CN109437463A - Coal calcination vanadium extraction high-salt wastewater advanced treatment and reclamation device and application method - Google Patents
Coal calcination vanadium extraction high-salt wastewater advanced treatment and reclamation device and application method Download PDFInfo
- Publication number
- CN109437463A CN109437463A CN201811632206.0A CN201811632206A CN109437463A CN 109437463 A CN109437463 A CN 109437463A CN 201811632206 A CN201811632206 A CN 201811632206A CN 109437463 A CN109437463 A CN 109437463A
- Authority
- CN
- China
- Prior art keywords
- water
- reverse osmosis
- pump
- super
- tank
- 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.)
- Granted
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/02—Treatment of water, waste water, or sewage by heating
- C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/38—Treatment of water, waste water, or sewage by centrifugal separation
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
- C02F1/441—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by reverse osmosis
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2301/00—General aspects of water treatment
- C02F2301/08—Multistage treatments, e.g. repetition of the same process step under different conditions
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/22—Eliminating or preventing deposits, scale removal, scale prevention
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F5/00—Softening water; Preventing scale; Adding scale preventatives or scale removers to water, e.g. adding sequestering agents
- C02F5/08—Treatment of water with complexing chemicals or other solubilising agents for softening, scale prevention or scale removal, e.g. adding sequestering agents
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
Abstract
The present invention relates to a kind of coal calcination vanadium extraction high-salt wastewater advanced treatment and reclamation devices and methods therefors, the characteristics of highly acid for being generated for blank roasting sulfuric acid suppression silicon water logging process for extracting vanadium, high-salt wastewater containing a large amount of iron, aluminium, sulfate radical, other heavy metal ion and a small amount of metavanadic acid root, vanadium extraction high-salt wastewater is passed through into pretreatment system first, add the pH value that a large amount of lime improves waste water, utilize neutralization, precipitating, oxidation, film filtering, with heavy-metal ion removal and part of sulfuric acid radical ion, COD, suspended matter and TDS are reduced；Secondly by concentrating and treating system, using it is reverse osmosis with super-pressure is reverse osmosis is reduced Waste water concentrating；Finally, going out crystal salt by evaporation and crystallization system evaporative crystallization；The condensate liquid of reverse osmosis production water, super-pressure reverse osmosis production water and evaporation and crystallization system meets the requirement of recycle-water, is back to use vanadium extraction production workshop section, achievees the purpose that coal calcination vanadium extraction high-salt wastewater advanced treatment and reclamation.
Description
Technical field
The present invention is a kind of coal calcination vanadium extraction high-salt wastewater advanced treatment and reclamation device and application method, belongs to work
Industry technical field of waste water processing.
Background technique
Vanadium is a kind of transition elements, atomic number 23, atomic weight 50.9.Vanadium is that have body-centered cubic in silver grey non-ferrous metal
Structure, 1890 ± 10 DEG C of fusing point, 3380 DEG C of boiling point.Vanadium possesses good physical property, stable chemical property and catalytic activity,
It is widely used in the fields such as metallurgy, steel, chemical industry, building materials, dyestuff, battery.
It is vanadium titano-magnetite and bone coal in the primary raw material of China, vanadium extraction, and the bone coal reserves in China are very rich, extensively
It is distributed in the ground such as Hunan, Hubei, Zhejiang, Jiangxi, Guangdong, Guangxi, Guizhou, Anhui, Henan, Shaanxi, Gansu.Vanadium master in bone coal
To exist with trivalent, most process for extracting vanadium will first be oxidized to 5 valences, be dissolved out with sodium metavanadate, ammonium chloride precipitation is then utilized,
Ammonium metavanadate is generated, and then vanadic anhydride can be made with deamination.Currently, extracting vanadium from stone coal main technique has: low sodium roasts water logging
Technique, calcium salt baking acid immersion technique, is exempted to roast direct dilute sulfuric acid technique blank baking acid immersion technique.
Blank roasts sulfuric acid and presses down silicon water logging process for extracting vanadium, production process are as follows: " broken ore grinding → blank roasting → sulfuric acid suppression
Silicon → leaching filtering → ion exchange → purification and washing → precipitation is dry, and product is ammonium metavanadate ".It is main during it to generate two
Kind waste water, one is deposition vanadium mother liquid, is a kind of high ammonia-nitrogen wastewater；It is a kind of strong secondly being the resin adsorption extraction raffinate of ion exchange
The acid, high-salt wastewater containing a large amount of iron, aluminium, sulfate radical, other heavy metal ion and a small amount of metavanadic acid root, to environment
It is very harmful.Currently, still without pressing down the highly acid of silicon water logging process for extracting vanadium generation, containing a large amount of for novel blank roasting sulfuric acid
Iron, aluminium, sulfate radical, other heavy metal ion and a small amount of metavanadic acid root high-salt wastewater technology, it is similar to have part
Patent is handled for extracting vanadium from stone coal high-salt wastewater, such as a kind of 201210110313.3 General Office of extracting vanadium from stone coal brine waste
Reason method, main technique are that " extracting vanadium from stone coal brine waste, pole-reversing electroosmosis carry out desalination, pressure reducing film distillation is concentrated, is crystallized
It evaporates brine, electric osmose division fresh water and recycling condensing water "；200910273138.8 a kind of high-salinity heavy metal-enriched waste water from vanadium extraction from stone coal
Recycling processing method, main technique are that " vanadium extraction high-salinity heavy metal-enriched waste water adds lime, sodium carbonate, PAC and PAM coagulation heavy
It forming sediment, the filter cake of bed mud filters pressing is used as building admixture, and supernatant is through electrodialysis desalination, concentrated water evaporative crystallization, the Nacl of generation,
Fresh water and Condensate reuse process for extracting vanadium from stone coal "；It is both the high-salt wastewater generated for the roasting water logging technique vanadium extraction of low sodium,
Treatment for Reuse, while reuse sodium chloride have been carried out to extracting vanadium from stone coal high-salt wastewater using electrodialysis desalination and concentrated water evaporative crystallization,
But unrecovered metavanadic acid root.And electrodialysis energy consumption is larger, and producing water water quality is lower than reverse osmosis again, still there is many defects.It needs out
It sends out a kind of and presses down the highly acid of silicon water logging process for extracting vanadium generation for novel blank roasting sulfuric acid, contains a large amount of iron, aluminium, sulfuric acid
The advanced treatment and reclamation technology of the high-salt wastewater of root, other heavy metal ion and a small amount of metavanadic acid root.
Summary of the invention
Proposed by the present invention is a kind of coal calcination vanadium extraction high-salt wastewater advanced treatment and reclamation device and application method,
Its object is to the highly acid generated for novel blank roasting sulfuric acid suppression silicon water logging process for extracting vanadium, contain a large amount of iron, aluminium, sulphur
The characteristics of high-salt wastewater of acid group, other heavy metal ion and a small amount of metavanadic acid root, and can be serious dirty if processing is bad
Environment is contaminated, and wastes the defect of valuable vanadium resource, proposes a kind of coal calcination vanadium extraction high-salt wastewater advanced treatment and reclamation
Wastewater treatment to the requirement for meeting recycle-water can be back to use vanadium extraction production workshop section, it is high to reach coal calcination vanadium extraction by device
The purpose of salt waste water advanced treatment recovery.
Technical solution of the invention: coal calcination vanadium extraction high-salt wastewater advanced treating treatment for reuse device,
Structure include pretreatment system PTS, concentrating and treating system CTS, evaporation and crystallization system VCS, recycle-water storage send system RCWT；Wherein
Resin adsorption extraction raffinate TW is connected to the water inlet of pretreatment system PTS, the water outlet and concentrating and treating system of pretreatment system PTS
The water inlet of CTS connects, and the mud mouth of pretreatment system PTS sends out mud cake SC, and the liquid outlet of pretreatment system PTS sends out desorption
Sodium metavanadate solution NaVO3；Pretreatment system PTS not only improves the pH value of waste water, eliminates heavy metal ion and part
Sulfate ion, it is often more important that further recycled the metavanadic acid root in waste water, vanadium resource is more effectively utilized；Concentration
The liquid outlet of system CTS connects with the inlet of evaporation and crystallization system VCS, the water outlet and recycle-water of concentrating and treating system CTS
Storage send the 1# water inlet of system RCWT to connect；Waste water concentrating is reduced output concentrated water by concentrating and treating system CTS, is convenient for subsequent evaporation
Crystal system steams crystal salt, while output fresh water meets reuse requirement；The salt outlet of evaporation and crystallization system VCS sends out crystal salt
The condensate outlet of Salt, evaporation and crystallization system VCS send the 2# water inlet of system RCWT to connect with recycle-water storage；Evaporative crystallization system
System VCS evaporative crystallization output crystal salt, while the condensed water of output also meets reuse requirement；Going out for system RCWT is sent in recycle-water storage
Recycle-water RCW is sent out at the mouth of a river, is back to use the different workshop sections of vanadium extraction production, is reached coal calcination vanadium extraction high-salt wastewater depth
Manage the purpose of reuse.
