WO2007011420A2

WO2007011420A2 - Composition for improving the retention and drainage in the manufacture of paper

Info

Publication number: WO2007011420A2
Application number: PCT/US2005/046949
Authority: WO
Inventors: John C. Harrington; Robert A. Gelman; Frank J. Sutman
Original assignee: Hercules Incorporated
Priority date: 2004-12-29
Filing date: 2005-12-22
Publication date: 2007-01-25
Also published as: JP2008530377A; WO2007011420A3; KR20070103397A; CA2594338A1; US20060142432A1; EP1848771A2; TW200634208A; AU2005334474A1; BRPI0519673A2

Abstract

A method of improving retention and drainage in a papermaking process is disclosed. The method provides for the addition of an associative polymer, a polyelectrolyte and optionally a siliceous material to the papermaking slurry. Additionally, a composition comprising an associative polymer, and a polyelectrolyte and optionally further comprising cellulose fiber is disclosed.

Description

IMPROVED RETENTION AND DRAINAGE IN THE MANUFACTURE OF PAPER

CROSS REFERENCE TO RELATED APPLICATIONS

[0001] This application claims the benefit of U.S. Provisional Application No.

60/640,180, filed December 29, 2004 and U.S. Provisional Application No. 60/694,058, filed June 24, 2005, the entire contents of each are herein incorporated by reference.

FIELD OF THE INVENTION

[0002] This invention relates to the process of making paper and paperboard from a cellulosic stock, employing a flocculating system.

BACKGROUND

[0003] Retention and drainage is an important aspect of papermaking. It is known that certain materials can provide improved retention and/or drainage properties in the production of paper and paperboard.

[0004] The making of cellulosic fiber sheets, particularly paper and paperboard, includes the following: 1) producing an aqueous slurry of cellulosic fiber which may also contain inorganic mineral extenders or pigments; 2) depositing this slurry on a moving papermaking wire or fabric; and 3) forming a sheet from the solid components of the slurry by draining the water.

[0005] The foregoing is followed by pressing and drying the sheet to further remove water. Organic and inorganic chemicals are often added to the slurry prior to the sheet-forming step to make the papermaking method less costly, more rapid, and/or to attain specific properties in the final paper product.

[0006] The paper industry continuously strives to improve paper quality, increase productivity, and reduce manufacturing costs. Chemicals are often added to the fibrous slurry before it reaches the papermaking wire or fabric to improve drainage/dewatering and solids retention; these chemicals are called retention and/or drainage aids.

[0007] Drainage or dewatering of the fibrous slurry on the papermaking wire or fabric is often the limiting step in achieving faster paper machine speeds. Improved dewatering can also result in a drier sheet in the press and dryer sections, resulting in reduced energy consumption. In addition, as this is the stage in the papermaking method that determines many of the sheet final properties, the retention and/or drainage aid can impact performance attributes of the final paper sheet. [0008] With respect to solids, papermaking retention aids are used to increase the retention of fine furnish solids in the web during the turbulent method of draining and forming the paper web. Without adequate retention of the fine solids, they are either lost to the mill effluent or accumulate to high levels in the recirculating white water loop, potentially causing deposit buildup. Additionally, insufficient retention increases the papermakers' cost due to loss of additives intended to be adsorbed on the fiber. Additives can provide opacity, strength, sizing or other desirable properties to the paper.

[0009] High molecular weight (MW) water-soluble polymers with either cationic or anionic charge have traditionally been used as retention and drainage aids. Recent development of inorganic microparticles, when used as retention and drainage aids, in combination with high MW water-soluble polymers, have shown superior retention and drainage efficacy compared to conventional high MW water-soluble polymers. U.S. Patent Nos. 4,294,885 and 4,388,150 teach the use of starch polymers with colloidal silica. U.S. Patent Nos. 4,643,801 and 4,750,974 teach the use of a coacervate binder of cationic starch, colloidal silica, and anionic polymer. U.S. Patent No. 4,753,710 teaches flocculating the pulp furnish with a high MW cationic flocculant, inducing shear to the flocculated furnish, and then introducing bentonite clay to the furnish. [0010] The efficacy of the polymers or copolymers used will vary depending upon the type of monomers from which they are composed, the arrangement of the monomers in the polymer matrix, the molecular weight of the synthesized molecule, and the method of preparation. [0011] It had been found recently that water-soluble copolymers when prepared under certain conditions exhibit unique physical characteristics. These polymers are prepared without chemical cross linking agents. Additionally, the copolymers provide unanticipated activity in certain applications including papermaking applications such as retention and drainage aids. The anionic copolymers which exhibit the unique characteristics were disclosed in WO 03/050152 A1 , the entire content of which is herein incorporated by reference. The cationic and amphoteric copolymers which exhibit the unique characteristics were disclosed in U.S. serial number 10/728,145, the entire content of which is herein incorporated by reference.

[0012] The use of inorganic particles with linear copolymers of acrylamide, is known in the art. Recent patents teach the use of these inorganic particles with water- soluble anionic polymers (US 6,454,902) or specific crosslinked materials (US 6,454,902, US 6,524,439 and US 6,616,806).

[0013] However, there still exists a need to improve drainage and retention performance.

SUMMARY OF THE INVENTION

[0014] A method of improving retention and drainage in a papermaking process is disclosed. The method provides for the addition of an associative polymer and a synthetic polyelectrolyte to a papermaking slurry.

[0015] A method of improving retention and drainage in a papermaking process is disclosed. The method provides for the addition of an associative polymer and a cyclic organic material to a papermaking slurry.

[0016] Additionally, a composition comprising an associative polymer, a synthetic polyelectrolyte and optionally further comprising cellulose fiber is disclosed.

[0017] Additionally, a composition comprising an associative polymer, a synthetic polyelectrolyte, a siliceous material and optionally further comprising cellulose fiber is disclosed. DETAILED DESCRIPTION OF THE INVENTION

[0018] The present invention provides for a synergistic combination comprising a water soluble copolymer prepared under certain conditions (hereinafter referred to as "associative polymer") and at least one synthetic polyelectrolyte. It has surprising been found that this synergistic combination results in retention and drainage performance superior to that of the individual components. Synergistic effects occur when the combination of components are used together.

[0019] It has been found, unexpectedly, that the use of a synthetic polyelectrolyte in combination with associative polymers, such as the copolymers disclosed in WO 03/050152 A1 or US 2004/0143039 A1, results in enhanced retention and drainage.

[0020] The present invention also provides for a composition comprising an associative polymer and at least one synthetic polyelectrolyte.

[0021] The present invention also provides for a composition comprising an associative polymer, a synthetic polyelectrolyte and a siliceous material. [0022] The present invention also provides for a composition comprising an associative polymer and a synthetic polyelectrolyte and cellulose fiber. [0023] The present invention also provides for a composition comprising an associative polymer, a synthetic polyelectrolyte, a siliceous material and cellulose fiber.

