CN106145463A - The processing method of a kind ofization tinning bronze alloy waste plating solution - Google Patents

The processing method of a kind ofization tinning bronze alloy waste plating solution Download PDF

Info

Publication number
CN106145463A
CN106145463A CN201610644150.5A CN201610644150A CN106145463A CN 106145463 A CN106145463 A CN 106145463A CN 201610644150 A CN201610644150 A CN 201610644150A CN 106145463 A CN106145463 A CN 106145463A
Authority
CN
China
Prior art keywords
plating solution
processing method
copper
bronze alloy
waste plating
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.)
Pending
Application number
CN201610644150.5A
Other languages
Chinese (zh)
Inventor
倪自飞
姚利丽
华欣
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.)
Jiangsu Xingda Steel Tyre Cord Co Ltd
Original Assignee
Jiangsu Xingda Steel Tyre Cord Co Ltd
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 Jiangsu Xingda Steel Tyre Cord Co Ltd filed Critical Jiangsu Xingda Steel Tyre Cord Co Ltd
Priority to CN201610644150.5A priority Critical patent/CN106145463A/en
Publication of CN106145463A publication Critical patent/CN106145463A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F9/00Multistage treatment of water, waste water or sewage
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B25/00Obtaining tin
    • C22B25/06Obtaining tin from scrap, especially tin scrap
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B7/00Working up raw materials other than ores, e.g. scrap, to produce non-ferrous metals and compounds thereof; Methods of a general interest or applied to the winning of more than two metals
    • C22B7/006Wet processes
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25CPROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
    • C25C1/00Electrolytic production, recovery or refining of metals by electrolysis of solutions
    • C25C1/12Electrolytic production, recovery or refining of metals by electrolysis of solutions of copper
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/001Processes for the treatment of water whereby the filtration technique is of importance
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/46Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/72Treatment of water, waste water, or sewage by oxidation
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/16Nature 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
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling

Abstract

The invention discloses the processing method of a kind ofization tinning bronze alloy waste plating solution, waste plating solution adds oxidant stirring and stands, and takes its supernatant, the tin ion concentration in detection supernatant;Filtering, filtering residue is delivered to Xi Ni treatment plant and is carried stannum;Filtrate electrolysis cathode analysis copper, the plating solution after electrolysis detects the concentration of its copper ion;It is discharged to Sewage Disposal the most again process together with sour water.The processing method changing tinning bronze alloy waste plating solution that the present invention provides, has not only reclaimed copper, stannum heavy metal, has also solved the problem that waste plating solution is difficult, easily cause environmental pollution, have dual economic benefit and environmental benefit.

Description

The processing method of a kind ofization tinning bronze alloy waste plating solution
Technical field
The present invention relates to the processing method of a kind ofization tinning bronze alloy waste plating solution, belong to liquid waste processing heavy metal recovery skill Art field.
Background technology
At present in the plating solution of tinning bronze alloy, plate in high solution of tin the content of tin ion at 0.7-1.0g/L, copper ion Content at about 5g/L, and in order to allow copper and tin ion co-deposit, plating solution with the addition of multiple complexant.If just allowing such Discharging of waste liquid is to waste water treatment plant, it is clear that Conventional waste water processing method is not all right.To use the copper in substep electroextraction solution Tin metal, due to the existence of complexant in its solution so that it is copper and tin current potential difference is less, and the method can not reach separating effect. For this waste liquid containing noble metal, it is necessary to find feasible processing method.
Summary of the invention
Purpose: in order to overcome the deficiencies in the prior art, the present invention provides oneization tinning bronze alloy waste plating solution Processing method.
Technical scheme: for solving above-mentioned technical problem, the technical solution used in the present invention is:
The processing method of a kind ofization tinning bronze alloy waste plating solution, it is characterised in that comprise the following steps: waste plating solution adds oxidation Agent stirring stands, and takes its supernatant, the tin ion concentration in detection supernatant;Filtering, filtering residue is delivered to Xi Ni treatment plant and is carried stannum;Filter Liquid electrolysis cathode analysis copper, the plating solution after electrolysis detects the concentration of its copper ion;Be discharged to the most again Sewage Disposal with Sour water processes together;Specific as follows:
1) in waste plating solution, oxidizer stirring stands;
2) take the tin ion concentration in supernatant detection supernatant, to tin ion concentration≤0.1g/L, terminate to stand;
3) filtering, filtering residue is delivered to Xi Ni treatment plant and is carried stannum, and filtrate analyses copper by electrolysis cathode;
4) the solution copper ion concentration after detection electrolysis, to copper ion concentration≤0.1g/L, terminates electrolysis;
5) taking out tough cathode, solution is delivered to sewage treatment plant and is processed together with acid solution.
The described processing method changing tinning bronze alloy waste plating solution, it is characterised in that: described oxidant can be air, One or more of oxygen or hydrogen peroxide.
The described processing method changing tinning bronze alloy waste plating solution, it is characterised in that: the waste plating solution after standing takes it Supernatant, detects the tin ion concentration in its supernatant with chemical titration (iodimetry), as its tin ion concentration≤0.1g/ During L, next step operation can be carried out.
The described processing method changing tinning bronze alloy waste plating solution, it is characterised in that: filtrate electrolysis cathode analysis copper, anode Using platinum electrode, negative electrode uses copper electrode, and electric current density is 195-210A/m2, voltage is 0.3-0.5V, and temperature is room temperature, stirs Mixing speed is 200-300r/min.
The described processing method changing tinning bronze alloy waste plating solution, it is characterised in that: the plating solution after electrolysis, with chemistry The concentration of titrimetry (Reduction by Thiosulfate titration) detection copper ion, as copper ion concentration≤0.1g/L, under can carrying out Single stepping.
Preferably, the described processing method changing tinning bronze alloy waste plating solution, it is characterised in that: described filtration The method using pressure filter filter pressing is carried out.
Beneficial effect: the processing method changing tinning bronze alloy waste plating solution that the present invention provides, uses and adds in plating solution The method of oxidant makes the tin ion oxidation precipitation in solution, so that stannum, copper ion in solution separate;Oxidant is oxygen Gas, hydrogen peroxide, will not give in solution and bring other foreign ions;In solution, copper, the detection of tin ion use electronation titration Method, the method is simple, quickly, accurately.The processing method of the present invention simplifies the process step of waste plating solution, not only reclaimed copper, Stannum heavy metal, also solves the problem that waste plating solution is difficult, easily cause environmental pollution, has dual economic benefit and environment Benefit.
Accompanying drawing explanation
Fig. 1 is the process chart of the present invention.
Detailed description of the invention
Below in conjunction with specific embodiment, the present invention is further described.
As it is shown in figure 1, the processing method of a kind ofization tinning bronze alloy waste plating solution, take following processing procedure: waste plating solution Add oxidant stirring to stand, take its supernatant, the tin ion concentration in detection solution;Filtering subsequently, its filtering residue delivers to stannum mud Treatment plant carries out carrying stannum and processes;Its filtrate reclaims metallic copper by the method for electrolysis cathode analysis copper;Plating solution detection after electrolysis The concentration of its copper ion;It is discharged to Sewage Disposal the most again process together with other sour waters.Specifically comprise the following steps that
1. in waste plating solution, oxidizer stirring stands;
2. taking the tin ion concentration in supernatant detection supernatant, detected value must make tin ion concentration≤0.1g/L;
3. filtering above-mentioned solution, filtering residue is delivered to Xi Ni treatment plant and is carried stannum, and filtrate analyses copper by electrolysis cathode;
4. the solution after electrolysis detects its copper ion concentration, and detected value must make copper ion concentration≤0.1g/L;
5. taking out tough cathode, solution is delivered to sewage treatment plant and is processed together with acid solution.
Embodiment 1:
Taking tinning bronze alloy waste plating solution 500ml, in its plating solution copper ions concentration be 5.8g/L, the concentration of tin ion be 0.85g/L, sulfuric acid concentration are possibly together with different kinds of ions additive in 27g/L, solution.
In taken solution, add 40ml hydrogen peroxide, stand 3 hours after being sufficiently stirred for, take supernatant 10ml, use iodometric titration It is 0.03g/L that method records the concentration of tin ion in supernatant;Will stand after solution filter, filtrate carry out electrolysis cathode analysis copper: Anode uses platinum electrode, and negative electrode uses copper sheet to do electrode, and electric current density is 200 A/m2, voltage is 0.4V, and temperature is room temperature, stirs Mixing speed is 200-300r/min, is electrolysed 1 hour;Solution 10ml after power taking solution, with sodium thiosulfate titration detect in solution The concentration of copper ion is 0.08g/L, subsequently by solution discharge to Sewage Disposal.
The above is only the preferred embodiment of the present invention, it should be pointed out that: for the ordinary skill people of the art For Yuan, under the premise without departing from the principles of the invention, it is also possible to make some improvements and modifications, these improvements and modifications also should It is considered as protection scope of the present invention.

