 h in a phosphoric acid solution at the temperature of 80 ° C., thus realizing the recycle of the epoxy resin. The invention has simple process, and the product is degradable and has self-strengthening and self-toughening functions, and is expected to be used in the fields of strengthening and toughening of epoxy resins, solvent-free coatings etc.

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07-01-2021 дата публикации

LAMINATING ADHESIVES USING POLYESTER FROM TRANSESTERIFICATION OF POLYLACTIC ACID WITH NATURAL OILS

Номер: US20210002422A1
Принадлежит:

A specific mixture of polyols, at least one of which contains the transesterification product of the polymer polylactic acid with natural oils. The mixture of polyols can be used as one component of a two-component adhesive for laminating flexible packaging. The other component comprises an isocyanate-functionalized compound. The two components are combined before use and the resulting adhesive can be used to bond films to form a flexible packaging material. 1. An isocyanate reactive component for reaction with an isocyanate functionalized component to form a two-component laminating adhesive , comprising:a transesterification product of a reaction mixture comprising polymeric polylactic acid and at least one natural oil; anda high OH functionality polyol product.2. The isocyanate reactive component of wherein the reaction mixture comprises polymeric polylactic acid claim 1 , at least one natural oil and a diol having a molecular weight of about 50 to about 2000 daltons.3. The isocyanate reactive component of wherein the reaction mixture comprises:polylactic acid present in an amount of from 50 to 85 weight percent based on a total weight of the reaction mixture;at least one natural oil present in an amount of from 13 to 30 weight percent based on the total weight of the reaction mixture;a diol present in an amount of from 2 to 36 weight percent based on the total weight of the reaction mixture; andoptionally, a transesterification catalyst.4. The isocyanate reactive component of having a renewable content in the range of at least 70%.5. The isocyanate reactive component of having a viscosity of 3 claim 1 ,000 to 20 claim 1 ,000 cps at 25° C.6. The isocyanate reactive component of any of wherein the high OH functionality polyol product has at least about two primary hydroxyl groups and at least about two secondary hydroxyl groups.7. The isocyanate reactive component of wherein the natural oil is castor oil and/or soybean oil.8. A two-component adhesive for ...

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01-01-2015 дата публикации

ORGANOTIN COMPOUNDS, PREPARATION METHOD THEREOF, AND PREPARATION OF POLYLACTIDE RESIN USING THE SAME

Номер: US20150005470A1
Принадлежит:

The present invention relates to an organotin compound represented by RO—Sn—OR(where Rand Rare independently a primary, secondary, or tertiary alkyl group having 5 to 30 carbon atoms), a preparation method thereof, and a preparation method for polylactide using the organotin compound. The organotin compound of the present invention is easy to prepare and is used to prepare a polylactide resin having a high molecular weight at a high yield without using a separate initiator. 16-. (canceled)7. A method for preparing an organotin compound , comprising: {'br': None, 'sub': 1', '2, 'RO—Sn—OR\u2003\u2003[Formula 1]'}, 'reacting a tin(II) salt with a primary, secondary, or tertiary alcohol having 5 to 30 carbon atoms to form an organotin compound represented by the following Formula 1{'sub': 1', '2, 'wherein Rand Rare independently a primary, secondary, or tertiary alkyl group having 5 to 30 carbon atoms.'}8. A method for preparing an organotin compound , comprising:(a) reacting a tin(II) salt with a primary, secondary, or tertiary alcohol having 1 to 12 carbon atoms to form an intermediate of tin(II) alkoxide; and {'br': None, 'sub': 1', '2, 'RO—Sn—OR\u2003\u2003[Formula 1]'}, '(b) reacting the intermediate of tin(II) alkoxide with a primary, secondary, or tertiary alcohol having 5 to 30 carbon atoms to form an organotin compound represented by the following Formula 1{'sub': 1', '2, 'wherein Rand Rare independently a primary, secondary, or tertiary alkyl group having 5 to 30 carbon atoms.'}9. The method as claimed in claim 8 , wherein the step (b) of reacting the intermediate of tin(II) alkoxide with a primary claim 8 , secondary claim 8 , or tertiary alcohol having 5 to 30 carbon atoms is conducted in an at least one-step reaction process.10. The method as claimed in claim 7 , wherein the step of reacting a tin(II) salt with a primary claim 7 , secondary claim 7 , or tertiary alcohol having 5 to 30 carbon atoms is conducted in the presence of a base.11. The method as ...

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11-01-2018 дата публикации

CATALYTIC COMPOSITION FOR PREPARING PET RESIN

Номер: US20180009939A1
Принадлежит:

A catalytic composition for preparing a polyethylene terephthalate (PET) resin is provided. The catalytic composition comprises a polycondensation catalyst and cesium tungsten oxide (CsWOCl), and 0 Подробнее

14-01-2021 дата публикации

WOOL-LIKE POLYESTER FILAMENT AND PREPARING METHOD THEREOF

Номер: US20210009755A1
Принадлежит: JIANGSU HENGLI CHEMICAL FIBRE CO., LTD.

A type of wool-like polyester filament and preparing method thereof are disclosed. The preparing method is manufacturing filament from a modified polyester through a POY process and a successive DTY processes, wherein the modified polyester is the product of the esterification and the successive polycondensation reactions of evenly mixed terephthalic acid, 1,4-butanediol, fluorinated dicarboxylic acid, tert-butyl branched hexanediol and 2,5,6,6-tetramethyl-2,5-heptanediol. The obtained fiber has a dye uptake of 90.32-93.27% and a K/S value of 22.15-23.42 when dyed at 100° C., and has an intrinsic viscosity drop of 17-20% when stored at 25° C. and R.H. 65% for 60 months. This invention features a method with ease of application and a product with good dyeing and degradation performance. 2. The preparing method of claim 1 ,wherein the tert-butyl branched hexanediol is synthesized by means of:mixing a 300-350 g/L solution of material A and a 200-300 g/L solution of dilute sulfuric acid at a molar ratio of (1.5-2):1 of the material A to the sulfuric acid to form a mixed solution, and adding the mixed solution into an electrolytic cell, then cooling the mixed solution to 10-15° C. and carrying out an electrolytic reduction until a concentration of the material A decreases to less 10 wt %, and finally obtaining the target compound through a series of processes of cooling crystallization, separation and purification;{'sub': 2', '3', '3', '3, 'wherein the material A is 2,2-methylpropionaldehyde, 2,2-dimethyl-3-pentanone or 2,2,4,4-tetramethyl-3-pentanone when R (in Formula 1) stands for —H, —CHCHor —C(CH), respectively;'}wherein the 2,5,6,6-tetramethyl-2,5-heptanediol is synthesized by means of:(1) mixing KOH, 3-methyl-3-hydroxybutyne, 3,3-dimethyl-2-butanone and isopropyl ether in a molar ratio of (1-1.2):1:(1.2-1.3):(2.0-3.0), then carrying out the reaction in an ice bath for 2-4 hrs, finally obtaining octyne diol through a series of processes of cooling crystallization, ...

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09-01-2020 дата публикации

Polymer Compositions With PBSA Plasticizer

Номер: US20200010628A1
Принадлежит: Danimer Bioplastics, Inc.

A polymeric composition is disclosed which includes from about 40 to about 99 weight percent of a first polymer and from about 1 to about 60 weight percent of polybutylene(succinate-co-adipate) (“PBSA”). Preferably the first polymer is selected from the group consisting of polyvinyl chloride, polylactic acid, polyhydroxy alkanoates, and mixtures thereof. A method for making the composition is also disclosed. 1. A polymeric composition comprising:from about 40 to about 99 weight percent of a first polymer which comprises polyhydroxy alkanoates; andfrom about 1 to about 60 weight percent of polybutylene(succinate-co-adipate) (“PBSA”).2. (canceled)3. The polymeric composition of claim 1 , wherein the PBSA has a weight average molecular weight from about 50 claim 1 ,000 to about 200 claim 1 ,000.4. The polymeric composition of claim 1 , wherein the PBSA has a weight average molecular weight from about 80 claim 1 ,000 to about 120 claim 1 ,000.5. The polymeric composition of claim 1 , wherein the PBSA has a viscosity from about 15 claim 1 ,000 to about 40 claim 1 ,000 centipoise at a temperature of about 215° C.6. The polymeric composition of claim 1 , wherein the PBSA has a melting point from about 20° C. to about 75° C.7. The polymeric composition of claim 1 , wherein the PBSA has a melting point from about 25° C. to about 40° C.8. The polymeric composition of claim 1 , wherein the PBSA comprises:from about 40 to about 60 mole percent moieties derived from 1,4-butanediol,from about 10 to about 50 mole percent moieties derived from succinic acid, andfrom about 10 to about 50 mole percent moieties derived from adipic acid.9. The polymeric composition of claim 1 , wherein the composition comprises from about 1 to about 10 weight percent of the PBSA.10. The polymeric composition of claim 1 , wherein the composition comprises from about 50 to about 60 weight percent of the PBSA.11. The polymeric composition of claim 1 , wherein the composition further comprises at least one ...

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03-02-2022 дата публикации

BIFURAN-MODIFIED POLYESTERS

Номер: US20220033573A1
Принадлежит:

Copolyesters such as polyethylene terephthalate (PET) or polyethylene furanoate (PEF) modified with bifuran polyacids such as dimethyl-2,2′-bifuran-5,5′-dicarboxylate (BFE), 2,2′-bifuran-5,5′-dicarboxylic acid (BDA), or bis(2-hydroxyethyl)-2,2′-bifuran-5,5′-dicarboxylate (BHEB), and/or bifuran polyhydroxyls, may have improved properties such as glass transition temperature (T), tensile modulus, barrier properties, crystallinity, and/or impact strength. Polyethylene terephthalate-co-bifuranoate (PETBF) has an improved T. Also described are polyethylene furanoate-co-bifuranoates (PEFBF). 1. A bifuran-modified polyester comprising:a diacid component;a diol component; anda bifuran comonomer in an amount of from 1 to 50 weight percent based on the total weight of the polyester.2. The bifuran-modified polyester of wherein the bifuran comonomer comprises a bifuran diacid; a bifuran diester; a diol bifuran diester; an ester-forming equivalent thereof; or a combination thereof.3. The bifuran-modified polyester of wherein the bifuran comonomer comprises a polyhydroxyl bifuran.4. The bifuran-modified polyester of claim 1 , wherein the diacid component comprises a polyfunctional carboxylic acid monomer selected from terephthalic acid claim 1 , furan dicarboxylic acid claim 1 , isophthalic acid claim 1 , naphthalic acid claim 1 , bibenzoic acid claim 1 , 1 claim 1 ,3-cyclohexanedicarboxylic acid claim 1 , 1 claim 1 ,4-cyclohexanedicarboxylic acid claim 1 , succinic acid claim 1 , glutaric acid claim 1 , adipic acid claim 1 , azelaic acid claim 1 , and sebacic acid claim 1 , ester forming equivalents thereof claim 1 , and combinations thereof.5. The bifuran-modified polyester of claim 4 , wherein the diol component comprises a polyhydroxyl compound selected from the group consisting of: aliphatic polyols; C-Ccyclic polyols; polyhydroxyl furans; and combinations thereof.6. The bifuran-modified polyester of claim 5 , wherein the polyhdroxyl compound is selected from the group ...

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16-01-2020 дата публикации

PROCESS FOR PREPARING POLY(TRIMETHYLENE FURANDICARBOXYLATE) USING ZINC CATALYST

Номер: US20200017634A1
Принадлежит:

A process is disclosed herein comprising the steps: a) contacting a mixture comprising furandicarboxylic acid dialkyl ester, 1,3-propanediol, a zinc compound, and optionally a poly(alkylene ether) diol, at a temperature in the range of from about 120° C. to about 220° C. to form prepolymer, wherein the mole ratio of the furandicarboxylic acid dialkyl ester to the 1,3-propanediol is in the range of from 1:1.3 to 1:2.2; and b) heating the prepolymer under reduced pressure to a temperature in the range of from about 220° C. to about 260° C. to form polymer. The mixture of step a) can further comprise an anthraquinone compound. 1. A process comprising the steps:a) contacting a mixture comprising furandicarboxylic acid dialkyl ester, 1,3-propanediol, a zinc compound, and optionally a poly(alkylene ether) diol, at a temperature in the range of from about 120° C. to about 220° C. to form prepolymer,wherein the mole ratio of the furandicarboxylic acid dialkyl ester to the 1,3-propanediol is in the range of from 1:1.3 to 1:2.2; andb) heating the prepolymer under reduced pressure to a temperature in the range of from about 220° C. to about 260° C. to form a polymer.2. The process of claim 1 , wherein the furandicarboxylic acid dialkyl ester is 2 claim 1 ,5-furandicarboxylate dimethyl ester and the polymer is poly(trimethylene furandicarboxylate).3. The process of claim 1 , wherein the zinc compound comprises zinc acetate claim 1 , zinc acetylacetonate claim 1 , zinc glycolate claim 1 , zinc p-toluenesulfonate claim 1 , zinc carbonate claim 1 , zinc trifluoroacetate claim 1 , zinc oxide claim 1 , or zinc nitrate.4. The process of claim 1 , wherein the concentration of the zinc compound is in the range of from about 20 ppm to about 300 ppm claim 1 , based on the total weight of the polymer.5. The process of claim 1 , wherein step a) is performed in the absence of a titanium compound.6. The process of claim 1 , wherein step b) is performed in the absence of a titanium compound.7 ...

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25-01-2018 дата публикации

A novel process for the preparation of hydroxyl functional esters and polyesters therefrom

Номер: US20180022681A1

The present invention relates to a novel process for the preparation of a linear monomer alkyl lactyl lactate by a simple esterification reaction of acid with ester in presence of suitable catalysts or reagents. The present invention further relates to a process for the preparation of poly acid from alkyl lactyl lactate by using suitable catalyst.

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25-01-2018 дата публикации

Aliphatic polyester composition, molded product, and manufacturing method of aliphatic polyester

Номер: US20180022868A1
Принадлежит: Kureha Corp

A method of continuously manufacturing an aliphatic polyester composition from a cyclic ester and the like, wherein the temperature in an extruder is increased in two or more stages from a raw material supply port to a discharge port, the temperature at the discharge port is a temperature where the melt viscosity of the composition at the discharge port is from 100 to 2000 Pa·s, the free acid concentration in the cyclic ester is 10 eq/t or less, and the unreacted cyclic ester concentration in the composition is less than 2 wt. %.

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22-01-2015 дата публикации

PRODUCTION METHOD FOR ALIPHATIC POLYESTER

Номер: US20150025216A1
Принадлежит:

To efficiently produce an aliphatic polyester and to improve the thermal stability of the resulting aliphatic polyester. 1. A method of producing an aliphatic polyester comprising a step of subjecting a cyclic ester to ring-opening polymerization in the presence of a tin compound serving as a catalyst , a polymerization initiator , and a sulfonic acid compound serving as a co-catalyst.2. The method of producing an aliphatic polyester according to claim 1 , wherein the tin compound is at least one type selected from tin dichloride and tin octanoate.3. The method of producing an aliphatic polyester according to claim 1 , wherein the polymerization initiator is an alcohol.4. The method of producing an aliphatic polyester according to claim 1 , wherein the sulfonic acid compound is methane sulfonic acid or paratoluene sulfonic acid.5. The method of producing an aliphatic polyester according to claim 1 , wherein the cyclic ester is at least one type of glycolide or lactide. This application claims the benefit of Japanese Patent Application No. 2013-151493 filed Jul. 22, 2013, the disclosure of which is herein incorporated by reference in its entirety.The present invention relates to a method for efficiently producing an aliphatic polyester with improved thermal stability using ring-opening polymerization of a cyclic ester such as a glycolide.Aliphatic polyesters such as polyglycolic acid or polylactic acid are decomposed by water, microorganisms, or enzymes present in the natural world such as the ground or the sea and have therefore attracted attention as biodegradable polymer materials with a small environmental burden. In addition, since these aliphatic polyesters have biodegradable absorbent properties, they are also used as polymer materials for medical purposes such as surgical sutures or artificial skin. Among aliphatic polyesters, polyglycolic acid (hereafter called “PGA”) has a high melting point and can be melt-molded, and applications are therefore being ...

