CN208747798U - Integrated deoiling separator for removing dirt - Google Patents
Integrated deoiling separator for removing dirt Download PDFInfo
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- CN208747798U CN208747798U CN201820928168.2U CN201820928168U CN208747798U CN 208747798 U CN208747798 U CN 208747798U CN 201820928168 U CN201820928168 U CN 201820928168U CN 208747798 U CN208747798 U CN 208747798U
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- flocculation reaction
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- water
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- 238000005189 flocculation Methods 0.000 claims abstract description 77
- 230000016615 flocculation Effects 0.000 claims abstract description 77
- 238000006243 chemical reaction Methods 0.000 claims abstract description 73
- 239000010802 sludge Substances 0.000 claims abstract description 51
- 239000002893 slag Substances 0.000 claims abstract description 16
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 110
- 239000006004 Quartz sand Substances 0.000 claims description 15
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 15
- RHZUVFJBSILHOK-UHFFFAOYSA-N anthracen-1-ylmethanolate Chemical compound C1=CC=C2C=C3C(C[O-])=CC=CC3=CC2=C1 RHZUVFJBSILHOK-UHFFFAOYSA-N 0.000 claims description 14
- 239000003830 anthracite Substances 0.000 claims description 14
- 239000003245 coal Substances 0.000 claims description 12
- 239000000945 filler Substances 0.000 claims description 9
- 239000000203 mixture Substances 0.000 claims description 4
- 235000009496 Juglans regia Nutrition 0.000 claims description 3
- 238000007599 discharging Methods 0.000 claims description 3
- 239000012535 impurity Substances 0.000 claims description 3
- 235000020234 walnut Nutrition 0.000 claims description 3
- 238000001179 sorption measurement Methods 0.000 claims description 2
- 240000007049 Juglans regia Species 0.000 claims 1
- 238000005352 clarification Methods 0.000 claims 1
- 239000000126 substance Substances 0.000 abstract description 4
- 239000010410 layer Substances 0.000 description 30
- 239000003921 oil Substances 0.000 description 23
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 20
- 238000001914 filtration Methods 0.000 description 11
- 229910052742 iron Inorganic materials 0.000 description 10
- 238000013461 design Methods 0.000 description 7
- 238000004062 sedimentation Methods 0.000 description 6
- 239000003814 drug Substances 0.000 description 5
- 239000002351 wastewater Substances 0.000 description 5
- 229910000831 Steel Inorganic materials 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 238000012856 packing Methods 0.000 description 4
- 239000002245 particle Substances 0.000 description 4
- 239000010959 steel Substances 0.000 description 4
- 230000009286 beneficial effect Effects 0.000 description 3
- 239000008187 granular material Substances 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 241000758789 Juglans Species 0.000 description 2
- 238000009749 continuous casting Methods 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 238000005098 hot rolling Methods 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 102000002322 Egg Proteins Human genes 0.000 description 1
- 108010000912 Egg Proteins Proteins 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 238000011001 backwashing Methods 0.000 description 1
- 239000000701 coagulant Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000000706 filtrate Substances 0.000 description 1
- 230000003311 flocculating effect Effects 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 210000004681 ovum Anatomy 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 239000011435 rock Substances 0.000 description 1
- 238000009991 scouring Methods 0.000 description 1
- 239000002344 surface layer Substances 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
Landscapes
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
The utility model discloses integrated deoiling separator for removing dirt, including device noumenon, described device body upper part is settling section, lower part is the area Ni Jiang, symmetrical sludge hopper is equipped with below the area Ni Jiang, the flocculation reaction room is divided into the first flocculation reaction room and the second flocculation reaction room, first flocculation reaction room is nested in the second flocculation reaction room, first flocculation reaction room is connected to the second flocculation reaction room by the open lower end in the first flocculation reaction room, slag gathering hopper is connected below second flocculation reaction room, apopore is equipped with above second flocculation reaction room, the apopore is close to the symmetrical sludge hopper, the symmetrical expression sludge hopper includes two pieces of symmetrical bucket cone-plates, the angle of the bucket cone-plate and horizontal plane is 45 degree, " ridge " structure that angle is 90 degree is formed between two pieces of bucket cone-plates.The utility model combines chemical oil remover and the institute of high rate filter is functional, reduces occupied area.
