CN109502833A - A kind of use in waste water treatment flocculant and preparation method thereof - Google Patents
A kind of use in waste water treatment flocculant and preparation method thereof Download PDFInfo
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/34—Treatment of water, waste water, or sewage with mechanical oscillations
- C02F1/36—Treatment of water, waste water, or sewage with mechanical oscillations ultrasonic vibrations
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
- C02F1/441—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by reverse osmosis
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
- C02F1/5236—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
- C02F1/5236—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents
- C02F1/5245—Treatment 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
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
- C02F1/54—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using organic material
- C02F1/56—Macromolecular compounds
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/66—Treatment of water, waste water, or sewage by neutralisation; pH adjustment
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/72—Treatment of water, waste water, or sewage by oxidation
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/72—Treatment of water, waste water, or sewage by oxidation
- C02F1/727—Treatment of water, waste water, or sewage by oxidation using pure oxygen or oxygen rich gas
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/10—Inorganic compounds
- C02F2101/105—Phosphorus compounds
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/08—Chemical Oxygen Demand [COD]; Biological Oxygen Demand [BOD]
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/22—O2
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2301/00—General aspects of water treatment
- C02F2301/08—Multistage treatments, e.g. repetition of the same process step under different conditions
Abstract
The present invention provides a kind of flocculants applied to wastewater treatment to belong to technical field of water treatment chemical more particularly to the flocculant for the processing for being applied to phosphorous oily waste water.The flocculant that the present invention uses is a kind of flocculant of modified polyacrylamide, has the effect of preferably removing COD, sediment and oils for phosphorous oiliness sewage treatment.
Description
Technical field
The present invention be number of patent application be 2016106042384, the applying date is on 07 28th, 2016, entitled " a kind of
The processing method of phosphorous oily waste water " patent of invention divisional application.
The present invention provides a kind of flocculants applied to wastewater treatment, more particularly to applied to phosphorous oily waste water
The flocculant of processing, belongs to technical field of water treatment chemical.
Background technique
Certain mechanical technologies will largely be made using the emulsion of oil-in-water type especially in the machinings such as cutting, grinding
Lubrication, cooling circulation liquid.Its main ingredient is machine oil or dormant oil (can also use animal and vegetable oil), emulsifier, lubricating and antirust agent and water
Emulsifier often uses sulfonated oil, petroleum sodium sulfonate and oleic acid etc..Antirust agent often uses zinc naphthenate, barium mahogany sulfonate, sodium nitrite, three
Ethanol amine, certain benzene homologues etc..In emulsion, although the content of oil emulsion is not high, less than 1% in emulsifying waste water.But
It is, due to the surface-active action of emulsifier, so that the structure of emulsion is highly stable, to be not easy to be destroyed.In certain emulsions
Mineral oil and additive toxicity it is very big, contain carcinogen.Such a waste emulsified mixture, if do not dealt with, direct emission,
On the pollution of environment and influence, than general oily wastewater zhang much.Therefore, to mechanical oily waste water, wherein especially elbow
The processing and prevention and treatment of emulsifying waste water, are very necessary.
In addition, the waste water discharged in machining industry can also be brought more serious other than bringing serious oily pollution
Phosphorus pollution.These pollution hands will be from machine plus the phosphorization treatment process in industry.So-called phosphorating treatment be to metal material and
A kind of chemical reprocessing technique that its article surface carries out.Dipped type is formed through parkerized metal material and its product surface
Phosphate film layer, the film layer and metallic matrix have good binding ability, wearability and the adhesive ability to coating, therefore, machine
The industries such as tool, steel all use phosphorization treatment technology to carry out the protective layer of production machinery part.Phosphorization treatment process generally comprises alkali
Remove several steps such as oil, hot water rinsing, cold rinse, acid pickling and rust removing, secondary cold rinse and phosphatization.It is main during its
Generate four kinds of waste water such as alkali-wash waste water, poaching wastewater, pickle liquor and etching waste liquor.