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10-02-2022 дата публикации

RMA CROSSLINKABLE POLYMER

Номер: US20220041802A1
Принадлежит:

The invention relates to an RMA crosslinkable polymer comprising: a) at least one RMA Donor moiety X comprising a C—H acidic proton in activated methylene or methine groups, b) at least one moiety Y comprising one or more 5- or 6-membered heterocycles containing an ether-, acetal- or ketal group which in case of two or more of such heterocycles can be fused or linked, wherein the polymer has a weight-average molecular weight Mw of at least 400 g/mol and a C—H equivalent molecular weight CH EQW of at least 80 g/mol. The invention also relates to a process for the preparation of the RMA crosslinkable polymer, to an RMA crosslinkable composition comprising the RMA crosslinkable polymer and coated substrates. 2. The RMA crosslinkable polymer of claim 1 , further comprising a fatty moiety F claim 1 , preferably a fatty moiety F derived from one or more of the group of fatty acids claim 1 , fatty alcohols claim 1 , fatty amines claim 1 , fatty thiols and dimeric fatty acid claim 1 , preferably fatty acids claim 1 , preferred fatty moieties having 8-40 carbons claim 1 , preferably more than 8 claim 1 , 9 or 10 and less than 14 claim 1 , 20 claim 1 , 26 or 30 claim 1 , most preferably the fatty moiety F is derived from fatty acids obtained from coconut oil.3. The RMA crosslinkable polymer of claim 1 , wherein the moiety X comprises at least one activated hydrogen atom attached to a carbon atom that is located between two electron-withdrawing groups claim 1 , preferably —C(═O)— and/or —C≡N groups claim 1 , more preferably a moiety derived from a component A selected from the group of malonate esters claim 1 , acetoacetate esters claim 1 , malonamides claim 1 , and acetoacetamides claim 1 , cyanoacetate esters and cyanoacetamides.4. The RMA crosslinkable polymer of claim 1 , comprising 2 different types of RMA Donor moieties X claim 1 , referred to as moiety X1 and X2 claim 1 , wherein moiety X2 comprises a C—H acidic proton in activated methylene or methine having a pKa ( ...

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24-02-2022 дата публикации

METHOD FOR MANUFACTURING POLYESTER POLYHYDRIC ALCOHOL

Номер: US20220056201A1
Принадлежит:

A method for manufacturing polyester polyhydric alcohol is provided. The method for manufacturing polyester polyhydric alcohol includes steps as follows. A polybasic acid and a polyhydric alcohol are mixed for oligomerization to form an oligomer mixture. A catalyst is added into the oligomer mixture at a temperature ranging from 190° C. to 210° C. for polycondensation to obtain a polyester polyhydric alcohol product. The polyester polyhydric alcohol product has a number average molecular weight lower than 1000 g/mol and an acid value lower than or equal to 0.3 mg KOH/g. 1. A method for manufacturing polyester polyhydric alcohol , comprising:mixing a polybasic acid and a polyhydric alcohol for oligomerization to form an oligomer mixture; andadding a catalyst into the oligomer mixture at a temperature ranging from 190° C. to 210° C. for polycondensation to obtain a polyester polyhydric alcohol product;wherein the polyester polyhydric alcohol product has a number average molecular weight lower than 1000 g/mol and an acid value lower than or equal to 0.3 mg KOH/g.2. The method according to claim 1 , wherein the oligomerization is carried out at a temperature ranging from 130° C. to lower than 190° C.3. The method according to claim 2 , wherein the oligomerization is carried out at a pressure ranging from 100 Torr to lower than or equal to 760 Torr.4. The method according to claim 3 , wherein the oligomerization continues to be carried out until an acid value of the oligomer mixture is lower than or equal to 1 mg KOH/g and is then stopped.5. The method according to claim 1 , wherein the polycondensation is carried out at a pressure ranging from 10 Torr to lower than or equal to 760 Torr.6. The method according to claim 1 , further comprising: the polyester polyhydric alcohol product being maintained at a pressure ranging from 200 Torr to lower than 760 Torr and a temperature ranging from 80° C. to 140° C.7. The method according to claim 1 , wherein the polybasic acid and ...

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24-02-2022 дата публикации

PLASTICIZER AND METHOD FOR PRODUCING THE SAME

Номер: US20220056203A1
Принадлежит:

A plasticizer and a method for producing the same are provided. The method for producing the plasticizer includes: reacting a reaction mixture at each of a plurality of temperature holding stages in a heating process to form a semi-finished product; and purifying the semi-finished product at each of a plurality of low pressure stages of a decompression process to obtain a plasticizer. A temperature range of the heating process is from 140° C. to 220° C., a pressure range of the decompression process is from 750 Torr to 20 Torr, and the reaction mixture contains dibasic acid, diol, monohydric alcohol, and catalyst. 1. A method for producing a plasticizer , comprising:reacting a reaction mixture at each of a plurality of temperature holding stages in a heating process to form a semi-finished product, a temperature range of the heating process being from 140° C. to 220° C., and the reaction mixture containing dibasic acid, diol, monohydric alcohol, and catalyst; andpurifying the semi-finished product at each of a plurality of low pressure stages of a decompression process to obtain the plasticizer, a pressure range of the decompression process being from 750 Torr to 20 Torr.2. The method for producing the plasticizer according to claim 1 , wherein the temperature holding stages are respectively a first temperature holding stage claim 1 , a second temperature holding stage claim 1 , a third temperature holding stage claim 1 , and a fourth temperature holding stage claim 1 , and wherein a temperature of the first temperature holding stage is from 140° C. to 155° C. claim 1 , a temperature of the second temperature holding stage is greater than 155° C. and up to 170° C. claim 1 , a temperature of the third temperature holding stage is greater than 170° C. and up to 190° C. claim 1 , and a temperature of the fourth holding stage is greater than 190° C. and up to 220° C.3. The method for producing the plasticizer according to claim 2 , wherein a duration time of each of the ...

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24-02-2022 дата публикации

METHOD FOR MANUFACTURING POLYESTER POLYHYDRIC ALCOHOL

Номер: US20220056205A1
Принадлежит:

A method for manufacturing polyester polyhydric alcohol is provided. The method for manufacturing the polyester polyhydric alcohol includes steps as follows. A polybasic acid and a first polyhydric alcohol are mixed for a first oligomerization reaction, so as to form a first oligomer mixture. A second polyhydric alcohol is added into the first oligomer mixture for a second oligomerization reaction when a remaining amount of the first polyhydric alcohol in the first oligomer mixture is lower than or equal to 1 mol %, so as to form a second oligomer mixture. A catalyst is added into the second oligomer mixture for a polycondensation reaction, so as to obtain a polyester polyhydric alcohol product. The polyester polyhydric alcohol product has an Alpha value of lower than 30. 1. A method for manufacturing polyester polyhydric alcohol , comprising:mixing a polybasic acid and a first polyhydric alcohol for a first oligomerization reaction, so as to form a first oligomer mixture;adding a second polyhydric alcohol into the first oligomer mixture for a second oligomerization reaction when a remaining amount of the first polyhydric alcohol in the first oligomer mixture is lower than or equal to 1 mol %, so as to form a second oligomer mixture; andadding a catalyst into the second oligomer mixture for a polycondensation reaction, so as to obtain a polyester polyhydric alcohol product;wherein the polyester polyhydric alcohol product has an Alpha value of lower than 30.2. The method according to claim 1 , wherein the first polyhydric alcohol includes ethylene glycol claim 1 , and the second polyhydric alcohol is selected from the group consisting of: diethylene glycol claim 1 , triethylene glycol claim 1 , 1 claim 1 ,3-propanediol claim 1 , 2-methyl-1 claim 1 ,3-propanediol claim 1 , 1 claim 1 ,4-butanediol claim 1 , pentanediol claim 1 , neopentyl glycol claim 1 , 3-methyl-1 claim 1 ,5-pentanediol claim 1 , hexanediol claim 1 , 1 claim 1 ,4-cyclohexanedimethanol claim 1 , ...

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07-02-2019 дата публикации

PROCESS FOR THE PRODUCTION OF POLY(BUTYLENE TEREPHTHALATES)

Номер: US20190040192A1
Принадлежит:

The present invention relates to a process for the production of poly(butylene terephthalate) comprising the steps of: (i) providing a poly(butylene terephthalate) oligomer having an intrinsic viscosity (IV) of 0.25-0.35 dl/g, a carboxylic end group (CEG) content of 25-35 mmol/kg, and a ratio of IV:CEG of ≤15 dl/mmol; (ii) introducing said poly(butylene terephthalate) oligomer to a low-pressure reactor; and (iii) performing a polycondensation reaction in said low-pressure reactor by subjecting the poly(butylene terephthalate) oligomer to a pressure of ≥0.05 and ≤5.0 mbar at a temperature of 235 to 255° C., for such average residence time to obtain a poly(butylene terephthalate) having a ratio of IV:CEG of ≥18 dl/mmol, preferably ≥25 dl/mmol and having an IV of ≥0.45 dl/g; wherein steps (i), (ii) and (iii) are conducted in that order. Such process allows for the production of poly(butylene terephthalates) having a desired low CEG at given, desired high, IV using a poly(butylene terephthalate) oligomer having a relatively high CEG at given IV. Such process allows for the production of poly(butylene terephthalates) using poly(butylene terephthalate) oligomers obtained from an esterification process using PTA and 1,4-butanediol. 1. A process for the production of poly(butylene terephthalate) comprising the steps of:(i) providing a poly(butylene terephthalate) oligomer having an intrinsic viscosity (IV) of 0.25-0.35 dl/g, a carboxylic end group (CEG) content of 25-35 mmol/kg, and a ratio of IV:CEG of ≤15 dl/mmol;(ii) introducing said poly(butylene terephthalate) oligomer to a low-pressure reactor; and(iii) performing a polycondensation reaction in said low-pressure reactor by subjecting the poly(butylene terephthalate) oligomer to a pressure of ≥0.05 and ≤5.0 mbar at a temperature of 235 to 255° C., for such average residence time to obtain a poly(butylene terephthalate) having a ratio of IV:CEG of ≥18 dl/mmol and having an IV of ≥0.45 dl/g; the CEG is determined in ...

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18-02-2021 дата публикации

Medical devices containing compositions of poly(butylene succinate) and copolymers thereof

Номер: US20210046212A1
Принадлежит: Tepha Inc

Resorbable implants, coverings and receptacles comprising poly(butylene succinate) and copolymers thereof have been developed. The implants are preferably sterilized, and contain less than 20 endotoxin units per device as determined by the limulus amebocyte lysate (LAL) assay, and are particularly suitable for use in procedures where prolonged strength retention is necessary, and can include one or more bioactive agents. The implants may be made from fibers and meshes of poly(butylene succinate) and copolymers thereof, or by 3d printing molding, pultrusion or other melt or solvent processing method. The implants, or the fibers preset therein, may be oriented. These coverings and receptacles may be used to hold, or partially/fully cover, devices such as pacemakers and neurostimulators. The coverings, receptacles and implants described herein, may be made from meshes, webs, lattices, non-wovens, films, fibers, foams, molded, pultruded, machined and 3D printed forms.

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12-02-2015 дата публикации

CATALYST SOLUTION FOR USE IN PRODUCTION OF POLYESTER, AND METHOD FOR PRODUCING POLYESTER RESIN USING SAME

Номер: US20150045530A1
Принадлежит: Toray Industries, Inc.

A catalyst solution for polyester production includes a titanium compound (A) and an organic solvent (B), wherein particle diameter of particles included in the solution, which is measured by dynamic light scattering method and is subsequently determined by cumulant analysis method, is not greater than 200 nm. 110-. (canceled)11. A catalyst solution for polyester production , comprising a titanium compound (A) , an organic solvent (B) , and a compound (C) that has either a pyrrole ring or a pyridine ring and includes one or more oxygen atoms , wherein particle diameter of particles included in the solution , which is measured by dynamic light scattering method and is subsequently determined by cumulant analysis method , is not greater than 200 nm.12. The catalyst solution according to claim 11 , wherein content of the titanium compound (A) is not greater than 20% by weight.13. The catalyst solution according to claim 11 , wherein the titanium compound (A) is a titanate or a condensation product thereof of formula: (RO)Ti(OR)(wherein Rand Rare identical with or different from each other and respectively represent an aliphatic claim 11 , alicyclic or aromatic hydrocarbon group containing 1 to 10 carbon atoms claim 11 , wherein n indicates a range of 0 to 4 (including decimals)).14. The catalyst solution according to claim 11 , wherein the organic solvent (B) is an alcohol of formula: R(OH)(wherein Rrepresents an aliphatic claim 11 , alicyclic or aromatic hydrocarbon group or a heterocyclic ring containing 1 to 10 carbon atoms claim 11 , wherein m indicates either 1 or 2).15. The catalyst solution according to claim 11 , wherein a molar ratio (C/A) of content of the compound (C) to content of the titanium compound (A) is not less than 0.01 and less than 1.0.16. A production method of a catalyst solution for polyester production claim 11 , the catalyst solution comprising a titanium compound (A) and an organic solvent (B) claim 11 , wherein particle diameter of ...

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19-02-2015 дата публикации

COMPLEX METAL OXIDE, AND METHOD OF PREPARING POLYESTER USING THE SAME

Номер: US20150051366A1
Принадлежит:

Disclosed herein are a novel complex metal oxide catalyst, and a method of preparing polyester using the same. The metal-bound compound of the present invention has a higher catalytic activity as compared to an antimony catalyst and existing titanium catalysts to be easily synthesized and stabilized, have a sufficient polymerization activity even with a small amount, and be used as an environmentally friendly catalyst for polyester polymerization. In addition, when preparing polyester by using the complex metal oxide of the present invention, since catalytic activity caused by phosphorus (P) which is a thermal stabilizer used to decrease pyrolysis at the time of hot-melting and molding is not deteriorated, an excessive amount of phosphorus may be used as compared to the related art, such that pyrolysis less occurs, whereby the yellowing phenomenon may be decreased and high viscosity may be maintained. Therefore, the complex metal oxide may be usefully applied to the preparation of polyester having good physical properties, in particular, polyethylene terephthalate. 1. A complex metal oxide used as a catalyst for polyester polymerization , comprising:one kind of a metal (M) selected from the group consisting of magnesium (Mg), zinc (Zn), copper (Cu), manganese (Mn), calcium (Ca), and iron (Fe), and titanium (Ti) and aluminum (Al).2. The complex metal oxide of claim 1 , wherein it is titanium alkoxide represented by the following Chemical Formula 1 claim 1 , aluminum alkoxide represented by the following Chemical Formula 2 claim 1 , and a coprecipitate of a metal alkoxide represented by the following Chemical Formula 3:{'br': None, 'sup': '1', 'sub': '4', 'Ti(OR)\u2003\u2003[Chemical Formula 1]'}{'br': None, 'sup': '2', 'sub': '3', 'Al(OR)\u2003\u2003[Chemical Formula 2]'}{'br': None, 'sup': '3', 'sub': '2', 'M(OR)\u2003\u2003[Chemical Formula 3]'}{'sup': 1', '2', '3, 'sub': 1', '20', '2', '20', '3', '20', '6', '20', '1', '20', '7', '20', '7', '20, 'in Chemical ...

