CN107399801A - Industrial waste water treatment agent based on multiple-effect dephosphorization - Google Patents

Industrial waste water treatment agent based on multiple-effect dephosphorization Download PDF

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Publication number
CN107399801A
CN107399801A CN201610331281.8A CN201610331281A CN107399801A CN 107399801 A CN107399801 A CN 107399801A CN 201610331281 A CN201610331281 A CN 201610331281A CN 107399801 A CN107399801 A CN 107399801A
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CN
China
Prior art keywords
waste water
water treatment
industrial waste
processing
treatment agent
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
CN201610331281.8A
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Chinese (zh)
Inventor
周文圣
周文忠
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.)
Dongguan Top Environmental Protection Technology Co Ltd
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Dongguan Top Environmental Protection 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 Dongguan Top Environmental Protection Technology Co Ltd filed Critical Dongguan Top Environmental Protection Technology Co Ltd
Priority to CN201610331281.8A priority Critical patent/CN107399801A/en
Publication of CN107399801A publication Critical patent/CN107399801A/en
Pending legal-status Critical Current

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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
    • C02F1/52Treatment 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
    • C02F1/58Treatment of water, waste water, or sewage by removing specified dissolved compounds

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  • 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)
  • Removal Of Specific Substances (AREA)
  • Water Treatment By Sorption (AREA)

Abstract

A kind of Industrial waste water treatment agent based on multiple-effect dephosphorization disclosed by the invention, in the reactor with reflux condensate device, add dimethyl diallyl ammonium chloride cationic monomer 240kg, the kg of diallylamine 10, the kg of glacial acetic acid 8, it is heated to 82 DEG C, composite initiator 0.2kg is added, controlling reaction temperature is no more than 100 DEG C, during after naturally cool to 82 DEG C, add 0.2kg composite initiators, after heating terminates, 0.3kg composite initiators are added, after heating terminates, it is heated to 95 DEG C and is incubated 2 hours, it is standby that cationic polymer is made.60 parts of water, 100 parts of technical hydrochloric acids, 10 parts of ferric trichlorides, 60 parts of calcium aluminates are added in another reactor, stirring reaction, when temperature rises to 80 DEG C, add cationic polymer made from 10 parts of said process, 90 ~ 95 DEG C are warming up to, is reacted 4 hours, blowing cures 24 hours and produces product.Product prepared by the present invention has excellent phosphor-removing effect, while has the functions such as flocculation, decolouring, deodorization, removal COD concurrently.

Description

Industrial waste water treatment agent based on multiple-effect dephosphorization
Technical field
This patent is related to a kind of industry for having excellent phosphor-removing effect, while having the functions such as flocculation, decolouring, COD removals concurrently Waste water treatment medicament -- the technology of preparing of multiple-effect dephosphorization agent, belong to environmentally friendly water treatment agent field.
Background technology
The traditional phosphorus removing method of sewage treatment industry mainly has chemical precipitation method and microbial method.Chemical precipitation method it is basic Principle is to add one or more of metal ions that precipitation can be generated with phosphate radical, by generating insoluble phosphatic side Method so that phosphate radical removes from water.The conventional precipitating reagent of traditional dephosphorization method have calcium chloride, aluminium polychloride, bodied ferric sulfate, The aluminium such as aluminum sulfate, alchlor, ferric trichloride, frerrous chloride, iron, calcium salt.Due to traditional dephosphorization method phosphor-removing effect not only with The dosage of precipitating reagent is relevant, sewage remained after processing phosphorus concentration additionally depend on formed insoluble salt solubility product it is big It is small, so, it is good selection using traditional dephosphorization method when the emission request to phosphorus is not high.It is but higher for emission request Occasion, traditional dephosphorization method just can not meet requirement.
The content of the invention
The invention aims to overcome traditional dephosphorization agent phosphor-removing effect not reach emission request and the single disadvantage of performance End, there is provided one kind both has good phosphor-removing effect, has flocculation, decolouring, the multiple-effect water treatment agent for removing COD and other effects concurrently again.
The formula and preparation technology of the present invention is as follows:
The cationic polymerization composition formula of table 1
The multiple-effect dephosphorization agent basic recipe of table 2
Cationic polymer preparation technology:
In the enamel or stainless steel cauldron with reflux condensate device and heating jacket, dimethyl diallyl is sequentially added Ammonium chloride, diallylamine, glacial acetic acid, stirring is started, be heated to 82 DEG C, add part composite initiator, control reaction Temperature is no more than 100 DEG C, when being cooled to 82 DEG C, adds part composite initiator, and after heating terminates, it is multiple to add remaining Initiator is closed, after heating terminates, 95 DEG C is heated to and is incubated 2 hours, standing makes it be naturally cooling to room temperature, obtains cationic polymerization Thing.
The preparation technology of multiple-effect dephosphorization agent:
In the reactor with heating and device for absorbing tail gas, water, hydrochloric acid and ferric trichloride are sequentially added, starts stirring, delayed Slow to add calcium aluminate, reaction temperature meeting nature rises, when calcium aluminate adds and temperature rises to 80 DEG C(Do not reach 80 such as DEG C, then heat temperature raising), cationic polymer is added, is warming up to 90 ~ 95 DEG C, is reacted 4 hours, is cured 24 hours.
Technical key point is:The polymerization that cationic polymer participates in aluminium chloride ferrum is introduced, obtained product is not Only there is excellent phosphor-removing effect, while have the function such as decolouring and COD removals concurrently.
Embodiment
Embodiment 1
In the reactor with reflux condensate device, dimethyl diallyl ammonium chloride cationic monomer 240kg, diene are added The kg of propyl group amine 10, the kg of glacial acetic acid 8,82 DEG C are heated to, add composite initiator 0.2kg, controlling reaction temperature is no more than 100 DEG C, during after naturally cool to 82 DEG C, 0.2kg composite initiators are added, after heating terminates, add the compound initiations of 0.3kg Agent, after heating terminates, it is heated to 95 DEG C and is incubated 2 hours, cationic monomer is made.60 parts of water of addition in another reactor, 100 Part technical hydrochloric acid, 10 parts of ferric trichlorides, 60 parts of calcium aluminates, stirring reaction, when temperature rises to 80 DEG C, add 10 parts of said process Obtained cationic polymer, 90 ~ 95 DEG C are warming up to, reacted 4 hours, blowing cures 24 hours and produces product.
Application examples 1
The multiple-effect dephosphorization agent prepared with embodiment 1 handles total effluent of certain printing and dyeing mill, and the waste water has already passed through anaerobic and aerobic Biochemical treatment, adds multiple-effect dephosphorization agent after biochemical treatment, result is as shown in the table.
The multiple-effect dephosphorization agent of 3 embodiment of table 1 handles dyeing waste water
Application examples 2
The multiple-effect dephosphorization agent prepared with embodiment 1 handles municipal wastewater, and result is as shown in the table.
The multiple-effect dephosphorization agent of 4 embodiment of table 1 handles municipal wastewater
The invention is not restricted to above-mentioned implementation, all numerous embodiments that constructed effect is realized using same principle and its method Duplicated with this patent.

Claims (5)

1. it is a kind of based on efficient decolorizing processing Industrial waste water treatment agent, it is characterised in that the preparation method of the processing include with Lower step:
The each constituent of inorganic agent includes following components by mass fraction:
Dicyandiamide 8 ~ 10
Formaldehyde 21 ~ 25
Ammonium chloride 3 ~ 7
Alkali 1 ~ 3.
2. the Industrial waste water treatment agent as claimed in claim 1 based on efficient decolorizing processing, it is characterised in that this method includes Following steps:
The each constituent of inorganic agent includes following components by mass fraction:
Dicyandiamide 8
Formaldehyde 22
Ammonium chloride 6
Alkali 2.
3. the Industrial waste water treatment agent as claimed in claim 1 based on efficient decolorizing processing, it is characterised in that the system of the processing Preparation Method comprises the following steps:
It is anti-so as to change polymerization with acid in alkali and caused by polycondensation process during dicandiamide-formaldehyde condensation polymer is prepared The course answered, improve the molecular weight of polymer.
4. the Industrial waste water treatment agent as claimed in claim 1 based on efficient decolorizing processing, it is characterised in that the system of the processing Preparation Method comprises the following steps:
Be inorganic base for neutralizing alkali acid caused by polycondensation process, including sodium hydroxide, sodium carbonate, aqua ammonia and it One, or organic base:Dimethylamine.
5. the Industrial waste water treatment agent as claimed in claim 1 based on efficient decolorizing processing, it is characterised in that the system of the processing Preparation Method comprises the following steps:
In preparation process or by the way that mentioned component is added portionwise, to control the molecular weight distribution of decolorising agent, so as to obtain molecular weight Distribution is concentrated, the condensation polymer of good decolorizing effect.
CN201610331281.8A 2016-05-18 2016-05-18 Industrial waste water treatment agent based on multiple-effect dephosphorization Pending CN107399801A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610331281.8A CN107399801A (en) 2016-05-18 2016-05-18 Industrial waste water treatment agent based on multiple-effect dephosphorization

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201610331281.8A CN107399801A (en) 2016-05-18 2016-05-18 Industrial waste water treatment agent based on multiple-effect dephosphorization

Publications (1)

Publication Number Publication Date
CN107399801A true CN107399801A (en) 2017-11-28

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN201610331281.8A Pending CN107399801A (en) 2016-05-18 2016-05-18 Industrial waste water treatment agent based on multiple-effect dephosphorization

Country Status (1)

Country Link
CN (1) CN107399801A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110606534A (en) * 2019-10-30 2019-12-24 常州市振邦化工制造有限公司 Preparation method of flocculating agent for treating oil-containing sewage of petroleum refining delayed coking
CN112340827A (en) * 2020-09-28 2021-02-09 鞍钢贝克吉利尼水处理有限公司 Phosphorus removing agent taking acid regeneration silicon-containing mud cake as raw material and preparation method thereof
CN114106238A (en) * 2021-12-14 2022-03-01 西南石油大学 Zwitterionic flocculant and preparation method thereof
CN114426326A (en) * 2020-09-21 2022-05-03 中国石油化工股份有限公司 Oily sewage treatment flocculant and preparation method and application thereof

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110606534A (en) * 2019-10-30 2019-12-24 常州市振邦化工制造有限公司 Preparation method of flocculating agent for treating oil-containing sewage of petroleum refining delayed coking
CN110606534B (en) * 2019-10-30 2021-09-28 常州市振邦化工制造有限公司 Preparation method of flocculating agent for treating oil-containing sewage of petroleum refining delayed coking
CN114426326A (en) * 2020-09-21 2022-05-03 中国石油化工股份有限公司 Oily sewage treatment flocculant and preparation method and application thereof
CN114426326B (en) * 2020-09-21 2023-04-18 中国石油化工股份有限公司 Oily sewage treatment flocculant and preparation method and application thereof
CN112340827A (en) * 2020-09-28 2021-02-09 鞍钢贝克吉利尼水处理有限公司 Phosphorus removing agent taking acid regeneration silicon-containing mud cake as raw material and preparation method thereof
CN114106238A (en) * 2021-12-14 2022-03-01 西南石油大学 Zwitterionic flocculant and preparation method thereof

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Application publication date: 20171128