WO1995011341A1

WO1995011341A1 - Improved polymer solution for sizing paper

Info

Publication number: WO1995011341A1
Application number: PCT/US1994/011531
Authority: WO
Inventors: Kang In Lee
Original assignee: Monsanto Company
Priority date: 1993-10-18
Filing date: 1994-10-12
Publication date: 1995-04-27

Abstract

Paper surface sizing properties of aqueous solutions of high molecular weight (at least 100,000 Daltons weight average) styrene-maleate half ester polymers are improved by forming the maleate half ester using oxyalkylene-alkyl alcohol, preferably 2-(n-butoxy) ethyl alcohol.

Description

IMPROVED POLYMER SOLUTION FOR SIZING PAPER BACKGROUND OF THE INVENTION This invention relates to paper sizing formulations and more particularly to aqueous alkaline solutions of polymers of styrene and maleate half esters for such applications. Alkaline salt solutions of high molecular weight styrene-maleic half ester copolymers for sizing paper are known. See, for example US. 5,237,024, issued August 17, 1993 where C-_ - C₁₈ alcohols are used in forming the aleic half ester. Ease of synthesis of these polymers without loss of sizing properties is of continuing interest in the paper sizing art.

SUMMARY OF THE INVENTION Now improvements have been made in further enhancing the properties of paper sizing formulations.

Accordingly, a principal object of this invention is to provide an improved aqueous alkaline paper sizing solution of styrene-maleate half ester polymers.

Other objects will in part be obvious and will in part appear from the following detailed description and claims.

These and other objects are accomplished by providing an aqueous solution of polymer for sizing paper wherein the polymer has a weight average molecular weight of at least 100,000 Daltons, preferably 150,000 to 250,000 Daltons, and comprising the following recurring units of formula: CH,

CH

<^

M∞O C - CH B

CH₃-[(CH₂)_n-0]_m-(CH₂)₀- O - C - CH

CH,

R - 0 - C - C - R^J

in proportions such that the weight fractions of units A, B, C and D are respectively: 0.45 to 0.83; 0.15 to 0.35; 0.10 to 0.45; and 0 to 0.20; and wherein n, m and o are integers within the following ranges: n = 1 to 10; m = 1 to 10 and o = 1 to 4; R is C_j to C₃ alkyl; R¹ is H or C_λ to C₃ alkyl and M is K, Na or NH₄.

DETAILED DESCRIPTION The maleic anhydride partial ester component of the polymers of the solutions of the invention is prepared by partially esterifying maleic anhydride and an oxyalkylene-alkyl alcohol of the formula:

O

CH₃-[(CH₂)_n-0]_m-(CH₂)_o- 0 - C II - CIH In the above formula n and m are each from 1 to 10 and o from 1 to 4. Preferred ranges of m and n are 1 to 4 and of o, either 1 or 2. In the most preferred form of I, n=3, m=l and o=2, i.e. 2-(n- butoxy) ethyl alcohol. Oxygen atoms in the oxyalkylene, (i.e. (CH₂)_n-0) side chains of component C of the polymer enhance the flexibility of such side chains to preserve polymer solubility in the final solution while at the same time providing alkylene (CH₂) groups to promote hydrophobicity of the polymer which aids in helping keep water from the sizing solution and ink from smearing on the surface of the paper to which the formulation is applied. Though preferred (for ease of synthesis in minimizing reaction medium viscosity when using solution polymerization) to form the maleate half ester of the polymer using only the oxyalkylene- alkyl alcohols of formula I, mixtures of the latter with one or more primary or secondary C₁-C₁₈ alcohols can be used. Usable primary alcohols include methanol, ethanol, n-propanol, n-butanol, isobutanol, n-pentanol, n-hexanol, n-heptanol, n- octanol, n-decanol and higher alcohols up to n- octadecanol. Usable secondary alcohols include isopropanol, secondary-butanol etc. When alcoholic mixtures are used, the molar ratio of oxyalkylene- alkyl maleate to C_χ - C₁₈ maleate should be 0.5:1 to 4:1, preferably 1:1 to 2:1. Optionally includable with the styrene and maleate half ester components of the polymer is copolymerizable monomer of the formula: CH,

II

R - O - C - C

wherein R is C_χ to C₃ alkyl and R¹ is H or C₂ to C₃ alkyl. Representative compounds satisfying this formula include methyl methacrylate, ethyl methacrylate, methyl acrylate, ethyl acrylate, methyl maleate, ethyl maleate, propyl maleate and butyl maleate. Inclusion of such copolymerized monomer can further improve the sizing properties of the solutions of the invention. The weight fractions (i.e. weight of the constituents in the polymer per 100 parts of polymer) of the polymerized monomers are 40 to 70 (preferably 50 to 60) styrene, 20 to 60 (preferably 30 to 40 maleic half ester) and 2 to 30 (preferably 5 to 15) acrylate or methacrylate component.

The polymers of styrene-oxyalkylene-alkyl maleate half ester are prepared by any conventional free radical process providing relatively high molecular weight polymers of at least a molecular weight of 100,000 (weight average) determined by size exclusion chromatography using tetrahydrofuran as solvent and low angle laser light scattering with a Waters Model 401 Differential Refractive Index Detector instrument. Preferably, the polymers are prepared by in situ esterification of maleic anhydride with oxyalkylene-alkyl alcohol followed by solution polymerization of the mixture with styrene at a temperature in the range of 70 to 150"C using peroxide or hydroperoxide initiators or mixtures thereof, such as t-butyl peroctoate, benzyl peroxide, t-butyl hydroperoxide, t-butyl peroxide, cumene hydroperoxide and cumene peroxide or azo-dinitriles such as azo-di(isobutyronitrile) and azo-di cyclohexanecarbonitrile.

The polymeric salt is formed by mixing the polymer in aqueous alkaline solution, preferably without the presence of additional components. In doing so, the acid component reacts with the alkaline metal or ammonium of the polymer providing an ester group attached to one C atom and an alkali metal or ammonium cation associated with a carboxylic group. The concentration of polymer salt in solution is 5 to 20 weight percent.

Exemplary of the invention are the following specific examples.

EXAMPLE 1 A) Preparation of Aqueous Ammonium Salt

Solution of a Copoly er of Styrene and Mono-2-(n- Butoxy)Ethyl Maleate

Maleic anhydride (85.05 gm, 0.87 mole) and 2-butoxyethanol (102.82 gm, 0.87 mole) were charged to a kettle. The reaction mixture is heated to

140°C and a 30 to 40"C exotherm allowed to occur. The solution was then cooled to 140"C and maintained at 140°C for one additional hour. At the end of this esterification step forming the mono-2-(n-butoxy)ethyl ester of maleic anhydride, the solution was cooled to room temperature. In a separate kettle, styrene monomer (29.50 gm, 0.28 mole) and xylene (118.40 gm) were added to the 50.50 gm of the maleic anhydride half ester solution. A solution of tert-butyl peroctoate

(1.60 gm) catalyst in xylene(3 ml) was added to the kettle through an addition funnel in three separate 1 ml slugs at 0, 1 and 2 hours of the reaction time, while the reaction temperature was maintained at 95'C. After complete addition of catalyst, the polymerization mixture was heated at the refluxing 140°C for an additional one hour. After the reaction mixture was cooled, polymer conversion analyses was determined from an aliquot sample both gravimetrically and by gas chromatograph (GC) .

Conversion was 100% gravimetrically and 99.99% by residual styrene analysis with GC from an aliquot of polymer solution. From such aliquot, the polymer was dissolved in ethylacetate and was precipitated in hexane and the solid polymer filtered and dried. Molecular weight (weight average) was 150,000 by size exclusion chromatography using polystyrene as standard. The infrared spectrum of the polymer exhibited the ester carbonyl band at 1735 cm^-1, the acid carbonyl band at 1710 cm^"1 and styrene band at 700 cm^-1.

The agitated kettle containing the above polymer solution was fitted with a distillation apparatus was charged concentrated 30% ammonium hydroxide (10.65 gm) and 85°C tap water (425.6 gm) was charged over a 10 min period. Since xylene is essentially immiscible in water, after agitation was stopped a two layer mixture was formed of the solvent and water solution. The xylene layer was decanted off and the residual xylene was further removed from the water solution layer by distillation at 100^βC. The resulting aqueous ammonium salt solution was cooled to 25"C and pH adjusted to 9.2. The solution was water clear to the eye and had a Brookfield viscosity of 30 cps (0.03 Pa.s). Residual xylene in the solution was less than 0.01 wt. % by gas chromatography.

B) Preparation of the Aqueous Ammonium Salt Solution of the Styrene-Mono-2-(n-butoxy)ethyl Maleate-Methyl Methacrylate Copolvmer Maleic anhydride (45.1 gm, 0.46 mole), styrene (145.6 gm, 1.4 mole) and methyl methacrylate (14 gm, 0.14 mole) were charged to an agitated kettle and heated to 60^βC to ensure melting of all the maleic anhydride. Tert-butyl peroctoate (2 gm) and methyl ethyl ketone (500 ml) were added and the mixture heated to 105^βC under a nitrogen atmosphere. Polymerization was evident by an increase in viscosity of the reaction mixture. After 5 hrs the batch was cooled to room temperature. The viscous syrupy solution was coagulated in a large quantity of hexane. The polymer was precipitated and dried in a vacuum over night. Analysis showed styrene/maleic anhydride/methyl methacrylate weight ratios of 0.71/0.22/0.07 by integrating peaks of the NMR spectrum.

The above prepared styrene-maleic anhydride- methyl methacrylate terpolymer (120 gm) , 2- butoxyethanol (8.66 gm) and water (800 gm) were charged to a kettle and heated to the refluxing temperature for 3 hours. After cooling to 80°C, thirty percent aqueous ammonium hydroxide (54 gm) was added through an addition funnel over 2 hours to form a homogeneous translucent solution. When the solution temperature reached room temperature, the pH was adjusted to 9.5 with thirty percent aqueous ammonium hydroxide. The infrared spectrum of the isolated solid shows an ester carbonyl stretching band at 1735 cm^-1, carboxylic salt carbonyl stretching band at 1450 cm^-1, and the ether band at 1100 cm^-1. EXAMPLE 2 Evaluation of Amide-Ammonium Polymeric Salt Solutions As Paper Surface Sizing Agent

A) Hercules Sizing Test - Ten gm of corn starch in 100 gm of water were heated at 90°C for 30 minutes. To aid miscibility the starch solution was diluted with an additional 100 gm of water. Then the pH of the solution was adjusted with caustic soda to 8. 10 gms of the ester/ammonium salt of the polymer of Examples 1A and IB above as a 10% solids concentration in water were mixed with the starch solution to prepare the surface sizing formulations. The surface sizing solution was held in a 55°C water bath until used in the size press. The press used was a horizontal size press which is a two roll metering device which applied the surface sizing solution to paper sheet as the latter passes downwardly through a nip defined between a sheet contact surface of a first roll and a sheet contact surface of a second roll. The rolls turn in opposite direction in the horizontal plane. The above-prepared surface sizing solutions were applied to the paper stock (alkaline paper containing 12% precipitate calcium carbonate, 0.5 % alum and 0.03% alkyl ketene dimer) through the horizontal size press at 90^βC. The amount of sizing solution taken up by the paper was 0.09 gm per square meter. The paper was redried after application of the alkaline sizing solution. The sized paper was tested for ink penetration using a Hercules sizing test apparatus. In this test (conducted at 23 ° C) , the change is noted in light reflection from the surface of one side of the sized paper sample as ink or a colored solution of naphthol green dye (to simulate ink) is allowed to penetrate from the other side. The naphthol green dye is confined within a ring on the tope side of a section of sized paper and the change in light reflectance from the bottom side is measured photoelectrically. An end point of 80% reduction in reflected light is chosen. The reflectance measuring system includes a timer measuring seconds which stops automatically when the reflected light falls below 80%. The time in seconds which has passed from the start of the test until the point at which reduction in reflected light is 80% is recorded. The higher the number of recorded seconds, the better is the performance of the sizing agent in the test. Six samples are tested and the result is the average thereof. In the present Example, such elapsed time was 105 sec. for polymer 1A and 110 sec. for polymer IB. B) Contact Angle Measurement Test This measures the hydrophobicity of the sizing agent. Samples for analysis were prepared by spin-coating the polymer solution onto a clean glass slide using a Headway spinner. Then the samples were dried in air at 23°C and 45 + 5% relative humidity. Then the samples were checked under an optical microscope for microcracks and those showing signs of cracks were redone at a slower rpm. Static contact angle measurements were made using a Rame-Hart Goniometer. The contact liquid used to study the time dependence of contact angle was de-ionized water. Small drops of the liquid (approximately 4.0 mm in diameter) were placed on the prepared sample using a microsyringe and the initial contact angle immediately noted. Time dependent measurements of the contact angles were performed in the range of 0.5 to 10 min thereafter. The higher the contact angle, the better is considered the performance, or considered alternatively, the slower the rate of decrease in contact angle the better is considered the sizing efficiency. Results obtained were as follows:

Time (Min.) Polymer 1A Polymer IB

Contact Angle Contact Angle

(deg •) (deg .)

0 68 71

0.5 68 71

1.0 66 71

2.0 66 70

3.0 64 68

4.0 62 66

5.0 62 65

6.0 59 64

7.0 59 63

8.0 58 63

9.0 58 63

10.0 58 63

From the above data, the rate of decrease of contact angle with time shows the superior hydrophobic character of the formulations of the Example, which in turn results in desirable sizing properties. EXAMPLE Cl

This control example, not according to the invention, evaluates performance in the tests described above of solutions containing the ammonium salt of styrene/maleic anhydride/methyl methacrylate terpolymer as disclosed in copending

US application SN-07/972,338 filed November 6, 1992 and assigned to the assignee of the present invention.

A terpolymer of styrene, maleic anhydride and methyl methacrylate was prepared as disclosed in Example 1, page 4 of the subject application as was the amide/ammonium salt solution of such terpolymer, as disclosed on page 5 of said application, the content of which is incorporated herein by reference.

Results of the Hercules Sizing Test with this formulation was 80 sec. Contact Angle Measurement Test results were:

Time (min.) Contact Angle (deg.)

0 49

0. ,5 48

1. ,0 47

2. .0 42

33.. .00 38

4. ,0 33

5. ,0 32

6. .0 30

7. .0 28

88.. .00 26

9. .0 25

10. .0 25

The rate of decrease of the contact angle with time is undesirably much faster than that of invention Examples 1A and IB.

The preceding description is for illustration only and is not to be taken in a limited sense. Various modifications and alterations will be readily suggested to persons skilled in the art. It is intended, therefore, that the foregoing be considered as exemplary only and that the scope of the invention be ascertained from the following claims.

Claims

I CLAIM

1. An aqueous solution of polymer for sizing paper, said polymer having a weight average molecular weight of at least 100,000 Daltons and comprising the following recurring units of formula:

CH,

<__ CH

0 M∞O - C - CH B

I

0 CH₃-[(CH₂)_n-0]_m-(CH₂)_o- O - C II - CIH C

in proportions such that the weight fractions of units A, B, C and D are respectively: 0.45 to

0.83; 0.15 to 0.35; 0.10 to 0.45; and 0 to 0.20; and wherein n, m and o are integers within the following ranges: n = 1 to 10; m = 1 to 10 and o =

1 to 4; R is C_j to C₃ alkyl; R¹ is H or C_x to C₃ alkyl and M is K, Na or NH .

2. The aqueous solution of claim 1 wherein

M is NH₄.

3. The aqueous solution of claim 1 wherein n = l to 4; m = l to 4 and o = 1 or 2.

4. The aqueous solution of claim 3 wherein n = 3, m = 1, and o = 2.

5. The aqueous solution of any of claims 1, 2 or 3 wherein the weight fractions of units A, B, C and D are respectively: 0.50 to 0.78; 0.20 to 0.30; 0.15 to 0.30; and 0.02 to 0.10.

6. The aqueous solution of claim 5 wherein the concentration of polymer in solution is 5 to 20 weight %.

7. The aqueous solution of claim 6 wherein the weight average molecular weight of the polymer in solution is between 150,000 to 250,000 Daltons.