CN106277262A - A kind of environmental protection air supporting synergist for treatment of dyeing wastewater - Google Patents

A kind of environmental protection air supporting synergist for treatment of dyeing wastewater Download PDF

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Publication number
CN106277262A
CN106277262A CN201610718672.5A CN201610718672A CN106277262A CN 106277262 A CN106277262 A CN 106277262A CN 201610718672 A CN201610718672 A CN 201610718672A CN 106277262 A CN106277262 A CN 106277262A
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CN
China
Prior art keywords
parts
agent
air supporting
synergist
treatment
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN201610718672.5A
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Chinese (zh)
Inventor
任松洁
林伟青
徐贝
李伟
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Zhejiang Zhengjie Environmental Science And Technology Co Ltd
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Zhejiang Zhengjie Environmental Science And Technology Co Ltd
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Application filed by Zhejiang Zhengjie Environmental Science And Technology Co Ltd filed Critical Zhejiang Zhengjie Environmental Science And Technology Co Ltd
Priority to CN201610718672.5A priority Critical patent/CN106277262A/en
Publication of CN106277262A publication Critical patent/CN106277262A/en
Pending legal-status Critical Current

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    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/52Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
    • C02F1/54Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using organic material
    • C02F1/56Macromolecular compounds
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/24Treatment of water, waste water, or sewage by flotation

Abstract

The invention discloses a kind of environmental protection air supporting synergist for treatment of dyeing wastewater, including the A agent 10 in terms of parts by weight~50 parts and B agent 50~90 parts, described A agent and B agent are formed by following parts by weight preparation of raw material respectively: A agent component is: dodecyl sodium sulfate 10~40 parts, α sodium olefin sulfonate 40~70 parts and glycine betaine 20~50 parts;B agent component is: inorganic villaumite 10~40 parts and mineral sulfates 60~80 parts;Described inorganic villaumite is one or both combination in KCl and NaCl;Described mineral sulfates is K2SO4And Na2SO4In one or both combination.

