CN205933455U - Industrial waste water high -efficiency processing device - Google Patents
Industrial waste water high -efficiency processing device Download PDFInfo
- Publication number
- CN205933455U CN205933455U CN201620784993.0U CN201620784993U CN205933455U CN 205933455 U CN205933455 U CN 205933455U CN 201620784993 U CN201620784993 U CN 201620784993U CN 205933455 U CN205933455 U CN 205933455U
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- Prior art keywords
- depurator
- industrial wastewater
- treatment device
- efficient treatment
- wastewater high
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- 239000010842 industrial wastewater Substances 0.000 title claims abstract description 20
- 238000012545 processing Methods 0.000 title claims abstract description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 46
- 238000001914 filtration Methods 0.000 claims abstract description 22
- 238000006243 chemical reaction Methods 0.000 claims abstract description 7
- 239000010865 sewage Substances 0.000 claims description 23
- 241000256844 Apis mellifera Species 0.000 claims description 13
- 239000003814 drug Substances 0.000 claims description 12
- 238000005189 flocculation Methods 0.000 claims description 11
- 230000016615 flocculation Effects 0.000 claims description 11
- 230000001105 regulatory effect Effects 0.000 claims description 8
- 239000000701 coagulant Substances 0.000 claims description 5
- 229940079593 drug Drugs 0.000 claims description 5
- 238000001727 in vivo Methods 0.000 claims description 4
- 239000007921 spray Substances 0.000 claims 1
- 230000006641 stabilisation Effects 0.000 claims 1
- 238000011105 stabilization Methods 0.000 claims 1
- 238000003756 stirring Methods 0.000 claims 1
- 238000000034 method Methods 0.000 abstract description 19
- 230000008569 process Effects 0.000 abstract description 16
- 239000010802 sludge Substances 0.000 abstract description 13
- 230000005484 gravity Effects 0.000 abstract description 9
- 238000005119 centrifugation Methods 0.000 abstract description 4
- 238000000926 separation method Methods 0.000 abstract description 4
- 238000013461 design Methods 0.000 abstract description 3
- 238000004891 communication Methods 0.000 abstract 1
- 230000010354 integration Effects 0.000 abstract 1
- 230000008719 thickening Effects 0.000 abstract 1
- 239000002245 particle Substances 0.000 description 13
- 230000006872 improvement Effects 0.000 description 11
- 238000009833 condensation Methods 0.000 description 10
- 230000005494 condensation Effects 0.000 description 10
- 238000004062 sedimentation Methods 0.000 description 9
- 239000002351 wastewater Substances 0.000 description 8
- 230000008901 benefit Effects 0.000 description 7
- 230000001112 coagulating effect Effects 0.000 description 7
- 230000006835 compression Effects 0.000 description 6
- 238000007906 compression Methods 0.000 description 6
- 230000007246 mechanism Effects 0.000 description 6
- 239000008187 granular material Substances 0.000 description 5
- 238000001179 sorption measurement Methods 0.000 description 5
- 230000000694 effects Effects 0.000 description 4
- 238000010521 absorption reaction Methods 0.000 description 3
- 238000011001 backwashing Methods 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 239000013618 particulate matter Substances 0.000 description 3
- 238000001556 precipitation Methods 0.000 description 3
- 230000003068 static effect Effects 0.000 description 3
- 230000009471 action Effects 0.000 description 2
- 230000010062 adhesion mechanism Effects 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000000706 filtrate Substances 0.000 description 2
- 238000013508 migration Methods 0.000 description 2
- 230000005012 migration Effects 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 241000894007 species Species 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- 230000002745 absorbent Effects 0.000 description 1
- 239000002250 absorbent Substances 0.000 description 1
- 239000007900 aqueous suspension Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000003139 buffering effect Effects 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000003340 mental effect Effects 0.000 description 1
- 238000005272 metallurgy Methods 0.000 description 1
- 230000000116 mitigating effect Effects 0.000 description 1
- 239000008213 purified water Substances 0.000 description 1
- 230000003134 recirculating effect Effects 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000004148 unit process Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Landscapes
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
The utility model discloses an industrial waste water high -efficiency processing device, a serial communication port, processing system includes the equalizing basin, the subassembly that dispenses, clarifier, sludge impoundment and clean water basin, the equalizing basin is through pipe connection purifier water inlet, the sludge impoundment passes through pipe connection clarifier drain, the clean water basin passes through the delivery port of pipe connection clarifier. Whole structural design is ingenious, compact, has improved work efficiency, 2) this technical scheme will thoughtlessly congeal the reaction, and five process organic integrations such as centrifugation, gravity separation, filtration and sludge thickening are as an organic whole, same jar of internal completion, realize online quick continuous efficient handling of.
Description
Technical field
This utility model is related to a kind of processing meanss and in particular to a kind of industrial wastewater high-efficient treatment device, belongs to and uphangs
Float, high-turbidity industrial wastewater processing equipment technical field.
Background technology
With the quickening of industrial development and urbanization process, the waste water producing in commercial production gets more and more, and gradually
Become the one of the main reasons of pollution urban environment, the general traditional handicraft of industrial wastewater adopts Multistage settling, also adopts dosing
The method of coagulating sedimentation or tube settling is processed, but floor space is big, and the sedimentation time is long, and swash plate, inclined tube easily block, and mud is aqueous
Rate is high, and operation runs difficulty, goes out aqueous suspension Chang Chaobiao after process, also has and is processed using pneumatically supported method, due to complex process,
Gas-water ratio flows back, is more difficult to control than dosing, and release easily blocks, and effluent quality is unstable, often cannot reuse.Cause
This, a kind of new scheme of exigence solves this technical problem.
Content of the invention
This utility model is exactly directed to technical problem present in prior art, provides a kind of industrial wastewater efficient process dress
Put, this technical scheme overall construction design is ingenious, flexibility and reliability, process high suspended matter, high concentrtion Industry Waste dedicated for collecting
Such waste water itself can quickly processed up to standard and discharge, be suitable for machinery, chemical industry, electric power, metallurgy by water treatment facilities in vivo
Application etc. industry.
In order to solve technical problem present in prior art, the technical solution of the utility model is as follows：Industrial wastewater is high
Effect processing meanss are it is characterised in that described processing system includes regulating reservoir, drug dispensing component, depurator, sludge-tank and clear water
Pond, described regulating reservoir connects depurator water inlet through piping, and described sludge-tank connects depurator sewage draining exit by pipeline, described
Clear water reserviors connect the outlet of depurator by pipeline, and described depurator includes depurator body, described depurator originally in vivo from
Top to bottm it is disposed with clear water zone, filtering area, decanting zone, flocculation reaction area and enrichment region, described depurator body sets
It is equipped with manhole, outlet and steam vent, the side of described depurator body is provided with water inlet.Can be right in this technical scheme
Sewage carries out the processes such as coagulating, centrifugation, Gravity Separation, dynamic filtration and sludge condensation, by these processing procedures
Organically combined, whole equipment small volume, disposal ability is big, process route end, high treating effect, reached real quick online
The purpose that continuous high-efficient is processed.
As a kind of improvement of the present utility model, in described enrichment region, include playpipe, mud dredging pipe and circular cone
Shape bucket part, the side of described cone bucket part is provided with sewage draining exit.After larger particles enter sludge condensation area, in centrifugal force and quiet
Mud Fast Compression is made to precipitate in the presence of pressure, moisture content is generally individually smaller than 95%, and regularly or continuously drains into mudpan.
Mud is continuous or timing gap spoil disposal depends primarily on into water SS concentration, when general SS is more than 3000mg/l, for continuous spoil disposal, little
It is timing spoil disposal when 3000mg/l.