[0024] The use of multi-component systems in the manufacture of paper and paperboard provides the opportunity to enhance performance by utilizing materials that have different effects on the process and/or product. Moreover, the combinations may provide properties unobtainable with the components individually. Synergistic effects occur in the multi component systems of the present invention. [0025] It is also observed that the use of the associative polymer as a retention and drainage aid has an impact on the performance of other additives in the papermaking system. Improved retention and/or drainage can have both a direct and indirect impact. A direct impact refers to the retention and drainage aid acting to retain the additive. An indirect impact refers to the efficacy of the retention and drainage aid to retain filler and fines onto which the additive is attached by either physical or chemical means. Thus, by increasing the amount of filler or fines retained in the sheet, the amount of additive retained is increased in a concomitant manner. The term filler refers to particulate materials, typically inorganic in nature, that are added to the cellulosic pulp slurry to provide certain attributes or be a lower cost substitute of a portion of the cellulose fiber. Their relatively small size, on the order of 0.2 to 10 microns, low aspect ratio and chemical nature results in their not being adsorbed onto the large fibers yet too small to be entrapped in the fiber network that is the paper sheet. The term "fines" refers to small cellulose fibers or fibrils, typically less than 0.2 mm in length and /or ability to pass through a 200 mesh screen. [0026] As the use level of the retention and drainage aid increases the amount of additive retained in the sheet increases. This can provide either an enhancement of the property, providing a sheet with increased performance attribute, or allows the papermaker to reduce the amount of additive added to the system, reducing the cost of the product. Moreover, the amount of these materials in the recirculating water, or Whitewater, used in the papermaking system is reduced. This reduced level of material, that under some conditions can be considered to be an undesirable contaminant, can provide a more efficient papermaking process or reduce the need for scavengers or other materials added to control the level of undesirable material. [0027] The term additive, as used herein, refers to materials added to the paper slurry to provide specific attributes to the paper and/or improve the efficiency of the papermaking process. These materials include, but are not limited to, sizing agents, wet strength resins, dry strength resins, starch and starch derivatives, dyes, contaminant control agents, antifoams, and biocides.

[0028] The associative polymer useful in the present invention can be described as follows:

[0029] A water-soluble copolymer composition comprising the formula:

wherein B is a nonionic polymer segment formed from the polymerization of one or more ethylenically unsaturated nonionic monomers; F is an anionic, cationic or a combination of anionic and cationic polymer segment(s) formed from polymerization of one or more ethylenically unsaturated anionic and/or cationic monomers; the molar % ratio of B: F is from 95:5 to 5:95; and the water-soluble copolymer is prepared via a water-in-oil emulsion polymerization technique that employs at least one emulsification surfactant consisting of at least one diblock or triblock polymeric surfactant wherein the ratio of the at least one diblock or triblock surfactant to monomer is at least about 3:100 and wherein; the water-in-oil emulsion polymerization technique comprises the steps of: (a) preparing an aqueous solution of monomers, (b) contacting the aqueous solution with a hydrocarbon liquid containing surfactant or surfactant mixture to form an inverse emulsion, (c) causing the monomer in the emulsion to polymerize by free radical polymerization at a pH range of from about 2 to less than 7. [0030] The associative polymer can be an anionic copolymer. The anionic copolymer is characterized in that the Huggins' constant (k') determined between 0.0025 wt. % to 0.025 wt. % of the copolymer in 0.01 M NaCI is greater than 0.75 and the storage modulus (G') for a 1.5 wt. % actives copolymer solution at 4.6 Hz greater than 175 Pa.

[0031] The associative polymer can be a cationic copolymer. The cationic copolymer is characterized in that its Huggins' constant (k¹) determined between 0.0025 wt. % to 0.025 wt. % of the copolymer in 0.01 M NaCI is greater than 0.5; and it has a storage modulus (G') for a 1.5 wt. % actives copolymer solution at 6.3 Hz greater than 50 Pa.

[0032] The associative polymer can be an amphoteric copolymer. The amphoteric copolymer is characterized in that its Huggins' constant (k¹) determined between 0.0025 wt. % to 0.025 wt. % of the copolymer in 0.01 M NaCI is greater than 0.5; and the copolymer has a storage modulus (G') for a 1.5 wt. % actives copolymer solution at 6.3 Hz greater than 50 Pa.

[0033] Inverse emulsion polymerization is a standard chemical process for preparing high molecular weight water-soluble polymers or copolymers. In general, an inverse emulsion polymerization process is conducted by 1) preparing an aqueous solution of the monomers, 2) contacting the aqueous solution with a hydrocarbon liquid containing appropriate emulsification surfactant(s) or surfactant mixture to form an inverse monomer emulsion, 3) subjecting the monomer emulsion to free radical polymerization, and, optionally, 4) adding a breaker surfactant to enhance the inversion of the emulsion when added to water.

[0034] Inverse emulsions polymers are typically water-soluble polymers based upon ionic or non-ionic monomers. Polymers containing two or more monomers, also referred to as copolymers, can be prepared by the same process. These co- monomers can be anionic, cationic, zwitterionic, nonionic, or a combination thereof. [0035] Typical nonionic monomers, include, but are not limited to, acrylamide; methacrylamide; N-alkylacrylamides, such as N-methylacrylamide; N₁N- dialkylacrylamides, such as N,N-dimethylacrylamide; methyl acrylate; methyl methacrylate; acrylonitrile; N-vinyl methylacetamide; N-vinyl formamide; N-vinyl methyl formamide; vinyl acetate; N-vinyl pyrrolidone; hydroxyalky(meth)acrylates such as hydroxyethyl(meth)acrylate or hydroxypropyl(meth)acrylate; mixtures of any of the foregoing and the like.

[0036] Nonionic monomers of a more hydrophobic nature can also be used in the preparation of the associative polymer. The term 'more hydrophobic' is used here to indicate that these monomers have reduced solubility in aqueous solutions; this reduction can be to essentially zero, meaning that the monomer is not soluble in water. It is noted that the monomers of interest are also referred to as polymerizable surfactants or surfmers. These monomers include, but are not limited to, alkylacryamides; ethylenically unsaturated monomers that have pendant aromatic and alkyl groups, and ethers of the formula CH₂=CR'CH₂OA_mR where R' is hydrogen or methyl; A is a polymer of one or more cyclic ethers such as ethyleneoxide, propylene oxide and/or butylene oxide; and R is a hydrophobic group; vinylalkoxylates; allyl alkoxylates; and allyl phenyl polyolether sulfates. Exemplary materials include, but are not limited to, methylmethacrylate, styrene, t-octyl acrylamide, and an allyl phenyl polyol ether sulfate marketed by Clariant as Emulsogen® APG 2019.

[0037] Exemplary anionic monomers include, but are not limited to, the free acids and salts of: acrylic acid; methacrylic acid; maleic acid; itaconic acid; acrylamidoglycolic acid; 2-acrylamido-2-methyl-1-propanesulfonic acid; 3-allyloxy-2- hydroxy-1-propanesulfonic acid; styrenesulfonic acid; vinylsulfonic acid; vinylphosphonic acid; 2-acrylamido-2-methylpropane phosphonic acid; mixtures of any of the foregoing and the like.

[0038] Exemplary cationic monomers include, but are not limited to, cationic ethylenically unsaturated monomers such as the free base or salt of: diallyldialkylammonium halides, such as diallyldimethylammonium chloride; the (meth)acrylates of dialkylaminoalkyl compounds, such as dimethylaminoethyl (meth)acrylate, diethylaminoethyl (meth)acrylate, dimethyl aminopropyl (meth)acrylate, 2-hydroxydimethyl aminopropyl (meth)acrylate, aminoethyl (meth)acrylate, and the salts and quaternaries thereof; the N,N-dialkylaminoalkyl(meth)acrylamides, such as N,N-dimethylaminoethylacrylamide, and the salts and quaternaries thereof and mixture of the foregoing and the like.

[0039] The co-monomers may be present in any ratio. The resultant associative polymer can be non-ionic, cationic, anionic, or amphoteric (contains both cationic and anionic charge).

[0040] The molar ratio of nonionic monomer to anionic monomer (B:F or

Formula I) may fall within the range of 95:5 to 5:95, preferably the range is from about 75:25 to about 25:75 and even more preferably the range is from about 65:35 to about 35:65 and most preferably from about 60:40 to about 40:60. In this regard, the molar percentages of B and F must add up to 100%. It is to be understood that more than one kind of nonionic monomer may be present in the Formula I. It is also to be understood that more than one kind of anionic monomer may be present in the Formula I.