Description

A kind of environmental protection air supporting synergist for treatment of dyeing wastewater
Technical field
The present invention relates to a kind of environmental protection air supporting synergist for treatment of dyeing wastewater, belong to waste water in environmental conservation and process The field of waste water treatment in field, especially dyeing.
Background technology
Air supporting is one of the most conventional water technology, as a kind of quick, efficient, solid-liquid separation skill of low energy consumption Art, is not only suitable for the water purification that feeds water, is applicable to again the process of various wastewater, particularly to separating miscellaneous close to water of some proportions Matter is more superior than general settling methods.Pneumatically supported principle is to produce substantial amounts of fine gas bubbles in water, at interfacial tension, bubble Under the common effect of the many kinds of forces such as rising buoyancy and hydrostatic pressure difference, micro air bubble is promoted to stick to removed impurity particle On, because adherend density floats to the water surface, so that impurities in water is separated removal less than water.
Dyeing waste water contains the granule of a large amount of different-grain diameters, including clay, antibacterial, virus, humic acid and protein Deng.Commonly used air supporting method in printing-dyeing waste water treatment process at present, and its design has because water quality situation is different with field condition Distinguished, be divided into the air supporting used by pretreatment and the air supporting used by end advanced treating after biochemistry before biochemistry.Both air supporting Waste water in pond all contains the float of multiple different-grain diameter, and major part can use air supporting method to remove, but some because of The bigger removal efficiency of proportion low (this is also the major reason causing air flotation effect the best).
The principal element of decision air flotation effect is the character of the fine gas bubbles in water, only small at acquisition diameter, density Greatly, in the case of the good a large amount of fine gas bubbles of uniformity, just can obtain good air flotation effect, reason is:
1, bubble is little, and floating speed is fast, and the disturbance to water body is little, will not crash wadding grain, and can increase bubble and wadding grain collision Probability.But not bubble is the thinnest more good, and bubble is meticulous to be affected ascent rate and increase size and the cost of flotation tank;
2, bubble diameter is the least, and in bubble, suffered additional pressure is the biggest, the interior collision probability to air molecule to bubble chamber film of bubble The most, the most violent.Therefore to obtain stable fine bubble, air bubble intensity to ensure;
3, the number of contained microbubble in bubble density, i.e. unit volume outgassing water, determines bubble and the collision that suspends Probability, density is the biggest, and collision probability is the biggest;
4, the uniformity of bubble, diameter difference and minor diameter bubble including largest air bubbles with minimum bubble account for bubble total amount ratio Example, increasing of air pocket can reduce daf efficiency.
The research improving treatment of dyeing wastewater solid-liquid separation effect at present is concentrated mainly on the improvement to bubble generator On, these achieve preferable effect, but often add more processing cost.The method improving solid-liquid separation effect is also wrapped Include by adjusting the method that flocculant interpolation kind makes the flco proportion of generation reduce, as changed Ferric Salt Flocculants into PAC, PAM Flocculant etc..Increase bubbles volume in addition with the surfactant adding a small amount of single kind, thus improve solid-liquid separation efficiency Method.But the surfactant adding single kind is not easily controlled Air Bubble Size, density and uniformity, if add Surfactant is not suitable for, and even can reduce air flotation effect.
Summary of the invention
For solving deficiency of the prior art, present invention aim at providing a kind of compound, low cost, nontoxic, efficient Air supporting synergist, there is the generation amount dramatically increasing micro-bubble and the effect of stability, uniformity improving micro-bubble, Water can be obviously enhanced process, the especially air flotation effect in printing-dyeing waste water treatment process and efficiency.
For achieving the above object, the technical scheme is that a kind of environmental protection air supporting potentiation for treatment of dyeing wastewater Agent, including the A agent 10 in terms of parts by weight~50 parts and B agent 50~90 parts, described A agent and B agent are respectively by following parts by weight Preparation of raw material forms:
A agent component is: dodecyl sodium sulfate 10~40 parts, α-sodium olefin sulfonate 40~70 parts and glycine betaine 20~50 Part;
B agent component is: inorganic villaumite 10~40 parts and mineral sulfates 60~80 parts;
Described inorganic villaumite is one or both combination in KCl and NaCl;Described mineral sulfates is K2SO4With Na2SO4In one or both combination.
As preferably, described A agent component is: dodecyl sodium sulfate 20~40 parts, α-sodium olefin sulfonate 40~60 parts With glycine betaine 20~30 parts;B agent component is: KCl 10~40 parts, Na2SO460~80 parts;Described A agent is 40 parts, and B agent is 60 Part.
As preferably, described A agent component is: dodecyl sodium sulfate 25~35 parts, α-sodium olefin sulfonate 45~55 parts With glycine betaine 20~25 parts;B agent component is: NaCl 30 parts, Na2SO470 parts;Described A agent is 30 parts, and B agent is 70 parts.
As preferably, described A agent component is: dodecyl sodium sulfate 30 parts, α-sodium olefin sulfonate 50 parts and glycine betaine 20 parts;B agent component is: NaCl30 part, Na2SO4With K2SO470 parts of mixture, wherein Na2SO4With K2SO4Ratio be 1:1; Described A agent is 25 parts, and B agent is 75 parts.
Beneficial effects of the present invention: the surfactant that A agent is compounding surfactant, relatively single kind of the present invention Effect is more preferable, addition is few, can not only improve the foam performance of waste water, moreover it is possible to change the surface activity of suspended particles in water body. The B agent of this invention is made up of inorganic salt, and it adds the effect of the water quality that can regulate foamed solution, makes surface tension further Reduce, reduce the addition of A agent.
Detailed description of the invention
Embodiment 1.
Certain dye house effluents treating stations have employed air supporting and makees pretreatment, and flocculation medicament uses PAC and PAM, added 40 parts of A Agent and 60 parts of B agent compositions:
A agent component is: 20 parts of dodecyl sodium sulfates, 50 parts of α-sodium olefin sulfonates and 30 parts of glycine betaines;
B agent component is: 30 parts of KCl and 70 parts of Na2SO4
Compared with not adding air supporting synergist, solid-liquid separation effect dramatically increases, and COD clearance increases from 25% 50%, float (SS) clearance increases 75% from 60%, and chroma removal rate adds 5% simultaneously.
Embodiment 2.
In embodiment 1, dye house effluents treating stations have employed air supporting and makees pretreatment, and flocculation medicament uses PAC and PAM, adds 30 parts of A agent and 70 parts of B agent compositions:
A agent component is: 35 parts of dodecyl sodium sulfates, 45 parts of α-sodium olefin sulfonates and 20 parts of glycine betaines;
B agent component is: 30 parts of NaCl and 70 parts of Na2SO4
Compared with not adding air supporting synergist, solid-liquid separation effect dramatically increases, and COD clearance increases from 25% 55%, float (SS) clearance increases 80% from 60%, and chroma removal rate adds 8% simultaneously.
Embodiment 3.
In embodiment 1, dye house effluents treating stations have employed air supporting and makees pretreatment, and flocculation medicament uses PAC and PAM, adds 25 parts of A agent and 75 parts of B agent compositions:
A agent component is: 30 parts of dodecyl sodium sulfates, 50 parts of α-sodium olefin sulfonates and 20 parts of glycine betaines;
B agent component is: B agent component is: 30 parts of NaCl, 70 parts of Na2SO4With K2SO4Mixture, wherein Na2SO4With K2SO4 Ratio be 1:1.
Compared with not adding air supporting synergist, solid-liquid separation effect dramatically increases, and COD clearance increases from 25% 58%, float (SS) clearance increases 83% from 60%, and chroma removal rate adds 10% simultaneously.
Embodiment 4.
Certain dye house effluents treating stations have employed air supporting and makees pretreatment, and flocculation medicament uses PAC and decolorising agent, added 25 Part A agent and 75 parts of B agent compositions:
A agent component is: 30 parts of dodecyl sodium sulfates, 50 parts of α-sodium olefin sulfonates and 20 parts of glycine betaines;
B agent component is: 30 parts of NaCl, 70 parts of Na2SO4With K2SO4Mixture, wherein Na2SO4With K2SO4Ratio be 1: 1。
Compared with not adding air supporting synergist, solid-liquid separation effect dramatically increases, and COD clearance increases from 30% 60%, float (SS) clearance increases 85% from 70%, and chroma removal rate adds 40% simultaneously.
Embodiment 5.
Certain dye house effluents treating stations have employed air supporting and makees end advanced treating, and front technique is that the waste water after biochemical treatment makes Residual organic substances is aoxidized, containing ferric hydroxide precipitate and biochemical sludge in water outlet by Fenton method.25 parts of A agent have been added before air supporting With 75 parts of B agent compositions:
A agent component is: 30 parts of dodecyl sodium sulfates, 50 parts of α-sodium olefin sulfonates and 20 parts of glycine betaines;
B agent component is: B agent component is: 30 parts of NaCl, 70 parts of Na2SO4With K2SO4Mixture, wherein Na2SO4With K2SO4 Ratio be 1:1.
Compared with not adding air supporting synergist, solid-liquid separation effect dramatically increases, and COD clearance increases from 5% 15%, float (SS) content is reduced to 45mg/L from 100mg/L, and chroma removal rate adds 5% simultaneously.
The foregoing is only presently preferred embodiments of the present invention, not in order to limit the present invention, all essences in the present invention Any amendment, equivalent or the improvement etc. made within god and principle, should be included within the scope of the present invention.

Claims (4)

1. for an environmental protection air supporting synergist for treatment of dyeing wastewater, including the A agent 10 in terms of parts by weight~50 parts and B agent 50~90 parts, it is characterised in that described A agent and B agent are formed by following parts by weight preparation of raw material respectively:
A agent component is: dodecyl sodium sulfate 10~40 parts, α-sodium olefin sulfonate 40~70 parts and glycine betaine 20~50 parts;
B agent component is: inorganic villaumite 10~40 parts and mineral sulfates 60~80 parts;
Described inorganic villaumite is one or both combination in KCl and NaCl;Described mineral sulfates is K2SO4And Na2SO4In One or both combination.
A kind of environmental protection air supporting synergist for treatment of dyeing wastewater the most according to claim 1, it is characterised in that described A agent component be: dodecyl sodium sulfate 20~40 parts, α-sodium olefin sulfonate 40~60 parts and glycine betaine 20~30 parts;B agent group It is divided into: KCl 10~40 parts, Na2SO460~80 parts;Described A agent is 40 parts, and B agent is 60 parts.
A kind of environmental protection air supporting synergist for treatment of dyeing wastewater the most according to claim 1, it is characterised in that described A agent component be: dodecyl sodium sulfate 25~35 parts, α-sodium olefin sulfonate 45~55 parts and glycine betaine 20~25 parts;B agent group It is divided into: NaCl 30 parts, Na2SO470 parts;Described A agent is 30 parts, and B agent is 70 parts.
A kind of environmental protection air supporting synergist for treatment of dyeing wastewater the most according to claim 1, it is characterised in that described A agent component be: dodecyl sodium sulfate 30 parts, α-sodium olefin sulfonate 50 parts and glycine betaine 20 parts;B agent component is: NaCl30 Part, Na2SO4With K2SO470 parts of mixture, wherein Na2SO4With K2SO4Ratio be 1:1;Described A agent is 25 parts, and B agent is 75 parts.
CN201610718672.5A 2016-08-24 2016-08-24 A kind of environmental protection air supporting synergist for treatment of dyeing wastewater Pending CN106277262A (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111470571A (en) * 2020-04-18 2020-07-31 浙江伊诺环保科技股份有限公司 Air floatation auxiliary agent and sewage treatment process applying same

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4772425A (en) * 1985-12-23 1988-09-20 Colgate-Palmolive Company Light duty liquid dishwashing composition containing abrasive
US5308499A (en) * 1989-05-22 1994-05-03 Commonwealth Scientific And Industrial Research Organisation Effluent treatment

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4772425A (en) * 1985-12-23 1988-09-20 Colgate-Palmolive Company Light duty liquid dishwashing composition containing abrasive
US5308499A (en) * 1989-05-22 1994-05-03 Commonwealth Scientific And Industrial Research Organisation Effluent treatment

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
柳姝等: "混凝-微气泡气浮法处理含藻废水的研究", 《环境工程学报》 *

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111470571A (en) * 2020-04-18 2020-07-31 浙江伊诺环保科技股份有限公司 Air floatation auxiliary agent and sewage treatment process applying same

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