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    • 4. 发明公开
    • Hydrocarbon conversion process and apparatus
    • 石油转化过程和装置
    • EP0226421A3
    • 1987-10-07
    • EP86309518
    • 1986-12-05
    • ENGELHARD CORPORATION
    • Bartholic, David B.Barger, Dwight F.
    • C10G11/18B01J08/18
    • B01J8/18C10G11/18
    • A hydrocarbon conversion system wherein a hydrocarbon feed is converted to lower boiling products in a reactor (K) by contact at elevated temperature with fluidized solid material, spent material containing coke from said reactor is separated from reaction products and stripped of volatile hydrocarbons in a stripping zone (D), stripped solid material is regenerated with oxygen-containing gas in a regeneration zone (B), and hot freshly regenerated fluidized material is returned to the reactor (K), characterised by carrying out both the conversion and the regeneration in a dilute phase and passing all of the solid material from the reactor (K) and the regeneration zone (B) through respective preseparators (E) wherein rapid disengagement of solids and gases occur and from which the solid material is returned to respective beds in respective vessels (C,D) other than said reactor (K) and regenerator (B).
    • 一种烃转化系统,其中通过在高温下与流化固体材料接触将烃进料在反应器(K)中转化为低沸点产物,将来自所述反应器的含有焦炭的废料与反应产物分离并汽提汽提中的挥发性烃 区域(D)中,汽提固体物质在再生区(B)中用含氧气体再生,热新鲜再生的流化物质返回到反应器(K),其特征在于,在 稀释相,并使来自反应器(K)和再生区(B)的所有固体物质通过各自的预分离器(E)通过,其中固体和气体迅速脱离,固体材料从该分离器(E)返回到相应容器中的相应床 (C,D)除了所述反应器(K)和再生器(B)之外。
    • 5. 发明公开
    • Hydrocarbon treatment process
    • Verfahren zur Behandlung von Kohlenwasserstoffen。
    • EP0236055A2
    • 1987-09-09
    • EP87301612.5
    • 1987-02-24
    • ENGELHARD CORPORATION
    • Bartholic, David B.Barger, Dwight F.
    • C10G11/18
    • C10G11/18
    • A process wherein lower boiling products (H) are obtained from a hydrocarbon feed (J and/or HH) by contacting the feed with fluidized solid contact material at elevated temperature in a riser (K), spent contact material is separated and stripped of volatile hydrocarbons in a stripping zone (D), stripped contact material is regenerated with oxygen-containing gas (A) in a regeneration zone (B), and hot freshly regenerated fluidized solid contact material is returned to the riser (K), the process further including two or more of the following:

      (i) suspending hot regenerated contact material in a carbonizable lift gas at the lower portion of the riser and injecting hydrocarbon feed higher in the riser;
      (ii) charging hydrocarbon feed into the base of the riser, steam cooling a portion of the hot freshly regenerated contact material, and contacting the hydrocarbon feed with hot regenerated contact material upstream of where said hydrocarbon feed is contacted with the steam cooled contact material;
      (iii) cooling a portion of hot freshly regenerated contact material before returning it to the riser; and
      (iv) adding a portion of freshly heated regenerated contact material to said stripping zone.
    • 低沸点产物的过程 是obtd。 通过(a)在高温下将其与流化的固体接触材料接触从烃进料中。 在一个冒口,(b)sepg。 废弃的接触材料并在汽提区中汽提挥发性烃,(c)通过与O2-contg接触再生剥离的接触材料。 在再生区中的气体,以及(d)将热的新鲜再生的接触材料返回到提升管中还包括以下2个或更多个:(i)将热再生接触材料悬浮在提升管的下部的可燃提升气体中并注射 碳氢化合物进料在提升管中较高; (ii)将烃进料加入到提升管的底部中,蒸汽冷却一部分热的新鲜再生的接触材料,并使烃进料与热再生接触材料接触,该进料与蒸汽冷却的接触材料接触的点 ; (ii)在将热的新鲜再生接触材料的一部分返回到提升管之前冷却; 和(iv)将一部分新鲜再生的接触材料添加到汽提区。 触点材料首选 包括具有酸性位点的沸石催化剂。
    • 6. 发明公开
    • Hydrocarbon treatment process
    • EP0234924A2
    • 1987-09-02
    • EP87301613.3
    • 1987-02-24
    • ENGELHARD CORPORATION
    • Bartholic, David B.Barger, Dwight F.
    • C10G11/18
    • C10G11/18
    • A process wherein lower boiling products (H) are obtained from a hydrocarbon feed (J and/or HH) by contacting the feed with fluidized solid contact material at elevated temperature in a riser (K), spent contact material is separated and stripped of volatile hydrocarbons in a stripping zone (D), stripped contact material is regenerated with oxygen-containing gas (A) in a regeneration zone (B), and hot freshly regenerated fluidized solid contact material is returned to the riser (K), the process further including two or more of the following:

      (i) suspending hot regenerated contact material in a carbonizable lift gas at the lower portion of the riser and injecting hydrocarbon feed higher in the riser;
      (ii) charging hydrocarbon feed into the base of the riser, steam cooling a portion of the hot freshly regenerated contact material, and contacting the hydrocarbon feed with hot regenerated contact material upstream of where said hydrocarbon feed is contacted with the steam cooled contact material;
      (iii) cooling a portion of hot freshly regenerated contact material before returning it to the riser; and
      (iv) adding a portion of freshly heated regenerated contact material to said stripping zone.
    • 8. 发明公开
    • Hydrocarbon treatment process
    • 油气处理工艺
    • EP0236054A3
    • 1987-10-07
    • EP87301611
    • 1987-02-24
    • ENGELHARD CORPORATION
    • Bartholic, David B.Barger, Dwight F.
    • C10G11/18
    • B01J8/18C10G11/18
    • A process wherein lower boiling products (H) are obtained from a hydrocarbon feed (J and/or HH) by contacting the feed with fluidized solid contact material at elevated temperature in a riser (K), spent contact material is separated and stripped of volatile hydrocarbons in a stripping zone (D), stripped contact material is regenerated with oxygen-containing gas (A) in a regeneration zone (B), and hot freshly regenerated fluidized solid contact material is returned to the riser (K), the process further including two or more of the following:
      (i) suspending hot regenerated contact material in a carbonizable lift gas at the lower portion of the riser and injecting hydrocarbon feed higher in the riser; (ii) charging hydrocarbon feed into the base of the riser, steam cooling a portion of the hot freshly regenerated contact material, and contacting the hydrocarbon feed with hot regenerated contact material upstream of where said hydrocarbon feed is contacted with the steam cooled contact material; (iii) cooling a portion of hot freshly regenerated contact material before returning it to the riser; and (iv) adding a portion of freshly heated regenerated contact material to said stripping zone.
    • 通过在提升管(K)中将进料与流化固体接触材料在升高的温度下接触,从烃进料(J和/或HH)获得低沸点产物(H)的方法,分离废弃的接触材料并除去挥发性 在汽提区(D)中的烃,剥离的接触材料在再生区(B)中用含氧气体(A)再生,热新鲜再生的流化固体接触材料返回到提升管(K),该方法进一步 包括以下两个或更多个:(i)将热再生接触材料悬浮在提升管下部的可碳化提升气体中并在提升管中注入烃进料; (ii)将烃进料加入到提升管的底部中,蒸汽冷却热新鲜再生接触材料的一部分,以及使烃进料与热再生接触材料接触,在所述烃再生接触材料的上游,所述烃进料与蒸汽冷却的接触材料接触; (iii)在将一部分热的新鲜再生的接触材料返回到提升管之前冷却; 和(iv)将一部分新鲜再生的接触材料添加到所述汽提区。
    • 9. 发明公开
    • Hydrocarbon treatment process
    • 碳氢化合物处理过程
    • EP0234924A3
    • 1987-10-07
    • EP87301613
    • 1987-02-24
    • ENGELHARD CORPORATION
    • Bartholic, David B.Barger, Dwight F.
