Thermal cracking of heavy hydrocarbon oils
    1.
    发明授权
    Thermal cracking of heavy hydrocarbon oils 失效
    重质烃油的热裂解

    公开(公告)号:US4477334A

    公开(公告)日:1984-10-16

    申请号:US583183

    申请日:1984-02-24

    IPC分类号: C10G51/02 C10G9/14

    CPC分类号: C10G51/023

    摘要: A heavy hydrocarbon feed stock is, after being heat-treated in a first cracking zone, introduced into a second thermal cracking zone for obtaining a thermally cracked product and a pitch product. The second cracking zone has a plurality of cracking reactors which are connected in series, through which is successively passed the treated feed stock and to each of which is supplied a gaseous heat transfer medium to maintain the liquid phase therein at a temperature sufficient for effecting the thermal cracking and to strip the resulting distillable, cracked components from the liquid phase. The thermal cracking temperature in one reactor is so controlled as to become higher than that in its adjacent upstream-side reactor. The distillable, cracked components in respective reactors are removed overhead therefrom and separated into a heavy fraction and a light fraction, while the liquid phase in the downstream-end reactor is discharged therefrom for recovery as the pitch product. The light fraction is recovered as a light product oil, while the heavy fraction is fed to a third thermal cracking zone for obtaining a tar-containing product which is recycled to at least one of the reactors of the second thermal cracking zone.

    摘要翻译: 在第一裂解区热处理后,将重质烃原料引入第二热裂解区以获得热裂化产物和沥青产物。 第二裂解区具有多个串联连接的裂解反应器,通过该裂化反应器连续通过处理过的原料,并将其中的每一个供应气态传热介质,以保持其中的液相在足以实现 热裂解并从液相中剥离得到的可馏出的裂化组分。 一个反应器中的热裂解温度被控制得高于其相邻的上游侧反应器中的热裂解温度。 各反应器中的可蒸馏的裂化组分在其上从其上除去并分离成重馏分和轻馏分,而下游反应器中的液相从其排出,作为沥青产物进行回收。 将轻馏分作为轻质产物油回收,同时将重馏分进料至第三热裂解区,以获得再循环至第二热裂解区的至少一个反应器的含焦油产物。

    Process of thermally cracking heavy hydrocarbon oils
    2.
    发明授权
    Process of thermally cracking heavy hydrocarbon oils 失效
    重质烃油热裂解工艺

    公开(公告)号:US4487686A

    公开(公告)日:1984-12-11

    申请号:US583182

    申请日:1984-02-24

    IPC分类号: C10G51/02 C10G9/16 C10G9/14

    CPC分类号: C10G51/023

    摘要: A heavy hydrocarbon feed stock is, after being heat-treated in a first cracking zone, is introduced into a second thermal cracking zone for obtaining a thermally cracked product and a pitch product. The second cracking zone has a plurality of cracking reactors which are connected in series, through which is successively passed the treated feed stock and to each of which is supplied a gaseous heat transfer medium to maintain the liquid phase therein at a temperature sufficient for effecting the thermal cracking and to strip the resulting distillable, cracked components from the liquid phase. The thermal cracking temperature in one reactor is so controlled as to become higher than that in its adjacent upstream-side reactor. The distillable, cracked components in respective reactors are removed overhead therefrom and separated into a heavy fraction and a light fraction, while the liquid phase in the downstream-end reactor is discharged therefrom for recovery as the pitch product. The light fraction is recovered as a light product oil, while the heavy fraction is fed to a third thermal cracking zone for obtaining a tar-containing product which is recycled to at least one of the reactors of the second thermal cracking zone together with a naphthene base heavy hydrocarbon oil.

    摘要翻译: 在第一裂解区热处理后,将重质烃原料引入第二热裂解区以获得热裂化产物和沥青产物。 第二裂解区具有多个串联连接的裂解反应器,通过该裂化反应器依次通过处理过的原料,并将其中的每一个供应气态传热介质,使其中的液相保持在足以实现 热裂解并从液相中剥离得到的可馏出的裂化组分。 一个反应器中的热裂解温度被控制得高于其相邻的上游侧反应器中的热裂解温度。 各反应器中的可蒸馏的裂化组分在其上从其上除去并分离成重馏分和轻馏分,而下游反应器中的液相从其排出,作为沥青产物进行回收。 将轻馏分作为轻质产物油回收,同时将重质馏分进料至第三热裂解区,以获得含焦油的产物,其与第二热裂解区的至少一个反应器一起再循环至环烷烃 基础重烃油。

    Catalyst combustor
    4.
    发明授权
    Catalyst combustor 失效
    催化剂燃烧器

    公开(公告)号:US5375999A

    公开(公告)日:1994-12-27

    申请号:US087860

    申请日:1993-07-09

    摘要: A catalyst combustor is here disclosed which comprises a catalyst section for permitting the catalyst combustion of a fuel, a burner for preheating the catalyst section, a cross flow type heat exchanger for preheating air for combustion which is disposed in a combustion gas generated by the catalyst combustion, and a fan for feeding the air for combustion to the burner via the cross flow type heat exchanger.

    摘要翻译: 这里公开了一种催化剂燃烧器,其包括用于允许燃料的催化剂燃烧的催化剂部分,用于预热催化剂部分的燃烧器,用于预热燃烧空气的交叉流型热交换器,其布置在由催化剂产生的燃烧气体中 燃烧,以及用于经由横流型热交换器将燃烧空气供给燃烧器的风扇。