CN201390660Y - Flocculation sedimentation degreaser - Google Patents
Flocculation sedimentation degreaser Download PDFInfo
- Publication number
- CN201390660Y CN201390660Y CN200920070684U CN200920070684U CN201390660Y CN 201390660 Y CN201390660 Y CN 201390660Y CN 200920070684 U CN200920070684 U CN 200920070684U CN 200920070684 U CN200920070684 U CN 200920070684U CN 201390660 Y CN201390660 Y CN 201390660Y
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- degreaser
- waved plate
- oil
- grease
- oil eliminator
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Abstract
The utility model discloses a flocculation sedimentation degreaser which is characterized in that the one side of the shell of the degreaser is provided with an inlet pipe, and the other side of the shell of the degreaser is provided with an outlet pipe; the inlet pipe is provided with a perforated pipe distributing device, the upper part of which is provided with a pipeline mixer; the shell of the degreaser is internally provided with a crossing fluid type corrugated plate mechanism; the grease in the free state can be removed effectively; the grease content of effluent is reduced to 2mg/l, the suspended matter content of the effluent is lower than 10mg/l; the device is internally provided with a grease storage groove and a slurry V-shaped storage groove with a worm propeller; and investment and the operating cost of the whole system are reduced; and the maximum capability of a single machine is 1000m<3>/h; and the flocculation sedimentation degreaser can reduce the pollution load of the downstream equipment, reduce the investment and operating cost of the whole system. The flocculation sedimentation degreaser adopts aggregating type corrugated plate fillers; the outlet is provided with an adjustable stainless steel cofferdam; the materials of the equipment shell structure comprise carbon steel (internal and external preservative treatment), concrete, stainless steel and the like; and the separated grease can be removed by a tubular collector or a grease scraper.
Description
Technical field:
The utility model relates to the technical field of industrial wastewater treatment system, specifically to the oil-containing industrial water of discharging clarify, oily water separation handles, recycle after making it to reach standards for industrial water usage, particularly its mechanical connecting structure.
Background technology:
Oil-containing industrial water generally adopts ordinary methods such as coalescing agent, DGF, waterpower sand separator and whizzer, and ordinary method has separating medium to stop up easily, and parting material needs frequent regenerated shortcoming.It is the waved plate material of flyover formula that the utility model flocculent settling degreaser adopts filler, basic functional principle meets the stokes law fully, can remove the oil droplet of the unbound state more than the 20 μ m in the water. when removing oil droplet, remove the suspended substance solid again, reached good oil-water separation.
Conventional method floor space is big, is not easy to arrange on the ground that flocculent settling degreaser can be arranged on the ground, also can adopt buried layout. and be as low as zero following 30 degrees centigrade the time in temperature, do not adopt the heating measure still can works better.
Summary of the invention:
The purpose of this utility model is to provide a kind of flocculent settling degreaser, for a kind of system flow is simple, takes up an area of for a short time, and Collecting flocculation, precipitation, oil removing are in the flocculation oily-water seperating equipment of one.Wherein the material structure of flocculent settling degreaser is shaped to the waved plate of flyover formula, and the direction of the plate of flyover formula waved plate is intersected, and the contact area of particle and plate increases, and is easy to precipitation, has overcome the shortcoming and defect that prior art exists.
To achieve these goals, technical scheme of the present invention is: a kind of flocculent settling degreaser, it mainly comprises the oil eliminator housing, it is characterized in that: described oil eliminator housing one side is provided with inlet pipe, oil eliminator housing opposite side is provided with outlet pipe, inlet pipes is provided with the perforated pipe flow distribution apparatus, perforated pipe flow distribution apparatus top is provided with line mixer, be provided with intersection fluid-type waved plate mechanism in the oil eliminator housing, one side of intersection fluid-type waved plate mechanism is the perforated pipe flow distribution apparatus, the opposite side of intersection fluid-type waved plate mechanism is provided with oil trap, but the oil trap place is provided with regulating weir, the oil eliminator housing bottom is provided with the V-arrangement mud-collecting slot, and V-arrangement mud-collecting slot place is provided with the screw rod slurry conveying machine.
The utility model discloses a kind of flocculent settling degreaser, its characteristics are: the oil that can efficiently remove unbound state, the water outlet oleaginousness is low to moderate 2mg/l, the water outlet suspension content is lower than 10mg/l, device has the mud V-type storage tank of built-in oily storage tank and band worm propeller, separate unit maximum output: 1000m
3/ h, the utility model can reduce the pollution load of upstream device, reduces the investment and the working cost of total system.The utility model adopts the accumulation type corrugated plate packing, and the exit is provided with adjustable stainless steel cofferdam, the device housings structured material: carbon steel (internal and external anti-corrosive processing), and concrete, stainless steel etc., the oil of separating can be removed by tubular collector or Oil scraper.
Description of drawings:
Fig. 1 is the utility model structural representation
Fig. 2 is the total vertical view of the utility model
Fig. 3 is the utility model intersection fluid-type waved plate mechanism structure synoptic diagram
Embodiment:
With reference to the accompanying drawings, the utility model further is described
The utility model is a kind of flocculent settling degreaser, it mainly comprises the oil eliminator housing, it is characterized in that: described oil eliminator housing one side is provided with inlet pipe 1, oil eliminator housing opposite side is provided with outlet pipe 9, inlet pipe 1 place is provided with perforated pipe flow distribution apparatus 8, perforated pipe flow distribution apparatus 8 tops are provided with line mixer 7, be provided with intersection fluid-type waved plate mechanism 2 in the oil eliminator housing, one side of intersection fluid-type waved plate mechanism 2 is a perforated pipe flow distribution apparatus 8, the opposite side of intersection fluid-type waved plate mechanism 2 is provided with oil trap 3, but oil trap 3 places are provided with regulating weir 4, and the oil eliminator housing bottom is provided with V-arrangement mud-collecting slot 5, and V-arrangement mud-collecting slot 5 places are provided with screw rod slurry conveying machine 6.
In the specific implementation, described intersection fluid-type waved plate mechanism 2 is by being parallel to each other and horizontally disposed waved plate constitutes, spacing between the waved plate is 10mm-20mm, decide as required, described waved plate is a polyvinyl chloride, hard chlorine polyethylene and polypropylene, stainless steel, described oil eliminator housing bottom is provided with water shoot 10, and described intersection fluid-type waved plate mechanism 2 tops are provided with baffle plate 11.
Water (flow) direction is normally along the waved plate percolation or to dirty.Recommend (API publishes 421 water-and-oil separator standard and operational standards) according to U.S. API standard, the typical distance between plates between the waved plate is between 0.75 to 1.5 inch.Yet the case of successfully using when reducing to 0.25 inch, distance between plates is arranged also.When waved plate uses the greasy filth that can cause when overstocked in the waved plate dirty stifled.Generally we just use high pressure water washing in order to address this problem.The waved plate of big quantity theoretically can more effective removals oil, and the while also needs more frequent maintenance.Generally between the 45-60 degree, angle is big more for the angle of waved plate, and the sedimentation congregational rate of mud is good more.
The accumulation type filler is made up of PVC or PP waved plate.Every waved plate is the 45-60 degree and combines, and relies on the hasp of ripple connecting portion to bond between the every waved plate.Therefore form the space of relative percolation, guaranteed the passage of current.The waved plate medium of percolation forces current chop and change direction, and this helps little elaioleucite to contact with the surface collision of waved plate.Advection separates very important for liquid liquid, small turbulent flow helps oil droplet to assemble separation in the waved plate.
The carbon steel system of being illustrated in figure 1 as ground type flocculent settling degreaser, the normal water inlet of design SS≤300mg/l, interior in short-term influent turbidity is not more than 400mg/l, and delivery turbidity is not more than 20mg/l, the oleaginousness≤500mg/L of normally intaking, water outlet oleaginousness≤2mg/L.The utility model can be realized automatic control, can move continuously, guarantees that effluent quality is even, but monitoring continuously.
Oily(waste)water enters flocculent settling degreaser by inlet pipe.Owing to be provided with the perforated pipe flow distribution apparatus in ingress, oily(waste)water produces laminar flow stably after changing flow direction, slowly enters intersection fluid-type waved plate, and this waved plate is called collector on chemical industry.This corrugated plate is a base mateiral with PVC, includes multiple additives, makes it have oleophylic and sticking oily, aging-resistant characteristics.Waved plate stacks up one by one, and distance between plates is 12.7mm.Usually the employing level is installed.When the liquid flow mistake, oil droplet is caught rapidly by waved plate, promptly can accumulate on the waved plate, and come with water sepn.Because the principle of collector, short grained oil droplet is easy to be caught by lipophilic waved plate, being caught the back by waved plate moves up and constantly is gathered into oarse-grained oil droplet along the hyperchannel of waved plate, the oil droplet of larger particles is according to the Stokes principle, float to the surface of water-and-oil separator rapidly, profit is thoroughly separated.
One oil trap is set in the flocculent settling degreaser, flows into when the sump oil of separating reaches certain thickness in the oil trap, but on float to the water surface the regulating weir 4 of sump oil by oil trap flow in the oil traps, flow into outside 1m by gravity again
3PP material fuel tank in, thereby finished the whole process of oily water separation.
The flocculent settling degreaser bottom of device is established V-arrangement mud-collecting slot 5, and the mud of collecting in the mud-collecting slot is discharged by the screw rod slurry conveying machine, and sludge discharging period is 6 hours.The flocculation agent that adds by volume pump in line mixer 7 with the waste water thorough mixing after, form oarse-grained alumen ustum, alumen ustum is settled down in the flyover waved plate in the V-arrangement mud groove.
Flocculent settling degreaser adopts the waved plate material of flyover formula--figure (3), this material had both had the characteristic of waved plate, the moulding (60 ° of swash plate angles) that has swash plate again, flyover formula waved plate adopts PVC (temperature can reach 60 ℃), HPVC (high-temperature PVC, temperature can reach 65 ℃) and three kinds of materials of PP (polypropylene, temperature can reach 85 ℃).But when medium temperature surpasses more than 85 ℃, can adopt stainless material, specification be high 1 foot, 2 feet, wide 1 foot, 2 feet, long 4,6,8,10 feet.For non-metallic material, base mateiral contains multiple additives, makes it have oleophylic performance (but sticking oil), anti-chemical, UV resistant and characteristics such as anti-aging.Spacing is 12.7mm (for the waste water of high suspended matter, can adopt spacing is the design of 19mm) between plate.Therefore, when current passed through filler, short grained oil droplet only needed rising 12.7mm under the effect of gravity, can touch and hit the collector plate, is promptly caught by waved plate.We claim that this phenomenon is that gravity quickens separation principle.Because the effect of collector, short grained oil droplet can be gathered into larger oil droplet, and oil droplet upwards flows along the plate structure of filler.According to the stocks law, the oil droplet of larger particles can climb up on top of the water rapidly, separates fully with water body.
According to Fig. 3 as can be seen, the waved plate of flyover formula is similar to the swash plate in the inclined-plate clarifying basin, and it is except the passage that water stream channel, oil come-up are provided, and is the same with inclined-plate clarifying basin, the passage that also provides suspended substance to sink, its slagging-off function is the same with inclined-plate clarifying basin.And its slagging-off effect is better than inclined-plate clarifying basin, the direction unanimity of the plate of inclined-plate clarifying basin, and the direction of the plate of the waved plate of three-dimensional staggered form is intersected, the contact area of particle and plate increases, easier precipitation.
Claims (5)
1, a kind of flocculent settling degreaser, it mainly comprises the oil eliminator housing, it is characterized in that: described oil eliminator housing one side is provided with inlet pipe (1), oil eliminator housing opposite side is provided with outlet pipe (9), inlet pipe (1) locates to be provided with perforated pipe flow distribution apparatus (8), perforated pipe flow distribution apparatus (8) top is provided with line mixer (7), be provided with intersection fluid-type waved plate mechanism (2) in the oil eliminator housing, one side of intersection fluid-type waved plate mechanism (2) is perforated pipe flow distribution apparatus (8), the opposite side of intersection fluid-type waved plate mechanism (2) is provided with oil trap (3), oil trap (3) but locate to be provided with regulating weir (4), the oil eliminator housing bottom is provided with V-arrangement mud-collecting slot (5), and V-arrangement mud-collecting slot (5) locates to be provided with screw rod slurry conveying machine (6).
2, a kind of flocculent settling degreaser according to claim 1 is characterized in that: described intersection fluid-type waved plate mechanism (2) is by being parallel to each other and horizontally disposed waved plate constitutes, and the spacing between the waved plate is 10mm-20mm.
3, a kind of flocculent settling degreaser according to claim 2 is characterized in that: described waved plate is a polyvinyl chloride, hard chlorine polyethylene and polypropylene, stainless steel.
4, a kind of flocculent settling degreaser according to claim 1 is characterized in that: described oil eliminator housing bottom is provided with water shoot (10).
5, a kind of flocculent settling degreaser according to claim 1 is characterized in that: described intersection fluid-type waved plate mechanism (2) top is provided with baffle plate (11).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN200920070684U CN201390660Y (en) | 2009-04-17 | 2009-04-17 | Flocculation sedimentation degreaser |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN200920070684U CN201390660Y (en) | 2009-04-17 | 2009-04-17 | Flocculation sedimentation degreaser |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201390660Y true CN201390660Y (en) | 2010-01-27 |
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ID=41597482
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN200920070684U Expired - Fee Related CN201390660Y (en) | 2009-04-17 | 2009-04-17 | Flocculation sedimentation degreaser |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201390660Y (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102320679A (en) * | 2011-06-22 | 2012-01-18 | 浙江大学 | The whirlwind-type corrugated plate intercepter |
-
2009
- 2009-04-17 CN CN200920070684U patent/CN201390660Y/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102320679A (en) * | 2011-06-22 | 2012-01-18 | 浙江大学 | The whirlwind-type corrugated plate intercepter |
| CN102320679B (en) * | 2011-06-22 | 2012-08-15 | 浙江大学 | Spiral-flow type corrugated plate oil separation pool |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| ASS | Succession or assignment of patent right |
Owner name: WATER SERVICE (HOLDING) INC., SHANGHAI. Free format text: FORMER OWNER: BAIN WATER TREATMENT ENGINEERING CO., LTD. SHANGHAI Effective date: 20100630 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| COR | Change of bibliographic data |
Free format text: CORRECT: ADDRESS; FROM: 200040 ROOM 102-B, NO.3035, ZHUFENG HIGHWAY, LIANTANG TOWN, QINGPU DISTRICT, SHANGHAI CITY TO: 201700 ROOM 305, DISTRICT A, 3RD FLOOR, BUILDING 1, NO.3424, ZHUFENG HIGHWAY, QINGPU DISTRICT, SHANGHAI CITY |
|
| TR01 | Transfer of patent right |
Effective date of registration: 20100630 Address after: 201700, Qingpu District, Shanghai Zhu Feng Road No. 1, 3424, 3, A District, Room 305 Patentee after: Shanghai Safbon Water Service Co., Ltd. Address before: Liantang Town Qingpu District Shanghai City 200040 Zhu Feng Highway No. 3035 room 102-B Patentee before: Shanghai Baan Water Treatment Engineering Co., Ltd. |
|
| 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: 20100127 Termination date: 20180417 |