CN203803160U - Unpowered pulse accelerated settler - Google Patents
Unpowered pulse accelerated settler Download PDFInfo
- Publication number
- CN203803160U CN203803160U CN201420046738.7U CN201420046738U CN203803160U CN 203803160 U CN203803160 U CN 203803160U CN 201420046738 U CN201420046738 U CN 201420046738U CN 203803160 U CN203803160 U CN 203803160U
- Authority
- CN
- China
- Prior art keywords
- tank
- jar
- bell
- mozzle
- 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.)
- Expired - Fee Related
Links
Landscapes
- Physical Water Treatments (AREA)
Abstract
An unpowered pulse accelerated settler comprises a settling tank, a water outlet pipe, a mud pipe, a baffle plate and a guide pipe, wherein the guide pipe is vertically arranged in the settling tank; the water inlet end of the guide pipe extends out of the top of the settling tank; the water outlet end of the guide pipe stretches into the lower half part of the settling tank; the unpowered pulse accelerated settler further comprises a pulse tank, a bell jar, a first vent pipe, a second vent pipe and a water inlet pipe; the bottom of the bell jar is opened; the bell jar covers the water inlet end of the guide pipe; a gap is formed between the top of the inner cavity of the bell jar and the water inlet end of the guide pipe; the bell jar is arranged in the inner chamber of the pulse tank; the inner chamber of the pulse tank is communicated with that of the bell jar through the opened bottom of the bell jar; a gap is formed between the top of the inner chamber of the pulse tank and the top of the bell jar; one end of the second vent pipe extends from the water inlet of the guide pipe to the interior of the guide pipe; the other end of the second vent pipe passes through the top of the bell jar and the top of the pulse tank and extends outwards; a switch is arranged on the second vent pipe; the first vent pipe is arranged at the top of the pulse tank; the pulse tank is provided with a water inlet pipe. The unpowered pulse accelerated settler is high in solid-liquid mixture separation efficiency and low in energy consumption and equipment investment cost.
Description
Technical field
The utility model relates to Separation of Solid and Liquid professional skill field, particularly a kind of unpowered pulsation accelerated clariqier.
Background technology
What in the numerous areas such as sewage disposal, medicine and food, Separation of Solid and Liquid was generally used is centrifuge, but there is in some liquid solid content order number minimum, be difficult to separate with common centrifuge, must adopt the higher centrifuge of rotating speed, this centrifuge power consumption is very large, make power consumption large, cause cost of investment higher.
At present because with cost of investment problem, operating cost problems etc., are commonly used in processing the large multi-steering flat flow of equipment settling tank, vertical-flow settling tank, radial-flow settling tank and the ramp type settling tank of Separation of Solid and Liquid.In traditional settler, be 20～40% left and right to the efficiency of Separation of Solid and Liquid, but these precipitation apparatus in actual use effect of settling are very poor, during especially for the very little liquid of solid content order number, need to lodge auxiliary equipment or dosing etc. is just achieved, and there are problems in the method, so just increase the production cost of unit product, reduce the competitive advantage of product.
Summary of the invention
The utility model is for the equipment that overcomes Separation of Solid and Liquid in prior art is to granule solid content inferior separating effect, problem that equipment investment cost is high, invent a kind of unpowered pulsation accelerated clariqier, make the liquid handling better effects if to containing granule solid content, simultaneously, equipment investment cost is reduced greatly, and power consumption is few.
For solving the problem of above-mentioned technology, the utility model by the following technical solutions:
A kind of unpowered pulsation accelerated clariqier, comprises:
Settling tank, outlet pipe, discharge pipeline, deflection plate, mozzle, described mozzle is vertically placed in described settling tank, and the inlet end of mozzle stretches out in described settling tank top, and mozzle water outlet end extends to the latter half of settling tank;
Wherein, also comprise pulser, described pulser comprises Impulsive tank, bell-jar, the first breather pipe, the second breather pipe, water inlet pipe, described bell-jar bottom end opening, it covers described mozzle inlet end, and its inner chamber top and described mozzle inlet end are provided with space; Described bell-jar is arranged in described Impulsive tank inner chamber, and described Impulsive tank inner chamber communicates with described bell-jar inner chamber by the bottom of bell-jar opening, and described Impulsive tank inner chamber top and described bell-jar top are provided with space; Extend in from mozzle water inlet toward mozzle described second breather pipe one end, and its other end stretches out through bell-jar top and Impulsive tank top, on described the second breather pipe, have switch, described the first breather pipe is arranged at described Impulsive tank top, and described Impulsive tank is provided with water inlet pipe.
Preferably, the bottom taper surface of described settling tank is provided with circular pressure guard, and described pressure guard surrounding outer is connected with described taper surface.
Preferably, on described pressure guard, have hole.
Preferably, between described bell-jar and described Impulsive tank, be provided with reinforcement.
Preferably, between described mozzle and described bell-jar, be provided with reinforcement.
Preferably, the switch on described the second breather pipe is check valve.
Compared with prior art, the beneficial effects of the utility model are:
The utility model is on the basis of original solid-liquid sedimenting system, filled an Impulsive tank more, the liquid that need to carry out solid-liquid sedimentation enters into Impulsive tank, make the liquid pulsation entering, simultaneously, molecule suspension in liquid produces a downward acceleration, thus, make the easier sedimentation of molecule suspension, the utility model Impulsive tank used, without power consumption, can well carry out Separation of Solid and Liquid, and molecule suspension in solidliquid mixture is separated, separative efficiency can reach 75%, is 2～5 times of traditional settler separative efficiency; The pressure guard simultaneously arranging in settling tank can prevent that the solid content of precipitation is deposited in spoil disposal mouth of pipe place, causes discharge pipeline to stop up, and causes settling tank normally to work, simultaneously, avoid solid content directly settling tank to be exerted pressure, improve the resistivity of settling tank bottom, extend settling tank service life; The utility model cost of investment is low, and separative efficiency is high, is applicable to the separation of each enterprise to the solid content that suspends in the numerous areas such as sewage, medicine or food.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model.
Fig. 2 is the profile of the utility model A-A.
Wherein, 1-deflection plate; 2-settling tank; 3-Impulsive tank; 4-water inlet pipe; 5-bell-jar; 6-mozzle; 7-strengthens gusset; 8-outlet pipe; 9-discharge pipeline; 10-pressure guard; 11-the first breather pipe; 12-the second breather pipe; 13-check valve.
Detailed description of the invention
Further describe the utility model referring to detailed description of the invention, to make those skilled in the art can implement according to this with reference to description word, the utility model protection domain is not limited by embodiment of the present utility model.
Embodiment
As shown in Figure 1, a kind of unpowered pulsation accelerated clariqier, comprise settling tank 2, outlet pipe 8, discharge pipeline 9, deflection plate 1, mozzle 6, mozzle 6 is vertically placed in settling tank 2, and the inlet end of mozzle 6 stretches out in settling tank 2 tops, mozzle 6 water outlet ends extend to the latter half of settling tank 2; Also comprise pulser, pulser comprises Impulsive tank 3, bell-jar 5, the second breather pipe 11, the second breather pipe 12, water inlet pipe 4, bell-jar 5 bottom end openings, it covers mozzle 6 inlet end, and its inner chamber top and mozzle 6 inlet end are provided with space, between mozzle 6 and bell-jar, are provided with reinforcement; Bell-jar 5 is arranged in Impulsive tank 3 inner chambers, between bell-jar 5 and Impulsive tank 3, is provided with reinforcement, and Impulsive tank 3 inner chambers communicate with bell-jar 5 inner chambers by the bottom of bell-jar 5 openings, and Impulsive tank 3 inner chamber tops and bell-jar 5 tops are provided with space; Second breather pipe 12 one end are from mozzle 6 water inlets toward the interior extension of mozzle 6, and its other end stretches out through bell-jar 5 tops and Impulsive tank 3 tops, on the second breather pipe 12, there is check valve, Impulsive tank top is provided with the second breather pipe 11, Impulsive tank 3 is provided with water inlet pipe, and the bottom taper surface of settling tank 2 is provided with two-layer pressure guard 10, and pressure guard 10 is circular steel plate, its surrounding outer is connected with taper surface, has several circular ports on pressure guard 10.The sewage that carries out Separation of Solid and Liquid is extracted in Impulsive tank 3 by water inlet pipe 4 with suction pump, bell-jar 5 communicates with Impulsive tank 3 inner chambers, sewage enters in bell-jar 5 by the bottom of bell-jar 5 openings from Impulsive tank 3 bottoms, sewage is full of gradually Impulsive tank 3 inner chambers and passes through the first breather pipe 11 by the Bas Discharged in Impulsive tank 3, in the time that the interior liquid level of bell-jar 5 rises to mozzle 6 inlet end height, sewage will flow in settling tank 2 by mozzle 6, while just beginning, the defluent speed of the interior sewage of mozzle 6 is less than suction pump and is drawn into the speed of Impulsive tank 3 sewage, along with liquid level constantly rises, it is more and more faster that sewage flows into the speed of mozzle 6, part air in bell-jar 5 is brought in mozzle 6 inlet end, discharge outside Impulsive tank 3 by the second breather pipe 12, in the time that the interior air of bell-jar 5 drains, sewage has also been full of in bell-jar 5, now, speed in bell-jar 5 sewage inflow mozzles 6 is much larger than the speed that enters sewage in Impulsive tank, between mozzle 6 water inlets and bell-jar 5 inner chamber tops, form vacuum, make the interior siphonage that occurs of bell-jar 5, sewage in Impulsive tank 3 chambeies is sucked in bell-jar 5, in the time being reduced to 11 mouthfuls of Impulsive tank 3 top the second breather pipes under liquid level, the air of outside enters in Impulsive tank 3 by the second breather pipe 11, the atmospheric pressure of outside air, add the siphonage in bell-jar 5, cause the interior sewage of Impulsive tank 3 complete by siphon rapidly, air also enters in bell-jar 5 simultaneously, now, the speed that enters Impulsive tank 3 sewage is greater than again sewage and enters the speed in mozzle 6, then start the step that repetition sewage has just started to enter Impulsive tank 3, so repeatedly, effluent flow rate trend is slowly, hurry up, slowly, fast form, current are pulsating current, in the time of siphon, defluent sewage speed is for the fastest, now molecule suspension in sewage etc. also has a downward acceleration, make the downward precipitations such as molecule suspension, reach thus effect of settling.When sewage enters into settling tank 2 by mozzle 6, below mozzle 6, there is a deflection plate 1 in exit, buffering fast and under sewage, molecule, suspension etc. under sedimentation is deposited on deposition on pressure guard 10, and then by the circular port of opening on pressure guard 10, drop on lower one deck pressure guard, finally discharge by discharge pipeline 9 through alleviation in layer.Pressure guard 10 has avoided too much precipitum to be deposited in discharge pipeline 9 places, causes discharge pipeline to stop up, and finally causes settler normally to work; Meanwhile, slow down precipitum and directly settling tank 2 bottom taper surfaces have been exerted pressure, extension device service life.
The utility model is in running, less because sewage when slow to lower flow velocity in bell-jar, flows into water in settling tank, when flow velocity is fast, flow into the larger ratio of accounting in settling tank, so, this pulser is very high to sewage solid-liquid separation efficiency, can reach 75%.The utility model is on the basis of original solid-liquid sedimenting system, filled an Impulsive tank more, the liquid that need to carry out solid-liquid sedimentation enters into Impulsive tank, make the liquid pulsation entering, simultaneously, molecule suspension in liquid produces a downward acceleration, thus, make the easier sedimentation of molecule suspension, the utility model Impulsive tank used, without power consumption, can well carry out Separation of Solid and Liquid, and molecule suspension in solidliquid mixture is separated, separative efficiency is high, is 2～5 times of traditional settler separative efficiency; The utility model cost of investment is low, and separative efficiency is high, is applicable to the separation of each enterprise to the solid content that suspends in the numerous areas such as sewage, medicine or food.
Claims (6)
1. a unpowered pulsation accelerated clariqier, comprise: settling tank, outlet pipe, discharge pipeline, deflection plate, mozzle, described mozzle is vertically placed in described settling tank, and the inlet end of mozzle stretches out in described settling tank top, and mozzle water outlet end extends to the latter half of settling tank; It is characterized in that: also comprise pulser, described pulser comprises Impulsive tank, bell-jar, the first breather pipe, the second breather pipe, water inlet pipe, described bell-jar bottom end opening, it covers described mozzle inlet end, and its inner chamber top and described mozzle inlet end are provided with space; Described bell-jar is arranged in described Impulsive tank inner chamber, and described Impulsive tank inner chamber communicates with described bell-jar inner chamber by the bottom of bell-jar opening, and described Impulsive tank inner chamber top and described bell-jar top are provided with space; Extend in from mozzle water inlet toward mozzle described second breather pipe one end, and its other end stretches out through bell-jar top and Impulsive tank top, on described the second breather pipe, have switch, described the first breather pipe is arranged at described Impulsive tank top, and described Impulsive tank is provided with water inlet pipe.
2. unpowered pulsation accelerated clariqier according to claim 1, is characterized in that: the bottom taper surface of described settling tank is provided with circular pressure guard, described pressure guard surrounding outer is connected with described taper surface.
3. unpowered pulsation accelerated clariqier according to claim 2, is characterized in that: described pressure guard is provided with hole.
4. unpowered pulsation accelerated clariqier according to claim 1, is characterized in that: between described bell-jar and described Impulsive tank, be provided with reinforcement.
5. unpowered pulsation accelerated clariqier according to claim 1, is characterized in that: between described mozzle and described bell-jar, be provided with reinforcement.
6. unpowered pulsation accelerated clariqier according to claim 1, is characterized in that: the switch on described the second breather pipe is check valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420046738.7U CN203803160U (en) | 2014-01-24 | 2014-01-24 | Unpowered pulse accelerated settler |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420046738.7U CN203803160U (en) | 2014-01-24 | 2014-01-24 | Unpowered pulse accelerated settler |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203803160U true CN203803160U (en) | 2014-09-03 |
Family
ID=51441973
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420046738.7U Expired - Fee Related CN203803160U (en) | 2014-01-24 | 2014-01-24 | Unpowered pulse accelerated settler |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203803160U (en) |
-
2014
- 2014-01-24 CN CN201420046738.7U patent/CN203803160U/en not_active Expired - Fee Related
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101810941B (en) | Compound oil-water separation system | |
| CN105668834B (en) | A kind of multitubular bundles cyclone sediment separator | |
| CN107694156B (en) | Ship type sewage precipitation treatment device | |
| CN204138447U (en) | A kind of aeration horizontal-flow grit chamber | |
| CN104649370A (en) | Dish oil-water separator | |
| CN204434326U (en) | A kind of dish-style water-and-oil separator | |
| CN103239905A (en) | Siphon type valveless filtering pool | |
| CN203803160U (en) | Unpowered pulse accelerated settler | |
| CN210261223U (en) | Oil-water separation device | |
| CN108862688A (en) | A kind of central tube cyclonic separation settler | |
| CN110104838A (en) | A kind of the AUTOMATIC ZONING separating treatment system and its processing method of oily wastewater | |
| CN106669280A (en) | Spiral flow diversion and hydrocyclone separation settling device | |
| CN204125218U (en) | Quadrant elevation type pressure transverse flow produced water disposal device | |
| CN203253216U (en) | Siphonic valveless filtering pool | |
| CN102765835A (en) | Closed multistage purified water device and production process | |
| CN203112606U (en) | Skid-mounted desanding device | |
| CN106315713B (en) | Integrated girt-water separation device | |
| CN214634446U (en) | Three-phase separator | |
| CN202297196U (en) | Rotary flow flotation device for treating oily wastewater | |
| CN203803164U (en) | Efficient mud-water separation precipitation system | |
| CN203170110U (en) | Gas phase-liquid phase-solid phase separation precipitator | |
| CN202945114U (en) | Large-volume tank-type air floating/aerating/settling device | |
| CN204699466U (en) | Gas stripping type desander for rotational flow grit pit | |
| CN201275433Y (en) | Bucket type oil and water separator | |
| CN206521301U (en) | A kind of cyclone separator of straight tube eddy flow water inlet structure |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| PP01 | Preservation of patent right |
Effective date of registration: 20170222 Granted publication date: 20140903 |
|
| RINS | Preservation of patent right or utility model and its discharge | ||
| PD01 | Discharge of preservation of patent | ||
| PD01 | Discharge of preservation of patent |
Date of cancellation: 20170822 Granted publication date: 20140903 |
|
| PP01 | Preservation of patent right | ||
| PP01 | Preservation of patent right |
Effective date of registration: 20170918 Granted publication date: 20140903 |
|
| PD01 | Discharge of preservation of patent | ||
| PD01 | Discharge of preservation of patent |
Date of cancellation: 20200918 Granted publication date: 20140903 |
|
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140903 Termination date: 20180124 |