CN1319640C - Method for preparing active fly ash phosphorus adsorbent - Google Patents
Method for preparing active fly ash phosphorus adsorbent Download PDFInfo
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- CN1319640C CN1319640C CNB2004100991975A CN200410099197A CN1319640C CN 1319640 C CN1319640 C CN 1319640C CN B2004100991975 A CNB2004100991975 A CN B2004100991975A CN 200410099197 A CN200410099197 A CN 200410099197A CN 1319640 C CN1319640 C CN 1319640C
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Abstract
The present invention relates to a method for preparing active fly ash phosphorus adsorbent agents. Fly ash and alkaline activating agents are evenly mixed in a high speed mixer and thrown into a calciner for calcination and activation; cooled materials after calcination are thrown into an acid resistant reaction jar, acid modifying agents are added, and the materials are heated and react; the materials after reaction are dried and ground; thus, the powdery high active phosphorus adsorbent agents are made. By using industrial waste of the fly ash as the raw material and using the activating agents and the modifying agents with low cost, the present invention dissolves large amount of substances in the fly ash, which have the potential to absorb phosphorus. The prepared adsorbent agents have high phosphorus removing efficiency.
Description
Technical field
The present invention relates to a kind of preparation method of active fly ash phosphorus adsorbent, be a kind of be the preparation of adsorbent method that is used for removing water phosphorus of raw material with trade waste flyash, belong to water-treatment technology field.
Background technology
In recent years, lake, the river eutrophication pollution that too much causes owing to the nutriments such as nitrogen phosphorus in the water body become the great environmental problem that China faces.Scientific research shows, just may break out the blue-green alge wawter bloom when the total phosphorus content in the unhurried current water bodys such as lake and reservoir surpasses 0.02mg/L.Mostly adopt bioanalysis or physico-chemical process dephosphorization at present both at home and abroad.Need the sewage treatment plant of the cities of secondary grade of routine be transformed on a large scale when adopting the biological phosphate-eliminating method, construction cost and operating cost increase greatly.Though need not reconstruct when adopting physico-chemical process, can directly add chemical agent or phosphorus adsorbent at the preliminary sedimentation tank or the second pond of Sewage Plant, but up to the present, selected medicament mostly is conventional aluminium salt or adsorbents such as molysite and active oxidation ferro-aluminum, its dispensing cost is too high, and removal effect is limited.
On the other hand, be accompanied by China's rapid economic development, the energy demand surge.Coal occupies the principal status of public economy always in the energy resource structure of China.Flyash is the trade waste that produces in the coal burning process, and the flyash total amount of China power plant generation every year on average is more than 100,000,000 tons.At present, the disposal options of flyash is based on the ash disposal area stacking.According to measuring and calculating, the construction cost of the large-scale ash disposal area of general power plant is all about in the of 100,000,000 yuan, but also taken a large amount of soils, and environment is produced huge potential hazard.In China, comprehensive utilization rate of coal ash only is about 40%, substantially all is applied to building industry, to produce the admixture in light building material such as flyash brick, lytag and concrete, the mortar.But this type of flyash production cost of products height, added value is low, is unfavorable for extensive popularization.Therefore,, press for to find and can improve the flyash added value of product for solving the problem of complex utilization of flyash, and technology new purposes with low cost.
Numerous discovering both domestic and external, the alternative chemical agent of flyash adds dephosphorization in sewage.Pertinent literature as: 1, modified coal ash is removed phosphorus and the colourity in the antibiotic waste water. Chinese water supply and drainage .2002.18 (10) .49-51.2, flyash Study on Removal of Phosphorus in Wastewater. Shanghai environmental science .2000.19 (1) .33-34.Utilize the flyash dephosphorization, the treatment of wastes with processes of wastes against one another, with low cost, be fit to China's national situation.Although generally believing the maximum phosphorus adsorption capacity of flyash reaches about 20g/kg, but for complicated component, phosphorus concentration is the real life sewage of 2-5mg/L, and the dephosphorization ability of flyash only can be brought into play about 5-10%, thereby has increased the dosage of flyash in the unit sewage greatly.Facts have proved that will seek out the removal efficient more than 60%, the dosage of conventional flyash must reach more than the 2g/L, and the content of activated sludge also only is 2g/L in the B-grade sewage treatment plant aeration tank.So high dosage causes following three big problems: 1. ash content is too much, and the Ash Water Separator difficulty causes solid suspension in the water outlet-SS severe overweight; 2. contain a large amount of free state calcium oxide in the flyash, generate calcium hydroxide behind calcium oxide and the water generation chemical reaction, thereby promote basicity, practical study shows, when dosage is 2g/L in the sewage pH value significantly be elevated to 10, exceed national B-grade sewage discharge standard; 3. sludge output is excessive, and it is big that Treatment of Sludge is disposed difficulty.Therefore be necessary flyash is activated and modification,, increase substantially the phosphorus treating capacity of its Unit Weight part to give full play to the dephosphorization usefulness of flyash, thus the dosage when reducing practical engineering application greatly.
