CN204224358U - Stainless-steel cold-rolling acid waste water treatment unit - Google Patents
Stainless-steel cold-rolling acid waste water treatment unit Download PDFInfo
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- CN204224358U CN204224358U CN201420634392.2U CN201420634392U CN204224358U CN 204224358 U CN204224358 U CN 204224358U CN 201420634392 U CN201420634392 U CN 201420634392U CN 204224358 U CN204224358 U CN 204224358U
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- rolling acid
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- 229910001220 stainless steel Inorganic materials 0.000 title claims abstract description 259
- 239000010935 stainless steel Substances 0.000 title claims abstract description 259
- 239000002253 acid Substances 0.000 title claims abstract description 248
- 238000005097 cold rolling Methods 0.000 title claims abstract description 244
- 238000004065 wastewater treatment Methods 0.000 title claims abstract description 20
- 239000002351 wastewater Substances 0.000 claims abstract description 248
- 230000001264 neutralization Effects 0.000 claims abstract description 61
- 230000005591 charge neutralization Effects 0.000 claims abstract description 58
- 238000006386 neutralization reaction Methods 0.000 claims abstract description 52
- 239000011651 chromium Substances 0.000 claims abstract description 47
- 238000005189 flocculation Methods 0.000 claims abstract description 46
- 230000016615 flocculation Effects 0.000 claims abstract description 46
- 238000005273 aeration Methods 0.000 claims abstract description 45
- 238000001914 filtration Methods 0.000 claims abstract description 43
- VYZAMTAEIAYCRO-UHFFFAOYSA-N chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 claims abstract description 41
- 229910052804 chromium Inorganic materials 0.000 claims abstract description 35
- 239000004519 grease Substances 0.000 claims abstract description 34
- 238000003860 storage Methods 0.000 claims abstract description 23
- 239000000126 substance Substances 0.000 claims abstract description 13
- 238000004519 manufacturing process Methods 0.000 claims description 9
- 230000005540 biological transmission Effects 0.000 claims description 3
- 238000000034 method Methods 0.000 abstract description 55
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 31
- 229910001385 heavy metal Inorganic materials 0.000 abstract description 22
- 150000002500 ions Chemical class 0.000 abstract description 14
- 230000003472 neutralizing Effects 0.000 abstract description 8
- 239000002699 waste material Substances 0.000 abstract description 7
- 238000009713 electroplating Methods 0.000 abstract description 5
- 238000003912 environmental pollution Methods 0.000 abstract description 4
- 238000004064 recycling Methods 0.000 abstract description 4
- QAOWNCQODCNURD-UHFFFAOYSA-L sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 abstract description 4
- 238000002203 pretreatment Methods 0.000 description 184
- 238000001556 precipitation Methods 0.000 description 23
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 18
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 14
- 239000002245 particle Substances 0.000 description 13
- 229920002401 polyacrylamide Polymers 0.000 description 12
- AXCZMVOFGPJBDE-UHFFFAOYSA-L Calcium hydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 description 11
- 239000000920 calcium hydroxide Substances 0.000 description 11
- 235000011116 calcium hydroxide Nutrition 0.000 description 11
- 238000003756 stirring Methods 0.000 description 11
- VSCWAEJMTAWNJL-UHFFFAOYSA-K Aluminium chloride Chemical compound Cl[Al](Cl)Cl VSCWAEJMTAWNJL-UHFFFAOYSA-K 0.000 description 10
- AEIXRCIKZIZYPM-UHFFFAOYSA-M hydroxy(oxo)iron Chemical compound [O][Fe]O AEIXRCIKZIZYPM-UHFFFAOYSA-M 0.000 description 10
- 239000007764 o/w emulsion Substances 0.000 description 10
- 230000000694 effects Effects 0.000 description 9
- 238000005429 turbidity Methods 0.000 description 9
- 238000006243 chemical reaction Methods 0.000 description 7
- 239000003795 chemical substances by application Substances 0.000 description 7
- 239000000463 material Substances 0.000 description 7
- 239000010802 sludge Substances 0.000 description 7
- 229910004261 CaF 2 Inorganic materials 0.000 description 6
- OSGAYBCDTDRGGQ-UHFFFAOYSA-L Calcium sulfate Chemical compound [Ca+2].[O-]S([O-])(=O)=O OSGAYBCDTDRGGQ-UHFFFAOYSA-L 0.000 description 6
- 235000019738 Limestone Nutrition 0.000 description 6
- GEHJYWRUCIMESM-UHFFFAOYSA-L Sodium sulfite Chemical compound [Na+].[Na+].[O-]S([O-])=O GEHJYWRUCIMESM-UHFFFAOYSA-L 0.000 description 6
- 239000003814 drug Substances 0.000 description 6
- 230000005484 gravity Effects 0.000 description 6
- 239000006028 limestone Substances 0.000 description 6
- MYMOFIZGZYHOMD-UHFFFAOYSA-N oxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 6
- 229910052760 oxygen Inorganic materials 0.000 description 6
- 239000001301 oxygen Substances 0.000 description 6
- 239000002244 precipitate Substances 0.000 description 6
- 230000002378 acidificating Effects 0.000 description 5
- 230000001112 coagulant Effects 0.000 description 5
- 239000000701 coagulant Substances 0.000 description 5
- 238000009300 dissolved air flotation Methods 0.000 description 5
- 238000005188 flotation Methods 0.000 description 5
- 230000002045 lasting Effects 0.000 description 5
- 239000007788 liquid Substances 0.000 description 5
- PXHVJJICTQNCMI-UHFFFAOYSA-N nickel Substances [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 5
- 230000001105 regulatory Effects 0.000 description 5
- 238000004062 sedimentation Methods 0.000 description 5
- 238000000926 separation method Methods 0.000 description 5
- 239000003513 alkali Substances 0.000 description 4
- 239000003153 chemical reaction reagent Substances 0.000 description 4
- 230000003311 flocculating Effects 0.000 description 4
- 150000002815 nickel Chemical class 0.000 description 4
- 230000002829 reduced Effects 0.000 description 4
- 239000002893 slag Substances 0.000 description 4
- CDBYLPFSWZWCQE-UHFFFAOYSA-L sodium carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 4
- 230000001276 controlling effect Effects 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 159000000007 calcium salts Chemical class 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 239000001569 carbon dioxide Substances 0.000 description 2
- 229910002092 carbon dioxide Inorganic materials 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 2
- 238000004891 communication Methods 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000000706 filtrate Substances 0.000 description 2
- KRHYYFGTRYWZRS-UHFFFAOYSA-M fluoride anion Chemical compound [F-] KRHYYFGTRYWZRS-UHFFFAOYSA-M 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N iron oxide Chemical group [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 description 2
- 238000006396 nitration reaction Methods 0.000 description 2
- 238000005554 pickling Methods 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 235000017550 sodium carbonate Nutrition 0.000 description 2
- 229910000029 sodium carbonate Inorganic materials 0.000 description 2
- 239000011780 sodium chloride Substances 0.000 description 2
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-N HCl Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 1
- 229910001030 Iron–nickel alloy Inorganic materials 0.000 description 1
- 229910003301 NiO Inorganic materials 0.000 description 1
- 235000015450 Tilia cordata Nutrition 0.000 description 1
- 235000011941 Tilia x europaea Nutrition 0.000 description 1
- REDXJYDRNCIFBQ-UHFFFAOYSA-N aluminium(3+) Chemical compound [Al+3] REDXJYDRNCIFBQ-UHFFFAOYSA-N 0.000 description 1
- 238000000137 annealing Methods 0.000 description 1
- 230000003851 biochemical process Effects 0.000 description 1
- 230000000903 blocking Effects 0.000 description 1
- 229910001861 calcium hydroxide Inorganic materials 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 238000005008 domestic process Methods 0.000 description 1
- 238000005868 electrolysis reaction Methods 0.000 description 1
- 238000005530 etching Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 238000011010 flushing procedure Methods 0.000 description 1
- 238000005242 forging Methods 0.000 description 1
