Upgrading low rank coals as fuel
    1.
    发明授权
    Upgrading low rank coals as fuel 失效
    升级低排放燃料作为燃料

    公开(公告)号:US3754876A

    公开(公告)日:1973-08-28

    申请号:US3754876D

    申请日:1971-12-10

    CPC classification number: C10L9/00 C10G1/00 C10G1/02

    Abstract: A process in which lumps of sub-bituminous or lower rank coal are heated to pyrolysis temperatures of up to about 1,000* F. by contact, preferably countercurrent, with an inert hydrogen-poor hydrocarbonaceous heat transfer fluid, preferably a coal-derived oil, thereby transforming the coal to a char product in lump form of upgraded calorific value, such product, moreover, being less pyrophoric than a char product produced by pyrolysis at the same temperatures in an inert gaseous (nitrogen) atmosphere.

    Coal conversion process
    2.
    发明授权
    Coal conversion process 失效
    煤转化过程

    公开(公告)号:US3841991A

    公开(公告)日:1974-10-15

    申请号:US34839773

    申请日:1973-04-05

    Inventor: COHEN S HOCHMAN J

    CPC classification number: C10B55/10 C10G1/002 C10G1/006 C10G45/44

    Abstract: 1. A PROCESS FOR THE PREPARATION OF LIQUID PRODUCTS FROM COAL WHICH COMPRISES: (A) PREPARING A SLURRY OF FINELY DIVIDED COAL PARTICLES IN A HYDROGENATED AROMATIC HYDROGEN-DONOR SOLVENT HAVING A BOILING POINT IN THE RANGE BETWEEN ABOUT 350*F. AND ABOUT 800*F. IN A SLURRY PREPARATION ZONE; (B) INTRODUCING SAID SLURRY FROM SAID SLURRY PREPARATION ZONE INTO A FLUIDIZED BED COKING UNIT REACTION ZONE; (C) WITHDRAWING OVERHEAD PRODUCTS FROM SAID FLUIDIZED BED COKING UNIT REACTION ZONE AND RECOVERING AN INTERMEDIATE FRACTION BOILING IN THE RANGE BETWEEN ABOUT 350*F. AND ABOUT 800*F. (D) HYDROGENATING SAID INTERMEDIATE FRACTION AND INTRODUCING AT LEAST PART OF THE HYDROGENATED PRODUCT INTO SAID SLURRY PREPARATION ZONE; (E) TRANSFERRING SOLIDS FROM SAID FLUIDIZED BED COKING UNIT TO A BURNER AND BURNING A PORTION OF THE SOLIDS TO PROVIDE HEAT FOR THE PROCESSL AND (F) RECYCLING HOT SOLIDS FROM SAID BURNER TO SAID FLUIDIZED BED COKING UNIT REACTION ZONE.

    Coal liquefaction using high and low boiling solvents
    3.
    发明授权
    Coal liquefaction using high and low boiling solvents 失效
    使用高和低沸点溶剂的煤气化

    公开(公告)号:US3726785A

    公开(公告)日:1973-04-10

    申请号:US3726785D

    申请日:1971-03-03

    CPC classification number: C10G1/006 C10G1/04 C10G1/065 C10G45/00

    Abstract: First and second slurries of a particulate coal are formed with low and high boiling fractions of a coal-derived solvent boiling within the range from 300* to 1,000* F., the cut point of the two fractions being from about 500* F. to about 600* F. The slurries are separately liquefied, producing a higher total cylcohexane conversion of the coal than if the coal had been slurried instead in the total coal-derived solvent and liquefied under like conditions.

    Abstract translation: 颗粒状煤的第一和第二浆料形成沸点在300-1000°F范围内的煤衍生溶剂的低沸点和高沸点馏分,两个馏分的馏分为约500°F至 大约600°F。这些浆液是分开液化的,产生的煤的总环己烷转化率高于如果煤已经在总的煤源溶剂中浆化而在类似条件下液化的话。

    Reactor vessel and up-down mixer
    4.
    发明授权
    Reactor vessel and up-down mixer 失效
    反应釜和升降混合器

    公开(公告)号:US3734469A

    公开(公告)日:1973-05-22

    申请号:US3734469D

    申请日:1970-12-31

    CPC classification number: B01F7/0025

    Abstract: A mixer comprising sets of multi-bladed 45* axial impellers for providing substantially perfect mixing in a cylindrical reactor vessel having an L/D ratio greater than one. A first set of impellers located closest the impeller shaft pump downward while a second set of impellers located outwardly from the first set of impellers pump upward enhancing the flow along the vessel walls.

