Abstract:
PROBLEM TO BE SOLVED: To provide an IC tray material which while having low water absorbency, achieves a sufficiently high molecular weight, has a wide moldable temperature range calculated from the difference between the melting point and the thermal decomposition temperature thereof, has excellent melt moldability and excellent electrical conductivity, and is more excellent in heat resistance, chemical resistance, hydrolysis resistance and the like as compared with conventional aliphatic polyamide resins. SOLUTION: The IC tray material contains an electrical conductivity-imparting agent in a polyamide resin wherein the dicarboxylic acid component is composed of oxalic acid and the diamine component is composed of 1,9-nonanediamine and 2-methyl-1,8-octanediamine. The molar ratio between 1,9-nonanediamine and 2-methyl-1,8-octanediamine is from 1:99 to 99:1. COPYRIGHT: (C)2011,JPO&INPIT
Abstract:
PROBLEM TO BE SOLVED: To provide a method for controlling the molecular weight of a polyoxamide resin, which conventional production methods of the polyoxamide resin failed to achieve. SOLUTION: In the production method of the polyoxamide resin including a step in which a diester of oxalic acid is mixed with a diamine in a pressure-resistant container and pressure polymerization is performed in the presence of an alcohol produced by a condensation reaction, the method for controlling the molecular weight of the polyoxamide resin controls the pressure during the pressure polymerization to predetermined pressure within the range of 0.1(±0.07) to 3(±0.07) MPa according to the target molecular weight. COPYRIGHT: (C)2011,JPO&INPIT
Abstract:
PROBLEM TO BE SOLVED: To provide a separation membrane for efficiently separating ether and alcohol especially MTBE and methanol from a mixed solution containing the ether and the alcohol, and a separation method using the separation membrane. SOLUTION: A membrane comprising a compound containing agar and/or agarose or a membrane comprising a mixture prepared by adding at least one kind of a compound selected from polyoxyethylene, hydroxyalkylcellulose and sericin to the compound containing the agar and/or the agarose is provided. When ether and alcohol are separated from a mixed solution containing the ether and the alcohol by using the separation membrane, separation is performed in such a condition that an upstream side of the membrane is set in a liquid state, and a downstream side thereof is set in a vapor state.
Abstract:
PROBLEM TO BE SOLVED: To obtain a copolyamide with excellent optical and mechanical properties, and to provide a method for producing the copolyamide. SOLUTION: This copolyamide is such one containing (A) dicarboxylic acid unit with 5-100 wt.% of the dicarboxylic acid consisting of 6-22C branched saturated dicarboxylic acid, (B) diamine unit, and (C) aliphatic polyamide- forming unit; wherein the unit C accounts for 75-99.9 wt.% of this copolyamide. This copolyamide is obtained by producing a prepolymer of 800-5,000 in number- average molecular weight in the 1st stage polymerization followed by bringing the number-average molecular weight to 7,000-50,000 in the 2nd stage polymerization.
Abstract:
PROBLEM TO BE SOLVED: To obtain a polyamide excellent in properties for a serialized biaxial orientation and a mechanical strength. SOLUTION: This polyamide consisting essentially of diamines comprising an alicyclic diamine having one cyclohexane ring and dicarboxylic acids comprising a 6-22C branched type saturated carboxylic acid has a preferable composition of 50-99.95 mol.% lactam and/or aminocarboxylic acid, 0.025-25 mol.% diamine and 0.025-25 mol.% dicarboxylic acid, and regulated so that 5-100 mol.% of the diamines may consist of an alicyclic diamine, and 5-100 mol.% of the dicarboxylic acids may consist of a 6-22C branched type saturated carboxylic acid.
Abstract:
PROBLEM TO BE SOLVED: To obtain a process for producing a polyamide which has m- xylylenediamine units as essential units, does not gel nor yellow, and has a homogeneous quality and a good film-forming properties by using specific components. SOLUTION: An oligomer having a number average mol.wt. of 800 or higher and comprising 25-50mol% diamine units comprising 20-100mol% m- xylylenediamine units and 0-80mol% units derived from an aliph. and/or alicyclic diamine having a 4-18C alkylene group, 25-50mol% 6-18C linear aliph. dicarboxylic acid units, and 0-50mol% 4-12C aliph. ω-aminocarboxylic acid units is produced by the prepolymn. at 240 deg.C or lower. The oligomer is subjected to melt polymn. at a temp. at least 10 deg.C higher than the m.p. of the polymer obtd. from the oligomer but not higher than 280 deg.C and/or is subjected to solid phase polymn. at a temp. not lower than the glass transition point of the polymer but at least 10 deg.C lower than the m.p.