- 229910000041 hydrogen chloride Inorganic materials 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000005342 ion exchange Methods 0.000 description 1
- -1 iron ion Chemical class 0.000 description 1
- 239000004571 lime Substances 0.000 description 1
- GNRSAWUEBMWBQH-UHFFFAOYSA-N nickel(II) oxide Inorganic materials [Ni]=O GNRSAWUEBMWBQH-UHFFFAOYSA-N 0.000 description 1
- 230000001590 oxidative Effects 0.000 description 1
- 239000010970 precious metal Substances 0.000 description 1
- 238000010791 quenching Methods 0.000 description 1
- 230000000171 quenching Effects 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 239000002910 solid waste Substances 0.000 description 1
- 239000002352 surface water Substances 0.000 description 1
- 238000003466 welding Methods 0.000 description 1
Abstract
A kind of stainless-steel cold-rolling acid waste water treatment unit, comprise wastewater storage tank, grease removal tank, except chromium groove, the first neutralization tank, the second neutralization tank, flocculation basin, settling tank, concentration basin, storage basin, press filtration pond, backflow pool, the 3rd neutralization tank and filter vat.First neutralization tank is provided with aerating apparatus and chemicals dosing plant, is respectively used to pass into air and add alkaline matter.Above-mentioned electro-plating waste disposal plant is by arranging grease removal tank, except chromium pond, three grades of neutralization tanks, flocculation basin, settling tank, filter vat, concentration basin and press filtration ponds, oil, contents of many kinds of heavy metal ion, fluorion and sulfate ion can be removed simultaneously, the stainless-steel cold-rolling acid waste water produced in the current producing stainless steel process of effective solution, because the bed mud water content after process is lower, recycle after bed mud directly can being carried out nature mummification, thus decrease secondary environmental pollution, improve resource recycling.Meanwhile, utilize aeration neutralizing treatment, can cost be saved.
Description
Technical field
The utility model relates to stainless-steel cold-rolling acid waste water process field, particularly relates to a kind of stainless-steel cold-rolling acid waste water treatment unit.
Background technology
Along with the development of stainless steel industry, the waste water containing heavy metal produced in its process of manufacture and the impact of solid waste on surrounding soil and surface water environment also manifest day by day.In the complete processings such as stainless steel annealing, normalizing, quenching, normalizing, welding, forging, stainless steel surface can produce iron scale, its main component is FeO, Fe
2o
3, NiO
2, Cr
2o
3, Fe
3o
4, FeOCr
2o
3, NiFe
2o
3, FeOCr
2o
3fe
2o
3deng dense form oxide compound.The basic strong adhesion of these oxide compounds, at employing ball blast, in the treatment process of the combination procesies such as high temperature alkaline etching, fused salt electrolysis, nitration mixture pickling, multistage rinsing, inevitably discharge the multichannel pickling waste waterss such as neutral salt waste liquid, mixed acid waste liquor, fluoride waste, poaching wastewater.And these stainless-steel cold-rolling waste component and generation operation difference time are very large, there is complicated component, the acidity major part features such as harmful substance contents exceeds standard, environmental hazard is large.
At present, the domestic process to stainless-steel cold-rolling waste water mainly contains: (1) utilizes neutralizing device fully to neutralize; (2) burning facility is utilized fully to burn; (3) utilize the miscellaneous equipments such as ion-exchange unit to carry out regeneration to reclaim.But these method Problems existing mainly easily cause secondary pollution or high in cost of production.
Such as, chromium, nickel salt extracting method in Chinese patent 200710069398.4 1 kinds of stainless steel acid cleaning waste waters, disclose a kind for the treatment of process of acid waste water, refers in particular to the extracting method of chromium, nickel salt in a kind of stainless steel acid waste water.The present invention is by removing objectionable impurities in acid waste water stage by stage, added calcium salt before this, and control pH is 2.0 ~ 4.0, removes fluoride ion, add highly basic or soda ash again, control pH is 7.0 ~ 8.0, after filtration, can effectively realize qualified discharge liquid, again the filter residue acid solution after filtration is carried out acidifying oxidizing reaction, control pH is 1.0 ~ 4.0, filters the iron ion removed wherein, is precious metal chromium, the nickel salt of extraction in remaining filtrate.Advantage of the present invention is, can reduce the add-on of calcium salt, highly basic or soda ash, can realize the qualified discharge of liquid, and can not cause the situation of heavy metal secondary pollution, recycles chromium, nickel salt, effectively increases economic efficiency.The present invention can be widely used in the wastewater treatment of various stainless steel manufacturing concern, and similar enterprises.
Chinese patent 201110262416.7 stainless steel acid waste water reduces Cr
6+treatment process, this invention be stainless steel acid waste water reduce Cr
6+treatment process, its step comprises: stainless steel nitration mixture waste water and sulfuric acid wastewater containing sent in reduction pond; In reduction pond, add reductive agent and stir, making Cr in waste water
6+be converted into Cr
3+, reach the water outlet inflow neutralization tank that ORP requires; To neutralization tank feeding lime, and drum oxygen aeration, by Fe in waste water
2+be oxidized to Fe
3+, form Cr (OH)
3, CaF
2, Fe (OH)
3, CaSO
4precipitation; The water outlet of neutralization tank enters flocculation basin; Add PAM to flocculation basin and form large alumen ustum, dosage is 2 ~ 5mg/L, and the water outlet of flocculation basin flows in settling tank; The water outlet of flocculation basin after settling tank precipitation, water outlet to subsequent disposal facility, this water outlet Cr
6+should emission request be met, then the mud in settling tank regularly be transported outward.The present invention can meet environmental requirement, and is beneficial to subsequent biochemical process.
But above-mentioned disclosed patent still cannot provide a kind of Integrated Processing Unit that can process all kinds of waste water that stainless-steel cold-rolling process produces.
Utility model content
Based on this, be necessary a kind of low cost, high-level efficiency to be provided, the stainless-steel cold-rolling waste water plant produced in producing stainless steel process can be processed.
A kind of stainless-steel cold-rolling acid waste water treatment unit, comprise wastewater storage tank, grease removal tank, except chromium groove, the first neutralization tank, the second neutralization tank, flocculation basin, settling tank, concentration basin, storage basin, press filtration pond, backflow pool, the 3rd neutralization tank and filter vat;
Described wastewater storage tank is communicated with described grease removal tank, described grease removal tank is communicated with the described chromium groove that removes, described first neutralization tank is communicated with the described chromium groove that removes, described second neutralization tank is communicated with described first neutralization tank, described flocculation basin is communicated with described second neutralization tank, described settling tank is communicated with described flocculation basin and described concentration basin respectively, described storage basin is communicated with described concentration basin, described press filtration pond is communicated with described storage basin, described backflow pool is communicated with described press filtration pond and described settling tank respectively, described 3rd neutralization tank is communicated with described settling tank, described filter vat is communicated with described 3rd neutralization tank,
Described first neutralization tank is provided with aerating apparatus and chemicals dosing plant, is respectively used to pass into air and add alkaline matter.
Wherein in an embodiment, described aerating apparatus is many aeration tubes.
Wherein in an embodiment, many described aeration tubes are arranged in array.
Wherein in an embodiment, the many rectangular array arrangements of described aeration tube.
Wherein in an embodiment, aeration tube described in each arranges multiple production well.
Wherein in an embodiment, production well described in each is arranged at described first neutralization tank.
Wherein in an embodiment, described grease removal tank is provided with vapour pipe.
Wherein in an embodiment, in described concentration basin, be provided with central transmission concentrator.
Wherein in an embodiment, in described press filtration pond, be provided with plate-and-frame filter press.
Above-mentioned stainless-steel cold-rolling acid waste water treatment unit is by arranging grease removal tank, except chromium pond, three grades of neutralization tanks, flocculation basin, settling tank, filter vat, concentration basin and press filtration ponds, oil, contents of many kinds of heavy metal ion, fluorion and sulfate ion can be removed simultaneously, the stainless-steel cold-rolling acid waste water produced in the current producing stainless steel process of effective solution, simultaneously due to the bed mud water content lower (being less than 35%) after process, recycle after bed mud directly can being carried out nature mummification, thus decrease secondary environmental pollution, improve resource recycling.In addition, utilize aeration neutralizing treatment, can cost be saved.
Accompanying drawing explanation
Fig. 1 is the schema of the stainless-steel cold-rolling process for treating acidic waste water of an embodiment;
Fig. 2 is the structural representation of the stainless-steel cold-rolling acid waste water treatment unit 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 stainless-steel cold-rolling process for treating acidic waste water of an embodiment comprises the steps:
S110: after the slagging-off of stainless-steel cold-rolling acid waste water and oil removing, obtain the first pre-treatment stainless-steel cold-rolling acid waste water.
By carrying out stainless-steel cold-rolling acid waste water, except Slag treatment, foreign material larger for volume in stainless-steel cold-rolling acid waste water to be removed, avoiding pipeline and occurring to block the problems such as stuck, being conducive to stainless-steel cold-rolling acid waste water and entering aftertreatment device swimmingly.
Stainless-steel cold-rolling acid waste water after slagging-off is passed into grease removal tank, such as, by stainless-steel cold-rolling acid waste water after leave standstill 2h ~ 3h after grease removal tank, make the oil slick in stainless-steel cold-rolling acid waste water and the larger oil in water emulsion of particle rise to surface, collect surperficial oil reservoir and reach the object removing oil slick.And for example, also stainless-steel cold-rolling acid waste water can be passed into air flotation pool, by dissolved air flotation process, like this, the oil in water emulsion in stainless-steel cold-rolling acid waste water can be removed.
In order to be removed by the oil of stainless-steel cold-rolling acid waste water to a greater degree, such as, can control temperature in grease removal tank is 40 DEG C ~ 50 DEG C, like this, can improve efficiency of deoiling, and promotes deoil rate.
S120: the first pre-treatment stainless-steel cold-rolling acid waste water is carried out reduction treatment, obtains the second pre-treatment stainless-steel cold-rolling acid waste water.
Such as, in the first pre-treatment stainless-steel cold-rolling acid waste water, add concentration is 0.05-5% sulfuric acid, after regulating pH to 2.5 ~ 3.0, adding concentration toward it is again 2%wt ~ 10%wt (massfraction) S-WAT or V-Brite B, make the ORP value of the cold rolling acid waste water of chromium stainless steel for 250mV ~ 300mV, after abundant stirring, the hexavalent chrome reduction in the first pre-treatment stainless-steel cold-rolling acid waste water is made to become trivalent chromium.
S130: the second pre-treatment stainless-steel cold-rolling acid waste water is carried out one-level aeration, meanwhile, adding alkaline matter, to carry out neutralizing treatment to pH be 3.5 ~ 4.0, and wherein, alkaline matter is Wingdale, and aeration intensity is 0.5m
3~ 5m
3(air)/m
3(the second pre-treatment stainless-steel cold-rolling acid waste water) h.
Add alkaline matter toward the second pre-treatment stainless-steel cold-rolling acid waste water, and give Air Exposure, by pH regulator to 3.5 ~ 4.0 of the second pre-treatment cold rolling wastewater, obtain the 3rd pre-treatment stainless-steel cold-rolling acid waste water.
General, in traditional technology, some difficulties are usually produced owing to adopting Wingdale neutralizing treatment stainless-steel cold-rolling acid waste water, such as, the calcium sulfate produced in neutralization reaction covers the carrying out that limestone surfaces can hinder neutralization reaction, therefore, with stainless-steel cold-rolling acid waste water in generally adopting price slaked lime costly.
Such as, and in order to reduce reagent cost, the present embodiment uses aeration means, e.g., aeration intensity is 0.5m
3~ 5m
3(air)/m
3(the second pre-treatment stainless-steel cold-rolling acid waste water) h, adopt cheap Wingdale that the second pre-treatment stainless-steel cold-rolling acid waste water is neutralized to slightly acidic, due to aeration can guarantee limestone particle can not cover by the calcium sulfate precipitation that generates in reaction process, thus ensure that continuing of reacting carries out, and, the carbon dioxide that Air Exposure can also effectively produce in stripping reaction process, reduce input amount and the body refuse growing amount of alkali in secondary N-process, like this, the cost of medicament can be reduced further.
S140: the 3rd pre-treatment stainless-steel cold-rolling acid waste water carried out in secondary and after Air Exposure, obtain the 4th pre-treatment stainless-steel cold-rolling acid waste water.
Alkaline matter is added in the 3rd pre-treatment stainless-steel cold-rolling acid waste water, if concentration is the milk of lime of 5%, and continue aeration, along with the lasting dropping of milk of lime, the throw out of the 3rd pre-treatment stainless-steel cold-rolling acid waste water continues to increase and becomes reddish-brown, behind pH regulator to 8.5 ~ 9.5 of the 3rd pre-treatment stainless-steel cold-rolling acid waste water, continues aeration 5 ~ 10 minutes, as, aeration intensity is: 1m
3~ 10m
3(air)/m
3(the 3rd pre-treatment stainless-steel cold-rolling acid waste water) h, makes the Fe in the 3rd pre-treatment stainless-steel cold-rolling acid waste water
2+fe is oxidized under the effect of oxygen
3+, and form CaF
2, Fe (OH)
3, Ni (OH)
2, Cr (OH)
3and CaSO
4throw out, obtains the 4th pre-treatment stainless-steel cold-rolling acid waste water.
S150: after being carried out by the 4th pre-treatment stainless-steel cold-rolling acid waste water flocculating and precipitate, obtain the 5th pre-treatment stainless-steel cold-rolling acid waste water and the first pre-treatment bed mud.