The elements such as phosphorus, nitrogen are exceeded in water, can accelerate the eutrophication of water body, and this phenomenon is more serious in China, give work
Industry, aquatic products industry, agricultural and tourist industry all bring great harm.The nutrient concentrations such as nitrogen, phosphorus increase, and are that algae is a large amount of
The reason of breeding, wherein again using phosphorus as key factor.Therefore, the concentration of phosphor in sewage how is effectively reduced, offsets depollution, protects
Retaining ring border, has a very important significance.Currently, sewage dephosphorization technology mainly has bioanalysis, chemical method two major classes both at home and abroad.It is raw
Object method such as A/O, A2/O technique are mainly suitable for processing low concentration and organic phosphorus-containing wastewater；Chemical method and physical-chemical process are main
There are the techniques such as coagulant sedimentation, crystallisation, ion exchange adsorption, electrodialysis, reverse osmosis, it is phosphorous to be mainly suitable for processing inorganic states
Waste water.
CN105417785A discloses a kind of reaction unit for handling high-concentration phosphorus-containing wastewater, is pre-processed by desulfurization wastewater single
Member, phosphorus recovery unit, deep phosphorous removal unit and desulfurization wastewater sludge pump form, and are provided with desulfurization in desulfurization wastewater pretreatment unit
Water intake, dosing mouth, blender, desulfurization wastewater supernatant water outlet and desulfurization wastewater mud discharging mouth；Phosphorus recovery unit
In be provided with high-concentration phosphorus-containing wastewater water inlet, blender, phosphorus-containing wastewater water outlet and phosphorous sediment discharge mouth；Deep phosphorous removal
The import of desulfurization wastewater sludge, blender, total water outlet and mud discharging mouth are provided in unit.Desulfurization wastewater after pretreatment can
Heavy metal and suspended matter therein are enough removed, the supernatant of high ph-values, high calcium magnesium ion is formed, is formed with high-concentration phosphorus-containing wastewater
The very low phosphorous sediment of height of content of beary metal；Phosphorus-containing wastewater after dephosphorization enters deep phosphorous removal unit, utilizes desulfurization wastewater dirt
Mud carries out chemisorption dephosphorization to phosphorus-containing wastewater, reduces water outlet phosphorus concentration, reaches discharge standard.CN103159341A discloses one
Kind treatment of Phosphorus Containing Waste Water technique.The treatment process includes the following steps: phosphorus-containing wastewater and oxidant after mixing, through pH tune
It saves agent adjustment pH value and obtains positive phosphorus acid ion to 4~6 progress oxidation reactions, then pH value is adjusted to 7~9 with pH adjusting agent to make just
Metal ion contained in phosphate radical and oxidant, which generates, to be precipitated, and precipitating is removed.
But above-mentioned method is bad for oil-containing and phosphorous water treatment effect simultaneously.
Summary of the invention
The purpose of the present invention is: solve the problems, such as the processing of the waste water simultaneously containing high concentration phosphorus and grease type COD, mainly
It is handled by the integration mode of oxidation, precipitating, ultrasonic wave added.
Technical solution is:
A kind of processing method of phosphorous oily waste water, includes the following steps:
Phosphorous oily waste water is first carried out pre-filtering, then is handled by wet oxidation by step 1；
The pH of feed liquid after oxidation processes is adjusted to 9~11 by step 2, then under conditions of ultrasonic wave added, and calcium precipitation is added
Agent and polyacrylamide flocculant carry out precipitation reaction and obtain the first feed liquid after removal precipitates；
The pH of first feed liquid is adjusted to 3~5, aluminium polychloride is added by step 3, carries out flocculation precipitation reaction, removal precipitating
Afterwards, the second feed liquid is obtained；
Second feed liquid is sent into reverse osmosis membrane and be filtered, obtains that treated and produce water by step 4.
Contain 0.1~5g/L of mineral oil, 0.1~3g/L of total phosphorus (TP) concentration in the phosphorous oily waste water.
The mineral oil is white oil, and the total phosphorus is made of phosphate, hypophosphites, phosphite.
In the step 1, the temperature range of wet oxidation is 125~220 DEG C, pressure limit is 0.5~5Mpa, oxygen
1~4g/L of gas additional amount.
In the step 1, ultrasound condition is 400~600kHz of frequency, 1~5W/cm of ultrasonic power2。
The calcium precipitation agent is selected from that calcium chloride, calcium oxide are one or more, the additional amount of calcium precipitation agent and total phosphorus
Molar ratio range is 2~4:1.
The additional amount of polyacrylamide is 0.5~3g/L.
The additional amount of aluminium polychloride is 1~5g/L respectively.
The preparation method of the polyacrylamide flocculant includes the following steps: S1, by weight, in reactor
Middle 35 parts of addition acrylamide monomer, 2 parts of tung oil, 3 parts of 2- acrylamido -2- methyl propane sulfonic acid (AMPS), N- butoxy
2 parts of Methacrylamide (NBMA), 4 parts of acrylic acid double cyclopentenyl ester (DCPA), 2 parts of chain extender l, 4- butanediol, water 150
Part, 3 parts of crosslinking agent acrylonitrile, 1 part of sorbitan ester class surfactant, 2 parts of catalyst dibutyltin dilaurylate are mixed
It closes uniformly, phosphoric acid regulation system pH value is added to 6, is passed through inert gas to remove the dissolved oxygen in reaction system；S2, by S1 institute
The reaction system obtained cools to 10 DEG C, adds 2 parts of initiator azo-bis-isobutyrate hydrochloride, heating carries out polymerization reaction；S3,
The jelly that the reactant that S2 is obtained obtains takes out, and after being granulated, dry, crushing, obtains polyacrylamide flocculant.
Beneficial effect
Wastewater treatment method provided by the invention can preferably be handled phosphorous and oil-containing waste water simultaneously, have technique
Simply, the advantages of high treating effect.
Specific embodiment
The unit of heretofore described additional amount, such as mg/L, g/L etc. all refer to outer in no special instruction
Ratio between the weight of adding medicine and the volume of waste water.
In method of the invention, the grease in waste water is decomposed by small-molecule substance by wet oxidation first, it is therefore prevented that
The influence that grease reacts calcium precipitate improves precipitation reaction efficiency；In addition, preventing small molecule grease pair by ultrasonic wave added
The influence of precipitation reaction enables flocculation reaction be removed more impurity.
Embodiment 1
Step 1, will contain white oil 0.1g/L, and the phosphorous oily waste water of total phosphorus (TP) concentration 0.1g/L first carries out quartz filter
Pre-filtering, then handled by wet oxidation, the temperature range of wet oxidation is 125 DEG C, pressure limit is 0.5Mpa, and oxygen adds
Enter 1~4g/L of amount；
The pH of feed liquid after oxidation processes is adjusted to 9 by step 2, then under conditions of ultrasonic wave added, and calcium chloride precipitation agent is added
Precipitation reaction is carried out with 0.5g/L polyacrylamide flocculant, the additional amount of calcium precipitation agent and the molar ratio of total phosphorus are 2:1, are surpassed
Sound condition is frequency 400kHz, ultrasonic power 1W/cm2, after removal precipitates, obtain the first feed liquid；
The pH of first feed liquid is adjusted to 3,1g/L aluminium polychloride is added by step 3, carries out flocculation precipitation reaction, removal precipitating
Afterwards, the second feed liquid is obtained；
Second feed liquid is sent into reverse osmosis membrane and be filtered, obtains that treated and produce water by step 4.
The preparation method of the polyacrylamide flocculant includes the following steps: S1, by weight, in reactor
Middle 35 parts of addition acrylamide monomer, 2 parts of tung oil, 3 parts of 2- acrylamido -2- methyl propane sulfonic acid (AMPS), N- butoxy
2 parts of Methacrylamide (NBMA), 4 parts of acrylic acid double cyclopentenyl ester (DCPA), 2 parts of chain extender l, 4- butanediol, water 150
Part, 3 parts of crosslinking agent acrylonitrile, 1 part of sorbitan ester class surfactant, 2 parts of catalyst dibutyltin dilaurylate are mixed
It closes uniformly, phosphoric acid regulation system pH value is added to 5, is passed through inert gas to remove the dissolved oxygen in reaction system；S2, by S1 institute
The reaction system obtained cools to 10 DEG C, adds 2 parts of initiator azo-bis-isobutyrate hydrochloride, heating carries out polymerization reaction；3rd
The jelly that the reactant that step, S2 are obtained obtains takes out, and after being granulated, dry, crushing, obtains polyacrylamide flocculant.