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25-02-2021 дата публикации

Advanced Processing of Absorbable Poly(p-dioxanone) Containing High Level of p-Dioxanone Monomer

Номер: US20210054141A1
Принадлежит:

The present invention is directed methods of making absorbable poly(p-dioxanone) pellets by melt polymerization of p-dioxanone conducted in a single reactor with a temperature regulator by charging a melt reactor with a mixture of p-dioxanone (PDO) monomer, initiator, catalyst, and optionally a dye; melt polymerizing the mixture in the melt reactor with sufficient agitation of the mixture to allow complete mixing of the monomer and for sufficient time to form a PDO polymer product having an unreacted PDO monomer content of at least 65 mole percent; placing the PDO polymer product under a vacuum to remove at least portion of unreacted PDO; discharging the PDO polymer product from the melt reactor directly into an in-line, underwater pelletizer to produce undried PDO pellets, collecting the undried PDO pellets, and storing the collected PDO pellets in the freezer or a vacuum chamber prior to drying. 1. A polymeric filament extruded from a PDO pellet made in accordance with the method of making absorbable poly(p-dioxanone) pellets by melt polymerization of p-dioxanone conducted in a single reactor with a temperature regulator , and comprising the steps of:i. charging a melt reactor with a mixture of p-dioxanone (PDO) monomer, initiator, catalyst, and optionally a dye;ii. melt polymerizing the mixture at a reaction temperature of between 95° C. and 145° C. in the melt reactor with sufficient agitation of the mixture to allow complete mixing of the monomer and for sufficient time to form a PDO polymer product of at least 65 mole percent having an unreacted PDO monomer content;iii. placing the PDO polymer product under a vacuum for about 60 to 180 minutes to remove at least portion of unreacted PDO, as measured by monomer content;iv. discharging the PDO polymer product from the melt reactor directly into an in-line, underwater pelletizer to produce undried PDO pellets,v. collecting the undried PDO pellets, andvi. storing the collected PDO pellets in the freezer or a ...

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26-02-2015 дата публикации

Polymers, the process for the synthesis thereof and compositions comprising same

Номер: US20150057424A1
Принадлежит: Roquette Freres SA

The present invention relates to copolymers, in particular poly(butylenesuccinate-co-furanoate) (PBSF) copolymers, which have advantageous mechanical properties, and also to polymeric compositions comprising them. It also relates to a process for preparing these polymers.

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05-03-2015 дата публикации

METHOD FOR THE PRODUCTION OF ALIPHATIC POLYESTERS

Номер: US20150065678A1
Принадлежит: UHDE INVENTA-FISCHER GMBH

The present invention relates to a method for the production of aliphatic polyesters in a two-step method. There are thereby added, in a first step, to a precondensate of an aliphatic dicarboxylic acid or to a mixture of aliphatic dicarboxylic acids and an aliphatic dialcohol or to a mixture of aliphatic dialcohols, further monomeric components, i.e. further aliphatic dicarboxylic acids and also a further aliphatic dialcohol, a polyester prepolymer being obtained. In a further step, polycondensation of the prepolymer obtained in the first step is effected. 1. A method for the production of a polyester or copolyester , in whicha) at least one aliphatic dicarboxylic acid with 2 to 12 carbon atoms and/or acid anhydrides derived therefrom and at least one aliphatic alcohol with 2 to 12 carbon atoms and at least two hydroxyl functionalities are mixed together and the dicarboxylic acid is dissolved in the dialcohol by means of a suitable temperature increase,b) the solution obtained in step a) is added to an esterification product which comprises at least one diester and/or at least one an oligoester that was obtained from at least one aliphatic dicarboxylic acid with at least one aliphatic alcohol, and made to react there,andc) the reaction product obtained from step b) is polycondensed or copolycondensed at reduced pressure relative to normal conditions.2. The method according to claim 1 , wherein the solution in step a) is produced at temperatures of 50° C. to 250° C.3. The method according to claim 1 , wherein the esterification product comprises the diester in an amount of at least 10% by weight.4. The method according to claim 1 , wherein the esterification product comprises claim 1 , in addition to the diester claim 1 , oligomers from the at least one dicarboxylic acid and the at least one alcohol with on average 2 to 10 claim 1 , repetition units.5. The method according to claim 1 , wherein claim 1 , in step a) claim 1 , the stoichiometric ratio of the totality of ...

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10-03-2016 дата публикации

METHOD FOR PRODUCING POLY-L-LACTIC ACID BY DIRECTLY POLYCONDENSATING L-LACTIC ACID

Номер: US20160068628A1
Принадлежит: TECHNISCHE UNIVERSITAET BERLIN

A method for producing high-molecular poly-L lactic acid by directly polycondensating L-lactic acid using a melt-phase condensation and a subsequent solid-phase condensation using acidic and supported solid catalysts. A method of using an acidic and supported solid catalyst for producing high-molecular poly-L lactic acid by directly polycondensating L-lactic acid, preferably supported and calcined zirconium sulfate is also disclosed. 1. A process for preparing poly-L-lactic acid by direct polycondensation of L-lactic acid by means of melt-phase condensation and subsequent solid phase condensation , wherein L-lactic acid is subjected in the presence of an acidic and supported solid-state catalyst to the melt phase condensation and the catalyst is removed from the melt before the subsequent solid phase condensation or from the end product after the solid phase condensation.2. The process as claimed in claim 1 , wherein calcined zirconium sulfate (Zr(SO)) which is coupled to a support is used as acidic solid-state catalyst.3. The process as claimed in claim 1 , wherein the support is a mesoporous material claim 1 , preferably selected from among SiO claim 1 , TiO claim 1 , AlO claim 1 , ZrO claim 1 , SbO claim 1 , CaO claim 1 , MgO and SnO.4. The process as claimed in claim 1 , wherein the acidic and supported solid-state catalyst has been produced by impregnation of a support with zirconium sulfate tetrahydrate and subsequent calcination of the supported zirconium sulfate tetrahydrate at from 200 to 600° C. claim 1 , preferably from 250 to 350° C.5. The process as claimed in claim 1 , wherein calcined zirconium sulfate which is coupled to SiOas support is used as acidic and supported solid-state catalyst.6. The process as claimed in claim 1 , wherein the melt phase condensation is carried out at from 150 to 200° C. with removal of the water liberated claim 1 , preferably under reduced pressure.7. The process as claimed in claim 1 , wherein the catalyst is removed from ...

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12-03-2015 дата публикации

Composite of filler and polymer resin and method for preparing the same

Номер: US20150073088A1

Disclosed is a composite of filler and polymer resin and a method for preparing the same, including preparing a thermoplastic resin composition by mixing a polymerization catalyst with a polymerizable thermoplastic resin, preparing a pre-pellet including a filler and a polymer resin by mixing a filler with the thermoplastic resin composition and heating to perform in-situ polymerization of the polymerizable thermoplastic resin to the polymer resin, and compounding the pre-pellet or the pre-pellet to which a polymer resin is further added to be pelletized.

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12-03-2015 дата публикации

METHOD FOR THE PREPARATION OF (POLYBUTYLENE-CO-ADIPATE TEREPHTHALATE) THROUGH THE IN SITU PHOSPHORUS CONTAINING TITANIUM BASED CATALYST

Номер: US20150073117A1
Принадлежит:

Biodegradable compositions containing an aliphatic-aromatic copolyester derived from aromatic polyesters. Methods of making the compositions through an in situ phosphorus containing titanium based catalyst and articles made from the compositions. 123.-. (canceled)24. A process for preparing an aliphatic-aromatic copolyester , comprising:(a) depolymerizing an aromatic polyester component, by reacting(i) the aromatic polyester component with(ii) a diol component selected from ethylene glycol, 1,2-propylene glycol, 1,3-propylene glycol, 1,2-butanediol, 2,3-butanediol, 1,4-butanediol, tetramethyl cyclobutanediol, isosorbide, 1,3-cyclohexanedimethanol isomers, 1,4-cyclohexanedimethanol isomers, hexylene glycol, bio-derived diols, and combinations thereof, in the presence of(iii) an adipic acid component selected from adipic acid, adipic acid oligomers, and combinations thereof,wherein reaction is carried out in a reactor; at a pressure that is at least atmospheric pressure, at a temperature from 160° C. to 250° C., under an inert atmosphere and with agitation, under conditions sufficient to depolymerize the aromatic polyester component into a molten mixture; and(b) increasing the temperature of the molten mixture under subatmospheric conditions and agitation to a temperature from 240° C. to 270° C., thereby forming the aliphatic-aromatic copolyester;wherein the process is carried out in the presence of the titanium catalyst composition comprising titanium and a color-reducing amount of a compound selected from phosphorus-containing compounds, nitrogen-containing compounds, boron-containing compounds, and combinations thereof.25. The process of claim 24 , wherein the diol component comprises 1 claim 24 ,4-butane diol.26. The process of claim 24 , whereinthe diol component comprises a diol selected from ethylene glycol, 1,2-propylene glycol, 1,3-propylene glycol, and combinations thereof; andthe process further comprises adding 1,4-butane diol to the molten mixture.27. The ...

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17-03-2016 дата публикации

Method to Manufacture PLA Using a New Polymerization Catalyst

Номер: US20160075821A1
Принадлежит: Purac Biochem BV

The invention relates to a method for manufacturing polylactide, comprising the steps of mixing lactide and a metal-coordination compound as polymerization catalyst to obtain a reaction mixture, polymerizing the lactide in liquid phase at a temperature of at least 150° C. to form polylactide in liquid phase and allowing the polylactide to solidify, characterized in that the polymerization catalyst comprises a metal-ligand coordination compound whereby the parent ligand answers the formula (I), whereby R represents an H atom, an aliphatic group, a halide atom or a nitro group and the metal is at least one of Zr and Hf. The invented catalysts show kinetics which is comparable to the kinetics of the known Sn-octoate catalyst. 2. The method according to claim 1 , characterized in that the R group is a methyl group.3. The method according to claim 1 , characterized in that the metal is Zr.4. The method according to claim 1 , characterized in that a co-initiator is added to the reaction mixture.5. The method according to claim 1 , characterized in that the amount of metal originating from the catalyst ranges between 1 and 2000 ppm.6. The method according to claim 1 , characterized in that the temperature of the liquid phase ranges between 160° C. and 220° C.7. The method according to claim 1 , characterized in that the liquid phase is subjected to a devolatilization step before solidifying the formed polylactide.8. The method according to claim 1 , characterized in that a catalyst deactivating agent is added to the liquid phase when at least 90% of the lactide is converted into polylactide.10. Polylactide containing a Zr-containing compound claim 1 , characterized in that the amount of Zr metal originating from the compound is 1-2000 ppm.11. Polylactide according to claim 10 , characterized in that the racemization rate of the lactoyl units within the polylactide during its manufacture is less than 2%.12. The method according to claim 2 , characterized in that the metal ...

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24-03-2016 дата публикации

IMPROVED PROCESS FOR THE PREPARATION OF MODIFIED POLY(ALKYLENE TEREPHTHALATE) EMPLOYING AN IN-SITU TITANIUM-CONTAINING CATALYST

Номер: US20160083511A1
Принадлежит:

Disclosed is an improved process for preparing a modified polyalkylene terephthalate by melt polycondensation followed optionally by solid state condensation comprising reacting an alkylene diol and polyethylene terephthalate, wherein polymerization occurs in the presence of a catalyst complex formed by reaction of tetra(alkyl) titanate and a compound selected from phosphorus-containing compounds, nitrogen-containing compounds, boroncontaining compounds, and combinations thereof. 1. A process for preparing a modified polyalkylene terephthalate from recycled polyethylene terephthalate , the process comprising:{'sub': 1', '8', '1', '8, 'forming a catalyst consisting of the reaction product of tetra(C-Calkyl) titanate and a complexing agent selected from the group consisting of phosphorus-containing compounds, nitrogen-containing compounds, boron-containing compounds, and combinations thereof, wherein the molar ratio of the complexing agent to the tetra(C-Calkyl) titanate is from about 0.2:1 to 0.90:1;'}{'sub': 2', '4, 'depolymerizing recycled polyethylene terephthalate by combining the recycled polyethylene terephthalate, in the presence of the catalyst, with a dihydric alcohol selected from the group consisting of C-Calkylene diols to obtain a molten mixture;'}{'sub': 3', '4, 'transesterifying the depolymerized recycled polyethylene terephthalate in the continued presence of the catalyst and a C-Calkylene diol, which alkylene diol is added during or after depolymerisation to form a molten mixture; and'}{'sub': 3', '4, 'polymerizing the molten mixture in the continued presence of the catalyst and C-Calkylene diol, which alkylene diol is added during or after depolymerisation such that the same or different alkylene diol can be present during depolymerization and polymerization, to yield modified polyalkylene terephthalate; and'}optionally subjecting the modified polyalkylene terephthalate to solid state polymerization to yield a modified polyalkylene terephthalate ...

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05-05-2022 дата публикации

Process for the production of a terephthalate polyester from a monomer mixture comprising a diester

Номер: US20220135735A1
Принадлежит: IFP ENERGIES NOUVELLES

A process for the production of a terephthalate polyester, containing a stage a) for preparing an esterification feedstock containing at least one mixing section fed with at least one terephthalic acid feedstock and one diester monomer feedstock, where the ratio of the total number of moles of diol units with respect to the total number of moles of terephthalate units introduced into the mixing section is between 1.0 and 2.0, the mixing section being operated at a temperature between 25° C. and 250° C. and at a pressure greater than or equal to 0.1 MPa, an esterification stage b) to produce at least one reaction effluent and one aqueous effluent, a polycondensation stage c) to obtain at least the terephthalate polyester and an effluent containing at least one diol monomer, and a stage d) of treatment of the diols to obtain a purified diol stream.

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26-03-2020 дата публикации

Biodegradable Triblock Copolymers and Implantable Medical Devices Made Therefrom

Номер: US20200095374A1
Принадлежит:

A biodegradable triblock copolymer comprising: an A-B-A′ structure wherein the A and A′ blocks each include polylactide, the B block includes from about 55 to about 100 mole percent of polytrimethylene carbonate and 0 to about 45 mole percent polylactide, and the biodegradable triblock copolymer overall includes from about 15 to about 25 mole percent of the polytrimethylene carbonate and from about 75 to about 85 mole percent of the polylactide. Also provided are compositions and implantable medical devices made therefrom. 1. A biodegradable triblock copolymer comprising:an A-B-A′ structure wherein the A and A′ blocks each include polylactide, the B block includes from about 55 to about 100 mole percent of polytrimethylene carbonate and 0 to about 45 mole percent polylactide, and the biodegradable triblock copolymer overall includes from about 15 to about 25 mole percent of the polytrimethylene carbonate and from about 75 to about 85 mole percent of the polylactide.219-. (canceled)20. The biodegradable triblock copolymer of claim 1 , wherein the B block includes from about 100 mole percent polytrimethylene carbonate and about 0 mole percent polylactic acid.21. The biodegradable triblock copolymer of claim 1 , wherein the B block includes from about 55 to about 95 mole percent polytrimethylene carbonate and about 5 to about 15 mole percent polylactic acid.22. The biodegradable triblock copolymer of claim 1 , wherein the B block includes from about 85 to about 95 mole percent polytrimethylene carbonate and about 5 to about 15 mole percent polylactic acid.23. The biodegradable triblock copolymer of claim 1 , wherein the B block includes from about 85 mole percent polytrimethylene carbonate and about 15 mole percent polylactic acid.24. The biodegradable triblock copolymer of claim 1 , wherein the biodegradable triblock copolymer overall includes about 20 mole percent of the polytrimethylene carbonate and about 80 mole percent of the polylactide.25. The biodegradable ...

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02-06-2022 дата публикации

POLYMERIZATION CATALYST FOR THE PRODUCTION OF POLYESTER AND METHOD OF PRODUCING POLYESTER USING THE SAME

Номер: US20220169784A1
Принадлежит:

Disclosed are a polymerization catalyst for the production of polyester, which includes an inorganic stannous (tin (II)) compound, and a method of producing polyester using the same. The polymerization catalyst for the production of polyester is safe without toxicity, has equal or higher catalytic activity compared to an antimony-based catalyst, may increase the polymerization reaction rate, may ensure a high viscosity level even when used in small amounts, may reduce the production of acetaldehyde, and may also improve the thermal stability and color of the polymer compared to those of a polyester polymer obtained by the related art. 1. A polymerization catalyst for production of polyester , the polymerization catalyst comprising an inorganic stannous (tin (II)) compound.2. The polymerization catalyst of claim 1 , wherein the inorganic stannous (tin (II)) compound is selected from the group consisting of stannous oxide claim 1 , stannous pyrophosphate claim 1 , stannous phosphate claim 1 , stannous tartrate claim 1 , stannous acetate claim 1 , stannous oxalate claim 1 , stannous stearate claim 1 , stannous oleate claim 1 , stannous gluconate claim 1 , stannous citrate claim 1 , stannous 2-ethylhexanoate claim 1 , stannous ethoxide claim 1 , stannous acetylacetonate claim 1 , and stannous glycolate.3. The polymerization catalyst of claim 1 , which is a polymerization catalyst for production of homopolyester.4. A composition for production of polyester claim 2 , the composition comprising the polymerization catalyst set forth in .5. The composition of claim 4 , which comprises the inorganic stannous (tin (II)) compound in an amount of 10 ppm to 200 ppm.6. The composition of claim 4 , which is a composition for production of homopolyester.7. A method of producing polyester by polycondensation of a polymerization starting material comprising an esterification product of a dicarboxylic acid component and a glycol component claim 4 , wherein a polymerization catalyst for ...

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23-04-2015 дата публикации

Sustainable Polyester Resin of Defined Acid Value

Номер: US20150111147A1
Принадлежит: XEROX CORPORATION

The disclosure describes a process for making a polyester resin of defined acid value using a temperature-sensitive reaction and dipropylene glycol as a reagent. 1. A process for making a polyester polymer in a single reactor comprising the steps of:(i) reacting at least one alcohol and at least one carboxylic acid under condensation reaction conditions to produce a polyester polymer, wherein said at least one alcohol comprises dipropylene glycol; and(ii) collecting said polyester polymer comprising an acid value (AV) of from about 10 to about 16 mg of KOH per gram of resin and a softening point of from about 114° C. to about 118° C.2. The process of claim 1 , wherein said at least one carboxylic acid is selected from the group consisting of terephthalic acid claim 1 , phthalic acid claim 1 , isophthalic acid claim 1 , fumaric acid claim 1 , trimellitic acid claim 1 , diethyl fumarate claim 1 , dimethyl itaconate claim 1 , cis-1 claim 1 ,4-diacetoxy-2-butene claim 1 , dimethyl fumarate claim 1 , diethyl maleate claim 1 , maleic acid claim 1 , succinic acid claim 1 , itaconic acid claim 1 , succinic acid claim 1 , cyclohexanoic acid claim 1 , succinic anhydride claim 1 , dodecylsuccinic acid claim 1 , dodecylsuccinic anhydride claim 1 , glutaric acid claim 1 , glutaric anhydride claim 1 , adipic acid claim 1 , pimelic acid claim 1 , suberic acid claim 1 , azelaic acid claim 1 , dodecanedioic acid claim 1 , dimethyl naphthalenedicarboxylate claim 1 , dimethyl terephthalate claim 1 , diethyl terephthalate claim 1 , dimethylisophthalate claim 1 , diethylisophthalate claim 1 , dimethylphthalate claim 1 , phthalic anhydride claim 1 , diethylphthalate claim 1 , dimethylsuccinate claim 1 , naphthalene dicarboxylic acid claim 1 , dimer diacid claim 1 , dimethylfumarate claim 1 , dimethylmaleate claim 1 , dimethylglutarate claim 1 , dimethyladipate claim 1 , dimethyl dodecylsuccinate claim 1 , and combinations thereof.3. The process of claim 1 , comprising at least one ...

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20-04-2017 дата публикации

HETEROATOM CONTAINING CYCLIC DIMERS

Номер: US20170107192A1
Принадлежит:

The present invention provides cyclic dimers of alpha acids and polymers derived therefrom. Also provided are processes for preparing and methods of using the cyclic dimers and the polymers derived from the cyclic dimers. 2. The process of claim 1 , wherein Ris hydrogen claim 1 , alkyl claim 1 , or substituted alkyl claim 1 , R claim 1 , R claim 1 , R claim 1 , and Rare hydrogen; Ris C-Calkyl; and n is from 1 to 10.4. The process of claim 3 , wherein R claim 3 , R claim 3 , R claim 3 , R claim 3 , Rand Rare hydrogen; Rand Rare C-Calkyl; and each of n and m is from 1 to 10.5. The process of claim 4 , wherein Rand Rare methyl; Y and Z are sulfur claim 4 , and each of n and m is 2.6. The process of claim 1 , wherein the polymer comprising repeat units of Formula (XX) has a number average molecular weight of at least about 2 claim 1 ,000 Da claim 1 , at least about 10 claim 1 ,000 Da claim 1 , at least about 100 claim 1 ,000 Da claim 1 , or at least about 1 claim 1 ,000 claim 1 ,000 Da.7. The process of claim 1 , wherein the polymer comprising repeat units of Formula (XX) contains less than about 5% by weight of free monomer.8. The process of claim 1 , wherein the reaction is conducted in the absence or presence of a catalyst.9. The process of claim 1 , wherein the temperature is from about 120° C. to about 180° C.10. The process of claim 1 , wherein the heating occurs in an extruder claim 1 , the extruder being a twin screw extruder claim 1 , a single screw extruder claim 1 , or an extruder thermoforming machine.11. An extrudate prepared by the process of .12. The process of claim 1 , wherein the process further comprises heating in the presence of a plurality of additional monomers to form a copolymer.13. The process of claim 12 , wherein the plurality of additional monomers is chosen from acrylates claim 12 , aminoacrylates claim 12 , alkylene succinates claim 12 , alkylene oxalates claim 12 , amides claim 12 , amino acids claim 12 , anhydrides claim 12 , arylates ...

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11-04-2019 дата публикации

Process for producing a flame-retardant polyester and flame-retardant polyester produced thereby

Номер: US20190106567A1
Принадлежит: Far Eastern New Century Corp

A process for producing a flame-retardant polyester includes step (a) and step (b). In step (a), a combination of a bis-hydroxy alkyl terephthalate monomer and an organic diacid monomer mixture which includes an aromatic dicarboxylic acid monomer and a carboxy-phosphinic acid monomer is subjected to an esterification reaction to form an esterification reaction product. In step (b), the esterification reaction product is subjected to a polycondensation reaction.

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09-06-2022 дата публикации

Method for Preparing High Molecular Weight Polybutylene Succinate

Номер: US20220177643A1
Автор: Herui Dou, Rong Lv, Xiaohang Xu
Принадлежит: Ningbo Dou Chemical Co Ltd

A method for preparing high molecular weight polybutylene succinate includes: (a) using maleic anhydride (MAH) and C1-C4 alcohols to produce dialkyl maleates and water, in which dialkyl fumarate is calculated as dialkyl maleate of an equivalent mole. A reactive distillation process is used for the purification and obtains dialkyl maleates; (b) selective hydrogenation of those dialkyl maleates in the presence of high pressure hydrogen to produce the corresponding dialkyl succinates; (c) condensation of dialkyl succinates with mostly 1,4-butanediol (BDO) and other aliphatic diols to produce high molecular weight polybutylene succinates by adding catalysts. Compared with the existing technologies, the present procedure uses a new source of raw bulk feedstocks, and circumvents or overcomes problems associated with the acidic monomer's corrosiveness, excessive formation of by-products, low yields of desired products and the relatively low molecular weight of the polybutylene succinate produced by existing technologies.

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18-04-2019 дата публикации

ENVIRONMENTALLY FRIENDLY DEMULSIFIERS

Номер: US20190111360A1
Принадлежит: Baker Hughes, a GE company, LLC

Environmentally friendly demulsifiers are useful to break emulsions, e.g. water-in-oil and oil-in-water emulsions, particularly oilfield emulsions, where the demulsifiers are polymers made by reacting a suitable resin with at least two different monomers, one having a Hansen solubility parameter similar to ethylene oxide and the other having a Hansen solubility parameter similar to propylene oxide, and where the polymers have an absence of ethylene oxide and/or propylene oxide. In a non-limiting embodiment, suitable resins include butyl resin, nonyl resin, nonyl/butyl resin, amyl resin, nonyl/butyl/amyl resin, phenol/formaldehyde resin, and combinations thereof. Suitable monomers include caprolactone, lactic acid, lactide, methacrylic acid ester, stearyl ester, hexyl ester, lauryl ester, urethane, ethylene adipate, vinyl esters, amides, allyl ethers, vinyl ethers, vinyl chloride, vinyl acetate, acrylic acid methyl ester, and combinations thereof. 1. A method for making demulsifiers comprising reacting at least two different monomers with a resin , where at least one of the two different monomers is selected from the group consisting of a monomer having a Hansen solubility parameter of from about 18 to about 22 that is not ethylene oxide , a monomer having a Hansen solubility parameter of from about 14 to about 18 that is not propylene oxide , and combinations thereof.2. The method of wherein the two different monomers are a monomer having a Hansen solubility parameter of from about 18 to about 22 which is not ethylene oxide and a monomer having a Hansen solubility parameter of from about 14 to about 18 which is not propylene oxide.3. The method of consists of reacting the resin with two different monomers with a resin claim 1 , where one of the monomers is a monomer having a Hansen solubility parameter between from about 18 to about 22 and is not ethylene oxide and the other monomer has a Hansen solubility parameter of from about 14 to about 18 and is not propylene ...

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03-05-2018 дата публикации

Polymer Compositions With PBSA Plasticizer

Номер: US20180118895A1
Принадлежит: Danimer Bioplastics Inc

A polymeric composition is disclosed which includes from about 40 to about 99 weight percent of a first polymer and from about 1 to about 60 weight percent of polybutylene(succinate-co-adipate) (“PBSA”). Preferably the first polymer is selected from the group consisting of polyvinyl chloride, polylactic acid, polyhydroxy alkanoates, and mixtures thereof. A method for making the composition is also disclosed.

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04-05-2017 дата публикации

Liquid Titanium-Based Catalyst And Method For Preparing Polyester Polymer Thereof

Номер: US20170121455A1
Принадлежит: Anqing Hexing Chemical., Ltd.

A liquid titanium-based catalyst and method for preparing polyester polymer thereof are disclosed herein. The catalyst is made by tetrabutyl titanate, 1-4 butanediol, phosphate ester, hydroxycarboxylic acid, TEOS, acetates of metal element through heating reactions in an appropriate amount of solvent. While the catalyst maintains a high activity, the synthetic slices have good hue, with high molecular weight, stable property, resistance to hydrolysis, moreover, the catalyst is a stable multicomponent liquid catalyst based on titanium, silicon. It can be directly added or diluted to add to the raw material ester or oligoester to be poly-condensed used for synthesis of polyesters which can be used in the production of fibers, engineering plastics, films, PET bottles, sheets and profiles, etc. 1: A liquid titanium-based catalyst comprising the following compositions (in mass ratio):1,4 butanediol 450-900 portionsTEOS and/or n-methyl silicate and/or n-propyl silicate 10.4-41.6 portionsAcetates or aluminum nitrate 10.7-42.8 portionsTetrabutyl titanate and/or tetraethyl titanate and/or tetraisopropyl titanate 228-340 portionsSolvent 92-2700 portionsHydroxycarboxylic acid 15-150 portionsPhosphate ester 273-546 portions2: The liquid titanium-based catalyst according to claim 1 , wherein the solvents are one or more of anhydrous ethanol claim 1 , cyclohexane claim 1 , toluene claim 1 , mixed xylene.3: The liquid titanium-based catalyst according to claim 1 , wherein the acetates are selected from one or more of acetates of IA claim 1 , IIA claim 1 , IIIA claim 1 , IIB claim 1 , IIIB claim 1 , VIIB claim 1 , VIIIB metal elements.4: The liquid titanium-based catalyst according to claim 1 , wherein the hydroxycarboxylic acids are one or more of citric acid claim 1 , L-lactic acid claim 1 , tartaric acid claim 1 , salicylic acid.5: The method liquid titanium-based catalyst according to claim 1 , wherein the phosphate esters are one or more of trimethyl phosphate claim 1 , ...

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04-05-2017 дата публикации

Fiber and method of manufacturing the same

Номер: US20170121859A1

A fiber is provided, which includes a polyester copolymerized of a diacid monomer, an esterified diacid monomer or a combination thereof with a polyol monomer. The diacid monomer, the esterified diacid monomer or a combination thereof includes (1) furan dicarboxylic acid, dialkyl furandicarboxylate, or a combination thereof or (2) furan dicarboxylic acid, dialkyl furandicarboxylate, or a combination thereof and spiro-diacid. The polyol monomer includes (3) C 2 -C 14 polyol or (4) C 2 -C 14 polyol and spiro-diol. The diacid monomer, the esterified diacid monomer or a combination thereof and the polyol monomer meet the following conditions: (a) The diacid monomer, the esterified diacid monomer or a combination thereof includes (2) furan dicarboxylic acid, dialkyl furandicarboxylate, or a combination thereof and spiro-diacid, (b) The polyol monomer includes (4) C 2 -C 14 polyol and spiro-diol, or (c) a combination thereof. The polyester has an inherent viscosity at 30° C. of 0.5 dL/g to 1.5 dL/g.

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24-07-2014 дата публикации

POLYLACTIDE RESIN HAVING EXCELLENT HEAT RESISTANCE AND PREPARATION METHOD THEREOF

Номер: US20140206834A1
Принадлежит: LG CHEM, LTD.

The present invention relates to a polylactide resin having excellent heat resistance, a preparation method thereof, and a polylactide resin composition including the same. 115-. (canceled)16. A preparation method of the polylactide resin , comprising the step ofcarrying out ring opening polymerization with lactide monomers in the presence of an organometallic complex catalyst of the following Chemical Formula 1, {'chemistry': {'@id': 'CHEM-US-00010', '@num': '00010', 'img': {'@id': 'EMI-C00010', '@he': '14.48mm', '@wi': '69.85mm', '@file': 'US20140206834A1-20140724-C00010.TIF', '@alt': 'embedded image', '@img-content': 'chem', '@img-format': 'tif'}}, 'br': None, 'Catalytic activity=kg(polymer)/g(cat)·hr\u2003\u2003[Equation 2]'}, 'wherein the organometallic complex has 10 or higher of a catalytic activity represented by the following Equation 2{'sup': 1', '3', '2, 'wherein n is an integer of 0˜15, p is an integer of 0˜2, M is Sn, Rand Rare the same as or different from each other, and each of them is hydrogen, substituted or unsubstituted C3 to C10 alkyl, substituted or unsubstituted C3 to C10 cycloalkyl, or substituted or unsubstituted C6 to C10 aryl, Ris substituted or unsubstituted C3 to C10 alkylene, substituted or unsubstituted C3 to C10 cycloalkylene, or substituted or unsubstituted C6 to C10 arylene, and each of X and Y is independently an alkoxy group or a carboxyl group.'}17. The preparation method according to claim 16 , wherein the compound of Chemical Formula 3 is added in the polymerization catalyst at a ratio of 1:200 claim 16 ,000˜1:100 claim 16 ,000 (mole/mole ratio) with respect to the lactide monomers.18. The preparation method according to claim 16 , wherein MXYis tin(II) 2-ethylhexanoate (Sn(Oct)).19. The preparation method according to claim 16 , wherein the carbodiimide component of Chemical Formula 2 is included in the polymerization catalyst in an amount of less than 0.1% by weight.20. The preparation method according to claim 16 , wherein ...