Description
Technical field
The utility model relates to field of environment protection equipment, and in particular to integrated deoiling separator for removing dirt.
Background technique
Contain iron scale and oil in steel industry continuous casting or hot rolling turbid circulating water, original treatment process is using " chemistry removes
Oily device+high rate filter ", oil-containing muddy water are discharged overflow to hot water after pump is promoted to chemical oil remover oil removing turbidity removal from workshop
Then pond is forced into the further oil removing turbidity removal of high rate filter with elevator pump and handles, high rate filter water outlet is directly entered cooling
Tower cools down, and cooling tower discharges water to circulating water pool, is forced into workshop reuse by water supply pump.High rate filter needs regular backwash,
Backwash need to separately set backwashing pump.
The above Processing Equipment, which takes up a large area, invests high operating cost, cumbersome, water quality and spoil disposal is difficult to control
System.
Utility model content
The utility model provides a kind of integrated deoiling separator for removing dirt, and which solves all of above shortcomings.
The utility model one takes up little area: equipment combines chemical oil remover and the institute of high rate filter is functional, reduces occupied area；
Two is with low investment: system eliminates hot-tub, elevator pump, filter backwash water pump etc., saves system investments；Three energy consumptions are small: being
System eliminates elevator pump, filter backwash water pump, saves electric energy；Four water consumption are small: higher speed filter, greatly reduce anti-
Wash water consumption；Five equipment are Automatic Control, have prevented due to artificial carelessness and caused the failure of equipment, and mitigate the work of personnel
It measures.
To achieve the above object, the utility model provides the following technical solutions:
Integrated deoiling separator for removing dirt, including device noumenon, described device body upper part are settling section, and lower part is mud drop
Area, the settling section lower part are equipped with porous spherical filler, symmetrical sludge hopper, described device ontology are equipped with below the area Ni Jiang
Center is equipped with central tube and flocculation reaction room, and the flocculation reaction room connects water inlet pipe, and the upper end of the central tube is catch basin,
Lower end is water distributing trough, and the water distributing trough side is equipped with sparge pipe, and the flocculation reaction room is sunk type flocculation reaction room, under described
Heavy formula flocculation reaction room passes through the lower part that the symmetrical sludge hopper protrudes into described device ontology, and the flocculation reaction room is divided into the
One flocculation reaction room and the second flocculation reaction room, first flocculation reaction room are nested in the second flocculation reaction room, and described
One flocculation reaction room lower end is open, and first flocculation reaction room and the second flocculation reaction room are open by the first flocculation reaction room
Lower end connection, slag gathering hopper is connected below second flocculation reaction room, is equipped with apopore above second flocculation reaction room,
For the apopore close to the symmetrical sludge hopper, the symmetrical expression sludge hopper includes two pieces of symmetrical bucket cone-plates, the mud
The angle of bucket cone-plate and horizontal plane is 45 degree, and " ridge " structure that angle is 90 degree, institute are formed between two pieces of bucket cone-plates
The top for stating symmetrical sludge hopper is equipped with backwash discharge outlet, and the bottom of the symmetrical expression sludge hopper is connected to device by sludge pipe
Filter layer is arranged in the mud discharging mouth of this body side surface, symmetrical expression sludge hopper lower section, and described device body bottom portion is provided with water outlet.
Preferably, the slag gathering hopper of second flocculation reaction room and lower end is integrated, and the slag gathering hopper is taper
Structure, the slag gathering hopper lower end are equipped with Residue extraction pipeline.
Preferably, the water distributing trough side is symmetrically arranged with 6 sparge pipes, and the every sparge pipe is by transverse pipe and longitudinal pipe
Composition, the transverse pipe are connected with longitudinal pipe by connector, and the sparge pipe transverse pipe is by equidistantly distributing in water distributing trough
Side, the longitudinal pipe pass through symmetrical sludge hopper, and the water distribution tube end is equipped with inlet damper.
Preferably, the filter layer includes anthracite coal measure, quartz sand layer and boulder bed, anthracite coal measure, quartz sand layer and ovum
Rock layers are sequentially arranged composition filter layer from top to bottom.
