CN205133304U - Aluminium alloy waste water processing cycle utilizes system - Google Patents
Aluminium alloy waste water processing cycle utilizes system Download PDFInfo
- Publication number
- CN205133304U CN205133304U CN201520931658.4U CN201520931658U CN205133304U CN 205133304 U CN205133304 U CN 205133304U CN 201520931658 U CN201520931658 U CN 201520931658U CN 205133304 U CN205133304 U CN 205133304U
- Authority
- CN
- China
- Prior art keywords
- order reaction
- reaction groove
- groove
- pond
- filling tube
- 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
Links
Landscapes
- Water Treatment By Electricity Or Magnetism (AREA)
- Removal Of Specific Substances (AREA)
Abstract
The utility model discloses an aluminium alloy waste water processing cycle utilizes system, including acid pond and alkaline pond, acid pond and alkaline pond all have from left to right connected gradually first order reaction groove, a microstrainer, second order reaction groove, third -stage reaction groove, two microstrainer and overflow heavy settle pond with the pond with pond left side intercommunication in, in with, first order reaction groove top is provided with saturated lime whey cistern, and saturated lime whey cistern is linked together with first order reaction tank bottom portion through first filling tube, second order reaction groove top is provided with the salt acid storage, and the salt acid storage passes through second filling tube and second order reaction tank bottom portion intercommunication, third -stage reaction groove upper end is provided with the calcium chloride cistern. This novel structural design is reasonable, and it is few to throw the dosage, and reagent cost is low, and the processing time is short, and the treatment effect is stable, mud sediment recycle is convenient, improves economic benefits, can realize waste water treatment full automation control, reach the purpose of water conservation, avoid the direct emission of sewage simultaneously, the environmental protection.
Description
Technical field
The utility model relates to a kind of technical field of waste water processing, specifically a kind of aluminium section bar production wastewater treatment cyclic utilization system.
Background technology
Aluminium section bar factory effluent complicated component, containing alkali, aluminum ion and suspension object height, in fact, contained most of pollutent all has certain economic worth, if waste water directly outer row, on the one hand, factory effluent inherently to environment, on the other hand, the huge waste of resource can be caused.Therefore, waste water reclamation utilizes the production cost for reducing product, alleviates environmental pollution, increases economic efficiency and have vital role, can improve again the environmental capacity of enterprise location simultaneously to a certain extent, be directly connected to living environment and Sustainable development.
Aluminium section bar production process mainly comprises degreasing to shaping aluminium, alkaline etching, pickling, oxidation, sealing of hole and painted, a large amount of alkaline waters and sour water is produced in aluminium section bar treating processes, and the waste water of aluminium section bar plant is except containing metal ions such as zinc, nickel, copper, also containing a large amount of aluminum ions.
Each metal ion species in waste water can not get recycling, and the water up to standard obtained after wastewater treatment generally direct discharge, do not recycled, this just causes the huge waste of resource.
Utility model content
The purpose of this utility model is to provide a kind of aluminium section bar production wastewater treatment cyclic utilization system, to solve the problem proposed in above-mentioned background technology.
For achieving the above object, the utility model provides following technical scheme:
A kind of aluminium section bar production wastewater treatment cyclic utilization system, comprise acid pond and alkaline pond, described acid pond and alkaline pond are all communicated with on the left of neutralizing water tank, and described neutralizing water tank is from left to right connected with first order reaction groove, the first Microfilter, second order reaction groove, third order reaction groove, the second Microfilter and overflow settling pool in turn; Be provided with saturated milk of lime clear liquid groove above described first order reaction groove, described saturated milk of lime clear liquid groove is connected with first order reaction trench bottom by the first filling tube; Described first Microfilter lower end is provided with the first residue outlet, and described first residue outlet lower end is provided with the first storage mud groove; Be provided with hydrochloric acid liquid bath above described second order reaction groove, described hydrochloric acid liquid bath is communicated with second order reaction trench bottom by the second filling tube; Described third order reaction groove upper end is provided with calcium chloride liquid bath; Described second Microfilter lower end is provided with the second residue outlet, and described second residue outlet lower end is provided with the second storage mud groove; Be provided with the dividing plate of staggered arrangement in described overflow settling pool, be provided with on the right side of described overflow settling pool and recycle pipe.
