CN106554133A - A kind of sewage disposal automation control system - Google Patents
A kind of sewage disposal automation control system Download PDFInfo
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- CN106554133A CN106554133A CN201611006161.7A CN201611006161A CN106554133A CN 106554133 A CN106554133 A CN 106554133A CN 201611006161 A CN201611006161 A CN 201611006161A CN 106554133 A CN106554133 A CN 106554133A
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- flocculant
- sewage
- flow
- pipeline
- delivery device
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- 239000010865 sewage Substances 0.000 title claims abstract description 83
- 238000001514 detection method Methods 0.000 claims abstract description 24
- 239000004576 sand Substances 0.000 claims abstract description 14
- 238000001914 filtration Methods 0.000 claims abstract description 13
- 230000000694 effects Effects 0.000 claims abstract description 12
- 208000014451 palmoplantar keratoderma and congenital alopecia 2 Diseases 0.000 claims abstract description 12
- 238000010079 rubber tapping Methods 0.000 claims abstract description 11
- 238000013507 mapping Methods 0.000 claims abstract description 9
- 230000007246 mechanism Effects 0.000 claims abstract description 8
- 238000004458 analytical method Methods 0.000 claims abstract description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 32
- 229920000642 polymer Polymers 0.000 claims description 5
- 238000004659 sterilization and disinfection Methods 0.000 claims description 4
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 3
- 159000000013 aluminium salts Chemical class 0.000 claims description 3
- 229910000329 aluminium sulfate Inorganic materials 0.000 claims description 3
- 150000002505 iron Chemical class 0.000 claims description 3
- RUTXIHLAWFEWGM-UHFFFAOYSA-H iron(3+) sulfate Chemical compound [Fe+3].[Fe+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O RUTXIHLAWFEWGM-UHFFFAOYSA-H 0.000 claims 1
- 229910000360 iron(III) sulfate Inorganic materials 0.000 claims 1
- 238000012545 processing Methods 0.000 abstract description 7
- 238000009825 accumulation Methods 0.000 abstract description 3
- 239000012535 impurity Substances 0.000 abstract description 3
- 238000000034 method Methods 0.000 description 18
- 230000008569 process Effects 0.000 description 7
- 230000002776 aggregation Effects 0.000 description 5
- 238000004220 aggregation Methods 0.000 description 5
- 239000000126 substance Substances 0.000 description 5
- 230000008859 change Effects 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 239000003921 oil Substances 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 241000196324 Embryophyta Species 0.000 description 2
- 229910021578 Iron(III) chloride Inorganic materials 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 239000000084 colloidal system Substances 0.000 description 2
- 230000007812 deficiency Effects 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- 239000000835 fiber Substances 0.000 description 2
- 238000005189 flocculation Methods 0.000 description 2
- 230000016615 flocculation Effects 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 230000006872 improvement Effects 0.000 description 2
- RBTARNINKXHZNM-UHFFFAOYSA-K iron trichloride Chemical compound Cl[Fe](Cl)Cl RBTARNINKXHZNM-UHFFFAOYSA-K 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 238000004062 sedimentation Methods 0.000 description 2
- 239000010802 sludge Substances 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 241001465754 Metazoa Species 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 239000005864 Sulphur Substances 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 230000003851 biochemical process Effects 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 238000009388 chemical precipitation Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000005345 coagulation Methods 0.000 description 1
- 230000015271 coagulation Effects 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 230000003311 flocculating effect Effects 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 238000002955 isolation Methods 0.000 description 1
- 229920002521 macromolecule Polymers 0.000 description 1
- 239000002480 mineral oil Substances 0.000 description 1
- 235000010446 mineral oil Nutrition 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 238000012163 sequencing technique Methods 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 238000005728 strengthening Methods 0.000 description 1
- 238000000108 ultra-filtration Methods 0.000 description 1
- 235000013311 vegetables Nutrition 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 238000004065 wastewater treatment Methods 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
- C02F9/00—Multistage treatment of water, waste water or sewage
-
- 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
- C02F1/283—Treatment of water, waste water, or sewage by sorption using coal, charred products, or inorganic mixtures containing them
-
- 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
- C02F1/30—Treatment of water, waste water, or sewage by irradiation
- C02F1/32—Treatment of water, waste water, or sewage by irradiation with ultraviolet light
-
- 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
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
- C02F1/5236—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents
-
- 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
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
- C02F1/5281—Installations for water purification using chemical agents
-
- 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
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
- C02F1/54—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using organic material
- C02F1/56—Macromolecular compounds
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/40—Liquid flow rate
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2301/00—General aspects of water treatment
- C02F2301/08—Multistage treatments, e.g. repetition of the same process step under different conditions
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
The invention discloses a kind of sewage disposal automation control system, including：Sewage draw-off pump, CASS biochemistry pools, pipe-line mixer, active sand filtering ponds, tapping equipment and flow quantity detection mechanism, the flow quantity detection mechanism include flow detector, data acquisition unit, controller, flocculant delivery device；The controller, for previously generating the mapping table of pipeline flow and flocculant volume dosed, pipeline flow is obtained according to the detection signal analysis of collection, and by control is to the corresponding flocculant volume dosed of mapping table acquisition and is calculated the required release time, and control signal is generated by the required release time；The electromagnetic valve of the flocculant delivery device is opened according to control signal so that the flocculant in flocculant delivery device is thrown to pipe-line mixer by acquired volume dosed Jing conduit.The present invention puies forward the processing speed that effectively can be lifted to the sewage in corresponding volume, effectively causes the accumulation of impurities in sewage, can realize the effect of oil removal well.
