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    • 4. 发明申请
    • PROCESS FOR SULPHIDE CONCENTRATION
    • 硫化氢浓度的方法
    • WO2002083316A1
    • 2002-10-24
    • PCT/AU2002/000471
    • 2002-04-11
    • WMC RESOURCES LTDSENIOR, Geoffrey, DavidTHOMAS, ScottJUDD, Brian
    • SENIOR, Geoffrey, DavidTHOMAS, ScottJUDD, Brian
    • B03D1/08
    • B03B7/00B03B9/00B03D1/08C22B1/00C22B23/005
    • The present invention relates to a gravity/flotation circuit where a mineral stream, such as a flotation rougher or cleaner concentrate, undergoes a two stage size separation wherein: i) the screen of the first stage provides a coarse stream of particles greater than 110 microns and a fines stream of particles less than 110 microns; and ii) the fines stream of less than 110 microns is subjected to the second stage separation whereupon a cyclone provides an ultrafine/slimes stream of p80 less than about 25 microns and a middlings stream of p80 greater than around 25 microns. The middlings stream is subjected to flotation to recover nickel sulphide which is sent to final concentrate, and reject or depress magnesia which undergoes gravity separation to concentrate the MgO. It has been discovered that a large proportion of the MgO minerals in the concentrate are contained in the 30 to 100 micron size fraction and that they are well liberated making physical separation possible. Furthermore, the nickel sulphide minerals and magnesia minerals have a significantly different specific gravity which can be exploited using gravity separation equipment to achieve magnesia rejection.
    • 本发明涉及一种重力/浮选回路,其中矿物流,例如浮选粗糙剂或清洁剂浓缩物,经历两阶段大小分离,其中:i)第一阶段的筛网提供大于110微米的粗颗粒流 和小于110微米的细粉粒料流; 和ii)小于110微米的细小流经受第二阶段分离,于是旋风分离器提供p80小于约25微米的超细/流浆,p80的中间流大于约25微米。 将中草料进行浮选以回收被送到最终浓缩物的硫化镍,并且排除或抑制进行重力分离的氧化镁以浓缩MgO。 已经发现,浓缩物中的大部分MgO矿物质包含在30至100微米尺寸级分中,并且它们被很好地释放,使物理分离成为可能。 此外,硫化镍矿物和氧化镁矿物具有显着不同的比重,可以使用重力分离设备来实现氧化镁排除。
    • 6. 发明申请
    • PROCESSING ASPHALTENE-CONTAINING TAILINGS
    • 加工含ASPHALTENE的尾矿
    • WO2007102819A1
    • 2007-09-13
    • PCT/US2006/008263
    • 2006-03-07
    • WESTERN OIL SANDS USA, INC.DUYVESTEYN, Willem, P., C.KIFT, JulianMORLEY, Raymond. L.
    • DUYVESTEYN, Willem, P., C.KIFT, JulianMORLEY, Raymond. L.
    • B03D1/14C01G1/04C01G1/00
    • C01G49/00B03B9/02B03D1/06B03D1/08B03D3/06C01G1/00C01G1/02C01G23/047C01G25/02C10G1/045C10G1/047C22B34/1204Y02P70/34
    • Embodiments of a method and a system for recovering energy, materials or both from asphaltene-containing tailings are disclosed. The asphaltene-containing tailings can be generated, for example, from a process for recovering hydrocarbons from oil sand. Embodiments of the method can include a flotation separation and a hydrophobic agglomeration separation. Flotation can be used to separate the asphaltene-containing tailings into an asphaltene-rich froth and an asphaltene-depleted aqueous phase. The asphaltene-rich froth, or an asphaltene-rich slurry formed from the asphaltene-rich froth, then can be separated into a heavy mineral concentrate and a light tailings. Hydrophobic agglomeration can be used to recover an asphaltene concentrate from the light tailings. Another flotation separation can be included to remove sulfur-containing minerals from the heavy mineral concentrate. Oxygen-containing minerals also can be recovered from the heavy mineral concentrate. Water removed by the various separation steps can be recycled and its heat energy recovered.
    • 公开了用于从含沥青质的尾矿中回收能量,材料或二者的方法和系统的实施例。 含沥青烯的尾矿可以例如从用于从油砂中回收烃的方法产生。 该方法的实施方案可以包括浮选分离和疏水性聚集分离。 浮选可用于将含沥青质的尾矿分离成富含沥青质的泡沫和不含沥青质的水相。 富含沥青质的泡沫或富含沥青质的泡沫形成的富含沥青质的浆料然后可以分离成重的矿物浓缩物和轻质尾矿。 疏水聚集可用于从轻尾矿中回收沥青质浓缩物。 可以包括另一种浮选分离以从重矿物质浓缩物中除去含硫矿物。 含氧矿物也可从重矿物精矿中回收。 通过各种分离步骤除去的水可以回收并回收其热能。
    • 8. 发明申请
    • SYSTEM, METHOD AND APPARATUS FOR FROTH FLOTATION
    • 系统,方法和装置的快速浮选
    • WO2017035580A1
    • 2017-03-09
    • PCT/AU2016/050806
    • 2016-08-29
    • HUNTER PROCESS TECHNOLOGIES PTY LIMITED
    • JAMESON, Graeme John
    • B03D1/24B03D1/08
    • B03D1/247B03D1/028B03D1/08B03D1/1475B03D2203/08
    • A separation system is disclosed for separating selected particles from a mixture of particles in a fluid. The system includes a froth flotation vessel (10) into which in use the mixture of particles and fluid are subjected to an upward flow of an introduced gas to form a froth layer (13) which rises above an interface (14) formed between the froth layer (13) and the mixture of particles and fluid (12), such that a quantity of the selected particles is conveyed out of the vessel (10) by the froth layer (13) to become a first product of the system. The vessel (10) also has a first outlet (29) arranged in use for receiving a flow of some of the mixture of particles and fluid from the vessel (10), an entry to the first outlet (29) being located in a region proximate to, but below, the interface (14). The vessel also has a second outlet (20) arranged in use for receiving a flow of some of the mixture of particles and fluid from a region of the vessel (10) which is located below the first outlet (29). In use the first outlet (29) receives a quantity of the selected particles which were not conveyed out of the vessel by the froth layer (13), and the second outlet (20) receives a quantity of the selected particles in a first by-product of the system. The first by-product comprises a relatively higher percentage of solids compared to the flow of particles and fluid in the first outlet (29). The flow of the mixture of particles and fluid from the(vessel (10) via the first outlet (29) passes to a classification device (31, 76) which separates the flow into two or more fractions on the basis of their size or density or a combination of the two.
    • 公开了用于从流体中的颗粒混合物中分离所选择的颗粒的分离系统。 该系统包括泡沫浮选容器(10),在使用中,颗粒和流体的混合物经受引入气体的向上流动以形成泡沫层(13),其在形成于泡沫之间的界面(14)上方上升 层(13)和颗粒和流体(12)的混合物,使得所选择的颗粒的量被泡沫层(13)输送出容器(10)以成为系统的第一产品。 容器(10)还具有第一出口(29),第一出口(29)布置成用于接收来自容器(10)的一些颗粒和流体混合物的流动,第一出口(29)的入口位于区域 接近但在下面的界面(14)。 容器还具有第二出口(20),第二出口(20)布置成用于接收位于第一出口(29)下方的容器(10)的区域中的一些颗粒和流体混合物的流动。 在使用中,第一出口(29)接收一定数量的未被泡沫层(13)输送出容器的选定颗粒,第二出口(20)以第一副产物 系统的产品。 与第一出口(29)中的颗粒和流体的流动相比,第一副产物包含相对较高百分比的固体。 来自(容器10)经由第一出口(29)的颗粒和流体的混合物的流动传递到分级装置(31,76),分级装置基于其尺寸或密度将流分离成两个或更多个部分 或两者的组合。
    • 10. 发明申请
    • MOLYBDENUM PROCESS OF IDENTIFYING THE COLLECTIVE CONCENTRATE CU-MO
    • 识别收集浓度的莫尔方法
    • WO2010019063A1
    • 2010-02-18
    • PCT/RS2008/000036
    • 2008-11-25
    • DRAGOSAN, LjubomirGRUJIC, MiloradVRHOVSEK, MiroslavBARBULOVIC, Igor
    • DRAGOSAN, LjubomirGRUJIC, MiloradVRHOVSEK, MiroslavBARBULOVIC, Igor
    • B03D1/02C22B15/00C22B61/00B03D1/08
    • B03D1/02B03D1/08B03D1/24C22B15/0002C22B34/34
    • The process for extraction of molybdenum from the collective concentrate Cu-Mo, according to the invention, enables an economic production of molybdenum form a copper ore which has, on the average, 25-30% lower copper concentration and 50% lower molybdenum concentration compared to the ores being exploited in the world. The process has three stages, and the essence of the new technical solution is adding, besides the reagents for the minerals of copper, a reagent for Mo - SYNTEX-L (0,2 g/t) and D2 (2 g/t) in the process of flotation of the copper minerals in order to improve the exploitation of Mo for 20%. The condensed collective concentrate of copper and molybdenum is conditioned, and then the desorbent on of the collector membrane from the mineral surfaces is conducted with sodium hydrosulfide as the primary desorbent, and NaCN as the secondary desorbent. After the depression, the pulp that is the drain of the basic flotation and first purification goes to the second condenser, and the drains of the third, forth, and fifth purification go to the third condenser for the concentrate washing. The role of the condenser is very important: washing of the concentrate and better distribution of the useful elements compared to the entered ore. Coarse concentrate of molybdenum goes to the hydrocyclone for two-stage grinding and classification. The sand of the hydrocyclone is additionally ground in a grinder with balls, which works in a closed cycle with the hydrocyclone. The overflow of the hydrocyclone is taken in the purification process. The final concentrate of molybdenum is reached after the fifth purification and it goes to the filter for the filtration, and then in the drying furnace. The existing technologies have minimum 7-10 purifications.
    • 根据本发明,从集体浓缩物Cu-Mo中提取钼的方法使得经济生产钼形成铜矿石,其平均比较低的铜浓度为25-30%,钼浓度为50%较低 到世界上被开采的矿石。 该方法有三个阶段,除了铜矿物试剂外,还添加了Mo-SYNTEX-L(0.2g / t)和D2(2g / t)试剂, 在铜矿矿物浮选过程中,为了提高Mo的利用率20%。 对铜和钼的浓缩浓缩物进行调理,然后用矿物表面的收集​​器膜上的解吸剂作为主要的解吸剂和NaCN作为第二解吸剂进行。 在凹陷之后,作为基本浮选和第一纯化的排水的纸浆进入第二冷凝器,并且第三,第四和第五纯化物的排水口进入第三冷凝器进行浓缩清洗。 冷凝器的作用非常重要:与进入的矿石相比,浓缩物的洗涤和有用元素的分布更好。 钼的粗精矿去水力旋流器进行两级研磨和分级。 水力旋流器的砂子另外在带球的研磨机中研磨,其与水力旋流器在封闭的循环中工作。 在净化过程中采用水力旋流器的溢流。 在第五次纯化后达到钼的最终浓缩物,并进入过滤器过滤,然后在干燥炉中。 现有技术的纯度至少为7-10。