CN109250803A - A kind of electroplating waste processing equipment and processing method - Google Patents

A kind of electroplating waste processing equipment and processing method Download PDF

Info

Publication number
CN109250803A
CN109250803A CN201811441562.4A CN201811441562A CN109250803A CN 109250803 A CN109250803 A CN 109250803A CN 201811441562 A CN201811441562 A CN 201811441562A CN 109250803 A CN109250803 A CN 109250803A
Authority
CN
China
Prior art keywords
reaction pond
waste water
cobalt
electroplating
mixed
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
Application number
CN201811441562.4A
Other languages
Chinese (zh)
Other versions
CN109250803B (en
Inventor
刘洪波
菅浩然
黄志伟
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Yellow River Conservancy Technical Institute
Original Assignee
Yellow River Conservancy Technical Institute
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Yellow River Conservancy Technical Institute filed Critical Yellow River Conservancy Technical Institute
Priority to CN201811441562.4A priority Critical patent/CN109250803B/en
Publication of CN109250803A publication Critical patent/CN109250803A/en
Application granted granted Critical
Publication of CN109250803B publication Critical patent/CN109250803B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • 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
    • C02F1/72—Treatment of water, waste water, or sewage by oxidation
    • C02F1/722—Oxidation by peroxides
    • 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
    • C02F1/72—Treatment of water, waste water, or sewage by oxidation
    • C02F1/76—Treatment of water, waste water, or sewage by oxidation with halogens or compounds of halogens
    • 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
    • C02F1/72—Treatment of water, waste water, or sewage by oxidation
    • C02F1/76—Treatment of water, waste water, or sewage by oxidation with halogens or compounds of halogens
    • C02F1/763—Devices for the addition of such compounds in gaseous form
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00—Electrodes
    • H01M4/02—Electrodes composed of, or comprising, active material
    • H01M4/36—Selection of substances as active materials, active masses, active liquids
    • H01M4/362—Composites
    • H01M4/366—Composites as layered products
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00—Electrodes
    • H01M4/02—Electrodes composed of, or comprising, active material
    • H01M4/36—Selection of substances as active materials, active masses, active liquids
    • H01M4/48—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00—Electrodes
    • H01M4/02—Electrodes composed of, or comprising, active material
    • H01M4/36—Selection of substances as active materials, active masses, active liquids
    • H01M4/48—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides
    • H01M4/50—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of manganese
    • H01M4/505—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of manganese of mixed oxides or hydroxides containing manganese for inserting or intercalating light metals, e.g. LiMn2O4 or LiMn2OxFy
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00—Electrodes
    • H01M4/02—Electrodes composed of, or comprising, active material
    • H01M4/36—Selection of substances as active materials, active masses, active liquids
    • H01M4/48—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides
    • H01M4/52—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of nickel, cobalt or iron
    • H01M4/525—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of nickel, cobalt or iron of mixed oxides or hydroxides containing iron, cobalt or nickel for inserting or intercalating light metals, e.g. LiNiO2, LiCoO2 or LiCoOxFy
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00—Electrodes
    • H01M4/02—Electrodes composed of, or comprising, active material
    • H01M4/36—Selection of substances as active materials, active masses, active liquids
    • H01M4/58—Selection of substances as active materials, active masses, active liquids of inorganic compounds other than oxides or hydroxides, e.g. sulfides, selenides, tellurides, halogenides or LiCoFy; of polyanionic structures, e.g. phosphates, silicates or borates
    • H01M4/5825—Oxygenated metallic salts or polyanionic structures, e.g. borates, phosphates, silicates, olivines
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00—Nature of the contaminant
    • C02F2101/10—Inorganic compounds
    • C02F2101/105—Phosphorus compounds
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00—Nature of the contaminant
    • C02F2101/10—Inorganic compounds
    • C02F2101/20—Heavy metals or heavy metal compounds
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00—Nature of the contaminant
    • C02F2101/10—Inorganic compounds
    • C02F2101/20—Heavy metals or heavy metal compounds
    • C02F2101/206—Manganese or manganese compounds
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/16—Nature of the water, waste water, sewage or sludge to be treated from metallurgical processes, i.e. from the production, refining or treatment of metals, e.g. galvanic wastes
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2209/00—Controlling or monitoring parameters in water treatment
    • C02F2209/06—Controlling or monitoring parameters in water treatment pH
    • 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
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10—Energy storage using batteries