Blank roasts sulfuric acid suppression silicon water logging process for extracting vanadium for the high siliceous feature of bone coal, and silicon is mostly present in stone with metasilicic acid root
In coal, it can largely be dissolved out in water logging, influence vanadium extraction efficiency；In production, metasilicic acid root is converted to SiO by adding sulfuric acid2
And stay in slag, achieve the purpose that press down silicon；But sulfuric acid dissolves out the metal ions such as a large amount of aluminium, iron, water logging in bone coal again simultaneously
When not only leached metavanadic acid root, can also leach a large amount of heavy metal ion, in vanadium extracting process, meeting after resin adsorption metavanadic acid root
Highly acid, the high-salt wastewater containing a large amount of iron, aluminium, sulfate radical, other heavy metal ion and a small amount of metavanadic acid root are generated, i.e.,
For resin adsorption extraction raffinate, processing will add a large amount of lime neutralisation of sulphuric acid, form saturation calcium sulfate and remove sulphate moiety
It removes, while the metal ion in remaining hydroxyl and waste water is combined into the precipitate metal hydroxides of indissoluble, reaches and improve pH
Value, heavy-metal ion removal and the purpose for partially removing sulfate radical, while the TDS value of waste water is reduced, be conducive to subsequent concentration and subtract
Amount and evaporative crystallization.
Its main chemical reactions equation is as follows:
CaO + H2O = Ca2+ + 2OH- ①
Ca2+ + SO4 2- = CaSO4↓ ②
Fe3+ + 3OH- = Fe(OH)3↓ ③
Al3+ + 3OH- = Al(OH)3↓ ④
Me2+ + 2OH- = Me(OH)2↓ ⑤
Formula 2. in, under room temperature, the saturated concentration of calcium sulfate is 2600ppm, formula 5. in, Me indicates bivalent metal ion.
Coal calcination vanadium extraction high-salt wastewater advanced treatment and reclamation method, includes the following steps:
1) resin adsorption extraction raffinate is utilized the neutralization of a large amount of lime, precipitating and advanced oxygen by the preceding part for passing through pretreatment system
Change, the pH value of film filtering lifting waste water is to 6~8, while heavy-metal ion removal and part of sulfuric acid radical ion, reducing COD and outstanding
TDS is reduced to 8000~12000ppm by floating object content；
2) the rear part for passing through pretreatment system is effectively recycled using the metavanadic acid root in resin adsorption recycling waste water
Vanadium resource；
3) pretreatment water outlet carries out concentration decrement using reverse osmosis technology, is concentrated 10~15 times by concentrating and treating system, will
TDS is concentrated to 120000~150000ppm, in order to which subsequent evaporation crystal system steams crystal salt, while output fresh water,
TDS < 200ppm meets reuse requirement；
4) concentrated water of concentrating and treating system goes out crystal salt, while output condensed water by evaporation and crystallization system, evaporative crystallization,
TDS < 200ppm meets reuse requirement；
5) recycle-water is made in the condensed water remittance of the production water of concentrating and treating system, evaporation and crystallization system, send system by recycle-water storage, into
Row storage, the different workshop sections for being transmitted back to vanadium extraction production, reach the mesh of coal calcination vanadium extraction high-salt wastewater advanced treatment and reclamation
's.
Beneficial effects of the present invention: press down the highly acid of silicon water logging process for extracting vanadium generation for novel blank roasting sulfuric acid, contain
There is the characteristics of high-salt wastewater of a large amount of iron, aluminium, sulfate radical, other heavy metal ion and a small amount of metavanadic acid root, will mention first
Vanadium high-salt wastewater adds the pH value that a large amount of lime improves waste water by pretreatment system, using neutralizing, precipitating, aoxidizes, film mistake
Filter reduces COD, suspended matter and TDS with heavy-metal ion removal and part of sulfuric acid radical ion；Secondly by concentration system
System, using it is reverse osmosis with super-pressure is reverse osmosis is reduced Waste water concentrating；Finally, going out to crystallize by evaporation and crystallization system evaporative crystallization
Salt；The condensate liquid of reverse osmosis production water, super-pressure reverse osmosis production water and evaporation and crystallization system meets the requirement of recycle-water, reuse
Workshop section is produced to vanadium extraction, achievees the purpose that coal calcination vanadium extraction high-salt wastewater advanced treatment and reclamation.
Detailed description of the invention
Attached drawing 1 is the general structure schematic diagram of coal calcination vanadium extraction high-salt wastewater advanced treatment and reclamation device.
Attached drawing 2 is the structural representation of coal calcination vanadium extraction high-salt wastewater advanced treatment and reclamation device pretreatment system
Figure.
Attached drawing 3 is that coal calcination vanadium extraction high-salt wastewater advanced treatment and reclamation device concentration systems and recycle-water storage are sent and be
The structural schematic diagram of system.
Attached drawing 4 is the technique stream of coal calcination vanadium extraction high-salt wastewater advanced treatment and reclamation devices and methods therefor embodiment
Cheng Tu.
Attached drawing 5 is the water balance of coal calcination vanadium extraction high-salt wastewater advanced treatment and reclamation devices and methods therefor embodiment
Figure.
TW indicates that resin adsorption extraction raffinate, Salt indicate crystal salt, NaVO in figure3Indicate sodium metavanadate solution, the SC of desorption
Indicate that mud cake, RCW indicate recycle-water (reverse osmosis produced water and evaporative crystallization condensate)；PTS indicates that pretreatment system, CTS indicate dense
Contracting processing system, VCS indicate that evaporation and crystallization system, RCWT indicate that system is sent in recycle-water storage.
PTS indicates pretreatment system；TW indicates that resin adsorption extraction raffinate, SC indicate mud cake, NaVO3Indicate the metavanadic acid of desorption
Sodium solution, PTout indicate pretreatment system water outlet；T1Indicate extraction raffinate water tank, T2Indicate intermediate water tank, T3Expression ultrafiltration water producing tank,
T4Indicate sodium metavanadate liquor box；D1Indicate lime throwing device, D2Indicate sodium carbonate, coagulant, flocculation aid throwing device, D3
Indicate feeding apparatus for powdered activated charcoal, D4Indicate fungicide throwing device, D5Indicate sodium hydroxide strippant throwing device；NR1Table
Show level-one neutralization reaction pond, ST1Indicate first stage precipitation tank, NR2Indicate second level neutralization reaction pond, ST2Indicate second-level settling pond, AOD
Indicate that advanced oxidation device, HT indicate that resolution case, MSD indicate that membrane separation device, RET indicate that absorption resin container, SD indicate sludge
Dehydration device；P1Indicate extraction raffinate elevator pump, P2Indicate middle water pump, P3Indicate ultrafiltration suction pump, P4Indicate reverse osmosis booster pump, P5
Indicate hyperfiltration reverse-rinsing pump, P6Indicate first stage precipitation tank sludge pump, P7Indicate second-level settling pond sludge pump, P8Indicate that sodium metavanadate is molten
Liquid delivery pump.
CTS indicates that concentrating and treating system, RCWT indicate that system is sent in recycle-water storage；The water outlet of PTout expression pretreatment system,
RCW indicates that recycle-water, Salt indicate crystal salt；T5Indicate reverse osmosis concentrated water tank, T6The expression reverse osmosis concentrated water tank of super-pressure (and
Evaporation and crystallization system liquid supply box), T7Indicate reuse water tank；D6Indicate antisludging agent and reducing agent throwing device, D7Indicate that antisludging agent is thrown
Feeder apparatus；SAF1Indicate that reverse osmosis cartridge filter, RO indicate reverse osmosis unit, SAF2Indicate the filtering of super-pressure reverse osmosis cartridge
Device, UHPRO indicate that super-pressure reverse osmosis unit, VCS indicate evaporation and crystallization system；P9Indicate reverse osmosis high-pressure pump, P10Indicate super
High pressure reverse osmosis booster pump, P11Indicate the reverse osmosis plunger pump of super-pressure, P12Indicate evaporation and crystallization system solution feed pump, P13It indicates back
Use water pump.
