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WO2002009881A1 - Procede de triage hydraulique de matieres a fractions fines - Google Patents

Procede de triage hydraulique de matieres a fractions fines Download PDF

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Publication number
WO2002009881A1
WO2002009881A1 PCT/RU2000/000315 RU0000315W WO0209881A1 WO 2002009881 A1 WO2002009881 A1 WO 2002009881A1 RU 0000315 W RU0000315 W RU 0000315W WO 0209881 A1 WO0209881 A1 WO 0209881A1
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Prior art keywords
gidροsmesi
chτο
hydraulic
οτsτοyniκa
emκοsτi
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PCT/RU2000/000315
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English (en)
Russian (ru)
Inventor
Boris Pavlovich Derkachev
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Priority to AU2000270442A priority Critical patent/AU2000270442A1/en
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Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03B—SEPARATING SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS
    • B03B9/00—General arrangement of separating plant, e.g. flow sheets

Definitions

  • the invention is related to the classification of small materials (including small particles and particles), which are in the form of free particles in a liquid medium.
  • the invention may be used for hydraulic classification of particles of a single mass, which is present in the form of a small phase in a liquid.
  • the invention may be used to enrich the original foreign mass or its interest in order to receive and extract from it the profit-sharing in- vestments of minerals.
  • Iz ⁇ b ⁇ e ⁇ enie m ⁇ zhe ⁇ by ⁇ is ⁇ lz ⁇ van ⁇ for ⁇ chis ⁇ i s ⁇ v ( ⁇ v ⁇ s ⁇ v) ⁇ myshlenn ⁇ y gid ⁇ avliches ⁇ y ⁇ e ⁇ e ⁇ ab ⁇ i is ⁇ dn ⁇ y g ⁇ n ⁇ y mass for the purpose ⁇ chis ⁇ i zhid ⁇ y ⁇ azy (v ⁇ dy) to discharge therefrom and glinis ⁇ y ⁇ ⁇ ganiches ⁇ i ⁇ v ⁇ lyucheny for ⁇ lucheniya ⁇ e ⁇ n ⁇ l ⁇ giches ⁇ i chis ⁇ y v ⁇ dy ⁇ b ⁇ n ⁇ g ⁇ v ⁇ d ⁇ snabzheniya.
  • Iz ⁇ b ⁇ e ⁇ enie m ⁇ zhe ⁇ by ⁇ is ⁇ lz ⁇ van ⁇ ne ⁇ s ⁇ eds ⁇ venn ⁇ on mes ⁇ zhdeniya ⁇ where d ⁇ bycha mine ⁇ al ⁇ v ⁇ izv ⁇ di ⁇ sya on shlyuz ⁇ vy ⁇ ⁇ ib ⁇ a ⁇ for ⁇ e ⁇ e ⁇ ab ⁇ i ⁇ e ⁇ uschi ⁇ ⁇ v ⁇ s ⁇ v the purpose d ⁇ izvlecheniya ⁇ lezny ⁇ mine ⁇ al ⁇ v and ⁇ lucheniya ⁇ e ⁇ n ⁇ l ⁇ giches ⁇ i chis ⁇ y v ⁇ dy ⁇ b ⁇ n ⁇ g ⁇ v ⁇ d ⁇ snabzheniya.
  • the invention may be used in the form of a separate installation, as well as in the components of the process lines of the processing and processing plants.
  • Iz ⁇ b ⁇ e ⁇ enie m ⁇ zhe ⁇ by ⁇ is ⁇ lz ⁇ van ⁇ ⁇ b ⁇ gascheniya ma ⁇ e ⁇ ial ⁇ v for the purpose of extraction (d ⁇ izvlecheniya) ⁇ lezny ⁇ ⁇ m ⁇ nen ⁇ v in ⁇ myshlenn ⁇ s ⁇ i s ⁇ i ⁇ elny ⁇ ma ⁇ e ⁇ ial ⁇ v in ⁇ m including ⁇ i ⁇ izv ⁇ ds ⁇ ve s ⁇ i ⁇ elny ⁇ ma ⁇ e ⁇ ial ⁇ v of ⁇ d ⁇ v ⁇ e ⁇ e ⁇ ab ⁇ i g ⁇ n ⁇ udn ⁇ y and ⁇ imiches ⁇ y ⁇ myshlenn ⁇ s ⁇ i and ⁇ a ⁇ zhe for ⁇ chis ⁇ i s ⁇ chny ⁇ v ⁇ d ⁇ e ⁇ n ⁇ l ⁇ giches ⁇ i ⁇ ⁇ tsess ⁇ v v ⁇ eu ⁇ azanny ⁇ and d ⁇ ugi ⁇ ⁇ myshlenny ⁇ ⁇ iz
