WO2016157645A1 - 急速撹拌機 - Google Patents
急速撹拌機 Download PDFInfo
- Publication number
- WO2016157645A1 WO2016157645A1 PCT/JP2015/085528 JP2015085528W WO2016157645A1 WO 2016157645 A1 WO2016157645 A1 WO 2016157645A1 JP 2015085528 W JP2015085528 W JP 2015085528W WO 2016157645 A1 WO2016157645 A1 WO 2016157645A1
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- WIPO (PCT)
- Prior art keywords
- rapid
- blade
- drive shaft
- tank body
- tank
- Prior art date
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Classifications
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
- C02F11/14—Treatment of sludge; Devices therefor by de-watering, drying or thickening with addition of chemical agents
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/50—Mixing liquids with solids
- B01F23/53—Mixing liquids with solids using driven stirrers
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/05—Stirrers
- B01F27/11—Stirrers characterised by the configuration of the stirrers
- B01F27/112—Stirrers characterised by the configuration of the stirrers with arms, paddles, vanes or blades
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/80—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis
- B01F27/808—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis with stirrers driven from the bottom of the receptacle
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/80—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis
- B01F27/84—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis with two or more stirrers rotating at different speeds or in opposite directions about the same axis
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/80—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis
- B01F27/85—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis with two or more stirrers on separate shafts
- B01F27/851—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis with two or more stirrers on separate shafts the receptacle being subdivided in adjacent compartments
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/80—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis
- B01F27/87—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis the receptacle being divided into superimposed compartments
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/80—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis
- B01F27/90—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis with paddles or arms
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/80—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis
- B01F27/90—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis with paddles or arms
- B01F27/902—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis with paddles or arms cooperating with intermeshing elements fixed on the receptacle walls
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/80—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis
- B01F27/91—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis with propellers
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- 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
- C02F1/5281—Installations for water purification using chemical agents
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F2101/00—Mixing characterised by the nature of the mixed materials or by the application field
- B01F2101/305—Treatment of water, waste water or sewage
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F2215/00—Auxiliary or complementary information in relation with mixing
- B01F2215/04—Technical information in relation with mixing
- B01F2215/0413—Numerical information
- B01F2215/0418—Geometrical information
- B01F2215/0431—Numerical size values, e.g. diameter of a hole or conduit, area, volume, length, width, or ratios thereof
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
- C02F11/14—Treatment of sludge; Devices therefor by de-watering, drying or thickening with addition of chemical agents
- C02F11/147—Treatment of sludge; Devices therefor by de-watering, drying or thickening with addition of chemical agents using organic substances
Definitions
- the present invention relates to an agglomeration and mixing technique used in water treatment facilities and the like, and relates to a rapid agitator that rapidly agitates and mixes a flocculant and raw water.
- Patent Document 1 As a conventional agglomeration mixing tank, for example, there is one described in Patent Document 1.
- stirring blades are arranged in two upper and lower stages, and a slurry to which a flocculant is added is supplied in an upward flow to be stirred and mixed.
- the agglomeration mixing tank is divided into a rapid stirring section in the lower half and a slow stirring section in the upper half, and the barrel inner diameter of the rapid stirring section is smaller than the barrel inner diameter of the slow stirring section.
- the rapid stirring section has a rapid stirring blade and a drive shaft that drives the rapid stirring blade.
- the rapid stirring blade is composed of a turbine blade, and the turbine blade has a plurality of blade plates radially arranged around the drive shaft on the surface of the rotating plate.
- the slow stirring section has a slow stirring blade and a drive shaft for driving the slow stirring blade, and the slow stirring blade is composed of a flat paddle blade.
- a flocculant is dispersed in the water to be treated to form a core for forming a floc floc, and turbidity in the water to be treated is aggregated around the core to form a fine floc.
- the flocculant is not rapidly and sufficiently dispersed, the formation of fine flocs becomes insufficient, which inhibits the formation of flocculent flocs during slow stirring, resulting in subsequent processes such as dehydrators and concentrators. Dehydration performance is a factor.
