CN102952045A - 2-acrylamide-2-methylpropanesulfonic acid (AMPS) crude product and refining method thereof - Google Patents
2-acrylamide-2-methylpropanesulfonic acid (AMPS) crude product and refining method thereof Download PDFInfo
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Abstract
The invention provides a refining method of a 2-acrylamide-2-methylpropanesulfonic acid (AMPS) crude product. The refining method is characterized by comprising the following steps of: (1) dissolving the AMPS crude product in an acetic acid water solution; (2) contacting the solution obtained in the step (1) with activated alumina and then filtering the solution, wherein the mass ratio of the activated alumina to the AMPS crude product is 1:(2-10) and the contact time is 0.8-1.2 hours; and (3) cooling and crystallizing the solution obtained after filtration in the step (2) and carrying out solid-liquid separation. The invention also provides AMPS refined by the method. The method has the advantages that the molecular weight of the polymer formed by polymerizing the refined AMPS is greatly increased and the requirement of high temperature and salt resistance of the polymer for tertiary oil recovery can be met.
Description
Technical field
The present invention relates to the process for purification of the thick product of a kind of 2-acrylamide-2-methylpro panesulfonic acid and the 2-acrylamide-2-methylpro panesulfonic acid that is obtained by this process for purification.
Background technology
2-acrylamide-2-methylpro panesulfonic acid (2-Acrylamide-2-methylpropanesulfonicacid is designated hereinafter simply as AMPS) is the multifunctional water-soluble anionic monomer, has carbon-carbon double bond, carbonyl and sulfonic acid functional group in its molecular structure.Sulfonic acid group makes molecule that good water-soluble and good salt tolerance be arranged, and has good stability, carbonyl to make molecule have good adsorptivity and complexing, carbon-carbon double bond can make molecule self or with other molecule homopolymerization and copolymerization, form superpolymer.The water-soluble polymers of AMPS has important purposes in petroleum industry, can be used as the flocculation agent in oil field and fall the filter humectant.Adopt and the successively discovery of deep-well, ultra deep well along with carry out three in the oil field, require high temperature resistant salt tolerant degree higher, polyacrylamide can reduce its viscosity in the presence of high temperature, heavy metal etc., replaced by the polymkeric substance of polymerization single polymerization monomer take AMPS at present.In addition, AMPS can also be applied to the fields such as water conditioner, chemical fibre, plastics, printing and dyeing, coating, gas separation membrane, electronic industry.
Be applied to tertiary oil production in oil field and require higher molecular weight with the polymkeric substance take AMPS as polymerization single polymerization monomer of high temperature resistant salt tolerant, therefore the polymerization single polymerization monomer AMPS that forms polymkeric substance there is higher requirement, at present, most researchists are devoted to study the molecular weight that the purity that improves AMPS improves the polymkeric substance that forms take AMPS as polymerization single polymerization monomer.
The purification treating method of AMPS mainly is recrystallization and solvent wash method in the world at present, and the solvent of use has certain solubleness to AMPS, and AMPS is partly or entirely dissolved, to remove the impurity in AMPS plane of crystal or the whole crystal.US Patent No. 4337215 has proposed at high temperature to dissolve with acetic acid-water solvent, cools off crystallization again, the method for filtering separation.Although this method yield is about 70%, the AMPS quality behind the recrystallization greatly improves.Japanese Patent JP5125037 discloses a kind of water and as solvent AMPS has been carried out the method for recrystallization, because polymerization occurs in the presence of water AMPS easily, needs the stopper of adding 0.01-0.5%, such as Resorcinol or p methoxy phenol etc.Romania patent RO103538 adopts the method for vinyl cyanide-water mixed solvent washing AMPS.Chinese patent CN1114646 then proposes to use the method for Ethanol-Acetic Acid double solvents washing AMPS.
Although existing various purification process can improve the purity of AMPS, the molecular weight of the polymkeric substance that AMPS polymerization behind the purifying forms is still lower, can't satisfy tertiary oil production in oil field with the requirement of high temperature resistant salt tolerant polymkeric substance.
Summary of the invention
The objective of the invention is in order to overcome the lower defective of molecular weight of the polymkeric substance that the 2-acrylamide-2-methylpro panesulfonic acid polymerization behind the purifying in the prior art forms, a kind of process for purification of the new thick product of 2-acrylamide-2-methylpro panesulfonic acid is provided.
The present inventor is unexpected the discovery when adopting recrystallization method that the thick product of 2-acrylamide-2-methylpro panesulfonic acid is purified under study for action, with the thick product of aqueous acetic acid dissolving 2-acrylamide-2-methylpro panesulfonic acid, and add activated alumina in the solution after dissolving, solution after will filtering again carries out crystallization, although the purity impact on the 2-acrylamide-2-methylpro panesulfonic acid is little, but the molecular weight of the polymkeric substance that the 2-acrylamide-2-methylpro panesulfonic acid polymerization after refining forms is increased substantially, thereby satisfy tertiary oil production in oil field with the requirement of high temperature resistant salt tolerant polymkeric substance.
Therefore, to achieve these goals, on the one hand, the invention provides the process for purification of the thick product of a kind of 2-acrylamide-2-methylpro panesulfonic acid, it is characterized in that described method comprises the steps:
(1) the thick product of 2-acrylamide-2-methylpro panesulfonic acid is dissolved in the aqueous acetic acid;
(2) step (1) gained solution is contacted rear the filtration with activated alumina, the mass ratio of activated alumina and the thick product of 2-acrylamide-2-methylpro panesulfonic acid is 1: 2-10, and the time of contact is 0.8-1.2 hour;
(3) the solution crystallisation by cooling that obtains after step (2) is filtered also carries out solid-liquid separation.
On the other hand, the invention provides a kind of 2-acrylamide-2-methylpro panesulfonic acid, it is characterized in that, described 2-acrylamide-2-methylpro panesulfonic acid is made with extra care and is got by aforesaid method.
The process for purification of the thick product of 2-acrylamide-2-methylpro panesulfonic acid provided by the invention, when the 2-acrylamide-2-methylpro panesulfonic acid is carried out recrystallization purifying, by dissolving the thick product of 2-acrylamide-2-methylpro panesulfonic acid with aqueous acetic acid, and add activated alumina in the solution after dissolving, greatly improved the molecular weight of the polymkeric substance of the 2-acrylamide-2-methylpro panesulfonic acid polymerization formation after making with extra care, make the viscosity-average molecular weight of polymkeric substance up to 2,000 ten thousand, can satisfy the requirement of the high temperature resistant salt tolerant of used for tertiary oil recovery polymkeric substance.
Other features and advantages of the present invention will partly be described in detail in embodiment subsequently.
Embodiment
Below the specific embodiment of the present invention is elaborated.Should be understood that embodiment described herein only is used for description and interpretation the present invention, is not limited to the present invention.
On the one hand, the invention provides the process for purification of the thick product of a kind of 2-acrylamide-2-methylpro panesulfonic acid, described method comprises the steps:
(1) the thick product of 2-acrylamide-2-methylpro panesulfonic acid is dissolved in the aqueous acetic acid;
(2) step (1) gained solution is contacted rear the filtration with activated alumina, the mass ratio of activated alumina and the thick product of 2-acrylamide-2-methylpro panesulfonic acid is 1: 2-10, and the time of contact is 0.8-1.2 hour;
(3) the solution crystallisation by cooling that obtains after step (2) is filtered also carries out solid-liquid separation.
According to the present invention, can realize purpose of the present invention although step (1) gained solution contacted with activated alumina, the molecular weight of the polymkeric substance that the 2-acrylamide-2-methylpro panesulfonic acid polymerization after namely making with extra care forms increases substantially, among the present invention step (1) gained solution contacted with activated alumina and refer to step (1) gained solution is contacted with activated alumina under the condition of 2-acrylamide-2-methylpro panesulfonic acid dissolving, generally the temperature by the control contact is dissolved the 2-acrylamide-2-methylpro panesulfonic acid in step (1) gained solution, therefore, the present invention can realize purpose of the present invention as long as step (1) gained solution contacted with activated alumina under the temperature of 2-acrylamide-2-methylpro panesulfonic acid dissolving, but under the preferable case, the temperature of described contact is 50-110 ℃, more preferably 80-100 ℃.Under the temperature of preferred contact, the solution of step (1) gained is contacted with activated alumina better, can further improve the molecular weight of the polymkeric substance of the 2-acrylamide-2-methylpro panesulfonic acid polymerization formation after making with extra care.What it should be appreciated by those skilled in the art is, contacts with activated alumina better in order to make step (1) gained solution, can adopt the mode of continuous stirring to contact.
For step (1), the thick product of 2-acrylamide-2-methylpro panesulfonic acid is dissolved in the aqueous acetic acid, can take this area the whole bag of tricks commonly used that the thick product of 2-acrylamide-2-methylpro panesulfonic acid is dissolved in the aqueous acetic acid, for example can adopt the mode of control solvent temperature that the thick product of 2-acrylamide-2-methylpro panesulfonic acid is dissolved in the aqueous acetic acid, the present invention is preferably 50-110 ℃, more preferably 80-100 ℃ for the temperature of dissolving.It will be understood by those skilled in the art that for the thick product of 2-acrylamide-2-methylpro panesulfonic acid is dissolved under solvent temperature in the aqueous acetic acid quickly, can under solvent temperature, adopt the mode accelerate dissolution that constantly stirs.The temperature of the temperature of step (2) and activated alumina contact and the dissolving of step (1) can be identical, also can be different, so long as contacting with activated alumina, the solution form gets final product, for easy to operate, it is identical with the temperature of the dissolving of step (1) that the temperature of step (2) and activated alumina contact is preferably.
Among the present invention, the purity of the thick product of 2-acrylamide-2-methylpro panesulfonic acid is preferably the 95-98 % by weight.
Among the present invention, the mass ratio of the thick product of 2-acrylamide-2-methylpro panesulfonic acid and aqueous acetic acid is preferably 1: 2-7, more preferably 1: 2-5.For the thick product of 2-acrylamide-2-methylpro panesulfonic acid is dissolved in the aqueous acetic acid better, the water content of aqueous acetic acid is preferably the 5-40 % by weight, more preferably the 8-20 % by weight.
Among the present invention, the mass ratio of activated alumina and the thick product of 2-acrylamide-2-methylpro panesulfonic acid is preferably 1: 4-6.In order to play better adsorption, under the preferable case, the specific surface area of activated alumina is 100-200m
2/ g, pore volume are 0.25-0.6cm
3/ g; Further under the preferable case, the specific surface area of activated alumina is 135-148m
2/ g, pore volume are 0.35-0.42cm
3/ g.Among the present invention, the specific surface area of activated alumina and pore volume adopt the nitrogen adsorption desorption method to record, and nitrogen adsorption-desorption experiment condition comprises: the U.S. Autosorb-1 of Kang Ta company nitrogen adsorption desorption instrument, sample is degassed 4 hours at 200 ℃.
For with the filtration of carrying out after activated alumina contacts without particular requirement, can adopt this area variety of way commonly used to filter, as long as the activated alumina after will adsorbing leaches from solution.
As long as the temperature of crystallisation by cooling can make 2-acrylamide-2-methylpro panesulfonic acid crystallization from solution, under the preferable case, the temperature of crystallisation by cooling is 0-10 ℃ for step (3), and the time is 1-3 hour.Those skilled in the art what should be thought of is, after crystal is separated out, also to carry out the operations such as solid-liquid separation and drying, to obtain the 2-acrylamide-2-methylpro panesulfonic acid product for polymerization, solid-liquid separation can adopt the mode of this area routine to carry out solid-liquid separation, and drying can be at 50-100 ℃ of lower dry 4-8h.
On the other hand, the invention provides a kind of 2-acrylamide-2-methylpro panesulfonic acid, described 2-acrylamide-2-methylpro panesulfonic acid is made with extra care and is got by aforesaid method.
More than describe preferred implementation of the present invention in detail; but the present invention is not limited to the detail in the above-mentioned embodiment, in technical conceive scope of the present invention; can carry out multiple simple variant to technical scheme of the present invention, these simple variant all belong to protection scope of the present invention.
Need to prove in addition, each concrete technical characterictic described in above-mentioned embodiment in reconcilable situation, can make up by any suitable mode, for fear of unnecessary repetition, the present invention is to the no longer separately explanation of various possible array modes.
In addition, also can carry out arbitrary combination between the various embodiment of the present invention, as long as it is without prejudice to thought of the present invention, it should be considered as content disclosed in this invention equally.
Embodiment
Following embodiment will the present invention is further illustrated, but therefore do not limit the present invention.
In following embodiment and Comparative Examples:
Aqueous acetic acid is that the analytical pure acetic acid and the deionized water preparation that are purchased get.
Activated alumina: be purchased from Shandong Aluminum Co., Ltd. company limited.
Acrylamide: be purchased from Shandong Polymer Bio-Chemicals Co., Ltd..
The measuring method of 2-acrylamide-2-methylpro panesulfonic acid purity: use high performance liquid chromatography to measure.The analysis condition of liquid chromatography is: Zorbax SAX chromatographic column, moving phase are 0.1mol/L KH
2PO
4Solution, flow velocity are 1.0mL/min, UV-detector.
The measuring method of polymericular weight: polymericular weight is viscosity-average molecular weight, uses dark type viscometer to adopt one point method to measure.
The yield of 2-acrylamide-2-methylpro panesulfonic acid accounts for the ratio of the amount of 2-acrylamide-2-methylpro panesulfonic acid in the thick product of 2-acrylamide-2-methylpro panesulfonic acid for the amount of the 2-acrylamide-2-methylpro panesulfonic acid after refining.
The polymerization process of 2-acrylamide-2-methylpro panesulfonic acid and acrylamide: the 2-acrylamide-2-methylpro panesulfonic acid of the 3.5g after will making with extra care and the acrylamide of 6.5g join in the polyreaction bottle, add deionized water dissolving, regulating pH with sodium hydroxide solution again is 7.0, and then adding successively concentration is the EDTA-2Na aqueous solution 1.0g of 1 % by weight and the aqueous solution of urea 0.5g that concentration is 1 % by weight.The polyreaction bottle is put into 10 ℃ of waters bath with thermostatic control, logical nitrogen flooding oxygen is after 30 minutes, adding concentration is the persulfate aqueous solution 1.0g of 0.1 % by weight and the bisulfite aqueous solutions of potassium 1.0g that concentration is 0.1 % by weight again, in 5 ℃ of initiated polymerizations, continuing logical nitrogen stopped after five minutes, after the polyreaction 2 hours, be warming up to 50 ℃ and continue reaction 3 hours, obtain blob of viscose.Take out blob of viscose, cutting, granulation, the white polymer of pulverizing, sieve and to get.
Embodiment 1
This embodiment is used for illustrating the process for purification of the thick product of 2-acrylamide-2-methylpro panesulfonic acid provided by the invention.
The preparation of the thick product of 2-acrylamide-2-methylpro panesulfonic acid: in the four-hole boiling flask that is provided with temperature regulating device, agitator, thermometer and gas feeding unit, add the 330g vinyl cyanide, vinyl cyanide being cooled to after-10 ℃ to add concentration is the sulfuric acid 40g of 100 % by weight, in the reinforced process and complete rear holding temperature be-10 ℃ and continue stirring 1 hour; Then be warmed up to 40 ℃, passing into the 15g iso-butylene reacts, then add concentration in the reaction system and be the sulfuric acid 21g of 98 % by weight and continue to pass into iso-butylene, after the total amount of the iso-butylene that adds reaches 35g, close the iso-butylene valve in reaction system, be incubated and finish after 1 hour to react.Reaction solution is carried out vacuum filtration, obtain filter cake and filtrate.Filter cake is carried out vacuum-drying, and temperature is 110 ℃, and pressure is 10kPa, obtains dried filter cake, is the thick product of 2-acrylamide-2-methylpro panesulfonic acid, and purity is 96.8 % by weight.
The thick product of 2-acrylamide-2-methylpro panesulfonic acid refining: the aqueous acetic acid 500g and the thick product 150g of the above-mentioned 2-acrylamide-2-methylpro panesulfonic acid that makes that add moisture 15 % by weight in the four-hole boiling flask, warming while stirring to 90 ℃, after the dissolving and the 30g activated alumina (specific surface area is 140m
2/ g, pore volume are 0.38cm
3/ g) contact keeps 90 ℃ of temperature to stir 1 hour, then with solution filter, and again 5 ℃ of lower crystallisation by cooling 2 hours, crystallization.Through solid after the solid-liquid separation in 80 ℃ of baking ovens dry 6 hours, obtain the 2-acrylamide-2-methylpro panesulfonic acid after refining, record yield and purity sees Table 1.
With the 2-acrylamide-2-methylpro panesulfonic acid after refining as stated above with acrylamide polymerization, the molecular weight of measuring the polymkeric substance that obtains sees Table 1.
