SE452121B - FLOTATIONSANLEGGNING - Google Patents
FLOTATIONSANLEGGNINGInfo
- Publication number
- SE452121B SE452121B SE8202540A SE8202540A SE452121B SE 452121 B SE452121 B SE 452121B SE 8202540 A SE8202540 A SE 8202540A SE 8202540 A SE8202540 A SE 8202540A SE 452121 B SE452121 B SE 452121B
- Authority
- SE
- Sweden
- Prior art keywords
- cell
- foam
- air
- liquid
- cells
- Prior art date
Links
- 239000006260 foam Substances 0.000 claims abstract description 36
- 239000007788 liquid Substances 0.000 claims abstract description 21
- 238000005188 flotation Methods 0.000 claims description 7
- 239000000356 contaminant Substances 0.000 claims description 5
- 230000003134 recirculating effect Effects 0.000 claims description 4
- 230000000694 effects Effects 0.000 claims description 2
- 239000012530 fluid Substances 0.000 claims description 2
- 238000005273 aeration Methods 0.000 claims 2
- 230000015572 biosynthetic process Effects 0.000 claims 1
- 238000007664 blowing Methods 0.000 claims 1
- 238000002347 injection Methods 0.000 claims 1
- 239000007924 injection Substances 0.000 claims 1
- 239000002245 particle Substances 0.000 claims 1
- 230000001105 regulatory effect Effects 0.000 claims 1
- 239000007787 solid Substances 0.000 claims 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 5
- 238000000034 method Methods 0.000 abstract description 3
- 239000000203 mixture Substances 0.000 abstract description 2
- 239000005995 Aluminium silicate Substances 0.000 abstract 1
- 235000012211 aluminium silicate Nutrition 0.000 abstract 1
- 239000012535 impurity Substances 0.000 abstract 1
- NLYAJNPCOHFWQQ-UHFFFAOYSA-N kaolin Chemical compound O.O.O=[Al]O[Si](=O)O[Si](=O)O[Al]=O NLYAJNPCOHFWQQ-UHFFFAOYSA-N 0.000 abstract 1
- 238000011084 recovery Methods 0.000 abstract 1
- 238000004064 recycling Methods 0.000 abstract 1
- 239000000725 suspension Substances 0.000 description 5
- 239000002699 waste material Substances 0.000 description 4
- 238000000746 purification Methods 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- 239000000835 fiber Substances 0.000 description 2
- 210000002837 heart atrium Anatomy 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 239000000956 alloy Substances 0.000 description 1
- 229910045601 alloy Inorganic materials 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000004088 foaming agent Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000007689 inspection Methods 0.000 description 1
- 239000010899 old newspaper Substances 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
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
- C02F1/24—Treatment of water, waste water, or sewage by flotation
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21B—FIBROUS RAW MATERIALS OR THEIR MECHANICAL TREATMENT
- D21B1/00—Fibrous raw materials or their mechanical treatment
- D21B1/04—Fibrous raw materials or their mechanical treatment by dividing raw materials into small particles, e.g. fibres
- D21B1/12—Fibrous raw materials or their mechanical treatment by dividing raw materials into small particles, e.g. fibres by wet methods, by the use of steam
- D21B1/30—Defibrating by other means
- D21B1/32—Defibrating by other means of waste paper
- D21B1/325—Defibrating by other means of waste paper de-inking devices
- D21B1/327—Defibrating by other means of waste paper de-inking devices using flotation devices
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D19/00—Degasification of liquids
- B01D19/02—Foam dispersion or prevention
-
- 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
-
- 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
- B03D1/02—Froth-flotation processes
- B03D1/028—Control and monitoring of flotation processes; computer models therefor
-
- 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
- B03D1/1406—Flotation machines with special arrangement of a plurality of flotation cells, e.g. positioning a flotation cell inside another
-
- 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
- B03D1/1418—Flotation machines using centrifugal forces
-
- 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
- B03D1/1443—Feed or discharge mechanisms for flotation tanks
- B03D1/1456—Feed mechanisms for the slurry
-
- 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
- B03D1/1443—Feed or discharge mechanisms for flotation tanks
- B03D1/1462—Discharge mechanisms for the froth
-
- 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
- B03D1/1443—Feed or discharge mechanisms for flotation tanks
- B03D1/1475—Flotation tanks having means for discharging the pulp, e.g. as a bleed stream
-
- 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