As further program of the utility model: described first filling tube is provided with the first magnetic valve, a pH monitoring probe is provided with in described first order reaction groove, a described pH monitoring probe is electrically connected with the first digital display type pH monitoring device outside first order reaction groove, and described first digital display type pH monitoring device is electrically connected with the first magnetic valve.
As the utility model further scheme: described second filling tube is provided with the second magnetic valve, the 2nd pH monitoring probe is provided with in described second order reaction groove, described 2nd pH monitoring probe is electrically connected with the second digital display type pH monitoring device outside second order reaction groove, and described second digital display type pH monitoring device is electrically connected with the second magnetic valve.
As the utility model further scheme: be provided with whipping appts in described first order reaction groove, second order reaction groove and third order reaction groove.
Compared with prior art, the beneficial effects of the utility model are: the acid rinse water in acid pond and the alkaline rinse water in alkaline pond are passed in neutralizing water tank and neutralize, nickel ion is made to generate nickel hydroxide precipitate in neutralizing water tank, sewage after neutralization enters in first order reaction groove, saturated milk of lime clear liquid groove adds saturated milk of lime clear liquid by the first filling tube to first order reaction groove, nickel ion is made to generate nickel hydroxide precipitate further, fluorion generates calcium fluoride precipitate simultaneously, aluminum ion is hydrolyzed in the basic conditions and generates various positively charged hydroxyl complex ion, carry calcium fluoride particles secretly, nickel hydroxide particle forms flco jointly, this waste water is after a Microfilter filters, and in filtrate, nickel ion concentration is up to standard, filtrate is inputted second order reaction groove, adds hydrochloric acid soln readjustment filtrate pH, impel between micelle and condensed by compression double electric layer in second order reaction groove, pass in third order reaction groove afterwards, calcium chloride solution in calcium chloride liquid bath is joined in third order reaction groove, calcium ion and fluorion can be made to react generation calcium fluoride particles further, filtered by secondary Microfilter and remove, after above-mentioned reaction, the fluorion in filtrate, nickel ion are all up to standard, filtrate after up to standard is passed into overflow settling pool, and is finally supplied to each cleaning equipment of aluminium section bar production from recycling pipe, recycle.Acid pond, alkaline pond and neutralizing water tank are set, reduce the consumption of saturated milk of lime clear liquid in subsequent disposal; First storage mud groove and the second storage mud groove are set, for collecting the mud containing heavy metal, are conducive to recycling, increase economic efficiency; Whipping appts is set, adds fast response, increase work efficiency; First digital display type pH monitoring device, a pH monitoring probe, the second digital display type pH monitoring device and the 2nd pH monitoring probe are set, be convenient to the pH value of Real-Time Monitoring first order reaction groove and second order reaction groove, and automatically control the first magnetic valve and the second magnetic valve, thus meet the processing requirement of producing, facilitate Automated condtrol.
In sum, this new structural design is reasonable, and adding less, reagent cost is low, and the treatment time is short, and treatment effect is stablized; Body refuse is recycled convenient, increases economic efficiency; Wastewater treatment whole-course automation can be realized control; By the recycling to waste water, reach the object of water saving, avoid sewage directly to discharge, protection of the environment simultaneously.
Accompanying drawing explanation
Fig. 1 is the structural representation of aluminium section bar production wastewater treatment cyclic utilization system.