- the turbine blades are arranged near the bottom of the tank of the rapid stirring section, and the rotation of the turbine blades causes all of the fluid to be pushed upward as a strong upward flow. Variations occur in the residence time in which the treated water and the flocculant stay in the tank, thereby inhibiting the formation of fine flocs.
- This invention solves the above-mentioned subject, and it aims at providing the rapid stirrer which can aim at the reduction of power consumption which can disperse
- a rapid stirrer of the present invention comprises a tank body for stirring sludge and a flocculant, a drive shaft disposed inside the tank body, and a shear type stirring blade attached to the drive shaft.
- the shear type agitating blades are arranged along at least one of the front side and the back side in the axial direction of the drive shaft along a virtual circle centered on the axis of the drive shaft, and the axis of the drive shaft It has the turbine blade which stood up in the center direction.
- the turbine blade is arranged along a tangential direction of an imaginary circle having the center of the axis of the drive shaft as a center point.
- the shear type stirring blade has a rotating plate that rotates integrally with the drive shaft, and has a turbine blade on the outer peripheral edge in the radial direction of the rotating plate.
- the shear type stirring blade is an edged turbine blade.
- the shear type stirring blade is disposed at a position separated from the bottom of the tank body by a predetermined distance, and there is a space between the shear type stirring blade and the bottom of the tank body. To do.
- the shear type stirring blade is located at a position facing the sludge inlet.
- the ratio d1 / D1 between the diameter d1 of the circumscribed circle circumscribing the shear type stirring blade and the inner diameter D1 of the tank body is 0.6 or more.
- the agglomeration and mixing apparatus of the present invention is a rapid agitation apparatus in which a slow agitator is disposed above a rapid agitator and the tank top of the rapid agitator communicates with the tank bottom of the slow agitator.
- the machine is characterized in that it is any one of the rapid agitators mentioned above.
- the diameter of the opening communicating with the tank top of the rapid agitator and the tank bottom of the slow agitator is smaller than the inner diameter of the tank of the rapid agitation tank.
- the slow agitator is provided with paddle blades arranged in a plurality of stages, and the paddle blade on the quick agitator side has a diameter d2 of a circumscribed circle circumscribing the paddle blade and an inner diameter D2 of the tank body.
- the ratio d2 / D2 is 0.6 or more
- the next paddle blade has a ratio d3 / D3 of a circumscribed circle diameter d3 circumscribing the paddle blade and an inner diameter D3 of the tank body of 0.8 or more.
- the sludge treatment system of the present invention includes any one of the above-described coagulation and mixing apparatuses, and is characterized in that a dehydrator is disposed in a subsequent process of the coagulation and mixing apparatus.
- the sludge treatment system of the present invention includes any one of the above-described coagulation and mixing devices, and is characterized in that a concentrator is disposed in a subsequent process of the coagulation and mixing device.
- the edged turbine blades are rotated in the tank body by the rotation of the drive shaft, and the sludge and the flocculant are stirred in the tank body.
- the flocculant supplied in the tank stays in a lump in the sludge, but the turbine blade cuts into the flocculant lump in a blade shape and atomizes the flocculant by a shearing action and disperses it. Therefore, a large amount of agglomerated floc-forming nuclei, which are nuclei for forming agglomerated flocs, are rapidly generated in the sludge.
- the contact frequency between the solid fine particles in the sludge and the aggregated floc-forming nuclei is sufficiently ensured for a predetermined time in which the flocculant and the sludge stay in the tank, and a large amount of fine flocs are generated.
- a fine and uniform floc is stably generated in the rapid stirrer, and the floc is flocculated by the slow stirrer, so that a floc having a predetermined size suitable for dehydration can be stably generated.
- Sectional drawing which shows the aggregation mixing apparatus in embodiment of this invention Schematic showing the edged turbine blade in the same embodiment Chart showing the specifications of the rapid stirrer used in the experiment
- the graph which shows the shaft power measurement result of Example 1 The graph which shows the shaft power measurement result of Example 2.
- the graph which shows the moisture content reduction result with the paddle blade in Example 2, and an edged turbine blade The top view which shows the edged turbine blade in other embodiment of this invention Cross section of the edged turbine blade
- the top view which shows the edged turbine blade in other embodiment of this invention Cross section of the edged turbine blade The top view which shows the edged turbine blade in other embodiment of this invention Cross section of the edged turbine blade
- the top view which shows the edged turbine blade in other embodiment of this invention Cross section of the edged turbine blade The top view which shows the edged turbine blade in other embodiment of this invention Cross section of the edged turbine blade.
- the agglomeration and mixing apparatus 100 includes a rapid stirrer 10 and a slow stirrer 50, and the slow stirrer 50 is disposed above the rapid stirrer 10, so The ceiling 11 and the tank bottom 51 of the slow agitator 50 communicate with each other at the opening 12.
- the rapid agitator 10 includes a rapid agitation tank body 13 for agitating the sludge and the flocculant, and the opening 12 communicating the rapid agitator 10 and the slow agitator 50 has a diameter of the rapid agitation tank body 13.
- the tank ceiling part 11 exists in an annular shape around the opening 12.
- the sludge is a slurry substance such as sewage sludge
- the flocculant is a polymer flocculant or the like.
- the rapid stirring tank body 13 has a cylindrical shape of about ⁇ 300 mm, has a sludge inlet 14 for supplying sludge to one side of the side wall of the rapid stirring tank body 13, and supplies flocculant to the other side.
- the sludge inflow port 14 and the flocculant supply port 15 are located at the same level in the tank axis direction (height direction) of the rapid stirring tank body 13.
- a drive shaft 16 is arranged vertically along the tank body axis, and an edged turbine blade 17 is attached to the drive shaft 16.
- a motor 18 that rotationally drives the drive shaft 16 is provided outside the bottom of the rapid stirring tank body 13.
- the edged turbine blade 17 has a rotating plate 19 that rotates integrally with the drive shaft 16, and has a plurality of turbine blades 20 raised in the axial direction of the drive shaft 16 on the outer peripheral edge in the radial direction of the rotating plate 19. is doing.
- the turbine blade 20 has a blade shape specialized for the shearing action, and the front edge in the rotational direction has a receding angle.
- the turbine blade 20 is provided on both the front surface side and the back surface side in the axial direction of the drive shaft 16 of the rotating plate 19, but it can also be provided only on either one surface side, It is also possible to arrange on the plate surface of the plate 19.
- the turbine blades 20 in the radially arranged spokes 191.
- the turbine blades 20 facing upward are arranged.
- the turbine blade 20 faces downward on the radially outer peripheral edge of the rotating plate 19.
- the turbine blades 20 that face each other and be configured to bend the rear end in the rotational direction of the turbine blades 20 radially inward.
- the plurality of turbine blades 20 are arranged along an imaginary circle centered on the axis of the drive shaft 16 and are arranged along the tangential direction of the imaginary circle to form a shape specialized for shearing action. .
- the turbine blade 20 may have a slight inclination angle with respect to the tangential direction.
- the position of the edged turbine blade 17 in the tank body axial direction (height direction) of the rapid stirring tank body 13 is not limited, and the edged turbine blade 17 is predetermined from the tank bottom 21 of the rapid stirring tank body 13. It is disposed at a position separated by a distance, and it is sufficient that a space exists between the edged turbine blade 17 and the tank bottom 21. This space is the space capacity required for the swirling flow of sludge and flocculant.
- the sludge and the flocculant flowing into the rapid stirring tank body 13 can be immediately sheared and stirred, so that the space between the tank body bottom 21 can be secured sufficiently.
- the size of the edged turbine blade 17 is such that the ratio D1 / D2 between the diameter D1 of the circumscribed circle circumscribing the edged turbine blade 17 and the inner diameter D2 of the rapid stirring tank body 13 is 0.6 or more, preferably 0.8 ⁇ It satisfies the condition of 0.9.
- the edged turbine blade 17 having this configuration weakens the force of pushing the sludge and the flocculant upward, and the sludge and the flocculant are retained inside the rapid stirring tank body 13 to sufficiently give the action of shearing and stirring. Can do.
- paddle blades 531, 532, 533 are arranged in a plurality of stages inside the slow stirring tank body 52, and each paddle blade 531, 532, 533 is composed of a plurality of paddles 55, and a plurality of paddle blades are provided. 55 is arranged radially from the axis of the drive shaft 54 on the drive shaft 54 arranged vertically along the tank body axis.
- the paddle blade 531 on the side close to the rapid agitator 10 has a ratio d2 / D2 between the diameter d2 of the circumscribed circle circumscribing the paddle blade 531 and the inner diameter D2 of the tank body of 0.6 or more.
- the ratio d3 / D3 between the diameter d3 of the circumscribed circle circumscribing the paddle blade and the inner diameter D3 of the tank body is 0.8 or more.
- a motor 56 that rotationally drives the drive shaft 54 is provided outside the upper portion of the slow stirring tank body 52.
- An agglomerated sludge outlet 57 is provided at an upper position on the side wall of the slow stirring tank body 52, and a dehydrator (not shown) is disposed in a subsequent process following the agglomerated sludge outlet 57 of the agglomeration and mixing apparatus 100.
- Configures a sludge treatment system It is also possible to configure a sludge treatment system by arranging a concentrator instead of this dehydrator (not shown).
- the drive shaft 16 is rotationally driven by the motor 18, the edged turbine blade 17 is rotated inside the rapid stirring tank body 13, and the sludge and the flocculant are stirred and mixed.
- These swirling flows can prevent a short path from the rapid stirring tank body 13 to the slow stirring tank body 52, and can secure a time for the flocculant and sludge to stay in the tank.
- the flocculant supplied to the inside of the rapid stirring tank 13 stays in a lump in the sludge, but the turbine blade 20 cuts into the flocculant lump in a blade shape, and the flocculant is atomized by a shearing action. Since they are dispersed, agglomerated floc-forming nuclei serving as nuclei for forming agglomerated flocs are generated in a large amount and rapidly in the sludge.
- the turbine blade 20 cuts through the flocculant in a blade shape, and the sludge turns into a swirl flow into the space between the edged turbine blade 17 and the tank bottom of the rapid stirring tank body 13, The occurrence of upward flow in the tank is suppressed. As a result, the dispersion of sludge and flocculant residence time due to the short path is reduced, and the dewatering performance of the floc flocs in the dehydrator can be stabilized.
- the turbine blade 20 rotates like a blade in the sludge, so that the liquid circulation action can be suppressed, power loss can be reduced, and power consumption can be reduced.
- the sludge in which fine flocs are formed in the rapid stirring tank body 13 flows into the slow stirring tank body 52 of the slow stirring machine 50 from the opening 12.
- the drive shaft 54 is rotated by a motor 56, and the paddle blade 53 is rotated in the sludge at a slow speed.
- Sludge containing fine flocs is gently agitated by the first-stage paddle blade 53 of the slow agitator 50 and granulated.
- the granulated floc is agitated more strongly by the next paddle blade 53 than the first paddle blade 53, the excessively granulated floc is decomposed and densified, and becomes an aggregated floc having a small particle size and not easily broken. .
- the moisture content of the dehydrated cake is reduced.
- FIG. 3 shows the specifications of the rapid stirrer of Example 1 and Example 2.
- FIG. 4 is a graph showing the shaft power measurement result of Example 1.
- FIG. 5 is a graph showing the shaft power measurement results of Example 2.
- FIG. 6 is a graph showing the moisture content reduction results of the paddle blade and the edged turbine blade in Example 2.
- the shaft power becomes 0.143 kW when the rotational speed reaches 711 times / min.
- the shaft power is 0.0216 kW even when the rotational speed reaches 711 times / minute, and it is clear that the shaft power required to drive the edged turbine blade is much smaller than that of the conventional paddle blade. It is.
- Fig. 6 shows that when edged turbine blades are used, the shaft power is smaller and the moisture content reduction effect is better than when paddle blades are used. This indicates that when an edged turbine blade is used, floc formation is good, and as a result, the moisture content of dewatered sludge in a dehydrator such as a screw press decreases. Therefore, the superiority of the edged turbine blade over the paddle blade in dewatering efficiency is clear.
- the present invention is applied to a sludge treatment system using a dehydrator or a concentrator.