  • the invention can be used only with the help of clean water by isolating from it positive and negative inclusions to the KEC and consumer goods that are used.
  • the invention may be used to make lab and industrial installations. 2
  • Izves ⁇ na " ⁇ e ⁇ n ⁇ l ⁇ giches ⁇ aya line gid ⁇ avliches ⁇ g ⁇ z ⁇ ly and isolation of shla ⁇ a z ⁇ l ⁇ shla ⁇ vy ⁇ ⁇ d ⁇ v" (Pa ⁇ en ⁇ ⁇ 2,074,340) s ⁇ de ⁇ zhaschaya nas ⁇ s with mn ⁇ g ⁇ a ⁇ tsi ⁇ nnym ⁇ b ⁇ ga ⁇ i ⁇ elnym ag ⁇ ega ⁇ m, shne ⁇ vy ⁇ bezv ⁇ zhiva ⁇ el, va ⁇ uumny ⁇ il ⁇ , ⁇ n ⁇ sl ⁇ yny sgus ⁇ i ⁇ el and len ⁇ chnye ⁇ nveye ⁇ y.
  • the access to this line is the greater power consumption and the use of free-of-charge mining equipment; ⁇ me e ⁇ g ⁇ ⁇ b ⁇ ud ⁇ vanie line ⁇ zv ⁇ lyae ⁇ ⁇ luchi ⁇ ⁇ l ⁇ ⁇ i ⁇ a ⁇ tsii ⁇ u ⁇ n ⁇ s ⁇ i ⁇ e ⁇ e ⁇ aba ⁇ yvaem ⁇ y ⁇ ve ⁇ d ⁇ y ⁇ azy gid ⁇ smesi - ⁇ u ⁇ nuyu, and s ⁇ ednyuyu mel ⁇ uyu and ⁇ a ⁇ same usl ⁇ zhnyae ⁇ ⁇ tsess ⁇ chis ⁇ i zhid ⁇ y ⁇ azy (v ⁇ dy) ⁇ imeneniem d ⁇ g ⁇ s ⁇ yaschi ⁇ and ene ⁇ g ⁇ em ⁇ i ⁇ va ⁇ uumny ⁇ ⁇ il ⁇ v.
  • the purpose of the proposed invention is to eliminate any disadvantages.
  • the goal is achieved by the following.
  • Lab ⁇ a ⁇ nymi analyzes ⁇ edelyae ⁇ sya g ⁇ anul ⁇ me ⁇ iches ⁇ y s ⁇ s ⁇ av is ⁇ dn ⁇ y g ⁇ n ⁇ y mass (in the case ⁇ lassi ⁇ i ⁇ atsii ⁇ ⁇ lassam ⁇ dn ⁇ dn ⁇ y g ⁇ n ⁇ y mass or ⁇ chis ⁇ i v ⁇ dy) and g ⁇ anul ⁇ me ⁇ iches ⁇ y s ⁇ s ⁇ av vydelyaem ⁇ g ⁇ ⁇ lezn ⁇ g ⁇ mine ⁇ ala with ⁇ as ⁇ edeleniem and s ⁇ de ⁇ zhaniem in ⁇ azhd ⁇ m of ⁇ lass ⁇ v ⁇ e ⁇ e ⁇ aba ⁇ yvaem ⁇ y is ⁇ dn ⁇ y g ⁇ n ⁇ y mass.
  • the volumes of the separated (by classes) particles of the hydraulic mixture and the corresponding components of the separation are divided.
  • ⁇ sh ⁇ si maya of ⁇ s ⁇ ans ⁇ va labi ⁇ in ⁇ n ⁇ y ⁇ eshe ⁇ i moving ⁇ m zhid ⁇ y ⁇ azy gid ⁇ smesi ⁇ ve ⁇ daya ⁇ aza gid ⁇ smesi, vmes ⁇ e with its ⁇ e ⁇ edvigayuschim ⁇ m, ⁇ adayu ⁇ in ⁇ y ⁇ uyu ⁇ niches ⁇ uyu em ⁇ s ⁇ g ⁇ avi ⁇ atsi ⁇ nn ⁇ g ⁇ ⁇ s ⁇ yni ⁇ a, imeyuscheg ⁇ in d ⁇ nn ⁇ y chas ⁇ i vy ⁇ dn ⁇ y ⁇ a ⁇ ub ⁇ , and ve ⁇ ney chas ⁇ i l ⁇ vy sb ⁇ ni ⁇ v ⁇ ni ⁇ v ⁇ g ⁇ ⁇ i ⁇ a.
  • P ⁇ izves ⁇ n ⁇ mu ⁇ bemu gid ⁇ smesi have g s ⁇ s ⁇ u ⁇ ayuschey in ⁇ niches ⁇ uyu em ⁇ s ⁇ g ⁇ avi ⁇ atsi ⁇ nn ⁇ g ⁇ ⁇ s ⁇ yni ⁇ a and diame ⁇ u chas ⁇ its ⁇ ⁇ e ⁇ v ⁇ g ⁇ e ⁇ a ⁇ a ⁇ sazhdeniya, ⁇ edelyae ⁇ sya s ⁇ s ⁇ s ⁇ esnenn ⁇ g ⁇ ⁇ sazhdeniya chas ⁇ its ⁇ U s ⁇ and ⁇ l ⁇ schad ⁇ e ⁇ echn ⁇ g ⁇ section ⁇ sn ⁇ vaniya ⁇ niches ⁇ y em ⁇ s ⁇ i g ⁇ avi ⁇ atsi ⁇ nn ⁇ g ⁇ ⁇ s ⁇ yni ⁇ a ⁇ .
  • a third dimensionless coating takes up the second layer of planting 8 2 , which is dependent on:
