CN205773760U - Ecosystem water treatment system - Google Patents
Ecosystem water treatment system Download PDFInfo
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- CN205773760U CN205773760U CN201620623215.3U CN201620623215U CN205773760U CN 205773760 U CN205773760 U CN 205773760U CN 201620623215 U CN201620623215 U CN 201620623215U CN 205773760 U CN205773760 U CN 205773760U
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- Separation Using Semi-Permeable Membranes (AREA)
Abstract
This utility model relates to a kind of ecosystem water treatment system, being connected with multiple ozonators by the first pipeline after stating liquid oxygen tank, heat exchanger, cooler series connection including transformator, electric control room, liquid oxygen tank, heat exchanger, cooler, each ozonator is connected with pre-ozonation processing means by the second pipeline；Also include source water lifting device, source water is delivered to pre-filtrating equipment by one-level elevator pump by source water lifting device, water is delivered to pre-ozonation processing means by water diversion tank, booster pump, the 3rd pipeline, two-stage hoisting pump by pre-filtrating equipment, pre-ozonation processing means connects preposition ozone reactor group by Venturi tube, and described preposition ozone reactor group is connected with degassing intermediate pool in the middle of degassing room group, underground and by three grades of elevator pumps, degassing opisthogenesis water is delivered to ultrafilter membrane.It is only existing external water treatment technology 40% that this utility model takes up an area, and investment is only domestic existing water treatment technology 95%, and operating cost can save 62% compared with domestic prior art.
Description
Technical field
The present invention relates to water treatment technology apparatus field, particularly relate to ecosystem water treatment system.
Background technology
At present, the most now set by coagulation apparatus, dosing PAC equipment, settling apparatus, flocculation by conventional water supply processing system
Standby, dosing PAM equipment, clarifying equipment, water elevator pump, mechanical filter equipment, backwashing equipment, secondary filter equipment, add chemical medicine
Medicament equipment, ultrafiltration apparatus, sterilizing equipment decontaminating apparatus, sludge lifting pump, sludge concentration device, dosing PAM flocculation, device for dehydrating sladge waste,
The plurality of devices such as sludge transportation equipment is constituted, the technological process of its controlling the water circulation be water pump throw coagulation after coagulant, chlorination, precipitation,
Filtering (rear chlorination), clear water reserviors, Water-supply station, urban pipe network, above-mentioned watering place reason Processes and apparatus is at water treatment procedure
In need to add multiple water treatment medicament, and mud can be produced in water treatment procedure, it needs sludge dewatering system to equip
Carrying out Treatment of Sludge, therefore the floor space of water treatment system is big, and operating cost is high, and total investment of engineering is big.Additionally, due to above-mentioned
Adding multiple water treatment medicament in water treatment procedure, therefore user's gained tap water is the process adding all kinds of water treatment agent
Use water.
Summary of the invention
The applicant, for above-mentioned existing issue, has carried out Improvement, it is provided that ecosystem water treatment system, this process system
System need not add any water treatment agent in running, and produces without mud, it is not necessary to additionally increases sludge dewatering
System is equipped.
The technical solution adopted in the present invention is as follows:
Ecosystem water treatment system, including transformator, electric control room, liquid oxygen tank, heat exchanger, cooler, described liquid oxygen
It is connected with the multiple ozonators connected each other by the first pipeline after the series connection of tank, heat exchanger, cooler, connects the most each other
Multiple ozonators are connected with pre-ozonation processing means by the second pipeline, make the ozone of preparation transport to pre-ozonation
In reason device；Also including the source water lifting device for extracting river, source, lake water, described source water lifting device is carried by one-level
Rising pump and source water is delivered to pre-filtrating equipment, described pre-filtrating equipment passes through water diversion tank, booster pump, the 3rd pipeline, two-stage hoisting
Water is delivered to pre-ozonation processing means by pump, and described pre-ozonation processing means is for mixing water with ozone；Described pre-smelly
Oxidation treatment device connects preposition ozone reactor group by Venturi tube, described preposition ozone reactor group and degassing room group,
In the middle of underground, degassing intermediate pool connects and by three grades of elevator pumps, degassing opisthogenesis water is delivered to ultrafilter membrane, and described ultrafilter membrane leads to
Crossing pipeline to be connected with underground clear water reserviors, water is expelled to user by ultra-filtration water pipe and level Four elevator pump by described underground clear water reserviors
Use.