- the present invention can be applied to any treatment system having a coagulation action, for example, coagulation.
- the present invention is also applicable to a coagulation sedimentation processing system using a sedimentation tank, other processing systems, and the like.
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Organic Chemistry (AREA)
- Dispersion Chemistry (AREA)
- Mixers Of The Rotary Stirring Type (AREA)
- Treatment Of Sludge (AREA)
Abstract
Description
緩速撹拌槽体52の側壁の上部位置には凝集汚泥流出口57が設けられており、凝集混和装置100の凝集汚泥流出口57に続く後工程には脱水機(図示省略)が配置されて汚泥処理システムを構成している。この脱水機(図示省略)に替えて濃縮機を配置して汚泥処理システムを構成することも可能である。
Claims (12)
- 汚泥と凝集剤を撹拌するための槽体と、槽体の内部に配置した駆動軸と、駆動軸に装着したせん断型撹拌翼を備え、
せん断型撹拌翼は、駆動軸の軸心方向における表面側と裏面側の少なくとも一方面側に、駆動軸の軸心を中心点とする仮想円に沿って配列し、かつ駆動軸の軸心方向に起ち上がったタービンブレードを有することを特徴とする急速撹拌機。 - タービンブレードは、駆動軸の軸心を中心点とする仮想円の接線方向に沿って配置することを特徴とする請求項1に記載の急速撹拌機。
- せん断型撹拌翼は、駆動軸と一体に回転する回転板を有し、回転板の半径方向外周縁にタービンブレードを有することを特徴とする請求項1または2に記載の急速撹拌機。
- せん断型撹拌翼はエッジドタービン翼であることを特徴とする請求項3に記載の急速撹拌機。
- せん断型撹拌翼は、槽体の底部から所定距離だけ隔てた位置に配置し、せん断型撹拌翼と槽体の底部との間にスペースが存在することを特徴とする請求項1から4の何れか1項に記載の急速撹拌機。
- せん断型撹拌翼は汚泥流入口に対向する位置にあることを特徴とする請求項5に記載の急速撹拌機。
- せん断型撹拌翼に外接する外接円の直径d1と槽体の内径D1との比d1/D1が0.6以上であることを特徴とする請求項1から6の何れか1項に記載の急速撹拌機。
- 急速撹拌機の上方に緩速撹拌機を配置し、急速撹拌機の槽体天井部と緩速撹拌機の槽体底部とが連通する凝集混和装置において、急速撹拌機が請求項1から7の何れか1項に記載の急速撹拌機であることを特徴とする凝集混和装置。
- 急速撹拌機の槽体天井部と緩速撹拌機の槽体底部とが連通する開口部の口径が急速撹拌槽体の槽体の内径より小さいことを特徴とする請求項8に記載の凝集混和装置。
- 緩速撹拌機は複数段に配置したパドル翼を備え、急速撹拌機側のパドル翼は、パドル翼に外接する外接円の直径d2と槽体の内径D2との比d2/D2が0.6以上であり、次段のパドル翼はパドル翼に外接する外接円の直径d3と槽体の内径D3との比d3/D3が0.8以上であることを特徴とする請求項8または9に記載の凝集混和装置。
- 請求項8から10の何れか1項に記載の凝集混和装置を備え、凝集混和装置の後工程に脱水機を配置したことを特徴とする汚泥処理システム。
- 請求項8から10の何れか1項に記載の凝集混和装置を備え、凝集混和装置の後工程に濃縮機を配置したことを特徴とする汚泥処理システム。
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CA2978533A CA2978533C (en) | 2015-03-31 | 2015-12-18 | Rapid stirring machine |
JP2017509175A JP6609624B2 (ja) | 2015-03-31 | 2015-12-18 | 凝集混和装置 |
US15/559,957 US10369535B2 (en) | 2015-03-31 | 2015-12-18 | Rapid stirring machine |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2015-070483 | 2015-03-31 | ||
JP2015070483 | 2015-03-31 |
Publications (1)
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WO2016157645A1 true WO2016157645A1 (ja) | 2016-10-06 |
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Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2002307100A (ja) * | 2001-02-08 | 2002-10-22 | Saitama Livestock Farm Ltd | 汚泥処理方法 |
JP2004267880A (ja) * | 2003-03-07 | 2004-09-30 | Kansai Kako Kk | 有機性汚泥の処理方法及び処理システム |
