CN205925089U - Big circular sedimentation tank of tripe - Google Patents
Big circular sedimentation tank of tripe Download PDFInfo
- Publication number
- CN205925089U CN205925089U CN201620601341.9U CN201620601341U CN205925089U CN 205925089 U CN205925089 U CN 205925089U CN 201620601341 U CN201620601341 U CN 201620601341U CN 205925089 U CN205925089 U CN 205925089U
- Authority
- CN
- China
- Prior art keywords
- region
- diameter
- regional
- central region
- area
- 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.)
- Active
Links
Landscapes
- Treatment Of Sludge (AREA)
Abstract
The utility model provides a big circular sedimentation tank of tripe, from the top down divide into in proper order upper portion regional 1, go up transition region 2, middle part regional 3, transition region 4, lower region 5 down, 3 regional diameters at the middle part are the biggest, and 1 regional diameter on the upper portion is slightly little, and the lower region 5 diameter is minimum, the upper end on upper portion regional 1 is equipped with annular water collecting tank 7, transition region 2 is gone up in upper portion regional 1 and middle part region, is the cone and connects, and go to the bottom and respectively install the horizontal stainless steel meshwork of one deck in the top on last transition region 2, installs the filler between the two -layer net, and mesh aperture is less than the filler external diameter, it is connected to be the radius cone between middle part regional 3 and the lower region 5, there is a central inlet tube 6 from 1 regional central downwardly extending on the upper portion to 3 regional centers at the middle part, bottom from lower region 5 is connected with mud pipe 8, returns mud pipe 9, it links to each other with central inlet tube 6 through circulating pump 10, circulating line 11 to return mud pipe 9. It is little that the water yield is handled in the effective solution of this invention, and suspended solid concentration is high, and the poor problem of solid -liquid separation effect improves and separates the effect, and it is high that the underflow contains concentration admittedly.
Description
Technical field
A kind of big tripe circular settling tank and its solid-liquid separating method, belong to solid-liquid separation technique field.
Background technology
At present, solid-liquid separation is the necessary process in water treatment procedure, and is early stage process, and the effect of solid-liquid separation is straight
Connect and have influence on later stage process.There are multiple sedimentation tanks in solid-liquid separation technique field, for example, vertical sedimentation tank, radial-flow sedimentation tank, advection
Sedimentation tank, mechanical accelerating purifying pool, potassium permanganate composites etc..Vertical sedimentation tank is suitable for the little occasion of the water yield, goes out aqueous suspension dense
Degree is of a relatively high, and radial-flow sedimentation tank and horizontal sedimentation tank are suitable for into aqueous suspension in certain limit, mechanical accelerating purifying pool and height
Density sedimentation tank complex structure, cost is high.Processing, the water yield is little, and water inlet concentration of suspension is high and changes repeatedly it is desirable to underflow is solid
Containing high occasion, lack a kind of means of effective solid-liquid separation.
Content of the invention
This utility model provides a kind of big tripe circular settling tank, and its energy effectively solving process water yield is little, enters aqueous suspension dense
Degree is high, the problem of solid-liquid separation effect difference, improves separating effect, it is high that underflow contains concentration admittedly.
The technical solution of the utility model is realized in
This utility model provides a kind of big tripe circular settling tank, is divided into upper area 1, upper transitional region from top to bottom
2nd, central region 3, lower transitional region 4, lower area 5；Central region 3 diameter is maximum, and upper area 1 diameter is slightly smaller, lower region
Domain 5 diameter is minimum；The upper end of upper area 1 is provided with annular collecting vat 7；It is upper transition region between upper area 1 and central region 3
Domain 2, connects in cone, pushes up one layer of horizontal stainless (steel) wire of each installation of going to the bottom, be provided between two layers of mesh in upper transitional region 2
Filler, mesh aperture is less than filler external diameter；It is connected in inverted cone between central region 3 and lower area 5；From upper area 1
Center extends downward central region 3 center You Yige center water inlet pipe 6；From the bottom of lower area 5 be connected with discharge pipeline 8,
Return mud pipe 9；Return mud pipe 9 to be connected with center water inlet pipe 6 by circulating pump 10, circulating line 11.
