US20150182874A1 - Method of manufacturing a launder and launder - Google Patents

Method of manufacturing a launder and launder Download PDF

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Publication number
US20150182874A1
US20150182874A1 US14/407,219 US201314407219A US2015182874A1 US 20150182874 A1 US20150182874 A1 US 20150182874A1 US 201314407219 A US201314407219 A US 201314407219A US 2015182874 A1 US2015182874 A1 US 2015182874A1
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United States
Prior art keywords
launder
corner
settler
fixedly connected
shell
Prior art date
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Abandoned
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US14/407,219
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English (en)
Inventor
Jussi Vaarno
Rami Saario
Henri Fredriksson
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Outotec Finland Oy
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Outotec Finland Oy
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Assigned to OUTOTEC (FINLAND) OY reassignment OUTOTEC (FINLAND) OY ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: VAARNO, JUSSI, FREDRIKSSON, HENRI, SAARIO, RAMI
Publication of US20150182874A1 publication Critical patent/US20150182874A1/en
Abandoned legal-status Critical Current

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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D11/00—Solvent extraction
    • B01D11/04—Solvent extraction of solutions which are liquid
    • B01D11/0446—Juxtaposition of mixers-settlers
    • C—CHEMISTRY; METALLURGY
    • C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B3/00—Extraction of metal compounds from ores or concentrates by wet processes
    • C22B3/02—Apparatus therefor
    • C—CHEMISTRY; METALLURGY
    • C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B3/00—Extraction of metal compounds from ores or concentrates by wet processes
    • C22B3/20—Treatment or purification of solutions, e.g. obtained by leaching
    • C22B3/22—Treatment or purification of solutions, e.g. obtained by leaching by physical processes, e.g. by filtration, by magnetic means, or by thermal decomposition
    • C—CHEMISTRY; METALLURGY
    • C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B3/00—Extraction of metal compounds from ores or concentrates by wet processes
    • C22B3/20—Treatment or purification of solutions, e.g. obtained by leaching
    • C22B3/26—Treatment or purification of solutions, e.g. obtained by leaching by liquid-liquid extraction using organic compounds
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00—Technologies related to metal processing
    • Y02P10/20—Recycling
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T29/00—Metal working
    • Y10T29/49—Method of mechanical manufacture
    • Y10T29/49826—Assembling or joining

Definitions

  • the present invention relates to a method of manufacturing a launder to be used in co-operation with a solvent extraction settler adapted for hydrometallurgical liquid-liquid extraction processes. Further, the invention relates to a launder.
  • the aqueous and organic phases are pumped into a mixer or mixers in order to achieve a uniform liquid-liquid dispersion and a small droplet size.
  • this first step is performed in a pump-mixer called Dispersion Overflow Pump (DOP®) (disclosed e.g. in U.S. Pat. No. 5,662,871) and in a set of two SPIROK® helical mixers (disclosed in e.g. U.S. Pat. No. 5,185,081).
  • DOP® Dispersion Overflow Pump
  • the dispersion is fed into a settler.
  • the settler is typically a large tank which is square in plan and its square area is about several hundred square meteres.
  • Dispersion is fed into the settler at the front end of the settler.
  • a distributor fence is arranged at the feed end of the settler to distribute the flow of the dispersion to the whole width of the settler.
  • the dispersion moves towards the settler back wall and, at the same time, the phases separate by gravity into two layers with a dispersion band remaining between them.
  • separation fences are arranged in the settler tank to enhance coalescence of the dispersion.
  • the separation fences are so-called DDG® fences ( D ispersion D epletor G ate) (disclosed e.g. in U.S. Pat. No. 7,517,461).
  • an adjustable weir and launders are used to control the vertical position of the phase interface anal. to collect and discharge both phases, respectively.
  • Arrangements of settlers and launders are disclosed also e.g. in documents WO 97/40899, WO 97/40900, WO 97/40901, WO 2009/063128 A1 and WO 2010/097516 A1.
