CN105540797A - Efficient water-treatment composite flocculant - Google Patents

Efficient water-treatment composite flocculant Download PDF

Info

Publication number
CN105540797A
CN105540797A CN201610045097.7A CN201610045097A CN105540797A CN 105540797 A CN105540797 A CN 105540797A CN 201610045097 A CN201610045097 A CN 201610045097A CN 105540797 A CN105540797 A CN 105540797A
Authority
CN
China
Prior art keywords
component
parts
chloride
weight
usage quantity
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.)
Granted
Application number
CN201610045097.7A
Other languages
Chinese (zh)
Other versions
CN105540797B (en
Inventor
任松洁
周立新
李伟
王昆
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Zhejiang Zhengjie Environmental Science And Technology Co Ltd
Original Assignee
Zhejiang Zhengjie Environmental Science And Technology Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Zhejiang Zhengjie Environmental Science And Technology Co Ltd filed Critical Zhejiang Zhengjie Environmental Science And Technology Co Ltd
Priority to CN201610045097.7A priority Critical patent/CN105540797B/en
Publication of CN105540797A publication Critical patent/CN105540797A/en
Application granted granted Critical
Publication of CN105540797B publication Critical patent/CN105540797B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • 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
    • C02F1/5236Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents
    • C02F1/5245Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents using basic salts, e.g. of aluminium and iron
    • 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
    • C02F1/28Treatment of water, waste water, or sewage by sorption
    • C02F1/281Treatment of water, waste water, or sewage by sorption using inorganic sorbents
    • 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
    • C02F1/28Treatment of water, waste water, or sewage by sorption
    • C02F1/285Treatment of water, waste water, or sewage by sorption using synthetic organic sorbents
    • 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
    • C02F1/5236Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents
    • 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

Landscapes

  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Separation Of Suspended Particles By Flocculating Agents (AREA)

Abstract

The invention relates to an efficient water-treatment composite flocculant which is prepared from an aluminum salt component, a ferric salt component, a coagulation enhancement component, an organic flocculation component and an activated silicic acid component. The aluminum salt component is any combination of one or more of poly aluminum chloride, polymeric aluminum sulfate, polymeric phosphato-aluminum chloride, poly-aluminum silicate, aluminum chloride and aluminum sulfate, and the usage amount is 10-40 parts by weight. The ferric salt component is any combination of one or more of polymeric ferric sulfate, polymeric ferric chloride, ferrous sulfate, ferric sulfate and ferric chloride, and the usage amount is 1-30 parts by weight. The coagulation enhancement component is any combination of one or more of carbide slag, magnesium hydroxide, magnesium chloride and zinc chloride, and the usage amount is 1-10 parts by weight. When the efficient water-treatment composite flocculant is used in a compounded mode, the flocculant can be combined with aluminum salt, is good in adsorption capacity, quick in compact precipitation and high in ferric salt hydrolysis speed, formed alumen ustum is large and dense, and the synergic effect of the aluminum salt and ferric salt can be effectively played.