Above-mentioned big tripe circular settling tank is it is characterised in that sedimentation tank total height is between 5m-14m；Central region 3 straight
Footpath is 1: 0.7-0.9 with the diameter ratio of upper area 1；The diameter of central region 3 is 1 with the diameter ratio of lower area 5:
0.4-0.6.
The application also provides a kind of solid-liquid separating method, and it utilizes above-mentioned big tripe circular settling tank separation solidliquid mixture,
First solidliquid mixture is entered central region 3 by center water inlet pipe 6, open the circulation pump 10 simultaneously, by lower area 5
Partly precipitated thing enters center water inlet pipe 6 by returning mud pipe 9, circulating pump 10 and circulating line 11, mixes with the new solid-liquid entering
Compound mixes, and big tripe circular settling tank is full of solidliquid mixture, in diameter maximum central region 3, coagulation, shape occurs
Become flco, solid-liquid initial gross separation completed by the effect of gravity, current rise, by upper transitional region 2, then collide with filler,
Tiny flco is intercepted further, forms clear water in upper area 1, by annular collecting vat 7 row of upper area 1 upper end
Go out, lower area 5 forms precipitate, is discharged by discharge pipeline 8.
According to above-mentioned solid-liquid separating method it is characterised in that sedimentation tank total height is between 5m-14m；Central region 3
The diameter ratio of diameter and upper area 1 be 1: 0.7-0.9；The diameter of central region 3 and the diameter ratio of lower area 5
For 1: 0.4-0.6.
If solidliquid mixture is mud slurry, upper area is clear water zone, and zone line is body refuse flocculation zone, bottom
Region is body refuse enrichment region；The body refuse circulating pump of lower area bottom is recycled to center water inlet pipe, and the dirt entering central canal
After material-mud mixing, central region is entered by center water inlet pipe, after central region completes coagulation, clear water mud, slag wadding upwards
Solidifying body sinks, and completes solid-liquid separation.
In central region, due to sludge circulation be increased by circulating pump, mix float in later mud slurry dense
Degree is high, and between mud granule, collision probability is big, quickly completes initial stage coagulation, flocculation process, and the batting-unit structure due to being formed is close
Real, ratio is great, easily precipitates, and enters the lower transitional region of cone, occur further in lower transitional region after separating with water
Crowded precipitation, flocculation bulk concentration improves further, finally enters lower area：Body refuse enrichment region, in body refuse enrichment region, floccule body
Concentration improves constantly, and floccule body is agglomerating, and proportion is bigger, compresses further, becomes body refuse, opens mud valve and discharges from discharge pipeline.
In central region, some tiny floccule body not flocculated, rise such as current, in upper transitional region
Push up one layer of horizontal stainless (steel) wire of each installation of going to the bottom, filler is installed between two layers of mesh, mesh aperture is less than filler external diameter, is equivalent to
Increase mud granule concentration in mud slurry, increase the collision probability of floccule body and filler, filler is equivalent to filter medium simultaneously,
Also there is adsorption on filler surface to floccule body, can effectively intercept tiny floccule body, purify water further.By adjusting filler
Highly (thickness), form of bio-carrier, the flow of adjustment sludge circulation pump, it is adapted to the change of water quality treatment it is ensured that separating effect.
On filler, the sludge solid of attachment is come off by downward current scour during lower area spoil disposal, enters middle region
Domain：Sludge suspension layer；Finally, the clear water after separating is concentrated by the annular collecting vat of upper area upper end and is discharged.
This utility model, according to the requirement processing the water yield, Inlet and outlet water concentration of suspension, bottom sediment, can design each
Plant parameter：The diameter (clear water zone diameter) of ￠ 1- upper area 1, the diameter (sludge suspension layer) of ￠ 2- central region 3, under ￠ 3-
The diameter (body refuse enrichment region) in portion region 5, the height (body refuse enrichment region) of H5- lower area 5, the height of transitional region 4 under H4-
(body refuse transition region), the height (sludge suspension layer) of H3- central region 3, the height (separating transition region) of the upper transitional region of H2- 2,
The height (clear water zone) of H1- upper area 1.Typically above-mentioned ginseng is determined by MaterialBalance Computation, structure design and model test
Number.
By above-mentioned big this design concept of tripe circular settling tank, the effect reaching is that the effectively solving process water yield is little, outstanding
Float concentration is high, the problem of solid-liquid separation effect difference, improves separating effect, it is high that underflow contains concentration admittedly.
Brief description
Fig. 1 is the structural representation of this utility model big tripe circular settling tank.
1- upper area；The upper transitional region of 2-；3- central region；Transitional region under 4-；5- lower area；6- center intakes
Pipe；7- annular collecting vat；8- discharge pipeline；9- returns mud pipe；10- circulating pump；11- circulating line；12- inlet channel.
Specific embodiment
Embodiment 1
A kind of big tripe circular settling tank, be divided into from top to bottom upper area 1, upper transitional region 2, central region 3, under
Transitional region 4, lower area 5；Central region 3 diameter is maximum, and upper area 1 diameter is slightly smaller, and lower area 5 diameter is minimum；On
The upper end in portion region 1 is provided with annular collecting vat 7；It is upper transitional region 2 between upper area 1 and central region 3, in cone
Connect, one layer of horizontal stainless (steel) wire of each installation of going to the bottom is pushed up on upper transitional region 2, filler, netted hole are installed between two layers of mesh
Footpath is less than filler external diameter；It is connected in inverted cone between central region 3 and lower area 5；Extend downwardly from upper area 1 center
To central region 3 center You Yige center water inlet pipe 6；It is connected with discharge pipeline 8, returns mud pipe 9 from the bottom of lower area 5；Return mud
Pipe 9 passes through circulating pump 10, circulating line 11 is connected with center water inlet pipe 6.This big tripe circular settling tank is used for processing electroplating and gives up
Water, this big tripe circular settling tank maximum gauge 2600mm, total height 6000mm, process water yield 250m3/ d, enters aqueous suspension
180mg/l, goes out aqueous suspension 15-20mg/l, body refuse concentration 8%-10%.
Comparative example 1
The straight tube vertical sedimentation tank of the same diameter 2600mm corresponding with embodiment 1, processes water yield 250m3/ d, water inlet
Float 180mg/l, goes out aqueous suspension >=40mg/l, body refuse concentration 5%.
Embodiment 2
A kind of solid-liquid separating method, it utilizes above-mentioned big tripe circular settling tank separation solidliquid mixture, mixes solid-liquid first
Compound enters central region 3, open the circulation pump 10 simultaneously by center water inlet pipe 6, and the partly precipitated thing in lower area 5 is led to
Cross back mud pipe 9, circulating pump 10 and circulating line 11 and enter center water inlet pipe 6, mix with the new solidliquid mixture entering, will be big
Tripe circular settling tank is full of solidliquid mixture, by the effect of gravity, forms clear water in upper area 1, by upper area 1
The annular collecting vat 7 at end is discharged, and lower area 5 forms precipitate, is discharged by discharge pipeline 8.This big tripe circular settling tank is used
In processing certain industrial wastewater, this big tripe circular settling tank maximum gauge 3200mm, total height 7000mm, process water yield 360m3/ d,
Enter aqueous suspension 280mg/l, go out aqueous suspension 18-22mg/l, body refuse concentration 10%-11%.
Comparative example 2
The straight tube vertical sedimentation tank of the same diameter 3200mm corresponding with embodiment 2, processes water yield 360m3/ d, water inlet
Float 180mg/l, goes out aqueous suspension >=40mg/l, body refuse concentration≤5%.
Claims (2)
1. a kind of big tripe circular settling tank, is divided into upper area (1), upper transitional region (2), central region from top to bottom
(3), lower transitional region (4), lower area (5)；Central region (3) diameter is maximum, and upper area (1) diameter is slightly smaller, lower region
Domain (5) diameter is minimum；The upper end of upper area (1) is provided with annular collecting vat (7)；Between upper area (1) and central region (3)
It is upper transitional region (2), connects in cone, go to the bottom one layer of horizontal stainless (steel) wire of each installation on the upper top of upper transitional region (2), two
Between layer net, filler is installed, mesh aperture is less than filler external diameter；It is in inverted cone between central region (3) and lower area (5)
Body connects；Extend downward central region (3) center You Yige center water inlet pipe (6) from upper area (1) center；From lower region
The bottom in domain (5) is connected with discharge pipeline (8), returns mud pipe (9)；Return mud pipe (9) pass through circulating pump (10), circulating line (11) with
Heart water inlet pipe (6) is connected.
2. big tripe circular settling tank according to claim 1 is it is characterised in that sedimentation tank total height is between 5m-14m；Middle part
The diameter in region (3) is 1: 0.7-0.9 with the diameter ratio of upper area (1)；The diameter of central region (3) and lower area
(5) diameter ratio is 1: 0.4-0.6.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620601341.9U CN205925089U (en) | 2016-06-09 | 2016-06-09 | Big circular sedimentation tank of tripe |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620601341.9U CN205925089U (en) | 2016-06-09 | 2016-06-09 | Big circular sedimentation tank of tripe |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205925089U true CN205925089U (en) | 2017-02-08 |
Family
ID=57932172
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620601341.9U Active CN205925089U (en) | 2016-06-09 | 2016-06-09 | Big circular sedimentation tank of tripe |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205925089U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107485894A (en) * | 2016-06-09 | 2017-12-19 | 余承烈 | A kind of big tripe circular settling tank and its solid-liquid separating method |
-
2016
- 2016-06-09 CN CN201620601341.9U patent/CN205925089U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107485894A (en) * | 2016-06-09 | 2017-12-19 | 余承烈 | A kind of big tripe circular settling tank and its solid-liquid separating method |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN208824000U (en) | A kind of overflow settling tank | |
| CN205925089U (en) | Big circular sedimentation tank of tripe | |
| CN205516881U (en) | Strengthen superposed layer spiral vertical flow settling pond | |
| CN112374653A (en) | Hydraulic classification separation and fine sand recovery method for treating wastewater from sandstone production | |
| JP2003503200A (en) | Wastewater purification method and apparatus | |
| CN201292297Y (en) | Integral water purifier | |
| CN105999776A (en) | Sludge layer filtering and settling pond and method thereof | |
| CN213012293U (en) | Mine water and electricity thickening vortex pretreatment system | |
| CN104496056A (en) | Method and device for treating high-turbidity source water | |
| CN212292954U (en) | Heavy-core high-density sewage purification device | |
| CN205867667U (en) | Mud slag blanket filter tank | |
| CN213037569U (en) | Cyclone air-float clarification tank | |
| CN211770698U (en) | Wastewater zero-discharge pretreatment integrated purification equipment in steel industry | |
| CN211595130U (en) | Variable-speed upflow expansion type coagulation reaction and central water distribution integrated precipitation device | |
| CN210163235U (en) | Vertical flow type sedimentation tank | |
| CN107485894A (en) | A kind of big tripe circular settling tank and its solid-liquid separating method | |
| CN206173070U (en) | Gravity type full -automatic water purification devices | |
| CN2885842Y (en) | High-turbidity sewage clarifier | |
| CN2179371Y (en) | Floating water purifier | |
| CN105585090B (en) | A kind of heavy auxiliary flocculation clarifier and method | |
| CN205398188U (en) | Heavily assist flocculation clarification device | |
| CN2144528Y (en) | Settling tower with pipe chute setting tank | |
| CN205472778U (en) | A radial flow , perpendicular heterogeneous attitude separator of combined type that flows for oil field extraction water | |
| CN101293149A (en) | Deposition technique and apparatus for sewage sludge funnel body refuse layer sloping plate (pipe chute) | |
| CN103265112B (en) | A kind of IC anaerobic reactor |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |