CN204224354U - Electroplating waste processing equipment - Google Patents
Electroplating waste processing equipment Download PDFInfo
- Publication number
- CN204224354U CN204224354U CN201420624202.9U CN201420624202U CN204224354U CN 204224354 U CN204224354 U CN 204224354U CN 201420624202 U CN201420624202 U CN 201420624202U CN 204224354 U CN204224354 U CN 204224354U
- Authority
- CN
- China
- Prior art keywords
- electroplating
- storagetank
- electroplating wastewater
- chromium
- water
- 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.)
- Expired - Fee Related
Links
Landscapes
- Water Treatment By Electricity Or Magnetism (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
A kind of electroplating waste processing equipment, comprise electroplating wastewater storagetank, broken cyanide groove, except chromium groove, flocculation tank, settling bath, adsorption tank and reverse osmosis treatment device; Electroplating wastewater storagetank comprises the first storagetank, the second storagetank and the 3rd storagetank, first storagetank is communicated with broken cyanide groove, broken cyanide groove is communicated with the 3rd storagetank, second storagetank is communicated with except chromium groove, flocculation tank and the 3rd storagetank and be all communicated with except chromium groove, flocculation tank is communicated with settling bath, and adsorption tank is communicated with settling bath, and reverse osmosis treatment device is communicated with adsorption tank; Except chromium groove arranges the first adding set, the second adding set and the 3rd adding set, be respectively used to add sulfuric acid, S-WAT and alkaline matter.Above-mentioned electroplating waste processing equipment can improve the processing efficiency of electroplating wastewater, can reduce the input of electroplating wastewater process Chinese traditional medicine, reduce processing cost.
Description
Technical field
The utility model relates to electroplating wastewater processing field, particularly relates to a kind of electroplating waste processing equipment.
Background technology
At present, the waste water and waste liquids composition that electroplating wastewater is discharged primarily of electroplating facility (or workshop), e.g., plating piece rinse water, useless tank liquor, component cooling water and the flushing surface water etc.Because plating is more, technique is loaded down with trivial details, its water quality is complicated, composition is wayward, electroplating wastewater is mainly containing heavy metal ion and prussiates etc. such as chromium, cadmium, nickel, copper, zinc, gold and silver, these electroplating wastewaters belong to carcinogenic, teratogenesis, mutagenic highly toxic substance, all cause great harm to the living environment of the mankind and other biological.
Electroplating wastewater generally can be divided three classes: the first kind is electroplating wastewater of chromium, and the chromium ion concentration in this electroplating wastewater is higher; Equations of The Second Kind is cyanide-containing electroplating water, and the cyanide ion concentration in such electroplating wastewater is higher; 3rd class is general electroplating wastewater, and this electroplating wastewater is mainly containing contents of many kinds of heavy metal ion.
Existing electroplating effluent treatment method generally processes for a certain electroplating wastewater in above-mentioned three kinds, like this, just need to design different treatment processs and treatment unit for different types of electroplating wastewater, drastically increase processing cost, and processing efficiency is also lower.
Such as, Chinese patent 201110431946.X mono-kind contains electroplating wastewater processing and the heavy metal recovery Application way of heavy metal, disclose a kind of electroplating wastewater processing containing heavy metal and heavy metal recovery Application way, the lower concentration electroplating wastewater containing heavy metal ion is the steps include: to pass through ion exchange resin, heavy metal ion contained in electroplating wastewater is made to be adsorbed in ion exchange resin completely and to isolate clean water, until the absorption of ion exchange resin reaches capacity, add the electroplating wastewater that heavy metal ion that elutriant makes to be adsorbed in ion exchange resin departs from ion exchange resin and output high density, then add reductive agent to high-concentration electroplating wastewater and carry out reduction reaction, obtain the water-fast reduzate containing heavy metal ion, add flocculation agent and accelerate reduzate coagulation, finally by filtration or the method such as centrifugal, throw out is separated, and reclaim heavy metal substance as useful industrial raw material by high-temperature calcination.Technique of the present invention has that cost is low, efficiency is high and the advantage such as highly versatile, effectively reduces secondary pollution, is adapted at plating, electron trade widespread use.
Such as, Chinese patent 201110080981.1 is containing chromium ion waste water treatment process and equipment thereof, disclose and the invention discloses a kind of containing chromium ion waste water treatment process and equipment, comprise cartridge filter, be loaded with the ion-exchanger of H type strong-acid cation-exchange resin, be mounted with ion-exchanger except chromium anionite-exchange resin; Waste water is after pre-filtering, and by H type strong-acid cation-exchange resin, the positively charged ion in waste water is by the strong-acid cation-exchange resin enrichment of H type and displace hydrogen ion and make waste water be acid, and the hexavalent chromium in waste water is converted into Cr in acid waste water
2o
7 2-, then waste water enters except chromium anionite-exchange resin, Cr
2o
7 2-removed the enrichment of chromium anionite-exchange resin.This technique only can carry out resin absorption enrichment then wash-out removing to the various ions in waste water, namely whole technological process can reduce the salinity of waste water, and can not increase, therefore the comparatively pure reusable edible of water quality obtained after process is in Electroplating Production, even if directly discharge also can not have any impact to environment.
But above-mentioned disclosed patent still cannot provide a kind for the treatment of process and the treatment unit that can process above-mentioned three kinds of electroplating wastewaters simultaneously.
Summary of the invention
Based on this, be necessary a kind of low cost, high-level efficiency to be provided, the electroplating waste processing equipment discharged in all kinds of electroplating facility can be met simultaneously.
A kind of electroplating waste processing equipment, comprise electroplating wastewater storagetank, broken cyanide groove, except chromium groove, flocculation tank, settling bath, adsorption tank and reverse osmosis treatment device;
Described electroplating wastewater storagetank comprises the first storagetank, the second storagetank and the 3rd storagetank, described first storagetank is communicated with described broken cyanide groove, described broken cyanide groove is communicated with described 3rd storagetank, described second storagetank is communicated with the described chromium groove that removes, described flocculation tank is all communicated with described 3rd storagetank and the described chromium groove that removes, described flocculation tank is communicated with described settling bath, and described adsorption tank is communicated with described settling bath, and described reverse osmosis treatment device is communicated with described adsorption tank;
The described chromium groove that removes arranges the first adding set, the second adding set and the 3rd adding set, is respectively used to add sulfuric acid, S-WAT and alkaline matter.