Specific embodiment
Further explanation of the technical solution of the present invention with reference to the accompanying drawing
As shown in Fig. 1, coal calcination vanadium extraction high-salt wastewater advanced treatment and reclamation device, structure include pretreatment system
System RCWT is sent in PTS, concentrating and treating system CTS, evaporation and crystallization system VCS, recycle-water storage；Wherein resin adsorption extraction raffinate TW is connected to
The water outlet of the water inlet of pretreatment system PTS, pretreatment system PTS connects with the water inlet of concentrating and treating system CTS, pre- to locate
The mud mouth of reason system PTS sends out mud cake SC, and the liquid outlet of pretreatment system PTS sends out the sodium metavanadate solution NaVO of desorption3；
Pretreatment system PTS not only improves the pH value of waste water, eliminates heavy metal ion and part of sulfuric acid radical ion, it is often more important that
The metavanadic acid root in waste water has further been recycled, vanadium resource is more effectively utilized；The liquid outlet of concentrating and treating system CTS and evaporation
The inlet of crystal system VCS connects, and the 1# water inlet of system RCWT is sent in water outlet and the recycle-water storage of concentrating and treating system CTS
Connect；Waste water concentrating is reduced output concentrated water by concentrating and treating system CTS, steams crystal salt convenient for subsequent evaporation crystal system, together
When output fresh water meet reuse requirement；The salt outlet of evaporation and crystallization system VCS sends out crystal salt Salt, evaporation and crystallization system VCS
The storage of condensate outlet and recycle-water send the 2# water inlet of system RCWT to connect；Evaporation and crystallization system VCS evaporative crystallization output knot
Brilliant salt, while the condensed water of output also meets reuse requirement；Recycle-water storage send the water outlet of system RCWT to send out recycle-water RCW,
The different workshop sections of vanadium extraction production are back to use, achieve the purpose that coal calcination vanadium extraction high-salt wastewater advanced treatment and reclamation.
Coal calcination vanadium extraction high-salt wastewater advanced treatment and reclamation device pretreatment system PTS, structure includes extraction raffinate
Water tank T1, level-one neutralization reaction pond NR1, first stage precipitation tank ST1, second level neutralization reaction pond NR2, second-level settling pond ST2, intermediate water
Case T2, advanced oxidation device AOD, resolution case HT, membrane separation device MSD, ultrafiltration water producing tank T3, absorption resin container RET, metavanadic acid
Sodium solution case T4, sludge dehydration device SD, lime throwing device D1, sodium carbonate, coagulant, flocculation aid throwing device D2, powder
Activated charcoal adding apparatus D3, fungicide throwing device D4, sodium hydroxide strippant throwing device D5 and extraction raffinate elevator pump P1,
Middle water pump P2, ultrafiltration suction pump P3, reverse osmosis booster pump P4, hyperfiltration reverse-rinsing pump P5, first stage precipitation tank sludge pump P6, second level are heavy
Shallow lake pond sludge pump P7, sodium metavanadate solution transfer pump P8.Wherein resin adsorption extraction raffinate TW is connected to the water inlet of extraction raffinate water tank T1, remaining
The water outlet of liquid water tank T1 is connected by extraction raffinate elevator pump P1 with the water inlet of level-one neutralization reaction pond NR1, lime throwing device
The medicine outlet of D1 connects with the feeding opening of level-one neutralization reaction pond NR1, and the water outlet and level-one of level-one neutralization reaction pond NR1 precipitates
The water inlet of pond ST1 connects, and the mud mouth of first stage precipitation tank ST1 passes through first stage precipitation tank sludge pump P6 and sludge dehydration device SD
1# mud inlet connect, the water outlet of first stage precipitation tank ST1 connects with the water inlet of second level neutralization reaction pond NR2, sodium carbonate, mixed
Coagulate agent, the medicine outlet of flocculation aid throwing device D2 connects with the feeding opening of second level neutralization reaction pond NR2, second level neutralization reaction pond
The water outlet of NR2 connects with the water inlet of second-level settling pond ST2, and the mud mouth of second-level settling pond ST2 is arranged by second-level settling pond
Dredge pump P7 connects with the 2# mud inlet of sludge dehydration device SD, and pressing filtering liquid is connected to extraction raffinate water by the liquid outlet of sludge dehydration device SD
The mud mouth of the inlet of case T1, sludge dehydration device SD sends out mud cake SC；The water outlet and intermediate water tank of second-level settling pond ST2
The water inlet of T2 connects, and the water outlet of intermediate water tank T2 is connected by middle water pump P2 with the water inlet of advanced oxidation device AOD,
The water outlet of advanced oxidation device AOD with resolution case HT water inlet connect, the medicine outlet of feeding apparatus for powdered activated charcoal D3 with
The feeding opening of resolution case HT connects, and the water outlet of resolution case HT connects with the water inlet of membrane separation device MSD, and fungicide adds dress
The medicine outlet for setting D4 connects with the feeding opening of membrane separation device MSD；The water outlet of membrane separation device MSD passes through ultrafiltration suction pump P3
Connect with the water inlet of ultrafiltration water producing tank T3, the backwash water out of ultrafiltration water producing tank T3 pumps P5 by hyperfiltration reverse-rinsing and UF membrane fills
The backwash water inlet for setting MSD connects, the backwash discharge outlet and the 3# mud inlet phase of sludge dehydration device SD of membrane separation device MSD
It connects；The water outlet of ultrafiltration water producing tank T3 is connected by reverse osmosis booster pump P4 with the water inlet of absorption resin container RET, sodium hydroxide
The liquid outlet of strippant throwing device D5 with absorption resin container RET inlet connect, adsorb resin container RET liquid outlet and partially
The inlet of sodium vanadate solution case T4 connects, and the liquid outlet of sodium metavanadate liquor box T4 is sent by sodium metavanadate solution transfer pump P8
The sodium metavanadate solution NaVO3 desorbed out；The water outlet for adsorbing resin container RET sends out pretreatment system and is discharged PTout.
Compare attached drawing 3, coal calcination vanadium extraction high-salt wastewater advanced treatment and reclamation device concentration systems CTS and recycle-water
System RCWT is sent in storage, structure include reverse osmosis cartridge filter SAF1, RO indicate reverse osmosis unit, reverse osmosis concentrated water tank T5,
Super-pressure reverse osmosis cartridge filter SAF2, super-pressure reverse osmosis unit UHPRO, the reverse osmosis concentrated water tank T6(of super-pressure are also to steam
Send out crystal system liquid supply box), evaporation and crystallization system VCS, reuse water tank T7, antisludging agent and reducing agent throwing device D6, antisludging agent
Throwing device D7 and reverse osmosis high-pressure pump P9, it super-pressure reverse osmosis booster pump P10, the reverse osmosis plunger pump P11 of super-pressure, steams
Send out crystal system solution feed pump P12, reuse water pump P13.Wherein pretreatment system water outlet PTout is connected to reverse osmosis cartridge filter
The medicine outlet of the water inlet of SAF1, antisludging agent and reducing agent throwing device D6 are also connected to the water inlet of reverse osmosis cartridge filter SAF1
Mouthful, the water outlet of reverse osmosis cartridge filter SAF1 pumps P9 by reverse osmosis high-pressure and connects with the water inlet of reverse osmosis unit RO,
The concentrated water outlet of reverse osmosis unit RO connects with the water inlet of reverse osmosis concentrated water tank T5, and the water outlet of reverse osmosis concentrated water tank T5 passes through
Super-pressure reverse osmosis booster pump P10 is connected to the water inlet of super-pressure reverse osmosis cartridge filter SAF2, scale inhibitor feeding device D7
Medicine outlet be also connected to the water inlet of super-pressure reverse osmosis cartridge filter SAF2, super-pressure reverse osmosis cartridge filter SAF2's
Water outlet is connected by the reverse osmosis plunger pump P11 of super-pressure with the water inlet of super-pressure reverse osmosis unit UHPRO；Reverse osmosis unit
The production water out of RO and the production water out of super-pressure reverse osmosis unit UHPRO are all connected to the 1# water inlet of reuse water tank T7, reuse
The water outlet of water tank T7 sends out recycle-water RCW by reuse water pump P13；Super-pressure reverse osmosis unit UHPRO concentrated water outlet with
The reverse osmosis concentrated water tank T6 of super-pressure connects, and the reverse osmosis concentrated water tank T6(of super-pressure is also evaporation and crystallization system liquid supply box) pass through evaporation
Crystal system solution feed pump P12 is connected to the inlet of evaporation and crystallization system VCS, and the condensation-water drain of evaporation and crystallization system VCS is connected to
The salt outlet of the 2# water inlet of reuse water tank T7, evaporation and crystallization system VCS sends out crystal salt Salt.