Description

Efficient water treatment composite flocculant
Technical field
The present invention relates to water treatment field, particularly relate to a kind of efficient water treatment composite flocculant.
Background technology
In recent years, along with industrial or agricultural develops rapidly, industrial water consumption and quantity of wastewater effluent constantly increase, and environmental pollution by water problem is more and more serious.Protection and rational utilization of water resources become the major issue of people's common concern.The flocculation treatment of water is the important step in wastewater treatment.Flocculation process can go turbid scrubbing to sewage effectively.Flocculation agent is the key factor determining coagulating treatment effect, all has material impact to the operation conditions of the follow-up flow process for the treatment of process, effluent quality and running cost expense etc.
Flocculation, mainly by increasing the collision of suspended particle in water, making it be combined with each other gathering and becoming large, thus makes suspended particle " de-steady " be easy to separate from water.Flocculation agent can be divided into inorganic flocculating agent, organic floculant and biological flocculant according to the difference of its chemical composition structure.Wherein, biological flocculant is responsive to water quality, is vulnerable to the interference of toxic substance, must carry out a large amount of pre-treatment to the water sample of process.Be scarcely out of swaddling-clothes in actual development application.
Organic floculant refers to the organic substance that can produce the natural of throwing out or synthetic to waste water.Natural organic floculant mostly is protein or polyose water-soluble linear polymer.Natural organic high-molecular flocculant due to its electric density little, molecular weight is lower, the problems such as biological respinse inactivation easily occurs and limits its development.In use there is certain insecurity and easily secondary pollution caused to environment in synthesis organic floculant.
The flocculation agent that inorganic flocculating agent is mainly made up of inorganic component.Conventional in water treatment procedure have aluminium salt and molysite and inorganic polymer flocculant.Still its flocculation sediment speed is slow, reagent consumption is high for micromolecular alite low price, no matter is the density and the speed that form alumen ustum, or the speed of precipitation, has the space raised.
At present, along with industrial and agricultural development, wastewater flow rate is more and more, composition becomes increasingly complex, and the oil-displacing agent in sewage, oil, suspended substance, silt and mechanical impurity equal size are high, common flocculation agent has some limitations and deficiency in actual applications, and result of use is far not by far up to the mark.
Summary of the invention
When the object of this invention is to provide a kind of compound use, the flocs unit body of generation is large and structure is closely knit, and settling velocity is fast, be easy to water body be separated, wastewater treatment efficiency obviously improves, simultaneously high to the color removal of waste water, and the efficient water treatment composite flocculant that dosage reduces.
Technical scheme of the present invention is:
The efficient water treatment composite flocculant of one of the present invention, by aluminium salt component, molysite component, solidifying component, organic-flocculation component and activated silicic acid component is helped to form, aluminium salt component adopts one or more arbitrary combination of polymerize aluminum chloride, polyaluminium sulfate, poly-phosphorus aluminum chloride, polymer aluminium silicate, aluminum chloride, Tai-Ace S 150, and usage quantity is 10 ~ 40 parts with parts by weight; Molysite component adopts one or more arbitrary combination of bodied ferric sulfate, poly-ferric chloride, ferrous sulfate, ferric sulfate, iron(ic) chloride, and usage quantity is 1 ~ 30 part with parts by weight; Help solidifying component to adopt one or more arbitrary combination of carbide slag, magnesium hydroxide, magnesium chloride, zinc chloride, usage quantity is 1 ~ 10 part with parts by weight; Organic-flocculation component adopts one or more arbitrary combination of polyacrylamide, Poly Dimethyl Diallyl Ammonium Chloride, poly-third vinyl sulfonic acid sodium, Dyhard RU 100 formaldehyde resin, and usage quantity is 1 ~ 10 part with parts by weight; Activated silicic acid component usage quantity is 1 ~ 10 part with parts by weight.
