STRUCTURED LATEX POLYMER PARTICLES SUITABLE FOR USE IN THE PREPARATION OF COMPOSITE SHEETS AND PROCESS FOR PREPARING THE SAME

Abstract: A structured latex polymer particle suitable for use in the preparation of a wet-laid composite sheet having good wet-end and end-­ use properties, has a core region comprising from 10 to 40 percent of the total polymer particle volume and a shell region comprising from 60 to 90 percent of the total polymer particle volume and comprising a vinyl acid. The core region is prepared to have good end-use properties as measured by tensile and elongation and the shell region is prepared to have good wet-end properties as measured by deposition and drainage time. The subject structured latex polymer particles are advantageously employed in the preparation of composite sheets of all types to form an economical and high quality composite sheet.

Description: The preparation of wet-laid composite sheets is generally well known in the art. A composite sheet materialcan be of a cellulose, polymeric or other fibrous material product prepared by methods as outlined in U.S. Patents 4,225,383; 4,189,345 and 4,187,142. The techniques for manufacturing composite sheets can include an aqueous wet-laid method or a beater addition process for convertingfibers into a sheet or paper material. Typically, a latex is employed as a binder in the preparation of a composite sheet for two roles. The first is a wet-end role wherein the latex assists in the preparation of the composite sheet into a unitary mass. The second is an end-use role wherein the physical properties of the latex are contributed to the overall properties of the sheet. Wet-end characteristics are important to the efficient preparation of composite sheets while end-use characteristics are important to the final properties of the composite sheet. Unfortunately, a latex which has good wet-end propertiesmay not yield good end-use properties. For example, optimization of the wet-end properties of deposition time and drainage time will usually result in a final product having low end-use properties such as tensile strength. On the other hand, optimization of tensile strength can lead to poor drainage time and deposition time. Therefore, it would be desirable to prepare a single latex composition having both good wet-end and end-use properties for the preparation of wet-laid composite materials. One solution is to blend various latexes especially designed for wet-end properties and end-use properties. However, this would involve the addition of at least two latexes to the aqueous slurry for preparing a composite sheet which carries inherent problems of limited drain time and strength. Also, employing more than one latex would involve extra preparation, handling and storage. Another solution to preparing a latex having both good wet-end and end-use properties is to copolymerize various monomers together; however, this is not always satisfactory because the wet-end properties are predominantly affected by the surface chemistry of the latex polymer particles and the softness of the latex polymer particles. Thus, the mere copolymerization of various monomers would not allow one to adjust the wet-end properties independently from the end-use properties which depend largely on the hardness of the polymers. The subject invention is directed toward the use as a binder in the preparation of a wet-laid composite sheet of structured latex particles having a shell/core morphology whereby the wet-end and end-use properties are optimized. Structured latex polymer particles are generally known in the art as demonstrated by US-A-4,017,442; US-A-4,134,872; US-A-4,156,669; US-A-4,325,856; US-A-4,419,471 and US-A-4,264,678. It has now been discovered that by careful adjustment of structured latex polymer particle parameters, a binder can be selected having good wet-end and end-use properties for composite sheets. In connection with the above, US-A-4,134,872 (corresponding to FR-A-2,391,234) discloses the use of certain structured latex polymer particles as binder for pigmented paper coatings. These particles comprise per 100 parts of weight of the polymer particle:- (1) from about 50 to about 90 parts by weight of a soft interpolymer domain having a glass transition temperature equal to or less than about 25 °C and comprising, based upon the total soft interpolymer: (a) from about 30 to about 69 weight percent of a monovinylidene aromatic monomer; (b) from about 30 to about 60 weight percent of an open-chain aliphatic conjugated diene having from 4 to about 9 carbon atoms; and (c) from about 1 to about 10 weight percent of a monoethylenically unsaturated carboxylic acid; and (2) from about 10 to about 50 parts by weight of a hard resinous polymer domain having a glass transition temperature of at least about 85 °C. There is no suggestion that said particles would be of use in the aqueous wet-laid method of manufacturing composite sheets. The structured latex of the present invention has a core/shell morphology