Landscapes

  • Chemical & Material Sciences (AREA)
  • General Chemical & Material Sciences (AREA)
  • Electrochemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Inorganic Chemistry (AREA)
  • Water Supply & Treatment (AREA)
  • Organic Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Environmental & Geological Engineering (AREA)
  • Engineering & Computer Science (AREA)
  • Hydrology & Water Resources (AREA)
  • Composite Materials (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Removal Of Specific Substances (AREA)
  • Treatment Of Water By Oxidation Or Reduction (AREA)
  • Water Treatment By Electricity Or Magnetism (AREA)

Abstract

The present invention provides a kind of electroplating waste processing equipment and processing methods, including wastewater storage tank, the wastewater storage tank is connected with oxidation reaction pond, agitating device is equipped in oxidation reaction pond, oxidation reaction pond is connected with mixed reaction pond, mixed reaction pond is connected with filtering ponds, and carbon dioxide access equipment is equipped in the mixed reaction pond.Discarded lithium battery and electroplating wastewater are combined, pass through the content of each metal in regulation waste water, reach the requirement of lithium battery, without individually removing the aluminium in waste battery, it is reacted using carbon dioxide with sodium metaaluminate and the nickle cobalt lithium manganate of generation is coated, improve the chemical property of lithium battery, while final electroplating wastewater qualified discharge.

