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158 results about "Characteristic viscosity" patented technology

Viscosity is characteristic property of liquid, viscosity describes the flow of a liquid. Definition: Viscosity is defined as the resistance in the flow of a liquid Or. which resists the flow of liquid is commonly known as Viscosity. A liquid with high viscosity is thick and flows slowly. A liquid with low viscosity is thin and flows quickly.

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

Propylene Random Block Copolymer, Resin Composition Containing the Copolymer and Molded Article Made Thereof

The invention provides a propylene random block copolymer (A) that has a melt flow rate from 0.1 to 100 g/10 min and a melting point from 100 to 155° C. and includes 90 to 60% by weight of a portion insoluble (Dinsol) in n-decane at room temperature and 10 to 40% by weight of a portion soluble (Dsol) in n-decane at room temperature, wherein the Dinsol satisfies the following requirements (1) through (3) and the Dsol satisfies the following requirements (4) through (6). The invention further provides molded articles such as sheets, films, injection molded articles, hollow molded articles, injection blow molded articles and fibers, which are formed of the propylene random block copolymer (A) or a propylene resin composition containing the propylene random block copolymer (A). (1) The molecular weight distribution (Mw/Mn) obtained by GPC of the Dinsol is from 1.0 to 3.5, (2) the content of skeletons derived from ethylene in the Dinsol is from 0.5 to 13% by mole, (3) the total amount of 2,1- and 1,3-propylene units in the Dinsol is 0.2% by mole or less, (4) the molecular weight distribution (Mw/Mn) obtained by GPC of the Dsol is from 1.0 to 3.5, (5) the intrinsic viscosity [η] in decalin at 135° C. of the Dsol is from 1.5 to 4 dl/g and (6) the content of skeletons derived from ethylene in the Dsol is from 15 to 35% by mole.
Owner:MITSUI CHEM INC +1

Preparation of biodegradable block copolyester

The invention belongs to the technical field of macromolecular materials, and in particular relates to a preparation method for biodegradable blocked copolyester. The preparation method comprises the following steps: carrying out esterification reaction between adipate and 1,4 butanediol in the presence of catalyst, wherein the reaction time is 3 to 5h, nitrogen is adopted for protection, the reaction pressure is between 0.1 and 0.8MPa and the reaction temperature is between 130 and 180 DEG C during a first stage; and the reaction time is 1.5 to 5h, the reaction pressure is between 0.3 and 0.6MPa and the reaction temperature is between 150 and 200 DEG C during a second stage so as to generate polybutylene adipate; and carrying out ester exchange reaction of dimethyl terephthalate (DMT) and 1,4 butanediol in the presence of catalyst, wherein the nitrogen is adopted for protection, the reaction time is 2 to 5h, the reaction pressure is between 0.1 and 0.7MPa and the reaction temperature is between 150 and 170 DEG C so as to generate polybutylene terephthalate (pbt); and mixing both prepolymers and carrying out melt copolycondensation reaction under negative pressure, wherein the vacuum degree is controlled to be between 0 and 200Pa, the reaction temperature is between 210 and 260 DEG C and the reaction time is 3 to 8h. The preparation method carries out esterification reaction and ester exchange reaction, and the esterification reaction has two stages so as to effectively reduce secondary reaction of 1,4 butanediol. A prepared product has a characteristic viscosity number above 1.2dl/g, a melting point controlled between 100 and 140 DEG C, a tensile strength between 18 and 37MPa and a breaking elongation ratio from 800 to 1,500 percent.
Owner:TONGJI UNIV

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

Polypropylene resin composition and expanded molding

A polypropylene-based resin composition is provided that can provide a foam molding that exhibits an excellent closed cell characteristic and excellent extrusion characteristics, that is light weight and has a rigid feel, and that has an excellent recyclability.This polypropylene-based resin composition contains 100 weight % or is less than 100 weight % but at least 70 weight % of component (A) below and contains 0 weight % or is greater than 0 weight % but not more than 30 weight % of component (B) below,component (A):a propylene-based resin composition that comprises at least the following two components: a propylene-α-olefin copolymer (A1) satisfying conditions (A-1) to (A-3) and a propylene homopolymer (A2), (A1) and (A2) being obtained by polymerization by a multistage polymerization method, and this propylene-based resin composition having a content of (A1) of 1 to 20 weight % and a content of (A2) of 99 to 80 weight %, having a melt flow rate in the range from 5 to 20 g / 10 minutes and exhibiting strain hardening in a measurement of extensional viscosity at a temperature of 180° C. and a strain rate of 10 s−1,(A-1) an α-olefin content of 15 to 85 weight %,(A-2) an intrinsic viscosity η of 5 to 20 dL / g,(A-3) a Mw / Mn of 5 to 15;component (B):a propylene-based resin composition comprising at least the following two components: a propylene homopolymer or a propylene-α-olefin copolymer having a content of non-propylene α-olefin of less than 1 weight % (B1), which has an MFR of 10 to 1000 g / 10 minutes, and a propylene-α-olefin copolymer (B2) that has a weight-average molecular weight of 500,000 to 10,000,000 and a content of non-propylene α-olefin of 1 to 15 weight %, (B1) and (B2) being obtained by polymerization by a multistage polymerization method, and this propylene-based resin composition having a content of (B1) of 50 to 90 weight % and a content of (B2) of 50 to 10 weight %, and satisfying prescribed conditions (B-1) to (B-3).
Owner:JAPAN POLYPROPYLENE CORP

Propylene resin composition and interior automotive member comprising the same

A propylene-based resin composition has good external appearance due to good weld appearance and low gloss and has excellent mechanical properties such as impact resistance and stiffness. The composition is well-balanced in the external appearance and mechanical properties. Automotive interior trims made of the composition are also described. The propylene-based resin composition comprises (A) 60 to 90% by weight of a propylene-based resin (1) comprising 78 to 88% by weight of 23° C. p-xylene insolubles (a) and 12 to 22% by weight of 23° C. p-xylene solubles (b), (2) the insolubles (a) having an isotactic pentad fraction of 95% or higher, a relaxation time (τ) of 0.01 to 0.35 second at an angular frequency (ω) of 10°/sec when measured by melt viscoelastometry and a molecular weight distribution index (PDI) of 1 to 18 which is expressed by ω2/10ω1 wherein ω1 is an angular frequency at which a storage modulus (G′) as measured by melt viscoelastometry is 2×102 Pa and ω2 is an angular frequency at which a storage modulus (G′) as measured by melt viscoelastometry is 2×104 Pa, and (3) the solubles (b) having an intrinsic viscosity [η] (in decalin at 135° C.) of 3.3 dl/g or higher and an ethylene unit content of 43% by weight or smaller; (B) 0 to 10% by weight of a rubberlike elastomer; and (C) 10 to 30% by weight of tale. The automotive interior trims are produced by injection-molding the composition.
Owner:PRIME POLYMER CO LTD +1

Method for preparing filaments for spinning through recycled PET (polythylene terephthalate) bottle

The invention discloses a method for preparing filaments for spinning through a recycled PET (polythylene terephthalate) bottle. The method comprises the steps of smashing, washing and drying the recycled PET bottle to obtain PET fragments; adding the PET fragments into a parallel homonymous double-screw extruder, and performing melt blending and filtering to obtain a melt; conveying the melt into a closed reaction container, injecting nitrogen into the closed reaction container, adding dihydric alcohol under the driving of nitrogen flow, then adding an aluminum-based catalyst, and mixing and stirring to perform alcoholysis reaction to obtain a treated melt; conveying the treated melt into a pressure-resistant reaction container through a closed pipeline from the closed reaction container, vacuumizing the closed pressure-resistant reaction container, stirring the melt under negative pressure to perform condensation polymerization, forming silks through a neck mold after the melt characteristic viscosity is 0.65dl / g-0.70dl / g, and performing high spinning to obtain the filaments for spinning. The filaments for spinning prepared by the method disclosed by the invention are high and stable in mechanical property, the operation is simple, the production efficiency is high, and the method is suitable for industrial production.
Owner:HANGZHOU HUAERLI CHEM FIBER CO LTD

