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CN109437380A - A kind of hydraulic cyclone formula sewage-treatment plant - Google Patents

A kind of hydraulic cyclone formula sewage-treatment plant Download PDF

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Publication number
CN109437380A
CN109437380A CN201811517828.9A CN201811517828A CN109437380A CN 109437380 A CN109437380 A CN 109437380A CN 201811517828 A CN201811517828 A CN 201811517828A CN 109437380 A CN109437380 A CN 109437380A
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CN
China
Prior art keywords
sewage
water
flocculant
tank
pipe
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
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CN201811517828.9A
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Chinese (zh)
Inventor
杨胜发
胡江
付旭辉
宋媛媛
张鹏
曹长来
唐定丹
王硕
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Chongqing Jiao Power Science & Technology Co Ltd
Chongqing Jiaotong University
Original Assignee
Chongqing Jiao Power Science & Technology Co Ltd
Chongqing Jiaotong University
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Application filed by Chongqing Jiao Power Science & Technology Co Ltd, Chongqing Jiaotong University filed Critical Chongqing Jiao Power Science & Technology Co Ltd
Priority to CN201811517828.9A priority Critical patent/CN109437380A/en
Publication of CN109437380A publication Critical patent/CN109437380A/en
Pending legal-status Critical Current

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    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/52Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
    • C02F1/5281Installations for water purification using chemical agents

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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)
  • Separation Of Suspended Particles By Flocculating Agents (AREA)

Abstract

本发明公开了一种水力旋流式污水处理装置,包括旋流池,旋流池上部沿切向设置有旋流池进水口,旋流池进水口上方的侧壁上设有溢流口以供处理后的污水排出;旋流池底部设有底孔以供沉积物排出;其特征在于,还包括设置于旋流池上方的水箱,水箱的进水口连接有抽水管和污水源相连,且在抽水管上设有抽水泵;水箱底部的出水口与旋流池进水口通过进水管导通相连,并且在水箱上还设有絮凝剂添加口,在絮凝剂添加口上连接有絮凝剂添加管,絮凝剂添加管的外端形成絮凝剂输入端。本发明具有提高处理效率,提高处理能力,提高污水处理质量的优点。

The invention discloses a hydrocyclone type sewage treatment device, comprising a cyclone pool, the upper part of the cyclone pool is provided with a water inlet of the cyclone pool along a tangential direction, and an overflow port is arranged on the side wall above the water inlet of the cyclone pool to The sewage after treatment is discharged; the bottom of the whirlpool is provided with a bottom hole for sediment discharge; it is characterized in that it also includes a water tank arranged above the whirlpool, and the water inlet of the water tank is connected with a suction pipe and is connected with the sewage source, and A suction pump is provided on the suction pipe; the water outlet at the bottom of the water tank is connected with the water inlet of the cyclone pool through the water inlet pipe, and a flocculant addition port is also provided on the water tank, and a flocculant addition pipe is connected to the flocculant addition port , the outer end of the flocculant addition pipe forms the flocculant input end. The invention has the advantages of improving treatment efficiency, improving treatment capacity and improving the quality of sewage treatment.

Description

A kind of hydraulic cyclone formula sewage-treatment plant
Technical field
The present invention relates to dirty water decontamination handles technical field more particularly to a kind of hydraulic cyclone formula sewage-treatment plants.
Background technique
With the fast development of economy and urbanization, city black and odorous water problem is increasingly severe, for the rain after raining The processing of water discharge, sanitary sewage etc. faces the challenge.
At present.There are many setting pots of sewage treatment: horizontal sedimentation tank, aerated grit chamber, rotational flow grit chamber.
Horizontal flow type grit chamber is designed using the sedimentation theory of particle dispersion, when operation only when sewage in setting pot Between be equal to or more than design the sand fallout time, can realize the retention of sand grains.Therefore, the pond of setting pot is long according to level Residence time in flow velocity and sewage determines.Due to intake in actual motion water and sand content the case where be constantly to change In addition amplitude of variation it is very big;Therefore when water inlet fluctuation is larger, the removal effect of horizontal flow type grit chamber it is difficult to ensure that, and Horizontal flow type grit chamber itself does not have the ability of organic matter in separated sand, must carry out special sand for the sand grains of discharge It washes.And the characteristics of aerated grit chamber is to form the eddy flow of water by being aerated and generate washed-out sand effect, to improve desanding efficiency and organic Object separative efficiency;But, there are many uncertainties, often there is excess aeration in practical operation and control in aerated grit chamber The problem of, energy is wasted, and larger in pollution of the summer for air, also needs setting defoaming facility not so to have considerable Suspended matter takes pond body out of with foam and pollutes environment.
Rotational flow grit chamber is to make water impurity particle under the action of centrifugal force and gravity, edge using flow-shape and flow velocity To achieve the purpose that sand fallout, raw water enters the precipitating of pool wall helically line accelerated sedimentation accelerating impurity along pond internal tangent direction Guarantee the appropriate rotation of water flow, be in line flowing after, and the turbulent fluctuation of water inlet is reduced to minimum, is formed in pond along the flat of pool wall Face eddy flow, the centrifugal force which generates generate wall attachment effect, so that impurity is affixed to pool wall, and rely on power for support and fall to bottom of pond.
Application number: in the file of 2009-12-25, it is husky 200910113598.4 applyings date: to disclose a kind of round middle ring water Separator, including the straight culvert pipe being connected to inlet channel, the settling pit being arranged in the annular charge for remittance canal closed-loop with water outlet, The through-hole of its top surface of straight culvert pipe setting in settling pit is connected to settling pit water outlet, and straight culvert pipe connects with annular scouring sluice Scouring sluice in pond is set at mouthful, and the sand surfing culvert pipe of annular scouring sluice connection is passed through from the lower part of annular charge for remittance canal, and outlet connects Then outer scouring sluice is arranged in sand surfing canal on sand surfing canal, is supported and is fixed by bracket on the interior weir wall surface of annular charge for remittance canal The annular water retaining wall hanging into settling pit, in the flow surface in the bottom of annular water retaining wall and annular charge for remittance canal between the wall of weir On filter device is uniformly installed.For the present invention not only for the water sand good separating effect of sediment laden flow, the time used in sand discharge is few, Sand surfing water consumption is few, it can be achieved that continuous water supply, and drainage effect is good, can precipitate the lesser mud of particle in water with separating sedimentation basin Husky and suspended particulate improves quality of water supply.
And an other application number 201620178670.7, in the file of applying date 2016-03-09, disclose a kind of filter Net formula rotational flow water-sand separator comprising cylindrical drum, reverse taper, sand discharge bottom tube and rotary table strainer, cylindrical drum lower end and back taper Body upper end is coaxially fixed and is connected to, and reverse taper lower end connect and communicates with sand discharge bottom tube, and cylindrical drum lower outside is equipped with and cylinder Tube inner chamber tangent feed channel is successively fixed at least one rotary table strainer in cylindrical drum from the bottom to top.Structure letter of the invention It is single, low in cost, occupied area is small;The fixed rotary table strainer of layer set is arranged in it in cylindrical drum, and it is right to substantially increase the present invention The sedimentation separation efficiency of sand grain in water sand turbidity fluid;Helical line feed pipe and annular overflow weir are set, filter net type eddy flow is made Water and sand separating device processing capacity with higher.
Although above-mentioned document makes improvement to water and sand separating device, to improve water sand separating capacity.But in fact, it is having Low there are still treatment effeciency in body implementation, processing capacity is poor, the defect that can't meet the quality requirement to the processing of sewage.
Summary of the invention
In view of the above shortcomings of the prior art, the technical problems to be solved by the present invention are: how to design one kind can be more Good raising treatment effeciency, can be improved processing capacity, at the hydraulic cyclone formula sewage of the quality after can be improved sewage treatment Manage device.
In order to solve the above-mentioned technical problem, present invention employs the following technical solutions:
A kind of hydraulic cyclone formula sewage-treatment plant, including Whirlwind tank, Whirlwind tank top are tangentially provided with Whirlwind tank water inlet, Sewage discharge of the side wall equipped with overflow port after for processing above Whirlwind tank water inlet;Eddy flow bottom of pond portion be equipped with bottom outlet for Deposit discharge;It is characterized in that, further include the water tank being set to above Whirlwind tank, the water inlet of water tank be connected with drinking-water pipe and Source of sewage is connected, and suction pump is equipped on drinking-water pipe;The water outlet of water tank bottom is led with Whirlwind tank water inlet by water inlet pipe It is logical to be connected, and flocculant adding mouth is additionally provided on water tank, it is connected with flocculant adding tube in flocculant adding mouth, flocculates The outer end of agent adding tube forms flocculant input terminal.
In this way, by the way that a water tank is arranged above Whirlwind tank, it is first that the treatment sewage of cesspool is defeated by suction pump It send to water tank, and the flocculant adding mouth by being arranged on water tank adds flocculant, by first making sewage and flocculant It is reacted in advance in water tank and under an opposing stationary environment, so that with positive (negative) electrical property in flocculant It is close to each other with negative (just) electrical some particles for being difficult to separate or particle in group and sewage, its potential is reduced, is made It plays pendulum, and using its aggregation property these particles is concentrated.While carrying out preliminary treatment to sewage Mix flocculant with sewage more uniform.The degree of mixedness for improving sewage and flocculant, is wadded a quilt with cotton with improving in subsequent reactions Processing effect of solidifying agent.And then passed through the mixed liquor to be processed after water inlet pipe mixes sewage and flocculant and pass through itself Gravity is delivered to downwards Whirlwind tank, so that after flocculant and sewage mixed liquor enter Whirlwind tank, the high speed under the processing of Whirlwind tank Centrifugal movement improves processing capacity to improve whole device to the treatment effeciency of sewage.
As optimization, the source of sewage includes the cesspool being connected with drinking-water pipe.
In such manner, it is possible to the practical application of more convenient entire processing unit, and more rationally.
As optimization, water inlet on Whirlwind tank is two and corresponding to be set to Whirlwind tank same level diametric Two sides;Two water inlets of Whirlwind tank, which are connected each by water inlet pipe with the water outlet of water tank bottom, to be connected.
In this way, by designing two water inlets on Whirlwind tank, and two water inlets are that corresponding to be set to Whirlwind tank same The two sides in one horizontal diameter direction, enabling to the sewage that Whirlwind tank is entered from water tank is entered from the two sides of same diameter , can preferably guarantee the stationarity of Whirlwind tank, and can more convenient Whirlwind tank with sewage do centrifugal movement, improve rotation Flow the processing capacity and treatment effect in pond.
As optimization, flocculant adding tube extend into the normal of one end end face in water tank and the inner sidewall of water tank in tangent Setting;Drinking-water pipe protrudes into the normal of one end end face of water tank and the inner sidewall of water tank in tangent setting.
In such manner, it is possible to flow into sewage and flocculant along the inner sidewall of water tank, enable flocculant and sewage more preferable Mixing to be reacted in advance, improve sewage enter the ability processed after Whirlwind tank.
It further include bottom plate as optimization, bottom plate is in horizontal circular ring shape plate structure and is arranged and is connected to Whirlwind tank periphery On wall, the inside of bottom plate and the periphery wall of Whirlwind tank are connected and fixed, and are folded upward on the outside of bottom plate and are extended to form outer panel, and outer The collecting tank of whole structure in a ring is collectively formed in side plate, bottom plate and Whirlwind tank periphery wall;And it is equipped in the collecting tank perpendicular To partition, partition in vertically arranged and projection in the horizontal plane in a closed annulus of circle, on the lower end and bottom plate of partition Surface is connected and fixed so that collecting tank to be separated to the lautertuns of a ring shape of the overflow launder and outside in a ring shape of inside, and Filter structure is equipped in lautertuns;Whirlwind tank is equipped with level-one overflow port and is connected to the overflow launder upper end;On partition End is equipped with second level overflow port so that overflow launder to be connected to lautertuns, and sewage outlet is additionally provided on outer side plate and is connected with sewage Efferent duct is to export filtered sewage;And the vertical height of level-one overflow port, second level overflow port and sewage outlet be according to Secondary reduction setting.
In this way, sewage flows in overflow launder from the level-one overflow port of Whirlwind tank, overflow launder can carry out the sewage of entrance Precipitating is overflow from the second level of partition upper end again later so that high speed centrifugation post exercise sewage carries out static deposition out of Whirlwind tank Head piece flows to lautertuns, and sewage at this time has already passed through deposition, then is once filtered, after preferably capable of improving sewage treatment Quality.And the sewage that Whirlwind tank overflow port flows out preferably can be collected and be handled by the structure of entire collecting tank, The structure of entire collecting tank is more compact simultaneously, and structure is more reasonable.Also, to sewage in the process of processing, because adding Added with flocculant, this can have partial flocculation agent and not react completely with sewage completely, or reaction is not enough, the overflow of design Slot further can carry out reaction for sewage and flocculant and provide reacting environment and reaction time, and not anti-for part Flocculant can be filtered by the flocculant answered, lautertuns, to obtain the sewage of better quality.
As optimization, the filter structure includes the cobblestone being arranged in lautertuns.
In this way, filter structure is simpler, and it can be improved filter efficiency.
As optimization, deposit delivery pipe, the other end and sewage of deposit delivery pipe are connected on Whirlwind tank bottom outlet Pond conducting is connected;And check valve and electronic flowmeter are equipped in deposit delivery pipe.
In this way, the deposited object delivery pipe of the deposit of eddy flow bottom of pond portion is delivered to cesspool, it is able to carry out recycling.
As optimization, mixing pump is equipped in cesspool.
In such manner, it is possible to which the deposit of eddy flow bottom of pond portion is stirred evenly with treatment sewage, facilitate subsequent processing.
As optimization, the inside bottom surface of water tank is recessed tapered surface, and the center of recessed tapered surface is provided with water tank Water outlet.
In such manner, it is possible to which the sewage in water tank is preferably facilitated to be flowed into Whirlwind tank.
It further include control centre as optimization;It is equipped with the first electromagnetism check valve on drinking-water pipe, the is equipped on water inlet pipe Two electromagnetism check valves are equipped with third electromagnetism check valve in flocculant adding tube;The automatically controlled end of the first electromagnetism check valve, The automatically controlled end of two electromagnetism check valves and the automatically controlled end of third electromagnetism check valve are connected with control centre.
In such manner, it is possible to which convenient remove to control the first electromagnetism check valve, the second electromagnetism check valve and the by operational control center Three electromagnetism check valves, to reach the sewage quantity that control enters water tank, the sewage quantity into Whirlwind tank and the flocculation into water tank The amount of agent, so that the intelligence degree of whole equipment is higher, it is more convenient to use.
As optimization, the suction pump is Sewage metering pump;It is additionally provided with sediment content detector on drinking-water pipe, is flocculating Agent adding tube is equipped with flocculant metering pump;And sediment content detector, Sewage metering pump and reagent metering pump with control Center is connected;Pre-set control programs are used for according to water flow in sediment content in drinking-water pipe and drinking-water pipe to wadding in control centre Flocculant addition concentration carries out automatically controlling in solidifying agent adding tube, and control program confirms corresponding pass between three according to the following formula System,
The concentration of the flocculant of addition is wherein set as n,
In formula: the sediment content of sewage, unit g/L in the drinking-water pipe that s measures for sediment content detector;
Q is the flow that Sewage metering pumps sewage in the drinking-water pipe measured, unit L/s;
N flocculant concentration, unit mg/L.
In this way, can go to be taken out by sediment content detector by the way that sediment content detector is arranged on drinking-water pipe The content value s of silt in water pipe;Sewage metering is arranged on drinking-water pipe to pump, can be pumped by Sewage metering and go to obtain drinking-water pipe Water flow value Q;Control centre is the computer with input function, inputs above-mentioned formula in control centre, removes to obtain the n in formula Value, by control flocculant metering pump so that in the flocculant and drinking-water pipe of addition silt content value s and drinking-water pipe Water flow value Q carries out Corresponding matching.It enables to whole equipment more convenient to use in this way, different Q value and s value can be directed to The concentration of matching flocculant is gone, preferably to improve the treatment effeciency to sewage, processing capacity, the quality that improves that treated.
In conclusion the present invention has the following advantages that;
1, the present invention only relies on waterpower and runs, and combines with specific flocculant and carries out clean water treatment to sewage to obtain clearly Water, silt removal rate reach as high as 90%.
2, the present invention combines with flocculation handles sewage, and the concentration about flocculant can be according to the resulting difference of experiment Required flocculant concentration is different under sediment concentration, is added, to reach optimal purifying water effect, also save the cost.
3, size of the invention can be adjusted according to the sediment content of required processing and the required water purification rate reached, Both it is applicable to municipal sewage treatment, is equally applicable to the pretreatment of agricultural irrigation technology, in other industry also in combination with corresponding dress It sets and is applied.
4, structure is simple, cheap, purchases convenient for required.
5, operational management is very convenient, keeps an eye on without special messenger, it is only necessary to inspect periodically.
Detailed description of the invention
The structural schematic diagram of hydraulic cyclone formula sewage-treatment plant in Fig. 1 specific embodiment of the invention.
Fig. 2 is the structural schematic diagram of Whirlwind tank and tank parts in Fig. 1.
Fig. 3 is the top view of Fig. 2.
Specific embodiment
The present invention is described in further detail with reference to the accompanying drawing.
When specific implementation: as shown in Figure 1 to Figure 3, a kind of hydraulic cyclone formula sewage-treatment plant, including Whirlwind tank 2, eddy flow Pond top is tangentially provided with Whirlwind tank water inlet, the side wall above Whirlwind tank water inlet be equipped with overflow port it is for processing after Sewage discharge;Eddy flow bottom of pond portion is equipped with bottom outlet for deposit discharge;It is characterized in that, further including being set to above Whirlwind tank Water tank 3, the water inlet of water tank are connected with drinking-water pipe 4 and are connected with source of sewage, and suction pump is equipped on drinking-water pipe;Water tank bottom Water outlet is connected with Whirlwind tank water inlet by the conducting of water inlet pipe 5, and flocculant adding mouth is additionally provided on water tank, is being flocculated Flocculant adding tube 6 is connected in agent adding mouth, the outer end of flocculant adding tube forms flocculant input terminal.
In this way, by the way that a water tank is arranged above Whirlwind tank, it is first that the treatment sewage of cesspool is defeated by suction pump It send to water tank, and the flocculant adding mouth by being arranged on water tank adds flocculant, by first making sewage and flocculant It is reacted in advance in water tank and under an opposing stationary environment, so that with positive (negative) electrical property in flocculant It is close to each other with negative (just) electrical some particles for being difficult to separate or particle in group and sewage, its potential is reduced, is made It plays pendulum, and using its aggregation property these particles is concentrated.While carrying out preliminary treatment to sewage Mix flocculant with sewage more uniform.The degree of mixedness for improving sewage and flocculant, is wadded a quilt with cotton with improving in subsequent reactions Processing effect of solidifying agent.And then passed through the mixed liquor to be processed after water inlet pipe mixes sewage and flocculant and pass through itself Gravity is delivered to downwards Whirlwind tank, so that after flocculant and sewage mixed liquor enter Whirlwind tank, the high speed under the processing of Whirlwind tank Centrifugal movement improves processing capacity to improve whole device to the treatment effeciency of sewage.
As optimization, the source of sewage includes the cesspool 1 being connected with drinking-water pipe.
In such manner, it is possible to the practical application of more convenient entire processing unit, and more rationally.
In present embodiment, water inlet on Whirlwind tank 2 is two and corresponding is set to Whirlwind tank same level Diametric two sides;Two water inlets of Whirlwind tank 2, which are connected each by water inlet pipe with the water outlet of 3 bottom of water tank, to be connected.
In this way, by designing two water inlets on Whirlwind tank, and two water inlets are that corresponding to be set to Whirlwind tank same The two sides in one horizontal diameter direction, enabling to the sewage that Whirlwind tank is entered from water tank is entered from the two sides of same diameter , can preferably guarantee the stationarity of Whirlwind tank, and can more convenient Whirlwind tank with sewage do centrifugal movement, improve rotation Flow the processing capacity and treatment effect in pond.
In present embodiment, flocculant adding tube 6 extend into one end end face in water tank 3 normal and water tank it is interior Side wall is in tangent setting;Drinking-water pipe 4 protrudes into the normal of one end end face of water tank 3 and the inner sidewall of water tank in tangent setting.
In such manner, it is possible to flow into sewage and flocculant along the inner sidewall of water tank, enable flocculant and sewage more preferable Mixing to be reacted in advance, improve sewage enter the ability processed after Whirlwind tank.When it is implemented, flocculant adding tube The normal direction for one end end face that the normal direction for one end end face extending into water tank protrudes into water tank with drinking-water pipe is in opposite sets It sets, enables to flocculant and sewage to form convection current in this way, increase its mixing uniformity, improve pre-reaction effect.
It further include bottom plate 7 in present embodiment, bottom plate is in horizontal circular ring shape plate structure and is arranged and is connected to rotation It flows on the periphery wall of pond, the inside of bottom plate and the periphery wall of Whirlwind tank are connected and fixed, and are folded upward at outside extending to form on the outside of bottom plate Side plate 8, and the collecting tank of whole structure in a ring is collectively formed in outer panel 8, bottom plate 7 and Whirlwind tank periphery wall;And in the collection Vertical partition 10 is equipped in liquid bath, partition encloses closed annulus, partition in one in projection vertically arranged and in the horizontal plane Lower end and plate upper surface be connected and fixed with by collecting tank separate in inside a ring shape overflow launder 11 and outside one The lautertuns 12 of ring shape, and filter structure is equipped in lautertuns;Whirlwind tank be equipped with level-one overflow port and with the overflow The connection of slot upper end;Second level overflow port is equipped with so that overflow launder to be connected to lautertuns in partition upper end, is additionally provided with dirt on outer side plate Water water outlet is simultaneously connected with sewage efferent duct 9 to export filtered sewage;And level-one overflow port, second level overflow port and sewage The vertical height of water outlet is in successively reduction setting.
In this way, sewage flows in overflow launder from the level-one overflow port of Whirlwind tank, overflow launder can carry out the sewage of entrance Precipitating is overflow from the second level of partition upper end again later so that high speed centrifugation post exercise sewage carries out static deposition out of Whirlwind tank Head piece flows to lautertuns, and sewage at this time has already passed through deposition, then is once filtered, after preferably capable of improving sewage treatment Quality.And the sewage that Whirlwind tank overflow port flows out preferably can be collected and be handled by the structure of entire collecting tank, The structure of entire collecting tank is more compact simultaneously, and structure is more reasonable.Also, to sewage in the process of processing, because adding Added with flocculant, this can have partial flocculation agent and not react completely with sewage completely, or reaction is not enough, the overflow of design Slot further can carry out reaction for sewage and flocculant and provide reacting environment and reaction time, and not anti-for part Flocculant can be filtered by the flocculant answered, lautertuns, to obtain the sewage of better quality.
In present embodiment, the filter structure includes the cobblestone 13 being arranged in lautertuns.
In this way, filter structure is simpler, and it can be improved filter efficiency.
In present embodiment, be connected with deposit delivery pipe 14 on Whirlwind tank bottom outlet, deposit delivery pipe it is another One end is connected with cesspool to be connected;And check valve and electronic flowmeter are equipped in deposit delivery pipe.
In this way, the deposited object delivery pipe of the deposit of eddy flow bottom of pond portion is delivered to cesspool, it is able to carry out recycling.
In present embodiment, mixing pump 15 is equipped in cesspool.
In such manner, it is possible to which the deposit of eddy flow bottom of pond portion is stirred evenly with treatment sewage, facilitate subsequent processing.
In present embodiment, the inside bottom surface of water tank 3 is recessed tapered surface, is installed in the centre bit of recessed tapered surface It is equipped with water outlet of water tank.
In such manner, it is possible to which the sewage in water tank is preferably facilitated to be flowed into Whirlwind tank.
It further include control centre in present embodiment;It is equipped with the first electromagnetism check valve 16 on drinking-water pipe, is intaking Pipe is equipped with the second electromagnetism check valve 17, and third electromagnetism check valve 18 is equipped in flocculant adding tube;The first electromagnetism list It is connected to the automatically controlled end, the automatically controlled end of the second electromagnetism check valve and the automatically controlled end of third electromagnetism check valve of valve with control centre.
In such manner, it is possible to which convenient remove to control the first electromagnetism check valve, the second electromagnetism check valve and the by operational control center Three electromagnetism check valves, to reach the sewage quantity that control enters water tank, the sewage quantity into Whirlwind tank and the flocculation into water tank The amount of agent, so that the intelligence degree of whole equipment is higher, it is more convenient to use.
In present embodiment, the suction pump is Sewage metering pump 19;Sediment content inspection is additionally provided on drinking-water pipe Instrument 20 is surveyed, flocculant metering pump 21 is equipped in flocculant adding tube;And sediment content detector, Sewage metering pump and reagent Metering pump is connected with control centre;Pre-set control programs are used for according to sediment content in drinking-water pipe and draw water in control centre Water flow carries out automatically controlling flocculant addition concentration in flocculant adding tube in pipe, and control program confirms according to the following formula Corresponding relationship between three,
The concentration of the flocculant of addition is wherein set as n,
In formula: the sediment content of sewage, unit g/L in the drinking-water pipe that s measures for sediment content detector;
Q is the flow that Sewage metering pumps sewage in the drinking-water pipe measured, unit L/s;
N flocculant concentration, unit mg/L.
In this way, can go to be taken out by sediment content detector by the way that sediment content detector is arranged on drinking-water pipe The content value s of silt in water pipe;Sewage metering is arranged on drinking-water pipe to pump, can be pumped by Sewage metering and go to obtain drinking-water pipe Water flow value Q;Control centre is the computer with input function, inputs above-mentioned formula in control centre, removes to obtain the n in formula Value, by control flocculant metering pump so that in the flocculant and drinking-water pipe of addition silt content value s and drinking-water pipe Water flow value Q carries out Corresponding matching.It enables to whole equipment more convenient to use in this way, different Q value and s value can be directed to The concentration of matching flocculant is gone, preferably to improve the treatment effeciency to sewage, processing capacity, the quality that improves that treated.Mud The model of husky content detection instrument wins wind ULS133M1-LSK100, is the existing equipment for detecting sediment content.
In conclusion the present invention has the following advantages that;
1, the present invention only relies on waterpower and runs, and combines with specific flocculant and carries out clean water treatment to sewage to obtain clearly Water, silt removal rate reach as high as 90%.
2, the present invention combines with flocculation handles sewage, and the concentration about flocculant can be according to the resulting difference of experiment Required flocculant concentration is different under sediment concentration, is added, to reach optimal purifying water effect, also save the cost.
3, size of the invention can be adjusted according to the sediment content of required processing and the required water purification rate reached, Both it is applicable to municipal sewage treatment, is equally applicable to the pretreatment of agricultural irrigation technology, in other industry also in combination with corresponding dress It sets and is applied.
4, structure is simple, cheap, purchases convenient for required.
5, operational management is very convenient, keeps an eye on without special messenger, it is only necessary to inspect periodically.

