CN1296920A - Process for high-quality treatment of waste dyeing water with waste solution of ferrous sulfate or ferrous chloride - Google Patents
Process for high-quality treatment of waste dyeing water with waste solution of ferrous sulfate or ferrous chloride Download PDFInfo
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- CN1296920A CN1296920A CN 00135440 CN00135440A CN1296920A CN 1296920 A CN1296920 A CN 1296920A CN 00135440 CN00135440 CN 00135440 CN 00135440 A CN00135440 A CN 00135440A CN 1296920 A CN1296920 A CN 1296920A
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Abstract
A process for treating the printing and dyeing sewage with the waste solution of ferrous sulfate or ferrous chloride includes adding polar medium to said printing and dyeing sewage to change its ionicity, treating with waste solution of FeSO4 or FeCl2, mixing the treated water with the untreated sewage in ratio of 1:(1-2), neutralizing by regulating pH value, coagutation and solid-liquid separation. Its advantages are decreasing COD by over 50%, decolouring by 70-90%, saving cost by 30% and use of waste.
Description
The present invention relates to use FeSO
4Or FeCl
2The waste liquid high-quality is handled the method for waste water, especially treatment of dyeing and printing, belongs to the wastewater processing technology category.
The physico-chemical process of dyeing waste water is handled most water purification agents that use, and impels that some compositions and water purification agent in the waste water adsorbs, aggregation, produces coagulative precipitation, through after the solid-liquid separation, makes waste water obtain effective improvement.At present, domestic water purification agent is various in style, and the price comparison that has is expensive.China produces 3,000,000 tons of dyeing waste waters every day approximately, and the annual thus consumption hundreds of thousands of ton water purification agent that needs is worth at several hundred million yuans.FeSO
4, FeCl
2Waste liquid is commonly called as and turns over the cylinder tank liquor, is the large pollutent after metal acid is handled.Because of it contains very abundant Fe
2+Ion, being used for wastewater treatment has very tempting prospect, but because of it does not have functions such as adsorption bridging, hydrogen bond association, detergent power is lower, and water outlet is often blushing, and people have to abandon use.And FeSO
4, FeCl
2The method of comprehensive utilization of waste liquid is few, and the method that has is the demand of incompatibility medium-sized and small enterprises production also, most FeSO
4, FeCl
2Waste liquid all falls as wastewater treatment, and this has not only wasted resource, but also must consume a large amount of manpower and materials, is that the strategy of sustainable development carried out energetically with us is contrary.The waste water that forms in the industrial production, especially dyeing waste water, some supplementary material material or intermediate product such as dyestuff, auxiliary agent etc. can be dissolved in water, form molecular solution, claim true solution again, and its intractability is just bigger.In the past if use FeSO
4Or FeCl
2Waste liquid is handled it, and not only consumption is big, and COD clearance and decolorizing effect are all lower, and water outlet is often blushing, is difficult to widespread use.
The objective of the invention is to propose a kind of FeSO of using
4Or FeCl
2The waste liquid high-quality is handled the especially method of dyeing waste water of waste water.It is exactly to add polarizable medium such as CuSO in the dyeing waste water that so-called high-quality is handled
4And auxiliary material, transfer pH value again, change the degree of ionization of dyeing waste water, impel Fe
2+Reactions such as the dispersion particle in ion and the molecular solution adsorbs, complexing form baroque macromole complex compound, have reduced water-solublely, and have colloidal character, Ca afterwards (OH)
2In the N-process, because Fe
2+Ionic absorption complexing action, Cu
2+The strong polarized action of ionic, the cohesion of auxiliary material, formation precipitates and obtains removing.Practice shows, above-mentioned upper clear supernate after primary treatment is called for short treatment solution, down together, except that the discharging that can directly neutralize, also can be mixed mutually with certain proportion with undressed raw wastewater, again through Ca (OH)
2Adjust after the pH value, formation precipitates and obtains removing, and reaching further is mixed handles the effect of raw wastewater.
The inventive method content is described in detail as follows:
One, used supplementary material
1,95% sulfuric acid: commercially available, technical grade.
2,60 order white carbon blacks: commercially available, proportion 2.0 contains SiO
280～85%, specific surface area 160m
2/ g, white particle is insoluble to acidity or slightly acidic waste water.
3,60 order granulated active carbons: commercially available, proportion about 1.3, specific surface area 800m
2About/g, make with wood charcoal powder, tar, pitch.
4,5%CuSO
4Liquid: add the clear water preparation with commercially available solid sulphuric acid copper, about PH3.
5,10%Ca (OH)
2Liquid: add clear water preparation, PH14 with commercially available dry lime.
6, FeSO
4Waste liquid: from certain seamless steel tubing mill, proportion is about about 1.18, FeSO
4Content 170～220g/l, H
2SO
4Content 150～180g/l talks green or yellow-green liquid.
7, FeCl
2Waste liquid: from certain cold-rolled steel factory, proportion is about about 1.10, FeCl
2Content 110～130g/l, HCl content 30～40g/l, grass green or yellow-green liquid.
8, dyeing waste water: from each printing and dyeing mill.
Two, treatment process
1, auxiliary material is made
Ready white carbon black and granulated active carbon are measured in 1: 1.1～1.15 (w/w) ratio, drop in the beaker and mix and stir, use dyeing waste water wetting then, stir into half wet shape, be auxiliary material.
2, the treatment process of dyeing waste water
Proportioning (w/w) is an example with the batch process
100 parts of waste water
FeSO
4Or FeCl
20.3～0.6 part of waste liquid
5%CuSO
40.06～0.08 part
20～35 parts of auxiliary materials
Get the dyeing waste water of some amount, add FeSO by proportioning
4Or FeCl
2Waste liquid and 5%CuSO
4Liquid adds auxiliary material again, mixes together, uses H again
2SO
4Transfer pH value to 4～5.5, artificial or mechanical stirring 15 minutes.Moments later static, take out the top mixed solution, promptly treatment solution is used 10%Ca (OH)
2Transfer pH value 7～11, coagulative precipitation, solid-liquid separation, its supernatant liquor can discharge or enter biochemical treatment.
3, the treatment process that further is mixed
Above-mentioned gained treatment solution and undressed former dyeing waste water are mixed in the ratio of 1: 1～2 (w/w) again, use 10%Ca (OH) after the stirring again
2PH value 7～11 is transferred in neutralization, coagulative precipitation, and solid-liquid separation, its supernatant liquor can discharge or enter biochemical treatment.
Above technological process is carried out at normal temperatures and pressures, can periodical operation, also can carry out continuously.The auxiliary material that is deposited in the treating pond bottom can give over to handle next time and continue to use, and needn't regenerate.After operation for some time, suitably replenish and get final product.
Advantage of the present invention is, process using is added polarizable medium and changed principle such as waste water degree of ionization, and the design philosophy science is rationally advanced, creative, whole COD removal 〉=50%, and percent of decolourization 70～90%, and also water outlet is not blushing.Reduce cost for wastewater treatment about 30%.Be FeSO
4Or FeCl
2Waste liquid is widely used in the processing of dyeing waste water and has created condition, also is suitable for the processing of other solution state waste water that come true.Implement the inventive method, can not only produce good benefits in environment, and can the treatment of wastes with processes of wastes against one another create the economic worth of tens million of units, its meaning is fairly obvious.
Embodiment 1
Dyeing waste water is from Xishan city beam letter silk printing and dyeing mill, and dye vat waste water adds the dilution of part clear water, is dark livid purple look.Dyestuff is based on matching stain, and active, dispersed dye take second place.Waste water pH value 10.5, COD5295mg/l, 1400 times of colourities.
