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    • 1. 发明授权
    • Enhancing filtration yields in tangential flow filtration
    • 提高切向流过滤中的过滤产量
    • US06350382B1
    • 2002-02-26
    • US09603148
    • 2000-06-23
    • Karl G. Schick
    • Karl G. Schick
    • B01D6112
    • B01D61/145B01D61/16B01D61/18B01D61/22B01D2311/04B01D2313/58B01D2315/16B01D2311/14B01D2311/16
    • A system is provided for proceeding with filtration of liquids in a manner having enhanced control characteristics. Yields are enhanced. The system and method can be used to maintain a substantially constant trans-membrane pressure. When desired, that constant trans-membrane pressure is especially well-suited to yield enhancement for the particular liquid being filtered, concentrated or collected, while minimizing a risk of damage to or loss of valuable components. Additionally, a constant feed rate or pump output can be maintained. Approaches also are described for determining optimal filtration conditions, including trans-membrane pressure and feed rate. Also described is a system and method for determining pressures in a pulsating system with enhanced accuracy by using a peak pressure mode.
    • 提供了一种以具有增强的控制特性的方式进行液体过滤的系统。 产量提高。 该系统和方法可用于维持基本恒定的跨膜压力。 当需要时,恒定的跨膜压力特别适合于对被过滤,浓缩或收集的特定液体产生增强,同时最小化损坏或损失有价值的组分的风险。 另外,可以保持恒定的进给速率或泵输出。 还描述了用于确定最佳过滤条件的方法,包括跨膜压力和进料速率。 还描述了一种通过使用峰值压力模式来提高精度的脉动系统中的压力的​​系统和方法。
    • 4. 发明授权
    • Desalination method and apparatus utilizing nanofiltration and reverse osmosis membranes
    • 采用纳滤和反渗透膜的脱盐方法和设备
    • US06190556B1
    • 2001-02-20
    • US09170142
    • 1998-10-12
    • Robert A. Uhlinger
    • Robert A. Uhlinger
    • B01D6112
    • C02F1/442B01D61/022B01D61/12B01D63/12B01D65/02B01D2321/02B01D2321/10C02F1/441Y02A20/131
    • Apparatus and methods for producing potable water from an aqueous feed such as seawater utilizing a pressure vessel designed for operation in the range of about 250 psig to about 350 psig having reverse osmosis (RO) separation elements disposed upstream of at least one nanofiltrate separation element. The supply of seawater at such pressure creates no permeate flow through the RO membranes, so the seawater flushes the feed side of the RO elements on its way to the NF element where very substantial permeate flux occurs, producing a NF permeate substantially depleted in divalent ions and optionally moderately depleted in monovalent ions. The NF permeate is collected in a holding tank having liquid level switches, and when a desired level is reached, a control system causes the pump to draw suction from the holding tank while shutting off feed from the seawater source. When the NF permeate is supplied to the feed side of the RO elements, its osmotic pressure is such that substantial RO permeation now occurs creating a stream of good quality potable water. During both stages of operation, energy is conserved by routing the concentrate stream leaving the pressure vessel through an energy recovery device that boosts the pressure of the liquid being discharged from the positive displacement pump.
    • 使用设计用于在约250psig至约350psig范围内操作的压力容器的含水进料如海水生产饮用水的装置和方法,其具有设置在至少一个纳滤滤器分离元件上游的反渗透(RO)分离元件。 在这种压力下的海水供应不会产生通过RO膜的渗透物流,因此海水在其途中被RO元素的进入侧冲击到NF元件,其中产生非常实质的渗透通量,产生基本上耗尽二价离子的NF渗透物 并且任选地适度地耗尽一价离子。 NF渗透物​​被收集在具有液位开关的储存罐中,并且当达到期望水平时,控制系统使得泵在从海水源关闭的同时从储存罐抽吸。 当NF渗透物​​被供应到RO元件的进料侧时,其渗透压使得现在产生大量的RO渗透,产生优质的饮用水流。 在两个操作阶段,通过使离开压力容器的浓缩物料流通过能量回收装置来节省能量,该能量回收装置可以增加从正排量泵排出的液体的压力。