CN102765790A - Preparation method of inorganic-organic composite coagulant - Google Patents

Preparation method of inorganic-organic composite coagulant Download PDF

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Publication number
CN102765790A
CN102765790A CN2012102758448A CN201210275844A CN102765790A CN 102765790 A CN102765790 A CN 102765790A CN 2012102758448 A CN2012102758448 A CN 2012102758448A CN 201210275844 A CN201210275844 A CN 201210275844A CN 102765790 A CN102765790 A CN 102765790A
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inorganic
water
preparation
fecl
ammonium chloride
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高宝玉
曹百川
赵爽
王萌萌
岳钦艳
王燕
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Shandong University
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Shandong University
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Abstract

The invention relates to a preparation method of an inorganic-organic composite coagulant, which comprises the following steps: inorganic matters AlCl3 and/or FeCl3 are dissolved in distilled water, and added with Na2CO3 to allow degree of alkalization to be 0.5-2.0; when Na2CO3 is dissolved in water, dimethyl diallyl ammonium chloride homopolymer is added in the solution according to that the mass ratio of Al and/or Fe to dimethyl diallyl ammonium chloride homopolymer is (4-8):1; and the homopolymer is mixed with the solution uniformly, and reacted for 1-3h to obtain the inorganic-organic composite coagulant. The inorganic-organic composite coagulant provided by the invention is prepared by taking AlCl3, FeCl3, Na2CO3, NaH2PO4 and PDMDAAC (poly dimethyl diallyl ammonium chloride) as main raw materials, has the characteristics of low dose, strong electric neutralizing capacity, large molecular weight and little sludge amount when being used, and has better treatment effect on the algae-containing raw water.