- B03D1/1487—Means for cleaning or maintenance
-
- 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
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21F—PAPER-MAKING MACHINES; METHODS OF PRODUCING PAPER THEREON
- D21F1/00—Wet end of machines for making continuous webs of paper
- D21F1/66—Pulp catching, de-watering, or recovering; Re-use of pulp-water
- D21F1/70—Pulp catching, de-watering, or recovering; Re-use of pulp-water by flotation
-
- 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
- C02F2103/26—Nature of the water, waste water, sewage or sludge to be treated from the processing of plants or parts thereof
- C02F2103/28—Nature of the water, waste water, sewage or sludge to be treated from the processing of plants or parts thereof from the paper or cellulose industry
-
- 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
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/64—Paper recycling
Landscapes
- Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Biotechnology (AREA)
- Chemical & Material Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Organic Chemistry (AREA)
- Wood Science & Technology (AREA)
- Mechanical Engineering (AREA)
- Dispersion Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Engineering & Computer Science (AREA)
- Paper (AREA)
- Physical Water Treatments (AREA)
- Apparatus Associated With Microorganisms And Enzymes (AREA)
Abstract
Description
452 121 Vid en sådan flotationsanläggning utgör separering av de skum innehållande föroreningarna från den renade vätskan en viktig funktion, eftersom om denna icke sker på adekvat sätt, anläggningen icke kommer att arbeta effektivt och medföra svårigheter till följd av själva skummets natur. Företagna prov har därvid givit vid han- den att man bör undvika användning av på mekanisk väg rör- lig utrustning för behandling av skummet. In such a flotation plant, separation of the foams containing the contaminants from the purified liquid is an important function, because if this is not done adequately, the plant will not work efficiently and cause difficulties due to the nature of the foam itself. Tests carried out have suggested that the use of mechanically movable equipment for treating the foam should be avoided.
US-A-3.523.891 (Mehl) beskriver en anordning för att avlägsna skum som flyter vid vätskeytan i en rektangulär cellkammare vilken är indelad av med avstånd anordnade elektrodplattor som tillförsäkrar en sinusformad bana för vätskan.US-A-3,523,891 (Mehl) discloses a device for removing foam floating at the liquid surface in a rectangular cell chamber which is divided by spaced apart electrode plates which ensure a sinusoidal path for the liquid.
SE-B-7114902-5 (Degremont, publ. nr. 381.410) be- skriver en flotationstank som använder en vätska vilken är mättad med en gas under tryck för att behandla ytter- ligare en vätska som skall renas. De båda vätskorna in- föres i en förkammare anordnad vid flotationstankens botten, varvid förkammaren är öppen i anslutning till tanken. Behandlingsvätskan insprutas i förkammaren genom ett rör och tvingas i en horisontell ström för att i största möjliga utsträckning hindras från att alltför tidigt bringas i kontakt med vätskan som behandlas, vil- ken införes i riktning vertikalt uppåt. Förkammarens an- slutning vid vätskans behandling anges vara "icke tangen- tiell". vätskan kommer därvid icke att följa ett generellt cirkulärt strömningsmönster omkring cellens axel.SE-B-7114902-5 (Degremont, Publ. No. 381,410) describes a flotation tank which uses a liquid which is saturated with a gas under pressure to treat another liquid to be purified. The two liquids are introduced into an antechamber arranged at the bottom of the flotation tank, the antechamber being open adjacent to the tank. The treatment liquid is injected into the atrium through a tube and forced into a horizontal flow in order to prevent as far as possible from being brought into contact too early with the liquid being treated, which is introduced in a vertical upward direction. The connection of the atrium to the treatment of the fluid is stated to be "non-tangential". the liquid will then not follow a generally circular flow pattern around the axis of the cell.
Ett ändamål med uppfinningen är att åstadkomma en förbättrad anläggning vilken med undvikande av angiven mekanisk utrustning medger effektiv separering av skum innehållande föroreningar från renad vätska.An object of the invention is to provide an improved plant which, while avoiding the stated mechanical equipment, allows efficient separation of foams containing contaminants from purified liquid.