Abstract:
PROBLEM TO BE SOLVED: To prepare a film having excellent oxygen barrier properties and reduced in the dependency of the properties on temperatures by performing a step of prepolymerizing a specified polyamide resin under conditions in which the reaction mixture is molten under pressure so that a specified conditions may be held between the product of the steam pressure and the polymerization time and the polymerization temperature, and starting the post- polymerization step. SOLUTION: In producing a polyamide resin containing 20mol % or above, based on the entire resin, amide repeating units such as meta-xyleneadipamide units by a polycondensation process comprising a prepolymerization step under conditions in which the reaction mixture is molten under pressure and a subsequent post-polymerization step at normal pressure or in a vacuum, the precondensation step is performed under conditions in which the polymerization temperature (T) is 170-220 deg.C, the steam pressure (P) is 3kgf/cm G or above, and the relationship between Pt (t) is the polymerization time) and T is specified, the state is brought into one in which the temperature is 220 deg.C or below and the pressure is normal pressure or below, the water of condensation is removed, and the post-polymerization step is started. The water absorptivity of the amorphous part of the formed resin is 8wt.% or below (at an RH of 100% and 25 deg. and the activation energy for β relaxation is 18kJ/mol or below (at 100Hz and a strain of 0.05%).
Abstract:
PURPOSE:To prepare a straight-chain nylon 12 having a relative viscosity and a melt flow in respective particular ranges by prepolymn. using a laurolactam as a starting material under particular polymn. temp., pressure, and time. CONSTITUTION:A substantially straight-chain nylon 12 having a relative viscosity (etar) of 1.9 to 3.3 as measured at 25 deg.C in the form of a 10g/dm solution thereof dissolved in 98% sulfuric acid and a melt flow rate satisfying a requirement that the relationship between the etar and the melt flow rate (MFR) as measured under conditions of 235 deg.C and load of 2160 g falls within the range represented by the formula I. The nylon 12 is prepd. by a polycondensation method which comprises the step of conducting prepolymn. using epsilon-laurolactam and water as starting materials in the form of a melt under pressure and the step of subsequently conducting polymn. under atmospheric or reduced pressure. Prepolymn. conditions are such that the polymn. temp. (T) is 230 to 320 deg.C and the relationship between the polymerization temp. and the product of the water vapor pressure (P) in terms of kgf/cm G within the polymn. system and the polymerization time (t) in terms of hour, i.e., pt, simultaneously satisfies the formulae II and III.
Abstract:
PURPOSE:To obtain a polyamide copolymer being lowly colored, being excellent in mechanical and thermal properties and having low water absorptivity by mixing a specified dicarboxylic acid component with a specified diamine component in equimolar amounts and subjecting the mixture to two-stage melt polymerization. CONSTITUTION:A dicarboxylic acid component comprising 30-60 pts.wt. aromatic dicarboxylic acid component and 70-40 pts.wt. aliphatic dicarboxylic acid component is mixed with a diamine component comprising an aliphatic diamine component in equimolar amounts, and the resulting mixture is subjected to homogeneous melt polymerization at 230-280 deg.C in the presence of water under a pressure of 20kg/cm G or more to obtain a precondensate. Subsequently, this precondensate is subjected to melt polymerization at a temperature in the range from the melting point of the finally obtained copolymer to the melting point +30 deg.C. Thus, an aromatic-ring-containing polyamide copolymer being lowly colored, being excellent in mechanical and thermal properties, having low water absorptivity and not turning pink even on water absorption can be obtained.
Abstract:
PURPOSE:To provide a porous membrane stable in hydrophilicity and heat stability by coating the surface of a high-molecular porous membrane with a water-insoluble hydrophilic high-molecular material. CONSTITUTION:A microporous membrane is obtained by coating the surface of a high-molecular porous membrane having micropores with polyvinyl ether and further coating the surface polyvinyl ether layer with a water-insoluble hydrophylic high-molecular material.