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    Process for the preparation of carbon fibers
    1.
    发明授权
    Process for the preparation of carbon fibers 失效
    碳纤维制备方法

    公开(公告)号：US4554148A

    公开(公告)日：1985-11-19

    申请号：US611152

    申请日：1984-05-17

    申请人： Shimpei Gomi ,  Tomio Arai ,  Fumio Mogi ,  Kunio Miura ,  Sugio Otani

    发明人： Shimpei Gomi ,  Tomio Arai ,  Fumio Mogi ,  Kunio Miura ,  Sugio Otani

    IPC分类号： D01F9/155 ,  C10C3/00 ,  D01F9/145 ,  D01F9/12

    CPC分类号： D01F9/145 ,  C10C3/00

    摘要： A process for the preparation of carbon fibers, including the steps of:subjecting a raw material oil to thermal cracking conditions at a temperature of between 400.degree. to 500.degree. C. while removing cracked, light hydrocarbon components to obtain a pitch product containing at least 5 weight % of mesophase and not more than 10 weight % of light hydrocarbon components with a boiling point at 60 mmHg (absolute) of 300.degree. C. or less and having a softening point of between 140.degree. and 220.degree. C., the raw material oil having a boiling point of at least 500.degree. C. and containing at least 30 weight % of a residual oil which has a boiling point of at least 500.degree. C. and a metal content of at least 200 weight ppm and which is derived from a napthene base and/or intermediate base petroleum crude;removing the mesophase having a particle size of more than 10 .mu.m from the pitch product to obtain a substantially mesophase-free carbonaceous pitch;spinning the substantially mesophase-free pitch into fibers;rendering the spun fibers infusible; andcarbonizing the infusible fibers.

    摘要翻译： 一种制备碳纤维的方法，包括以下步骤：在400-500℃的温度下对原料油进行热裂解条件，同时除去裂化的轻烃组分，得到至少含有 5重量％的中间相和不超过10重量％的沸点在60mmHg（绝对值）为300℃或更低，软化点在140-220℃之间的轻烃组分，原料 沸点至少为500℃，含有至少30重量％的沸点为至少500℃，金属含量至少为200重量ppm的残油的材料油，其衍生物 来自一个萘环和/或中间基石油原油; 从沥青产物中除去具有大于10μm的粒度的中间相，以获得基本上不含中间相的碳质沥青; 将基本上无中间相沥青纺丝成纤维; 使纺丝纤维不可渗透; 并将可熔纤维碳化。

    Method of preparing carbonaceous pitch
    2.
    发明授权
    Method of preparing carbonaceous pitch 失效
    碳质沥青的制备方法

    公开(公告)号：US4591424A

    公开(公告)日：1986-05-27

    申请号：US611072

    申请日：1984-05-17

    申请人： Shimpei Gomi ,  Tomio Arai ,  Fumio Mogi ,  Takao Nakagawa ,  Kunio Miura ,  Sugio Otani

    发明人： Shimpei Gomi ,  Tomio Arai ,  Fumio Mogi ,  Takao Nakagawa ,  Kunio Miura ,  Sugio Otani

    IPC分类号： C10C3/04 ,  C10C3/00 ,  C10C3/10 ,  D01F9/145 ,  D01F9/155 ,  C10C3/18

    CPC分类号： C10C3/00 ,  D01F9/145

    摘要： A method of preparing an carbonaceous pitch, including the steps of:subjecting a raw material oil to thermal cracking conditions while removing cracked, light hydrocarbon components to obtain a pitch product containing at least 5 weight % of mesophase and not more than 10 weight % of light hydrocarbon components with a boiling point at 60 mmHg of 300.degree. C. or less and having a softening point of between 160.degree. and 220.degree. C., the raw material oil being composed mainly of a residual oil which has a boiling point of 350.degree. C. or more and which is derived from a naphthene base petroleum crude; andremoving the mesophase from the pitch product to obtain a substantially mesophase-free carbonaceous pitch.

    摘要翻译： 一种制备碳质沥青的方法，包括以下步骤：将原料油进行热裂解处理，同时除去裂化的轻烃组分，得到含有至少5重量％的中间相的沥青产物，并且不超过10重量％ 沸点在60mmHg的轻质烃成分为300℃以下，软化点为160〜220℃，原料油主要由沸点为350℃的残油组成 ℃以上，衍生自环烷烃基石油原油; 并从沥青产物中除去中间相以获得基本上无中间相的碳质沥青。

    Carbonaceous pitch, process for the preparation thereof and use thereof to make carbon fibers
    3.
    发明授权
    Carbonaceous pitch, process for the preparation thereof and use thereof to make carbon fibers 失效
    碳质沥青，其制备方法及其制备碳纤维的用途

    公开(公告)号：US4504455A

    公开(公告)日：1985-03-12

    申请号：US577695

    申请日：1984-02-07

    申请人： Sugio Otani ,  Shimpei Gomi ,  Fumio Mogi

    发明人： Sugio Otani ,  Shimpei Gomi ,  Fumio Mogi

    IPC分类号： C10C3/02 ,  D01F9/145 ,  D01F9/155 ,  C10C3/06 ,  C10C3/08

    CPC分类号： D01F9/145

    摘要： A novel reformed mesophase pitch having a mesophase content MC of between 40 and 100%, a quinoline-insoluble content QI of between 5 and 70 weight % and anisotropic domains forming a continuous phase. The reformed mesophase pitch is obtained by heat-treating a dormant mesophase pitch which comprises dormant anisotropic components which are partially hydrogenated, polycyclic polycondensed ring aromatic hydrocarbons derived from the mesophase of a mesophase pitch by hydrogenation of the mesophase and which are soluble in quinoline. The dormant mesophase pitch is optically isotropic in nature but, upon being subjected to shear forces in one direction, capable of being oriented in said direction. Preferably, the reformed mesophase pitch has a softening point SP in .degree.C. satisfying the following conditions:when 40 .ltoreq.MC

    摘要翻译： 中间相含量MC为40〜100％，喹啉不溶成分QI为5〜70重量％，形成连续相的各向异性畴的新型中间相沥青。 重整的中间相沥青是通过热处理休眠中间相沥青得到的，该休眠中间相沥青包括由中间相氢化得到的中间相沥青的衍生自中间相沥青的部分氢化的多环缩聚环芳烃的休眠各向异性成分，并且可溶于喹啉。 休眠中间相沥青本质上是光学各向同性的，但是在一个方向受到剪切力时，能够沿所述方向取向。 优选地，重整的中间相沥青具有在℃下的软化点SP，满足以下条件：当40 = MC <100，＆lt; IMAGE＆gt;当MC = 100时，重整的中间相沥青可用作前体材料 用于碳纤维。

    Thermal cracking of heavy hydrocarbon oils
    4.
    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

    申请人： Shimpei Gomi ,  Tomomitsu Takeuchi ,  Itaru Matsuo ,  Masaki Fujii ,  Toru Takatsuka ,  Ryuzo Watari

    发明人： Shimpei Gomi ,  Tomomitsu Takeuchi ,  Itaru Matsuo ,  Masaki Fujii ,  Toru Takatsuka ,  Ryuzo Watari

    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 for producing high quality pitch
    6.
    发明授权
    Process for producing high quality pitch 失效
    生产高品质音调的过程

    公开(公告)号：US4240898A

    公开(公告)日：1980-12-23

    申请号：US968771

    申请日：1978-12-12

    申请人： Shimpei Gomi

    发明人： Shimpei Gomi

    IPC分类号： C10C3/00 ,  C10G9/00 ,  C10G55/04 ,  C10G9/14

    CPC分类号： C10C3/002 ,  C10G55/04 ,  C10G9/00

    摘要： A process is disclosed for producing pitches of high quality in a high yield by subjecting selected crude oil to adiabatic thermal and steam cracking process at a temperature between 700.degree. C. and 1000.degree. C. to produce gases containing ethylene, propylene and the like and a tar pitch having an ethylene-to-acetylene ratio above 5; adjusting the pitch content of the tar pitch in the range between 20 and 80 wt % (if this content is outside this specified range); heat-treating at a temperature between about 450.degree. C. and about 550.degree. C. under a pressure between about 50 and about 150 kg/cm.sup.2 (G) for about 1 to 15 minutes, and subsequently heat-soaking at a temperature between about 350.degree. and about 450.degree. C. under a pressure between about 0.5 and about 10 kg/cm.sup.2 (G) for about 15 minutes to 10 hours.

    摘要翻译： 公开了通过在700℃至1000℃之间的温度下对选定的原油进行绝热的热蒸汽和蒸汽裂解处理以产生含有乙烯，丙烯等的气体，以及 乙炔与乙炔的比率高于5的焦油沥青; 将焦油沥青的沥青含量调节在20〜80重量％的范围内（若该含量在规定范围之外）; 在约50至约150kg / cm 2（G）之间的压力下在约450℃至约550℃之间的温度下热处理约1至15分钟，随后在约 在约0.5至约10kg / cm 2（G）之间的压力下，约350分钟至约450℃约15分钟至10小时。

    Process for the production of carbonaceous pitch
    9.
    发明授权
    Process for the production of carbonaceous pitch 失效
    生产碳质沥青的方法