Anläggningen enligt uppfinningen är av inlednings- vis angivet slag och kännetecknas väsentligen av att in- loppet befinner sig i nedre delen av cellen och är tangen- tiellt riktat mot dennas yttervägg för bildning av ett väsentligen cirkulärt strömningsmönster hos den inkommande 452 121 vätskan omkring cellens axel, och att skumutloppet inne- fattar ett axiellt avgångsrör i cellen, vilket leder genom cellens botten och sträcker sig till skumskiktet.The plant according to the invention is of an initially stated type and is characterized essentially in that the inlet is located in the lower part of the cell and is tangentially directed towards its outer wall to form a substantially circular flow pattern of the incoming liquid around the axis of the cell. , and that the foam outlet comprises an axial outlet tube in the cell, which leads through the bottom of the cell and extends to the foam layer.
Uppfinningen åstadkommer effektiv behandling av skummet utan användning av rörliga delar för ändamålet.The invention provides effective treatment of the foam without the use of moving parts for the purpose.
Recirkulationsorganen kan lämpligen innefatta ett axiellt i avgångsröret i cellen anordnat rör med en öppen ände exponerad för den med skum bemängda luften till nämnda avgångsrör och vid sin motstående ände i förbin- delse med sugorganen.The recirculation means may suitably comprise a pipe arranged axially in the outlet pipe in the cell with an open end exposed to the foam-laden air to said outlet pipe and at its opposite end in connection with the suction means.
Anläggningen innefattar vidare lämpligen ett antal celler vilka är inrättade att staplas koaxiellt den ena på den andra med kommunicerande avgângsrör.The plant further suitably comprises a number of cells which are arranged to be stacked coaxially one on top of the other with communicating outlet pipes.
Ytterligare kännetecken för och närmare detaljer i samband med uppfinningen kommer att framgå av nedanstående beskrivning av en anläggning som hänvisar till bifogade ritningar. På dessa visas endast som exempel en utförings- form av uppfinningen, som är speciellt lämpad för avfärg- ning av pappersmassa som framställts av gamla tidningar.Further features and further details in connection with the invention will appear from the following description of a plant which refers to the accompanying drawings. These show only by way of example an embodiment of the invention, which is particularly suitable for decolorizing pulp produced from old newspapers.
Fig. 1 är en schematisk sidovy av en av flera våningar bestående anläggning.Fig. 1 is a schematic side view of a multi-storey facility.
Fig. 2 är ett horisontalsnitt utmed linjen II-II i fig. 1.Fig. 2 is a horizontal section along the line II-II in Fig. 1.
Anläggningen innefattar fyra flotationsceller 1, 2, 3, 4. Dessa celler är ringformade och axiellt överlagrade den ena på den andra, så att de bildar fyra steg eller nivåer i ett torn med ett antal bottnar eller golv 5. Det är uppenbart att tornet kan ha ett antal steg som skiljer sig från fyra.The plant comprises four flotation cells 1, 2, 3, 4. These cells are annular and axially superimposed on each other, so that they form four steps or levels in a tower with a number of bottoms or floors 5. It is obvious that the tower can have a number of steps that differ from four.
Den defibrerade, kemiskt förbehandlade pappersmassan i form av en fibrös suspension innehållande ett skumnings- medel avges medelst en pump 6 via ett rör 7 till cellens 1 inlopp 11a, varvid den först passerar en blandningskammare 8. Denna kammare har en trång passage, i vilken den fibrösa suspensionen cirkulerar i form av ett tunt skikt, samtidigt som luft tillföres till densamma tvärs skiktets rörelseväg 452 121 utmed en del av denna genom ett rör 9 som är förenat med en lufttryckskälla (icke visad) via en ventil 10.The defibrated, chemically pretreated pulp in the form of a fibrous suspension containing a foaming agent is delivered by means of a pump 6 via a tube 7 to the inlet 11a of the cell 1, whereby it first passes a mixing chamber 8. This chamber has a narrow passage in which it the fibrous suspension circulates in the form of a thin layer, at the same time as air is supplied to the same transverse movement path 452 121 along a part thereof through a tube 9 which is connected to an air pressure source (not shown) via a valve 10.
Blandningskammaren 8 står i förbindelse med den ringformade cellen 1 genom ett rör 11 som leder tangen- tiellt in i cellens cylindriska vägg nära dess golv 5, så att den fibrösa suspensionen bringas att cirkulera om- kring den ringformade cellens centrala rör 12. De bubblor som skapas i suspensionen fastnar på föroreningarna och bringar dessa att stiga till ytan i form av skum. Detta föres ut ur cellen via rörets 12 utlopp 18, delvis till följd av suspensionens virvelrörelse och delvis av en luftström som alstras över desamma. En vertikal platta som är anordnad över massans nivå styr skummet till utloppet.The mixing chamber 8 communicates with the annular cell 1 through a tube 11 which leads tangentially into the cylindrical wall of the cell near its floor 5, so that the fibrous suspension is caused to circulate around the central tube 12 of the annular cell 12. created in the suspension adheres to the contaminants and causes them to rise to the surface in the form of foam. This is carried out of the cell via the outlet 18 of the tube 12, partly due to the vortex movement of the suspension and partly due to a stream of air generated over them. A vertical plate arranged above the level of the pulp guides the foam to the outlet.
Skummet uppsamlas i ett kärl 13 som omger röret 12 och av- går i en avfallstank 37 som är fylld med vatten. Luft- strömmen för avgivning av skummet införes i cellens över- del genom ett rör 14 som är anslutet till en vakuumsug 15, vilken befinner sig över ett stympat koniskt axiellt rör 16 för recirkulering av luften som bringar skummet att av- gå. Detta rör är anordnat koncentriskt i det centrala av- gångsröret 12 för skum och är gemensamt för samtliga över- lagrade celler. Luften som avger skummet inkommer i cellen via öppningen 17 och lämnar denna genom utloppet 48 medfö- rande skummet, vilket under inverkan av tyngdkraften ned- faller i kärlet 13, under det att luften avgår genom röret 16. Det sistnämnda sträcker sig in i intilliggande cell 2 under bildning av en kon, som avsmalnar uppåt och är riktad mot det vidare röret för recirkulering av luften som åstad- kommer avgivning av skummet till sagda intilliggande cell samt till övriga celler 3, 4. De delar som utgör röret 16 bildar en cyklon, och ger sålunda skummet en virvlande rörelse, vilket medger separering av luft som insugits i röret under inverkan av suganordningen 15, då den återgår till röret 14 för att åter användas för avgivning av skum.The foam is collected in a vessel 13 surrounding the tube 12 and discharges into a waste tank 37 which is filled with water. The air stream for dispensing the foam is introduced into the upper part of the cell through a tube 14 which is connected to a vacuum suction 15, which is located over a frustoconical axial tube 16 for recirculating the air which causes the foam to escape. This tube is arranged concentrically in the central outlet tube 12 for foam and is common to all superimposed cells. The air discharging the foam enters the cell via the opening 17 and leaves it through the outlet 48 carrying the foam, which under the influence of gravity falls into the vessel 13, while the air exits through the tube 16. The latter extends into the adjacent cell 2 while forming a cone, which tapers upwards and is directed towards the further pipe for recirculation of the air which causes the foam to be delivered to said adjacent cell and to the other cells 3, 4. The parts constituting the pipe 16 form a cyclone, and thus gives the foam a swirling movement, which allows separation of air sucked into the tube under the action of the suction device 15, when it returns to the tube 14 to be used again for dispensing foam.
Massan som är delvis renad i cell 1 lämnar den sist- nämnda via ett rör 19 försett med en pump 20 som medger en ökning av trycket. Röret 19 ingår i blandningskammaren 452 121 till påföljande cell 4 belägen i tornets sista steg, och den process som äger rum är identisk med den som utnytt- jas i den första cellen liksom fallet är i övriga celler.The mass which is partially purified in cell 1 leaves the latter via a pipe 19 provided with a pump 20 which allows an increase in the pressure. The tube 19 is included in the mixing chamber 452 121 of the subsequent cell 4 located in the last stage of the tower, and the process that takes place is identical to that used in the first cell as is the case in the other cells.
Dessa matas successivt med massan eller vatten som inne- håller fibrer med ökande renhetsgrad, under det att skum- met som uppsamlas i övriga celler i sin tur recirkuleras till den lägre cellen.These are successively fed with the pulp or water containing fibers of increasing purity, while the foam collected in the other cells is in turn recycled to the lower cell.
Skummet som innehåller avfallet från den första cellen och övriga celler kan naturligtvis antingen re- cirkuleras eller avges vid varje steg för behandling i en separat anordning i beroende av för vilken produkttyp massan är avsedd.The foam containing the waste from the first cell and other cells can, of course, either be recycled or dispensed at each step for treatment in a separate device depending on the product type of pulp.
