FLUID INJECTION NOZZLE FOR FLUID BED REACTORS
    81.
    发明申请
    FLUID INJECTION NOZZLE FOR FLUID BED REACTORS 有权
    流体反应器流体注射喷嘴

    公开(公告)号:US20160060541A1

    公开(公告)日:2016-03-03

    申请号:US14812363

    申请日:2015-07-29

    Abstract: The liquid feed nozzle assemblies for a circulating fluid bed reactor comprise (i) a throttle body premixer to combine liquid feed with atomization steam to form a liquid feed/steam mixture comprising gas bubbles in liquid; (ii) a conduit connected to the premixer and to a discharge nozzle to convey a flow of the liquid/steam mixture created by the premixer to the nozzle body; (iii) a discharge nozzle connected to the flow conduit to shear the liquid feed/steam mixture to create liquid feed droplets of reduced size and (iv) a disperser at the outlet of the discharge nozzle to provide a spray jet of liquid feed having an increased surface area relative to a cylindrical jet. The nozzle assembles are particularly useful in fluid coking units using heavy oil feeds such a tar sands bitumen.

    Abstract translation: 用于循环流化床反应器的液体进料喷嘴组件包括(i)节流阀体预混合器,其将液体进料与雾化蒸汽组合以形成液体进料/蒸汽混合物,其包含液体中的气泡; (ii)连接到预混合器和排放喷嘴的导管,以将由预混合器产生的液体/蒸汽混合物的流动传送到喷嘴体; (iii)排放喷嘴,其连接到流动管道以剪切液体进料/蒸汽混合物以产生尺寸减小的液体进料液滴;以及(iv)在排放喷嘴出口处的分散器,以提供具有 相对于圆柱形射流增加表面积。 喷嘴组件在使用重油进料如沥青砂沥青的流体焦化装置中特别有用。

    Process for the production of xylenes and light olefins
    86.
    发明授权
    Process for the production of xylenes and light olefins 有权
    生产二甲苯和轻质烯烃的方法

    公开(公告)号:US09181146B2

    公开(公告)日:2015-11-10

    申请号:US13465721

    申请日:2012-05-07

    Abstract: In a hydrocarbon upgrading process, a hydrocarbon feed is treated in at least one of a steam cracker, catalytic cracker, coker, hydrocracker, and reformer under suitable conditions to produce a first stream comprising olefinic and aromatic hydrocarbons. A second stream composed mainly of C4 to C12 olefinic and aromatic hydrocarbons is recovered from the first stream and at least part of the second stream is contacted with a catalyst in the absence of added hydrogen under reaction conditions including a temperature of about 450° C. to about 70° C. effective to dealkylate, transalkylate, crack and aromatize components of the second stream to produce a third stream having an increased benzene and/or toluene content compared with the second stream and a C3− olefin by-product. The C3− olefin by-product and a fourth stream comprising toluene are then recovered from the third stream.

    Abstract translation: 在烃改质方法中,在合适条件下,在蒸汽裂化器,催化裂化器,焦化器,加氢裂化器和重整器中的至少一种中处理烃进料以产生包含烯烃和芳族烃的第一流。 在第一料流中回收主要由C4至C12烯属和芳烃组成的第二料流,并且在包括约450℃的温度的反应条件下,至少部分第二料流在不加入氢气的情况下与催化剂接触。 至约70℃有效地使第二物流的烷基化,烷基转移,裂解和芳构化成分,以产生与第二物流和C3-烯烃副产物相比具有增加的苯和/或甲苯含量的第三物流。 然后从第三流中回收C3-烯烃副产物和包含甲苯的第四料流。

    In-situ kerogen conversion and recycling
    89.
    发明授权
    In-situ kerogen conversion and recycling 有权
    原位干酪根转化和回收利用

    公开(公告)号:US09133398B2

    公开(公告)日:2015-09-15

    申请号:US13335673

    申请日:2011-12-22

    Abstract: Methods for extracting a kerogen-based product from subsurface (oil) shale formations rely on chemically modifying the shale-bound kerogen using a chemical oxidant so as to render it mobile. The oxidant is provided to a formation fluid in contact with the kerogen in the subsurface shale. An alkaline material is also provided to the formation fluid to mobilize organic acids which are produced during oxidation of the kerogen. A mobile kerogen-based product which includes the organic acids is withdrawn from the subsurface shale formation and further processed to isolate the organic acids contained therein. These organic acids are valuable as hydrocarbon products for creating commercial products and a portion of these organic acids can also be used in the process for extracting the kerogen-based product from the subsurface shale formation.

    Abstract translation: 从地下(油)页岩层中提取含有油母质的产品的方法依靠使用化学氧化剂对页岩结合的干酪根进行化学修饰,以使其移动。 将氧化剂提供给与地下页岩中的干酪根接触的地层流体。 还向地层流体提供碱性物质以移动在干酪根氧化期间产生的有机酸。 包括有机酸的基于移动干酪根的产品从地下页岩地层中排出并进一步处理以分离其中所含的有机酸。 这些有机酸作为用于产生商业产品的烃产品是有价值的,并且这些有机酸的一部分也可用于从地下页岩层中提取干酪根基产物的方法。

    Heat exchanger for cooling reaction gas, including a tubular connection between a cooled tube and an uncooled tube
    90.
    发明授权
    Heat exchanger for cooling reaction gas, including a tubular connection between a cooled tube and an uncooled tube 有权
    用于冷却反应气体的热交换器,包括冷却管和非冷却管之间的管状连接

    公开(公告)号:US09074821B2

    公开(公告)日:2015-07-07

    申请号:US12816578

    申请日:2010-06-16

    Abstract: A heat exchanger for cooling reaction gas. A cooled tube receives hot reaction gas from a hot, uncooled tube. The cooled tube comprises a cooled inner tube and a tubular jacket that extends about the inner tube. A tubular connection is disposed between the uncooled and the cooled tubes, and includes a fork-shaped inlet head via which the inner tube is in communication with the uncooled tube. The inlet head is provided with an outer tubular section and an inner tubular section between which is disposed an intermediate space filled with heat-insulating material. The outer tubular section is connected to the tubular jacket. The inner tubular section is spaced slightly axially from the inner tube and is provided with an edge region that juts outwardly and is spaced slightly axially from the inner tube, this slight axial spacing being equal to or less than a maximum thermal expansion of the inlet head. A U-shaped sealing ring is disposed between facing end faces of the inner tube and the inner tubular section, and is disposed in a recess formed in the end face of the inner tubular section, the recess being disposed radially outwardly of the edge region of the inner tubular section.

    Abstract translation: 用于冷却反应气体的热交换器。 冷却的管接收来自热的未冷却管的热反应气体。 冷却的管包括冷却的内管和围绕内管延伸的管状护套。 管状连接件设置在未冷却和冷却的管之间,并且包括叉形入口头,内管与未冷却的管连通。 入口头设置有外部管状部分和内部管状部分,在其间设有填充有隔热材料的中间空间。 外管状部分连接到管状护套。 内管状部分与内管略微轴向间隔开并且设置有向外突出并与内管稍微轴向间隔开的边缘区域,该轻微轴向间距等于或小于入口头部的最大热膨胀 。 U形密封环设置在内管和内管状部分的相对端面之间,并且设置在形成在内管状部分的端面中的凹部中,凹部设置在径向外侧的边缘区域 内管状部分。

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