Get 300g waste water in the 500ml beaker, add 1.5gFeSO
4Waste liquid and 0.2gCuSO
4Liquid, the auxiliary material add-on is 75g, uses H after mixing again
2SO
4Transfer PH4.2, continuously stirring 15 minutes after static 2～3 minutes, is taken out the top treatment solution, makes neutralizing treatment respectively and the processing that is mixed.Test result such as following table.Things such as the auxiliary material that stays in the beaker are equipped with the usefulness of doing test next time, do not need manipulation of regeneration, and follow-up test technology is the same.
Table 1, treatment solution add 10%Ca (OH)
2The liquid neutralization precipitation
| PH value | Supernatant liquor (CODmg/l) | COD clearance (%) | Supernatant liquor colourity (doubly) | Chroma removal rate (%) |
| ????8.8 | ????2275 | ????57.0 | ????70 | ????＞90 |
| ????7.8 | ????1896 | ????64.2 | ????60 | ????＞90 |
| ????8.0 | ????2198 | ????58.5 | ????70 | ????＞90 |
| ???10.0 | ????2160 | ????59.2 | ????60 | ????＞90 |
Table 2, the result that is mixed (treatment solution is 1, (w/w))
| Mixed ratio | PH value | Supernatant liquor (CODmg/l) | COD clearance (%) | Supernatant liquor colourity (doubly) | Chroma removal rate (%) |
| ????1∶1 | ????7.6 | ????2180 | ????58.8 | ????100 | ????＞90 |
| ????1∶1 | ????8.1 | ????2246 | ????57.6 | ????100 | ????＞90 |
| ????1∶2 | ????9.0 | ????2414 | ????54.4 | ????150 | ????89.3 |
| ????1∶2 | ???10.7 | ????2444 | ????53.8 | ????170 | ????87.9 |
Embodiment 2
Dyeing waste water is from Changshu City first and second printing and dyeing mills of company, and cotton dyes, and active, dispersed dye are main, and cationic dyestuff takes second place.Waste water pH value 7.2 is brown, COD856mg/l, 340 times of colourities.
Get the 300g dyeing waste water in the 500ml of example 1 beaker, add FeCl
2Waste liquid 1.5g, CuSO
4Liquid 0.2g, auxiliary material reside in the beaker after example 1 is implemented.Use H again
2SO
4Transfer pH value to 4.0.All the other operations are identical with embodiment 1.Wastewater treatment liquid neutralization be mixed test result such as following table.
| Mixed ratio | PH value | Supernatant liquor (CODmg/l) | COD clearance (%) | Supernatant liquor colourity (doubly) | Chroma removal rate (%) |
| ????1∶0 | ?7.8 | ????241 | ????71.8 | ????＜10 | ????＞90 |
| ????1∶0 | ?8.1 | ????268 | ????68.7 | ????＜10 | ????＞90 |
| ????1∶1 | ?9.0 | ????363 | ????57.6 | ????45 | ????86.7 |
| ????1∶1 | ?9.6 | ????380 | ????55.6 | ????50 | ????85.3 |
| ????1∶2 | ?10.0 | ????405 | ????52.7 | ????80 | ????76.5 |
| ????1∶2 | ?8.7 | ????412 | ????51.9 | ????78 | ????77 |
Annotate: mixed ratio expression in 1: 0 treatment solution directly adds 10%Ca (OH)
2Neutralization precipitation.Down together.
Embodiment 3
Dyeing waste water is from the modish dyeing and finishing of Wuxi City factory, and chemical fibre dyeing uses weak acid dye to be the master, and dispersed dye take second place.Waste water is Steel Gray, PH7.0, COD408mg/l, 200 times of colourities.
