CN205419995U - Groundwater Water Treatment System - Google Patents
Groundwater Water Treatment System Download PDFInfo
- Publication number
- CN205419995U CN205419995U CN201620157921.3U CN201620157921U CN205419995U CN 205419995 U CN205419995 U CN 205419995U CN 201620157921 U CN201620157921 U CN 201620157921U CN 205419995 U CN205419995 U CN 205419995U
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- CN
- China
- Prior art keywords
- water
- equipment
- supply station
- tank
- pipeline
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 131
- 239000003673 groundwater Substances 0.000 title claims abstract description 11
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims abstract description 53
- DIZPMCHEQGEION-UHFFFAOYSA-H aluminium sulfate (anhydrous) Chemical compound [Al+3].[Al+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O DIZPMCHEQGEION-UHFFFAOYSA-H 0.000 claims abstract description 17
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 claims abstract description 12
- 239000000460 chlorine Substances 0.000 claims abstract description 12
- 229910052801 chlorine Inorganic materials 0.000 claims abstract description 12
- 239000003814 drug Substances 0.000 claims abstract description 8
- 238000001914 filtration Methods 0.000 claims description 32
- 238000010521 absorption reaction Methods 0.000 claims description 16
- 238000007599 discharging Methods 0.000 claims description 15
- 238000011045 prefiltration Methods 0.000 claims description 9
- 239000003513 alkali Substances 0.000 claims description 7
- 238000011001 backwashing Methods 0.000 claims description 7
- 238000005660 chlorination reaction Methods 0.000 claims description 7
- 238000010790 dilution Methods 0.000 claims description 7
- 239000012895 dilution Substances 0.000 claims description 7
- 229940079593 drug Drugs 0.000 claims description 7
- 238000012545 processing Methods 0.000 claims description 7
- 239000001117 sulphuric acid Substances 0.000 claims description 7
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims description 6
- 235000011149 sulphuric acid Nutrition 0.000 claims description 6
- 238000000746 purification Methods 0.000 claims description 5
- 238000001556 precipitation Methods 0.000 claims description 3
- 150000003839 salts Chemical class 0.000 abstract description 7
- 241000195493 Cryptophyta Species 0.000 abstract description 6
- 230000000694 effects Effects 0.000 abstract description 5
- 241000233866 Fungi Species 0.000 abstract 1
- 238000000034 method Methods 0.000 description 12
- 238000004659 sterilization and disinfection Methods 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- 235000001674 Agaricus brunnescens Nutrition 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 3
- 101100298222 Caenorhabditis elegans pot-1 gene Proteins 0.000 description 2
- 241000588724 Escherichia coli Species 0.000 description 2
- YCKRFDGAMUMZLT-UHFFFAOYSA-N Fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 description 2
- 230000000844 anti-bacterial effect Effects 0.000 description 2
- 244000052616 bacterial pathogen Species 0.000 description 2
- 229910052731 fluorine Inorganic materials 0.000 description 2
- 239000011737 fluorine Substances 0.000 description 2
- 239000008187 granular material Substances 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 230000001954 sterilising effect Effects 0.000 description 2
- 206010016807 Fluid retention Diseases 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000008239 natural water Substances 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 238000003911 water pollution Methods 0.000 description 1
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- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The utility model relates to a water treatment system of groundwater, local groundwater water treatment system include primary filter equipment, refilter equipment, clean water basin, suction well, water pump and controlgear. The system achieves the effect of removing dissolved salts, organic matters, algae and fungi in raw water mainly by adding sodium hydroxide, aluminum sulfate, chlorine and other medicaments, and simultaneously greatly improves the total water treatment amount of the existing building area in unit time.
Description
Technical field
This utility model belongs to water treatment field, particularly relates to the water treatment system of a kind of groundwater source.
Background technology
Water is Source of life, is also a ring important in ecology, is also a fragile ring simultaneously.Former water is taken from natural water body or water-retention water body, such as river, lake, pond or underground aquifers etc., as the water of resource of water supply；Former water can also refer to flow into the water of first processing unit of water treatment plant.The former water of crude underground water source, the most all with the slight granule of such as algae, silt etc.All the more serious due to economic development and activity, China's underground water pollution and the exhaustive exploitation phenomenon such as daily life of society in recent years, what quality of groundwater cannot meet people just commonly uses water requirement.Water technology is by water filtration regeneration, makes water reach a standard specified, then can be used other field, as pouring, drinks.But the water treatment facilities of the water treatment plant of routine have the shortcomings such as floor space is wide, cost is high, water treatment efficiency is low, seriously limit the treating capacity of water, people can not be met at all and live required water supply requirement.The most important thing that after the most how improving water treatment efficiency and water process, the quality of water quality becomes in water treatment field.
