CN103232101A - Water treatment flocculating agent - Google Patents
Water treatment flocculating agent Download PDFInfo
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- CN103232101A CN103232101A CN2013102125632A CN201310212563A CN103232101A CN 103232101 A CN103232101 A CN 103232101A CN 2013102125632 A CN2013102125632 A CN 2013102125632A CN 201310212563 A CN201310212563 A CN 201310212563A CN 103232101 A CN103232101 A CN 103232101A
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Abstract
The invention discloses a water treatment flocculating agent. The water treatment flocculating agent consists of the following components: 15 to 30 weight parts of aluminum-containing compound, 15 to 20 weight parts of ferric citrate, 5 to 8 weight parts of polymeric ferric sulfate, 3 to 5 weight parts of sodium ferrate, 5 to 10 weight parts of polymeric aluminum chloride. 10 to 15 weight parts of non-ionic polyacrylamide, 5 to 10 weight parts of polyamine compounds and 3 to 5 weight parts of the mixer of porous perlite micro-powder and coal ash micro-powder. According to the water treatment flocculating agent, the molecular weight of the flocculating agent is increased by introducing the polyamine compounds, so that the water treatment flocculating agent is high in viscosity and high in stability, facilitates industrial production,and has the characteristics of quick sedimentation, good decoloring effect and the like.
Description
Technical field
The invention discloses a kind of water treatment additive, particularly a kind of water treatment flocculant.
Background technology
Flocculation agent mainly is just to have (bearing) electrical group to neutralize and have some particles that negative (just) electrically be difficult to separate in some water or be particle, reduce its electromotive force, it is played pendulum, and utilize its aggregation property to make these particles concentrate, and separate by physics or chemical process.Be generally the medicament that reaches this purpose and use, be referred to as flocculation agent.Flocculation agent is mainly used in feedwater and sewage treatment area.The chemical agent coagulating sedimentation is the method for generally using in the water technology.This method has less investment, takes up an area of little, characteristics such as working cost is low, wide adaptability.In the water treatment coagulating sedimentation, relate to flocculation agent feed intake opportunity, feed intake environment control, charging capacity, stimulation effect etc. widely, to reach suitable flocculating effect, satisfy the requirement to water treatment.The dyeing waste water complicated component, colourity is big, the concentration height, hard-degraded substance is many, and the COD value is high, and water quality is changeable, the main difficult point of handling such waste water is decolouring, adopt flucculation process treatment of dyeing and printing medicament commonly used based on inorganic aluminate, molysite at present, but these materials are relatively poor to the decolorizing effect of reactive dyestuffs, matching stain etc., are difficult to reach actual environment and administer requirement.
Summary of the invention
For addressing the above problem, the invention discloses a kind of water treatment flocculant, form simple, raw material sources are extensive, with low cost, to produce easy to usely, charging capacity is little, stimulation effect is good, flocculating effect is good, can efficiently generate gel flocculation deposition, thereby can reduce the flocculating and purifying cost effectively, improve the utilization ratio of water treatment efficiency and flocculation agent, be conducive to reduce the cost of water treatment.
For achieving the above object, the method that the present invention adopts is: a kind of water treatment flocculant, and composed of the following components: the aluminum contained compound of 15-30 weight part, the ironic citrate of 15-20 weight part, the bodied ferric sulfate of 5-8 weight part, the Na2Fe04 of 3-5 weight part; The polymerize aluminum chloride of 5-10 weight part, the non-ionic polyacrylamide of 10-15 weight part, 5-10 weight part polyamine compounds, and expanded perlite micro mist and the flyash micro mist mixture of 3-5 weight part; When described flocculation agent is 1g/l in usage quantity, be 97%-99% to the COD value for the percent of decolourization of the soil mud draining of 300-400mg/l, the COD clearance is 85%-89%, and the BOD clearance is 73%-76%, and total tp removal rate is 93%-95%, and total ammonia clearance is 44%-47%.