In figure: the acid pond of 1-, 2-alkalescence pond, 3-neutralizing water tank, 4-first order reaction groove, 41-first filling tube, 42-first magnetic valve, 43-saturated milk of lime clear liquid groove, 44-first digital display type pH monitoring device, 45-the one pH monitoring probe, 5-first Microfilter, 51-first residue outlet, 52-first stores up mud groove, 6-second order reaction groove, 61-second filling tube, 62-second magnetic valve, 63-hydrochloric acid liquid bath, 64-second digital display type pH monitoring device, 65-the 2nd pH monitoring probe, 7-third order reaction groove, 71-calcium chloride liquid bath, 8-second Microfilter, 81-second residue outlet, 82-second stores up mud groove, 9-overflow settling pool, 91-dividing plate, 92-recycles pipe.
Embodiment
Below in conjunction with the accompanying drawing in the utility model embodiment, be clearly and completely described the technical scheme in the utility model embodiment, obviously, described embodiment is only the utility model part embodiment, instead of whole embodiments.Based on the embodiment in the utility model, those of ordinary skill in the art are not making the every other embodiment obtained under creative work prerequisite, all belong to the scope of the utility model protection.
Refer to Fig. 1, a kind of aluminium section bar production wastewater treatment cyclic utilization system, comprise acid pond 1 and alkaline pond 2, described acid pond 1 and alkaline pond 2 all with on the left of neutralizing water tank 3 are communicated with, and described neutralizing water tank 3 is from left to right connected with first order reaction groove 4, first Microfilter 5, second order reaction groove 6, third order reaction groove 7, second Microfilter 8 and overflow settling pool 9 in turn; Be provided with saturated milk of lime clear liquid groove 43 above described first order reaction groove 4, described saturated milk of lime clear liquid groove 43 is connected with bottom first order reaction groove 4 by the first filling tube 41; Described first Microfilter 5 lower end is provided with the first residue outlet 51, and described first residue outlet 51 lower end is provided with the first storage mud groove 52; Be provided with hydrochloric acid liquid bath 63 above described second order reaction groove 6, described hydrochloric acid liquid bath 63 is communicated with bottom second order reaction groove 6 by the second filling tube 61; Described third order reaction groove 7 upper end is provided with calcium chloride liquid bath 71; Described second Microfilter 8 lower end is provided with the second residue outlet 81, and described second residue outlet 81 lower end is provided with the second storage mud groove 82; Be provided with the dividing plate 91 of staggered arrangement in described overflow settling pool 9, be provided with on the right side of described overflow settling pool 9 and recycle pipe 92.
Principle of work of the present utility model is: the acid rinse water in acid pond 1 and the alkaline rinse water in alkaline pond 2 are passed into neutralization in neutralizing water tank 3, nickel ion is made to generate nickel hydroxide precipitate in neutralizing water tank 3, sewage after neutralization enters in first order reaction groove 4, saturated milk of lime clear liquid groove 43 adds saturated milk of lime clear liquid by the first filling tube 41 to first order reaction groove 4, nickel ion is made to generate nickel hydroxide precipitate further, fluorion generates calcium fluoride precipitate simultaneously, aluminum ion is hydrolyzed in the basic conditions and generates various positively charged hydroxyl complex ion, carry calcium fluoride particles secretly, nickel hydroxide particle forms flco jointly, this waste water is after a Microfilter 5 filters, and in filtrate, nickel ion concentration is up to standard, filtrate is inputted second order reaction groove 6, adds hydrochloric acid soln readjustment filtrate pH, impel between micelle and condensed by compression double electric layer in second order reaction groove 6, pass in third order reaction groove 7 afterwards, calcium chloride solution in calcium chloride liquid bath 71 is joined in third order reaction groove 7, calcium ion and fluorion can be made to react generation calcium fluoride particles further, filtered by secondary Microfilter 8 and remove, after above-mentioned reaction, the fluorion in filtrate, nickel ion are all up to standard, filtrate after up to standard is passed into overflow settling pool 9, and is finally supplied to each cleaning equipment of aluminium section bar production from recycling pipe 92, recycle.Acid pond 1, alkaline pond 2 and neutralizing water tank 3 are set, reduce the consumption of saturated milk of lime clear liquid in subsequent disposal; First storage mud groove 52 and the second storage mud groove 82 is set, for collecting the mud containing heavy metal, is conducive to recycling, increases economic efficiency; Whipping appts is set, adds fast response, increase work efficiency; First digital display type pH monitoring device the 44, the one pH monitoring probe 45, second digital display type pH monitoring device 64 and the 2nd pH monitoring probe 65 is set, be convenient to the pH value of Real-Time Monitoring first order reaction groove 4 and second order reaction groove 6, and automatically control the first magnetic valve 42 and the second magnetic valve 62, thus meet the processing requirement of producing, facilitate Automated condtrol.