  • ⁇ ⁇ is the dynamic viscosity
  • the therapeutic rate of planting ⁇ ⁇ the only particulate of the common particle in the laminate mode is divided by: ⁇ 2
  • ⁇ ⁇ - velocity of particle deposition ⁇ svi - the density of the hydraulic mixture
  • ⁇ is the kinematic viscosity of the mixture
  • ⁇ is the dynamic viscosity
  • ⁇ - density of yashdosti 9.81
  • ⁇ ⁇ - effective density The transitional mode is characterized by the following critical values of the deposition criteria:
  • a particle moving downward (settling down) of a solid phase in a liquid medium is affected by its form, this effect for the process of settling is taken into account by the coefficient of form ⁇ .
  • ⁇ 1, for particles of a non-large form, the value of ⁇ varies from 0, 77 to 0, 43.
  • the area of the ⁇ planting area or the area of the cross-section of the base of the external capacity of the plant is shared with the factory:
  • ⁇ 0 is the quantitative liquid phase of the hydraulic mixture
  • the level of the seat in the tank is equipped with a simple visual control unit through the lower windows (upper and lower).
  • av ⁇ ma ⁇ iches ⁇ g ⁇ v ⁇ lyucheniya and vy ⁇ lyucheniya nas ⁇ sa ⁇ ach ⁇ i ⁇ sad ⁇ a of em ⁇ s ⁇ i g ⁇ avi ⁇ atsi ⁇ nn ⁇ g ⁇ ⁇ s ⁇ yni ⁇ a on u ⁇ vne sm ⁇ vy ⁇ ⁇ n us ⁇ anavlivayu ⁇ sya da ⁇ chi ⁇ i av ⁇ ma ⁇ iches ⁇ g ⁇ v ⁇ lyucheniya and vy ⁇ lyucheniya nas ⁇ sa ⁇ ach ⁇ i ⁇ sad ⁇ a of em ⁇ s ⁇ i g ⁇ avi ⁇ atsi ⁇ nn ⁇ g ⁇ ⁇ s ⁇ yni ⁇ a.
  • the seat of the sitting is shared by the mule of Zhukov:
  • the angle ⁇ should be greater than the angle of the natural flow rate ⁇ for precipitated particles of the solid phase of the hydraulic mixture.
  • the value of ⁇ is divided from the hydraulic tables. 10
  • the length of the channels of the lamellar block is divided by the formula:
  • ⁇ ⁇ ct the rate of depreciation of the particles of the solid phase of the hydraulic mixture, separated by the field depending on the mode of deposition; ⁇ is the tilt angle of the channels of the lamella block to the horizontal area.
  • P ⁇ i gid ⁇ avliches ⁇ y ⁇ lassi ⁇ i ⁇ atsi ⁇ ⁇ edlagaem ⁇ mu s ⁇ s ⁇ bu ne ⁇ dn ⁇ dn ⁇ y ⁇ mine ⁇ al ⁇ giches ⁇ mu s ⁇ s ⁇ avu g ⁇ n ⁇ y mass in the form is ⁇ dn ⁇ y gid ⁇ smesi (na ⁇ ime ⁇ , ⁇ ssy ⁇ ny ⁇ mes ⁇ zhdeny ⁇ asse ⁇ i ⁇ i ⁇ a) in g ⁇ avi ⁇ atsi ⁇ nn ⁇ m ⁇ s ⁇ yni ⁇ e ⁇ sazhdayu ⁇ sya chas ⁇ itsy ⁇ dina ⁇ v ⁇ g ⁇ ( ⁇ avn ⁇ g ⁇ ) weight.
  • the particle sizes are divided with the unit specific gravity.
  • the subsequent separation of the particles, depending on the size of the components, is produced in hydraulic units, in dry or motorized applications, in the event of a hydraulic drive d.
  • P ⁇ i gid ⁇ avliches ⁇ y ⁇ lassi ⁇ i ⁇ atsi ⁇ ⁇ edlagaem ⁇ mu s ⁇ s ⁇ bu ne ⁇ dn ⁇ dn ⁇ y ⁇ mine ⁇ al ⁇ giches ⁇ mu s ⁇ s ⁇ avu g ⁇ n ⁇ y mass in the form is ⁇ dn ⁇ y gid ⁇ smesi (na ⁇ ime ⁇ , ⁇ ssy ⁇ nzh mes ⁇ zhdeny ⁇ asse ⁇ e ⁇ i ⁇ a) in g ⁇ avi ⁇ atsi ⁇ nn ⁇ m ⁇ s ⁇ yni ⁇ e ⁇ sazhdayu ⁇ sya chas ⁇ itsy ⁇ dina ⁇ v ⁇ g ⁇ ( ⁇ avn ⁇ g ⁇ ) weight.
  • the particle sizes are divided with the unit specific gravity.
  • the subsequent separation of the particles, depending on the size of the unit, is produced in hydraulic units, in dry or motorized applications, in the case of hydraulic d.
  • the level of the seat in the tank is equipped with a simple visual control unit through the lower windows (upper and lower).
  • av ⁇ ma ⁇ iches ⁇ g ⁇ v ⁇ lyucheniya and vy ⁇ lyucheniya nas ⁇ sa ⁇ ach ⁇ i ⁇ sad ⁇ a of em ⁇ s ⁇ i g ⁇ avi ⁇ atsi ⁇ nn ⁇ g ⁇ ⁇ s ⁇ yni ⁇ a on u ⁇ vne sm ⁇ vzh ⁇ n us ⁇ anavlivayu ⁇ sya da ⁇ chi ⁇ i av ⁇ ma ⁇ iches ⁇ g ⁇ v ⁇ lyucheniya and v ⁇ slyucheniya nas ⁇ sa ⁇ ach ⁇ i ⁇ sad ⁇ a of em ⁇ s ⁇ i g ⁇ avi ⁇ atsi ⁇ nn ⁇ g ⁇ ⁇ s ⁇ yni ⁇ a.
  • the proposed method of beneficiating heavy duty of small amounts of money is included in the combination and combination of the means of beneficiation and the payment of money.
  • the section of the labyrinth lattice with the horizontal surface is shown in FIG. 2.
  • the cross-section of the lamellar block compulsively executed from the apartment of the industrial or quadrant channels, of the flat 4.
  • the process is carried out as follows.
  • Lab ⁇ a ⁇ nymi analyzes ⁇ edelyae ⁇ sya g ⁇ anul ⁇ me ⁇ iches ⁇ y s ⁇ s ⁇ av is ⁇ dn ⁇ y g ⁇ n ⁇ y mass (in the case ⁇ lassi ⁇ i ⁇ atsii ⁇ ⁇ lassam ⁇ dn ⁇ dn ⁇ y g ⁇ n ⁇ y mass or ⁇ chis ⁇ i v ⁇ dy) and g ⁇ anul ⁇ me ⁇ iches ⁇ y s ⁇ s ⁇ av vydelyaem ⁇ g ⁇ ⁇ lezn ⁇ g ⁇ mine ⁇ ala with ⁇ as ⁇ edeleniem and s ⁇ de ⁇ zhaniem in ⁇ azhd ⁇ m of ⁇ lass ⁇ v ⁇ e ⁇ e ⁇ aba ⁇ yvaem ⁇ y is ⁇ dn ⁇ y g ⁇ n ⁇ y mass. 14
  • the volume of all the (part of) the particles of the hydraulic mixture and the associated parts is divided (the classes).
  • ⁇ yn ⁇ si maya of ⁇ s ⁇ ans ⁇ va labi ⁇ in ⁇ n ⁇ y ⁇ eshe ⁇ i 7 moving ⁇ m lsid ⁇ y ⁇ azy gid ⁇ smesi ⁇ ve ⁇ daya ⁇ aza gid ⁇ smesi (vmes ⁇ e with its ⁇ e ⁇ edvigayuschim ⁇ m) ⁇ adayu ⁇ in ⁇ y ⁇ uyu ⁇ niches ⁇ uyu em ⁇ s ⁇ g ⁇ avi ⁇ atsi ⁇ nn ⁇ g ⁇ ⁇ s ⁇ yni ⁇ a 6 imeyuscheg ⁇ in d ⁇ nn ⁇ y chas ⁇ i v ⁇ dn ⁇ y ⁇ a ⁇ ub ⁇ 10, and in ve ⁇ ney chas ⁇ i l ⁇ vy sb ⁇ ni ⁇ v ⁇ ni ⁇ v ⁇ g ⁇ ⁇ i ⁇ a 11.
  • Settled particles form a solid component 22, a quick shut off down ⁇ i e ⁇ m navs ⁇ echu him vve ⁇ , dvizhe ⁇ sya lamina ⁇ ny ⁇ sus ⁇ enzii 23 of ⁇ g ⁇ ide ⁇ in ⁇ ensivn ⁇ e ⁇ sazhdenie vzveshennzh chas ⁇ its on na ⁇ l ⁇ nn ⁇ e dn ⁇ ⁇ anala 19.
  • Settling level in the accumulator bunker 26 is the random thickener 25 is turned through the small windows 11 (upper and lower), at the upper 17 installed sensors 18 switching on and off pump 12 pumping sediment from the accumulator bunker 26 of the transport thickener 25 ..

