CN109665588A - Integrated crude oil wastewater efficient fine processing device - Google Patents
Integrated crude oil wastewater efficient fine processing device Download PDFInfo
- Publication number
- CN109665588A CN109665588A CN201910131669.7A CN201910131669A CN109665588A CN 109665588 A CN109665588 A CN 109665588A CN 201910131669 A CN201910131669 A CN 201910131669A CN 109665588 A CN109665588 A CN 109665588A
- Authority
- CN
- China
- Prior art keywords
- water
- pipeline
- backwash
- valve
- tank
- 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.)
- Pending
Links
- 239000002351 wastewater Substances 0.000 title claims abstract description 34
- 238000012545 processing Methods 0.000 title claims abstract description 26
- 239000010779 crude oil Substances 0.000 title claims abstract description 24
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 438
- 238000001914 filtration Methods 0.000 claims abstract description 159
- 230000007246 mechanism Effects 0.000 claims abstract description 68
- 238000010926 purge Methods 0.000 claims abstract description 50
- 239000010865 sewage Substances 0.000 claims abstract description 44
- 238000011001 backwashing Methods 0.000 claims abstract description 28
- 230000007704 transition Effects 0.000 claims description 82
- 238000009826 distribution Methods 0.000 claims description 63
- 239000000706 filtrate Substances 0.000 claims description 47
- 239000003921 oil Substances 0.000 claims description 45
- 239000000463 material Substances 0.000 claims description 24
- 239000007788 liquid Substances 0.000 claims description 18
- 239000003814 drug Substances 0.000 claims description 17
- 230000010354 integration Effects 0.000 claims description 10
- 238000009434 installation Methods 0.000 claims description 9
- NJPPVKZQTLUDBO-UHFFFAOYSA-N novaluron Chemical compound C1=C(Cl)C(OC(F)(F)C(OC(F)(F)F)F)=CC=C1NC(=O)NC(=O)C1=C(F)C=CC=C1F NJPPVKZQTLUDBO-UHFFFAOYSA-N 0.000 claims description 8
- 229910001220 stainless steel Inorganic materials 0.000 claims description 6
- 239000010935 stainless steel Substances 0.000 claims description 6
- 230000013011 mating Effects 0.000 claims description 5
- 238000000034 method Methods 0.000 abstract description 16
- 230000008569 process Effects 0.000 abstract description 11
- 238000004519 manufacturing process Methods 0.000 abstract description 10
- 230000008901 benefit Effects 0.000 abstract description 5
- 238000002156 mixing Methods 0.000 abstract description 5
- 239000002184 metal Substances 0.000 abstract description 4
- 229910052751 metal Inorganic materials 0.000 abstract description 4
- 238000005374 membrane filtration Methods 0.000 abstract description 2
- 239000000178 monomer Substances 0.000 abstract description 2
- 239000002245 particle Substances 0.000 description 15
- 230000000694 effects Effects 0.000 description 9
- 239000007787 solid Substances 0.000 description 9
- 239000010408 film Substances 0.000 description 7
- 238000011010 flushing procedure Methods 0.000 description 6
- 238000010521 absorption reaction Methods 0.000 description 4
- 239000012535 impurity Substances 0.000 description 4
- 241000894006 Bacteria Species 0.000 description 3
- 230000002776 aggregation Effects 0.000 description 3
- 238000004220 aggregation Methods 0.000 description 3
- 238000005265 energy consumption Methods 0.000 description 3
- 238000007667 floating Methods 0.000 description 3
- 238000011084 recovery Methods 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- 238000001179 sorption measurement Methods 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 241000758789 Juglans Species 0.000 description 2
- 235000009496 Juglans regia Nutrition 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 238000007630 basic procedure Methods 0.000 description 2
- 239000000084 colloidal system Substances 0.000 description 2
- 239000013039 cover film Substances 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 2
- 238000011049 filling Methods 0.000 description 2
- 239000004519 grease Substances 0.000 description 2
- 230000014759 maintenance of location Effects 0.000 description 2
- 239000012528 membrane Substances 0.000 description 2
- 235000020234 walnut Nutrition 0.000 description 2
- 239000006004 Quartz sand Substances 0.000 description 1
- 230000005856 abnormality Effects 0.000 description 1
- 230000004913 activation Effects 0.000 description 1
- 239000011149 active material Substances 0.000 description 1
- 229910000323 aluminium silicate Inorganic materials 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
- 230000000903 blocking effect Effects 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000012459 cleaning agent Substances 0.000 description 1
- 238000005354 coacervation Methods 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 239000010432 diamond Substances 0.000 description 1
- 229910003460 diamond Inorganic materials 0.000 description 1
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 1
- 238000011065 in-situ storage Methods 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 238000009533 lab test Methods 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000011159 matrix material Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 239000003027 oil sand Substances 0.000 description 1
- 239000003129 oil well Substances 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 230000002085 persistent effect Effects 0.000 description 1
- 238000005554 pickling Methods 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 230000002441 reversible effect Effects 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 238000010008 shearing Methods 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 230000001502 supplementing effect Effects 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 238000010998 test method Methods 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/281—Treatment of water, waste water, or sewage by sorption using inorganic sorbents
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/40—Devices for separating or removing fatty or oily substances or similar floating material
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/16—Regeneration of sorbents, filters
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Analytical Chemistry (AREA)
- Filtration Of Liquid (AREA)
Abstract
The invention discloses a kind of integrated crude oil wastewater efficient fine processing devices, including filtering tank, elevator pump, backwashing pump, air compressor machine, air accumulator, gas source distributor box, PLC control cabinet, water pipeline, air purge pipeline, electric wire, signal wire, Pneumatic butterfly valve, air purge valve and threeway；The top of the filtering tank inner cavity is equipped with water distributing mechanism, middle part is equipped with AFM active filter mechanism, lower part is equipped with water collection agencies；The Pneumatic butterfly valve includes filtered water inlet valve, filtering outlet valve, backwash inlet valve and backwash outlet valve.The present invention can stably reach fine filtering level-one water standard for the sewage of different quality；Using new A FM active filter, Yi Chongxi, non-scaling, long service life；The backwash mode washed by rubbing with the hands using mixing wastewater with air is saved water and energy significant；Overall skid-mounted is suitble to monomer production；Automatic control level is high；Peculiar advantage with " short route "；Thorough substituted metal membrane filtration process equipment simultaneously realizes surmounting comprehensively for performance.
Description
Technical field
The present invention relates to sewage treatment fields, and in particular to a kind of integration crude oil wastewater efficient fine processing device is fitted
Close oil field extracted water in-situ processing and fine sewage treatment.
Background technique
Currently, onshore oil field mostly enters the exploitation later period, the moisture content of produced liquid in oil well is higher and higher, will be in production fluid
Reinjection into reservoir is the important measures of oil field Persisting exploitation after the sewage treatment isolated is qualified, and the water quality of return water is oily to improving
The ultimate recovery tool in field is marginal.In order to guarantee that injection water quality is up to standard steadily in the long term, oil field is to recycled produced water treatment work
The transformation dynamics of skill gradually increases, and high pressure low permeability block exploitation water filling in oil field needs level-one water quality, and (oil content of wastewater≤5 ㎎/L hangs
Floating solid content≤1.0 ㎎/L, suspended particle median diameter≤1.0 μm) it can be only achieved water filling demand, edge small complex fault block
Small scale is filled the water, water quality requirement is high, it is also desirable to level-one water quality sewage.
It is well known that oil field extracted water water quality is complicated, sewage quality characteristic is changeable, pollution and corrosivity are strong, this to work as
Preceding oil field produced water process reaches level-one water standard, and metal membrane separation process technology, metal membrane separation process skill is widely used
Art has the function of separation, concentration and purifying, removes the suspended solid and oil droplet in recovered water.But it is required that water inlet pretreatment reaches
To B1 grade standard (oil content of wastewater≤8 ㎎/L, suspended solids content≤3.0 ㎎/L, suspended particle median diameter≤2.0 μ
M), water outlet just reaches primary standard.All it is very accurate from structure and material, but can only is in preferable situation of intaking
Under, as the functional device for intercepting a small amount of partial size exceeded suspended solid and a small amount of oil droplet, if water inlet pretreatment index fluctuation
Unstable exceeded, effluent index fluctuates exceeded therewith.The easy fouling of film causes treating capacity to decline, and pickling is wanted in application for a long time；Once dirty
Dye blocking, is difficult to restore filter capability completely；And filter core is replaced, cost then can be very high.
Summary of the invention
To overcome the shortcomings of existing technologies, the present invention provides a kind of integrated crude oil wastewater efficient fine processing device,
It can adapt to water quality sewage source complicated and changeable, filtrate non-scaling, Yi Chongxi and long service life, use cost are low.
Its technical solution is: including filtering tank, elevator pump, backwashing pump, air compressor machine, air accumulator, gas source distributor box, PLC control
Cabinet, water pipeline, air purge pipeline, electric wire, signal wire, Pneumatic butterfly valve, air purge valve and threeway processed；The top of the filtering tank is equipped with
Exhaust pipe and oil exit pipe inside and outside tank skin, exhaust pipe are externally provided with exhaust valve in tank, and oil exit pipe is externally provided with draining valve, mistake in tank
The top of filter tank inner cavity is equipped with water distributing mechanism, middle part is equipped with AFM active filter mechanism, lower part is equipped with water collection agencies；It is described pneumatic
Butterfly valve includes filtered water inlet valve, filtering outlet valve, backwash inlet valve and backwash outlet valve；The threeway include upper threeway and under
Position threeway；The water pipeline includes filtering water pipeline, backwash water pipeline and transition water pipeline, and filtering water pipeline includes filtered water inlet
Pipeline and water pipeline is filtered out, backwash water pipeline includes backwash back with water inlet line and backwash water outlet pipeline, and transition water pipeline includes tank
Push up transition water pipeline and tank bottom transition water pipeline；The filtered water inlet pipeline is equipped with branch, top with lower section above it respectively
Branch connects upper threeway and installs filtered water inlet valve on branch line, and lower section branch connects elevator pump water outlet；The mistake
It filters out water pipeline and is equipped with branch thereunder, lower section branch connects the next threeway and the installation filtering outlet valve on branch line；
The backwash back with water inlet line is equipped with branch above it, top branch connect the next threeway and installed on branch line backwash into
Water valve；The backwash water outlet pipeline is equipped with branch thereunder, and lower section branch connects upper threeway and installs on branch line
Backwash outlet valve；The lower end of the tank deck transition water pipeline connects upper threeway, and upper end enters in filtering tank at the top of filtering tank
Chamber is simultaneously connect with water distributing mechanism；The upper end of the tank bottom transition water pipeline connects the next threeway, and lower end enters from filtering pot bottom
Filtering tank inner cavity is simultaneously connect with water collection agencies；One end of the air purge pipeline connects air compressor machine gas outlet, and the other end connects tank bottom
Transition water pipeline is sequentially connected in series air accumulator, gas source distributor box and air purge valve on pipeline；The PLC control cabinet by electric wire with
Power supply connection, connect with elevator pump, backwashing pump, operated pneumatic valve and air purge valve respectively simultaneously also by signal wire.
Above-mentioned technical proposal can advanced optimize are as follows:
It further include medicating mechanism；The medicating mechanism includes dosing tank, dosing pump and liquid medicine feed-line, liquid medicine feed-line
Beginning connects dosing tank, tail end connects filtered water inlet pipeline, installs dosing pump on pipeline.
It further include sewage pipe；One end of the sewage pipe connects tank bottom transition water pipeline, and the pipeline of sewage pipe is equipped with hand
Dynamic blowdown valve.
The water distributing mechanism includes water distribution supervisor and its 6 water distribution branch pipes, and water distribution supervisor erects setting and the upper end and tank
Push up transition water pipeline connection, water distribution branch pipe it is laterally uniform water distribution supervisor around and tilt down.
Catchment supervisor and its collection branch pipe that the water collection agencies are made of the vertical tube that catchments with the transverse tube that catchments, catchment vertical tube
Lower end is connect with tank bottom transition water pipeline, the lateral symmetry two sides for being distributed in the transverse tube that catchments of collection branch pipe；It catchments every side
Branch pipe is 5, the collection branch pipe length longest positioned at middle part, and the collection branch pipe length successively arranged to both ends is gradually short.
The water distribution branch pipe and collection branch pipe are all made of the wire-wrapped screen of 316 type stainless steel materials.
The filtering tank is set as 2, mating common filtering water pipeline and backwash water pipeline；The elevator pump is set as 2,
1 is standby with 1.
Skid pedestal is laid, each component part of the device is both secured on skid pedestal.
AFM active filter mechanism include 4 layers, be from top to bottom followed successively by 0 grade of active filter layer, 1 grade of active filter layer,
2 grades of active filter layers and 3 grades of active filter layers.
Volume ratio shared by each active filter layer is respectively as follows: 0 grade of active filter layer and accounts for 20%, and 1 grade of active filter layer accounts for
50%, 2 grades of active filter layers account for 15%, and 3 grades of active filter layers account for 15%.
Compared with prior art, the present invention has following advantageous effects:
1. suitable oil field production is practical, fine filtering level-one water standard can be stably reached for the sewage of different quality, really
Oil-field flooding quality, injecting good water, injecting enough water are protected, and realizes making full use of for sewage resource.
2. using new A FM active filter, the moisture film of one layer of hydrophilic and oleophobic type can be generated after the chance water of surface, in operation process
Middle greasy dirt and suspended particulates are attached to water film surface, easily rinse very much, more non flouling behaviour, and service life was saved up to 15 years as long as
Sewage treatment expense, is conducive to environmental protection.
3. the backwash mode washed by rubbing with the hands using mixing wastewater with air, than backwash water consume, the section that conventional backwash saves 50% or more
About 50% or more backwash energy consumption, performance is restored completely after filtrate backwash.
4. using the mentality of designing of modularization, miniaturization, lightness, the amount of progress is required according to water index and effluent index
Body custom design, is optimal outlet effect, meets the requirement of oilfield sewage fine processing.
5. overall skid-mounted is suitble to monomer production, integrated, convenient transportation, the advantage for saving land occupation with production scene assembling.
6. using advanced PLC control system and software programming, realize that the high level of operational process automatically controls, and have
There is transporting function, creation data uploads to production command centre, can match with Oilfield Information system.
7. the peculiar advantage with " short route ", contact is few, and level is few, and equipment is few, and influence factor is few, and overall efficiency is high,
Filtering velocity is high, and the pressure loss is small.
8. investment is quick, the benefit phase is long, and management cost is low, and operating cost saves, and maintenance cost is small.
9. thorough substituted metal membrane filtration process equipment, and realize surmounting comprehensively for performance, there is good promotion prospect.
Detailed description of the invention
Fig. 1 is that structure of the invention is laid out top view；
Fig. 2 is that structure of the invention is laid out main view；
Fig. 3 is that structure of the invention is laid out left view one；
Fig. 4 is that structure of the invention is laid out left view two；
Fig. 5 is water distributing mechanism top view of the present invention；
Fig. 6 is water distributing mechanism main view of the present invention；
Fig. 7 is water collection agencies top view of the present invention；
Fig. 8 is active filter of the present invention layering setting schematic diagram；
Fig. 9 is ordinary filter and active filter rear state vs' schematic diagram before filtration；
Figure 10 is 1# filter tank control flow chart；
Figure 11 is 2# filter tank control flow chart；
Figure 12 is to promote pump startup control flow chart；
Figure 13 is that elevator pump stops control flow chart；
Figure 14 is backwash pump startup control flow chart；
Figure 15 is that backwashing pump stops control flow chart；
Figure 16 is dosing pump startup control flow chart；
Figure 17 is that dosing pump stops control flow chart；
In figure: 1- elevator pump, 2- filtered water inlet pipeline, 3- backwashing pump, 4- liquid medicine feed-line, 5- dosing pump, 6- backwash water inlet
Pipeline, 7- air purge valve, 8- tank deck transition water pipeline, 9- filtering tank, 10- exhaust pipe, 11- oil exit pipe, 12- skid pedestal, 13-
Gas source distributor box, 14- air accumulator, 15- air purge pipeline, 16- air compressor machine, 17- dosing tank, 18- backwash inlet valve, 19- tank bottom mistake
Cross water pipeline, 20- filters outlet valve, 21- sewage pipe, the threeway of the bottom 22-, the upper threeway of 23-, 24- filtered water inlet valve, and 25- is anti-
Water valve is washed out, 26- backwash is discharged pipeline, and 27- filters out water pipeline, 28- water distribution supervisor, 29- water distribution branch pipe, and 30- catchments vertical tube,
31- catchments transverse tube, 32- collection branch pipe, 33-0 grades of active filter layers, 34-1 grades of active filter layers, 35-2 grades of active filter layers,
36-3 grades of active filter layers.
Specific embodiment
Below with reference to embodiment, principle and attached drawing, the present invention is described in detail.
