Patent Application
20050234205
The present invention relates to novel copolymers, paper treatment agents comprising the copolymers, and paper treated with the paper treatment agents.
Hitherto the following water- and oil-resistance processing agents for paper have been proposed:
(1) A processing agent which comprises a phosphate ester compound having a polyfluoroalkyl group (hereinafter referred as a Rf group) as an essential component (cf. JP-A-64-6196 and JP-A-3-123786).
(2) A processing agent which comprises a copolymer of an acrylate having a Rf group and vinylidene chloride, as an essential component (cf. JP-A-55-69677, JP-A-51-133511 and JP-B-53-22547).
(3) A processing agent which comprises a copolymer of an acrylate having a Rf group, dimethylaminoalkyl methacrylate and vinyl acetate, as an essential component (cf. JP-A-7-206942).
The phosphate ester compound having a Rf group, contained in the processing agent (1), is a water-soluble compound, and therefore can not impart water repellency to paper, and further markedly lowers oil repellency, if a sizing agent is contained in the processing agent.
To generally proof paper against oil, external addition processing methods which impregnate or coat a base paper with a processing agent are employed. In the external addition processing methods, a size press and various coaters are used, and the treated paper is dried at a temperature of 80 to 100° C. for such short time as several seconds to several tens seconds. When the processing agent is used in the external addition processing method, it is necessary to select such a processing agent that can impart high water- and oil-resistance properties to paper at a relatively low temperature for relatively short time.
When the processing agent (2) is diluted with water for external addition to paper and the immersion, drawing or circulation is carried out at a high speed, the following problems arise: the stability of the processing agent becomes poor; scum occurs in the processing agent; dirt deposits on the rolls; the adsorption of the processing agent onto the paper becomes insufficient, and so on. Thus, sufficient properties can not be imparted to the paper.
The processing agent (3) can not impart sufficient performance to paper when used in combination with a cationic agent such as a paper strength agent or sizing agent.
The present inventors have discovered that sufficient performance can be imparted to paper by treating the paper with a paper treatment agent which comprises, as an essential component, a copolymer having specified repeating units, even if the agent is used in combination with a cationic agent (e.g., a paper strength agent), and that this paper treatment agent has a low viscosity and thus is easily handled.
The subject matter of the present invention relates to a fluorine-containing copolymer comprising:
The copolymer of the present invention may further comprise 0 to 10% by weight of at least one monomer (e) other than the monomers (a), (b), (c) and (d). The copolymer of the present invention has constituting units derived from the monomers (a), (b), (c) and (d), and if needed, the monomer (e).
Throughout the present specification, an acrylate and a methacrylate are generally referred to as (meth)acrylate. Likewise, (meth)acrylamide and the like are used as generic terms as above.
The Rf group is a group in which at least two hydrogen atoms of a C1-C21 alkyl group are substituted with fluorine atoms. The Rf group may have a linear or branched chain structure, and preferably has 2 to 20 carbon atoms, particularly 4 to 16 carbon atoms. The ratio of fluorine atoms in the Rf group is preferably at least 60%, more preferably at least 80%, in particular, substantially 100%, when expressed by the equation: (the number of fluorine atoms in the Rf group)/(the number of hydrogen atoms in an alkyl group which has the same number of carbon atoms as that of the Rf group)×100 (%). Particularly preferred Rf group is a perfluoroalkyl group which is formed by substituting all the hydrogen atoms in the alkyl group with fluorine atoms.
The fluoromonomer (a) is a (meth)acrylate having a Rf group, which is a compound having the Rf group in the ester residue of (meth)acrylate. One or at least two different (meth)acrylates having Rf groups may be used.
For example, the fluoromonomer (a) may be a fluoroalkyl group-containing (meth)acrylate of the general formula:
Rf-A-OCOCR11═CH2 (I-a)
wherein Rf, R11 and A are as defined in the formula (I).
In the formula (I) or (I-a), the A group may be a linear or branched alkylene group having 1 to 20 carbon atoms, a group of the formula: —SO2N(R21)R22— or a group of the formula: —CH2CH(OR23)CH2— (in which R21 represents an alkyl group having 1 to 10 carbon atoms; R22 represents a linear or branched alkylene group having 1 to 10 carbon atoms; and R23 represents a hydrogen atom or an acyl group having 1 to 10 carbon atoms).
Examples of the fluoromonomer (a) include the followings:
wherein Rf represents a fluoroalkyl group having 1 to 21 carbon atoms; R1 represents a hydrogen atom or an alkyl group having 1 to 10 carbon atoms; R2 represents an alkylene group having 1 to 10 carbon atoms; R3 represents a hydrogen atom or a methyl group; Ar represents an optionally substituted arylene group; and n is an integer of 1 to 10.
Specific examples of the fluoromonomer (a) include the following compounds, in each of which R6 represents a hydrogen atom or a methyl group:
More specific examples of the fluoromonomer (a) include the following compounds:
The nitrogen-containing monomer (b) is a compound having at least one nitrogen atom (particularly an amino group) and one carbon-carbon double bond. The nitrogen-containing monomer (b) is a compound of the formula (II) in which the nitrogen atom is not cationic, or a compound of the formula (III) in which the nitrogen atom is cationic. The nitrogen-containing monomer (b) of the formula (II) is a (meth)acrylate having no cationic group. The nitrogen-containing monomer of the formula (III) is a (meth)acrylate having a cationic group.
The groups R22 and R23 in the formula (II) are each independently an alkyl group, or the groups R22 and R23 together may form a divalent organic group. The alkyl group is preferably a methyl group or an ethyl group.
A quaternary ammonium salt group may be present as the cationic group in the monomer (b). In other words, R22R23 and R24 in the formula (III) are each independently an alkyl group; or otherwise, R22 and R23 together may form a divalent organic group, and R24 may be an alkyl group. The alkyl group is preferably a methyl group or an ethyl group.
The divalent organic group which is formed by R22 and R23 in the formula (II) or (III) is preferably a polymethylene group having at least 2 carbon atoms, a group formed by substituting at least one hydrogen atom of said polymethylene group, or a group formed by inserting an ether-like oxygen atom into the carbon-carbon bond of the polymethylene group. The substituent for the hydrogen atom of the polymethylene group is preferably an alkyl group such as a methyl group, ethyl group or n-propyl group. The groups R22 and R23 may form a morpholino group, piperidino group or 1-pyrrolidinyl group, together with the nitrogen atom bonded to both of them.
The group X− is a counter ion (an anionic group). The group X is a halogen atom or a residue remaining after one cationic hydrogen atom is allowed to leave from an acid (an inorganic acid or an organic acid). Example of the group X− include a chlorine ion (Cl−), bromine ion (Br−), iodine ion (I−), hydrogensulfate ion (HSO4−) and acetic acid ion (CH3COO−).
Examples of the nitrogen-containing monomer (b) include dimethylaminoethyl methacrylate, dimethylaminopropyl methacrylate, diethylaminoethyl methacrylate, diethylaminopropyl methacrylate, N-tert.-butylaminoethyl methacrylate, dimethylaminoethyl acrylate, dimethylaminopropyl acrylate, diethylaminoethyl acrylate, diethylaminopropyl acrylate, and N-tert-butylaminoethyl acrylate.
One or at least two repeating units derived from the nitrogen-containing monomer (b) may be contained in the copolymer. When the copolymer comprises at least two repeating units, the repeating units preferably contain alkyl moieties or counter ions which are different. The presence of the nitrogen-containing monomer (b) can give paper treated with the processing agent the high resistance to water and oil after dried at a relatively low temperature for relatively short time, and also, can improve the stability of the processing agent itself.
Examples of the repeating unit having no cationic group, derived from the nitrogen-containing monomer (b), include the followings:
Examples of the repeating unit having a cationic group, derived from the nitrogen-containing monomer (b), include the followings:
The pyrrolidone monomer (c) is a compound which has a pyrrolidone group and one carbon-carbon double bond. In the formula (IV), R31R32, R33 and R34 are each preferably a hydrogen atom or a methyl group. Examples of the pyrrolidone monomer (c) include N-vinyl-2-pyrrolidone, N-vinyl-3-methyl-2-pyrrolidone, N-vinyl-4-methyl-2-pyrrolidone, N-vinyl-5-methyl-2-pyrrolidone and N-vinyl-3,3-dimethyl-2-pyrrolidone.
The monomer (d) having an anionic functional group is a compound having an anionic functional group and one carbon-carbon double bond. Examples of the anionic functional group include —C(═O)OH, —SO3H, and —SO3Na. Examples of the monomer (d) include an acrylic acid, methacrylic acid, sodium styrene sulfonate, itaconic acid and fumaric acid.
The copolymer of the present invention may comprise other monomer (e) in addition to the monomers (a), (b), (c) and (d). Examples of the other monomer (e) include the followings: ethylene, vinyl acetate, vinyl chloride, vinyl fluoride, vinylstyrene halide, α-methylstyrene, p-methylstyrene, polyoxyalkylene mono(meth)acrylate, (meth)acrylamide, diacetone (meth)acrylamide, methylol(meth)acrylamide, N-methylol(meth)acrylamide, alkyl vinyl ether, alkyl vinyl ether halide, alkyl vinyl ketone, butadiene, isoprene, chloroprene, glycidyl(meth)acrylate, 2-hydroxyethyl(meth)acrylate, aziridinyl(meth)acrylate, benzyl(meth)acrylate, isocyanate ethyl(meth)acrylate, cyclohexyl(meth)acrylate, short chain alkyl(meth)acrylate, maleic anhydride, (meth)acrylate having a polydimethylsiloxane group, and N-vinylcarbazole.
The amounts of the monomers may be as follows, based on the weight of the copolymer:
The copolymer of the present invention can be prepared by polymerizing the monomers (a), (b), (c) and (d), and if needed, the monomer (e), in a liquid medium. The liquid medium is preferably a water-soluble organic solvent, or may be a mixture containing a water-soluble organic solvent. The monomers and the liquid medium are preferably in the form of a solution of the monomers dissolved in the liquid medium. Preferably, the polymerization of the monomers is carried out in the manner of solution polymerization.
According to the present invention, the repeating unit derived from the monomer (b) may be neutralized by adding an aqueous solution of an inorganic or organic acid after the completion of the copolymerization; or the copolymerization may be carried out by using the nitrogen-containing monomer (a) which has been previously neutralized with an organic acid. When the monomers are polymerized after the nitrogen-containing monomer of the formula (II) has been beforehand neutralized with an acid, the neutralization with an aqueous solution of an organic acid is not needed.
If needed, the polymer mixture resulting from the copolymerization may be admixed with a liquid medium (such as water or an aqueous solution of an inorganic or organic acid) to dilute the mixture.
Examples of the water-soluble organic solvent, i.e., the liquid medium for use in the copolymerization, include, but not limited to, ketones (e.g., acetone and methyl ethyl ketone), alcohols (e.g., methanol, ethanol and isopropanol), ethers (e.g., methyl or ethyl ether of ethylene glycol or propylene glycol and acetate ester thereof, tetrahydrofuran, and dioxane), acetonitrile, dimethylformamide, N-methyl-2-pyrrolidone, butyrolactone, and dimethyl sulfoxide. Among those, N-methyl-2-pyrrolidone (NMP) or a mixture of N-methyl-2-pyrrolidone and acetone is preferably used as the solvent. The concentration of all the monomers in the solution may be 20 to 70% by weight, preferably 40 to 60% by weight.
The copolymerization may be conducted by using 0.1 to 2.0%, based on the weight of all the monomers, of at least one initiator. As the initiator, there may be used a peroxide such as benzoyl peroxide, lauroyl peroxide, succinyl peroxide or tert-butyl perpivalate; or an azo compound such as 2,2-azobisisobutylonitrile, 4,4-azobis(4-cyanopentanoic acid) or azodicarbonamide.