Utility model content
In order to overcome the technological deficiency existing for above-mentioned prior art, this utility model provides a kind of Groundwater processing system, native system mainly reaches to remove the effect of dissolved salts, Organic substance, algae and mushroom in former water by medicines such as input sodium hydroxide, aluminum sulfate, chlorine, also substantially increases existed building area water within the unit interval simultaneously and processes total amount.
This subsoil water water treatment system include prefiltration equipment, refilter between equipment, drug storage, clear water reserviors, absorbing well, absorption well, Water-supply station and control equipment, the outlet of described prefiltration equipment refilters equipment entrance described in connecting, the described equipment that refilters exports the described clear water reserviors entrance of connection, the outlet of described clear water reserviors connects described absorbing well, absorption well entrance, the outlet of described absorbing well, absorption well connects described Water-supply station entrance, and the outlet of described Water-supply station connects feedwater piping；Described prefiltration equipment includes grit water separator, for the main workshop of raw water filtration, mainly the former water in former water pot is separated and is filtered；The described equipment that refilters is filtering tank, and described filtering tank is another main workshop of raw water filtration, mainly the former water in former water pot is carried out further fluorine removal, except dissolved salts and sterilization；Include between described drug storage between sodium hydroxide storage, between aluminum sulfate storage and between chlorine storage；Between described sodium hydroxide stores, capital equipment is sodium hydroxide storage tank, and between described aluminum sulfate stores, capital equipment is aluminum sulfate storage tank, and between described chlorine stores, capital equipment is chlorination tank；One discharging opening of described sodium hydroxide storage tank is connected with described filtering tank charging aperture by alkali liquor dilution tunnel, and the pipeline that another discharging opening is exported with described Water-supply station by alkali liquor dilution tunnel is connected；One discharging opening of described aluminum sulfate storage tank adds pipe by sulphuric acid and is connected with described filtering tank charging aperture, and another discharging opening adds pipeline by sulphuric acid and is connected with the entrance of described grit water separator；The discharging opening of described chlorination tank is connected with the pipeline between described filtering tank and described clear water reserviors；Described clear water reserviors are between the precipitation after raw water filtration, are mainly separated off the impurity such as particle by standing；Described absorbing well, absorption well be filter after water purification water between；It is provided with conveying pump in described Water-supply station, feedwater piping is delivered in water purification pressurization good for filtration existing in absorbing well, absorption well；Described control equipment is positioned at Control Room, is monitored water treatment system and data record.
Described grit water separator is spiral grit-water separator or spiral-flow type grit water separator.
Described water treatment system is additionally provided with backwashing equipment, and the two ends of backwashing equipment connect charging aperture and the pipeline of Water-supply station outlet of filtering tank respectively.
Described water treatment system, by adding sodium hydroxide, aluminum sulfate, can eliminate the dissolved salts in water and Organic substance, kills algae in water, mushroom by adding chlorine.Former water is stored through clear water reserviors after filtering, and again adds chlorine in clear water reserviors and carry out disinfection, and kills the pathogenic bacterias such as the antibacterial of water body, escherichia coli, completes whole clean water treatment process, deliver to municipal pipeline by Water-supply station the most again and supply domestic water.
This utility model compared with prior art, has the advantage that and has the beneficial effect that: this subsoil water water treatment system has the advantage that
(1) installation is simple, rapidly；
(2) this apparatus system water treating capacity is big, and processing means floor space is the least, unit are and in the unit interval water process total amount and improve a lot；
(3) filtering accuracy reaches nanoscale, it is possible to effectively remove the dissolved salts in water, microorganism, Organic substance etc..
Accompanying drawing explanation
Accompanying drawing 1 is the structural representation of this groundwater treatment system.
The former water pot of label in figure: 1-, 2-grit water separator, 3-filtering tank, 4-chlorination tank, 5-clear water reserviors, 6-absorbing well, absorption well, 7-Water-supply station, 8-backwashing equipment, 9-sodium hydroxide storage tank, 10-aluminum sulfate storage tank, 11-alkali liquor dilution tunnel, 12-sulphuric acid add pipeline, 13-feedwater piping.