In sum, this new structural design is reasonable, and adding less, reagent cost is low, and the treatment time is short, and treatment effect is stablized; Body refuse is recycled convenient, increases economic efficiency; Wastewater treatment whole-course automation can be realized control; By the recycling to waste water, reach the object of water saving, avoid sewage directly to discharge, protection of the environment simultaneously.
To those skilled in the art, obvious the utility model is not limited to the details of above-mentioned one exemplary embodiment, and when not deviating from spirit of the present utility model or essential characteristic, can realize the utility model in other specific forms.Therefore, no matter from which point, all should embodiment be regarded as exemplary, and be nonrestrictive, scope of the present utility model is limited by claims instead of above-mentioned explanation, and all changes be therefore intended in the implication of the equivalency by dropping on claim and scope are included in the utility model.Any Reference numeral in claim should be considered as the claim involved by limiting.
In addition, be to be understood that, although this specification sheets is described according to embodiment, but not each embodiment only comprises an independently technical scheme, this narrating mode of specification sheets is only for clarity sake, those skilled in the art should by specification sheets integrally, and the technical scheme in each embodiment also through appropriately combined, can form other embodiments that it will be appreciated by those skilled in the art that.
Claims (4)
1. an aluminium section bar production wastewater treatment cyclic utilization system, comprise acid pond and alkaline pond, it is characterized in that, described acid pond and alkaline pond are all communicated with on the left of neutralizing water tank, and described neutralizing water tank is from left to right connected with first order reaction groove, the first Microfilter, second order reaction groove, third order reaction groove, the second Microfilter and overflow settling pool in turn; Be provided with saturated milk of lime clear liquid groove above described first order reaction groove, described saturated milk of lime clear liquid groove is connected with first order reaction trench bottom by the first filling tube; Described first Microfilter lower end is provided with the first residue outlet, and described first residue outlet lower end is provided with the first storage mud groove; Be provided with hydrochloric acid liquid bath above described second order reaction groove, described hydrochloric acid liquid bath is communicated with second order reaction trench bottom by the second filling tube; Described third order reaction groove upper end is provided with calcium chloride liquid bath; Described second Microfilter lower end is provided with the second residue outlet, and described second residue outlet lower end is provided with the second storage mud groove; Be provided with the dividing plate of staggered arrangement in described overflow settling pool, be provided with on the right side of described overflow settling pool and recycle pipe.
2. aluminium section bar production wastewater treatment cyclic utilization system according to claim 1, it is characterized in that, described first filling tube is provided with the first magnetic valve, a pH monitoring probe is provided with in described first order reaction groove, a described pH monitoring probe is electrically connected with the first digital display type pH monitoring device outside first order reaction groove, and described first digital display type pH monitoring device is electrically connected with the first magnetic valve.
3. aluminium section bar production wastewater treatment cyclic utilization system according to claim 1, it is characterized in that, described second filling tube is provided with the second magnetic valve, the 2nd pH monitoring probe is provided with in described second order reaction groove, described 2nd pH monitoring probe is electrically connected with the second digital display type pH monitoring device outside second order reaction groove, and described second digital display type pH monitoring device is electrically connected with the second magnetic valve.
