CN109160547A - Aluminum subtract slag hole sealing agent recycling and Waste water utilization method with configure - Google Patents
Aluminum subtract slag hole sealing agent recycling and Waste water utilization method with configure Download PDFInfo
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- CN109160547A CN109160547A CN201810841899.8A CN201810841899A CN109160547A CN 109160547 A CN109160547 A CN 109160547A CN 201810841899 A CN201810841899 A CN 201810841899A CN 109160547 A CN109160547 A CN 109160547A
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01G—COMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
- C01G53/00—Compounds of nickel
- C01G53/04—Oxides; Hydroxides
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B25/00—Phosphorus; Compounds thereof
- C01B25/16—Oxyacids of phosphorus; Salts thereof
- C01B25/26—Phosphates
- C01B25/37—Phosphates of heavy metals
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- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05F—ORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
- C05F7/00—Fertilisers from waste water, sewage sludge, sea slime, ooze or similar masses
- C05F7/005—Waste water from industrial processing material neither of agricultural nor of animal origin
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- 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
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A40/00—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
- Y02A40/10—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
- Y02A40/20—Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses
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Abstract
Aluminum subtracts the hole sealing agent recycling and Waste water utilization method of slag, including nickel-containing waste water collection step, nickel hydroxide recycling step, nickel phosphate recycling step, compound fertilizer's recycling step.It is an object of the invention to propose Aluminum subtract slag hole sealing agent recycling and Waste water utilization method with configure, 60,000 tons of nickel hydroxide of recycling, on the basis of medicament is compatible, it is converted to medium temperature hole sealing agent, recycles 24,000,000 tons of water during treated, be converted to compound liquid fertilizer, it applies fertilizer for plant area's land use for greening, pollution of the nickel-containing waste water to wastewater treatment center is blocked, industrial dangerous waste discharge is reduced, realizes that the resource recycling of toxic waste utilizes.
Description
Technical field
The present invention relates to hole sealing agent recycling and middle water conservancy that aluminium material surface processing technology field more particularly to Aluminum subtract slag
With method and configuration.
Background technique
Aluminium alloy has many advantages, such as that processing performance is excellent, corrosion resistance is good, surface aesthetic, the rate of recovery are high, in building, traffic
The industries such as transport, machinery, electric power are applied widely.In recent years, aluminium is for copper, aluminium generation wood, aluminium for steel, expansion aluminium application model
The trend enclosed is more obvious.Aluminium processing industry is both conventional industries, is even more full of the rising industry of vitality.But in economy
Under new normality, the common problem that aluminium processing industry energy consumption is high, total amount of pollutants discharged is big, resource recycling rate is low is highlighted as system
The about bottleneck and obstacle of industry development.
Aluminium industry production includes the processes such as electrolysis, founding, pressure processing, surface treatment, and each process can generate when production
Different degrees of exhaust gas, waste water, waste residue.A large amount of aluminium ash is generated when electrolysis and founding, it is useless that extrusion process generates pot mould alkalinity
Liquid, it is useless that surface treatment process generates all kinds of waste water containing the complicated components such as acid, alkali, treatment agent and chromium, nickel heavy metal ion
Slag.
Modern aluminum processing enterprise, the nickel-containing waste water waste residue for having oxidation sealing of hole to generate is in need of immediate treatment, and traditional water for cleaning
The method reprocessed after mixing is too simple, generates a large amount of nickel-containing waste water waste residue, to handle these waste water and dregs, and society will
Expensive environmentally friendly cost is paid thus, and there is an urgent need to develop new technologies, individually handle sealing of hole process nickel-containing waste water.
Summary of the invention
The purpose of the present invention is to solve the above problem propose Aluminum subtract slag hole sealing agent recycling and Waste water utilization method and
Configuration.
In order to achieve this goal, the invention adopts the following technical scheme:
Aluminum subtracts the hole sealing agent recycling and Waste water utilization method of slag, including nickel-containing waste water collection step, nickel hydroxide recycle
Step, nickel phosphate recycling step, compound fertilizer's recycling step；
The nickel-containing waste water collection step includes opening valve 1, opens pump 1, by 17# flowing rinsing bowl slot bottom water outlet row
Nickel-containing waste water out is pumped into spare in nickel-containing waste water collecting tank；
The nickel hydroxide recycling step includes opening valve 2, valve 3, closes valve 4, opens pump 2, nickel-containing waste water is pumped into
Nickel hydroxide recycling can；Valve 4, valve 6 are opened, pump 3, the stirring of 1# electricity, circular response liquid are opened；Valve 5 is slowly opened, liquefied ammonia is inhaled
Enter pump 3, using the high speed rotation of pump 3, is sufficiently mixed reaction solution；Liquefied ammonia is added on side, and frontier inspection surveys the pH value of reaction solution, works as pH value
When reaching 8.5-9.0, valve 5 is closed, stops dosing, continues cycling through stirring 1 hour；1# filter press is opened, valve 7 is opened, closes valve
6, valve 8 are separated by solid-liquid separation nickel hydroxide；It sprays repeatedly, rinse nickel hydroxide solid after ten minutes, recycle nickel hydroxide product；
The nickel phosphate recycling step includes closing valve 9, valve 11, opens valve 8, valve 10, opens pump 4, the stirring of 2# electricity, follows
Ring reaction solution；Valve 9 is slowly opened, phosphoric acid suction pump 4 is sufficiently mixed reaction solution using the high speed rotation of pump 4；Add phosphorus in side
Acid, frontier inspection surveys the pH value of reaction solution, when pH value reaches 6.5-7.5, closes valve 9, stops dosing, it is small to continue cycling through stirring 1
When；2# filter press is opened, valve 11 is opened, closes valve 10, is separated by solid-liquid separation nickel phosphate；It sprays repeatedly, rinsing nickel phosphate solid 10 divides
Zhong Hou recycles nickel phosphate product；
Compound fertilizer's recycling step includes opening valve 12, valve 13, opens pump 5, after recovered liquid is filtered,
It is delivered to land use for greening, is used as compound fertilizer.
