CN201179383Y - High-efficiency aggregation oil-removing settling separator - Google Patents
High-efficiency aggregation oil-removing settling separator Download PDFInfo
- Publication number
- CN201179383Y CN201179383Y CNU2008200334619U CN200820033461U CN201179383Y CN 201179383 Y CN201179383 Y CN 201179383Y CN U2008200334619 U CNU2008200334619 U CN U2008200334619U CN 200820033461 U CN200820033461 U CN 200820033461U CN 201179383 Y CN201179383 Y CN 201179383Y
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- China
- Prior art keywords
- chamber
- water
- water collecting
- inclined tube
- collecting 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
- 238000004220 aggregation Methods 0.000 title abstract 2
- 230000002776 aggregation Effects 0.000 title abstract 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 43
- 238000002156 mixing Methods 0.000 claims abstract description 18
- 238000001914 filtration Methods 0.000 claims abstract description 13
- 229910001220 stainless steel Inorganic materials 0.000 claims description 10
- 239000010935 stainless steel Substances 0.000 claims description 10
- 239000004519 grease Substances 0.000 claims description 5
- 230000001154 acute effect Effects 0.000 claims description 3
- 239000010865 sewage Substances 0.000 abstract description 16
- 238000006243 chemical reaction Methods 0.000 abstract description 7
- 239000003814 drug Substances 0.000 abstract description 7
- 230000000694 effects Effects 0.000 abstract description 5
- 230000002035 prolonged effect Effects 0.000 abstract description 2
- 238000000746 purification Methods 0.000 abstract description 2
- 238000005238 degreasing Methods 0.000 abstract 1
- 239000000706 filtrate Substances 0.000 description 6
- WYTGDNHDOZPMIW-RCBQFDQVSA-N alstonine Natural products C1=CC2=C3C=CC=CC3=NC2=C2N1C[C@H]1[C@H](C)OC=C(C(=O)OC)[C@H]1C2 WYTGDNHDOZPMIW-RCBQFDQVSA-N 0.000 description 5
- 238000010521 absorption reaction Methods 0.000 description 3
- 239000000701 coagulant Substances 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- 230000006835 compression Effects 0.000 description 2
- 238000007906 compression Methods 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000006004 Quartz sand Substances 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- RHZUVFJBSILHOK-UHFFFAOYSA-N anthracen-1-ylmethanolate Chemical compound C1=CC=C2C=C3C(C[O-])=CC=CC3=CC2=C1 RHZUVFJBSILHOK-UHFFFAOYSA-N 0.000 description 1
- 239000003830 anthracite Substances 0.000 description 1
- 238000011001 backwashing Methods 0.000 description 1
- 238000005345 coagulation Methods 0.000 description 1
- 230000015271 coagulation Effects 0.000 description 1
- 239000000084 colloidal system Substances 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000011152 fibreglass Substances 0.000 description 1
- 238000013467 fragmentation Methods 0.000 description 1
- 238000006062 fragmentation reaction Methods 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 238000012216 screening Methods 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
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- Water Treatment By Sorption (AREA)
Abstract
High-efficiency aggregation oil-removing settling separator. Relates to a treatment device for oily sewage. The two ends of the tank body are respectively provided with a water inlet and a water outlet, a buffer chamber, a rough filtering chamber, a degreasing chamber, a water collecting chamber, a reaction chamber, an inclined tube settling chamber and a filtering chamber which are communicated with each other are sequentially arranged in the tank body, a horn-shaped tangential mixing chamber is arranged in the reaction chamber, a water collecting pipe is arranged between the water collecting chamber and the tangential mixing chamber, a water inlet of the water collecting pipe is arranged at the upper part of the water collecting chamber, a water outlet of the water collecting pipe is arranged at the eccentric position of the small opening part of the tangential mixing chamber, and. The utility model is provided with an all-directional reaction chamber in the reaction chamber, the sewage after rough filtration is collected into the water collecting pipe in the water collecting chamber, the bottom of the water collecting pipe is provided with a medicine adding port, and the medicine is mixed into the sewage; the outlet of the water collecting pipe is arranged at the eccentric position of the small opening part of the tangential mixing chamber, and the outlet water forms a rotational flow in the horn-shaped component along the conical surface, so that the water flow path is prolonged, the water flow is more fully mixed, and the purification reaction effect of the medicament is more remarkable.
Description
Technical field
The utility model relates to a kind for the treatment of apparatus of oil-polluted water, particularly a kind of oil removing settlement separator.
Background technology
A kind of oily waste water treatment device is arranged in the prior art, and primary structure comprises the cylinder tank body of horizontal setting, and the tank body two ends are provided with intake-outlet, and first section is the absorption of serpentine filtrate; Second section is fiberglass swash plate Gravity Separation.During work, sewage enters, by the absorption Gravity Separation, the oil in the filtrate adsorbed water, thus realize water-oil separating, separation of glasses steel inclined tube produces the influence of deadweight, intensity, junk is smashed to pieces easily, so easy generation water quality deterioration, and the loss of flood peak increases, thereby influence water quality requirement, bring influence to treatment effect.Most critical be that in processing, the effect of find handling is poor, analyzes reason, mainly is sewage and the undercompounding of handling medicament, causes reaction inhomogeneous, complete.
The utility model content
For solving the above problems, the utility model provides a kind of efficient gathering oil removing settlement separator.Should remove the interior tangential mixing chamber of oil eliminator to producing eddy current, sewage can fully be mixed with medicament through the sewage after the dosing; The stainless steel inclined tube is difficult for being smashed to pieces by junk when work in addition, and it is effective that oil removing removes mechanical admixture like this, and service life of equipment is long.
The technical solution of the utility model is such: entery and delivery port is established at the tank body two ends respectively, be sequentially with the surge chamber that is interconnected, coarse filtration chamber in its tank body, remove grease chamber, collecting chamber, reative cell, inclined tube expansion chamber, filter chamber, in reative cell, be provided with horn-like tangential mixing chamber, between collecting chamber and tangential mixing chamber, establish collector pipe, the collector pipe water inlet is located at collecting chamber top, the collector pipe delivery port is located at the eccentric position at tangential mixing chamber osculum position, and water inlet is higher than delivery port.
Described collector pipe takes the shape of the letter U, and also is provided with dosing mouth in the bottom.
At the indoor oil removing stainless steel inclined tube of establishing of coarse filtrationization, angle is the obtuse angle between the horizontal plane of its incline direction and water (flow) direction; Be provided with the stainless steel inclined tube in the inclined tube expansion chamber, angle is an acute angle between its incline direction and water (flow) direction horizontal plane.
The utility model is provided with a trumpet-shaped tangential reative cell in reative cell, the sewage of process coarse filtration is collected into collector pipe in collecting chamber, and dosing mouth is established in the collector pipe bottom, and medicament is mixed in the sewage; The collector pipe outlet is arranged on the eccentric position at tangential mixing chamber osculum position, and like this, water outlet forms eddy flow along the conical surface in horn-like parts, prolonged flow path, and current mix more fully, make the purification reaction effect of medicament more remarkable.
Description of drawings
Fig. 1 is a structural representation of the present utility model
1 is water inlet among the figure, the 2nd, and surge chamber, the 3rd, oil drain out, the 4th, coarse filtration chamber, the 5th, collecting chamber, the 6th, collector pipe water inlet, the 7th, reative cell, the 8th, tangential mixing chamber, the 9th, receiving port, the 10th, stainless steel inclined tube, the 11st, serpentine, the 12nd, natural pebble, the 13rd, delivery port, the 14th, filter chamber, the 15th, inclined tube expansion chamber, the 16th, the collector pipe outlet, the 17th, dosing mouth, the 18th, remove the grease chamber, the 19th, mud discharging mouth, the 20th, oil removing inclined tube, the 21st, coarse filtration natural pebble.
Fig. 2 be among Fig. 1 A to view
The specific embodiment
As shown in Figure 1, 2, the utility model tank body two ends are established water inlet 1, delivery port 13 respectively, be sequentially with the surge chamber 2 that is interconnected, coarse filtration chamber 4 in its tank body, remove grease chamber 18, collecting chamber 5, reative cell 7, inclined tube expansion chamber 15, filter chamber 14, in reative cell 7, be provided with horn-like tangential mixing chamber 8, between collecting chamber 5 and tangential mixing chamber 8, establish collector pipe, collector pipe water inlet 6 is located at collecting chamber 5 tops, collector pipe delivery port 16 is located at the eccentric position at tangential mixing chamber 8 osculum positions, and water inlet 6 is higher than delivery port 16.
Collector pipe takes the shape of the letter U, and also is provided with dosing mouth 17 in the bottom.
Establish oil removing stainless steel inclined tube 20 in coarse filtration chamber 4, angle is the obtuse angle between the horizontal plane of its incline direction and water (flow) direction; Be provided with stainless steel inclined tube 10 in inclined tube expansion chamber 15, angle is an acute angle between its incline direction and water (flow) direction horizontal plane.
