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    • 62. 发明专利
    • FLEXIBLE EPOXY RESIN COMPOSITION
    • JPH06136090A
    • 1994-05-17
    • JP28314992
    • 1992-10-21
    • KOBE STEEL LTD
    • YAMAMOTO KOJIFUJISAWA KAZUHISA
    • C08G59/18C08G59/42
    • PURPOSE:To provide a flexible epoxy resin composition giving cured products excellent in their electric insulating properties and having a good balance between heat resistance and flexibility by compounding an epoxy resin with a flexible curing agent so as to satisfy specific conditions. CONSTITUTION:The composition contains (A) an epoxy resin (preferably a bisphenol A type epoxy resin, a bisphenol F type epoxy resin, etc.,) and (B) a flexible curing agent (e.g. a dicarboxylic acid dehydrative polycondensation product such as polyadipic acid polyanhydride) as essential components and satisfies the heat resistance parameter P of the inequality (PE is the whole bond enthalpy of bond sites except C-H bonds in the skeleton of the component A/ the whole bond enthalpy of the C-H bond sites in the skeleton of the component A; PF is the whole bond enthalpy of bond sites except the C-H bond sites in the skeleton of the component B/ the whole bond enthalpy of the C-H bond sites in the skeleton of the component B; XE is the molar fraction of the component A in the composition; XF is the molar fraction of the component B in the composition). The composition is generally preferably cured at 50-150 deg.C.
    • 65. 发明专利
    • PRODUCTION OF DIALKYLNAPHTHALENE
    • JPH04283523A
    • 1992-10-08
    • JP7456591
    • 1991-03-13
    • KOBE STEEL LTD
    • MIFUJI YUTAKAYAMAMOTO KOJI
    • C07B61/00B01J29/40C07C2/86C07C15/24
    • PURPOSE:To produce th subject compound in a high yield by, in reaction between alkylnaphthalenes and an alkylating agent in the presence of a porous solid acid catalyst, divisionally adding the alkylating agent and improving conversion of naphthalene and selectivity of the objective compound. CONSTITUTION:In production of dialkylnaphthalenes by using alkylnaphthalenes as a raw material and reacting an alkylating agent therewith in the presence of a porous solid acid catalyst (e.g. zeolite), the alkylnaphthalenes are allowed to pass through the inside of a tubular reactor and the alkylating agent is divisionally added from plural positions on the above-mentioned passage in an amount of 2-10 equipvalents in total based on the alkylnaphthalenes so that tha amount of the alkylating agent added at one time may not exceed 1 equipvalent. The alkylating agent is added preferably by making introducing- holes in the tabular reactor and introducing it therethrough or by connecting plural tubular reactors, making introducing-holes at an intermediate position thereof and introducing it therethrough.