More preferably, 0.5-1.5g/L containing nickel acetate in the 17# flowing rinsing bowl.
More preferably, pure water and acetic acid are added in the recycling nickel hydroxide product, are converted to nickel acetate；
Acetic acid additive amount is 95% of addition weight needed for chemical reaction completely, and nickel hydroxide is suitably excessive in reaction solution,
Ensure reacting liquid pH value >=6；
Under conditions of pure water weight/weight of nickel hydroxide is equal to 10, reaction solution acetic acid nickel content is 14.5-
15.5wt%, far below the saturated concentration of nickel acetate, it is ensured that reaction solution is precipitated without nickel acetate crystal；
Precipitating, filtering reacting liquid obtain pH value >=6.0 contents lower than saturation point, can make nickel acetate raw material.
More preferably, the content of liquid nickel acetate is first titrated, nickel acetate/triethanolamine=10, nickel acetate/isobutyl are then pressed
The weight ratio addition triethanolamine and isobutanol of alcohol=10, are converted to liquid medium temperature hole sealing agent for nickel acetate solution.
More preferably, when being converted to nickel acetate using nickel hydroxide, only rinsing, without drying, add after pure water directly and acetic acid
Reaction.
More preferably, precipitating, filtered filter residue reside in reaction vessel, and waiting converts next time.
More preferably, subtract the configuration of the hole sealing agent recycling and Waste water utilization method of slag using Aluminum, including nickel-containing waste water is collected
System, nickel hydroxide recovery system, nickel phosphate recovery system and compound fertilizer's recovery system；
The nickel-containing waste water collection system, the nickel hydroxide recovery system, the nickel phosphate recovery system and described multiple
Hefei recovery system is sequentially connected；
The nickel-containing waste water collection system includes 17# flowing rinsing bowl, valve 1, pump 1 and sealing of hole nickel-containing waste water collecting tank, institute
It states pump 1 and is connected to the 17# flowing rinsing bowl, the valve 1 is set between 17# flowing rinsing bowl and pump 1, and the sealing of hole contains
Nickel waste water collecting tank is connected to the pump 1；
The nickel hydroxide recovery system includes valve 2, valve 3, valve 4, valve 5, valve 6, valve 7, pump 2, pump 3,1# filter press, 1#
Electricity stirring, nickel hydroxide recycling can and ammonia tank, the valve 2 and the valve 3 are set to the both ends of the pump 2, and the pump 2 connects
It is connected to the nickel hydroxide recycling can, the 1# electricity stirring is set to above the nickel hydroxide recycling can, 3 setting of pump
Below the nickel hydroxide recycling can, the valve 4 is set between pump 3 and nickel hydroxide recycling can, one end of the pump 3
It is connected to the upper end of the nickel hydroxide recycling can, the valve 6 is set to one end of the pump 3, and the ammonia tank is connected to institute
Pump 3 is stated, the valve 5 is set between the ammonia tank and the pump 3, and the 1# filter press is set to the lower section of the pump 3,
The valve 7 is set between the pump 3 and the 1# filter press；
The nickel phosphate recovery system includes valve 8, valve 9, valve 10, valve 11, pump 4, the stirring of 2# electricity, nickel phosphate recycling can, phosphorus
Sour tank and 2# filter press, the nickel phosphate recycling can are connected to the 1# filter press, and the 2# electricity stirring is set to the phosphoric acid
The top of nickel recycling can, the pump 4 are connected to the nickel phosphate recycling can, and the valve 8 is set to pump 4 and nickel phosphate recycling can
Between, the 2# filter press is connected to the pump 4, and the valve 11 is set between pump 4 and 2# filter press, and the phosphoric acid tank connects
It is connected to the pump 4, the valve 9 is set between phosphoric acid tank and pump 4, and one end of the pump 4 is connected to the nickel phosphate recycling can
Upper end, the valve 10 be set to it is described pump 4 one end；
Compound fertilizer's recovery system includes valve 12, valve 13, pump 5, compound fertilizer's recycling can and filter, the compound fertilizer
Recycling can is connected to the 2# filter press, and the filter is connected to compound fertilizer's recycling can, and the valve 12 is set to filtering
Between device and compound fertilizer's recycling can, the pump 5 is connected to the filter, and the valve 13 is set to the pump 5.
It is an object of the invention to propose Aluminum subtract slag hole sealing agent recycling and Waste water utilization method and configuration, recycling hydrogen
60,000 tons of nickel oxide, on the basis of medicament is compatible, it is converted to medium temperature hole sealing agent, recycles water 24,000,000 during treated
Ton, is converted to compound liquid fertilizer, applies fertilizer for plant area's land use for greening, blocks pollution of the nickel-containing waste water to wastewater treatment center,
Industrial dangerous waste discharge is reduced, realizes that the resource recycling of toxic waste utilizes.