Summary of the invention
The objective of the invention is to deficiency, a kind of preparation method of active fly ash phosphorus adsorbent is provided, have the adsorbent that method is easy, production cost is low, prepare and have the big characteristics of Unit Weight part phosphorus treating capacity at existing technology.
For realizing such purpose, the present invention utilizes trade waste flyash to be raw material, flyash and alkaline activation agent are mixed calcination activation in the input roaster of back in high-speed mixer, again the material that cools off after the roasting is dropped in the acid tolerance response jar, add sour modifier and add thermal response, with the levigate highly active phosphorus adsorbent of powdery of promptly making of reacted drying materials.The present invention will have phosphorus absorption potentiality by activator and modifier cheaply in the flyash a large amount of strippings of material, the adsorbent that makes has great dephosphorization usefulness.
The composition of active fly ash phosphorus adsorbent of the present invention and consumption (weight portion) are as follows:
Flyash: 100, activator: 20-100, modifier: 50
The used activator of the present invention is a sodium metasilicate, calcium silicates, and calcium carbonate, sodium carbonate etc., modifier is 5-10% hydrochloric acid by weight percentage, 5-30% sulfuric acid, acid solutions such as 5-10% nitric acid.
The preparation method of active fly ash phosphorus adsorbent of the present invention is as follows:
1, be that 100 parts flyash and the activator of 20-100 part mix in high-speed mixer with weight portion.
2, mixture is dropped into the activation of medium temperature roast kiln roasting.Sintering temperature is at 600 ℃-1000 ℃, roasting time 1-4 hour.Material behind the calcination activation is taken out and cooling.
3, cooled material is dropped in the acid tolerance response jar, add weight portion and be 50 parts sour modifier and be heated to 60 ℃, reacted 4-10 hour.
4, reacted material is taken out, the oven dry back is levigate promptly makes Powdered highly active phosphorus adsorbent.
Innovation part of the present invention is will have in the flyash by activator and modifier cheaply a large amount of strippings of material of phosphorus absorption potentiality, has given play to the dephosphorization potentiality of flyash to greatest extent.Contain a large amount of glass microballoon bodies as script in the flyash, but, many holes occur after the glass microballoon body weathers, greatly increased the specific area of glass microballoon, improved the materialization of glass microballoon self and inhaled the phosphorus ability through after the above PROCESS FOR TREATMENT; Also contain a large amount of aluminium oxide, iron oxide for another example in the flyash,, can directly act on phosphate and generate aluminum phosphate, ferric phosphate precipitation through meeting stripping aluminium ion, iron ion after the above PROCESS FOR TREATMENT.
Advantage of the present invention and positive role are embodied in: 1. the Unit Weight phosphorus adsorbance at actual sewage reaches per kilogram flyash 10 gram phosphorus to per kilogram flyash 30 gram phosphorus, be more than 10 times of ordinary fly ash, if the phosphorus content of real life sewage is 3mg/L, obtain the clearance more than 70%, required flyash dosage is about 2-5g/L, and required active fly ash adsorbent dosage only is 50-100mg/L, thereby the dosage when reducing practical engineering application has greatly solved a series of problems of bringing owing to dosage is too high simultaneously.2. inhale phosphorus in this adsorbent input sewage and be exceedingly fast, one minute with the interior effect that just can reach more than 90%.3. be neutral after this adsorbent drops in the water, effectively the pH scope is very wide, between 4-11.4. employing wide material sources, supplying stable trade waste flyash is raw material, and its production cost is far below aluminium salt commonly used, and medicaments such as molysite and activated alumina are fit to China's national situation.Regeneration resource, solved the handling problems of flyash effectively.Phosphorus content is high in the mud that generates after disposing of sewage, and can directly reclaim phosphorus, also can be used for soil improvement.
The specific embodiment
Below by specific embodiment technical scheme of the present invention is further described.Enforcement of the present invention is not limited to following examples.
Embodiment 1
Raw material adopts the Shanghai fly ash in electric power plant, and 10 kilograms of flyash and 2 kilograms of sodium metasilicate are mixed in high-speed mixer.Mixture drops in the medium temperature roast stove at 600 ℃ of calcination activations, roasting time 1 hour.Taking-up of material behind the calcination activation and cooling back are dropped in the acid tolerance response jar, add 5L5% hydrochloric acid and also be heated to 60 ℃, reacted 4 hours.The reaction back generates material, with levigate totally 11.2 kilograms of the Powdered highly active phosphorus adsorbent products of promptly making behind this drying materials.
The phosphorus adsorbent that utilizes above-mentioned technology to make carries out sanitary sewage dephosphorization experiment.Sanitary sewage is taken from purification of water quality factory of Shanghai shen village, and former water phosphorus content is 2.9mg/L, and pH is 7.1.Get 1 gram phosphorus adsorbent and drop in this sanitary sewage of 10L, stirred fast 1 minute, staticly settled 2 minutes.PH is 7.0 in the water of processing back, and phosphorus concentration is 1.3mg/L, and tp removal rate is 55.2%, and the phosphorus adsorbance is 16mg/kg.
Embodiment 2
Raw material adopts the Shanghai fly ash in electric power plant, and 10 kilograms of flyash and 10 kilograms of calcium silicates are mixed in high-speed mixer.Mixture drops in the medium temperature roast stove at 1000 ℃ of calcination activations, roasting time 4 hours.Taking-up of material behind the calcination activation and cooling back are dropped in the acid tolerance response jar, add 5L10% sulfuric acid and also be heated to 60 ℃, reacted 10 hours.The reaction back generates material, with levigate totally 19.7 kilograms of the Powdered highly active phosphorus adsorbent products of promptly making behind this drying materials.
The phosphorus adsorbent that utilizes above-mentioned technology to make carries out sanitary sewage dephosphorization experiment.Sanitary sewage is taken from purification of water quality factory of Shanghai shen village, and former water phosphorus content is 2.9mg/L, and pH is 7.1.Get 1 gram phosphorus adsorbent and drop in this sanitary sewage of 10L, stirred fast 1 minute, staticly settled 2 minutes.PH is 6.9 in the water of processing back, and phosphorus concentration is 0.2mg/L, and tp removal rate is 93%, and the phosphorus adsorbance is 27mg/kg.
Embodiment 3
Raw material adopts the Shanghai fly ash in electric power plant, and 10 kilograms of flyash and 3 kilograms of calcium carbonate are mixed in high-speed mixer.Mixture drops in the medium temperature roast stove at 700 ℃ of calcination activations, roasting time 2 hours.Taking-up of material behind the calcination activation and cooling back are dropped in the acid tolerance response jar, add 5L7% nitric acid and also be heated to 60 ℃, reacted 6 hours.The reaction back generates material, with levigate totally 12.6 kilograms of the Powdered highly active phosphorus adsorbent products of promptly making behind this drying materials.
The phosphorus adsorbent that utilizes above-mentioned technology to make carries out sanitary sewage dephosphorization experiment.Sanitary sewage is taken from purification of water quality factory of Shanghai shen village, and former water phosphorus content is 2.9mg/L, and pH is 7.1.Get 1 gram phosphorus adsorbent and drop in this sanitary sewage of 10L, stirred fast 1 minute, staticly settled 2 minutes.PH is 6.9 in the water of processing back, and phosphorus concentration is 0.6mg/L, and tp removal rate is 79.3%, and the phosphorus adsorbance is 23mg/kg.
Embodiment 4
Raw material adopts the Shanghai fly ash in electric power plant, and 10 kilograms of flyash and 4 kilograms of sodium carbonate are mixed in high-speed mixer.Mixture drops in the medium temperature roast stove at 700 ℃ of calcination activations, roasting time 3 hours.Taking-up of material behind the calcination activation and cooling back are dropped in the acid tolerance response jar, add 5L7% hydrochloric acid and also be heated to 60 ℃, reacted 7 hours.The reaction back generates material, with levigate totally 13.5 kilograms of the Powdered highly active phosphorus adsorbent products of promptly making behind this drying materials.
The phosphorus adsorbent that utilizes above-mentioned technology to make carries out sanitary sewage dephosphorization experiment.Sanitary sewage is taken from purification of water quality factory of Shanghai shen village, and former water phosphorus content is 2.9mg/L, and pH is 7.1.Get 1 gram phosphorus adsorbent and drop in this sanitary sewage of 10L, stirred fast 1 minute, staticly settled 2 minutes.PH is 6.8 in the water of processing back, and phosphorus concentration is 1.3mg/L, and tp removal rate is 55.2%, and the phosphorus adsorbance is 16mg/kg.
Claims (3)
1, a kind of preparation method of active fly ash phosphorus adsorbent, it is characterized in that with weight portion being that 100 parts flyash and the alkaline activation agent of 20-100 part mix in high-speed mixer, then mixture is dropped into calcination activation in the roaster, 600 ℃-1000 ℃ of sintering temperatures, after roasting 1-4 hour material is taken out and cooling, again cooled material is dropped in the acid tolerance response jar, adding weight portion is 50 parts sour modifier and is heated to 60 ℃, reacted 4-10 hour, after the reaction material is taken out, the oven dry back is levigate promptly makes Powdered highly active phosphorus adsorbent.
2, according to the preparation method of the active fly ash phosphorus adsorbent of claim 1, it is characterized in that described alkaline activation agent is sodium metasilicate, calcium silicates, calcium carbonate or sodium carbonate.
3,, it is characterized in that described sour modifier is 5-10% hydrochloric acid, 5-30% sulfuric acid or 5-10% nitric acid by weight percentage according to the preparation method of the active fly ash phosphorus adsorbent of claim 1.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2004100991975A CN1319640C (en) | 2004-12-29 | 2004-12-29 | Method for preparing active fly ash phosphorus adsorbent |
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| Application Number | Priority Date | Filing Date | Title |
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| CNB2004100991975A CN1319640C (en) | 2004-12-29 | 2004-12-29 | Method for preparing active fly ash phosphorus adsorbent |
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| CN1669632A CN1669632A (en) | 2005-09-21 |
| CN1319640C true CN1319640C (en) | 2007-06-06 |
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| CNB2004100991975A Expired - Fee Related CN1319640C (en) | 2004-12-29 | 2004-12-29 | Method for preparing active fly ash phosphorus adsorbent |
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| CN100366337C (en) * | 2005-09-29 | 2008-02-06 | 上海交通大学 | Method for preparing absorbent with phosphor concentration and phosphor reclaim function |
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| CN102531092A (en) * | 2012-01-17 | 2012-07-04 | 中国科学院水生生物研究所 | Method for removing phosphorus by utilizing waste cement |
| CN102631890A (en) * | 2012-05-02 | 2012-08-15 | 湖北富邦科技股份有限公司 | Preparation method of modified fly ash adsorbent |
| CN102746023B (en) * | 2012-06-15 | 2013-09-18 | 中国建筑股份有限公司 | Constructed wetland matrix filling material for simultaneous nitrogen and phosphorus removal and its preparation method |
| CN102728311A (en) * | 2012-06-20 | 2012-10-17 | 湖北富邦科技股份有限公司 | Preparation method of modified fly ash adsorbent used in phosphorous-containing waste water treatment |
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| CN103449559A (en) * | 2013-09-16 | 2013-12-18 | 中国科学院城市环境研究所 | Method and application for using building abandoned cement brick as dephosphorization filler |
| CN103816871A (en) * | 2014-02-28 | 2014-05-28 | 吴从兵 | Method for modifying fly ash by employing low-energy particles |
| CN105858776A (en) * | 2016-04-07 | 2016-08-17 | 合肥市市政设计院有限公司 | Method for removing phosphates in water body on basis of sulfuric-acid-modified fly ash brick powder (S-FABP) |
| CN111019693A (en) * | 2019-12-05 | 2020-04-17 | 渭南师范学院 | Universal diesel oil decoloring deodorant and preparation and regeneration method thereof |
| CN111807632B (en) * | 2020-07-21 | 2023-01-31 | 吉林化工学院 | Method for treating dye wastewater by using modified fly ash |
| CN113000014B (en) * | 2021-03-02 | 2023-04-21 | 常熟理工学院 | Method for preparing efficient dephosphorizing agent by utilizing waste incineration fly ash and product thereof |
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| CN1220978A (en) * | 1997-12-25 | 1999-06-30 | 张耀伦 | Less clinker high early strength flyash cement |
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2004
- 2004-12-29 CN CNB2004100991975A patent/CN1319640C/en not_active Expired - Fee Related
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1220978A (en) * | 1997-12-25 | 1999-06-30 | 张耀伦 | Less clinker high early strength flyash cement |
Non-Patent Citations (1)
| Title |
|---|
| 改性粉煤灰去除抗生素沸水中的磷和色度 张杰等，中国给水排水，第18卷第10期 2002 * |
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| CN1669632A (en) | 2005-09-21 |
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