As preferably, described aluminium salt component adopts polymerize aluminum chloride, and usage quantity is 20 ~ 30 parts with parts by weight.
As preferably, described molysite component is bodied ferric sulfate, and usage quantity is 5 ~ 20 parts with parts by weight.
As preferably, the described solidifying component that helps is carbide slag, and usage quantity is 5 ~ 10 parts with parts by weight.
As preferably, described organic-flocculation component is Poly Dimethyl Diallyl Ammonium Chloride, and usage quantity is 1 ~ 5 part with parts by weight.
Its main component of carbide slag is calcium hydroxide, and the adsorptive power adding enhancing flocculation agent of calcium magnesium salts, effectively improves its flocculating effect, and increase flco density, the interpolation of organic-flocculation component can improve throw out settling velocity.
When composite flocculation agent of the present invention uses, composite flocculation agent directly can be added, or first adding dissolving vessel, mass concentration is 1 ~ 30%, stirs 3 ~ 30min, reaction tank is added to pump, add 0.1 ~ 3 kilogram in water per ton, after joining pending wastewater disposal basin, stir 5 ~ 30 minutes, after having reacted, air supporting or precipitation can be adopted to carry out solid-liquor separation according to field condition.
During efficient water treatment composite flocculant compound use of the present invention, can in conjunction with aluminium salt high adsorption capacity, form that large, the close precipitation of matter of alumen ustum is fast and iron salt hydrolysis speed is fast, alumen ustum is closely knit, effectively can play the synergy of aluminium salt and molysite.
Embodiment
Embodiment one:
Efficient water treatment composite flocculant is: by polymerize aluminum chloride 40 weight part, bodied ferric sulfate 10 weight part, carbide slag 5 weight part, Poly Dimethyl Diallyl Ammonium Chloride 1 weight part and activated silicic acid 5 weight part, be mixed with composite flocculation agent of the present invention, and certain Pig raising wastewater is processed.Getting 100mL waste water regulates pH to be 5, and add this example flocculation agent 150mg, stirring and evenly mixing, is precipitated to clarification, then detects.The turbidity removal rate of this example flocculation agent is 91.1%, and percent of decolourization is 83.6%, and total tp removal rate can reach 90.1%, and the clearance of total ammonia clearance 47.8%, COD can reach 47.6%, flocculation agent residual rate 14.9%.
Embodiment two:
Efficient water treatment composite flocculant is: by polymerize aluminum chloride 35 weight part, bodied ferric sulfate 20 weight part, carbide slag 5 weight part, Poly Dimethyl Diallyl Ammonium Chloride 1 weight part and activated silicic acid 5 weight part, be mixed with composite flocculation agent of the present invention, and certain Pig raising wastewater is processed.Getting 100mL waste water regulates pH to be 5, and add this example flocculation agent 150mg, stirring and evenly mixing, is precipitated to clarification, then detects.The turbidity removal rate of this example flocculation agent is 93.2%, and percent of decolourization is 87.3%, and total tp removal rate can reach 91.6%, and the clearance of total ammonia clearance 47.5%, COD can reach 48.5%, flocculation agent residual rate 14.3%.
Embodiment three:
Efficient water treatment composite flocculant is: by polymerize aluminum chloride 30 weight part, bodied ferric sulfate 5.5 weight part, iron(ic) chloride 5 weight part, carbide slag 5.5 weight part, Poly Dimethyl Diallyl Ammonium Chloride 0.5 weight part and activated silicic acid 5 weight part, be mixed with composite flocculation agent of the present invention, and certain Pig raising wastewater is processed.Getting 100mL waste water regulates pH to be 4, and add this example flocculation agent 150mg, stirring and evenly mixing, is precipitated to clarification, then detects.The turbidity removal rate of this example flocculation agent is 87.6%, and percent of decolourization is 80.9%, and total tp removal rate can reach 86.4%, and the clearance of total ammonia clearance 47.6%, COD can reach 41.9%, flocculation agent residual rate 17.3%.
Embodiment four:
Efficient water treatment composite flocculant is: by polymerize aluminum chloride 20 weight part, bodied ferric sulfate 7.5 weight part, iron(ic) chloride 0.5 weight part, carbide slag 5.5 weight part, polyacrylamide 1 weight part and activated silicic acid 3 weight part, be mixed with composite flocculation agent of the present invention, and certain Pig raising wastewater is processed.Getting 100mL waste water regulates pH to be 5, and add this example flocculation agent 150mg, stirring and evenly mixing, is precipitated to clarification, then detects.The turbidity removal rate of this example flocculation agent is 85.3%, and percent of decolourization is 80.1%, and total tp removal rate can reach 84.7%, and the clearance of total ammonia clearance 46.5%, COD can reach 40.1%, flocculation agent residual rate 17.7%.
Embodiment five:
Efficient water treatment composite flocculant is: by polymerize aluminum chloride 35 weight part, iron(ic) chloride 5.5 weight part, carbide slag 10 weight part, polyacrylamide 0.5 weight part and activated silicic acid 5 weight part, be mixed with multiple flocculation agent of the present invention, and certain Pig raising wastewater is processed.Getting 100mL waste water regulates pH to be 4, and add this example flocculation agent 150mg, stirring and evenly mixing, is precipitated to clarification, then detects.The turbidity removal rate of this example flocculation agent is 90.7%, and percent of decolourization is 82.4%, and total tp removal rate can reach 87.3%, and the clearance of total ammonia clearance 47.1%, COD can reach 44.6%, flocculation agent residual rate 15.8%.
Embodiment six:
Efficient water treatment composite flocculant is: by polymerize aluminum chloride 30 weight part, bodied ferric sulfate 7.5 weight part, carbide slag 10 weight part, Poly Dimethyl Diallyl Ammonium Chloride 0.5 weight part and activated silicic acid 5 weight part, be mixed with multiple flocculation agent of the present invention, and certain Pig raising wastewater is processed.Getting 100mL waste water regulates pH to be 3, and add this example flocculation agent 150mg, stirring and evenly mixing, is precipitated to clarification, then detects.The turbidity removal rate of this example flocculation agent is 88.3%, and percent of decolourization is 82.1%, and total tp removal rate can reach 86.7%, and the clearance of total ammonia clearance 47.4%, COD can reach 43.7%, flocculation agent residual rate 15.7%.
Embodiment seven:
Efficient water treatment composite flocculant is: by polymerize aluminum chloride 35 weight part, bodied ferric sulfate 8 weight part, iron(ic) chloride 2 weight part, carbide slag 10 weight part, polyacrylamide 0.5 weight part, Poly Dimethyl Diallyl Ammonium Chloride 0.5wt% and activated silicic acid 5 weight part, be mixed with multiple flocculation agent of the present invention, and process certain Pig raising wastewater.Getting 100mL waste water regulates pH to be 5, and add this example flocculation agent 150mg, stirring and evenly mixing, is precipitated to clarification, then detects.The turbidity removal rate of this example flocculation agent is 90.3%, and percent of decolourization is 82.3%, and total tp removal rate can reach 89.6%, and the clearance of total ammonia clearance 46.7%, COD can reach 46.6%, flocculation agent residual rate 15.6%.
Embodiment eight:
Efficient water treatment composite flocculant is: by polymerize aluminum chloride 20 weight part, aluminum chloride 5 weight part, bodied ferric sulfate 7.5 weight part, iron(ic) chloride 2.5 weight part, carbide slag 5.5 weight part, polyacrylamide 0.5 weight part, Poly Dimethyl Diallyl Ammonium Chloride 1 weight part and activated silicic acid 5 weight part, be mixed with multiple flocculation agent of the present invention, and certain Pig raising wastewater is processed.Getting 100mL waste water regulates pH to be 4, and add this example flocculation agent 150mg, stirring and evenly mixing, is precipitated to clarification, then detects.The turbidity removal rate of this example flocculation agent is 88.2%, and percent of decolourization is 81.7%, and total tp removal rate can reach 86.1%, and the clearance of total ammonia clearance 46.7%, COD can reach 40.9%, flocculation agent residual rate 16.5%.
Above one embodiment of the present of invention are described in detail, but described content being only preferred embodiment of the present invention, can not being considered to for limiting practical range of the present invention.All equalizations done according to the present patent application scope change and improve, and all should still belong within patent covering scope of the present invention.

Claims (5)

1. an efficient water treatment composite flocculant, it is characterized in that: its by aluminium salt component, molysite component, help solidifying component, organic-flocculation component and activated silicic acid component to form, aluminium salt component adopts one or more arbitrary combination of polymerize aluminum chloride, polyaluminium sulfate, poly-phosphorus aluminum chloride, polymer aluminium silicate, aluminum chloride, Tai-Ace S 150, and usage quantity is 10 ~ 40 parts with parts by weight; Molysite component adopts one or more arbitrary combination of bodied ferric sulfate, poly-ferric chloride, ferrous sulfate, ferric sulfate, iron(ic) chloride, and usage quantity is 1 ~ 30 part with parts by weight; Help solidifying component to adopt one or more arbitrary combination of carbide slag, magnesium hydroxide, magnesium chloride, zinc chloride, usage quantity is 1 ~ 10 part with parts by weight; Organic-flocculation component adopts one or more arbitrary combination of polyacrylamide, Poly Dimethyl Diallyl Ammonium Chloride, poly-third vinyl sulfonic acid sodium, Dyhard RU 100 formaldehyde resin, and usage quantity is 1 ~ 10 part with parts by weight; Activated silicic acid component usage quantity is 1 ~ 10 part with parts by weight.
2. efficient water treatment composite flocculant according to claim 1, is characterized in that: described aluminium salt component adopts polymerize aluminum chloride, and usage quantity is 20 ~ 30 parts with parts by weight.
3. efficient water treatment composite flocculant according to claim 1, is characterized in that: described molysite component is bodied ferric sulfate, and usage quantity is 5 ~ 20 parts with parts by weight.
4. efficient water treatment composite flocculant according to claim 1, is characterized in that: the described solidifying component that helps is carbide slag, and usage quantity is 5 ~ 10 parts with parts by weight.
5. efficient water treatment composite flocculant according to claim 1, is characterized in that: described organic-flocculation component is Poly Dimethyl Diallyl Ammonium Chloride, and usage quantity is 1 ~ 5 part with parts by weight.
CN201610045097.7A 2016-01-22 2016-01-22 Efficient water treatment composite flocculant Active CN105540797B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610045097.7A CN105540797B (en) 2016-01-22 2016-01-22 Efficient water treatment composite flocculant

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201610045097.7A CN105540797B (en) 2016-01-22 2016-01-22 Efficient water treatment composite flocculant

Publications (2)

Publication Number Publication Date
CN105540797A true CN105540797A (en) 2016-05-04
CN105540797B CN105540797B (en) 2018-10-19

Family

ID=55820429

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201610045097.7A Active CN105540797B (en) 2016-01-22 2016-01-22 Efficient water treatment composite flocculant

Country Status (1)

Country Link
CN (1) CN105540797B (en)

Cited By (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107162135A (en) * 2017-05-27 2017-09-15 广东睿洁环保工程有限公司 A kind of fast purification agent of cities and towns black and odorous water
CN107500472A (en) * 2017-09-05 2017-12-22 成都锐达机电实业有限公司 High efficiency dephosphorating technique
CN108059278A (en) * 2017-12-26 2018-05-22 重庆丰望环保科技有限公司 A kind of papermaking wastewater air-flotation process system and coagulant
CN108083500A (en) * 2017-12-26 2018-05-29 重庆丰望环保科技有限公司 A kind of papermaking wastewater flocculation sediment processing system and flocculant
CN108101179A (en) * 2017-12-28 2018-06-01 新疆水处理工程技术研究中心有限公司 A kind of composite decoloration flocculant and preparation method thereof
CN108163948A (en) * 2018-01-12 2018-06-15 常州华禹环保科技有限公司 Poly-ferric chloride-PDMDAAC compound coagulants and preparation method thereof
CN108178269A (en) * 2017-12-07 2018-06-19 淮北市中芬矿山机器有限责任公司 A kind of powdery flocculant
CN108585144A (en) * 2018-04-10 2018-09-28 洛阳和天环保科技有限公司 A kind of modified wide spectrum sewage disposal composite flocculation agent and preparation method thereof
CN109052602A (en) * 2018-09-05 2018-12-21 南京大学 A kind of natural macromolecule flocculating agent and its processing method for starch wastewater treatment
CN109534471A (en) * 2019-01-14 2019-03-29 北京万云华锐化工有限公司 A kind of flocculant and its preparation method and application
CN112079590A (en) * 2020-09-28 2020-12-15 武汉聚信创为科技有限公司 Anti-mud agent and use method thereof
CN112939166A (en) * 2021-01-29 2021-06-11 常州市振邦化工制造有限公司 Flocculating agent for treating oil-containing sewage of delayed coking in petroleum refining
CN114314787A (en) * 2021-12-31 2022-04-12 华融化学股份有限公司 Turbidity removal clarifying agent and preparation method and application thereof
CN114988602A (en) * 2022-05-26 2022-09-02 欣格瑞(山东)环境科技有限公司 Coking wastewater purifying agent
CN108059278B (en) * 2017-12-26 2024-06-11 重庆丰望环保科技有限公司 Papermaking sewage air-floatation treatment system and coagulant

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1648063A (en) * 2004-12-21 2005-08-03 李迎来 Mixed flocculant for treating waste water containing oil
US20080296232A1 (en) * 2007-05-31 2008-12-04 Paul Wegner Wastewater clarifier and process
CN101704569A (en) * 2009-11-19 2010-05-12 长安大学 Flocculant for purifying emulsified oil-containing waste water and preparation method thereof
CN101774731A (en) * 2010-01-27 2010-07-14 四川大学 Enhanced coagulation-gas stripping-membrane integration method and device for lightening membrane pollution
CN102115235A (en) * 2009-12-31 2011-07-06 宋晓东 Environment-friendly flocculating degreaser
CN102126803A (en) * 2011-04-22 2011-07-20 中国科学院生态环境研究中心 Process for catalytic oxidation-compound flocculation integrated treatment of comprehensive waste water
WO2012042530A1 (en) * 2010-09-27 2012-04-05 Tata Consultancy Services Limited Apparatus for water purification
CN102491465A (en) * 2011-11-25 2012-06-13 亿利资源集团有限公司 Flocculant and preparation method thereof

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1648063A (en) * 2004-12-21 2005-08-03 李迎来 Mixed flocculant for treating waste water containing oil
US20080296232A1 (en) * 2007-05-31 2008-12-04 Paul Wegner Wastewater clarifier and process
CN101704569A (en) * 2009-11-19 2010-05-12 长安大学 Flocculant for purifying emulsified oil-containing waste water and preparation method thereof
CN102115235A (en) * 2009-12-31 2011-07-06 宋晓东 Environment-friendly flocculating degreaser
CN101774731A (en) * 2010-01-27 2010-07-14 四川大学 Enhanced coagulation-gas stripping-membrane integration method and device for lightening membrane pollution
WO2012042530A1 (en) * 2010-09-27 2012-04-05 Tata Consultancy Services Limited Apparatus for water purification
CN102126803A (en) * 2011-04-22 2011-07-20 中国科学院生态环境研究中心 Process for catalytic oxidation-compound flocculation integrated treatment of comprehensive waste water
CN102491465A (en) * 2011-11-25 2012-06-13 亿利资源集团有限公司 Flocculant and preparation method thereof

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
严瑞瑄主编: "《水处理剂应用手册 第二版》", 30 June 2003, 化学工业出版社 *
柳荣展、石宝龙主编: "《轻化工水污染控制》", 30 September 2008, 中国纺织出版社 *

Cited By (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107162135A (en) * 2017-05-27 2017-09-15 广东睿洁环保工程有限公司 A kind of fast purification agent of cities and towns black and odorous water
CN107500472B (en) * 2017-09-05 2021-05-11 成都锐达机电实业有限公司 High-efficiency dephosphorization process
CN107500472A (en) * 2017-09-05 2017-12-22 成都锐达机电实业有限公司 High efficiency dephosphorating technique
CN108178269A (en) * 2017-12-07 2018-06-19 淮北市中芬矿山机器有限责任公司 A kind of powdery flocculant
CN108059278A (en) * 2017-12-26 2018-05-22 重庆丰望环保科技有限公司 A kind of papermaking wastewater air-flotation process system and coagulant
CN108083500A (en) * 2017-12-26 2018-05-29 重庆丰望环保科技有限公司 A kind of papermaking wastewater flocculation sediment processing system and flocculant
CN108059278B (en) * 2017-12-26 2024-06-11 重庆丰望环保科技有限公司 Papermaking sewage air-floatation treatment system and coagulant
CN108083500B (en) * 2017-12-26 2023-12-19 重庆丰望环保科技有限公司 Papermaking sewage flocculation and precipitation treatment system and flocculant
CN108101179A (en) * 2017-12-28 2018-06-01 新疆水处理工程技术研究中心有限公司 A kind of composite decoloration flocculant and preparation method thereof
CN108163948A (en) * 2018-01-12 2018-06-15 常州华禹环保科技有限公司 Poly-ferric chloride-PDMDAAC compound coagulants and preparation method thereof
CN108585144A (en) * 2018-04-10 2018-09-28 洛阳和天环保科技有限公司 A kind of modified wide spectrum sewage disposal composite flocculation agent and preparation method thereof
CN109052602B (en) * 2018-09-05 2021-04-23 南京大学 Natural polymeric flocculant for starch wastewater treatment and treatment method thereof
CN109052602A (en) * 2018-09-05 2018-12-21 南京大学 A kind of natural macromolecule flocculating agent and its processing method for starch wastewater treatment
CN109534471A (en) * 2019-01-14 2019-03-29 北京万云华锐化工有限公司 A kind of flocculant and its preparation method and application
CN112079590A (en) * 2020-09-28 2020-12-15 武汉聚信创为科技有限公司 Anti-mud agent and use method thereof
CN112939166A (en) * 2021-01-29 2021-06-11 常州市振邦化工制造有限公司 Flocculating agent for treating oil-containing sewage of delayed coking in petroleum refining
CN114314787A (en) * 2021-12-31 2022-04-12 华融化学股份有限公司 Turbidity removal clarifying agent and preparation method and application thereof
CN114988602A (en) * 2022-05-26 2022-09-02 欣格瑞(山东)环境科技有限公司 Coking wastewater purifying agent

Also Published As

Publication number Publication date
CN105540797B (en) 2018-10-19

Similar Documents

Publication Publication Date Title
CN105540797A (en) Efficient water-treatment composite flocculant
Sahu et al. Review on chemical treatment of industrial waste water
CN102295335B (en) Flocculating-agent composition
CN105000680B (en) Compound water treatment agent
CN100579913C (en) Polymeric ferric polysulfate composite coagulant and application thereof
CN106430495B (en) A kind of preparation method of the composite decoloration flocculant for wastewater treatment
CN104761029A (en) Composite inorganic high-molecular waste water treatment flocculant
CN105016494A (en) Composite water treatment agent
KR101640368B1 (en) Method of preparation for coagulant contains low basicity and treating method of water/wastewater using the same
KR101278230B1 (en) The method and Appuratus of removing total nitrogen and phosphate in sewage and wastewater using precipitation-agent of rapidity for coagulation an flocculation
CN105110395A (en) Water treatment agent and preparing method
CN1385373A (en) Coagulant for sewage treatment
CN101423275A (en) Method for preparing composite flocculant
CN1321073C (en) Safety and ecological natural built-up flocculant, its production and use
CN101648731B (en) Coking wastewater advanced treatment agent and application thereof
CN105060510A (en) Phosphor-free water treating agent
CN103922453B (en) A kind of coking chemical waste water flocculation agent and preparation method thereof and application
CN105110441A (en) Water treatment agent and preparing method
CN102092826B (en) Environmental-friendly type coagulant for purifying water
CN105060513A (en) Green water treatment agent
CN105000685B (en) Chemical water treatment agent
CN109775779A (en) A kind of Water Treatment agent
CN104118925B (en) A kind of composite inorganic flocculation agent
CN104986871B (en) Environmentally friendly water treatment agent
CN105036268A (en) Multifunctional water treatment agent

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant
CB03 Change of inventor or designer information

Inventor after: Ren Songjie

Inventor after: Xiang Hai

Inventor after: Zhou Lixin

Inventor after: Li Wei

Inventor after: Wang Kun

Inventor before: Ren Songjie

Inventor before: Zhou Lixin

Inventor before: Li Wei

Inventor before: Wang Kun

CB03 Change of inventor or designer information