As a kind of improvement of the present utility model, described flocculation reaction area includes spoiler, separator, blender and cone
Shape baffle plate, what described spoiler was symmetrical is arranged on the both sides of blender, the described conical baffled underface being arranged on separator.Dirty
Water is evacuated to cushion region in depurator through sewage pump, is also sucked inorganic medicament in the lump using the principle of negative pressure of pump simultaneously,
Organic medicament is added, adding of agent species and quantity are determined by quality test of water, are quickly mixed by pipeline, and entrance sets after pump
After high-speed rotation, medicinal liquid and sewage mix again for standby inside, in compression double electric layer, absorption charge neutrality, adsorption bridging, precipitation
Catch etc. under coagulating mechanism with net, gradually form alumen ustum, and constantly increase and quickly form larger floc sedimentation, gravity and from
Under mental power function, larger particles are precipitated to sludge condensation area, and smaller particle is blocked in baffle plate 8, to outlet in the presence of negative pressure
Move in direction.
As a kind of improvement of the present utility model, described decanting zone includes honeybee pipe, upper bracket and lower carriage, and described honeybee pipe sets
Put in the middle of upper bracket and lower carriage, described carrier parts are used for fixing honeybee pipe；Sewage after initial concentration is in decanting zone
Coagulate again in the presence of honeybee pipe and close, the floc sedimentation of larger particles enters enrichment region, under gravity containing smaller particle
Sewage enters filtering area.
As a kind of improvement of the present utility model, described filtering area is provided with stabilier, and sewage is in the presence of stabilier
Filtered again, equipment filtering area employs special filtrate, be characterized in surface adsorption, filter capacity is big, high precision is retained
Thing is easy to fall off, and its operation principle is by migration mechanism it is achieved that dynamic filtration, adhesion mechanism and the mechanism that comes off, by special knot
Structure is realizing.When waste water is through filter layer, the particulate matter overwhelming majority more than 5 μm for the particle diameter is trapped it is ensured that water outlet
Water quality.
As a kind of improvement of the present utility model, described clear water zone is provided with porous plate, and water after filtering is through clear water zone
Clear water reserviors are drained into by outlet, for reuse or outer row, described depurator body is arranged with supporting leg.
As a kind of improvement of the present utility model, described drug dispensing component includes agitator A, medicine-chest A and agitator B, medicine
It is provided with flocculation aid in case B, wherein agitator A, in agitator B, is provided with coagulant, described medicine-chest A is delivered to by dosing pump
Depurator is originally internal, and described medicine-chest B is delivered to depurator body by the intake pump on pipeline.
With respect to prior art, advantage of the present utility model is as follows：1）Total design is ingenious, compact, improves work
Make efficiency, 2）, by coagulating, five processes such as centrifugation, Gravity Separation, filtration and sludge condensation are organic for this technical scheme
Combine together, complete in same tank body, realize online quick continuous high-efficient and process；3）This technical scheme treatment effeciency
Height, the purification of waste water time needs 20-30 minute for unusual according to water quality, and purified water can reuse；4）This technical scheme takes up an area face
Amass little, only the 1/6 of traditional handicraft, separate unit processes 100m3The equipment of/h waste water, floor space is only 9m2；5）This technical scheme
Sludge condensation is fast, and mud discharging moisture content is less than 95%, and power consumption is low, and operating cost is few, only need to once be lifted in operation, place
The medicament expense of reason waste water is 0.06-0.20 unit/T water；Process route is short, stable and reliable operation, manages easy to operate, maintenance capacity
Little；6）This technical scheme backwash is convenient, and backwashing water can use clear water water, processes due to employing special process, backwash
Cycle, up to 3-4 month once each backwashing time was only 3-5 minute, and backwashing pump can be by intake pump dual-purpose；7）This technology
Formula investing expense is low, and the suitability is wide, is applicable not only to high suspended matter, high-turbidity water is processed, and is simultaneously suitable for rainwater, river
Purify and Industrial Recirculating Cooling Water treatment for reuse, be also applied for the system for advanced treatment and recycle with industrial wastewater of living, be easy to big
The popularization and application of scale.
