CN205892904U - A integration equipment for automaticallying process sewage - Google Patents
A integration equipment for automaticallying process sewage Download PDFInfo
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- CN205892904U CN205892904U CN201620714073.1U CN201620714073U CN205892904U CN 205892904 U CN205892904 U CN 205892904U CN 201620714073 U CN201620714073 U CN 201620714073U CN 205892904 U CN205892904 U CN 205892904U
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Abstract
A integration equipment for automaticallying process sewage, relates to the field of sewage treatment technology, it includes air supporting oil removal unit, ultrafiltration unit, receive and strain unit and water purification case (20), air supporting oil removal unit is by stealthily defiling pump (1), air supporting oil interceptor (2) and aerator (3) are constituteed, stealthily dirty pump (1) communicates with each other through the sewage entry of pipeline with air supporting oil interceptor (2), install in air supporting oil interceptor (2) bottom aerator (3), the water export that ultrafiltration unit's water inlet passes through pump and pipeline and air supporting oil interceptor (2) communicates with each other, the water inlet of straining the unit water export through pump and pipeline and ultrafiltration unit of receiving communicates with each other, the water inlet of water purification case (20) communicates with each other through pump and pipeline and the delivery port of straining the unit of receiving. The utility model has the advantages of product water good quality is good, area is little, sewage zero release treatment effeciency high, goes out water quality of water and reaches water standard from the beginning.
Description
Technical field
The utility model is related to technical field of sewage and in particular to being used for automatically processing the integration apparatus of sewage.
Background technology
At present, the environmental protection pressure of the shortage of water resource and blowdown, governs the development of China's economic society.Therefore, each work
Industry enterprise, municipal sewage plant etc. are numerous and confused to be attempted proceeding by advanced treatment of wastewater and Treated sewage reusing, to realize sewage recycling profit
With, more preferable environmental protection, solve water problems.For Treated sewage reusing, the basic basis of consideration first are the uses of reuse
Place.Industrial enterprise is included with water occasion: recirculated cooling water, boiler water, process water, flushing water etc..Municipal water use is mainly wrapped
Include: drinking water, greening water, landscape water etc..These typically all comprise two main, comprehensive fingers with water water standard
Mark: turbidity/suspended solid (ss), salt content (tds).
It is divided into two steps: 1) turbidity removal, removal suspended particulate: ultrafiltration using the process that embrane method technology of middle water recycle mainly includes
Film, microfiltration membranes, by biological floe remaining for sewage disposal,
Mushroom etc. retains, and uses clarification of water, can reach reuse or further treatment for reuse.Membrane technology bag for turbidity removal
Include: hollow fiber ultrafiltration membrane, membrane bioreactor (mbr) etc..2) desalination: reverse osmosis membrane ro or nanofiltration nf, by going out of clarification
Water carries out film desalination, is divided into two bursts of concentrated waters (discharge) and fresh water (reuse).
Advanced treating to general biochemistry secondary clarifier effluent, the most frequently used process step is exactly to filter, and makes secondary clarifier effluent
Biological floe and colloidal substance can be trapped in above filtrate, reduce the ss of water outlet and turbidity.Advanced treating to waste water, warp
Filter frequently with sand filtration and activated carbon.Sand filtration as be mainly used in remove ss, colloidal substance, and activated carbon may filter that absorption organic
Thing, heavy metal classes, oxidizing substance.There is fluctuation during for water outlet ss, longtime running can be stablized for ensureing to filter, water inlet can be increased
If measures such as coagulating sedimentation, to extend the recoil cycle of filter.Through filtration water outlet ss can be reduced to < 5mg/l, absolutely mostly
The big particle diameter colloidal solid of number also can remove, but to less than 0.1um particles below, still part exists.Therefore, it is necessary to
Carry out pre-filtering to before ro film.The filtration particle diameter of hollow-fibre membrane ultrafiltration is 0.01um to 0.2um, passes through doughnut in principle
The delivery turbidity of film ultrafiltration is 0, and the bacterium in trap water simultaneously prevents the germ contamination of rear class film.And the rate of recovery of system is high,
More than 90% can be reached.Therefore hollow-fibre membrane ultrafiltration, is a good pretreatment.
The property of kitchen waste water pollutant, to analyze, is characterized in waste water containing substantial amounts of grease, colloidal particle and hangs
Float, main component is animal and plant fat, inorganic salinity, surfactant, protein and amino acid etc..The process of such waste water
Method has Physical, chemical method, physico-chemical process, bioanalysis and biochemical process etc..It is analyzed as follows for this method of wastewater treatment:
1st, gravitational separation process, to the clearance of suspended things, oil slick and dispersed oil more than 60%, treatment effect is stable, running cost
With low, treating capacity is big, but system footprint area is big, and the sedimentation time is long.
2nd, centrifugal separation, to the clearance of suspended things, oil slick and dispersed oil more than 60%, process time is short, and effect
Good, but operating cost is high, and energy consumption is big.
3rd, filtration method, to the clearance of suspended things, dispersed oil and oil emulsion more than 10%, water quality is good, and equipment investment is few, no
Scum silica frost；It is big that filter bed will rinse water consumption repeatedly.
4th, absorption method, to suspended things, dissolved oil clearance 10% about, water quality is good, and equipment takes up an area few；But equipment is thrown
Money is high, and adsorbent reactivation is difficult.
5th, Bubble-floating Method, is more than 10% to the clearance of suspended things, oil emulsion and dispersed oil, effect is good, technical maturity.
6th, coagulant sedimentation, is more than 10% to the clearance of suspended things, oil emulsion, high treating effect；But take up an area big, medicament
Consumption is big, and mud is difficult.
Utility model content
The purpose of this utility model is exactly to solve above-mentioned technical problem, and provides the one for automatically processing sewage
Change equipment.
The utility model includes air supporting oil removal unit, ultra filtration unit, nano-filtration unit and clear water tanks, and air supporting oil removal unit is by diving
Dirty pump, air supporting oil interceptor and aerator composition, submersible sewage pump is communicated with the sewage inlet of air supporting oil interceptor by pipeline, and aerator is pacified
It is contained in air supporting oil interceptor bottom, the water inlet of ultra filtration unit is communicated with the water out of air supporting oil interceptor by pump and pipeline, nanofiltration
The water inlet of unit is communicated with the water out of ultra filtration unit by pump and pipeline, and the water inlet of clear water tanks passes through pump and pipeline and receives
The delivery port of filter unit communicates.
Ultra filtration unit is produced water tank by ultrafiltration raw water box, ultrafiltration booster pump, ultrafiltration apparatus and ultrafiltration and is formed, ultrafiltration raw water box
Water inlet is communicated with the water out of air supporting oil interceptor by pump and pipeline, and ultrafiltration apparatus pass through ultrafiltration booster pump and pipeline and ultrafiltration
The delivery port of raw water box communicates, and the water inlet that water tank is produced in ultrafiltration is communicated with the delivery port of ultrafiltration apparatus 6 by pipeline.
Nano-filtration unit is produced water tank by nanofiltration booster pump, nanofiltration device and nanofiltration and is formed, and the water inlet of nanofiltration device passes through to receive
Filter booster pump and pipeline are communicated with the delivery port of ultrafiltration product water tank, and the water inlet that water tank is produced in nanofiltration passes through pipeline and nanofiltration device
Delivery port communicates.
Ultra filtration unit also has hyperfiltration reverse-rinsing pump, the water inlet of hyperfiltration reverse-rinsing pump and delivery port to produce water tank respectively with ultrafiltration and surpass
Filter device communicates, and hyperfiltration reverse-rinsing pump is used for cleaning the milipore filter of ultrafiltration apparatus.
Nano-filtration unit also has nanofiltration medicine to wash pump, nanofiltration medicine wash pump and water inlet and delivery port respectively with nanofiltration produce water tank and
Nanofiltration device communicates, and nanofiltration medicine washes pump for cleaning the NF membrane of nanofiltration device 9.
The utility model has the advantage that
1. use membrane technology, producing water water quality is excellent, meet more, higher water demand；
2. floor space is little, sewage zero-discharge.
3. treatment effeciency is high, and effluent quality reaches water quality standard from the beginning.
4. operating cost is low, high degree of automation.
5. continuously run, stable effluent quality.Produce ultra-pure water yield and can be up to 95%.
6. acid-alkali regeneration need not be used, will not shut down because of regeneration.
7. save recoil and water for cleaning.
8. no regenerated sewage, is not necessary to sewage treatment facility, transports facility without soda acid deposit and soda acid dilution.
9. safe and reliable, it is to avoid worker exposure's soda acid.
10. reduce workshop construction area, low operation and maintenance cost, installation are simply, easy to maintenance.
Brief description
Fig. 1 is the utility model process flow diagram.
In figure: 1, submersible sewage pump；2nd, air supporting oil interceptor；3rd, aerator；4th, ultrafiltration raw water box；5th, ultrafiltration booster pump；6th, ultrafiltration
Device；7th, water tank is produced in ultrafiltration；8th, nanofiltration booster pump；9th, nanofiltration device；10th, water tank is produced in nanofiltration；11st, hyperfiltration reverse-rinsing pump；12nd, nanofiltration
Pump washed by medicine；20th, clear water tanks.
Specific embodiment
Below in conjunction with the accompanying drawings the utility model is described further.