Embodiment 2
This embodiment is used for illustrating the process for purification of the thick product of 2-acrylamide-2-methylpro panesulfonic acid provided by the invention.
The preparation of the thick product of 2-acrylamide-2-methylpro panesulfonic acid: in the four-hole boiling flask that is provided with temperature regulating device, agitator, thermometer and gas feeding unit, add the 330g vinyl cyanide, vinyl cyanide being cooled to after-10 ℃ to add concentration is the oleum 40g of 103 % by weight, in the reinforced process and complete rear holding temperature be-10 ℃ and continue stirring 1 hour; Then be warmed up to 40 ℃, passing into the 15g iso-butylene reacts, then add concentration in the reaction system and be the oleum 21g of 102 % by weight and continue to pass into iso-butylene, after the total amount of the iso-butylene that adds reaches 35g, close the iso-butylene valve in reaction system, be incubated and finish after 1 hour to react.Reaction solution is carried out vacuum filtration, obtain filter cake and filtrate.Filter cake is carried out vacuum-drying, and temperature is 110 ℃, and pressure is 10kPa, obtains dried filter cake, is the thick product of 2-acrylamide-2-methylpro panesulfonic acid, and purity is 95%.
The thick product of 2-acrylamide-2-methylpro panesulfonic acid refining: the aqueous acetic acid 500g and the thick product 100g of the above-mentioned 2-acrylamide-2-methylpro panesulfonic acid that makes that add moisture 20 % by weight in the four-hole boiling flask, warming while stirring to 100 ℃, after the dissolving and the 25g activated alumina (specific surface area is 135m
2/ g, pore volume are 0.35cm
3/ g) contact keeps 100 ℃ of temperature to stir 1 hour, then with solution filter, and again 0 ℃ of lower crystallisation by cooling 1 hour, crystallization.Through solid after the solid-liquid separation in 50 ℃ of baking ovens dry 8 hours, obtain the 2-acrylamide-2-methylpro panesulfonic acid after refining, record yield and purity sees Table 1.
With the 2-acrylamide-2-methylpro panesulfonic acid after refining as stated above with acrylamide polymerization, the molecular weight of measuring the polymkeric substance that obtains sees Table 1.
Embodiment 3
This embodiment is used for illustrating the process for purification of the thick product of 2-acrylamide-2-methylpro panesulfonic acid provided by the invention.
The preparation of the thick product of 2-acrylamide-2-methylpro panesulfonic acid: in the four-hole boiling flask that is provided with temperature regulating device, agitator, thermometer and gas feeding unit, add the 330g vinyl cyanide, vinyl cyanide being cooled to after-10 ℃ to add concentration is the oleum 20g of 102 % by weight, in the reinforced process and complete rear holding temperature be-10 ℃ and continue stirring 1 hour; Then be warmed up to 40 ℃, passing into the 10g iso-butylene reacts, then add concentration in the reaction system and be the sulfuric acid 41g of 98 % by weight and continue to pass into iso-butylene, after the total amount of the iso-butylene that adds reaches 35g, close the iso-butylene valve in reaction system, be incubated and finish after 1 hour to react.Reaction solution is carried out vacuum filtration, obtain filter cake and filtrate.Filter cake is carried out vacuum-drying, and temperature is 110 ℃, and pressure is 10kPa, obtains dried filter cake, is the thick product of 2-acrylamide-2-methylpro panesulfonic acid, and purity is 98 % by weight.
The thick product of 2-acrylamide-2-methylpro panesulfonic acid refining: the aqueous acetic acid 500g and the thick product 250g of the above-mentioned 2-acrylamide-2-methylpro panesulfonic acid that makes that add moisture 8 % by weight in the four-hole boiling flask, warming while stirring to 80 ℃, after the dissolving and the 42g activated alumina (specific surface area is 148m
2/ g, pore volume are 0.42cm
3/ g) contact keeps 80 ℃ of temperature to stir 1 hour, then with solution filter, and again 10 ℃ of lower crystallisation by cooling 3 hours, crystallization.Through solid after the solid-liquid separation in 100 ℃ of baking ovens dry 4 hours, obtain the 2-acrylamide-2-methylpro panesulfonic acid after refining, record yield and purity sees Table 1.
With the 2-acrylamide-2-methylpro panesulfonic acid after refining as stated above with acrylamide polymerization, the molecular weight of measuring the polymkeric substance that obtains sees Table 1.
Embodiment 4
According to the refining 2-acrylamide-2-methylpro panesulfonic acid of the method for embodiment 1, different is, the amount of activated alumina of contact is 15g, records the yield of the 2-acrylamide-2-methylpro panesulfonic acid after refining and purity and the molecular weight of the polymkeric substance that obtains sees Table 1.
Embodiment 5
According to the refining 2-acrylamide-2-methylpro panesulfonic acid of the method for embodiment 1, different is, the amount of activated alumina of contact is 75g, records the yield of the 2-acrylamide-2-methylpro panesulfonic acid after refining and purity and the molecular weight of the polymkeric substance that obtains sees Table 1.
Embodiment 6
According to the refining 2-acrylamide-2-methylpro panesulfonic acid of the method for embodiment 1, different is that the specific surface area of activated alumina is 100m
2/ g, pore volume are 0.37cm
3/ g.The molecular weight of the polymkeric substance that records the yield of the 2-acrylamide-2-methylpro panesulfonic acid after refining and purity and obtain sees Table 1.
Comparative Examples 1
According to the refining 2-acrylamide-2-methylpro panesulfonic acid of the method for embodiment 1, different is not add activated alumina, after the thick product of 2-acrylamide-2-methylpro panesulfonic acid dissolves in aqueous acetic acid, direct cooling crystallization was through solid after the solid-liquid separation in 80 ℃ of baking ovens dry 6 hours.The molecular weight of the yield of the 2-acrylamide-2-methylpro panesulfonic acid that records and purity and the polymkeric substance that obtains sees Table 1.
Table 1
| Embodiment | The AMPS yield | AMPS purity | Polymericular weight |
| 1 | 72.18 | 99.91 | 1,900 ten thousand |
| 2 | 73.49 | 99.95 | 2,000 ten thousand |
| 3 | 73.69 | 99.88 | 1,800 ten thousand |
| 4 | 73.54 | 99.87 | 1,600 ten thousand |
| 5 | 71.44 | 99.85 | 1,800 ten thousand |
| 6 | 73.26 | 99.83 | 1,400 ten thousand |
| Comparative Examples 1 | 72.93 | 99.82 | 9,000,000 |
Embodiment 1 is compared and can find out with Comparative Examples 1, in with the solution after the dissolving of the thick product of aqueous acetic acid dissolving 2-acrylamide-2-methylpro panesulfonic acid, add activated alumina, although the purity of 2-acrylamide-2-methylpro panesulfonic acid changes little, can obviously improve the molecular weight of the polymkeric substance that polymerization obtains.
Embodiment 1 and embodiment 4 are compared and can find out, the amount of activated alumina reduces, and is little on the purity impact of 2-acrylamide-2-methylpro panesulfonic acid, but is unfavorable for the raising of the polymericular weight that polymerization obtains; Embodiment 1 and embodiment 5 are compared and can find out, the amount of activated alumina is too high, the molecular weight of the polymkeric substance that purity and the polymerization of 2-acrylamide-2-methylpro panesulfonic acid obtained does not only further improve, and the yield of 2-acrylamide-2-methylpro panesulfonic acid is reduced; Embodiment 1 and embodiment 6 are compared and can find out, the raising of the molecular weight of the polymkeric substance that the specific surface area of activated alumina reduces to be unfavorable for that the polymerization of 2-acrylamide-2-methylpro panesulfonic acid obtains.
The process for purification of 2-acrylamide-2-methylpro panesulfonic acid provided by the invention, can greatly improve the molecular weight of the polymkeric substance of the 2-acrylamide-2-methylpro panesulfonic acid polymerization formation after making with extra care, make the viscosity-average molecular weight of polymkeric substance up to 2,000 ten thousand, can satisfy the requirement of the high temperature resistant salt tolerant of used for tertiary oil recovery polymkeric substance.
Claims (10)
1. the process for purification of the thick product of 2-acrylamide-2-methylpro panesulfonic acid is characterized in that, described method comprises the steps:
(1) the thick product of 2-acrylamide-2-methylpro panesulfonic acid is dissolved in the aqueous acetic acid;
(2) step (1) gained solution is contacted rear the filtration with activated alumina, the mass ratio of activated alumina and the thick product of 2-acrylamide-2-methylpro panesulfonic acid is 1: 2-10, and the time of contact is 0.8-1.2 hour;
(3) the solution crystallisation by cooling that obtains after step (2) is filtered also carries out solid-liquid separation.
