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268 条记录 (耗时 0.022 秒)

    Process for producing low-sulfur liquid and solid fuels from coal
    1.
    发明授权
    Process for producing low-sulfur liquid and solid fuels from coal 失效
    从煤生产低硫液体和固体燃料的方法

    公开(公告)号：US4077866A

    公开(公告)日：1978-03-07

    申请号：US728660

    申请日：1976-10-01

    申请人： Hartley Owen ,  Paul B. Venuto ,  Tsoung-Yuan Yan

    发明人： Hartley Owen ,  Paul B. Venuto ,  Tsoung-Yuan Yan

    IPC分类号： C10G1/00 ,  C10G1/04

    CPC分类号： C10G1/04 ,  C10G1/00

    摘要： An improved process for the conversion of coal to low-sulfur products is disclosed wherein coal is heated with a liquid phase coal dissolution solvent, which is preferably a heavy aromatic petroleum solvent, in the presence of a solid, sulfur scavenger such as iron. Improved separation of inorganic solids, including both coal-derived and solvent-derived sulfur combined with the scavenger, is obtained by using a light cycle-oil modified slurry settler operation followed by separation. Vacuum distillation of the filtrate provides a low-sulfur solid which is used directly as fuel or coked to form low-sulfur distillates and coke. The scavenger is separated from other inorganics, regenerated, and recycled. Moderate amounts of fuel gas are also formed.

    摘要翻译： 公开了一种将煤转化为低硫产物的改进方法，其中在固体硫清除剂如铁的存在下，用液相煤溶解溶剂（其优选为重芳族石油溶剂）加热煤。 通过使用光循环 - 油改性的淤浆沉降器操作，然后分离，获得包括煤和衍生的硫与清除剂组合的无机固体的分离。 滤液的真空蒸馏提供了低硫固体，其直接用作燃料或焦化以形成低硫馏出物和焦炭。 清道夫与其他无机物分离，再生和再循环。 还形成了适量的燃料气体。

    Catalytic conversion of high metals feed stocks
    3.
    发明授权
    Catalytic conversion of high metals feed stocks 失效
    高金属饲料的催化转化

    公开(公告)号：US4002557A

    公开(公告)日：1977-01-11

    申请号：US556251

    申请日：1975-03-07

    申请人： Hartley Owen ,  Paul B. Venuto

    发明人： Hartley Owen ,  Paul B. Venuto

    IPC分类号： C10G11/05 ,  C10G49/20 ,  C10G11/04 ,  B01J8/24

    CPC分类号： C10G49/20 ,  C10G2400/30

    摘要： The conversion of high metals containing feed stock is accomplished in the presence of a low molecular weight carbon-hydrogen fragment contributing material and an acid function crystalline zeolite catalyst to produce gasoline of high quality and yields superior to that obtained heretofore.

    摘要翻译： 含有高含金属原料的转化是在低分子量碳 - 氢碎片贡献材料和酸性结晶沸石催化剂的存在下实现的，以生产高质量的产物，产率优于迄今为止。

    Combination process for solvent deasphalting and catalytic upgrading of heavy petroleum stocks
    6.
    发明授权
    Combination process for solvent deasphalting and catalytic upgrading of heavy petroleum stocks 失效
    重油石油溶剂脱沥青和催化改质的组合工艺

    公开(公告)号：US3951781A

    公开(公告)日：1976-04-20

    申请号：US525436

    申请日：1974-11-20

    申请人： Hartley Owen ,  Paul B. Venuto

    发明人： Hartley Owen ,  Paul B. Venuto

    IPC分类号： C10G55/06 ,  C10G13/18

    CPC分类号： C10G55/06

    摘要： A raffinate product of residual oil solvent extraction is upgraded in a fluid zeolite catalyst cracking operation in the presence of one or more low molecular weight carbon-hydrogen fragment contributors. Gas oil products of atmospheric and vacuum distillation may be simultaneously converted by admixture with the raffinate charge. In addition the process is enhanced by the addition of straight run naphtha product of distillation with the raffinate charge.

    摘要翻译： 在一种或多种低分子量碳氢化合物片段的贡献者的存在下，在流体沸石催化剂裂解操作中，提高了剩余油溶剂萃取的萃余物。 大气和真空蒸馏的瓦斯油产品可以与萃余液装料混合同时转化。 此外，通过加入具有萃余液装料的蒸馏的直馏石脑油产物来增强该方法。

    Processing heavy reformate feedstock
    9.
    发明授权
    Processing heavy reformate feedstock 失效
    加工重型改性饲料

    公开(公告)号：US4066531A

    公开(公告)日：1978-01-03

    申请号：US616964

    申请日：1975-09-26

    申请人： Hartley Owen ,  Paul B. Venuto ,  Edward J. Rosinski

    发明人： Hartley Owen ,  Paul B. Venuto ,  Edward J. Rosinski

    IPC分类号： C10G11/18 ,  C10G11/02

    CPC分类号： C10G11/18 ,  C10G2400/20 ,  C10G2400/30

    摘要： Liquid product rich in benzene, toluene and xylene and having a substantially lower mid-boiling point than heavy reformate feedstock or similar feedstock, such as, for example, from pyrolysis gasoline, of a class having an initial boiling point between about 230.degree. F and about 250.degree. F and an end point between about 350.degree. F and about 430.degree. F, and gaseous product rich in light olefins and isoparaffins which is good alkylation plant feed are produced by contacting said heavy reformate feedstock or said similar feedstock with a porous acid-active zeolite catalyst having a fluid activity index of at least about 18 in a fluidized catalyst system absent added hydrogen at a temperature of from about 800.degree. F to about 1200.degree. F, a catalyst/oil (i.e. heavy reformate or similar feedstock) weight ratio of from about 0.5 to about 40 and a catalyst residence time of from about 0.1 second to about 20 seconds.

    High selectivity transalkylation
    10.
    发明授权
    High selectivity transalkylation 失效
    高选择性烷基转移

    公开(公告)号：US4046827A

    公开(公告)日：1977-09-06

    申请号：US616966

    申请日：1975-09-26

    申请人： Hartley Owen ,  Paul B. Venuto ,  Edward T. Habib, Jr.

    发明人： Hartley Owen ,  Paul B. Venuto ,  Edward T. Habib, Jr.

    IPC分类号： C07C6/12 ,  C07C3/62

    CPC分类号： C07C6/126 ,  Y02P20/582

    摘要： A process is provided for high selectivity transalkylation of alkylaromatic hydrocarbon compounds of from 7 to 10 carbon atoms which comprises contacting said alkylaromatic hydrocarbon compounds with a transalkylating agent in the presence of a porous acid-active zeolite catalyst having a fluid activity index of at least about 18 in a fluidized catalyst system absent added hydrogen at a temperature of from about 300.degree. F to about 1200.degree. F, pressure of from about 0 psig to about 200 psig and a catalyst residence time of from about 0.01 second to about 300 seconds.

    摘要翻译： 提供了一种用于7至10个碳原子的烷基芳族烃化合物的高选择性烷基转移的方法，其包括在多孔酸活性沸石催化剂存在下使所述烷基芳族烃化合物与烷基转移剂接触，所述多孔酸活性沸石催化剂的流体活性指数为至少约 18在流化催化剂体系中没有加入氢气，温度为约300°F至约1200°F，压力为约0psig至约200psig，催化剂停留时间为约0.01秒至约300秒。