• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    1527731 Sewage flotation treatment IMPERIAL CHEMICAL INDUSTRIES Ltd 24 March 1976 [7 April 1975] 14142/75 Heading C1C A method for solids-liquid separation wherein a solids-liquid sewage mixture is circulated around a circulatory system which comprises at least two substantially vertical ducts communicating with each other at the upper and lower ends so that the mixture flows downwardly in one duct and upwardly in another, a gas containing free oxygen being supplied to, and at least partly dissolved in, the mixture; a portion of the upwardly-flowing mixture containing dissolved gas passes into a flotation chamber (connected to the circulatory system) in which the hydrostatic pressure gradually decreases as the mixture flows upwards and consequently gas is released from solution and forms gas bubbles attached to solid particles present, which carry the solid particles to the top of the liquid; and the solid particles carried to the top of the liquid and the resulting clarified liquid are removed separately from the system. The liquid, carrying biologically-degradable waste, may be sewage or effluents from farms or food factories. An apparatus is also described.
    公开号:SU997603A3
    申请号:SU762343706
    申请日:1976-04-07
    公开日:1983-02-15
    发明作者:Альберт Хайнс Дэвид；Тревор Джонс Ричард；Корнелиус Роеслер Фрэнк
    申请人:Империал Кемикал Индастриз Лимитед (Фирма)；
    IPC主号:
    专利说明:

    • The invention relates to a method and apparatus for wastewater treatment and can be used in various industries for the treatment of domestic and industrial water. 5 kov.
    Closest to the invention is a method of wastewater treatment by continuous circulation at atmospheric pressure of contaminated water 10 containing suspended solids, in the form of ascending and descending flows, introducing oxygen-containing gas, such as air, and solids content into the descending stream.
    A device for implementing the method is known, comprising a housing having two vertical channels communicating with each other in the lower and 2 upper parts, an input of the liquid to be cleaned attached to the upper part of the first of the channels, and a device for introducing gas into the upper part of the first channel. 1].
    However, the known method has insufficient efficiency of purification of the loaded water.
    The purpose of the invention is the intensification of the process
    This goal is achieved in that according to the method of wastewater treatment by continuous circulation at atmospheric pressure of contaminated water containing suspended solids in the form of ascending and descending flows, introducing oxygen-containing gas, such as air, into the descending stream, and; the flow from is withdrawn in the form of a separate upward flow into the flotation chamber, where solid particles are separated.
    '' In a device for implementing the method of wastewater treatment, comprising a housing having two vertical channels communicating with each other, in the lower and upper parts, an input of the liquid to be cleaned connected to the upper part of the first channel, and a device for introducing gas into the upper part of the first channel equipped with a flotation chamber mounted outside the housing in it. the upper part and communicating with the cavity of the second channel through an opening made in the wall of the lower part of the housing, and a jack peak installed behind the hole in the upstream direction.
    • In addition, the device is equipped with ’. Louvers installed in the hole.
    In FIG. 1-3 shows the proposed device, General view, section; on the. FIG. 4 is a section AA in FIG. 3 "
    The method of treating wastewater consists in pretreatment with physical methods, for example, by screening or screening and sedimentation, to remove large suspended particles of solid matter, and in secondary treatment with biological methods to remove dissolved and fine suspended substances.
    's;
    Flotation is used in the second stage of wastewater treatment, (wastewater) to remove suspended solids from wastewater and to isolate and concentrate biologically flocculated ·. . precipitation or sludge. The main components of the flotation system are a discharge pump, a device for blowing air (blowers), a storage tank and a flotation unit. Wastewater or part of the purified or clarified eluent is injected in the presence of a sufficient amount of air to ensure saturation compared to atmospheric conditions. When pressure is removed in a supersaturated liquid, which is combined with displacement or mixing with wastewater at atmospheric pressure, small air bubbles form in the liquid. Suspended solids are floated by small air bubbles that adhere or adhere and entangle solids. A mixture of solid particles with air 5 rises to the surface from which it is removed. The purified or clarified liquid drains down.
    In flotation systems, a special * pump, blowers, and a pressurized tank or boiler are needed to ensure the supersaturation of the mixture of liquids : solids and solids.
    According to the proposed method of separation or separation of solids from liquid, a mixture of liquid and solid substance circulates through a system consisting of at least two vertical channels communicating with each other at their upper and lower ends so that it flows down one channel of the system and rises up to another, gas is supplied and partially dissolved in the system into the mixture flowing downward, and part of the upwardly directed mixture containing dissolved gas enters the flotation-> flotation chamber connected to the circulation system, and in the fleets of the ion chamber, the pressure and pressure gradually decrease or decrease as the mixture rises upward,
    ! .gas is released from the solution and forms bubbles (gas) that adhere to the solid particles contained in the mixture and carry them to the top (surface) of the liquid in the mixture. Then, at the bottom of the solid, particles that have fallen on top of the liquid and the liquid left or left behind that are purified are removed separately from the system.
    The proposed device for separating solids from a liquid includes a circulation system and a flotation chamber associated with it, moreover, a circulation system; consists of two vertical kana! fishing, communicating with each other top and. lower ends, devices for circulating a liquid-solid mixture. ·.
    The flotation chamber is connected to the e- system so that part of the upwardly directed mixture containing dissolved gas enters the flotation chamber and is directed upwardly in it. There are devices for s output from. systems of solid particles transferred to the top of the liquid; and devices for withdrawing or discharging from the system of the liquid thus purified.