where the shell region is prepared such that the wet-end properties are optimized, i.e. good drainage time and deposition time. The core region is prepared such that the end-use properties are optimized, i.e. sufficient strength to satisfy the end-use properties desired of the composite sheet. The polymer particle is prepared such that it comprises from 10 to 40 percent of the total particle volume of a core region which is non-film forming at ambient, preferably having a T g (glass transition temperature) of from 20° to 120 °C, and from 60 to 90 percent of the total polymer particle volume of a shell region which is film forming at ambient, preferably having a T g of from 10° to -90 °C, and comprising a vinyl acid. Preferably, the vinyl acid content is less than 5 percent by total weight of the shell region. The glass transition temperature (T g ) of a polymer of copolymer is defined as the temperature at which the polymer changes from a hard glass to a rubbery mass. More particularly, the core region of the subject structured latex polymer particle comprises from 15 to 30, more preferably from 18 to 22 percent of the total polymer particle volume and the shell region comprises from 85 to 70, more preferably from 82 to 78 percent of the total polymer particle volume. More preferably, the vinyl acid content of the shell region is from 1 to 3 percent by total weight of the shell region. In addition, the shell region can comprise a strong acid group in an amount of less than 2 percent by total weight of the shell region. The structured latex polymer particles used in the subject invention provide good wet-end and end-use properties such that the composite sheet will not only be conveniently and economically prepared but will have good final physical properties. The volumes of shell and core region are important for obtaining the good wet-end and end-use properties. A larger core will affect the shell surface chemistry and thus hamper the wet-end properties, while a smaller core will diminish the effect of the core polymers such that the end-use properties are reduced. Thus, the above ranges represent an optimization for best wet-end and end-use properties. The core region is essentially surrounded by the shell region while the interface between the regions can be abrupt or gradual. This is, of course, dependent on the manner of preparation. The core region comprises a polymer which is non-film forming at ambient, preferably having a T g of greater than 20° to 120°C. More preferably, the core region polymer is chosen to provide the desired end-use characteristics for the composite sheet as defined by the physical properties, i.e., tensile and elongation. Typical core polymers comprise styrene and copolymers thereof or other polymers having similarly high T g 's, for example polyvinylidene chloride, polyvinyl chloride, polyvinyl toluene, α-methylstyrene and copolymers thereof. Copolymers of sufficient hardness can be prepared with comonomers of ethyl acrylate, butyl acrylate, butadiene or isoprene with hard monomers such as styrene, vinyl chloride, vinyl toluene, α-methyl styrene or vinylidene chloride. In one preferred embodiment, the structured latex particle has a core region comprising styrene or copolymers thereof. The shell region of the subject structured latex polymer particle essentially surrounds the aforementioned core region. The shell comprises polymer which is film-forming at ambient, preferably having a T g of from 10° to -90°C. Representative shell polymers include butadiene, vinyl acetate, acrylate and isoprene polymers or copolymers thereof provided they are still film-forming at ambient. Alternatively, plasticizers can be employed with the shell polymer or copolymer to make them film-forming at ambient. More preferably, the shell region polymer is prepared to provide good wet-end properties with respect to deposition and drain times. Two important variables for adjusting the wet-end properties are the monomer ratio and the vinyl acid content. For example, for a styrene/butadiene copolymer, the rate of water removal is improved by increasing the proportion of butadiene and decreasing the amount of vinyl acid in the copolymer. The copolymer ratios are preferably adjusted to maintain a T g as defined above for the shell region. The vinyl acid content of the shell region is important to optimize the rate of drainage. Generally, a vinyl acid content of less than 5 percent by total weight of the shell polymer is sufficient to provide satisfactory drain rates. More preferably, a vinyl acid content of from 1 to 3 percent by total weight of the shell polymer is employed. Representative vinyl acids include itaconic acid, fumaric acid, maleic acid, acrylic acid, methacrylic acid or other carboxylic acids copolymerizable with the shell monomers. In addition, a minor amount of a strong acid group can be included in the shell polymer to improve the wet-end properties. The strong acid component or group is understood to have an effect on the deposition time of a wet-laid composite. A minor amount thereof reduces the deposition time. A minor amount is in the range of less than 2 percent, preferably less than 1 percent by total weight of the polymer comprising the shell region. An increase over this amount lengthens the deposition time. Generally, this group can be provided by means of the free radical initiator employed in the polymerization. Typical initiators are, for example, ammonium persulfate, sodium persulfate, or strong peroxyacids. The manner in which the structured latex particles of this invention are prepared is not particularly critical, so long as the hereinbefore described compositional parameters are satisfied. Thus, for example, the latex can be prepared by encapsulating dispersed polymer particles of a pre-existing core polymer or copolymer with a polymeric shell portion. The latexes can also be prepared by a stage addition of monomers, i.e., each monomer feed individually added and polymerized to form one region of the polymer particle prior to the addition of the remaining monomer feeds to form the other region of the polymer particle. In yet another aspect, the structured polymeric particle can be prepared by a continuous feed process. The continuous feed process involves the incremental addition of the monomer feeds such that, as one monomer feed is reduced, the subsequent monomer feed is increased to provide a smooth transition between various monomer feeds. The polymerization process can be conducted pursuant to conventional emulsion polymerization techniques. Thus, for example, the monomers to be employed for the particular region to be prepared are typically dispersed with agitation sufficient to emulsify the mixture in an aqueous medium which may contain known emulsifying agents (i.e., surfactants) as well as other ingredients conventionally employed in the art as polymerization aids (e.g., conventional chain transfer agents, etc.). Such monomers are then subjected to polymerization with the aid of a conventional source for generating free radicals, such as, for example, conventional free radical polymerization catalyst and activating radiation. Optionally, conventional seeding procedures can be employed in the first stage polymerization to aid in the control of polymerization and to achieve the desired average particle size and particle size distribution for the dispersed copolymer particles. Also, as has been noted, conventional chain transfer agents can be employed in the practice of the present invention and, indeed, in polymerization stages employing aliphatic conjugated dienes if it is preferable to do so. Examples of such conventional chain transfer agents include bromoform, carbon tetrachloride and organic mercaptans (e.g., dodecylmercaptans). Conventional amounts, in general, of from 0.1 to 10 weight percent based on total monomer charge of such chain transfer agents are typically employed. In addition, it is sometimes desirable to have small amounts of certain known additives incorporated into the latex. Typical examples of such additives are surfactants, bacteriocides, anti-foamers and antioxidants. Such additives can be incorporated into the latex of the invention in a conventional manner and at any convenient point in the preparation of such latexes. The following examples are provided to illustrate the present invention and are not intended to limit the scope thereof. All amounts are in parts per one hundred parts total polymer, unless otherwise indicated. Example I A series of latexes was prepared for use in the preparation of a composite sheet. The polymer composition and morphology of each were as follows. Comparative Sample A was a homogeneous latex of 61 parts styrene, 38 parts butadiene and 1 part itaconic acid. This composition was employed because it has good deposition and drain time when employed in the preparation of a composite sheet. Unfortunately, the Control Latex did not exhibit good tensile properties which was expected because the latex was designed for good wet-end properties. The composition of Comparative Sample A was modified by adding 4 parts of styrene in an attempt to increase tensile strength. This modified latex was identified as Comparative Sample B. In addition, another comparative sample was prepared by adding 4 parts of styrene to and removing 0.25 parts of the vinyl acid component from the Comparative Sample A composition in an attempt to balance the wet-end and end-use properties. This was identified as Comparative Sample C. Comparative Samples A, B and C were all homogeneous polymer latexes in morphology. Finally, a structured latex particle of the subject invention (Sample 1) was prepared having a styrene polymer core region and a shell region consisting of the Comparative Sample A composition. Thus, the core region was designed for good tensile and the shell region was designed for good deposition and drain time properties. The core region was prepared such that it comprised 19 percent of the total polymer particle by volume and the