Coal calcination vanadium extraction high-salt wastewater advanced treatment and reclamation method, includes the following steps:
1) resin adsorption extraction raffinate is utilized the neutralization of a large amount of lime, precipitating and advanced oxygen by the preceding part for passing through pretreatment system
Change, the pH value of film filtering lifting waste water is to 6~8, while heavy-metal ion removal and part of sulfuric acid radical ion, reducing COD and outstanding
TDS is reduced to 8000~12000ppm by floating object content；
2) the rear part for passing through pretreatment system is effectively recycled using the metavanadic acid root in resin adsorption recycling waste water
Vanadium resource；
3) pretreatment water outlet carries out concentration decrement using reverse osmosis technology, is concentrated 10~15 times by concentrating and treating system, will
TDS is concentrated to 120000~150000ppm, in order to which subsequent evaporation crystal system steams crystal salt, while output fresh water,
TDS < 200ppm meets reuse requirement；
4) concentrated water of concentrating and treating system goes out crystal salt, while output condensed water by evaporation and crystallization system, evaporative crystallization,
TDS < 200ppm also meets reuse requirement；
5) recycle-water is made in the condensed water remittance of the production water of concentrating and treating system, evaporation and crystallization system, send system by recycle-water storage, into
Row storage, the different workshop sections for being transmitted back to vanadium extraction production, reach the mesh of coal calcination vanadium extraction high-salt wastewater advanced treatment and reclamation
's.
The step 1) by the preceding part of pretreatment system, specifically resin adsorption extraction raffinate pass sequentially through extraction raffinate water tank,
Extraction raffinate elevator pump, level-one neutralization reaction pond, first stage precipitation tank, second level neutralization reaction pond, second-level settling pond, intermediate water tank, centre
Water pump, advanced oxidation device, resolution case, membrane separation device, ultrafiltration suction pump are until ultrafiltration water producing tank, by level-one and anti-
Ying Chizhong adds a large amount of lime and is neutralized, precipitated, by adding sodium carbonate in second level neutralization reaction pond, coagulant, helping
Solidifying agent is neutralized, is precipitated, and absorption and drainage is carried out by adding Powdered Activated Carbon in resolution case, by throwing in membrane separation device
Adding of germicide protects ultrafiltration membrane, finally reduces COD using advanced oxidation, is further removed by filtration suspended matter using ultrafiltration membrane, most
The pH value of waste water is increased to 6~8 from 1~2 at last, forms solid metal using hydroxide ion a large amount of in water and metal ion
Hydroxide and heavy-metal ion removal, and using the low solubility characteristic of calcium sulfate at normal temperature remove most of sulfate radical from
TDS is reduced to 8000~12000ppm from 50000~80000ppm by son；Ultrafiltration membrane timing backwash, guarantees flux, and ultrafiltration is anti-
The spoil disposal for washing draining, one and second-level settling pond is dehydrated using sludge dehydration device, filtrate return processing, sludge outward transport.
The step 2 passes through the rear part of pretreatment system, and the specifically water outlet of ultrafiltration water producing tank passes through reverse osmosis pressurization
Absorption resin container is sent into pump pressurization, using the metavanadic acid root in macroporous anion exchange resin absorption waste water, adsorbs metavanadic acid root
Water afterwards is the water outlet of entire pretreatment system；After resin adsorption saturation, set using 5~15% sodium hydroxide strippant from absorption
Rouge tank desorbs sodium metavanadate, and utilizes sodium metavanadate liquor box and sodium metavanadate solution transfer pump by sodium metavanadate solution storage
With send precipitation pond back to, effectively recycle vanadium resource.
The step 3) pretreatment water outlet passes sequentially through reverse osmosis by concentrating and treating system, specifically pretreatment system water outlet
Saturating cartridge filter, reverse osmosis high-pressure pump, reverse osmosis unit RO, reverse osmosis concentrated water tank, super-pressure reverse osmosis booster pump, super-pressure
The reverse osmosis plunger pump of reverse osmosis cartridge filter, super-pressure, super-pressure reverse osmosis unit, the reverse osmosis concentrated water tank of super-pressure, evaporation
Crystal system feed flow pumps out the concentrated water of super-pressure reverse osmosis unit；Reverse osmosis unit is by antisludging agent and reducing agent, reverse osmosis guarantor
Peace filter is protected, by 5~6 times of waste water initial concentration, its TDS is concentrated to 48000 from 8000~12000ppm~
60000ppm；Super-pressure is reverse osmosis to be protected by antisludging agent super-pressure reverse osmosis cartridge filter, further will be reverse osmosis concentrated
Water is concentrated 2~2.5 times, its TDS is concentrated to 120000~150000ppm from 48000~60000ppm；Whole system is by waste water
10~15 times of concentration, in order to which subsequent evaporation crystal system steams crystal salt, while output fresh water, TDS < 200ppm meets
The requirement of recycle-water.
The concentrated water of the step 4) concentrating and treating system passes through evaporation and crystallization system, the specifically reverse osmosis concentrated water of super-pressure
Concentration be 120000~150000ppm, by heat exchanger in evaporation and crystallization system, crystal separator, hydrops tank, force to follow
The evaporative crystallizations such as ring pump, discharging pump, centrifuge isolate crystal salt, while output condensed water, and TDS < 200ppm also meets back
With the requirement of water.
Recycle-water is made in the production water of the step 5) concentrating and treating system, the condensed water remittance of evaporation and crystallization system, passes through reuse
System is sent in water storage, what specifically concentrating and treating system was reverse osmosis produce water, super-pressure it is reverse osmosis produce water and evaporation and crystallization system
Condensed water imports reuse water tank and is stored, and the different workshop sections of vanadium extraction production are sent to by recycle-water blowback, reaches bone coal sky
The purpose of white roasting vanadium extraction high-salt wastewater advanced treatment and reclamation.
Embodiment 1
Certain Mining Development Co., Ltd is using in Rock coal containing alum vanadium extracting process, according to local bone coal is siliceous and the high spy of carbon
Point carries out bone coal ore first with recirculating fluidized bed decarburization boiler pre- to avoid bone coal calorific value height from easily causing sintering phenomenon
First decarburization power generation, then tunnel oven blank roasting technique is utilized to the cinder after decarburization, trivalent vanadium is oxidized to 5 valence vanadium, and utilize sulphur
Acid suppression silicon, water logging filtering, resin inhale vanadium, sodium hydroxide and common salt and desorb to obtain sodium metavanadate, finally utilize ammonium chloride precipitation,
Obtain ammonium metavanadate product.Extracting vanadium from stone coal band cogeneration project year utilizes 500,000 tons of bone coal, and 3 kiloton of year vanadium extraction generates electricity
1.75 hundred million degree, achieve preferable economic benefit.
Various wastewater can be generated in vanadium extraction production, considers to carry out sub-prime multiplexing to waste water as far as possible, reduces waste water discharge, here
Mainly there are 2 kinds of waste water to be discharged into waste water processing station and carry out treatment for reuse, one is the high ammonia nitrogen mother liquor of precipitation (is washed containing ammonium metavanadate
Water), ammonium chloride, sodium chloride containing high concentration can use evaporative crystallization and ammonium chloride and sodium chloride is separately recovered.The second is tree
Rouge adsorbs extraction raffinate (including power plant cycle sewerage, part resin regeneration wash water), be a kind of highly acid, containing a large amount of iron, aluminium,
The high-salt wastewater of sulfate radical, other heavy metal ion and a small amount of metavanadic acid root corresponds to the art of this patent below and only lists resin
Adsorb the treatment for reuse engineering design of extraction raffinate.
