PRODUCTION OF 4C DICARBOXYLIC ACID DI LOWER ALKYL ESTER

    公开(公告)号:JPH06199736A

    公开(公告)日:1994-07-19

    申请号:JP36133692

    申请日:1992-12-28

    Abstract: PURPOSE:To provide a method for producing a 4c dicarboxylic acid di lower alkyl ester from lower alkyl ester, of acrylic acid, carbon monoxide and a lower saturated aliphatic monohydric alcohol in the presence of a cobalt carbonyl catalyst, giving the objective compound in a high yield even under industrially advantageous low pressure. CONSTITUTION:The method for producing a 4C dicarboxylic acid di lower alkyl ester by reacting a lower alkyl ester of acrylic acid with carbon monoxide and a lower saturated aliphatic monohydric alcohol in the presence of cobalt carbonyl and pyridine base at 100-120 deg.C comprises employing carbon monoxide containing 0.25-2vol.% of hydrogen gas to perform the reaction under a pressure of 25-50atm.

    PRODUCTION OF CARBON MONOXIDE-FORMALDEHYDE COPOLYMER

    公开(公告)号:JPH05112624A

    公开(公告)日:1993-05-07

    申请号:JP29791891

    申请日:1991-10-18

    Abstract: PURPOSE:To efficiently obtain the subject copolymer free from corrosion, capable of readily carrying out separation and recovery of a catalyst and useful for coating, etc., by copolymerizing carbon monoxide with formaldehyde under specific conditions. CONSTITUTION:In a method for producing a carbon monoxide-formaldehyde copolymer by reacting carbon monoxide with formaldehyde, a solid catalyst such as silica-alumina is used as the catalyst and an organic solvent (e.g. hexafluoroisopropanol) capable of exhibiting a liquid-like state at ordinary temperature to 100 deg.C C and dissolving the copolymer or mixture thereof is used as the reaction solvent and a copolymer produced by the reaction is dissolved in the reaction solvent to provide the objective copolymer.

    PRODUCTION OF DICARBOXYLIC ACID ESTER FROM BUTADIENE, CARBON MONOXIDE AND ALCOHOL

    公开(公告)号:JPH0426652A

    公开(公告)日:1992-01-29

    申请号:JP13052090

    申请日:1990-05-21

    Abstract: PURPOSE:To obtain the title compound in high yield by reacting butadiene with CO and an alcohol in the presence of cobalt-carbonyl and pyridine at two stages of different temperatures and adding paraffin to the resultant product and separating a catalyst complex. CONSTITUTION:Butadiene is reacted with CO and alcohol (preferably ethanol) in the presence of cobalt carbonyl and pyridine, preferably 3,5-dimethylpyridine at 120 deg.C to a temperature lower than 160 deg.C to afford 3-pentenoic acid ester as the intermediate. Then reaction temperature is raised directly without separating the intermediate and a reaction is carried out at 160-200 deg.C and paraffin is added to the resultant product to separate most of a pyridine complex which is a catalyst from a product layer and the separated pyridine complex is dissolved in acetone and recycled for next reaction. According to the above- mentioned method, troublesomeness of processes containing separation, recovery and regeneration of catalyst which was a defect of the conventional technique is remarkably reduced.

    PRODUCTION OF POLYOL
    55.
    发明专利

    公开(公告)号:JPS63179839A

    公开(公告)日:1988-07-23

    申请号:JP1181887

    申请日:1987-01-21

    Abstract: PURPOSE:To readily obtain a polyol in good yield, by reacting formaldehyde in the presence of H2, etc., using a specific catalyst. CONSTITUTION:Formaldehyde such as paraformaldehyde, etc., is reacted in the presence of H2 or mixed gas of H2 and CO, as necessary previously reacted under N2 for prescribed time and then reacted after substituting the mixed gas by H2, in an inert organic solvent such as dioxane, using an imidazolium salt expressed by formula I (R1-R4 are aliphatic or aromatic group or H; X is halogen) such as 3-ether-1-methylbenzimidazolium bromide, formula II or formula III (n is 1-10) and a ruthenium compound such as dodecacarbonyltriruthenium, as necessary an organic amine such as triethanolamine, as a catalyst to provide 2-4C polyol such as ethylene glycol, glycerin, erythritol. The above-mentioned reaction is carried out at ordinary temperature -300 deg.C in H2 pressure of 1-500 atmosphere when H2 exists.

    PRODUCTION OF HIGH MOLECULAR WEIGHT ALIPHATIC POLYESTER- BASED POLYMER

    公开(公告)号:JP2001081168A

    公开(公告)日:2001-03-27

    申请号:JP30285799

    申请日:1999-09-18

    Abstract: PROBLEM TO BE SOLVED: To provide a method for industrially advantageously producing in the presence of a low-cost iron-based catalyst a high molecular weight aliphatic polyester-based polymer having a practically sufficient molecular weight and excellent in mechanical strength, and to provide the same polymer obtained by the method. SOLUTION: In polycondensation reaction using (i) a mixture of an aliphatic dicarboxylic acid (or its diester) with an aliphatic diol or (ii) a precondensate obtained from the mixture as a reaction raw material in the presence of a transesterification catalyst comprising an iron-based catalyst or the iron-based catalyst and a co-catalyst, this method for producing the aliphatic polyester- based polymer comprises using at least one protonic acid or its ester selected from the group consisting of an organic phosphonic acid represented by general formula (1) O=P(OH)2R or O=P(OH)R2 (R is an aliphatic group or an aromatic group), a silicate represented by formula (2) (RO)2SiR2 (R is an aliphatic group or an aromatic group), phosphoric acid, ammonium phosphate, an aliphatic and/or aromatic compound having sulfonate group or sulfate group and sulfuric acid as the co-catalyst.

    PRODUCTION OF CARBONIC ESTER FROM CARBON DIOXIDE

    公开(公告)号:JP2001031629A

    公开(公告)日:2001-02-06

    申请号:JP20119999

    申请日:1999-07-15

    Abstract: PROBLEM TO BE SOLVED: To obtain a carbonic ester useful as a raw material or the like for e.g. production of polycarbonates, with an extremely inexpensive carbonylation agent having no toxicity and corrosiveness and a catalyst easy in handling by reacting carbon dioxide with an acetal compound in the presence of a tin oxide. SOLUTION: This compound is obtained by reacting carbon dioxide with an acetal compound such acetonedimethylacetal in the presence of a tin oxide such as dibutyltin oxide, preferably in the presence of a Lewis acid such as a compound of the formula: BF3.OEt2 (Et is ethyl), preferably at 80-200 deg.C for 1-100 h. The amount of the above tin oxide to be used as a catalyst is preferably 1/10,000 to 1/50 mol per mol of the above acetal compound.

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