During the utility model work, sewage enters from water inlet 1, earlier be cushioned adjusting at surge chamber 2, enter coarse filtration chamber 4 afterwards by coarse filtration natural pebble 21 coarse filtration, the preliminary part oil of removing in the sewage, effluent stream after then being filtered is to removing grease chamber 18, oil droplet major part in the sewage is removed, mixed when the collecting chamber 5 and by the sewage after the oil removing from the coagulant of dosing mouth 17, enter tangential mixing chamber 8 then, water inlet produces eddy flow in tangential mixing chamber 8, thereby coagulant is further mixed with sewage, suspension colloid collides mutually in the water, stir, strengthened coagulation effect.Coagulant and sewage fully mix in reative cell 7, formed bigger flco, the flco that forms in inclined tube expansion chamber 15 is along 10 sedimentations of stainless steel inclined tube subsequently, last sewage is further adsorbed by serpentine 11 filtrates and natural pebble 12 in filter chamber 14, form oil-containing and mechanical admixture water up to standard, discharge from delivery port 13.Oil that produces in the equipment running process and mud are discharged from receiving port 9, receipts mud mouth, oil drain out 3, mud discharging mouth 19 respectively.During backwash, backwashing water carries out backwash from the backwash mouth to natural pebble 12, serpentine filtrate 11 and stainless steel swash plate 10 and recovers its performance.The serpentine filtrate that equipment adopted is the granular product that is processed into through fragmentation, screening, wet concentration, and it is a kind of novel filtrate behind quartz sand, anthracite.Its main feature is compression strength height (the average resistance to compression limit is 528kg/cm3); Absorption property is (adsorption rate to oily waste water is 27%) better; Lipophilic-hydrophobic property is good, and oil resistivity is strong, does not produce and hardens, and backwash is easy, and it is convenient to change; Chemical property is stable, and the proportion of goods damageds are very little in acid, aqueous slkali, can not cause change of water quality.
Claims (3)
1, efficiently assembles the oil removing settlement separator, entery and delivery port is established at the tank body two ends respectively, be sequentially with the surge chamber that is interconnected, coarse filtration chamber in its tank body, remove grease chamber, collecting chamber, reative cell, inclined tube expansion chamber, filter chamber, it is characterized in that, in reative cell, be provided with horn-like tangential mixing chamber, between collecting chamber and tangential mixing chamber, establish collector pipe, the collector pipe water inlet is located at collecting chamber top, the collector pipe delivery port is located at the eccentric position at tangential mixing chamber osculum position, and water inlet is higher than delivery port.
2, efficient gathering oil removing settlement separator according to claim 1 is characterized in that described collector pipe takes the shape of the letter U, and also is provided with dosing mouth in the bottom.
3, efficient gathering oil removing settlement separator according to claim 1 is characterized in that, at the indoor oil removing stainless steel inclined tube of establishing of coarse filtrationization, angle is the obtuse angle between the horizontal plane of its incline direction and water (flow) direction; Be provided with the stainless steel inclined tube in the inclined tube expansion chamber, angle is an acute angle between its incline direction and water (flow) direction horizontal plane.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2008200334619U CN201179383Y (en) | 2008-03-25 | 2008-03-25 | High-efficiency aggregation oil-removing settling separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2008200334619U CN201179383Y (en) | 2008-03-25 | 2008-03-25 | High-efficiency aggregation oil-removing settling separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201179383Y true CN201179383Y (en) | 2009-01-14 |
Family
ID=40248886
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2008200334619U Expired - Fee Related CN201179383Y (en) | 2008-03-25 | 2008-03-25 | High-efficiency aggregation oil-removing settling separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201179383Y (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101781040A (en) * | 2010-03-12 | 2010-07-21 | 余金海 | Treatment device of oily sewage of oil field |
| CN104649453A (en) * | 2015-02-27 | 2015-05-27 | 江苏江大环境工程有限责任公司 | Oil-separation recovery combination apparatus |
| CN104694156A (en) * | 2015-03-12 | 2015-06-10 | 崔斌 | Eccentric sedimentation pre-dehydrator and method for separating oil-water mixed solution in oil field |
| CN115340200A (en) * | 2022-08-29 | 2022-11-15 | 廊坊市北方天宇机电技术有限公司 | Device and method for circularly treating finishing liquid |
-
2008
- 2008-03-25 CN CNU2008200334619U patent/CN201179383Y/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101781040A (en) * | 2010-03-12 | 2010-07-21 | 余金海 | Treatment device of oily sewage of oil field |
| CN101781040B (en) * | 2010-03-12 | 2011-12-21 | 余金海 | Treatment device of oily sewage of oil field |
| CN104649453A (en) * | 2015-02-27 | 2015-05-27 | 江苏江大环境工程有限责任公司 | Oil-separation recovery combination apparatus |
| CN104649453B (en) * | 2015-02-27 | 2016-11-30 | 江苏江大环境工程有限责任公司 | Unit equipment is reclaimed in a kind of oil removal |
| CN104694156A (en) * | 2015-03-12 | 2015-06-10 | 崔斌 | Eccentric sedimentation pre-dehydrator and method for separating oil-water mixed solution in oil field |
| CN115340200A (en) * | 2022-08-29 | 2022-11-15 | 廊坊市北方天宇机电技术有限公司 | Device and method for circularly treating finishing liquid |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20090114 Termination date: 20110325 |