As shown in figure 1, the utility model includes air supporting oil removal unit, ultra filtration unit, nano-filtration unit and clear water tanks 20, air supporting
Oil removal unit is made up of submersible sewage pump 1, air supporting oil interceptor 2 and aerator 3, and submersible sewage pump 1 passes through the sewage of pipeline and air supporting oil interceptor 2
Entrance communicates, and aerator 3 is arranged on air supporting oil interceptor 2 bottom, and the water inlet of ultra filtration unit passes through pump and pipeline and air supporting oil removal
The water out in pond 2 communicates, and the water inlet of nano-filtration unit is communicated with the water out of ultra filtration unit by pump and pipeline, clear water tanks 20
Water inlet is communicated with the delivery port of nano-filtration unit by pump and pipeline.
Ultra filtration unit is produced water tank 7 by ultrafiltration raw water box 4, ultrafiltration booster pump 5, ultrafiltration apparatus 6 and ultrafiltration and is formed, ultrafiltration raw water
The water inlet of case 4 is communicated with the water out of air supporting oil interceptor 2 by pump and pipeline, and ultrafiltration apparatus 6 pass through ultrafiltration booster pump 5 and pipe
Road is communicated with the delivery port of ultrafiltration raw water box 4, and the delivery port phase by pipeline and ultrafiltration apparatus 6 for the water inlet of water tank 7 is produced in ultrafiltration
Logical.
Nano-filtration unit is produced water tank 10 by nanofiltration booster pump 8, nanofiltration device 9 and nanofiltration and is formed, and the water inlet of nanofiltration device 9 leads to
The delivery port crossing nanofiltration booster pump 8 and pipeline with ultrafiltration product water tank 7 communicates, and the water inlet that water tank 10 is produced in nanofiltration passes through pipeline and receives
The delivery port of filter device 9 communicates.
Ultra filtration unit also has hyperfiltration reverse-rinsing pump 11, the water inlet of hyperfiltration reverse-rinsing pump 11 and delivery port to produce water tank with ultrafiltration respectively
7 and ultrafiltration apparatus 6 communicate, hyperfiltration reverse-rinsing pump 11 is used for cleaning the milipore filter of ultrafiltration apparatus 6.
Nano-filtration unit also has nanofiltration medicine to wash pump 12, nanofiltration medicine wash pump 12 and water inlet and delivery port respectively with nanofiltration produce water
Case 10 and nanofiltration device 9 communicate, and nanofiltration medicine washes pump 12 for cleaning the NF membrane of nanofiltration device 9.
Working method principle: sewage is pumped into air supporting oil interceptor 2 by submersible sewage pump 1, air supporting oil interceptor 2 adopts oil interceptor and air supporting
The mode that technology combines, pneumatically supported effect is to be sufficiently mixed, contact with oil or impurity in water with the microbubble group of a constant volume
And adhere to, to reach and to separate with water.Oil interceptor then be separate waste water in oil slick or scum silica frost and silt, it using oil in water it
Between density variation carry out water-oil separating, be also with floating method remove waste water in relative density be less than 1 oil slick or scum silica frost.
After oil removing, the sewage pump excess of imports of deoiling is filtered the ultrafiltration raw water box 4 of unit, then be passed through ultrafiltration after the supercharging of ultrafiltration booster pump 5
Device 6, ultrafiltration is mainly Ultra filtration membrane process, is a kind of sieve aperture separation process related to membrane aperture size, with film both sides
Pressure differential be driving force, with milipore filter as filter medium, that is, certain pressure effect under, when containing large and small molecule solute
When mixed solution flows through film surface, solvent and small molecule solute (as inorganic salts) will transmit through film.Macromolecular solute is then due to body
Amass more than membrane aperture and be rejected by, be recovered as concentrate.Thus realize the purification to stoste, the mesh separating and concentrating
's.Filter membrane between 0.002-0.1 μm for the pore size filter of ultrafiltration is referred to as milipore filter, and general colloidal volume all >=0.1 μm,
Latex >=0.5 μm, the bacterium such as coliform, staphylococcus volume >=0.2 μm, suspension, particulate equal-volume >=5 μm, therefore super
Filter membrane can filter out the macromolecular substances such as bacterium in solution, colloid, suspension, protein.Filtration through ultrafiltration apparatus 6
After pump into ultrafiltration produce water tank 7, hyperfiltration reverse-rinsing pump 11 using ultrafiltration produce water tank 7 water milipore filter is backwashed, ultrafiltration produce water
The water of case 7 passes through the nanofiltration device 9 that nanofiltration booster pump 8 supercharging pumps into nano-filtration unit, and nanofiltration is that one kind passes through (half by means of selection
Through) skill of property film can membrane separation technique with pressure as motive force, ooze into the aqueous solution when added pressure in system is more than
When thoroughly pressing, hydrone constantly passes through film, flows into central tube through producing water flow passage, then the impurity in outflow water at one end, such as
Hardness ions, organic matter, bacterium, virus etc., are trapped within the influent side of film, then flow out in concentrated water water side, thus reaching
Isolation of purified purpose, the sewage after nanofiltration device 9 filters reaches setting water standard, is pumped into clear water tanks 20 for using.