Wherein in an embodiment, described broken cyanide groove is provided with the first dosing mouth.
Wherein in an embodiment, the described chromium groove that removes is provided with the second dosing mouth.
Wherein in an embodiment, described flocculation tank is provided with the 3rd dosing mouth.
Wherein in an embodiment, electroplating wastewater storagetank is formed in one structure.
Wherein in an embodiment, the bottom sidewall of described settling bath is ramp structure.
Wherein in an embodiment, described broken cyanide groove is provided with the first whipping appts.
Wherein in an embodiment, the described chromium groove that removes is provided with the second whipping appts.
Wherein in an embodiment, described flocculation tank is provided with the 3rd whipping appts.
Above-mentioned electro-plating waste disposal plant, carries out different treatment processs according to different types of electroplating wastewater, can improve electroplating wastewater processing efficiency and, single equipment can meet the process of the different electroplating sewerages of different electroplating sewerage factory, saves equipment cost; Electroplating wastewater in broken cyanide process is recycled simultaneously, the input of electroplating wastewater process Chinese traditional medicine can be reduced, decrease the wasting of resources, reduce processing cost.
Accompanying drawing explanation
Fig. 1 is the schema of the electroplating effluent treatment method of an embodiment;
Fig. 2 is the structural representation of the electroplating waste processing equipment of an embodiment.
Embodiment
For enabling above-mentioned purpose of the present utility model, feature and advantage become apparent more, are described in detail embodiment of the present utility model below in conjunction with accompanying drawing.Set forth a lot of detail in the following description so that fully understand the utility model.But the utility model can be much different from alternate manner described here to implement, those skilled in the art can when doing similar improvement without prejudice to when the utility model intension, and therefore the utility model is by the restriction of following public concrete enforcement.
As shown in Figure 1, the electroplating effluent treatment method of an embodiment comprises the steps:
S110: collect general electroplating wastewater, cyanide-containing electroplating water and electroplating wastewater of chromium.
Common, electroplating wastewater is due to the difference of plating, and in the electroplating wastewater of generation, composition is also different.Such as, in the electroplating wastewater produced in the technique of plating cyanogen, the concentration of prussiate can be higher, in the electroplating wastewater produced in the technique of electrodeposited chromium, the concentration of chromium is general higher, and electroplates in the electroplating wastewater produced in other heavy metals, and the concentration of heavy metal is general also larger.For different electroplating technologies, by the electroplating wastewater categorised collection produced, as the electroplating wastewater containing cyanogen, containing electroplating wastewater and the general electroplating wastewater of chromium, like this, the consumption of electroplating wastewater processing Chinese traditional medicine can be reduced, reduce processing cost, also improve processing efficiency simultaneously.
S120: general electroplating wastewater is carried out flocculation treatment, precipitation process respectively, after solid-liquid separation, is undertaken adsorbing and reverse-osmosis treated by supernatant liquid;
General electroplating wastewater is carried out flocculation treatment, such as, add alkaline matter in general electroplating wastewater after, as sodium hydroxide and calcium hydroxide etc., regulate pH to 7.5 ~ 8, adding polymerize aluminum chloride (PAC) is flocculation agent, and dosage is 1 ‰ ~ 5 ‰ (thousandths) of pending general electroplating wastewater volume, adding polyacrylamide (PAM) is coagulant aids, and its dosage is 0.1 ‰ of pending general electroplating wastewater volume.After flocculation, general electroplating wastewater is carried out deposition and leave standstill, heavy metal ion is precipitated completely with the form of oxyhydroxide.Such as, the general electroplating wastewater after flocculation is passed into sedimentation tank, and heavy metal ion, under the effect of alkali, is deposited into the bottom of settling bath with the form of oxyhydroxide.In order to make heavy metal precipitate completely, and avoid carrying it into subsequent technique process, such as, time of repose is 1h ~ 2h, like this, heavy metal can be made to deposit completely, solid-liquid is separated completely.
Supernatant liquid after precipitation process is adsorbed, such as, the filler with physical adsorption and ion-exchange is flowed through through supernatant liquid, as gac, hydroxylapatite and tired drag two or three of stone (Rectorite) to be composited, and filling surface cultivation has microorganism, after organism in supernatant liquid and heavy metal ion are adsorbed by matrix material, organism is by the microbiological deterioration of composite material surface thus destruction adsorption equilibrium makes absorption proceed, heavy metal is entered the inside of matrix material after adsorbing in the mode of diffusion, and carry out ion-exchange with matrix material thus destroy adsorption equilibrium physical adsorption is proceeded.
Supernatant liquid after absorption is carried out reverse-osmosis treated further, and the impurity in supernatant liquid is then retained by reverse osmosis membrane as soluble solids, organism, colloidalmaterial and bacterium etc., obtains water purification.
Life standard for drinking is reached in order to make the water purification obtained, such as, pretreated water is adopted two-pass reverse osmosis process, pretreated water enters first-stage reverse osmosis treatment unit through high-pressure pump, obtain one-level pure water, one-level pure water is further across two-pass reverse osmosis treatment unit, and further desalination, obtains secondary pure water.The electrodeionization water purification conductance obtained thus reaches 10 μ s/cm, is better than Ministry of Health's bottled water standard for drinking.
By the lower floor's bed mud drying and crushing after solid-liquid separation, such as, be transported to refuse landfill and carry out landfill disposal, and for example, lower floor's bed mud, after sterilization, is directly used as agriculture bed mud, like this, and can emissions reduction.
S130: the pH of cyanide-containing electroplating water is adjusted to 10.5 ~ 11, and carry out broken cyanide process, obtain pre-treatment cyanide-containing electroplating water, pre-treatment cyanide-containing electroplating water is passed into general electroplating wastewater, obtains integrative electroplating waste.
By adding clorox in cyanide-containing electroplating water, the oxygenizement of reactive chlorine in hypochlorite, under certain pH, cyanide oxidation can be made to become cyanate, cyanate is oxidized to nontoxic carbonic acid gas and nitrogen then further, like this, the prussiate in electroplating wastewater can be removed.
Sodium hydroxide is added in cyanide-containing electroplating water, after regulating pH to 10.5 ~ 11 of cyanide-containing electroplating water, clorox is added in cyanide-containing electroplating water, control the dosage of clorox, the dispensing mass ratio of clorox and hydrogen radical ion is made to be greater than 3.5, after stirring 15min ~ 30min, sulfuric acid is added in above-mentioned cyanide-containing electroplating water, after regulating pH to 7.5 ~ 8.5, clorox is added in above-mentioned cyanide-containing electroplating water, make the dispensing mass ratio of clorox and hydrogen radical ion be 10-15, stir 15min ~ 30min, obtain pre-treatment cyanide-containing electroplating water.
Pre-treatment cyanide-containing electroplating water is passed into general electroplating wastewater, because pre-treatment cyanide-containing electroplating water is after treatment in alkalescence, be passed in general electroplating wastewater, the acidity in general electroplating wastewater can be neutralized, like this, the consumption of alkali can be reduced, reduce the cost.
S140: by integrative electroplating waste by step S120 process.
Integrative electroplating waste is carried out flocculation treatment, such as, add alkaline matter in integrative electroplating waste after, adding polymerize aluminum chloride (PAC) is flocculation agent, dosage is 1 ‰ ~ 5 ‰ of pending integrative electroplating waste volume, adding polyacrylamide (PAM) is coagulant aids, and its dosage is 0.1 ‰ of pending integrative electroplating waste volume.After flocculation, integrative electroplating waste is carried out deposition and leave standstill, heavy metal ion is precipitated completely with the form of oxyhydroxide.Such as, the integrative electroplating waste after flocculation is passed into sedimentation tank, and heavy metal ion, under the effect of alkali, is deposited into the bottom of settling bath with the form of oxyhydroxide.In order to make heavy metal precipitate completely, and avoid carrying it into subsequent technique process, such as, time of repose is 1h ~ 2h, like this, heavy metal can be made to deposit completely, solid-liquid is separated completely.
Supernatant liquid after precipitation process is adsorbed, such as, the filler with physical adsorption and ion-exchange is flowed through through supernatant liquid, as gac, hydroxylapatite and tired drag two or three of stone (Rectorite) to be composited, and filling surface cultivation has microorganism, after organism in supernatant liquid and heavy metal ion are adsorbed by matrix material, organism is by the microbiological deterioration of composite material surface thus destruction adsorption equilibrium makes absorption proceed, heavy metal is entered the inside of matrix material after adsorbing in the mode of diffusion, and carry out ion-exchange with matrix material thus destroy adsorption equilibrium physical adsorption is proceeded.
Supernatant liquid after absorption is carried out reverse-osmosis treated further, and the impurity in supernatant liquid is then retained by reverse osmosis membrane as soluble solids, organism, colloidalmaterial and bacterium etc., obtains water purification.
Life standard for drinking is reached in order to make the water purification obtained, such as, pretreated water is adopted two-pass reverse osmosis process, pretreated water enters first-stage reverse osmosis treatment unit through high-pressure pump, obtain one-level pure water, one-level pure water is further across two-pass reverse osmosis treatment unit, and further desalination, obtains secondary pure water.The electrodeionization water purification conductance obtained thus reaches 10 μ s/cm, is better than Ministry of Health's bottled water standard for drinking.
S150: enter sulfuric acid, S-WAT and alkaline matter successively in electroplating wastewater of chromium, carries out, except chromium process, obtaining pre-treatment electroplating wastewater of chromium.
Such as, in electroplating wastewater of chromium, add concentration is 0.05-5% sulfuric acid, after regulating pH to 2.5 ~ 3.0, then add S-WAT toward it, make the ORP value of electroplating wastewater of chromium for 250mV, after abundant stirring, after making the hexavalent chrome reduction in electroplating wastewater of chromium become trivalent chromium, add sodium hydroxide solution or aqua calcis adjustment pH to 7.5 ~ 8.0 toward it, make trivalent chromium change chromium hydroxide precipitation into, like this, the effect except chromium can be reached.
S160: by electroplating wastewater of chromium by step S120 process.
Electroplating wastewater of chromium is carried out flocculation treatment, such as, add alkaline matter in electroplating wastewater of chromium after, adding polymerize aluminum chloride (PAC) is flocculation agent, dosage is 1 ‰ ~ 5 ‰ of pending electroplating wastewater of chromium volume, adding polyacrylamide (PAM) is coagulant aids, and its dosage is 0.1 ‰ of pending electroplating wastewater of chromium volume.After flocculation, electroplating wastewater of chromium is carried out deposition and leave standstill, heavy metal ion is precipitated completely with the form of oxyhydroxide.Such as, the electroplating wastewater of chromium after flocculation is passed into sedimentation tank, and heavy metal ion, under the effect of alkali, is deposited into the bottom of settling bath with the form of oxyhydroxide.In order to make heavy metal precipitate completely, and avoid carrying it into subsequent technique process, such as, time of repose is 1h ~ 2h, like this, heavy metal can be made to deposit completely, solid-liquid is separated completely.
Supernatant liquid after precipitation process is adsorbed, such as, the filler with physical adsorption and ion-exchange is flowed through through supernatant liquid, as gac, hydroxylapatite and tired drag two or three of stone (Rectorite) to be composited, and filling surface cultivation has microorganism, after organism in supernatant liquid and heavy metal ion are adsorbed by matrix material, organism is by the microbiological deterioration of composite material surface thus destruction adsorption equilibrium makes absorption proceed, heavy metal is entered the inside of matrix material after adsorbing in the mode of diffusion, and carry out ion-exchange with matrix material thus destroy adsorption equilibrium physical adsorption is proceeded.
Supernatant liquid after absorption is carried out reverse-osmosis treated further, and the impurity in supernatant liquid is then retained by reverse osmosis membrane as soluble solids, organism, colloidalmaterial and bacterium etc., obtains water purification.
Life standard for drinking is reached in order to make the water purification obtained, such as, pretreated water is adopted two-pass reverse osmosis process, pretreated water enters first-stage reverse osmosis treatment unit through high-pressure pump, obtain one-level pure water, one-level pure water is further across two-pass reverse osmosis treatment unit, and further desalination, obtains secondary pure water.The electrodeionization water purification conductance obtained thus reaches 10 μ s/cm, is better than Ministry of Health's bottled water standard for drinking.
It should be noted that, step S130 and S150 can process simultaneously, or S150 also can carry out before S130.The comprehensive wastewater obtained through S130 and step S120 process again after the pre-treatment chromate waste water of S150 can mix.
The treatment process of above-mentioned electroplating wastewater, different treatment processs is carried out according to different types of electroplating wastewater, the processing efficiency of electroplating wastewater can be improved, electroplating wastewater in broken cyanide process is recycled simultaneously, the input of electroplating wastewater process Chinese traditional medicine can be reduced, decrease the wasting of resources, reduce processing cost.
In order to introduce electroplating effluent treatment method of the present utility model further, such as, a kind of electroplating waste processing equipment is also provided.
As shown in Figure 2, it is the structural representation of the electroplating waste processing equipment 10 of an embodiment.
Refer to Fig. 2, electroplating waste processing equipment 10, comprise electroplating wastewater storagetank 100, broken cyanide groove 200, except chromium groove 300, flocculation tank 400, settling bath 500, adsorption tank 600 and reverse osmosis treatment device 700.
Refer to Fig. 2, electroplating wastewater storagetank 100 comprises the first storagetank 110, second storagetank 120 and the 3rd storagetank 130.
Due to the difference of electroplating technology, the composition of the electroplating wastewater of generation is also different.By the kind of electroplating technology, electroplating wastewater can be divided into general electroplating wastewater, cyanide-containing electroplating water, electroplating wastewater of chromium collect.First storagetank 110, second storagetank 120 and the 3rd storagetank 130 can be used to store these three kinds different electroplating wastewaters.Such as, cyanide-containing electroplating water is imported the first storagetank 110, electroplating wastewater of chromium is imported the second storagetank 120, general electroplating wastewater is imported the 3rd storagetank 130.
In order to save space, such as, electroplating wastewater storagetank 100 is formed in one structure, like this, can save the space of electroplating wastewater storage 100, also be convenient to the management of equipment simultaneously.
Refer to Fig. 2, the first storagetank 110 is communicated with broken cyanide groove 200, and the cyanide-containing electroplating water in the first storagetank 100 can carry out broken cyanide process by broken cyanide groove 200.
Such as, by adding clorox in broken cyanide groove 200, the oxygenizement of reactive chlorine in hypochlorite, under certain pH, cyanide oxidation can be made to become cyanate, cyanate is oxidized to nontoxic carbonic acid gas and nitrogen then further, like this, the prussiate in electroplating wastewater can be removed.
And for example, sodium hydroxide is added in cyanide-containing electroplating water, after regulating pH to 10.5 ~ 11 of cyanide-containing electroplating water, clorox is added in cyanide-containing electroplating water, control the dosage of clorox, the dispensing mass ratio of clorox and hydrogen radical ion is made to be greater than 3.5, after stirring 15min ~ 30min, sulfuric acid is added in above-mentioned cyanide-containing electroplating water, after regulating pH to 7.5 ~ 8.5, clorox is added in above-mentioned cyanide-containing electroplating water, the dispensing mass ratio of clorox and hydrogen radical ion is made to be 10-15, stir 15min ~ 30min, prussiate is made to be converted into carbonic acid gas and nitrogen completely.
Because needs drop into a certain amount of medicine in broken cyanide groove 200, as sodium hydroxide, clorox and sulfuric acid etc., be provided with the first charging opening 210 in broken cyanide groove 200, adding of medicine can be facilitated like this.
In order to improve the speed of reaction of prussiate and hypochlorite, such as, in broken cyanide groove 200, being provided with the first whipping appts 220, accelerating the speed of reaction of prussiate, improve processing efficiency.
Refer to Fig. 2, broken cyanide groove 200 is communicated with the 3rd storagetank 130, and the pre-treatment cyanide-containing electroplating water after broken cyanide is recycled to the 3rd storagetank 130 through pipeline.Because pre-treatment cyanide-containing electroplating water is after treatment in alkalescence, is passed in general electroplating wastewater, the acidity in general electroplating wastewater can be neutralized, like this, the consumption of alkali can be reduced, reduce the cost.
Refer to Fig. 2, except chromium groove 300 is communicated with the second storagetank 120.The electroplating wastewater of chromium being stored in the second storagetank 120 passes into except in chromium groove 300, toward being 0.05 ~ 5% sulfuric acid except adding concentration in chromium groove 300, after regulating pH to 2.5 ~ 3.0, S-WAT is added again toward it, make the ORP value of electroplating wastewater of chromium for 250mV, after abundant stirring, after making the hexavalent chrome reduction in electroplating wastewater of chromium become trivalent chromium, sodium hydroxide solution or aqua calcis adjustment pH to 7.5 ~ 8.0 are added toward it, trivalent chromium is made to change chromium hydroxide precipitation into, like this, the effect except chromium can be reached.
Because needs drop into a certain amount of medicine toward in chromium groove 300, as sulfuric acid, S-WAT and sodium hydroxide etc., except being provided with the second charging opening 310 in chromium groove 300, adding of medicine can be facilitated like this.
Such as, in order to improve the speed of reaction except chromium groove 300, except being provided with the second whipping appts 320 in chromium groove 300, accelerating the speed of reaction of hexavalent chrome reduction, improving processing efficiency.
