CN201370979Y - Three-stage continuous settling sloping plate pipe precipitator - Google Patents
Three-stage continuous settling sloping plate pipe precipitator Download PDFInfo
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- CN201370979Y CN201370979Y CN200920010318U CN200920010318U CN201370979Y CN 201370979 Y CN201370979 Y CN 201370979Y CN 200920010318 U CN200920010318 U CN 200920010318U CN 200920010318 U CN200920010318 U CN 200920010318U CN 201370979 Y CN201370979 Y CN 201370979Y
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Abstract
The utility model relates to sewage disposal equipment, in particular to a three-stage continuous settling sloping plate pipe precipitator, wherein a water inlet and a sludge outlet are formed at the lower end of the precipitator, a water outlet and an exhaust port are formed at the upper end thereof, the lower, the middle and the upper parts of the precipitator are formed to be a water inlet and distribution area, a settling area and a water outlet and distribution area respectively, the middle settling area is a three-stage continuous settling area, which is provided with a big particle settling plate section, an intermediate particle settling plate section and a small particle settling pipe section from the bottom to the top in sequence. The three-stage continuous settling is adopted in the utility model, which settles the big particle, the intermediate particle and the small particle in sequence, as a result, the settling is continuous and highly efficient; for the settling disposal of sewage with high suspended matters and big water quality variation at one moment, the utility model has the advantages of high disposal efficiency, stable effect and small equipment area occupation; the utility model is the ideal choice of high suspended matter sewage settling disposal for the industries such as mining, metallurgy and metrification, etc., and has a remarkable economic and social effect.
Description
One, technical field:
The utility model relates to a kind of sewage disposal device, particularly settling vessel.
Two, background technology:
Sewage disposal has at present overcome the deficiency of original horizontal sedimentation tank, preferable scheme is to adopt the tube settling jar, as the disclosed tube settling jar of Chinese utility model patent CN2368585Y, as the core settling apparatus, it is big to have improved floor space to a certain extent, the energy consumption height, the problem of water treatment weak effect, but, find that in actual applications it still exists certain not enough problem, be provided with unreasonable as flow distribution plate, just consider that from prolonging the time of flow through after long-time the use, deposition is more in flow distribution plate and the tank body in addition, the precipitation ability descends gradually, so that water treatment effect instability; The artificial spoil disposal of mud discharging mouth in addition, automaticity is low, operation, maintenance cost height, energy consumption is big etc.
Three, summary of the invention:
The purpose of this utility model provides a kind of three grades of continuous sedimentation swash plate pipe settling vessels exactly for overcoming above-mentioned not enough problem, and is scientific and reasonable for structure, treatment effeciency is high, strong shock resistance, treatment effect stable, and its automaticity height, repair and maintenance are convenient in addition.
The technical scheme that the utility model is adopted for achieving the above object is as follows: a kind of three grades of continuous sedimentation swash plate pipe settling vessels, the settling vessel lower end has water inlet and mud discharging mouth, the upper end has delivery port and exhaust outlet, the bottom is the water inlet water distributing area in the settling vessel, the middle part is the decanting zone, top is the water outlet water distributing area, and the decanting zone, middle part is three grades of continuous decanting zones, and it is disposed with coarse granule settlement plate section, middle particles settling plate section and SEDIMENTATION FOR FINE PARTICLE pipeline section from bottom to top.
Top, described decanting zone is provided with the high pressure washing district, and high pressure is equipped with towards Xian's device in the high pressure washing district.
Described high pressure washing device is on the housing high-pressure water pipe to be housed, and high pressure nozzle is installed on the high-pressure water pipe.
Described settling vessel lower housing portion is that water inlet is provided with into water water distribution orifice plate, and water inlet water distribution orifice plate is the two-layer orifice plate that support connects, and upper strata orifice plate area is greater than lower floor's orifice plate, and top, high pressure washing district is the water outlet water distributing area, is provided with water outlet water distribution orifice plate.
Described water inlet water distributing area bottom is provided with independently automatic sludge discharger for heavy mud discharge area.
Described mud discharging device be one by motor-driven two-way conveyor screw, mud discharging mouth is equipped with sludge concentration monitoring device and electronic mud control valve.
The utility model adopts three grades of continuous sedimentations, sedimentation coarse granule, middle particle and fine grained successively, and sedimentation is continuous and efficient is high; Be provided with the high pressure washing device on the top of SEDIMENTATION FOR FINE PARTICLE pipeline section, connect external flushing water and can wash, remove deposition, guarantee that the sedimentation capacity of settling vessel does not descend settling vessel inside; At heavy mud discharge area automatic sludge discharger is housed, when settled sludge concentration reaches concentration of emission, then starts mud discharging device automatically and carry out spoil disposal; It is reasonable that water inlet distributing pore plate bilayer is provided with even water distribution.The utility model is for the precipitation process that contains the big sewage of high suspended matter and instantaneous change of water quality, have treatment effeciency height, effect stability, equipment and take up an area of characteristics such as few, be that the ideal that industry high suspended matter settlements of sewage such as mine, metallurgy, petrochemical industry are handled is selected its economic benefit and obvious social benefit.
Four, description of drawings:
Fig. 1 is the utility model structural representation.
Fig. 2 is an A enlarged drawing among Fig. 1.
Fig. 3 is a B enlarged drawing among Fig. 1.
Five, the specific embodiment:
Below in conjunction with specific embodiment and accompanying drawing the utility model is described in further detail:
A kind of three grades of continuous sedimentation swash plate pipe settling vessels as shown in Figure 1, the settling vessel housing is the cylindrical container of a steel, saddle support 8 is equipped with in order to support whole settling vessel in the bottom, the settling vessel upper and lower end is the ellipse end socket, have water inlet, inspection manhole and mud discharging mouth on the end socket of lower end, into water water distribution orifice plate 1 is equipped with for the water inlet water distributing area in settling vessel housing 7 lower ends on the water inlet; Water inlet water distributing area bottom offers mud discharging mouth and mud valve is installed for heavy mud discharge area; Settling vessel housing middle part is three grades of continuous decanting zones, be disposed with coarse granule settlement plate section 2, middle particles settling plate section 3 and SEDIMENTATION FOR FINE PARTICLE pipeline section 4 from bottom to top, the settlement plate spacing is adjustable, adopt anticorrosion, anti-stick, the assembly of high abrasion material, sedimentation pipe then is made up of one group of tube bank of different tube diameters, tube-surface all carries out the anti-stick intensive treatment, and the spoil disposal of each settling zone is independent separately; The settling vessel upper end has delivery port, inspection manhole f2 and steam vent e for the water outlet water distributing area on the end socket of upper end, delivery port is equipped with water outlet water distribution orifice plate 6.
Embodiment 2
Basic structure is identical with embodiment 1, be provided with the high pressure washing device on the top of SEDIMENTATION FOR FINE PARTICLE pipeline section, on the high pressure washing device case high-pressure water pipe is housed, the high pressure nozzle that many group multi-angles are arranged is installed on the high-pressure water pipe, the high-pressure water pipe inlet is connected external flushing water and can be washed settling vessel inside, removes deposition.
Embodiment 3
Basic structure is identical with embodiment 1 or 2, automatic sludge discharger 9, mud discharging device 9 are housed as shown in Figure 2 at heavy mud discharge area, it is a two-way conveyor screw that drives by motor 17, can discharge the mud of settling vessel lower end sedimentation automatically, mud discharging mouth is provided with sludge concentration monitoring device 10 and electronic mud control valve 11, sludge concentration monitoring device signal input control valve then starts mud discharging device automatically and carries out spoil disposal when settled sludge concentration reaches concentration of emission.
Claims (6)
1, a kind of three grades of continuous sedimentation swash plate pipe settling vessels, the settling vessel lower end has water inlet and mud discharging mouth, the upper end has delivery port and exhaust outlet, the bottom is the water inlet water distributing area in the device of sedimentation shallow lake, the middle part is the decanting zone, top is the water outlet water distributing area, it is characterized in that: the decanting zone is three grades of continuous decanting zones, and it is disposed with coarse granule settlement plate section, middle particles settling plate section and SEDIMENTATION FOR FINE PARTICLE pipeline section from bottom to top.
2, a kind of three grades of continuous sedimentation swash plate pipe settling vessels according to claim 1, it is characterized in that: top, decanting zone is provided with the high pressure washing district, and high pressure is equipped with towards Xian's device in the high pressure washing district.
3, a kind of three grades of continuous sedimentation swash plate pipe settling vessels according to claim 2, it is characterized in that: the high pressure washing device is on the housing high-pressure water pipe to be housed, and high pressure nozzle is installed on the high-pressure water pipe.
4, according to the arbitrary described a kind of three grades of continuous sedimentation swash plate pipe settling vessels of claim 1-3, it is characterized in that: the settling vessel lower housing portion is that water inlet is provided with into water water distribution orifice plate, water inlet water distribution orifice plate is the two-layer orifice plate that support connects, and upper strata orifice plate area is greater than lower floor's orifice plate; Top, high pressure washing district is the water outlet water distributing area, is provided with water outlet water distribution orifice plate.
5, according to the arbitrary described a kind of three grades of continuous sedimentation swash plate pipe settling vessels of claim 1-3, it is characterized in that: water inlet water distributing area bottom is provided with independently automatic sludge discharger for heavy mud discharge area.
6, a kind of three grades of continuous sedimentation swash plate pipe settling vessels according to claim 5 is characterized in that: mud discharging device be one by motor-driven two-way conveyor screw, mud discharging mouth is equipped with sludge concentration monitoring device and electronic mud control valve.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN200920010318U CN201370979Y (en) | 2009-01-19 | 2009-01-19 | Three-stage continuous settling sloping plate pipe precipitator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN200920010318U CN201370979Y (en) | 2009-01-19 | 2009-01-19 | Three-stage continuous settling sloping plate pipe precipitator |
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CN201370979Y true CN201370979Y (en) | 2009-12-30 |
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CN200920010318U Expired - Fee Related CN201370979Y (en) | 2009-01-19 | 2009-01-19 | Three-stage continuous settling sloping plate pipe precipitator |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106883128A (en) * | 2015-12-16 | 2017-06-23 | 巴斯夫欧洲公司 | The method that the method for heterogeneous catalysis is removed from product and aromatic amine is prepared |
WO2023066218A1 (en) * | 2021-10-18 | 2023-04-27 | 山东华通环境科技股份有限公司 | Precipitation plate, precipitation unit, and precipitation module |
-
2009
- 2009-01-19 CN CN200920010318U patent/CN201370979Y/en not_active Expired - Fee Related
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106883128A (en) * | 2015-12-16 | 2017-06-23 | 巴斯夫欧洲公司 | The method that the method for heterogeneous catalysis is removed from product and aromatic amine is prepared |
CN106883128B (en) * | 2015-12-16 | 2021-05-28 | 巴斯夫欧洲公司 | Method for removing heterogeneous catalyst from reaction product and method for producing aromatic amine |
WO2023066218A1 (en) * | 2021-10-18 | 2023-04-27 | 山东华通环境科技股份有限公司 | Precipitation plate, precipitation unit, and precipitation module |
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Legal Events
Date | Code | Title | Description |
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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: 20091230 Termination date: 20180119 |
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CF01 | Termination of patent right due to non-payment of annual fee |