Description

A kind of electroplating waste processing equipment and processing method
Technical field
The present invention relates to electroplating wastewater processing fields, and in particular to a kind of electroplating waste processing equipment and processing method.
Background technique
The waste water and waste liquid that electroplating wastewater is mainly discharged by electroplating facility or workshop form, such as plating piece rinse water, useless tank liquor, Component cooling water and the flushing surface water etc..Since plating is more, technique is cumbersome, and water quality is complicated, and ingredient is not easy to control, and plating is useless Water mainly contains the heavy metal ion such as chromium, nickel, copper and cyanide etc., these electroplating wastewaters belong to carcinogenic, teratogenesis, mutagenic play Noxious material causes great injury to the living environment of the mankind and other biological.
Electroplating wastewater can be generally divided into three classes, and the first kind is electroplating wastewater of chromium, the chromium ion in this electroplating wastewater Concentration is higher, and the second class is cyanide-containing electroplating water, and the cyanide ion concentration in this waste water is higher, and third class is general plating Waste water, this waste water mainly contain a large amount of heavy metal ion.
Such as a kind of compound for treatment of electroplating wastes heavy metal recovery utilization side containing heavy metal Chinese patent 201110431946X Method discloses a kind of compound for treatment of electroplating wastes heavy metal recovery containing heavy metal using method, step are as follows: will contain heavy metal ion Low concentration electroplating wastewater by ion exchange resin, so that heavy metal ion contained in electroplating wastewater is adsorbed in ion friendship completely It changes resin and isolates clean water, until the absorption of ion exchange resin reaches saturation, eluent, which is added, to be made to be adsorbed in ion The heavy metal ion of exchanger resin is detached from the electroplating wastewater of ion exchange resin and output high concentration, then useless to high concentration plating Reducing agent is added in water and carries out reduction reaction, obtains the reduzate not soluble in water containing heavy metal ion, and flocculant is added and adds Fast reduzate coagulation, separates sediment finally by the methods of filtering or centrifugation, and recycle heavy metal by high-temperature calcination Substance is as the useful raw material of industry.
Alloy plating is the key areas of electroplating technology, because the advantages of alloy can integrate single metal, and have single The new characteristic, such as hardness, corrosion resistance, functionality etc. that one metal does not have.
Galvanoplastic manufacture diamond bit is the electro-deposition by metal, and loose diamond particles are fixedly arranged at electroplated layer In, make diamond particles that there is cutting function, since the manufacture of electroplated diamond bit carries out at normal temperature, diamond is not It is lost by high temperature, while diamond bit is secured, process of drill bit manufacture is simple, and equipment investment is few, one-pass molding.Diamond bit Working life be heavily dependent on the property of carcass, therefore diamond bit proposes extremely the performance of carcass material Strict requirements, the more ternary alloy coating of diamond bit is nickel-cobalt-manganese ternary alloy at present.
Electroplating wastewater industry average annual waste water yield in China's is up to 4,000,000,000 tons, accounts for the 1/6 of total discharged volume of industrial waste water, due to The complexity of electroplating wastewater causes the waste component generated complicated and changeable.Reality of the current most of electroplate factories to phosphorus-containing wastewater Processing mode is lime chemical precipitation method, but the water outlet phosphorus concentration usually after precipitation process is still maintained at 5-10mg/L, it is difficult to Reach standard.
For the electroplating wastewater containing heavy metal and a large amount of phosphorus, main methods are the precipitation method at present, and this method is main There is following defect: complex process, high to subsequent treatment process and environmental requirement, purification efficiency is not high, it is difficult to reach state's household electrical appliances The discharge standard of waste electroplating, and input cost is high, needs more treatment process steps and processing unit, consumes during processing Take a large amount of chemical reagent, the heavy metal in waste water is easy waste, can not turn waste into wealth.
Summary of the invention
The invention proposes a kind of electroplating waste processing equipment and processing method, by phosphorous, aluminium, cobalt, manganese electroplating wastewater into Row processing, recycles with waste and old nickel-cobalt-manganese ternary lithium battery, the nickel-cobalt lithium manganate material of alumina-coated is finally prepared, To improve the rate of recovery of heavy metal out of electroplating wastewater and old and useless battery.
It realizes the technical scheme is that a kind of electroplating waste processing equipment, including wastewater storage tank, the waste water store up It deposits slot to be connected with oxidation reaction pond, agitating device is equipped in oxidation reaction pond, oxidation reaction pond is connected with mixed reaction pond, mixes Reaction tank is connected with filtering ponds, and carbon dioxide access equipment is equipped in the mixed reaction pond.
The oxidation reaction pond is connected with chlorine dioxide tank, dioxygen water pot and sodium hypochlorite tank.
The method of the processing waste water of the electroplating waste processing equipment, steps are as follows:
(a) phosphorous, aluminium, cobalt, manganese electroplating wastewater, storage to wastewater storage tank are collected；
(b) sodium hydroxide solution is added into waste water, adjusts wastewater pH, compound oxidant is added, carries out oxygen in oxidation reaction pond Change reaction；
(c) waste and old nickel-cobalt-manganese ternary lithium battery anode piece is immersed in acid solution, to positive electrode active materials and aluminum foil current collector point From rear, taking-up aluminium foil, reducing agent is added in acid solution, filtrate is obtained by filtration to tertiary cathode material dissolution in heating stirring；
(d) step (b) waste water and step (c) filtrate are mixed, it is 1.5-5.0 that pH is adjusted in mixed reaction pond, and regulation is mixed Nickel, cobalt, manganese content in liquid are closed, molecular formula LiNi is complied withxCoyMn1-x-yO2, wherein x>0, y>0, x+y<1 are regulated original Liquid；
(e) sodium hydroxide solution is added into step (d) regulation stoste to be reacted, CO is passed through after reaction2Gas works as mixed base Aluminium content in liquid stops logical CO when being lower than 50ppm2Gas obtains solid material；
(f) solid material for obtaining step (e) is filtered, washs, dries, and lithium carbonate is added after dry and is uniformly mixed progress High-temperature calcination obtains the nickel-cobalt lithium manganate material of alumina-coated after calcining.
The mass concentration of sodium hydroxide solution is 15-25wt% in the step (b), and pH value is adjusted to 7-9.
Compound oxidant is that chlorine dioxide, hydrogen peroxide and liquor natrii hypochloritis mix in the step (b), wherein titanium dioxide The mass ratio of the material of chlorine, hydrogen peroxide and sodium hypochlorite is 1:(1-2): (2-5).
Acid solution includes hydrochloric acid or sulfuric acid in the step (c), and acid strength is 0.1-10 mol/L；With the waste and old nickel cobalt of 10g On the basis of manganese ternary lithium battery anode piece, acid solution dosage is 0. 5-1 L.
Reducing agent is hydrogen peroxide, sulphite, bisulfites, thiosulfate in the step (c), and reducing agent is dense Degree is 0.1-5 mol/L；On the basis of the waste and old nickel-cobalt-manganese ternary lithium battery anode piece of 10g, the additive amount of reducing agent is 0.25- 0.5L。
Heating temperature is 30-100 DEG C in the step (c), and mixing time is 40-120 min.
The mass ratio of regulation stoste and sodium hydroxide solution is (20-30): (70-80), sodium hydroxide in the step (e) The mass concentration of solution is 15-25wt%.
Calcination temperature is 680-720 DEG C in the step (e), calcination time 9-12h.
The beneficial effects of the present invention are:
(1) the invention firstly uses compound oxidants to the phosphorus removing in phosphorous short concentration waste water, so that Phosphorus From Wastewater is dense Degree is reduced to 2-5mg/L, and the sodium metaaluminate generated in later-stage utilization sodium hydroxide adjustment process can adsorb a part again P, so that water outlet total phosphorus concentration meets discharge standard；
(2) present invention combines discarded lithium battery and electroplating wastewater, by the content of each metal in regulation waste water, makes it The requirement for reaching lithium battery react pair without individually removing the aluminium in waste battery using carbon dioxide and sodium metaaluminate The nickle cobalt lithium manganate of generation is coated, and the chemical property of lithium battery, while final electroplating wastewater qualified discharge are improved.
Detailed description of the invention
In order to more clearly explain the embodiment of the invention or the technical proposal in the existing technology, to embodiment or will show below There is attached drawing needed in technical description to be briefly described, it should be apparent that, the accompanying drawings in the following description is only this Some embodiments of invention for those of ordinary skill in the art without creative efforts, can be with It obtains other drawings based on these drawings.
Fig. 1 is schematic structural view of the invention.
Specific embodiment
Below in conjunction with the embodiment of the present invention, technical solution of the present invention is clearly and completely described, it is clear that institute The embodiment of description is only a part of the embodiment of the present invention, instead of all the embodiments.Based on the embodiments of the present invention, Those of ordinary skill in the art's every other embodiment obtained under that premise of not paying creative labor, belongs to this hair The range of bright protection.
A kind of electroplating waste processing equipment, including wastewater storage tank 1, the wastewater storage tank 1 and 2 phase of oxidation reaction pond Even, it is equipped with agitating device in oxidation reaction pond 2, oxidation reaction pond 2 is connected with mixed reaction pond 3, mixed reaction pond 3 and filtering ponds 4 are connected, and are equipped with carbon dioxide access equipment 5 in the mixed reaction pond 3.
The oxidation reaction pond 2 is connected with chlorine dioxide tank 6, dioxygen water pot 7 and sodium hypochlorite tank 8.
Embodiment 1
A kind of electroplating wastewater comprehensive processing technique, steps are as follows:
(1) phosphorous, aluminium, cobalt, manganese electroplating wastewater are collected；Wherein the content of phosphorus is 48.9mg/L, total manganese content in electroplating wastewater 18.2 mg/L, total 6.3 mg/L of cobalt content, total 7.38 mg/L of aluminium content；
(2) it is 15wt% morning sodium hydroxide solution that mass concentration is added into waste water, adjusts wastewater pH 7, and compounding oxidation is added Agent, compound oxidant are that chlorine dioxide, hydrogen peroxide and liquor natrii hypochloritis mix, wherein chlorine dioxide, hydrogen peroxide and hypochlorous acid The mass ratio of the material of sodium is 1:1:2, carries out oxidation reaction；
(3) waste and old nickel-cobalt-manganese ternary lithium battery anode piece is immersed in the hydrochloric acid solution that concentration is 0.1mol/L, it is waste and old with 10g On the basis of nickel-cobalt-manganese ternary lithium battery anode piece, acid solution dosage is 0.5 L；It is separated to positive electrode active materials with aluminum foil current collector Afterwards, aluminium foil is taken out, is added in acid solution in the hydrogen peroxide that concentration is 0.1 mol/L, heats 30 DEG C of stirring 120 min to three First positive electrode dissolution, is obtained by filtration filtrate；On the basis of the waste and old nickel-cobalt-manganese ternary lithium battery anode piece of 10g, reducing agent Additive amount is 0.25 L；
(4) step (2) waste water and step (3) filtrate are mixed, adjusting pH is 1.5, regulates and controls nickel, cobalt, manganese in mixed liquor and contains Amount, complies with molecular formula LiNi0.5Co0.2Mn0.3O2, it is regulated stoste；
(5) sodium hydroxide solution is added into step (4) regulation stoste to be reacted, regulates and controls the matter of stoste and sodium hydroxide solution For amount than being 20:80, the mass concentration of sodium hydroxide solution is 15wt%, is passed through CO after reaction2Gas, when in mixed alkali liquor Aluminium content stops logical CO when being lower than 50ppm2Gas obtains solid material；
(6) solid material that step (5) obtains is filtered, washed, dried, lithium carbonate is added after dry and is uniformly mixed progress High-temperature calcination, calcination temperature are 680 DEG C, and calcination time 12h obtains the nickel-cobalt lithium manganate material of alumina-coated after calcining, Lithium content reaches 8wt% in the nickel-cobalt lithium manganate material of alumina-coated.
The performance of the nickel-cobalt lithium manganate material of alumina-coated prepared by embodiment 1
The content of Phosphorus From Wastewater can be reduced to 0.5mg/L in the present embodiment hereinafter, reaching discharge standard for electroplating pollutants, given up The content of underwater gold category ion can recycle, final discharged wastewater met the national standard.
Embodiment 2
A kind of electroplating wastewater comprehensive processing technique, steps are as follows:
(1) phosphorous, aluminium, cobalt, manganese electroplating wastewater are collected；Wherein the content of phosphorus is 48.9mg/L, total manganese content in electroplating wastewater 18.2 mg/L, total 6.3 mg/L of cobalt content, total 7.38 mg/L of aluminium content；
(2) it is 20wt% morning sodium hydroxide solution that mass concentration is added into waste water, adjusts wastewater pH 8, and compounding oxidation is added Agent, compound oxidant are that chlorine dioxide, hydrogen peroxide and liquor natrii hypochloritis mix, wherein chlorine dioxide, hydrogen peroxide and hypochlorous acid The mass ratio of the material of sodium is 1:1.5:3, carries out oxidation reaction；
(3) waste and old nickel-cobalt-manganese ternary lithium battery anode piece is immersed in the hydrochloric acid or sulfuric acid solution that concentration is 5 mol/L, to just After pole active material is separated with aluminum foil current collector, aluminium foil is taken out, is added in acid solution in the sodium sulfite that concentration is 3 mol/L, It heats 80 DEG C of 80 min of stirring to dissolve to tertiary cathode material, filtrate is obtained by filtration；With the waste and old nickel-cobalt-manganese ternary lithium battery of 10g On the basis of anode pole piece, the additive amount of reducing agent is 0.4 L；
(4) step (2) waste water and step (3) filtrate are mixed, adjusting pH is 3.0, regulates and controls nickel, cobalt, manganese in mixed liquor and contains Amount, complies with molecular formula LiNi0.5Co0.2Mn0.3O2, it is regulated stoste；
(5) sodium hydroxide solution is added into step (4) regulation stoste to be reacted, regulates and controls the matter of stoste and sodium hydroxide solution For amount than being 25:75, the mass concentration of sodium hydroxide solution is 20wt%, is passed through CO after reaction2Gas, when in mixed alkali liquor Aluminium content stops logical CO when being lower than 50ppm2Gas obtains solid material；
(6) solid material that step (5) obtains is filtered, washed, dried, lithium carbonate is added after dry and is uniformly mixed progress High-temperature calcination, calcination temperature are 700 DEG C, and calcination time 10h obtains the nickel-cobalt lithium manganate material of alumina-coated after calcining, Lithium content reaches 7wt% in the nickel-cobalt lithium manganate material of alumina-coated.
The performance of the nickel-cobalt lithium manganate material of alumina-coated prepared by embodiment 2
The content of Phosphorus From Wastewater can be reduced to 0.48mg/L in the present embodiment hereinafter, reaching discharge standard for electroplating pollutants, The content of metal ion can recycle in waste water, final discharged wastewater met the national standard.
Embodiment 3
A kind of electroplating wastewater comprehensive processing technique, steps are as follows:
(1) phosphorous, aluminium, cobalt, manganese electroplating wastewater are collected；Wherein the content of phosphorus is 48.9mg/L, total manganese content in electroplating wastewater 18.2 mg/L, total 6.3 mg/L of cobalt content, total 7.38 mg/L of aluminium content；
(2) it is 25wt% morning sodium hydroxide solution that mass concentration is added into waste water, adjusts wastewater pH 9, and compounding oxidation is added Agent, compound oxidant are that chlorine dioxide, hydrogen peroxide and liquor natrii hypochloritis mix, wherein chlorine dioxide, hydrogen peroxide and hypochlorous acid The mass ratio of the material of sodium is 1:2:5, carries out oxidation reaction；
(3) waste and old nickel-cobalt-manganese ternary lithium battery anode piece is immersed in the hydrochloric acid or sulfuric acid solution that concentration is 10 mol/L, to After positive electrode active materials are separated with aluminum foil current collector, aluminium foil is taken out, the bisulfite that concentration is 5 mol/L is added in acid solution Sodium heats 100 DEG C of 40 min of stirring and dissolves to tertiary cathode material, filtrate is obtained by filtration；With the waste and old nickel-cobalt-manganese ternary lithium of 10g On the basis of battery positive pole piece, the additive amount of reducing agent is 0.5 L；
(4) step (2) waste water and step (3) filtrate are mixed, adjusting pH is 5.0, regulates and controls nickel, cobalt, manganese in mixed liquor and contains Amount, complies with molecular formula LiNi0.6Co0.2Mn0.2O2, wherein x>0, y>0, x+y<1 are regulated stoste；
(5) sodium hydroxide solution is added into step (4) regulation stoste to be reacted, regulates and controls the matter of stoste and sodium hydroxide solution For amount than being 30:70, the mass concentration of sodium hydroxide solution is 25wt%, is passed through CO after reaction2Gas, when in mixed alkali liquor Aluminium content stops logical CO when being lower than 50ppm2Gas obtains solid material；
(6) solid material that step (5) obtains is filtered, washed, dried, lithium carbonate is added after dry and is uniformly mixed progress High-temperature calcination, calcination temperature are 720 DEG C, and calcination time 9h obtains the nickel-cobalt lithium manganate material of alumina-coated, oxygen after calcining Change lithium content in the nickel-cobalt lithium manganate material of aluminium cladding and reaches 7.5wt%.
The performance of the nickel-cobalt lithium manganate material of alumina-coated prepared by embodiment 3
The content of Phosphorus From Wastewater can be reduced to 0.35mg/L in the present embodiment hereinafter, reaching discharge standard for electroplating pollutants, The content of metal ion can recycle in waste water, final discharged wastewater met the national standard.
The foregoing is merely illustrative of the preferred embodiments of the present invention, is not intended to limit the invention, all in essence of the invention Within mind and principle, any modification, equivalent replacement, improvement and so on be should all be included in the protection scope of the present invention.

Claims (10)

1. a kind of electroplating waste processing equipment, it is characterised in that: including wastewater storage tank (1), the wastewater storage tank (1) and oxygen To change reaction tank (2) to be connected, agitating device is equipped in oxidation reaction pond (2), oxidation reaction pond (2) are connected with mixed reaction pond (3), Mixed reaction pond (3) is connected with filtering ponds (4), is equipped with carbon dioxide access equipment (5) in the mixed reaction pond (3).
2. electroplating waste processing equipment according to claim 1, it is characterised in that: the oxidation reaction pond (2) and dioxy Change chlorine tank (6), dioxygen water pot (7) is connected with sodium hypochlorite tank (8).
3. the method for the processing waste water using electroplating waste processing equipment described in as claimed in claim 1 or 22, it is characterised in that step is such as Under:
(a) phosphorous, aluminium, cobalt, manganese electroplating wastewater, storage to wastewater storage tank (1) are collected；
(b) sodium hydroxide solution is added into waste water, adjusts wastewater pH, compound oxidant is added, is carried out in oxidation reaction pond (2) Oxidation reaction；
(c) waste and old nickel-cobalt-manganese ternary lithium battery anode piece is immersed in acid solution, to positive electrode active materials and aluminum foil current collector point From rear, taking-up aluminium foil, reducing agent is added in acid solution, filtrate is obtained by filtration to tertiary cathode material dissolution in heating stirring；
(d) step (b) waste water and step (c) filtrate are mixed, it is 1.5-5.0, regulation that pH is adjusted in mixed reaction pond (3) Nickel, cobalt, manganese content in mixed liquor, comply with molecular formula LiNixCoyMn1-x-yO2, wherein x>0, y>0, x+y<1 are regulated Stoste；
(e) sodium hydroxide solution is added into step (d) regulation stoste to be reacted, CO is passed through after reaction2Gas works as mixed base Aluminium content in liquid stops logical CO when being lower than 50ppm2Gas obtains solid material；
(f) solid material for obtaining step (e) is filtered, washs, dries, and lithium carbonate is added after dry and is uniformly mixed progress High-temperature calcination obtains the nickel-cobalt lithium manganate material of alumina-coated after calcining.
4. the method for processing waste water according to claim 3, it is characterised in that: sodium hydroxide solution in the step (b) Mass concentration be 15-25wt%, pH value is adjusted to 7-9.
5. the method for processing waste water according to claim 3, it is characterised in that: compound oxidant is in the step (b) Chlorine dioxide, hydrogen peroxide and liquor natrii hypochloritis's mixing, wherein the mass ratio of the material of chlorine dioxide, hydrogen peroxide and sodium hypochlorite is 1:(1-2): (2-5).
6. the method for processing waste water according to claim 3, it is characterised in that: acid solution includes hydrochloric acid in the step (c) Or sulfuric acid, acid strength are 0.1-10 mol/L；On the basis of the waste and old nickel-cobalt-manganese ternary lithium battery anode piece of 10g, acid solution is used Amount is 0. 5-1 L.
7. the method for processing waste water according to claim 3, it is characterised in that: reducing agent is peroxide in the step (c) Change hydrogen, sulphite, bisulfites, thiosulfate, reductant concentration is 0.1-5 mol/L；With the waste and old nickel cobalt manganese three of 10g On the basis of first lithium battery anode piece, the additive amount of reducing agent is 0.25-0.5 L.
8. the method for processing waste water according to claim 3, it is characterised in that: heating temperature is 30- in the step (c) 100 DEG C, mixing time is 40-120 min.
9. the method for processing waste water according to claim 3, it is characterised in that: regulation stoste and hydrogen in the step (e) The mass ratio of sodium hydroxide solution is (20-30): (70-80), and the mass concentration of sodium hydroxide solution is 15-25wt%.
10. the method for processing waste water according to claim 3, it is characterised in that: calcination temperature is in the step (e) 680-720 DEG C, calcination time 9-12h.
CN201811441562.4A 2018-11-29 2018-11-29 Electroplating wastewater treatment device and treatment method Active CN109250803B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201811441562.4A CN109250803B (en) 2018-11-29 2018-11-29 Electroplating wastewater treatment device and treatment method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201811441562.4A CN109250803B (en) 2018-11-29 2018-11-29 Electroplating wastewater treatment device and treatment method

