Spinning Fluids Reactor
    1.
    发明申请
    Spinning Fluids Reactor 有权
    纺纱液反应堆

    公开(公告)号:US20110223091A1

    公开(公告)日:2011-09-15

    申请号:US13056720

    申请日:2009-07-31

    摘要: A spinning fluids reactor, includes a reactor body (24) having a circular cross-section and a fluid contactor screen (26) within the reactor body (24). The fluid contactor screen (26) having a plurality of apertures and a circular cross-section concentric with the reactor body (24) for a length thus forming an inner volume (28) bound by the fluid contactor screen (26) and an outer volume (30) bound by the reactor body (24) and the fluid contactor screen (26). A primary inlet (20) can be operatively connected to the reactor body (24) and can be configured to produce flow-through first spinning flow of a first fluid within the inner volume (28). A secondary inlet (22) can similarly be operatively connected to the reactor body (24) and can be configured to produce a second flow of a second fluid within the outer volume (30) which is optionally spinning.

    摘要翻译: 纺丝流体反应器包括具有圆形横截面的反应​​器主体(24)和反应器主体(24)内的流体接触器筛(26)。 流体接触器屏幕(26)具有多个孔和与反应器主体(24)同心的圆形横截面,从而形成由流体接触器筛网(26)结合的内部容积(28)的长度,以及外部体积 (30)与反应器主体(24)和流体接触器筛(26)结合。 主入口(20)可以可操作地连接到反应器主体(24)并且可以被构造成在内部容积(28)内产生第一流体的流过第一纺丝流。 次级入口(22)可以类似地可操作地连接到反应器主体(24)并且可以被配置为在外部容积(30)内产生可选地旋转的第二流体的第二流。

    Spinning fluids reactor
    2.
    发明授权
    Spinning fluids reactor 有权
    旋转流体反应器

    公开(公告)号:US08313716B2

    公开(公告)日:2012-11-20

    申请号:US13056720

    申请日:2009-07-31

    摘要: A spinning fluids reactor, includes a reactor body (24) having a circular cross-section and a fluid contactor screen (26) within the reactor body (24). The fluid contactor screen (26) having a plurality of apertures and a circular cross-section concentric with the reactor body (24) for a length thus forming an inner volume (28) bound by the fluid contactor screen (26) and an outer volume (30) bound by the reactor body (24) and the fluid contactor screen (26). A primary inlet (20) can be operatively connected to the reactor body (24) and can be configured to produce flow-through first spinning flow of a first fluid within the inner volume (28). A secondary inlet (22) can similarly be operatively connected to the reactor body (24) and can be configured to produce a second flow of a second fluid within the outer volume (30) which is optionally spinning.

    摘要翻译: 纺丝流体反应器包括具有圆形横截面的反应​​器主体(24)和反应器主体(24)内的流体接触器筛(26)。 流体接触器筛(26)具有多个孔,并且具有与反应器主体(24)同心的圆形横截面,从而形成由流体接触器筛网(26)结合的内部容积(28)的长度,以及外部容积 (30)与反应器主体(24)和流体接触器筛(26)结合。 主入口(20)可以可操作地连接到反应器主体(24)并且可以被构造成在内部容积(28)内产生第一流体的流过第一纺丝流。 次级入口(22)可以类似地可操作地连接到反应器主体(24)并且可以被配置为在外部容积(30)内产生可选地旋转的第二流体的第二流。

    Bitumen recovery from tar sands
    4.
    发明授权
    Bitumen recovery from tar sands 失效
    沥青从沥青砂中回收

    公开(公告)号:US4470899A

    公开(公告)日:1984-09-11

    申请号:US466282

    申请日:1983-02-14

    IPC分类号: C10G1/04

    CPC分类号: C10G1/047

    摘要: A process for recovering bitumen from tar sands wherein the tar sands are pretreated with a diluent, such as kerosene in the preferred embodiment, to lower the viscosity of the bitumen such that it is in the range of about 5 to about 20 poise at the digestion temperature. The tar sands are then digested at a temperature in the range of about 45.degree. C. to about 60.degree. C. and at a pH of about 7.8 to about 8.6. The tar sands are then transferred to a flotation cell where the bitumen-rich concentrate is separated from the sand.

    摘要翻译: 从焦油砂中回收沥青的方法,其中焦油砂在优选实施方案中用稀释剂例如煤油进行预处理,以降低沥青的粘度,使其在消化时在约5至约20泊的范围内 温度。 沥青砂然后在约45℃至约60℃的温度和约7.8至约8.6的pH下消化。 然后将焦油砂转移到浮选槽中,其中富含沥青的浓缩物与砂分离。

    Emulsion based oil simulant and associated methods
    6.
    发明授权
    Emulsion based oil simulant and associated methods 有权
    基于乳液的油模拟和相关方法

    公开(公告)号:US07691908B2

    公开(公告)日:2010-04-06

    申请号:US11198864

    申请日:2005-08-04

    IPC分类号: B01F3/08

    摘要: A crude oil simulant is disclosed that is an emulsion of an organic continuous phase, an aqueous dispersed phase, and an emulsifier. To enhance the biodegradability rate of the simulant various strains of bacteria can be added to the aqueous phase. Nutrients can be added to the aqueous phase to increase activity of the bacteria. The components of the simulant of the invention can be mixed under high shear conditions such as 1,000-12,000 reciprocal minutes. The emulsion based oil simulants can be prepared on-site and can be readily tailored to simulant a wide variety of crude oils under various conditions.

    摘要翻译: 公开了一种原油模拟物,其是有机连续相,水性分散相和乳化剂的乳液。 为了提高模拟物的生物降解率,可以将各种细菌菌株加入到水相中。 可以向水相中加入营养物以增加细菌的活性。 本发明的模拟物的组分可以在高剪切条件下混合,例如1,000-12,000相互分钟。 基于乳液的油模拟物可以现场制备,并且可以容易地定制成在各种条件下模拟各种各样的原油。

    Emulsion based oil simulant and associated methods
    7.
    发明申请
    Emulsion based oil simulant and associated methods 有权
    基于乳液的油模拟和相关方法

    公开(公告)号:US20060030628A1

    公开(公告)日:2006-02-09

    申请号:US11198864

    申请日:2005-08-04

    IPC分类号: B01F3/08 B01F17/00

    摘要: A crude oil simulant is disclosed that is an emulsion of an organic continuous phase, an aqueous dispersed phase, and an emulsifier. To enhance the biodegradability rate of the simulant various strains of bacteria can be added to the aqueous phase. Nutrients can be added to the aqueous phase to increase activity of the bacteria. The components of the simulant of the invention can be mixed under high shear conditions such as 1,000-12,000 reciprocal minutes. The emulsion based oil simulants can be prepared on-site and can be readily tailored to simulant a wide variety of crude oils under various conditions.

    摘要翻译: 公开了一种原油模拟物,其是有机连续相,水性分散相和乳化剂的乳液。 为了提高模拟物的生物降解率,可以将各种细菌菌株加入到水相中。 可以向水相中加入营养物以增加细菌的活性。 本发明的模拟物的组分可以在高剪切条件下混合,例如1,000-12,000相互分钟。 基于乳液的油模拟物可以现场制备,并且可以容易地定制成在各种条件下模拟各种各样的原油。