As a kind of improvement of the present invention, the granularity of described expanded perlite micro mist is the 200-300 order.
As a kind of improvement of the present invention, described flocculation agent activating component is the combination of described expanded perlite micro mist and flyash micro mist, and the weight ratio scope of expanded perlite micro mist and flyash micro mist is 3:2-5:3.
As a kind of improvement of the present invention, described polyamine compounds is a kind of in quadrol, the butanediamine or two kinds.
The invention has the beneficial effects as follows:
Flocculation agent disclosed by the invention, raw material sources are extensive, low production cost, charging capacity is little, the flocculation stimulation effect is good, and flocculation treatment is with low cost, and moisture resistance has good quality stability well simultaneously, long quality-guarantee period has good adaptive faculty to physical environment, and is easy to use.
Compound increases the flocculating agent molecule amount in the polyamines by introducing, and its viscosity is increased, and good stability is convenient to industrial production, and it is fast to have a sedimentation, characteristics such as good decolorizing effect.
By in flocculation agent, having added the flocculation agent activating component that is selected from a kind of or two combinations, the 3-5 weight part in expanded perlite micro mist and the flyash micro mist, not only improved the nucleation performance of stimulation effect and the gel of flocculation agent effectively, be conducive to reduce charging capacity, promote water treatment capacity, can regulate simultaneously the proportion of flocculation jello, increase the deposition capability of flocculation agent gel, thereby promoted the water treatment effect, reduce secondary pollution, improved the quality of handling water.
Embodiment
Embodiment one
The flocculation agent of present embodiment consists of the aluminum contained compound of 15 weight parts, the ironic citrate of 15 weight parts, the bodied ferric sulfate of 5 weight parts, the Na2Fe04 of 3 weight parts; The polymerize aluminum chloride of 5 weight parts, the non-ionic polyacrylamide of 10 weight parts, the expanded perlite micro mist of 5 weight part quadrols and 3 weight parts.
After getting the draining of 200mL soil mud, experimental group 1 and experimental group 2 are set: experimental group 1 is added present embodiment flocculation agent 200mg, and experimental group 2 is added commercially available flocculation agent 200mg, and stirring and evenly mixing is precipitated to clarification respectively, detects again.
Wherein the processing water ph value of experimental group 1 is 7.3, and percent of decolourization is 97.4%, COD clearance 85.9%, and the BOD clearance is 74.2%, total tp removal rate 93.7%, total 45.2%, 20 micron solid substance residual rate 28.3% of ammonia clearance, flocculation agent residual rate 10.2%.
The processing water ph value of experimental group 2 is 7.5, and percent of decolourization is 60%, COD clearance 50%, and the BOD clearance is 35%, total tp removal rate 50%, total 10%, 20 micron solid substance residual rate 65% of ammonia clearance, flocculation agent residual rate 53%.
Embodiment two
Flocculation agent consists of the aluminum contained compound of 30 weight parts, the ironic citrate of 20 weight parts, the bodied ferric sulfate of 8 weight parts, the Na2Fe04 of 5 weight parts; The polymerize aluminum chloride of 10 weight parts, the non-ionic polyacrylamide of 15 weight parts, the expanded perlite micro mist of 10 weight part quadrols and 5 weight parts.
After experimental group 3 is got the draining of 200mL soil mud, add present embodiment flocculation agent 200mg, stirring and evenly mixing, be precipitated to clarification, detect, wherein the processing water ph value of experimental group 3 is 7.1 again, and percent of decolourization is 98.7%, COD clearance 88.3%, the BOD clearance is 75.6%, total tp removal rate 94.6%, total ammonia clearance 46.3%, 20 microns solid substance residual rates 12.3%, flocculation agent residual rate 18.2%.
Embodiment three
Flocculation agent consists of the aluminum contained compound of 20 weight parts, the ironic citrate of 17 weight parts, the bodied ferric sulfate of 6 weight parts, the Na2Fe04 of 3.5 weight parts; The polymerize aluminum chloride of 7 weight parts, the non-ionic polyacrylamide of 12 weight parts, 7 weight part quadrols, 200 order expanded perlite micro mists of 2 weight parts and the flyash micro mist of 1.2 weight parts.
After experimental group 4 is got the draining of 200mL soil mud, add present embodiment flocculation agent 200mg, stirring and evenly mixing, be precipitated to clarification, detect, wherein the processing water ph value of experimental group 4 is 7.2 again, and percent of decolourization is 98.1%, COD clearance 86.6%, the BOD clearance is 75.1%, total tp removal rate 94.2%, total ammonia clearance 45.8%, 20 microns solid substance residual rates 15.8%, flocculation agent residual rate 14.2%.
Embodiment four
Flocculation agent consists of the aluminum contained compound of 25 weight parts, the ironic citrate of 19 weight parts, the bodied ferric sulfate of 7 weight parts, the Na2Fe04 of 4 weight parts; The polymerize aluminum chloride of 8 weight parts, the non-ionic polyacrylamide of 14 weight parts, 8.5 weight part quadrols, 200 order expanded perlite micro mists of 2.1 weight parts and the flyash micro mist of 1.4 weight parts.
After experimental group 5 is got the draining of 200mL soil mud, add present embodiment flocculation agent 200mg, stirring and evenly mixing, be precipitated to clarification, detect, wherein the processing water ph value of experimental group 5 is 7.1 again, and percent of decolourization is 98.3%, COD clearance 87.8%, the BOD clearance is 75.2%, total tp removal rate 94.2%, total ammonia clearance 45.8%, 20 microns solid substance residual rates 14.3%, flocculation agent residual rate 16.4%.
The disclosed technique means of the present invention program is not limited only to the disclosed technique means of above-mentioned technique means, also comprises the technical scheme of being made up of above technical characterictic arbitrary combination.The above is the specific embodiment of the present invention; should be pointed out that for those skilled in the art, under the prerequisite that does not break away from the principle of the invention; can also make some improvements and modifications, these improvements and modifications also are considered as protection scope of the present invention.
Claims (4)
1. a water treatment flocculant is composed of the following components: the aluminum contained compound of 15-30 weight part, the ironic citrate of 15-20 weight part, the bodied ferric sulfate of 5-8 weight part, the Na2Fe04 of 3-5 weight part; The polymerize aluminum chloride of 5-10 weight part, the non-ionic polyacrylamide of 10-15 weight part, 5-10 weight part polyamine compounds, and expanded perlite micro mist and the flyash micro mist mixture of 3-5 weight part; When described flocculation agent is 1g/l in usage quantity, be 97%-99% to the COD value for the percent of decolourization of the soil mud draining of 300-400mg/l, the COD clearance is 85%-89%, and the BOD clearance is 73%-76%, and total tp removal rate is 93%-95%, and total ammonia clearance is 44%-47%.
2. a kind of water treatment flocculant according to claim 1, it is characterized in that: the granularity of described expanded perlite micro mist is the 200-300 order.
3. a kind of water treatment flocculant according to claim 2, it is characterized in that: described flocculation agent activating component is the combination of described expanded perlite micro mist and flyash micro mist, and the weight ratio scope of expanded perlite micro mist and flyash micro mist is 3:2-5:3.
4. a kind of water treatment flocculant according to claim 1 is characterized in that: it is characterized in that: described polyamine compounds is a kind of in quadrol, the butanediamine or two kinds.
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CN201310212563.2A CN103232101B (en) | 2013-05-31 | 2013-05-31 | Water treatment flocculating agent |
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CN201310212563.2A CN103232101B (en) | 2013-05-31 | 2013-05-31 | Water treatment flocculating agent |
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Cited By (7)
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CN103496835A (en) * | 2013-09-30 | 2014-01-08 | 广东省微生物研究所 | In situ repair agent for sediments contaminated by polycyclic aromatic hydrocarbon compounds and repair method thereof |
CN104291425A (en) * | 2014-11-10 | 2015-01-21 | 北京泛博化学股份有限公司 | Special flocculation decolorizing agent for fur oxidation dyeing sewage and preparing method thereof |
CN105906008A (en) * | 2016-05-19 | 2016-08-31 | 太仓协大申泰羊毛衫有限公司 | Composite flocculant for processing printing and dyeing wastewater of wool fabric and preparation method of composite flocculant |
CN106186241A (en) * | 2016-09-27 | 2016-12-07 | 合肥天翔环境工程有限公司 | Flocculant for Acid Dye Wastewater |
CN107963690A (en) * | 2017-11-28 | 2018-04-27 | 芜湖上水源环保科技有限公司 | A kind of efficiently dyeing waste water flocculant preparation method |
CN107973382A (en) * | 2017-11-28 | 2018-05-01 | 芜湖上水源环保科技有限公司 | A kind of composite flocculation agent of rapid precipitation |
CN114132977A (en) * | 2021-11-30 | 2022-03-04 | 华中科技大学 | Natural water body purifying agent and preparation method and application thereof |
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CN101327976A (en) * | 2008-07-15 | 2008-12-24 | 南通立源水处理技术有限公司 | Efficient water treatment flocculant |
CN101428873A (en) * | 2008-11-28 | 2009-05-13 | 东莞理工学院 | Method for producing wastewater treatment material with microporous flyash brick fragment |
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CN102838195A (en) * | 2012-09-14 | 2012-12-26 | 大连格兰清水环境工程有限公司 | Composite flocculant for sewage treatment |
CN103102020A (en) * | 2012-11-14 | 2013-05-15 | 青岛海颐天仪器有限公司 | Wastewater treatment agent for paper mill |
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CN100430325C (en) * | 2003-01-31 | 2008-11-05 | 出光兴产株式会社 | Method for treating waste water containing hardly decomposable harmful substances |
CN101327976A (en) * | 2008-07-15 | 2008-12-24 | 南通立源水处理技术有限公司 | Efficient water treatment flocculant |
CN101428873A (en) * | 2008-11-28 | 2009-05-13 | 东莞理工学院 | Method for producing wastewater treatment material with microporous flyash brick fragment |
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CN102838195A (en) * | 2012-09-14 | 2012-12-26 | 大连格兰清水环境工程有限公司 | Composite flocculant for sewage treatment |
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Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
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CN103496835A (en) * | 2013-09-30 | 2014-01-08 | 广东省微生物研究所 | In situ repair agent for sediments contaminated by polycyclic aromatic hydrocarbon compounds and repair method thereof |
CN104291425A (en) * | 2014-11-10 | 2015-01-21 | 北京泛博化学股份有限公司 | Special flocculation decolorizing agent for fur oxidation dyeing sewage and preparing method thereof |
CN104291425B (en) * | 2014-11-10 | 2016-06-29 | 北京泛博化学股份有限公司 | The special flocculating decoloring agent of fur coat oxidising dyeing sewage and preparation method |
CN105906008A (en) * | 2016-05-19 | 2016-08-31 | 太仓协大申泰羊毛衫有限公司 | Composite flocculant for processing printing and dyeing wastewater of wool fabric and preparation method of composite flocculant |
CN106186241A (en) * | 2016-09-27 | 2016-12-07 | 合肥天翔环境工程有限公司 | Flocculant for Acid Dye Wastewater |
CN107963690A (en) * | 2017-11-28 | 2018-04-27 | 芜湖上水源环保科技有限公司 | A kind of efficiently dyeing waste water flocculant preparation method |
CN107973382A (en) * | 2017-11-28 | 2018-05-01 | 芜湖上水源环保科技有限公司 | A kind of composite flocculation agent of rapid precipitation |
CN114132977A (en) * | 2021-11-30 | 2022-03-04 | 华中科技大学 | Natural water body purifying agent and preparation method and application thereof |
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