4th pre-treatment stainless-steel cold-rolling acid waste water is carried out flocculation treatment, such as, in the 4th stainless-steel cold-rolling acid waste water, add polymerize aluminum chloride (PAC) is flocculation agent, dosage is 1 ‰ ~ 5 ‰ (thousandths) of the 4th pre-treatment stainless-steel cold-rolling acid waste water volume, after stirring 15min, adding polyacrylamide (PAM) is coagulant aids, and its dosage is 0.1 ‰ of the 4th pre-treatment stainless-steel cold-rolling acid waste water volume.After flocculation, the 4th pre-treatment stainless-steel cold-rolling acid waste water is carried out deposition and leave standstill, heavy metal ion is precipitated completely with the form of oxyhydroxide.Such as, the 4th pre-treatment stainless-steel cold-rolling acid waste water after flocculation is passed into sedimentation tank, and heavy metal ion in the basic conditions, 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.
S160: by the 5th pre-treatment stainless-steel cold-rolling acid waste water through three grades of neutralizations and after filtering, outer row.
In the 5th pre-treatment stainless-steel cold-rolling acid waste water, add acid, regulate pH to 6.5 ~ 7.2, and filter, by suspended substance removal, reduce its turbidity, make to reach emission standard.
S170: after the first pre-treatment bed mud being carried out concentrated and press filtration, obtain the 6th pre-treatment stainless-steel cold-rolling acid waste water and the second pre-treatment bed mud.
The first pre-treatment bed mud that step S150 produces being concentrated to concentration basin by sludge pump positive delivery, in order to improve sludge condensation and dehydrating effect, such as, in the first pre-treatment bed mud, adding PAM with auxiliary mud-water separation.By the first pre-treatment bed mud extracting being carried out pressure rate to pressure filter with pump, the 6th pre-treatment stainless-steel cold-rolling acid waste water obtained flows out under gravity, and the water ratio of the second pre-treatment bed mud after press filtration is less than 35%.
S180: by the 6th pre-treatment stainless-steel cold-rolling acid waste water after precipitation, three grades of neutralizations and filtration, outer row.
The 6th pre-treatment stainless-steel cold-rolling acid waste water in step S170 after press filtration is back to settling tank and carries out precipitation process, be appreciated that, 6th pre-treatment stainless-steel cold-rolling acid waste water is owing to have passed through in second and Air Exposure and in alkalescence, be back to settling tank, the input amount of precipitation process process neutral and alkali material can be reduced, reduce reagent cost.
In the 6th pre-treatment stainless-steel cold-rolling acid waste water after precipitation process, add acid, regulate pH to 6.5 ~ 7.2, and filter, by suspended substance removal, reduce its turbidity, guarantee to reach emission standard.
The treatment process of above-mentioned stainless-steel cold-rolling acid waste water, by removing the gred to stainless-steel cold-rolling acid waste water, oil removing, except steps such as chromium, neutralization, flocculation, precipitation and filtrations, oil, contents of many kinds of heavy metal ion, fluorion and sulfate ion can be removed simultaneously, the stainless-steel cold-rolling acid waste water produced in the current producing stainless steel process of effective solution, simultaneously due to the bed mud water content lower (being less than 35%) after process, recycle after bed mud directly can being carried out nature mummification, thus decrease secondary environmental pollution, improve resource recycling.
In order to introduce stainless-steel cold-rolling process for treating acidic waste water of the present utility model further, such as, a kind of stainless-steel cold-rolling acid waste water treatment unit is also provided.
As shown in Figure 2, it is the structural representation of the stainless-steel cold-rolling acid waste water treatment unit 10 of an embodiment.
Refer to Fig. 2, stainless-steel cold-rolling acid waste water treatment unit 10, comprise wastewater storage tank 100, grease removal tank 200, except chromium groove 300, first neutralization tank 400, second neutralization tank 500, flocculation basin 600, settling tank 700, concentration basin 800, storage basin 900, press filtration pond 900a, backflow pool 900b, the 3rd neutralization tank 900c and filter vat 900d.
Such as, described wastewater storage tank, described grease removal tank, described except chromium groove, described first neutralization tank, described second neutralization tank, described flocculation basin, described settling tank, described concentration basin, described storage basin, described press filtration pond, described backflow pool sequential communication; Described settling tank also with described 3rd neutralization tank, described filter vat sequential communication; Described backflow pool is also communicated with described settling tank.
Refer to Fig. 2, be provided with grid 110 in wastewater storage tank 100, grid 110 is for removing the larger foreign material of volume in sewage, so that waste water is smooth and easy enter rear portion treatment unit.
Such as, grid 110 is a kind of H type structures, and filter grid is two, and can be used alone and use in parallel, filter grid is made up of stainless steel.
Refer to Fig. 2, wastewater storage tank 100 is communicated with grease removal tank 200, and the stainless-steel cold-rolling acid waste water being stored in wastewater storage tank 100 passes into grease removal tank 200, in grease removal tank 200, the oil in stainless-steel cold-rolling acid waste water can be made to remove.
Such as, after stainless-steel cold-rolling acid waste water is left standstill 2h ~ 3h after grease removal tank, make the oil slick in stainless-steel cold-rolling acid waste water and the larger oil in water emulsion of particle rise to surface, collect surperficial oil reservoir and reach the object removing oil slick.And for example, also stainless-steel cold-rolling acid waste water can be passed into air flotation pool, by dissolved air flotation process, like this, the oil in water emulsion in stainless-steel cold-rolling acid waste water can be removed.
In order to a greater degree the oil of stainless-steel cold-rolling acid waste water be removed, such as, grease removal tank 200 is provided with vapour pipe 210, and the quantity of vapour pipe 210 is many, each vapour pipe 210 all has an opening, makes temperature in grease removal tank 200 control at 40 DEG C ~ 50 DEG C, like this, can efficiency of deoiling be improved, promote deoil rate.
Refer to Fig. 2, grease removal tank 200 is communicated with except chromium groove 300, the first pre-treatment stainless-steel cold-rolling acid waste water after grease removal tank 200 processes passes into except in chromium groove 300, in the first pre-treatment stainless-steel cold-rolling acid waste water, add concentration is 0.05-5% sulfuric acid, after regulating pH to 2.5 ~ 3.0, adding concentration toward it is again 2%wt ~ 10%wt S-WAT or V-Brite B, make the ORP value of the first pre-treatment stainless-steel cold-rolling acid waste water for 250mV ~ 300mV, after abundant stirring, the hexavalent chrome reduction in the cold rolling acid waste water of chromium stainless steel is made to become trivalent chromium.
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 charging opening in chromium groove 300, adding of medicine can be facilitated like this.
In order to improve the speed of reaction except chromium groove 300, such as, being provided with whipping appts except in chromium groove 300, accelerating the speed of reaction of hexavalent chrome reduction, improve processing efficiency.
Refer to Fig. 2, the first neutralization tank 400 is communicated with except chromium groove 300.Pass into the first neutralization tank by through the second pre-treatment stainless-steel cold-rolling acid waste water except chromium groove 300, in the first neutralization tank 300, add alkaline matter, and give Air Exposure, by pH regulator to 3.5 ~ 4.0 of the second pre-treatment cold rolling wastewater.
And in order to reduce reagent cost, such as, in the present embodiment, use aeration means, e.g., aeration intensity is: 0.5m
3~ 5m
3(air)/m
3(the second pre-treatment stainless-steel cold-rolling acid waste water) h, adopt cheap Wingdale that the second pre-treatment stainless-steel cold-rolling acid waste water is neutralized to slightly acidic, due to aeration can guarantee limestone particle can not cover by the calcium sulfate precipitation that generates in reaction process, thus ensure that continuing of reacting carries out, and, the carbon dioxide that Air Exposure can also effectively produce in stripping reaction process, reduce input amount and the body refuse growing amount of alkali in secondary N-process, like this, the cost of medicament can be reduced further.
Such as, aerating apparatus is many aeration tubes, and and for example, many aeration tubes are arranged in array, and for example, the many rectangular array arrangements of aeration tube, and for example, each aeration tube arranges multiple production well, and for example, each production well is arranged in the first neutralization tank 400, like this, can improve aeration efficiency.
Refer to Fig. 2, the second neutralization tank 500 is communicated with the first neutralization tank 400.Alkaline matter is added in the 3rd pre-treatment stainless-steel cold-rolling acid waste water, if concentration is the milk of lime of 5%, and continue aeration, along with the lasting dropping of milk of lime, the throw out of the 3rd pre-treatment stainless-steel cold-rolling acid waste water continues to increase and becomes reddish-brown, behind pH regulator to 8.5 ~ 9.5 of the 3rd pre-treatment stainless-steel cold-rolling acid waste water, continues aeration 5 ~ 10 minutes, as, aeration intensity is: 1m
3~ 10m
3(air)/m
3(the 3rd pre-treatment stainless-steel cold-rolling acid waste water) h, makes the Fe in the 3rd pre-treatment stainless-steel cold-rolling acid waste water
2+fe is oxidized under the effect of oxygen
3+, and form CaF
2, Fe (OH)
3, Ni (OH)
2, Cr (OH)
3and CaSO
4throw out.
Refer to Fig. 2, flocculation basin 600 is communicated with the second neutralization tank 500, the 4th pre-treatment cold rolling wastewater of the second neutralization tank 500 is passed into flocculation basin 600 and carries out flocculation treatment.
Such as, in the 4th stainless-steel cold-rolling acid waste water, add polymerize aluminum chloride (PAC) is flocculation agent, dosage is 1 ‰ ~ 5 ‰ (thousandths) of the 4th pre-treatment stainless-steel cold-rolling acid waste water volume, after stirring 15min, adding polyacrylamide (PAM) is coagulant aids, and its dosage is 0.1 ‰ of the 4th pre-treatment stainless-steel cold-rolling acid waste water volume.After flocculation, the 4th pre-treatment stainless-steel cold-rolling acid waste water is carried out deposition and leave standstill, heavy metal ion is precipitated completely with the form of oxyhydroxide.Such as, the 4th pre-treatment stainless-steel cold-rolling acid waste water after flocculation is passed into sedimentation tank, and heavy metal ion in the basic conditions, 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 basin 600, as PAC and PAM etc., in flocculation basin 600, be provided with charging opening, adding of medicine can be facilitated like this.
In order to improve the flocculation rate of flocculation basin 600, such as, in flocculation basin 600, be provided with whipping appts, stainless-steel cold-rolling acid waste water is fully mixed with flocculation agent etc., improve flocculation efficiency.
Refer to Fig. 2, settling tank 700 is communicated with flocculation basin 600, flocculation basin 600 is carried out the importing of the treatment solution after flocculation treatment settling tank 700 and carries out precipitation process.
In order to prevent heavy metal precipitation to be mixed into subsequent processes, such as, settling tank 700 is tube settler, that is, the radius bottom settling tank 700 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.
Refer to Fig. 2, concentration basin 800 is communicated with settling tank 700, and the first pre-treatment bed mud produced in settling tank 700 is carried out concentration by sludge pump positive delivery to concentration basin 800.
Concentrating and dehydrating effect to improve the first pre-treatment bed mud, such as, in concentration basin 800, adding PAM with auxiliary mud-water separation, the concentrated of the first pre-treatment bed mud and dehydrating effect can be improved like this.And for example, in concentration basin 800, be provided with central transmission concentrator, improve the concentrated of the first pre-treatment bed mud and dehydrating effect.
In order to reduce costs, such as, the top of concentration basin 800 is communicated with the bottom of settling tank 700, can reduce the running cost of sludge pump.
Refer to Fig. 2, storage basin 900 is communicated with concentration basin 800, and press filtration pond 900a is communicated with storage basin 900, and backflow pool 900b is communicated with press filtration pond 900a.Storage basin 900 is entered by the first pre-treatment bed mud after concentration basin 800 processes, by the pump in storage basin, the first pre-treatment bed mud extracting is carried out pressure rate to press filtration pond 900a, the 6th pre-treatment stainless-steel cold-rolling acid waste water obtained flows into backflow pool 900b under gravity, and the water ratio of the second pre-treatment bed mud after the 900a process of press filtration pond is less than 35%.
Be provided with plate-and-frame filter press in the 900a of press filtration pond, be used for sloughing the water in the first pre-treatment bed mud further.For preventing the filter cloth in plate-and-frame filter press from blocking, such as, arranging backwash high pressure water pump and carrying out routine cleaning, back flushing draining flows into backflow pool 900b under gravity together with filtrate after press filtration.
Refer to Fig. 2, backflow pool 900b is communicated with settling tank 700, and the 6th pre-treatment stainless-steel cold-rolling acid waste water being stored in backflow pool 900b enters settling tank 700 by high-pressure pump and carries out further precipitation process.
Can to understand, the 6th pre-treatment stainless-steel cold-rolling acid waste water, owing to have passed through in second and Air Exposure and in alkalescence, be back to settling tank 700b, can reduce the input amount of precipitation process process neutral and alkali material, reduces reagent cost.
Refer to Fig. 2, the 3rd neutralization tank 900c is communicated with settling tank 700, and filter vat 900d is communicated with the 3rd settling tank 900c.
Owing to entering the waste water of the 3rd neutralization tank in alkalescence, can't emission standard be reached, by adding acid, as HCl, regulate pH to 6.5 ~ 7.2, making it reach emission standard.
After the 3rd neutralization tank 900c process, imported filtering basin further, by suspended substance removal, reduce its turbidity, make to reach emission standard.
Above-mentioned electro-plating waste disposal plant 10 is by arranging except grease removal tank, except chromium pond, three grades of neutralization tanks, flocculation basin, settling tank, filter vat, concentration basin and press filtration ponds, oil, contents of many kinds of heavy metal ion, fluorion and sulfate ion can be removed simultaneously, the stainless-steel cold-rolling acid waste water produced in the current producing stainless steel process of effective solution, simultaneously due to the bed mud water content lower (being less than 35%) after process, recycle after bed mud directly can being carried out nature mummification, thus decrease secondary environmental pollution, improve resource recycling.
Be specific embodiment part below.
Embodiment 1:
The process of the stainless-steel cold-rolling acid waste water of certain stainless steel factory, day quantity discharged be 1000 tons.Wherein, the water quality situation of the stainless-steel cold-rolling acid waste water of this stainless steel factory is as table 1.
Table 1
Now as follows the stainless-steel cold-rolling acid waste water of this electroplating facility is processed:
After the slagging-off of stainless-steel cold-rolling acid waste water and oil removing, obtain the first pre-treatment stainless-steel cold-rolling acid waste water.
By carrying out stainless-steel cold-rolling acid waste water, except Slag treatment, foreign material larger for volume in stainless-steel cold-rolling acid waste water being removed.
Stainless-steel cold-rolling acid waste water after slagging-off is passed into grease removal tank, by stainless-steel cold-rolling acid waste water after leave standstill 3h after grease removal tank, controlling temperature in grease removal tank is 50 DEG C, the oil slick in stainless-steel cold-rolling acid waste water and the larger oil in water emulsion of particle is made to rise to surface, after collecting surperficial oil reservoir, stainless-steel cold-rolling acid waste water is passed into air flotation pool, by dissolved air flotation process, the oil in water emulsion in removing stainless-steel cold-rolling acid waste water.