[0041] In one preferred embodiment of the invention the associative polymer, when it is an anionic copolymer, is defined by Formula I where B, the nonionic polymer segment, is the repeat unit formed after polymerization of acrylamide; and F, the anionic polymer segment, is the repeat unit formed after polymerization of a salt or free acid of acrylic acid and the molar percent ratio of B:F is from about 75:25 to about 25:75

[0042] The physical characteristics of the associative polymer, when it is an anionic copolymer, are unique in that their Huggins¹ constant (k¹) as determined in 0.01 M NaCI is greater than 0.75 and the storage modulus (G') for a 1.5 wt. % actives polymer solution at 4.6 Hz is greater than 175 Pa, preferably greater than 190 and even more preferably greater than 205. The Huggins¹ constant is greater than 0.75, preferably greater than 0.9 and even more preferably greater than 1.0 [0043] The molar ratio of nonionic monomer to cationic monomer (B:F of

Formula I) may fall within the range of 99:1 to 50:50, or 95:5 to 50:50, or 95:5 to 75:25, or 90:10 to 60:45, preferably the range is from about 85:15 to about 60:40 and even more preferably the range is from about 80:20 to about 50:50. In this regard, the molar percentages of B and F must add up to 100%. It is to be understood that more than one kind of nonionic monomer may be present in the Formula I. It is also to be understood that more than one kind of cationic monomer may be present in the Formula I.

[0044] With respect to the molar percentages of the amphoteric copolymers of

Formula I, the minimum amount of each of the anionic, cationic and non-ionic monomer is 1 % of the total amount of monomer used to form the copolymer. The maximum amount of the non-ionic, anionic or cationic is 98% of the total amount of monomer used to form the copolymer. Preferably the minimum amount of any of anionic, cationic and non-ionic monomer is 5%, more preferably the minimum amount of any of anionic, cationic and non-ionic monomer is 7% and even more preferably the minimum amount of any of anionic, cationic and non-ionic monomer is 10% of the total amount of monomer used to form the copolymer. In this regard, the molar percentages of anionic, cationic and non-ionic monomer must add up to 100%. It is to be understood that more than one kind of nonionic monomer may be present in the Formula I, more than one kind of cationic monomer may be present in the Formula I, and that more than one kind of anionic monomer may be present in the Formula I. [0045] The physical characteristics of the associative polymer, when it is a cationic or amphoteric copolymer, are unique in that their Huggins' constant (k¹) as determined in 0.01 M NaCI is greater than 0.5 and the storage modulus (G') for a 1.5 wt. % actives polymer solution at 6.3 Hz is greater than 50 Pa, preferably greater than 10 and even more preferably greater than 25, or greater than 50, or greater than 100, or greater than 175, or greater than 200. The Huggins' constant is greater than 0.5, preferably greater than 0.6, or greater than 0.75, or greater than 0.9 or greater than 1.0.

[0046] The emulsification surfactant or surfactant mixture used in an inverse emulsion polymerization system have an important effect on both the manufacturing process and the resultant product. Surfactants used in emulsion polymerization systems are known to those skilled in the art. These surfactants typically have a range of HLB (Hydrophilic Lipophilic Balance) values that is dependent on the overall composition. One or more emulsification surfactants can be used. The emulsification surfactant(s) of the polymerization products that are used to produce the associative polymer include at least one diblock or triblock polymeric surfactant. It is known that these surfactants are highly effective emulsion stabilizers. The choice and amount of the emulsification surfactant(s) are selected in order to yield an inverse monomer emulsion for polymerization. Preferably, one or more surfactants are selected in order to obtain a specific HLB value.

[0047] Diblock and triblock polymeric emulsification surfactants are used to provide unique materials. When the diblock and triblock polymeric emulsification surfactants are used in the necessary quantity, unique polymers exhibiting unique characteristic result, as described in WO 03/050152 A1 and US 2004/0143039 A1, the entire contents of each is herein incorporated by reference. Exemplary diblock and triblock polymeric surfactants include, but are not limited to, diblock and triblock copolymers based on polyester derivatives of fatty acids and poly[ethyleneoxide] (e.g., Hypermer® B246SF, Uniqema, New Castle, DE), diblock and triblock copolymers based on polyisobutylene succinic anhydride and poly[ethyleneoxide], reaction products of ethylene oxide and propylene oxide with ethylenediamine, mixtures of any of the foregoing and the like. Preferably the diblock and triblock copolymers are based on polyester derivatives of fatty acids and poly[ethyleneoxide]. When a triblock surfactant is used, it is preferable that the triblock contains two hydrophobic regions and one hydrophilic region, i.e., hydrophobe-hydrophile-hydrophobe. [0048] The amount (based on weight percent) of diblock or triblock surfactant is dependent on the amount of monomer used to form the associative polymer. The ratio of diblock or triblock surfactant to monomer is at least about 3 to 100. The amount of diblock or triblock surfactant to monomer can be greater than 3 to 100 and preferably is at least about 4 to 100 and more preferably 5 to 100 and even more preferably about 6 to 100. The diblock or triblock surfactant is the primary surfactant of the emulsification system.

[0049] A secondary emulsification surfactant can be added to ease handling and processing, to improve emulsion stability, and/or to alter the emulsion viscosity. Examples of secondary emulsification surfactants include, but are not limited to, sorbitan fatty acid esters, such as sorbitan monooleate (e.g., Atlas G-946, Uniqema, New Castle, DE), ethoxylated sorbitan fatty acid esters, polyethoxylated sorbitan fatty acid esters, the ethylene oxide and/or propylene oxide adducts of alkylphenols, the ethylene oxide and/or propylene oxide adducts of long chain alcohols or fatty acids, mixed ethylene oxide/propylene oxide block copolymers, alkanolamides, sulfosuccinates and mixtures thereof and the like.

[0050] Polymerization of the inverse emulsion may be carried out in any manner known to those skilled in the art. Examples can be found in many references, including, for example, Allcock and Lampe, Contemporary Polymer Chemistry, (Englewood Cliffs, New Jersey, PRENTICE-HALL, 1981), chapters 3-5. [0051] A representative inverse emulsion polymerization is prepared as follows.

To a suitable reaction flask equipped with an overhead mechanical stirrer, thermometer, nitrogen sparge tube, and condenser is charged an oil phase of paraffin oil (135.Og, Exxsol® D80 oil, Exxon - Houston, TX) and surfactants (4.5g Atlas® G- 946 and 9.Og Hypermer® B246SF). The temperature of the oil phase is then adjusted to 37°C.

[0052] An aqueous phase is prepared separately which comprised 53-wt. % acrylamide solution in water (126.5g), acrylic acid (68.7g), deionized water (70.Og), and Versenex® 80 (Dow Chemical) chelant solution (0.7g). The aqueous phase is then adjusted to pH 5.4 with the addition of ammonium hydroxide solution in water (33.1 g, 29.4 wt. % as NH₃). The temperature of the aqueous phase after neutralization is 39°C.

[0053] The aqueous phase is then charged to the oil phase while simultaneously mixing with a homogenizer to obtain a stable water-in-oil emulsion. This emulsion is then mixed with a 4-blade glass stirrer while being sparged with nitrogen for 60 minutes. During the nitrogen sparge the temperature of the emulsion is adjusted to 50+1 °C. Afterwards, the sparge is discontinued and a nitrogen blanket implemented.

[0054] The polymerization is initiated by feeding a 3-wt. % solution of 2,2'- azobisisobutyronitrile (AIBN) in toluene (0.213g). This corresponds to an initial AIBN charge, as AIBN, of 250 ppm on a total monomer basis. During the course of the feed the batch temperature was allowed to exotherm to 62⁰C (~50 minutes), after which the batch was maintained at 62+1 °C. After the feed the batch was held at 62+1 °C for 1 hour. Afterwards 3-wt. % AIBN solution in toluene (0.085g) is then charged in under one minute. This corresponds to a second AIBN charge of 100 ppm on a total monomer basis. Then the batch is held at 62+1⁰C for 2 hours. Then batch is then cooled to room temperature, and breaker surfactant(s) is added. [0055] The associative polymer emulsion is typically inverted at the application site resulting in an aqueous solution of 0.1 to 1% active copolymer. This dilute solution of the associative polymer is then added to the paper process to affect retention and drainage. The associative polymer may be added to the thick stock or thin stock, preferably the thin stock. The associative polymer may be added at one feed point, or may be split fed such that the associative polymer is fed simultaneously to two or more separate feed points. Typical stock addition points include feed point(s) before the fan pump, after the fan pump and before the pressure screen, or after the pressure screen.

[0056] The associative polymer may be added in any effective amount to achieve flocculation. The amount of copolymer could be more than 0.5 Kg per metric ton of cellulosic pulp (dry basis). Preferably, the associative polymer is employed in an amount of at least about 0.03 Ib. to about 0.5 Kg. of active copolymer per metric ton of cellulosic pulp, based on the dry weight of the pulp. The concentration of copolymer is preferably from about 0.05 to about 0.5 Kg of active copolymer per metric ton of dried cellulosic pulp. More preferably the copolymer is added in an amount of from about 0.05 to 0.4 Kg per metric ton cellulose pulp and, most preferably, about 0.1 to about 0.3 Kg per metric ton based on dry weight of the cellulosic pulp. [0057] The second component of the retention and drainage system can be one of a number of ionic polymeric materials or synthetic polyelectrolytes ("polyelectrolytes"). The material may be a single product or blend of materials. These materials may differ in their chemical nature, as influenced by the monomer composition, nature of the ionic functionality, amount of ionic functionality, distribution of the ionic functionality along the polymer chain, and the physical nature of the polymer, such as the molecular weight, charge density and secondary/tertiary structure.

[0058] This component can be selected from at least one of several groups of polymers including, but not limited to acrylamide-based polymers, such as anionic polyacrylamides and cationic polyacrylamides; polyamidoamine-epihalohydrin resins; polyamines; polyimines; and derivatives of any of the preceding, and the like. What is meant by derivative is polymers with at least one additional functional group or component. The functional groups can be selected from, but not limited to, the group that includes epoxy, azetidinium, aldehyde, carboxyl group, acrylate and derivatives thereof, acrylamide and derivatives thereof, and quaternary amine. Examples include, but are not limited to, acrylamide based reactive polymers, polyamidoamine- epihalohydrin resins, and polyamines, and polyiminies, such as cationic functionalized polyacrylamides (HERCOBOND 1000® manufactured by Hercules Incorporated) such as those disclosed in U.S. Pat. No. 5,543,446 which is incorporated herein in its entirety, creping aids such as CREPETROL® A3025 disclosed in U.S. Pat. No. 5,338,807 which is incorporated herein in its entirety, and polyamidoamine- epihalohydrin resins such as those disclosed in U.S. Pat. Nos. 2,926,116 and 2,926,154, incorporated by reference in their entirety. The polymers may be known in the art under a number of terms, including, but not limited to, coagulant, dry strength resin, flocculant, promoter resin and wet strength resin.

[0059] The term synthetic polyelectrolyte is used here to mean a polymer comprising one or more monomers, of which at least one monomer is anionic or cationic. Synthetic polyelectrolyte that are derivatized are contemplated with the scope of this invention and are considered for the purposes of this invention to be within the definition of synthetic polyelectrotyles. The anionic or cationic monomers are most often used to make copolymers with a non-ionic monomer such as acrylamide. These polymers can be provided by a variety of synthetic processes including, but not limited to, suspension, dispersion and inverse emulsion polymerization. For the last process, a microemulsion may also be used. [0060] Alternatively, the term synthetic polyelectrolyte is used to mean a polymer obtained by polymerization of one or more nonionic monomers followed by derivitization or reaction with another moiety. An example is a polyamidoamine- epihalohydrin polymer formed by the reaction of an amine and a dicarboxylic acid that is the reation with an epihalohydrin. Exemplary amine include, but are not limited to, diamine such as ethylene diamine; triamines such as diethyltriamine; and tetramines such as triethylene tetramine. Exemplary dicarboxylic acid include, but is not limited to, adipic acid. Exemplary epihalohydrins include, but is not limited to epichlorohydrin. [0061] The co-monomers of the synthetic polyelectrolyte may be present in any ratio. The resultant synthetic polyelectrolyte can be cationic, anionic, or amphoteric (contains both cationic and anionic charge). Ionic water-soluble polymers, or polyelectrolytes, are typically produced by copolymerizing a non-ionic monomer with an ionic monomer, or by post polymerization treatment of a non-ionic polymer to impart ionic functionality. An example of this is post polymerization hydrolysis of N- vinyl formamide polymers and copolymers to produce poly(vinylamine). [0062] Examples of preferred synthetic polyelectrolytes useful in the present include but are not limited cationic copolymers with 20 mole percent or greater cationic monomer content, an anionic copolymer with 20 mole percent or less anionic monomer content, polyamines, poly-diallyldimethylammonium chlorides, polyamidoamine-epichlorohydrin resins, or modified polyethyleneimines. One example of a cationic copolymers with 20 mole percent or greater cationic monomer content is 2-acryloyloxytrimethylammonium chloride (AETAC)/acrylamide copolymer with 20 mole percent or greater AETAC content. In one embodiment the anionic copolymer with 20 mole percent or less anionic monomer content is an acrylic acid/acrylamide copolymer acid content..

[0063] The terms coagulant and flocculant are best defined in comparative terms as their chemical nature can be similar. One mode of differentiation is that coagulants typically are lower in molecular weight than flocculants. A second mode is the mechanism by which they cause aggregation of colloidal particles. A coagulant acts to aggregate suspension of particles by destabilization or changing the ionic nature of the particle. This results in the overall system having a zeta potential closer to zero. Flocculation destabilizes the suspension by bonding the particles together via the long chains of the polymer. A coagulant causes an irreversible aggregation, whereas the effect of a flocculant is reversible. Finally, most coagulants are cationic in nature, while flocculants are either cationic or anionic.

[0064] Examples of coagulants that can be used as polyelectrolytes in the present invention include, but are not limited to, linear and branched polyamine condensation products with epichlorohydrin and amines (dimethylamine, ethylenediamine, etc.), such as PerForm® PC1279, a product of Hercules Incorporated, Wilmington, DE; poly(diallydimethyl ammonium chloride) or poly (DADMAC), such as PerForm® 8717, a product of Hercules Incorporated; polyethylene imine and modified polyethylene imines such as Polymin® SK, a product of BASF Corporation (Mount Olive, NJ); polyamidoamines, such as Reten® 204LS, a product of Hercules Incorporated; hydrolyzates and quaternized hydrolyzates, and chemical derivatives of N-vinyl formamide polymers and copolymers; and the like. [0065] Flocculants are typically high molecular weight polyelectrolytes.

Materials in commercial use include anionic materials, cationic materials, amphoteric polymers, as well as blends of anionic and cationic copolymers. It is also noted that homopolymers of either anionic or cationic monomer also act as flocculants. [0066] The general structure of the synthetic polyelectrolytes used in the present invention is provided in Formulas II, III and IV. N represents a nonionic polymer segment. A represents an anioinic polymer segment. C represents a cationic polymer segment.