2. method according to claim 1, wherein, the temperature of contact is 50-110 ℃ described in the step (2), is preferably 80-100 ℃.
3. method according to claim 1 and 2, wherein, the temperature of dissolving is 50-110 ℃ described in the step (1), is preferably 80-100 ℃.
4. the described method of any one according to claim 1-3, wherein, the mass ratio of the thick product of described 2-acrylamide-2-methylpro panesulfonic acid and described aqueous acetic acid is 1: 2-7 is preferably 1: 2-5.
5. the described method of any one according to claim 1-4, wherein, the water content of described aqueous acetic acid is the 5-40 % by weight, is preferably the 8-20 % by weight.
6. the described method of any one according to claim 1-5, wherein, the mass ratio of described activated alumina and the thick product of described 2-acrylamide-2-methylpro panesulfonic acid is 1: 4-6.
7. the described method of any one according to claim 1-6, wherein, the specific surface area of described activated alumina is 100-200m
2/ g, pore volume are 0.25-0.6cm
3/ g; Under the preferable case, the specific surface area of described activated alumina is 135-148m
2/ g, pore volume are 0.35-0.42cm
3/ g.
8. the described method of any one according to claim 1-7, wherein, the temperature of described crystallisation by cooling is 0-10 ℃, the time is 1-3 hour.
9. the described method of any one according to claim 1-8, wherein, the purity of the thick product of described 2-acrylamide-2-methylpro panesulfonic acid is the 95-98 % by weight.
10. a 2-acrylamide-2-methylpro panesulfonic acid is characterized in that, described 2-acrylamide-2-methylpro panesulfonic acid is made with extra care and got by the described method of any one among the claim 1-9.
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| CN108966649A (en) * | 2017-03-20 | 2018-12-07 | 爱森（中国）絮凝剂有限公司 | The method for handling the suspension of solid particle in water using the (co) polymer of the 2- acrylamide-2-methyl propane sulfonic of hydrated crystalline form |
| CN113651732A (en) * | 2020-09-19 | 2021-11-16 | 寿光市荣晟新材料有限公司 | Preparation process of 2-acrylamide-2-methylpropanesulfonic acid sodium salt |
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| CN103254102A (en) * | 2013-06-06 | 2013-08-21 | 合肥艾普拉斯环保科技有限公司 | Method for purifying acrylamide alkyl sulfonic acid |
| CN103254102B (en) * | 2013-06-06 | 2015-09-30 | 梅龙毅 | A kind of method of purifying acrylamide alkyl sulfonic acid |
| CN108966649A (en) * | 2017-03-20 | 2018-12-07 | 爱森（中国）絮凝剂有限公司 | The method for handling the suspension of solid particle in water using the (co) polymer of the 2- acrylamide-2-methyl propane sulfonic of hydrated crystalline form |
| CN108966649B (en) * | 2017-03-20 | 2022-03-01 | 爱森（中国）絮凝剂有限公司 | Method for treating a suspension of solid particles in water with a (co) polymer of 2-acrylamido-2-methylpropanesulfonic acid in hydrated crystalline form |
| CN107129447A (en) * | 2017-05-10 | 2017-09-05 | 潍坊金石环保科技有限公司 | A kind of process for purification of the methyl propane sulfonic acid of 2 acrylamido 2 |
| CN107129447B (en) * | 2017-05-10 | 2022-03-15 | 潍坊金石环保科技有限公司 | Refining method of 2-acrylamide-2-methylpropanesulfonic acid |
| CN114195685A (en) * | 2020-09-18 | 2022-03-18 | Spcm股份公司 | Purification method of 2-acrylamide-2-methylpropanesulfonic acid |
| CN114195685B (en) * | 2020-09-18 | 2024-02-06 | 爱森集团 | Purification method of 2-acrylamido-2-methylpropanesulfonic acid |
| CN113651732A (en) * | 2020-09-19 | 2021-11-16 | 寿光市荣晟新材料有限公司 | Preparation process of 2-acrylamide-2-methylpropanesulfonic acid sodium salt |
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