Anläggningen innefattar även ett lock 40 som för- sluter cellen i det första steget; ett inspektionsfönster 41 som medger snabb tömning för åstadkommande av rening, en tömningsventil 42 till varje cell, en klaff 46 i luft- röret för transport av skum, ett golv eller en botten 43 i röret T2 för att uppta recirkulerat avfallsmaterial, ett rör 44 för avgivning av detta avfallsmaterial i cell 1, och ett rör för avgivning av accepterad massa i cellen 2 som behandlar den mest höggradigt renade massan.The plant also includes a lid 40 that closes the cell in the first stage; an inspection window 41 which allows rapid emptying to effect purification, an emptying valve 42 to each cell, a flap 46 in the air tube for transporting foam, a floor or a bottom 43 in the tube T2 for receiving recycled waste material, a tube 44 for dispensing this waste material into cell 1, and a tube for dispensing accepted pulp into cell 2 which processes the most highly purified pulp.
Den beskrivna uppfinningen avser en anläggning för avfärgning av pappersmassa. Den kan användas för andra ändamål, exempelvis rening av legeringar eller för rening av fiberbemängt vatten genom flotation av fibrer.The described invention relates to a plant for decolorizing pulp. It can be used for other purposes, for example purification of alloys or for purification of fiber-laden water by flotation of fibers.
Det står klart att uppfinningen icke är begränsad till den utföringsform som ovan beskrivits och illustreras på ritningarna utan att många modifikationer kan göras med avseende på utformning, arrangemang och sammansättning av vissa ingående element utan att uppfinningens grundtanke frångâs. Uppfinningen avser sålunda allaltänkbara modifi- kationer-inom ramen för dess grundtanke sådan denna defi- nieras av bifogade patentkrav.It is clear that the invention is not limited to the embodiment described above and illustrated in the drawings without many modifications being made to the design, arrangement and composition of certain constituent elements without departing from the spirit of the invention. The invention thus relates to all conceivable modifications - within the scope of its basic idea as defined by the appended claims.
Claims (7)
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
BE166085A BE840662A (en) | 1976-04-12 | 1976-04-12 | METHOD AND INSTALLATION FOR THE REMOVAL BY FLOTATION OF IMPURITIES IN THE FORM OF SOLID PARTICLES, CONTAINED IN A LIQUID |
Publications (2)
Publication Number | Publication Date |
---|---|
SE8202540L SE8202540L (en) | 1982-04-22 |
SE452121B true SE452121B (en) | 1987-11-16 |
Family
ID=3842869
Family Applications (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
SE7704203A SE425145B (en) | 1976-04-12 | 1977-04-12 | KIT AND PLANT TO AVOID MEDIUM FLOTATION POLLUTANTS IN THE FORM OF SOLID PARTICLES IN LIQUID |
SE8202540A SE452121B (en) | 1976-04-12 | 1982-04-22 | FLOTATIONSANLEGGNING |
Family Applications Before (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
SE7704203A SE425145B (en) | 1976-04-12 | 1977-04-12 | KIT AND PLANT TO AVOID MEDIUM FLOTATION POLLUTANTS IN THE FORM OF SOLID PARTICLES IN LIQUID |
Country Status (13)
Country | Link |
---|---|
JP (2) | JPS52124273A (en) |
AT (1) | AT358499B (en) |
BR (1) | BR7702266A (en) |
CA (1) | CA1096515A (en) |
CH (1) | CH614636A5 (en) |
DE (2) | DE2712947C2 (en) |
ES (1) | ES458029A1 (en) |
FI (1) | FI68093C (en) |
FR (2) | FR2347984A1 (en) |
GB (1) | GB1570345A (en) |
IT (2) | IT1073184B (en) |
NL (2) | NL180076C (en) |
SE (2) | SE425145B (en) |