Brief description
Fig. 1 is this utility model overall structure diagram；
Fig. 2 is depurator structural representation；
In figure：1st, porous plate, 2, stabilier, 3, honeybee pipe, 4, support, 5, spoiler, 6, separator, 7, blender, 8, gear
Plate, 9, playpipe, 10, mud dredging pipe, 11, supporting leg, 12, conical bucket part, 13, depurator body, 14, water inlet, 15, go out
The mouth of a river, 16, sewage draining exit, 17, air vent, 18, overfall, 19, manhole, 20, clear water reserviors, 21, sludge-tank, 22, regulating reservoir, 23,
Pressure gauge, 24, intake pump, 25, dosing pump, 26, recoil pump, 27, agitator A, 28, medicine-chest A, 29, agitator B, 30, medicine-chest B.
Specific embodiment
In order to deepen to be appreciated and understood by of the present utility model, with reference to the accompanying drawings and detailed description, it is situated between further
Continue this utility model.
Embodiment 1：
Referring to Fig. 1, Fig. 2, a kind of industrial wastewater high-efficient treatment device, described processing system includes regulating reservoir 22, group of making up a prescription
Part, depurator, sludge-tank 21 and clear water reserviors 20, described regulating reservoir 22 connects depurator water inlet, described mud through piping
Pond 21 connects depurator sewage draining exit by pipeline, and described clear water reserviors 20 connect the outlet of depurator, described purification by pipeline
Device includes depurator body 13, be disposed with from top to bottom in described depurator body 13 clear water zone, filtering area, decanting zone,
Flocculation reaction area and enrichment region, described depurator body 13 is provided with manhole 19, outlet 15 and steam vent 17, described
The side of depurator body 13 is provided with water inlet 14, and described depurator body 13 is arranged with supporting leg 11.In this technical scheme
The processes such as coagulating, centrifugation, Gravity Separation, dynamic filtration and sludge condensation can be carried out to sewage, at these
Reason process is organically combined, whole equipment small volume, and disposal ability is big, process route end, high treating effect, reaches online
The purpose that real quick continuous high-efficient is processed.
Embodiment 2：
Referring to Fig. 1, Fig. 2, as a kind of improvement of the present utility model, in described enrichment region, include playpipe 9, mud is dredged
Siphunculus 10 and conical bucket part 12, the side of described cone bucket part is provided with sewage draining exit 16.It is dense that larger particles enter mud
Behind contracting area, so that mud Fast Compression is precipitated in the presence of centrifugal force and static pressure, moisture content is generally individually smaller than 95%, and timing or
Continuously drain into mudpan.Mud is continuous or timing gap spoil disposal depends primarily on into water SS concentration, and general SS is more than
During 3000mg/l, for continuous spoil disposal, less than being timing spoil disposal during 3000mg/l.Remaining structure and advantage complete phase with embodiment 1
With.
Embodiment 3：
Referring to Fig. 1, Fig. 2, as a kind of improvement of the present utility model, described flocculation reaction area includes spoiler 5, separator
6th, blender 7 and conical baffled 8, the symmetrical both sides being arranged on blender of described spoiler 5, described conical baffled 8 settings
In the underface of separator 6, sewage is evacuated to cushion region in depurator through sewage pump, and the principle of negative pressure simultaneously also utilizing pump will
Inorganic medicament sucks in the lump, adds organic medicament, adding of agent species and quantity are determined by quality test of water, by pipeline after pump
Quickly mixed, after high-speed rotation, medicinal liquid and sewage mix again, in compression double electric layer, absorption for access arrangement inside
Charge neutrality, adsorption bridging, precipitation and net are caught etc. under coagulating mechanism, gradually form alumen ustum, and constantly increase quick shape
Become larger floc sedimentation, larger particles are precipitated to sludge condensation area under gravity and centrifugal action, smaller particle is blocked in baffle plate 8,
Move to outlet direction in the presence of negative pressure.Remaining structure is identical with embodiment 1 with advantage.
Embodiment 4：
Referring to Fig. 1, Fig. 2, as a kind of improvement of the present utility model, described decanting zone includes honeybee pipe 3, upper bracket and lower
Frame, described honeybee pipe is arranged in the middle of upper bracket and lower carriage, and described carrier parts are used for fixing honeybee pipe 3；After initial concentration
Sewage coagulate again in the presence of honeybee pipe in decanting zone and close, the floc sedimentation of larger particles enters enrichment region under gravity,
Sewage containing smaller particle enters filtering area.Remaining structure is identical with embodiment 1 with advantage.
Embodiment 5：
Referring to Fig. 1, Fig. 2, as a kind of improvement of the present utility model, described filtering area is provided with stabilier 2, and sewage is steady
Filtered again in the presence of stream plate 2, equipment filtering area employs special filtrate, is characterized in surface adsorption, filter capacity
Greatly, high precision trapped substance easy to fall off it is achieved that dynamic filtration, its operation principle is by migration mechanism, adhesion mechanism and shedding machine
Reason, is realized by special construction.When waste water is through filter layer, the particulate matter overwhelming majority more than 5 μm for the particle diameter is cut
Stay it is ensured that effluent quality.Remaining structure is identical with embodiment 1 with advantage.
Embodiment 6：
Referring to Fig. 1, Fig. 2, as a kind of improvement of the present utility model, described clear water zone is provided with porous plate 1, after filtering
Water through clear water zone, clear water reserviors are drained into by outlet 15, for reuse or outer arrange.Remaining structure and advantage complete phase with embodiment 1
With.
Embodiment 7：
Referring to Fig. 1, Fig. 2, described drug dispensing component includes agitator A27, medicine-chest A28 and agitator B29, medicine-chest B30, its
It is provided with flocculation aid in middle agitator A, in agitator B, is provided with coagulant, described medicine-chest A is delivered to depurator by dosing pump
This is internal, and described medicine-chest B is delivered to depurator body by the intake pump on pipeline.Remaining structure and advantage are complete with embodiment 1
Exactly the same.
Operation principle：Referring to shown in Fig. 1 Fig. 2, industrial wastewater initially enters regulating reservoir 22 and carries out a certain degree of buffering,
Then, through piping, this is internal to be delivered to depurator under the pressure of intake pump 24, and the flocculation aid in medicine-chest A passes through simultaneously for waste water
Dosing pump 25 is delivered to depurator entrance, and coagulant is delivered in depurator by medicine-chest B by intake pump, coagulant and flocculation aid
Quickly mixed by pipeline with industrial wastewater, entered in the depurator internal mitigation phase 7 after high-speed rotation, medicinal liquid with
Sewage mixes again, under compression double electric layer, absorption charge neutrality, adsorption bridging, precipitation and net such as catch at the coagulating mechanism,
Gradually form alumen ustum, and constantly increase the quickly larger floc sedimentation of formation, the granule with diameter greater than 70 μm is in gravity and centrifugal action
Under be precipitated to sludge condensation area, be less than 70 μm of granule in sewage and colloidal solid gradually form floc sedimentation in the presence of medicament,
And move toward outlet direction, reach when decanting zone, in the presence of honeybee pipe 18, floc sedimentation is gradually increased, certain when increasing to
During degree, sink rapidly in the presence of lower spin and centrifugal force, the speed of sinking is far longer than the subsidence velocity of static state, granule
Sink down into sludge condensation area, the less granule of diameter continues to move toward outlet direction, when sewage reaches filtering area, in filtering area
In the presence of absorbent filter medium, the particulate matter overwhelming majority more than 5 μm for the particle diameter is trapped it is ensured that effluent quality, after filtering
Water through clear water zone, clear water reserviors 20 are drained into by outlet pipe, for reuse or outer arrange, after a period of time, need by recoil pump
The 26 pairs of filtering areas carry out backwash it is ensured that filter effect；After granule enters sludge condensation area, in the presence of centrifugal force and static pressure
Mud Fast Compression is made to precipitate, moisture content is generally individually smaller than 95%, in time mud is drained into sludge-tank 21.
This utility model can also be by 1 group of at least one of technical characteristic described in embodiment 2,3,4,5,6 and embodiment
Close, form new embodiment.
It should be noted that above-described embodiment is only preferred embodiment of the present utility model, it is not used for limiting this practicality
New protection domain, protection domain of the present utility model is defined by claims.
Claims (8)
1. industrial wastewater high-efficient treatment device it is characterised in that described processing system include regulating reservoir, drug dispensing component, depurator,
Sludge-tank and clear water reserviors, described regulating reservoir connects depurator water inlet through piping, and described sludge-tank is connected net by pipeline
Change device sewage draining exit, described clear water reserviors connect the outlet of depurator by pipeline, and described depurator includes depurator body, described
Depurator is originally disposed with clear water zone, filtering area, decanting zone, flocculation reaction area and enrichment region in vivo from top to bottom, described
Manhole, outlet and steam vent are provided with depurator body, the side of described depurator body is provided with water inlet.
2. industrial wastewater high-efficient treatment device according to claim 1 is it is characterised in that include spray in described enrichment region
Penetrate pipe, mud dredging pipe and conical bucket part, the side of described cone bucket part is provided with sewage draining exit.
3. industrial wastewater high-efficient treatment device according to claim 2 is it is characterised in that described flocculation reaction area includes hindering
Stream plate, separator, blender and conical baffled, what described spoiler was symmetrical is arranged on the both sides of blender, described taper gear
Plate is arranged on the underface of separator.
4. the industrial wastewater high-efficient treatment device according to Claims 2 or 3 is it is characterised in that described decanting zone includes honeybee
Pipe, upper bracket and lower carriage, described honeybee pipe is arranged in the middle of upper bracket and lower carriage, and described carrier parts are used for fixing honeybee pipe.
5. industrial wastewater high-efficient treatment device according to claim 4 is it is characterised in that described filtering area is provided with current stabilization
Plate.
6. industrial wastewater high-efficient treatment device according to claim 5 is it is characterised in that described clear water zone is provided with porous
Plate.
7. industrial wastewater high-efficient treatment device according to claim 6 is it is characterised in that arrange under described depurator body
There is supporting leg.
8. industrial wastewater high-efficient treatment device according to claim 7 is it is characterised in that described drug dispensing component includes stirring
Bucket A, medicine-chest A and agitator B, medicine-chest B, are provided with flocculation aid, are provided with coagulant, institute in agitator B in wherein agitator A
State medicine-chest A and depurator is delivered to originally in vivo by dosing pump, described medicine-chest B is delivered to depurator originally by the intake pump on pipeline
Body.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2015207976378 | 2015-10-16 | ||
| CN201520797637 | 2015-10-16 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205933455U true CN205933455U (en) | 2017-02-08 |
Family
ID=57926946
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620784993.0U Expired - Fee Related CN205933455U (en) | 2015-10-16 | 2016-07-25 | Industrial waste water high -efficiency processing device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205933455U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109650596A (en) * | 2019-01-28 | 2019-04-19 | 江苏融汇环境工程有限公司 | High efficiency water purification system |
| CN111890146A (en) * | 2020-07-16 | 2020-11-06 | 徐州徐工液压件有限公司 | Grinding fluid automatic circulation and physical and chemical precipitation filter pressing purification device for centerless grinding machine |
| CN115215485A (en) * | 2022-08-11 | 2022-10-21 | 北京市生态环境保护科学研究院 | High-speed solid-liquid separation integrated device |
-
2016
- 2016-07-25 CN CN201620784993.0U patent/CN205933455U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109650596A (en) * | 2019-01-28 | 2019-04-19 | 江苏融汇环境工程有限公司 | High efficiency water purification system |
| CN111890146A (en) * | 2020-07-16 | 2020-11-06 | 徐州徐工液压件有限公司 | Grinding fluid automatic circulation and physical and chemical precipitation filter pressing purification device for centerless grinding machine |
| CN115215485A (en) * | 2022-08-11 | 2022-10-21 | 北京市生态环境保护科学研究院 | High-speed solid-liquid separation integrated device |
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| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170208 |