Publications (2)

Publication Number Publication Date
CN109250803A true CN109250803A (en) 2019-01-22
CN109250803B CN109250803B (en) 2021-07-30

Family

ID=65042257

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201811441562.4A Active CN109250803B (en) 2018-11-29 2018-11-29 Electroplating wastewater treatment device and treatment method

Country Status (1)

Country Link
CN (1) CN109250803B (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110156056A (en) * 2019-04-18 2019-08-23 新疆众和股份有限公司 A method of special-alumina is prepared containing phosphorus waste liquid using corrosive aluminum foil

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104071887A (en) * 2014-07-14 2014-10-01 南京大学 Compound oxidant for advanced treatment of electroplate phosphorate wastewater and wastewater treatment method
CN104480317A (en) * 2014-11-13 2015-04-01 朱蕾 Cobalt nickel metallurgy wastewater sludge recycling method
CN106785177A (en) * 2017-03-10 2017-05-31 中南大学 A kind of method for being reclaimed from waste and old nickel-cobalt-manganese ternary lithium ion battery, preparing nickel cobalt manganese aluminium quaternary positive electrode
JP2017115179A (en) * 2015-12-22 2017-06-29 日本リサイクルセンター株式会社 Recovery method of valuable substance
CN108172799A (en) * 2017-12-28 2018-06-15 清远佳致新材料研究院有限公司 A kind of tertiary cathode material of nucleocapsid structure lithium ion battery and preparation method thereof
CN108682915A (en) * 2018-05-29 2018-10-19 江苏理工学院 A kind of waste and old nickel-cobalt-manganese ternary lithium battery and silver-nickel are jointly processed by method
CN108862755A (en) * 2018-07-23 2018-11-23 师海荣 A kind of processing method of nickel cyano complex electroplating wastewater
CN108899604A (en) * 2018-06-28 2018-11-27 郑州中科新兴产业技术研究院 Utilize the method for waste lithium cell anode pole piece preparation ternary anode material precursor