shell region was overpolymerized on the core and comprised the remaining volume. Each of the latexes was employed in the preparation of a composite sheet and the wet-end and end-use properties for each was measured and are shown below in Table I. Table I indicates that modifications to the Comparative Sample A which had very good wet-end properties (drain time) did not improve the end-use properties (tensile and stiffness) without a corresponding loss of wet-end properties. For instance, increasing the styrene level of Comparative Sample B dramatically increased drain time while reducing the vinyl acid in Comparative Sample C brought the drain time back down. However, this had a poor effect on tensile and stiffness. Only Sample 1 provided good wet-end and end-use properties. This demonstrates that the particular composition and morphology of Sample 1 takes advantage of the good wet-end properties of the shell region and the high tensile contribution of the core region. Example II Structured latex particles having various shell/core ratios were prepared to determine the effect of core size on maintaining good wet-end and end-use properties. Comparative Sample D was also prepared for comparison purposes having 61 parts styrene, 38 parts butadiene and 1 part itaconic acid. This Comparative Sample D was similar to Comparative Sample A of Example I and exhibited good wet-end properties. The structured latex polymer particles were prepared with styrene core regions of varying percentages (19, 24 and 29 percent) of the total volume of the particle and the remainder of the particle, the shell region, comprised a composition consisting essentially of Comparative Sample A. The latexes were used to prepare composite sheets and the wet-end and end-use properties of the sheets were measured and are recorded below in Table II. Table II demonstrates that increasing the core size had an effect on the wet-end properties of the latex in that the drain time was lengthened. However 30 seconds is not completely undesirable in view of the very good end-use properties achieved. Meanwhile, the two smaller core volumes gave better drain time and still maintained good end-use properties. Thus, Example II demonstrates that a single latex can be prepared having both good wet-end and end-use properties when the basic structural parameters, as outlined above, are followed. Example II also demonstrates the criticality of the core/shell volumes in balancing the wet-end and end-use properties.

Claims: The use as a binder in the preparation of a wet-laid composite sheet of structured latex polymer particles comprising:- (a) from 10 to 40 percent of the total polymer particle volume of a core region which is non-film forming at ambient; and (b) from 60 to 90 percent of the total polymer particle volume of a shell region which is film forming at ambient and comprising a vinyl acid. A use as claimed in Claim 1, wherein said core region has a T g of from 20 to 120 °C. A use as claimed in Claim 1 or Claim 2, wherein said shell region has a T g of from 10 to -90 °C. A use as claimed in any one of the preceding claims, wherein said vinyl acid component is present in an amount of less than 5 percent by total weight of said shell region. A use as claimed in any one of the preceding claims, wherein said vinyl acid content is from 1 to 3 percent by total weight of said shell region. A use as claimed in any one of the preceding claims, wherein said core region comprises from 15 to 30 percent of the total polymer particle volume and said shell region comprises from 70 to 85 percent of the total polymer particle volume. A use as claimed in Claim 6, wherein said core region comprises from 18 to 22 percent of the total polymer particle volume and said shell region comprises from 82 to 78 percent of the total polymer particle volume. A use as claimed in any one of the preceding claims, wherein said shell region additionally comprises a strong acid group in an amount of less than 2 percent by total weight of said shell region. A use as claimed in any of the preceding claims, wherein said core region comprises styrene or copolymers thereof. A use as claimed in any one of the preceding claims, wherein said shell region comprises butadiene or copolymers thereof. A method of preparing a composite sheet by an aqueous wet-laid process employing latex polymer particles as a binder, characterised in that said particles comprise:- (a) from 10 to 40 percent of the total polymer particle volume of a core region which is non-film forming at ambient; and (b) from 60 to 90 percent of the total polymer particle volume of a shell region which is film forming at ambient and comprising a vinyl acid. A method as claimed in Claim 11, wherein the structured latex polymer particles are as claimed in any one of Claims 1 to 10.

Inventors: ASH, MARY LYNNE, FRICK, CARL H., LEE, DO IK
Applicants: THE DOW CHEMICAL COMPANY
Application year: 1987
Main classification: C08F257
IPC codes: C08F259, C08L51, C08L21, C08L9, C08F257, C08F291