Get 300g waste water in the 500ml of example 2 beaker, use FeSO
4Liquid waste disposal adds 1.2g, CuSO
4Liquid 0.18g, auxiliary material are that example 2 is retained.Use H after the stirring again
2SO
4Transfer pH value to 4.2, other operating process are identical with example 1.The neutralization precipitation of wastewater treatment liquid and be mixed test result such as following table.
| Mixed ratio | PH value | Supernatant liquor (CODmg/l) | COD clearance (%) | Supernatant liquor colourity (doubly) | Chroma removal rate (%) |
| ????1∶0 | ????7.8 | ????115 | ????71.8 | ????＜10 | ????＞90 |
| ????1∶0 | ????8.2 | ????118 | ????71.1 | ????＜10 | ????＞90 |
| ????1∶1 | ????9.1 | ????130 | ????68.1 | ????45 | ????77.5 |
| ????1∶1 | ????9.6 | ????125 | ????69.4 | ????50 | ????75 |
| ????1∶2 | ????8.5 | ????200 | ????51 | ????56 | ????72 |
| ????1∶2 | ????8.7 | ????197 | ????51.7 | ????60 | ????70 |
Embodiment 4
Waste water is the close fermentation system yeast wastewater of Zhuhai factory sugar.Waste water is the muddy shape of dark brown brown, acid smell is arranged, PH5.6, COD13585mg/l, 1380 times of colourities.Test is used FeSO in the 500ml of example 3 beaker
4Liquid waste disposal, FeSO
4Liquid and CuSO
4Liquid dosage and operation are with example 1.Treatment solution test result such as following table.
| PH value | Supernatant liquor (CODmg/l) | COD clearance (%) | Supernatant liquor colourity (doubly) | Chroma removal rate (%) |
| ?11.0 | ????3600 | ????73.5 | ????210 | ????84.8 |
| ?11.0 | ????4099 | ????69.8 | ????310 | ????77.5 |
| ?10.5 | ????4300 | ????68.3 | ????340 | ????75.3 |
Claims (7)
1, a kind of method with ferrous sulfate or ferrous chloride waste fluid treatment of dyeing and printing, feature of the present invention are to add the FeSO of some amount in dyeing waste water
4Or FeCl
2Behind the waste liquid, also must add the polarizable medium CuSO of some amount
4Liquid and auxiliary material are used H again
2SO
4Transfer pH value to 4～5.5 to change the degree of ionization of dyeing waste waters, stirred 15 minutes, static a moment, the top mixed solution, i.e. treatment solution, after neutralizing, coagulative precipitation, the supernatant liquor after the solid-liquid separation can directly discharge or enter biochemical treatment; All right and the raw wastewater of this treatment solution, two kinds of waste water are mixed mutually with certain proportion, after neutralization, coagulative precipitation, the supernatant liquor after the solid-liquid separation can directly discharge or enter biochemical treatment, whole COD removal 〉=50%, chroma removal rate 70～90%, water outlet is not blushing, and above-mentioned technology is carried out at normal temperatures and pressures.
2, in accordance with the method for claim 1, it is characterized in that used FeSO
4Or FeCl
2Waste liquid is to turn over the cylinder tank liquor after metal acid is handled; FeSO
4Waste liquid: be light green or yellow-green liquid, proportion is about 1.18, contains FeSO
4170～220g/l contains H
2SO
4150～180g/l; FeCl
2Waste liquid: grass green or yellow-green liquid, proportion is about 1.1, contains FeCl
2110～130g/l contains HCl30～40g/l; FeSO
4Or FeCl
2The consumption of waste liquid is 0.3～0.6% (w/w) of dyeing waste water amount.
3, in accordance with the method for claim 1, it is characterized in that used CuSO
4Liquid is to add clear water with commercially available solid sulphuric acid copper to be mixed with 5%CuSO
4Solution, consumption are 0.06～0.08% (w/w) of dyeing waste water.
4, in accordance with the method for claim 1; it is characterized in that the composition of used auxiliary material and require to form by 1: 1.1～1.15 (w/w) by 60 order white carbon blacks and 60 order granulated active carbons; both mix and stir in mixing; wetting with dyeing waste water; stir into half wet shape, be auxiliary material, intermittent type treatment process supplementary product consumption is 25～35% (w/w) of dyeing waste water amount; after operation for some time, suitably replenished.
5, in accordance with the method for claim 1, it is characterized in that two kinds of waste water are mixed, the mixed ratio of treatment solution and undressed former dyeing waste water is 1: 1～2 (w/w).
6, in accordance with the method for claim 1, it is characterized by after the wastewater treatment with 10%Ca (OH)
2In the liquid and transfer pH value 7-11, through coagulative precipitation, solid-liquid separation, its supernatant liquor can discharge or enter biochemical treatment.
7, in accordance with the method for claim 1, it is characterized by the wastewater treatment that also is suitable for other solution states that come true.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 00135440 CN1212978C (en) | 2000-12-21 | 2000-12-21 | Process for high-quality treatment of waste dyeing water with waste solution of ferrous sulfate or ferrous chloride |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 00135440 CN1212978C (en) | 2000-12-21 | 2000-12-21 | Process for high-quality treatment of waste dyeing water with waste solution of ferrous sulfate or ferrous chloride |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1296920A true CN1296920A (en) | 2001-05-30 |
| CN1212978C CN1212978C (en) | 2005-08-03 |
Family
ID=4596712
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 00135440 Expired - Fee Related CN1212978C (en) | 2000-12-21 | 2000-12-21 | Process for high-quality treatment of waste dyeing water with waste solution of ferrous sulfate or ferrous chloride |
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|---|---|
| CN (1) | CN1212978C (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1300009C (en) * | 2003-01-27 | 2007-02-14 | 费兴祖 | Physical and chemical dyeing and printing effluent treating process throwing no coagulant and the prepn of supplementary material used |
| CN101717111B (en) * | 2008-10-09 | 2012-01-11 | 广州康瑞德生物技术股份有限公司 | Method for producing feed-grade bluestone by using cupreous etching waste liquor of circuit board |
| CN103464174A (en) * | 2012-06-08 | 2013-12-25 | 中国石油化工股份有限公司 | Preparation method for FeSO4 catalyst used for postprocessing of biochemical waste water of aniline and nitrobenzene |
| CN110078184A (en) * | 2019-05-11 | 2019-08-02 | 中铁二十一局集团第六工程有限公司 | Patina/active carbon compound coagulant preparation method and be used for tunnel sewage treatment |
-
2000
- 2000-12-21 CN CN 00135440 patent/CN1212978C/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1300009C (en) * | 2003-01-27 | 2007-02-14 | 费兴祖 | Physical and chemical dyeing and printing effluent treating process throwing no coagulant and the prepn of supplementary material used |
| CN101717111B (en) * | 2008-10-09 | 2012-01-11 | 广州康瑞德生物技术股份有限公司 | Method for producing feed-grade bluestone by using cupreous etching waste liquor of circuit board |
| CN103464174A (en) * | 2012-06-08 | 2013-12-25 | 中国石油化工股份有限公司 | Preparation method for FeSO4 catalyst used for postprocessing of biochemical waste water of aniline and nitrobenzene |
| CN110078184A (en) * | 2019-05-11 | 2019-08-02 | 中铁二十一局集团第六工程有限公司 | Patina/active carbon compound coagulant preparation method and be used for tunnel sewage treatment |
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| Publication number | Publication date |
|---|---|
| CN1212978C (en) | 2005-08-03 |
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|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| EE01 | Entry into force of recordation of patent licensing contract |
Assignee: Wuxi Xingyi Coating Environmental Protection Equipment Co., Ltd. Assignor: Fei Xingzu Contract fulfillment period: 2006.2.15 to 2020.12.21 contract change Contract record no.: 2008320000096 Denomination of invention: Process for high-quality treatment of waste dyeing water with waste solution of ferrous sulfate or ferrous chloride Granted publication date: 20050803 License type: Exclusive license Record date: 2008.8.19 |
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| LIC | Patent licence contract for exploitation submitted for record |
Free format text: EXCLUSIVE LICENCE; TIME LIMIT OF IMPLEMENTING CONTACT: 2006.2.15 TO 2020.12.21 Name of requester: NONE WUXI XINGYI PAINTING ENVIRONMENTAL PROTECTION Effective date: 20080819 |
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