Detailed description of the invention
In order to deepen the understanding of the present invention, below in conjunction with the drawings and specific embodiments this utility model is further described explanation:
As shown in Figure 1, this subsoil water water treatment system include prefiltration equipment, refilter between equipment, drug storage, clear water reserviors 5, absorbing well, absorption well 6, Water-supply station 7 and control equipment, the outlet of described prefiltration equipment refilters equipment entrance described in connecting, the described equipment that refilters exports described clear water reserviors 5 entrance of connection, the outlet of described clear water reserviors 5 connects described absorbing well, absorption well 6 entrance, the outlet of described absorbing well, absorption well connects described Water-supply station 7 entrance, and the outlet of described Water-supply station 7 connects feedwater piping 13；Described prefiltration equipment includes grit water separator 2, for the main workshop of raw water filtration, mainly the former water in former water pot 1 is separated and is filtered；The described equipment that refilters is filtering tank 3, and described filtering tank 3 is another main workshop of raw water filtration, mainly the former water in former water pot 1 is carried out further fluorine removal, except dissolved salts and sterilization；Include between sodium hydroxide storage, between aluminum sulfate storage and between chlorine storage between described drug storage, between described sodium hydroxide stores, capital equipment is sodium hydroxide storage tank 9, between described aluminum sulfate stores, capital equipment is aluminum sulfate storage tank 10, and between described chlorine stores, capital equipment is chlorination tank 4；One discharging opening of described sodium hydroxide storage tank 9 is connected with described filtering tank 3 charging aperture by alkali liquor dilution tunnel 11, the pipeline that another discharging opening of described sodium hydroxide storage tank 9 is exported with described Water-supply station by alkali liquor dilution tunnel 11 is connected, one discharging opening of described aluminum sulfate storage tank 10 adds pipeline 12 by sulphuric acid and is connected with described filtering tank 3 charging aperture, and another discharging opening of described aluminum sulfate storage tank 10 adds pipeline 12 by sulphuric acid and is connected with the entrance of described grit water separator；Pipeline between the discharging opening of described chlorination tank 4 with described filtering tank 3 and described clear water reserviors 5 is connected；Described clear water reserviors 5 are between the precipitation after raw water filtration, are mainly separated off the impurity such as particle by standing；Described absorbing well, absorption well 6 be filter after water purification water between；It is provided with conveying pump in described Water-supply station 7, feedwater piping 13 is delivered in water purification pressurization good for filtration existing in absorbing well, absorption well；Described control equipment is positioned at Control Room, is monitored water treatment system and data record.
Described grit water separator 2 is spiral grit-water separator or spiral-flow type grit water separator.
Described water treatment system is additionally provided with backwashing equipment 8, and the two ends of backwashing equipment 8 connect charging aperture and the pipeline of Water-supply station 7 outlet of filtering tank 3 respectively.
This water treatment system carries out the main operational procedure of water process: prepare before marching into the arena, and------equipment hoisting is in place, and------wire casing, cable are installed, and---equipment wiring--equipment debugging--is overall to be checked and accepted in process pipe installation in preparation of construction.
Former water refers to crude underground water source, all with the slight granule of such as algae, silt etc in usual former water.After former water flows into this water treatment system, by filtering tank and the direct effect adding sodium hydroxide, aluminum sulfate, dissolved salts in removable water and Organic substance, by killing algae in water, mushroom with the directly effect adding chlorine, water is stored through clear water reserviors after filtering, and in clear water reserviors, again add chlorine carry out disinfection and precipitate, the pathogenic bacterias such as the antibacterial of water body, escherichia coli are killed, complete whole clean water treatment process, then deliver to feedwater piping supply domestic water by absorbing well, absorption well, Water-supply station.The control equipment of water treatment system is located at the Control Room of complex building, and the operation to complete equipment is managed and monitors.
The total floor space of this water treatment system about 3500, day water process total amount reaches 1.5 ten thousand tons, processes water inventory and reach 109,500,000 tons in 20 years.Estimate that in unit are, the unit interval internal ratio tradition water treatment technology multiprocessing water yield be 4562.5 ten thousand tons, substantially increase water treatment system water in the unit interval under existed building area and process total amount.
Above this utility model and embodiment thereof are described; this description is the most restricted; for the ordinary skill in the art; in the case of without departing from principle of the present utility model and spirit; these detailed description of the invention can be carried out multiple change, revise, replace and modification; these design constructional device same or analogous with the technical program or product and using method thereof without creative, all should fall within protection domain of the present utility model.
Claims (3)
1. a Groundwater processing system, it is characterized in that: described system include prefiltration equipment, refilter between equipment, drug storage, clear water reserviors, absorbing well, absorption well, Water-supply station and control equipment, the outlet of described prefiltration equipment refilters equipment entrance described in connecting, the described equipment that refilters exports the described clear water reserviors entrance of connection, the outlet of described clear water reserviors connects described absorbing well, absorption well entrance, the outlet of described absorbing well, absorption well connects described Water-supply station entrance, and the outlet of described Water-supply station connects domestic water pipeline；Described prefiltration equipment includes grit water separator；The described equipment that refilters is filtering tank；Include between described drug storage between sodium hydroxide storage, between aluminum sulfate storage and between chlorine storage；Described sodium hydroxide is provided with sodium hydroxide storage tank between storing, described aluminum sulfate is provided with aluminum sulfate storage tank between storing, and described chlorine is provided with chlorination tank between storing；One discharging opening of described sodium hydroxide storage tank is connected with described filtering tank charging aperture by alkali liquor dilution tunnel, and the pipeline that another discharging opening is exported with described Water-supply station by alkali liquor dilution tunnel is connected；One discharging opening of described aluminum sulfate storage tank adds pipe by sulphuric acid and is connected with described filtering tank charging aperture, and another discharging opening adds pipeline by sulphuric acid and is connected with the entrance of described grit water separator；The discharging opening of described chlorination tank is connected with the pipeline between described filtering tank and described clear water reserviors；Described clear water reserviors are between the precipitation after raw water filtration, described absorbing well, absorption well be filter after water purification water between, be provided with conveying pump in described Water-supply station, described control equipment is positioned at Control Room.
Groundwater processing system the most according to claim 1, it is characterised in that: described grit water separator is spiral grit-water separator or spiral-flow type grit water separator.
Groundwater processing system the most according to claim 1, it is characterised in that: described water treatment system is additionally provided with backwashing equipment, and the two ends of backwashing equipment connect charging aperture and the pipeline of Water-supply station outlet of filtering tank respectively.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620157921.3U CN205419995U (en) | 2016-03-02 | 2016-03-02 | Groundwater Water Treatment System |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620157921.3U CN205419995U (en) | 2016-03-02 | 2016-03-02 | Groundwater Water Treatment System |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205419995U true CN205419995U (en) | 2016-08-03 |
Family
ID=56544867
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620157921.3U Expired - Fee Related CN205419995U (en) | 2016-03-02 | 2016-03-02 | Groundwater Water Treatment System |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205419995U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106219822A (en) * | 2016-08-31 | 2016-12-14 | 河南台冠电子科技股份有限公司 | A kind of industrial underground water treating device |
| CN111453893A (en) * | 2020-06-03 | 2020-07-28 | 中国电建集团山东电力建设有限公司 | Raw water treatment system and method |
| CN114482195A (en) * | 2022-02-17 | 2022-05-13 | 湖南艾布鲁环保科技股份有限公司 | Urban and rural water supply integrated system taking surface water as water source and treatment method |
-
2016
- 2016-03-02 CN CN201620157921.3U patent/CN205419995U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106219822A (en) * | 2016-08-31 | 2016-12-14 | 河南台冠电子科技股份有限公司 | A kind of industrial underground water treating device |
| CN106219822B (en) * | 2016-08-31 | 2022-10-18 | 河南台冠电子科技股份有限公司 | Industrial groundwater processing apparatus |
| CN111453893A (en) * | 2020-06-03 | 2020-07-28 | 中国电建集团山东电力建设有限公司 | Raw water treatment system and method |
| CN114482195A (en) * | 2022-02-17 | 2022-05-13 | 湖南艾布鲁环保科技股份有限公司 | Urban and rural water supply integrated system taking surface water as water source and treatment method |
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Legal Events
| 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 |
Granted publication date: 20160803 Termination date: 20170302 |
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| CF01 | Termination of patent right due to non-payment of annual fee |