Such as, the described chromium groove that removes arranges the first adding set, the second adding set and the 3rd adding set, is respectively used to add sulfuric acid, S-WAT and alkaline matter.
Refer to Fig. 2, flocculation tank 400 is all communicated with the 3rd storagetank 130 and the described chromium groove 300 that removes.By be stored in 130 general electroplating wastewater and through the reacted pre-treatment cyanide wastewater of broken cyanide, and pass into flocculation tank 400 through the pre-treatment chromate waste water except chromium groove 300, after regulating pH to 7.5 ~ 8.0 after add alkaline matter in flocculation tank, adding polymerize aluminum chloride (PAC) is flocculation agent, dosage is 1 ‰ ~ 5 ‰ of pending electroplating wastewater of chromium volume, adding polyacrylamide (PAM) is coagulant aids, and its dosage is 0.1 ‰ of pending electroplating wastewater of chromium volume.After flocculation, leave standstill carrying out deposition containing the electroplating wastewater in flocculation tank 400, heavy metal ion is precipitated completely with the form of oxyhydroxide.Such as, the electroplating wastewater of chromium after flocculation is passed into sedimentation tank, and heavy metal ion, under the effect of alkali, is deposited into the bottom of settling bath with the form of oxyhydroxide.In order to make heavy metal precipitate completely, and avoid carrying it into subsequent technique process, such as, time of repose is 1h ~ 2h, like this, heavy metal can be made to deposit completely, solid-liquid is separated completely.
Because needs drop into a certain amount of medicine in flocculation tank 400, as sodium hydroxide, PAC and PAM etc., be provided with the 3rd charging opening 410 in flocculation tank 400, adding of medicine can be facilitated like this.
In order to improve the flocculation rate of flocculation tank 400, such as, being provided with the 3rd whipping appts 420 in flocculation tank 400, electroplating wastewater is fully mixed with flocculation agent etc., improve processing efficiency.
Refer to Fig. 2, settling bath 500 is communicated with flocculation tank 400, and the electroplating wastewater through flocculation tank 400 passes into settling bath 500, makes the depositions settle of generation to the bottom of settling bath 500.
In order to prevent heavy metal precipitation to be mixed into subsequent processes, such as, the bottom sidewall of settling bath 500 is ramp structure, that is, the radius bottom settling bath 500 is less than the radius on its top, like this, heavy metal precipitation thing can be made to be not easy to enter subsequent processes.
In order to process the bed mud of settling bath 500 bottom deposit better, to reduce the quantity discharged to outside, such as, electroplating waste processing equipment 10 also arranges bed mud receiving tank and bed mud drying and crushing machine, settling bath is communicated with bed mud receiving tank, and bed mud drying and crushing machine is communicated with bed mud receiving tank, like this, bed mud can be avoided directly to be disposed to outside, reach the effect of energy-saving and emission-reduction, such as, the dry direct landfill disposal of bed mud, and for example, dry bed mud is directly used as agriculture bed mud.And for example, described bed mud receiving tank is communicated with the bottom of described settling bath, for the bed mud of collecting precipitation trench bottom deposition.And for example, be provided with stirring mechanism in described bed mud receiving tank, lump to prevent bed mud.And for example, be communicated with by slush pump between described bed mud receiving tank and described bed mud drying and crushing machine.
Refer to Fig. 2, adsorption tank 600 is communicated with settling bath 500, and the supernatant liquid processed through settling bath 500 passes into adsorption tank 600.Filler is filled with in adsorption tank 600, such as, there is the filler of physical adsorption and ion-exchange, as, gac, hydroxylapatite and tired two or three filler be composited dragging stone (Rectorite), and filling surface cultivation has microorganism, after organism in supernatant liquid and heavy metal ion are adsorbed by matrix material, organism is by the microbiological deterioration of composite material surface thus destruction adsorption equilibrium makes absorption proceed, heavy metal is entered the inside of matrix material after adsorbing in the mode of diffusion, and carry out ion-exchange with matrix material thus destroy adsorption equilibrium physical adsorption is proceeded.
Refer to Fig. 2, reverse osmosis unit 700 is communicated with adsorption tank 600, supernatant liquid after absorption is carried out reverse-osmosis treated further, and the impurity in supernatant liquid is then retained by reverse osmosis membrane as soluble solids, organism, colloidalmaterial and bacterium etc., obtains water purification.
Life standard for drinking is reached in order to make the water purification obtained, such as, pretreated water is adopted two-pass reverse osmosis process, pretreated water enters first-stage reverse osmosis treatment unit through high-pressure pump, obtain one-level pure water, one-level pure water is further across two-pass reverse osmosis treatment unit, and further desalination, obtains secondary pure water.The electrodeionization water purification conductance obtained thus reaches 10 μ s/cm, is better than Ministry of Health's bottled water standard for drinking.
Above-mentioned electro-plating waste disposal plant, carries out different treatment processs according to different types of electroplating wastewater, can improve electroplating wastewater processing efficiency and, single equipment can meet the process of the different electroplating sewerages of different electroplating sewerage factory, saves equipment cost; Electroplating wastewater in broken cyanide process is recycled simultaneously, the input of electroplating wastewater process Chinese traditional medicine can be reduced, decrease the wasting of resources, reduce processing cost.
Be specific embodiment part below.
Embodiment 1:
The process of certain electroplating facility electroplating wastewater, day quantity discharged be 2000 tons.Wherein, the water quality situation of the electroplating wastewater of this electroplating facility is as table 1.
Table 1
| CN - | Cr 6+ | Cu 2+ | Ni 2+ | Zn 2+ | COD | pH | |
| General electroplating wastewater | Do not detect | 0.32mg/L | 58.2mg/L | 62.4mg/L | 159mg/L | 364mg/L | 3.5 |
| Cyanide-containing electroplating water | 82mg/L | Do not detect | 422mg/L | 6.16mg/L | 42.6mg/L | Do not detect | 8.8 |
| Electroplating wastewater of chromium | Do not detect | 156mg/L | 12.6mg/L | 20.4mg/L | 21.5mg/L | Do not detect | 2.9 |
Now as follows the electroplating wastewater of this electroplating facility is processed:
Collect general electroplating wastewater, cyanide-containing electroplating water and electroplating wastewater of chromium.
By the difference of electroplating technology, general electroplating wastewater, cyanide-containing electroplating water, electroplating wastewater of chromium is divided into by electroplating wastewater to collect.
General electroplating wastewater is carried out flocculation treatment, precipitation process respectively, after solid-liquid separation, supernatant liquid is adsorbed, reverse-osmosis treated.
Sodium hydroxide solution is added in general flocculation tank, its pH is regulated to be 7.5, add polymerize aluminum chloride (PAC), input amount is treat general electroplating wastewater volume 1 ‰, adds polyacrylamide (PAM), its dosage is 0.1 ‰ of pending general electroplating wastewater volume, after abundant stirring, after leaving standstill 1h ~ 2h, passed into sedimentation tank, the precipitation of generation is made to be deposited into bottom settling bath, by its solid-liquid separation.The supernatant liquid of generation is passed into adsorption tank, and adsorption tank filler is the granular composite material that gac and hydroxyl phosphorus lime are made.By the supernatant liquid after absorption further across two-pass reverse osmosis process.
Cyanide-containing electroplating water is carried out broken cyanide process, obtains pre-treatment cyanide-containing electroplating water, pre-treatment cyanide-containing electroplating water is passed into general electroplating wastewater, obtains integrative electroplating waste.
Sodium hydroxide is added in cyanide-containing electroplating water, after regulating the pH to 10.5 of cyanide-containing electroplating water, clorox is added in cyanide-containing electroplating water, control the dosage of clorox, the dispensing mass ratio of clorox and hydrogen radical ion is made to be 4, after stirring 15min ~ 30min, sulphuric acid soln is added in above-mentioned cyanide-containing electroplating water, after regulating pH to 8.0, clorox is added in above-mentioned cyanide-containing electroplating water, make the dispensing mass ratio of clorox and hydrogen radical ion be 12, stir 15min ~ 30min, obtain pre-treatment cyanide-containing electroplating water.Pre-treatment cyanide wastewater is recycled in general electroplating wastewater, obtains integrative electroplating waste.
Integrative electroplating waste is carried out flocculation treatment, precipitation process successively, after solid-liquid separation, supernatant liquid is adsorbed, reverse-osmosis treated.
Electroplating wastewater of chromium is carried out, except chromium process, obtain pre-treatment electroplating wastewater of chromium.
In electroplating wastewater of chromium, add concentration is 0.05-5% sulfuric acid, after regulating pH to 2.5, S-WAT is added again toward it, make the ORP value of electroplating wastewater of chromium for 250mV, after abundant stirring, add sodium hydroxide solution or aqua calcis adjustment pH to 8.0 toward it, obtain pre-treatment electroplating wastewater of chromium.
Electroplating wastewater of chromium is carried out flocculation treatment, precipitation process successively, after solid-liquid separation, supernatant liquid is adsorbed, reverse-osmosis treated process.
After above-mentioned treatment step, the clear water obtained after testing after, water quality the results are shown in Table 2.
Table 2
| CN - | Cr 6+ | Cu 2+ | Ni 2+ | Zn 2+ | COD | pH | |
| Clear water | Do not detect | 0.01mg/L | 0.28mg/L | 0.02mg/L | 0.01mg/L | 12 | 7.2 |
Embodiment 2:
The process of certain electroplating facility electroplating wastewater, day quantity discharged be 2000 tons.Wherein, the water quality situation of the electroplating wastewater of this electroplating facility is as table 1.
Table 3
| CN - | Cr 6+ | Cu 2+ | Ni 2+ | Zn 2+ | COD | pH | |
| General electroplating wastewater | Do not detect | 0.48mg/L | 62.2mg/L | 62.8mg/L | 142mg/L | 355mg/L | 3.2 |
| Cyanide-containing electroplating water | 95mg/L | Do not detect | 452mg/L | 6.3mg/L | 41.6mg/L | Do not detect | 8.5 |
| Electroplating wastewater of chromium | Do not detect | 206mg/L | 12.8mg/L | 25.4mg/L | 21.8mg/L | Do not detect | 2.6 |
Now as follows the electroplating wastewater of this electroplating facility is processed:
Collect general electroplating wastewater, cyanide-containing electroplating water and electroplating wastewater of chromium.
By the difference of electroplating technology, general electroplating wastewater, cyanide-containing electroplating water, electroplating wastewater of chromium is divided into by electroplating wastewater to collect.
General electroplating wastewater is carried out flocculation treatment, precipitation process respectively, after solid-liquid separation, supernatant liquid is adsorbed, reverse-osmosis treated.
Sodium hydroxide solution is added in general electroplating wastewater, its pH is regulated to be 7.5, add polymerize aluminum chloride (PAC), input amount is treat general electroplating wastewater volume 1 ‰, adds polyacrylamide (PAM), its dosage is 0.1 ‰ of pending general electroplating wastewater volume, after abundant stirring, after leaving standstill 1h ~ 2h, passed into sedimentation tank, the precipitation of generation is made to be deposited into bottom settling bath, by its solid-liquid separation.The supernatant liquid of generation is passed into adsorption tank, and adsorption tank filler is the granular composite material that gac and hydroxyl phosphorus lime are made.By the supernatant liquid after absorption further across two-pass reverse osmosis process.
Cyanide-containing electroplating water is carried out broken cyanide process, obtains pre-treatment cyanide-containing electroplating water, pre-treatment cyanide-containing electroplating water is passed into general electroplating wastewater, obtains integrative electroplating waste.