First pre-treatment stainless-steel cold-rolling acid waste water is carried out reduction treatment, obtains the second pre-treatment stainless-steel cold-rolling acid waste water.
In the first pre-treatment stainless-steel cold-rolling acid waste water, add concentration is 0.05-5% sulfuric acid, after regulating pH to 3.0, adding concentration toward it is again 2%wt ~ 10%wt (massfraction) S-WAT, make the ORP value of the cold rolling acid waste water of chromium stainless steel for 280mV, 30min after abundant stirring, makes hexavalent chrome reduction become trivalent chromium.
After second pre-treatment stainless-steel cold-rolling acid waste water is carried out one-level aeration neutralizing treatment, obtain the 3rd pre-treatment stainless-steel cold-rolling acid waste water.
Adding particle diameter toward the second pre-treatment stainless-steel cold-rolling acid waste water is 0.5mm ~ 3mm limestone particle, and gives Air Exposure, and aeration intensity is: 2m
3(air)/m
3(the second pre-treatment stainless-steel cold-rolling acid waste water) h, by pH regulator to 3.5 ~ 4.0 of the second pre-treatment cold rolling wastewater, obtains the 3rd pre-treatment stainless-steel cold-rolling acid waste water.
3rd pre-treatment stainless-steel cold-rolling acid waste water carried out in secondary and after Air Exposure, obtain the 4th pre-treatment stainless-steel cold-rolling acid waste water.
The milk of lime that concentration is 5% is added in the 3rd pre-treatment stainless-steel cold-rolling acid waste water, and continue aeration, along with the lasting dropping of milk of lime, the throw out of the 3rd pre-treatment stainless-steel cold-rolling acid waste water continues to increase and becomes reddish-brown, behind pH regulator to 8.5 ~ 9.5 of the 3rd pre-treatment stainless-steel cold-rolling acid waste water, continue aeration 10 minutes, e.g., aeration intensity is 5m
3(air)/m
3(the 3rd pre-treatment stainless-steel cold-rolling acid waste water) h, makes the Fe in the 3rd pre-treatment stainless-steel cold-rolling acid waste water
2+fe is oxidized under the effect of oxygen
3+, and form CaF
2, Fe (OH)
3, Ni (OH)
2, Cr (OH)
3and CaSO
4throw out, obtains the 4th pre-treatment stainless-steel cold-rolling acid waste water.
After being carried out by 4th pre-treatment stainless-steel cold-rolling acid waste water flocculating and precipitate, obtain the 4th pre-treatment stainless-steel cold-rolling acid waste water and the first pre-treatment bed mud.
In the 4th stainless-steel cold-rolling acid waste water, add polymerize aluminum chloride (PAC) is flocculation agent, dosage is 1 ‰ ~ 5 ‰ (thousandths) of the 4th pre-treatment stainless-steel cold-rolling acid waste water volume, after stirring 15min, adding polyacrylamide (PAM) is coagulant aids, and its dosage is 0.1 ‰ of the 4th pre-treatment stainless-steel cold-rolling acid waste water volume.After flocculation, the 4th pre-treatment stainless-steel cold-rolling acid waste water is carried out deposition and leave standstill, heavy metal ion is precipitated completely with the form of oxyhydroxide.Such as, the 4th pre-treatment stainless-steel cold-rolling acid waste water after flocculation is passed into sedimentation tank, and heavy metal ion in the basic conditions, is deposited into the bottom of settling bath with the form of oxyhydroxide.Time of repose is 1h ~ 2h.
By the 5th pre-treatment stainless-steel cold-rolling acid waste water through three grades of neutralizations and after filtering, outer row.
In the 5th pre-treatment stainless-steel cold-rolling acid waste water, add acid, regulate pH to 6.5 ~ 7.2, and filter, by suspended substance removal, reduce its turbidity, make to reach emission standard.
After first pre-treatment bed mud being carried out concentrated and press filtration, obtain the 6th pre-treatment stainless-steel cold-rolling acid waste water and the second pre-treatment bed mud.
The the first pre-treatment bed mud produced is concentrated to concentration basin by sludge pump positive delivery, in the first pre-treatment bed mud, adds PAM with auxiliary mud-water separation.By the first pre-treatment bed mud extracting being carried out pressure rate to pressure filter with pump, the 6th pre-treatment stainless-steel cold-rolling acid waste water obtained flows out under gravity, and the water ratio of the second pre-treatment bed mud after press filtration is less than 35%.
By the 6th pre-treatment stainless-steel cold-rolling acid waste water after precipitation, three grades of neutralizations and filtration, outer row.
The 6th pre-treatment stainless-steel cold-rolling acid waste water after press filtration is back to settling tank and carries out precipitation process, acid is added in the 6th pre-treatment stainless-steel cold-rolling acid waste water after precipitation process, regulate pH to 6.5 ~ 7.2, and filter, by suspended substance removal, reduce its turbidity, guarantee to reach emission standard.
After above-mentioned treatment step, the discharge water obtained after testing after, water quality the results are shown in Table 2.
Table 2
Embodiment 2:
The process of the stainless-steel cold-rolling acid waste water of certain stainless steel factory, day quantity discharged be 500 tons.Wherein, the water quality situation of the stainless-steel cold-rolling acid waste water of this stainless steel factory is as table 3.
Table 3
Now as follows the stainless-steel cold-rolling acid waste water of this electroplating facility is processed:
After the slagging-off of stainless-steel cold-rolling acid waste water and oil removing, obtain the first pre-treatment stainless-steel cold-rolling acid waste water.
By carrying out stainless-steel cold-rolling acid waste water, except Slag treatment, foreign material larger for volume in stainless-steel cold-rolling acid waste water being removed.
Stainless-steel cold-rolling acid waste water after slagging-off is passed into grease removal tank, by stainless-steel cold-rolling acid waste water after leave standstill 3h after grease removal tank, controlling temperature in grease removal tank is 40 DEG C, the oil slick in stainless-steel cold-rolling acid waste water and the larger oil in water emulsion of particle is made to rise to surface, after collecting surperficial oil reservoir, stainless-steel cold-rolling acid waste water is passed into air flotation pool, by dissolved air flotation process, the oil in water emulsion in removing stainless-steel cold-rolling acid waste water.
First pre-treatment stainless-steel cold-rolling acid waste water is carried out reduction treatment, obtains the second pre-treatment stainless-steel cold-rolling acid waste water.
In the first pre-treatment stainless-steel cold-rolling acid waste water, add concentration is 0.05-5% sulfuric acid, after regulating pH to 3.0, adding concentration toward it is again 10%wt (massfraction) S-WAT, make the ORP value of the cold rolling acid waste water of chromium stainless steel for 280mV, 30min after abundant stirring, makes hexavalent chrome reduction become trivalent chromium.
After second pre-treatment stainless-steel cold-rolling acid waste water is carried out one-level aeration neutralizing treatment, obtain the 3rd pre-treatment stainless-steel cold-rolling acid waste water.
Adding particle diameter toward the second pre-treatment stainless-steel cold-rolling acid waste water is 0.5mm ~ 3mm limestone particle, and gives Air Exposure, and aeration intensity is: 2m
3(air)/m
3(the second pre-treatment stainless-steel cold-rolling acid waste water) h, by the pH regulator to 4.0 of the second pre-treatment cold rolling wastewater, obtains the 3rd pre-treatment stainless-steel cold-rolling acid waste water.
3rd pre-treatment stainless-steel cold-rolling acid waste water carried out in secondary and after Air Exposure, obtain the 4th pre-treatment stainless-steel cold-rolling acid waste water.
The milk of lime that concentration is 5% is added in the 3rd pre-treatment stainless-steel cold-rolling acid waste water, and continue aeration, along with the lasting dropping of milk of lime, the throw out of the 3rd pre-treatment stainless-steel cold-rolling acid waste water continues to increase and becomes reddish-brown, after the pH regulator to 9.5 of the 3rd pre-treatment stainless-steel cold-rolling acid waste water, continue aeration 10 minutes, e.g., aeration intensity is 8m
3(air)/m
3(the 3rd pre-treatment stainless-steel cold-rolling acid waste water) h, makes the Fe in the 3rd pre-treatment stainless-steel cold-rolling acid waste water
2+fe is oxidized under the effect of oxygen
3+, and form CaF
2, Fe (OH)
3, Ni (OH)
2, Cr (OH)
3and CaSO
4throw out, obtains the 4th pre-treatment stainless-steel cold-rolling acid waste water.
After being carried out by 4th pre-treatment stainless-steel cold-rolling acid waste water flocculating and precipitate, obtain the 4th pre-treatment stainless-steel cold-rolling acid waste water and the first pre-treatment bed mud.
In the 4th stainless-steel cold-rolling acid waste water, add polymerize aluminum chloride (PAC) is flocculation agent, dosage is 1 ‰ ~ 5 ‰ (thousandths) of the 4th pre-treatment stainless-steel cold-rolling acid waste water volume, after stirring 15min, adding polyacrylamide (PAM) is coagulant aids, and its dosage is 0.1 ‰ of the 4th pre-treatment stainless-steel cold-rolling acid waste water volume.After flocculation, the 4th pre-treatment stainless-steel cold-rolling acid waste water is carried out deposition and leave standstill, heavy metal ion is precipitated completely with the form of oxyhydroxide.Such as, the 4th pre-treatment stainless-steel cold-rolling acid waste water after flocculation is passed into sedimentation tank, and heavy metal ion in the basic conditions, is deposited into the bottom of settling bath with the form of oxyhydroxide.Time of repose is 1h ~ 2h.
By the 5th pre-treatment stainless-steel cold-rolling acid waste water through three grades of neutralizations and after filtering, outer row.
In the 5th pre-treatment stainless-steel cold-rolling acid waste water, add acid, regulate pH to 6.5 ~ 7.2, and filter, by suspended substance removal, reduce its turbidity, make to reach emission standard.
After first pre-treatment bed mud being carried out concentrated and press filtration, obtain the 6th pre-treatment stainless-steel cold-rolling acid waste water and the second pre-treatment bed mud.
The the first pre-treatment bed mud produced is concentrated to concentration basin by sludge pump positive delivery, in the first pre-treatment bed mud, adds PAM with auxiliary mud-water separation.By the first pre-treatment bed mud extracting being carried out pressure rate to pressure filter with pump, the 6th pre-treatment stainless-steel cold-rolling acid waste water obtained flows out under gravity, and the water ratio of the second pre-treatment bed mud after press filtration is less than 35%.
By the 6th pre-treatment stainless-steel cold-rolling acid waste water after precipitation, three grades of neutralizations and filtration, outer row.
The 6th pre-treatment stainless-steel cold-rolling acid waste water after press filtration is back to settling tank and carries out precipitation process, acid is added in the 6th pre-treatment stainless-steel cold-rolling acid waste water after precipitation process, regulate pH to 6.5 ~ 7.2, and filter, by suspended substance removal, reduce its turbidity, guarantee to reach emission standard.
After above-mentioned treatment step, the discharge water obtained after testing after, water quality the results are shown in Table 4.
Table 4
Embodiment 3:
The process of the stainless-steel cold-rolling acid waste water of certain stainless steel factory, day quantity discharged be 5000 tons.Wherein, the water quality situation of the stainless-steel cold-rolling acid waste water of this stainless steel factory is as table 5.
Table 5
Now as follows the stainless-steel cold-rolling acid waste water of this electroplating facility is processed:
After the slagging-off of stainless-steel cold-rolling acid waste water and oil removing, obtain the first pre-treatment stainless-steel cold-rolling acid waste water.
By carrying out stainless-steel cold-rolling acid waste water, except Slag treatment, foreign material larger for volume in stainless-steel cold-rolling acid waste water being removed.
Stainless-steel cold-rolling acid waste water after slagging-off is passed into grease removal tank, by stainless-steel cold-rolling acid waste water after leave standstill 3h after grease removal tank, controlling temperature in grease removal tank is 40 DEG C, the oil slick in stainless-steel cold-rolling acid waste water and the larger oil in water emulsion of particle is made to rise to surface, after collecting surperficial oil reservoir, stainless-steel cold-rolling acid waste water is passed into air flotation pool, by dissolved air flotation process, the oil in water emulsion in removing stainless-steel cold-rolling acid waste water.
First pre-treatment stainless-steel cold-rolling acid waste water is carried out reduction treatment, obtains the second pre-treatment stainless-steel cold-rolling acid waste water.
In the first pre-treatment stainless-steel cold-rolling acid waste water, add concentration is 0.05-5% sulfuric acid, after regulating pH to 3.0, adding concentration toward it is again 10%wt (massfraction) S-WAT, make the ORP value of the cold rolling acid waste water of chromium stainless steel for 280mV, 30min after abundant stirring, makes hexavalent chrome reduction become trivalent chromium.
After second pre-treatment stainless-steel cold-rolling acid waste water is carried out one-level aeration neutralizing treatment, obtain the 3rd pre-treatment stainless-steel cold-rolling acid waste water.
Adding particle diameter toward the second pre-treatment stainless-steel cold-rolling acid waste water is 0.5mm ~ 3mm limestone particle, and gives Air Exposure, and aeration intensity is: 2m
3(air)/m
3(the second pre-treatment stainless-steel cold-rolling acid waste water) h, by the pH regulator to 4.0 of the second pre-treatment cold rolling wastewater, obtains the 3rd pre-treatment stainless-steel cold-rolling acid waste water.
3rd pre-treatment stainless-steel cold-rolling acid waste water carried out in secondary and after Air Exposure, obtain the 4th pre-treatment stainless-steel cold-rolling acid waste water.
The milk of lime that concentration is 5% is added in the 3rd pre-treatment stainless-steel cold-rolling acid waste water, and continue aeration, along with the lasting dropping of milk of lime, the throw out of the 3rd pre-treatment stainless-steel cold-rolling acid waste water continues to increase and becomes reddish-brown, after the pH regulator to 9.5 of the 3rd pre-treatment stainless-steel cold-rolling acid waste water, continue aeration 10 minutes, e.g., aeration intensity is 8m
3(air)/m
3(the 3rd pre-treatment stainless-steel cold-rolling acid waste water) h, makes the Fe in the 3rd pre-treatment stainless-steel cold-rolling acid waste water
2+fe is oxidized under the effect of oxygen
3+, and form CaF
2, Fe (OH)
3, Ni (OH)
2, Cr (OH)
3and CaSO
4throw out, obtains the 4th pre-treatment stainless-steel cold-rolling acid waste water.
After being carried out by 4th pre-treatment stainless-steel cold-rolling acid waste water flocculating and precipitate, obtain the 4th pre-treatment stainless-steel cold-rolling acid waste water and the first pre-treatment bed mud.
In the 4th stainless-steel cold-rolling acid waste water, add polymerize aluminum chloride (PAC) is flocculation agent, dosage is 1 ‰ ~ 5 ‰ (thousandths) of the 4th pre-treatment stainless-steel cold-rolling acid waste water volume, after stirring 15min, adding polyacrylamide (PAM) is coagulant aids, and its dosage is 0.1 ‰ of the 4th pre-treatment stainless-steel cold-rolling acid waste water volume.After flocculation, the 4th pre-treatment stainless-steel cold-rolling acid waste water is carried out deposition and leave standstill, heavy metal ion is precipitated completely with the form of oxyhydroxide.Such as, the 4th pre-treatment stainless-steel cold-rolling acid waste water after flocculation is passed into sedimentation tank, and heavy metal ion in the basic conditions, is deposited into the bottom of settling bath with the form of oxyhydroxide.Time of repose is 1h ~ 2h.
By the 5th pre-treatment stainless-steel cold-rolling acid waste water through three grades of neutralizations and after filtering, outer row.
In the 5th pre-treatment stainless-steel cold-rolling acid waste water, add acid, regulate pH to 6.5 ~ 7.2, and filter, by suspended substance removal, reduce its turbidity, make to reach emission standard.
After first pre-treatment bed mud being carried out concentrated and press filtration, obtain the 6th pre-treatment stainless-steel cold-rolling acid waste water and the second pre-treatment bed mud.
The the first pre-treatment bed mud produced is concentrated to concentration basin by sludge pump positive delivery, in the first pre-treatment bed mud, adds PAM with auxiliary mud-water separation.By the first pre-treatment bed mud extracting being carried out pressure rate to pressure filter with pump, the 6th pre-treatment stainless-steel cold-rolling acid waste water obtained flows out under gravity, and the water ratio of the second pre-treatment bed mud after press filtration is less than 35%.
By the 6th pre-treatment stainless-steel cold-rolling acid waste water after precipitation, three grades of neutralizations and filtration, outer row.
The 6th pre-treatment stainless-steel cold-rolling acid waste water after press filtration is back to settling tank and carries out precipitation process, acid is added in the 6th pre-treatment stainless-steel cold-rolling acid waste water after precipitation process, regulate pH to 6.5 ~ 7.2, and filter, by suspended substance removal, reduce its turbidity, guarantee to reach emission standard.
After above-mentioned treatment step, the discharge water obtained after testing after, water quality the results are shown in Table 6.
Table 6
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. a stainless-steel cold-rolling acid waste water treatment unit, it is characterized in that, comprise wastewater storage tank, grease removal tank, except chromium groove, the first neutralization tank, the second neutralization tank, flocculation basin, settling tank, concentration basin, storage basin, press filtration pond, backflow pool, the 3rd neutralization tank and filter vat;
Described wastewater storage tank is communicated with described grease removal tank, described grease removal tank is communicated with the described chromium groove that removes, described first neutralization tank is communicated with the described chromium groove that removes, described second neutralization tank is communicated with described first neutralization tank, described flocculation basin is communicated with described second neutralization tank, described settling tank is communicated with described flocculation basin and described concentration basin respectively, described storage basin is communicated with described concentration basin, described press filtration pond is communicated with described storage basin, described backflow pool is communicated with described press filtration pond and described settling tank respectively, described 3rd neutralization tank is communicated with described settling tank, described filter vat is communicated with described 3rd neutralization tank,
Described first neutralization tank is provided with aerating apparatus and chemicals dosing plant, is respectively used to pass into air and add alkaline matter.
2. stainless-steel cold-rolling acid waste water treatment unit according to claim 1, is characterized in that, described aerating apparatus is many aeration tubes.
3. stainless-steel cold-rolling acid waste water treatment unit according to claim 2, is characterized in that, many described aeration tubes are arranged in array.
4. stainless-steel cold-rolling acid waste water treatment unit according to claim 3, is characterized in that, the many rectangular array arrangements of described aeration tube.
5. stainless-steel cold-rolling acid waste water treatment unit according to claim 1, it is characterized in that, aeration tube described in each arranges multiple production well.
6. stainless-steel cold-rolling acid waste water treatment unit according to claim 1, is characterized in that, production well described in each is arranged at described first neutralization tank.
7. stainless-steel cold-rolling acid waste water treatment unit according to claim 1, it is characterized in that, described grease removal tank is provided with vapour pipe.
8. stainless-steel cold-rolling acid waste water treatment unit according to claim 1, is characterized in that, be provided with central transmission concentrator in described concentration basin.
9. stainless-steel cold-rolling acid waste water treatment unit according to claim 1, is characterized in that, is provided with plate-and-frame filter press in described press filtration pond.
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104310652A (en) * | 2014-10-28 | 2015-01-28 | 温玉友 | Stainless steel cold-rolled acidic wastewater treatment device and method |
| CN104787928A (en) * | 2015-04-16 | 2015-07-22 | 南阳师范学院 | Recovery processing method of stainless steel acid pickling waste liquid containing iron, chromium and nickel |
| CN105834194A (en) * | 2016-04-18 | 2016-08-10 | 青海洁神环境能源产业有限公司 | Waste treatment system as well as treatment method and application thereof |
| CN104310652B (en) * | 2014-10-28 | 2017-01-04 | 温玉友 | Stainless-steel cold-rolling process for treating acidic waste water |
| CN106745960A (en) * | 2016-11-25 | 2017-05-31 | 江苏省沙钢钢铁研究院有限公司 | A kind of method for making steel refining dedusting ash comprehensive utilization |
| CN109851110A (en) * | 2018-12-20 | 2019-06-07 | 安徽楚江特钢有限公司 | A kind of steel band pickling waste waters processing method |
-
2014
- 2014-10-28 CN CN201420634392.2U patent/CN204224358U/en not_active Expired - Fee Related
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104310652A (en) * | 2014-10-28 | 2015-01-28 | 温玉友 | Stainless steel cold-rolled acidic wastewater treatment device and method |
| CN104310652B (en) * | 2014-10-28 | 2017-01-04 | 温玉友 | Stainless-steel cold-rolling process for treating acidic waste water |
| CN104787928A (en) * | 2015-04-16 | 2015-07-22 | 南阳师范学院 | Recovery processing method of stainless steel acid pickling waste liquid containing iron, chromium and nickel |
| CN104787928B (en) * | 2015-04-16 | 2016-10-05 | 南阳师范学院 | A kind of iron content, chromium, the recovery and treatment method of nickel and stainless steel pickle liquor |
| CN105834194A (en) * | 2016-04-18 | 2016-08-10 | 青海洁神环境能源产业有限公司 | Waste treatment system as well as treatment method and application thereof |
| CN106745960A (en) * | 2016-11-25 | 2017-05-31 | 江苏省沙钢钢铁研究院有限公司 | A kind of method for making steel refining dedusting ash comprehensive utilization |
| CN109851110A (en) * | 2018-12-20 | 2019-06-07 | 安徽楚江特钢有限公司 | A kind of steel band pickling waste waters processing method |
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