GB355211A - Improvements in the separation or concentration of solid substances by flotation - Google Patents

Improvements in the separation or concentration of solid substances by flotation

Info

Publication number
GB355211A
GB355211A GB4870/30A GB487030A GB355211A GB 355211 A GB355211 A GB 355211A GB 4870/30 A GB4870/30 A GB 4870/30A GB 487030 A GB487030 A GB 487030A GB 355211 A GB355211 A GB 355211A
Authority
GB
United Kingdom
Prior art keywords
emulsion
baffle
pipe
space
froth
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
GB4870/30A
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Publication of GB355211A publication Critical patent/GB355211A/en
Expired legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION 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
    • B03DFLOTATION; DIFFERENTIAL SEDIMENTATION
    • B03D1/00Flotation
    • B03D1/14Flotation machines
    • B03D1/1406Flotation machines with special arrangement of a plurality of flotation cells, e.g. positioning a flotation cell inside another
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION 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
    • B03DFLOTATION; DIFFERENTIAL SEDIMENTATION
    • B03D1/00Flotation
    • B03D1/14Flotation machines
    • B03D1/1412Flotation machines with baffles, e.g. at the wall for redirecting settling solids
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION 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
    • B03DFLOTATION; DIFFERENTIAL SEDIMENTATION
    • B03D1/00Flotation
    • B03D1/14Flotation machines
    • B03D1/1493Flotation machines with means for establishing a specified flow pattern
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION 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
    • B03DFLOTATION; DIFFERENTIAL SEDIMENTATION
    • B03D1/00Flotation
    • B03D1/14Flotation machines
    • B03D1/24Pneumatic
    • B03D1/242Nozzles for injecting gas into the flotation tank

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Biotechnology (AREA)
  • Physical Water Treatments (AREA)

Abstract

355,211. Concentrating ores. ELI•, A. D. J., Tananarive, Madagascar. Feb. 13, 1930, No. 4870. Convention date, March 29, 1929. [Class 82 (ii).] In concentrating ores, e.g. graphite, by flotation an emulsion is formed of gas, e.g. air, water or other liquid and a foaming agent, e.g. cresol, turpentine, tar or gasoline, and the emulsion is brought into contact with the ore pulp, which has been previously mixed with a selective agent, e.g. oil, in such a manner that a froth is formed without mechanical agitation. In an elongated vessel 1 is provided a liquidtight cylinder 8 with conical bottom 15 and top 10. The ore mixed with selective agent is introduced through a funnel 12 and passes down a channel 14 formed between the top 10 of the cylinder 8 and a conical extension 13 of the funnel into the annular space 9 between the vessel 1 and the cylinder 8 which constitutes an emulsion chamber, the emulsion containing the foaming agent being introduced into the bottom of the space 9 through a channel 40 formed by a conical baffle 25. The emulsion chamber 9 may be provided with projections or baffles 9a. The froth rises out of the space 9, is deflected inwards by a baffle 22, passes over the top of the baffle into the space 24 and is collected in an inclined trough 6. Liquid may be introduced into the space 23 below the baffle 22 to cause the overflow of the froth, or the froth may be removed by mechanical means, an overflow pipe 29 being provided. The tailings and the degasefied emulsion pass down from the space 9 through a passage 41 between the baffle 25 and a coaxial conical baffle 26 into a settling compartment and thence through an annular space 28 between the vessel 1 and the edge of an inverted conical hood 27 to a discharge outlet. Liquid or steam may be supplied through a pipe 3 to assist the evacuation of the tailings. The degasefied emulsion is withdrawn by suction through a pipe 19 opening under the hood 27 and passes to a pump 18 where it is again mixed with air or other gas and passed to the emulsion chamber through a pipe 17 opening in the channel 40. The pump is provided with a feed tube 20 for foaming agent and air and may have an additional tube 21 if compressed air or a gas other than air is used for the emulsion. In a modification, Fig. 3, the emulsion is made in the settling chamber. Compressed air or gas is supplied by a pipe 33 to a nozzle 34 and draws liquid containing foaming agent up a tube 31 surrounding the nozzle 34 and opening into the channel 40. Additional foaming agent may be supplied through a pipe 30. Several apparatus may be arranged in series, the froth from the first concentration being fed to the second apparatus and so on and, when the external emulsifying pump 18 is used, several separating vessels may be arranged round a common pump.
GB4870/30A 1929-03-29 1930-02-13 Improvements in the separation or concentration of solid substances by flotation Expired GB355211A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
FR355211X 1929-03-29

Publications (1)

Publication Number Publication Date
GB355211A true GB355211A (en) 1931-08-13

Family

ID=8893364

Family Applications (1)

Application Number Title Priority Date Filing Date
GB4870/30A Expired GB355211A (en) 1929-03-29 1930-02-13 Improvements in the separation or concentration of solid substances by flotation

Country Status (1)

Country Link
GB (1) GB355211A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2572778A1 (en) * 2011-09-23 2013-03-27 Siemens Aktiengesellschaft Dispenser nozzle, flotation machine with dispenser nozzle and method for its operation

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2572778A1 (en) * 2011-09-23 2013-03-27 Siemens Aktiengesellschaft Dispenser nozzle, flotation machine with dispenser nozzle and method for its operation
WO2013041343A1 (en) 2011-09-23 2013-03-28 Siemens Aktiengesellschaft Dispersion nozzle, flotation machine equipped therewith, and method for operating same

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