Claims (8)

1. the processing method changing tinning bronze alloy waste plating solution, it is characterised in that comprise the following steps: waste plating solution adds oxygen Agent stirring stands, and takes its supernatant, the tin ion concentration in detection supernatant;Filtering, filtering residue is delivered to Xi Ni treatment plant and is carried stannum; Filtrate electrolysis cathode analysis copper, the plating solution after electrolysis detects the concentration of its copper ion;It is discharged to Sewage Disposal the most again Process together with sour water;Specific as follows:
1) in waste plating solution, oxidizer stirring stands;
2) take the tin ion concentration in supernatant detection supernatant, to tin ion concentration≤0.1g/L, terminate to stand;
3) filtering, filtering residue is delivered to Xi Ni treatment plant and is carried stannum, and filtrate analyses copper by electrolysis cathode;
4) the solution copper ion concentration after detection electrolysis, to copper ion concentration≤0.1g/L, terminates electrolysis;
5) taking out tough cathode, solution is delivered to sewage treatment plant and is processed together with acid solution.
2. the processing method of according to claim 1ization tinning bronze alloy waste plating solution, it is characterised in that: described oxidant Can be one or more of air, oxygen or hydrogen peroxide.
3. the processing method of according to claim 1ization tinning bronze alloy waste plating solution, it is characterised in that: after standing Waste plating solution takes its supernatant, detects the tin ion concentration in its supernatant with chemical titration, as its tin ion concentration≤0.1g/ During L, next step operation can be carried out.
4. the processing method of according to claim 3ization tinning bronze alloy waste plating solution, it is characterised in that: use iodimetry Detect the tin ion concentration in its supernatant.
5. the processing method of according to claim 1ization tinning bronze alloy waste plating solution, it is characterised in that: filtrate electrolysis the moon Pole analysis copper, anode uses platinum electrode, and negative electrode uses copper electrode, and electric current density is 195-210A/m2, voltage is 0.3-0.5V, temperature Degree is room temperature, and mixing speed is 200-300r/min.
6. the processing method of according to claim 1ization tinning bronze alloy waste plating solution, it is characterised in that: after electrolysis Plating solution, by the concentration of chemical titration detection copper ion, as copper ion concentration≤0.1g/L, can carry out next step operation.
7. the processing method of according to claim 6ization tinning bronze alloy waste plating solution, it is characterised in that: use thiosulfuric acid The concentration of sodium reduction titration detection copper ion.
8. the processing method of according to claim 1ization tinning bronze alloy waste plating solution, it is characterised in that: described filtration is adopted Carry out by the method for pressure filter filter pressing.
CN201610644150.5A 2016-08-09 2016-08-09 The processing method of a kind ofization tinning bronze alloy waste plating solution Pending CN106145463A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610644150.5A CN106145463A (en) 2016-08-09 2016-08-09 The processing method of a kind ofization tinning bronze alloy waste plating solution

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201610644150.5A CN106145463A (en) 2016-08-09 2016-08-09 The processing method of a kind ofization tinning bronze alloy waste plating solution

Publications (1)

Publication Number Publication Date
CN106145463A true CN106145463A (en) 2016-11-23

Family

ID=57329279

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201610644150.5A Pending CN106145463A (en) 2016-08-09 2016-08-09 The processing method of a kind ofization tinning bronze alloy waste plating solution

Country Status (1)

Country Link
CN (1) CN106145463A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107500436A (en) * 2017-07-26 2017-12-22 张家港市亚亨金属制品有限公司 A kind of processing method of cupric, nickel ion waste plating solution

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB918934A (en) * 1959-11-24 1963-02-20 Graham Savage & Associates Inc Improvements in recovery of high purity copper from copper scrap
CN101643852A (en) * 2009-09-02 2010-02-10 北京科技大学 Heap-leaching method for separating copper and tin from tin-plated copper wires
CN102701263A (en) * 2012-05-04 2012-10-03 昆明理工大学 Method for preparing copper sulfate in mode that stanniferous copper slag is leached in selective mode and free of evaporation
CN102766883A (en) * 2011-06-14 2012-11-07 湖南万容科技股份有限公司 Spent solder stripper recovery method and equipment

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB918934A (en) * 1959-11-24 1963-02-20 Graham Savage & Associates Inc Improvements in recovery of high purity copper from copper scrap
CN101643852A (en) * 2009-09-02 2010-02-10 北京科技大学 Heap-leaching method for separating copper and tin from tin-plated copper wires
CN102766883A (en) * 2011-06-14 2012-11-07 湖南万容科技股份有限公司 Spent solder stripper recovery method and equipment
CN102701263A (en) * 2012-05-04 2012-10-03 昆明理工大学 Method for preparing copper sulfate in mode that stanniferous copper slag is leached in selective mode and free of evaporation

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107500436A (en) * 2017-07-26 2017-12-22 张家港市亚亨金属制品有限公司 A kind of processing method of cupric, nickel ion waste plating solution

Similar Documents

Publication Publication Date Title
CN104152905B (en) Acidic copper chloride etching liquid electrolytic regeneration recycling and copper plate recovery device and method
US9199867B2 (en) Removal of metals from water
Wang et al. Sustainable electrochemical recovery of high-purity Cu powders from multi-metal acid solution by a centrifuge electrode
CN109022795B (en) Method for removing components on waste printed circuit board by alkaline electrochemistry and special device thereof
CN103710706A (en) Purification and regeneration method of iron trichloride etching waste liquid
CN104152701B (en) The method that tin is reclaimed from tin refinement slag
CN112234238B (en) Method for preparing iron-chromium redox battery electrolyte
US4256557A (en) Copper electrowinning and Cr+6 reduction in spent etchants using porous fixed bed coke electrodes
CN104947155B (en) Process for recovering copper from waste circuit board to prepare high purity and high strength copper foil based on electrochemical method
CN112695345A (en) Method for recovering brownification waste liquid of printed circuit board
CN104355463A (en) Deep treatment method for landfill leachate
CN106145463A (en) The processing method of a kind ofization tinning bronze alloy waste plating solution
CN109518225B (en) Method for separating ferrous iron and cobalt nickel in solution
CN113707352A (en) Method for treating radioactive comprehensive wastewater
US11566333B2 (en) Method for cleanly extracting metallic silver
Nan et al. Process and anodic reaction mechanism of cadmium electrically enhanced cementation on zinc plate under an ultrasonic field in ammoniacal system
JP4168959B2 (en) Method for leaching copper electrolytic starch
KR20040052844A (en) The nickel collecting method from waste nickel fluid and oxidic acid nickel sludge
CN205892820U (en) System for ammonia nitrogen in electrolytic oxidation method processing ammonia nature copper chloride waste water
CN112250226A (en) Brownification waste liquid treatment method
KR101435762B1 (en) Method for reducing of glycol including wastewater and reductor glycol using the same
CN110904338B (en) Method for selectively recovering tin or lead from waste circuit board
CN102515392A (en) Method for processing electroplating wastewater
CN213327146U (en) Acid copper-containing etching liquid treatment system
CN101117252A (en) Drinking original water arsenic-removing and arsenic reclaiming technique

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
RJ01 Rejection of invention patent application after publication
RJ01 Rejection of invention patent application after publication

Application publication date: 20161123