    0 The flotation chamber is for the most part of its length a cylindrical pipeline or channel into which a liquid-solid mixture / containing dissolved gas enters through an opening or openings at the lower ends. At the upper end, the channel or pipeline has an outlet to a tank or tank with a larger Area S 997 603 4
    Dew cross section than channel. Such a tank or boiler is called a flotation pool, in which the separated solid particles float to the surface of the purified 5 liquid and the separated solid particles and the purified or clarified liquid are removed separately from the pool.
    The hole through which the liquid * solid mixture enters the flotation chamber is equipped with a trap or trap to prevent large 15 bubbles of gas contained in the mixture from entering the flotation chamber, which can disrupt the flow. A trap shape is preferred that causes the mixture to flow initially down when it enters the flotation chamber. »The trap can be in the form of a plate mounted on the wall of the chamber, protruding in the chamber behind the hole and at an angle to the wall of the chamber. Several of these plates can form a 15 blind structure. The flow rate through the trap or louvres is less than the rate of rise of the bubbles, i.e. no more than 10 cm / s, which prevents the flow of bubbles with a diameter greater than 1 mm (or in the slots of the blinds) into the zone of the current flowing down in the trap. The flow rate through the trap or blinds is less than 5 cm / s.
    • To ensure the efficiency of the 35 flotation process, i.e. full separation or separation of solid particles from the liquid, it is necessary that the flotation chamber does not have a strong turbulent flow, which contributes to the grinding of solid particles, which complicates their separation or separation, therefore it is necessary to exclude the ingress of large gas bubbles into the flotation chamber. In order to avoid turbulence, the average velocity of the upwardly directed liquid flow in the flotation chamber must be maintained at a maximum of 0.3 m / s, preferably at most 0.1 m / s. m
    The depth of the flotation chamber is 20–40 m. The duration of upward fluid flow in the flotation chamber is 60–1000 s, which contributes to the formation of large flakes with air bubbles associated with them.
    The invention is used in the biological treatment of wastewater, in particular at the aeration stage, for separating flocculated sludge particles from liquid effluent, as well as at the digestion stage. For biological treatment of wastewater, oxygen or any gaseous mixture, such as air, serves as a gas containing oxygen.
    The apparatus for circulating liquids consists of a chamber with a downward flow (release) and an upward flow chamber (lift) communicating with each other by the upper and lower ends and a device for supplying gas to the liquid in the release chamber. This apparatus can be used at the stage of aeration and / or digestion of the biological treatment of wastewater, and the wastewater circulates through the start-up lifting chamber system and is supplied with oxygen-containing gas as it passes through the release chamber.
    The flotation chamber is connected to the lifting chamber and a part of the liquid-solid mixture, for example, wastewater, floating in the lifting chamber, enters the flotation chamber.
    The launching and lifting chambers have any cross-sectional shape, for example round 'or semicircular, and are located in a single structure, preferably cylindrical, divided inside by a partition or partitions, or with a launching chamber formed by a pipe placed inside a structural pipeline, and the space between it forms a lifting chamber. Very diverse geometrical arrangements or patterns are possible. The system may include many lifting and lowering chambers. The flotation chamber is preferably located near the top of the lift 'chamber e are connected with it through a hole or holes in the walls of the lifting chamber.
    The vertical channel or pipe inserted into the upper part of the lifting chamber can be expanded when the lifting chamber surrounds the flotation chamber. Communication between the lifting and flotation chambers is carried out by means of holes with traps for gas bubbles in the wall of the flotation chamber. One or more external connections penetrating the lifting chamber are provided to remove fluid and float. . 997603 8 solid particles from the flotation chamber.
    Waste water after pretreatment enters the tank * forming the gas-emitting part of the circulating system 5. The trigger and lift chambers are located below the level of the base or bottom of the gas recovery pool. The flotation chamber is located along the upper part * 0 of the lifting chamber and forms a flotation pool at the upper end, located next to the gas separation pool. The flotation chamber can also be located at an angle (kver-> 5 xy) to the upper part of the lifting chamber, and in the upper part it has access to the flotation pool, connecting to the gas-emitting pool, but located at a distance from it. 20 Solids floating on. the surface of the liquid in the flotation pool, is collected, for example, using scrapers and returned to the gas separation pool and to the circulation system <. The purified effluent is transferred from the flotation pool to another stage of wastewater treatment. When the basins are located on the ground or below the soil level, the structure, including the circulation system and flotation chamber, has the appearance of a shaft (preferably cylindrical with a sidewall for the flotation chamber) located in the ground. J3
    The shaft may be located in the ground outside the pools, but preferably below them, the upper ends of the lifting and lowering chambers have access to the gas separation pool, and the upper end of the flotation chamber to the flotation pool.
    The lifting and lowering chambers are located at least 40 m vertically below the level of wastewater in the gas separation basin, preferably 80 m, and preferably 150-250 m. The ratio of the cross-sectional area of the flotation chamber to the cross-sectional area of the lifting chamber varies widely depending on the duration processing in the circulation system and is in the range of 0.01-2.0. With easily decomposing effluents, it is 0.25 ”2.0.
    In order to circulate wastewater in the circulation system, oxygen-containing gas is injected into the system.
    Flotation is achieved with a gradual decrease in pressure; there is no sharp decrease in pressure with a large shear force.
    When treating wastewater, it is possible to apply pressure to the wastewater rather than the purified effluent without subjecting the brittle sludge to high shear or shear stresses and without dispersing the flakes into small particles that are difficult to separate.
    The use of this method in the treatment of wastewater allows significant recycling of sludge without sedimentation and eliminates the possibility of prolonged residence in anaerobic tanks, which provides increased intensity of wastewater treatment. Flotation is achieved without a special compressor chamber and pressure release system.
    The device (Fig. 1) has a gas release pool 1, below which a trunk is buried, or a shaft 2, including a lifting chamber 3 and a descent chamber 4, separated by a partition 5. The lifting 3 and the descent 4 chambers communicate with their upper ends in the pool 1, and at the lower end of the barrel or shaft 2 - below the partition 5. To ensure an appropriate flow pattern in the pool 1, the upper end 6 of the launch chamber 4, formed by the extension of the shaft wall 2 and the partition 5, is located above the base of the pool and is equipped with a flow guide device 7. The lifting chamber 3 communicates through an opening 8 with a flotation chamber 9 in the lower part, of the shaft 2. In the upper part of the flotation chamber 9 there is a hole in the flotation pool 10. located adjacent to the gas-emitting pool -1 The hole 8 is equipped with a trap 11. Oxygen-containing , gas is supplied to the lifting chamber 3 and the descent chamber 4, respectively, through the atomizer (nozzle) 12 and 13.
    The device (Fig. 2) has a gas separation pool 1 with a shaft 2 located below it in the ground and a lifting chamber 3 and a launching chamber 4, separated from each other first (G 5 · The lifting chamber 3 communicates through an opening 8 provided with a trap 11, flotation chamber, 9, the upper ... end of which has access to the flotation pool 10, located at
    997603 10 · adjacent to the gas evacuation pool 1. Lifting 3 and triggering 4 chambers communicate with their upper ends in pool 1 and lower ends - at the lower end of the shaft 2. Trigger 5 shaft 4 is located coaxial to the lifting chamber 3 and extended!
    above the pool 1, the upper end of the partition 5 is tilted with respect to the pipe 14 and the id 15 * The fluid is circulated mechanically in the apparatus with the help of a propeller 16 in the 15 'elbow and oxygen-containing gas. injected into the liquid through the air distributor (nozzle) 15 17 located in the upper suit of the trigger chamber 4,
    The proposed device can be used at the stages of aeration and the secondary treatment of stoma-20 waters, the methods of which are similar. ·
    In the aeration stage, the wastewater after pretreatment to remove coarse or dense (heavy) 25 and difficult to process solid particles and primary sedimentation enter the gas separation pool 1 through an inlet (not shown) having exit to the pool 1, for example, close to the open end of the knee 15 in the apparatus (Fig. 2). The fluid plus activated sludge is removed from pool 1 through another channel (not shown) *. Exiting pool 1 below the level of BB fluid in a pool located at a distance from. input channel., 'and enter the sedimentation (slop) tank or pool. Liquid ‘exits (poured) out of the apparatus also through channel 18 (Fig. 1), which has access to the flotation pool 10 Below the level of BB liquid in the pool.
    The device (Fig. 1) begins to work when air is injected from compressor 45 litter. the lifting chamber 3 through the distributor (air) 12. This causes the upper part of the lifting chamber 3 to work as a pneumatic pump (airlift) and waste water 50 begin to circulate through the device in the direction shown by arrows in FIG. 1. When the flow rate reaches its minimum value, air is supplied to the trigger chamber. ' 5 through the distributor 13 and gradually increase it. This is carried out as the fluid velocity in the trigger chamber increases. During steady-state operation, all or most of the air is supplied to the trigger chamber 4.
    In the device (Fig. 2), the circulation is carried out mechanically using a propeller 16, air is supplied to the upper part of the descent chamber through the distributor 17. *
    Bubbles of gas entering the trigger chamber are quickly lowered by circulating wastewater in the direction of higher pressure, and their size decreases. B lower level submerged. Many bubbles are completely absorbed by the apparatus. As the wastewater rises in the lifting chamber, the bubbles first reappear and then increase in size. Part of the wastewater from the lifting chamber 3 enters the flotation chamber 9 through the hole 8. The trap 11 prevents large air bubbles from entering through the hole 8 into the flotation chamber 9 and disrupt the flow in it. In the flotation chamber 9, small air bubbles form in the wastewater, which adhere to solid particles in the wastewater and rise to the surface of the liquid in the flotation pool 10, entrainment; solid particles. Thus, solids from the branch waters rise up to the surface of the liquid in the flotation pool 10 by air flotation. The liquid leaves the flotation pool 10 along the channel. 18 (Fig. 3) j> and the solids are scraped from its surface and returned to the gas separation pool 1 using a scraper 19 (Fig. 3)
    In the device (FIGS. 3 and 4), fluid also circulates through. to the apparatus. <<. the action of oxygen-containing gas supplied to it through distributors, 12 and 13 "and the trigger chamber 4>. connected by a tubular baffle 5, placed coaxially relative to the lifting chamber 3 ”connected by a tubular recessed barrel 2. But the flotation chamber 9 is tilted up and out of the lifting chamber 3 instead of being vertically close to it, the flotation chamber 9 has £ t * at the upper end, exit (hole) 'to the flotation pool 10, from the bottom of which the purified or clarified liquid effluent enters the sedimentary or slop bass
    1.1 a seine (not shown) through discharge channel 18, and on top of which emerged. Are solids * removed with a scraper 19 and returned to the gassing bass
    • Seine 1. For simplicity, the scraper device 19 is shown only on the surface between pools 1 and 10, in practice it> spreads almost all over the surface of the solid in pool 10 and at least partially on the surface in pool 1.
    The hole 8 from the lifting 3 into the flotation chamber 9 is equipped with a trap 11, and in addition, the blinds 2 () and are tilted downward from the chamber 3 into the flotation chamber 9 to ensure flow. Through the hole 8 in the downward direction. The transition from the flotation chamber 9 to the flotation pool 10 passes through the well 21, half of which goes into the semi-cylindrical pipe 22 and allows the solid substance to float directly to the top of the flotation pool 10, and the second half 23, from which the purified liquid from the flotation chamber 9 goes directly down flotation pool 10, poured out of it through the lowering channel 18 for liquid effluent.
    权利要求:
    Claims (2)
    [1]
    399 of the upper part of the first channel, and the gas pipe for gas inlet, and the upper part of the first channel, equipped with a flotation chamber installed outside the hull in it.  the upper part and communicating with the cavity of the second canal through an opening made in the wall of the lower part of the housing and an air shield installed behind the opening along the flow.   In addition, the device is equipped. installed in the hole blinds myo On (} wr.  1 to 3 depict the preliminary device, a general view, a section in FIG. , 4 - AA section on (| mg.  3  The wastewater treatment method is pretreatment with the help of zic methods, for example, by screening or screening and sedimentation, to remove large suspended particles of solid matter, in secondary processing by biological methods to remove dissolved and small suspended substances; Flotation is used in the second stage wastewater treatment, (wastewater) to remove suspended solids from wastewater and to isolate and concentrate biologically flocculated.  .  precipitation or sludge.  The main components of a flotation system are a pressure pump, a device for blowing air (blowers), a storage tank and a flotation unit.  Sewage MEASURES or part of the purified or clarified eluent is injected in the presence of sufficient air to provide supersaturation compared to NEC) with atmospheric conditions. When pressure is removed in supersaturated liquid, which is combined with displacement or mixing with waste at atmospheric pressure, fine air bubbles.  The suspended solids are floated with fine air bubbles that adhere or adhere and entangle the solids.  The mixture of solids and air rises to the surface from which it is removed.  The cleaned or os bilge fluid drains down.  In flotation systems for obes.  The liver is oversaturated with a mixture of liquids and solids. Special 11 pumps, blowers and a tank or boiler with pressure are required. According to the proposed method of separating or separating solids from the liquid, the mixture of liquids and solids circulates through a system consisting of at least two vertical channels communicating with each other G with their upper and lower ends in such a way that it flows down through one channel of the system and rises up along the other, the gas is supplied and partially dissolved in the system in a mixture b, flowing downward, and part of the upwardly directed mixture containing the dissolved gas enters the flotation chamber connected to the circulating system, with hydrostatic pressure gradually decreasing or decreasing in the flotation chamber as the mixture rises upwards, gas evolves from (solution and it forms bubbles (gas) that adhere to the mixtures of solid hgg mixtures, and carry them to the top (surface) of the liquid in the mixture.  Then the solid particles trapped on. top of the liquid, and preserve with lower left or. the purified liquid, separated from the system separately; the proposed apparatus for separating solids from the liquid includes a circulating system and a flotation cell associated therewith, the circulating system; consists of two vertical BKV CGBs, which are in common with each other upper and.  lower ends, devices 1a for circulating a liquid-solid mixture,.  The flotation cell is connected to the system so that a part of the upwardly directed mixture containing the diluted gas enters the flotation chamber and goes up to it. Devices are provided for withdrawal from.  systems of solid particles transferred to the top of the liquid; and devices for withdrawing or draining the liquid thus purified.  sti.  The flotation chamber represents a cylindrical pipe or channel over most of its length, and the liquid-solid mixture 7 containing the dissolved gas enters through the opening or openings at the lower end. At the upper end the channel or pipe has an outlet and a tank or tank with a larger cross section plojkadv than the channel.  Such a tank or boiler is referred to as a flotation basin in which the separated solids float to the surface of the purified liquid and the separated solids and the cleaned or clarified liquid is removed separately from the basin.  The opening through which the liquid-solid mixture enters the flotation cell is equipped with a trap or catcher to prevent the large gas bubbles contained in the mixture from entering the mixture, which can disrupt the flow, from entering the flotation cell.  Such a form of trap is preferred, which causes the mixture to flow initially downwards when it enters the flotation cell.  The trap can be in the form of a plate, fixed on the wall of the chamber, protruding openings in the chamber behind the wall and at an angle to the wall of the chamber.  The flow rate — through a trap or louver — is lower than the bubble rise rate.  t, e no more than 10 cm / s, which does not allow the flow of bubbles with a diameter greater than 1 mm (or into slits of the blinds) to fall into the zone of the current flowing down in the trap.  The flow rate through the trap or pitch is less than 5 cm / s.   Dp to ensure the efficiency of the flotation process, t, e, complete separation or separation of the solid part from the liquid, it is necessary that the flotation cell does not have a strong turbulent flow that contributes to the grinding of the solid part which complicates their separation or separation, therefore it is necessary to exclude the entry of large bubbles ha per flotation cell.  In order to avoid turbulence, the average speed of the upwardly directed fluid flow in the flotation cell must be maintained at a maximum of 0.3 m / s, preferably not more than 0.1 m / s, the depth of the flotation cell. is m.  The residence time of the upstream liquid stream in the flotation chamber is 60-1000, which contributes to the formation of large pops. with associated air bubbles.  The invention is used in biological treatment of wastewater iods, i.e., i.a. sludge from liquid effluenza, as well as at the stage of digestion. For biological treatment of wastewater, gas is oxygen or any gas-phase mixture, for example air containing oxygen.  The apparatus for circulating liquids consists of a chamber with a downward flow (descent) and an upflow chamber (ascent), communicating between the upper and lower | | C1 ends and devices for supplying gas to a liquid in the trigger chamber.  This apparatus can be used at the stage of aeration and / or digestion of biological wastewater treatment, with the wastewater circulating through the system (starting lift chambers and supplied with oxygen-containing gas as it passes through the release chamber.  The flotation cell is connected to the lifting chamber and a portion of the liquid-solid mixture, for example, wastewater, which pops up in the lifting chamber, enters the flotation cell.  The trigger and lift chambers have any cross-sectional shape, for example round or semicircular, and are arranged in a single structure, preferably cylindrical, divided inside by a partition or partitions, or with a trigger chamber formed by a pipeline placed inside the structural pipeline, and the space between it forms a lifting chamber. highly diverse geometries or patterns.  The system may include many lifting and lowering cams.  The flotation cell is preferably located close to the upper suit of the lifting chamber and connected.  with her through the hole; or, openings, in the walls of the lifting chamber.  A vertical channel or tube inserted in the upper part of the lifting chamber can be expanded when the lifting chamber surrounds the flotation cell.  The communication between the lifting and flotation chambers is carried out by means of holes with holes for gas bubbles in the wall of the flotation cell.  One or more external connections, penetrating the lifting chamber, are provided to remove the liquid and float 7.  .  9 solid particles from the flotation cell.  After pretreatment, wastewater enters the tank, which forms the gas-emitting part of the circulating system.  The trigger and elevation chambers are located below the base or bottom of the gas separation basin.  The flotation cell is located along the top. parts of the lifting chamber and forms at the upper end a flotation basin located near the gas separation basin.  The flotation cell is also located at an angle (upwards) to the upper part of the lifting chamber, and in the upper part it has access to the flotation basin, connected to the gas separation basin, but located at a distance from it. .  the surface of the liquid in the flotation basin, for example, is collected with the help of scrapers and returned to the gas separation basin and to the circulation system. Purified effluent comes from the flotation basin to another stage of wastewater treatment.  When pools are located on the ground or below the level of the soil, structures in the tour, including a circulation system and flotation. An on-site camera looks like a shaft (preferably cylindrical with a sidewall for a flotation chamber) located in the ground. The mine can be located in the ground outside the basins, but preferably below them, the upper ends of the lifting and lowering chambers have an outlet to the gas separating pool. the upper end of the flotation cell is in the flotation basin.  The elevating and lowering chambers are located at least on the central heating station vertically but below the level of sewage in the gas separation basin, preferably at 80 m, and preferably at 150-250 m.  0t — the wearing of the cross-sectional area of the flotation cell to the cross-sectional area of the lifting chamber varies widely depending on the treatment time in the circulating system and is in the range of 0.01-2.0. For easily decomposing effluents it is 0,, 0.  For the circulation of wastewater in the circulation system, injection of oxygen-containing gas into the system is used.  3 Flotation is achieved with a gradual decrease in pressure; there is no abrupt decrease in pressure with a large shear force.  When treating sewage, it is possible to exert pressure on the sewage, and not on the purified effluent, not subjecting the fragile sludge to high shear or shear stresses and not dispersing the flake into small particles that are difficult to isolate.  The use of this method in the treatment of wastewater allows for significant recycling of sludge without sedimentation and eliminates the possibility of prolonged stay in anaerobic tanks, which provides increased treatment of wastewater. Flotation is achieved without a special compressor chamber and pressure release system.  The device (FIG.  1) it has a gas-separating basin 1, below which the barrel is buried in the ground, or a shaft 2, including a lifting chamber 3 and a launching chamber k, divided by a partition 5.  Elevating 3 and lowering k of the chamber are connected between :: the upper ends of pool 1, and at the lower end of the shaft or shaft 2 - below the partition 5.  To provide a suitable flow pattern in the basin 1, the upper end 6 of the launch chamber k formed by the extension of the wall of the shaft 2 and the partition 5 is open above the base of the basin and provided with a flow direction 7o. The lifting chamber 3 communicates through the opening 8 with the flotation chamber 9 in the lower part of the shaft 2  In the upper part of the flotation cell 9 there is a hole in the factional pool 10. , is located Located adjacent to the gas separation pool 1, Hole 8 is equipped with a trap 11.  Oxygenated.  the gas is supplied to the lifting chamber 3 and the trigger chamber 4, respectively, through a sprayer (nozzle) 12 and 13.  The device (FIG.  2) it has a gas-evacuating pool 1 with a shaft 2 and elevator 3 3 located below it in the ground and 4 launch chambers separated by a partition (.  Lifting chamber 3 is connected through an opening 8 provided with a trap 11 with a flotation chamber. 9, the upper end of which has access to the flotation basin 10, located adjacent to the gas &amp;  Lifting 3 and lowering k of the chamber communicate with each other by the upper ends in pool 1 and the lower ends of the MI in the lower shaft of mine 2, the Trigger chamber 4 is coaxially lifting, chamber 3 and protruding) above pool 1, the upper end of the partition 5 is higher with slope with respect to the pipeline I and the knee 15 "The fluid is circulated mechanically in the apparatus by means of a propeller 16 in the knee, oxygen-containing gas.  Injected into the liquid through the air distributor (nozzle) 17 located in the upper part of the trigger chamber t.  The proposed device can be used at the stages of aeration and differentiation of secondary wastewater treatment, the methods of which are similar.   At the aeration stage, wastewater after pretreatment to remove coarse or dense (heavy) and hard-to-remove solid particles and primary sedimentation enters the gas separation basin 1 through an inlet channel (not shown) having.  access to pool 1, for example, near the open end of the knee 15 in the apparatus (|) ig.  2).  The fluid plus activated sludge is removed from pool 1 via another channel (not shown). leaving the pool 1 of the liquid level BB liquid in the pool located at a distance of.  input channel. , and enter the settling (settling) tank or pool.  The liquid exits (pours out) from the apparatus also through the channel 18 (Fig.  1), and | The exit to the flotation basin 10 Below the level of the liquid B-B in the basin.  The device (Fig „1) starts to work when air is injected from the compressor c.  lifting chamber 3 through the distribution of itel (air) 12.  This causes the upper part of the lift 3 to work as a pneumatic pump (airlift) and the wastewater begins to circulate through the device in the direction indicated by the arrows on the pound.  one.  When the flow rate reaches the minimum value, I start the air supply to the trigger valve through the distributor 13 and gradually see it.  This is done as the velocity of the fluid in the launching chamber increases.  In steady state operation, all or most of the air is supplied to the escapement chamber 4.  In the device (FIG.  2) the circulation is carried out mechanically by means of a propeller 16, air is supplied to the upper part, the trigger chamber through the distributor. . .  Gas bubbles entering the escape chamber, &amp; The wastewater is circulated directly in the direction of higher pressure, and its size is reduced.  In the lower level immersed.  Many bubbles are completely absorbed by the wastewater.  As the sewage rises in the lifting chamber bubbles. first appears again and then grows in size.  Part of the wastewater chamber 3 enters from the lifting flotation chamber 9 through the hole 8.  The trap 11 prevents large air bubbles from entering through the opening 8 into the flotation cell 9 and disrupting the flow in it.  In the flotation cell 9, small air bubbles are formed in the wastewater, which adhere to solid particles in the wastewater and rise to the surface of the liquid in the flotation tank 10, which is carried along; solid particles.  Thus, the solids of the branch waters are raised to the surface of the liquid in the flotation pool 10 by means of air flotation.  The liquid leaves the flotation tank 10 through the canal. 18 (FIG.  3JJ, and the solids are fastened from its surface and returned to the gas-emitting basin 1 using a scraper device 19 (Fig. 3) 8 device (FIG.  3 i) the liquid is also circulated through the apparatus by the action of an oxygen-containing gas supplied to it through distributors.  12 and 13, and the camera release 4.  connected by a tubular partition: 5, placed coaxially with respect to the lifting chamber 3t of the associated tubular recessed barrel 2.  But the flotation chamber 9 of HaJOioHeHa is up and out from the lifting chamber 3, instead of being vertically near it.  Flotation cell 9 imedt ": at the upper end, exit t from the top) into the flotation pool 10, cleaned or clarified liquid effluent from the bottom of the tank flows into the settling or settling basin (not shown) through the discharge channel 18, and from above which floated solid substances are removed with the help of the scraper device 19 and are returned to the gas separation bass, sein 1.  For simplicity, the scraper device 19 is shown only on the surface between basins 1 and 10, in practice it is distributed to almost the entire surface of a solid in pool 10 and at least partially on the surface in pool 1.  The opening 8 of the lifting, 3 into the flotation chamber 9 is provided with a trap 11, and in addition, the louver 2Q and inclined downwardly from the chamber 3 into the flotation cell 9 to ensure flow. through the hole 8 in the downward direction.  The transition from the flotation chamber 9 to the subsidized basin 10 passes through the well 21, half of which goes into the semi-cylindrical pipe 22 and allows the solid to float directly to the top of the flotation basin 10, and the second half 23, from which the purified liquid from the flotation chamber 9 flows directly downstream of the flotation basin 10, is poured out of it through the α-outlet channel 18 for the H and 1 effluent.  Claim 1.  The method of sewage treatment by continuous circulation at atm. 12 of the atmospheric pressure of polluted water containing suspended solids, in the form of ascending and descending currents, is introduced into the descending sweat. an oxygen-containing groove, such as air, and separation of solid particles, characterized in that, in order to intensify the process, a portion of the upstream stream is diverted as a separate upstream stream into the flotation cell, where the solid particles are separated,
    [2]
    2. A device for cleaning waste water, comprising a housing having two vertical channels communicating with each other in the lower and upper parts, introducing the liquid to be purified, connected to the upper part of the first channel, and a device for introducing gas into the upper part of the first channel, about In order to intensify the process, it is equipped with a flotation chamber installed outside the hull in its upper part and communicating with the cavity of the second channel through an opening made in the wall of the lower part of the hull and a baffle plate, installed behind the hole along the flow, 3 The device according to claim., characterized in that it is equipped with blinds installed in the hole. Sources of information taken into account during the examination 1. Lonii's patent tf 7-13958, cl. C 02 C, publish. 1972.
    S
    five
    X
    /
    /.
    AT
    u
    /
    .Yu
    hh
    0l4t.l
    Z3
    Fchg
    类似技术:
    公开号 | 公开日 | 专利标题
    SU997603A3|1983-02-15|Process and apparatus for purifying effluents
    FI70874C|1986-10-27|BIOREACTOR ORGANIZATION WITH VERTICAL SCHEME SAMT FOERFARANDE FOERSKYDDANDE AV EN UNDER TRYCK STAOENDE BIOREACTOR SOM UPPVI SA VERTICAL SCHAKT MOT NETWORK AV OEVERSVAEMNING AV INKOMMA ND AVFALLSVAETSKA
    US5382358A|1995-01-17|Apparatus for dissolved air floatation and similar gas-liquid contacting operations
    US5728304A|1998-03-17|Method and apparatus for dissolved air flotation and related waste treatments
    US4192740A|1980-03-11|Two zone process for biological treatment of waste water
    JP2011110520A|2011-06-09|Apparatus for treating organic waste water and method of treating organic waste water
    FI89703C|1993-11-10|Device for the treatment of liquids, especially waste water
    US6719911B2|2004-04-13|Apparatus and method for the treatment of a contaminated fluid
    US5421999A|1995-06-06|Floating nitrification reactor in a treatment pond
    EP0028093A1|1981-05-06|Method and apparatus for the separation of gas and solids from waste mixed liquors
    JP2008502472A|2008-01-31|Water treatment process and apparatus by fluid flow
    KR20070039057A|2007-04-11|Process and reactor for intensified and energy-efficient, biological |-water treatment
    US5792363A|1998-08-11|Method for removing solids from a contaminated liquid
    KR20110047453A|2011-05-09|The method and apparatus to treat municipal and industrial wastewater
    PL114233B1|1981-01-31|Apparatus for sewage treatment
    JP3169117B2|2001-05-21|Biological wastewater treatment equipment
    CS271652B1|1990-11-14|Complex device for multistep water conditioning treatment and water purification
    JP2577673B2|1997-02-05|Sewage treatment tank
    RU38755U1|2004-07-10|BIOLOGICAL WASTE WATER TREATMENT PLANT
    CN112279366B|2021-08-31|Prevent sludge anaerobic fermentation&#39;s sediment device and sewage treatment system
    SU1031914A1|1983-07-30|Combination apparatus for biological treatment of effluents
    CN1463928A|2003-12-31|Water treatment clarification apparatus
    JP3652473B2|2005-05-25|Wastewater treatment system
    SU1011555A1|1983-04-15|Apparatus for purifying effluents
    SU912657A1|1982-03-15|Apparatus for purifying effluents
    同族专利:
    公开号 | 公开日
    NZ180494A|1978-03-06|
    PL109935B1|1980-06-30|
    AU1265476A|1977-10-13|
    DD125326A5|1977-04-13|
    CS194237B2|1979-11-30|
    CA1065508A|1979-10-30|
    SE7604037L|1976-10-08|
    GB1527731A|1978-10-11|
    NO149841C|1984-07-04|
    NO149841B|1984-03-26|
    ZA761907B|1977-03-30|
    DE2614881A1|1976-10-21|
    BE840493A|1976-10-07|
    HK44884A|1984-06-01|
    ES446794A1|1977-06-01|
    US4253949A|1981-03-03|
    JPS6139879B2|1986-09-05|
    JPS5884093A|1983-05-20|
    NL180653C|1987-04-01|
    NL7603577A|1976-10-11|
    AT351463B|1979-07-25|
    CH612361A5|1979-07-31|
    IN142380B|1977-07-02|
    JPS55109459A|1980-08-22|
    JPS5524960B2|1980-07-02|
    JPS6139880B2|1986-09-05|
    FR2306745B1|1980-02-08|
    JPS6139119B2|1986-09-02|
    DE2614881C2|1984-04-19|
    AU498541B2|1979-03-15|
    JPS51122947A|1976-10-27|
    NO761132L|1976-10-08|
    NL180653B|1986-11-03|
    FR2306745A1|1976-11-05|
    ATA249976A|1978-12-15|
    JPS53134275A|1978-11-22|
    TR19275A|1978-10-06|
    IT1059589B|1982-06-21|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    WO2006043850A1|2004-10-15|2006-04-27|Pol Emanuilovich Blank|Method for processing a fluid medium and device for carrying out said method|BE504471A|
    US895229A|1908-03-30|1908-08-04|Cecil C E Beddoes|Method of treating sewage.|
    US1401598A|1918-01-29|1921-12-27|Pneumatic Process Flotation Co|Flotation apparatus|
    US1646019A|1925-07-29|1927-10-18|Forrester David Lawton|Flotation method and apparatus|
    GB573198A|1944-04-21|1945-11-09|Paxman & Co Ltd Davey|Improvements in or relating to vacuum flotation apparatus|
    FR1042193A|1950-09-18|1953-10-29|Stamicarbon|Device for separating particles differing in density or grain size|
    NL84802C|1951-08-31|
    US2987186A|1957-11-21|1961-06-06|Yeomans Brothers Co|Apparatus for treating waste materials|
    DE1584885A1|1965-09-14|1970-02-05|Danjes Dipl Ing Martin|Device for the biological cleaning of waste water|
    DE1517967C3|1966-03-16|1978-09-14|Sesojuznyj Zaotschnyj Politechnitscheskij Institut, Moskau|Device for cleaning liquids|
    FR1548964A|1967-12-20|1968-12-06|
    DE1642838A1|1968-03-04|1971-04-22|Inst Wasserwirtschaft|Flotation process and device for carrying out the separation of substances from solutions and for thickening slurries|
    DE2050635C3|1970-10-15|1983-11-10|Otto Dürr Anlagenbau GmbH, 7000 Stuttgart|Method and device for separating paint and waste water|
    FR2206985B1|1972-11-22|1977-04-22|Saint Gobain Techn Nouvelles|
    US3925208A|1973-03-13|1975-12-09|Coate Burial Vault Inc|Aerobic sewage treatment system|
    GB1473665A|1973-05-16|1977-05-18|Ici Ltd|Treatment of biologically-degradable waste|
    US3794303A|1973-06-11|1974-02-26|B Hirshon|Method and apparatus for aerating bodies of water|
    JPS5938031B2|1974-05-16|1984-09-13|Imuperiaru Chem Ind Plc|
    JPS5312387B2|1974-09-30|1978-04-28|
    GB1527731A|1975-04-07|1978-10-11|Ici Ltd|Sewage treatment-flotation apparatus|
    JPS5524960A|1978-08-11|1980-02-22|Seiko Epson Corp|Watch armor products|GB1527731A|1975-04-07|1978-10-11|Ici Ltd|Sewage treatment-flotation apparatus|
    JPS541964U|1977-06-08|1979-01-08|
    JPS5845313B2|1977-09-10|1983-10-08|Kubota Ltd|
    JPS5448474U|1977-09-10|1979-04-04|
    JPS5728318B2|1978-01-20|1982-06-16|
    FI790165A|1978-02-06|1979-08-07|Itt|FOERFARANDE FOER SEKUNDAER BEHANDLING AV AVFALLSVATTEN|
    DE2805793A1|1978-02-11|1979-08-16|Hoechst Ag|METHOD FOR BIOLOGICAL PURIFICATION OF WASTE WATER|
    JPS5757198B2|1978-03-13|1982-12-03|Kubota Ltd|
    JPS5521053U|1978-07-25|1980-02-09|
    JPS5518268A|1978-07-25|1980-02-08|Kubota Ltd|Waste water treatment apparatus|
    JPS5720313Y2|1978-08-01|1982-04-30|
    JPS5549777U|1978-09-28|1980-04-01|
    DE2964035D1|1979-01-15|1982-12-16|Ici Plc|Process and apparatus for treatment of wastewater|
    GB2040276A|1979-01-29|1980-08-28|Paterson Candy Int|Treatment of biologically-degradable waste|
    EP0015680B1|1979-03-09|1982-06-30|Imperial Chemical Industries Plc|Fermentation process and apparatus|
    EP0021570B1|1979-05-23|1983-10-05|Imperial Chemical Industries Plc|Process and apparatus for the treatment of waste water|
    JPS5639198U|1979-09-04|1981-04-13|
    CA1115433A|1979-10-26|1981-12-29|David C.I. Pollock|Method for protecting a bioreactorpressurized head tank against extremesurges of influent waste water|
    CA1114963A|1979-10-26|1981-12-22|Canadian Industries Limited|Means for separation of gas and solids from wastemixed liquor|
    EP0037659B1|1980-04-03|1984-08-01|Imperial Chemical Industries Plc|Method and apparatus for the treatment of wastewater|
    JPS5750597A|1980-09-10|1982-03-25|Kubota Ltd|Water treatment device|
    NL8502330A|1985-08-23|1987-03-16|Mutlireaktor Bv|METHOD AND INSTALLATION FOR THE ANAEROBIC PURIFICATION OF WASTE WATER.|
    DE4411991A1|1994-04-11|1995-10-12|Hoechst Ag|Method and device for separating suspended substances from liquids|
    FR2733164B1|1995-04-21|1997-05-23|Degremont|DEVICE FOR THE BIOLOGICAL TREATMENT OF LIQUID, ESPECIALLY WASTE WATER|
    US5643459A|1995-04-26|1997-07-01|Cominco Engineering Services Ltd.|Flotation method and apparatus|
    US5650070A|1996-03-14|1997-07-22|Deep Shaft Technology Inc.|Aerobic long vertical shaft bioreactors|
    US5645726A|1996-03-14|1997-07-08|Deep Shaft Technology Inc.|Treatment of waste liquor in a vertical shaft bioreactor|
    US5660724A|1996-05-28|1997-08-26|Deep Shaft Technology Inc.|Multi-pressure head tank for use with vertical shaft bioreactors|
    US5755976A|1996-11-13|1998-05-26|Kortmann; Robert W.|Pneumatic bubble aeration reactor and method of using same|
    SE518105C2|2000-08-11|2002-08-27|Itt Mfg Enterprises Inc|Methods and apparatus for aerating liquids|
    WO2002072485A2|2001-02-23|2002-09-19|V.A.I. Ltd.|Methods and apparatus for biological treatment of waste waters|
    NL1017690C2|2001-03-26|2002-09-27|Paques Bio Syst Bv|Process and apparatus for anaerobically purifying an organic-containing slurry.|
    BR0301519B1|2003-05-30|2014-01-28|Coupling a sewage treatment plant - ETE to the flocculation and flotation treatment set of watercourses|
    US20050218074A1|2004-04-06|2005-10-06|Pollock David C|Method and apparatus providing improved throughput and operating life of submerged membranes|
    JP4591678B2|2004-12-14|2010-12-01|栗田工業株式会社|Biological treatment equipment|
    GB2451870A|2007-08-15|2009-02-18|United Utilities Plc|Method and Apparatus for Aeration|
    JP5408600B2|2008-05-28|2014-02-05|インターナショナル・ビジネス・マシーンズ・コーポレーション|Determination apparatus, database apparatus, program, and determination method|
    US7992845B1|2010-08-16|2011-08-09|Farrell Dean E|Counter current supersaturation oxygenation system|
    US8618522B2|2011-07-22|2013-12-31|Jerry L. McKinney|Flow through apparatus for UV disinfection of water|
    GB201323151D0|2013-12-31|2014-02-12|United Utilities Plc|Process|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    GB1414275A|GB1527731A|1975-04-07|1975-04-07|Sewage treatment-flotation apparatus|
    [返回顶部]