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    • 31. 发明授权
    • Catalytic process for conversion of a petroleum residue using a fixed
bed hydrodemetallization catalyst
    • 使用固定床加氢脱金属催化剂转化石油残渣的催化方法
    • US6117306A
    • 2000-09-12
    • US942051
    • 1997-10-01
    • Frederic MorelJean-Luc DuplanThierry ChapusAlain BillonStephane KressmannGerard Heinrich
    • Frederic MorelJean-Luc DuplanThierry ChapusAlain BillonStephane KressmannGerard Heinrich
    • C10G69/04C10G45/00
    • C10G69/04Y10S208/95
    • A process for converting a heavy hydrocarbon fraction comprises treating the hydrocarbon feed in a hydrodemetallization section, the section containing at least one fixed bed hydrodemetallization catalyst. At least a portion of the hydrotreated liquid effluent from step a) is sent to an atmospheric distillation zone from which a distillate and an atmospheric residue are recovered; at least a portion of the atmospheric residue is sent to a vacuum distillation zone from which a vacuum distillate and a vacuum residue are recovered; at least a portion of the vacuum residue is sent to a deasphalting section from which a deasphalted hydrocarbon cut and residual asphalt are recovered; at least a portion of the deasphalted hydrocarbon cut is sent to a hydrotreatment section from which a gas fraction, a fuel fraction and a heavier liquid fraction of the hydrotreated feed are recovered, and at least a portion of the heavier liquid fraction of the hydrotreated feed is sent to a catalytic cracking section in which it is treated under conditions such that a gaseous fraction, a gasoline fraction, a gas oil fraction and a slurry fraction are produced.
    • 用于转化重质烃馏分的方法包括在加氢脱金属部分中处理烃进料,所述部分含有至少一个固定床加氢脱金属催化剂。 将来自步骤a)的加氢处理的液体流出物的至少一部分送至常压蒸馏区,回收馏出物和大气残留物; 将至少一部分大气残留物送至减压蒸馏区,从真空蒸馏区回收真空馏分和真空残渣; 将至少一部分真空残渣送至脱沥青部分,从其中回收脱沥青烃馏分和残余沥青; 将脱沥青烃馏分的至少一部分送到加氢处理部分,加氢处理的进料的气体馏分,燃料馏分和较重液体馏分从该加氢处理部分回收,加氢处理的进料的至少一部分较重液体馏分 被送到催化裂化部分,其中在气态馏分,汽油馏分,粗柴油馏分和淤浆馏分产生的条件下进行处理。
    • 37. 发明授权
    • Apparatus for purification of raw gasoline from catalytic cracking
    • 用于从催化裂化中净化原料汽油的装置
    • US06709639B1
    • 2004-03-23
    • US09522179
    • 2000-03-09
    • Thierry ChapusBlaise DidillonChristian MarcillyCharles Cameron
    • Thierry ChapusBlaise DidillonChristian MarcillyCharles Cameron
    • B01J804
    • C10G67/12C10G2400/02
    • An apparatus for the purification of catalytic cracking gasolines containing dienic and/or acetylenic impurities, and mercaptans, said apparatus comprising at least one selective hydrogenation reactor 3 containing at least one fixed catalyst bed, and having at least one line 1 for introducing a feed, at least one effluent outlet line, and a line supplying hydrogen to the reactor, said reactor being followed by at least one stabilization drum 4 connected to said effluent outlet line, the drum having at least one gas outlet line 5 and at least one stabilized effluent outlet line, and said effluent passing into at least one sweetening reactor 8 comprising at least one effluent inlet line 6 and at least one effluent outlet line, said reactor having close thereto at least one oxidizing agent supply line, said apparatus also comprising at least one drum 9 for degassing the effluent from the sweetening reactor 8, said drum 9 having at least one gas outlet line and at least one outlet line 11 for dedienized, stabilized and sweetened gasoline.
    • 一种用于纯化含有二烯和/或炔属杂质的催化裂解汽油的装置和硫醇,所述装置包括至少一个含有至少一个固定催化剂床的选择性氢化反应器3,并具有至少一条用于引入进料的管线1, 至少一个流出物出口管线和向反应器供应氢气的管线,所述反应器后面连接有至少一个与所述流出物出口管线连接的稳定鼓筒,所述转鼓具有至少一个气体出口管线5和至少一个稳定的流出物 出口管线,并且所述流出物进入至少一个甜味反应器8,其包含至少一个流出物入口管线6和至少一个流出物出口管线,所述反应器具有至少一个氧化剂供应管线,所述设备还包括至少一个 鼓9用于对来自甜味反应器8的流出物进行脱气,所述滚筒9具有至少一个气体出口管线和至少一个出口管线11 用于发明,稳定和增甜的汽油。
    • 39. 发明授权
    • Multi-step catalytic process for conversion of a heavy hydrocarbon
fraction
    • 用于转化重质烃馏分的多步催化方法
    • US6017441A
    • 2000-01-25
    • US942047
    • 1997-10-01
    • Frederic MorelGerard HeinrichStephane KressmannAlain BillonJean-Luc DuplanThierry Chapus
    • Frederic MorelGerard HeinrichStephane KressmannAlain BillonJean-Luc DuplanThierry Chapus
    • C10G67/04C10G69/04C10G21/00
    • C10G67/0454C10G69/04
    • A process for converting a heavy hydrocarbon fraction comprises treating the hydrocarbon feed in a hydroconversion section in the presence of hydrogen, the section comprising at least one three-phase reactor containing at least one ebullated bed hydroconversion catalyst, operating in liquid and gas riser mode, said reactor comprising at least one means for removing catalyst from said reactor and at least one means for adding fresh catalyst to said reactor. At least a portion of the hydroconverted liquid effluent is sent to an atmospheric distillation zone from which a distillate and an atmospheric residue are recovered; at least a portion of the atmospheric residue is sent to a vacuum distillation zone from which a vacuum distillate and a vacuum residue are recovered; at least a portion of the vacuum residue is sent to a deasphalting section from which a deasphalted hydrocarbon cut and residual asphalt are recovered; and at least a portion of the deasphalted hydrocarbon cut is sent to a hydrotreatment section from which a gas fraction, an atmospheric distillate and a heavier liquid fraction of the hydrotreated feed are recovered by atmospheric distillation separation, said section comprising at least one three-phase reactor containing at least one ebullated bed hvdroconversion catalyst operating in liquid and gas riser mode, the reactor comprising at least one means for extracting catalyst from the reactor and at least one means for adding fresh catalyst to the reactor.
    • 用于转化重质烃馏分的方法包括在氢的存在下在加氢转化段中处理烃进料,该部分包含至少一个含有至少一个沸腾床加氢转化催化剂的三相反应器,其以液体和气体提升管模式运行, 所述反应器包括至少一种用于从所述反应器除去催化剂的装置和用于将新鲜催化剂加入到所述反应器中的至少一种装置。 将至少一部分加氢转化的液体流出物送入常压蒸馏区,回收馏出物和大气残留物; 将至少一部分大气残留物送至减压蒸馏区,从真空蒸馏区回收真空蒸馏物和真空残渣; 将至少一部分真空残渣送至脱沥青部分,从其中回收脱沥青烃馏分和残余沥青; 并且至少一部分脱沥青烃切割被送到加氢处理部分,通过常压蒸馏分离回收加氢处理的进料的气体馏分,常压馏出物和较重的液体馏分,所述部分包含至少一个三相 反应器包含至少一种以液体和气体提升管模式运行的沸腾床转化催化剂,该反应器包括至少一种用于从反应器中提取催化剂的装置和至少一种用于向反应器中加入新鲜催化剂的装置。
    • 40. 发明授权
    • Multi-step process for conversion of a petroleum residue
    • 用于转化石油残渣的多步法
    • US6007703A
    • 1999-12-28
    • US942901
    • 1997-10-01
    • Frederic MorelStephane KressmannJean-Luc DuplanAlain BillonThierry ChapusGerard Heinrich
    • Frederic MorelStephane KressmannJean-Luc DuplanAlain BillonThierry ChapusGerard Heinrich
    • C10G67/04C10G69/04C10G45/00
    • C10G69/04C10G67/0454
    • A process for converting a heavy hydrocarbon fraction comprises treating the hydrocarbon feed in a hydrodemetallization section, the section comprising at least one fixed bed hydrodemetallization catalyst. At least a portion of the hydrotreated liquid effluent from step a) is sent to an atmospheric distillation zone from which a distillate and an atmospheric residue are recovered; at least a portion of the atmospheric residue is sent to a vacuum distillation zone from which a vacuum distillate and a vacuum residue are recovered; at least a portion of the vacuum residue is sent to a deasphalting section from which a deasphalted hydrocarbon cut and residual asphalt are recovered; and at least a portion of the deasphalted hydrocarbon cut is sent to a hydrotreatment section from which a gas fraction, a fuel fraction and a heavier liquid fraction of the hydrotreated feed are recovered, said section comprising at least one three-phase reactor containing at least one ebullated bed hydrotreatment catalyst operating in liquid and gas riser mode, the reactor comprising at least one means for removing catalyst from the reactor and at least one means for adding fresh catalyst to the reactor.
    • 用于转化重质烃馏分的方法包括在加氢脱金属部分中处理烃进料,该部分包含至少一个固定床加氢脱金属催化剂。 将来自步骤a)的加氢处理的液体流出物的至少一部分送至常压蒸馏区,回收馏出物和大气残留物; 将至少一部分大气残留物送至减压蒸馏区,从真空蒸馏区回收真空馏分和真空残渣; 将至少一部分真空残渣送至脱沥青部分,从其中回收脱沥青烃馏分和残余沥青; 并且至少一部分脱沥青烃切割被送到加氢处理部分,从该馏分回收加氢处理的进料的气体馏分,燃料馏分和较重的液体馏分,所述部分包含至少一个至少包含一个三相反应器 一种以液体和气体提升管模式运行的沸腾床加氢处理催化剂,该反应器包括至少一种用于从反应器中除去催化剂的装置和至少一种用于向反应器中加入新鲜催化剂的装置。