CN205188021U - Coal slime water purifier - Google Patents
Coal slime water purifier Download PDFInfo
- Publication number
- CN205188021U CN205188021U CN201520931093.XU CN201520931093U CN205188021U CN 205188021 U CN205188021 U CN 205188021U CN 201520931093 U CN201520931093 U CN 201520931093U CN 205188021 U CN205188021 U CN 205188021U
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- China
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- water
- coal slurry
- water inlet
- purifier according
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- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
Coal slime water purifier. A coal slime water purifier that purifier among the environmental protection field especially relates to one kind and is applied to trades such as colliery, electric power is related to. The settling property is high, the treatment effect is good. Including setting up the drain and the delivery port at top in clarifier body bottom, establish the water inlet between drain and the delivery port, establish in proper order between water inlet and delivery port and thoughtlessly congeal reaction zone, inclined tube sedimentation area and filtering area, establish the bagger in the below of water inlet and distinguish, the inlet tube is connected to the water inlet, the top of inlet tube is equipped with the barrel of left -hand thread. The beneficial effects of the utility model are that: establishing the barrel of a left -hand thread in the top of inlet tube, making rivers can thoughtlessly not congeal the reaction zone by direct impact, it is poor to lead to the flocculation and deposit the effect, and do not use the whirl, saved and hindered board soon, do not receive the hindrance when making the flocculating constituent subside.
Description
Technical field
The utility model relates to the refining plant in field of Environment Protection, particularly relates to a kind of coal slurry purifier be applied in the industry such as colliery, electric power.
Background technology
For a long time, the materializing strategy of black water adopts the traditional technologys such as coagulating, tube settling, filtration, air supporting reaction and sludge condensation substantially, the shortcoming such as traditional technology also exists cumbersome, floor space is large, the clarification time is long, energy consumption is high and treatment effect is unstable.For this reason, within 2009200381987 years, create the coal slurry purifier integrating centrifugation, coagulating sedimentation and filtering separation being specifically designed to process black water, its structure design is compact and in technique, add eddy flow district, overcomes the shortcoming of traditional technology preferably.Eddy flow water inlet enters into sloping plate deposition district by resistance rotating plate, then to filtering layer water outlet, the water-in of coal slurry purifier is offered along body tangential direction, establishes a resistance rotating plate between eddy flow district and current stabilization district.Mud-water separation is carried out in the tangential force effect that sewage produces through eddy flow, and medicament and sewage carry out mixing to produce fully flocculating simultaneously.Because the eddy flow of waterpower makes sewage be difficult to leave standstill when sewage enters into settling region, cause the sedimentation function of sewage to reduce, although the resistance rotating plate of equipment decreases eddy flow in tank body, eddy flow has also been broken flocs unit by resistance rotating plate and has been caused sedimentation function to decline.
Utility model content
The utility model, for above problem, provides the coal slurry purifier that a kind of settling property is high, treatment effect is good.
The technical solution of the utility model is: comprise and be arranged on sewage draining exit bottom purification body and the water outlet at top, water-in is established between sewage draining exit and water outlet, coagulating district, tube settling district and filtrating area is established successively between water-in and water outlet, bucket district is established in the below of water-in, described water-in connects water inlet pipe, and the top of described water inlet pipe is provided with the cylindrical shell of left-hand thread.
Described water inlet pipe is L-type, and extends to the middle part of described cleaner.
Establish sieve plate above described filtrating area, sieve plate offers some posticums.
Described tube settling district is made up of the deposition sloped tube somely be arranged in parallel, have certain interval each other.
Described deposition sloped tube and horizontal plane are inclined to set.
Described pitch angle is 60 °.
Described filtrating area is made up of supporting plate and the filtrate in suspension be arranged on supporting plate and backwash agitator.
Offer multiple porthole at body sidewall, set up defences at the lower sides of body and block up.
The beneficial effects of the utility model: the cylindrical shell establishing a left-hand thread above water inlet pipe, make current can not directly impact coagulating district, cause flocculation and sedimentation effect poor; And do not use eddy flow, eliminate resistance rotating plate, not interrupted when making floc settlement.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model,
In figure, 1 is water outlet, and 2 is sieve plates, and 3 is filtrates, and 4 is posticums, and 5 is deposition sloped tubes, and 6 is deposition sloped tube brackets, and 7 is cylindrical shells, and 8 is water inlet pipes, and 9 is water-ins, and 10 is sewage draining exits.
Embodiment
Below in conjunction with accompanying drawing, the utility model is illustrated.
As shown in Figure 1, the utility model comprises and is arranged on sewage draining exit 10 bottom purification body and the water outlet 1 at top, water-in 9 is established between sewage draining exit 10 and water outlet 1, coagulating district, tube settling district and filtrating area is established successively between water-in 9 and water outlet 1, bucket district is established in the below of water-in 9, described water-in 9 connects water inlet pipe 8, and the top of described water inlet pipe 8 is provided with the cylindrical shell 7 of left-hand thread.
Described water inlet pipe 8 in L-type, and extends to the middle part of described cleaner.
Establish sieve plate 2 above described filtrating area, sieve plate 2 offers some posticums 4.
Described tube settling district is made up of the deposition sloped tube 5 be located on deposition sloped tube bracket 6 somely be arranged in parallel, have certain interval each other.
In order to increase collision between tube settling district particle, friction probability as far as possible, described deposition sloped tube 5 and horizontal plane are inclined to set, and pitch angle is preferably 60 °.
Described filtrating area is made up of supporting plate and the filtrate in suspension be arranged on supporting plate and backwash agitator.
Offer multiple porthole at body sidewall, set up defences at the lower sides of body and block up.
Other structure formations of the present utility model are with patent application 2009200381987.
Workflow of the present utility model is: 1) first black water carries out pre-treatment, namely before entering cleaner, is mixed for the first time, add corresponding flocculation agent simultaneously and mix mutually by negative pressure by black water and liquid press-in pump; 2) then entered body, cleaner Hydraulic Circulation baffling by the cylindrical shell of left-hand thread by baffling reaction, the colloidalmaterial in coagulating district black water carries out gathering and forms alumen ustum, and then black water enters into tube settling district; 3) small-particle in the black water in tube settling district is entered from deposition sloped tube 5 through out-of-date, collision, friction is produced with deposition sloped tube 5, the probability of increase small-particle contact, reuniting, small-particle slides to bucket district under therefore forming macrobead gradually, and the black water through above-mentioned secondary purification then continues to rise to filtrating area; 4) small in filtrating area suspended filter material 3 rises to sieve plate 2 place under the effect of buoyancy, now suspended filter material 3 produces and perturbs under the effect of water eddy flow, thus molecule collides mutually, rubbing forms large granular impurity and sink, through the water of above-mentioned three grades of purifications then by water outlet in posticum 4 that sieve plate 2 is offered; 5) by after above-mentioned process bottom body the mud in bucket district mutually extrude shape in aggregates after sink gradually, because bottom bore is less, make the sludge density of bottom larger, between particle, gap is little, be extruded by from sewage draining exit 10 gradually under the effect of top water and upper strata particle, the dirt now extruded has formed the briquette of certain density, then it is stand-by to be transported to the energy that corresponding link carries out processing rear formation new.
Claims (8)
1. coal slurry purifier, comprise and be arranged on sewage draining exit bottom purification body and the water outlet at top, water-in is established between sewage draining exit and water outlet, coagulating district, tube settling district and filtrating area is established successively between water-in and water outlet, bucket district is established in the below of water-in, it is characterized in that, described water-in connects water inlet pipe, and the top of described water inlet pipe is provided with the cylindrical shell of left-hand thread.
2. coal slurry purifier according to claim 1, is characterized in that, described water inlet pipe is L-type, and extends to the middle part of described cleaner.
3. coal slurry purifier according to claim 1, is characterized in that, establishes sieve plate above described filtrating area, sieve plate offers some posticums.
4. coal slurry purifier according to claim 1, is characterized in that, described tube settling district is made up of the deposition sloped tube somely be arranged in parallel, have certain interval each other.
5. coal slurry purifier according to claim 4, is characterized in that, described deposition sloped tube and horizontal plane are inclined to set.
6. coal slurry purifier according to claim 5, is characterized in that, described pitch angle is 60 °.
7. coal slurry purifier according to claim 1, is characterized in that, described filtrating area is made up of supporting plate and the filtrate in suspension be arranged on supporting plate and backwash agitator.
8. coal slurry purifier according to claim 1, is characterized in that, offers multiple porthole at body sidewall, sets up defences block up at the lower sides of body.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520931093.XU CN205188021U (en) | 2015-11-19 | 2015-11-19 | Coal slime water purifier |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520931093.XU CN205188021U (en) | 2015-11-19 | 2015-11-19 | Coal slime water purifier |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205188021U true CN205188021U (en) | 2016-04-27 |
Family
ID=55781037
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520931093.XU Expired - Fee Related CN205188021U (en) | 2015-11-19 | 2015-11-19 | Coal slime water purifier |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205188021U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106517595A (en) * | 2016-12-21 | 2017-03-22 | 重庆市沃利克环保设备有限公司 | Integrated water purifier |
-
2015
- 2015-11-19 CN CN201520931093.XU patent/CN205188021U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106517595A (en) * | 2016-12-21 | 2017-03-22 | 重庆市沃利克环保设备有限公司 | Integrated water purifier |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160427 Termination date: 20191119 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |