PRODUCTION OF AROMATIC CARBONATE OLIGOMER

    公开(公告)号:JPH01258648A

    公开(公告)日:1989-10-16

    申请号:JP8679588

    申请日:1988-04-08

    Abstract: PURPOSE:To obtain the subject compound having OH groups at both ends, by reacting a dihydric phenolic compound with diaryl carbonates at a specific ratio and removing the unreacted dihydric phenolic compound together with produced phenols from the system, thereby controlling the molecular weight of the product. CONSTITUTION:An aromatic polycarbonate oligomer having OH groups on >=90% of both ends can be produced by compounding a dihydric phenolic compound with diaryl carbonate at a molar ratio (phenol/carbonate) of >=1.2, especially >=1.5, reacting the components in the presence of a catalyst, removing the produced phenols (>=95mol% based on 2mol of the diaryl carbonate used in the reaction) from the system and, at the same time, removing a part or total of the unreacted dihydric phenolic compound from the system. The molecular weight of the oligomer can be controlled especially by removing the dihydric phenolic compound at a specific rate. The oligomer can be produced easily in high selectivity and the product is useful as a raw material for polymer.

    FLUORINATED DEALUMINIZED Y TYPE ZEOLITE

    公开(公告)号:JPH01257122A

    公开(公告)日:1989-10-13

    申请号:JP8374188

    申请日:1988-04-05

    Abstract: PURPOSE:To increase the efficiency of Y type zeolite as a catalyst for a liq. phase dehydration reaction by dealuminizing the zeolite and fluorinating the surface of the zeolite so as to obtain a prescribed ratio of SiO2 to Al2O3 and a prescribed fluorine content. CONSTITUTION:Y type zeolite is dealuminized and the surface of the zeolite is fluorinated to obtain fluorinated dealuminized Y type zeolite having 5.5-20 molar ratio of SiO2/Al2O3, 0.1-30wt.% fluorine content and a crystal structure similar to that of Y type zeolite. Fluorinated dealuminized Y type zeolite having proton exchange ability has an X-ray diffraction pattern shown by table 1. The pattern is formed by diffraction analysis with CuKalpha rays and the relative intensity of a diffracted ray at 6.4+ or -0.2 is represented by 100.

    EPOXY RESIN AND ITS PRODUCTION
    133.
    发明专利

    公开(公告)号:JPH0198613A

    公开(公告)日:1989-04-17

    申请号:JP25794587

    申请日:1987-10-13

    Abstract: PURPOSE:To obtain an epoxy resin which can be easily handled and can give a cured product excellent in a toughness such as bending strength and bending modulus, by reacting a specified oligocarbonate with an epihalohydrin and conducting the ring closure of the product through dehydrohalogenation by the addition of an alkali. CONSTITUTION:A bisphenol such as bisphenol A or bisphenol F is reacted with phosgene or diphenyl carbonate to obtain an oligocarbonate (A) of formula I (wherein R2-3 are each H, a lower alkyl or a phenyl, or they may be combined together to form a ring, X is a lower alkyl or a halogen, m is the number of substituents other than H and is 0-4, and n is 0-5). Component A is reacted with 2-20mol., per OH group of component A, of an epihalohydrin (B) of formula II (wherein R1 is H or an alkyl, and Y is a halogen) at 50-120 deg.C in an anhydrous state in the presence of a catalyst (C) such as quat. ammonium salt, and the product is subjected to ring closure through dehydrohalogenation by slowly adding thereto an alkali such as NaOH to obtain an epoxy resin of formula III.

    PRODUCTION OF CYCLIC CARBONATE
    134.
    发明专利

    公开(公告)号:JPS6426576A

    公开(公告)日:1989-01-27

    申请号:JP18098487

    申请日:1987-07-22

    Abstract: PURPOSE:To simply obtain the titled compound useful in various fields such as additives for specific ink, e.g. high speed recording ink jet or reaction solvent, by reacting a diol used as a raw material with a dialkylcarbonate using a basic catalyst as a catalyst. CONSTITUTION:A 1,3-diol or 1,2-diol which is used as a raw material is reacted with a dialkylcarbonate in the presence of a basic catalyst (preferably strongly basic substance) under ordinary pressure - pressure (normally 10atm.) at 60-180 deg.C and then preferably the resultant reaction mixture is subjected to heating and aging treatments under reduced pressure in the presence of a basic catalyst to provide the aimed compound. The dialkylcarbonate are used at a ratio of 0.1-10mol., preferably 1-2mol. to 1mol. diol. The basic catalyst is used at a ratio of preferably 0.001-0.005mol. to 1mol. diol.

    SYNTHETIC METHOD OF ALKANE POLYOL
    135.
    发明专利

    公开(公告)号:JPS57130941A

    公开(公告)日:1982-08-13

    申请号:JP1436881

    申请日:1981-02-04

    Abstract: PURPOSE:To obtain the titled compound in high yield under a low pressure, by reacting carbon monoxide with hydrogen in the presence of a catalytic system consisting of a rhodium compound and a rhenium compound. CONSTITUTION:Carbon monoxide is reacted with hydrogen in the presence of a catalytic system containing a rhodium compound and a rhenium compound, e.g. ReCl3, ReO3 or NH4ReO4, preferably in an amount of give a ratio between the numbers of gram-atoms of rhenium in the rhenium compound and the rhodium in the rhodium compound of about 0.01-100, preferably 0.1-10, preferably about 150-300 deg.C to give the titled compound. The molar ratio (CO/H2) between the carbon monoxide and the hydrogen to be fed is usually about (2/1)-(1/5). A co- catalyst, e.g. an alkali metallic compound or ammonia, is preferably used in the catalytic system.

    PRODUCTION OF MACROCYCLIC ESTER
    136.
    发明专利

    公开(公告)号:JPS55120581A

    公开(公告)日:1980-09-17

    申请号:JP2674179

    申请日:1979-03-09

    Abstract: PURPOSE:Polyester from dibasic acid and alkylene glycol is subjected to depolymerization and cyclization under reduced pressure in the presence of a specific additive to reduce the viscosity of the reaction mixture, smoothen the reaction progress and give title compound in a short time in high yield. CONSTITUTION:The depolymerization and cyclization of polyester of formula I (n is 6-14; m is 2-8), resulting from polycondensation reaction between dibasic acid such as suberic acid and alkylene glycol such as ethylene glycol, is effected under reduced pressure, wherein at least one selected from polyoxyalkylene glycol, polyoxyalkylene glycol ester, monobasic acid, monobasic acid ester, monobasic anhydride, monohydric alcohol and monohydric alcohol ester is added to the reaction mixture to form the macrocyclic ester of formula II. EFFECT:The products are free from trace amounts of impurities. USE:Musk perfume.

    RECOVERY OF CYANOETHYLATED KETONE
    137.
    发明专利

    公开(公告)号:JPS554320A

    公开(公告)日:1980-01-12

    申请号:JP7639478

    申请日:1978-06-26

    Abstract: PURPOSE:To recover the title compound useful as a raw material for alpha-picoline or resorcinol in high yield, by pretreating a reaction mixture containing a cyanoethylated ketone with water and an inorganic base, and by distilling the mixture. CONSTITUTION:Arylonitrile is reacted with a ketone, e.g. acetone, in the presence of a primary amine or its Schiff base, and an acid to give a cyanoethylated ketone. The reaction mixture is pretreated with water and an inorganic base, preferably an alkali metal compound, e.g. NaOH, in an amount equivalent to the acid, and distilled to recover the cyanoethylated ketone. The amount of water is one mole or more per mole of the amine or Schiff base. EFFECT:Simple isolation procedures of the unreacted ketone, acrylonitrile, and high-boiling by-products.

    PRODUCTION OF 33AMINOO22CYCLOHEXENONE

    公开(公告)号:JPS5492942A

    公开(公告)日:1979-07-23

    申请号:JP15732677

    申请日:1977-12-28

    Abstract: PURPOSE:The cyclization of 5-oxohexanenitrile is effected in an organic polar solvent and in the presence of a basic catalyst at a specific temperature to produce selectively title compound useful as synthetic intermediate for m-aminophenol, resorcinol in high yield. CONSTITUTION:The cyclization of 5-oxohexanenitrile is conducted in an organic polar solvent as methanol and in the presence of a basic catalyst as KOH or NaOH, at 160-220 deg.C, preferably 170-200 deg.C to produce 3-amino-2-cyclohexenone. The amounts of the organic solvent and basic catalyst are 5-200 times the weight of the starting material and 0.02-0.2 mol per mol respectively.

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