Description

A kind of inorganic-preparation method of organic compound coagulant
Technical field
The present invention relates to a kind of inorganic-preparation method of organic compound coagulant, particularly a kind of preparation method who is used to contain inorganic-organic compound coagulant of the former water treatment of algae belongs to environment and technical field of chemistry.
Background technology
Coagulation is the agglomeration process of water-borne glue body particle and small suspended substance.Coagulation comprises the cohesion and two aspects of flocculating, and cohesion is meant the steady process of taking off of water-borne glue body, and flocculation is meant the steady agglomeration of particles process of taking off.Coagulation is one of most important technology in water and the wastewater treatment, and its treatment effect has determined the operation condition of subsequent technique, and effluent quality and running cost are had bigger influence.In decades in the past, the research of coagulation technology mainly concentrates on coagulation chemistry, coagulation physics and coagulation process and learns three aspects.Along with theoretical constantly perfect of coagulation, research focus in recent years turns to the exploitation of all kinds of coagulants and the aspects such as control of use, coagulating process and condition gradually.
The research and development of novel coagulating agent are the research focuses of water treatment field, its total development trend be from low molecule to polymer, single type to compound, single functional type to multifunctional type.According to the chemical ingredients of coagulating agent, can it be divided into inorganic coagulant, organic polymer coargulator, compound coagulant and microbial flocculant.Inorganic polymer coagulant have suitability good, to characteristics such as the growth of the applied widely and flco of water temperature and pH are fast, its main drawback is that the mud generation is big.The advantage of organic polymer coargulator is adding less, and shortcoming is that cost is high.Inorganic-organic compound coagulant is to pass through to take place physical-chemical reaction before use by inorganic coagulant and organic polymer coargulator; A kind of stable prod that forms; Have stronger charge neutrality ability and adsorption bridging ability, can bring into play the synergy of two kinds of components, improve coagulation effect.
Because industrial and agricultural production makes in the surface water the concentrating of nutrients such as nitrogen phosphorus increase, and causes algal bloom under optimum conditions easily, causes water pollution incidents such as wawter bloom, causes the rapid deterioration of water quality, influences the functions of use of surface water.In addition, in water technology, the algae too high levels can reduce deposition efficiency, stops up the filter tank, causes effluent quality to worsen.Water factory extensively adopts coagulation-filtration-sterilization conventional processes at present, and used coagulating agent is an inorganic coagulant, and this technology has removal effect preferably to turbidity, but not good to the removal effect of organism and algae.To above problem, when processing contains the former water of algae, adopt novel coagulating agent, can under the prerequisite that does not change existing technology, improve the algae removal rate, improve effluent quality, have good economy, society and Significance for Environment.
Chinese patent document CN101985373A (application number 201010566885.3) and Chinese patent document CN102276036A (application number 201110210583.7) adopt raw materials such as water glass, iron trichloride and mineral acid; Make polymeric silicicacid class inorganic coagulant, can effectively remove frustule.Chinese patent CN101054222 (CN200710020777.4) then adopts flyash, ultrapure magnetite powder and concentrated hydrochloric acid to process compound magnetic flocculation agent, is used for the processing of algal tufa.More than invention is the inorganic compounding coagulating agent, when processing contains the former water of algae, still has the high problem of dosage.
Summary of the invention
The present invention is directed to the deficiency of prior art, provide a kind of inorganic-preparation method of organic compound coagulant.
Terminological interpretation
Basicity: basicity refers to degree of hydroxylation, is the ratio of hydroxyl equivalent and the equivalent of aluminium and/or iron in Poly aluminum Chloride (PAC), poly-ferric chloride or the aluminium iron polychloride.
Technical scheme of the present invention is following:
A kind of inorganic-preparation method of organic composite coagulator, comprise the steps:
With inorganics AlCl 3And/or FeCl 3Be dissolved in the zero(ppm) water, add Na 2CO 3Making basicity is 0.5~2.0, treats Na 2CO 3After the dissolving; According to Al and/or Fe element and dimethyl diallyl ammonium chloride homopolymer (PDMDAAC) mass ratio is (4~8): 1 ratio adds the dimethyl diallyl ammonium chloride homopolymer; Mix under the normal temperature, reaction 1~3h makes inorganic-organic composite coagulator.
Preferred according to the present invention, said inorganics is FeCl 3Perhaps AlCl 3With FeCl 3Mixing the time, treat Na 2CO 3After the dissolving, also comprise adding stablizer NaH 2PO 4Step; Further preferred, said Fe element and NaH 2PO 4The mass ratio of middle P element is 25: (1~3).
Preferred according to the present invention, said inorganics is AlCl 3With FeCl 3Mixing the time, the mol ratio of Al element and Fe element is (3~11): 1.
Preferred according to the present invention, said inorganics is AlCl 3The time, add Na 2CO 3Making basicity is 1.0~2.0; Said inorganics is FeCl 3Perhaps AlCl 3With FeCl 3Mixing the time, add Na 2CO 3Making basicity is 0.5~1.5.
When to AlCl 3Solution, FeCl 3Solution or AlCl 3And FeCl 3Add Na in the mixing solutions 2CO 3The time, can produce Poly aluminum Chloride (PAC), poly-ferric chloride or aluminium iron polychloride.
When inorganics is AlCl 3The time, the inorganic-organic composite coagulator that makes is colourless liquid, wherein Al 2O 3Mass content be 9.4~10.5%; When inorganics is AlCl 3And FeCl 3The time, the inorganic-organic composite coagulator that makes is light brown liquid, wherein Al 2O 3And Fe 2O 3Mass content be 8.2~10.0%; When inorganics is FeCl 3The time, the inorganic-organic composite coagulator that makes is brown liquid, wherein Fe 2O 3Mass content be 5.8~7.1%.
Beneficial effect
Of the present invention inorganic-organic compound coagulant is with AlCl 3, FeCl 3, Na 2CO 3, NaH 2PO 4With PDMDAAC be that main raw material makes, have the characteristics that dosage is low, the charge neutrality ability is strong, molecular weight is big and sludge quantity is few during use, to containing the former glassware for drinking water of algae treatment effect is preferably arranged.
Embodiment
Raw material sources
AlCl 3: available from Chemical Reagent Co., Ltd., Sinopharm Group, composition is AlCl 36H 2O, purity is analytical pure;
FeCl 3: available from Tianjin Da Mao chemical reagent factory, composition is FeCl 36H 2O, purity is analytical pure;
Poly Dimethyl Diallyl Ammonium Chloride: english abbreviation PDMDAAC, available from Binzhou, Shandong Jia Yuan environmental protection company, purity is CP, and solid content is 40.0wt%, and viscosity is 1.20mL/g;
Other reagent is commercially available prod commonly used, this area.
Detection method
The detection method of specific conductivity adopts GB/T 27502-2011 among the embodiment; The detection method of turbidity adopts GB/T13200-1991; The detection method of dissolved organic carbon adopts ISO 8245-1999; The chlorophyll-a content detecting method adopts GB/T 22182-2008.
Embodiment 1
The preparation method of polyaluminium chloride e-poly-dimethyl-diallyl-ammonium chloride composite flocculation agent, step is following:
Take by weighing the AlCl of 44.17g 36H 2The O solid adds dissolved in distilled water in beaker, make AlCl 3Solution;
Take by weighing the anhydrous Na of 19.63g 2CO 3, under agitation condition to AlCl 3Add Na in the solution 2CO 3, treat lather collapse after, add the 6.25g Poly Dimethyl Diallyl Ammonium Chloride, at room temperature continue then to stir 3h, be settled to 500mL with zero(ppm) water, making basicity is 2.0, Al 2O 3Content is the polyaluminium chloride e-poly-dimethyl-diallyl-ammonium chloride composite flocculation agent of 18.89g/L.
Embodiment 2
Like embodiment 1 described preparation method, difference is, adds the 3.12g Poly Dimethyl Diallyl Ammonium Chloride, at room temperature continues then to stir 3h, is settled to 500mL with zero(ppm) water then, and making basicity is 2.0, Al 2O 3Content is the polyaluminium chloride e-poly-dimethyl-diallyl-ammonium chloride composite flocculation agent of 18.89g/L.
Embodiment 3
The preparation method of poly-ferric chloride-Poly Dimethyl Diallyl Ammonium Chloride composite flocculation agent, step is following:
Take by weighing the FeCl of 23.88g 3Solid adds dissolved in distilled water in beaker, make FeCl 3Solution;
Take by weighing the anhydrous Na of 2.36g 2CO 3, under agitation condition to FeCl 3Add Na in the solution 2CO 3, treat lather collapse after, according to FeCl 3Middle Fe element and NaH 2PO 4The mol ratio of middle P element is that the amount of 25:2 adds NaH 2PO 4, add the 6.25g Poly Dimethyl Diallyl Ammonium Chloride, at room temperature continue then to stir 3h, be settled to 500mL with zero(ppm) water, making basicity is 0.5, Fe 2O 3Content is poly-ferric chloride-Poly Dimethyl Diallyl Ammonium Chloride composite flocculation agent of 13.33g/L.
Embodiment 4
Like embodiment 3 described preparing methods, difference is, adds the 3.12g Poly Dimethyl Diallyl Ammonium Chloride, at room temperature continues then to stir 3h, is settled to 500mL with zero(ppm) water then, and making basicity is 0.5, Fe 2O 3Content is poly-ferric chloride-Poly Dimethyl Diallyl Ammonium Chloride composite flocculation agent of 10g/L.
Embodiment 5
The preparation method of polymeric aluminum ferric chloride-polydimethyldiallylachloride chloride composite flocculation agent, step is following:
Take by weighing the AlCl of 34.07g 3The FeCl of solid and 5.46g 3Solid adds dissolved in distilled water in beaker, take by weighing the anhydrous Na of 8.65g 2CO 3, under agitation condition, in solution, add above-mentioned anhydrous Na 2CO 3, treat lather collapse after, according to FeCl 3Middle Fe element and NaH 2PO 4The mol ratio of middle P element is that the amount of 25:2 adds NaH 2PO 4, add the 6.25g Poly Dimethyl Diallyl Ammonium Chloride, at room temperature continue then to stir 3h, be settled to 500mL with zero(ppm) water, making basicity is 1.0, Al 2O 3+ Fe 2O 3Content is the polymeric aluminum ferric chloride-polydimethyldiallylachloride chloride composite flocculation agent of 17.84g/L.
Embodiment 6
Like embodiment 5 described preparing methods, difference is,
Add the 3.12g Poly Dimethyl Diallyl Ammonium Chloride, at room temperature continue then to stir 3h, be settled to 500mL with zero(ppm) water, making basicity is 1.0, Al 2O 3+ Fe 2O 3Content is the polymeric aluminum ferric chloride-polydimethyldiallylachloride chloride composite flocculation agent of 17.84g/L.
The effect experiment
The experiment raw water quality
Contain algae Yellow River Reservoir water, water quality is following: 19.5~24.3 ℃ of water temperatures, pH 8.17~8.43, specific conductivity 825~887 μ S/cm, turbidity 4.76~6.19NTU, 245nm absorbancy (UV 254) 0.037~0.046cm -1, dissolved organic carbon (DOC) 2.891~3.563mg/L, chlorophyll-a content 18.68~34.73 μ g/L.
Test Example 1
The polyaluminium chloride e-poly-dimethyl-diallyl-ammonium chloride composite flocculation agent of preparation among embodiment 1 and the embodiment 2 is added in the former water; Under the 200rpm rotating speed, stir 1min fast; Under the rotating speed of 40rpm, stir 15min then slowly; After staticly settling 15min, 2cm place water sampling carries out water under liquid level, and the result is as shown in table 1.
Poly aluminium chloride is as contrast, and step is the same, and the result is as shown in table 1 for treating water water quality.
Table 1
From table 1, can find out; Stronger according to embodiment 1 with the charge neutrality ability of the polyaluminium chloride e-poly-dimethyl-diallyl-ammonium chloride composite flocculation agent of embodiment 2 preparations, and the removal effect of testing turbidity, DOC and chlorophyll-a in the former water all obviously is superior to traditional inorganic polymer coagulant poly aluminium chloride.
Test Example 2
Poly-ferric chloride-Poly Dimethyl Diallyl Ammonium Chloride the composite flocculation agent of preparation among embodiment 3 and the embodiment 4 is added in the former water; Under the 200rpm rotating speed, stir 1min fast; Under the rotating speed of 40rpm, stir 15min then slowly; After staticly settling 15min, 2cm place water sampling carries out water under liquid level, and the result is as shown in table 2.
Poly-iron chloride is as contrast, and step is the same, and the result is as shown in table 2 for treating water water quality.
Table 2
Figure BDA00001972305600042
Figure BDA00001972305600051
From table 2, can find out; Stronger according to embodiment 3 with the charge neutrality ability of the poly-ferric chloride-Poly Dimethyl Diallyl Ammonium Chloride composite flocculation agent of embodiment 4 preparations, and the removal effect of testing turbidity, DOC and chlorophyll-a in the former water all obviously is superior to traditional inorganic polymer coagulant poly-iron chloride.
Test Example 3
The polymeric aluminum ferric chloride-polydimethyldiallylachloride chloride composite flocculation agent of preparation among embodiment 5 and the embodiment 6 is added in the former water; Under the 200rpm rotating speed, stir 1min fast; Under the rotating speed of 40rpm, stir 15min then slowly; After staticly settling 15min, 2cm place water sampling carries out water under liquid level, and the result is as shown in table 3.
Poly aluminium chloride iron is as contrast, and step is the same, and the result is as shown in table 3 for treating water water quality.
Table 3
Figure BDA00001972305600052
From table 3, can find out; Stronger according to embodiment 5 with the charge neutrality ability of the polymeric aluminum ferric chloride-polydimethyldiallylachloride chloride composite flocculation agent of embodiment 6 preparations, and the removal effect of testing turbidity, DOC and chlorophyll-a in the former water all obviously is superior to traditional inorganic polymer coagulant poly aluminium chloride iron.

