会员体验
专利管家(专利管理)
工作空间(专利管理)
风险监控(情报监控)
数据分析(专利分析)
侵权分析(诉讼无效)
联系我们
交流群
官方交流:
QQ群: 891211   
微信请扫码    >>>
现在联系顾问~
热词
    • 3. 发明授权
    • Apparatus for separation and processing of materials
    • US09370753B2
    • 2016-06-21
    • US14346672
    • 2012-09-21
    • CYDAF TECHNOLOGIES LIMITED
    • Richard George Paxton
    • B01D45/16B01D47/00B01F3/04B04C5/10B04C5/06B04C5/103B04C5/13B04C5/14B04C5/28B01D21/24B01D21/26B03D1/14B01D17/02B01D19/00
    • B01F3/0446B01D17/0217B01D19/0057B01D21/2411B01D21/267B01D45/16B01D47/00B03D1/1418B04C5/06B04C5/10B04C5/103B04C5/13B04C5/14B04C5/28
    • This invention relates to a tubular cyclonic separation device the style of which was presented in PCT/ZA2003/000160 and which enables all of the inlet and outlet connections to be completely contained within a tubular profile, the diameter of which is that of the body of the cyclonic section. This disclosure adds further novel and inventive developments to the cyclonic device which enable it to be used as a separating device for systems involving all three phases (gas, liquid and solid) and where two, three or more different product streams may be separated, all within the same cylindrical profile. These further inventive developments also relate to the use of externally supplied gas and/or additional liquid phases which are injected through the walls of the cyclonic body using specifically located slots and/or holes in combination with specifically located stepped edges. These further novel and inventive developments enable the concepts of froth floatation (FF) and Dispersed Air Floatation (DAF) to be exploited within an enhanced gravitational field together with the options for washing the separated froth and/or the separated heavier fractions, all within the same cyclonic unit. As part of the novel and inventive introduction of the stepped edges, means are provided whereby gas bubbles smaller than 30 microns can be created on a large scale and with a reduced energy input relative to typical conventional equipment. Also, the size of the gas bubbles may be controlled together with the intensity of any particle on particle interactions that may be created. This latter has many potential applications within FF and/or DAF processes, including applications within oil and tar separation from solid surfaces and within many ore preparation and ore leaching processes. The tubular profile enables processing and separation to be achieved “within the pipe line” or for very closely packed arrangements to be assembled within carrier vessels.
    • 7. 发明授权
    • Method for separating suspended solids from a waste fluid
    • 从废液中分离悬浮固体的方法
    • US08404121B2
    • 2013-03-26
    • US12462878
    • 2009-08-11
    • Joel BiasBrian Ross
    • Joel BiasBrian Ross
    • C02F1/24
    • B01D35/00B03D1/028B03D1/1418B03D1/1431B03D1/1487C02F1/24
    • The disclosure relates to a separation process. An aerated inlet mixture of fluid and solids is fed to a flotation separation vessel and is separated into an upper float layer and a lower clarified layer. The upper float layer is withdrawn from the vessel when the height of the upper float layer exceeds the height of an overflow conduit and forms a concentrated solids effluent. The lower clarified layer is withdrawn from the separation vessel as a clarified fluid effluent. The separation process is performed continuously using a control process that maintains a relatively stable distribution between the lower clarified layer and the upper float layer. The control process is a closed loop process that monitors the instantaneous height of the vessel contents and computes an error function based on the instantaneous height and a set-point height. The error function is used to periodically adjust the outlet flowrate of the clarified fluid effluent. The resulting process has improved stability (e.g., being continuously operable without interruption and/or operable for extended periods between intermittent cleaning processes) and provides a concentrated solids effluent with solids concentrations higher than those previously attainable in similar separation processes.
    • 本公开涉及分离过程。 将流体和固体的充气入口混合物进料到浮选分离容器中,并分离成上浮体层和下澄清层。 当上浮体层的高度超过溢流导管的高度并形成浓缩固体流出物时,将上浮体层从容器中取出。 下层澄清层作为澄清的流体流出物从分离容器中取出。 使用在下澄清层和上浮体层之间保持相对稳定的分布的控制过程连续进行分离过程。 控制过程是闭环过程,监视容器内容物的瞬时高度,并根据瞬时高度和设定点高度计算误差函数。 误差函数用于周期性地调节澄清流体流出物的出口流量。 所得到的方法具有改善的稳定性(例如,连续操作而不间断地和/或可在间歇清洗过程之间延长的时间间隔地操作),并且提供固体浓度高于在类似分离过程中可获得的固体浓度的浓缩固体流出物。
    • 9. 发明授权
    • Hydrocyclone and associated methods
    • 水力旋流器及相关方法
    • US07708146B2
    • 2010-05-04
    • US11940099
    • 2007-11-14
    • Jan Kruyer
    • Jan Kruyer
    • B03B5/28B01D21/26
    • B03B5/34B03D1/1418B03D1/1456B03D1/1487B03D1/247B04C3/06B04C5/04B04C9/00B04C2009/008C10G1/045
    • A hydrocyclone can be used for separating components of a fluid. The hydrocyclone can include a substantially open cylindrical vessel and a helical confined path connected upstream of the cylindrical vessel. The open vessel can include an open vessel inlet configured to introduce a fluid tangentially into the open vessel. The helical confined path can be connected to the open vessel at the open vessel inlet. One or more wash inlets can be used to introduce a wash fluid into the helical confined path and/or the open vessel. An overflow outlet and underflow outlet can be operatively attached to the open vessel for removal of the separated fluid components. Although a number of fluids can be effectively treated, de-sanding of bitumen slurries from oil sands can be readily achieved.
    • 水力旋流器可用于分离流体的组分。 水力旋流器可以包括基本上开放的圆柱形容器和连接在圆柱形容器上游的螺旋限制通道。 开放容器可以包括开放容器入口,其被构造成将流体切向地引入到开放容器中。 螺旋限制路径可以在开放的容器入口连接到开放的容器。 可以使用一个或多个洗涤入口将洗涤流体引入螺旋限制路径和/或敞开的容器中。 溢流出口和下溢出口可以可操作地连接到开放容器上,以去除分离的流体组分。 尽管可以有效地处理许多流体,但是可以容易地实现从油砂中去除沥青浆料。