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47results about How to "Inherent viscosity" patented technology

Polyester fiber and methods for making same

InactiveUS6063495AGood useImproved strength and elasticity and abrasion resistanceMonocomponent polyetheresters artificial filamentCeramic shaping apparatusPolyesterChemistry
A polyester fiber made from a polymer having ethylene glycol moieties, isosorbide moieties and terepthaloyl moieties, and the method of making the fiber is described. The polyester fiber is used to form articles suitable for commercial, especially textile, and industrial uses, and has an inherent viscosity of at least 0.35 dL / g when measured as a 1% (weight / volume) solution of the polyester in o-chlorophenol at a temperature of 25 DEG C.
Owner:EI DU PONT DE NEMOURS & CO

Polyesters including isosorbide as a comonomer blended with other thermoplastic polymers

InactiveUS6140422AHigh inherent viscosityInherent viscosityIsosorbidePolyester
A polymer blend including a polyester and another thermoplastic polymer. The polyester includes terephthaloyl moieties and, optionally, other aromatic diacid moieties; and ethylene glycol moieties; optionally diethylene glycol moieties; isosorbide moieties; and, optionally one or more other diol moieties. The polyester has an inherent viscosity of at least about 0.35 dL / g.
Owner:EI DU PONT DE NEMOURS & CO

Certain polyester compositions which comprise cyclohexanedimethanol, moderate cyclobutanediol, cyclohexanedimethanol, and high trans cyclohexanedicarboxylic acid

Described as one aspect of the invention are polyester compositions A polyester composition comprising at least one polyester which comprises:
    • (A) a dicarboxylic acid component comprising:
      • i) 70 to 100 mole % of cyclohexanedicarboxylic acid residues or an ester thereof comprising:
        • (a) 80 to 99 mole % trans-cyclohexanedicarboxylic acid residues or an ester thereof; and
        • (b) 1 to 20 mole % cis-cyclohexanedicarboxylic acid residues or an ester thereof;
      • ii) 0 to 30 mole % of aliphatic dicarboxylic acid residues, other than cyclohexanedicarboxylic acid residues, having up to 16 carbon atoms or esters thereof, other than cyclohexanedicarboxylic acid residues; and
      • iii) 0 to 10 mole % of aromatic dicarboxylic acid residues having up to 20 carbon atoms; and
    • (B) a glycol component comprising:
      • i) 5 to 35 mole % of 2,2,4,4-tetramethyl-1,3-cyclobutanediol residues; and
      • ii) 65 to 95 mole % of 1,4-cyclohexanedimethanol residues, 1,3-cyclohexanedimethanol residues, 1,2-cyclohexanedimethanol residues or esters thereof or mixtures thereof,
wherein the total mole % of said dicarboxylic acid component is equal to 100 mole %;
the total mole % of said glycol component is equal to 100 mole %;
wherein the inherent viscosity of said polyester is from 0.35 to 1.2 dL/g as determined in 60/40 (wt/wt) phenol/tetrachloroethane at a concentration of 0.5 g/100 ml at 25° C.; and wherein said polyester has a Tg of from 66 to 120° C. The polyesters may be manufactured into articles.
Owner:EASTMAN CHEM CO

Methods for forming amorphous ultra-high molecular weight polyalphaolefin drag reducing agents

A composition including polyalphaolefins that function as drag reducing agents and a process for the preparation of polyalphaolefins that function as drag reducing agents are disclosed. The process includes contacting alpha olefin monomers with a catalyst system, which includes a catalyst and an activator (co-catalyst) in a reactant mixture. The catalyst is a transition metal catalyst, preferably titanium trichloride, and the co-catalyst may include an alkylaluminoxane, alone or in combination, with a dialkylaluminum halide or a halohydrocarbon. The polymerization of the alpha olefin monomers produces a non-crystalline, ultra-high molecular weight polyalphaolefin having an inherent viscosity of at least 10 dL/g. The addition of the alkylaluminoxane during the polymerization process provides for a non-crystalline, ultra-high molecular weight polyalphaolefin and a more uniform molecular weight distribution of the resulting polyalphaolefin, thereby creating a drag reducing agent superior to known drag reducing agents. A process for forming a drag reducing agent comprising a non-crystalline, ultra-high molecular weight polyalphaolefin having an inherent viscosity of about at least 10 dL/g and a process for reducing drag in a conduit are also disclosed.
Owner:MPOWER SPECIALTY CHEM

