1.
    发明专利
    未知

    公开(公告)号:DE60101020T2

    公开(公告)日:2004-06-24

    申请号:DE60101020

    申请日:2001-06-19

    Applicant: DAICEL CHEM

    Abstract: Heliotropin is oxidized with a percarboxylic acid in the presence of formic acid and an optionally added organic solvent, to thereby produce sesamol at high efficiency while suppressing by-production of heliotropic acid.

    3.
    发明专利
    未知

    公开(公告)号:DE60101020D1

    公开(公告)日:2003-11-27

    申请号:DE60101020

    申请日:2001-06-19

    Applicant: DAICEL CHEM

    Abstract: Heliotropin is oxidized with a percarboxylic acid in the presence of formic acid and an optionally added organic solvent, to thereby produce sesamol at high efficiency while suppressing by-production of heliotropic acid.

    5.
    发明专利
    未知

    公开(公告)号:NO20013046L

    公开(公告)日:2001-12-20

    申请号:NO20013046

    申请日:2001-06-19

    Applicant: DAICEL CHEM

    Abstract: Heliotropin is oxidized with a percarboxylic acid in the presence of formic acid and an optionally added organic solvent, to thereby produce sesamol at high efficiency while suppressing by-production of heliotropic acid.

    6.
    发明专利
    未知

    公开(公告)号:NO20013046D0

    公开(公告)日:2001-06-19

    申请号:NO20013046

    申请日:2001-06-19

    Applicant: DAICEL CHEM

    Abstract: Heliotropin is oxidized with a percarboxylic acid in the presence of formic acid and an optionally added organic solvent, to thereby produce sesamol at high efficiency while suppressing by-production of heliotropic acid.

    PURIFICATION OF EPSILON-CAPROLACTONE

    公开(公告)号:JPH08311058A

    公开(公告)日:1996-11-26

    申请号:JP13986695

    申请日:1995-05-15

    Applicant: DAICEL CHEM

    Abstract: PURPOSE: To provide a method for purifying ε-caprolactone by which a high yield of the ε-caprolactone is obtained from a reactional mixture prepared by oxidizing cyclohexanone by distillation. CONSTITUTION: Low-boiling substances contained in a reactional mixture prepared by oxidizing cyclohexanone are distilled away by the first distillation step and high-boiling fraction impurities are then taken out in a low concentrated state as a bottom product in the second distillation step for distilling away the product ε-caprolactone from the first bottom product and separating the ε-caprolactone from high-boiling substances so as to provide at least >=20wt.% lactone concentration in the second bottom product. The ε- caprolactone contained in the second bottom product is subsequently evaporated with an evaporator and recovered in a method for purifying the ε-caprolactone by distilling the reactional mixture and separating the ε-caprolactone from the impurities.

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