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11-05-2017 дата публикации

METHOD FOR PRODUCING BIODEGRADABLE POLYESTER RESIN AND BIODEGRADABLE RESIN PRODUCED THEREFROM

Номер: US20170129991A1
Принадлежит: LOTTE FINE CHEMICAL CO., LTD.

The present invention relates to a method for using a combination of two kinds of thermal stabilizers in a production process in order to improve the thermal stability of biodegradable polyester resins, and to biodegradable polyester resin produced therefrom. In said method, two kinds of thermal stabilizers improve thermal stability by acting complementarily with each other. Thus, a high temperature reaction is possible, and due to an increase in the reactivity, the reaction time is shortened and the molecular weight is increased. In addition, the obtained resin can provide high quality products, since the acid value thereof is reduced to improve the hydrolysis resistance thereof, and the chromaticity thereof is enhanced to thereby be capable of preventing a yellowing phenomenon of the final product. 1. A method of preparing a biodegradable resin , comprising:esterifying 1,4-butanediol and one or more dicarhoxylic acids selected from the group consisting of terephthalic acid (TA) or a derivative thereof and an aliphatic dicarboxylic acid having a backbone consisting of 2 to 6 carbon atoms by using a thermal stabilizer in which one or more compounds selected from a first group consisting of phosphate-based compounds and one or more compounds selected from a second group consisting of phosphite-based compounds and an acrylate-based compound are combined; andpolycondensing a product of the esterification reaction.2. The method of preparing a biodegradable resin according to claim 1 , wherein the first group includes triphenyl phosphate claim 1 , trimethyl phosphate claim 1 , triethyl phosphate claim 1 , isopropyl acid phosphate claim 1 , diisopropyi acid phosphate claim 1 , butyl acid phosphate claim 1 , octyl acid phosphate claim 1 , dioctyl acid phosphate claim 1 , isodecyl acid phosphate claim 1 , diisodecyl acid phosphate claim 1 , tridecanol acid phosphate claim 1 , and bis(tridecanol acid)phosphate.3. The method of preparing a biodegradable resin according to ...

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31-07-2014 дата публикации

PREPARATION METHOD OF POLYLACTIDE RESIN

Номер: US20140213752A1
Принадлежит: LG CHEM, LTD.

The present invention relates to a preparation method of a polylactide resin, in which the preparation method includes the step of performing ring opening polymerization of lactide monomers in the presence of an organometallic catalyst and an aromatic monomer scavenger, and the aromatic monomer scavenger is used in an amount of 0.1 to 20 parts by weight, based on 100 parts by weight of the lactide monomers. 1. A preparation method of a polylactide resin , comprising the step of performing ring opening polymerization of lactide monomers in the presence of an organometallic catalyst and an aromatic monomer scavenger , wherein the aromatic monomer scavenger is used in an amount of 0.1 to 20 parts by weight , based on 100 parts by weight of the lactide monomers.2. The preparation method according to claim 1 , wherein the aromatic monomer scavenger is one or more selected from the group consisting of ethyl benzene claim 1 , toluene claim 1 , xylene claim 1 , diphenyl ether claim 1 , benzene claim 1 , chlorobenzene claim 1 , and dichlorobenzene.3. The preparation method according to claim 1 , wherein the organometallic catalyst is added at a ratio of 0.001 to 1.0 mole claim 1 , based on 100 moles of the lactide monomers.4. The preparation method according to claim 1 , wherein the organometallic catalyst is a Sn-containing catalyst.5. The preparation method according to claim 4 , wherein the Sn-containing catalyst is a Sn-(Oct)catalyst.6. The preparation method according to claim 5 , wherein the ring opening polymerization is performed in the presence of an initiator containing a hydroxyl-containing compound.7. The preparation method according to claim 6 , wherein the hydroxyl-containing compound has carbon atoms of 8 or more.8. The preparation method according to claim 6 , wherein the initiator is added at a ratio of 0.001 to 1 mole claim 6 , based on 100 moles of the lactide monomers.9. The preparation method according to claim 1 , wherein the ring opening polymerization ...

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02-05-2019 дата публикации

METHOD FOR PREPARING POLYETHERESTER COPOLYMER

Номер: US20190127521A1
Принадлежит:

The present invention relates to a method for preparing a polyetherester copolymer having excellent economical efficiency by recycling unreacted diol and excellent physical properties. Accordingly, the preparation method may prepare a polyetherester copolymer of high purity having excellent economical efficiency by purifying a byproduct to separate a recycle stream including unreacted diol therefrom, and reusing the recycle stream. 1. A method for preparing a polyetherester copolymer , the method comprising:1) preparing an intermediate reaction product by transesterifying a reaction raw material including dicarboxylate, diol, and polyol in the presence of a reaction catalyst; and2) separating and recovering a reaction product and a byproduct by subjecting the intermediate reaction product to a condensation polymerization reaction, wherein the byproduct is purified to separate a recycle stream including unreacted diol therefrom such that the recycle stream is used as a reaction raw material for the step 1), wherein the byproduct includes diol and an oligomer of polyol, and the oligomer of polyol is removed by the purification.2. The method of claim 1 , wherein the oligomer of polyol is a cyclic oligomer having a degree of polymerization of 3 to 9.3. The method of claim 1 , wherein the purification is performed using a plurality of distillation columns in which a first distillation column and a second distillation column are connected in series.4. The method of claim 1 , wherein the purification is performed using a single distillation column claim 1 , and the recycle stream is discharged from a middle portion in the height direction of the single distillation column.5. The method of claim 1 , wherein the byproduct comprises 10 to 30 wt % of oligomer of polyol.6. The method of claim 1 , wherein the byproduct further comprises a low boiling point compound including water claim 1 , tetrahydrofuran claim 1 , and methanol claim 1 , and the low boiling point compound is ...

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19-05-2016 дата публикации

METHOXYPOLYETHYLENE GLYCOL-POLYLACTIC ACID BLOCK COPOLYMER AND PREPARATION METHOD THEREOF

Номер: US20160137775A1
Принадлежит: Suzhou High-Tech Bioscience Co., Ltd.

A methoxypolyethylene glycol-polylactic acid block copolymer is disclosed, the methoxypolyethylene glycol-polylactic acid block copolymer being a block copolymer formed by ring opening polymerization of D,L-lactide and methoxypolyethylene glycol. A mass ratio of the methoxypolyethylene glycol to the D,L-lactide is 1:0.55-0.65 or 1:0.73-0.89 or 1:0.91-0.99. A preparation method of the foregoing block copolymer is also provided. When the block copolymer is used as a carrier for preparing a drug micelle, the encapsulation efficiency of the drug micelle prepared after being re-dissolved by water can be greater than 90% at 12 hours. 1. A methoxypolyethylene glycol-polylactic acid block copolymer , wherein the methoxypolyethylene glycol-polylactic acid block copolymer is a block copolymer formed by ring opening polymerization of D ,L-lactide and methoxypolyethylene glycol , and wherein a mass ratio of the methoxypolyethylene glycol to the D ,L-lactide is 1:0.55-0.65 or 1:0.73-0.89 or 1:0.91-0.99.2. A method of preparing the methoxypolyethylene glycol-polylactic acid block copolymer according to claim 1 , the method comprising:weighing D,L-lactide and methoxypolyethylene glycol with a formula ratio for standby application, subjecting methoxypolyethylene glycol with a formula ratio to vacuum drying for 2-8 hours at 60-130° C. in a reactor, performing nitrogen displacement, then adding the D,L-lactide with the formula ratio, then adding a metal catalyst, then performing evacuation, performing nitrogen displacement for three times after the D,L-lactide is completely fused, then performing evacuation, ensuring that the reactor has a negative pressure and is sealed or protected by nitrogen, then raising the temperature to 125-150° C., reacting for 6-20 hours, thus obtaining a pale yellow clear viscous liquid after the reaction is completed; adding an organic solvent in the pale yellow clear viscous liquid for dissolution, stirring for 30-50 minutes, then continuously adding ...

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21-05-2015 дата публикации

PROCESS FOR THE PRODUCTION OF POLY(ETHYLENE 2,5-FURANDICARBOXYLATE) FROM 2,5-FURANDICARBOXYLIC ACID AND USE THEREOF, POLYESTER COMPOUND AND BLENDS THEREOF

Номер: US20150141584A1
Принадлежит: NATURA COSMETICOS S.A.

The present invention generally concerns polyester compounds derived from renewable monomer materials and manufacturing process thereof. The invention further pertains to polyester blends presenting improved maximum elongation characteristic. 1. Process for the production of poly(ethylene 2 ,5-furandicarboxylate) from 2 ,5-furandicarboxylic acid comprising the steps of:(1) esterification of 2,5-furandicarboxylic acid with ethylene glycol in the presence of 3,4-furandicarboxylic acid and triol in the presence of at least one catalyst in order to obtain a compound that is subsequently submitted to(2) polycondensation in the presence of at least one catalyst.2. Process claim 1 , according to claim 1 , wherein the triol used in the step (1) is tris hydroxy methyl propane.3. Process claim 1 , according to claim 1 , wherein the catalyst used in steps (1) or (2) is titanium isopropoxide and/or antimony.4. Process claim 1 , according to claim 1 , wherein the 2 claim 1 ,5-furandicarboxylic acid used in the step (1) is previously purified by fractionation and washing steps.5. Process claim 4 , according to claim 4 , wherein the fractionation is carried out by adjusting the pH to 5-6 and filtered to remove the first part of the precipitate.6. Process claim 5 , according to claim 5 , comprising a second step wherein the solution is adjusted to pH 1-2 to obtain total precipitation claim 5 , before cooling to 10° C. and filtering to obtain purified 2 claim 5 ,5 furandicarboxylic acid7. Process claim 5 , according to claim 5 , wherein the pH is controlled by adding concentrated HCl.8. Process claim 4 , according to claim 4 , wherein the washing is carried out twice with ice water and five times with room temperature water.9. Poly(ethylene 2 claim 1 ,5-furandicarboxylate) obtained by the process according to .10. Poly(ethylene 2 claim 9 ,5-furandicarboxylate) according to comprising a number average molecular weight (Mn) in the region of 35 claim 9 ,000 and 46 claim 9 ,000gmol.11. ...

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28-05-2015 дата публикации

PROCESS FOR IMMORTAL RING-OPENING POLYMERISATION OF CYCLIC ESTERS AND CYCLIC CARBONATES

Номер: US20150148516A1
Принадлежит:

The present invention discloses new catalyst systems based on complexes of divalent metals supported by chelating phenoxy ligands for immortal ring-opening polymerisation of cyclic esters and cyclic carbonates. 17-. (canceled)9. The process of claim 8 , wherein an amount of the alcohol or the poly-ol is of from 1 to 10 claim 8 ,000 equivalents per the divalent metal.10. The process of claim 8 , wherein the system comprises the alcohol claim 8 , wherein the alcohol is R′OH claim 8 , and wherein R′ is a primary or secondary alkyl residue or benzylic group.12. The process of claim 8 , wherein the system comprises the alcohol claim 8 , wherein the alcohol is functionalized claim 8 , and wherein the ring-opening polymerisation is carried out in styrene in order to prepare end-functionalised polymers.13. The process of claim 12 , wherein the functionalised alcohol is selected from TEMPO-OH claim 12 , HEMA or hydroxy-alkoxyamines.14. The process of claim 12 , further comprising using the end-functionalised polymers to prepare in situ copolymers of lactide or TMC and styrene.15. Polymers or copolymers obtained by the process of .16. The polymers or copolymers of claim 15 , wherein the polymers or copolymers exhibit a unimodal molecular weight distribution ranging from 1.1 to 5.0.17. The polymers or copolymers of claim 15 , wherein the polymers or copolymers exhibit a number average molecular weight Mranging from 1 claim 15 ,000 to 1 claim 15 ,000 claim 15 ,000 g/mol.18. Copolymers obtained by the process of .20. The process of claim 8 , wherein the ring-opening polymerization is carried out in solution in an organic solvent.21. The process of claim 8 , wherein the ring-opening polymerization is carried out in melt in the absence of solvent.22. The process of claim 8 , wherein the ring-opening polymerization is carried out at a temperature ranging from 20° C. to 200° C.23. The process of claim 8 , wherein the ring-opening polymerization is carried out at a pressure ranging ...

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10-06-2021 дата публикации

POLYCONDENSATION CATALYST FOR PRODUCING POLYESTER AND PRODUCTION OF POLYESTER USING THE SAME

Номер: US20210170371A1
Автор: KAMON Akihiro, SOGA Yuhei
Принадлежит: SAKAI CHEMICAL INDUSTRY CO., LTD.

The invention provides a polycondensation catalyst for producing polyester by an esterification reaction or a transesterification reaction of a dicarboxylic acid or an ester-forming derivative thereof and a glycol, wherein the polycondensation catalyst comprises particles of a water-insoluble or hardly water-soluble phosphate having on the surfaces a coating layer of titanic acid in an amount, of 0.1 to 100 parts by weight in terms of TiOper parts by weight of the phosphate. 1. A polycondensation catalyst for producing polyester by an esterification reaction or a transesterification reaction of a dicarboxylic acid or an ester-forming derivative thereof and a glycol , wherein the polycondensation catalyst comprises particles of a water-insoluble or hardly water-soluble phosphate having on the surfaces a coating layer of titanic acid in an amount of 0.1 to 100 parts by weight in terms of TiOper 100 parts by weight of the phosphate.2. The polycondensation catalyst according to claim 1 , wherein the phosphate is an orthophosphate claim 1 , a metaphosphate claim 1 , a pyrophosphate claim 1 , a phosphate glass claim 1 , a phosphite or a hypophosphite.3. The polycondensation catalyst according to claim 1 , wherein the counter ion of the phosphate anion is at least one cation of a metal selected from the group consisting of alkaline earth metals claim 1 , aluminum claim 1 , titanium claim 1 , zirconium claim 1 , and zinc.4. The polycondensation catalyst according to claim 3 , wherein the alkaline earth metal is calcium or magnesium.5. The polycondensation catalyst according to claim 1 , wherein the phosphate is dibasic calcium phosphate claim 1 , tribasic calcium phosphate claim 1 , calcium pyrophosphate claim 1 , calcium dihydrogenpyrophosphate claim 1 , magnesium pyrophosphate or magnesium metaphosphate.6. The polycondensation catalyst according to claim 1 , wherein the particles of the phosphate have on the surfaces a coating layer formed of titanic acid in an amount of ...

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07-05-2020 дата публикации

Copolyester Material with Low Melting Point, Spinning and Weaving Functions and Method for Forming the Copolyester Material

Номер: US20200141030A1
Принадлежит:

A method for forming a copolyester material includes preparing a solution of monomers, applying a polymerization to form a copolyester having a low melting point, spinning the copolyester into fiber threads to form a copolyester fiber, weaving or knitting the copolyester fiber with a common fiber to form a composite cloth having a sheet shape, cutting the composite cloth to form a determined shape, applying a hot-press process on the composite cloth under a temperature of about 120° C. to 200° C., to release tackiness of the copolyester, so that the copolyester fiber and the common fiber are bonded tightly and closely, and forming a tough film on a surface of the composite cloth by the copolyester, so that the composite cloth has functions of stiffness and abrasion resistance by the tough film. 1. A method for forming a copolyester material , comprising:preparing a solution of monomers;applying a polymerization on the solution of monomers to form a copolyester having a low melting point;spinning the copolyester into fiber threads to form a copolyester fiber;weaving or knitting the copolyester fiber of the copolyester with a fiber into cloth, to form a composite cloth having a sheet shape;cutting the composite cloth to form a determined shape;applying a hot-press process on the composite cloth under a temperature of about 120° C. to 200° C., to release tackiness of the copolyester, such that the copolyester fiber and the fiber are bonded tightly and closely; andthe tackiness released from the copolyester during the hot-press process forming a film on a surface of the composite cloth by the copolyester in the composite cloth, such that the composite cloth has stiffness and abrasion resistance by presence of the film;wherein:the copolyester has an intrinsic viscosity after the polymerization, and the copolyester is spun into the fiber threads and forms the copolyester fiber by the intrinsic viscosity;the tackiness released from the copolyester during the hot-press ...

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07-06-2018 дата публикации

A ONE STEP PROCESS FOR THE PELLETISATION OF POLY LACTIC ACID WITHOUT MELT PROCESSING

Номер: US20180155494A1
Принадлежит:

The present invention relates to a one step process for the palletization of poly lactic acid of molecular weight in the range of 6-8 lakhs without melt processing such that the pellets obtained exhibit minimal molecular weight reduction. The molecular weight of poly lactic acid (PLA) in the obtained pellets is retained in the range of 6-8 lakhs. 1. A one step process for the synthesis of PLA pellets comprising dissolving poly lactic acid of molecular weight in the range of 6-8 lakhs in a solvent followed by extrusion at the temperature ranging from 25° C. to 30° C. to obtain fibre morphologies , said fibres are cut to obtain pellets , wherein the molecular weight of PLA in the pellets is retained in the range of 6-8 lakhs.2. The process as claimed in claim 1 , wherein said pellets are selected from flat-filaments claim 1 , oblong non porous or hollow non porous pellets.3. The process as claimed in claim 1 , wherein the lactide content of the pellets is in a range from 0-10%.4. The process as claimed in claim 1 , wherein said solvent for dissolution is selected from dichloromethane and chloroform claim 1 , said solvent is chloroform.5. The process as claimed in claim 1 , wherein process of preparation of production of high molecular weight poly-l-lactic acid lactide claim 1 , comprising the following steps:a) carrying out ring opening polymerization in the presence of a suitable catalyst;b) subjecting compound of step (a) to solid state polymerization to obtain high molecular weight poly-l-lactic acid with low lactide content;6. The process as claimed in claim 5 , wherein said ring opening polymerization is carried out at the temperature ranging from 140-220° C. for a time period ranging from 0-60 hours; said ring opening polymerization is carried out at 140° C. for 75 minutes.7. The process as claimed in claim 5 , wherein said solid state polymerization is carried out at temperature ranging from 110-140° C. for a time period ranging from 1 to 384 hours to get high ...

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23-05-2019 дата публикации

LACTIDE COPOLYMERS AND RING-OPENED LACTIDE COPOLYMERS

Номер: US20190153153A1
Принадлежит:

A process of forming a lactide copolymer includes forming a dimethylidene lactide molecule from an L-lactide molecule. The process also includes forming a functionalized lactide monomer from the dimethylidene lactide molecule. The process includes forming a mixture that includes the functionalized lactide monomer and a bisphenol A (BPA) monomer or a BPA-derived monomer. The process further includes polymerizing the mixture to form a lactide copolymer. 2. The compound of claim 1 , wherein the compound reacts with a second monomer to form a lactide copolymer.3. The compound of claim 2 , wherein the lactide copolymer participates in a reaction to form a ring-opened lactide copolymer.4. The compound of claim 2 , wherein the second monomer is bisphenol A diglycidyl ether (DGEBA).5. The compound of claim 2 , wherein the second monomer is bisphenol A (BPA).8. The compound of claim 2 , wherein the lactide copolymer participates in a reaction to form a ring-opened lactide copolymer claim 2 , and wherein the ring-opened lactide copolymer is cross-linked with moieties selected from the group consisting of epoxies claim 2 , isocyanates claim 2 , carbonates claim 2 , esters claim 2 , and combinations thereof.10. The compound of claim 9 , wherein the compound reacts with a second monomer to form a lactide copolymer.11. The compound of claim 10 , wherein the lactide copolymer participates in a reaction to form a ring-opened lactide copolymer.12. The compound of claim 10 , wherein the second monomer is selected from the group consisting of bisphenol A (BPA) and BPA diglycidyl ether (DGEBA).15. The compound of claim 10 , wherein the lactide copolymer participates in a reaction to form a ring-opened lactide copolymer claim 10 , and wherein the ring-opened lactide copolymer is cross-linked with moieties selected from the group consisting of epoxies claim 10 , isocyanates claim 10 , carbonates claim 10 , esters claim 10 , and combinations thereof.17. The compound of claim 16 , wherein ...

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21-05-2020 дата публикации

Method for preparing polyesters

Номер: US20200157277A1
Принадлежит: Technip Zimmer GmbH

The present application relates to a process for preparing polyesters comprising reacting a dicarboxylic acid with butanediol in the presence of a catalyst, wherein in the process an aluminosilicate is present, as well as the use of aluminosilicates in such a process.

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23-06-2016 дата публикации

ABSORBABLE COPOLYMERS WITH IMPROVED THERMAL STABILITY

Номер: US20160177026A1
Принадлежит: POLY-MED, INC.

The present invention relates to absorbable block copolymers with improved characteristics including thermal stability, molecular weight consistency, inherent viscosity retention following melt extrusion, and fibers made from the polymers exhibit increased strength. 1. An absorbable aliphatic polyester copolymer comprising:a polyaxial core, with at least three axes, including a pre-polymer;wherein the at least three axes comprise polymeric chains;at least one flexible linking segment; andat least one polymeric end graft comprising repeat units derived from at least one cyclic monomer capable of crystallization, the at least one polymeric end graft attached to each of the at least three axes.2. The absorbable aliphatic polyester copolymer of claim 1 , wherein the polyaxial core comprises crystallizable polymeric chain segments.3. The absorbable aliphatic polyester copolymer of claim 1 , wherein the polyaxial core comprises amorphous chain segments.4. The absorbable aliphatic polyester copolymer of claim 1 , wherein the flexible linking segment and the crystallizable cyclic monomer share a common monomer.5. The absorbable aliphatic polyester copolymer of claim 1 , wherein the flexible linking segments are comprised of the same prepolymer as the polyaxial core and the same crystallizable cyclic monomer as the at least one polymeric end grafts.6. The absorbable aliphatic polyester copolymer of claim 1 , wherein the prepolymer may be a homopolymer claim 1 , copolymer or terpolymer formed from the group consisting of L claim 1 ,L-lactide and D claim 1 ,L-lactide claim 1 , glycolide claim 1 , substituted glycolides claim 1 , para-dioxanone claim 1 , 1 claim 1 ,5-dioxepan-2-one claim 1 , trimethylene carbonate claim 1 , epsilon-caprolactone claim 1 , alpha-Angelica lactone claim 1 , gamma-valerolactone and delta-valerolactone claim 1 , or combinations thereof.7. The absorbable aliphatic polyester copolymer of claim 6 , wherein the pre-polymer is derived from epsilon- ...

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28-05-2020 дата публикации

POLYESTER COMPOSITIONS WHICH COMPRISE TETRAMETHYLCYCLOBUTANDIOL AND ETHYLENE GLYCOL, WITH IMPROVED CATALYST SYSTEM

Номер: US20200165379A1
Принадлежит: EASTMAN CHEMICAL COMPANY

Described as one aspect of the invention are polyester compositions comprising at least one polyester which comprises: 2. The polyester composition of claim 1 , further comprising: (c) a catalyst/stabilizer component which comprises: (i) titanium atoms in the range of 10-60 ppm based on polymer weight claim 1 , (ii) manganese atoms in the range of 10-100 ppm based on polymer weight claim 1 , and (iii) phosphorus atoms in the range of 10-200 ppm based on polymer weight.3. The polyester composition of claim 2 , wherein the catalyst/stabilizer component comprises tin atoms in the range of 0-20 ppm based on polymer weight.4. The polyester composition of claim 2 , wherein the catalyst/stabilizer component comprises no intentionally added tin atoms.5. The polyester composition of claim 1 , wherein 2 claim 1 ,2 claim 1 ,4 claim 1 ,4-tetramethyl-1 claim 1 ,3-cyclobutanediol is present in the amount of about 32 to about 38 mole %.6. The polyester composition of claim 1 , wherein the 2 claim 1 ,2 claim 1 ,4 claim 1 ,4-tetramethyl-1 claim 1 ,3-cyclobutanediol residues is a mixture comprising about 55 to about 65 mole % of cis-2 claim 1 ,2 claim 1 ,4 claim 1 ,4-tetramethyl-1 claim 1 ,3-cyclobutanediol residues and about 35 to about 45 mole % of trans-2 claim 1 ,2 claim 1 ,4 claim 1 ,4-tetramethyl-1 claim 1 ,3-cyclobutanediol residues.7. The polyester composition of claim 1 , wherein the inherent viscosity of the polyester is from 0.54 to 0.65 dL/g.8. The polyester composition of claim 1 , wherein the polyester has a Tof 102 to 108° C.9. The polyester composition of claim 2 , wherein the weight ratio of P to total catalyst is from 0.15:1 to 1.0:1.10. The polyester composition of claim 2 , wherein the weight ratio of Ti to Mn is from 0.8:1 to 1.9:1.11. (canceled)12. The polyester composition of claim 2 , comprising at least one phosphorus compound chosen from at least one of the following: triaryl phosphates claim 2 , alkyl diaryl phosphates claim 2 , and mixed alkyl aryl ...

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28-05-2020 дата публикации

Advanced Processing of Absorbable Poly(p-dioxanone) Containing High Level of p-Dioxanone Monomer

Номер: US20200165380A1
Принадлежит:

The present invention is directed methods of making absorbable poly(p-dioxanone) pellets by melt polymerization of p-dioxanone conducted in a single reactor with a temperature regulator by charging a melt reactor with a mixture of p-dioxanone (PDO) monomer, initiator, catalyst, and optionally a dye; melt polymerizing the mixture in the melt reactor with sufficient agitation of the mixture to allow complete mixing of the monomer and for sufficient time to form a PDO polymer product having an unreacted PDO monomer content of at least 65 mole percent; placing the PDO polymer product under a vacuum to remove at least portion of unreacted PDO; discharging the PDO polymer product from the melt reactor directly into an in-line, underwater pelletizer to produce undried PDO pellets, collecting the undried PDO pellets, and storing the collected PDO pellets in the freezer or a vacuum chamber prior to drying. 1. A method of making absorbable poly(p-dioxanone) pellets by melt polymerization of p-dioxanone conducted in a single reactor with a temperature regulator , and comprising the steps of:i. charging a melt reactor with a mixture of p-dioxanone (PDO) monomer, initiator, catalyst, and optionally a dye;ii. melt polymerizing the mixture at a reaction temperature of between 95° C. and 145° C. in the melt reactor with sufficient agitation of the mixture to allow complete mixing of the monomer and for sufficient time to form a PDO polymer product having an unreacted PDO monomer content of at least 65 mole percent;iii. placing the PDO polymer product under a vacuum for about 60 to 180 minutes to remove at least portion of unreacted PDO, as measured by monomer content;iv. discharging the PDO polymer product from the melt reactor directly into an in-line, underwater pelletizer to produce undried PDO pellets,v. collecting the undried PDO pellets, andvi. storing the collected PDO pellets in the freezer or a vacuum chamber prior to drying.2. A method of claim 1 , wherein the melt ...

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28-05-2020 дата публикации

LACTIDE COPOLYMERS AND RING-OPENED LACTIDE COPOLYMERS

Номер: US20200165381A1
Принадлежит:

An article of manufacture. The article of manufacture includes a ring-opened lactide copolymer. The ring-opened lactide copolymer is formed in a process that includes reacting a functionalized lactide monomer with a BPA-derived monomer. The reaction forms a lactide copolymer, which is reacted to form the ring-opened lactide copolymer. 1. An article of manufacture , comprising a ring-opened lactide copolymer.4. The article of manufacture of claim 4 , wherein the ring-opened lactide copolymer is a component of a resin.5. The article of manufacture of claim 4 , wherein the resin is a thermoset epoxy resin.6. The article of manufacture of claim 1 , wherein the article of manufacture is selected from the group consisting of: a coating claim 1 , an electrical insulator claim 1 , a fiber-reinforced plastic claim 1 , and an adhesive.7. The article of manufacture of claim 1 , wherein the ring-opened lactide copolymer is cross-linked by crosslinking moieties.8. The article of manufacture of claim 7 , wherein the cros slinking moieties are selected from the group consisting of epoxies claim 7 , isocyanates claim 7 , carbonates claim 7 , esters claim 7 , and combinations thereof.9. The article of manufacture of claim 1 , wherein the ring-opened lactide copolymer is formed in a process that includes a reaction to form a lactide copolymer.10. The article of manufacture of claim 9 , wherein the reaction is a polymerization reaction between a functionalized lactide monomer and a difunctional epoxide monomer.12. The article of manufacture of claim 10 , wherein the difunctional epoxide monomer is bisphenol A diglycidyl ether. Plastics are typically derived from a finite and dwindling supply of petrochemicals, resulting in price fluctuations and supply chain instability. Replacing non-renewable petroleum-based polymers with polymers derived from renewable resources may be desirable. However, there may be limited alternatives to petroleum-based polymers in certain contexts. To ...

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08-07-2021 дата публикации

COPOLYMER BLENDS

Номер: US20210206963A1
Принадлежит:

Copolymer blends comprising a first copolymer and a second copolymer, wherein the first and second copolymers each independently comprise units of A and B as defined herein. 8. The copolymer blend according to claim 1 , wherein each Ris identical.13. The copolymer blend according to claim 1 , wherein the first copolymer comprises at least two units selected from B(i) claim 1 , B(ii) and B(iii).14. The copolymer blend according to claim 13 , wherein the second copolymer comprises at least two units selected from B(i) claim 13 , B(ii) and B(iii).15. The copolymer blend according to claim 13 , wherein each of the first copolymer and/or the second copolymer and/or claim 13 , when present claim 13 , the third copolymer comprise units of all three of B(i)-(iii).17. The copolymer according to claim 16 , comprising B(i) and B(ii).22. The copolymer according to claim 16 , wherein each Ris identical.27. The copolymer according to claim 16 , comprising units of all three of (a)-(c).30. The copolymer blend or copolymer according to claim 1 , wherein each Rand/or each R claim 1 , when present claim 1 , is independently an optionally substituted straight-chain claim 1 , branched or cyclic Cto Csaturated alkylene claim 1 , optionally a Cto Coptionally substituted saturated alkylene claim 1 , optionally a Cto Coptionally substituted saturated alkylene claim 1 , and optionally Cto Coptionally substituted saturated alkylene claim 1 , optionally wherein Ris unsubstituted.31. The copolymer blend or copolymer according to claim 1 , wherein each Rand/or each R claim 1 , when present claim 1 , is independently a branched or unbranched moiety claim 1 , optionally wherein one or more instances of Ris branched claim 1 , optionally wherein all instances of Rare branched.32. The copolymer blend or copolymer according to claim 1 , wherein (i) claim 1 , (ii) and/or claim 1 , when present claim 1 , (iii) is of non-renewable origin.33. (canceled)34. An article comprising a copolymer blend or ...