  • the known launder typically comprises two launders arranged in parallel side-by-side.
  • One of the launders is an overflow launder arranged to receive the lighter solution (e.g. organic phase) as an overflow from the settler and the other launder is an underflow launder arranged to receive the heavier solution (e.g. aqueous solution) as an underflow from the settler.
  • the launder arrangement is made of a fiber-reinforced plastic composite by hand laminating, or by filament winding as described in WO 2010/097516 A1.
  • WO 2009/063128 discloses that the whole launder is manufactured at a place of manufacture, such as in an engineering workshop, into a self-supporting subassembly which is transferred as a uniform entity to the site of installation where i is installed on the bottom of the settler.
  • the maintenance of the present launders requires a long downtime of the whole solvent extraction settler with which the launder requiring maintenance is connected.
  • the object of the invention is to eliminate the disadvantages mentioned above.
  • the present invention provides a method of manufacturing a launder to be used in co-operation with a solvent extraction settler adapted for hydrometallurgical liquid-liquid extraction processes, in which method the launder is installed at the discharge end of the settler.
  • the method comprises the steps of manufacturing at the site of manufacture, such as in an engineering workshop, a plurality of self-supporting launder element modules each having exterior dimensions, strength and handling and securing means conforming to shipping container standards; transporting the launder element modules to the site of installation as normal freight by transport equipment, such as trucks, trailers and container ships, capable of handling and transporting shipping container standard compatible units; and assembling at the site of installation the launder element modules into a module group forming a complete launder.
  • the present invention provides a launder to be used in co-operation with a solvent extraction settler adapted for hydrometallurgical liquid-liquid extraction processes.
  • the launder comprises a launder module group consisting of self-supporting launder element modules each having exterior dimensions, strength and handling and securing means conforming to shipping container standards to enable shipping container standard compatible transportability.
  • the advantage of the invention is that the launder element modules can be manufactured in the factory environment, which is different from the installation site environment, which provides good quality.
  • the launder modules being shipping container standard compatible units provides all benefits of the normal shipping containers: they can be handled with normal transport equipment and there is no need for oversize transport equipment.
  • the launder element modules having dimensions, strength and handling and securing means conforming to—shipping container standards thus have all the benefits of the transportability of normal shipping containers.
  • the launder element modules can be transported on land by trucks and trailers and with container ships by sea. In ports they can be handled with normal container handling equipment.
  • a complete launder, which may comprise a plurality of launder element modules, can be shipped in one delivery.
  • the modular structure enables flexible capacity since more capacity can be built while the solvent extraction plant is running by increasing the number of modules.
  • the launder can easily be re-located and recycled by disassembling the modules at one site and reassembling them into a launder located at another site.
  • the launder element module conforms to ISO shipping container standards to enable ISO shipping container standard compatible transportability.
  • the launder is arranged to feed dispersion to a solvent extraction settler.
  • the launder is arranged to receive and discharge solution phases separated in the solvent extraction settler.
  • both feeding and discharging functions are combined into a common launder element module, discharging functions serving one settler while the feeding function is serving another settler.
  • the launder element module comprises a self-supporting framework structure having a shape of a rectangular parallelepiped with exterior dimensions and corner fittings conforming to shipping container standards, said corner fittings being attached to each corner of the framework structure. Further, the launder element module comprises a shell, said shell being supported inside the framework structure and forming at least a part of a flow path for the solutions flowing in the launder.
  • the launder element module conforms to standard ISO 668 Series 1 “Freight containers—Classification, dimensions and ratings”;
  • the shell is a tubular hollow body made of a fibre-reinforced plastic composite.
  • the shell is manufactured by filament winding technology.
  • the shells connected to each other form a gas-tight tubular flow path for the dispersion and separated solutions.
  • the gas-tight sealed construction eliminates oxidation of the reagent by air, thus lowering make-up costs.
  • the gas-tight construction also decreases evaporation of the reagent, decreasing the release of Volatile Organic Compounds (VOC) to the environment.
