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    • 4. 发明授权
    • Process for isolating cyclopentane and/or cyclopentene
    • 用于分离环戊烷和/或环戊烯的方法
    • US06264799B1
    • 2001-07-24
    • US09264145
    • 1999-03-05
    • Arnd StüweRolf Dieter WurtzMichael MüllerJens HerwigChristian GabelJoachim Grub
    • Arnd StüweRolf Dieter WurtzMichael MüllerJens HerwigChristian GabelJoachim Grub
    • B01D300
    • C07C13/10C07C9/18C07C13/12C07C2601/08C07C2601/10Y10S203/20
    • Cyclopentane and/or cyclopentene and, if desired, isopentane can be obtained by distillative separation from a pre-benzene fraction or a C5 fraction which has in each case being partially hydrogenated to remove acetylene compounds and diolefins, wherein a) in a first fractional distillation, low boilers are removed as first top product and, either b1) the first bottom product is fed to a second fractional distillation and there cyclopentene is taken off as second top product and cyclopentane and higher-boiling hydrocarbons are taken off as second bottom product and this second bottom product is separated into cyclopentene and higher boilers in a third fractional distillation, or b2) the first bottom product is subjected to a catalytic hydrogenation and subsequently, in a fractional distillation, separated into cyclopentane as top product and higher boilers as bottom product, or b3) the first bottom product is subjected to a fractional distillation to separate off the relatively high boilers as bottom product and the top product is subjected to a catalytic hydrogenation to form cyclopentene.
    • 如果需要,可以通过蒸馏分离前苯馏分或C5馏分获得环戊烷和/或环戊烯,每个馏分在每种情况下都被部分氢化除去乙炔化合物和二烯烃,其中a)在第一分馏中, 作为第一顶级产品除去低锅炉,并且b)将第一底部产物进料至第二次分馏,并且将环戊烯作为第二顶部产物取出,将环戊烷和较高沸点烃作为第二底部产物取出, 底部产物在第三次分馏中分离成环戊烯和更高级的锅炉,orb2)第一个底部产物进行催化氢化,随后在分馏中分离成环戊烷作为顶部产物,较高的锅炉作为底部产物,orb3) 第一个底部产品进行分馏以分离相对较高的锅炉 作为底部产物,顶部产物进行催化氢化以形成环戊烯。
    • 7. 发明授权
    • Process for isolating cyclopentane and/or cyclopentene
    • 用于分离环戊烷和/或环戊烯的方法
    • US06468399B2
    • 2002-10-22
    • US09784853
    • 2001-02-16
    • Arnd StüweRolf Dieter WurtzMichael MüllerJens HerwigChristian GabelJoachim Grub
    • Arnd StüweRolf Dieter WurtzMichael MüllerJens HerwigChristian GabelJoachim Grub
    • B01D300
    • C07C13/10C07C9/18C07C13/12C07C2601/08C07C2601/10Y10S203/20
    • Cyclopentane and/or cyclopentene and, if desired, isopentane can be obtained by distillative separation from a pre-benzene fraction or a C5 fraction which has in each case being partially hydrogenated to remove acetylene compounds and diolefins, wherein a) in a first fractional distillation, low boilers are removed as first top product and, either b1) the first bottom product is fed to a second fractional distillation and there cyclopentene is taken off as second top product and cyclopentane and higher-boiling hydrocarbons are taken off as second bottom product and this second bottom product is separated into cyclopentene and higher boilers in a third fractional distillation, or b2) the first bottom product is subjected to a catalytic hydrogenation and subsequently, in a fractional distillation, separated into cyclopentane as top product and higher boilers as bottom product, or b3) the first bottom product is subjected to a fractional distillation to separate off the relatively high boilers as bottom product and the top product is subjected to a catalytic hydrogenation to form cyclopentene.
    • 如果需要,可以通过蒸馏分离前苯馏分或C5馏分获得环戊烷和/或环戊烯,每个馏分在每种情况下都被部分氢化除去乙炔化合物和二烯烃,其中a)在第一分馏中, 作为第一顶级产品除去低锅炉,并且b)将第一底部产物进料至第二次分馏,并且将环戊烯作为第二顶部产物取出,将环戊烷和较高沸点烃作为第二底部产物取出, 底部产物在第三次分馏中分离成环戊烯和更高级的锅炉,orb2)第一个底部产物进行催化氢化,随后在分馏中分离成环戊烷作为顶部产物,较高的锅炉作为底部产物,orb3) 第一个底部产品进行分馏以分离相对较高的锅炉 作为底部产物,顶部产物进行催化氢化以形成环戊烯。