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30-06-2016 дата публикации

FUNCTIONALIZED POLYMER COMPOSITIONS

Номер: US20160185899A1
Принадлежит:

The invention relates to functionalized polymers including homopolymers and copolymers and their uses in industrial applications and in agricultural applications. In particular, the homopolymers and copolymers may be, for example, used in polymer blends, used as nutritives and in feed compositions, and used in combination with a pharmaceutical or nutritive. 2. The process of claim 1 , wherein the acid catalyst is stannous octoate.3. The process of claim 1 , wherein dehydration comprises azeotropic distillation.4. The process of claim 1 , where in the homopolymer or copolymer produced contains less than 2% of a free monomer.5. The process of claim 1 , where in the homopolymer or copolymer produced contains less than 1% of a free monomer.6. The process of claim 1 , where in the homopolymer or copolymer produced contains less than 0.5% of a free monomer.7. The process of claim 1 , wherein Z is sulfur claim 1 , Ris methyl claim 1 , n is 1 claim 1 , and Ris not present.9. The process of claim 8 , wherein the acid catalyst is stannous octoate.10. The process of claim 8 , wherein dehydration comprises azeotropic distillation.11. The process of claim 8 , where in the homopolymer or copolymer produced contains less than 2% of a free monomer.12. The process of claim 8 , where in the homopolymer or copolymer produced contains less than 1% of a free monomer.13. The process of claim 8 , where in the homopolymer or copolymer produced contains less than 0.5% of a free monomer.14. The process of claim 8 , wherein Z is sulfur and Ris methyl.16. The process of claim 15 , wherein dehydration conditions comprise azeotropic distillation.17. The process of claim 15 , wherein stannous octoate is added after azeotropic distillation under nitrogen at a temperature of about 120° C. to about 150° C. for about 4 to about 5 hours. This application is a divisional application of U.S. application Ser. No. 13/763,135, filed Feb. 8, 2013, which claims the priority of U.S. provisional application No ...

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29-06-2017 дата публикации

TISSUE ENGINEERING SCAFFOLD MATERIAL AND BIODEGRADABLE POLYESTER ELASTOMER THEREOF

Номер: US20170182210A1
Принадлежит:

Disclosed is a biodegradable polyester elastomer which is formed by an esterification reaction between an acidic compound and an alcohol compound using a superacidic catalyst. Thereby, the reaction time of the esterification reaction can be reduced remarkably. 1. A biodegradable polyester elastomer characterized in that it is formed by an esterification reaction between an acidic compound and an alcohol compound with a superacidic catalyst.2. The biodegradable polyester elastomer according to claim 1 , wherein the superacidic catalyst is selected from zirconium oxides with sulfate ion (ZrO/SO) claim 1 , titanium oxides with sulfate ion (TiO/SO) claim 1 , stannum oxides with sulfate ion (SnO/SO) claim 1 , hafnium oxides with sulfate ion (HfO/SO) claim 1 , iron oxides with sulfate ion (FeO/SO) claim 1 , aluminum oxides with sulfate ion (AlO/SO) claim 1 , and any combination thereof.3. The biodegradable polyester elastomer according to claim 1 , wherein the superacidic catalyst is in an amount between 0.01 to 1.00 wt % based on 100 wt % of the total weight of the acidic compound and the alcohol compound.4. The biodegradable polyester elastomer according to claim 1 , wherein the acidic compound is selected from polybasic acids having more than 6 carbon atoms claim 1 , the alcohol compound is selected from polyhydric alcohols having 4 to 10 carbon atoms claim 1 , dihydric alcohols having 4 to 10 carbon atoms claim 1 , and any combination thereof.5. The biodegradable polyester elastomer according to claim 4 , wherein the molar ratio of the alcohol compound to the acidic compound is 2:1 or greater than 2:1.6. The biodegradable polyester elastomer according to claim 1 , wherein the acidic compound is sebacic acid claim 1 , and the alcohol compound is glycerol.7. The biodegradable polyester elastomer according to claim 1 , wherein the esterification reaction is carried out at a temperature in the range of 120 to 170° C.8. The biodegradable polyester elastomer according to ...

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09-07-2015 дата публикации

HETEROATOM CONTAINING CYCLIC DIMERS

Номер: US20150191444A1
Принадлежит:

The present invention provides cyclic dimers of alpha acids and polymers derived therefrom. Also provided are processes for preparing and methods of using the cyclic dimers and the polymers derived from the cyclic dimers. 2. The process of claim 1 , wherein the acid catalyst is p-toluene sulfonic acid; the reaction mixture is heated to a temperature from about 100° C. to about 150° C.; and the reaction mixture is dehydrated by distillation.4. The process of claim 1 , wherein the compound comprising Formula (IX) is isolated as a substantially pure isomer claim 1 , the isomer having a configuration at ring atoms 3 and 6 chosen from RR claim 1 , RS claim 1 , SR claim 1 , and SS claim 1 , respectively.7. The process of claim 5 , wherein step (a) is conducted at a temperature from about 100° C. to about 150° C.8. The process of claim 5 , wherein the compound comprising Formula (IX) is isolated as a substantially pure isomer claim 5 , the isomer having a configuration at ring atoms 3 and 6 chosen from RR claim 5 , RS claim 5 , SR claim 5 , and SS claim 5 , respectively.10. The polymer of claim 9 , wherein R claim 9 , R claim 9 , R claim 9 , R claim 9 , and Rare hydrogen; n is from 1 to 10; Z is chosen from sulfur claim 9 , sulfone claim 9 , sulfoxide claim 9 , and selenium; Ris lower chain alkyl claim 9 , and R claim 9 , if present claim 9 , is hydrogen or lower chain alkyl.12. The polymer of claim 9 , wherein R claim 9 , R claim 9 , R claim 9 , R claim 9 , Rand Rare hydrogen; each of n and m is from 1 to 10; Y and Z are independently chosen from sulfur claim 9 , sulfone claim 9 , sulfoxide claim 9 , and selenium; Rand Rare lower chain alkyl; and Rand R claim 9 , if present claim 9 , are independently hydrogen or lower chain alkyl.14. The polymer of claim 9 , wherein the polymer is substantially free of a monomer.15. The polymer of claim 9 , wherein the average molecular weight of the polymer is at least about 10 claim 9 ,000 Da claim 9 , at least about 100 claim 9 ,000 ...

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15-07-2021 дата публикации

Catalyst composition for a polyester manufacturing process

Номер: US20210214491A1
Принадлежит: Clariant Plastics and Coatings Ltd

A catalyst composition for a polyester manufacturing process, comprising a titanium catalyst and/or an antimony catalyst as main catalyst, and either(i) at least one co-catalyst A, or(ii) at least one co-catalyst Band at least one co-catalyst C, or(iii) a combination thereof, andwherein co-catalyst A is selected from the group consisting of a metal salt of an alkyl or an aryl phosphinic acid, or a metal salt of an alkyl or aryl diphosphinic acid, or a combination thereof, and co-catalyst B is selected from the group consisting of an alkyl or aryl phosphinic acid, an alkyl or aryl diphosphinic acid a combination thereof, and co-catalyst C selected from the group of a metal salt, a metal hydroxide or a metal organyl compound.

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13-07-2017 дата публикации

BATCH PROCESS FOR MAKING POLYBUTYLENE TEREPHTHALATE

Номер: US20170198090A1
Принадлежит:

An improved process for making polybutylene terephthalate resin is disclosed. The resin is prepared from oligomers of purified terephthalic acid and 1,4-butane diol in the presence of a catalyst. 1. A batch process for preparing polybutylene terephthalate (PBT) , comprising:{'sub': 1', '8, 'heating at approximately 245-260° C. and 1 atmosphere of pressure PBT oligomer having an intrinsic viscosity (IV) of 0.1 to 0.2 dL/g and a carboxylic acid end group concentration [CEG] of 90 to 180 mmol/kg until the PBT melts and becomes homogeneous to form melted homogeneous PBT oligomer; wherein the PBT oligomer contains 0 to 300 ppm tetra(C-Calkyl) titanate catalyst;'}{'sub': 1', '8, 'polycondensing the melted homogeneous PBT oligomer by adding 0.1 to 250 ppm tetra(C-Calkyl) titanate catalyst, reducing the pressure to approximately 0.1 to 4 mm Hg, and maintaining the temperature at approximately 245-260° C. for a sufficient time to provide PBT having an IV of between 0.55 and 1.20 dL/g.'}2. The batch process of claim 1 , wherein the PBT oligomer is flaked claim 1 , particulate claim 1 , or chunked.3. The batch process of claim 1 , further comprising adding to the melted homogeneous PBT oligomer 0.1 to 10 weight percent of 1 claim 1 ,4 butane diol (BDO) claim 1 , 0.1 to 300 ppm tetra(C-Calkyl) titanate catalyst claim 1 , or both 0.1 to 10 weight percent BDO and 0.1 to 300 ppm tetra(C-Calkyl) titanate catalyst.4. The batch process of claim 3 , wherein:{'sub': 1', '8', '1', '8, '0.1 to 10 weight percent BDO is added to the melted homogeneous PBT oligomer; 0.1 to 300 ppm tetra(C-Calkyl) titanate catalyst is added to the melted homogeneous PBT oligomer, wherein the tetra(C-Calkyl) titanate catalyst is tetraisopropyl titanate (TPT).'}5. The batch process of claim 4 , further comprising preparing the PBT oligomer by heating a 2.5:1 to 3.5:1 molar ratio mixture of BDO and purified terephthalic acid (PTA) in the presence of 0.1 to 300 ppm tetra isopropyl titanate catalyst to 230 to 280 ...

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25-09-2014 дата публикации

CATALYST FOR SYNTHESIZING POLYESTER RESIN AND METHOD OF MANUFACTURING POLYESTER RESIN USING THE SAME

Номер: US20140288261A1
Принадлежит:

A catalyst used to manufacture a biodegradable polyester resin, in particular, an organic titanium catalyst which does not contain a heavy-metal component, and a method of manufacturing a polyester resin using the same. Accordingly, the method of manufacturing a polyester resin can be useful in attaining desired physical properties without using a catalyst harmful to environments and a human body. The biodegradable resin, which can be safely used in the field of applications in which the use of harmful components is a sensitive issue without using the components harmful to environments and a human body during the manufacture of a resin, can be prepared. 1. A method of manufacturing a polyester resin comprising:esterifying an alcohol monomer and a carboxylic acid monomer at a temperature of 200 to 220° C. in the presence of 0.1 to 1.5 g of an organic titanium catalyst with respect to 1 mol of the carboxylic acid monomer, and polycondensing the esterification reaction product at a temperature of 220 to 240° C. under a vacuum of less than 2 Torr.2. The method of claim 1 , wherein claim 1 , in the esterification of the alcohol monomer and the carboxylic acid monomer claim 1 , the alcohol monomer is at least one selected from the group consisting of 1 claim 1 ,4-butylene glycol claim 1 , 1 claim 1 ,3-butylene glycol claim 1 , 1 claim 1 ,3-propylene glycol and 1 claim 1 ,2-ethylene glycol claim 1 , and the carboxylic acid monomer is at least one selected from the group consisting of succinic acid claim 1 , adipic acid claim 1 , suberic acid claim 1 , sebacic acid claim 1 , terephthalic acid claim 1 , their anhydrides and their derivatives.3. The method of claim 1 , wherein the organic titanium catalyst comprising 5 to 15 wt % of titanium is used in the esterification.4. The method of claim 1 , wherein the esterification is performed by further adding triphenyl phosphate or trimethyl phosphate.54. A polyester resin manufactured by the method defined in any one of to .6. An ...

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30-07-2015 дата публикации

Biodegradable Stealth Polymeric Particles Fabricated Using The Macromonomer Approach By Free Radical Dispersion Polymerization

Номер: US20150209287A1
Принадлежит:

The present invention is directed to a crosslinked or non-crosslinked polymer particle, wherein the crosslinked polymer particle comprises a copolymer of poly(alklyene glycol-graft-lactate) that is crosslinked by at least one hydrolysable monomer. Another embodiment of the present invention is a polymer particle comprising a crosslinked polymer particle that is a product of starting materials comprising (a) a hydrophilic monomer, (b) a hydrophobic monomer, and (c) a hydrolysable crosslinking agent. Another embodiment of the present invention is a polymer particle comprising, a crosslinked copolymer comprises structures represented by Formulas (I), (II), and (III), where Formulas (I), (II) and (III) are defined in the specification. Yet other embodiments of the present invention include a method of preparing a methacrylate terminated macromonomer, a method of preparing a crosslinking agent, and a method of preparing a therapeutic agent loaded nanosphere by dispersion polymerization. 125.-. (canceled)26. A method of preparing a methacrylate terminated macromonomer , the method comprising the steps of:(i) reacting L-lactide, an initiator and a catalyst under vacuum for 10 minutes(ii) flushing the reaction vessel with nitrogen for 24 to 38 hours at a temperature of 120-240° C.(iii) extracting the resulting polymer from an organic solution.27. The method of claim 26 , wherein the initiator is selected from the group consisting of hydroxymethacrylate (HEMA) or hydroxypropylmethacrylamide (HPMA).28. The method of claim 26 , wherein the amount of L-lactide is 0.0418 moles.29. The method of claim 26 , wherein the amount of initiator is 0.00738 mole.30. A method of preparing a therapeutic agent loaded nanosphere by dispersion polymerization claim 26 , wherein the method comprises the steps of:(i) reacting a hydrophilic macromonomer, a hydrophobic macromonomer with or without a crosslinker in an organic solvent/water solvent system;(ii) adding NPDEA and BPO at predetermined ...

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30-07-2015 дата публикации

POLY(2-HYDROXYALKANOIC ACID) AND METHOD OF ITS MANUFACTURE

Номер: US20150210802A1
Принадлежит:

A method for manufacturing poly(2-hydroxyalkanoic acid) included the steps of a) mixing a cyclic diester of a 2-hydroxyalkanoic acid and a polymerization catalyst, b) polymerizing the cyclic diester to form poly(2-hydroxyalkanoic acid) in liquid phase, c) adding a phosphoric acid ester as a catalyst deactivating agent to the liquid phase, d) applying a devolatilisation step to the liquid phase, and e) allowing the poly(2-hydroxyalkanoic acid) to solidify. The catalyst deactivating agent is added after the devolatilisation step is applied. The method results in an improved melt stability of the manufactured polymer. 1. Method for manufacturing poly (2-hydroxyalkanoic acid) , comprising the steps of mixing a cyclic diester of a 2-hydroxyalkanoic acid and a polymerization catalyst , polymerizing the cyclic diester to form poly (2-hydroxyalkanoic acid) in liquid phase , adding a phosphoric acid ester as a catalyst deactivating agent to the liquid phase , applying a devolatilisation step to the liquid phase , and allowing the poly (2-hydroxyalkanoic acid) to solidify , wherein the catalyst deactivating agent is added after the devolatilisation step is applied.2. Method according to claim 1 , wherein the phosphoric acid ester comprises an alkanoic acid phosphate compound.3. Method according to claim 1 , wherein the cyclic diester is lactide.4. Method according to claim 1 , wherein an end-capping agent is added to the poly (2-hydroxyalkanoic acid) in the liquid phase.5. Method according to claim 4 , wherein the end-capping agent is added in the liquid phase after at least 90% by weight of the cyclic diester is converted into the corresponding poly (2-hydroxyalkanoic acid).6. Method according to claim 4 , wherein the end-capping agent and the catalyst deactivating agent are added to the poly (2-hydroxyalkanoic acid) in the liquid phase at different stages of the polymerization process.7. Method according to claim 4 , wherein the end-capping agent is added prior to the ...

