CN102580368A - Spiral-flow type primary settling device for running water - Google Patents
Spiral-flow type primary settling device for running water Download PDFInfo
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- CN102580368A CN102580368A CN2012100833887A CN201210083388A CN102580368A CN 102580368 A CN102580368 A CN 102580368A CN 2012100833887 A CN2012100833887 A CN 2012100833887A CN 201210083388 A CN201210083388 A CN 201210083388A CN 102580368 A CN102580368 A CN 102580368A
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- Prior art keywords
- spiral
- running water
- water
- cylinder
- flow type
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances data:image/svg+xml;base64,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 data:image/svg+xml;base64,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 O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 58
- 239000008394 flocculating agent Substances 0.000 claims description 3
- 239000010865 sewage Substances 0.000 claims description 3
- 238000010276 construction Methods 0.000 abstract description 2
- 238000004140 cleaning Methods 0.000 abstract 1
- 230000001112 coagulant Effects 0.000 abstract 1
- 239000000701 coagulant Substances 0.000 abstract 1
- 238000004062 sedimentation Methods 0.000 description 6
- 239000007787 solid Substances 0.000 description 4
- 238000000975 co-precipitation Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000012071 phase Substances 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 230000001737 promoting Effects 0.000 description 1
Abstract
The invention provides a spiral-flow type primary settling device for running water, and relates to a water treatment device. The spiral-flow type primary settling device for the running water is characterized in that a cover is arranged at the top of a cylinder; the bottom of the cylinder is connected with a funnel; a spiral guiding plate is arranged in the cylinder; a water outlet is arranged at the upper part of the cylinder; a water inlet tube is arranged on the lower part of the cylinder; the outlet of the water inlet tube is located on an upper surface of the lower part of the spiral guiding plate; a drain outlet and a blow-off valve are arranged at the bottom of the funnel; and a coagulant feeding jar is connected to the water inlet tube. Compared with a running water primary settling tank, the spiral-flow type primary settling device for the running water provided by the invention has the advantages that the occupied area is small, the efficiency for running water primary settling treatment is high, the construction cost of the running water primary settling treatment is low, the cost of the running water primary settling treatment is low, and the spiral-flow type primary settling device for the running water is easily cleaned and quickly switched and has popularization value.
Description
Technical field
The present invention relates to a kind of water treatment facilities, particularly a kind of running water spiral-flow type is sink device just.
Background technology
At present, the former water to muddiness when running water is produced need carry out just heavy the processing earlier, and preliminary sedimentation tank is generally adopted in its just heavy processing, is provided with inclined tube or swash plate in the preliminary sedimentation tank, silt and flocculate in the special precipitinogen water, and its coprecipitation mode is natural sedimentation.There is a drawback in natural sedimentation, needs water to flow through very long distance exactly, causes the area of preliminary sedimentation tank huge, cleans difficulty, causes the running water production cost high.For this reason, remain to be explored new running water sink device just.
Summary of the invention
The object of the invention: a kind of running water spiral-flow type sink device just is provided.
Design of the present invention is: a kind of running water spiral-flow type is sink device just, and it is characterized in that: the top of cylinder is provided with lid, is connected with funnel in the bottom of cylinder; In cylinder, be provided with spiral deflector; Top at cylinder is provided with delivery port, is provided with water inlet pipe in the bottom of cylinder, and the outlet of water inlet pipe is positioned at the upper surface of the bottom of spiral deflector; Be provided with sewage draining exit and blowoff valve in the bottom of funnel, on water inlet pipe, be connected with flocculating agent and add jar.
Described running water spiral-flow type is sink device just, and the water tangent line that its water inlet pipe outlet jet goes out gets into the upper surface of spiral deflector bottom.
Described running water spiral-flow type is sink device just, and described blowoff valve is an automatic blowdown valve.
Operation principle of the present invention is: the solid, liquid two-phase mixture in curl field, under the effect of centrifugal force, gravity, centripetal force, solid matter total oriented in the bottom trend gathering, precipitate.Water tangential under certain pressure gets into spiral deflector; Make water in cylinder, form eddy current; The curl field of this programme is provided by spiral deflector; Built-in spiral deflector gradient moves downward solid matter silt and the flocculate that proportion is heavier in the water greater than the angle of repose of solid matter, and the water of liquid phase moves upward.
Running water spiral-flow type of the present invention just sink device is compared with the running water preliminary sedimentation tank, and it is little to have floor space, and the just heavy treatment effeciency of running water is high; The just heavy construction costs of handling of running water is low; The just heavy processing cost of running water is low, and running water just sink device cleans easily, cuts soon, has promotional value.
Description of drawings
Accompanying drawing is a structural representation of the present invention.
The specific embodiment
Through embodiment, the present invention is further described below.
Embodiment
With reference to accompanying drawing, a kind of running water spiral-flow type is sink device just, and it is characterized in that: the top of cylinder 3 is provided with covers 1; Be connected with funnel 5 in the bottom of cylinder 3, in cylinder 3, be provided with spiral deflector 4, be provided with delivery port 2 on the top of cylinder 3; Be provided with water inlet pipe 8 in the bottom of cylinder 3; The outlet of water inlet pipe 8 is positioned at the upper surface of the bottom of spiral deflector 4, is provided with sewage draining exit 7 and blowoff valve 6 in the bottom of funnel 5, on water inlet pipe 8, is connected with flocculating agent and adds jar 9.Described running water spiral-flow type is sink device just, and the water tangent line that its water inlet pipe 8 outlet jets go out gets into the upper surface of spiral deflector 4 bottoms.Described running water spiral-flow type is sink device just, and described blowoff valve 6 is an automatic blowdown valve.