Detailed description of the invention
Fig. 1 is the system diagram of one embodiment of the present of invention；
Fig. 2 be one embodiment of the present of invention oxidation line discharge of wastewater to waste water center schematic diagram.
Specific embodiment
With reference to the accompanying drawing and pass through specific embodiment mode to further illustrate the technical scheme of the present invention.
Aluminum subtracts the hole sealing agent recycling and Waste water utilization method of slag, including nickel-containing waste water collection step, nickel hydroxide recycle
Step, nickel phosphate recycling step, compound fertilizer's recycling step；
The nickel-containing waste water collection step includes opening valve 1, opens pump 1, by 17# flowing rinsing bowl slot bottom water outlet row
Nickel-containing waste water out is pumped into spare in nickel-containing waste water collecting tank；
The nickel hydroxide recycling step includes opening valve 2, valve 3, closes valve 4, opens pump 2, nickel-containing waste water is pumped into
Nickel hydroxide recycling can；Valve 4, valve 6 are opened, pump 3, the stirring of 1# electricity, circular response liquid are opened；Valve 5 is slowly opened, liquefied ammonia is inhaled
Enter pump 3, using the high speed rotation of pump 3, is sufficiently mixed reaction solution；Liquefied ammonia is added on side, and frontier inspection surveys the pH value of reaction solution, works as pH value
When reaching 8.5-9.0, valve 5 is closed, stops dosing, continues cycling through stirring 1 hour；1# filter press is opened, valve 7 is opened, closes valve
6, valve 8 are separated by solid-liquid separation nickel hydroxide；It sprays repeatedly, rinse nickel hydroxide solid after ten minutes, recycle nickel hydroxide product；
The nickel phosphate recycling step includes closing valve 9, valve 11, opens valve 8, valve 10, opens pump 4, the stirring of 2# electricity, follows
Ring reaction solution；Valve 9 is slowly opened, phosphoric acid suction pump 4 is sufficiently mixed reaction solution using the high speed rotation of pump 4；Add phosphorus in side
Acid, frontier inspection surveys the pH value of reaction solution, when pH value reaches 6.5-7.5, closes valve 9, stops dosing, it is small to continue cycling through stirring 1
When；2# filter press is opened, valve 11 is opened, closes valve 10, is separated by solid-liquid separation nickel phosphate；It sprays repeatedly, rinsing nickel phosphate solid 10 divides
Zhong Hou recycles nickel phosphate product；
Compound fertilizer's recycling step includes opening valve 12, valve 13, opens pump 5, after recovered liquid is filtered,
It is delivered to land use for greening, is used as compound fertilizer.
As shown in Fig. 2, oxidation hole-sealing technology process is as shown, 1#, 4#, 7#, 10#, 13#, 16# slot are work nest, often
A work nest matches two flowing rinsing bowls, and oxidation processes need 18 slot positions, and wherein 16# is medium temperature sealing of hole slot, contains nickel acetate,
Its subsequent rinsing bowl takes nickel-containing waste water out of and enters wastewater treatment center, and 2.25 hundred million tons of pollution whole industry water generates 1,500,000 tons
The toxic waste residue of nickeliferous mixing, the present invention, which retains, collects 24,000,000 tons of nickeliferous sealing of hole water for cleaning, individually recycles Nickel-bearing Waste
Slag is converted into hole sealing agent, realizes the zero-emission of nickel-containing waste water waste residue.
The function of the 16# medium temperature sealing of hole slot: the purpose that this slot is arranged is the micropore for sealing oxidation film, it is ensured that its corrosion resistant
Corrosion energy, it is also possible to which electrophoresis tank replaces sealing of hole slot.Method for sealing by operating temperature be divided into high temperature, in mild normal-temperature hole sealing.High temperature
Sealing of hole is that aluminium is handled in 95-100 DEG C of pure water, and sealing quality is preferable, but energy consumption is high, and evaporated quantity of water is big, easy dust, easily
Foreign ion poisoning, need to often replace tank liquor；The method that medium temperature sealing of hole generally uses nickel acetate additive, at 55-65 DEG C
Reason, sealing of hole speed is fast, and few dust does not split film, but nickeliferous, is unfavorable for environmental protection；Normal-temperature hole sealing uses nickel fluoride doping side
Method is handled at 25-35 DEG C, and sealing of hole fast speed, low energy consumption, easy to use.But film easy to crack, dust, and fluorine-containing and nickel is unfavorable
In environmental protection.Medium temperature sealing of hole slot Con trolling index are as follows:
The function of 17# flowing rinsing bowl and 18# flowing rinsing bowl: the purpose that this twice rinsing bowl is arranged is cleaning sealing of hole
The nickeliferous residual medicament that slot is taken out of is not corroded after protecting aluminium to dispatch from the factory.