Embodiment 2
Step 1, will contain white oil 5g/L, and the phosphorous oily waste water of total phosphorus (TP) concentration 3g/L first carries out the pre- of quartz filter
Filtering, then by wet oxidation processing, the temperature range of wet oxidation is 220 DEG C, pressure limit is 5Mpa, oxygen additional amount 1
~4g/L；
The pH of feed liquid after oxidation processes is adjusted to 11 by step 2, then under conditions of ultrasonic wave added, and calcium chloride precipitation is added
Agent and 3g/L polyacrylamide flocculant carry out precipitation reaction, and the additional amount of calcium precipitation agent and the molar ratio of total phosphorus are 4:1, surpass
Sound condition is frequency 600kHz, ultrasonic power 5W/cm2, after removal precipitates, obtain the first feed liquid；
The pH of first feed liquid is adjusted to 5,5g/L aluminium polychloride is added by step 3, carries out flocculation precipitation reaction, removal precipitating
Afterwards, the second feed liquid is obtained；
Second feed liquid is sent into reverse osmosis membrane and be filtered, obtains that treated and produce water by step 4.
The preparation method of the polyacrylamide flocculant includes the following steps: S1, by weight, in reactor
Middle 35 parts of addition acrylamide monomer, 2 parts of tung oil, 3 parts of 2- acrylamido -2- methyl propane sulfonic acid (AMPS), N- butoxy
2 parts of Methacrylamide (NBMA), 4 parts of acrylic acid double cyclopentenyl ester (DCPA), 2 parts of chain extender l, 4- butanediol, water 150
Part, 3 parts of crosslinking agent acrylonitrile, 1 part of sorbitan ester class surfactant, 2 parts of catalyst dibutyltin dilaurylate are mixed
It closes uniformly, phosphoric acid regulation system pH value is added to 5, is passed through inert gas to remove the dissolved oxygen in reaction system；S2, by S1 institute
The reaction system obtained cools to 10 DEG C, adds 2 parts of initiator azo-bis-isobutyrate hydrochloride, heating carries out polymerization reaction；3rd
The jelly that the reactant that step, S2 are obtained obtains takes out, and after being granulated, dry, crushing, obtains polyacrylamide flocculant.
Embodiment 3
Step 1, will contain white oil 3g/L, and the phosphorous oily waste water of total phosphorus (TP) concentration 1g/L first carries out the pre- of quartz filter
Filtering, then by wet oxidation processing, the temperature range of wet oxidation is 170 DEG C, pressure limit is 2Mpa, oxygen additional amount
2g/L；
The pH of feed liquid after oxidation processes is adjusted to 10 by step 2, then under conditions of ultrasonic wave added, and calcium chloride precipitation is added
Agent and 2g/L polyacrylamide flocculant carry out precipitation reaction, and the additional amount of calcium precipitation agent and the molar ratio of total phosphorus are 3:1, surpass
Sound condition is frequency 500kHz, ultrasonic power 2W/cm2, after removal precipitates, obtain the first feed liquid；
The pH of first feed liquid is adjusted to 4,2g/L aluminium polychloride is added by step 3, carries out flocculation precipitation reaction, removal precipitating
Afterwards, the second feed liquid is obtained；
Second feed liquid is sent into reverse osmosis membrane and be filtered, obtains that treated and produce water by step 4.