Embodiment of above is merely to illustrate the utility model, and is not limitation of the utility model, relevant technology neck
The those of ordinary skill in domain, in the case of without departing from spirit and scope of the present utility model, can also make a variety of changes and
Modification, therefore all equivalent.Technical scheme fall within category of the present utility model, scope of patent protection of the present utility model should
It is defined by the claims.
Claims (5)
1. it is used for automatically processing the integration apparatus of sewage it is characterised in that it includes air supporting oil removal unit, ultra filtration unit, nanofiltration
Unit and clear water tanks (20), air supporting oil removal unit is made up of submersible sewage pump (1), air supporting oil interceptor (2) and aerator (3), submersible sewage pump
(1) communicated with the sewage inlet of air supporting oil interceptor (2) by pipeline, aerator (3) is arranged on air supporting oil interceptor (2) bottom, surpass
The water inlet of filter unit is communicated with the water out of air supporting oil interceptor (2) by pump and pipeline, and the water inlet of nano-filtration unit passes through pump
Communicate with the water out of ultra filtration unit with pipeline, the water inlet of clear water tanks (20) passes through the delivery port of pump and pipeline and nano-filtration unit
Communicate.
2. the integration apparatus for automatically processing sewage according to claim 1 are it is characterised in that ultra filtration unit is by surpassing
Water tank (7) composition, the water inlet of ultrafiltration raw water box (4) are produced in filter raw water box (4), ultrafiltration booster pump (5), ultrafiltration apparatus (6) and ultrafiltration
Mouth is communicated with the water out of air supporting oil interceptor (2) by pump and pipeline, and ultrafiltration apparatus (6) pass through ultrafiltration booster pump (5) and pipeline
Communicate with the delivery port of ultrafiltration raw water box (4), the water outlet by pipeline and ultrafiltration apparatus (6) for the water inlet of water tank (7) is produced in ultrafiltration
Mouth communicates.
3. the integration apparatus for automatically processing sewage according to claim 1 are it is characterised in that nano-filtration unit is by receiving
Water tank (10) composition is produced in filter booster pump (8), nanofiltration device (9) and nanofiltration, and the water inlet of nanofiltration device (9) passes through nanofiltration booster pump
(8) communicate with the delivery port of ultrafiltration product water tank (7) with pipeline, the water inlet that water tank (10) is produced in nanofiltration passes through pipeline and nanofiltration device
(9) delivery port communicates.
4. the integration apparatus for automatically processing sewage according to claim 1 and 2 it is characterised in that ultra filtration unit also
Hyperfiltration reverse-rinsing pump (11), the water inlet of hyperfiltration reverse-rinsing pump (11) and delivery port is had to produce water tank (7) and ultrafiltration apparatus with ultrafiltration respectively
(6) communicate, hyperfiltration reverse-rinsing pump (11) is used for cleaning the milipore filter of ultrafiltration apparatus (6).
5. the integration apparatus for automatically processing sewage according to claim 1 or 3 it is characterised in that nano-filtration unit also
Have nanofiltration medicine to wash pump (12), nanofiltration medicine wash pump (12) and water inlet and delivery port respectively with nanofiltration produce water tank (10) and nanofiltration fill
Put (9) to communicate, nanofiltration medicine is washed pump (12) and is used for cleaning the NF membrane of nanofiltration device (9).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620714073.1U CN205892904U (en) | 2016-07-07 | 2016-07-07 | A integration equipment for automaticallying process sewage |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620714073.1U CN205892904U (en) | 2016-07-07 | 2016-07-07 | A integration equipment for automaticallying process sewage |
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| Publication Number | Publication Date |
|---|---|
| CN205892904U true CN205892904U (en) | 2017-01-18 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620714073.1U Active CN205892904U (en) | 2016-07-07 | 2016-07-07 | A integration equipment for automaticallying process sewage |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107459174A (en) * | 2017-09-18 | 2017-12-12 | 广东普施德泽环保股份有限公司 | A kind of food and drink waste water recycle device |
| CN107628698A (en) * | 2017-11-02 | 2018-01-26 | 江苏中科睿赛污染控制工程有限公司 | A kind of waste water reuse cleaning system and its processing method |
-
2016
- 2016-07-07 CN CN201620714073.1U patent/CN205892904U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107459174A (en) * | 2017-09-18 | 2017-12-12 | 广东普施德泽环保股份有限公司 | A kind of food and drink waste water recycle device |
| CN107628698A (en) * | 2017-11-02 | 2018-01-26 | 江苏中科睿赛污染控制工程有限公司 | A kind of waste water reuse cleaning system and its processing method |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |