CN105884068A - Electroplating solution purifying system - Google Patents
Electroplating solution purifying system Download PDFInfo
- Publication number
- CN105884068A CN105884068A CN201610377411.1A CN201610377411A CN105884068A CN 105884068 A CN105884068 A CN 105884068A CN 201610377411 A CN201610377411 A CN 201610377411A CN 105884068 A CN105884068 A CN 105884068A
- Authority
- CN
- China
- Prior art keywords
- purifying
- electroplating solution
- activated carbon
- nonactive
- filler
- 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
Links
- 238000009713 electroplating Methods 0.000 title claims abstract description 40
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 101
- 229910052799 carbon Inorganic materials 0.000 claims abstract description 37
- 239000000945 filler Substances 0.000 claims abstract description 35
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 29
- 239000004744 fabric Substances 0.000 claims abstract description 15
- 239000008187 granular material Substances 0.000 claims description 24
- 239000012528 membrane Substances 0.000 claims description 14
- 239000003463 adsorbent Substances 0.000 claims description 13
- 239000000919 ceramic Substances 0.000 claims description 13
- 239000002808 molecular sieve Substances 0.000 claims description 13
- 238000012856 packing Methods 0.000 claims description 13
- 239000011347 resin Substances 0.000 claims description 13
- 229920005989 resin Polymers 0.000 claims description 13
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 claims description 13
- RBTBFTRPCNLSDE-UHFFFAOYSA-N 3,7-bis(dimethylamino)phenothiazin-5-ium Chemical compound C1=CC(N(C)C)=CC2=[S+]C3=CC(N(C)C)=CC=C3N=C21 RBTBFTRPCNLSDE-UHFFFAOYSA-N 0.000 claims description 12
- ZCYVEMRRCGMTRW-UHFFFAOYSA-N 7553-56-2 Chemical compound [I] ZCYVEMRRCGMTRW-UHFFFAOYSA-N 0.000 claims description 12
- 235000013162 Cocos nucifera Nutrition 0.000 claims description 12
- 244000060011 Cocos nucifera Species 0.000 claims description 12
- 239000004743 Polypropylene Substances 0.000 claims description 12
- 230000001413 cellular effect Effects 0.000 claims description 12
- 239000010903 husk Substances 0.000 claims description 12
- 229910052740 iodine Inorganic materials 0.000 claims description 12
- 239000011630 iodine Substances 0.000 claims description 12
- 229960000907 methylthioninium chloride Drugs 0.000 claims description 12
- 238000001179 sorption measurement Methods 0.000 claims description 12
- 239000006004 Quartz sand Substances 0.000 claims description 10
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 10
- 238000000746 purification Methods 0.000 claims description 9
- -1 polypropylene Polymers 0.000 claims description 7
- 229920001155 polypropylene Polymers 0.000 claims description 7
- 230000004323 axial length Effects 0.000 claims description 6
- 239000000835 fiber Substances 0.000 claims description 6
- 238000011068 loading method Methods 0.000 claims description 6
- 239000000463 material Substances 0.000 claims description 5
- 239000004677 Nylon Substances 0.000 claims description 3
- 238000009954 braiding Methods 0.000 claims description 3
- 239000004745 nonwoven fabric Substances 0.000 claims description 3
- 229920001778 nylon Polymers 0.000 claims description 3
- 229950000845 politef Drugs 0.000 claims description 3
- 239000011148 porous material Substances 0.000 claims description 3
- 239000007921 spray Substances 0.000 claims description 3
- 239000004753 textile Substances 0.000 claims description 3
- 238000009941 weaving Methods 0.000 claims description 3
- 239000003610 charcoal Substances 0.000 claims description 2
- 239000002184 metal Substances 0.000 abstract description 3
- 229910021645 metal ion Inorganic materials 0.000 abstract description 3
- 230000003749 cleanliness Effects 0.000 abstract 1
- 238000003912 environmental pollution Methods 0.000 abstract 1
- 239000000383 hazardous chemical Substances 0.000 abstract 1
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 230000002378 acidificating effect Effects 0.000 description 1
- 238000005352 clarification Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 238000010792 warming Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D21/00—Processes for servicing or operating cells for electrolytic coating
- C25D21/06—Filtering particles other than ions
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/281—Treatment of water, waste water, or sewage by sorption using inorganic sorbents
-
- 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
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/283—Treatment of water, waste water, or sewage by sorption using coal, charred products, or inorganic mixtures containing them
-
- 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
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/285—Treatment of water, waste water, or sewage by sorption using synthetic organic sorbents
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2301/00—General aspects of water treatment
- C02F2301/08—Multistage treatments, e.g. repetition of the same process step under different conditions
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Water Treatment By Sorption (AREA)
Abstract
The invention provides an electroplating solution purifying system. An electroplating solution to be treated in a solution groove is pumped by a circulation pump into a water guide pipe of a purifying device, large metal blocks to enter the water guide pipe are filtered away through a filter film or a filter cloth at the lower end of the water guide pipe at first, purifying filler in the water guide pipe makes sufficient contact with the electroplating solution and adsorbs hazardous substance and metal ions in the electroplating solution, online treatment of the electroplating solution is achieved, no additional carbon treating groove or standing groove is needed, occupied area is reduced, treating time is short, the electroplating solution can be thoroughly purified, and cleanliness and environmental pollution are achieved.
Description
Technical field
The invention belongs to electroplating technology field, particularly relate to a kind of purifying electroplating solution system.
Background technology
At present, existing purifying electroplating solution system uses following steps: first the electroplating solution purified will be needed to be pumped into carbon treatment trough by circulating pump, adds hydrogen peroxide, hydrogen peroxide is warming up to 60 DEG C and processes a period of time in carbon treatment trough；It is subsequently added into active carbon powder, stir process certain time, then after standing a period of time；Finally the solution on carbon treatment trough upper strata is pumped into additionally mounted standing groove, in standing groove, uses PP filter element filtering, fully remove the carbon dust of residual in solution；By above operation, the longest, purify the most up to standard.
Summary of the invention
It is an object of the invention to overcome above-mentioned the deficiencies in the prior art, it is provided that a kind of clarification time is short and the purifying electroplating solution system of good purification.
The present invention is realized in, a kind of purifying electroplating solution system, the solution tank of electroplating solution, a circulating pump and a purifier is filled including one, the water inlet of described circulating pump and water inlet pipe connection, the outlet of described circulating pump and outlet pipe connection, the described water inlet pipe other end is located at the bottom of described solution tank, the water inlet of described water inlet pipe is provided with a drainage screen, described outlet pipe connects with described purifier, the outlet of described purifier and drain pipe connection, the other end of described drain pipe is located in described solution tank；
Described purifier includes a support and some intervals and vertically-mounted aqueduct on the bracket, the lower end of each described aqueduct connects with described outlet pipe respectively, the upper end of each described aqueduct connects with drain pipe respectively, the water inlet of described aqueduct and outlet are separately installed with a filter membrane or filter cloth, purification filler it is filled with in described aqueduct, described purification filler includes ceramic packing, molecular sieve, activated carbon powder, nonactive powdered carbon, activated carbon granule, charcoal non activated granule, any one or two or more combination in quartz sand and adsorbent resin；
When purifying filler and being ceramic packing, the parameter of ceramic packing is: specific surface area: 1-2000m2/ g, voidage: 1-90%, bulk density: 1-2000KG/m, ceramic packing be shaped as ball, elliptical shape ball, corrugated, lamellar, cellular or cylindric；
When purifying filler and being molecular sieve, the parameter of molecular sieve is: mesh number: 1-1000, bulk density: 1-2000KG/m, specific surface area: 1-2000 m2/ g, pore volume: 0.1-10 cm3/ g, molecular sieve be shaped as ball, elliptical shape ball, corrugated, lamellar, cellular or cylindric；
When purifying filler and being activated carbon powder, the parameter of activated carbon powder is: granularity: 10-800 mesh, iodine sorption value >=40 mg/g, methylene blue number >=30 ml/g, ash≤15%, specific surface area: 1-3000m2/ g, PH:3-12, activated carbon powder is medium, wooden or coconut husk matter；
When purifying filler and being nonactive powdered carbon, the parameter of nonactive powdered carbon is: granularity: 10-800 mesh, iodine sorption value >=40 mg/g, methylene blue number >=30 ml/g, ash≤15%, specific surface area: 1-3000m2The nonactive powdered carbon of/g, PH:3-12 is medium, wooden or coconut husk matter；
When purifying filler and being activated carbon grain, the parameter of activated carbon grain is: granularity: 80-800 mesh, iodine sorption value >=40 mg/g, methylene blue number >=20 ml/g, loading density 20-1000 g/l, PH:3-12, specific surface area 1-2000m2/ g, activated carbon grain is medium, wooden or coconut husk matter, activated carbon grain be shaped as ball, elliptical shape ball, corrugated, lamellar, cylindric or cellular；
When purifying the nonactive carbon granule of filler, the parameter of nonactive carbon granule is: granularity: 80-800 mesh, iodine sorption value >=40 mg/g, methylene blue number >=20 ml/g, loading density 20-1000 g/l, PH:3-12, specific surface area 1-2000m2/ g, nonactive carbon granule be activated carbon grain be medium, wooden or coconut husk matter, nonactive carbon granule be shaped as ball, elliptical shape ball, corrugated, lamellar, cylindric or cellular；
When purifying filler and being quartz sand, the parameter of quartz sand is: bulk density is 0.5-5 ton/cubic meter, fusing point less than 2500 DEG C, and magnitude range is: 0.1-50mm；
When purifying filler and being adsorbent resin, the parameter of adsorbent resin is: aperture: 1-1000nm, specific surface area: 1-2000m2/ g, granularity 1-800 mesh, being shaped as of adsorbent resin is spherical.
Further, described water inlet pipe, described outlet pipe and described drain pipe are mounted on a control valve.
Specifically, as when being shaped as cylindric of activated carbon grain, a diameter of 0.1-100mm of activated carbon grain, axial length is 1-100mm.
Specifically, as when being shaped as cylindric of nonactive carbon granule, a diameter of 0.1-100mm of nonactive carbon granule, axial length is 1-100mm.
Preferably, described filter membrane is polypropylene thermal spray fiber membrane, polypropylene superfine fiber film or nylon politef microporous filter membrane.
Preferably, described filter cloth is non-woven fabrics or the weaving cloth by the braiding of textile fabric yarn.
Preferably, the material of described circulating pump, described water inlet pipe, described outlet pipe, described drain pipe, described support, described aqueduct and described control valve is PP.
The purifying electroplating solution system that the present invention provides, by circulating pump, electroplating solution pending in solution tank is pumped in the aqueduct of purifier, first filter membrane or filter cloth by aqueduct lower end filters the bigger metal agglomerates being prepared to enter in aqueduct, then the harmful substance being fully contacted by the purification filler in aqueduct and electroplating solution and adsorb in electroplating solution and metal ion, achieve the online treatment of electroplating solution, need not extra carbon treatment trough and stand groove, decrease floor space, the process time is short, electroplating solution can be made thoroughly to purify, clean environment firendly.
Accompanying drawing explanation
In order to be illustrated more clearly that technical scheme, the accompanying drawing used required in embodiment will be briefly described below, apparently, accompanying drawing in describing below is only some embodiments of the present invention, for those of ordinary skill in the art, on the premise of not paying creative work, it is also possible to obtain other accompanying drawing according to these accompanying drawings.
Fig. 1 is the schematic diagram of the purifying electroplating solution system that the present invention provides.
Detailed description of the invention
Below in conjunction with the accompanying drawing in the embodiment of the present invention, the technical scheme in the embodiment of the present invention is clearly and completely described.
As shown in Figure 1, a kind of purifying electroplating solution system that the embodiment of the present invention provides, including solution tank 1, circulating pump 2 filling electroplating solution and a purifier 3, water inlet and a water inlet pipe 4 of circulating pump 2 connect, outlet and an outlet pipe 5 of circulating pump 2 connect, water inlet pipe 4 other end is located at the bottom of solution tank 1, the water inlet of water inlet pipe 4 is provided with a drainage screen 41, outlet pipe 5 connects with purifier 3, outlet and a drain pipe 6 of purifier 3 connect, and the other end of drain pipe 6 is located in solution tank 1；
Purifier 3 includes a support 31 and some intervals and the aqueduct 32 being vertically installed on support 31, the lower end of each aqueduct 32 connects with outlet pipe 5 respectively, the upper end of each aqueduct 32 connects with drain pipe 6 respectively, the water inlet of aqueduct 32 and outlet are separately installed with filter membrane 33 or a filter cloth, it is filled with purification filler in aqueduct 32, purifies filler and include the combination of any one or more in ceramic packing, molecular sieve, activated carbon powder, nonactive powdered carbon, activated carbon grain, nonactive carbon granule, quartz sand or adsorbent resin；
When purifying filler and being ceramic packing, the parameter of ceramic packing is: specific surface area: 1-2000m2/ g, voidage: 1-90%, bulk density: 1-2000KG/m, ceramic packing be shaped as ball, elliptical shape ball, corrugated, lamellar, cellular or cylindric；
When purifying filler and being molecular sieve, the parameter of molecular sieve is: mesh number: 1-1000, bulk density: 1-2000KG/m, specific surface area: 1-2000 m2/ g, pore volume: 0.1-10 cm3/ g, molecular sieve be shaped as ball, elliptical shape ball, corrugated, lamellar, cellular or cylindric；
When purifying filler and being activated carbon powder, the parameter of activated carbon powder is: granularity: 10-800 mesh, iodine sorption value >=40 mg/g, methylene blue number >=30 ml/g, ash≤15%, specific surface area: 1-3000m2/ g, PH:3-12, activated carbon powder is medium, wooden or coconut husk matter；
When purifying filler and being nonactive powdered carbon, the parameter of nonactive powdered carbon is: granularity: 10-800 mesh, iodine sorption value >=40 mg/g, methylene blue number >=30 ml/g, ash≤15%, specific surface area: 1-3000m2The nonactive powdered carbon of/g, PH:3-12 is medium, wooden or coconut husk matter；
When purifying filler and being activated carbon grain, the parameter of activated carbon grain is: granularity: 80-800 mesh, iodine sorption value >=40 mg/g, methylene blue number >=20 ml/g, loading density 20-1000 g/l, PH:3-12, specific surface area 1-2000m2/ g, activated carbon grain is medium, wooden or coconut husk matter, activated carbon grain be shaped as ball, elliptical shape ball, corrugated, lamellar, cylindric or cellular；
When purifying the nonactive carbon granule of filler, the parameter of nonactive carbon granule is: granularity: 80-800 mesh, iodine sorption value >=40 mg/g, methylene blue number >=20 ml/g, loading density 20-1000 g/l, PH:3-12, specific surface area 1-2000m2/ g, nonactive carbon granule be activated carbon grain be medium, wooden or coconut husk matter, nonactive carbon granule be shaped as ball, elliptical shape ball, corrugated, lamellar, cylindric or cellular；
When purifying filler and being quartz sand, the parameter of quartz sand is: bulk density is 0.5-5 ton/cubic meter, fusing point less than 2500 DEG C, and magnitude range is: 0.1-50mm；
When purifying filler and being adsorbent resin, the parameter of adsorbent resin is: aperture: 1-1000nm, specific surface area: 1-2000m2/ g, granularity 1-800 mesh, being shaped as of adsorbent resin is spherical.
Wherein, when purifying filler and being two or more combinations, in composition included by above-mentioned purification filler, the percentage by weight of ceramic packing can be 0 ~ 50%, the percentage by weight of molecular sieve can be 0 ~ 50%, the percentage by weight of activated carbon powder can be 0 ~ 50%, the percentage by weight of nonactive powdered carbon can be 0 ~ 50%, the percentage by weight of activated carbon grain can be 0 ~ 100%, the percentage by weight of nonactive carbon granule can be 0 ~ 100%, the percentage by weight of quartz sand can be 0 ~ 50%, and the percentage by weight of adsorbent resin can be 0 ~ 60%.
Further, described water inlet pipe 4, outlet pipe 5 and drain pipe 6 are mounted on a control valve 7, the size of current in water inlet pipe 4, outlet pipe 5 and drain pipe 6 can be controlled respectively by control valve 7, it is simple to purify the electroplating solution in aqueduct 32.
Specifically, as when being shaped as cylindric of activated carbon grain, a diameter of 0.1-100mm of activated carbon grain, axial length is 1-100mm.
Specifically, as when being shaped as cylindric of nonactive carbon granule, a diameter of 0.1-100mm of nonactive carbon granule, axial length is 1-100mm.
Preferably, described filter membrane is polypropylene thermal spray fiber membrane, polypropylene superfine fiber film or nylon politef microporous filter membrane.
Preferably, described filter cloth is non-woven fabrics or the weaving cloth by the braiding of textile fabric yarn.
Preferably, the material of described circulating pump 2, water inlet pipe 4, outlet pipe 5, drain pipe 6, support 31, aqueduct 32 and control valve 7 is PP(polypropylene), select PP material, the acidic materials corrosion in resistance to electroplating solution.
The purifying electroplating solution system that the present invention provides, by circulating pump 2, pending electroplating solution in solution tank 1 is pumped in the aqueduct 32 of purifier 3, first filter membrane 33 or filter cloth by aqueduct 32 lower end filters the bigger metal agglomerates being prepared to enter in aqueduct 32, then the harmful substance being fully contacted by the purification filler in aqueduct 32 and electroplating solution and adsorb in electroplating solution and metal ion, achieve the online treatment of electroplating solution, need not extra carbon treatment trough and stand groove, decrease floor space, the process time is short, electroplating solution can be made thoroughly to purify, clean environment firendly.
The above is the preferred embodiment of the present invention; it should be pointed out that, for those skilled in the art, under the premise without departing from the principles of the invention; can also make some improvements and modifications, these improvements and modifications are also considered as protection scope of the present invention.
Claims (7)
1. a purifying electroplating solution system, it is characterized in that, the solution tank of electroplating solution, a circulating pump and a purifier is filled including one, the water inlet of described circulating pump and water inlet pipe connection, the outlet of described circulating pump and outlet pipe connection, the described water inlet pipe other end is located at the bottom of described solution tank, the water inlet of described water inlet pipe is provided with a drainage screen, described outlet pipe connects with described purifier, the outlet of described purifier and drain pipe connection, the other end of described drain pipe is located in described solution tank；
Described purifier includes a support and some intervals and vertically-mounted aqueduct on the bracket, the lower end of each described aqueduct connects with described outlet pipe respectively, the upper end of each described aqueduct connects with drain pipe respectively, the water inlet of described aqueduct and outlet are separately installed with a filter membrane or filter cloth, being filled with purification filler in described aqueduct, described purification filler includes the combination of any one or more in ceramic packing, molecular sieve, activated carbon powder, nonactive powdered carbon, activated carbon granule, charcoal non activated granule, quartz sand and adsorbent resin；
When purifying filler and being ceramic packing, the parameter of ceramic packing is: specific surface area: 1-2000m2/ g, voidage: 1-90%, bulk density: 1-2000KG/m, ceramic packing be shaped as ball, elliptical shape ball, corrugated, lamellar, cellular or cylindric；
When purifying filler and being molecular sieve, the parameter of molecular sieve is: mesh number: 1-1000, bulk density: 1-2000KG/m, specific surface area: 1-2000
m2/ g, pore volume: 0.1-10 cm3/ g, molecular sieve be shaped as ball, elliptical shape ball, corrugated, lamellar, cellular or cylindric；
When purifying filler and being activated carbon powder, the parameter of activated carbon powder is: granularity: 10-800 mesh, iodine sorption value >=40 mg/g, methylene blue number >=30 ml/g, ash≤15%, specific surface area: 1-3000m2/ g, PH:3-12, activated carbon powder is medium, wooden or coconut husk matter；
When purifying filler and being nonactive powdered carbon, the parameter of nonactive powdered carbon is: granularity: 10-800 mesh, iodine sorption value >=40 mg/g, methylene blue number >=30 ml/g, ash≤15%, specific surface area: 1-3000m2The nonactive powdered carbon of/g, PH:3-12 is medium, wooden or coconut husk matter；
When purifying filler and being activated carbon grain, the parameter of activated carbon grain is: granularity: 80-800 mesh, iodine sorption value >=40 mg/g, methylene blue number >=20 ml/g, loading density 20-1000 g/l, PH:3-12, specific surface area 1-2000m2/ g, activated carbon grain is medium, wooden or coconut husk matter, activated carbon grain be shaped as ball, elliptical shape ball, corrugated, lamellar, cylindric or cellular；
When purifying the nonactive carbon granule of filler, the parameter of nonactive carbon granule is: granularity: 80-800 mesh, iodine sorption value >=40 mg/g, methylene blue number >=20 ml/g, loading density 20-1000 g/l, PH:3-12, specific surface area 1-2000m2/ g, nonactive carbon granule be activated carbon grain be medium, wooden or coconut husk matter, nonactive carbon granule be shaped as ball, elliptical shape ball, corrugated, lamellar, cylindric or cellular；
When purifying filler and being quartz sand, the parameter of quartz sand is: bulk density is 0.5-5 ton/cubic meter, fusing point less than 2500 DEG C, and magnitude range is: 0.1-50mm；
When purifying filler and being adsorbent resin, the parameter of adsorbent resin is: aperture: 1-1000nm, specific surface area: 1-2000m2/ g, granularity 1-800 mesh, being shaped as of adsorbent resin is spherical.
Purifying electroplating solution system the most according to claim 1, it is characterised in that be mounted on a control valve on described water inlet pipe, described outlet pipe and described drain pipe.
Purifying electroplating solution system the most according to claim 1, it is characterised in that as when being shaped as cylindric of activated carbon grain, a diameter of 0.1-100mm of activated carbon grain, axial length is 1-100mm.
Purifying electroplating solution system the most according to claim 1, it is characterised in that as when being shaped as cylindric of nonactive carbon granule, a diameter of 0.1-100mm of nonactive carbon granule, axial length is 1-100mm.
Purifying electroplating solution system the most according to claim 1, it is characterised in that described filter membrane is polypropylene thermal spray fiber membrane, polypropylene superfine fiber film or nylon politef microporous filter membrane.
Purifying electroplating solution system the most according to claim 1, it is characterised in that described filter cloth is non-woven fabrics or the weaving cloth by the braiding of textile fabric yarn.
Purifying electroplating solution system the most according to claim 2, it is characterised in that the material of described circulating pump, described water inlet pipe, described outlet pipe, described drain pipe, described support, described aqueduct and described control valve is PP.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610377411.1A CN105884068A (en) | 2016-06-01 | 2016-06-01 | Electroplating solution purifying system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610377411.1A CN105884068A (en) | 2016-06-01 | 2016-06-01 | Electroplating solution purifying system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN105884068A true CN105884068A (en) | 2016-08-24 |
Family
ID=56709958
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610377411.1A Pending CN105884068A (en) | 2016-06-01 | 2016-06-01 | Electroplating solution purifying system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105884068A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106865644A (en) * | 2017-03-08 | 2017-06-20 | 王慈 | A kind of environment-protection electroplating filter |
| CN113274805A (en) * | 2020-02-20 | 2021-08-20 | 林士隆 | Filter module and etching solution regeneration method |
| CN113846371A (en) * | 2021-10-28 | 2021-12-28 | 株洲岱勒新材料有限责任公司 | Plating solution purification method for electroplated diamond wire saw |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN205222853U (en) * | 2015-12-16 | 2016-05-11 | 吴海潮 | Nickel rinsing purifying water process device |
| CN105601000A (en) * | 2015-11-18 | 2016-05-25 | 苏浩强 | Acidic electroplating waste liquid purifying system |
| EP3165269A1 (en) * | 2015-11-06 | 2017-05-10 | Ruscho-Schotenröhr GmbH | Water filter designed in the form of an outlet mouthpiece |
-
2016
- 2016-06-01 CN CN201610377411.1A patent/CN105884068A/en active Pending
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP3165269A1 (en) * | 2015-11-06 | 2017-05-10 | Ruscho-Schotenröhr GmbH | Water filter designed in the form of an outlet mouthpiece |
| CN105601000A (en) * | 2015-11-18 | 2016-05-25 | 苏浩强 | Acidic electroplating waste liquid purifying system |
| CN205222853U (en) * | 2015-12-16 | 2016-05-11 | 吴海潮 | Nickel rinsing purifying water process device |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106865644A (en) * | 2017-03-08 | 2017-06-20 | 王慈 | A kind of environment-protection electroplating filter |
| CN113274805A (en) * | 2020-02-20 | 2021-08-20 | 林士隆 | Filter module and etching solution regeneration method |
| CN113846371A (en) * | 2021-10-28 | 2021-12-28 | 株洲岱勒新材料有限责任公司 | Plating solution purification method for electroplated diamond wire saw |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN105884068A (en) | Electroplating solution purifying system | |
| CN204625245U (en) | A kind of device utilizing absorption method to remove Mercury in Wastewater | |
| KR101254015B1 (en) | Electrode for electrokinetic soil remediation and soil remediation system using the same | |
| CN205773698U (en) | Purifying electroplating solution system | |
| RU2297389C2 (en) | Method of the drinking water purification and the installation for its implementation | |
| KR101494302B1 (en) | Apparatus for removal of manganese ions in backwashing water for membrane filtration | |
| CN207827997U (en) | A kind of household Quick purifying device easy to operate | |
| CN105884081A (en) | Water purification/water softening integrated facility | |
| CN210480947U (en) | Emergent water purification is with granule active carbon filter core | |
| CN207877423U (en) | Mineral water multi-stage, efficient adsorption filtration system | |
| CN205653269U (en) | Integrative equipment of water purification soft water | |
| CN204607633U (en) | A kind of rearmounted filter cylinder of water treating equipment | |
| CN207827998U (en) | A kind of household water purifier with automatic water-supply function | |
| Luo et al. | Electro-enhanced adsorption of As (V) by activated carbon in three-dimensional electrode reactor | |
| KR101346312B1 (en) | Water purification system using the drop of gravity and method | |
| CN113173659A (en) | Self-cleaning long-life household water purifier | |
| CN204824252U (en) | Water filter unit | |
| CN206494872U (en) | Metal ion removing means in thick adipic acid | |
| CN206437954U (en) | Drinking water defluorination turbidity removal filter | |
| CN204111361U (en) | A kind of adsorption tower for purifying dirty acid | |
| CN205019793U (en) | Active carbon filter | |
| CN105126434B (en) | Filtering and defoaming combined treatment device for amine liquid | |
| CN208308559U (en) | A kind of purifier | |
| CN204508993U (en) | A kind of waste water containing thallium treatment unit | |
| CN214611647U (en) | Device capable of dynamically and circularly adsorbing heavy metal ion and organic dye mixed wastewater |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| WD01 | Invention patent application deemed withdrawn after publication | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20160824 |