The preparation method of the polyacrylamide flocculant includes the following steps: S1, by weight, in reactor
Middle 35 parts of addition acrylamide monomer, 2 parts of tung oil, 3 parts of 2- acrylamido -2- methyl propane sulfonic acid (AMPS), N- butoxy
2 parts of Methacrylamide (NBMA), 4 parts of acrylic acid double cyclopentenyl ester (DCPA), 2 parts of chain extender l, 4- butanediol, water 150
Part, 3 parts of crosslinking agent acrylonitrile, 1 part of sorbitan ester class surfactant, 2 parts of catalyst dibutyltin dilaurylate are mixed
It closes uniformly, phosphoric acid regulation system pH value is added to 5, is passed through inert gas to remove the dissolved oxygen in reaction system；S2, by S1 institute
The reaction system obtained cools to 10 DEG C, adds 2 parts of initiator azo-bis-isobutyrate hydrochloride, heating carries out polymerization reaction；3rd
The jelly that the reactant that step, S2 are obtained obtains takes out, and after being granulated, dry, crushing, obtains polyacrylamide flocculant.
Reference examples 1
Difference with embodiment 3 is: using ozone oxidation in step 1,40 DEG C of reaction temperature, and ozone dosage 500mg/
L。
Step 1, will contain white oil 3g/L, and the phosphorous oily waste water of total phosphorus (TP) concentration 1g/L first carries out quartz filter
Pre-filtering, then by ozone oxidation, 40 DEG C of reaction temperature, ozone dosage 500mg/L；
The pH of feed liquid after oxidation processes is adjusted to 10 by step 2, then under conditions of ultrasonic wave added, and calcium chloride precipitation is added
Agent and 2g/L polyacrylamide flocculant carry out precipitation reaction, and the additional amount of calcium precipitation agent and the molar ratio of total phosphorus are 3:1, surpass
Sound condition is frequency 500kHz, ultrasonic power 2W/cm2, after removal precipitates, obtain the first feed liquid；
The pH of first feed liquid is adjusted to 4,2g/L aluminium polychloride is added by step 3, carries out flocculation precipitation reaction, removal precipitating
Afterwards, the second feed liquid is obtained；
Second feed liquid is sent into reverse osmosis membrane and be filtered, obtains that treated and produce water by step 4.
The preparation method of the polyacrylamide flocculant includes the following steps: S1, by weight, in reactor
Middle 35 parts of addition acrylamide monomer, 2 parts of tung oil, 3 parts of 2- acrylamido -2- methyl propane sulfonic acid (AMPS), N- butoxy
2 parts of Methacrylamide (NBMA), 4 parts of acrylic acid double cyclopentenyl ester (DCPA), 2 parts of chain extender l, 4- butanediol, water 150
Part, 3 parts of crosslinking agent acrylonitrile, 1 part of sorbitan ester class surfactant, 2 parts of catalyst dibutyltin dilaurylate are mixed
It closes uniformly, phosphoric acid regulation system pH value is added to 5, is passed through inert gas to remove the dissolved oxygen in reaction system；S2, by S1 institute
The reaction system obtained cools to 10 DEG C, adds 2 parts of initiator azo-bis-isobutyrate hydrochloride, heating carries out polymerization reaction；3rd
The jelly that the reactant that step, S2 are obtained obtains takes out, and after being granulated, dry, crushing, obtains polyacrylamide flocculant.
Reference examples 2
Difference with embodiment 3 is: ultrasonic wave added not being added.
Step 1, will contain white oil 3g/L, and the phosphorous oily waste water of total phosphorus (TP) concentration 1g/L first carries out quartz filter
Pre-filtering, then handled by wet oxidation, the temperature range of wet oxidation is 170 DEG C, pressure limit is 2Mpa, and oxygen is added
Measure 2g/L；
The pH of feed liquid after oxidation processes is adjusted to 10 by step 2, adds calcium chloride precipitation agent and 2g/L polyacrylamide wadding
Solidifying agent carries out precipitation reaction, and the additional amount of calcium precipitation agent and the molar ratio of total phosphorus are 3:1, after removal precipitating, obtains the first material
Liquid；
The pH of first feed liquid is adjusted to 4,2g/L aluminium polychloride is added by step 3, carries out flocculation precipitation reaction, removal precipitating
Afterwards, the second feed liquid is obtained；
Second feed liquid is sent into reverse osmosis membrane and be filtered, obtains that treated and produce water by step 4.
The preparation method of the polyacrylamide flocculant includes the following steps: S1, by weight, in reactor
Middle 35 parts of addition acrylamide monomer, 2 parts of tung oil, 3 parts of 2- acrylamido -2- methyl propane sulfonic acid (AMPS), N- butoxy
2 parts of Methacrylamide (NBMA), 4 parts of acrylic acid double cyclopentenyl ester (DCPA), 2 parts of chain extender l, 4- butanediol, water 150
Part, 3 parts of crosslinking agent acrylonitrile, 1 part of sorbitan ester class surfactant, 2 parts of catalyst dibutyltin dilaurylate are mixed
It closes uniformly, phosphoric acid regulation system pH value is added to 5, is passed through inert gas to remove the dissolved oxygen in reaction system；S2, by S1 institute
The reaction system obtained cools to 10 DEG C, adds 2 parts of initiator azo-bis-isobutyrate hydrochloride, heating carries out polymerization reaction；3rd
The jelly that the reactant that step, S2 are obtained obtains takes out, and after being granulated, dry, crushing, obtains polyacrylamide flocculant.
Reference examples 3
Difference with embodiment 3 is: N- butoxymethyl acryloyl is not added in the preparation of polyacrylamide flocculant, in S1
Amine.
Step 1, will contain white oil 3g/L, and the phosphorous oily waste water of total phosphorus (TP) concentration 1g/L first carries out quartz filter
Pre-filtering, then handled by wet oxidation, the temperature range of wet oxidation is 170 DEG C, pressure limit is 2Mpa, and oxygen is added
Measure 2g/L；
The pH of feed liquid after oxidation processes is adjusted to 10 by step 2, then under conditions of ultrasonic wave added, and calcium chloride precipitation is added
Agent and 2g/L polyacrylamide flocculant carry out precipitation reaction, and the additional amount of calcium precipitation agent and the molar ratio of total phosphorus are 3:1, surpass
Sound condition is frequency 500kHz, ultrasonic power 2W/cm2, after removal precipitates, obtain the first feed liquid；
The pH of first feed liquid is adjusted to 4,2g/L aluminium polychloride is added by step 3, carries out flocculation precipitation reaction, removal precipitating
Afterwards, the second feed liquid is obtained；
Second feed liquid is sent into reverse osmosis membrane and be filtered, obtains that treated and produce water by step 4.
The preparation method of the polyacrylamide flocculant includes the following steps: S1, by weight, in reactor
Middle 35 parts of addition acrylamide monomer, 2 parts of tung oil, 3 parts of 2- acrylamido -2- methyl propane sulfonic acid (AMPS), acrylic acid are double
4 parts of cyclopentene base ester (DCPA), 2 parts of chain extender l, 4- butanediol, 150 parts of water, 3 parts of crosslinking agent acrylonitrile, sorbitan
1 part of esters surface active agent, 2 parts of catalyst dibutyltin dilaurylate are uniformly mixed, addition phosphoric acid regulation system pH value to 5,
Inert gas is passed through to remove the dissolved oxygen in reaction system；S2, the resulting reaction system of S1 is cooled to 10 DEG C, adds and draws
2 parts of agent azo-bis-isobutyrate hydrochloride of hair, heating carry out polymerization reaction；The jelly that the reactant that step 3, S2 are obtained obtains takes
Out, after being granulated, dry, crushing, polyacrylamide flocculant is obtained.
By being investigated to the second material liquid component and reverse osmosis membrane operating condition.
As can be seen from the above table, waste water treatment process provided by the invention can be removed preferably while oil-containing and phosphorous useless
Pollutant in water, embodiment 3 and reference examples 1 are compared as can be seen that wet oxidation can preferably remove grease in waste water,
Prevent grease from influencing precipitating flocculation reaction；Embodiment 3 is compared with reference examples 2 as can be seen that can be improved by ultrasonic wave added
Flocculation precipitation reaction effect, prevents grease from having an impact to precipitation process, improves the removal rate of total phosphorus；Embodiment 3 is relative to right
2 by the way that N- butoxy methyl acrylamide monomer is added in preparing to acrylamide flocculating agent as can be seen that can be improved as usual
For the removal effect of sediment and grease.
Claims (9)
1. a kind of preparation method of polyacrylamide flocculant, which comprises the steps of:
Acrylamide monomer, tung oil, 2- acrylamido -2- methyl propane sulfonic acid is added in S1, by weight in the reactor
3 parts, N- butoxy methyl acrylamide, acrylic acid double cyclopentenyl ester, chain extender, water, crosslinking agent, 1 part of surfactant, urge
Agent is uniformly mixed, and regulation system pH value is passed through inert gas to remove the dissolved oxygen in reaction system；
S2, the resulting reaction system of S1 is cooled down, adds initiator, heating carries out polymerization reaction；
The jelly that S3, the reactant for obtaining S2 obtain takes out, and after being granulated, dry, crushing, obtains polyacrylamide flocculation
Agent.
2. the preparation method of polyacrylamide flocculant described in claim 1, which is characterized in that regulation system pH value is to pass through
Phosphoric acid is added.
3. the preparation method of polyacrylamide flocculant according to claim 1, which is characterized in that regulation system pH value is extremely
6。
4. the preparation method of polyacrylamide flocculant according to claim 1, which is characterized in that catalyst is two laurels
Sour dibutyl tin；Chain extender is l, 4- butanediol；Crosslinking agent is acrylonitrile；Surfactant is sorbitan ester class surface
Activating agent；Initiator is azo-bis-isobutyrate hydrochloride.
5. the preparation method of polyacrylamide flocculant according to claim 1, which is characterized in that the additional amount of raw material is pressed
Be according to parts by weight meter: preferably 35 parts of acrylamide monomer, preferably 2 parts of tung oil, 2- acrylamido -2- methyl propane sulfonic acid are preferred
3 parts, preferably 2 parts of N- butoxy methyl acrylamide, preferably 4 parts of acrylic acid double cyclopentenyl ester, preferably 2 parts of chain extender, water it is excellent
Select 150 parts, preferably 3 parts of crosslinking agent, preferably 1 part of surfactant, preferably 2 parts of catalyst, preferably 2 parts of initiator.
6. the preparation method of polyacrylamide flocculant according to claim 1, which is characterized in that except temperature is cooling in S2
To 10 DEG C.
7. the obtained flocculant of preparation method described in any one of claims 1-6.
8. flocculant as claimed in claim 7 is for handling the purposes in phosphorous oily waste water.
9. phosphorous oily waste water according to claim 8,0.1~5g/ of mineral oil is contained in the phosphorous oily waste water
L, 0.1~3g/L of total phosphorus (TP) concentration；The mineral oil is white oil, and the total phosphorus is by phosphate, hypophosphites, phosphorous
Hydrochlorate composition.