    • C10G11/18
    • C10G11/18
    • A process wherein lower boiling products (H) are obtained from a hydrocarbon feed (J and/or HH) by contacting the feed with fluidized solid contact material at elevated temperature in a riser (K), spent contact material is separated and stripped of volatile hydrocarbons in a stripping zone (D), stripped contact material is regenerated with oxygen-containing gas (A) in a regeneration zone (B), and hot freshly regenerated fluidized solid contact material is returned to the riser (K), the process further including two or more of the following:
      (i) suspending hot regenerated contact material in a carbonizable lift gas at the lower portion of the riser and injecting hydrocarbon feed higher in the riser; (ii) charging hydrocarbon feed into the base of the riser, steam cooling a portion of the hot freshly regenerated contact material, and contacting the hydrocarbon feed with hot regenerated contact material upstream of where said hydrocarbon feed is contacted with the steam cooled contact material; (iii) cooling a portion of hot freshly regenerated contact material before returning it to the riser; and (iv) adding a portion of freshly heated regenerated contact material to said stripping zone.
    • 通过在提升管(K)中在升高的温度下使进料与流化固体接触材料接触,从烃进料(J和/或HH)获得较低沸点产物(H),将失活的接触物质分离并除去挥发物 在汽提区(D)中的烃,在再生区(B)中用含氧气体(A)再生剥离的接触材料,并且热的新鲜再生的流态化固体接触材料返回到提升管(K),该工艺进一步 包括以下两种或更多种:(i)将热再生接触材料悬浮在提升管下部的可碳化提升气体中,并在提升管中注入更高的烃进料; (ii)将烃进料装入提升管底部,蒸汽冷却一部分热的新鲜再生的接触材料,并使烃进料与热再生接触材料接触,在所述烃进料与蒸汽冷却的接触材料接触的位置上游; (iii)在将其一部分热的新鲜再生的接触材料返回到立管之前冷却; 和(iv)将一部分新鲜加热的再生接触材料加入到所述汽提区中。
    • 10. 发明公开
    • Hydrocarbon treatment process
    • Verfahren zur Behandlung von Kohlenwasserstoffen。
    • EP0236054A2
    • 1987-09-09
    • EP87301611.7
    • 1987-02-24
    • ENGELHARD CORPORATION
    • Bartholic, David B.Barger, Dwight F.
    • C10G11/18
    • B01J8/18C10G11/18
    • A process wherein lower boiling products (H) are obtained from a hydrocarbon feed (J and/or HH) by contacting the feed with fluidized solid contact material at elevated temperature in a riser (K), spent contact material is separated and stripped of volatile hydrocarbons in a stripping zone (D), stripped contact material is regenerated with oxygen-containing gas (A) in a regeneration zone (B), and hot freshly regenerated fluidized solid contact material is returned to the riser (K), the process further including two or more of the following:

      (i) suspending hot regenerated contact material in a carbonizable lift gas at the lower portion of the riser and injecting hydrocarbon feed higher in the riser;
      (ii) charging hydrocarbon feed into the base of the riser, steam cooling a portion of the hot freshly regenerated contact material, and contacting the hydrocarbon feed with hot regenerated contact material upstream of where said hydrocarbon feed is contacted with the steam cooled contact material;
      (iii) cooling a portion of hot freshly regenerated contact material before returning it to the riser; and
      (iv) adding a portion of freshly heated regenerated contact material to said stripping zone.
    • 通过在提升管(K)中将进料与流化固体接触材料在升高的温度下接触,从烃进料(J和/或HH)获得低沸点产物(H)的方法,分离废弃的接触材料并除去挥发性 在汽提区(D)中的烃,剥离的接触材料在再生区(B)中用含氧气体(A)再生,并且热新鲜再生的流化固体接触材料返回到提升管(K),该方法进一步 包括以下两个或更多个:(i)将热再生接触材料悬浮在提升管下部的可碳化提升气体中并在提升管中注入烃进料; (ii)将烃进料加入到提升管的底部中,蒸汽冷却热新鲜再生接触材料的一部分,以及使烃进料与热再生接触材料接触,在所述烃再生接触材料的上游,所述烃进料与蒸汽冷却的接触材料接触; (iii)在将一部分热的新鲜再生的接触材料返回到提升管之前冷却; 和(iv)将一部分新鲜再生的接触材料添加到所述汽提区。