Preparing method for PDMC with high monomer conversion rate and serialized relative molecular mass

The invention discloses a preparing method for PDMC with a high monomer conversion rate and serialized relative molecular mass. The amount of adopted monomer initial content coupling initiator is controlled for preparing the PDMC with the high monomer conversion rate and the serialized relative molecular mass, the monomer conversion rate of a serialized PDMC product obtained through preparation is larger than 98%, the characteristic viscosity value is 2.0-14.0 dL/g, a monomer is DMC, the mass fraction of the monomer is 35-70%, the initiator is water-soluble peroxide initiator, and the amount of the adopted initiator accounts for 0.20-2.00% of the mass fraction of the monomer. According to the method, the industrial product DMC concentrated, adsorbed, purified and cleaned is used as a raw material, a metal ion chelating agent and the water-soluble peroxide initiator are added under the nitrogen condition, and two-step temperature rising initiates polymerizing so that a target product can be generated. The obtained product serves as a positive ion water-soluble polymer with the high monomer conversion rate and the serialized relative molecular mass, is stable in quality, and is widely applied to multiple fields of oil exploitation, papermaking, mining, spinning and printing and dyeing, daily-use chemical industry, water treatment and the like.
Owner:NANJING UNIV OF SCI & TECH

Benzene imide structure based high-temperature self-crosslinking copolyester with effects of flame retardancy, smoke suppression and melt drop resistance and preparation method of copolyester

ActiveCN108359084APreserve thermoplastic processabilityIncrease melt viscosityStructural unitStructure based
The invention discloses a benzene imide structure based high-temperature self-crosslinking copolyester with effects of flame retardancy, smoke suppression and melt drop resistance. Copolyester is prepared from structural units represented by I, II and III or structural units represented by I, II and IV through random copolymerization, wherein the characteristic viscosity [eta] of copolyester is 0.41-1.12 dL / g, and the limit oxygen index is 24.2%-38.7%; the vertical combustion class is in a range from V-2 to V-0; the p-HRR (peak of heat release rate) in a cone calorimetry test is reduced by 7.1%-72.1% as compared with that of pure PET, and total smoke release is decreased by 2.0%-59.2% as compared with that of pure PET. The invention further discloses a preparation method of copolyester. Ahigh-temperature self-crosslinking group introduced in the preparation process is a benzene imide group, and prepared copolyeste cannot be subjected to crosslinking during processing and polymerization, so that thermoplastic processability of polyester is retained; meanwhile, due to the tackifying effect and high charring property brought by the self-crosslinking action at high temperature or during combustion, prepared copolyester has excellent flame retardancy, smoke suppression and melt drop resistance effects.
Owner:SICHUAN UNIV

Monomer containing benzimide phenylacetylene structure, high temperature self-crosslinked copolyester and preparation method thereof

ActiveCN104592094AHigh self-crosslinking flame retardant efficiencyGood flame retardantOrganic chemistryPolymer scienceChemical reaction
The invention discloses a monomer containing a benzimide phenylacetylene structure. The monomer can enable self-crosslinking chemical reaction of a synthesized polymer under high temperature. The monomer containing a benzimide phenylacetylene structure and the structural units represented by I and II for synthesis of polyester can undergo random copolymerization to obtain high temperature self-crosslinked copolyester, and when the copolyester contains a PET structural unit, the characteristic viscosity number [eta] is 0.44-1.38dL/g, the vertical combustion UL-94 grade is from V-2 to V-0, the oxygen index LOI is 24.0-35.0%, and the cone calorimeter test peak heat release rate PHRR and the smoke release total amount are both lower than pure polyester. The invention also discloses a preparation method of the copolyester. The benzimide and phenylacetylene in the copolyester involved in the invention can generate synergistic cross-linking effect, so that the copolyester has very high flame-retardant and anti-dripping efficiency, and also the copolyester is endowed with excellent flame retardant, anti-dripping and smoke suppressing performance. The method provided by the invention is basically consistent with the synthesis method of conventional polyester, not only is mature in technology, and easy and convenient to operate, but also is easy to control and convenient for industrial production.
Owner:SICHUAN UNIV
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