[N-CO-C] (Formula II)

[N-CO-A] (Formula III)

[N-co-C-co-A] (Formula IV) [0067] The nonionic polymer segment N in Formula II, Formula III and Formula

IV is the repeat unit formed after polymerization of one or more nonionic monomers. Exemplary monomers encompassed by N include, but are not limited to, acrylamide; methacrylamide; N-alkylacrylamides, such as N-methylacrylamide; N₁N- dialkylacrylamide, such as N,N-dimethylacrylamide; methyl methacrylate; methyl acrylate; acrylonitrile, of N-vinyl formamide, N-vinyl pyrrolidone, mixtures of any of the foregoing and the like. Other types of nonionic monomer may be used. [0068] The cationic polymer segment C in Formula Il and Formula IV is the repeat unit formed after polymerization of one or more cationic monomers. Exemplary monomers encompassed by C include, but are not limited to, cationic ethylenically unsaturated monomers such as the salts and free bases of: diallydialkylammonium halides, such as diallydimethylammonium chloride; the (meth)acrylates of dialkylaminoalkyl compounds, such as dimethylaminoethyl (meth) acrylate, diethylaminoethyl(meth)acrylate, dimethyl aminopropyl (meth)acrylate, 2- hydroxydimethyl aminopropyl(meth)acrylate, aminoethyl (meth)acrylate;, the N₁N- dialkylaminoalkyl(meth)acrylamides, such as N.N-dimethylaminoethylacrylamide, and the salt and quaternaries thereof and mixture of the foregoing and the like. [0069] The anionic polymer segment A in Formula III and Formula IV is the repeat unit formed after polymerization of one or more anionic monomers. Exemplary monomers encompassed by A include, but are not limited to, the free acids and salts of: acrylic acid; methacrylic acid, maleic acid; itaconic acid; acrylamidoglycolic acid; 2- acrylamido-2-methyl-1-propanesulfonic acid; 3-allyloxy-2-hydroxy-1-propanesulfonic acid; styrenesulfonic acid; vinylsulfonic acid; vinylphosphonic acid; 2-acrylamido-2- methylpropane phosphonic acid; mixtures of any of the foregoing and the like. [0070] The molar percentage of N:C of nonionic monomer to cationic monomer of Formula Il may fall within the range of about 99:1 to about 1 :99. The molar percentages of N and C must add up to 100%. It is to be understood that more than one kind of nonionic monomer may be present in Formula II. It is also to be understood that more than one kind of cationic monomer may be present in Formula II. [0071] The molar percentage of N:A of nonionic monomer to anionic monomer of Formula III may fall within the range of about 99:1 to 1:99. The molar percentages of N and A must add up to 100%. It is to be understood that more than one kind of nonionic monomer may be present in Formula III. It is also to be understood that more than one kind of anionic monomer may be present in Formula III. [0072] With respect to the molar percentages of the amphoteric polymers of

Formula IV, the minimum amount of each A, N and C is about 1% of the total amount of monomer used to form the polyelectrolyte. The maximum amount of A, N or C is about 98% of the total amount of monomer used to form the polyelectrolyte polymer. The molar percentages of A, N and C must add up to 100%. It is to be understood that more than one kind of nonionic monomer may be present in Formula IV, more than one kind of cationic monomer may be present in Formula IV, and that more than one kind of anionic monomer may be present in Formula IV.

[0073] Examples of cationic polyelectrolytes used as flocculants include, but are not limited to, cationic copolymers of acrylamide, such as PerForm® PC8713 and PerForm® PC8138, products of Hercules Incorporated, Wilmington, DE; poly(diallyldimethyl ammonium chloride), such as PerForm® PC8717, a product of Hercules Incorporated; reaction product of polyacrylamide with dimethylamine and formaldehyde known in the art as Mannich reaction products, such as PerForm® PC 8984, a product of Hercules Incorporated; polymer blends of more than one cationic polymer, poly(vinylamine), and the like. It is contemplated that cationic functionalized polymers based on acrylamide can be used as the second component. An exemplary material is Hercobond® 1000, a product of Hercules Incorporated. [0074] Examples of anionic polyelectrolytes include, but are not limited to, copolymers of acrylic acid and acrylamide, such as Perform® 8137 and Reten® 1523H, products of Hercules Incorporated. It is contemplated that anionic functionalized polymers based on acrylamide, can be used as the second component. An exemplary material is Hercobond® 2000, a product of Hercules Incorporated. [0075] Polyelectrolytes can vary in molecular weight from 50,000 to 50,000,000 and can be linear, branched or dendritic. They vary in charge density from 1 to 99% on a molar basis.

[0076] Alternatively, as noted above, the second component can be a polyamidoamine-epihalohydrin resin, polyamine or polyimine. Preferred are polyamidoamine-epihalohydrin resins such as those disclosed in U.S. Pat. Nos. 2,926,116 and 2,926,154, which are herein incorporated by reference in their entirety. Preferred polyamidoamine-epihalohydrin resins can also be prepared in accordance with the teachings of U.S. Pat. No. 5,614,597 which are herein incorporated by reference in their entirety. As discussed in U.S. Pat. No. 5,614,597, these processes typically involve reacting aqueous polyamidoamine with an excess of epihalohydrin to completely convert amine groups in the polyamidoamine to epihalohydrin adducts. During the reaction halohydrin groups are added at the secondary amine groups of the polyamidoamine. Preferred polyamidoamine-epihalohydrin resins include polyamidoamine-epichlorohydrins such as those sold by Hercules Incorporated of Wilmington, DE, under various trade names. Preferred polyamidoamine-epihalohydrin resins available from Hercules include, but are not limited to, the KYMENE® resins and the HERCOBOND® resins, KYMENE® 557H resin; KYMENE® 557LX2 resin, KYMENE® 557SLX resin; KYMENE® 557ULX resin, KYMENE® 557ULX2 resins; KYMENE® 709 resin; KYMENE® 736 resin; and HERCOBOND® 5100 resin. Of these, KYMENE® 557H resin and HERCOBOND® 5100 are especially preferred polyamidoamines, available in the form of aqueous solutions. KYMENE® 736 resin (a polyamine) can also be employed as component (A). It is expressly contemplated that equivalents to each of the foregoing resins are within the scope of the present invention.

[0077] An alternative second component of the retention and drainage system can be a cyclic organic material. One of the unique aspects of these materials is their ability to form a complex with other, typically low molecular weight, molecules or ions. These interactions have been termed "guest-host¹ chemistry, with the cyclic material being the host and the smaller guest molecule forming a complex where it assumes a position inside the ring-like 'host'. Examples of these compounds, also called macrocyclic compounds, include, but are not limited to, crown ethers, cyclodextrins and macrocyclic antibiotics.

[0078] Crown ethers are cyclic oligomers of ethylene glycol comprising carbon hydrogen and oxygen. Each oxygen atom is bound to two carbon atoms, resulting in the 'crown' like ring. These molecules are such that atoms of certain metallic elements, such as sodium potassium, attach themselves to the exposed oxygen atoms of the ring, sequestering it.

[0079] Cyclodextrin are cyclic starch derivatives that occur in nature or can be synthesized using enzymes such as cyclomaltodextrin glucosyltransferase. The naturally occurring cyclodextrins, are referred to alpha-, beta-, and gamma- cyclodextrin. Cyclodextrins form stable complexes with other compounds.

[0080] Macrocyclic antibiotic is a term given to a series of cyclic compounds with antibiotic activity. Due to their structure, they will selectively complex with molecules. Examplary macrocyclic antibiotics include, but are not limited to rifamycin, vancomycin and ristocetin A.

[0081] The second component of the retention and drainage system can be added at amounts up to 20 Kg of active material per metric ton of cellulose pulp based on dry weight of the pulp, with the ratio of the associative polymer to second component being 1 :100 to 100:1. It is contemplated that more than one second component can be used in the papermaking system.

[0082] Optionally siliceous materials can be used as an additional component of a retention and drainage aid used in making paper and paperboard. The siliceous material may be any of the materials selected from the group consisting of silica based particles, silica microgels, amorphous silica, colloidal silica, anionic colloidal silica, silica sols, silica gels, polysilicates, polysilicic acid, and the like. These materials are characterized by the high surface area, high charge density and submicron particle size.

[0083] This group includes stable colloidal dispersion of spherical amorphous silica particles, referred to in the art as silica sols. The term sol refers to a stable colloidal dispersion of spherical amorphous particles. Silica gels are three dimensional silica aggregate chains, each comprising several amorphous silica sol particles that can also be used in retention and drainage aid systems; the chains may be linear or branched. Silica sols and gels are prepared by polymerizing monomeric silicic acid into a cyclic structure that result in discrete amorphous silica sols of polysilicic acid.

These silica sols can be reacted further to produce three-dimensional gel network. The various silica particles (sols, gels, etc.) can have an overall size of 5-50 nm. Anionic colloidal silica can also be used.

[0084] The siliceous material can be added to the cellulosic suspension in an amount of at least 0.005 Kg per metric ton based on dry weight of the cellulosic suspension. The amount of siliceous material may be as high as 50 Kg per metric ton. Preferably, the amount of siliceous material is from about 0.05 to about 25 Kg per metric ton. Even more preferably the amount of siliceous material is from about 0.25 to about 5 Kg per metric ton based on the dry weight of the cellullosic suspension. [0085] The amount of siliceous material in relationship to the amount of associative polymer used in the present invention can be about 100:1 to about 1 :100 by weight, or from about 50:1 to 1 :50 or about 10:1 to 1 :10.

[0086] Yet other additional components that can be part of the inventive system are aluminum sources such as alum (aluminum sulfate), polyaluminum sulfate, polyaluminum chloride and aluminum chlorohydrate.

[0087] The components of a retention and drainage system may be added substantially simultaneously to the cellulosic suspension. The term retention and drainage system is used here to encompass two or more distinct materials added to the papermaking slurry to provide improved retention and drainage. For instance, the components may be added to the cellulosic suspension separately either at the same stage or dosing point or at different stages or dosing points. When the components of the inventive system are added simultaneously any two or more of the materials may be added as a blend. The mixture may be formed in-situ by combining any two or more of the materials at the dosing point or in the feed line to the dosing point. Alternatively the inventive system comprises a preformed blend of the any two or more of the materials. In an alternative form of the invention the components of the inventive system are added sequentially. A shear point may or may not be present between the addition points of the components. The components can be added in any order.

[0088] The inventive system is typically added to the paper process to affect retention and drainage. The inventive system may be added to the thick stock or thin stock, preferably the thin stock. The system may be added at one feed point, or may be split fed such that the inventive system is fed simultaneously to two or more separate feed points. Typical stock addition points include feed points(s) before the fan pump, after the fan pump and before the pressure screen, or after the pressure screen.

EXAMPLES

[0089] To evaluate the performance of the present invention, a series of drainage tests were conducted utilizing a synthetic alkaline furnish. This furnish is prepared from hardwood and softwood dried market lap pulps, and from water and additional materials. First, the hardwood and softwood dried market lap pulp are refined separately. These pulps are then combined at a ratio of about 70 percent by weight of hardwood to about 30 percent by weight of softwood in an aqueous medium. The aqueous medium utilized in preparing the furnish comprises a mixture of local hard water and deionized water to a representative hardness. Inorganic salts are added in amounts so as to provide this medium with a total alkalinity of 75 ppm as CaCU₃ and hardness of 100 ppm as CaCO₃. Precipitated calcium carbonate (PCC) is introduced into the pulp furnish at a representative weight percent to provide a final furnish containing 80% fiber and 20% PCC filler. The drainage tests were conducted by mixing the furnish with a mechanical mixer at a specified mixer speed, and introducing the various chemical components into the furnish and allowing the individual components to mix for a specified time prior to the addition of the next component. The specific chemical components and dosage levels are described in the data tables. The drainage activity of the invention was determined utilizing the Canadian Standard Freeness (CSF). The CSF test, a commercially available device (Lorentzen & Wettre, Stockholm, Sweden), can be utilized to determine relative drainage rate or dewatering rate is also known in the art; a standard test method (TAPPI Test Procedure T-227) is typical. The CSF device consists of a drainage chamber and a rate measuring funnel, both mounted on a suitable support. The drainage chamber is cylindrical, fitted with a perforated screen plate and a hinged plate on the bottom, and with a vacuum tight hinged lid on the top. The rate- measuring funnel is equipped with a bottom orifice and a side overflow orifice. [0090] The CSF drainage tests are conducted with 1 liter of the furnish. The furnish is prepared for the described treatment externally from the CSF device in a square beaker to provide turbulent mixing. Upon completion of the addition of the additives and the mixing sequence, the treated furnish is poured into the drainage chamber, closing the top lid, and then immediately opening the bottom plate. The water is allowed to drain freely into the rate-measuring funnel; water flow that exceeds that determined by the bottom orifice will overflow through the side orifice and is collected in a graduate cylinder. The values generated are described in milliliters (ml) of filtrate; higher quantitative values represent higher levels of drainage or dewatering. [0091] Test samples were prepared as follows: to the furnish prepared as described above is added, first, 5 Kg cationic starch (Stalok® 400, AE., Staley, Decatur, IL) per metric ton of furnish (dry basis). The additive(s) of interest, as noted in the tables, are then added.

[0092] The data in Table 1 illustrate the drainage activity of various cationic coagulants within the inventive process. PC 1279 is PerForm® PC1279, a branched polyamine; PC 1290 is PerForm® PC1290, a linear polyamine; PC8229 is PerForm® PC8229 and PC8717 is PerForm®™ PC8717, polymers of diallyldimethyl ammonium chloride; SP9232 is PerForm® SP9232, a retention and drainage aid product; and PC8138 is PerForm® PC8138, a cationic copolymer of polyacrylamide; all are products of Hercules Incorporated, Wilmington, DE. Polymin® SK is a modified polyethyleneimine from BASF (Mount Olive, NJ).

TABLE 1

JN # ADD # 2 Kg/MT ADD # 3 Kg/MT ADD # 4 Kg/MT CSF

(active) (active) (active)

1 None PC 8138 0.2 none 400

2 PC 1279 0.25 PC 8138 0.2 SP 9232 0.2 540

3 PC 1279 0.5 PC 8138 0.2 SP 9232 0.2 510

4 PC 1290 0.25 PC 8138 0.2 SP 9232 0.2 465

5 PC 1290 0.5 PC 8138 0.2 SP 9232 0.2 435

6 PC 8229 0.25 PC 8138 0.2 SP 9232 0.2 465

7 PC 8229 0.5 PC 8138 0.2 SP 9232 0.2 440

8 PC 8717 0.25 PC 8138 0.2 SP 9232 0.2 485

9 PC 8717 0.5 PC 8138 0.2 SP 9232 0.2 465

10 Polymin SK 0.25 PC 8138 0.2 SP 9232 0.2 550

11 Polymin SK 0.5 PC 8138 0.2 SP 9232 0.2 560 [0093] The data in Table 1 demonstrate the improved drainage provided by the current invention with the utilization of a cationic coagulant.

[0094] Next, a series of drainage experiments were conducted with cationic polyvinylamine polymers, as shown in Table 2. The materials are as indicated in Table 1 , Alum is aluminum sulfate octadecahydrate as a 50% solution (Delta Chemical Corp., Baltimore, MD). PPD M-1188, PPD M-1189, and PPD M-5088 (Hercules Incorporated, Wilmington, DE) are cationic polyvinylamine copolymers, prepared by the partial hydrolysis of N-vinyl formamide to produce poly(N-vinyl formamide - co - vinylamine).

TABLE 2

RUN Additive Kg/MT Additive #3 Kg/MT Additive #4 Kg/MT CSF, mis

# #2 (active) (active) (active)

1 Alum 2.5 None SP 9232 0.25 520

2 Alum 2.5 PC 8138 0.25 SP 9232 0.25 680

3 Alum 2.5 PC 8138 0.5 SP 9232 0.25 688

4 Alum 2.5 PPD M-1188 0.25 SP 9232 0.25 702

5 Alum 2.5 PPD M-1188 0.5 SP 9232 0.25 718

6 Alum 2.5 PPD M-1189 0.25 SP 9232 0.25 698

7 Alum 2.5 PPD M-1189 0.5 SP 9232 0.25 704

8 Alum 2.5 PPD M-5088 0.25 SP 9232 0.25 716

9 Alum 2.5 PPD M-5088 0.5 SP 9232 0.25 730

[0095] The data in Table 2 illustrate the drainage activity of cationic polyvinylamine copolymers within the current invention.

[0096] A series of cationic and anionic flocculants were evaluated next, where the specific polymer molar charge density and physical form is noted in Table 3. The

EM, FO, AN, and EM series flocculants are products of SNF Floerger (Riceboro, GA), and the Superfloc flocculants are products of Cytec Industries Inc. (West Patterson,

NJ).

TABLE 3

Flocculant Charge Form

EM 140CT Cationic Powder 2 EM240CT Cationic Powder

3 EM340CT Cationic Powder

4 EM440CT Cationic Powder

5 FO4190SH Cationic Powder

6 FO4290SH Cationic Powder

7 FO4400SH Cationic Powder

8 FO4490SH Cationic Powder

9 AN 910 Anionic Powder

10 AN 910 SH Anionic Powder

11 AN 910 VHM Anionic Powder

12 AN 923 Anionic Powder

13 AN 923 SH Anionic Powder

14 AN 923 VHM Anionic Powder

15 AN 934 Anionic Powder

16 AN 934 SH Anionic Powder

17 AN 934 VHM Anionic Powder

18 AN 945 Anionic Powder

19 AN 945 SH Anionic Powder

20 AN 945 VHM Anionic Powder

21 AN 956 Anionic Powder

22 AN 956 SH Anionic Powder

23 AN 956 VHM Anionic Powder

24 AN 970 SH Anionic Powder

25 AN 977 VHM Anionic Powder

26 EM 533 Anionic Emulsion

27 EM 533H Anionic Emulsion

28 EM 630 Anionic Emulsion

29 EM 635 Anionic Emulsion

30 Superfloc 4814 Anionic Emulsion

31 Superfloc 4816 Anionic Emulsion

32 Superfloc 4818 Anionic Emulsion

TABLE 4

RUN Additive Kg/MT Additive #3 Kg/MT Additive #4 Kg/MT CSF,

# #2 (active) (active) (active) mis

1 Alum 2.5 None SP 9232 0.2 520

2 Alum 2.5 PC 8138 0.2 SP 9232 0.2 688

3 Alum 2.5 EM 140CT 0.2 SP 9232 0.2 700

4 Alum 2.5 EM240CT 0.2 SP 9232 0.2 694

5 Alum 2.5 EM340CT 0.2 SP 9232 0.2 714

6 Alum 2.5 EM440CT 0.2 SP 9232 0.2 704

7 Alum 2.5 FO4190SH 0.2 SP 9232 0.2 691

8 Alum 2.5 FO4290SH 0.2 SP 9232 0.2 713

9 Alum 2.5 FO4400SH 0.2 SP 9232 0.2 713

10 Alum 2.5 FO4490SH 0.2 SP 9232 0.2 704

11 Alum 2.5 PA 8137 0.2 SP 9232 0.2 685

12 Alum 2.5 AN 910 0.2 SP 9232 0.2 690

13 Alum 2.5 AN 910 SH 0.2 SP 9232 0.2 682

14 Alum 2.5 AN 91 O VHM 0.2 SP 9232 0.2 699

15 Alum 2.5 AN 923 0.2 SP 9232 0.2 678

16 Alum 2.5 AN 923 SH 0.2 SP 9232 0.2 692

17 Alum 2.5 AN 923 VHM 0.2 SP 9232 0.2 688

18 Alum 2.5 AN 934 0.2 SP 9232 0.2 672

19 Alum 2.5 AN 934 SH 0.2 SP 9232 0.2 681

20 Alum 2.5 AN 934 VHM 0.2 SP 9232 0.2 666

21 Alum 2.5 AN 945 0.2 SP 9232 0.2 666

22 Alum 2.5 AN 945 SH 0.2 SP 9232 0.2 659

23 Alum 2.5 AN 945 VHM 0.2 SP 9232 0.2 676

24 Alum 2.5 AN 956 0.2 SP 9232 0.2 680

25 Alum 2.5 AN 956 SH 0.2 SP 9232 0.2 673

26 Alum 2.5 AN 956 VHM 0.2 SP 9232 0.2 675

27 Alum 2.5 AN 970 SH 0.2 SP 9232 0.2 666

28 Alum 2.5 AN 977 VHM 0.2 SP 9232 0.2 660

29 Alum 2.5 EM 533 0.2 SP 9232 0.2 671

30 Alum 2.5 EM 533H 0.2 SP 9232 0.2 678

31 Alum 2.5 EM 630 0.2 SP 9232 0.2 670

32 Alum 2.5 EM 635 0.2 SP 9232 0.2 659

33 Alum 2.5 Superfloc 4814 0.2 SP 9232 0.2 680

34 Alum 2.5 Superfloc 4816 0.2 SP 9232 0.2 686

35 Alum 2.5 Superfloc 4818 0.2 SP 9232 0.2 682

[0097] The drainage data in Table 4 demonstrate the improved activity when cationic or anionic flocculants are utilized within the present invention. [0098] The table 5 illustrates the utility of cyclic organic materials. The test samples were prepared as follows: the furnish prepared as described above, is added, first, 5 Kg. of cationic starch (Stalok® 400, AE., Staley, Decatur, IL) per metric ton of furnish (dry basis), then 2.5 Kg. of alum (aluminum sulfate octadecahydrate obtained from Delta Chemical Corporation, Baltimore, MD as a 50% solution) per metric ton of furnish (dry basis), and then 0.5 Kg of PerForm® PC8138 (Hercules Incorporated, Wilmington, DE) per ton of furnish (dry basis). The additive(s) of interest, as noted in the table were then added in the examples provided in the table. SP9232 is PerForm® SP9232, a retention and drainage aid produced under certain conditions (see PCT WO 03/050152 A), is a product of Hercules Incorporated, Wilmington, DE; silica is BM 780 colloidal silica, a product of Eka Chemicals, Marietta, GA, crown ether is a 15-crown-5 compound (1 , 4, 7, 10, 13- pentaoxacyclopentadecane) obtained from Aldrich Chemicals, Milwaukee, Wl, and CD is alpha-cyclodextrin hydrate obtained from Aldrich Chemical, Milwaukee, Wl. [0099] The data indicate that the cyclic organic compounds provided improved drainage.

Table 5

(a) SP9232 and silica added at a level of 0.25 Kg per metric ton of furnish (dry basis), Crown ether and CD are added at a level of 0.5 Kg per metric ton of furnish (dry basis)

^(b) SIM indicates simultaneous addition and SEQ indicates sequential addition

Claims

CLAIMS:

1. A method of improving retention and drainage in a papermaking process wherein the improvement comprising adding to a papermaking slurry, an associative polymer and at least one synthetic polyelectrolyte, wherein the associative polymer comprising the formula:

^B-^CO-F+ <» wherein B is a nonionic polymer segment comprising one or more ethylenically unsaturated nonionic monomers; F is an polymer segment comprising at least one ethylenically unsaturated anionic or ethylenically unsaturated cationic monomer; and the molar percent ratio of B:F is 99:1 to 1 :99 and wherein the associative polymer has associative properties provided by an effective amount of at least emulsification surfactant chosen from diblock or triblock polymeric surfactants, and wherein the amount of the at least one diblock or triblock surfactant to monomer is at least about 3:100, wherein the at least one synthetic polyelectrolyte is selected from the group consisting of cationic copolymers with 20 mole percent or greater cationic monomer content, an anionic copolymer with 20 mole percent or less anionic monomer content, polyamines, poly-diallyldimethylammonium chlorides, polyamidoamine-epichlorohydrin resins, or modified polyethyleneimines.

2. The method of claim 1 wherein at least one synthetic polyelectrolyte is selected from the group consisting of cationic copolymers with 20 mole percent or greater cationic monomer content; and an anionic copolymer with 20 mole percent or less anionic monomer content; and wherein the cationic or anionic copolymer comprising at least one non-ionic monomer selected from acrylamide, methacrylamide, N, N- dialkylacrylamides, N-alkylacrylamides, N-vinyl methacetamide, N-vinyl formamide, N- vinyl methyl formamide, and N-vinyl pyrrolidone.

3. The method of claim 2 wherein the at least one synthetic polyelectrolyte is a anionic copolymer with 20 mole percent or less anionic monomer content wherein the anionic copolymer comprises at least one anionic monomer selected from the free acid or salt of: acrylic acid; methacrylic acid, maleic acid; itaconic acid; acrylamidoglycolic acid; 2-acrylamido-2-methyl-1-propanesulfonic acid; 3-allyloxy-2-hydroxy-1- propanesulfonic acid; styrenesulfonic acid; vinylsulfonic acid; vinylphosphonic acid; 2- acrylamido-2-methylpropane phosphonic acid.

4. The method of claim 3 wherein the at least one synthetic polyelectrolyte is a anionic copolymer with 20 mole percent or less anionic monomer content wherein the anionic copolymer comprises at least one anionic monomer selected from the free acid or salt of: acrylic acid, methacrylic acid, and styrenesulfonic acid.

5. The method of claim 2 wherein the at least one synthetic polyelectrolyte is a cationic copolymer with 20 mole percent or greater cationic monomer content wherein the cationic copolymer comprises at least one cationic monomer selected from the free base or salt of: diallyldimethylammonium halide; dialkylaminoalkyl (meth)acrylate, diethylaminoethyl (meth)acrylate, dimethyl aminopropyl (meth)acrylate, 2- hydroxydimethyl aminopropyl (meth)acrylate, aminoethyl (meth)acrylate, N, N- dimethylaminoethylacrylamide, and acryloyloxyethyl trimethyl ammonium chloride.

6. The method of claim 5 wherein the at least one synthetic polyelectrolyte is a cationic copolymer with 20 mole percent or greater cationic monomer content wherein the cationic copolymer comprises at least one cationic monomer selected from the free base or salt of: N,N-dimethylaminoethylacrylamide, and acryloyloxyethyl trimethyl ammonium chloride.

7. The method of claim 1 wherein the at least one synthetic polyelectrolyte is selected from the group consisting of polyamidoamine-epihalohydrin resins; polyamines; polyimines; and derivatives of any of the preceding.

8. The method of claim 7 wherein the at least one synthetic polyelectrolyte comprises polyamidoamine-epihalohydrin resins or derivatives thereof.

9. The method of claim 1 further comprising a siliceous material.

10. The method of claim 9 wherein the siliceous material is selected from the group consisting of silica based particles, silica microgels, amorphous silica, colloidal silica, anionic colloidal silica, silica sols, silica gels, polysilicates, polysilicic acid, and combinations thereof.

11. The method of claim 1 wherein the at least one synthetic polyelectrolyte comprises a polyamine or derivatives thereof.

12. The method of claim 1 wherein the associative polymer is anionic.

13. The method of claim 1 wherein the associative polymer comprises acrylamide and the free acid or salt of acrylic acid.

14. A composition comprising an associative polymer and at least one synthetic polyelectrolyte wherein the associative polymer comprising the formula: f-B-co-F-] (I) wherein B is a nonionic polymer segment comprising one or more ethylenically unsaturated nonionic monomers; F is an polymer segment comprising at least one ethylenically unsaturated anionic or ethylenically unsaturated cationic monomer; and the molar percent ratio of B:F is 99:1 to 1:99 and wherein the associative polymer has associative properties provided by an effective amount of at least emulsification surfactant chosen from diblock or triblock polymeric surfactants, and wherein the amount of the at least one diblock or triblock surfactant to monomer is at least about 3:100, wherein the at least one synthetic polyelectrolyte is selected from the group consisting of cationic copolymers with 20 mole percent or greater cationic monomer content, an anionic monomer copolymer with 20 mole percent or less anionic monomer content, polyamines, poly-diallyldimethylammonium chlorides, polyamidoamine-epichlorohydrin resins, or modified polyethyleneimines.

15. The composition of claim 14 further comprising cellulosic fiber.

16. The composition of claim 14 wherein at least one synthetic polyelectrolyte is selected from the group consisting of cationic copolymers with 20 mole percent or greater cationic monomer content; and an anionic copolymer with 20 mole percent or less anionic monomer content; and wherein the cationic or anionic copolymer comprises at least one non-ionic monomer selected from acrylamide, methacrylamide, N,N-dialkylacrylamides, N-alkylacrylamides, N-vinyl methacetamide, N-vinyl formamide, N-vinyl methyl formamide, and N-vinyl pyrrolidone.

17. The composition of claim 16 wherein the at least one synthetic polyelectrolyte is a anionic copolymer with 20 mole percent or less anionic monomer content wherein the anionic copolymer comprises at least one anionic monomer selected from the free acid or salt of: acrylic acid; methacrylic acid, maleic acid; itaconic acid; acrylamidoglycolic acid; 2-acrylamido-2-methyl-1-propanesulfonic acid; 3-allyloxy-2- hydroxy-1-propanesulfonic acid; styrenesulfonic acid; vinylsulfonic acid; vinylphosphonic acid; 2-acrylamido-2-methylpropane phosphonic acid.

18. The composition of claim 17 wherein the at least one synthetic polyelectrolyte is a anionic copolymer with 20 mole percent or less anionic monomer content wherein the anionic copolymer comprises at least one anionic monomer selected from the free acid or salt of: acrylic acid, methacrylic acid, and styrenesulfonic acid.

19. The composition of claim 16 wherein the at least one synthetic polyelectrolyte is a cationic copolymer with 20 mole percent or greater cationic monomer content wherein the cationic copolymer comprises at least one cationic monomer selected from the free base or salt of: diallyldimethylammonium halide; dialkylaminoalkyl (meth)acrylate, diethylaminoethyl (meth)acrylate, dimethyl aminopropyl (meth)acrylate, 2-hydroxydimethyl aminopropyl (meth)acrylate, aminoethyl (meth)acrylate, N₁N- dimethylaminoethylacrylamide, and acryloyloxyethyl trimethyl ammonium chloride.

20. The composition of claim 19 wherein the at least one synthetic polyelectrolyte is a cationic copolymer with 20 mole percent or greater cationic monomer content wherein the cationic copolymer comprises at least one cationic monomer selected from the free base or salt of: N.N-dimethylaminoethylacrylamide, and acryloyloxyethyl trimethyl ammonium chloride.

21. The composition of claim 14 wherein the at least one synthetic polyelectrolyte is selected from the group consisting of polyamidoamine-epihalohydrin resins; polyamines; polyimines; and derivatives of any of the preceding.

22. The composition of claim 14 wherein the at least one synthetic polyelectrolyte comprises polyamidoamine-epihalohydrin resins or derivatives thereof.