Design influent quality, water
Design water inlet (resin adsorption extraction raffinate) water is 2880T/D(120T/H).Its water quality indicator is as follows:
After lime, the processing of soda ash chemical precipitation method, water about 112t/h, water quality is as follows:
Here, removing heavy metals, part of sulfuric acid salt are gone using chemical precipitation method, heavy metal remaining is micro.Subsequent concentration, resin are inhaled
Attached, evaporative crystallization is designed with this water quality.
Sewage treatment technology process
Resin adsorption extraction raffinate advanced treatment recycling technique process is referring to 4 coal calcination vanadium extracting waste water advanced treatment and reclamation of attached drawing
The process flow chart of devices and methods therefor embodiment.
Resin adsorption extraction raffinate (including Electric Factory Air-Cooling draining, part resin regeneration wash water) enters conditioning tank progress water quality in figure
The well-balanced adjustment of water enters first order reaction pond using elevator pump, by adding a large amount of lime neutralisation of sulphuric acid, improving pH value,
So that calcium sulfate saturated crystallization, while metal ion and hydroxyl are formed into hydroxide, utilize booster pump, concentration squeezing one
Machine removes part of sulfuric acid root and heavy metal ion, and filtrate enters 1# intermediate pool, boosted to be pumped into second order reaction pond, then adds
Soda ash removes extra calcium ion by booster pump, concentration squeezing all-in-one machine, and filtrate enters 2# intermediate pool, boosted pumping
Enter one-step purifier further (passing through dosing coagulant) coagulation, precipitation and purification, I and II reaction tank concentration squeezing all-in-one machine
Sludge is sent out by sludge conveyer, and a small amount of spoil disposal of one-step purifier returns to conditioning tank；The water outlet of one-step purifier enters electricity
Solution and digestion instrument, carrying out electrolytic oxidation reduces COD, and carries out absorption and drainage by adding Powdered Activated Carbon, and then utilize
Membrane separation device and suction water pump further go oil removal to purify water, and the backwash water of membrane separation device returns to water among 2#
The production water in pond, membrane separation device enters membrane separation device water producing tank, passes through high pressure RO booster pump, (adding reducing agent, antisludging agent)
Cartridge filter, high-pressure pump enter high pressure RO device, carry out initial concentration, the TDS in waste water is increased to from 10158ppm
55978ppm, the concentrated water of high pressure RO device enter high pressure RO concentrated water case, are ensured public security by super-pressure RO booster pump, (adding antisludging agent)
Filter, plunger pump enter super-pressure RO device, carry out depth concentration decrement, and the TDS in waste water is further from 55978ppm
It is increased to 139885ppm, subsequently into evaporative crystallization material feeding box, evaporation and crystallization system is pumped by evaporative crystallization charging, benefit
Carnallite is isolated with centrifuge；The condensed water of high pressure RO device, the production water of super-pressure RO device and evaporation and crystallization system imports back
With pond, workshop section's reuse is produced by recycle-water pumped back.
Water balance figure
The water balance schematic diagram of resin adsorption extraction raffinate (including power plant cycle sewerage, part resin regeneration wash water) treatment for reuse system
Referring to the water balance figure of 5 coal calcination vanadium extracting waste water advanced treatment and reclamation devices and methods therefor embodiment of attached drawing.
4. system main design parameters
(1) civil engineering:
| Serial number | Title | Specification | Unit | Quantity | Structural shape |
| 1 | Adsorb extraction raffinate conditioning tank | V=400M3 | Seat | 1 | Steel concrete liner FRP |
| 2 | 1#, 2# intermediate pool | V=100M3 | Seat | 2 | Steel concrete liner FRP |
| 3 | Membrane separation device produces pond | V=150M3 | Seat | 1 | Steel concrete liner FRP |
| 4 | Reuse pool | V=400M3 | Seat | 1 | Steel concrete liner FRP |
| 5 | Effluent treatment plant | 80m×40m×10m | Seat | 1 | Light steel, steel concrete |
| 6 | Evaporative crystallization workshop | 40m×15m×24m | Seat | 1 | Light steel, steel concrete |
Wherein, effluent treatment plant includes deposition vanadium mother liquid processing system, and evaporative crystallization workshop includes the ammonium chloride of deposition vanadium mother liquid, chlorine
Evaporative crystallization point salt system is received in change.
(2) capital equipment:
| Serial number | Device name | Specifications and models | Material | Unit | Quantity |
| Two | Film separation system | ||||
| 1 | Electrolysis unit | Q=45m3/ h, 3 is standby with 1 | SS316L | Set | 4 |
| 2 | Digestion instrument | Q=45m3/ h, 3 is standby with 1 | SS316L | Set | 4 |
| 3 | Membrane separation device and corollary equipment | Net water yield Q=37.5m3/ h, 3 is standby with 1, includes pump, blower, chemicals dosing plant, chemically-cleaning device etc. | Film PVDF | Set | 4 |
| 4 | Feeding apparatus for powdered activated charcoal | It is mating | Set | 1 | |
| 5 | Instrument compressed air basin | V=2m3, mating safety valve, blowdown valve etc. | Q345R | Platform | 1 |
| Serial number | Device name | Specifications and models | Material | Unit | Quantity |
| Five | Evaporation and crystallization system | Inlet amount 10t/h, TDS ~ 14%, including material feeding box, feed pump, heat exchanger, Crystal separator, condensation water tank, hydrops tank, forced circulation pump, discharging pump, Both vapor compression unit, centrifuge etc., evaporation and crystallization system matching instrument, electricity Gas, automatic control | With concentrate contact portion Point titanium alloy, SS2507 | Set | 1 |
| Six | In-line meter | It is mating | Set | 1 | |
| Seven | Mounting material | It is mating | Batch | 1 | |
| Eight | Electrical system | It is mating | Set | 1 | |
| Nine | Other systems | Mating illumination, HVAC, plumbing, communication etc. | Set | 1 |
Claims (9)
1. coal calcination vanadium extraction high-salt wastewater advanced treatment and reclamation device, it is characterized in that including pretreatment system (PTS), dense
System (RCWT) is sent in contracting processing system (CTS), evaporation and crystallization system (VCS), recycle-water storage；Wherein resin adsorption extraction raffinate (TW) connects
To the water inlet of pretreatment system (PTS), the water outlet of pretreatment system (PTS) and the water inlet of concentrating and treating system (CTS)
Connect, the mud mouth of pretreatment system (PTS) sends out mud cake (SC), and the liquid outlet of pretreatment system (PTS) sends out the inclined of desorption
Sodium vanadate solution；The liquid outlet of concentrating and treating system (CTS) connects with the inlet of evaporation and crystallization system (VCS), concentration
The water outlet of system (CTS) send the 1st water inlet of system (RCWT) to connect with recycle-water storage；Evaporation and crystallization system (VCS) goes out
Salt mouth sends out crystal salt (Salt), and condensate outlet and the recycle-water storage of evaporation and crystallization system (VCS) send the 2nd of system (RCWT)
Water inlet connects；Recycle-water storage send the water outlet of system (RCWT) to send out recycle-water (RCW), is back to use the different works of vanadium extraction production
Section.