Claims (5)

1. the preparation method of inorganic-organic composite coagulator comprises the steps:
With inorganics AlCl 3And/or FeCl 3Be dissolved in the zero(ppm) water, add Na 2CO 3Making basicity is 0.5~2.0, treats Na 2CO 3After the dissolving, be (4~8) according to Al and/or Fe element and dimethyl diallyl ammonium chloride homopolymer mass ratio: 1 ratio adds the dimethyl diallyl ammonium chloride homopolymer, mixes under the normal temperature, and reaction 1~3h makes inorganic-organic composite coagulator.
2. preparation method as claimed in claim 1 is characterized in that, said inorganics is FeCl 3Perhaps AlCl 3With FeCl 3Mixing the time, treat Na 2CO 3After the dissolving, also comprise adding stablizer NaH 2PO 4Step.
3. preparation method as claimed in claim 2 is characterized in that, said Fe element and NaH 2PO 4The mass ratio of middle P element is 25: (1~3).
4. preparation method as claimed in claim 1 is characterized in that, said inorganics is AlCl 3With FeCl 3Mixing the time, the mol ratio of Al element and Fe element is (3~11): 1.
5. preparation method as claimed in claim 1 is characterized in that, said inorganics is AlCl 3The time, add Na 2CO 3Making basicity is 1.0~2.0; Said inorganics is FeCl 3Perhaps AlCl 3With FeCl 3Mixing the time, add Na 2CO 3Making basicity is 0.5~1.5.
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CN104150573A (en) * 2014-07-04 2014-11-19 安徽三环水泵有限责任公司 Primary physicochemical enhanced coagulant and treatment method of papermaking wastewater
CN106977003A (en) * 2016-01-15 2017-07-25 宝山钢铁股份有限公司 Electrical conductivity and the method and apparatus of total iron in a kind of cold rolling hydrochloric acid acid regeneration waste water of reduction
CN108298716A (en) * 2017-12-31 2018-07-20 天津泉洁科技有限公司 A kind of novel drink water purifying method
CN110776071A (en) * 2019-10-28 2020-02-11 德蓝水技术股份有限公司 Industrial acidic wastewater treatment agent

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Cited By (6)

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Publication number Priority date Publication date Assignee Title
CN104150573A (en) * 2014-07-04 2014-11-19 安徽三环水泵有限责任公司 Primary physicochemical enhanced coagulant and treatment method of papermaking wastewater
CN104150573B (en) * 2014-07-04 2015-10-28 安徽三环水泵有限责任公司 A kind of one-level materialization enhanced coagulation agent of papermaking wastewater and treatment process thereof
CN106977003A (en) * 2016-01-15 2017-07-25 宝山钢铁股份有限公司 Electrical conductivity and the method and apparatus of total iron in a kind of cold rolling hydrochloric acid acid regeneration waste water of reduction
CN106977003B (en) * 2016-01-15 2020-09-25 宝山钢铁股份有限公司 Method and device for reducing conductivity and total iron in cold rolling hydrochloric acid regeneration wastewater
CN108298716A (en) * 2017-12-31 2018-07-20 天津泉洁科技有限公司 A kind of novel drink water purifying method
CN110776071A (en) * 2019-10-28 2020-02-11 德蓝水技术股份有限公司 Industrial acidic wastewater treatment agent

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Application publication date: 20121107