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    • 4. 发明申请
    • Passive Injection of a Chemical Solution into a Process Stream
    • 将化学溶液无源注入工艺流
    • US20140360606A1
    • 2014-12-11
    • US14298191
    • 2014-06-06
    • Robert James LawRobert L. CowanThomas P. DiazSamson Hettiarachchi
    • Robert James LawRobert L. CowanThomas P. DiazSamson Hettiarachchi
    • B01F13/02
    • B01F15/0412B01F5/0495F16K19/003G05D11/006Y10T137/2218
    • A system and method of injecting a chemical into a high pressure process stream without pumps or other active components. The system utilizes the differential pressure created by resistive losses of downstream components within a high pressure process stream. A bypass side stream is taken from an upstream pressure location and returned to the downstream side of the resistive inline process component. The chemical solution vessel is pressurized by the higher side of the pressure differential. The solution then passes through a flow controlling capillary tube exiting on the lower pressure differential side into the bypass stream. The high flow rate chemically diluted bypass stream then returns to the process stream at the lower differential process stream tie-in. The chemical solution is isolated from the process water pressuring the vessel by a movable separating device preventing mixing of the two fluids. The vessel can also be pressurized by gas.
    • 将化学品注入高压工艺流而不使用泵或其他活性组分的系统和方法。 该系统利用由高压工艺流中的下游部件的电阻损耗产生的压差。 旁路侧流从上游压力位置获取,并返回到电阻内联过程组件的下游侧。 化学溶液容器由压力差的较高侧加压。 然后溶液通过从低压差侧出来的流动控制毛细管进入旁路流。 然后,高流量化学稀释的旁路流在较低的差分过程流束缚下返回到过程流。 化学溶液是通过可移动的分离装置从加工水中分离出来的,以防止两种流体的混合。 容器也可以用气体加压。
    • 7. 发明授权
    • Passive injection of a chemical solution into a process stream
    • 将化学溶液无源注入工艺流
    • US09533270B2
    • 2017-01-03
    • US14298191
    • 2014-06-06
    • Robert James LawRobert L CowanThomas P DiazSamson Hettiarachchi
    • Robert James LawRobert L CowanThomas P DiazSamson Hettiarachchi
    • B01F15/04B01F5/04G05D11/00F16K11/00
    • B01F15/0412B01F5/0495F16K19/003G05D11/006Y10T137/2218
    • A system and method of injecting a chemical into a high pressure process stream without pumps or other active components. The system utilizes the differential pressure created by resistive losses of downstream components within a high pressure process stream. A bypass side stream is taken from an upstream pressure location and returned to the downstream side of the resistive inline process component. The chemical solution vessel is pressurized by the higher side of the pressure differential. The solution then passes through a flow controlling capillary tube exiting on the lower pressure differential side into the bypass stream. The high flow rate chemically diluted bypass stream then returns to the process stream at the lower differential process stream tie-in. The chemical solution is isolated from the process water pressuring the vessel by a movable separating device preventing mixing of the two fluids. The vessel can also be pressurized by gas.
    • 将化学品注入高压工艺流而不使用泵或其他活性组分的系统和方法。 该系统利用由高压工艺流中的下游部件的电阻损耗产生的压差。 旁路侧流从上游压力位置获取,并返回到电阻内联过程组件的下游侧。 化学溶液容器由压力差的较高侧加压。 然后溶液通过从低压差侧出来的流动控制毛细管进入旁路流。 然后,高流量化学稀释的旁路流在较低的差分过程流束缚下返回到过程流。 化学溶液是通过可移动的分离装置从加工水中分离出来的,以防止两种流体的混合。 容器也可以用气体加压。