2. coal calcination vanadium extraction high-salt wastewater advanced treatment and reclamation device according to claim 1, it is characterized in that institute
The pretreatment system (PTS) stated, structure include including extraction raffinate water tank (T1), level-one neutralization reaction pond (NR1), first stage precipitation tank
(ST1), second level neutralization reaction pond (NR2), second-level settling pond (ST2), intermediate water tank (T2), advanced oxidation device (AOD), resolution
Case HT, membrane separation device (MSD), ultrafiltration water producing tank (T3), absorption resin container (RET), sodium metavanadate liquor box (T4), sludge it is de-
Water installations (SD), lime throwing device (D1), sodium carbonate, coagulant, flocculation aid throwing device (D2), Powdered Activated Carbon add dress
Set (D3), fungicide throwing device (D4), sodium hydroxide strippant throwing device (D5) and extraction raffinate elevator pump (P1), intermediate water
Pump (P2), ultrafiltration suction pump (P3), reverse osmosis booster pump (P4), hyperfiltration reverse-rinsing pump (P5), first stage precipitation tank sludge pump (P6), second level
Sludge from sedimentation tank pumps (P7), sodium metavanadate solution transfer pump (P8)；Wherein resin adsorption extraction raffinate (TW) is connected to extraction raffinate water tank (T1)
Water inlet, extraction raffinate water tank (T1) water outlet pass through extraction raffinate elevator pump (P1) and level-one neutralization reaction pond (NR1) water inlet phase
It connects, lime throwing device (D1) medicine outlet and level-one neutralization reaction pond (NR1) feeding opening connect, level-one neutralization reaction pond
(NR1) water outlet and first stage precipitation tank (ST1) water inlet connect, first stage precipitation tank (ST1) mud mouth pass through level-one precipitate
Pond sludge pump (P6) connect with the 1st mud inlet of sludge dehydration device (SD), first stage precipitation tank (ST1) water outlet and second level in
With reaction tank (NR2) water inlet connect, sodium carbonate, coagulant, flocculation aid throwing device (D2) medicine outlet and second level in and it is anti-
Ying Chi (NR2) feeding opening connect, second level neutralization reaction pond (NR2) water outlet and second-level settling pond (ST2) water inlet phase
It connects, second-level settling pond (ST2) mud mouth pass through second-level settling pond sludge pump (P7) with the 2nd of sludge dehydration device (SD) into mud
Mouth connects, and pressing filtering liquid is connected to extraction raffinate water tank (T by the liquid outlet of sludge dehydration device (SD)1) inlet, sludge dehydration device
(SD) mud mouth sends out mud cake (SC)；Second-level settling pond (ST2) water outlet and intermediate water tank (T2) water inlet connect, in
Between water tank (T2) water outlet pass through middle water pump (P2) connect with the water inlet of advanced oxidation device (AOD), advanced oxidation device
(AOD) water outlet connects with the water inlet of resolution case (HT), feeding apparatus for powdered activated charcoal (D3) medicine outlet and resolution case
(HT) feeding opening connects, and the water outlet of resolution case (HT) connects with the water inlet of membrane separation device (MSD), and fungicide adds dress
Set (D4) medicine outlet connect with the feeding opening of membrane separation device (MSD)；The water outlet of membrane separation device (MSD) is taken out by ultrafiltration
Sucking pump (P3) and ultrafiltration water producing tank (T3) water inlet connect, ultrafiltration water producing tank (T3) backwash water out pass through hyperfiltration reverse-rinsing pump
(P5) connect with the backwash water inlet of membrane separation device (MSD), the backwash discharge outlet of membrane separation device (MSD) and sludge dewatering fill
The 3# mud inlet for setting (SD) connects；Ultrafiltration water producing tank (T3) water outlet pass through reverse osmosis booster pump (P4) and absorption resin container
(RET) water inlet connects, sodium hydroxide strippant throwing device (D5) liquid outlet and absorption resin container (RET) inlet
Connect, adsorbs the liquid outlet and sodium metavanadate liquor box (T of resin container (RET)4) inlet connect, sodium metavanadate liquor box
(T4) liquid outlet pass through sodium metavanadate solution transfer pump (P8) send out the sodium metavanadate solution desorbed；Adsorb resin container (RET)
Water outlet sends out pretreatment system water outlet (PTout).
3. coal calcination vanadium extraction high-salt wastewater advanced treatment and reclamation device according to claim 1, it is characterized in that institute
System is sent in coal calcination vanadium extraction high-salt wastewater advanced treatment and reclamation device concentration systems (CTS) and the recycle-water storage stated
(RCWT), structure includes reverse osmosis cartridge filter (SAF1), (RO) indicate reverse osmosis unit, reverse osmosis concentrated water tank (T5), it is super
High pressure reverse osmosis cartridge filter (SAF2), super-pressure reverse osmosis unit (UHPRO), the reverse osmosis concentrated water tank (T of super-pressure6), evaporation
Crystal system (VCS), reuse water tank (T7), antisludging agent and reducing agent throwing device (D6), scale inhibitor feeding device (D7), and
Reverse osmosis high-pressure pumps (P9), super-pressure reverse osmosis booster pump (P10), the reverse osmosis plunger pump (P of super-pressure11), evaporation and crystallization system supply
Liquid pump (P12), reuse water pump (P13).Wherein pretreatment system water outlet (PTout) is connected to reverse osmosis cartridge filter (SAF1) into
The mouth of a river, antisludging agent and reducing agent throwing device (D6) medicine outlet be also connected to reverse osmosis cartridge filter (SAF1) water inlet, instead
Permeate cartridge filter (SAF1) water outlet pass through reverse osmosis high-pressure pump (P9) connect with the water inlet of reverse osmosis unit (RO),
Concentrated water outlet and the reverse osmosis concentrated water tank (T of reverse osmosis unit (RO)5) water inlet connect, reverse osmosis concentrated water tank (T5) water outlet
Mouth passes through super-pressure reverse osmosis booster pump (P10) it is connected to super-pressure reverse osmosis cartridge filter (SAF2) water inlet, antisludging agent throw
Feeder apparatus (D7) medicine outlet be also connected to super-pressure reverse osmosis cartridge filter (SAF2) water inlet, super-pressure reverse osmosis cartridge
Filter (SAF2) water outlet pass through the reverse osmosis plunger pump (P of super-pressure11) with the water inlet of super-pressure reverse osmosis unit (UHPRO)
Mouth connects；The production water out of reverse osmosis unit (RO) and the production water out of super-pressure reverse osmosis unit (UHPRO) are all connected to reuse
Water tank (T7) the 1st water inlet, reuse water tank (T7) water outlet pass through reuse water pump (P13) send out recycle-water (RCW)；Superelevation
Press concentrated water outlet and the reverse osmosis concentrated water tank (T of super-pressure of reverse osmosis unit (UHPRO)6) connect, the reverse osmosis concentrated water tank of super-pressure
(T6) pass through evaporation and crystallization system solution feed pump (P12) it is connected to the inlet of evaporation and crystallization system (VCS), evaporation and crystallization system (VCS)
Condensation-water drain be connected to reuse water tank (T7) the 2nd water inlet, the salt outlet of evaporation and crystallization system (VCS) sends out crystal salt
(Salt).
4. the application method of coal calcination vanadium extraction high-salt wastewater advanced treatment and reclamation device as described in claim 1,
It is characterized in including the following steps:
1) resin adsorption extraction raffinate is utilized the neutralization of a large amount of lime, precipitating and advanced oxygen by the preceding part for passing through pretreatment system
Change, the pH value of film filtering lifting waste water is to 6~8, while heavy-metal ion removal and part of sulfuric acid radical ion, reducing COD and outstanding
TDS is reduced to 8000~12000ppm by floating object content；
2) the rear part for passing through pretreatment system is effectively recycled using the metavanadic acid root in resin adsorption recycling waste water
Vanadium resource；
3) pretreatment water outlet carries out concentration decrement using reverse osmosis technology, is concentrated 10~15 times by concentrating and treating system, will
TDS is concentrated to 120000~150000ppm, in order to which subsequent evaporation crystal system steams crystal salt, while output fresh water,
TDS < 200ppm meets reuse requirement；
4) concentrated water of concentrating and treating system goes out crystal salt, while output condensed water by evaporation and crystallization system, evaporative crystallization,
TDS < 200ppm also meets reuse requirement；
5) recycle-water is made in the condensed water remittance of the production water of concentrating and treating system, evaporation and crystallization system, send system by recycle-water storage, into
Row storage, the different workshop sections for being transmitted back to vanadium extraction production, reach the mesh of coal calcination vanadium extraction high-salt wastewater advanced treatment and reclamation
's.
5. the application method of coal calcination vanadium extraction high-salt wastewater advanced treatment and reclamation device according to claim 4,
It is characterized in that the step 1) is by the preceding part of pretreatment system, specifically resin adsorption extraction raffinate pass sequentially through extraction raffinate water tank,
Extraction raffinate elevator pump, level-one neutralization reaction pond, first stage precipitation tank, second level neutralization reaction pond, second-level settling pond, intermediate water tank, centre
Water pump, advanced oxidation device, resolution case, membrane separation device, ultrafiltration suction pump are until ultrafiltration water producing tank, by level-one and anti-
Ying Chizhong adds a large amount of lime and is neutralized, precipitated, by adding sodium carbonate in second level neutralization reaction pond, coagulant, helping
Solidifying agent is neutralized, is precipitated, and absorption and drainage is carried out by adding Powdered Activated Carbon in resolution case, by throwing in membrane separation device
Adding of germicide protects ultrafiltration membrane, finally reduces COD using advanced oxidation, is further removed by filtration suspended matter using ultrafiltration membrane, most
The pH value of waste water is increased to 6~8 from 1~2 at last, forms solid metal using hydroxide ion a large amount of in water and metal ion
Hydroxide and heavy-metal ion removal, and using the low solubility characteristic of calcium sulfate at normal temperature remove most of sulfate radical from
TDS is reduced to 8000~12000ppm from 50000~80000ppm by son；Ultrafiltration membrane timing backwash, guarantees flux, and ultrafiltration is anti-
The spoil disposal for washing draining, one and second-level settling pond is dehydrated using sludge dehydration device, filtrate return processing, sludge outward transport.