Families Citing this family (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4157952A (en) * | 1978-03-24 | 1979-06-12 | Lenox Institute For Research | Apparatus for deinking waste paper pulp |
DE2836496C2 (en) * | 1978-08-21 | 1982-05-13 | E. & M. Lamort S.A., 51300 Vitry-le-François, Marne | Process and device for deinking pulp suspensions |
DE3111506C2 (en) * | 1981-03-24 | 1986-01-09 | Bergwerksverband Gmbh, 4300 Essen | Gas injection device for flotation systems |
DE3127290C2 (en) * | 1981-07-10 | 1986-10-30 | J.M. Voith Gmbh, 7920 Heidenheim | Flotation device for processing waste paper |
DE3320125A1 (en) * | 1983-06-03 | 1984-12-06 | J.M. Voith Gmbh, 7920 Heidenheim | METHOD AND DEVICE FOR PROCESSING WASTE PAPER |
US4613430A (en) * | 1984-01-30 | 1986-09-23 | Miller Francis G | Froth flotation separation method and apparatus |
AU3762285A (en) * | 1984-01-30 | 1985-08-08 | Miller, F.G. | Flotation separation apparatus and method |
DE3723502A1 (en) * | 1987-07-16 | 1989-01-26 | Henkel Kgaa | METHOD FOR FLOTATION OF FILLERS FROM WASTE PAPER |
DE3918025A1 (en) * | 1989-06-02 | 1990-12-06 | Bergwerksverband Gmbh | FLOTATION APPARATUS |
FR2772399B1 (en) * | 1997-12-15 | 2000-02-11 | Lamort E & M | PROCESS FOR DEINKING PAPER PULP FROM RECYCLED PAPER |
JP4802305B2 (en) * | 2009-07-17 | 2011-10-26 | 独立行政法人科学技術振興機構 | Floating separation apparatus and method, and manufacturing method of product using the same |
Family Cites Families (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR668406A (en) * | 1928-01-24 | 1929-10-31 | Phosphate Recovery Corp | Improvements in the treatment of phosphatic materials |
US1805830A (en) * | 1929-05-20 | 1931-05-19 | Mason Charles Dorel | Foam destroyer |
US1952727A (en) * | 1929-10-26 | 1934-03-27 | United Verde Copper Company | Froth flotation |
US2874842A (en) * | 1955-04-05 | 1959-02-24 | Krofta Milos | Process and apparatus for waste liquid purification |
US3148948A (en) * | 1961-12-26 | 1964-09-15 | Dorr Oliver Inc | Cooling and defoaming phosphoric acid slurries |
DE1792539A1 (en) * | 1968-09-17 | 1971-11-25 | Dr Baer Eberhardt H | Process for the separation of emulsified or dispersed substances from water |
AU464321B2 (en) * | 1970-10-28 | 1975-08-07 | Aktiengesellschaft Des Altenbergs Furberg Bau Und Zinkhuttenbetrieb | Process and apparatus forthe flotation of fine-grained mixtures of material, particularly of minerals |
DE2161015A1 (en) * | 1971-12-09 | 1973-06-20 | Escher Wyss Gmbh | FLOATING DEVICE FOR CLEANING A FIBER SUSPENSION BY FLOTATION IN THE PAPER INDUSTRY |
DE2420482A1 (en) * | 1974-04-27 | 1975-11-13 | Bergwerksverband Gmbh | METHOD AND SYSTEM FOR FLOTATION |
-
1977
- 1977-03-23 CH CH363277A patent/CH614636A5/en not_active IP Right Cessation
- 1977-03-24 FR FR7708842A patent/FR2347984A1/en active Granted
- 1977-03-24 DE DE2712947A patent/DE2712947C2/en not_active Expired
- 1977-03-24 DE DE2760246A patent/DE2760246C2/en not_active Expired
- 1977-03-30 FI FI770993A patent/FI68093C/en not_active IP Right Cessation
- 1977-04-04 CA CA275,438A patent/CA1096515A/en not_active Expired
- 1977-04-04 NL NL7703627A patent/NL180076C/en not_active IP Right Cessation
- 1977-04-06 ES ES458029A patent/ES458029A1/en not_active Expired
- 1977-04-07 GB GB14877/77A patent/GB1570345A/en not_active Expired
- 1977-04-08 IT IT4889477A patent/IT1073184B/en active
- 1977-04-08 AT AT247877A patent/AT358499B/en not_active IP Right Cessation
- 1977-04-11 BR BR7702266A patent/BR7702266A/en unknown
- 1977-04-12 JP JP4099577A patent/JPS52124273A/en active Granted
- 1977-04-12 SE SE7704203A patent/SE425145B/en not_active IP Right Cessation
-
1980
- 1980-11-29 JP JP55169014A patent/JPS6057903B2/en not_active Expired
-
1982
- 1982-04-22 SE SE8202540A patent/SE452121B/en not_active IP Right Cessation
-
1983
- 1983-04-18 FR FR8306300A patent/FR2544225B1/en not_active Expired
- 1983-06-10 IT IT4847683A patent/IT1218334B/en active
-
1986
- 1986-05-09 NL NL8601174A patent/NL8601174A/en not_active Application Discontinuation
Also Published As
Publication number | Publication date |
---|---|
ES458029A1 (en) | 1978-03-16 |
AT358499B (en) | 1980-09-10 |
FR2347984B1 (en) | 1983-08-26 |
FR2347984A1 (en) | 1977-11-10 |
DE2760246C2 (en) | 1985-09-12 |
FI68093C (en) | 1985-07-10 |
GB1570345A (en) | 1980-07-02 |
JPS52124273A (en) | 1977-10-19 |
SE7704203L (en) | 1977-10-13 |
FI770993A (en) | 1977-10-13 |
NL8601174A (en) | 1986-09-01 |
FR2544225B1 (en) | 1988-11-18 |
CH614636A5 (en) | 1979-12-14 |
IT1218334B (en) | 1990-04-12 |
IT1073184B (en) | 1985-04-13 |
JPS56161849A (en) | 1981-12-12 |
ATA247877A (en) | 1980-02-15 |
IT8348476A0 (en) | 1983-06-10 |
DE2712947C2 (en) | 1985-10-10 |
SE425145B (en) | 1982-09-06 |
NL7703627A (en) | 1977-10-14 |
JPS5623659B2 (en) | 1981-06-01 |
FI68093B (en) | 1985-03-29 |
FR2544225A1 (en) | 1984-10-19 |
CA1096515A (en) | 1981-02-24 |
JPS6057903B2 (en) | 1985-12-17 |
DE2712947A1 (en) | 1977-10-20 |
NL180076C (en) | 1987-01-02 |
NL180076B (en) | 1986-08-01 |
SE8202540L (en) | 1982-04-22 |
BR7702266A (en) | 1977-12-06 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US4214982A (en) | Process and device for removing printer's ink from a fiber suspension | |
US5300222A (en) | Water clarification method and apparatus | |
US4186094A (en) | Apparatus for eliminating by flotation impurities in the form of solid particles contained in a liquid | |
JPH01168984A (en) | Method and apparatus for deinking fiber suspension | |
FI88524C (en) | Pressure subject flotation module and a method of pressure submerge city foam separation | |
US5492622A (en) | Water clarification apparatus | |
EP0122747B1 (en) | Apparatus for deinking | |
US5529190A (en) | Gas sparged hydrocyclone with foam separating vessel | |
JPH04240284A (en) | Method for removal of hydrocyclone ink and adher- ing foreign material in paper recovery process | |
SE452121B (en) | FLOTATIONSANLEGGNING | |
JPH07500881A (en) | Improved apparatus and method for removing ink from waste paper pulp | |
US6475337B2 (en) | Process for aerating dispersions | |
JPS61501272A (en) | Method and apparatus for flotating a dispersion | |
US4220612A (en) | Flotation cell feed duct | |
JPH0718110B2 (en) | Purifier for paper pulp | |
US5240621A (en) | Method and apparatus for improving flotation separation | |
KR19990067062A (en) | Degassing vessel | |
KR20010042112A (en) | Method and device for flotation of pollutants from an aqueous fibrous material suspension | |
US3392114A (en) | Apparatus and method for decontaminating pulp and paper machine effluent | |
US5919289A (en) | Deaeration tank | |
US4882068A (en) | Method and apparatus for removing liquid from suspensions | |
JP2013508134A (en) | Method for removing solids from fiber material suspensions by flotation | |
FI73749C (en) | Plant for the elimination of liquid particulate pollutants by flotation. | |
KR810000822B1 (en) | A process and an installation for the elimination by floation of impurities in the form of solid particles contained in a liquid | |
JP2004209459A (en) | Gas dissolving apparatus |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
NAL | Patent in force |
Ref document number: 8202540-4 Format of ref document f/p: F |
|
NUG | Patent has lapsed |
Ref document number: 8202540-4 Format of ref document f/p: F |