Description
Technical field
The present invention relates to a kind of sewage disposal automation control system, belongs to the technical field of sewage disposal.
Background technology
With economic development and the improvement of people's living standards, the water quality of municipal sewage also is occurring to change, in sewage
The oily substance such as vegetable and animals oils and mineral oil gradually increases.Sewage disposal, to make sewage reach a certain water body of draining or making again
With water quality requirement process which is purified.Sewage disposal be widely used in building, agricultural, traffic, the energy, petrochemical industry,
The every field such as environmental protection, urban landscape, medical treatment, food and drink, also come into the daily life of common people more and more.
Classify by sewage source, sewage disposal is generally divided into production wastewater treatment and sanitary sewage disposal.Production waste bag
Trade effluent, rural sewage and medical sewage etc. are included, and sanitary sewage is exactly the sewage that daily life is produced, and refers to various shapes
The complex mixture of the inorganic matters and Organic substance of formula, including：1st, the size solid particle for floating and suspending；2nd, gluey and gel
Diffusate；3rd, pure solution.
At present, mainly there is following three class to the research method that oil-polluted water is administered both at home and abroad：Method of chemical treatment, physical treatment
Method and biochemical treatment process.Method of chemical treatment is mainly including chemical coagulation process, chemical precipitation method, catalytic oxidation and various methods
R. concomitans；Physical treatment process includes centrifugal separation, filters and ultra-filtration method, fining process and Bubble-floating Method；Biochemical process includes life
Thing contact oxidation method, bio-disc system.
With the development of science and technology, the direct utilization of sewage is possibly realized, using sewage source heat pump system to urban original
Sewage is utilized.Such as in application number：201310049743.3 the applying date：2013-02-07 is obtained in file, is related at sewage
Reason field, and in particular to a kind of sewage-treatment plant and sewage water treatment method, wherein, sewage-treatment plant includes：At least one
Water pot, each described water pot have water inlet and outlet, and the adjacent described water pot in the plurality of water pot is by connection
Pipe is sequentially communicated；Wherein, the water outlet is provided with drainage screen, is provided with heating arrangement at the drainage screen；Described in each
Circulating line is further provided with inside water pot, one end of the circulating line is connected with the outlet, the circulating line it is another
One end is communicated at the drainage screen by nozzle, is provided with high-pressure hydraulic pump at the circulating line；Enter one at the drainage screen
Step is provided with suction nozzle and sewage draining exit, and the suction nozzle is connected with the sewage draining exit；Control system, which is with the heating arrangement and described
First dynamic structure connects respectively.The sewage-treatment plant provided by the present invention and sewage water treatment method, can be to fibre-bearing
The sewage of thing is preferably processed.
And in an other application number：201510694980.4 the applying date：In the file of 2015-10-22, it is related to one kind
Sewage-treatment plant and sewage disposal component.The sewage-treatment plant includes shell, demarcation strip, flooding tube, division board and isolation
Bar.Water inlet and discharge outlet are offered on the side wall of shell；Containing cavity is separated into demarcation strip first be connected with water inlet
Accepting groove and the second accepting groove being connected with discharge outlet, flooding tube are connected with the first accepting groove, are opened on the side wall of flooding tube
It is provided with the first apopore；Isolating bar is with division board, the demarcation strip, flooding tube jointly with the first current for being encircled into planting plants
Passage, the first water stream channel are connected with the first apopore, and isolating bar and division board, demarcation strip, shell are jointly with being encircled into kind
Plant plant the second water stream channel, wherein, sewage successively Jing water inlets, the first accepting groove, flooding tube, the first apopore, first
Water stream channel, the second apopore and the second water stream channel, and discharge from discharge outlet.Above-mentioned sewage-treatment plant has preferably net
Change efficiency and preferable clean-up effect.
Although above-mentioned document makes improvement to sewage-treatment plant so as to the sewage of fibre-bearing thing can be carried out preferably
Process, or there is preferable purification efficiency and preferable clean-up effect, but which still suffers from deficiency in force.Existing sewage
Processing system cannot be processed with carrying out sequencing to sewage, it is impossible to control the reasonable input of flocculant to the flow detection of sewage,
Aggregation property cannot be made full use of to realize treatment effect so that flocculant is thrown in.
The content of the invention
The technical problem to be solved is to overcome the deficiencies in the prior art, there is provided a kind of sewage disposal automatization
Control system, solves the reasonable input that existing sewage disposal system cannot not control flocculant to the flow detection of sewage, makes
Obtain flocculant and throw in the problem that aggregation property cannot be made full use of to realize treatment effect.
The present invention specifically employs the following technical solutions solution above-mentioned technical problem：
A kind of sewage disposal automation control system, including：Sewage draw-off pump, CASS biochemistry pools, pipe-line mixer, active sand mistake
Filter tank, tapping equipment and flow quantity detection mechanism, the flow quantity detection mechanism include flow detector, data acquisition unit, controller,
Flocculant delivery device；The sewage draw-off pump is connected to the water inlet of CASS biochemistry pools by pipeline, and CASS biochemistry pools
Outlet is connected to the water inlet of active sand filtering ponds by pipe-line mixer；The outlet of the active sand filtering ponds is by pipe
Road is connected to tapping equipment；The dispensing port of the flocculant delivery device is connected to pipe-line mixer by conduit, and throws in
On mouthful, electromagnetic valve is set；The flow detector, obtains signal for the discharge of sewage detection to pipe-line mixer；The data
Harvester, for gathering to detection signal obtained by flow detector；The controller, for previously generating pipeline flow and flocculation
The mapping table of agent volume dosed, according to collection detection signal analysis obtain pipeline flow, and by gained pipeline flow compare to
Mapping table obtains corresponding flocculant volume dosed, is calculated required release time, Yi Jiyou according to flocculant volume dosed
The required release time generates control signal；The electromagnetic valve of the flocculant delivery device is opened according to control signal so that
Flocculant in flocculant delivery device is thrown to pipe-line mixer by acquired volume dosed Jing conduit.
Further, as a preferred technical solution of the present invention：Also include ultra violet sterilizer, the ultraviolet disinfection
Device is disinfected for carrying out ultraviolet-sterilization to the sewage in tapping equipment.
Further, as a preferred technical solution of the present invention：The flocculant is to combine shape by aluminium salt and iron salt
Into polymer.
Further, as a preferred technical solution of the present invention：The polymer is poly-ferric chloride or polymerised sulphur
Sour ferrum.
Further, as a preferred technical solution of the present invention：The pipe-line mixer and active sand filtering ponds
Water inlet link position arranges seal washer.
The present invention adopts above-mentioned technical proposal, can produce following technique effect：
The sewage disposal automation control system that the present invention is provided, by being improved to traditional system, is controlled using automatization
Technology application processed is in sewage disposal process, and according to the flow detection situation of flow detection meter, controls flocculant delivery device
Interior flocculant is thrown to pipe-line mixer by acquired volume dosed Jing conduit, using the flocculant of rational proportion so as to can
Effectively to lift the processing speed to the sewage in corresponding volume, the accumulation of impurities in sewage is effectively caused, due to molecular weight greatly,
Absorption float and colloid ability are strong, and the flco size of formation is big, and sedimentation is fast, and consumption is few, and the sludge quantity for producing is few, easily de-
Water, does not have a negative impact to processing water, therefore can realize the effect of oil removal well.Existing sewage can be solved
Processing system cannot not control the reasonable input of flocculant to the flow detection of sewage so that flocculant is thrown in and cannot be made full use of
Aggregation property realizes the problem for the treatment of effect.
Description of the drawings
Fig. 1 is the module diagram of the sewage disposal automation control system of the present invention.
Specific embodiment
Embodiments of the present invention are described with reference to Figure of description.
As shown in figure 1, the present invention devises a kind of sewage disposal automation control system, including：Sewage draw-off pump, CASS
Biochemistry pool, pipe-line mixer, active sand filtering ponds, tapping equipment and flow quantity detection mechanism, the flow quantity detection mechanism include stream
Amount detector, data acquisition unit, controller, flocculant delivery device；The sewage draw-off pump is connected to CASS lifes by pipeline
Change the water inlet in pond, and the outlet of CASS biochemistry pools is connected to the water inlet of active sand filtering ponds by pipe-line mixer；Institute
The outlet for stating active sand filtering ponds is connected to tapping equipment by pipeline；The dispensing port of the flocculant delivery device is by leading
Pipe is connected to pipe-line mixer, and electromagnetic valve is arranged on dispensing port；The flow detector, for the dirt to pipe-line mixer
Discharge detection obtains signal；The data acquisition unit, for gathering to detection signal obtained by flow detector；The control
Device, for previously generating the mapping table of pipeline flow and flocculant volume dosed, is managed according to the detection signal analysis of collection
Road flow, and gained pipeline flow is compareed into flocculant volume dosed corresponding to mapping table acquisition, body is thrown according to flocculant
Product is calculated the required release time, and generates control signal by the required release time；The electricity of the flocculant delivery device
Magnet valve is opened according to control signal so that the flocculant in flocculant delivery device is thrown by acquired volume dosed Jing conduit
Put to pipe-line mixer.
Wherein, first by sewage suction CASS biochemistry pools, CASS biochemistry pools are input into after carrying out biochemical treatment sewage draw-off pump
Pipe-line mixer；Active sand filtering ponds are carrying out activated carbon adsorption and sewage treatment to sewage, are then fed into tapping equipment.System
In, the controller previously generates the mapping table of pipeline flow and flocculant volume dosed, can need to carry out according to user pre-
First configure so as to reasonable disposition flocculant can be carried out according to actual sewage situation.And when controller is thrown according to flocculant
Volume can be calculated the required release time with reference to the injected volume size of delivery device, and generate control by the required release time
Signal processed, the control signal of gained persistently can be input into electromagnetic valve, until closed electromagnetic valve after the time reaches so that flocculant
Pipe-line mixer is thrown to by acquired volume dosed Jing conduit.
In order to further improve the discharge quality of sewage, can also include ultra violet sterilizer, the purple in systems
Outer decontaminating apparatuss are disinfected for carrying out ultraviolet-sterilization to the sewage in tapping equipment, sewage can be carried out using ultraviolet
Irradiation can be directly realized by disinfective action, the function of strengthening system.
Also, the flocculant is preferably that the polymer for being formed is combined by aluminium salt and iron salt, can be caused in sewage
Contaminant surface charging neutrality, promotes organic macromolecule flocculation, greatly improves flocculating effect.Further, the polymerization
Thing is poly-ferric chloride or polyaluminum sulfate, and ferrum can realize that removing suspended solid efficiency reaches 80%, and its aggregation property causes granule
Concentrate, and effectively realize separating.
In system, in order to increase seal, can be connected with the water inlet of active sand filtering ponds in the pipe-line mixer
Position arranges seal washer, realizes tightly sealed effect using seal washer.
Further, the sewage disposal automation control system that the present invention is provided, effectively can be lifted in corresponding volume
Sewage processing speed, effectively cause the accumulation of impurities in sewage, due to molecular weight it is big, absorption float and colloid ability
By force, the flco size of formation is big, and sedimentation is fast, and consumption is few, and the sludge quantity for producing is few, is easily dehydrated, and does not produce negatively to processing water
Affect, therefore the effect of oil removal can be realized well.Existing sewage disposal system can be solved cannot not be to sewage
Flow detection control flocculant reasonable input so that flocculant throw in aggregation property cannot be made full use of to realize treatment effect
Problem.
Embodiments of the present invention are explained in detail above in conjunction with accompanying drawing, but the present invention is not limited to above-mentioned enforcement
Mode, in the ken that those of ordinary skill in the art possess, can be with the premise of without departing from present inventive concept
Make a variety of changes.
Claims (5)
1. a kind of sewage disposal automation control system, it is characterised in that include：Sewage draw-off pump, CASS biochemistry pools, pipeline are mixed
Clutch, active sand filtering ponds, tapping equipment and flow quantity detection mechanism, the flow quantity detection mechanism include flow detector, data
Harvester, controller, flocculant delivery device；The sewage draw-off pump is connected to the water inlet of CASS biochemistry pools by pipeline,
And the outlet of CASS biochemistry pools is connected to the water inlet of active sand filtering ponds by pipe-line mixer；The active sand filtering ponds
Outlet tapping equipment is connected to by pipeline；The dispensing port of the flocculant delivery device is connected to pipeline by conduit and mixes
Clutch, and electromagnetic valve is set on dispensing port；The flow detector, obtains for the discharge of sewage detection to pipe-line mixer
Signal；The data acquisition unit, for gathering to detection signal obtained by flow detector；The controller, for previously generating
The mapping table of pipeline flow and flocculant volume dosed, obtains pipeline flow according to the detection signal analysis of collection, and by gained
Pipeline flow is compareed to mapping table and obtains corresponding flocculant volume dosed, is calculated required throwing according to flocculant volume dosed
Put the time, and control signal is generated by the required release time；The electromagnetic valve of the flocculant delivery device is according to control signal
Opened so that the flocculant in flocculant delivery device is thrown to pipe-line mixer by acquired volume dosed Jing conduit.
2. sewage disposal automation control system according to claim 1, it is characterised in that：Also include ultra violet sterilizer,
The ultra violet sterilizer is disinfected for carrying out ultraviolet-sterilization to the sewage in tapping equipment.
3. sewage disposal automation control system according to claim 1, it is characterised in that：The flocculant be by aluminium salt and
Iron salt combines the polymer to be formed.
4. sewage disposal automation control system according to claim 3, it is characterised in that：The polymer is polyaluminium
Ferrum or bodied ferric sulfate.
5. sewage disposal automation control system according to claim 1, it is characterised in that：The pipe-line mixer and activity
The water inlet link position of sand filtering ponds arranges seal washer.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611006161.7A CN106554133A (en) | 2016-11-16 | 2016-11-16 | A kind of sewage disposal automation control system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611006161.7A CN106554133A (en) | 2016-11-16 | 2016-11-16 | A kind of sewage disposal automation control system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106554133A true CN106554133A (en) | 2017-04-05 |
Family
ID=58444810
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201611006161.7A Pending CN106554133A (en) | 2016-11-16 | 2016-11-16 | A kind of sewage disposal automation control system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106554133A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107827228A (en) * | 2017-11-21 | 2018-03-23 | 谢远平 | A kind of medical institutions' sewage disposal device |
| CN113354134A (en) * | 2021-05-06 | 2021-09-07 | 郭彩 | Industrial automatic control instrument system |
| CN115523855A (en) * | 2022-10-10 | 2022-12-27 | 中建安装集团有限公司 | On-line monitoring system and monitoring method for flocculated aggregates in dredging mud |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102531131A (en) * | 2012-02-15 | 2012-07-04 | 泰山医学院 | System and method for controlling adding amount of flocculant |
| CN203582660U (en) * | 2013-12-10 | 2014-05-07 | 潘志成 | Reclaimed water recycling system based on CASS (Cyclic Activated Sludge System) process |
-
2016
- 2016-11-16 CN CN201611006161.7A patent/CN106554133A/en active Pending
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102531131A (en) * | 2012-02-15 | 2012-07-04 | 泰山医学院 | System and method for controlling adding amount of flocculant |
| CN203582660U (en) * | 2013-12-10 | 2014-05-07 | 潘志成 | Reclaimed water recycling system based on CASS (Cyclic Activated Sludge System) process |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107827228A (en) * | 2017-11-21 | 2018-03-23 | 谢远平 | A kind of medical institutions' sewage disposal device |
| CN107827228B (en) * | 2017-11-21 | 2020-06-12 | 合肥市科柏盛环保科技有限公司 | Medical institution sewage treatment equipment |
| CN113354134A (en) * | 2021-05-06 | 2021-09-07 | 郭彩 | Industrial automatic control instrument system |
| CN115523855A (en) * | 2022-10-10 | 2022-12-27 | 中建安装集团有限公司 | On-line monitoring system and monitoring method for flocculated aggregates in dredging mud |
| CN115523855B (en) * | 2022-10-10 | 2023-09-22 | 中建安装集团有限公司 | Online monitoring system and method for flocculation granules of dredging slurry |
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