Summary of the invention
The object of the present invention is to provide a kind of processability excellent in, eco-friendly magnesium ion modified polyacrylamide preparation method.Utilize water solution polymerization process, in the polymerization process of polyacrylamide, introduce Mg
2+, prepare have stronger flocculation ability containing magnesium ion modified polyacrylamide.
The object of the invention is to be achieved by the following scheme:
1, fill a prescription:
Namely magnesium hydroxide liquid 5 ~ 10mL is joined
Acrylamide (AM) 90g
Sodium hydroxide solution 1M
Hydrochloric acid 1M
Ammonium persulphate 70 ~ 80mg
Sodium bisulfite 8 ~ 12 mg
Urea 10 ~ 15mg
EDTA 6~10 mg
2, preparation method
(1) to learn from else's experience washing, dried four-hole boiling flask, first add the magnesium hydroxide solution of namely joining, then be fixed on 250 r/min on constant temperature electric mixer after adding acrylamide and 200mL deionized water and at the uniform velocity stir, acrylamide monomer is dissolved completely.
(2) continuing to pass in above-mentioned system in the process of nitrogen 28 ~ 35min, drip ammoniacal liquor 0.3 ~ 0.5mL, and control temperature is being 35 ~ 40 DEG C of scopes.
(3) system be placed in water-bath heat, temperature-stable in 63 ~ 65 DEG C time, add ammonium persulphate, sodium bisulfite, urea and EDTA, and with the pH of sodium hydroxide solution or hydrochloric acid regulation system in 7.5 ~ 8.2 scopes.
(4) keep the reaction of system continuously stirring, rotating speed is 200 ~ 250 r/min, is taken out by the mixed solution of reaction system and pour beaker into after 4.5 ~ 5.0 hours, and proceeds to rapidly in 80 ~ 82 DEG C of vacuum drying ovens and turn out colloid, then takes out and is cooled to room temperature.
(5) adopt volume ratio to be that Virahol and the deionized water mixing solutions of 1:1 carries out 4 ~ 6 times to above-mentioned colloid of turning out and wash, then with deionized water 3 ~ 5 flushings, remove washing process generation white precipitate, obtain a kind of new modified Laemmli sample.
(6) sample after washing in 80 DEG C of thermostatic drying chambers dry 48 hours, takes out after putting into moisture eliminator cooling, pulverizes with pulverizer, the final finished product obtained containing magnesium ion modified polyacrylamide.
Namely magnesium hydroxide liquid of joining of the present invention is formulated by dropwise adding sodium hydroxide solution in soluble magnesium salts solution, wherein solubility magnesium salts refers to magnesium sulfate, magnesium chloride or magnesium nitrate, and in soluble magnesium salts solution, the mass concentration of magnesium salts is 2 ~ 10 g/L.
Of the present invention continuing passes into nitrogen, and its air flow is 1 L/min.
Described ammoniacal liquor, refers to the volume mixture liquid of ammoniacal liquor and water 1:1.
The invention has the advantages that:
Adopt water solution polymerization process, method maturation is convenient, easily controls; Obtained contains magnesium ion modified polyacrylamide environmental friendliness, superior performance.In the application of disposing of sewage treatment plant's excess sludge, for same dosage, same dehydration equipment condition, the polyacrylamide of the moisture percentage in sewage sludge use more conventional than sewage work after containing magnesium ion modified polyacrylamide conditioning dehydration is adopted to reduce more than 10%.
Embodiment
embodiment 1
(1) to learn from else's experience washing, dried four-hole boiling flask, namely what first to add 5mL be 2g/L with magnesium chloride mass concentration joins magnesium hydroxide liquid, add 90g acrylamide (AM) monomer and 200ml deionized water again, after be fixed on constant temperature electric mixer, at the uniform velocity stir with 250 r/min rotating speeds, acrylamide monomer is dissolved completely.
(2) continue to pass into nitrogen 30min in system, and drip 0.3 mL ammoniacal liquor in the process.
(3) above-mentioned reaction system is put into 65 DEG C of thermostat water baths to heat, add 70mg ammonium persulphate, 8mg sodium bisulfite, 10mg urea and 6mgEDTA simultaneously, regulate reaction soln pH to be 7.5 with hydrochloric acid or sodium hydroxide solution.
(4) continue to stir, rotating speed is 250 r/min, successive reaction 4.5 hours, takes out and pours beaker into, and be placed in rapidly after colloid turned out by 80 DEG C of vacuum drying ovens and be cooled to room temperature.
(5) adopt the 1:1 mixing solutions of Virahol and deionized water to carry out 4 times to colloid wash, and with deionized water rinsing 3 times, remove washing process generation white precipitate, finally obtain modified polyacrylamide sample.
(6) sample after washing is placed in dry 48 hours of the thermostatic drying chamber of 80 DEG C, takes out and puts into after moisture eliminator is cooled to room temperature, pulverize, namely obtain containing Mg with pulverizer
2+modified polyacrylamide.
After measured, prepared containing Mg in magnesium ion modified polyacrylamide
2+content is 32.7ppm.
embodiment 2
(1) to learn from else's experience washing, dried four-hole boiling flask, namely what first to add 5mL be 5g/L with magnesium sulfate mass concentration joins magnesium hydroxide liquid, add 90g acrylamide (AM) monomer and 200ml deionized water again, after be fixed on constant temperature electric mixer, at the uniform velocity stir with 250 r/min rotating speeds, acrylamide monomer is dissolved completely.
(2) continue to pass into nitrogen 32min in system, and drip 0.4 mL ammoniacal liquor in the process.
(3) above-mentioned reaction system is put into 66 DEG C of thermostat water baths to heat, add 72mg ammonium persulphate, 10mg sodium bisulfite, 12mg urea and 8mgEDTA simultaneously, regulate reaction soln pH to be 7.6 with hydrochloric acid or sodium hydroxide solution.
(4) continue to stir, rotating speed is 250 r/min, successive reaction 4.75 hours, takes out and pours beaker into, and be placed in rapidly after colloid turned out by 80 DEG C of vacuum drying ovens and be cooled to room temperature.
(5) adopt the 1:1 mixing solutions of Virahol and deionized water to carry out 5 times to colloid wash, and with deionized water rinsing 3 times, remove washing process generation white precipitate, finally obtain modified polyacrylamide sample.
(6) the modified polyacrylamide sample after washing is placed in dry 48 hours of the thermostatic drying chamber of 80 DEG C, takes out and puts into after moisture eliminator is cooled to room temperature, pulverize, namely obtain containing Mg with pulverizer
2+modified polyacrylamide.
After measured, prepared containing Mg in magnesium ion modified polyacrylamide
2+content is 65.4ppm.
embodiment 3
(1) to learn from else's experience washing, dried four-hole boiling flask, namely what first to add 6mL be 6g/L with magnesium nitrate mass concentration joins magnesium hydroxide liquid, add 90g acrylamide (AM) monomer and 200ml deionized water again, after be fixed on constant temperature electric mixer, at the uniform velocity stir with 250 r/min rotating speeds, acrylamide monomer is dissolved completely.
(2) continue to pass into nitrogen 35min in system, and drip 0.5 mL ammoniacal liquor in the process.
(3) above-mentioned reaction system is put into 68 DEG C of thermostat water baths to heat, add 72mg ammonium persulphate, 10mg sodium bisulfite, 12mg urea and 10mgEDTA simultaneously, regulate reaction soln pH to be 7.8 with hydrochloric acid or sodium hydroxide solution.
(4) continue to stir, rotating speed is 200 r/min, successive reaction 5 hours, takes out and pours beaker into, and be placed in rapidly after colloid turned out by 80 DEG C of vacuum drying ovens and be cooled to room temperature.
(5) adopt the 1:1 mixing solutions of Virahol and deionized water to carry out 6 times to colloid wash, and with deionized water rinsing 4 times, remove washing process generation white precipitate, finally obtain modified polyacrylamide sample.
(6) the modified polyacrylamide sample after washing is placed in dry 48 hours of the thermostatic drying chamber of 80 DEG C, takes out and puts into after moisture eliminator is cooled to room temperature, pulverize, namely obtain containing Mg with pulverizer
2+modified polyacrylamide.
After measured, prepared containing Mg in magnesium ion modified polyacrylamide
2+content is 102.8ppm.
embodiment 4
(1) to learn from else's experience washing, dried four-hole boiling flask, namely what first to add 5mL be 10g/L with magnesium sulfate mass concentration joins magnesium hydroxide liquid, add 90g acrylamide (AM) monomer and 200ml deionized water again, after be fixed on constant temperature electric mixer, at the uniform velocity stir with 250 r/min rotating speeds, acrylamide monomer is dissolved completely.
(2) continue to pass into nitrogen 32min in system, and drip 0.5mL ammoniacal liquor in the process.
(3) above-mentioned reaction system is put into 68 DEG C of thermostat water baths to heat, add 75mg ammonium persulphate, 12mg sodium bisulfite, 12mg urea and 10mgEDTA simultaneously, regulate reaction soln pH to be 8.0 with hydrochloric acid or sodium hydroxide solution.
(4) continue to stir, rotating speed is 200 r/min, successive reaction 5 hours, takes out and pours beaker into, and be placed in rapidly after colloid turned out by 80 DEG C of vacuum drying ovens and be cooled to room temperature.
(5) adopt the 1:1 mixing solutions of Virahol and deionized water to carry out 5 times to colloid wash, and with deionized water rinsing 3 times, remove washing process generation white precipitate, finally obtain modified polyacrylamide sample.
(6) the modified polyacrylamide sample after washing is placed in dry 48 hours of the thermostatic drying chamber of 80 DEG C, takes out and puts into after moisture eliminator is cooled to room temperature, pulverize, namely obtain containing Mg with pulverizer
2+modified polyacrylamide.
After measured, prepared containing Mg in magnesium ion modified polyacrylamide
2+content is 132.4ppm.
embodiment 5
(1) to learn from else's experience washing, dried four-hole boiling flask, namely what first to add 10mL be 4g/L with magnesium chloride mass concentration joins magnesium hydroxide liquid, add 90g acrylamide (AM) monomer and 200ml deionized water again, after be fixed on constant temperature electric mixer, at the uniform velocity stir with 250 r/min rotating speeds, acrylamide monomer is dissolved completely.
(2) continue to pass into nitrogen 35min in system, and drip 0.5 mL ammoniacal liquor in the process.
(3) above-mentioned reaction system is put into 68 DEG C of thermostat water baths to heat, add 75mg ammonium persulphate, 12mg sodium bisulfite, 15mg urea and 10mgEDTA simultaneously, regulate reaction soln pH to be 8.5 with hydrochloric acid or sodium hydroxide solution.
(4) continue to stir, rotating speed is 200 r/min, successive reaction 5 hours, takes out and pours beaker into, and be placed in rapidly after colloid turned out by 80 DEG C of vacuum drying ovens and be cooled to room temperature.
(5) adopt the 1:1 mixing solutions of Virahol and deionized water to carry out 6 times to colloid wash, and with deionized water rinsing 4 times, remove washing process generation white precipitate, finally obtain modified polyacrylamide sample.
(6) the modified polyacrylamide sample after washing is placed in dry 48 hours of the thermostatic drying chamber of 80 DEG C, takes out and puts into after moisture eliminator is cooled to room temperature, pulverize, can obtain containing Mg with pulverizer
2+modified polyacrylamide.
After measured, prepared containing Mg in magnesium ion modified polyacrylamide
2+content is 117.1ppm.
embodiment 6
Adopt respectively prepared by the invention process case 3, case study on implementation 4 and case study on implementation 5 to process initial haze containing magnesium ion modified polyacrylamide association aggregation aluminum chloride (PAC) be 1823 NTU stone slab waste water, measure the turbidity of its supernatant liquor after flocculation sediment.Only with PAC(polyacrylamide) flocculation sediment after supernatant fluid turbidity be 60.2NTU, and use the turbidity containing magnesium ion modified polyacrylamide of PAC and above-mentioned 3 kinds of associating to be respectively 21.5NTU, 15.4NTU and 18.8 NTU, the highest clearance of turbidity is 99.16%, and effect ratio is used alone PAC and improves 74.4%.
embodiment 7
Adopt respectively prepared by the invention process case 3, case study on implementation 4 and case study on implementation 5 containing magnesium ion modified polyacrylamide and West, Fuzhou City sewage work use the commercially available cationic-type polyacrylamide of molecular weight 600-800 ten thousand to West sewage treatment plant residual mud (sludge specific resistance 2.14 × 10
13cm/g) flocculation conditioning is carried out, and sludge specific resistance after measuring conditioning.After commercially available cationic-type polyacrylamide conditioning, sludge specific resistance is 2.52 × 10
10cm/g, and use above-mentioned 3 kinds to be respectively 1.21 × 10 containing sludge specific resistance after the conditioning of magnesium ion modified polyacrylamide
10cm/g, 0.66 × 10
10cm/g and 1.04 × 10
10cm/g, wherein best effect improves 73.8% than commercially available cationic-type polyacrylamide.
embodiment 8
On the basis of case study on implementation 7, adopt plate-and-frame filter press to carry out press dewatering to the mud after 4 kinds of polyacrylamide conditionings, and measure the water ratio of the rear mud cake of dehydration.After adopting the dehydration of commercially available cationic-type polyacrylamide, moisture content of the cake is 84.2%, and use above-mentioned 3 kinds to be respectively 78. 5%, 73.8% and 76.3% containing moisture content of the cake after the dehydration of magnesium ion modified polyacrylamide, wherein best effect decreases 10.4% only than moisture content of the cake after the dehydration of the commercially available cationic-type polyacrylamide of employing.