    公开(公告)号：US4663022A

    公开(公告)日：1987-05-05

    申请号：US815923

    申请日：1986-01-03

    申请人： Shimpei Gomi ,  Takuya Ueda ,  Takao Nakagawa ,  Masaharu Tachibana

    发明人： Shimpei Gomi ,  Takuya Ueda ,  Takao Nakagawa ,  Masaharu Tachibana

    IPC分类号： C01B31/00 ,  C10C3/02 ,  C10C3/10 ,  C10G51/02 ,  C10G55/04 ,  D01F9/155 ,  C01G51/02 ,  C10C1/00 ,  C10C3/00

    CPC分类号： C10G51/023 ,  C10G55/04

    摘要： A continuous process for the production of carbonaceous pitch, including heat-treating an aromatic heavy oil in a first thermal cracking zone for obtaining a first cracked product, and introducing the first cracked product into a second thermal cracking zone where it is thermally cracked by direct contact with a gaseous heat transfer medium to form distillable cracked components and a mesophase-containing pitch. The liquid phase in the second thermal cracking zone, including the mesophase-containing pitch, is discharged therefrom and separated into a mesophase-rich pitch and a matrix pitch having a low concentration of mesophase. The mesophase-rich pitch is recovered while at least a portion of the matrix pitch is recycled to the second thermal cracking zone. The distillable cracked components are stripped from the liquid phase in the second thermal cracking zone with the heat transfer medium, and the resulting gas phase is withdrawn overhead therefrom and then separated into a light fraction and a heavy fraction. The heavy fraction is fed to the first thermal cracking zone.

    摘要翻译： 一种用于生产碳质沥青的连续方法，包括在第一热裂解区中热处理芳族重油以获得第一裂化产物，并将第一裂化产物引入第二热裂解区，其中它通过直接 与气体传热介质接触以形成可蒸馏的裂化组分和含中间相沥青。 包括含中间相沥青的第二热裂解区中的液相从其中排出并分离成富含中间相的沥青和具有低浓度中间相的基体沥青。 回收富含中间相沥青，而将至少一部分基质沥青再循环至第二热裂解区。 在第二热裂解区用传热介质从馏出的液相中蒸馏出馏出的裂化组分，将所得气相从塔顶馏出，然后分离成轻馏分和重馏分。 重馏分被送入第一热裂解区。

    Process for thermally cracking heavy hydrocarbon oil
    10.
    发明授权
    Process for thermally cracking heavy hydrocarbon oil 失效
    重质烃油热裂解工艺

    公开(公告)号：US4581124A

    公开(公告)日：1986-04-08

    申请号：US747710

    申请日：1985-06-24

    申请人： Shimpei Gomi ,  Terukatsu Miyauchi

    发明人： Shimpei Gomi ,  Terukatsu Miyauchi

    IPC分类号： C10G51/04 ,  C10C3/10 ,  C10G51/00 ,  C10G51/02 ,  C10G9/16 ,  C10G9/14

    CPC分类号： C10G51/023 ,  C10G51/00

    摘要： A continuous process for thermally cracking a heavy hydrocarbon oil, including heat-treating the heavy hydrocarbon oil in a first thermal cracking zone for obtaining a first cracked product, and introducing the first cracked product into a second thermal cracking zone where it is thermally cracked by direct contact with a gaseous heat transfer medium to form distillable cracked components and a mesophase-containing pitch. The liquid phase in the second thermal cracking zone, including the mesophase-containing pitch, is withdrawn therefrom and separated into a mesophase-rich pitch and a matrix pitch having a low concentration of mesophase. The matrix pitch is recycled to the second thermal cracking zone. The distillable cracked components are stripped from the liquid phase in the second thermal cracking zone with the heat transfer medium, and the resulting gas phase is discharged overhead therefrom and then separated into a light fraction and a heavy fraction. The heavy fraction is fed to a third thermal cracking zone to obtain light oil components and an aromatic tar. The aromatic tar is recycled to the second thermal cracking zone.

    摘要翻译： 一种用于热裂解重质烃油的连续方法，包括在第一热裂解区中对重质烃油进行热处理以获得第一裂化产物，并将第一裂化产物引入第二热裂解区，其中它被热裂化 与气体传热介质直接接触以形成可蒸馏的裂化组分和含中间相沥青。 包括含中间相沥青的第二热裂解区中的液相从其中排出并分离成富含中间相的沥青和具有低浓度中间相的基体沥青。 将基质沥青再循环至第二热裂解区。 在第二热裂解区用蒸发介质从馏出液中蒸馏出馏出的裂化成分，将得到的气相从塔顶排出，分离成轻馏分和重馏分。 将重馏分进料到第三热裂解区以获得轻油组分和芳族焦油。 芳香焦油被再循环到第二热裂解区。