Opththalmic devices comprising polyester compositions formed from 2,2,4,4-tetramethyl-1,3-cyclobutanediol and 1,4-cyclohexanedimethanol

InactiveUS20060287484A1Inherent viscosity and/or glass transition temperatureInherent temperatureDialysis systemsDialysisDicarboxylic acid2,2,4,4-Tetramethyl-1,3-cyclobutanediol
Described are ophthalmic products comprising polyester compositions comprising polyesters which comprise (a) a dicarboxylicacid component having terephthalic acid residues; optionally, aromatic dicarboxylic acid residues or aliphatic dicarboxylic acid residues or ester residues thereof; 2,2,4,4-tetramethyl-1,3-cyclobutanediol residues; and 1,4-cyclohexanedimethanol residues.
Owner:EASTMAN CHEM CO

Methods for forming amorphous ultra-high molecular weight polyalphaolefin drag reducing agents using a halohydrocarbon

A composition including polyalphaolefins that function as drag reducing agents and a process for the preparation of polyalphaolefins that function as drag reducing agents are disclosed. The process includes contacting alpha olefin monomers with a catalyst system, which includes a catalyst and an activator (co-catalyst) in a reactant mixture. The catalyst is a transition metal catalyst, preferably titanium trichloride, and the co-catalyst may include an alkylaluminoxane, alone or in combination, with a dialkylaluminum halide or a halohydrocarbon. The polymerization of the alpha olefin monomers produces a non-crystalline, ultra-high molecular weight polyalphaolefin having an inherent viscosity of at least 10 dL / g. The addition of the alkylaluminoxane during the polymerization process provides for a non-crystalline, ultra-high molecular weight polyalphaolefin and a more uniform molecular weight distribution of the resulting polyalphaolefin, thereby creating a drag reducing agent superior to known drag reducing agents. A process for forming a drag reducing agent comprising a non-crystalline, ultra-high molecular weight polyalphaolefin having an inherent viscosity of about at least 10 dL / g and a process for reducing drag in a conduit are also disclosed.
Owner:MPOWER SPECIALTY CHEM

Blood therapy containers comprising polyester compositions formed from 2,2,4,4-tetramethyl-1,3-cyclobutanediol and 1,4-cyclohexanedimethanol

ActiveUS20060286322A1Inherent viscosity and glass transition temperatureHigh impact strengthBottlesDialysis systemsChemistryPolyester
Described are blood therapy containers comprising polyester compositions comprising polyesters which comprise (a) a dicarboxylic acid component having terephthalic acid residues; optionally, aromatic dicarboxylic acid residues or aliphatic dicarboxylic acid residues or ester residues thereof; 2,2,4,4-tetramethyl-1,3-cyclobutanediol residues; and 1,4-cyclohexanedimethanol residues.
Owner:EASTMAN CHEM CO

Greenhouses comprising polyester compositions formed from 2,2,4,4-tetramethyl-1,3-cyclobutanediol and 1,4- cyclohexanedimethanol

InactiveUS20060287477A1Inherent viscosity and glass transition temperatureHigh impact strengthDialysis systemsDialysisDicarboxylic acid2,2,4,4-Tetramethyl-1,3-cyclobutanediol
Described are greenhouses comprising polyester compositions comprising polyesters which comprise (a) a dicarboxylic acid component having terephthalic acid residues; optionally, aromatic dicarboxylic acid residues or aliphatic dicarboxylic acid residues or ester residues thereof; 2,2,4,4-tetramethyl-1,3-cyclobutanediol residues; and 1,4-cyclohexanedimethanol residues.
Owner:EASTMAN CHEM CO
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