CN100504263C - Blue algae volume reduction technique - Google Patents
Blue algae volume reduction technique Download PDFInfo
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- CN100504263C CN100504263C CNB2007100256982A CN200710025698A CN100504263C CN 100504263 C CN100504263 C CN 100504263C CN B2007100256982 A CNB2007100256982 A CN B2007100256982A CN 200710025698 A CN200710025698 A CN 200710025698A CN 100504263 C CN100504263 C CN 100504263C
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Abstract
A volume reduction treatment process for cyanobacterias belongs to the technical field of the water treatment. The polyaluminium chloride is added in the cyanobacteria pulp and then the polyacrylamide is added in after the cyanobacteria pulp is stirred for five to sixty seconds, after the stirring is implemented for five to sixty seconds, the clay is added in and the cyanobacteria pulp is sufficiently stirred to be uniform so as to implement the dehydration, and then the cyanobacteria cakes or cyanobacteria slags are formed. After being treated by using the process, the cyanobacteria pulp is changed into the cyanobacteria cakes or cyanobacteria slag, the liquid water content of which is smaller than 90%; the volume reduction quantity is larger than or equal to 90%. The process is suitable for various cyanobacterias of different consistencies, allows continuous operation mode and also interval operation mode, is highly efficient and saves energy, is safe and reliable, causes no secondary pollution, not only can be implemented beside the lake, but also go into the mobile operation process on the cyanobacteria salving boat on the lake.
Description
Technical field
The invention belongs to water-treatment technology field, refer in particular to the technology of handling blue-green algae, i.e. blue algae volume reduction technique.
Background technology
Blue-green algae belongs to " unicellular ", and is widely distributed, no matter is all can grow in fresh water or depression or low foster or high waters of supporting.Blue-green algae can breed rapidly, discharges stench, makes water quality become poison, color change.The toxin that blue-green algae discharges in water body can directly have influence on the health of animal and human's class.The mankind swim in the waters that polluted by blue-green algae, can cause diseases such as skin sensitivity, gastrointestinal system and respiratory system.
To the processing of blue-green algae, directly land-fill method of back is salvaged in domestic common employing, but the blue-green algae water content that salvages is big, needs more occupation of land during landfill disposal, and processing fully of the nitrogen phosphorus in the blue-green algae, and landfill also can cause secondary pollution.
Summary of the invention
The invention provides a kind of blue algae volume reduction technique, obtain to carry out postorders processing such as compost or anhydration and incineration again behind algal biscuit or the algae-residue, main design philosophy is blue algae slurry to be mixed with flocculant stir, form in a short time than dehydration behind the big flocculating body and separate, specifically implement like this: blue algae volume reduction technique, it is characterized in that in blue algae slurry, adding aluminium polychloride (PAC), stir 5-60 and add polyacrylamide (PAM) after second again, stir 5-60 second, add clay, fully stir evenly the back dehydration, form algal biscuit or algae-residue.Adopt three kinds of flocculants in this technology, at first be PAC, main rising makes that the blue-green algae monomer polymerization becomes little zoogloea in the lake water, visible its of naked eyes forms graininess, and the compression double electric layer of its hydrolysate, electrically neutralization, the winding net is caught and the effect of adsorbing four aspects such as bridging is accomplished polymerization process; Next is PAM, and main effect is to utilize its huge surperficial suction-operated, makes the blue-green algae of the preliminary polymerization of the suspension in the algae water form flco, and its macromolecular chain twines crosslinked mutually, forms to build bridge, thereby makes flocculent structure increase chap, forms big blue-green algae flco at last; Be clay at last, it plays booster action in whole flocculation, by adding clay the blue-green algae flco is separated preferably with water.
In order to implement this technology better, the volumetric concentration of first sampling and measuring flco blue-green algae before the flocculation, determine the addition of PAC, PAM, clay again according to flco blue-green algae volumetric concentration, assay method is to add PAM in the blue algae slurry before flocculation until whole formation flcos, after the static layering, observe the volume ratio of water layer and blue-green algae layer, calculate the volumetric concentration of flco blue-green algae, and then flocculant is added in gradation, the PAC addition of every liter of flco blue-green algae is 1-5g, the PAM addition of every liter of flco blue-green algae is 0.01-0.1g, and the clay addition of every liter of flco blue-green algae is 10-50g.
In this technology, PAC and PAM add with the solution form, it is unlikely too big to add volume when considering to handle, PAC concentration is formulated in more than the 10g/L, and PAM is mixed with 0.05%-0.5%, and the concentration of PAM can not be too low, otherwise the volumetric errors when surveying blue-green algae concentration is bigger, the concentration of PAM can not be too high, otherwise solution viscosity is big, is not easy to flocculation.
Consider that the former algae slurry water content on salvaging is very high from the lake, it is big directly to carry out the flocculation treatment volume, increase load, for the ease of handling, this technology is carried out preliminary treatment to former algae slurry earlier, promptly with the former algae slurry of dissolved air water preliminary treatment, algae in the former algae slurry is combined with micro-bubble in the dissolved air water, come-up together, preliminary algae moisture from after, obtain the flocculation process that the higher blue algae slurry of concentration carries out postorder again.
The dehydration of this technology can be adopted the belt filter press dehydration, a strainer of belt filter press is coated on the drive pressure roller, another strainer places and forms a strainer circulation on the pressure roller group of drive pressure roller bottom, each roller of described pressure roller group is radially adjustable pressure roller, make the radial clearance of each roller of pressure roller group and drive pressure roller adjustable, except that utilizing the strainer tensile force to come the press filtration, increased gap squeezing mode, but the pressure size between two strainers of regulated at will, to blue-green algae flco squeezing better effects if, moisture content is lower, and the laying of this strainer, make the more reasonable compactness of equipment, reduced by a cover belt EGR, cost is low.When preventing press filtration, blue-green algae is flowed out from the strainer slit and forms secondary pollution, is implanted with fine hair on the strainer of belt filter press, cilium on the fine hair strainer can wrap up blue-green algae when press filtration, press filtration water flows away from the slit, and blue-green algae is then hindered on strainer by cilium, can not taken away by water.Separate for algal biscuit or algae-residue after will squeezing easily, belt filter press is equipped with scraper plate before the drive pressure roller of two fine hair strainer separation place, and fine hair strainer disengaging place of pressure roller group also is equipped with scraper plate.
Algal biscuit or algae-residue have been become with blue algae slurry after this PROCESS FOR TREATMENT, its moisture content<90%, blue-green algae subtract capacity 〉=90%, the blue-green algae that is suitable for various variable concentrations, mode of operation can be continuously can be intermittently, energy-efficient, safe and reliable, non-secondary pollution promptly can also can drag for mobile operational process on the algae ship in the lakeside effect in the lake.
Description of drawings
Accompanying drawing is the structural representation of this technology belt filter press.
The specific embodiment
Embodiment 1, blue algae volume reduction technique, the volumetric concentration of first sampling and measuring flco blue-green algae before the flocculation, assay method is to add polyacrylamide in the blue algae slurry before flocculation until whole formation flcos, after the static layering, observe the volume ratio of water layer and blue-green algae layer, calculate the volumetric concentration of flco blue-green algae, in blue algae slurry, add aluminium polychloride, the aluminium polychloride addition of every liter of flco blue-green algae is 1-5g, stir 5-60 and add polyacrylamide after second again, the polyacrylamide addition of every liter of flco blue-green algae is 0.01-0.1g, stirs 5-60 second, add clay, the clay addition of every liter of flco blue-green algae is 10-50g, fully stirs evenly the back with the belt filter press dehydration, forms algal biscuit or algae-residue.Aluminium polychloride and polyacrylamide are to add with the solution form in this technology, and aluminium polychloride concentration is formulated in more than the 10g/L, and polyacrylamide is mixed with 0.05%-0.5%.
The belt filter press of dehydration usefulness is through transforming (with reference to the accompanying drawings), article two, all be implanted with fine hair on the strainer 1, article one, strainer 1 is coated on the drive pressure roller 2, another strainer 1 places and forms a strainer circulation on the pressure roller group 3 of drive pressure roller 2 bottoms, each roller of pressure roller group 3 is radially adjustable pressure roller, be equipped with scraper plate 4 before the drive pressure roller 2 of two fine hair strainers, 1 separation place, fine hair strainer 1 disengaging place of pressure roller group 3 also is equipped with scraper plate 4.
Claims (8)
1. blue algae volume reduction technique is characterized in that adding flocculant poly aluminium chloride in blue algae slurry, stirs 5-60 and adds the flocculant polyacrylamide after second again, stirs 5-60 second, adds the flocculant clay, fully stirs evenly the back dehydration, forms algal biscuit or algae-residue.
2. blue algae volume reduction technique according to claim 1, the volumetric concentration of first sampling and measuring flco blue-green algae before it is characterized in that flocculating, assay method is to add polyacrylamide in the blue algae slurry before flocculation until whole formation flcos, after the static layering, observe the volume ratio of water layer and blue-green algae layer, calculate the volumetric concentration of flco blue-green algae, and then flocculant is added in gradation, the aluminium polychloride addition of every liter of flco blue-green algae is 1-5g, the polyacrylamide addition of every liter of flco blue-green algae is 0.01-0.1g, and the clay addition of every liter of flco blue-green algae is 10-50g.
3. blue algae volume reduction technique according to claim 1 and 2 is characterized in that aluminium polychloride and polyacrylamide add with the solution form, and aluminium polychloride concentration is formulated in more than the 10g/L, and polyacrylamide is mixed with 0.05%-0.5%.
4. blue algae volume reduction technique according to claim 1 is characterized in that the former algae slurry that elder generation directly salvages from the lake with the dissolved air water preliminary treatment, and preliminary algae moisture obtains blue algae slurry to be flocculated from the back.
5. blue algae volume reduction technique according to claim 1 is characterized in that the dehydration of dehydration employing belt filter press.
6. blue algae volume reduction technique according to claim 5, a strainer that it is characterized in that belt filter press is coated on the drive pressure roller, another strainer places and forms a strainer circulation on the pressure roller group of drive pressure roller bottom, and each roller of described pressure roller group is radially adjustable pressure roller.
7. blue algae volume reduction technique according to claim 6 is characterized in that being implanted with fine hair on the strainer of belt filter press.
8. blue algae volume reduction technique according to claim 7 is characterized in that belt filter press is equipped with scraper plate before the drive pressure roller of two fine hair strainer separation place, and fine hair strainer disengaging place of pressure roller group also is equipped with scraper plate.
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CNB2007100256982A CN100504263C (en) | 2007-08-14 | 2007-08-14 | Blue algae volume reduction technique |
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CNB2007100256982A CN100504263C (en) | 2007-08-14 | 2007-08-14 | Blue algae volume reduction technique |
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CN100504263C true CN100504263C (en) | 2009-06-24 |
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Families Citing this family (6)
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CN102303942B (en) * | 2011-04-16 | 2013-11-13 | 安徽合协生态环境科技有限公司 | Blue alga cake tubular pyrohydrolysis dewatering method and device |
CN103588380A (en) * | 2013-11-15 | 2014-02-19 | 江苏绿威环保科技有限公司 | Algae mud deep dehydration method by utilizing strong oxidizing agent |
CN103896429B (en) * | 2014-03-06 | 2015-10-28 | 复旦大学 | A kind of algae water separation device and method being applicable to lake treatment |
CN104402166A (en) * | 2014-10-16 | 2015-03-11 | 滁州友林科技发展有限公司 | Industrial sewage treatment process |
CN109626530A (en) * | 2018-12-21 | 2019-04-16 | 南开大学 | A kind of synchronous dephosphorization of landscape water body with high salt is except algae built-up flocculant and preparation method thereof |
CN116675391B (en) * | 2023-07-14 | 2024-03-12 | 河海大学 | Algae-water separation process for treating lake nannochloropsis water bloom |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1059644A (en) * | 1991-07-29 | 1992-03-25 | 天津市房地产开发经营集团塘沽总公司 | The processing method of algae paste after collecting of salt algae |
CN1267447A (en) * | 1999-03-19 | 2000-09-27 | 中国科学院水生生物研究所 | Harvest and processing method of microbial algae shuihua |
JP2004174305A (en) * | 2002-11-25 | 2004-06-24 | Sanei Kaihatsu:Kk | Method and apparatus for treating inorganic sludge |
CN1215166C (en) * | 2003-09-02 | 2005-08-17 | 中国科学院水生生物研究所 | Process for preparing water bloom blue-green algae harvest on lake |
CN1323035C (en) * | 2004-10-19 | 2007-06-27 | 殷肇君 | Method for cleaning out blue algae of water area |
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- 2007-08-14 CN CNB2007100256982A patent/CN100504263C/en active Active
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1059644A (en) * | 1991-07-29 | 1992-03-25 | 天津市房地产开发经营集团塘沽总公司 | The processing method of algae paste after collecting of salt algae |
CN1267447A (en) * | 1999-03-19 | 2000-09-27 | 中国科学院水生生物研究所 | Harvest and processing method of microbial algae shuihua |
JP2004174305A (en) * | 2002-11-25 | 2004-06-24 | Sanei Kaihatsu:Kk | Method and apparatus for treating inorganic sludge |
CN1215166C (en) * | 2003-09-02 | 2005-08-17 | 中国科学院水生生物研究所 | Process for preparing water bloom blue-green algae harvest on lake |
CN1323035C (en) * | 2004-10-19 | 2007-06-27 | 殷肇君 | Method for cleaning out blue algae of water area |
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