  • VOC Volatile Organic Compounds
  • the inner surface of the shell which in operation comes to contact with the dispersion and solvents, is inherently smooth because it is formed against a mandrel which has a smooth surface.
  • the smooth surface contacting the solvent flow minimizes local turbulences.
  • the smooth surface also minimizes electrostatic charging and thereby reduces the risk for fires due to igniting of volatile organic compounds in the inner atmosphere of the shell caused by electrostatic discharge.
  • Electrostatic charging can also be reduced by adding carbon staple fibers to the plastic composite. Automated filament winding of the shell enables lower fabrication costs compared to any other manufacturing method, such as hand laminating.
  • the module group comprises two or more launder element modules arranged in parallel and side-by-side with each other.
  • the side-by-side arrangement of the launder element modules is advantageous because thereby the launder can be made compact and the foundation can be implemented by a plurality of pillars supporting each corner of the launder element modules.
  • One pillar may support one to four corners of the modules.
  • the launder element module comprises a first shell to receive and conduct a light solution phase, and a second shell to receive and conduct a heavy solution phase.
  • the launder element module comprises a third shell adapted to feed dispersion to a next settler.
  • the launder module group comprises a plurality of launder element modules.
  • the first shells of the adjacently neighboring launder modules are abutting and connected to each other to form a first flow channel
  • the second shells of the adjacently neighboring launder modules are abutting and connected to each other to form a second flow channel.
  • the first shells are conical so that the sequentially connected first shells of the launder element modules in the launder module group together form a conical first flow channel.
  • the second shells are conical so that the sequentially connected second shells of the launder element modules in the launder module group together form a conical second flow channel.
  • the third shells are conical so that the sequentially connected third shells of the launder element modules in the launder module group together form a conical third flow channel.
  • the first, second and third flow channels are all tubular closed compartments which have many advantages.
  • the inner atmosphere of the launders can be sealed from the outer atmosphere so that mist emissions cannot escape from the atmosphere in the interior of the launders to the outer atmosphere to contaminate the air and worsen the working conditions.
  • the surrounding air and e.g. insects and birds cannot enter the launders.
  • the lighter solution is an organic phase
  • the oxidation degree of the organic phase decreases whereby solution costs are reduced.
  • the atmosphere of the launder above the liquid surface is flammable because it contains volatile organic compounds which are released from the hydrocarbon based solvents.
  • the gas-tight closed compartments of the tubular shells provide fire protection against accidental fires.
  • the conical first and second flow channels which form discharge channels for the lighter solution (normally organic) and the heavier solution (aqueous solution) have many inlets along their length.
  • the cross section of the conical first and second flow channels increases and the bottom is inclined downwards towards the first and second discharge boxes. After each inlet the flow rate in the first and second flow channels increases.
  • the flow rate remains the same for the whole length of the launder and no return eddies and standing flows are created. Thereby crud accumulation is avoided if the solutions contain solids.
  • the launder element module comprises a first inlet pipe having a first end opening to the inner space of the first shell and a second end opening to the settler, the second end being adapted to receive the light solution phase as an overflow from the settler.
  • the launder element module comprises a second inlet pipe having a third end opening to the inner space of the second shell at a bottom of the second shell, and a fourth end opening to the settler, the fourth end being adapted to receive the heavy solution phase as an underflow from the settler.
  • the overflow height position of the third end of the second inlet pipe inside the second shell is adjustable by a first level control valve to adjust the level of the heavier solution in the settler.
  • the first level control valve comprises an actuator by which the height position of the third end of the second inlet pipe is adjustable.
  • the launder element module comprises a feed outlet pipe having a fifth end opening to the inner space of the third shell via a second level control valve disposed at a bottom of the third shell, and a sixth end adapted to feed a solution to a settler.
  • the launder module group comprises a box module comprising a first discharge box supported inside a framework structure for receiving and discharging the lighter solution phase from the first flow channel, and a second discharge box supported inside the framework structure for receiving and discharging the heavier solution phase from the second flow channel.