6. the application method of coal calcination vanadium extraction high-salt wastewater advanced treatment and reclamation device according to claim 4,
It is characterized in that the step 2 passes through the rear part of pretreatment system, the specifically water outlet of ultrafiltration water producing tank passes through reverse osmosis pressurization
Absorption resin container is sent into pump pressurization, using the metavanadic acid root in macroporous anion exchange resin absorption waste water, adsorbs metavanadic acid root
Water afterwards is the water outlet of entire pretreatment system；After resin adsorption saturation, set using 5~15% sodium hydroxide strippant from absorption
Rouge tank desorbs sodium metavanadate, and utilizes sodium metavanadate liquor box and sodium metavanadate solution transfer pump by sodium metavanadate solution storage
With send precipitation pond back to, effectively recycle vanadium resource.
7. the application method of coal calcination vanadium extraction high-salt wastewater advanced treatment and reclamation device according to claim 4,
It is characterized in that the step 3) pretreatment water outlet, by concentrating and treating system, specifically pretreatment system water outlet passes sequentially through reverse osmosis
Saturating cartridge filter, reverse osmosis high-pressure pump, reverse osmosis unit (RO), reverse osmosis concentrated water tank, super-pressure reverse osmosis booster pump, superelevation
Press reverse osmosis cartridge filter, the reverse osmosis plunger pump of super-pressure, super-pressure reverse osmosis unit, the reverse osmosis concentrated water tank of super-pressure, steaming
Hair crystal system feed flow pumps out the concentrated water of super-pressure reverse osmosis unit；Reverse osmosis unit is by antisludging agent and reducing agent, reverse osmosis
Cartridge filter is protected, by 5~6 times of waste water initial concentration, its TDS is concentrated to 48000 from 8000~12000ppm~
60000ppm；Super-pressure is reverse osmosis to be protected by antisludging agent super-pressure reverse osmosis cartridge filter, further will be reverse osmosis concentrated
Water is concentrated 2~2.5 times, its TDS is concentrated to 120000~150000ppm from 48000~60000ppm；Whole system is by waste water
10~15 times of concentration, in order to which subsequent evaporation crystal system steams crystal salt, while output fresh water, TDS < 200ppm meets
The requirement of recycle-water.
8. the application method of coal calcination vanadium extraction high-salt wastewater advanced treatment and reclamation device according to claim 4,
It is characterized in that the concentrated water of the step 4) concentrating and treating system passes through evaporation and crystallization system, the specifically reverse osmosis concentrated water of super-pressure
Concentration be 120000~150000ppm, by heat exchanger in evaporation and crystallization system, crystal separator, hydrops tank, force to follow
The evaporative crystallizations such as ring pump, discharging pump, centrifuge isolate crystal salt, while output condensed water, and TDS < 200ppm meets reuse
The requirement of water.
9. the application method of coal calcination vanadium extraction high-salt wastewater advanced treatment and reclamation device according to claim 4,
It is characterized in that recycle-water is made in the condensed water remittance of the production water of the step 5) concentrating and treating system, evaporation and crystallization system, pass through reuse
System is sent in water storage, what specifically concentrating and treating system was reverse osmosis produce water, super-pressure it is reverse osmosis produce water and evaporation and crystallization system
Condensed water imports reuse water tank and is stored, and the different workshop sections of vanadium extraction production are sent to by recycle-water blowback, reaches bone coal sky
The purpose of white roasting vanadium extraction high-salt wastewater advanced treatment and reclamation.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811632206.0A CN109437463B (en) | 2018-12-29 | 2018-12-29 | Advanced treatment and recycling device for stone coal blank roasting vanadium extraction high-salt wastewater and using method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811632206.0A CN109437463B (en) | 2018-12-29 | 2018-12-29 | Advanced treatment and recycling device for stone coal blank roasting vanadium extraction high-salt wastewater and using method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN109437463A true CN109437463A (en) | 2019-03-08 |
| CN109437463B CN109437463B (en) | 2023-09-12 |
Family
ID=65538735
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201811632206.0A Active CN109437463B (en) | 2018-12-29 | 2018-12-29 | Advanced treatment and recycling device for stone coal blank roasting vanadium extraction high-salt wastewater and using method |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN109437463B (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112679014A (en) * | 2020-12-14 | 2021-04-20 | 江苏卓博环保科技有限公司 | Power plant concentrated wastewater zero-emission treatment device and treatment method |
| CN112679013A (en) * | 2020-12-14 | 2021-04-20 | 江苏卓博环保科技有限公司 | Copper smelting high-salinity wastewater zero-discharge treatment device and treatment method |
| CN112707563A (en) * | 2020-12-14 | 2021-04-27 | 江苏卓博环保科技有限公司 | Membrane method recycling treatment device and treatment method for copper smelting high-salinity wastewater |
| CN113880339A (en) * | 2021-10-09 | 2022-01-04 | 福建省环境保护设计院有限公司 | Advanced treatment and recycling process for high-salinity industrial wastewater |
| CN114212932A (en) * | 2021-11-21 | 2022-03-22 | 江苏卓博环保科技有限公司 | Desulfurization wastewater recycling treatment device and method |
| CN115465991A (en) * | 2022-09-06 | 2022-12-13 | 深圳市华虹清源环保科技有限公司 | Iron phosphate mother liquor wastewater treatment method and system |
Citations (17)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101054630A (en) * | 2007-05-28 | 2007-10-17 | 德物华经济信息研究院有限公司 | Integrated treatment method for the three wastes generated form method of extracting vanadium pentoxide from stone-like coal navajoite |
| CN101062783A (en) * | 2006-04-30 | 2007-10-31 | 邱宏麒 | Environment-friendly type technique for vanadium extraction of stone coal |
| CN101629249A (en) * | 2009-08-11 | 2010-01-20 | 紫金矿业集团股份有限公司 | Comprehensive treatment method of three wastes in extracting vanadium from stone coal navajoite |
| CN101709390A (en) * | 2009-12-15 | 2010-05-19 | 武汉科技大学 | On-line circulation method for process for extracting vanadium from stone coal |
| CN102642970A (en) * | 2012-04-28 | 2012-08-22 | 河北钢铁股份有限公司承德分公司 | Method for recycling waste water with high salinity by extracting vanadium from vanadium slag |
| CN103420520A (en) * | 2012-05-16 | 2013-12-04 | 中国石油化工股份有限公司 | Processing method of vanadium-containing aluminum-containing wastewater |
| CN103880218A (en) * | 2014-03-27 | 2014-06-25 | 湖南大学 | Complete cycle technology of vanadium smelting wastewater |
| CN105645439A (en) * | 2016-01-30 | 2016-06-08 | 内蒙古久科康瑞环保科技有限公司 | System for preparing potassium sulfate from high-salt-content industrial wastewater and technology of system |
| CN105695738A (en) * | 2016-03-25 | 2016-06-22 | 武汉科技大学 | Deironing method for vanadium-bearing stone coal lixivium |
| CN105907964A (en) * | 2016-04-28 | 2016-08-31 | 河南理工大学 | Method for separating vanadium, scandium and iron in acid solution |
| CN107827302A (en) * | 2017-09-26 | 2018-03-23 | 上海晶宇环境工程股份有限公司 | Vanadium-containing water technique of zero discharge and its special purpose device |
| CN108285239A (en) * | 2018-04-11 | 2018-07-17 | 攀钢集团攀枝花钢铁研究院有限公司 | A kind of process for treating waste liquor and system |
| US20180209014A1 (en) * | 2015-07-15 | 2018-07-26 | National University Corporation Gunma University | Vanadium Recovery Method, Method for Producing Electrolytic Solution for Redox Flow Batteries, Vanadium Recovery Device, and Device for Producing Electrolytic Solution for Redox Flow Batteries |