4. aluminium section bar production wastewater treatment cyclic utilization system according to claim 1, is characterized in that, is provided with whipping appts in described first order reaction groove, second order reaction groove and third order reaction groove.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520931658.4U CN205133304U (en) | 2015-11-20 | 2015-11-20 | Aluminium alloy waste water processing cycle utilizes system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520931658.4U CN205133304U (en) | 2015-11-20 | 2015-11-20 | Aluminium alloy waste water processing cycle utilizes system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205133304U true CN205133304U (en) | 2016-04-06 |
Family
ID=55619116
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520931658.4U Expired - Fee Related CN205133304U (en) | 2015-11-20 | 2015-11-20 | Aluminium alloy waste water processing cycle utilizes system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205133304U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108947027A (en) * | 2018-09-14 | 2018-12-07 | 兴发铝业（成都）有限公司 | Aluminum profile processing water pollution processing unit |
| CN110330134A (en) * | 2019-06-21 | 2019-10-15 | 浙江翔和环保工程有限公司 | A kind of alumina efficient treatment process for waster water with high |
-
2015
- 2015-11-20 CN CN201520931658.4U patent/CN205133304U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108947027A (en) * | 2018-09-14 | 2018-12-07 | 兴发铝业（成都）有限公司 | Aluminum profile processing water pollution processing unit |
| CN110330134A (en) * | 2019-06-21 | 2019-10-15 | 浙江翔和环保工程有限公司 | A kind of alumina efficient treatment process for waster water with high |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103553249B (en) | In electroplating effluent, acid is separated and heavy metal collection method | |
| CN102689956B (en) | Silicon removing method for silicone waste water | |
| CN104609613A (en) | Treatment device and treatment method for catalyst wastewater | |
| CN101289260B (en) | System and method for treating fluorine-containing acid wastewater after graphite purification | |
| CN102689999A (en) | Resourceful treatment method for silica gel waste water | |
| CN104817213A (en) | Heavy metal wastewater treatment process in electroplating and special device thereof | |
| CN205133304U (en) | Aluminium alloy waste water processing cycle utilizes system | |
| CN201433139Y (en) | Waste water treatment recirculation system used for PS plate production | |
| CN203382824U (en) | Device for recovering refined copper from low-copper-content wastewater | |
| CN204625394U (en) | Nickeliferous waste liquid electrolytic recovery device | |
| CN103771629A (en) | Pretreatment technology of hot-galvanizing wastewater | |
| CN204138483U (en) | Pickling nickel waste water reclaims cyclic regeneration device | |
| CN203904040U (en) | System for recycling manganese containing wastewater | |
| CN102838254A (en) | Treatment process for acidic heavy metal wastewater | |
| CN102560537A (en) | Silver recovery device for silver-containing waste liquor | |
| CN204727647U (en) | A kind of micro-electrolysis reactor | |
| CN210085182U (en) | Coal gasification grey water treatment system | |
| CN204174288U (en) | A kind of ion film caustic soda production equipment improving bittern usage ratio | |
| CN203065593U (en) | Copper-extracting device for low-copper diluted-acid wastewater | |
| CN204079655U (en) | A kind of containing cadmium electroplating waste water treatment system | |
| CN106430724A (en) | High-concentration heavy metal ion containing waste water treatment method and treatment system of waste water | |
| CN102703317A (en) | Electroflocculation microalgae-collecting device | |
| CN204874739U (en) | Electrolytic manganese passivation fluid recovery unit | |
| CN208378590U (en) | A kind of device for stainless steel electrolytic polishing wastewater treatment | |
| CN207929010U (en) | A kind of dilute sodium hydroxide electrodialysis concentration film group device |
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: 20160406 Termination date: 20161120 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |