Process for Cracking Heavy Hydrocarbon Feed
    22.
    发明申请
    Process for Cracking Heavy Hydrocarbon Feed 有权
    破碎重烃进料的工艺

    公开(公告)号:US20120125812A1

    公开(公告)日:2012-05-24

    申请号:US12952592

    申请日:2010-11-23

    IPC分类号: C10G69/06

    摘要: A process for cracking a heavy hydrocarbon feed comprising a vaporization step, a hydroprocessing step, and a steam cracking step is disclosed. The heavy hydrocarbon feed is passed to a first zone of a vaporization unit to separate a first vapor stream and a first liquid stream. The first liquid stream is passed to a second zone of the vaporization unit and contacted intimately with a counter-current steam produce a second vapor stream and a second liquid stream. The first vapor stream and the second vapor stream are cracked in the radiant section of the steam cracker to produce a cracked effluent. The second liquid stream reacted with hydrogen in the presence of a catalyst to produce a hydroprocessed product. A liquid hydroprocessed product is fed to the vaporization unit.

    摘要翻译: 公开了一种用于裂化重质烃进料的方法,包括蒸发步骤,加氢处理步骤和蒸汽裂解步骤。 将重质烃进料通入蒸发单元的第一区域以分离第一蒸气流和第一液体流。 第一液体流被传送到蒸发单元的第二区域并与逆流蒸汽紧密接触产生第二蒸气流和第二液体流。 第一蒸汽流和第二蒸汽流在蒸汽裂解器的辐射部分中裂开以产生裂化流出物。 在催化剂存在下,第二液体物流与氢气反应生成加氢产物。 将液体加氢产物送入汽化装置。

    Process for Cracking Heavy Hydrocarbon Feed
    23.
    发明申请
    Process for Cracking Heavy Hydrocarbon Feed 有权
    破碎重烃进料的工艺

    公开(公告)号:US20120125811A1

    公开(公告)日:2012-05-24

    申请号:US12952662

    申请日:2010-11-23

    IPC分类号: C10G69/06

    摘要: A process for cracking a heavy hydrocarbon feed comprising a vaporization step, a coking step, a hydroprocessing step, and a steam cracking step is disclosed. The heavy hydrocarbon feed is passed to a first zone of a vaporization unit to separate a first vapor stream and a first liquid stream. The first liquid stream is passed to a second zone of the vaporization unit and contacted intimately with a counter-current steam produce a second vapor stream and a second liquid stream. The first vapor stream and the second vapor stream are cracked in the radiant section of the steam cracker to produce a cracked effluent. The second liquid stream is thermally cracked in a coking drum to produce a coker effluent and coke. The coker effluent is separated into a coker gas and a coker liquid. The coker liquid is reacted with hydrogen in the presence of a catalyst to produce a hydroprocessed product. The hydroprocessed product is separated into a gas product and a liquid product. The liquid product is fed to the vaporization unit.

    摘要翻译: 公开了一种用于裂化重质烃进料的方法,包括蒸发步骤,焦化步骤,加氢处理步骤和蒸汽裂解步骤。 将重质烃进料通入蒸发单元的第一区域以分离第一蒸气流和第一液体流。 第一液体流被传送到蒸发单元的第二区域并与逆流蒸汽紧密接触产生第二蒸气流和第二液体流。 第一蒸汽流和第二蒸汽流在蒸汽裂解器的辐射部分中裂开以产生裂化流出物。 第二液体流在焦化鼓中热裂化以产生焦化器流出物和焦炭。 焦化流出物被分离成焦化气体和焦化液。 在催化剂存在下,将焦化液与氢气反应,生成加氢产物。 加氢处理的产物被分离成气体产物和液体产物。 将液体产物送入汽化装置。