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| CN107698059A (en) * | 2017-10-31 | 2018-02-16 | 惠州市宙邦化工有限公司 | A kind of phosphorus-containing wastewater contamination precipitation processing method |
| CN110357325A (en) * | 2019-07-10 | 2019-10-22 | 吉林建筑大学 | A kind of processing method of oily waste water |
| CN110981051B (en) * | 2020-03-03 | 2020-06-02 | 胜利油田盛嘉化工有限责任公司 | Ultrasonic treatment method for crude oil produced water |
| CN113526781A (en) * | 2020-04-22 | 2021-10-22 | 大连波美科技有限公司 | Treatment and recycling system and process for vegetable oil saponin wastewater |
| CN113461202B (en) * | 2021-06-24 | 2023-10-27 | 宜都兴发化工有限公司 | High-phosphorus and high-calcium magnesium recycling treatment method |
| CN114772836B (en) * | 2022-04-28 | 2024-02-27 | 青岛海纳能源环保科技开发有限公司 | Treatment method of waste emulsion |
| CN115448501A (en) * | 2022-10-20 | 2022-12-09 | 湖南天泰天润新能源科技有限公司 | Dephosphorization method for waste water recovered from waste lithium iron phosphate batteries |
| CN116622037B (en) * | 2023-07-25 | 2023-10-13 | 东明旭阳化工有限公司 | Method for removing total phosphorus from caprolactam oximation wastewater, calcium hydroxide precipitant used in method and preparation method of precipitant |
Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| BE667873A (en) * | 1964-08-04 | 1966-02-04 | ||
| IT1021738B (en) * | 1973-10-10 | 1978-02-20 | Allied Colloids Ltd | SYNTHETIC FLOCCULATING POLYMERS FOR ALKALINE SYSTEMS AND PROCEDURE FOR PRODUCING THEM |
| CN1235613A (en) * | 1996-09-03 | 1999-11-17 | 帝国化学工业公司 | Polyacrylamide polymerization |
| CN1884316A (en) * | 2006-06-23 | 2006-12-27 | 张金保 | Polymerization promoting initiator for producing super high molecular weight polyacrylamide and preparation method |
| CN101143742A (en) * | 2006-09-15 | 2008-03-19 | 中国石油化工股份有限公司 | Reversed phase emulsion synthesis method for polyacrylamide flocculant |
| CN101845115A (en) * | 2010-04-28 | 2010-09-29 | 北京化工大学 | Preparation method and application of water-based polyacrylamide composite dispersion liquid |
| CN101899129A (en) * | 2010-07-22 | 2010-12-01 | 江苏江达生态科技有限公司 | Preparation method of hydrophobic anion flocculant |
| EP2318109A1 (en) * | 2008-07-31 | 2011-05-11 | General Electric Company | Methods for removing fats, oil and grease and recovering tallow from wastewater |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102627361A (en) * | 2012-03-27 | 2012-08-08 | 浙江省环境保护科学设计研究院 | Method and device for removing phosphorous from glyphosate production wastewater |
| CN104276686A (en) * | 2013-07-09 | 2015-01-14 | 深圳海川环境科技有限公司 | Organic matter-rich sewage treatment and disposal method |
| CN103991987B (en) * | 2014-06-09 | 2016-07-06 | 北京碧水源环境工程有限公司 | A kind of pretreatment high phosphorus waste water removes technique and the process system thereof of total phosphorus |
-
2016
- 2016-07-28 CN CN201910009241.5A patent/CN109502833A/en active Pending
- 2016-07-28 CN CN201610604238.4A patent/CN106007128B/en active Active
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| BE667873A (en) * | 1964-08-04 | 1966-02-04 | ||
| IT1021738B (en) * | 1973-10-10 | 1978-02-20 | Allied Colloids Ltd | SYNTHETIC FLOCCULATING POLYMERS FOR ALKALINE SYSTEMS AND PROCEDURE FOR PRODUCING THEM |
| CN1235613A (en) * | 1996-09-03 | 1999-11-17 | 帝国化学工业公司 | Polyacrylamide polymerization |
| CN1884316A (en) * | 2006-06-23 | 2006-12-27 | 张金保 | Polymerization promoting initiator for producing super high molecular weight polyacrylamide and preparation method |
| CN101143742A (en) * | 2006-09-15 | 2008-03-19 | 中国石油化工股份有限公司 | Reversed phase emulsion synthesis method for polyacrylamide flocculant |
| EP2318109A1 (en) * | 2008-07-31 | 2011-05-11 | General Electric Company | Methods for removing fats, oil and grease and recovering tallow from wastewater |
| CN101845115A (en) * | 2010-04-28 | 2010-09-29 | 北京化工大学 | Preparation method and application of water-based polyacrylamide composite dispersion liquid |
| CN101899129A (en) * | 2010-07-22 | 2010-12-01 | 江苏江达生态科技有限公司 | Preparation method of hydrophobic anion flocculant |
Non-Patent Citations (2)
| Title |
|---|
| 云南科技学术交流中心等: "《科技学术论文集 2007》", 31 July 2007, 原子能出版社 * |
| 杨旭: "《中国科技发展精典文库 2003卷 中》", 31 May 2003 * |
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