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18-06-2020 дата публикации

IMPROVED RESORBABLE POLYMER PURIFICATION PROCESS

Номер: US20200190258A1
Принадлежит:

The present invention is directed to an improved purification process using additive and activated carbon for purifying resorbable polymers suitable for industrial manufacturing. The metal catalyst concentration in the purified resorbable polymers of this invention is preferably less than 1 ppm. The method can be used to obtain high molecular weight polymers that are substantially metal free. 1. A method of reducing the residual tin content in a tin containing resorbable polymer to less than 1 ppm , comprising:(d) dissolving a polymer in an organic solvent to produce a polymer solution;(e) combining the polymer solution with activated carbon and an additive; wherein said method results in the formation of a purified polymer; and(f) recovering the purified polymer by anti-solvent precipitation.2. The method of claim 1 , wherein the polymer is linear.3. The method of claim 2 , wherein the additive is up to 20 wt % of the solvent claim 2 , and activated carbon is up to 9 wt % of the linear polymer.4. The method of claim 1 , wherein the polymer is branched.5. The method of claim 4 , wherein the additive is up to 20 wt % of the solvent claim 4 , and activated carbon is between 50-100 wt % of the branched polymer.6. The method of claim 1 , wherein the additive and activated carbon is exposed to the polymer solution for 2 to 4 hours7. The method of claim 1 , wherein the additive is lactic acid claim 1 , glycolic acid claim 1 , or water.8. A purified polyester which is a branched or a linear polylactide-glycolide having a weight averaged molecular weight of 5 to 315 kDa claim 1 , a polydispersity M/Mof 1.5 to 2.5 claim 1 , prepared by the process of ring-opening polymerization of lactide and glycolide in the presence of tin (II)-(2-ethylhexanoate) or tin chloride followed by treatment with activated carbon and an additive.9. The purified polyester of claim 8 , wherein the additive is lactic acid claim 8 , glycolic acid claim 8 , or water.10. The purified polyester of having ...

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19-07-2018 дата публикации

PROCESS FOR MAKING POLYBUTYLENE TEREPHTHALATE OLIGOMERS

Номер: US20180201729A1
Принадлежит:

Disclosed is a process for making oligomers of polybutylene terephthalate (PBT) with desirable intrinsic viscosity and carboxylic end group concentrations. The PBT oligomers are used in a continuous process for making polybutylene terephthalate (PBT) resin. 1. A process for making oligomers of polybutylene terephthalate (PBT) , comprising:combining 1,4-butane diol (BDO), terephthalic acid and a catalyst to from a mixture;heating the mixture to a temperature of approximately 160° C. to 180° C.;raising the temperature of the mixture from approximately 160° C. to 180° C. to approximately 220° C. to 265° C.;maintaining the temperature at approximately 220° C. to 260° C., until the clearing point is reached based on visual inspection;optionally adjusting the pressure to approximately 50 to 760 mm Hg at approximately 220° C. to 265° C. for sufficient time to achieve desired intrinsic viscosity (IV) and carboxylic end group (CEG) values in the resulting PBT oligomer.2. The process of claim 1 , wherein the terephthalic acid is purified terephthalic acid (PTA).3. The process of claim 2 , wherein the catalyst is tetraisopropyl titanate (TPT).4. The process of claim 3 , wherein the BDO and TA are combined in a molar ratio of 6:1 to 2:1 in the presence of TPT.5. The process of claim 4 , wherein the BDO and TA are combined in a molar ratio of 4.25:1 to 2.95:1 in the presence of TPT.6. The process of claim 3 , wherein a BDO to PTA ratio of 3:1 is employed to achieve an IV of approximately 0.11-0.20 dl/g and a CEG of between 70 and 250 mmol/kg.7. The process of claim 3 , wherein a BDO to PTA ratio of 3:1 to 4:1 is employed to achieve an IV of 0.25-0.43 dl/g and a CEG of lower than 20 mmol/kg. Disclosed is a process for making oligomers of polybutylene terephthalate (PBT) with desirable intrinsic viscosity and carboxylic end group concentrations. The PBT oligomers are used in a continuous process for making polybutylene terephthalate (PBT) resin.Polybutylene terephthalate (PBT) ...

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25-06-2020 дата публикации

MODIFIED POLYLACTIC ACID, POLYMERIZED MODIFIED POLYLACTIC ACID, AND METHODS AND APPARATUSES FOR MANUFACTURING THE SAME

Номер: US20200199290A1
Автор: TAKAMURA Takatsugu
Принадлежит: OPTIMIZER INC.

Provided are: a modified polylactic acid that is environmentally friendly, potentially usable as a battery material of a secondary battery or the like, and obtained by chemically derivatizing polylactic acid having an L-lactide structure generated or obtained in the manufacture of polylactic acid; a polymerized modified polylactic acid obtained by further polymerizing this modified polylactic acid; and methods and apparatuses for manufacturing the modified polylactic acid and the polymerized modified polylactic acid. The present invention uses: a modified polylactic acid including a structure represented by general formula (1) below (in formula (1), R1 and R2 are structures containing a metal element and can be the same or different, AA and BB are CC or structures containing a metal element in R3 and R4 and can be the same or different, and R5 is a structure containing a metal element); a polymerized modified polylactic acid; and methods and apparatuses for manufacturing the modified polylactic acid and the polymerized modified polylactic acid. 3. The modified polylactic acid according to claim 1 , wherein in a modified polylactic acid represented by at least one of formulas (1) and (2) claim 1 , a metal element is an element selected from the group consisting of vanadium claim 1 , nickel claim 1 , iron claim 1 , aluminum claim 1 , titanium claim 1 , cerium claim 1 , silicon claim 1 , zirconium claim 1 , ruthenium claim 1 , manganese claim 1 , chromium claim 1 , cobalt claim 1 , platinum claim 1 , thorium claim 1 , palladium claim 1 , and tin.4. The modified polylactic acid according to claim 1 , manufactured by obtaining polylactic acid including a lactide structure and having a weight average molecular weight of 2 claim 1 ,000 to 20 claim 1 ,000 daltons by decomposing polylactic acid by an alkali catalyst claim 1 , aminating the lactide structure by adding an aminated metal compound to polylactic acid including the L-lactide claim 1 , and adding a functional group ...

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03-08-2017 дата публикации

Process For Preparing A High Molecular Weight Heteroaromatic Polyester Or Copolyester

Номер: US20170218118A1
Принадлежит:

A process for preparing a high molecular weight heteraromatic polyester or copolyester is disclosed. A process for preparing a high molecular weight heteroaromatic polyester or copolyester includes the steps of: (a) processing comonomers by mixing together to form a homogeneous solution (1) at least one heteroaromatic dicarboxylic acid having 2-12 carbon atoms or a diester or an acid anhydride derived therefrom, or a mixture thereof; (2) at least one alcohol having 2 to 12 carbon atoms and at least two hydroxyl functionalities; and (3) optionally aromatic or aliphatic dicarboxylic acids or diesters or acid anhydrides derived therefrom; (b) converting the paste/solution obtained in step a) into an esterification product containing at least one diester or at least one oligoester formed from the at least one heteroaromatic dicarboxylic acid and the at least one alcohol; and (c) polycondensing/copolycondensing the reaction product obtained from step b) under reduced pressure. 1. A high molecular weight heteroaromatic polyester or copolyester comprising:a) between about 50 mol % to about 100 mol %, based on the sum total of feed dicarboxylic acids, of a heteroaromatic dicarboxylic acid; andb) at least one diol component selected from the group consisting of ethylene glycol, propanediol, and 1,4-butanediol;wherein the high molecular weight heteroaromatic polyester or copolyester is prepared by a process comprising the steps of: at least one heteroaromatic dicarboxylic acid having 2-12 carbon atoms or a diester or an acid anhydride derived therefrom, or a mixture thereof;', 'at least one alcohol having 2 to 12 carbon atoms and at least two hydroxyl functionalities; and', 'optionally further aromatic or aliphatic dicarboxylic acids or diesters or acid anhydrides derived therefrom;, 'a) processing comonomers by mixing together to form a paste or by mixing under elevated temperature to form a homogeneous solution [{'sub': '1', 'b) an esterification product, the esterification ...

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03-08-2017 дата публикации

Thermoplastic resin composition and molded body using same

Номер: US20170218195A1
Принадлежит: Mitsubishi Gas Chemical Co Inc

One embodiment of the present invention provides: a thermoplastic resin composition which contains a polycarbonate resin and a polyester resin that contains a diol unit having a cyclic acetal skeleton, and wherein the polyester resin contains specific amounts of phosphorus atoms and titanium atoms and the weight ratio of the phosphorus atoms to the titanium atoms is within a specific range; and a molded body which uses this thermoplastic resin composition.

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12-08-2021 дата публикации

ARTICLES OF POLY(BUTYLENE SUCCINATE) AND COPOLYMERS THEREOF

Номер: US20210244860A1
Принадлежит:

Resorbable implants, coverings and receptacles comprising poly(butylene succinate) and copolymers thereof have been developed. The implants are preferably sterilized, and contain less than 20 endotoxin units per device as determined by the limulus amebocyte lysate (LAL) assay, and are particularly suitable for use in procedures where prolonged strength retention is necessary, and can include one or more bioactive agents. The implants may be made from fibers and meshes of poly(butylene succinate) and copolymers thereof, or by 3d printing molding, pultrusion or other melt or solvent processing method. The implants, or the fibers preset therein, may be oriented. These coverings and receptacles may be used to hold, or partially/fully cover, devices such as pacemakers and neurostimulators. The coverings, receptacles and implants described herein, may be made from meshes, webs, lattices, non-wovens, films, fibers, foams, molded, pultruded, machined and 3D printed forms. 112-. (canceled)131. A method of forming the article of claim , wherein the implant is produced by a method comprising the steps of: (a) preparing a polymeric composition comprising a polymer or copolymer of 1 ,4-butanediol unit , a succinic acid unit , and a metal catalyst , wherein the metal catalyst comprises scandium , yttrium , titanium , zirconium , vanadium , molybdenum , tungsten , zinc , iron , tin or germanium , and (b) forming the implant by a process comprising melt processing of the polymeric composition.14. The method of claim 13 , wherein the catalyst is present at a level of 0.1 to 1 claim 13 ,000 ppm.15. The method of claim 13 , wherein the article is formed by a process comprising one of the following melt processing processes: melt extrusion claim 13 , injection molding claim 13 , melt foaming claim 13 , film extrusion claim 13 , melt blowing claim 13 , melt spinning claim 13 , compression molding claim 13 , lamination claim 13 , thermoforming claim 13 , molding claim 13 , spun-bonding ...

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11-07-2019 дата публикации

ORIENTED FILMS AND SHRINK FILMS COMPRISING POLYESTERS WHICH COMPRISE TETRAMETHYLCYCLOBUTANEDIOL AND ETHYLENE GLYCOL

Номер: US20190211146A1
Принадлежит: EASTMAN CHEMICAL COMPANY

This invention relates to an oriented film or a shrink film comprising a polyester composition comprising: (1) at least one polyester which comprises: (a) a dicarboxylic acid component comprising: (i) about 90 to about 100 mole % of terephthalic acid residues; (ii) about 0 to about 10 mole % of aromatic and/or aliphatic dicarboxylic acid residues having up to 20 carbon atoms; and (b) a glycol component comprising: (i) about 10 to about 29 mole % 2,2,4,4-tetramethyl-1,3-cyclobutanediol residues; and (ii) about 71 to about 90 mole % ethylene glycol residues; and (iii) optionally, diethylene glycol residues; wherein the total mole % of the dicarboxylic acid component is 100 mole %, and wherein the total mole % of the glycol component is 100 mole %; wherein the inherent viscosity of the polyester is from 0.50 to 0.8 dL/g as determined in 60/40 (wt/wt) phenol/tetrachloroethane at a concentration of 0.25 g/50 ml at 25° C.; wherein the polyester has a Tg of from 80° C. to 105° C. or of from 80° C. to 100° C. as determined using a TA DSC 2920 from Thermal Analyst Instrument at a scan rate of 20° C./min.; and (2) optionally, wherein the polyester composition comprises at least one plasticizer. 3. The film of wherein said polyester comprises about 15 to about 28 mole % 2 claim 2 ,2 claim 2 ,4 claim 2 ,4-tetramethyl-1 claim 2 ,3-cyclobutanediol residues and 72 to 85 mole % ethylene glycol residues.4. The film of wherein said at least one polyester comprises a catalyst/stabilizer component which comprises: (i) titanium atoms in the range of 10-50 ppm based on total polymer weight claim 1 , and (ii) phosphorus atoms in the range of 10-200 ppm based on total polymer weight.5. The film of wherein said at least one polyester comprises manganese atoms in the range of 10-100 ppm based on total polymer weight claim 4 ,6. The film of claim 4 , wherein the catalyst/stabilizer component comprises tin atoms in the range of 0-5 ppm based on total polymer weight.7. The film of or claim 4 , ...

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11-07-2019 дата публикации

POLYESTER COMPOSITIONS WHICH COMPRISE TETRAMETHYL CYCLOBUTANEDIOL AND ETHYLENE GLYCOL, WITH IMPROVED CATALYST SYSTEM

Номер: US20190211147A1
Принадлежит: EASTMAN CHEMICAL COMPANY

Described as one aspect of the invention are polyester compositions including at least one polyester which comprises: 2. The polyester composition of claim 1 , further comprising: (c) a catalyst/stabilizer component which comprises: (i) titanium atoms in the range of 10-50 ppm based on polymer weight claim 1 , and (iii) phosphorus atoms in the range of 10-200 ppm based on polymer weight.3. The polyester composition of claim 2 , wherein the catalyst/stabilizer component comprises tin atoms in the range of 0-5 ppm based on polymer weight.4. The polyester composition of claim 3 , wherein the catalyst/stabilizer component comprises no tin atoms.5. The polyester composition of claim 1 , wherein 2 claim 1 ,2 claim 1 ,4 claim 1 ,4-tetramethyl-1 claim 1 ,3-cyclobutanediol is present in the amount of about 20 to about 25 mole %.6. The polyester composition of claim 1 , wherein the inherent viscosity of the polyester is from 0.60 to 0.70 dL/g.7. The polyester composition of claim 1 , wherein the polyester has a Tof 90 to 96° C.8. The polyester composition of claim 1 , wherein the 2 claim 1 ,2 claim 1 ,4 claim 1 ,4-tetramethyl-1 claim 1 ,3-cyclobutanediol residues is a mixture comprising about 55 to about 65 mole % of cis-2 claim 1 ,2 claim 1 ,4 claim 1 ,4-tetramethyl-1 claim 1 ,3-cyclobutanediol residues and about 35 to about 45 mole % of trans-2 claim 1 ,2 claim 1 ,4 claim 1 ,4-tetramethyl-1 claim 1 ,3-cyclobutanediol residues.9. The polyester composition of claim 2 , wherein the weight ratio of P to total catalyst is from 0.6:1 to 1.2:1.10. The polyester composition of claim 9 , wherein the catalyst/stabilizer component comprises phosphorus atoms in the range of 15-60 ppm based on polymer weight.11. The polyester composition of claim 10 , comprising at least one phosphorus compound chosen from at least one of the following: triaryl phosphates claim 10 , alkyl diaryl phosphates claim 10 , and mixed alkyl aryl phosphates.12. The polyester composition of claim 1 , wherein the ...

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12-08-2021 дата публикации

Water-soluble or dispersible polyester resins made from terephthalate plastic materials useful as dispersant resins for inks

Номер: US20210246282A1
Принадлежит: Sun Chemical Corp

The present invention provides water-soluble or water-dispersible polyester resins prepared by depolymerizing a tereph-thalate plastic material in an alcoholysis/glycolysis reaction, and re-polymerizing the product by reacting with a polybasic acid and/or anhydride. The polyester resins of the invention contain 70% to 95% by weight of the terephthalate material, based on the total weight of the composition. The polyester resins of the present invention are useful as dispersants, for example in pigment preparations, and as binders in let-down varnishes, inks, coatings, etc, and as adhesion promoters in aqueous-based inks.

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