Its further technical scheme is:
Also including air compressor and the compressed air cylinder connected each other, described air compressor, compressed air cylinder pass through
4th pipeline is connected with backwash pump and passes through backwash water inlet pipe connection ultrafilter membrane；
Also include the rearmounted ozone reactor for removing colourity in water, abnormal smells from the patient and organic pollution, rearmounted ozone reaction
Device and the second pipeline connect, and described rearmounted ozone reactor is connected with contact chamber also by the 5th pipeline；
Described ozonator is panel type ozone producer；Described ultrafilter membrane is powerful oxidation corrosion resistance ultrafilter membrane；
Described ultrafilter membrane is connected with chemically-cleaning device also by the 6th pipeline, and described chemically-cleaning device is for further
Cleaning ultrafilter membrane internal contamination thing, scavenging period is spaced apart 12-18 month, and described pollutant are discharged by backwash outlet pipe；
Described pre-filtrating equipment includes pre-grid defecator and preformed precipitate device, and described pre-grid defecator is for real
Solid and liquid in existing river, source, lake water separate, and are realized the removal of source water endoparticle thing by backwash；Described preliminary sedimentation
Shallow lake device is for processing the high concentrtion deposit brought season because of rainwater；
If arranging preformed precipitate device when source water turbidity is more than 150mg/l, described preformed precipitate device is with source water lifting device even
Connect；
Beneficial effects of the present invention is as follows:
(1) layout of pre-filtrating equipment can realize the solid-liquid separation of impurities in water, and it is turbid that it can effectively remove in water
Degree, humidity, abnormal flavour, escherichia coli, micro-content organism, CODmn, algae and eliminate pathogen and virus, except ferrum, violent, nitrone
And pesticide persists the water pollutants such as thing.
(2) present invention uses ozone strong oxidizing to produce micro-bubble, utilizes microvesicle reaction to realize anti-to ultrafilter membrane film body
Multiple collision, thus makes the pollutant being attached to ultrafilter membrane film body surface drop and discharge, and it not only achieves ultrafilter membrane film body
Automatic cleaning, prevent its pickup, it need not add any medicament, also avoids setting up sludge dewatering system equipment.
(3) present invention is taken up an area is only existing external water treatment technology 40%, and investment is only domestic existing water treatment technology
95%, operating cost can save 62% compared with domestic prior art, and intelligent operation only needs a people on duty, it is possible to directly lead to
Cross internet-based control.Effectively remove the turbidity in water, humidity, abnormal flavour, escherichia coli, micro-content organism, ferrum, violent, nitrone and
Pesticide persists the water pollutants such as thing.The mineral such as Mg, Ca of reservation needed by human body, pH value reaches neutral, water quality institute after process
Index is had to be better than the world and China's drinking water standard.
Accompanying drawing explanation
Fig. 1 is the structural representation of the present invention.
Fig. 2 is the process schematic that in the present invention, microvesicle contacts with ultrafilter membrane.
Wherein: 1, transformator；2, air compressor；3, compressed air cylinder；4, liquid oxygen tank；5, heat exchanger；6, in the middle of underground
Degassing pond；7, cooler；8, ozonator；9, three grades of elevator pumps；10, electric control room；11, backwash pump；12, connect
Touch pond；13, rearmounted ozone reactor；14, ultrafilter membrane；15, ultra-filtration water pipe.16, source water lifting device；1601, one-level promotes
Pump；17, pre-filtrating equipment；171, water diversion tank；18, booster pump；19, pre-ozonation processing means；1901, two-stage hoisting pump；
1902, Venturi tube；20, preposition ozone reactor group；21, degassing room group；2201, the first pipeline；2202, the second pipeline；
2203, the 3rd pipeline；2204, the 4th pipeline；2205, backwash water inlet pipe；2206, the 5th pipeline；2207, backwash outlet pipe；
2208, the 6th pipeline；23, preformed precipitate device；24, chemically-cleaning device；25, underground clear water reserviors；26, level Four elevator pump；
Detailed description of the invention
Below in conjunction with the accompanying drawings, the detailed description of the invention of the present invention is described.