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104071887A (en) * 2014-07-14 2014-10-01 南京大学 Compound oxidant for advanced treatment of electroplate phosphorate wastewater and wastewater treatment method
CN104480317A (en) * 2014-11-13 2015-04-01 朱蕾 Cobalt nickel metallurgy wastewater sludge recycling method
JP2017115179A (en) * 2015-12-22 2017-06-29 日本リサイクルセンター株式会社 Recovery method of valuable substance
CN106785177A (en) * 2017-03-10 2017-05-31 中南大学 A kind of method for being reclaimed from waste and old nickel-cobalt-manganese ternary lithium ion battery, preparing nickel cobalt manganese aluminium quaternary positive electrode
CN108172799A (en) * 2017-12-28 2018-06-15 清远佳致新材料研究院有限公司 A kind of tertiary cathode material of nucleocapsid structure lithium ion battery and preparation method thereof
CN108682915A (en) * 2018-05-29 2018-10-19 江苏理工学院 A kind of waste and old nickel-cobalt-manganese ternary lithium battery and silver-nickel are jointly processed by method
CN108899604A (en) * 2018-06-28 2018-11-27 郑州中科新兴产业技术研究院 Utilize the method for waste lithium cell anode pole piece preparation ternary anode material precursor
CN108862755A (en) * 2018-07-23 2018-11-23 师海荣 A kind of processing method of nickel cyano complex electroplating wastewater

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
杨重愚: "《氧化铝生产工艺学》", 31 January 1982, 冶金工业出版社 *

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110156056A (en) * 2019-04-18 2019-08-23 新疆众和股份有限公司 A method of special-alumina is prepared containing phosphorus waste liquid using corrosive aluminum foil
CN110156056B (en) * 2019-04-18 2021-12-28 新疆众和股份有限公司 Method for preparing special alumina by using phosphorus-containing waste liquid generated by corroding aluminum foil

Also Published As

Publication number Publication date
CN109250803B (en) 2021-07-30

Similar Documents

Publication Publication Date Title
CN203904113U (en) Classified treatment equipment for sewage
CN105541043B (en) Based on MBR and A2The waste lithium cell electrolyte of/O and the processing method of electrolyte waste water
CN102557299B (en) Recovery method of copper-nickel heavy metals in electroplated mixed-flow waste water
CN101423309B (en) Electroplating waste water and heavy metal double recovery method
CN104577243B (en) Method for recovering lithium resource from lithium-ion-containing solution by using lithium ion carrier
US9199867B2 (en) Removal of metals from water
CN104386874A (en) Processing technology for high-concentration waste liquid in circuit board industry
CN111268771A (en) Electrochemical method for dechlorinating and removing heavy metals from incineration fly ash water washing liquid
CN109439907A (en) A method of iron aluminium is removed from the pickle liquor during recycling used Li ion cell
CN106698759B (en) A kind for the treatment of method of chemical nickel-plating wastewater
CN102730742A (en) Technique for producing soluble copper oxide from acidic etching waste liquor
CN109536720A (en) The removal methods of chlorine in a kind of copper-bath
CN207158980U (en) Tubular type electric flocculation device
CN108101163A (en) It is a kind of that valuable metal is recycled from industrial wastewater and drops ammonia nitrogen and the method for COD
CN103011347B (en) Method for carrying out electrolytic treatment on copper-containing electroplating wastewater and recycling copper
CN107742760A (en) Method for extracting lithium from waste lithium ion battery
CN106282567A (en) A kind of method reclaiming metal from useless acidic etching liquid
CN109928553A (en) A kind of chemical nickel plating waste solution processing unit and method
CN110422948A (en) Copper sulphate Sewage treatment metallic copper treatment process is electroplated
KR20170130408A (en) Method for producing copper and apparatus for producing copper
CN106186185A (en) A kind of method that industry nickel-containing waste water reclaims preparation high-purity nickel salt
CN103922519A (en) Process for recycling cyaniding gold plating liquid carried by board surface in PCB (Printed Circuit Board) industry
CN105923854A (en) Treatment method of high-strength organic wastewater
CN103408164A (en) Recycling method of electroplating wastewater containing copper nitrate
CN109250803A (en) A kind of electroplating waste processing equipment and processing method

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