The copolymerization can be carried out at a temperature between 40° C. and the boiling point of the reaction mixture.
In the diluting step, a liquid medium such as water or an aqueous solution of an inorganic or organic acid having a high or medium acidity is added to the organic solvent solution of the copolymer. Examples of such an acid include hydrochloric acid, hydrobromic acid, sulfuric acid, nitric acid, phosphoric acid, acetic acid, formic acid, propionic acid and lactic acid, among which acetic acid is preferably used. It is preferable to use a sufficient amount of the aqueous solution and a sufficient concentration of the acid in the aqueous solution, enough to completely neutralize the amine functional group of the monomer of the formula (II), and to allow the final copolymer liquid to have a solid content of 5 to 30% by weight, preferably 20 to 30% by weight.
To completely convert the amine functional group the a salt, the amount of the acid is advantageously 1 to 5 acid equivalent, preferably 2 to 3 acid equivalent, based on the nitrogen-containing monomer (b).
Hydrogen peroxide (for example, an aqueous solution of hydrogen peroxide) may be added after the completion of the copolymerization. The amount of hydrogen peroxide to be used is 0.1 to 10% by weight, preferably 0.3 to 3% by weight, based on the total weight of the monomers. The treatment by reacting hydrogen peroxide is carried out at a temperature of 25 to 100° C., preferably 70 to 85°.
A treatment agent comprising the copolymer as an active ingredient can be used to treat a substrate, particularly paper.
Paper to be treated is paper produced by a known papermaking method. The treatment agent may be internally added to pulp slurry before the papermaking (an internal addition process), or may be externally applied to paper produced by the papermaking (an external addition process).
When the paper treatment agent is applied to the surface of paper, it is preferable to use the paper treatment agent in such an amount that the ratio of fluorine atoms in the treatment agent can be 0.02 to 5% by weight, particularly 0.05 to 0.2% by weight based on the weight of the paper. When the paper treatment agent is applied to a whole of paper including the internal part thereof, it is preferable to use the paper treatment agent in such an amount that the ratio of fluorine atoms in the treatment agent can be 0.05 to 1.0% by weight, particularly 0.2 to 0.4% by weight based on the weight of pulp.
The substrate thus treated is simply dried at a room temperature or a high temperature, and then, is optionally treated by heating at a temperature of at most 200° C., depending on the nature of the substrate. The substrate treated as above shows high lipophobic and hydrophobic properties.
Substrates to be treated in the present invention include base paper for gypsum board, coating base paper, medium grade paper, ordinary liner and core, pure white neutral roll paper, neutral liner, rust-preventive liner, metal composite paper and kraft paper. Examples of the substrate also include neutral printing or writing paper, neutral coating base paper, neutral PPC paper, neutral thermosensible paper, neutral pressure-sensitive paper, neutral ink jet paper, and neutral communication paper. Further, molded paper shaped by using a mold, particularly a molded container are included in the examples of the substrate. A pulp-molded container can be made by the method described in, for example, JP-A-9-183429.
As a pulp raw material for use in forming paper, there may be used any of bleached pulp or non-bleached chemical pulp such as kraft pulp or sulfite pulp, bleached or non-bleached high yield pulp such as chip pulp, mechanical pulp or thermomechanical pulp, and waste paper pulp of news paper, journals, corrugated board and ink-removed paper. Also, a mixture of the above pulp raw material with synthetic fibers such as asbestos, polyamide, polyimide, polyester, polyolefin or polyvinyl alcohol may be used.
The water resistance of paper can be improved by adding a sizing agent to the paper. Examples of the sizing agent are a cationic sizing agent, anionic sizing agent, and rosin-based sizing agent (e.g., acidic rosin-based sizing agent, or neutral rosin-based sizing agent). A styrene-acrylic acid copolymer and an alkylketene dimer are preferred. The amount of the sizing agent may be 0.01 to 5% by weight based on the weight of the pulp.
If needed, the paper may contain additives conventionally used in papermaking, for example, a paper strength-enhancing agent such as starch, modified starch, carboxylmethyl cellulose or polyamide-polyamine-epichlorohydrin resin, a yield-improving agent, a dye, a fluorescent dye, a slime-controlling agent, and a defoaming agent.
If needed, a size press, gate roll coater, bill blade coater, calender or the like may be used to apply the chemicals (e.g., starch, polyvinyl alcohol, dye, coating color, or slide-preventive agent) to paper.
Hereinafter, the present invention will be described in more detail by way of Examples which are illustrative only, and should not be construed as limiting the scope of the present invention in any way. Throughout Examples, “parts” and “%” are “parts by weight” and “% by weight”, unless otherwise specified.
The testing methods used are as follows.
Viscosity
The viscosity of a solution was measured with a rotary viscometer while the temperature of a liquid was controlled at 25° C.
Oil Resistance
The oil resistance of paper was measured according to the procedure of TAPPI UM-557. One drop of each of test oils indicated in Table 1 was placed on paper, and the penetration of the oil into the paper was observed 15 seconds later. The maximum of the oil resistance degrees of a test oil which did not penetrate paper was taken as oil resistance.
Degree of Size
Degree of size was measured according to the procedure of JIS P-8122.
A piece of paper having a size of 50 mm×50 mm, to be measured, was cut out of a sheet of paper. The paper piece was placed on a level surface, and folded along the lines each about 1 cm inside from the four sides of the paper piece so that the four sides could be directed upward. This folded paper piece was further folded near its four corners so that a paper box opened at the upper side could be shaped by folding along each line which connected each of the four corners to an intersection of the lines which were about 1 cm inside from two sides intersecting near each of the four corners. This paper box was floated on a 2% aqueous ammonium rhodanate solution having a temperature of 20±1° C. put in a Petridish, and simultaneously, one drop of a 1% cupper (II) chloride solution having the same temperature was fallen onto the paper box from a pipet. Then, time (seconds) required until three red spots appeared was measured, and the number of seconds was taken defined as the degree of size.
Resistance to Hot Oil and Resistance to Hot Brine
The resistance to hot oil or hot brine was measured according to the following method based on the inspection items of the China's Rail Ministry. Salad oil heated at 80° C. or brine heated at 80° C. (concentration: 10% by weight) was poured into a pulp-molded container, and was maintained at 80° C. for 30 minutes. Thirty minutes later, the degree of the salad oil or brine oozing from the container was estimated based on the following criteria:
A: No oozing or leaking was observed.
A′: A little oozing was observed.
B: Oozing was observed, but no leaking was observed.
C: Leaking from the container was observed.
To a reaction vessel having a volume of 500 parts, which was equipped with a stirrer, thermometer, reflux condenser, dropping funnel, nitrogen inlet and heater, were added N-methyl-2-pyrrolidone (NMP) (90 parts), dimethylaminoethyl methacrylate (13 parts), acetic acid (11 parts), N-vinyl-2-pyrrolidone (10 parts), acrylic acid (3 parts), fluorine-containing acrylate (80 parts) of the formula:
(a mixture of the compounds having the notations n of 5, 7, 9, 11 and 13 in the weight ratio of 1/63/25/9/2), and 4,4′-azobis(4-cyanopentanoic acid) (1 part).
This mixture was heated under a nitrogen atmosphere at 85° C. for 6 hours, and then, an aqueous solution containing water (195 parts) and hydrogen peroxide (35% by weight) (1.4 parts) was added dropwise at 70° C. over 20 minutes. Then, the reaction mixture was cooled to a room temperature. Thus, a transparent and amber-colored solution (S1) (400 parts) was obtained. The concentration of the solid content in this solution was 25%.
The same operation as in Synthesis Example 1 was repeated, except that dimethylaminoethyl methacrylate (13 parts) used in Synthesis Example 1 was changed to N-tert-butylaminoethyl methacrylate (13 parts). As a result, a transparent and amber-colored solution (S2) (400 parts) was obtained. The concentration of the solid content in this solution was 25%.
To a reaction vessel having a volume of 500 parts, which was equipped with a stirrer, thermometer, reflux condenser, dropping funnel, nitrogen inlet and heater, were added NMP (90 parts), dimethylaminoethyl methacrylate (15 parts), acetic acid (11 parts), N-vinyl-2-pyrrolidone (6 parts), methacrylic acid (2 parts), fluorine-containing acrylate (80 parts) of the formula:
(a mixture of the compounds having the notations n of 7 and 9 in the weight ratio of 85/15), and 4,4′-azobis(4-cyanopentanoic acid) (0.8 parts).
This mixture was heated under a nitrogen atmosphere at 75° C. for 3 hours, and then, 4,4′-azobis(4-cyanopentanoic acid) (0.4 parts) was added to further continue the reaction for 3 hours. Next, an aqueous solution containing water (195 parts) and hydrogen peroxide (35% by weight) (1.4 parts) was added dropwise at 70° C. over 20 minutes. Then, this reaction mixture was cooled to a room temperature. Thus, a transparent and amber-colored solution (S3) (400 parts) was obtained. The concentration of the solid content in this solution was 24.5%.
The same operation as in Synthesis Example 2 was repeated, except that acrylic acid (3 parts) was changed to sodium styrene sulfonate (1 part). As a result, a transparent and amber-colored solution (S4) (395 parts) was obtained. The concentration of the solid content in this solution was 25.7%.
To a reaction vessel having a volume of 500 parts, which was equipped with a stirrer, thermometer, reflux condenser, dropping funnel, nitrogen inlet and heater were added NMP (90 parts), quaternary product of dimethylaminoethyl methacrylate (15 parts) of the formula:
, N-vinyl-2-pyrrolidone (10 parts), methacrylic acid (2 parts), and the same fluorine-containing acrylate (80 parts) as used in Synthesis Example 1 (the mixture of the compounds having the notations n of 5, 7, 9, 11 and 13 in the weight ratio of 1/63/25/9/2).
This mixture was heated under a nitrogen atmosphere of 85° C. for 3 hours, and then, 4,4′-azobis(4-cyanopentanoic acid) (0.4 parts) was added to further continue the reaction for 3 hours. Next, an aqueous solution containing water (145 parts) and acetic acid (12 parts) was added dropwise at 70° C. over 20 minutes. Then, an aqueous solution containing water (50 parts) and hydrogen peroxide (35% by weight) (1.4 parts) was added dropwise at 70° C. over 20 minutes, and the mixture was stirred for 40 minutes. Then, the reaction mixture was cooled to a room temperature. Thus, a transparent and amber-colored solution (S5) (400 parts) was obtained. The concentration of the solid content in this solution was 24.5%.
To a reaction vessel having a volume of 500 parts, which was equipped with a stirrer, thermometer, reflux condenser, dropping funnel, nitrogen inlet and heater, were added NMP (90 parts), dimethylaminoethyl methacrylate (15 parts), acetic acid (11 parts), N-vinyl-2-pyrrolidone (6 parts), methacrylic acid (2 parts), fluorine-containing acrylate (80 parts) of the formula:
and 4,4′-azobis(4-cyanopentanoic acid) (0.8 parts).
This mixture was heated under a nitrogen atmosphere of 75° C. for 3 hours, and then, 4,4′-azobis(4-cyanopentanoic acid) (0.4 parts) was added to further continue the reaction for 3 hours. Next, an aqueous solution containing water (195 parts) and hydrogen peroxide (35% by weight) (1.4 parts) was added dropwise at 70° C. over 20 minutes. Then, the reaction mixture was cooled to a room temperature. Thus, a transparent and amber-colored solution (S6) (400 parts) was obtained. The concentration of the solid content in this solution was 24.5%.
The same operation as in Synthesis Example 1 was repeated, except that acrylic acid (3 parts) used in Synthesis Example 1 was changed to N-vinyl-2-pyrrolidone (3 parts). The concentration of the solid content in the resultant solution (T1) was 24.0%.
The same operation as in Synthesis Example 3 was repeated, except that methacrylic acid (2 parts) used in Synthesis Example 3 was changed to N-vinyl-2-pyrrolidone (2 parts). The concentration of the solid content in the resultant solution (T2) was 24.0%.
To a reaction vessel having a volume of 1,000 parts, which was equipped with a stirrer, thermometer, reflux condenser, dropping funnel, nitrogen inlet and heater, were added pure water (383 parts), acetone (140 parts), trimethyloleyl ammonium hydrochloride (3.75 parts), polyoxyethylene alkylphenol having HLB of 15 (3.43 parts), methoxyethyl acrylate (43.2 parts), N-methylolacrylamide (12 parts), 75% aqueous solution (12.8 parts) of a monomer of the formula:
and fluorine-containing acrylate (176.9 parts) of the formula:
To a reaction vessel having a volume of 600 parts, which was equipped with a stirrer, thermometer, reflux condenser, dropping funnel, nitrogen inlet and heater, were added methyl isobutyl ketone (40 parts), MEK (2 parts), acetone (27 parts), dimethylaminoethyl methacrylate (16 parts), vinyl acetate (8.8 parts), methacrylic acid (1.2 parts), and fluorine-containing acrylate (81.4 parts) of the formula:
(a mixture of the compounds having the notations n of 5, 7, 9, 11 and 13 in the average weight ratio of 1/63/24/9/3). This mixture was subjected to a nitrogen substitution, and then heated to 70° C. Then, a solution of 4,4′-azobis(4-cyanopentanoic acid) (0.4 parts) in water (8 parts) was added to continue the reaction for 4 hours. Next, an aqueous solution containing water (290 parts), acetic acid (8 parts) and 35% hydrogen peroxide (2.5 parts) was added dropwise at 70° C. over 20 minutes. This mixture was stirred at 70° C. under a stream of nitrogen for 40 minutes. Then, the resulting solution was distilled under reduced pressure to obtain a solution (T4) having a solid content of 25%.
The viscosities of the solutions obtained in Synthesis Examples 1 to 5 and Comparative Synthesis Examples 1 and 2 are shown in Table 2.
A styrene-acrylic acid copolymer-based sizing agent having a solid content of 1% (AS-233 manufactured by Nippon PMC) (8 g) was added in portions to a 1% aqueous dispersion (1,000 g) of bleached kraft pulp of broad-leaved trees under stirring. The stirring was continued for 2 minutes, and the solution S1 (2.4 g) of Synthesis Example 1, diluted until the solid content reached 1%, was added in portions, and the mixture was stirred for 2 minutes. The resultant pulp slurry was molded into a round tray having a level base, with a pulp-molding machine. The molded tray was dried at 180° C. for 30 minutes. The resultant paper tray had a diameter of 16 cm, a depth of 3 cm and a thickness of 0.6 mm. This paper tray was evaluated in oil resistance and resistance to hot oil and hot brine. The results are shown in Table 3.
The operation of Example 1 was repeated in the same manner, except that a polyamide-polyamine-epichlorohydrin reaction product having a solid content of 1% (WS-570 manufactured by Nippon PMC) (4 g) was firstly added in portions to pulp slurry in the step of Example 1, so as to enhance the strength of the resultant paper tray. This paper tray was evaluated in oil resistance and resistance to hot oil and hot brine. The results are shown in Table 3.
The operation of Example 2 was repeated in the same manner, except that the solution T1 was used instead of the solution S1 of Example 2. The resultant paper tray was evaluated in oil resistance and resistance to hot oil and hot brine. The results are shown in Table 3.
The same operation as in Example 1 (using no WS-570) or Example 2 (using WS-570) was repeated to obtain a paper tray in each of Examples 3 to 10, except that the solution, shown in Table 4, having the same solid content, was used. The results of oil resistance and resistance to hot oil and hot brine are shown in Table 4.
The same operation as in Example 2 was repeated in each of Comparative Examples 2 to 4, except that the solution T2 (Comparative Example 2), the solution T3 (Comparative Example 3) or the solution T4 (Comparative Example 4) was used instead of the solution S1 of Example 2. The resultant paper trays were evaluated in oil resistance and resistance to hot oil and hot brine. The results are 5 shown in Table 4.
The solution S1 (1.2 g) having a solid content of 1%, prepared in Synthesis Example 3, was added in portions to a 1% aqueous dispersion (500 g) of bleached kraft pulp of broad-leaved trees under stirring. The stirring was continued for 2 minutes. The resultant pulp slurry was made into paper with a standard papermaking system described in JIS P8209. The resultant wet paper was sandwiched between filter paper sheets under a pressure of 3.5 kg/cm2 so as to sufficiently absorb the moisture of the paper. The paper was dried over a drum drier (100° C.×2 minutes) to obtain oil resistance paper having a basis weight of 80 g/cm2.
The oil resistance and the degree of size of this oil resistance paper were evaluated. The results are shown in Table 5.
A polyamide-polyamine-epichlorohydrin reaction product (WS-570 manufactured by Nippon PMC) (2 g) having a solid content of 1% was added in portions to a 1% aqueous dispersion (500 g) of bleached kraft pulp of broad-leaved trees under stirring. The stirring was continued for 2 minutes. Then, the solution S1 having a solid content of 1% (1.2 g), prepared in Synthesis Example 3, was added in portions, and the mixture was stirred for 2 minutes. The resultant pulp slurry was made into paper with a standard papermaking system described in JIS P8209. The resultant wet paper was sandwiched between filter paper sheets under a pressure of 3.5 kg/cm2 so as to sufficiently absorb the moisture of the paper. The paper was dried over a drum drier (100° C.×2 minutes) to obtain oil-resistant paper having a basis weight of 80 g/cm2. The oil resistance and the degree of size of this oil-resistant paper were evaluated. The results are shown in Table 5.
The operation of Example 11 was repeated, except that the solution S6 prepared in Synthesis Example 6 was used instead of the solution S1 of Example 11. The oil resistance and the degree of size of the resultant paper were evaluated. The results are shown in Table 5.
The operation of Example 12 was repeated, except that the solution S6 prepared in Synthesis Example 6 was used instead of the solution S1 of Example 12. The oil resistance and the degree of size of the resultant paper were evaluated. The results are shown in Table 5.
The operation of Example 11 was repeated, except that the solution T2 was used instead of the solution S1 of Example 11. The oil resistance and the degree of size of the resultant paper were evaluated. The results are shown in Table 5.
The operation of Example 12 was repeated, except that the solution T2 was used instead of the solution S1 of Example 12. The oil resistance and the degree of size of the resultant paper were evaluated. The results are shown in Table 5.
The operation of Example 11 was repeated, except that the solution T3 was used instead of the solution S1 of Example 11. The oil resistance and the degree of size of the resultant paper were evaluated. The results are shown in Table 5.
The operation of Example 12 was repeated, except that the solution T3 was used instead of the solution S1 of Example 12. The oil resistance and the degree of size of the resultant paper were evaluated. The results are shown in Table 5.
The operation of Example 11 was repeated, except that the solution T4 was used instead of the solution S1 of Example 11. The oil resistance and the degree of size of 10 the resultant paper were evaluated. The results are shown in Table 5.
The operation of Example 12 was repeated, except that 15 the solution T4 was used instead of the solution S1 of Example 12. The oil resistance and the degree of size of the resultant paper were evaluated. The results are shown in Table 5.
The treatment agents of the present invention impart sufficient water resistance and oil resistance to paper, even when sizing agents and paper strength-enhancing agents are present.
| Number | Date | Country | Kind |
|---|---|---|---|
| 200-173040 | Jun 2002 | JP | national |
| Filing Document | Filing Date | Country | Kind | 371c Date |
|---|---|---|---|---|
| PCT/JP03/07464 | 6/12/2003 | WO | 12/2/2004 |