    Abstract translation: 一种混合器,包括一组多叶片45°轴向叶轮,用于在L / D比大于1的圆柱形反应器容器中提供基本上完美的混合。 从叶轮轴泵最靠近的第一组叶轮,而从第一组叶轮向外位置的第二组叶轮向上泵送,从而增强沿着容器壁的流动。

    Selective hydrotreating of different hydrocarbonaceous feedstocks in temperature regulated hydrotreating zones
    5.
    发明授权
    Selective hydrotreating of different hydrocarbonaceous feedstocks in temperature regulated hydrotreating zones 失效
    在温度调节加氢区中选择性加氢不同的碳氢化合物

    公开(公告)号:US3728249A

    公开(公告)日:1973-04-17

    申请号:US3728249D

    申请日:1971-02-05

    CPC classification number: C10G65/00 B01J8/0453 B01J2208/00283

    Abstract: IN THE SELECTIVE HYDROTREATMENT OF ANY PLURALITY OF DIFFERENTLY CONSTITUTED HYDROCARBONACEOUS FEEDSTOCKS IN A PLURALITY OF HYDROTREATING ZONES, WHEREIN A FIRST SUCH FEEDSTOCK IS HYDROTREATED IN ADMIXTURE WITH AN EXCESS OF HYDROGEN IN A FIRST HYDROTREATING ZONE TO OBTAIN A FIRST ZONE EFFLUENT THAT IS THEN FED TO A SECOND HYDROTREATING ZONE INT WHICH A SECOND HYDROCARBONACEOUS FEEDSTOCK IS INTRODUCED, THE FIRST ZONE EFFLUENT IS COOLED TO A TTEMPERATURE WITHIN A PREDETERMINED RANGE PRIOR TO HYDROTREATMENT IN THE SECOND ZONE, THE SECOND FEEDSTOCK CONSTITUTING A PARTIAL BUT NOT THE SOLE COOLANT FOR THE COOLING. SUPPLEMENTAL COOLING IS PROVIDED DIRECTLY BY CONTACT WIT INJECTED WATER OR INDIRECTLY BY INTERSTAGE COOLING EXTERIORLY OF THE HYDROTREATING ZONES.

    Integrated coal liquefaction and hydrotreating process
    6.
    发明授权
    Integrated coal liquefaction and hydrotreating process 失效
    一体化煤液化和加氢过程

    公开(公告)号:US3726784A

    公开(公告)日:1973-04-10

    申请号:US3726784D

    申请日:1971-02-18

    Inventor: CORREA J HOCHMAN J

    CPC classification number: C10G1/042 C10G1/002 C10G1/065

    Abstract: A hydrotreated liquid product from coal is obtained by a process in which liquefaction and hydrotreating zones are operated at essentially the same moderate pressures (1000-2000 psig). Without prior cooling, all the overhead vapor from the liquefaction reactor is admixed with a portion of a light liquid fraction (700* F.) recovered from the liquefaction liquid product, giving a hydrotreating feed having a temperature within a predetermined range. The remaining portion of the light liquid fraction of the liquefaction product is fed to the hydrotreating zone at quench points in the hydrotreating zone downstream from the point of introduction for the admixture, thus utilizing the heats of reaction in the hydrotreating zone to heat the remaining liquid portions (which provide quench to the hydrotreating zone).

    Abstract translation: 通过液化和加氢处理区以基本相同的中等压力(1000-2000psig)操作的方法获得来自煤的加氢处理的液体产物。 在没有预先冷却的情况下,来自液化反应器的所有顶部蒸气与从液化产物回收的部分轻液体馏分(700°F)混合,得到温度在预定范围内的加氢处理进料。 液化产物的轻液体部分的剩余部分在加氢处理区域的加氢处理区域的加氢处理区域进料到加料装置的引入点下游,从而利用加氢处理区域中的反应热量来加热剩余的液体 部分(为加氢处理区提供淬火)。

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