Claims (3)
1. the first sink device of a running water spiral-flow type; It is characterized in that: the top of cylinder (3) is provided with lid (1); Be connected with funnel (5) in the bottom of cylinder (3), in cylinder (3), be provided with spiral deflector (4), be provided with delivery port (2) on the top of cylinder (3); Be provided with water inlet pipe (8) in the bottom of cylinder (3); The outlet of water inlet pipe (8) is positioned at the upper surface of the bottom of spiral deflector (4), is provided with sewage draining exit (7) and blowoff valve (6) in the bottom of funnel (5), on water inlet pipe (8), is connected with flocculating agent and adds jar (9).
2. running water spiral-flow type according to claim 1 is sink device just, it is characterized in that: the water tangent line that water inlet pipe (8) outlet jet goes out gets into the upper surface of spiral deflector (4) bottom.
3. running water spiral-flow type according to claim 1 and 2 is sink device just, and it is characterized in that: described blowoff valve (6) is an automatic blowdown valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012100833887A CN102580368A (en) | 2012-03-27 | 2012-03-27 | Spiral-flow type primary settling device for running water |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012100833887A CN102580368A (en) | 2012-03-27 | 2012-03-27 | Spiral-flow type primary settling device for running water |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN102580368A true CN102580368A (en) | 2012-07-18 |
Family
ID=46469935
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2012100833887A CN102580368A (en) | 2012-03-27 | 2012-03-27 | Spiral-flow type primary settling device for running water |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN102580368A (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB2502670A (en) * | 2012-03-21 | 2013-12-04 | Innovative Ind Ltd | Water recycling unit |
| CN104436768A (en) * | 2014-10-22 | 2015-03-25 | 河海大学 | Vertical stratification water-sediment separation device based on curved inclined plates |
| US20150090649A1 (en) * | 2012-03-21 | 2015-04-02 | Innovative Industries Limited | Water recycling unit |
| CN105169772A (en) * | 2015-08-14 | 2015-12-23 | 南京航空航天大学 | Spiral vortex inertial gathered scum rapid clearing device and operation method thereof |
| CN107034865A (en) * | 2017-04-27 | 2017-08-11 | 刘海飞 | The equipment of solid refuse in a kind of recycle-water |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO1992017260A1 (en) * | 1991-03-27 | 1992-10-15 | Jack Baggaley | Material treatment apparatus |
| US5840198A (en) * | 1994-07-29 | 1998-11-24 | International Fluid Separation Pty Ltd | Separation apparatus and method |
| CN1743279A (en) * | 2004-09-01 | 2006-03-08 | 陈会超 | Fully-sealed multi-layer spiral combined tilted plate separating device and method |
| CN201049911Y (en) * | 2007-04-24 | 2008-04-23 | 浙江大学 | Screw-type self-circulation biological reactor |
| CN201410337Y (en) * | 2009-06-03 | 2010-02-24 | 中国科学院兰州化学物理研究所 | Anti-disturbance floc sediment reverse separating tank |
| CN201473358U (en) * | 2009-05-07 | 2010-05-19 | 西南科技大学 | Vortex photocatalysis sewage pretreatment device |
-
2012
- 2012-03-27 CN CN2012100833887A patent/CN102580368A/en not_active Application Discontinuation
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO1992017260A1 (en) * | 1991-03-27 | 1992-10-15 | Jack Baggaley | Material treatment apparatus |
| US5840198A (en) * | 1994-07-29 | 1998-11-24 | International Fluid Separation Pty Ltd | Separation apparatus and method |
| CN1743279A (en) * | 2004-09-01 | 2006-03-08 | 陈会超 | Fully-sealed multi-layer spiral combined tilted plate separating device and method |
| CN201049911Y (en) * | 2007-04-24 | 2008-04-23 | 浙江大学 | Screw-type self-circulation biological reactor |
| CN201473358U (en) * | 2009-05-07 | 2010-05-19 | 西南科技大学 | Vortex photocatalysis sewage pretreatment device |
| CN201410337Y (en) * | 2009-06-03 | 2010-02-24 | 中国科学院兰州化学物理研究所 | Anti-disturbance floc sediment reverse separating tank |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB2502670A (en) * | 2012-03-21 | 2013-12-04 | Innovative Ind Ltd | Water recycling unit |
| GB2502670B (en) * | 2012-03-21 | 2015-01-14 | Innovative Ind Ltd | Water recycling unit |
| US20150090649A1 (en) * | 2012-03-21 | 2015-04-02 | Innovative Industries Limited | Water recycling unit |
| CN104436768A (en) * | 2014-10-22 | 2015-03-25 | 河海大学 | Vertical stratification water-sediment separation device based on curved inclined plates |
| CN105169772A (en) * | 2015-08-14 | 2015-12-23 | 南京航空航天大学 | Spiral vortex inertial gathered scum rapid clearing device and operation method thereof |
| CN105169772B (en) * | 2015-08-14 | 2017-01-18 | 南京航空航天大学 | Spiral vortex inertial gathered scum rapid clearing device and operation method thereof |
| CN107034865A (en) * | 2017-04-27 | 2017-08-11 | 刘海飞 | The equipment of solid refuse in a kind of recycle-water |
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Application publication date: 20120718 |