JP2008168215A (ja) * | 2007-01-12 | 2008-07-24 | Ishigaki Co Ltd | 二段式凝集混和槽 |
JP2012179579A (ja) * | 2011-03-03 | 2012-09-20 | Kubota Corp | 凝集反応装置および凝集反応方法 |
Family Cites Families (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2891777A (en) * | 1955-03-08 | 1959-06-23 | Pittsburgh Plate Glass Co | Glass stirring mechanism |
JPS59203632A (ja) * | 1983-05-06 | 1984-11-17 | Fuji Photo Film Co Ltd | 乳化方法 |
JP2001257218A (ja) * | 2000-03-10 | 2001-09-21 | Sony Corp | 微細チップの実装方法 |
CA2349252C (en) * | 2000-10-13 | 2007-05-22 | Fkc Co., Ltd. | Sludge dewatering and pasteurization system and method |
JP4354341B2 (ja) * | 2004-06-11 | 2009-10-28 | 花王株式会社 | 反応装置 |
WO2010117457A2 (en) * | 2009-04-08 | 2010-10-14 | Applied Biosystems, Llc | System comprising dual-sided thermal cycler and emulsion pcr in pouch |
-
2015
- 2015-12-18 US US15/559,957 patent/US10369535B2/en active Active
- 2015-12-18 CA CA2978533A patent/CA2978533C/en active Active
- 2015-12-18 WO PCT/JP2015/085528 patent/WO2016157645A1/ja active Application Filing
- 2015-12-18 JP JP2017509175A patent/JP6609624B2/ja active Active
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2002307100A (ja) * | 2001-02-08 | 2002-10-22 | Saitama Livestock Farm Ltd | 汚泥処理方法 |
JP2004267880A (ja) * | 2003-03-07 | 2004-09-30 | Kansai Kako Kk | 有機性汚泥の処理方法及び処理システム |
JP2008168215A (ja) * | 2007-01-12 | 2008-07-24 | Ishigaki Co Ltd | 二段式凝集混和槽 |
JP2012179579A (ja) * | 2011-03-03 | 2012-09-20 | Kubota Corp | 凝集反応装置および凝集反応方法 |
Cited By (9)
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---|---|---|---|---|
CN107159044A (zh) * | 2017-06-30 | 2017-09-15 | 中山市程博工业产品设计有限公司 | 一种效果好的润滑油生产搅拌装置 |
CN107820818A (zh) * | 2017-11-30 | 2018-03-23 | 王成科 | 一种园林绿化用树木施肥装置 |
CN107915266A (zh) * | 2017-12-04 | 2018-04-17 | 东莞市天合机电开发有限公司 | 一种具有离心滑行式的过滤框的废水处理装置 |
CN108945999A (zh) * | 2018-05-30 | 2018-12-07 | 永春县裕顺工业设计有限公司 | 一种环保污泥处理用污泥输送装置 |
CN109019792A (zh) * | 2018-07-17 | 2018-12-18 | 安徽原上草节能环保科技有限公司 | 一种城市废水沉淀处理池 |
CN109052805A (zh) * | 2018-07-17 | 2018-12-21 | 安徽原上草节能环保科技有限公司 | 一种城市污水处理工艺 |
CN109279670A (zh) * | 2018-10-15 | 2019-01-29 | 佛山市思特四通化工有限公司 | 一种化学工业废水处理用水处理药剂投放装置 |
CN109200922A (zh) * | 2018-10-19 | 2019-01-15 | 颜全聪 | 一种应用于工业废水处理的循环处理系统 |
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JPWO2016157645A1 (ja) | 2018-02-01 |
CA2978533C (en) | 2023-01-10 |
US10369535B2 (en) | 2019-08-06 |
JP6609624B2 (ja) | 2019-11-20 |
CA2978533A1 (en) | 2016-10-06 |
US20180104661A1 (en) | 2018-04-19 |
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