Sealing of hole slot water for cleaning retains collection method
1) rinsing bowl individually retains after sealing of hole.By Fig. 2 and (1) formula, tap water is cleaned from 18# into differential concatenation to 17#
Slot is flowed out from 17# slot.It after aluminium presses 10-25min time sealing of hole, rises and hangs drip 30s, flow rinsing bowl, cleaning into 17#
1min rises and hangs drip 30s, flows rinsing bowl into 18#, cleans 1min, rises and hang drip 30s, into air drying area, completes sealing of hole
With washing process.When cleaning after aluminium sealing of hole, nickel acetate contained by pore-sealing liquid, triethanolamine and isobutanol bring 17#, 18# stream into
Dynamic rinsing bowl, pollutes the water for cleaning of flowing；The pH value of 16# medium temperature sealing of hole slot is the pH value of the water inlet of 5.5-6.5,18# slot
For 6.0-7.0, therefore 17#, 18# slot pH value, between 5.5-7.0, this section nickel acetate, triethanolamine and isobutanol are stablized, no
It decomposes, can be trapped in 17#, 18# rinse bath；
2) water lotion is collected separately after sealing of hole.17#, 18# flow rinsing bowl Con trolling index are as follows:
By Fig. 1 and Fig. 2,18# slot inlet valve is adjusted, under conditions of ensuring sealing of hole cleaning quality, presses (2) formula, titration
17#, 18# slot acetic acid nickel content, control sealing of hole clean water consumption, from 17# slot water outlet collect outflow nickeliferous water for cleaning to
Sealing of hole nickel-containing waste water collecting tank is spare.
Sealing of hole ejected wash water collects production hole sealing agent and middle water recycles quantitative and qualitative analysis
1) the recovered liquid 1L of sealing of hole nickel-containing waste water collecting tank is taken, nickel acetate, triethanolamine and isobutanol are contained, presses (2) formula,
Test agents concentration are as follows:
Nickel acetate 1.1g/L
Triethanolamine 0.11g/L (3)
Isobutanol 0.11g/L
pH 6.35
It is slowly added liquefied ammonia, stirring while adding, pH value is stepped up, there is following variation:
When pH value is lower than 7.0, due to the complexing of triethanolamine, tank liquor is clear, no precipitating, no precipitate；
When pH is between 7.0-7.5, tank liquor starts muddiness, and green crystal nickel hydroxide is precipitated:
NH3+H2O=NH4OH
Ni2++2NH4OH=2NH4++Ni (OH) 2 ↓ (4)
When pH is between 7.5-8.0, tank liquor is muddy, and green crystal precipitate nickel hydroxide increases；
When pH is between 8.0-8.5, tank liquor is muddy, and green crystal precipitate nickel hydroxide increases；
When pH is between 8.5-9.0, tank liquor is muddy, and green crystal precipitate nickel hydroxide is not further added by；
When pH is between 9.0-10.0, tank liquor is muddy, and green crystal precipitate nickel hydroxide is not further added by, takes
PH8.5-9.0 is reaction end；
2) ammonium acetate, triethanolamine and isobutanol do not precipitate, and retain in liquid.By (3) formula, with the addition of liquefied ammonia,
PH is constantly increased, and presses (4) formula, and Ni2+, which constantly reacts, generates Ni (OH) 2 but ammonium acetate, triethanolamine and isobutanol, is not decomposed,
It does not precipitate, retains in liquid；
3) it is separated by solid-liquid separation, with filtrate separation ammonium acetate, triethanolamine and isobutanol, recycles fixed nickel hydroxide.By (4)
Reaction product is separated by solid-liquid separation by formula.Ammonium acetate, triethanolamine and isobutanol are flowed out with filtrate, obtain solid hydroxide
Nickel；It rinsed, dried, obtain the technical grade nickel hydroxide product for meeting national standard；Nickel hydroxide solubility in filtrate
130mg/L, the discharge standard much higher than 0.5mg/L, needs secondary treatment, up to standard can recycle；
4) nickel hydroxide is converted, reaction generates nickel acetate.The nickel hydroxide product obtained after rinsing drying is weighed, is added
Pure water is wet, and being slowly added concentration is 98% acetic acid, reacts as follows:
Ni (OH) 2+2CH3COOH=Ni (CH3COO) 2+2H2O (5)
100g nickel hydroxide, completely reaction need to add glacial acetic acid (98%) 132.1g, generate nickel acetate 190.7g.It presses
Nickel acetate solubility 182g/L (20 DEG C), pH6.28 design recovery scheme.Nickel hydroxide 100g is taken, pure water 1000mL, pure water are added
Weight/weight of nickel hydroxide=10, stirs evenly；It is slowly added glacial acetic acid 132.1*95%=125.5g, nickel acetate is generated and connects
Nearly 190.7*95%=181.2g；Reaction solution total weight 1225.5g, acetic acid nickel content are 181.2/1225.5=
14.8wt.%, lower than the saturated concentration of nickel acetate, it is ensured that no nickel acetate saturation crystal is precipitated；Add by the 95% of acetic acid additive amount
Add, nickel hydroxide is excessive, i.e., beaker bottom has a small amount of nickel hydroxide solid residue after the reaction was completed, it can be ensured that nickel acetate solution
PH value close to 6.28, pH >=6.0, meet the sealing quality requirement that medium temperature hole sealing agent pH is greater than 5.5；
5) hole sealing agent is produced, realizes that useless nickel resourcesization utilize.It due to the nickel acetate liquid that (5) formula obtains, is flowed from 17#
The nickeliferous waste liquid of dynamic rinsing bowl recycling, which reacts, to be generated, and it is compatible to 16# medium temperature sealing of hole slot that 17#, 18# flow rinsing bowl, therefore presses (5)
The nickel acetate of formula production can be transformed completely by hole sealing agent, reuse to sealing of hole slot.By (1) formula, remodeling method are as follows:
A, acetic acid nickel concentration is titrated, X (g/L) is obtained；
B, triethanolamine X/10 (g/L) (6) are added
C, isobutanol X/10 (g/L) is added
It can be used as the fluting and addition medicament of 16# sealing of hole slot completely by the hole sealing agent of (6) transformation with reference to (1) formula；It examines
The working index for considering 16# slot is pH5.5-6.5, and the nickel acetate of (5) formula recycling has met pH value requirement；When sealing of hole, temperature
50-60 DEG C, there is a large amount of water evaporation, liquor of hole- sealing tank position shoals, and when adding by the liquid hole sealing agent of (6) formula production, just supplements
Drug concentration and liquid level save the cost of manufacture of the nickel acetate condensing crystallizing of (5) formula recycling；In addition, the hydrogen-oxygen of (4) formula recycling
Change nickel, rinsed clean not dry, because (5) formula needs to add a large amount of water when reacting, save cost of manufacture；
6) filtrate is handled, nickel phosphate is recycled, recycles sealing of hole water for cleaning.By (4) formula, nickel hydroxide solubility
130mg/L, the discharge standard much higher than 0.5mg/L, needs secondary treatment, up to standard can recycle.(4) filtrate of formula contains
Ammonium acetate, triethanolamine and isobutanol, while 130mg/L containing nickel hydroxide need to be reduced to 0.5mg/L or less；In filtrate
Addition concentration is 85wt.% phosphoric acid, and pH value 8.5-9.0 is adjusted to 6.5-7.5, reaction are as follows:
3Ni2++2H3PO4=(Ni) 3 (PO4) 2 ↓+6H2+ (7)
The solubility of nickel phosphate be 5 multiplied by 10 minus 31 power, filtrate much reaches recycling using standard；It filters again
Nickel phosphate, rinsing, drying, obtains nickel phosphate product；Filtrate is the N-P compound fertilizer of phosphoric acid ammonium, ammonium acetate, is afforested as plant area
Fertilizer application realizes that sealing of hole is recycled with water.
The sealing of hole capacity experimental of sealing of hole water for cleaning remanufacture hole sealing agent
The present invention presses (4) formula first, obtains nickel hydroxide, then produces nickel acetate by (5), finally by the allotment of (6) formula
Warm hole sealing agent.This serial experiment presses the medium temperature sealing of hole slot Con trolling index that (1) formula provides, and investigates the medium temperature by the production of (6) formula respectively
The sealing of hole ability of hole sealing agent.
1, influence of the hole sealing agent concentration recycled to sealing quality.Take 55 DEG C of pH 6.0, temperature, nickel acetate 2,3,4,5,
6,7g/L (triethanolamine and isobutanol are 1/10th of acetic acid nickel concentration, similarly hereinafter)；Taking oxide thickness is 15 microns, envelope
The hole time is 15 minutes, detects sealing quality by ISO3210 international standard, the results are shown in Table 1:
Influence of the 1 hole sealing agent concentration of table to sealing quality
2, influence of the sealing of hole slot pH value to sealing quality.Taking nickel acetate 5g/L, (triethanolamine and isobutanol are dense for nickel acetate
/ 10th of degree, similarly hereinafter), 55 DEG C of temperature, pH4.5,5.0,5.5,6.0,6.5,7.0；Taking oxide thickness is 15 microns,
The sealing of hole time is 15 minutes, detects sealing quality by ISO3210 international standard, the results are shown in Table 2:
Influence of the 2 sealing of hole slot pH value of table to sealing quality
3, influence of the sealing of hole temperature to sealing quality.Taking nickel acetate 5g/L, (triethanolamine and isobutanol are acetic acid nickel concentration
1/10th, similarly hereinafter), pH6.0,40,45,50,55,60,65 DEG C of temperature；Taking oxide thickness is 15 microns, the sealing of hole time
It is 15 minutes, detects sealing quality by ISO3210 international standard, the results are shown in Table 3:
Influence of the 3 sealing of hole temperature of table to sealing quality
4, influence of the sealing of hole time to sealing quality.Taking nickel acetate 5g/L, (triethanolamine and isobutanol are acetic acid nickel concentration
1/10th, similarly hereinafter), pH6.0,55 DEG C of temperature；Take oxide thickness be 15 microns, the sealing of hole time be 5,8,11,14,17,
20 minutes, sealing quality is detected by ISO3210 international standard, the results are shown in Table 4:
Influence of the 4 sealing of hole time of table to sealing quality
The analysis of experimental results that sealing of hole water for cleaning remanufacture hole sealing agent and middle water recycle
By formula (1)-(7) and experiment 1-4 and testing result, following analysis can be done:
1, the standard provided by formula (2) formula can retain online and collect sealing of hole water for cleaning；18# slot flow of inlet water is adjusted,
Nickel-containing waste water is collected in 17# slot water outlet, controls nickel-containing waste water total amount to be processed；
2, (4) formula is pressed, addition liquefied ammonia individually handles the nickel-containing waste water of retention online at pH value 8.5-9.0, recycles
The nickel hydroxide of technical grade converts nickeliferous solid dangerous waste to the industrial chemicals of high value, realizes the recycling benefit of solid dangerous waste
With；
3, (5) formula is pressed, converts nickel acetate solution for the nickel hydroxide of recycling, under the conditions of nickel hydroxide is excessive, instead
It answers the pH value of product to be greater than 6.0, meets subsequent transformation into the requirement of hole sealing agent；
4, (6) formula is pressed, nickel acetate solution is converted to liquid hole sealing agent, directly by the principle being compatible with using sealing of hole medicament itself
It connects and is added to sealing of hole slot；Sealing of hole slot is medium temperature sealing of hole, there is certain evaporation capacity, liquid hole sealing agent just supplement drug concentration and
Liquid level saves the trouble of drying nickel hydroxide, evaporative crystallization nickel acetate solution, substantially saves the cost of manufacture of hole sealing agent；
5, serial experiment result 1-4 is pressed it is found that pressing in the production of (6) formula within the scope of the Con trolling index as defined in (1) formula
Warm hole sealing agent is fully able to meet sealing of hole requirement；
6, (7) formula is pressed, in the filtrate after nickel hydroxide separation of solid and liquid, phosphoric acid is added, converts remnants Ni2+For nickel phosphate,
Remaining phosphoric acid nickel concentration be 5 multiplied by 10 minus 31 power, filtrate much reaches recycling using standard；Nickel phosphate is filtered again, is floated
It washes, dry, obtain nickel phosphate product；Filtrate is the compound fertilizer of phosphoric acid ammonium, ammonium acetate, afforests Fertilizer application as plant area, realizes
Sealing of hole is recycled with water；Filter residue is nickel phosphate, is resided in reaction vessel, and waiting is recycled next time.
Further description, the 17# flow 0.5-1.5g/L containing nickel acetate in rinsing bowl.
Further description adds pure water and acetic acid in the recycling nickel hydroxide product, is converted to nickel acetate；
Acetic acid additive amount is 95% of addition weight needed for chemical reaction completely, and nickel hydroxide is suitably excessive in reaction solution,
Ensure reacting liquid pH value >=6；
Under conditions of pure water weight/weight of nickel hydroxide is equal to 10, reaction solution acetic acid nickel content is 14.5-
15.5wt%, far below the saturated concentration of nickel acetate, it is ensured that reaction solution is precipitated without nickel acetate crystal；
Precipitating, filtering reacting liquid obtain pH value >=6.0 contents lower than saturation point, can make nickel acetate raw material.
Further description first titrates the content of liquid nickel acetate, then presses nickel acetate/triethanolamine=10, acetic acid
Nickel/isobutanol=10 weight ratio adds triethanolamine and isobutanol, and nickel acetate solution is converted to liquid medium temperature hole sealing agent.
Further description, when being converted to nickel acetate using nickel hydroxide, only rinsing, without drying, add straight after pure water
It connects and acetic acid reaction.
Further description, precipitating, filtered filter residue reside in reaction vessel, and waiting converts next time.
Further description subtracts the configuration of the hole sealing agent recycling and Waste water utilization method of slag using Aluminum, including nickeliferous
Wastewater collection system, nickel hydroxide recovery system, nickel phosphate recovery system and compound fertilizer's recovery system；
The nickel-containing waste water collection system, the nickel hydroxide recovery system, the nickel phosphate recovery system and described multiple
Hefei recovery system is sequentially connected；
The nickel-containing waste water collection system includes 17# flowing rinsing bowl, valve 1, pump 1 and sealing of hole nickel-containing waste water collecting tank, institute
It states pump 1 and is connected to the 17# flowing rinsing bowl, the valve 1 is set between 17# flowing rinsing bowl and pump 1, and the sealing of hole contains
Nickel waste water collecting tank is connected to the pump 1；
The nickel hydroxide recovery system includes valve 2, valve 3, valve 4, valve 5, valve 6, valve 7, pump 2, pump 3,1# filter press, 1#
Electricity stirring, nickel hydroxide recycling can and ammonia tank, the valve 2 and the valve 3 are set to the both ends of the pump 2, and the pump 2 connects
It is connected to the nickel hydroxide recycling can, the 1# electricity stirring is set to above the nickel hydroxide recycling can, 3 setting of pump
Below the nickel hydroxide recycling can, the valve 4 is set between pump 3 and nickel hydroxide recycling can, one end of the pump 3
It is connected to the upper end of the nickel hydroxide recycling can, the valve 6 is set to one end of the pump 3, and the ammonia tank is connected to institute
Pump 3 is stated, the valve 5 is set between the ammonia tank and the pump 3, and the 1# filter press is set to the lower section of the pump 3,
The valve 7 is set between the pump 3 and the 1# filter press；
The nickel phosphate recovery system includes valve 8, valve 9, valve 10, valve 11, pump 4, the stirring of 2# electricity, nickel phosphate recycling can, phosphorus
Sour tank and 2# filter press, the nickel phosphate recycling can are connected to the 1# filter press, and the 2# electricity stirring is set to the phosphoric acid
The top of nickel recycling can, the pump 4 are connected to the nickel phosphate recycling can, and the valve 8 is set to pump 4 and nickel phosphate recycling can
Between, the 2# filter press is connected to the pump 4, and the valve 11 is set between pump 4 and 2# filter press, and the phosphoric acid tank connects
It is connected to the pump 4, the valve 9 is set between phosphoric acid tank and pump 4, and one end of the pump 4 is connected to the nickel phosphate recycling can
Upper end, the valve 10 be set to it is described pump 4 one end；
Compound fertilizer's recovery system includes valve 12, valve 13, pump 5, compound fertilizer's recycling can and filter, the compound fertilizer
Recycling can is connected to the 2# filter press, and the filter is connected to compound fertilizer's recycling can, and the valve 12 is set to filtering
Between device and compound fertilizer's recycling can, the pump 5 is connected to the filter, and the valve 13 is set to the pump 5.
As shown in Figure 1, the nickel-containing waste water collection system is by 17# flowing rinsing bowl, valve 1, pump 1 and sealing of hole nickel-containing waste water
Collecting tank composition collects the nickeliferous water for cleaning of 17# flowing rinsing bowl, is pumped into sealing of hole by 17# flowing rinsing bowl slot bottom water outlet
Nickel-containing waste water collecting tank is spare.The nickel hydroxide recovery system is by valve 2, valve 3, valve 4, valve 5, valve 6, valve 7, pump 2, pump 3,1#
Filter press, the stirring of 1# electricity, nickel hydroxide recycling can and ammonia tank composition, are responsible for adding liquefied ammonia in nickel hydroxide recycling can, instead
Nickel hydroxide should be generated, after the filters pressing of 1# filter press, spray, drying, recycling meets the nickel hydroxide product of national standard.Institute
Nickel phosphate recovery system is stated to be pressed by valve 8, valve 9, valve 10, valve 11, pump 4, the stirring of 2# electricity, nickel phosphate recycling can, phosphoric acid tank and 2#
Filter composition, is responsible for adding phosphoric acid in nickel phosphate recycling can, and reaction generates nickel phosphate, through the filters pressing of 2# filter press, spray, baking
After dry, recycling meets the nickel phosphate product of national standard.Compound fertilizer's recovery system is returned by valve 12, valve 13, pump 5, compound fertilizer
Closed cans and filter composition are responsible for the filtrate that recycling filtering 2# filter press filters out, filter, are delivered to plant area's land use for greening, as
Compound fertilizer uses.
The technical principle of the invention is described above in combination with a specific embodiment.These descriptions are intended merely to explain the present invention
Principle, and shall not be construed in any way as a limitation of the scope of protection of the invention.Based on the explanation herein, this field
Technical staff can associate with other specific embodiments of the invention without creative labor, these modes are all
It will fall under the scope of the present invention.
Claims (7)
1. hole sealing agent recycling and Waste water utilization method that Aluminum subtracts slag, it is characterised in that: including nickel-containing waste water collection step, hydrogen-oxygen
Change nickel recycling step, nickel phosphate recycling step, compound fertilizer's recycling step；
The nickel-containing waste water collection step includes opening valve 1, opens pump 1, by 17# flowing rinsing bowl slot bottom water outlet discharge
Nickel-containing waste water is pumped into spare in nickel-containing waste water collecting tank；
The nickel hydroxide recycling step includes opening valve 2, valve 3, closes valve 4, opens pump 2, nickel-containing waste water is pumped into hydroxide
Nickel recycling can；Valve 4, valve 6 are opened, pump 3, the stirring of 1# electricity, circular response liquid are opened；Valve 5 is slowly opened, by liquefied ammonia suction pump 3, benefit
With the high speed rotation of pump 3, it is sufficiently mixed reaction solution；Liquefied ammonia is added on side, and frontier inspection surveys the pH value of reaction solution, when pH value reaches 8.5-
When 9.0, valve 5 is closed, stops dosing, continues cycling through stirring 1 hour；1# filter press is opened, valve 7 is opened, closes valve 6, valve 8, Gu
Liquid separates nickel hydroxide；It sprays repeatedly, rinse nickel hydroxide solid after ten minutes, recycle nickel hydroxide product；
The nickel phosphate recycling step includes closing valve 9, valve 11, opens valve 8, valve 10, opens pump 4, the stirring of 2# electricity, and circulation is anti-
Answer liquid；Valve 9 is slowly opened, phosphoric acid suction pump 4 is sufficiently mixed reaction solution using the high speed rotation of pump 4；Add phosphoric acid, side in side
The pH value for detecting reaction solution closes valve 9 when pH value reaches 6.5-7.5, stops dosing, continues cycling through stirring 1 hour；It opens
2# filter press opens valve 11, closes valve 10, is separated by solid-liquid separation nickel phosphate；It sprays repeatedly, rinse nickel phosphate solid after ten minutes, return
Receive nickel phosphate product；
Compound fertilizer's recycling step includes opening valve 12, valve 13, opens pump 5, after recovered liquid is filtered, conveying
To land use for greening, used as compound fertilizer.
2. hole sealing agent recycling and Waste water utilization method that Aluminum according to claim 1 subtracts slag, it is characterised in that: described
17# flows 0.5-1.5g/L containing nickel acetate in rinsing bowl.
3. hole sealing agent recycling and Waste water utilization method that Aluminum according to claim 1 subtracts slag, it is characterised in that: described
It recycles and adds pure water and acetic acid in nickel hydroxide product, be converted to nickel acetate；
Acetic acid additive amount is 95% of addition weight needed for chemical reaction completely, and nickel hydroxide is suitably excessive in reaction solution, it is ensured that
Reacting liquid pH value >=6；
Under conditions of pure water weight/weight of nickel hydroxide is equal to 10, reaction solution acetic acid nickel content is 14.5-15.5wt%, far
Lower than the saturated concentration of nickel acetate, it is ensured that reaction solution is precipitated without nickel acetate crystal；
Precipitating, filtering reacting liquid obtain pH value >=6.0 contents lower than saturation point, can make nickel acetate raw material.