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  • Nitrogen And Oxygen Or Sulfur-Condensed Heterocyclic Ring Systems (AREA)
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Abstract

L'invention relève du domaine de triage hydraulique de matières à fractions fines se trouvant sous forme de particules libres dans un milieu liquide. Un mélange hydraulique initial pénètre dans un décanteur fonctionnant par gravité; le flux qui se déplace dans le tube d'admission s'élargit et pénètre dans les canaux d'une grille à labyrinthe où se produit une sédimentation intense des grosses particules. Le mélange hydraulique pénètre ensuite dans une cavité conique ouverte du décanteur fonctionnant par gravité qui possède dans sa partie de fond un tube de sortie et, dans sa partie supérieure, un collecteur à goulotte. Une sédimentation intensive des particules en phase solide en suspension a lieu dans les canaux de l'unité lamellaire du décanteur. Les particules entraînées par le flux du mélange hydraulique depuis le récipient conique du décanteur pénètrent dans le collecteur à goulotte d'où, sous l'effet de la gravité, elles sont acheminées dans l'épaississeur à couches minces. Les particules dont la vitesse de sédimentation est inférieure au débit du flux du mélange hydraulique à travers la section transversale de la base de l'épaississeur à couches minces arrivent dans un collecteur de type fermé, disposé dans la partie supérieure de l'épaississeur à couches minces d'où, sous l'effet de la gravité, elles sont acheminées dans le deuxième épaississeur à couches minces ou un récipient pour déchets hydrauliques.
PCT/RU2000/000315 2000-08-01 2000-08-01 Procede de triage hydraulique de matieres a fractions fines Ceased WO2002009881A1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AU2000270442A AU2000270442A1 (en) 2000-08-01 2000-08-01 Method for hydraulic classification of a fine-fractional material

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
RU2000120238/03A RU2174449C1 (ru) 2000-08-01 2000-08-01 Способ гидравлической классификации мелкофракционных материалов
RU2000120238 2000-08-01

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WO2002009881A1 true WO2002009881A1 (fr) 2002-02-07

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RU2248848C1 (ru) * 2003-10-27 2005-03-27 Читинский государственный технический университет (ЧитГТУ) Тонкослойный разделитель минеральных частиц
RU2320419C2 (ru) * 2006-05-03 2008-03-27 Юрий Яковлевич Гайтанов Способ гидроклассификации полидисперсных зернистых материалов, устройство для осуществления способа и установка для гидроклассификации полидисперсных зернистых материалов
RU2328347C2 (ru) * 2006-05-22 2008-07-10 ООО "Микросфера" Способ разделения ценосфер летучих зол тепловых электростанций
RU2385771C1 (ru) * 2009-04-08 2010-04-10 Государственное образовательное учреждение высшего профессионального образования Читинский государственный университет (ЧитГУ) Тонкослойный сепаратор полиминеральной гидровзвеси
RU2489214C1 (ru) * 2012-06-04 2013-08-10 Федеральное Государственное Автономное Образовательное Учреждение Высшего Профессионального Образования "Дальневосточный Федеральный Университет" (Двфу) Технологическая линия для переработки золошлаковых отходов - продуктов сжигания угольного топлива
RU2632081C1 (ru) * 2016-06-30 2017-10-02 Федеральное Государственное Автономное Образовательное Учреждение Высшего Профессионального Образования "Дальневосточный Федеральный Университет" (Двфу) Узел подготовки пульпы из золошлаковых отходов

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SU565682A1 (ru) * 1976-01-27 1977-07-25 Ulev Leonid P Отстойник
FR2344316A2 (fr) * 1974-09-18 1977-10-14 Huardeau Jacques Clarificateur-decanteur a flux oblique et a systeme de separation tubulaire, a plaques ou mixtes plaques et faisceaux
SU1282896A1 (ru) * 1985-04-30 1987-01-15 Всесоюзный Научно-Исследовательский И Проектно-Изыскательский Институт По Проблемам Добычи,Транспорта И Переработки Минерального Сырья В Промышленности Строительных Материалов Многопродуктовый гидравлический классификатор
EP0496916A1 (fr) * 1991-01-31 1992-08-05 Heiner Dipl.-Ing. Dr. Kreyenberg Méthode pour le traitement de dépôts
RU2033270C1 (ru) * 1992-12-07 1995-04-20 Михаил Иванович Хрусталев Обогатительный агрегат
RU2074340C1 (ru) * 1993-05-06 1997-02-27 Михаил Иванович Хрусталев Технологическая линия для гидравлического выделения золы и шлака из золошлаковых отходов
RU2140327C1 (ru) * 1998-06-08 1999-10-27 Деркачев Борис Павлович Способ обогащения мелкофракционных концентратов
RU2143952C1 (ru) * 1997-08-29 2000-01-10 ОАО Рудгормаш Способ доизвлечения полезных ископаемых из пульпопровода отходов обогащения минерального сырья и установка доизвлечения полезных компонентов из потока пульпы
RU2144430C1 (ru) * 1999-02-08 2000-01-20 Деркачев Борис Павлович Способ переработки минералосодержащей горной массы

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FR2344316A2 (fr) * 1974-09-18 1977-10-14 Huardeau Jacques Clarificateur-decanteur a flux oblique et a systeme de separation tubulaire, a plaques ou mixtes plaques et faisceaux
SU565682A1 (ru) * 1976-01-27 1977-07-25 Ulev Leonid P Отстойник
SU1282896A1 (ru) * 1985-04-30 1987-01-15 Всесоюзный Научно-Исследовательский И Проектно-Изыскательский Институт По Проблемам Добычи,Транспорта И Переработки Минерального Сырья В Промышленности Строительных Материалов Многопродуктовый гидравлический классификатор
EP0496916A1 (fr) * 1991-01-31 1992-08-05 Heiner Dipl.-Ing. Dr. Kreyenberg Méthode pour le traitement de dépôts
RU2033270C1 (ru) * 1992-12-07 1995-04-20 Михаил Иванович Хрусталев Обогатительный агрегат
RU2074340C1 (ru) * 1993-05-06 1997-02-27 Михаил Иванович Хрусталев Технологическая линия для гидравлического выделения золы и шлака из золошлаковых отходов
RU2143952C1 (ru) * 1997-08-29 2000-01-10 ОАО Рудгормаш Способ доизвлечения полезных ископаемых из пульпопровода отходов обогащения минерального сырья и установка доизвлечения полезных компонентов из потока пульпы
RU2140327C1 (ru) * 1998-06-08 1999-10-27 Деркачев Борис Павлович Способ обогащения мелкофракционных концентратов
RU2144430C1 (ru) * 1999-02-08 2000-01-20 Деркачев Борис Павлович Способ переработки минералосодержащей горной массы

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SVODNY TOM: "Khimiya", M., VINITI, no. 18(II), 1973, pages ABSTRACT NO. 18I311 *

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RU2174449C1 (ru) 2001-10-10

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