Sodium hydroxide is added in cyanide-containing electroplating water, after regulating the pH to 11 of cyanide-containing electroplating water, clorox is added in cyanide-containing electroplating water, control the dosage of clorox, the dispensing mass ratio of clorox and hydrogen radical ion is made to be 4, after stirring 20min, sulphuric acid soln is added in above-mentioned cyanide-containing electroplating water, after regulating pH to 8.0, clorox is added in above-mentioned cyanide-containing electroplating water, make the dispensing mass ratio of clorox and hydrogen radical ion be 13, stir 30min, obtain pre-treatment cyanide-containing electroplating water.Pre-treatment cyanide wastewater is recycled in general electroplating wastewater, obtains integrative electroplating waste.
Integrative electroplating waste is carried out flocculation treatment, precipitation process successively, after solid-liquid separation, supernatant liquid is adsorbed, reverse-osmosis treated.
Electroplating wastewater of chromium is carried out, except chromium process, obtain pre-treatment electroplating wastewater of chromium.
In electroplating wastewater of chromium, add concentration is 0.05-5% sulfuric acid, after regulating pH to 2.5, S-WAT is added again toward it, make the ORP value of electroplating wastewater of chromium for 250mV, after abundant stirring, add sodium hydroxide solution or aqua calcis adjustment pH to 8.0 toward it, obtain pre-treatment electroplating wastewater of chromium.
Electroplating wastewater of chromium is carried out flocculation treatment, precipitation process successively, after solid-liquid separation, supernatant liquid is adsorbed, reverse-osmosis treated process.
After above-mentioned treatment step, the clear water obtained after testing after, water quality the results are shown in Table 4.
Table 4
| CN - | Cr 6+ | Cu 2+ | Ni 2+ | Zn 2+ | COD | pH | |
| Clear water | 0.03mg/L | 0.02mg/L | 0.3mg/L | 0.01mg/L | 0.3mg/L | 15 | 6.8 |
Embodiment 3:
The process of certain electroplating facility electroplating wastewater, day quantity discharged be 2000 tons.Wherein, the water quality situation of the electroplating wastewater of this electroplating facility is as table 5.
Table 5
| CN - | Cr 6+ | Cu 2+ | Ni 2+ | Zn 2+ | COD | pH | |
| General electroplating wastewater | Do not detect | 0.68mg/L | 62.2mg/L | 62.4mg/L | 146mg/L | 410mg/L | 3.2 |
| Cyanide-containing electroplating water | 88mg/L | Do not detect | 412mg/L | 6.9mg/L | 43.6mg/L | Do not detect | 8.2 |
| Electroplating wastewater of chromium | Do not detect | 206mg/L | 12.8mg/L | 25.4mg/L | 21.8mg/L | Do not detect | 2.6 |
Now as follows the electroplating wastewater of this electroplating facility is processed:
Collect general electroplating wastewater, cyanide-containing electroplating water and electroplating wastewater of chromium.
By the difference of electroplating technology, general electroplating wastewater, cyanide-containing electroplating water, electroplating wastewater of chromium is divided into by electroplating wastewater to collect.
General electroplating wastewater is carried out flocculation treatment, precipitation process respectively, after solid-liquid separation, supernatant liquid is adsorbed, reverse-osmosis treated.
Sodium hydroxide solution is added in general electroplating wastewater, its pH is regulated to be 7.8, add polymerize aluminum chloride (PAC), input amount is treat general electroplating wastewater volume 1 ‰, adds polyacrylamide (PAM), its dosage is 0.1 ‰ of pending general electroplating wastewater volume, after abundant stirring, after leaving standstill 1h ~ 2h, passed into sedimentation tank, the precipitation of generation is made to be deposited into bottom settling bath, by its solid-liquid separation.The supernatant liquid of generation is passed into adsorption tank, and adsorption tank filler is the granular composite material that gac and hydroxyl phosphorus lime are made.By the supernatant liquid after absorption further across two-pass reverse osmosis process.
Cyanide-containing electroplating water is carried out broken cyanide process, obtains pre-treatment cyanide-containing electroplating water, pre-treatment cyanide-containing electroplating water is passed into general electroplating wastewater, obtains integrative electroplating waste.
Sodium hydroxide is added in cyanide-containing electroplating water, after regulating the pH to 11 of cyanide-containing electroplating water, clorox is added in cyanide-containing electroplating water, control the dosage of clorox, the dispensing mass ratio of clorox and hydrogen radical ion is made to be 4, after stirring 15min ~ 30min, sulphuric acid soln is added in above-mentioned cyanide-containing electroplating water, after regulating pH to 8.0, clorox is added in above-mentioned cyanide-containing electroplating water, make the dispensing mass ratio of clorox and hydrogen radical ion be 12, stir 15min ~ 30min, obtain pre-treatment cyanide-containing electroplating water.Pre-treatment cyanide wastewater is recycled in general electroplating wastewater, obtains integrative electroplating waste.
Integrative electroplating waste is carried out flocculation treatment, precipitation process successively, after solid-liquid separation, supernatant liquid is adsorbed, reverse-osmosis treated.
Electroplating wastewater of chromium is carried out, except chromium process, obtain pre-treatment electroplating wastewater of chromium.
In electroplating wastewater of chromium, add concentration is 0.05-5% sulfuric acid, after regulating pH to 2.5, S-WAT is added again toward it, make the ORP value of electroplating wastewater of chromium for 250mV, after abundant stirring, add sodium hydroxide solution or aqua calcis adjustment pH to 8.0 toward it, obtain pre-treatment electroplating wastewater of chromium.
Electroplating wastewater of chromium is carried out flocculation treatment, precipitation process successively, after solid-liquid separation, supernatant liquid is adsorbed, reverse-osmosis treated process.
After above-mentioned treatment step, the clear water obtained after testing after, water quality the results are shown in Table 6.
Table 6
| CN - | Cr 6+ | Cu 2+ | Ni 2+ | Zn 2+ | COD | pH | |
| Clear water | 0.02mg/L | 0.02mg/L | 0.2mg/L | 0.01mg/L | 0.2mg/L | 15 | 7.1 |
The above embodiment only have expressed several embodiment of the present utility model, and it describes comparatively concrete and detailed, but therefore can not be interpreted as the restriction to the utility model the scope of the claims.It should be pointed out that for the person of ordinary skill of the art, without departing from the concept of the premise utility, can also make some distortion and improvement, these all belong to protection domain of the present utility model.Therefore, the protection domain of the utility model patent should be as the criterion with claims.
Claims (9)
1. an electroplating waste processing equipment, is characterized in that, comprise electroplating wastewater storagetank, broken cyanide groove, except chromium groove, flocculation tank, settling bath, adsorption tank and reverse osmosis treatment device;
Described electroplating wastewater storagetank comprises the first storagetank, the second storagetank and the 3rd storagetank, described first storagetank is communicated with described broken cyanide groove, described broken cyanide groove is communicated with described 3rd storagetank, described second storagetank is communicated with the described chromium groove that removes, described flocculation tank is all communicated with described 3rd storagetank and the described chromium groove that removes, described flocculation tank is communicated with described settling bath, and described adsorption tank is communicated with described settling bath, and described reverse osmosis treatment device is communicated with described adsorption tank;
The described chromium groove that removes arranges the first adding set, the second adding set and the 3rd adding set, is respectively used to add sulfuric acid, S-WAT and alkaline matter.
2. electroplating waste processing equipment according to claim 1, is characterized in that, described broken cyanide groove is provided with the first dosing mouth.
3. electroplating waste processing equipment according to claim 1, is characterized in that, the described chromium groove that removes is provided with the second dosing mouth.
4. electroplating waste processing equipment according to claim 1, is characterized in that, described flocculation tank is provided with the 3rd dosing mouth.
5. electroplating waste processing equipment according to claim 1, is characterized in that, electroplating wastewater storagetank is formed in one structure.
6. electroplating waste processing equipment according to claim 1, is characterized in that, the bottom sidewall of described settling bath is ramp structure.
7. electroplating waste processing equipment according to claim 1, is characterized in that, described broken cyanide groove is provided with the first whipping appts.
8. electroplating waste processing equipment according to claim 1, is characterized in that, the described chromium groove that removes is provided with the second whipping appts.
9. electroplating waste processing equipment according to claim 1, is characterized in that, described flocculation tank is provided with the 3rd whipping appts.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420624202.9U CN204224354U (en) | 2014-10-25 | 2014-10-25 | Electroplating waste processing equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420624202.9U CN204224354U (en) | 2014-10-25 | 2014-10-25 | Electroplating waste processing equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204224354U true CN204224354U (en) | 2015-03-25 |
Family
ID=52922472
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420624202.9U Expired - Fee Related CN204224354U (en) | 2014-10-25 | 2014-10-25 | Electroplating waste processing equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204224354U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104291493A (en) * | 2014-10-25 | 2015-01-21 | 吴长江 | Electroplating wastewater treatment method and electroplating wastewater treatment device |
| CN108218117A (en) * | 2018-01-06 | 2018-06-29 | 广州市绿潮环保工程有限公司 | A kind of wastewater treatment equipment and waste water treatment process |
-
2014
- 2014-10-25 CN CN201420624202.9U patent/CN204224354U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104291493A (en) * | 2014-10-25 | 2015-01-21 | 吴长江 | Electroplating wastewater treatment method and electroplating wastewater treatment device |
| CN104291493B (en) * | 2014-10-25 | 2016-04-27 | 吴长江 | Electroplating effluent treatment method |
| CN108218117A (en) * | 2018-01-06 | 2018-06-29 | 广州市绿潮环保工程有限公司 | A kind of wastewater treatment equipment and waste water treatment process |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN104326599B (en) | Electroplating wastewater containing cyanogens and chrome processing method | |
| CN102603097B (en) | Advanced treatment and recycling process for wastewater containing heavy metal ions | |
| CN104261526B (en) | The processing method of heavy metal wastewater thereby | |
| CN107601779B (en) | Method and device for treating and recycling mine copper-containing acidic wastewater | |
| RU2531828C2 (en) | Electrolysis method and method and apparatus for pretreatment of raw water | |
| CN102126799B (en) | Method for treating fluorine-containing and ammonia nitrogen-containing waste water in electronic industry | |
| CN104386874A (en) | Processing technology for high-concentration waste liquid in circuit board industry | |
| CN100513334C (en) | Deep treatment process of metallurgical sewage | |
| CN105601036B (en) | Method based on ozone oxidation and biochemical technology processing chemical nickle-plating wastewater | |
| CN108218129B (en) | Treatment method of chemical nickel plating wastewater | |
| CN103011347B (en) | Method for carrying out electrolytic treatment on copper-containing electroplating wastewater and recycling copper | |
| CN103641230B (en) | Method for carrying out organic wastewater pretreatment by using an iron-carbon-Fenton-integrated reactor | |
| CN102351351B (en) | Process for treating chemical nickel-plating discarded liquid | |
| CN104803504A (en) | Novel desulfurization waste water treatment method | |
| CN105565553A (en) | Zero-emission purifying and recycling system of cyanide-containing heavy metal wastewater | |
| CN104291493B (en) | Electroplating effluent treatment method | |
| CN106517578B (en) | Heavy metal wastewater treatment method for breaking complex by using granular sludge and ceramic membrane | |
| CN204224354U (en) | Electroplating waste processing equipment | |
| CN204224358U (en) | Stainless-steel cold-rolling acid waste water treatment unit | |
| CN104030500B (en) | A kind of Processes and apparatus removing nickel ion in section aluminum waste water | |
| CN204224356U (en) | Electroplating waste processing equipment | |
| CN104291492B (en) | Electroplating effluent treatment method | |
| CN108483608A (en) | A kind of electroplating wastewater removes cyanogen system and electroplating waste water treatment system | |
| CN103880218A (en) | Complete cycle technology of vanadium smelting wastewater | |
| CN109626638A (en) | A kind for the treatment of process of high P content waste water Zero-discharge reuse |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150325 Termination date: 20151025 |
|
| EXPY | Termination of patent right or utility model |