WO2017111205A1 - Procédé de production de résine superabsorbante - Google Patents

Procédé de production de résine superabsorbante Download PDF

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Publication number
WO2017111205A1
WO2017111205A1 PCT/KR2016/002725 KR2016002725W WO2017111205A1 WO 2017111205 A1 WO2017111205 A1 WO 2017111205A1 KR 2016002725 W KR2016002725 W KR 2016002725W WO 2017111205 A1 WO2017111205 A1 WO 2017111205A1
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Prior art keywords
polymer
surface crosslinking
super absorbent
water
weight
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PCT/KR2016/002725
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English (en)
Korean (ko)
Inventor
김주은
김기철
박세열
김기현
Original Assignee
주식회사 엘지화학
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Priority claimed from KR1020160029847A external-priority patent/KR101857702B1/ko
Application filed by 주식회사 엘지화학 filed Critical 주식회사 엘지화학
Priority to EP16879073.1A priority Critical patent/EP3321307B1/fr
Priority to CN201680052415.0A priority patent/CN108026283B/zh
Priority to US15/755,325 priority patent/US11198768B2/en
Priority to PL16879073T priority patent/PL3321307T3/pl
Publication of WO2017111205A1 publication Critical patent/WO2017111205A1/fr

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    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F2/00—Processes of polymerisation
    • C08F2/44—Polymerisation in the presence of compounding ingredients, e.g. plasticisers, dyestuffs, fillers
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F2/00—Processes of polymerisation
    • C08F2/46—Polymerisation initiated by wave energy or particle radiation
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F20/00—Homopolymers and copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical or a salt, anhydride, ester, amide, imide or nitrile thereof
    • C08F20/02—Monocarboxylic acids having less than ten carbon atoms, Derivatives thereof
    • C08F20/04—Acids, Metal salts or ammonium salts thereof
    • C08F20/06—Acrylic acid; Methacrylic acid; Metal salts or ammonium salts thereof
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J3/00—Processes of treating or compounding macromolecular substances
    • C08J3/02—Making solutions, dispersions, lattices or gels by other methods than by solution, emulsion or suspension polymerisation techniques
    • C08J3/03—Making solutions, dispersions, lattices or gels by other methods than by solution, emulsion or suspension polymerisation techniques in aqueous media
    • C08J3/075—Macromolecular gels
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J3/00—Processes of treating or compounding macromolecular substances
    • C08J3/24—Crosslinking, e.g. vulcanising, of macromolecules
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K3/00—Use of inorganic substances as compounding ingredients
    • C08K3/34—Silicon-containing compounds

Definitions

  • the present invention relates to a method for producing a super absorbent polymer. More specifically, the present invention relates to a method for producing a super absorbent polymer having improved water absorption characteristics without deterioration in water holding capacity and pressure absorbing capacity. Background technology
  • Super Absorbent Polymer is a synthetic polymer material capable of absorbing water of 500 to 1,000 times its own weight.As a developer, super absorbent material (AMG) and absorbent gel (AGM) They are named differently. Such super absorbent polymers have been put into practical use as physiological tools, and are currently used in sanitary products such as paper diapers for children, horticultural soil repair agents, civil engineering, building index materials, seedling sheets, food preservation crabs, and It is widely used as a material for steaming.
  • a method for producing such a super absorbent polymer a method by reverse phase suspension polymerization or a method by aqueous solution polymerization is known.
  • Reverse phase suspension polymerization is disclosed in, for example, Japanese Patent Laid-Open Nos. 56-161408, 57-158209, and 57-198714.
  • a thermal polymerization method in which a hydrous gel polymer is broken and polymerized in a kneader having a plurality of shafts, and photopolymerization which simultaneously performs polymerization and drying by irradiating ultraviolet rays or the like on a belt with a high concentration of aqueous solution Methods and the like are known.
  • the hydrous gel polymer obtained through the polymerization reaction as described above is generally subjected to a step of selectively crosslinking the surface of the polymer in order to have a desired absorption capacity and pressure absorption capacity after the grinding process.
  • a step of selectively crosslinking the surface of the polymer in order to have a desired absorption capacity and pressure absorption capacity after the grinding process.
  • it is necessary to control the penetration depth of the surface agent and for this purpose, it is common to control the penetration depth of the surface crosslinker using alcohol and water.
  • alcohol is used to control the penetration depth of the crosslinking agent, a large amount of alcohol is consumed, which is disadvantageous in terms of cost : an additional drying treatment is required.
  • the surface crosslinking agent by performing a surface crosslinking reaction using a surface crosslinking agent that satisfies specific conditions, the surface crosslinking agent can further improve the physical properties of the final product by adjusting the penetration depth. It is to provide a method for producing a super absorbent polymer.
  • the step of thermally polymerizing or photopolymerizing a monomer composition comprising a water-soluble ethylenically unsaturated monomer and a polymerization initiator to form a hydrogel polymer; Drying the hydrogel polymer;
  • the surface penetration depth of the surface crosslinking agent can be appropriately controlled by using a hydrophobic alcohol having 4 or more carbon atoms instead of the hydrophilic alcohol generally used as the surface crosslinking agent.
  • a hydrophobic alcohol having 4 or more carbon atoms instead of the hydrophilic alcohol generally used as the surface crosslinking agent.
  • product properties can be further improved, and in particular, it is possible to provide a superabsorbent polymer having improved absorption characteristics without deteriorating the pressure absorption capacity.
  • Method for producing a super absorbent polymer of the present invention comprises the steps of thermally polymerizing or photopolymerizing a monomer composition comprising a water-soluble ethylenically unsaturated monomer and a polymerization initiator to form a hydrogel polymer; Drying the hydrogel polymer; Pulverizing the dried polymer; And pulverized polymer, hydrophobic Mixing a surface crosslinking agent comprising an alcohol to perform a surface crosslinking reaction.
  • polymer or “polymer” means that the water-soluble ethylenically unsaturated monomer is in a polymerized state, and may cover all water content ranges or particle size ranges.
  • a polymer having a water content (water content) of about 40% by weight or more after being dried before polymerization may be referred to as a hydrous gel polymer.
  • base resin or “base resin powder” means that the polymer is dried and ground to form a powder.
  • Superabsorbent resin also means the polymer or the base resin itself depending on the context, or further processes for the polymer or the base resin, for example surface crosslinking, fine powder reassembly, drying, grinding, classification, etc. It is used to cover everything that has been made suitable for commercialization through.
  • the step of forming a hydrogel polymer, the drying of the hydrogel polymer, and the step of pulverizing the dried polymer is in the art for preparing a super absorbent polymer It can be carried out by the steps and methods commonly used in the art.
  • the monomer composition which is a raw material of the super absorbent polymer includes a water-soluble ethylenically unsaturated monomer and a polymerization initiator.
  • water-soluble ethylene-based unsaturated monomer as long as it is a monomer commonly used in the production of superabsorbent polymers, it may be used without limitation in the constitution.
  • any one or more selected from the group consisting of anionic monomers and salts thereof, nonionic hydrophilic-containing monomers, amino group-containing unsaturated monomers and quaternized compounds thereof can be used.
  • an alkali metal salt such as acrylic acid or a salt thereof, for example acrylic acid or a sodium salt thereof can be used, and the use of such a monomer makes it possible to prepare a super absorbent polymer having better physical properties.
  • acrylic acid may be neutralized with a basic compound such as caustic soda (NaOH).
  • NaOH caustic soda
  • the degree of neutralization of the water-soluble ethylenically unsaturated monomer may be adjusted to about 50 to about 95% or about 70 to about 85%, to provide a superabsorbent polymer having excellent water retention without fear of precipitation during neutralization within this range. can do.
  • the concentration of the water-soluble ethylenically unsaturated monomer, in which the subject from about 20 to about 60 weight 0/0, preferably from about 40 to about 50 increase% of the monomer composition containing a source material and a solvent of the water-absorbent resin, and In consideration of the polymerization time, the reaction conditions and the like, the concentration may be appropriate. However, when the concentration of the monomer is too low, the yield of the superabsorbent polymer may be low and there may be a problem in economics. On the contrary, when the concentration is too high, some of the monomer may be precipitated or the grinding efficiency of the polymerized hydrogel polymer may be low. Etc. may cause problems in the process and may decrease the physical properties of the super absorbent polymer.
  • the polymerization initiator used in the polymerization in the method for producing a super absorbent polymer of the present invention is not particularly limited as long as it is generally used for producing the super absorbent polymer.
  • the polymerization initiator may use a thermal polymerization initiator or a photopolymerization initiator according to UV irradiation depending on the polymerization method.
  • a thermal polymerization initiator since a certain amount of heat is generated by irradiation such as ultraviolet irradiation, and a certain amount of heat is generated in accordance with the progress of the polymerization reaction, which is an exothermic reaction, it may further include a thermal polymerization initiator.
  • the photopolymerization initiator may be used without any limitation as long as it is a compound capable of forming radicals by light such as ultraviolet rays.
  • persulfate initiators examples include sodium persulfate (Na 2 S 2 0 8 ), potassium persulfate (K 2 S 2 0 8 ), ammonium persulfate (NH 4 ) 2 S 2 0 8
  • examples of the azo (Azo) initiator include 2, 2-azobis- (2-amidinopropane) dihydrochloride (2, 2- azobis (2-amidinopropane) dihydrochloride), 2 2,2-azobis- (N, N-dimethylene) isobutyramidine dihydrochloride), 2-azobis- (N, N-dimethylene) isobutyramidine dihydrochloride
  • the thermal polymerization initiator may be included in a concentration of about 0.001 to about 0.5% by weight based on the monomer composition.
  • concentration of the thermal polymerization initiator is too low, additional thermal polymerization hardly occurs, and thus the effect of the addition of the thermal polymerization initiator may be insignificant.
  • concentration of the thermal polymerization initiator is too high, the molecular weight of the superabsorbent polymer may be low and the physical properties may be uneven. have.
  • photopolymerization initiator examples include benzoin ether, dialkyl acetophenone, hydroxyl alkylketone, phenyl glyoxylate, benzyl dimethyl ketal, and acyl. At least one selected from the group consisting of acyl phosphine and alpha -aminoketone may be used.
  • acylphosphine commercially available lucirin TPO, that is, 2,4,6-trimethyl- benzoyl-trimethyl phosphine oxide (2,4,6-trimethyl-benzoyl-trimethyl phosphine oxide) can be used.
  • 2,4,6-trimethyl- benzoyl-trimethyl phosphine oxide 2,4,6-trimethyl-benzoyl-trimethyl phosphine oxide
  • the photopolymerization initiator may be included in a concentration of about 0.005 to about 1.0 weight 0/0 with respect to the monomer composition. If the concentration of the photopolymerization initiator is too low, the polymerization rate may be slow. If the concentration of the photopolymerization initiator is too high, the molecular weight of the superabsorbent polymer may be low and the physical properties may be uneven.
  • the monomer composition may further include an internal crosslinking agent as a raw material of the super absorbent polymer.
  • the internal crosslinking agent may include at least one functional group capable of reacting with the water-soluble substituent of the water-soluble ethylenically unsaturated monomer and at least one ethylenically unsaturated group;
  • a crosslinking agent having two or more water-soluble substituents and / or functional groups capable of reacting with the water-soluble substituents formed by hydrolysis of the monomers may be used.
  • the internal crosslinking agent examples include bisacrylamide having 8 to 12 carbon atoms, bismethacrylamide, poly (meth) acrylate having 2 to 10 carbon atoms, poly (meth) allyl ether having 2 to 10 carbon atoms, and the like. More specifically, ⁇ , ⁇ '- methylenebis (meth) acrylate, ethyleneoxy (meth) acrylate, polyethyleneoxy (meth) acrylate, propyleneoxy (meth) acrylate, glycerol diacrylate , Glycerin triacrylate, trimethol triacrylate, triallylamine, triarylcyanurate, triallyl isocyanate, polyethylene glycol, diethylene glycol and propylene glycol may be used. Such an internal crosslinking agent may be included in a concentration of about 0.001 to about 2.0 wt% based on the monomer composition to crosslink the polymerized polymer.
  • the monomer composition of the super absorbent polymer may be prepared by thickener, plasticizer, preservative stabilizer, antioxidant, etc. It may further include an additive.
  • Raw materials such as the above-mentioned water-soluble ethylenically unsaturated monomers, photopolymerization initiators, thermal polymerization initiators, internal crosslinking agents and additives may be prepared in the form of a monomer composition solution dissolved in a solvent.
  • the solvent that can be used at this time can be used without limitation in the composition as long as it can dissolve the above-mentioned components, for example, water, ethanol, ethylene glycol, diethylene glycol, triethylene glycol, 1,4-butanedi , Propylene glycol, ethylene glycol monobutyl ether, propylene glycol monomethyl ether, propylene glycol monomethyl ether acetate, methyl ethyl ketone, acetone, methyl amyl ketone, cyclonucleanone, cyclopentanone, diethylene glycol monomethyl ether, diethylene Glycol ethyl ether, toluene, xylene, butyrolactone, carbye can be used in combination of 1 or more types chosen from methyl cellosolve acetate, N, N-dimethylacetamide, etc.
  • the solvent may be included in the remaining amount except for the above-described components with respect to the total content of the monomer composition.
  • the method of preparing a hydrogel polymer by thermally polymerizing or photopolymerizing such a monomer composition is not particularly limited as long as it is a commonly used polymerization method.
  • the polymerization method is largely divided into thermal polymerization and photopolymerization according to the polymerization energy source, and when the thermal polymerization is usually carried out, it can be carried out in a semi-unggi machine having a stirring shaft such as kneader, and when the polymerization proceeds, Although it can proceed in a semi-unggi equipped with a conveyor belt possible, the above-described polymerization method is an example, the present invention is not limited to the above-described polymerization method.
  • the hydrous gel polymer obtained by thermal polymerization by supplying hot air or by heating the reactor to a reactor such as a kneader having a stirring shaft as described above is discharged to the reactor outlet according to the shape of the stirring shaft provided in the reactor.
  • the gel polymer may be in the form of several centimeters to several millimeters.
  • the size of the water-containing gel polymer obtained may vary depending on the concentration and the injection speed of the monomer composition to be injected, the water-containing gel polymer having a particle size of 2 to 50 mm can be obtained.
  • the conveyor belt is movable as described above
  • the form of the polymer usually obtained may be a hydrous gel polymer on a sheet having the width of the belt.
  • the thickness of the polymer sheet depends on the concentration and the injection speed of the monomer composition to be injected, but it is usually preferable to supply the monomer composition so that a polymer on the sheet having a thickness of about 0.5 to about 5 cm can be obtained.
  • the production efficiency is not preferable because it is low, and when the thickness of the polymer on the sheet exceeds 5 cm, the polymerization reaction does not occur evenly over the entire thickness. You may not.
  • the water content of the thermally polymerized or photopolymerized hydrogel polymer is the water content of the thermally polymerized or photopolymerized hydrogel polymer.
  • water content means the weight of the water-containing gel polymer subtracted from the weight of the dried polymer by the content of moisture to account for the total weight of the water-containing gel polymer. Specifically, it is defined as a value calculated by measuring the weight loss due to moisture evaporation in the polymer in the process of raising the temperature of the polymer through infrared heating and drying. At this time, the drying condition is to increase the temperature to 180 ° C at room temperature and then maintained at 180 ° C. The total drying time is set to 20 minutes, including 5 minutes of the temperature rise step, the moisture content is measured.
  • the hydrous gel polymer obtained is dried.
  • the rough grinding step before drying may be further roughened.
  • the pulverizer used is not limited in configuration, specifically, a vertical pulverizer, a turbo cutter, a turbo grinder, a rotary cutter mill, a cutting machine mill (cutter mill), the one selected disk grinder in the crushing machine the group consisting of (disc mill), a piece crusher (Shred crasher), crusher (crusher), 'chopper (chopper) and source plate type cutter (disc cutter) It may include, but is not limited to the above-described example.
  • the grinding step may be pulverized so that the particle size of the hydrogel polymer is about 2 to about 10mm.
  • drying temperature of the drying step may be 150 ° C to 250 ° C.
  • "Drying temperature" throughout this specification may be defined as the temperature of the heating reactor, including the heating medium and the polymer in the drying process, or the temperature of the heating medium supplied for drying.
  • the drying temperature is less than 150 ° C, the drying time may be too long and the physical properties of the final superabsorbent polymer may be lowered. If the drying temperature is higher than 250 ° C, only the polymer surface is dried excessively. Fine powder may occur in the grinding step, and there is a fear that the physical properties of the superabsorbent polymer to be finally formed decrease.
  • the drying may be carried out at a temperature of 150 ° C to 200 ° C, more preferably at a temperature of 160 ° C to 180 ° C.
  • the drying time is not limited to the configuration, but in consideration of the process efficiency, etc., it may proceed for 20 to 90 minutes.
  • drying step may be selected and used without limiting its configuration.
  • the drying step may be performed by a method such as hot air supply, infrared irradiation, microwave irradiation, or ultraviolet irradiation.
  • the water content of the polymer after the drying step may be 0.1 to 10% by weight.
  • the dried polymer obtained through this drying step is subjected to a grinding step.
  • the polymer powder obtained after the final grinding step may have a weight average particle diameter of 150 to 850.
  • the grinder used to grind to such a weight average particle diameter is specifically a pin mill, a hammer mill, a screw mill, a mill, a disc mill. Or a jog mill (jog mill) and the like can be used, but the present invention is not limited to the above examples.
  • the polymer powder obtained after grinding according to the particle size There may be a separate process of classification.
  • the polymer having a particle size of about 150 to about 850 11 may be classified so that the surface crosslinking reaction step may be performed only on the polymer powder having such a particle size.
  • a surface crosslinking reaction is performed by adding a surface crosslinking agent to the ground polymer.
  • Surface crosslinking is the step of increasing the crosslink density near the polymer particle surface with respect to the crosslink density inside the particles.
  • the surface crosslinker is applied to the surface of the polymer particles.
  • this reaction occurs on the surface of the polymer particles, which improves the crosslinkability on the surface of the particles without substantially affecting the interior of the particles.
  • the surface crosslinked polymer particles thus have a higher degree of crosslinking near the surface than inside.
  • surface crosslinking reaction is performed using a surface crosslinking agent containing a hydrophobic alcohol.
  • the hydrophobic alcohol may be one or more selected from the group consisting of polyhydric alcohol (alcohol) having 4 or more carbon atoms. More specifically, a polyhydric alcohol having 4 to 10 carbon atoms, preferably 4 to 7 carbon atoms, and including a branched alkyl group, preferably 2,2-dimethyl-1,3- Propanedi (2,2 'Dimethyl-1,3-propanediol) can be used.
  • a hydrophilic alcohol such as alcohol having 3 or less carbon atoms such as 1,3-propanediol (1,3-PDO) has been used.
  • the hydrophilic alcohol is used as the surface crosslinking agent, as the reaction time increases, the degree of penetration of the surface crosslinking agent is too deep and crosslinking tends to proceed to the inside of the polymer. If the crosslinking reaction proceeds inside the polymer, the crosslinking density is increased, and thus the water holding capacity (CRC) and the pressure absorbing capacity (AUL) are reduced, resulting in a decrease in physical properties of the final product.
  • CRC water holding capacity
  • AUL pressure absorbing capacity
  • the superabsorbent polymer production method of the present invention by using a hydrophobic alcohol as a surface crosslinking agent solved this problem.
  • the surface crosslinking reaction is performed by adding hydrophobic alcohol to the polymer, it is difficult to penetrate into the polymer due to the hydrophobic property, so that the crosslinking reaction occurs only on the surface. Therefore, even if the crosslinking reaction time increases, crosslinking inside the polymer does not easily occur, and a crosslinking region is formed only on the polymer surface, and the water holding capacity and pressure absorbing ability of the base resin can be maintained.
  • the hydrophobic alcohol content may be used in an amount of about 0.01 to about 10 parts by weight, preferably about 0.01 to about 5 parts by weight, and more preferably about 0.01 to about 1 part by weight, based on 100 parts by weight of the polymer.
  • the surface crosslinked semi-finished silica (silica) or clay (clay) may further include. Since the silica or clay has a porosity, the transmissivity of the superabsorbent polymer may be further improved by adding these crosslinked reactions.
  • the surface crosslinking agent and the polymer powder may be mixed in a reaction tank, or a method of spraying the surface crosslinking agent on the polymer powder, a method of continuously supplying the polymer and the surface crosslinking agent to a mixer operated continuously, and the like may be used.
  • the surface crosslinking agent When the surface crosslinking agent is added, water, a low alcohol (e.g., methanol) or a mixture thereof may be mixed together as a solvent.
  • a solvent When the solvent is added, there is an advantage that the surface crosslinker can be evenly dispersed in the polymer.
  • the content of the solvent is about 0.1 to about 1 part by weight based on 100 parts by weight of the polymer for the purpose of inducing even dispersion of the surface crosslinking agent and preventing aggregation of the polymer powder and optimizing the surface penetration depth of the crosslinking agent. Is preferably added.
  • the surface crosslinking reaction and drying may take place simultaneously. If the crosslinking reaction temperature is less than 140 ° C, surface crosslinking reaction may not occur, and if it exceeds 220 ° C, foreign substances and odors may be generated due to carbonization, or property degradation and stable process operating conditions may be secured due to excessive reaction. Missing problems can occur. In addition, when the crosslinking reaction time is too short (less than 20 minutes), sufficient crosslinking reaction cannot be performed, and when the crosslinking reaction time exceeds 120 minutes, due to excessive surface crosslinking reaction, property degradation due to damage of the polymer particles may occur.
  • the temperature raising means for surface crosslinking reaction is not specifically limited. It can be heated by supplying a heat medium or by directly supplying a heat source.
  • a heated fluid such as steam, hot air, or hot oil may be used, but the present invention is not limited thereto, and the temperature of the heat medium to be supplied is a means of heating medium, a temperature increase rate, and a temperature increase. considering the target temperature can be 'appropriately selected.
  • the heat source directly supplied may be a heating method through electricity, a gas heating method, but the present invention is not limited to the above examples.
  • the superabsorbent polymer obtained according to the production method of the present invention as described above has improved water retention, pressure absorption capacity and transmittance.
  • the super absorbent polymer prepared according to the production method of the present invention has a water retention capacity (CRC) of about 25 to 50 g / g, preferably about 30 to about 40 g / g, measured according to the EDANA method WSP 241.2.
  • the pressure absorption capacity (AUP) measured according to the EDANA method WSP 242.2 is about 10 to about 30 g / g, preferably about 15 to about 30 g / g, showing excellent water retention and pressure absorption capacity.
  • the pressure absorbing ability in the case of the pressure absorbing ability, it may exhibit an effect of improving the pressure absorbing ability of about 5% or more, for example, about 5 to about 20%, or about 10 to about 20%, than when the hydrophobic alcohol is not used as the surface crosslinking agent.
  • the monomer composition was fed at a feed rate of 500 to 2,000 mL / min on a rotating belt having a width of 10 cm and a length of 2 m and rotating at a speed of 50 cm / min.
  • the polymerization reaction was performed for 60 seconds by irradiating ultraviolet rays having an intensity of 10 mW / cm 2 simultaneously with the supply of the monomer composition.
  • the mixture was cut by a meat chopper method and dried at 180 ° C. for 1 hour using a convection oven.
  • Example 1 After drying, it was pulverized with a pulverizer and classified to select a 150 to 850 ⁇ size to prepare a base resin having a water retention capacity of 50 g / g.
  • a pulverizer After drying, it was pulverized with a pulverizer and classified to select a 150 to 850 ⁇ size to prepare a base resin having a water retention capacity of 50 g / g.
  • Base resin of preparation example 50 g / g water retention capacity (CRC), 7.8 g / g pressurized absorption capacity (AUL)) 3.2 g of water, 4.0 g of methanol, 0.088 g of 2,2-dimethyl-1,3-propanediol and silica 0.008 g (trade name DM30S) were mixed to perform a surface crosslinking reaction for 60 minutes at a temperature of 185 ° C.
  • CRC water retention capacity
  • AUL pressurized absorption capacity
  • Superabsorbent polymer was prepared in the same manner as in Example 1, except that the surface crosslinking reaction was performed for 110 minutes. Comparative Example 1
  • the mixture was classified into a standard mesh of ASTM specification and 150 / m to
  • a super absorbent polymer was prepared in the same manner as in Comparative Example 1 except that the surface crosslinking reaction was performed for 60 minutes. Comparative Example 3
  • a super absorbent polymer was prepared in the same manner as in Comparative Example 1 except that the surface crosslinking reaction was performed for 90 minutes.
  • the superabsorbent polymers of the Examples and Comparative Examples were measured for centrifugal water retention (CRC) by unloaded absorption ratio according to EDANA method WSP 241.2. Specifically, examples and classifying the resin obtained resin obtained in Comparative example to 300 to 600 microns (), and the size W (g) (about 0. 2 g) placed uniformly on the envelope of the non-woven fabric sealed (seal) by After that, in normal saline of 0.9 mass% at room temperature Impregnated. After 30 minutes, the envelope was centrifuged and drained at 250 G for 3 minutes, and then the mass W2 (g) of the envelope was measured. Moreover, after carrying out the same operation without using resin, the mass W1 (g) at that time was measured. Using each mass obtained, CRC (g / g) was computed according to the following formula.
  • W (g) is the weight (g) of the absorbent resin
  • Wl (g) is a nonwoven absorbent bag containing 0.9% by weight of saline solution at room temperature .
  • Device weight measured after 30 minutes of impregnation and dehydration at 250G for 3 minutes using a centrifuge,
  • W2 (g) is the device weight including water absorbent resin after 30 minutes impregnation of 0.9% by weight of physiological saline in a nonwoven bag containing water absorbent resin and then dehydrated at 250G for 3 minutes using a centrifuge. .
  • the absorbency under pressure (AUL) of the superabsorbent polymers of the Examples and Comparative Examples was measured according to the EDANA method WSP 242.2.
  • the obtained resin is classified into 300-600 micrometers Cam) size, and W (g) (about 0.16g, A) is evenly sprayed on the AUL cylinder, and the 0.9psi weight is raised and weighed (B). 0.9 mass 0/0 up to a Petri dish containing a physiological saline was swollen for 60 minutes. After 60 minutes, taken out and weighed (C),
  • AUL (g / g) was computed according to the following formula.
  • AUL (g / g) (C-B) / A
  • A is the weight of absorbent resin (g) .

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Abstract

L'invention concerne un procédé de production d'une résine superabsorbante. Le procédé de préparation selon la présente invention permet la régulation adéquate de la profondeur de pénétration en surface d'un agent de réticulation de surface et permet également la production d'une résine superabsorbante présentant d'excellentes propriétés physiques via une réticulation de surface uniforme. Conformément, il est possible d'obtenir une résine superabsorbante présentant des propriétés d'absorption améliorées sans réduire la capacité d'absorption sous pression.
PCT/KR2016/002725 2015-12-23 2016-03-17 Procédé de production de résine superabsorbante WO2017111205A1 (fr)

Priority Applications (4)

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EP16879073.1A EP3321307B1 (fr) 2015-12-23 2016-03-17 Procédé de production de résine superabsorbante
CN201680052415.0A CN108026283B (zh) 2015-12-23 2016-03-17 超吸收性聚合物的制备方法
US15/755,325 US11198768B2 (en) 2016-03-11 2016-03-17 Preparation method of super absorbent polymer
PL16879073T PL3321307T3 (pl) 2015-12-23 2016-03-17 Sposób wytwarzania żywicy superabsorbującej

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2020096003A1 (fr) 2018-11-07 2020-05-14 株式会社日本触媒 Procédé de production d'un absorbant particulaire d'eau et absorbant particulaire d'eau
US12023646B2 (en) 2019-09-11 2024-07-02 Lg Chem, Ltd. Preparation method of super absorbent polymer

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR950006118B1 (ko) * 1991-01-22 1995-06-09 가부시끼가이샤 니혼 쇼꾸바이 흡수성 수지의 제조방법
KR20110049072A (ko) * 2009-11-04 2011-05-12 주식회사 엘지화학 높은 생산성을 갖는 흡수성수지의 제조방법
KR20110136597A (ko) * 2010-06-15 2011-12-21 주식회사 엘지화학 고흡수성 수지의 제조 방법
KR20120054836A (ko) * 2010-11-22 2012-05-31 주식회사 엘지화학 고흡수성 수지의 제조 방법
KR20130120300A (ko) * 2012-04-25 2013-11-04 주식회사 엘지화학 고흡수성 수지의 제조 방법

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR950006118B1 (ko) * 1991-01-22 1995-06-09 가부시끼가이샤 니혼 쇼꾸바이 흡수성 수지의 제조방법
KR20110049072A (ko) * 2009-11-04 2011-05-12 주식회사 엘지화학 높은 생산성을 갖는 흡수성수지의 제조방법
KR20110136597A (ko) * 2010-06-15 2011-12-21 주식회사 엘지화학 고흡수성 수지의 제조 방법
KR20120054836A (ko) * 2010-11-22 2012-05-31 주식회사 엘지화학 고흡수성 수지의 제조 방법
KR20130120300A (ko) * 2012-04-25 2013-11-04 주식회사 엘지화학 고흡수성 수지의 제조 방법

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2020096003A1 (fr) 2018-11-07 2020-05-14 株式会社日本触媒 Procédé de production d'un absorbant particulaire d'eau et absorbant particulaire d'eau
US12023646B2 (en) 2019-09-11 2024-07-02 Lg Chem, Ltd. Preparation method of super absorbent polymer

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