Classifications

• • C—CHEMISTRY; METALLURGY
  • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F1/00—Treatment of water, waste water, or sewage
  • C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
  • C02F1/461—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
  • C02F1/465—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electroflotation
• • 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
  • B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
  • B03D1/00—Flotation
  • B03D1/02—Froth-flotation processes
• • 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
  • B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
  • B03D1/00—Flotation
  • B03D1/14—Flotation machines
  • B03D1/1437—Flotation machines using electroflotation
• • 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
  • B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
  • B03D1/00—Flotation
  • B03D1/14—Flotation machines
  • B03D1/24—Pneumatic
  • B03D1/247—Mixing gas and slurry in a device separate from the flotation tank, i.e. reactor-separator type
• • 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
  • B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
  • B03D1/00—Flotation
  • B03D1/14—Flotation machines
  • B03D1/1412—Flotation machines with baffles, e.g. at the wall for redirecting settling solids
• • C—CHEMISTRY; METALLURGY
  • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F1/00—Treatment of water, waste water, or sewage
  • C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
  • C02F1/5236—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents
• • C—CHEMISTRY; METALLURGY
  • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F1/00—Treatment of water, waste water, or sewage
  • C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
  • C02F1/54—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using organic material
  • C02F1/56—Macromolecular compounds
• • C—CHEMISTRY; METALLURGY
  • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F2101/00—Nature of the contaminant
  • C02F2101/10—Inorganic compounds
  • C02F2101/20—Heavy metals or heavy metal compounds
• • C—CHEMISTRY; METALLURGY
  • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
  • C02F2103/32—Nature of the water, waste water, sewage or sludge to be treated from the food or foodstuff industry, e.g. brewery waste waters

Definitions

• the object of the invention is a method for purifying aqueous solutions or the like, where the component to be removed, for example in a dissolved or solid state, is converted to the solid phase, the said method including the addition of a precipitant, coagulating agents, and/or flocculating agents; the separation of larger solid particles from the suspension thus obtained by settling; and the removal of the remaining components from the suspension by electroflotation.
• the object of the invention also comprises an electroflotation device for purifying aqueous solutions or the like, consisting of a chamber, filling and discharge compartments, a foam removal device and electrode units in which the electrodes are parallel sheet elements, for carrying out the method relating to the invention.
• Known water purification methods include a purification process carried out by using coagulating and flocculating agents, where the reagents are introduced into the liquid to be purified in solution form, as disclosed in Finnish patent application no. 890493.
• Finnish patent no. 77 008 discloses a method for carrying out a purification process using coagulating agents, in which method coagulating agents are obtained through the anodic dissolution of aluminium sheets.
• US patent no. 4 156 648 discloses a solution for an apparatus for the utilisation of the above methods.
• the publication describes a process diagram and apparatus for treating water to remove grit by using centrifugal force to remove solid suspension particles, and coagulation and flocculation to sediment large flocculants and suspensions into a thin layer in a sedimentation basin. Saturation with a gas is followed by foaming with a gas in connection with pressurization and simultaneous oxidization of organic matter with ozone introduced into the flotation tank.
• the aim and object of the present invention is to achieve a new method and device for eliminating the disadvantages of the above-mentioned known purification processes, making the process more efficient and increasing the suspension separation capacity.
• the suspension is saturated in a turbulence process with the bubbles of electrolytic gases, the density of the electric current exceeding 20 mA/cm 2 , and
• the foam is separated by the laminar flow of a liquid, the density of the electric current being below 20 mA/cm 2 .
• a precipitant is added to the aqueous solution, the said precipitant being a substance that dissolves in water or a fine sorbent or a combination of these.
• Suitable dissolving precipitants include saline solutions such as iron oxide sulphates which, together with the component to be removed, form components insoluble in water.
• Activated carbon for example, is a suitable sorbent.
• a gas saturation chamber in which is mounted an electrode unit for saturating the suspension with the gas released during the electrolysis
• a suspension flow suppressor of a multicellular structure mounted above the electrode unit in the flotation compartment, and - an adjustable separating wall installed between the gas saturation chamber and the flotation compartment.
• a method and device are achieved which can be used for purifying the wastewaters of foodstuff, chemical, varnish and paint production plants, or for treatment of the technical solutions from mining chemistry and metallurgical plants, these solutions containing small amounts of useful recoverable components and, for example, heavy metal salts.
• Figure 1 shows the purification method relating to the invention as a block diagram
• Figure 2 shows diagrammatically the purification process of figure 1 and the purification device relating to the invention
• Figure 3 shows a cross-sectional view of the electroflotation device relating to figure 2, along line A-A and as seen from above.
• Figure 1 shows the purification method relating to the invention as a block diagram.
• the method for purifying water and technical solutions of different types of dissolved and solid components is carried out as follows: to the flow of water or a technical solution is added a saline solution acting as a precipitant, which together with the component to be removed forms insoluble components which settle as a sediment.
• fine-dispersed sorbent can be added to the mixture, the said sorbent sorbing the compound to be separated from the aqueous solution or the ion of a useful component.
• the suspension formed is treated with coagulating and flocculating agents. Solid suspensions are removed by precipitation and settling, and the fine- dispersed solid phase is removed by electrofoaming, that is, electroflotation.
• the electroflotation process is carried out in two stages combined in the same device.
• the suspension is saturated with the bubbles of electrolytic gases which are separated in the turbulence process of the suspension being purified, due to the high density of the electric current which is well in excess of 20 mA/cm 2 .
• the foam is separated in the foaming compartment of the chamber, the laminar flow of the liquid and the density of the electric current being minimal, significantly below 20 mA/cm 2 .
• FIG 2 shows diagrammatically the purification process of figure 1 and the structure of the purification device relating to the invention, by means of which the method shown in figure 1 is carried out.
• the purification device used in the purification process consists basically of reagent dosage units 1, 2 and 3, a mixer 4, a clarifier 5, tank spaces 6 and 7, a clarifier and sedimenter 9, an electroflotation device 10, a foam removal device 22, and a foam separator 23.
• a filling compartment 11 In the chamber 30 of the electroflotation device 10 is built a filling compartment 11, a gas saturation chamber 12 and a flotation compartment 15.
• the gas saturation space 12 is separated from the foaming or flotation compartment 15 by means of a separating wall 16.
• a suspension flow suppressor 17 In the flotation compartment 15 is mounted a suspension flow suppressor 17 built as a multicellular structure.
• the lower part of the discharge device 21 for purified liquid is separated from the lower part of the flotation compartment 15 by means of a separating wall 20.
• the vertically movable shutter flap 24 in the top part of the discharge device 21 regulates the area of the liquid to be purified in the electroflotation device 10.
• the electrode units 13 and 18 of the gas generators are built in the form of groups of flat parallel sheets, which are mounted in the vertical plane with respect to the direction of flow of the liquid, above the bottom of the electroflotation device 10.
• Power supply from the power source to the electrode units 13 and 18 is by current conductors fastened to rails 14 and 19.
• the current supplied from the power source is pulsating, as a result of which the polarisation of the electric current can be inverted.
• the aim is to prevent the premature passivation of the electrodes and to achieve an even, efficient generation of gas.
• the material used for the sheet-like electrodes is, for example, stainless steel, which is a virtually insoluble material. Commonly used electrodes made from other corrosion-resistant materials, such as platinum, acid-resistant steel or platinated titanium, can also be used.
• the purification of aqueous or technical solutions takes place as follows: wastewater is fed into the mixer 4; at the same time fine-dispersed sorbent and/or saline solution, and/or coagulating and flocculating agents precipitating the component to be removed are fed alternately into the clarifier 5 and tank spaces 6 and 7 from the reagent dosage units 1, 2 and 3.
• the suspension formed is mixed in the mixer 4 by means of compressed air supplied along feeder line 8, through the perforated hose fixed on the bottom of the mixer 4.
• the pretreated suspension is fed into the sedimenter 9 in which solid suspension parts and large flocculants are separated from it and removed in stages through the bottom of the sedimenter 9. If necessary, more coagulating and flocculating agents can be fed from the dosage units 2 and 3 into the sedimenter 9.
• the suspension From the sedimenter 9 the suspension, from which the largest particles have already been separated, is fed with its components to be removed, dissolved and/or fine- dispersed components, into the receiving compartment 11 of the chamber 30 of the electroflotation device 10. From there the suspension solution passes from the spaces between the sheets of the electrode unit 13 into the gas saturator 12. In the gas saturator 12, the electrodes of the electrode unit 13 are partly or completely immersed in the liquid. The first stage of the process, that is, the intensive release of gas takes place in the electrodes 13 of the gas saturator 12, the gas bubbles rising above the electrode unit 13 creating strong turbulence in the liquid.
• the adjustable separating wall 16 separating the gas saturator 12 and the flotation compartment 15 from each other, essentially adjustable by 1/3 - 5/6, partly prevents the discharge of foam from the gas saturator 12. In space 12 the turbulence of the suspension flow intensifies when the discharge duct is completely or partly closed by the inclined, adjustable separating wall 16.
• the suspension saturated with the bubbles of the electrolysis gases is led to the flotation compartment 15 of the electroflotation device 10.
• the so-called basic mass of the suspension rises to the surface of the liquid after the treatment of the suspension in the gas saturator 12 and the solid particles remaining in the suspension move into the foam due to the gas bubbles created in the electrode unit 18 of the flotation compartment 15.
• the flow of the suspension in the flotation compartment 15 is laminar flow and the densities of the electric current are lower than in the gas saturator 12.
• the laminarity of the suspension flow is guaranteed by suppressor gratings 17 mounted above the electrode unit 18.
• the foam deposited on the surface of the liquid is removed from the process by the vacuum foam remover 22 which removes periodically downstream and upstream the top surface of the foam, which has a low water content.
• the periodic nature of the foam removal is regulated by the operating frequency of the foam removal device 22.
• the solid components are separated from the foam by means of a vacuum, with a foam separator 23.
• From the flotation compartment the water - from which solid components have been removed as described above - discharges completely or partly through the spaces in the electrode unit 18 in the liquid and through the discharge device 21.
• the discharge device 21 is equipped with a suspension flow separator 20 which prevents the entry of solid components into the purified liquid flow discharging from the electroflotation device 10.
• the height of the suspension surface level is regulated by means of a shutter flap 24.
• Figure 3 shows a cross-sectional view of the electroflotation device 10 relating to figure 2, along line A-A and as seen from above.
• the suspension from which the largest particles have been removed, is fed with the components to be removed into the filling compartment 11 of the electroflotation device 10.
• the suspension liquid passes through the spaces between the sheets of the electrode unit into the gas saturator 12.
• the gas bubbles released from the electrode unit create strong turbulence in the solution.
• the turbulence of the suspension flow intensifies when the discharge duct is partly closed with the inclined separating wall 16.
• the suspension saturated with the bubbles of the electrolysis gases is led to the flotation compartment 15.
• the so-called basic mass of the suspension rises to the surface of the liquid after the treatment of the suspension in the gas saturator 12 and the solid particles remaining in the suspension pass into the foam due to the gas bubbles created in the electrode unit of the flotation compartment 15.
• the flow of the suspension is laminar flow and the densities of the electric current are lower than in the gas saturator 12.
• the laminarity of the suspension flow is guaranteed by suppressor gratings 17 mounted above the electrode unit.
• the purified water is discharged through the sheets in the electrode unit and through the discharge device 21.
• the discharge device 21 is equipped with a suspension flow separator which prevents the entry of solid components into the purified liquid flow discharging from the electroflotation device 10.
• the height of the suspension surface level is regulated by means of a shutter flap 24.
• the purification method and device relating to the invention were used to purify the wastewaters of a meat-processing plant.
• the plant's wastewater was fed into the mixer 4, the water containing, for example, 750 mg/1 of suspension, 44 mg/1 of common phosphorus, the biological oxygen demand (BOD) of the wastewater being 1000 mg 0 2 /l.
• BOD biological oxygen demand
• From dosage unit 1 was fed iron oxide sulphate solution in the amount of 120 g/m 3 , including salt, which acted as the precipitant for phosphorus.
• From dosage unit 2 was fed aluminium sulphate coagulating agent solution in the amount of 30 g/m 3 , and from dosage unit 3 flocculating agent solution, polyacryl amide, in the amount of 4 g/m 3 .
• the suspension formed in the mixer 4 was fed into the sedimenter 9, where the solid suspension settled on the bottom and was removed. From the sedimenter 9 the suspension containing the components to be removed was conducted to the electrcrflotation device 10, in which the saturation of the suspension with the gas bubbles released in the electrolysis took place in the saturation space 12, the density of the electric current being 40 mA/cm 2 . The solid phase part rose onto the surface of the suspension immediately on being discharged from the gas saturator 12.
• the suspension was further led to the flotation compartment 15, where the final purification of the wastewater took place, the density of the electric current being 10 mA/cm 2 .
• the purified water was removed from the device through discharge device 21.
• the waste material collected in the foam in the flotation compartment and was removed by the foam removal device 22 as necessary.
• the foam yield did not exceed 8.0% and its solid phase content was 2.2%. Measurements gave the following specific values for the purified water:
• the degree of purification was 93% when calculated on the basis of the suspended components, and 96% when calculated on the basis of phosphorus.
• the purification method and device relating to the invention were used for purifying oil-containing wastewaters.
• the oil-containing starting wastewater containing 360 mg of oil/1, was fed into a mixer 4, into which was also dosed, in consecutive order, finely ground activated carbon in the amount of 500 g/m 3 , aluminium sulphate coagulating agent in the amount of 50 g/m 3 , and polyacryl amide flocculating agent in the amount of 2 g/m 3 .
• the suspension was fed into the electroflotation device 10 in which gas saturation was carried out with the density of the electric current being 40 mA/cm 2 , and foaming with the density of the electric current being 8 mA/cm 2 .
• Foam yield was between 0.7 - 1.2%.
• the purification method and device were used for purifying the wastewaters of a leather manufacturing plant of chromium and other suspended substances.
• the wastewaters of the leather manufacturing plant contained 480 mg/1 of suspended substances, 230 mg/1 of sulphides, 160 mg/1 of common chromium, and the BOD was 1280 mg 0 2 /l.
• the wastewater was fed into the mixer 4, into which was dosed 280 g/m 3 iron monoxide sulphate to sediment the sulphides and to regenerate the chromium ions.
• aluminium sulphate coagulating agent and polyacryl amide flocculating agent in the respective amounts of 100 g/m 3 and 4 g/m 3 .
• the suspension thus pre-prepared was fed into the sedimentation tank 9, and after the sedimentation tank 9 the discharged material was led to the electroflotation device.
• the solid phase of the suspension was separated in the gas saturator 12 with the density of the electric current being 30 mA/cm 2 , and in the flotation compartment 15 with the density being 8 mA/cm 2 .
• the purified water contained 35 mg/1 of suspended substances, less than 2.0 mg/1 of sulphides, less than 0.1 mg/1 of common chromium, and the BOD was 240 mg 0 2 /l.
• the purification method and device relating to the invention were used for removing heavy metal ions from the wastewaters of a refinery and/or chemical plant.
• the starting solution contained 0.7 mg/1 of silver, 4.8 mg/1 of lead and 21 mg/1 of copper.
• Sodium sulphide in the amount of 35 g/m 3 was used as precipitant.
• the fine-dispersed heavy metal sulphide sediment settled on the bottom of the suspension tank was flocculated with polyacryl amide having a content of 1.0 g/m 3 .
• the removal of the solid phase from the suspension was carried out in the gas saturator 12 with the density of the electric current being 20 mA/cm 2 , and in the flotation compartment 15 with the density of the electric current being 5 mA/cm 2 .
• the foam yield was 0.05%.

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• Engineering & Computer Science (AREA)
• Life Sciences & Earth Sciences (AREA)
• Environmental & Geological Engineering (AREA)
• Water Supply & Treatment (AREA)
• Biotechnology (AREA)
• Chemical & Material Sciences (AREA)
• Chemical Kinetics & Catalysis (AREA)
• Electrochemistry (AREA)
• General Chemical & Material Sciences (AREA)
• Hydrology & Water Resources (AREA)
• Organic Chemistry (AREA)
• Water Treatment By Electricity Or Magnetism (AREA)
• Physical Water Treatments (AREA)

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Cited By (4)

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Citations (4)

• 1992
  • 1992-11-17 FI FI925204A patent/FI95234C/fi not_active IP Right Cessation
• 1993
  • 1993-11-17 WO PCT/FI1993/000485 patent/WO1994011308A1/en active Application Filing
  • 1993-11-17 AU AU54672/94A patent/AU5467294A/en not_active Abandoned

Patent Citations (4)

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