Claims (10)

1.一种水力旋流式污水处理装置,包括旋流池(2),旋流池上部沿切向设置有旋流池进水口,旋流池进水口上方的侧壁上设有溢流口以供处理后的污水排出;旋流池底部设有底孔以供沉积物排出;其特征在于,还包括设置于旋流池上方的水箱(3),水箱的进水口连接有抽水管(4)和污水源相连,且在抽水管上设有抽水泵;水箱底部的出水口与旋流池进水口通过进水管(5)导通相连,并且在水箱上还设有絮凝剂添加口,在絮凝剂添加口上连接有絮凝剂添加管(6),絮凝剂添加管的外端形成絮凝剂输入端。1. A hydrocyclone type sewage treatment device, comprising a cyclone pool (2), the upper part of the cyclone pool is provided with a cyclone pool water inlet along the tangential direction, and the side wall above the cyclone pool water inlet is provided with an overflow port The bottom of the whirlpool is provided with bottom holes for sediment discharge; it is characterized in that it also includes a water tank (3) arranged above the whirlpool, and the water inlet of the water tank is connected with a suction pipe (4). ) is connected to the sewage source, and a suction pump is installed on the suction pipe; the water outlet at the bottom of the water tank is connected to the water inlet of the cyclone pool through the water inlet pipe (5), and there is also a flocculant addition port on the water tank. The flocculant addition port is connected with a flocculant addition pipe (6), and the outer end of the flocculant addition pipe forms a flocculant input end. 2.如权利要求1所述的一种水力旋流式污水处理装置,其特征在于,所述污水源包括与抽水管相连的污水池(1)。2 . The hydrocyclone type sewage treatment device according to claim 1 , wherein the sewage source comprises a sewage pool ( 1 ) connected with a suction pipe. 3 . 3.如权利要求1所述的一种水力旋流式污水处理装置,其特征在于,旋流池(2)上的进水口为两个且对应的设置于旋流池同一水平直径方向的两侧;旋流池(2)的两个进水口各自通过进水管与水箱(3)底部的出水口导通相连。3. The hydrocyclone type sewage treatment device according to claim 1, characterized in that, there are two water inlets on the cyclone pool (2) and two correspondingly disposed in the same horizontal diameter direction of the cyclone pool. side; the two water inlets of the cyclone pool (2) are respectively connected to the water outlet at the bottom of the water tank (3) through a water inlet pipe. 4.如权利要求1所述的一种水力旋流式污水处理装置,其特征在于,絮凝剂添加管(6)伸入到水箱(3)内的一端端面的法线与水箱的内侧壁呈相切设置;抽水管(4)伸入水箱(3)的一端端面的法线与水箱的内侧壁呈相切设置。4. The hydrocyclone type sewage treatment device according to claim 1, wherein the normal line of one end face of the flocculant adding pipe (6) extending into the water tank (3) is in the shape of the inner side wall of the water tank. Tangent setting; the normal line of one end face of the water pumping pipe (4) extending into the water tank (3) is arranged tangentially to the inner side wall of the water tank. 5.如权利要求1所述的一种水力旋流式污水处理装置,其特征在于,还包括底板(7),底板呈水平的圆环形板状结构且套设连接于旋流池外周壁上,底板的内侧与旋流池的外周壁连接固定,底板的外侧向上弯折延伸形成外侧板(8),且外侧板(8)、底板(7)和旋流池外周壁共同形成整体呈环形结构的集液槽;且在所述集液槽内设有竖向的隔板(10),隔板呈竖向设置且在水平面上的投影呈一圈封闭的圆环,隔板的下端与底板上表面连接固定以将集液槽分隔呈内侧的一圈环形的溢流槽(11)和外侧的一圈环形的过滤槽(12),且在过滤槽内设有过滤结构;旋流池上设有一级溢流口并与所述溢流槽上端连通;在隔板上端设有二级溢流口以将溢流槽和过滤槽连通,在外侧板上还设有污水出水口并连接有污水输出管(9)以将过滤后的污水输出;且一级溢流口、二级溢流口和污水出水口的竖向高度呈依次降低设置。5. The hydrocyclone type sewage treatment device according to claim 1, characterized in that it further comprises a bottom plate (7), the bottom plate is a horizontal annular plate-like structure and is sleeved and connected to the outer peripheral wall of the cyclone pool Above, the inner side of the bottom plate is connected and fixed with the outer peripheral wall of the swirl pool, the outer side of the bottom plate is bent upwards and extends to form an outer plate (8), and the outer plate (8), the bottom plate (7) and the outer peripheral wall of the cyclone pool together form a whole. A liquid collecting tank with an annular structure; and a vertical partition plate (10) is arranged in the liquid collecting tank, the partition plate is arranged vertically and the projection on the horizontal plane is a closed ring, and the lower end of the partition plate It is connected and fixed with the upper surface of the bottom plate to separate the liquid collecting tank into an inner ring-shaped overflow groove (11) and an outer ring-shaped filter groove (12), and a filter structure is arranged in the filter groove; A first-level overflow port is arranged on the pool and communicated with the upper end of the overflow tank; a second-level overflow port is arranged at the upper end of the partition plate to connect the overflow tank and the filter tank, and a sewage outlet is also arranged on the outer plate and connected There is a sewage output pipe (9) to output the filtered sewage; and the vertical heights of the primary overflow outlet, the secondary overflow outlet and the sewage outlet are set to decrease in turn. 6.如权利要求5所述的一种水力旋流式污水处理装置,其特征在于,所述过滤结构包括设置在过滤槽内的鹅卵石(13)。6 . The hydrocyclone type sewage treatment device according to claim 5 , wherein the filtering structure comprises pebbles ( 13 ) arranged in the filtering tank. 7 . 7.如权利要求1所述的一种水力旋流式污水处理装置,其特征在于,在旋流池底孔上连接有沉积物输送管(14),沉积物输送管的另一端与污水池导通相连;且在沉积物输送管上设有单向阀和电子流量计。7. A hydrocyclone type sewage treatment device according to claim 1, characterized in that a sediment conveying pipe (14) is connected to the bottom hole of the swirl tank, and the other end of the sediment conveying pipe is connected to the sewage tank. Conduction and connection; and a one-way valve and an electronic flow meter are arranged on the sediment conveying pipe. 8.如权利要求6所述的一种水力旋流式污水处理装置,其特征在于,在污水池内设有搅拌泵(15)。8 . The hydrocyclone type sewage treatment device according to claim 6 , wherein a stirring pump ( 15 ) is arranged in the sewage pool. 9 . 9.如权利要求1所述的一种水力旋流式污水处理装置,其特征在于,水箱(3)的内侧底面为下凹锥形面,在下凹锥形面的中心位置设置有水箱出水口。9 . The hydrocyclone type sewage treatment device according to claim 1 , wherein the inner bottom surface of the water tank ( 3 ) is a concave conical surface, and a water tank outlet is provided at the center of the concave conical surface. 10 . . 10.如权利要求1所述的一种水力旋流式污水处理装置,其特征在于,还包括控制中心;在抽水管上设有第一电磁单向阀(16),在进水管上设有第二电磁单向阀(17),在絮凝剂添加管上设有第三电磁单向阀(18);所述第一电磁单向阀的电控端、第二电磁单向阀的电控端和第三电磁单向阀的电控端均与控制中心相连;10 . The hydrocyclone type sewage treatment device according to claim 1 , further comprising a control center; a first electromagnetic check valve ( 16 ) is arranged on the suction pipe, and a first electromagnetic check valve ( 16 ) is arranged on the water inlet pipe 10 . The second electromagnetic one-way valve (17) is provided with a third electromagnetic one-way valve (18) on the flocculant adding pipe; the electric control end of the first electromagnetic one-way valve and the electric control end of the second electromagnetic one-way valve The electric control end of the third electromagnetic one-way valve and the electric control end of the third electromagnetic one-way valve are connected to the control center; 所述抽水泵为污水计量泵(19);在抽水管上还设有泥沙含量检测仪(20),在絮凝剂添加管上设有絮凝剂计量泵(21);并且泥沙含量检测仪、污水计量泵和试剂计量泵均与控制中心相连;控制中心中预设控制程序用于根据抽水管中泥沙含量以及抽水管中水流量对絮凝剂添加管中絮凝剂添加浓度进行自动控制,控制程序根据以下公式确认三者之间对应关系,The suction pump is a sewage metering pump (19); a sediment content detector (20) is also arranged on the suction pipe, and a flocculant metering pump (21) is arranged on the flocculant adding pipe; and the sediment content detector , sewage metering pump and reagent metering pump are connected to the control center; the preset control program in the control center is used to automatically control the concentration of flocculant added in the flocculant addition pipe according to the sediment content in the suction pipe and the water flow in the suction pipe. The control program confirms the correspondence between the three according to the following formula, 其中设定添加的絮凝剂的浓度为n,The concentration of the added flocculant is set as n, 式中:s为泥沙含量检测仪测得的抽水管内污水的泥沙含量,单位g/L;In the formula: s is the sediment content of the sewage in the suction pipe measured by the sediment content detector, in g/L; Q为污水计量泵测得的抽水管内污水的流量,单位为L/s;Q is the flow rate of sewage in the suction pipe measured by the sewage metering pump, in L/s; n絮凝剂浓度,单位为mg/L。n flocculant concentration, in mg/L.
CN201811517828.9A 2018-12-12 2018-12-12 A kind of hydraulic cyclone formula sewage-treatment plant Pending CN109437380A (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114755056A (en) * 2022-03-22 2022-07-15 北京北排水环境发展有限公司 A new type of sewage sediment sampling device and using method

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN2311491Y (en) * 1997-05-12 1999-03-24 卢竟翔 Continuous mud-removing water purification pot
CN1280103A (en) * 1999-07-08 2001-01-17 雷树德 Water purifying method on physical and chemical principles
US20020195398A1 (en) * 2001-06-25 2002-12-26 Morse Dwain E. System and method for removing contaminants from liquid
CN102491571A (en) * 2011-12-19 2012-06-13 西南化工研究设计院 Scenic water recycling device and treatment method
CN205988682U (en) * 2016-08-29 2017-03-01 金川集团股份有限公司 A kind of enter liquid distributor for salt water preprocessor
WO2017127866A1 (en) * 2016-01-28 2017-08-03 Tim Straatmans Apparatus and method for waste and water treatment
US20170239629A1 (en) * 2016-02-22 2017-08-24 Oleksandr Galaka Multifunctional hydrodynamic vortex reactor
CN107265692A (en) * 2017-06-27 2017-10-20 同济大学 A kind of reinforcing solid-liquid cyclone separation device of flocculation in short-term and the method based on the device

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN2311491Y (en) * 1997-05-12 1999-03-24 卢竟翔 Continuous mud-removing water purification pot
CN1280103A (en) * 1999-07-08 2001-01-17 雷树德 Water purifying method on physical and chemical principles
US20020195398A1 (en) * 2001-06-25 2002-12-26 Morse Dwain E. System and method for removing contaminants from liquid
CN102491571A (en) * 2011-12-19 2012-06-13 西南化工研究设计院 Scenic water recycling device and treatment method
WO2017127866A1 (en) * 2016-01-28 2017-08-03 Tim Straatmans Apparatus and method for waste and water treatment
US20170239629A1 (en) * 2016-02-22 2017-08-24 Oleksandr Galaka Multifunctional hydrodynamic vortex reactor
CN205988682U (en) * 2016-08-29 2017-03-01 金川集团股份有限公司 A kind of enter liquid distributor for salt water preprocessor
CN107265692A (en) * 2017-06-27 2017-10-20 同济大学 A kind of reinforcing solid-liquid cyclone separation device of flocculation in short-term and the method based on the device

Non-Patent Citations (9)

* Cited by examiner, † Cited by third party
Title
向壮丽: "浅谈絮凝控制技术", 《工程设计与建设》 *
吴赳赳等: "《给水工程》", 31 December 1990, 中国建筑工业出版社 *
崔福义等: "《给排水工程仪表与控制 (第二版)》", 30 June 2006, 中国建筑工业出版社 *
张晋霞等: "《含锌冶金尘泥分选理论及应用》", 30 June 2017, 冶金工业出版社 *
张鹤清等: "絮凝快速分离水处理技术简介及发展趋势", 《环境工程》 *
李培军等: "混凝投药控制技术的现状及发展趋势研究", 《市政技术》 *
蒋明虎等: "液-液水力旋流器的入口形式及其研究", 《石油矿场机械》 *
袁惠新等: "不同入口形式的固液分离旋流器壁面磨损研究", 《化工进展》 *
韩占忠等: "《fluent-流体工程仿真计算实例与应用》", 30 June 2004, 北京理工大学出版社 *

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114755056A (en) * 2022-03-22 2022-07-15 北京北排水环境发展有限公司 A new type of sewage sediment sampling device and using method

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Application publication date: 20190308