Preferably, anthracite coal measure thickness is 350mm, uses partial size for the anthracite of 2~4mm, walnut shell or haydite, to inhale
It is attached to go in water removal to remain oil content；Quartz sand layer thickness is 350mm, uses partial size for the quartz sand of 1~2mm, to retain drainage
The impurity such as middle suspended matter；Cobble thickness is 250mm, uses partial size for the cobble of 2~8mm.
Preferably, the filter layer is stacked on porous filter plate, several water caps are disposed in porous filter plate plate face, porous
Filter plate arranged beneath has the gas distribution pipe being connected to compressed air inlet, and described device ontology is equipped with upper exhaust outlet.
Preferably, described device water inlet oil content≤50mg/L, SS content≤300mg/L are discharged oil content≤5mg/L,
SS content is in≤20mg/L.
Preferably, the oil removing separator for removing dirt is equipped with pipe-line mixer, and the pipe-line mixer is set on water inlet pipe, described
Pipe-line mixer is set as several, is respectively arranged on water inlet manifold and several water inlet pipes, set pipe on the water inlet manifold
Road mixer is equipped with PAC dosing mouth, and set pipe-line mixer is equipped with PAM dosing mouth on several water inlet pipes, it is described into
Water branch pipe is connect with water inlet manifold.
Compared with prior art, the beneficial effects of the utility model are as follows:
1. the utility model sets sunk type flocculation reaction room, not only increase the volume of reaction chamber, and it is more to increase top
The volume of hole Ball-type packing improves the flocculating setting effect of equipment.
2. the utility model increases slag gathering hopper in the second flocculation reaction room lower part, due to containing in steel industry turbid circulating water
A large amount of iron scales, and partial oxidation iron sheet volume is larger, and bulky grain iron scale carries out sedimentation separation herein first, periodically
Discharge, alleviates the load of filtering layer.
3. the utility model the second flocculation reaction room top apopore close to sludge hopper, the purpose of this equipment be in order to
Water inlet can flow back with partial sludge, and suspended particulate in water is made to form bigger particle in conjunction with mud granule, be conducive to sludge
The sedimentation of particle.
4. the utility model uses porous spherical filler, type of feed uses natural packing, and it is heavy that this design not only increases
Drop area, and porous spherical filler will not because of sludge quantity increase and cause to deform, improve equipment operation safety.
5. the utility model designs symmetrical sludge hopper design, bucket cone-plate and horizontal sextant angle are 45 degree, and sludge area is without dead
Angle, spoil disposal are more thorough.
6. " ridge " structure that angle is 90 degree is formed between two pieces of bucket cone-plates of the utility model symmetrical expression sludge hopper,
Top is equipped with backwash discharge outlet, this designs the discharge for being very beneficial to filtering layer backwash water.
7. the utility model water distributing trough is equipped with 6 sparge pipes, and is equipped with inlet damper in water distribution tube end, make water distribution more
Uniformly.
Detailed description of the invention
Fig. 1 is the schematic view of the front view of the utility model integrated deoiling separator for removing dirt；
Fig. 2 is the side structure schematic view of the utility model integrated deoiling separator for removing dirt；
Fig. 3 is the arrangement installation diagram of the utility model pipe-line mixer.
In figure: 1, device noumenon；2, settling section；3, the area Ni Jiang；4, porous spherical filler；5, symmetrical sludge hopper；6, in
Heart pipe；7, flocculation reaction room；8, water inlet pipe；9, catch basin；10, water distributing trough；11, sparge pipe；12, the first flocculation reaction room；13,
Second flocculation reaction room；14, slag gathering hopper；15, apopore；16, bucket cone-plate；17, backwash discharge outlet；18, sludge pipe；19, mistake
Filtering layer；20, water outlet；21, pipe-line mixer；22, water inlet manifold；23, water inlet pipe；24, scum pipe；25, anthracite coal measure；
26, quartz sand layer；27, boulder bed；28, porous filter plate；29, compressed air inlet；30, gas distribution pipe；31, upper exhaust outlet.
Specific embodiment
It is illustrated below in conjunction with preferred embodiment of the attached drawing to the utility model, it should be understood that described herein excellent
It selects embodiment to be only used for describing and explaining the present invention, is not used to limit the utility model.
As depicted in figs. 1 and 2, integrated deoiling separator for removing dirt, including device noumenon 1,1 top of described device ontology are clear
Clear area 2, lower part are the area Ni Jiang 3, and 2 lower part of settling section is equipped with porous spherical filler 4, is equipped with below the area Ni Jiang 3 symmetrical
Formula sludge hopper 5,1 center of described device ontology are equipped with central tube 6 and flocculation reaction room 7, the connection of flocculation reaction room 7 water inlet
Pipe 8, the upper end of the central tube 6 are catch basin 9, and lower end is water distributing trough 10, and 10 side of water distributing trough is equipped with sparge pipe 11, institute
Stating flocculation reaction room 7 is sunk type flocculation reaction room, and sunk type flocculation reaction room passes through the symmetrical sludge hopper 5 and stretches
Entering the lower part of described device ontology 1, the flocculation reaction room 7 is divided for the first flocculation reaction room 12 and the second flocculation reaction room 13,
First flocculation reaction room 12 is nested in the second flocculation reaction room 13, and first flocculation reaction room, 12 lower end is open, institute
It states the first flocculation reaction room 12 and is connected to the second flocculation reaction room 13 by the open lower end in the first flocculation reaction room 12, it is described
Connect slag gathering hopper 14 below second flocculation reaction room 13, be equipped with apopore 15 above second flocculation reaction room 13, it is described go out
Close to the symmetrical sludge hopper 5, the symmetrical expression sludge hopper 5 includes two pieces of symmetrical bucket cone-plates 16, the mud in water hole 15
The angle of bucket cone-plate 16 and horizontal plane is 45 degree, and " ridge " knot that angle is 90 degree is formed between two pieces of bucket cone-plates 16
Structure, the top of the symmetrical expression sludge hopper 5 are equipped with backwash discharge outlet 17, and the bottom of the symmetrical expression sludge hopper 5 passes through sludge pipe
18 are connected to the mud discharging mouth of 1 side of device noumenon, and filter layer 19, described device ontology 1 is arranged below the symmetrical expression sludge hopper 5
Bottom is provided with water outlet 20.
As shown in figure 3, the oil removing separator for removing dirt is equipped with pipe-line mixer 21, the pipe-line mixer 21 is set to water inlet
On pipe 8, the pipe-line mixer 21 is set as several, is respectively arranged on water inlet manifold 22 and several water inlet pipes 23, it is described into
Set pipe-line mixer 21 is equipped with PAC dosing mouth on supply mains 22, set pipeline mixing on several water inlet pipes 23
Device 21 is equipped with PAM dosing mouth, and the water inlet pipe 23 is connect with water inlet manifold 22.
The working principle of the utility model is as follows: iron and steel enterprise's continuous casting or the oil-containing of hot rolling workshop are containing SS content in turbid wastewater
≤ 300mg/L, water inlet oil content≤50mg/L, waste water are pumped into pipe-line mixer 21 by pump first after whirling well, mixed in pipeline
21 dosing mouth of clutch adds medicament, totally two kinds of the medicament added, separately adds, the first kind coagulant, puts into water inlet manifold 22
On pipe-line mixer 21；Second is flocculant, puts into the pipe-line mixer 21 on several water inlet pipes 23, first throws the first
Medicament throws second of medicament afterwards, and adds order and cannot overturn, and is then promoted to the oil-containing after dosing containing turbid wastewater practical
Novel all-in-one oil removing separator for removing dirt.
Waste water enters flocculation reaction room 7 through 1 middle part water inlet pipe 8 of device noumenon, and the utility model selects sunk type flocculation anti-
Room is answered, the volume of reaction chamber is not only increased, and increases the volume of upper porous Ball-type packing 4, improves the flocculation of equipment
Effect of settling, oil-containing is condensed in the first flocculation reaction room 12 first containing turbid wastewater, flocculation, since steel industry is turbid
Contain a large amount of iron scales in ring water, and partial oxidation iron sheet volume is larger, bulky grain iron scale is sunk herein first
Drop separation, bulky grain iron scale are deposited in 13 lower part of the second flocculation reaction room, and then the slag gathering hopper 14 through lower part is collected and led to
It crosses scum pipe 24 to be periodically discharged, alleviates the load of filtering layer, in order to make iron scale that noresidue, second flocculation be smoothly discharged
Reaction chamber 13 and the slag gathering hopper 14 of lower end are integrated, and the slag gathering hopper 14 is pyramidal structure, 14 lower end of slag gathering hopper
Equipped with scum pipe 24；Lightweight oils and suspended matter are solidifying into 13 top further occurrence of the second flocculation reaction room through medicament in water
Gather, flocculation, lightweight floc sedimentation, sludge and the top clear water that oils and suspended matter are formed in water are through on the second flocculation reaction room 13
The apopore 15 in portion is discharged, and the apopore 15 on 13 top of the second flocculation reaction room is close to symmetrical sludge hopper 5, the purpose of this equipment
It is so that suspended particulate in water is formed bigger particle in conjunction with mud granule in order to intake and can flow back with partial sludge, benefit
In the sedimentation of mud granule.
Clear water, lightweight floc sedimentation, the sludge being discharged through apopore 15 rise at porous spherical filler 4, make floc sedimentation, sludge
Its surface of product, free skating drops down onto symmetrical sludge hopper 5 after sludge is accumulated to certain thickness, and sludge is discharged by sludge pipe, adopts
With porous spherical filler 4, type of feed uses natural packing, this design not only increases settling area, and porous spherical is filled out
Material 4 will not because of sludge quantity increase and cause to deform, improve equipment operation safety, using symmetrical sludge hopper design
5, bucket cone-plate 16 and horizontal sextant angle are 45 degree, and without dead angle, spoil disposal is more thorough in sludge area, shape between two pieces of bucket cone-plates 16
" ridge " structure for being 90 degree at angle is equipped with backwash discharge outlet 17 at top, this design is very beneficial to 19 backwash water of filter layer
Discharge.
A large amount of suspended matter and wadding body in water inlet can be removed by porous spherical filler 4, into settling section, clean is clear
Water converges to the catch basin 10 of central tube upper end, and the water distributing trough 10 of lower end is flow to by central tube, and 10 side of water distributing trough is set
There is sparge pipe 11.10 side of water distributing trough is symmetrically arranged with 6 sparge pipes 11, and the every sparge pipe 11 is by transverse pipe and indulges
To Guan Zucheng, the transverse pipe is connected with longitudinal pipe by connector, and 11 transverse pipe of sparge pipe is by equidistantly distributing in matching
The side of sink 10, the longitudinal pipe pass through symmetrical sludge hopper 5, and 11 end of sparge pipe is equipped with inlet damper, makes water distribution
More evenly.
Water flows through sparge pipe 11 and is evenly distributed on filter layer 19, and the filter layer 19 includes anthracite coal measure 25, quartz sand
Layer 26 and boulder bed 27, anthracite coal measure 25, quartz sand layer 26 and boulder bed 27 are sequentially arranged composition filter layer 19, water from top to bottom
From top to bottom respectively slowly by anthracite coal measure 25, quartz sand layer 26 and boulder bed 27, each filtering layer plays absorption oil content and cuts stream
Filtering is realized in dirt effect, and 25 thickness of anthracite coal measure is 350mm, uses partial size for the anthracite of 2~4mm, walnut shell or haydite,
To remain oil content in Adsorption water；26 thickness of quartz sand layer is 350mm, uses partial size for the quartz sand of 1~2mm, with retention
Cross the impurity such as suspended matter in drainage；27 thickness of boulder bed is 250mm, uses partial size for the cobble of 2~8mm.
Anthracite coal measure 25 plays main filtering section dirt in the utility model, and quartz sand layer 26 only has surface layer and participated in
Filter, water outlet are discharged by water outlet 20, suspension content≤20mg/L, oil content≤5mg/L in final outflow water.
The filter layer 19 is stacked on porous filter plate 28, is disposed with several water caps in porous 28 plate face of filter plate, porous
28 arranged beneath of filter plate has the gas distribution pipe 30 being connected to compressed air inlet 29, and described device ontology 1 is equipped with upper exhaust outlet 31.
The oil removing separator for removing dirt is equipped with pipe-line mixer 21, and the pipe-line mixer 21 is set on water inlet pipe 8, described
Pipe-line mixer 21 is set as several, is respectively arranged on water inlet manifold 22 and several water inlet pipes 23, on the water inlet manifold 22
Set pipe-line mixer 21 is equipped with PAC dosing mouth, and set pipe-line mixer 21 is equipped with PAM on several water inlet pipes 23
Dosing mouth, the water inlet pipe 23 are connect with water inlet manifold 22.
For the utility model after long-term work, filter layer 19 will receive pollution, need to periodically carry out backwash.When carrying out backwash,
8 external valve of water inlet pipe close, 17 external valve of backwash discharge outlet open, 29 external valve of compressed air inlet open, with go out
Water (having pressure) enters inside device through water outlet 20 in the external outfall sewer that the mouth of a river 20 is connected to, and water flow passes through more from bottom to top
Hole filter plate 28 carries out backwash to filtering layer 19 after water cap uniform water distribution, and water flow loosens each filtering layer when backwash, is in filtering material particle
Suspended state simultaneously mutually collides, and the effect of compressed air is passed through by gas distribution pipe 30, forms the process of scouring.Since each layer is filtered
The sinking speed of material in water is different, and after backwash, each layer filtrate natural subsidence layering restores to former filtration condition
Again it puts into operation.
The utility model one takes up little area: equipment combines chemical oil remover and the institute of high rate filter is functional, reduces
Occupied area；Two is with low investment: system eliminates hot-tub, elevator pump, filter backwash water pump etc., saves system investments；Three
Energy consumption is small: system eliminates elevator pump, filter backwash water pump, saves electric energy；Four water consumption are small: higher speed filter, greatly
Reduce backwash water consumption greatly；Five equipment are Automatic Control, have prevented due to artificial carelessness and caused the failure of equipment, and are subtracted
The workload of light personnel.
Finally, it should be noted that being not limited to this reality the foregoing is merely the preferred embodiment of the utility model
With novel, although the utility model is described in detail with reference to the foregoing embodiments, come for those skilled in the art
Say, it is still possible to modify the technical solutions described in the foregoing embodiments, or to part of technical characteristic into
Row equivalent replacement.Within the spirit and principle of the utility model, any modification, equivalent replacement, improvement and so on, should all
It is included within the scope of protection of this utility model.
Claims (8)
1. integrated deoiling separator for removing dirt, including device noumenon (1), which is characterized in that described device ontology (1) top is clarification
Area (2), lower part are the area Ni Jiang (3), and settling section (2) lower part is equipped with porous spherical filler (4), below the area Ni Jiang (3)
Equipped with symmetrical sludge hopper (5), described device ontology (1) center is equipped with central tube (6) and flocculation reaction room (7), the flocculation
Reaction chamber (7) connects water inlet pipe (8), and the upper end of the central tube (6) is catch basin (9), and lower end is water distributing trough (10), described to match
Sink (10) side is equipped with sparge pipe (11), and the flocculation reaction room (7) is sunk type flocculation reaction room, the sunk type flocculation
Reaction chamber passes through the lower part that the symmetrical sludge hopper (5) protrudes into described device ontology (1), and the flocculation reaction room (7) is divided into
First flocculation reaction room (12) and the second flocculation reaction room (13), it is anti-that first flocculation reaction room (12) is nested in the second flocculation
It answers in room (13), first flocculation reaction room (12) lower end is open, and first flocculation reaction room (12) and the second flocculation are anti-
Answer the lower end connection that room (13) are open by the first flocculation reaction room (12), connection collection below second flocculation reaction room (13)
Slag bucket (14), second flocculation reaction room (13) top are equipped with apopore (15), and the apopore (15) is close to described symmetrical
Formula sludge hopper (5), it is described symmetrical expression sludge hopper (5) include two pieces of symmetrical bucket cone-plates (16), the bucket cone-plate (16) and
The angle of horizontal plane is (45) degree, and " ridge " structure that angle is 90 degree is formed between two pieces of bucket cone-plates (16), described
The top of symmetrical sludge hopper (5) is equipped with backwash discharge outlet (17), and the bottom of the symmetrical expression sludge hopper (5) passes through sludge pipe
(18) it is connected to the mud discharging mouth of device noumenon (1) side, filter layer (19) are set below the symmetrical expression sludge hopper (5), it is described
Device noumenon (1) bottom is provided with water outlet (20).
2. integrated deoiling separator for removing dirt according to claim 1, which is characterized in that second flocculation reaction room (13)
It is integrated with the slag gathering hopper (14) of lower end, the slag gathering hopper (14) is pyramidal structure, and slag gathering hopper (14) lower end is set
There are scum pipe (24).
3. integrated deoiling separator for removing dirt according to claim 1, which is characterized in that water distributing trough (10) side is symmetrical
Equipped with 6 sparge pipes (11), the every sparge pipe (11) is made of transverse pipe and longitudinal pipe, and the transverse pipe and longitudinal pipe are logical
Connector connection is crossed, sparge pipe (11) transverse pipe by equidistantly distributing in the side of water distributing trough (10), wear by the longitudinal pipe
Symmetrical sludge hopper (5) is crossed, sparge pipe (11) end is equipped with inlet damper.
4. integrated deoiling separator for removing dirt according to claim 1, which is characterized in that the filter layer (19) includes smokeless
Coal seam (25), quartz sand layer (26) and boulder bed (27), anthracite coal measure (25), quartz sand layer (26) and boulder bed (27) from upper and
Under be sequentially arranged composition filter layer (19).
5. integrated deoiling separator for removing dirt according to claim 4, which is characterized in that anthracite coal measure (25) thickness is
350mm uses partial size for the anthracite of 2~4mm, walnut shell or haydite, to remain oil content in Adsorption water；Quartz sand layer
(26) thickness is 350mm, uses partial size for the quartz sand of 1~2mm, to retain the impurity such as suspended matter in drainage；Boulder bed
(27) thickness is 250mm, uses partial size for the cobble of 2~8mm.
6. integrated deoiling separator for removing dirt according to claim 1, which is characterized in that the filter layer (19) is stacked on more
On hole filter plate (28), several water caps are disposed in porous filter plate (28) plate face, porous filter plate (28) arranged beneath has and compresses
The gas distribution pipe (30) of air intlet (29) connection, described device ontology (1) are equipped with upper exhaust outlet (31).
7. integrated deoiling separator for removing dirt according to claim 1, which is characterized in that described device water inlet oil content≤
50mg/L, SS content≤300mg/L are discharged oil content≤5mg/L, and SS content is in≤20mg/L.
8. integrated deoiling separator for removing dirt according to claim 1, which is characterized in that the oil removing separator for removing dirt is equipped with pipe
Road mixer (21), the pipe-line mixer (21) are set on water inlet pipe (8), and the pipe-line mixer (21) is set as several,
It is respectively arranged on water inlet manifold (22) and several water inlet pipes (23), set pipe-line mixer on the water inlet manifold (22)
(21) it is equipped with PAC dosing mouth, set pipe-line mixer (21) is equipped with PAM dosing mouth, institute on several water inlet pipes (23)
Water inlet pipe (23) is stated to connect with water inlet manifold (22).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820928168.2U CN208747798U (en) | 2018-06-15 | 2018-06-15 | Integrated deoiling separator for removing dirt |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820928168.2U CN208747798U (en) | 2018-06-15 | 2018-06-15 | Integrated deoiling separator for removing dirt |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208747798U true CN208747798U (en) | 2019-04-16 |
Family
ID=66053979
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
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| CN201820928168.2U Active CN208747798U (en) | 2018-06-15 | 2018-06-15 | Integrated deoiling separator for removing dirt |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN108483751A (en) * | 2018-06-15 | 2018-09-04 | 江苏德科环境科技有限公司 | Integrated deoiling separator for removing dirt |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN108483751A (en) * | 2018-06-15 | 2018-09-04 | 江苏德科环境科技有限公司 | Integrated deoiling separator for removing dirt |
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Effective date of registration: 20240827 Address after: No. 35, Jiaxiang, Gaoyao Village, Gaocheng Town, Yixing City, Jiangsu Province, China 214200 Patentee after: Shen Jun Country or region after: China Patentee after: Yu Aiqin Address before: 214200 Gaoyong Village, Gaoyong Town, Yixing City, Wuxi City, Jiangsu Province Patentee before: JIANGSU DECO ENVIRONMENTAL TECHNOLOGY Co.,Ltd. Country or region before: China |