  • the box module comprises a feed box supported inside the framework structure for feeding dispersion to the third flow channel.
  • the conical third channel which forms a feed launder for the dispersion has a cross section which decreases from the end connected to the feed box towards its other end which is distant from the feed box. This has the advantage that the delay time distribution of the dispersion in the feed launder is uniform so that no standing zones, in which the dispersion would separate, are formed.
  • the bottom of the third flow channel is inclined downwards towards the feed box, whereby the aqueous solution separated from the dispersion in the feed launder flows back to the mixer via the feed box.
  • the framework structure comprises a first end frame comprising: a horizontal first lower beam; a horizontal first upper beam at a distance from the first lower beam; a vertical first corner post which is fixedly connected to a first end of the first lower beam, defining a first corner, the vertical first corner post being fixedly connected to a first end of the first upper beam, defining a second corner; and a vertical second corner post at a distance from the first corner post, the vertical second corner post being fixedly connected to a second end of the first lower beam, defining a third corner, the vertical second corner post being fixedly connected to a second end of the first upper beam, defining a fourth corner.
  • the framework structure comprises a second end frame comprising a horizontal second lower beam; a horizontal second upper beam at a distance from the second lower beam; a vertical third corner post which is fixedly connected to a first end of the second lower beam, defining a fifth corner, the vertical third corner post being fixedly connected to a first end of the second upper beam, defining a sixth corner; and a vertical fourth corner post at a distance from the third corner post, the vertical fourth corner post being fixedly connected to a second end of the second lower beam, defining a seventh corner, the vertical fourth corner post being fixedly connected to a second end of the second upper beam, defining an eighth corner.
  • the framework structure comprises a first bottom side rail fixedly connected to the first end frame at the first corner and to the second end frame at the fifth corner; a second bottom side rail fixedly connected to the first end frame at the third corner and to the second end frame at the seventh corner; a first top side rail fixedly connected to the first end frame at the second corner and to the second end frame at the sixth corner; a second top side rail fixedly connected to the first end frame at the fourth corner and to the second end frame at the eighth corner; bottom cross members fixedly connected between and to the first and second bottom side rails; top cross members fixedly connected between and to the first and second top side rails; side cross members fixedly connected between and to the bottom side rails and the top side rails.
  • a corner fitting is attached to each of the first corner, second corner, third corner, fourth corner, fifth corner, sixth corner, seventh corner and eighth corner.
  • the launder comprises a foundation on which the launder module group is supported at a height above the ground level, thereby providing a space for piping and access below the settler.
  • the foundation comprises a plurality of pillars having ISO shipping standard compatible container lashing fittings to which the corner fittings of the launder element modules can be connected.
  • the installation of the launder on pillars has the advantage that a minimal amount of excavation work is needed.
  • the installation on piltars also makes it possible to speed up the installation and shortens the project lead time. Pillars also allow easy assembly and disassembly of the modules and launders. When more capacity is needed for the launder, it is easy to increase capacity by simply adding more pillars for the installation of more modules. The increasing of capacity can be done with a short interruption of the process.
  • the pillar comprises a lower end which is supported on the ground, an upper end, and one or more container lashing fittings attacked to the upper end of the pillar.
  • the container lashing fitting comprises a stacking cone.
  • the container lashing fitting comprises a twist lock.
  • the pillar comprises one to four container lashing fittings depending on the number of corner fittings to be connected onto the pillar.
  • the pillar comprises a plastic tube, a concrete reinforcement arranged inside the plastic tube, cast concrete cast inside the plastic tube, and a metal base plate attached at the upper end of the pillar, to which base plate one or more container lashing fittings are fixedly connected.
  • FIG. 1 is an axonometric schematic view of a solvent extraction settler equipped with a launder according to an embodiment of the present invention
  • FIG. 2 is an axonometric view of the framework structure of the launder element module of FIG. 1 ,
  • FIG. 3 is an axonometric view of detail A of FIG. 2 .
  • FIG. 4 is an axonometric view of three interconnected launder modules of FIG. 1 ,
  • FIG. 5 is a side view of the launder module of FIG. 4 .
  • FIG. 6 is an end view of the three interconnected launder modules of FIG. 3 , 15
  • FIG. 7 is a plan view of the three interconnected launder modules of FIG. 3 , seen from above,
  • FIG. 8 is a view of the layout of the foundation of the settler of FIG. 1 .
  • FIGS. 9 to 12 show an axonometric view of four different types of pillars used in the foundation of FIG. 8 , the pillars being equipped with stacking cones as container lashing fittings,
  • FIGS. 13 and 14 show another embodiment of the pillar equipped with a twist lock as a container lashing fitting
  • FIG. 15 shows a schematic longitudinal section of the pillar.
  • FIG. 1 shows one embodiment of a solvent extraction settler which is used in hydrometallurgical liquid-liquid extraction processes for separating solutions mixed in a dispersion into different solution phases.
  • the launder 1 is connected to the settler 2 .
  • the dispersion pump and mixers which are used to prepare the dispersion are not shown in FIG. 1 .
  • the settler 2 which is not part of this invention, is shown only schematically.
  • the settler 2 may be of a conventional type comprising a large tank built on the site, or it may be modular and composed of a number of pre-fabricated, ISO shipping container compatible settler element modules transferred and installed at the site into a complete settler as disclosed in another patent aplication filed in parallel with this aplication.
  • the launder 1 may have two functions. It may be arranged to feed dispersion to the settler 2 (see FIG. 4 ) and it may be arranged to receive and discharge the separated solutions obtained from the settler 2 .
  • the launder 1 comprises a launder module group 5 which consists of three self-supporting launder element modules 3 and a box module 24 arranged in parallel and side-by-side with each other.
  • Each launder element module 3 has exterior dimensions, strength and handling and securing means 4 conforming to ISO shipping container standards to enable ISO compatible transportability.
  • the launder element module 3 comprises a self-supporting framework structure 6 having a shape of a rectangular parallelepiped with exterior dimensions and corner fittings 4 conforming to ISO shipping container standards.
  • the corner fittings 4 are attached to each corner of the framework structure 6 .
  • the launder element module 3 conforms to standard ISO 668 Series 1 “Freight containers—Classification, dimensions and ratings”; and the corner fittings 4 conform to standard ISO 1161 Series 1 “Freight containers—Corner fittings—specification”.
  • Shells 7 , 8 , 9 are supported inside the framework structure 6 and format least a part of a flow path for the solutions flowing in the launder.
  • the shells 7 , 8 , 9 can be made of steel or a fibre-reinforced plastic composite.
  • the shells 7 , 8 , 9 are tubular hollow bodies which are preferably made of a fibre-reinforced plastic composite and preferably manufactured by filament winding technology.
  • the framework structure 6 encompassing the shells 7 , 8 , 9 may have the following structure.
  • the framework structure 6 comprises a first end frame 28 .
  • the first end frame 28 comprises a horizontal first lower beam 29 , a horizontal first upper beam 30 at a distance from the first lower beam, a vertical first corner post 31 which is fixedly connected to a first end of the first lower beam 29 , defining a first corner 32 , the vertical first corner post 31 being fixedly connected to a first end of the first upper beam 30 , defining a second corner 33 , a vertical second corner post 34 at a distance from the first corner post 31 , the vertical second corner post being fixedly connected to a second end of the first lower beam 29 , defining a third corner 35 , the vertical second corner post 34 being fixedly connected to a second end of the first upper beam 30 , defining a fourth corner 36 .
  • the framework structure 7 comprises a second end frame 37 .
  • the second end frame 37 comprises a horizontal second lower beam 38 , a horizontal second upper beam 39 at a distance from the second lower beam 38 , a vertical third corner post 40 which is fixedly connected to a first end of the second lower beam 38 , defining a fifth corner 41 , the vertical third corner post 40 being fixedly connected to a first end of the second upper beam 39 , defining a sixth corner 42 , and a vertical fourth corner post 43 at a distance from the third corner post 40 , the vertical fourth corner post being fixedly connected to a second end of the second lower beam 39 , defining a seventh corner 44 , the vertical fourth corner post being fixedly connected to a second end of the second upper beam 39 , defining an eighth corner 45 .
  • a first bottom side rail 46 is fixedly connected to the first end frame 28 at the first corner 32 and to the second end frame 37 at the fifth corner 41 .
  • a second bottom side rail 47 is fixedly connected to the first end frame 28 at the third corner 35 and to the second end frame 37 at the seventh corner 44 .
  • a first top side rail 48 is fixedly connected to the first end frame 28 at the second corner 33 and to the second end frame 37 at the sixth corner 42 .
  • a second top side rail 49 is fixedly connected to the first end frame 28 at the fourth corner 36 and to the second end frame 37 at the eighth corner 45 .
  • Bottom cross members 50 are fixedly connected between and to the first and second bottom side rails 46 , 47 .
  • Top cross members 51 are fixedly connected between and to the first and second top side rails 48 , 49 .
  • a corner fitting 4 is attached to each of the first corner 32 , second corner 33 , third corner 35 , fourth corner 36 , fifth corner 41 , sixth corner 42 , seventh corner 44 and eighth corner 45 .
  • the framework structure 6 conforms to standard ISO 668 Series 1 “Freight containers—Classification, dimensions and ratings”.
  • the framework structure 6 may preferably have an external length of 6.058 m (20 ft) or 2.991 m (10 ft) and a width of 2.438 m (8 ft).
  • FIG. 3 shows a corner fitting 4 fixedly connected to a corner of the framework structure 6 .
  • the corner fittings 4 conform to standard ISO 1161 Series 1 “Freight containers—Corner fittings—specification”.
  • the corner fitting 4 has a connecting hole at each of its three sides.
  • each launder element module 3 comprises a first shell 7 to receive and conduct a light solution phase. Further, the launder element module 3 comprises a second shell 8 to receive and conduct a heavy solution phase. Further, the launder element module 3 comprises a third shell 9 adapted to feed dispersion to a next settler 2 , as is seen in FIG. 4 .
  • the launder module group 5 of the shown embodiment comprises three launder element modules 3 .
  • the first shells 7 of the adjacently neighboring launder modules 3 are abutting and connected to each other to form a first flow channel 10 .
  • the second shells 8 of the adjacently neighboring launder modules are abutting and connected to each other to form a second flow channel 11 .
  • the third shells 9 of the adjacently neighboring launder modules are abutting and connected to each other to form a third flow channel 12 .
  • the first shells 7 are conical so that the sequentially connected first shells 7 of the launder element modules 3 in the launder module group 5 together form a conical first flow channel 10 .
  • the second shells 8 are conical so that the sequentially connected second shells 8 of the launder element modules 3 in the launder module group 5 together form a conical second flow channel 11 .
  • the third shells 9 are conical so that the sequentially connected third shells 9 of the launder element modules 3 in the launder module group 5 together form a conical third flow channel 12 .
  • the module group 5 comprises also a box module 24 .
  • the box module 24 comprises a self-supporting framework structure 6 having a shape of a rectangular parallelepiped with exterior dimensions and corner fittings 4 conforming to ISO shipping container standards, the corner fittings 4 being attached to each corner of the framework structure 6 .
  • a first discharge box 23 is supported inside the framework structure 6 for receiving and discharging the lighter solution phase from the first flow channel 10 .
  • the box module 24 also comprises a second discharge box 26 supported inside the framework structure 6 for receiving and discharging the heavier solution phase from the second flow channel 11 .
  • the box module 5 comprises a feed box 27 supported inside the framework structure 6 for feeding dispersion to the third flow channel 12 .
  • the framework structure 6 of the box module 24 may be similar to that shown and disclosed in connection with FIG. 2 .
  • the conical first and second flow channels 10 and 11 which form discharge channels for the lighter solution (normally organic) and the aqueous solution have many inlets along their length.
  • the cross section of the conical first and second flow channels 10 , 11 increases and their bottom is inclined downwards towards the first and second discharge boxes 25 , 26 .
  • the flow rate in the first and second flow channels 10 , 11 increases.
  • the flow rate remains the same for the whole length of the launder and no return eddies and standing flows are created. Thereby crud accumulation is avoided if the solutions contain solids.
  • the conical third channel 12 which forms a feed launder for the dispersion has a cross section which decreases from the end connected to the feed box 27 towards its other end which is distant from the feed box 27 .
  • This has the advantage that the delay time distribution of the dispersion in the feed launder 12 is uniform so that no standing zones, in which the dispersion would separate, are formed.
  • the bottom of the third flow channel 12 is inclined downwards towards the feed box 27 whereby the aqueous solution separated from the dispersion in the feed launder 12 flows back to the feed box and further to the mixer.
  • each launder element module 3 is different from the other due to different sizes of the shells 7 , 8 , 9 .
  • the system may be based on e.g. 14 standard elements which can be configured to a flow rate range of 150 to 8000 m 3 /h.
  • the full length conical flow channel 10 , 11 , 12 may be manufactured as one piece on a mold or mandrel, and thereafter the flow channel can be cut into separate parts having lengths which fit inside the framework structure 6 , and the parts are then installed inside the framework structures 6 of the launder element modules 3 .
  • the interconnection of the shells can be made by normal means and methods of connecting plastic tubes, such as by using connecting sleeves and/or by gluing the abutting ends together.
  • the launder element module 3 comprises a first inlet pipe 12 having a first end 13 opening to the inner space of the first shell 7 and a second end 14 opening to the settler 2 on the right hand side of FIG. 4 .
  • the second end 14 is adapted to receive the light solution phase as an overflow from the settler 2 on the right hand side of FIG. 4 .
  • the launder element module 3 comprises a second inlet pipe 15 having a third end 16 opening to the inner space of the second shell 8 at a bottom of the second shell 8 , and a fourth end 18 opening to the settler 2 .
  • the fourth end 18 is adapted to receive the heavy solution phase as an underflow from the settler.
  • the overflow height position of the third end 16 of the second inlet pipe 15 inside the second shell 8 is adjustable by a first level control valve 17 to adjust the level of the heavier solution in the settler 2 .
  • the first level control valve 17 comprises an actuator 19 by which the height position of the third end 16 of the second inlet pipe 15 is adjustable.
  • the launder element module 3 comprises a feed outlet pipe 20 having a fifth end 21 opening to the inner space of the third shell 9 via a second level control valve 22 disposed at a bottom of the third shell, and a sixth end 23 adapted to feed a solution to a settler 2 on the left hand side of FIG. 4 .
  • FIG. 8 shows a layout of the foundation designed for the whole settler 2 including the launder module group 5 shown in FIG. 1 .
  • the launder comprises a foundation 53 on which the module group 5 is supported at a height above the ground level, thereby providing a space for piping and access underneath the launder.
  • the foundation 53 comprises a plurality of pillars 54 having ISO shipping standard compatible container lashing fittings 55 , 56 to which the corner fittings 4 of the launder modules 3 and the box module 24 can be connected.
  • the pillar 54 comprises a lower end 57 which is supported on the ground, an upper end 58 , and one or more container lashing fittings 55 , 55 attached to the upper end 58 of the pillar 54 .
  • FIGS. 9 and 15 show that the pillar 54 comprises a lower end 57 supported on the ground and an upper end 58 .
  • One or more container lashing fittings 55 , 56 are attached to the upper end 58 .
  • the pillar 54 may comprise one to four container lashing fittings 55 , 56 depending on the number of corner fittings 4 to be connected onto the pillar.