Embodiment 1
Referring to Fig. 1, Fig. 2, Fig. 3, Fig. 4, Fig. 5, Fig. 6, Fig. 7 and Fig. 8.Integrated crude oil wastewater efficient fine processing device, including
Filtering tank 9, elevator pump 1, backwashing pump 3, air compressor machine 16, air accumulator 14, gas source distributor box 13, PLC control cabinet, water pipeline, air purge
Pipeline 15, electric wire, signal wire, Pneumatic butterfly valve, air purge valve 7 and threeway.The top of filtering tank 9 is equipped with the row inside and outside tank skin
Tracheae 10 and oil exit pipe 11, exhaust pipe 10 are externally provided with exhaust valve in tank, and oil exit pipe is externally provided with draining valve, 9 inner cavity of filtering tank in tank
Top be equipped with water distributing mechanism, middle part be equipped with AFM active filter mechanism, lower part be equipped with water collection agencies.Water distributing mechanism includes water distribution
28 and its 6 water distribution branch pipes 29 are responsible for, water distribution supervisor 28 erects setting and the upper end is connect with tank deck transition water pipeline 8, water distribution
Branch pipe 29 is laterally uniform to be responsible for around 28 and tilts down in water distribution.AFM active filter mechanism include 4 layers, by up to
Under be followed successively by 33,1 grades of 0 grade of active filter layer, 34,2 grades of active filter layer active filter layer 35 and 3 grades of active filter layers 36.It catchments
Catchment supervisor and its collection branch pipe 32 that mechanism is made of the vertical tube 30 that catchments with the transverse tube 31 that catchments, the lower end for the vertical tube 30 that catchments and tank
Bottom transition water pipeline 19 connects, the lateral symmetry two sides for being distributed in the transverse tube 31 that catchments of collection branch pipe 32；The collection branch pipe 32 of every side
It is 5, the 32 length longest of collection branch pipe positioned at middle part is successively gradually short to 32 length of collection branch pipe of both ends arrangement.Pneumatically
Butterfly valve includes filtered water inlet valve 24, filtering outlet valve 20, backwash inlet valve 18 and backwash outlet valve 25.Threeway includes upper threeway
23 and the next threeway 22.Water pipeline includes filtering water pipeline, backwash water pipeline and transition water pipeline, and filtering water pipeline includes filtering
Back with water inlet line 2 and water pipeline 27 is filtered out, backwash water pipeline includes backwash back with water inlet line 6 and backwash water outlet pipeline 26, transitional water
Pipeline includes tank deck transition water pipeline 8 and tank bottom transition water pipeline 19.Filtered water inlet pipeline 2 is equipped with lower section above it respectively
Branch, top branch connect upper threeway 23 and install filtered water inlet valve 24 on branch line, and lower section branch connects elevator pump 1
Water outlet.It filters out water pipeline 27 and is equipped with branch thereunder, lower section branch connects the next threeway 22 and pacifies on branch line
Dress filtering outlet valve 20.Backwash back with water inlet line 6 is equipped with branch above it, and top branch connects the next threeway 22 and in branched pipe
Road installation backwash inlet valve 18.Backwash is discharged pipeline 26 and is equipped with branch thereunder, and lower section branch connects upper threeway 23 simultaneously
Backwash outlet valve 25 is installed on branch line.The lower end of tank deck transition water pipeline 8 connects upper threeway 23, and upper end is from filtering tank
Top enters 9 inner cavity of filtering tank and connect with water distribution supervisor 28.The upper end of tank bottom transition water pipeline 19 connects the next threeway 22, under
End enters 9 inner cavity of filtering tank from 9 bottom of filtering tank and connect with the vertical tube 30 that catchments.One end of air purge pipeline 15 connects air compressor machine 16
Gas outlet, the other end connect tank bottom transition water pipeline 19, are sequentially connected in series air accumulator 14, gas source distributor box 13 and air purge valve on pipeline
Door 7.PLC control cabinet is connected to power supply by electric wire, simultaneously also by signal wire respectively with elevator pump 1, backwashing pump 3, pneumatic operated valve
Door and air purge valve 7 connect.
Embodiment 2
Referring to Fig. 1, Fig. 2, Fig. 3, Fig. 4, Fig. 5, Fig. 6, Fig. 7 and Fig. 8.Integrated crude oil wastewater efficient fine processing device, including
Filtering tank 9, elevator pump 1, backwashing pump 3, air compressor machine 16, air accumulator 14, gas source distributor box 13, PLC control cabinet, water pipeline, air purge
Pipeline 15, electric wire, signal wire, Pneumatic butterfly valve, air purge valve 7 and threeway.The top of filtering tank 9 is equipped with the row inside and outside tank skin
Tracheae 10 and oil exit pipe 11, exhaust pipe 10 are externally provided with exhaust valve in tank, and oil exit pipe is externally provided with draining valve, 9 inner cavity of filtering tank in tank
Top be equipped with water distributing mechanism, middle part be equipped with AFM active filter mechanism, lower part be equipped with water collection agencies.Water distributing mechanism includes water distribution
28 and its 6 water distribution branch pipes 29 are responsible for, water distribution supervisor 28 erects setting and the upper end is connect with tank deck transition water pipeline 8, water distribution
Branch pipe 29 is laterally uniform to be responsible for around 28 and tilts down in water distribution.AFM active filter mechanism include 4 layers, by up to
Under be followed successively by 33,1 grades of 0 grade of active filter layer, 34,2 grades of active filter layer active filter layer 35 and 3 grades of active filter layers 36.It catchments
Catchment supervisor and its collection branch pipe 32 that mechanism is made of the vertical tube 30 that catchments with the transverse tube 31 that catchments, the lower end for the vertical tube 30 that catchments and tank
Bottom transition water pipeline 19 connects, the lateral symmetry two sides for being distributed in the transverse tube 31 that catchments of collection branch pipe 32；The collection branch pipe 32 of every side
It is 5, the 32 length longest of collection branch pipe positioned at middle part is successively gradually short to 32 length of collection branch pipe of both ends arrangement.Pneumatically
Butterfly valve includes filtered water inlet valve 24, filtering outlet valve 20, backwash inlet valve 18 and backwash outlet valve 25.Threeway includes upper threeway
23 and the next threeway 22.Water pipeline includes filtering water pipeline, backwash water pipeline and transition water pipeline, and filtering water pipeline includes filtering
Back with water inlet line 2 and water pipeline 27 is filtered out, backwash water pipeline includes backwash back with water inlet line 6 and backwash water outlet pipeline 26, transitional water
Pipeline includes tank deck transition water pipeline 8 and tank bottom transition water pipeline 19.Filtered water inlet pipeline 2 is equipped with lower section above it respectively
Branch, top branch connect upper threeway 23 and install filtered water inlet valve 24 on branch line, and lower section branch connects elevator pump 1
Water outlet.It filters out water pipeline 27 and is equipped with branch thereunder, lower section branch connects the next threeway 22 and pacifies on branch line
Dress filtering outlet valve 20.Backwash back with water inlet line 6 is equipped with branch above it, and top branch connects the next threeway 22 and in branched pipe
Road installation backwash inlet valve 18.Backwash is discharged pipeline 26 and is equipped with branch thereunder, and lower section branch connects upper threeway 23 simultaneously
Backwash outlet valve 25 is installed on branch line.The lower end of tank deck transition water pipeline 8 connects upper threeway 23, and upper end is from filtering tank
Top enters 9 inner cavity of filtering tank and connect with water distribution supervisor 28.The upper end of tank bottom transition water pipeline 19 connects the next threeway 22, under
End enters 9 inner cavity of filtering tank from 9 bottom of filtering tank and connect with the vertical tube 30 that catchments.One end of air purge pipeline 15 connects air compressor machine 16
Gas outlet, the other end connect tank bottom transition water pipeline 19, are sequentially connected in series air accumulator 14, gas source distributor box 13 and air purge valve on pipeline
Door 7.PLC control cabinet is connected to power supply by electric wire, simultaneously also by signal wire respectively with elevator pump 1, backwashing pump 3, pneumatic operated valve
Door and air purge valve 7 connect.It further include medicating mechanism；Medicating mechanism includes dosing tank 17, dosing pump 5 and liquid medicine feed-line 4,
The beginning of liquid medicine feed-line 4 connects dosing tank 17, tail end connects filtered water inlet pipeline 2, installs dosing pump 5 on pipeline.
Embodiment 3
Referring to Fig. 1, Fig. 2, Fig. 3, Fig. 4, Fig. 5, Fig. 6, Fig. 7 and Fig. 8.Integrated crude oil wastewater efficient fine processing device, including
Filtering tank 9, elevator pump 1, backwashing pump 3, air compressor machine 16, air accumulator 14, gas source distributor box 13, PLC control cabinet, water pipeline, air purge
Pipeline 15, electric wire, signal wire, Pneumatic butterfly valve, air purge valve 7 and threeway.The top of filtering tank 9 is equipped with the row inside and outside tank skin
Tracheae 10 and oil exit pipe 11, exhaust pipe 10 are externally provided with exhaust valve in tank, and oil exit pipe is externally provided with draining valve, 9 inner cavity of filtering tank in tank
Top be equipped with water distributing mechanism, middle part be equipped with AFM active filter mechanism, lower part be equipped with water collection agencies.Water distributing mechanism includes water distribution
28 and its 6 water distribution branch pipes 29 are responsible for, water distribution supervisor 28 erects setting and the upper end is connect with tank deck transition water pipeline 8, water distribution
Branch pipe 29 is laterally uniform to be responsible for around 28 and tilts down in water distribution.AFM active filter mechanism include 4 layers, by up to
Under be followed successively by 33,1 grades of 0 grade of active filter layer, 34,2 grades of active filter layer active filter layer 35 and 3 grades of active filter layers 36.It catchments
Catchment supervisor and its collection branch pipe 32 that mechanism is made of the vertical tube 30 that catchments with the transverse tube 31 that catchments, the lower end for the vertical tube 30 that catchments and tank
Bottom transition water pipeline 19 connects, the lateral symmetry two sides for being distributed in the transverse tube 31 that catchments of collection branch pipe 32；The collection branch pipe 32 of every side
It is 5, the 32 length longest of collection branch pipe positioned at middle part is successively gradually short to 32 length of collection branch pipe of both ends arrangement.Pneumatically
Butterfly valve includes filtered water inlet valve 24, filtering outlet valve 20, backwash inlet valve 18 and backwash outlet valve 25.Threeway includes upper threeway
23 and the next threeway 22.Water pipeline includes filtering water pipeline, backwash water pipeline and transition water pipeline, and filtering water pipeline includes filtering
Back with water inlet line 2 and water pipeline 27 is filtered out, backwash water pipeline includes backwash back with water inlet line 6 and backwash water outlet pipeline 26, transitional water
Pipeline includes tank deck transition water pipeline 8 and tank bottom transition water pipeline 19.Filtered water inlet pipeline 2 is equipped with lower section above it respectively
Branch, top branch connect upper threeway 23 and install filtered water inlet valve 24 on branch line, and lower section branch connects elevator pump 1
Water outlet.It filters out water pipeline 27 and is equipped with branch thereunder, lower section branch connects the next threeway 22 and pacifies on branch line
Dress filtering outlet valve 20.Backwash back with water inlet line 6 is equipped with branch above it, and top branch connects the next threeway 22 and in branched pipe
Road installation backwash inlet valve 18.Backwash is discharged pipeline 26 and is equipped with branch thereunder, and lower section branch connects upper threeway 23 simultaneously
Backwash outlet valve 25 is installed on branch line.The lower end of tank deck transition water pipeline 8 connects upper threeway 23, and upper end is from filtering tank
Top enters 9 inner cavity of filtering tank and connect with water distribution supervisor 28.The upper end of tank bottom transition water pipeline 19 connects the next threeway 22, under
End enters 9 inner cavity of filtering tank from 9 bottom of filtering tank and connect with the vertical tube 30 that catchments.One end of air purge pipeline 15 connects air compressor machine 16
Gas outlet, the other end connect tank bottom transition water pipeline 19, are sequentially connected in series air accumulator 14, gas source distributor box 13 and air purge valve on pipeline
Door 7.PLC control cabinet is connected to power supply by electric wire, simultaneously also by signal wire respectively with elevator pump 1, backwashing pump 3, pneumatic operated valve
Door and air purge valve 7 connect.It further include medicating mechanism；Medicating mechanism includes dosing tank 17, dosing pump 5 and liquid medicine feed-line 4,
The beginning of liquid medicine feed-line 4 connects dosing tank 17, tail end connects filtered water inlet pipeline 2, installs dosing pump 5 on pipeline.Also wrap
Include sewage pipe 21；One end of sewage pipe 21 connects tank bottom transition water pipeline 19, and the pipeline of sewage pipe 21 is equipped with manual blowdown valve.
Sewage pipe 21 is mainly used for excluding 9 tank bottom dirt of filtering tank during turnaround of unit.
Embodiment 4
Referring to Fig. 1, Fig. 2, Fig. 3, Fig. 4, Fig. 5, Fig. 6, Fig. 7 and Fig. 8.Integrated crude oil wastewater efficient fine processing device, including
Filtering tank 9, elevator pump 1, backwashing pump 3, air compressor machine 16, air accumulator 14, gas source distributor box 13, PLC control cabinet, water pipeline, air purge
Pipeline 15, electric wire, signal wire, Pneumatic butterfly valve, air purge valve 7 and threeway.The top of filtering tank 9 is equipped with the row inside and outside tank skin
Tracheae 10 and oil exit pipe 11, exhaust pipe 10 are externally provided with exhaust valve in tank, and oil exit pipe is externally provided with draining valve, 9 inner cavity of filtering tank in tank
Top be equipped with water distributing mechanism, middle part be equipped with AFM active filter mechanism, lower part be equipped with water collection agencies.Water distributing mechanism includes water distribution
28 and its 6 water distribution branch pipes 29 are responsible for, water distribution supervisor 28 erects setting and the upper end is connect with tank deck transition water pipeline 8, water distribution
Branch pipe 29 is laterally uniform to be responsible for around 28 and tilts down in water distribution.AFM active filter mechanism include 4 layers, by up to
Under be followed successively by 33,1 grades of 0 grade of active filter layer, 34,2 grades of active filter layer active filter layer 35 and 3 grades of active filter layers 36.It catchments
Catchment supervisor and its collection branch pipe 32 that mechanism is made of the vertical tube 30 that catchments with the transverse tube 31 that catchments, the lower end for the vertical tube 30 that catchments and tank
Bottom transition water pipeline 19 connects, the lateral symmetry two sides for being distributed in the transverse tube 31 that catchments of collection branch pipe 32；The collection branch pipe 32 of every side
It is 5, the 32 length longest of collection branch pipe positioned at middle part is successively gradually short to 32 length of collection branch pipe of both ends arrangement.Pneumatically
Butterfly valve includes filtered water inlet valve 24, filtering outlet valve 20, backwash inlet valve 18 and backwash outlet valve 25.Threeway includes upper threeway
23 and the next threeway 22.Water pipeline includes filtering water pipeline, backwash water pipeline and transition water pipeline, and filtering water pipeline includes filtering
Back with water inlet line 2 and water pipeline 27 is filtered out, backwash water pipeline includes backwash back with water inlet line 6 and backwash water outlet pipeline 26, transitional water
Pipeline includes tank deck transition water pipeline 8 and tank bottom transition water pipeline 19.Filtered water inlet pipeline 2 is equipped with lower section above it respectively
Branch, top branch connect upper threeway 23 and install filtered water inlet valve 24 on branch line, and lower section branch connects elevator pump 1
Water outlet.It filters out water pipeline 27 and is equipped with branch thereunder, lower section branch connects the next threeway 22 and pacifies on branch line
Dress filtering outlet valve 20.Backwash back with water inlet line 6 is equipped with branch above it, and top branch connects the next threeway 22 and in branched pipe
Road installation backwash inlet valve 18.Backwash is discharged pipeline 26 and is equipped with branch thereunder, and lower section branch connects upper threeway 23 simultaneously
Backwash outlet valve 25 is installed on branch line.The lower end of tank deck transition water pipeline 8 connects upper threeway 23, and upper end is from filtering tank
Top enters 9 inner cavity of filtering tank and connect with water distribution supervisor 28.The upper end of tank bottom transition water pipeline 19 connects the next threeway 22, under
End enters 9 inner cavity of filtering tank from 9 bottom of filtering tank and connect with the vertical tube 30 that catchments.One end of air purge pipeline 15 connects air compressor machine 16
Gas outlet, the other end connect tank bottom transition water pipeline 19, are sequentially connected in series air accumulator 14, gas source distributor box 13 and air purge valve on pipeline
Door 7.PLC control cabinet is connected to power supply by electric wire, simultaneously also by signal wire respectively with elevator pump 1, backwashing pump 3, pneumatic operated valve
Door and air purge valve 7 connect.It further include medicating mechanism；Medicating mechanism includes dosing tank 17, dosing pump 5 and liquid medicine feed-line 4,
The beginning of liquid medicine feed-line 4 connects dosing tank 17, tail end connects filtered water inlet pipeline 2, installs dosing pump 5 on pipeline.Also wrap
Include sewage pipe 21；One end of sewage pipe 21 connects tank bottom transition water pipeline 19, and the pipeline of sewage pipe 21 is equipped with manual blowdown valve.
Sewage pipe 21 is mainly used for excluding 9 tank bottom dirt of filtering tank during turnaround of unit.Water distribution branch pipe 29 is all made of with collection branch pipe 32
The wire-wrapped screen of 316 type stainless steel materials.
Embodiment 5
Referring to Fig. 1, Fig. 2, Fig. 3, Fig. 4, Fig. 5, Fig. 6, Fig. 7 and Fig. 8.Integrated crude oil wastewater efficient fine processing device, including
Filtering tank 9, elevator pump 1, backwashing pump 3, air compressor machine 16, air accumulator 14, gas source distributor box 13, PLC control cabinet, water pipeline, air purge
Pipeline 15, electric wire, signal wire, Pneumatic butterfly valve, air purge valve 7 and threeway.The top of filtering tank 9 is equipped with the row inside and outside tank skin
Tracheae 10 and oil exit pipe 11, exhaust pipe 10 are externally provided with exhaust valve in tank, and oil exit pipe is externally provided with draining valve, 9 inner cavity of filtering tank in tank
Top be equipped with water distributing mechanism, middle part be equipped with AFM active filter mechanism, lower part be equipped with water collection agencies.Water distributing mechanism includes water distribution
28 and its 6 water distribution branch pipes 29 are responsible for, water distribution supervisor 28 erects setting and the upper end is connect with tank deck transition water pipeline 8, water distribution
Branch pipe 29 is laterally uniform to be responsible for around 28 and tilts down in water distribution.AFM active filter mechanism include 4 layers, by up to
Under be followed successively by 33,1 grades of 0 grade of active filter layer, 34,2 grades of active filter layer active filter layer 35 and 3 grades of active filter layers 36.It catchments
Catchment supervisor and its collection branch pipe 32 that mechanism is made of the vertical tube 30 that catchments with the transverse tube 31 that catchments, the lower end for the vertical tube 30 that catchments and tank
Bottom transition water pipeline 19 connects, the lateral symmetry two sides for being distributed in the transverse tube 31 that catchments of collection branch pipe 32；The collection branch pipe 32 of every side
It is 5, the 32 length longest of collection branch pipe positioned at middle part is successively gradually short to 32 length of collection branch pipe of both ends arrangement.Pneumatically
Butterfly valve includes filtered water inlet valve 24, filtering outlet valve 20, backwash inlet valve 18 and backwash outlet valve 25.Threeway includes upper threeway
23 and the next threeway 22.Water pipeline includes filtering water pipeline, backwash water pipeline and transition water pipeline, and filtering water pipeline includes filtering
Back with water inlet line 2 and water pipeline 27 is filtered out, backwash water pipeline includes backwash back with water inlet line 6 and backwash water outlet pipeline 26, transitional water
Pipeline includes tank deck transition water pipeline 8 and tank bottom transition water pipeline 19.Filtered water inlet pipeline 2 is equipped with lower section above it respectively
Branch, top branch connect upper threeway 23 and install filtered water inlet valve 24 on branch line, and lower section branch connects elevator pump 1
Water outlet.It filters out water pipeline 27 and is equipped with branch thereunder, lower section branch connects the next threeway 22 and pacifies on branch line
Dress filtering outlet valve 20.Backwash back with water inlet line 6 is equipped with branch above it, and top branch connects the next threeway 22 and in branched pipe
Road installation backwash inlet valve 18.Backwash is discharged pipeline 26 and is equipped with branch thereunder, and lower section branch connects upper threeway 23 simultaneously
Backwash outlet valve 25 is installed on branch line.The lower end of tank deck transition water pipeline 8 connects upper threeway 23, and upper end is from filtering tank
Top enters 9 inner cavity of filtering tank and connect with water distribution supervisor 28.The upper end of tank bottom transition water pipeline 19 connects the next threeway 22, under
End enters 9 inner cavity of filtering tank from 9 bottom of filtering tank and connect with the vertical tube 30 that catchments.One end of air purge pipeline 15 connects air compressor machine 16
Gas outlet, the other end connect tank bottom transition water pipeline 19, are sequentially connected in series air accumulator 14, gas source distributor box 13 and air purge valve on pipeline
Door 7.PLC control cabinet is connected to power supply by electric wire, simultaneously also by signal wire respectively with elevator pump 1, backwashing pump 3, pneumatic operated valve
Door and air purge valve 7 connect.It further include medicating mechanism；Medicating mechanism includes dosing tank 17, dosing pump 5 and liquid medicine feed-line 4,
The beginning of liquid medicine feed-line 4 connects dosing tank 17, tail end connects filtered water inlet pipeline 2, installs dosing pump 5 on pipeline.Also wrap
Include sewage pipe 21；One end of sewage pipe 21 connects tank bottom transition water pipeline 19, and the pipeline of sewage pipe 21 is equipped with manual blowdown valve.
Sewage pipe 21 is mainly used for excluding 9 tank bottom dirt of filtering tank during turnaround of unit.Water distribution branch pipe 29 is all made of with collection branch pipe 32
The wire-wrapped screen of 316 type stainless steel materials.Filtering tank 9 is set as 2, mating common filtering water pipeline and backwash water pipeline；It mentions
It rises pump 1 and is set as 2,1 is standby with 1.
Embodiment 6
Referring to Fig. 1, Fig. 2, Fig. 3, Fig. 4, Fig. 5, Fig. 6, Fig. 7 and Fig. 8.Integrated crude oil wastewater efficient fine processing device, including
Filtering tank 9, elevator pump 1, backwashing pump 3, air compressor machine 16, air accumulator 14, gas source distributor box 13, PLC control cabinet, water pipeline, air purge
Pipeline 15, electric wire, signal wire, Pneumatic butterfly valve, air purge valve 7 and threeway.The top of filtering tank 9 is equipped with the row inside and outside tank skin
Tracheae 10 and oil exit pipe 11, exhaust pipe 10 are externally provided with exhaust valve in tank, and oil exit pipe is externally provided with draining valve, 9 inner cavity of filtering tank in tank
Top be equipped with water distributing mechanism, middle part be equipped with AFM active filter mechanism, lower part be equipped with water collection agencies.Water distributing mechanism includes water distribution
28 and its 6 water distribution branch pipes 29 are responsible for, water distribution supervisor 28 erects setting and the upper end is connect with tank deck transition water pipeline 8, water distribution
Branch pipe 29 is laterally uniform to be responsible for around 28 and tilts down in water distribution.AFM active filter mechanism include 4 layers, by up to
Under be followed successively by 33,1 grades of 0 grade of active filter layer, 34,2 grades of active filter layer active filter layer 35 and 3 grades of active filter layers 36.It catchments
Catchment supervisor and its collection branch pipe 32 that mechanism is made of the vertical tube 30 that catchments with the transverse tube 31 that catchments, the lower end for the vertical tube 30 that catchments and tank
Bottom transition water pipeline 19 connects, the lateral symmetry two sides for being distributed in the transverse tube 31 that catchments of collection branch pipe 32；The collection branch pipe 32 of every side
It is 5, the 32 length longest of collection branch pipe positioned at middle part is successively gradually short to 32 length of collection branch pipe of both ends arrangement.Pneumatically
Butterfly valve includes filtered water inlet valve 24, filtering outlet valve 20, backwash inlet valve 18 and backwash outlet valve 25.Threeway includes upper threeway
23 and the next threeway 22.Water pipeline includes filtering water pipeline, backwash water pipeline and transition water pipeline, and filtering water pipeline includes filtering
Back with water inlet line 2 and water pipeline 27 is filtered out, backwash water pipeline includes backwash back with water inlet line 6 and backwash water outlet pipeline 26, transitional water
Pipeline includes tank deck transition water pipeline 8 and tank bottom transition water pipeline 19.Filtered water inlet pipeline 2 is equipped with lower section above it respectively
Branch, top branch connect upper threeway 23 and install filtered water inlet valve 24 on branch line, and lower section branch connects elevator pump 1
Water outlet.It filters out water pipeline 27 and is equipped with branch thereunder, lower section branch connects the next threeway 22 and pacifies on branch line
Dress filtering outlet valve 20.Backwash back with water inlet line 6 is equipped with branch above it, and top branch connects the next threeway 22 and in branched pipe
Road installation backwash inlet valve 18.Backwash is discharged pipeline 26 and is equipped with branch thereunder, and lower section branch connects upper threeway 23 simultaneously
Backwash outlet valve 25 is installed on branch line.The lower end of tank deck transition water pipeline 8 connects upper threeway 23, and upper end is from filtering tank
Top enters 9 inner cavity of filtering tank and connect with water distribution supervisor 28.The upper end of tank bottom transition water pipeline 19 connects the next threeway 22, under
End enters 9 inner cavity of filtering tank from 9 bottom of filtering tank and connect with the vertical tube 30 that catchments.One end of air purge pipeline 15 connects air compressor machine 16
Gas outlet, the other end connect tank bottom transition water pipeline 19, are sequentially connected in series air accumulator 14, gas source distributor box 13 and air purge valve on pipeline
Door 7.PLC control cabinet is connected to power supply by electric wire, simultaneously also by signal wire respectively with elevator pump 1, backwashing pump 3, pneumatic operated valve
Door and air purge valve 7 connect.It further include medicating mechanism；Medicating mechanism includes dosing tank 17, dosing pump 5 and liquid medicine feed-line 4,
The beginning of liquid medicine feed-line 4 connects dosing tank 17, tail end connects filtered water inlet pipeline 2, installs dosing pump 5 on pipeline.Also wrap
Include sewage pipe 21；One end of sewage pipe 21 connects tank bottom transition water pipeline 19, and the pipeline of sewage pipe 21 is equipped with manual blowdown valve.
Sewage pipe 21 is mainly used for excluding 9 tank bottom dirt of filtering tank during turnaround of unit.Water distribution branch pipe 29 is all made of with collection branch pipe 32
The wire-wrapped screen of 316 type stainless steel materials.Filtering tank 9 is set as 2, mating common filtering water pipeline and backwash water pipeline；It mentions
It rises pump 1 and is set as 2,1 is standby with 1.Skid pedestal 12 is laid, each component part of the device is both secured on skid pedestal 12.
Embodiment 7
Referring to Fig. 1, Fig. 2, Fig. 3, Fig. 4, Fig. 5, Fig. 6, Fig. 7 and Fig. 8.Integrated crude oil wastewater efficient fine processing device, including
Filtering tank 9, elevator pump 1, backwashing pump 3, air compressor machine 16, air accumulator 14, gas source distributor box 13, PLC control cabinet, water pipeline, air purge
Pipeline 15, electric wire, signal wire, Pneumatic butterfly valve, air purge valve 7 and threeway.The top of filtering tank 9 is equipped with the row inside and outside tank skin
Tracheae 10 and oil exit pipe 11, exhaust pipe 10 are externally provided with exhaust valve in tank, and oil exit pipe is externally provided with draining valve, 9 inner cavity of filtering tank in tank
Top be equipped with water distributing mechanism, middle part be equipped with AFM active filter mechanism, lower part be equipped with water collection agencies.Water distributing mechanism includes water distribution
28 and its 6 water distribution branch pipes 29 are responsible for, water distribution supervisor 28 erects setting and the upper end is connect with tank deck transition water pipeline 8, water distribution
Branch pipe 29 is laterally uniform to be responsible for around 28 and tilts down in water distribution.AFM active filter mechanism include 4 layers, by up to
Under be followed successively by 33,1 grades of 0 grade of active filter layer, 34,2 grades of active filter layer active filter layer 35 and 3 grades of active filter layers 36.It catchments
Catchment supervisor and its collection branch pipe 32 that mechanism is made of the vertical tube 30 that catchments with the transverse tube 31 that catchments, the lower end for the vertical tube 30 that catchments and tank
Bottom transition water pipeline 19 connects, the lateral symmetry two sides for being distributed in the transverse tube 31 that catchments of collection branch pipe 32；The collection branch pipe 32 of every side
It is 5, the 32 length longest of collection branch pipe positioned at middle part is successively gradually short to 32 length of collection branch pipe of both ends arrangement.Pneumatically
Butterfly valve includes filtered water inlet valve 24, filtering outlet valve 20, backwash inlet valve 18 and backwash outlet valve 25.Threeway includes upper threeway
23 and the next threeway 22.Water pipeline includes filtering water pipeline, backwash water pipeline and transition water pipeline, and filtering water pipeline includes filtering
Back with water inlet line 2 and water pipeline 27 is filtered out, backwash water pipeline includes backwash back with water inlet line 6 and backwash water outlet pipeline 26, transitional water
Pipeline includes tank deck transition water pipeline 8 and tank bottom transition water pipeline 19.Filtered water inlet pipeline 2 is equipped with lower section above it respectively
Branch, top branch connect upper threeway 23 and install filtered water inlet valve 24 on branch line, and lower section branch connects elevator pump 1
Water outlet.It filters out water pipeline 27 and is equipped with branch thereunder, lower section branch connects the next threeway 22 and pacifies on branch line
Dress filtering outlet valve 20.Backwash back with water inlet line 6 is equipped with branch above it, and top branch connects the next threeway 22 and in branched pipe
Road installation backwash inlet valve 18.Backwash is discharged pipeline 26 and is equipped with branch thereunder, and lower section branch connects upper threeway 23 simultaneously
Backwash outlet valve 25 is installed on branch line.The lower end of tank deck transition water pipeline 8 connects upper threeway 23, and upper end is from filtering tank
Top enters 9 inner cavity of filtering tank and connect with water distribution supervisor 28.The upper end of tank bottom transition water pipeline 19 connects the next threeway 22, under
End enters 9 inner cavity of filtering tank from 9 bottom of filtering tank and connect with the vertical tube 30 that catchments.One end of air purge pipeline 15 connects air compressor machine 16
Gas outlet, the other end connect tank bottom transition water pipeline 19, are sequentially connected in series air accumulator 14, gas source distributor box 13 and air purge valve on pipeline
Door 7.PLC control cabinet is connected to power supply by electric wire, simultaneously also by signal wire respectively with elevator pump 1, backwashing pump 3, pneumatic operated valve
Door and air purge valve 7 connect.It further include medicating mechanism；Medicating mechanism includes dosing tank 17, dosing pump 5 and liquid medicine feed-line 4,
The beginning of liquid medicine feed-line 4 connects dosing tank 17, tail end connects filtered water inlet pipeline 2, installs dosing pump 5 on pipeline.Also wrap
Include sewage pipe 21；One end of sewage pipe 21 connects tank bottom transition water pipeline 19, and the pipeline of sewage pipe 21 is equipped with manual blowdown valve.
Sewage pipe 21 is mainly used for excluding 9 tank bottom dirt of filtering tank during turnaround of unit.Water distribution branch pipe 29 is all made of with collection branch pipe 32
The wire-wrapped screen of 316 type stainless steel materials.Filtering tank 9 is set as 2, mating common filtering water pipeline and backwash water pipeline；It mentions
It rises pump 1 and is set as 2,1 is standby with 1.Skid pedestal 12 is laid, each component part of the device is both secured on skid pedestal 12.
To realize optimum filtration effect, volume ratio shared by each active filter layer of AFM active filter mechanism is respectively as follows: 0 grade of activity filter
The bed of material 33 accounts for 20%, and 1 grade of active filter layer 34 accounts for 50%, and 2 grades of active filter layers 35 account for 15%, and 3 grades of active filter layers 36 account for 15%.
To better understand the present invention convenient for those skilled in the art, illustrated now in conjunction with attached drawing and table of the invention related
Basic principle and excellent results are as follows:
1. being arranged about filtering tank
Referring to Fig. 1, Fig. 2, Fig. 3, Fig. 5, Fig. 6, Fig. 7 and Fig. 8.In tank, water distributing mechanism, AFM active filter mechanism and water collection agencies
Arrangement orderly up and down is presented；Outside tank, exhaust pipe, oil exit pipe and sewage pipe are available in all varieties.The benefit of such setting is: water distribution is equal
It is even；Collect hydrologic(al) budget；Ensure to backwash without dead angle；Filtrate is stablized, and not random layer does not run filtrate；Suspended matter, oil droplet coacervation space be big,
Time is long, and recycling thoroughly, does not interfere filter field；Filtering pot bottom prevents slough and breeds bacterium.
2. about backwash mode
Referring to Fig. 1, Fig. 2, Fig. 3, Fig. 5, Fig. 6, Fig. 7 and Fig. 8.After filtering operation a period of time, filter material layer retention and absorption are certain
The suspended solid particles of amount, colloid, grease stain, cause effluent quality to decline, and the pressure difference of inflow and outflow pipeline increases, flow drop
Low, this is just backwashed, and allows flow reversal by filter material layer, is made filtering layer expansion, is suspended, by water flow shearing force and
The collision friction power of particle cleans filter material layer, so that the pollutant in filtering layer is detached from filtrate and is discharged with backwash water.Commonly used
Backwash mode is that simple backwash water is rinsed or backwash water flushing is washed again in first air-blowing, these backwash modes are to conventional filtration
Effect is fine, but fine filtering is often not achieved expected backwash effect.To obtain backwash effect outstanding, the present invention is used
Mixing wastewater with air washes mode by rubbing with the hands.Backwash water tube side is introduced compressed gas into, tangential air water is thoroughly mixed, and mixes gas backwash water from mistake
Filter tank bottom enters in filtering tank, mixes the bubble in gas backwash water to the smaller impurity adhesion and aggregation in filtrate into larger particles,
Larger particles are mobile to top with water, air-flow, are equivalent to aerated water and are sheared in filtering tank to impurity in filtrate, rub and touch
It hits, adhere to, assembling, cleaning, rinsing floating, to after top, gas is discharged from exhaust outlet, and water is discharged from water outlet.Before backwash terminates,
It stops the supple of gas or steam within 2 minutes in advance.Relative to conventional backwash mode, mixing wastewater with air of the invention washes mode by rubbing with the hands, and it is anti-not only to save 50% or more
Water consume is rinsed, and saves 50% or more and backwashes energy consumption, performance is restored completely after filtrate backwash, and efficiency reaches target.
3. about dosing method
Referring to Fig. 1 and Fig. 4.Dosing is not necessarily to when integrated crude oil wastewater efficient fine processing device operates normally, so that it may produce up to
Mark water.To cope with production upstream unexpected abnormality, when the water variation water quality that preparation enters device severely exceeds and pollution will cause
When the risk of filtering tank filtrate, the emergency measure of agent-feeding treatment is taken.The measure may be implemented in be changed without filtrate under the premise of, borrow
Mixing wastewater with air counter-flushing process is helped, makes filtrate rapid regeneration in conjunction with efficient filtrate cleaning agent is added, saves filter material replacement cost, subtract
Object amount is discarded less, and integrated crude oil wastewater efficient fine processing device is made to return to normal production in a short time operation.
4. about new A FM active filter
AFM active filter is a kind of aluminosilicate active material that the activation with glass structure matrix is mesoporous, belongs to nanometer and changes
Property filtrate, heap density about 1.25g/cm3.Specifically, AFM active filter is divided into four kinds of ranks, and basic parameter is referring to table 1.
1 AFM active filter rank statistical form of table
| Filtrate model | Partial size (mm) | K80 | Specification fills method | Heap density (g/cm3) |
| 0 grade | 0.25-0.5 | 1.2 | 20% | 1.28 |
| 1 grade | 0.4-1.0 | 1.2 | 50% | 1.25 |
| 2 grades | 1.0-2.0 | 1.2 | 15% | 1.23 |
| 3 grades | 2.0-4.0 | 1.3 | 15% | 1.22 |
AFM active filter has following 4 outstanding features:
(1) strong adsorption
Ordinary filter retains the process of suspended matter, generally must be by molecule to " conveying " of filter material surface and in filtrate
" attachment " two stages on surface can be only achieved.That is the particle to suspend in water must be first sent to filtering material particle
Then surface could be retained by filtrate.And AFM active filter surface has charge, has been formed on its surface different charge layers,
Can be by the active force between charge particle when particle is close to filtrate " absorption " in filter material surface, increase adsorption plane
Long-pending and adsorption strength.
(2) long service life
Currently, the filtrate in oil field extracted water for filtering technique mainly has quartz sand, anthracite, magnetic iron ore, walnut shell etc..
According to statistics, it will be replaced, be had every 2-3 according to the filtering filtrate at the different disposing polluted water in oil stations of filtrate pollution level
It will even replace within 1 year, and cause the increase of sewage treatment expense and the serious pollution of environment.And AFM active filter is due to it
In operation process, greasy dirt and suspended particulates are attached to the covering film surface of filtrate, do not contact with filtrate itself, not only from root
On prevented attachment of the bacterium on filtrate, while reducing the percentage of damage of filtrate, extend the service life of filtrate.Common filter
Material is with the state vs before and after the use of AFM active filter referring to Fig. 9.
The excellent properties of AFM active filter can also be verified in the comparative experiments in laboratory.With 25kg oil content
It is filtered for the oily wastewater of 50mg/L, takes 20 grams of upper layer filtrate to be placed in a beaker after the completion of filtering and be put into (105 ± 1) DEG C
4 h of drying in oven.Taking-up, which is put into drier, puts to room temperature, measures a small amount of blank gasoline and repeatedly rinses the oil after drying
Sand, the gasoline after flushing are collected in the colorimetric cylinder of 50 mL.Then, oil-sand is poured into the funnel equipped with filter paper, with blank vapour
Oil flushing is until the gasoline color and blank gasoline solid colour filtered out after flushing.Gasoline after flushing is closed at into above-mentioned 50 mL
Colorimetric cylinder in, and be diluted to scale.If being diluted to 100 mL more than 50 mL.According to oil-containing in SY/T 5329-1994
It is 2.5mg/g that the test method of amount, which measures oil content,.Then it is backwashed under same flow velocity, is stopped when backwashing 10 minutes
Backwash opens filter tank and takes upper layer filtrate 20g respectively, then measures three kinds of filtrates respectively according to above-mentioned method with blank gasoline
Oil content are as follows: walnut shell 0.8mg/g, diamond dust 0.5mg/g, nano modification filtrate are 0.15mg/g.Laboratory experiment card
It is filtrate floating 20% to 30% that bright AFM active filter, which most preferably backwashes condition, is continuously backwashed under the conditions of best backwash
The breakage rate of filtrate is less than 3% at 1000 hours.
Scene is by backwash 10 minutes daily, and the service life of AFM active filter is for 15 years.(3) influent quality is wanted
Ask low
" double 50 " oil content of wastewater≤50 ㎎/L, suspended solids content≤50.0 ㎎/L, water outlet can reach level-one water gauge for water inlet
Quasi- " oil content of wastewater≤5 ㎎/L, suspended solids content≤1.0 ㎎/L, suspended particle median diameter≤1.0 μm ".
The moisture film of one layer of hydrophilic and oleophobic type can be generated after the chance water of AFM active filter surface.AFM active filter is in its operation
Cheng Zhong, greasy dirt and suspended particulates are attached to the covering film surface of filtrate, do not contact with filtrate itself, and filter will not be more entered with water flow
Material is internal, causes the pollution of filtrate, has prevented attachment of the bacterium on filtrate from the root.In backwash, greasy dirt, microactuator suspension
Grain is easy to disengaging filtrate absorption under the driving of backwashing water and filter tank is discharged through sewage draining exit, while reducing the broken of filtrate
Rate extends the service life of filtrate, reduces the pollution to environment.
(4) energy-saving and water-saving is backwashed
Ordinary filter filtering is located against porosity between filtering material particle and particle to retain greasy dirt and suspended particulates, allow greasy dirt with
Suspended particulates are attached to filter material surface to realize expected filter effect.However attachment when thus causing filtrate backwash
Object is difficult to the phenomenon that being detached from filtrate.And after new A FM active filter contacts water, surface will form one layer of smooth covering
Film, since its surface can be adsorbed on the suspended particulates of retention on this layer of smooth cover film with charge, so as to avoid oil
Contact of the dirty and suspended particulates directly with filtrate.It is easier that greasy dirt is allowed to reach with suspended particulate disengaging cover film when backwashing in this way
Preferable backwash effect.
Experiments have shown that novel nano modified filter material only needs 5-8 minutes when backwashing, the removal rate of filter material surface greasy dirt is up to 95%
More than, and ordinary filter backwashing time then needs 10-20 minutes, and the oily waste degradation rate of filter material surface is up to 80%.Backwashing time
Reduction electricity consumption and water consumption is greatly saved, save 50% or more backwash water consume on year-on-year basis, save 50% or more on year-on-year basis and recoil
Wash energy consumption.
5. about operational process
Referring to Fig. 1, Fig. 2, Fig. 3, Fig. 4, Fig. 5, Fig. 6, Fig. 7, Fig. 8, Figure 10, Figure 11, Figure 12, Figure 13, Figure 14, Figure 15, Tu16Ji
Figure 17.The present invention uses advanced PLC control system and software programming, realizes and automatically controls, and creation data uploads to production and refers to
Wave center.Meanwhile it can also use and manually control as the means of supplementing out economy according to production actual conditions.
(1) filter process
The basic procedure of filtering is: water into elevator pump → pump out water into filtering tank → filtering tank filtering → filtering tank filter after be discharged
→ water buffer tank.
When equipment investment is run, filtered water inlet valve is automatically opened, outlet valve (automatically opens oil extraction, exhaust valve, pays attention to normal
Draining valve is opened 3 minutes every 4 hours when filtering), sewage enters filtering tank by inlet valve, through water distributor water distribution, from upper
It is filtered down by filter bed (AFM active filter mechanism), greasy dirt and suspended particulates are intercepted by active filter absorption in filter bed in water
In, drainage collects through water collector excessively passes by outlet valve outflow filtering tank by outlet pipe, filters, equipment entrance normally opened into and out of water valve
Filtration operating status.
(2) backwash process
The basic procedure of backwash is: reverse washing tank water → backwash pump → filtering tank filtrate backwash → backwash water discharge →
Sewage recovery pond.
Backwash refers to filter after running for a period of time, and filter material layer retains and adsorb a certain amount of suspended solid
Grain, colloid, grease stain cause sewage quality after normally filtering to be deteriorated, and the pressure difference of inflow and outflow pipeline increases, separate unit filter
Flow-reduction etc..
When being backwashed, elevator pump of stopping transport automatically closes filtering Inlet and outlet water valve, automatically opens backwash inlet/outlet valve
Door starts backwash pump (opening simultaneously air purge valve) automatically, and backwash aerated water enters filtering by backwash inlet valve
In tank, by water collector water distribution from bottom to top through filter bed, carrying out backwash to filtrate, (backwash terminated first two minutes in eight minutes
Air purge valve is closed in advance)；Bubble in mixed gas backwash water to the smaller impurity adhesion and aggregation in filtrate at larger particles, it is larger
Particle is mobile to top with water, air-flow, be equivalent to aerated water impurity in filtrate is sheared in filtering tank, frictional impact,
Adherency aggregation, cleans, rinses and float, and to after top, backwashing water is recovered to sewage recovery pond, filtrate through backwash flowing water Valve
Performance is restored as before completely after backwash.
Claims (10)
1. integrated crude oil wastewater efficient fine processing device, it is characterised in that: including filtering tank, elevator pump, backwashing pump, pneumatics
Machine, air accumulator, gas source distributor box, PLC control cabinet, water pipeline, air purge pipeline, electric wire, signal wire, Pneumatic butterfly valve, air purge valve
And threeway；The top of the filtering tank is equipped with exhaust pipe and oil exit pipe inside and outside tank skin, and exhaust pipe is externally provided with exhaust in tank
Valve, oil exit pipe are externally provided with draining valve in tank, and the top of filtering tank inner cavity is equipped with water distributing mechanism, middle part is equipped with AFM active filter machine
Structure, lower part are equipped with water collection agencies；The Pneumatic butterfly valve includes that filtered water inlet valve, filtering outlet valve, backwash inlet valve and backwash go out
Water valve；The threeway includes upper threeway and the next threeway；The water pipeline includes filtering water pipeline, backwash water pipeline and transition
Water pipeline, filtering water pipeline include filtered water inlet pipeline and filter out water pipeline, backwash water pipeline include backwash back with water inlet line and
Backwash is discharged pipeline, and transition water pipeline includes tank deck transition water pipeline and tank bottom transition water pipeline；The filtered water inlet pipeline point
It is not equipped with branch with lower section above it, top branch connects upper threeway and installs filtered water inlet valve on branch line, under
Square branch connects elevator pump water outlet；The water pipeline that filters out is equipped with branch thereunder, and lower section branch connects the next threeway
And the installation filtering outlet valve on branch line；The backwash back with water inlet line is equipped with branch above it, under the connection of top branch
Position threeway simultaneously installs backwash inlet valve on branch line；The backwash water outlet pipeline is equipped with branch, lower section branch thereunder
It connects upper threeway and backwash outlet valve is installed on branch line；The lower end connection upper three of the tank deck transition water pipeline
Logical, upper end enters filtering tank inner cavity at the top of filtering tank and connect with water distributing mechanism；The upper end of the tank bottom transition water pipeline connects
The next threeway is connect, lower end enters filtering tank inner cavity from filtering pot bottom and connect with water collection agencies；One end of the air purge pipeline
Air compressor machine gas outlet is connected, the other end connects tank bottom transition water pipeline, is sequentially connected in series air accumulator, gas source distributor box and gas on pipeline
Wash valve；The PLC control cabinet is connected to power supply by electric wire, simultaneously also by signal wire respectively with elevator pump, backwashing pump, gas
Movable valve and the connection of air purge valve.
2. integration crude oil wastewater efficient fine processing device according to claim 1, it is characterised in that: it further include dosing
Mechanism；The medicating mechanism includes dosing tank, dosing pump and liquid medicine feed-line, and the beginning of liquid medicine feed-line connects dosing
Case, tail end connection filtered water inlet pipeline install dosing pump on pipeline.
3. integration crude oil wastewater efficient fine processing device according to claim 2, it is characterised in that: it further include blowdown
Pipe；One end of the sewage pipe connects tank bottom transition water pipeline, and the pipeline of sewage pipe is equipped with manual blowdown valve.
4. integration crude oil wastewater efficient fine processing device according to claim 1 to 3, it is characterised in that: it is described
Water distributing mechanism includes water distribution supervisor and its 6 water distribution branch pipes, and water distribution supervisor erects setting and the upper end and tank deck transition water pipeline
Connection, water distribution branch pipe it is laterally uniform water distribution supervisor around and tilt down.
5. integration crude oil wastewater efficient fine processing device according to claim 4, it is characterised in that: the collection water dispenser
Catchment supervisor and its collection branch pipe that structure is made of the vertical tube that catchments with the transverse tube that catchments, the lower end for the vertical tube that catchments and tank bottom transition water pipe
Line connection, the lateral symmetry two sides for being distributed in the transverse tube that catchments of collection branch pipe；The collection branch pipe of every side is 5, is located at
The collection branch pipe length longest in portion, the collection branch pipe length successively arranged to both ends are gradually short.
6. integration crude oil wastewater efficient fine processing device according to claim 5, it is characterised in that: the water distribution branch
Pipe is all made of the wire-wrapped screen of 316 type stainless steel materials with collection branch pipe.
7. integration crude oil wastewater efficient fine processing device according to claim 6, it is characterised in that: the filtering tank
It is set as 2, mating common filtering water pipeline and backwash water pipeline；The elevator pump is set as 2, and 1 is standby with 1.
8. integration crude oil wastewater efficient fine processing device according to claim 7, it is characterised in that: lay skid bottom
Seat, each component part of the device is both secured on skid pedestal.
9. integration crude oil wastewater efficient fine processing device according to claim 8, it is characterised in that: the AFM is living
Property filtrate mechanism include 4 layers, be from top to bottom followed successively by 0 grade of active filter layer, 1 grade of active filter layer, 2 grades of active filter layers and 3
Grade active filter layer.
10. integration crude oil wastewater efficient fine processing device according to claim 9, it is characterised in that: each work
Volume ratio shared by property filter material layer is respectively as follows: 0 grade of active filter layer and accounts for 20%, and 1 grade of active filter layer accounts for 50%, 2 grades of active filters
Layer accounts for 15%, and 3 grades of active filter layers account for 15%.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910131669.7A CN109665588A (en) | 2019-02-22 | 2019-02-22 | Integrated crude oil wastewater efficient fine processing device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910131669.7A CN109665588A (en) | 2019-02-22 | 2019-02-22 | Integrated crude oil wastewater efficient fine processing device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN109665588A true CN109665588A (en) | 2019-04-23 |
Family
ID=66151707
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201910131669.7A Pending CN109665588A (en) | 2019-02-22 | 2019-02-22 | Integrated crude oil wastewater efficient fine processing device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN109665588A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110143684A (en) * | 2019-05-29 | 2019-08-20 | 湖南宇宙环保工程有限公司 | A kind of three-in-one clarifier of ion air bearing |
| CN110559702A (en) * | 2019-10-10 | 2019-12-13 | 北京万诺生态科技有限公司 | Adjustable composite dynamic filtering device |
| CN111960581A (en) * | 2020-09-09 | 2020-11-20 | 大庆市普罗石油科技有限公司 | Skid-mounted underground water treatment device and water treatment process |
Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| RU15991U1 (en) * | 2000-07-24 | 2000-11-27 | Санкт-Петербургское государственное унитарное предприятие "Инженерный центр "Водоканал" | WATER TREATMENT PLANT |
| CN202933527U (en) * | 2012-12-19 | 2013-05-15 | 大庆高新区百世环保科技开发有限公司 | Gas-liquid backwashing oil field high-polymer wastewater filter device |
| CN203678016U (en) * | 2013-10-25 | 2014-07-02 | 中国石油天然气集团公司 | Automatic control backwash filtering device for polymer oil recovery |
| CN204569519U (en) * | 2015-04-23 | 2015-08-19 | 东北石油大学 | Poly-repelling crude oil storage tank sewage purification machinery |
| CN204939084U (en) * | 2015-09-22 | 2016-01-06 | 四川新能水处理工程有限公司 | A kind of anaerobic water distributor |
| CN107522310A (en) * | 2017-10-16 | 2017-12-29 | 恩曼技术（北京）有限公司 | Not agent-feeding treatment oil-polluted water re-injection technique |
| US20190023587A1 (en) * | 2017-07-24 | 2019-01-24 | Notes Intellectual Properties, LLC | Produced water filtration |
| CN209537036U (en) * | 2019-02-22 | 2019-10-25 | 山东广域科技有限责任公司 | Integrated crude oil wastewater efficient fine processing device |
-
2019
- 2019-02-22 CN CN201910131669.7A patent/CN109665588A/en active Pending
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| RU15991U1 (en) * | 2000-07-24 | 2000-11-27 | Санкт-Петербургское государственное унитарное предприятие "Инженерный центр "Водоканал" | WATER TREATMENT PLANT |
| CN202933527U (en) * | 2012-12-19 | 2013-05-15 | 大庆高新区百世环保科技开发有限公司 | Gas-liquid backwashing oil field high-polymer wastewater filter device |
| CN203678016U (en) * | 2013-10-25 | 2014-07-02 | 中国石油天然气集团公司 | Automatic control backwash filtering device for polymer oil recovery |
| CN204569519U (en) * | 2015-04-23 | 2015-08-19 | 东北石油大学 | Poly-repelling crude oil storage tank sewage purification machinery |
| CN204939084U (en) * | 2015-09-22 | 2016-01-06 | 四川新能水处理工程有限公司 | A kind of anaerobic water distributor |
| US20190023587A1 (en) * | 2017-07-24 | 2019-01-24 | Notes Intellectual Properties, LLC | Produced water filtration |
| CN107522310A (en) * | 2017-10-16 | 2017-12-29 | 恩曼技术（北京）有限公司 | Not agent-feeding treatment oil-polluted water re-injection technique |
| CN209537036U (en) * | 2019-02-22 | 2019-10-25 | 山东广域科技有限责任公司 | Integrated crude oil wastewater efficient fine processing device |
Non-Patent Citations (1)
| Title |
|---|
| 杨作清等: "《钢铁工业水处理实用技术与应用》", 冶金工业出版社, pages: 340 - 341 * |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110143684A (en) * | 2019-05-29 | 2019-08-20 | 湖南宇宙环保工程有限公司 | A kind of three-in-one clarifier of ion air bearing |
| CN110559702A (en) * | 2019-10-10 | 2019-12-13 | 北京万诺生态科技有限公司 | Adjustable composite dynamic filtering device |
| CN110559702B (en) * | 2019-10-10 | 2024-06-07 | 北京万诺生态科技有限公司 | Adjustable compound dynamic filtering device |
| CN111960581A (en) * | 2020-09-09 | 2020-11-20 | 大庆市普罗石油科技有限公司 | Skid-mounted underground water treatment device and water treatment process |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN109665588A (en) | Integrated crude oil wastewater efficient fine processing device | |
| CN100564269C (en) | Continuous fiber agglomeration coarse-grain oil eliminator | |
| CN103100244A (en) | Multi-medium filter | |
| CN206604241U (en) | A kind of novel pressure formula mechanical filter | |
| CN209537036U (en) | Integrated crude oil wastewater efficient fine processing device | |
| CN205598762U (en) | Cut grinding fluid processing system | |
| CN202778086U (en) | Oily sewage filter and filtering method | |
| CN106946377A (en) | A kind of oil-containing process for treating waste water for car wash and equipment | |
| CN212404972U (en) | Water-saving washing and sweeping vehicle | |
| CN203620318U (en) | Fiber ball filter | |
| CN208229501U (en) | A kind of rotary drum accurate filter | |
| CN216986709U (en) | Unpowered sponge filler advanced treatment filter equipment | |
| WO2013170792A1 (en) | Oily wastewater filter and filtering method | |
| CN111302537A (en) | Car washing water circulation treatment system | |
| CN201087729Y (en) | Novel high-efficiency energy-saving oil-field flooding well washing vehicle | |
| CN207031131U (en) | More medium filter | |
| CN207760129U (en) | A kind of Self-help car washer wastewater from car washer recycling and processing equipment | |
| CN105600967B (en) | A kind of the domestic water cleaning equipment and method of suitable distributing rural households user | |
| CN201684444U (en) | Medium-speed filter | |
| CN214913677U (en) | Carwash sewage treatment plant | |
| CN206342982U (en) | One kind rotation filter pearl purifier | |
| CN206152425U (en) | Novel many filter medium filtration device | |
| CN205549707U (en) | Filtering pond is filtered to hypervelocity | |
| CN201823357U (en) | Pressure type mechanical filter | |
| CN220370588U (en) | Underground self-cleaning filtering station |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination |