CN104261532A - Mechanical cyclone flocculation separation high-efficiency settling pond - Google Patents
Mechanical cyclone flocculation separation high-efficiency settling pond Download PDFInfo
- Publication number
- CN104261532A CN104261532A CN201410500586.8A CN201410500586A CN104261532A CN 104261532 A CN104261532 A CN 104261532A CN 201410500586 A CN201410500586 A CN 201410500586A CN 104261532 A CN104261532 A CN 104261532A
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- flocculation
- high efficiency
- zone
- cyclone
- central tube
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Links
- 238000005189 flocculation Methods 0.000 title claims abstract description 81
- 230000016615 flocculation Effects 0.000 title claims abstract description 65
- 238000000926 separation method Methods 0.000 title abstract description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 49
- 238000006243 chemical reaction Methods 0.000 claims abstract description 24
- 238000005352 clarification Methods 0.000 claims description 17
- 238000004062 sedimentation Methods 0.000 abstract description 13
- 238000001556 precipitation Methods 0.000 abstract description 7
- 229920002401 polyacrylamide Polymers 0.000 description 6
- 239000002245 particle Substances 0.000 description 5
- 239000000701 coagulant Substances 0.000 description 4
- 238000005345 coagulation Methods 0.000 description 4
- 230000015271 coagulation Effects 0.000 description 4
- 238000010276 construction Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 238000000746 purification Methods 0.000 description 4
- 101150103639 PB1 gene Proteins 0.000 description 2
- 230000001174 ascending effect Effects 0.000 description 2
- 239000003814 drug Substances 0.000 description 2
- 230000003311 flocculating effect Effects 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 239000013049 sediment Substances 0.000 description 2
- 239000010802 sludge Substances 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 239000000725 suspension Substances 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 230000001112 coagulating effect Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 229940079593 drug Drugs 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000003292 glue Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 230000001932 seasonal effect Effects 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000004575 stone Substances 0.000 description 1
- 230000001360 synchronised effect Effects 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
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
- C02F1/5236—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
- C02F1/54—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using organic material
- C02F1/56—Macromolecular compounds
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2201/00—Apparatus for treatment of water, waste water or sewage
- C02F2201/002—Construction details of the apparatus
Landscapes
- 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)
- Inorganic Chemistry (AREA)
- Separation Of Suspended Particles By Flocculating Agents (AREA)
- Cyclones (AREA)
Abstract
The invention discloses a mechanical cyclone flocculation separation high-efficiency settling pond which comprises a center cylinder, a cyclone device, a straight guide cylinder and a flocculation zone, wherein the flocculation zone is positioned on the outer side of the center cylinder, and the flocculation zone and the center cylinder are connected through the straight guide cylinder; the cyclone device is arranged on the upper part, and a central shaft of the cyclone device is coincided with the central shaft of the center cylinder; the cyclone device comprises a blade bracket and multiple blades; the blades are fixedly arranged on the blade bracket; a first reaction clarifying zone is formed in the lower half part of the center cylinder and is an inverted conical cavity; and the position of the straight guide cylinder corresponds to the position of the cyclone device. According to the mechanical cyclone flocculation separation high-efficiency settling pond disclosed by the invention, the contradiction that flocculation and precipitation in the flocculation basin cannot be organically unified in the traditional water supply treatment scheme is solved, and the problem that flocculation and pre-sedimentation cannot be realized on a first-level flocculation and pre-sedimentation section by virtue of hydraulic cyclone only after the size of a single pond is enlarged is solved.
Description
?
Technical field
The present invention relates to experiment equipment manufacturing technology field, especially a kind of mobile rifle for drug sensitive test paper.
Background technology
Take Huanghe water as the ultra of representative, particle concentration is high and fine and closely woven, time change fast, seasonal variation large (in turbid, the winter low temperature of summer high temperature height turbid or low-temperature and low turbidity).Traditional ultra's treatment technology adopts preliminary sedimentation in conjunction with the mode of coagulation clarification.Major cause is flocculation is necessary front and back process (well do not flocculate and just well do not precipitate) with precipitation, is again that synchronous crossover process (will aspire for stability, and could design constant volume, stablize the flocculation basin of gradient by the object of flocculation.But when if change of water quality scope is large, in flocculation basin, often produced precipitation, would often sacrifice flocculating effect during design and solve flocculation basin sedimentation problem, flocculate under this situation making change of water quality large and precipitated into conflict body).Existing settling pond process raw water turbidity subject range is less, and water outlet is poor under impact load, and follow-up filter tank burden is too heavy, and recoiled in filter tank frequent, not only after filter, water is not easy to obtain high-quality cleaning water, and energy consumption strengthens.And existing settling pond list pool size is little, the too high and complex structure of pond body structure, is difficult to construction, then affects cost, cannot be applied in large-scale or super-huge water factory; And single pool size becomes greatly, first step flocculation preliminary sedimentation section is depended merely on hydrocyclone to flocculate preliminary sedimentation and cannot be realized.In order to solve the problem, obligee of the present invention has invented the settling pond of this technology.
Summary of the invention
The present invention is directed to the deficiencies in the prior art, propose a kind of mechanical cyclone-flocculation and be separated high efficiency clarification tank, solving the flocculation of flocculation basin in traditional Water purification scheme and precipitation cannot the contradiction of organic unity, and solve and single pool size become large after, first step flocculation preliminary sedimentation section is depended merely on hydrocyclone and has been carried out the problem that flocculation preliminary sedimentation cannot realize.
To achieve these goals, the invention provides following technical scheme:
A kind of mechanical cyclone-flocculation is separated high efficiency clarification tank, comprises central tube, swirl-flow devices, straight guide shell, flocculation zone,
Described flocculation zone is positioned at outside described central tube, is connected therebetween by straight guide shell,
Described swirl-flow devices is arranged on described top, and axis overlaps with described central tube axis,
Described swirl-flow devices comprises blade rack and some blades, and described blade is fixed on described blade rack,
Described central tube Lower Half is the first reaction settling section, and described first reaction settling section is inverted conical cavity,
The position of described straight guide shell is corresponding with described swirl-flow devices position.
Further, described blade rack comprise central shaft and distributed to free end by the inboardend of described central shaft, length increases successively and some with blade connecting rod with described central axis,
Described each blade is fixed on each described blade connecting rod, and the described blade connecting rod that length is the shortest is fixed with two blades, and the lobe numbers on the described blade connecting rod that length is larger is greater than the number of described blade on the less described blade connecting rod of length.
Further, also comprise water inlet pipe, described water inlet pipe gos deep in described central tube, and its nozzle is positioned at below described swirl-flow devices, the top of described first reaction settling section.
Further, described flocculation zone has one or more, and when arranging multiple described flocculation zone, each described flocculation zone is uniformly distributed around described central tube.
Further, described flocculation zone Lower Half is the second reaction settling section, and described second reaction settling section is inverted conical cavity.
Further, in described straight guide shell bottom, be provided with the oblique flow deflector tiltedly had a down dip in described flocculation zone around described central tube outer wall,
In described flocculation zone, the position relative with described oblique flow deflector be provided with the fanning strip tiltedly had a down dip in described flocculation zone.
Further, the angle that described oblique flow deflector and described fanning strip tilt is more than or equal to 55 degree and is less than or equal to 70 degree.
Further, in the below of top end opening place, described flocculation zone, water leg, sieve plate is installed, described sieve plate is distributed with some through holes tilting to extend.
Further, the inner entirety of described settling pond is cubes.
A kind of mechanical cyclone-flocculation of the present invention is separated high efficiency clarification tank, solving the flocculation of flocculation basin in traditional Water purification scheme and precipitation cannot the contradiction of organic unity, and solve and single pool size become large after, first step flocculation preliminary sedimentation section is depended merely on hydrocyclone and has been carried out the problem that flocculation preliminary sedimentation cannot realize.
Accompanying drawing explanation
Fig. 1 is the structural representation that a kind of mechanical cyclone-flocculation of the present invention is separated high efficiency clarification tank.
Embodiment
Describe the present invention below in conjunction with accompanying drawing, the description of part of the present invention is only exemplary and explanatory, should not have any restriction to protection scope of the present invention.
One machinery cyclone-flocculation is as shown in Figure 1 separated high efficiency clarification tank, comprises central tube 1, swirl-flow devices, straight guide shell 4, flocculation zone 11,
Flocculation zone 11 is positioned at outside central tube 1, is connected therebetween by straight guide shell 4,
Swirl-flow devices is arranged on top, and axis overlaps with central tube 1 axis,
Swirl-flow devices comprises blade rack 121 and some blades 122, and blade 122 is fixed on blade rack 121, blade rack 121 by driving arrangement, as electric motor, driven rotary, and then band rotor blade 122 rotate,
Central tube 1 Lower Half is the first reaction settling section I, and the first reaction settling section I is inverted conical cavity,
The position of straight guide shell 4 is corresponding with swirl-flow devices position.
Blade rack 121 comprise central shaft and distributed to free end by the inboardend of central shaft, length increases successively and some with blade connecting rod 121a with central axis, is designed to three in the embodiment of the present invention,
Each blade 122 is fixed on each blade connecting rod 121a, the blade connecting rod 121a that length is the shortest is fixed with two blades 122, blade 122 number on the blade connecting rod 121a that length is larger is greater than the number of the less blade connecting rod 121a blade 122 of length, and in the embodiment of the present invention, three blade connecting rods fix two, four and six blades 122 successively.This design of swirl-flow devices, makes it form vertical gradient, utilizes low speed to promote eddy flow and forms eddy flow energy gradient from bottom to top.High turbidity raw sewage directly enters in pond, eddy flow is formed under the pushing effect of swirl-flow devices, mutual Collision coagulation between water-borne glue body particle is made to carry out incorgruous flocculation formation flocculation preliminary sedimentation gradient from bottom to top, solving the flocculation of flocculation basin in traditional Water purification scheme and precipitation cannot the contradiction of organic unity, finally realizes high efficient solid and liquid separation.The swirl-flow devices set up and first reacts settling section I and designs and combine, be conducive to mud-water separation, greatly reduce the water ratio of spoil disposal water, save subsequent set mud sump volume, a difficult problem for spoil disposal difficulty when simultaneously also solving traditional settling tank coagulating kinetics ultra.Winter low temperature low turbidity raw water directly enters in central tube 1, and the existence of the suspension slime layer that the promotion due to swirl-flow devices in central tube 1 is formed, solves the unmanageable difficult problem of low temperature and low turbidity water.By the design to swirl-flow devices, swirl-flow devices can be made to change rotating speed to ensure flocculating effect with the change of water quality, the water yield, the water factory of any scale can be applied to.
Also comprise water inlet pipe 1, water inlet pipe 1 gos deep in central tube 1, and its nozzle 2 is positioned at below swirl-flow devices, the top of the first reaction settling section I.
Flocculation zone 11 has one or more, and when arranging multiple flocculation zone 11, each flocculation zone 11 is uniformly distributed around central tube 1.
Flocculation zone 11 Lower Half is the second reaction settling section II, second reaction settling section II is inverted conical cavity, sludge out pipe 10 has many, and the entrance end of sludge out pipe 10 is positioned at the bottom of the first reaction settling section I and second reaction settling section II, and exit end stretches out settling pond 100.The design of the second reaction settling section II, make spoil disposal smooth and easy, spoil disposal solid content is high.
In straight guide shell 4 bottom, be provided with the oblique flow deflector 5 tiltedly had a down dip in flocculation zone 11 around central tube 1 outer wall,
In flocculation zone 11, the position relative with oblique flow deflector 5 be provided with the fanning strip 6 tiltedly had a down dip in flocculation zone 11.
The angle that oblique flow deflector 5 and fanning strip 6 tilt is more than or equal to 55 degree and is less than or equal to 70 degree.
Be provided with sieve plate 7 in the below of top end opening place, flocculation zone 11, water leg 8, sieve plate 7 is distributed with some through holes tilting to extend, water leg 8 is connected with rising pipe.
The inner entirety of settling pond 100 is cubes.Adopt this design, teaming method is flexible, can share pool wall, reduce construction costs and difficulty of construction, be applicable to the large-scale water treatment scale that raw water quality variation range is large, save floor occupying area, decrease construction investment between the body of pond.
When the present invention uses, former water enters water inlet pipe 1 through water pump lifting, inorganic coagulant (as PB1 gene) or high-molecular coagulant adopting (as polyacrylamide PAM) is added at water inlet pipe 1 streamline central point, line mixer is relied on to complete the blending dispersion of medicament, former water flows after certain hour in the duct, add high-molecular coagulant adopting (as polyacrylamide PAM) or inorganic coagulant (as PB1 gene) in reducing place of the nozzle 2 of water inlet pipe 1, rely on submerged orifice outflow to complete instantaneous mixing; According to the difference of former water sediment concentration, during high sediment concentration, PAM adds at water inlet pipe 1 line mixer, and PAC adds in reducing place; During low sand-carrying capacity, PAC adds at water inlet pipe 1 line mixer, and PAM adds in reducing place; Former water enters central tube 1 by the eccentric reducing of water inlet pipe 1 nozzle 2, forms eddy flow state by swirl-flow devices, relies on swirl-flow devices pushing effect to form eddy flow and makes the mutual Collision coagulation of suspended particle, reach the effect of flocculation in central tube 1; The eddy flow stiffened region of water inlet pipe 1 nozzle more than 2 provides the higher turbulence intensity needed for the coagulation initial stage, higher upflow velocity completes the waterpower sorting of granular flocs unit simultaneously, namely Large stone, closely knit particle rely on gravity to overcome the jacking force of ascending current, be settled down to the first reaction settling section I of central tube 1 bottom, complete solid-liquid separation; The flocs unit of small particle size, is constantly grown up into the fine particle in water by catching at ascending current backwater effect low suspension in water.Former water enters after central tube 1 completes eddy flow, after straight guide shell 4 carries out fluid stable, routs up and enters flocculation zone 11, along with water-carrying section increase, flow velocity diminishes gradually, complete flco and grow up.The sieve plate 7 set up at top, flocculation zone 11 controls remaining flco in water further.Mud sinks in the first reaction settling section I and second reaction settling section II, because hydrostaticpressure is powerful, when opening mud valve, producing very high flow velocity, mud is discharged very smoothly.The conical design of the first reaction settling section I and second reaction settling section II, and the suction produced when swirl-flow devices promotes eddy flow and spoil disposal is all spoil disposal reason smoothly with promoting.
A kind of mechanical cyclone-flocculation of the present invention is separated high efficiency clarification tank, solving the flocculation of flocculation basin in traditional Water purification scheme and precipitation cannot the contradiction of organic unity, and solve and single pool size become large after, first step flocculation preliminary sedimentation section is depended merely on hydrocyclone and has been carried out the problem that flocculation preliminary sedimentation cannot realize.
Claims (9)
1. mechanical cyclone-flocculation is separated a high efficiency clarification tank, it is characterized in that, comprises central tube, swirl-flow devices, straight guide shell, flocculation zone,
Described flocculation zone is positioned at outside described central tube, is connected therebetween by straight guide shell,
Described swirl-flow devices is arranged on described top, and axis overlaps with described central tube axis,
Described swirl-flow devices comprises blade rack and some blades, and described blade is fixed on described blade rack,
Described central tube Lower Half is the first reaction settling section, and described first reaction settling section is inverted conical cavity,
The position of described straight guide shell is corresponding with described swirl-flow devices position.
2. a kind of mechanical cyclone-flocculation is separated high efficiency clarification tank as claimed in claim 1, it is characterized in that, described blade rack comprise central shaft and distributed to free end by the inboardend of described central shaft, length increases successively and some with blade connecting rod with described central axis
Described each blade is fixed on each described blade connecting rod, and the described blade connecting rod that length is the shortest is fixed with two blades, and the lobe numbers on the described blade connecting rod that length is larger is greater than the number of described blade on the less described blade connecting rod of length.
3. a kind of mechanical cyclone-flocculation is separated high efficiency clarification tank as claimed in claim 1, and it is characterized in that, also comprise water inlet pipe, described water inlet pipe gos deep in described central tube, and its nozzle is positioned at below described swirl-flow devices, the top of described first reaction settling section.
4. a kind of mechanical cyclone-flocculation is separated high efficiency clarification tank as claimed in claim 1, and it is characterized in that, described flocculation zone has one or more, and when arranging multiple described flocculation zone, each described flocculation zone is uniformly distributed around described central tube.
5. a kind of mechanical cyclone-flocculation is separated high efficiency clarification tank as claimed in claim 1, and it is characterized in that, described flocculation zone Lower Half is the second reaction settling section, and described second reaction settling section is inverted conical cavity.
6. as described in claim 1 or 5, a kind of mechanical cyclone-flocculation is separated high efficiency clarification tank, it is characterized in that, in described straight guide shell bottom, is provided with the oblique flow deflector tiltedly had a down dip in described flocculation zone around described central tube outer wall,
In described flocculation zone, the position relative with described oblique flow deflector be provided with the fanning strip tiltedly had a down dip in described flocculation zone.
7. a kind of mechanical cyclone-flocculation is separated high efficiency clarification tank as claimed in claim 6, and it is characterized in that, the angle that described oblique flow deflector and described fanning strip tilt is more than or equal to 55 degree and is less than or equal to 70 degree.
8. a kind of mechanical cyclone-flocculation is separated high efficiency clarification tank as claimed in claim 6, it is characterized in that, is provided with sieve plate in the below of top end opening place, described flocculation zone, water leg, described sieve plate is distributed with some through holes tilting to extend.
9. a kind of mechanical cyclone-flocculation is separated high efficiency clarification tank as claimed in claim 1, it is characterized in that, the inner entirety of described settling pond is cubes.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410500586.8A CN104261532B (en) | 2014-09-26 | 2014-09-26 | Mechanical cyclone flocculation separation high-efficiency settling pond |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410500586.8A CN104261532B (en) | 2014-09-26 | 2014-09-26 | Mechanical cyclone flocculation separation high-efficiency settling pond |
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| Publication Number | Publication Date |
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| CN104261532A true CN104261532A (en) | 2015-01-07 |
| CN104261532B CN104261532B (en) | 2017-02-01 |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104692508A (en) * | 2015-03-26 | 2015-06-10 | 杭州电子科技大学 | Flocculating basin with arc blade vortex generators and flocculating method thereof |
| CN106746013A (en) * | 2017-01-09 | 2017-05-31 | 甘肃金桥水科技（集团）股份有限公司 | A kind of high efficiency clarification tank and ultrafiltration group technology |
| CN108002500A (en) * | 2017-12-20 | 2018-05-08 | 中国华电集团科学技术研究总院有限公司 | Cyclone-flocculation device and the high turbid wastewater processing system of coal-burning power plant's high salt and application |
| CN110342621A (en) * | 2019-05-27 | 2019-10-18 | 安徽理工大学 | A kind of processing equipment of two sections of concentration and settlements high concentration beneficiation wastewater |
| CN116062868A (en) * | 2023-03-23 | 2023-05-05 | 北京东方启源环保科技有限公司 | Spiral-flow flocculation clarification device and method |
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Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104692508A (en) * | 2015-03-26 | 2015-06-10 | 杭州电子科技大学 | Flocculating basin with arc blade vortex generators and flocculating method thereof |
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| CN108002500B (en) * | 2017-12-20 | 2020-07-14 | 中国华电集团科学技术研究总院有限公司 | Rotational flow flocculation device, high-salinity high-turbidity wastewater treatment system of coal-fired power plant and application |
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| CN116062868A (en) * | 2023-03-23 | 2023-05-05 | 北京东方启源环保科技有限公司 | Spiral-flow flocculation clarification device and method |
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| Publication number | Publication date |
|---|---|
| CN104261532B (en) | 2017-02-01 |
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