  • a pillar 54 supporting one corner of the module comprises only one container lashing fitting 55 ( FIG. 9 ).
  • a pillar 54 supporting two corners of parallel modules comprises a pair of container lashing fittings 55 arranged side by side ( FIG. 10 ).
  • a pillar 54 supporting two corners of sequential modules comprises a pair of container lashing fittings 55 arranged in a row ( FIG. 11 ).
  • a pillar 54 supporting four corners of parallel and sequential modules comprises two pairs of container lashing fittings 55 ( FIG. 12 ).
  • the container lashing fittings may be stacking cones 55 as shown in FIGS. 9 to 12 , or alternatively, they may be twist locks 56 as shown in FIGS. 13 and 14 .
  • the pillar 54 comprises a plastic tube 59 , a concrete reinforcement of metal 60 arranged inside the plastic tube 59 , cast concrete 61 cast inside the plastic tube, and a metal base plate 62 attached at the upper end of the pillar, to which base plate one or more container lashing fittings 55 , 56 are fixedly connected.
  • the launder 1 is manufactured so that that at the site of manufacture, such as in an engineering workshop, a plurality of self-supporting launder element modules 3 , 24 are manufactured.
  • Each launder element module 3 , 24 has exterior dimensions, strength and handling and securing means 4 conforming to ISO shipping container standards.
  • the launder element modules 3 are transported to the site of installation as normal freight by transport equipment, such as trucks, trailers and container ships, capable of handling and transporting ISO compatible units.
  • transport equipment such as trucks, trailers and container ships, capable of handling and transporting ISO compatible units.
  • the launder element modules 3 are assembled into a module group 5 which forms a complete launder 1 .

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Geology (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Manufacturing & Machinery (AREA)
  • Environmental & Geological Engineering (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Geochemistry & Mineralogy (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Extraction Or Liquid Replacement (AREA)
  • Chutes (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Screw Conveyors (AREA)
  • Ship Loading And Unloading (AREA)
  • Packages (AREA)
  • Fittings On The Vehicle Exterior For Carrying Loads, And Devices For Holding Or Mounting Articles (AREA)
US14/407,219 2012-06-26 2013-06-12 Method of manufacturing a launder and launder Abandoned US20150182874A1 (en)

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US20150232960A1 (en) * 2012-06-26 2015-08-20 Outotec (Finland) Oy Solvent extraction method and solvent extraction settler
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US10220331B2 (en) 2012-06-26 2019-03-05 Outotec (Finland) Oy Method of manufacturing a solvent extraction settler and solvent extraction settler
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BR112014032060B1 (pt) 2019-10-15
BR112014032060A2 (pt) 2017-08-01
ES2718908T3 (es) 2019-07-05
CA2875906A1 (en) 2014-01-03
US20180015388A1 (en) 2018-01-18
AU2013283125A1 (en) 2015-01-22
BR112014032060B8 (pt) 2023-02-07
CA2875906C (en) 2016-11-29
EP2872659A4 (en) 2016-04-27
MX364846B (es) 2019-05-08
EA201590082A1 (ru) 2015-06-30
CN104685074B (zh) 2017-05-31
AU2013283125B2 (en) 2016-04-21
EP2872659B1 (en) 2019-01-30
AP2014008156A0 (en) 2014-12-31
ZA201500539B (en) 2016-11-30
FI20125712A (fi) 2013-11-15
WO2014001621A1 (en) 2014-01-03
IN2014KN02879A (pt) 2015-05-08
TR201904670T4 (tr) 2019-05-21
CL2014003491A1 (es) 2015-04-24
CN104685074A (zh) 2015-06-03
MX2014015962A (es) 2015-03-20
AP4048A (en) 2017-02-28
EA029647B1 (ru) 2018-04-30
PE20150106A1 (es) 2015-02-17
US10661199B2 (en) 2020-05-26
EP2872659A1 (en) 2015-05-20

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