4. hole sealing agent recycling and Waste water utilization method that Aluminum according to claim 3 subtracts slag, it is characterised in that: first titrate
Then the content of liquid acetic nickel adds three second by nickel acetate/triethanolamine=10, nickel acetate/isobutanol=10 weight ratio
Nickel acetate solution is converted to liquid medium temperature hole sealing agent by hydramine and isobutanol.
5. hole sealing agent recycling and Waste water utilization method that Aluminum according to claim 3 subtracts slag, it is characterised in that: utilize hydrogen
When nickel oxide is converted to nickel acetate, only rinsing, without drying, add after pure water directly and acetic acid reaction.
6. hole sealing agent recycling and Waste water utilization method that Aluminum according to claim 3 subtracts slag, it is characterised in that: precipitating,
Filtered filter residue resides in reaction vessel, and waiting converts next time.
7. subtract the configuration of the hole sealing agent recycling and Waste water utilization method of slag described in -6 using Aluminum according to claim 1, it is special
Sign is: including nickel-containing waste water collection system, nickel hydroxide recovery system, nickel phosphate recovery system and compound fertilizer's recovery system；
The nickel-containing waste water collection system, the nickel hydroxide recovery system, the nickel phosphate recovery system and the compound fertilizer
Recovery system is sequentially connected；
The nickel-containing waste water collection system includes 17# flowing rinsing bowl, valve 1, pump 1 and sealing of hole nickel-containing waste water collecting tank, the pump 1
It is connected to the 17# flowing rinsing bowl, the valve 1 is set between 17# flowing rinsing bowl and pump 1, the sealing of hole nickel-containing waste water
Collecting tank is connected to the pump 1；
The nickel hydroxide recovery system includes that valve 2, valve 3, valve 4, valve 5, valve 6, valve 7, pump 2, pump 3,1# filter press, 1# electricity stir
It mixes, nickel hydroxide recycling can and ammonia tank, the valve 2 and the valve 3 are set to the both ends of the pump 2, and the pump 2 is connected to institute
Nickel hydroxide recycling can is stated, the 1# electricity stirring is set to above the nickel hydroxide recycling can, and the pump 3 is set to the hydrogen
Below nickel oxide recycling can, the valve 4 is set between pump 3 and nickel hydroxide recycling can, and one end of the pump 3 is connected to described
The upper end of nickel hydroxide recycling can, the valve 6 are set to one end of the pump 3, and the ammonia tank is connected to the pump 3, described
Valve 5 is set between the ammonia tank and the pump 3, and the 1# filter press is set to the lower section of the pump 3, and the valve 7 is arranged
Between the pump 3 and the 1# filter press；
The nickel phosphate recovery system includes valve 8, valve 9, valve 10, valve 11, pump 4, the stirring of 2# electricity, nickel phosphate recycling can, phosphoric acid tank
With 2# filter press, the nickel phosphate recycling can is connected to the 1# filter press, and the 2# electricity stirring is set to the nickel phosphate and returns
The top of closed cans, the pump 4 are connected to the nickel phosphate recycling can, and the valve 8 is set between pump 4 and nickel phosphate recycling can,
The 2# filter press is connected to the pump 4, and the valve 11 is set between pump 4 and 2# filter press, and the phosphoric acid tank is connected to institute
Pump 4 is stated, the valve 9 is set between phosphoric acid tank and pump 4, and one end of the pump 4 is connected to the upper end of the nickel phosphate recycling can,
The valve 10 is set to one end of the pump 4；
Compound fertilizer's recovery system includes valve 12, valve 13, pump 5, compound fertilizer's recycling can and filter, compound fertilizer's recycling can
It is connected to the 2# filter press, the filter is connected to compound fertilizer's recycling can, and the valve 12 is set to filter and answers
Between the recycling can of Hefei, the pump 5 is connected to the filter, and the valve 13 is set to the pump 5.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810841899.8A CN109160547A (en) | 2018-07-27 | 2018-07-27 | Aluminum subtract slag hole sealing agent recycling and Waste water utilization method with configure |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810841899.8A CN109160547A (en) | 2018-07-27 | 2018-07-27 | Aluminum subtract slag hole sealing agent recycling and Waste water utilization method with configure |
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| Publication Number | Publication Date |
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| CN109160547A true CN109160547A (en) | 2019-01-08 |
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| Application Number | Title | Priority Date | Filing Date |
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Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101636353A (en) * | 2007-03-27 | 2010-01-27 | 麦克德米德尖端有限公司 | Method of recycling electroless nickel waste |
| CN108191107A (en) * | 2017-12-29 | 2018-06-22 | 佛山市三水雄鹰铝表面技术创新中心有限公司 | The recovery system and method for single nickel salt coloring and medium temperature sealing of hole medicament in aluminium processing |
-
2018
- 2018-07-27 CN CN201810841899.8A patent/CN109160547A/en not_active Withdrawn
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101636353A (en) * | 2007-03-27 | 2010-01-27 | 麦克德米德尖端有限公司 | Method of recycling electroless nickel waste |
| CN108191107A (en) * | 2017-12-29 | 2018-06-22 | 佛山市三水雄鹰铝表面技术创新中心有限公司 | The recovery system and method for single nickel salt coloring and medium temperature sealing of hole medicament in aluminium processing |
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| Title |
|---|
| 天津大学普通化学教研室编: "《无机化学课堂演示实验（第一版）》", 30 June 1981, 人民教育出版社 * |
| 戚文彬等: "《分析化学 上册（第一版）》", 31 May 1982, 上海科学技术出版社 * |
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Application publication date: 20190108 |