As it is shown in figure 1, ecosystem water treatment system includes transformator 1, electric control room 10, liquid oxygen tank 4, heat exchanger 5, cold
But device 7, by the first pipeline 2201 and the multiple ozonators connected each other after the series connection of liquid oxygen tank 4, heat exchanger 5, cooler 7
8 connect, and the multiple ozonators 8 connected the most each other are connected with pre-ozonation processing means 19 by the second pipeline 2202, make
The ozone of preparation transports to pre-ozonation processing means 19.As it is shown in figure 1, present invention additionally comprises for extracting river, lake
The source water lifting device 16 of source water, source water is delivered to pre-filtrating equipment by one-level elevator pump 1601 by source water lifting device 16
17, pre-filtrating equipment 17 includes that pre-grid defecator and preformed precipitate device, pre-grid defecator are used for realizing river, lake
Solid and liquid in the water of pool source separate, and are realized the removal of source water endoparticle thing by backwash；Preformed precipitate device 23 is used for
Processing the high concentrtion deposit brought season because of rainwater, preformed precipitate device is for processing the high concentrtion deposition brought season because of rainwater
Thing, if arranging preformed precipitate device 23 when source water turbidity is more than 150mg/l, preformed precipitate device 23 is connected with source water lifting device 16.
Above-mentioned pre-filtrating equipment 17 can effectively remove the turbidity in water, humidity, abnormal flavour, escherichia coli, micro-content organism, CODmn, algae
Class and eliminate pathogen and virus, persist the water pollutants such as thing except ferrum, violent, nitrone and pesticide.Retain needed by human body
The mineral such as Mg, Ca, pH value reaches neutral, and after process, all indexs of water quality are better than country's drinking water standard more.Such as Fig. 1 institute
Showing, water is delivered to pre-by water diversion tank 171, booster pump the 18, the 3rd pipeline 2203, two-stage hoisting pump 1901 by pre-filtrating equipment 17
Ozonation treatment device 19, pre-ozonation processing means 19 is for mixing water with ozone；Pre-ozonation processing means 19 is passed through
Venturi tube 1902 connects preposition ozone reactor group 20, and preposition ozone reactor group 20 takes off in the middle of degassing room group 21, underground
Air water pond 6 connects and by three grades of elevator pumps 9, degassing opisthogenesis water is delivered to ultrafilter membrane 14, and ultrafilter membrane 14 is by ultra-filtration water pipe
15 are connected with underground clear water reserviors 25, and water is expelled to user by pipeline and level Four elevator pump 26 and uses by underground clear water reserviors 25.As
Shown in Fig. 1, present invention additionally comprises the air compressor 2 and compressed air cylinder 3 connected each other, air compressor 2, compressed air cylinder
3 are connected with backwash pump 11 and pass through backwash water inlet pipe 2205 connected ultrafilter membrane 14, ultrafilter membrane 14 by the 4th pipeline 2204
For powerful oxidation corrosion resistance ultrafilter membrane.As it is shown in figure 1, present invention additionally comprises after removing colourity in water, abnormal smells from the patient and organic pollution
Putting ozone reactor 13, ozonator 8 is panel type ozone producer.Rearmounted ozone reactor 13 and the second pipeline 2202 are even
Connecing, rearmounted ozone reactor 13 is connected with contact chamber 12 also by the 5th pipeline 2206, as it is shown in figure 1, ultrafilter membrane 14 also by
6th pipeline 2208 is connected with chemically-cleaning device 24, and chemically-cleaning device 24 is for cleaning ultrafilter membrane internal contamination further
Thing, scavenging period is spaced apart 12-18 month, and pollutant are discharged by backwash outlet pipe 2207, as it is shown in figure 1, above-mentioned ultrafilter membrane
14, pre-filtrating equipment 17 is also connected with backwash outlet pipe 2207.
As shown in Figure 1 and Figure 2, this utility model is utilized to carry out specifically comprising the following steps that of water treatment technology
The first step: by one-level elevator pump 1601, the source water in river, lake is introduced pre-filtering by source water lifting device 16
Device 17 carries out pre-filtering.Pre-filtrating equipment 17 includes pre-grid defecator and preformed precipitate device 23, pre-grid defecator
For realizing the solid in river, source, lake water and liquid separation, and realized the removal of source water endoparticle thing by backwash；In advance
Settler 23 is for processing the high concentrtion deposit brought season because of rainwater, and preformed precipitate device 23 is for processing because of rainwater season
The high concentrtion deposit brought, if arranging preformed precipitate device 23, preformed precipitate device 23 and Yuan Shui when source water turbidity is more than 150mg/l
Lifting device 16 connects.Above-mentioned pre-filtrating equipment 17 can effectively remove the turbidity in water, humidity, abnormal flavour, escherichia coli, trace
Organic substance, CODmn, algae and eliminate pathogen and virus, persist the water pollutants such as thing except ferrum, violent, nitrone and pesticide.
Retaining the mineral such as Mg, Ca of needed by human body, pH value reaches neutral, and after process, all indexs of water quality are better than country's life more and drink
Water quality standard.Water is carried by pre-filtrating equipment 17 by water diversion tank 171, booster pump the 18, the 3rd pipeline 2203, two-stage hoisting pump 1901
To pre-ozonation processing means 19, in utilizing primer pump 171, there is the condition of water, booster pump 18 is filled water in advance, it is ensured that increase
The timely startup of press pump 18.
Second step: manufactured ozone by liquid oxygen tank 4, heat exchanger 5 and ozonator 8, ozone passes through the second pipeline 2202, two
Ozone is sent into pre-ozonation processing means 19 by level elevator pump 1901, utilizes pre-ozonation processing means 19 to make ozone and source aqueous phase
Molten.Ozone preparation is made up of with liquid oxygen tank 4, heat exchanger 5 ozonator 8, can also be occurred by ozone by air simultaneously
Ozone directly prepared by device 8.
3rd step: ozone carries out Strong oxdiative reaction in preposition ozone reactor group 20；Strong oxdiative reaction is used for processing source
Organic pollutants, inorganic pollution and heavy metal, the source water with ozone of above-mentioned outflow pre-ozonation processing means 19
Comprise soluble or less than 300 microns pollutant.
4th step: ozone enters degassing room group 21 with source water by pipeline after Strong oxdiative reacts, and utilizes degassing room group 21
The gas of insoluble source water in ozone is de-gassed formation oxygen, the complete ozone that do not deaerates formed micro-ozone and with source current
Enter degassing pond 6 in the middle of underground.
5th step: be lifted into ultrafilter membrane 14 with the source water of micro-ozone by three grades of elevator pumps 9 internal and carry out microvesicle
Reaction, source water is directly entered ultrafilter membrane 14 film body self-filtering continuous ultrafiltration water outlet.In above-mentioned microvesicle reacts, such as Fig. 2 institute
Show, by the bubble in the source water that three grades of elevator pumps 9 promote in ultrafilter membrane 14 film body traveling process volume in gradually successively decreasing,
Ultrafilter membrane 14 film body outer surface explodes continuously, makes the pollutant being attached to ultrafilter membrane 14 film body surface sink to ultrafilter membrane also
Discharge.The water continuous ultrafiltration water outlet of above-mentioned source comprises multiple post processing water exit mode, post processing water exit mode include normal water outlet,
Activated carbon filters water outlet and rear ozone water outlet.When rear ozone water outlet, by rearmounted ozone reactor 13 by the 5th pipeline 2206
It is connected with contact chamber 12 and by ozone and ultra-filtration water haptoreaction.As it is shown in figure 1, post processing water outlet flows into underground clear water reserviors
25, promote and discharge for user by level Four elevator pump 26, before discharge, suitable chlorination carries out disinfection.Source water pollutant surpasses
Carrying out activated carbon water outlet when crossing present system equipment disposal ability 20%, source water pollutant exceedes present system equipment and processes
Ozone water outlet after using during ability 10%.
Present invention process if desired recoils ultrafilter membrane 14 time, the backwash of ultrafilter membrane by air compressor 2, compression sky
Gas tank 3 and backwash pump 11 extract underground clear water reserviors clear water 25 and carry soda pop by backwash water inlet pipe 2205 to ultrafilter membrane 14
Mixing water often organizes the staged backwash of ultrafilter membrane 14, and the water after backwash is discharged by backwash outlet pipe 2207.
Need not add any medicament during the most whole process water conservancy project skill, and produce without mud, be not required to
Wanting sludge dewatering system to equip, in ultrafilter membrane 14 operation, ozone microbubbles is the most automatically cleaned and is prevented film pickup, the most clear in conjunction with soda pop
Washing and reach film non-scaling, backwash draining reaches direct discharge standard, and water outlet reaches original ecology healthy water quality standard, and it is only existing for taking up an area
Having external water treatment technology 30-40%, investment is only domestic tap water project technique 85-95%, operating cost be only domestic from
Water project technique 30%, present system can be manipulated by electric control room whole-course automation, it is only necessary to a people can be real
The now operation to a complete set of equipment, 0.26 yuan/ton of water of water oxygen consumption cost the most per ton, 0.11 yuan/ton of water of water power consumption cost per ton, often
Ton water consumption 0.01 yuan/ton of water of labour cost.
Table is contrasted as follows before and after the Effluent criteria of the present invention:
Above description is explanation of the invention, is not the restriction to invention, and limited range of the present invention sees right
Requirement, in the case of the basic structure of the present invention, the present invention can make any type of amendment.
Claims (8)
1. ecosystem water treatment system, it is characterised in that: include transformator (1), electric control room (10), liquid oxygen tank (4), heat exchange
Device (5), cooler (7), by the first pipeline (2201) with mutual after described liquid oxygen tank (4), heat exchanger (5), cooler (7) series connection
Multiple ozonators (8) for series connection connect, and the multiple ozonators (8) connected the most each other pass through the second pipeline (2202)
Being connected with pre-ozonation processing means (19), the ozone transport making preparation is interior to pre-ozonation processing means (19)；Also include using
In extracting river, source water lifting device (16) of source, lake water, described source water lifting device (16) passes through one-level elevator pump
(1601) Jiang Yuanshui is delivered to pre-filtrating equipment (17), and described pre-filtrating equipment (17) passes through water diversion tank (171), booster pump
(18), water is delivered to pre-ozonation processing means (19), described pre-ozone by the 3rd pipeline (2203), two-stage hoisting pump (1901)
Change processing means (19) for being mixed with ozone by water；Described pre-ozonation processing means (19) is by Venturi tube (1902) even
Connect in deaerating in the middle of preposition ozone reactor group (20), described preposition ozone reactor group (20) and degassing room group (21), underground
Between pond (6) connect and by three grades of elevator pumps (9), degassing opisthogenesis water be delivered to ultrafilter membrane (14), described ultrafilter membrane (14) leads to
Crossing pipeline to be connected with underground clear water reserviors (25), ultra-filtration water pipe is passed through in described underground clear water reserviors (25) and level Four elevator pump (26) will
Water is expelled to user and uses.
2. ecosystem water treatment system as claimed in claim 1, it is characterised in that: also include the air compressor connected each other
(2) and compressed air cylinder (3), described air compressor (2), compressed air cylinder (3) pass through the 4th pipeline (2204) and backwash
Water pump (11) connects and passes through backwash water inlet pipe (2205) connection ultrafilter membrane (14).
3. ecosystem water treatment system as claimed in claim 1, it is characterised in that: also include for removing colourity in water, gas
The rearmounted ozone reactor (13) of taste and organic pollution, rearmounted ozone reactor (13) is connected with the second pipeline (2202), institute
State rearmounted ozone reactor (13) to be connected with contact chamber (12) also by the 5th pipeline (2206).
4. ecosystem water treatment system as claimed in claim 1, it is characterised in that: described ozonator is that board-like ozone is sent out
Raw device；Described ultrafilter membrane is powerful oxidation corrosion resistance ultrafilter membrane.
5. ecosystem water treatment system as claimed in claim 1, it is characterised in that: described ultrafilter membrane (14) is also by the 6th pipe
Road (2208) is connected with chemically-cleaning device (24), and described chemically-cleaning device (24) is internal dirty for cleaning ultrafilter membrane further
Dye thing, scavenging period is spaced apart 12-18 month, and described pollutant are discharged by backwash outlet pipe (2207).
6. ecosystem water treatment system as claimed in claim 1, it is characterised in that: described pre-filtrating equipment (17) includes pre-lattice
Net filtration device and preformed precipitate device, described pre-grid defecator is for realizing the solid in river, source, lake water and liquid
Separate, and realized the removal of source water endoparticle thing by backwash；Described preformed precipitate device is for processing because rainwater brings season
High concentrtion deposit.
7. ecosystem water treatment system as claimed in claim 1, it is characterised in that: if setting when source water turbidity is more than 150mg/l
Putting preformed precipitate device (23), described preformed precipitate device (23) is connected with source water lifting device (16).
8. ecosystem water treatment system as claimed in claim 1, it is characterised in that: described ultrafilter membrane (14), pre-filtrating equipment
Also it is connected with backwash outlet pipe (2207).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620623215.3U CN205773760U (en) | 2016-06-22 | 2016-06-22 | Ecosystem water treatment system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620623215.3U CN205773760U (en) | 2016-06-22 | 2016-06-22 | Ecosystem water treatment system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205773760U true CN205773760U (en) | 2016-12-07 |
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ID=58130267
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620623215.3U Active CN205773760U (en) | 2016-06-22 | 2016-06-22 | Ecosystem water treatment system |
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| Country | Link |
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| CN (1) | CN205773760U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2017219892A1 (en) * | 2016-06-22 | 2017-12-28 | 江苏达格水务有限公司 | Raw ecological water treatment process and treatment system adopting the same |
-
2016
- 2016-06-22 CN CN201620623215.3U patent/CN205773760U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2017219892A1 (en) * | 2016-06-22 | 2017-12-28 | 江苏达格水务有限公司 | Raw ecological water treatment process and treatment system adopting the same |
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