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    • 2. 发明授权
    • METHOD FOR DESORBING MATERIAL
    • VERFAHREN ZUM DESORBIENEN VON材料
    • EP1622721B1
    • 2012-06-06
    • EP04731546.0
    • 2004-05-07
    • Clean Teq Pty Ltd
    • ZONTOV, Nikolai, Dr.
    • B01J47/10B01J49/00C22B3/24C22B3/42B01D15/18
    • C22B3/02B01D2215/021B01J49/10C22B3/24C22B3/42C22B15/0084C22B23/04C22B34/34Y02P10/234Y02P10/236
    • The present invention relates to a method and apparatus for the continuous countercurrent desorption of targeted materials including metals, non-metals and inorganic and/or organic compounds of thereof, wherein the desorption method is divided to the two modes namely: (I) desorption and (II) re-absorption. The desorption of the target material from the loaded resin using the fresh desorbent takes place in mode (I). According to mode (I) loaded resin moves upwardly in a chamber. According to mode (II) impurities are desorbed from resin and targeted material in solution can be re-absorbed. The resin moves downwardly in another chamber during mode (II). Concentrated eluates, which are suitable for the direct economical recovery of chemical elements and/or compounds thereof, can be produced using the present invention. The apparatus of the present invention includes desorption and re-absorption zones that are configured using a 'pipe-in-pipe' construction or a U-shape construction.
    • 本发明涉及一种用于连续逆流解吸目标材料的方法和装置,包括金属,非金属及其无机和/或有机化合物,其中解吸方法分为两种模式,即:(I)解吸和 (二)再吸收。 使用新鲜解吸剂从装载的树脂上解吸目标材料以模式(I)进行。 根据模式(I),加载的树脂在室中向上移动。 根据模式(II),杂质从树脂中解吸,溶液中的目标物质可以被再吸收。 在模式(II)期间,树脂在另一个室中向下移动。 适用于直接经济回收化学元素和/或其化合物的浓缩洗脱液可以使用本发明生产。 本发明的装置包括使用“管内管”结构或U形构造构造的解吸和再吸收区。
    • 5. 发明公开
    • APPARATUS AND PROCESS FOR RECOVERY OF METAL VALUES FROM LEACH OR WASTE SLURRIES
    • 装置和方法计算值金属不受碱或淤泥
    • EP1794332A2
    • 2007-06-13
    • EP05804695.4
    • 2005-09-13
    • FUTUREMET (PTY) LTD
    • WINTLE, Roger, Harvey
    • C22B3/02C22B3/24
    • B01D3/343B01D15/02B01D15/1807B01D2215/021B01J47/10B01J49/10B01J49/60C22B3/02C22B3/24Y02P10/234
    • A process and apparatus for continuously stripping or recovering values from a value bearing material, typically a slurry or solution thereof. The resin and value bearing material are contacted in a counter-current manner (242, 246) in a contact zone (254, 220, 222) to load the resin with values from the value bearing material. The resin is fluidised by the value bearing material in the contact zone. The loaded resin is passed through a first washing zone (256, 224) to displace excess value bearing material. The loaded resin then passes through a stripping zone (258, 228, 226), typically an acid or alkali, to strip the values from the resin and form an eluate, which is treated further to recover the values. The stripped resin is washed in a second washing zone (260, 230), to displace excess stripping agent, and returned to the contact zone.
    • 一种用于连续汽提或从一个值轴承材料,典型地,淤浆或溶液中回收它们的值的方法和装置。 树脂和值轴承材料接触以逆流方式在一个接触区到树脂从值轴承材料值加载。 该树脂是通过在接触区中的值的轴承材料流化。 加载的树脂通过第一洗涤区传递给移位过量值轴承材料。 加载的树脂然后通过汽提区,通常的酸或碱,剥去从树脂和洗脱液的形式的值,所有这一切都被处理并且恢复值。 将汽提的树脂在第二洗涤区洗涤,以置换过量的汽提剂,并返回到接触区。