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    • 30. 发明申请
    • DISTILLATION PROCESS AND MULTI-COLUMN HEAT-INTEGRATED DISTILLATION SYSTEM
    • 蒸馏过程和多塔加热蒸馏系统
    • WO2011131325A8
    • 2012-09-07
    • PCT/EP2011001951
    • 2011-04-18
    • SAUDI BASIC IND CORPABDELGHANI MOHAMED SABRI
    • ABDELGHANI MOHAMED SABRI
    • B01D3/00B01D3/14B01D3/32B01D3/42C07C7/00C07C15/067
    • B01D3/143B01D3/007B01D3/322B01D3/42B01D3/4283B01D3/4288B01D3/4294C07C7/04Y02P20/124Y02P20/57C07C15/08
    • The invention relates to a process for separating a multi-component feed mixture in a distillation system comprising a first distillation column having a first fired reboiler, and at least a second distillation column having a second heat-exchange reboiler, comprising the steps of a) introducing the feed mixture to the first column, and separating into at least a first top and a first bottom product; b) taking part of the first bottom product for providing heat to the second reboiler as a utility stream; and c) feeding part of said utility stream after heat-exchange as main feed to the second column for further separation. This process allows significant energy savings, by reduction of the amount of external heat required for the fired reboiler and omission of a conventionally used heat-exhanger. The invention also relates to such distillation system suitable for separating a multi-component mixture with the process of the invention.
    • 本发明涉及在蒸馏系统中分离多组分进料混合物的方法,所述蒸馏系统包括具有第一次再沸器的第一蒸馏塔和至少具有第二热交换再沸器的第二蒸馏塔,所述第二蒸馏塔包括以下步骤:a) 将进料混合物引入第一塔中,并分离成至少第一顶部和第一底部产物; b)将第一底部产物的一部分作为效用流提供给第二再沸器的热量; 和c)在热交换之后将所述有用物流的一部分作为主进料送入第二塔用于进一步分离。 该方法通过减少烧制的再沸器所需的外部热量和省去常规使用的热交换器,可显着节约能源。 本发明还涉及适于用本发明方法分离多组分混合物的这种蒸馏系统。