| CN109437444A (en) * | 2018-12-29 | 2019-03-08 | 江苏卓博环保科技有限公司 | Deposition vanadium mother liquid and wash water processing equipment for recycling and its method |
| CN209368011U (en) * | 2018-12-29 | 2019-09-10 | 江苏卓博环保科技有限公司 | Deposition vanadium mother liquid and wash water processing equipment for recycling |
| CN209412003U (en) * | 2018-12-29 | 2019-09-20 | 江苏卓博环保科技有限公司 | Coal calcination vanadium extraction high-salt wastewater advanced treatment and reclamation device |
| CN210313799U (en) * | 2018-12-29 | 2020-04-14 | 江苏卓博环保科技有限公司 | Resin adsorption tail water treatment recycling device for ammonium metavanadate production |
-
2018
- 2018-12-29 CN CN201811632206.0A patent/CN109437463B/en active Active
Patent Citations (17)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101062783A (en) * | 2006-04-30 | 2007-10-31 | 邱宏麒 | Environment-friendly type technique for vanadium extraction of stone coal |
| CN101054630A (en) * | 2007-05-28 | 2007-10-17 | 德物华经济信息研究院有限公司 | Integrated treatment method for the three wastes generated form method of extracting vanadium pentoxide from stone-like coal navajoite |
| CN101629249A (en) * | 2009-08-11 | 2010-01-20 | 紫金矿业集团股份有限公司 | Comprehensive treatment method of three wastes in extracting vanadium from stone coal navajoite |
| CN101709390A (en) * | 2009-12-15 | 2010-05-19 | 武汉科技大学 | On-line circulation method for process for extracting vanadium from stone coal |
| CN102642970A (en) * | 2012-04-28 | 2012-08-22 | 河北钢铁股份有限公司承德分公司 | Method for recycling waste water with high salinity by extracting vanadium from vanadium slag |
| CN103420520A (en) * | 2012-05-16 | 2013-12-04 | 中国石油化工股份有限公司 | Processing method of vanadium-containing aluminum-containing wastewater |
| CN103880218A (en) * | 2014-03-27 | 2014-06-25 | 湖南大学 | Complete cycle technology of vanadium smelting wastewater |
| US20180209014A1 (en) * | 2015-07-15 | 2018-07-26 | National University Corporation Gunma University | Vanadium Recovery Method, Method for Producing Electrolytic Solution for Redox Flow Batteries, Vanadium Recovery Device, and Device for Producing Electrolytic Solution for Redox Flow Batteries |
| CN105645439A (en) * | 2016-01-30 | 2016-06-08 | 内蒙古久科康瑞环保科技有限公司 | System for preparing potassium sulfate from high-salt-content industrial wastewater and technology of system |
| CN105695738A (en) * | 2016-03-25 | 2016-06-22 | 武汉科技大学 | Deironing method for vanadium-bearing stone coal lixivium |
| CN105907964A (en) * | 2016-04-28 | 2016-08-31 | 河南理工大学 | Method for separating vanadium, scandium and iron in acid solution |
| CN107827302A (en) * | 2017-09-26 | 2018-03-23 | 上海晶宇环境工程股份有限公司 | Vanadium-containing water technique of zero discharge and its special purpose device |
| CN108285239A (en) * | 2018-04-11 | 2018-07-17 | 攀钢集团攀枝花钢铁研究院有限公司 | A kind of process for treating waste liquor and system |
| CN109437444A (en) * | 2018-12-29 | 2019-03-08 | 江苏卓博环保科技有限公司 | Deposition vanadium mother liquid and wash water processing equipment for recycling and its method |
| CN209368011U (en) * | 2018-12-29 | 2019-09-10 | 江苏卓博环保科技有限公司 | Deposition vanadium mother liquid and wash water processing equipment for recycling |
| CN209412003U (en) * | 2018-12-29 | 2019-09-20 | 江苏卓博环保科技有限公司 | Coal calcination vanadium extraction high-salt wastewater advanced treatment and reclamation device |
| CN210313799U (en) * | 2018-12-29 | 2020-04-14 | 江苏卓博环保科技有限公司 | Resin adsorption tail water treatment recycling device for ammonium metavanadate production |
Non-Patent Citations (3)
| Title |
|---|
| 张传宝: "石煤提钒离子交换尾水处理及有价金属分离回收", no. 2014, pages 2 * |
| 张博等: "石煤矾矿提钒废水资源化处理技术及工程应用", vol. 46, no. 20, pages 79 - 81 * |
| 黄伟等: "减压膜蒸馏法处理石煤提钒废水", vol. 6, no. 12, pages 4377 * |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112679014A (en) * | 2020-12-14 | 2021-04-20 | 江苏卓博环保科技有限公司 | Power plant concentrated wastewater zero-emission treatment device and treatment method |
| CN112679013A (en) * | 2020-12-14 | 2021-04-20 | 江苏卓博环保科技有限公司 | Copper smelting high-salinity wastewater zero-discharge treatment device and treatment method |
| CN112707563A (en) * | 2020-12-14 | 2021-04-27 | 江苏卓博环保科技有限公司 | Membrane method recycling treatment device and treatment method for copper smelting high-salinity wastewater |
| CN113880339A (en) * | 2021-10-09 | 2022-01-04 | 福建省环境保护设计院有限公司 | Advanced treatment and recycling process for high-salinity industrial wastewater |
| CN113880339B (en) * | 2021-10-09 | 2024-01-16 | 福建省环境保护设计院有限公司 | Advanced treatment and reuse technology for high-salinity industrial wastewater |
| CN114212932A (en) * | 2021-11-21 | 2022-03-22 | 江苏卓博环保科技有限公司 | Desulfurization wastewater recycling treatment device and method |
| CN115465991A (en) * | 2022-09-06 | 2022-12-13 | 深圳市华虹清源环保科技有限公司 | Iron phosphate mother liquor wastewater treatment method and system |
| CN115465991B (en) * | 2022-09-06 | 2023-09-19 | 深圳市华虹清源环保科技有限公司 | Ferric phosphate mother liquor wastewater treatment method and system |
Also Published As
| Publication number | Publication date |
|---|---|
| CN109437463B (en) | 2023-09-12 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN109437463A (en) | Coal calcination vanadium extraction high-salt wastewater advanced treatment and reclamation device and application method | |
| CN209412003U (en) | Coal calcination vanadium extraction high-salt wastewater advanced treatment and reclamation device | |
| CN108623050B (en) | Desulfurization wastewater treatment method and system | |
| CN106315991B (en) | A kind of point salt technique for industrial wastewater | |
| CN105502790B (en) | A kind of desulfurization wastewater treatment system | |
| CN102627372B (en) | Method for treating vanadium pentoxide wastewater and circularly utilizing resources | |
| CN104176857B (en) | The treatment process of Mn-bearing waste water in wet method electrolysis manganese production process | |
| CN108623063A (en) | A kind of processing method and processing system of desulfurization wastewater | |
| CN103813987A (en) | Treatment of phosphate-containing wastewater with fluorosilicate and phosphate recovery | |
| CN105084587A (en) | Treatment method and equipment of high-salt waste water | |
| CN104986909B (en) | Acidic ammonium salt vanadium precipitation waste water recycling method | |
| CN103635436A (en) | Process for working up mine water | |
| CN106744721A (en) | The recovery separation method and application of sulfuric acid and dissolubility titanium in titanium white waste acid | |
| CN102627366B (en) | Method for treating vanadium pentoxide wastewater and circularly utilizing resources | |
| CN109970267A (en) | The processing method and processing unit of desulfurization wastewater sub-prime crystallization | |
| CN113105025B (en) | Combined treatment method for regenerating high-concentrated-salt wastewater by sodium ion exchanger | |
| CN108996791A (en) | A kind of sea water desalination and comprehensive utilization new process | |
| CN114702188A (en) | Method and system for co-processing high-salinity solid waste ash and acid wastewater of iron and steel plant | |
| CN202542982U (en) | Vanadium pentoxide waste water treating and resource recycling device | |
| CN109437444B (en) | Recycling treatment device and method for vanadium precipitation mother liquor and washing water | |
| CN110330165A (en) | Strong brine zero-emission and sub-prime crystallizing treatment process and processing system | |
| CN104671577A (en) | Treatment and resource recycling method for wastewater with precipitated vanadium | |
| CN107055886B (en) | A kind of depth graded divides salt technique | |
| CN104310659B (en) | Containing high density SO42-Percolate MBR+NF concentrated solution in humic acids process for separating and recovering | |
| Awadalla et al. | Opportunities for membrane technologies in the treatment of mining and mineral process streams and effluents |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant |