Extruded fragrance-containing polyvinyl alcohol and use thereof

Abstract: Described is a composition of matter particularly useful in fabricating toilet rim blocks consisting of: (a) extruded polyvinyl alcohol or partially hydrolyzed polyvinyl acetate with the maximum mole ratio of acetyl moiety:hydroxyl moiety being about 3:1 having a number average molecular weight of from about 15,000 up to about 68,000 containing from 0 up to about 13% by weight of an added polar plasticizer; (b) from about 1 up to about 20% by weight of a compatible fragrance contained within the polyvinyl alcohol or partially hydrolyzed polyvinyl acetate; (c) from 0 up to about 20% by weight of a "foaming agent" which is a first surfactant and which can be a detergent, contained within the polyvinyl alcohol or partially hydrolyzed polyvinyl acetate; (d) from 0 up to about 20% by weight of a hydrophobic silica contained within the polyvinyl alcohol or partially hydrolyzed polyvinyl acetate; (e) from 0 up to about 20% by weight of at least one second surfactant in addition to the "foaming agent"; (f) from 0 up to about 5% by weight of a water-soluble dye; and (g) from 0 up to about 4% by weight of a "foam booster". Also described are processes for preparing such compositions of matter and such toilet rim blocks. When used for the fabrication of toilet rim blocks, the maximum mole ratio of acetyl moiety:hydroxyl moiety is about 1:3.

Description: The present invention relates to a composition of matter consisting of: (a) extruded polyvinyl alcohol or partially hydrolyzed polyvinyl acetate with the maximum mole ratio of the acetyl moiety:hydroxyl moiety being about 3:1, having a number average molecular weight of from about 15,000 up to about 68,000 containing from 0 up to about 15% by weight of an added polar plasticizer; (b) from about 1 up to about 20% by weight of a compatible fragrance contained within the polyvinyl alcohol or the partially hydrolyzed polyvinyl acetate; (c) from 0 up to about 20% by weight of a "foaming agent" which is a first surfactant and which can be a detergent, contained within the polyvinyl alcohol or partially hydrolyzed polyvinyl acetate; (d) from 0 up to about 20% by weight of hydrophobic silica contained within the polyvinyl alcohol or the partially hydrolyzed polyvinyl acetate; (e) from 0 up to about 20% by weight of at least one second surfactant in addition to the aforementioned "foaming agent"; (f) from 0 up to about 5% of a water-soluble dye; and (g) from 0 up to about 4% of a "foam booster". The invention also contemplates toilet rim blocks having the following dimension ranges: 6.35 - 19.05 mm (1/4''-3/4'') thickness; 6.35 - 101.6 mm (1/4''-4'') width; and 6.35 - 127 mm (1/4''-5'') length. WO-A-92/03532 (Jeyes Limited) discloses a process for the production of lavatory cleaning blocks by extruding a mixture of ingredients, the mixture to be extruded comprising, based on the total weight of the mixture, (i) from 5 to 85% by weight of one or more surface active agents and (ii) from 0.5 to 40% by weight of one or more rheological control agents. According to the present invention, there is provided a composition of matter consisting of: (a) polyvinyl alcohol or partially hydrolyzed polyvinyl acetate with a maximum mole ratio of acetyl moiety:hydroxyl moiety being 3:1, having a number average molecular weight of from 15,000 up to 68,000 containing from 0 up to 15% by weight of an added polar plasticizer; (b) from 1 up to 20% by weight of compatible fragrance contained within the polyvinyl alcohol or partially hydrolyzed polyvinyl acetate; (c) from 0 up to 20% by weight of foaming agent contained within the polyvinyl alcohol or partially hydrolyzed polyvinyl acetate; (d) from 0 up to 20% by weight of hydrophobic silica contained within the polyvinyl alcohol or partially hydrolyzed polyvinyl acetate; (e) from 0 up to 20% by weight of at least one surfactant in addition to the said foaming agent; (f) from 0 up to 5% by weight of water-soluble dye; and (g) from 0 up to 4% by weight of foam booster, wherein the polyvinyl alcohol or partially hydrolyzed polyvinyl acetate is extruded. The toilet rim blocks fabricated from such compositions of matter are those where the preferred maximum mole ratio of acetyl moiety:hydroxyl moiety is about 3:1. It should be noted that partially hydrolyzed polyvinyl acetate having a mole ratio of acetyl moiety:hydroxyl moiety in the range of from 3:1 up to 1:3 is useful in toilet rim blocks, but the majority of the toilet rim block must be fabricated from either extruded polyvinyl alcohol or partially hydrolyzed polyvinyl acetate with the maximum mole ratio of acetyl moiety:hydroxyl moiety being about 3:1. Partially hydrolyzed polyvinyl acetate with a range of mole ratios of acetyl moiety:hydroxyl moiety between about 3:1 and about 1:3 are water-swellable; not water-soluble whereas partially hydrolyzed polyvinyl acetate with a maximum mole ratio of acetyl moiety:hydroxyl moiety of about 1:3 are water-soluble at ambient temperatures, e.g., 25-35°C. The invention also contemplates a process for preparing the aforementioned composition of matter as well as the toilet rim blocks. In practicing the invention, the polyvinyl alcohol or partially hydrolyzed polyvinyl acetate is prepared by means of any of Examples I-XIV of U.S. Letters Patent 5,051,222 issued on September 24, 1991. Thus, the polyvinyl alcohol or the partially hydrolyzed polyvinyl acetate is prepared first by polymerizing (via a "free radical" polymerization mechanism) vinyl acetate having the formula: according to the reaction: thereby forming a polyvinyl acetate wherein x + y are such that the number average molecular weight of the final product is between 15,000 and 68,000. The resulting polyvinyl acetate having the formula: is then hydrolyzed first to form a partially hydrolyzed polyvinyl alcohol according to the reaction: or a mixture of polyvinyl alcohol and partially hydrolyzed polyvinyl acetate according to the reaction: If desired, the partially hydrolyzed polyvinyl acetate may be further hydrolyzed to form polyvinyl alcohol without any acetyl groups present according to the reaction: In any event, the ratio of acetyl moieties to hydroxyl moieties is less than about 3:1 in the structure: and x and y are defined whereby x + y gives rise to a polymer that has a number average molecular weight of between about 15,000 and 68,000. The amount of plasticizer contained in the resulting polyvinyl alcohol or partially hydrolyzed polyvinyl acetate may vary from about 0 up to 13% by weight of the polyvinyl alcohol or partially hydrolyzed polyvinyl acetate. This presupposes that the polyvinyl alcohol or partially hydrolyzed polyvinyl acetate commercially available already contains approximately 2% by weight plasticizer. Thus, total plasticizer range varies from about 2% up to about 15%. The plasticizer is a polar plasticizer having a solubility parameter, δ t greater than about 20 MPa ½ (megapascals ½ ) (the square root of cohesive energy density) on the Hildebrand parameter scale (Reference: CRC Handbook of Solubility Parameters and Other Cohesion Parameters; Allen F.M. Barton; published 1983 by the CRC Press, Inc. of Boca Raton, Florida). The solubility parameter, δ t is in fact the root mean square sum of the three parameters: δ D , δ P , δ H according to the equation: δ t = δ 2 D + δ 2 P + δ 2 H wherein the parameter δ D is a measure of the Van der Waal's forces; δ P is a measure of the polar forces and δ H is a measure of the hydrogen bonding effect. Examples of such polar plasticizers are: glycerine; triethanolamine; ethylene glycol; propylene glycol; diethylene glycol; dipropylene glycol; diethanolamine; and methyldiethylamine. As stated above from about 1 up to about 20% by weight of a compatible fragrance may be contained within the polyvinyl alcohol or the partially hydrolyzed polyvinyl acetate. The compatible fragrance is added to the extruder at a point downstream from the addition of the polyvinyl alcohol or partially hydrolyzed polyvinyl acetate which is premixed with plasticizer or already contains plasticizer therein. When from about 1% up to about 10% by weight of the composition of compatible fragrance is added to the extruder, it is not necessary to add to the compatible fragrance hydrophobic silica. When the amount of compatible fragrance is from about 5 up to about 10% by weight of the composition, it is preferred, however, to add hydrophobic silica to the compatible fragrance prior to feeding the mixture thereof to the extruder. When the amount of compatible fragrance desired to be in the polyvinyl alcohol or partially hydrolyzed polyvinyl acetate is from 10% up to about 20% by weight of the composition of compatible fragrance, then although in most cases, it is necessary to add hydrophobic silica to the perfume composition in order to obtain a useful toilet rim block, use of certain polyvinyl alcohol materials such as GOHSENOL® KZ-06 described in detail, infra, have been surprisingly found not to require the use of silica (reference is made to Example III, infra). However, when silica is needed, the weight ratio of hydrophobic silica:compatible fragrance when the compatible fragrance is present in an amount of from about 10 up to about 20% is from about 1:1 silica:compatible fragrance up to about 1:2 silica:compatible fragrance. An example of hydrophobic silica useful in the practice of the invention is SIPERNAT® D17 silica. The polyvinyl alcohol or the partially hydrolyzed polyvinyl acetate may be premixed with other additives in addition to the plasticizers, for example, color additives, for example, Acid Blue No. 19 manufactured by Sandoz Pharmaceutical Corporation of Hanover, New Jersey; or antibacterial agents or both. Examples of the polyvinyl alcohol and partially hydrolyzed polyvinyl acetate useful in the practice of the invention are: AIRVOL® 205 (manufactured by Air Products & Chemicals, Inc. of Allentown, Pennsylvania) Low Viscosity unplasticized polyvinyl alcohol Molecular Weight: 15,000-27,000 Melting Point 230°C 88% Hydrolyzed VINEX® 2019 (manufactured by Air Products & Chemicals, Inc. of Allentown, Pennsylvania) Low Viscosity plasticized polyvinyl alcohol Molecular Weight: 15,000-27,000 Melting Point 170°C 88% Hydrolyzed VINEX® 2144 (manufactured by Air Products & Chemicals, Inc. of Allentown, Pennsylvania) Medium Viscosity plasticized polyvinyl alcohol Molecular Weight: 44,000-65,000 Melting Point 205°C 88% Hydrolyzed VINEX® 1025 (manufactured by Air Products & Chemicals, Inc. of Allentown, Pennsylvania) Low Viscosity plasticized polyvinyl alcohol Molecular Weight: 15,000-27,000 Melting Point 170°C 99% Hydrolyzed VINEX® 2025 (manufactured by Air Products & Chemicals, Inc. of Allentown, Pennsylvania) Low Viscosity plasticized polyvinyl alcohol Molecular Weight: 25,000-45,000 Melting Point 192°C 88% Hydrolyzed GOHSEFIMER® 5407 (manufactured by Nippon Gohsei K.K. of Osaka, Japan) Molecular Weight: 23,600 Melting Point 100°C 30-28% Hydrolyzed GOHSEFIMER® LL02 (manufactured by Nippon Gohsei K.K. of Osaka, Japan) Molecular Weight: 17,700 Melting Point 100°C 41-51% Hydrolyzed MOWIOL® 1074 (manufactured by American Hoechst Corp. of Parsippany, New Jersey) Molecular Weight: 15,000-27,000 Melting Point 190°C 74% Hydrolyzed Furthermore, additional polyvinyl alcohol-containing substances including polyvinyl alcohol and partially hydrolyzed polyvinyl acetate useful in the practice of the invention are as follows: Name Viscosity Range (Centipoises) Percent Hydrolysis ELVANOL® 51-05 (manufactured by The Du Pont Company, Polymer Products Department, Wilmington, Delaware 19898) 5-6 87-89 ELVANOL® 52-22 (manufactured by The Du Pont Company, Polymer Products Department, Wilmington, Delaware 19898) 21-26 87-89 ELVANOL® 50-42 (manufactured by The Du Pont Company, Polymer Products Department, Wilmington, Delaware 19898) 44-50 87-89 ELVANOL® 85-82 (manufactured by The Du Pont Company, Polymer Products Department, Wilmington, Delaware 19898) 24-32 99.0-99.8 ELVANOL® 75-15 (manufactured by The Du Pont Company, Polymer Products Department, Wilmington, Delaware 19898) 12-15 98.0-99.8 ELVANOL® T-25 (manufactured by The Du Pont Company, Polymer Products Department, Wilmington, Delaware 19898) 24-32 99.0-99.8 ELVANOL® T-66 (manufactured by The Du Pont Company, Polymer Products Department, Wilmington, Delaware 19898) 12-15 99.0-99.8 ELVANOL® 90-50 (manufactured by The Du Pont Company, Polymer Products Department, Wilmington, Delaware 19898) 12-15 99.0-99.8 ALCOTEX® 72.5 (manufactured by the Harlow Chemical Co. Ltd. of Templefields, Harlow, Essex, England CM20 2BH) 5.6-6.6 71.5-73.5 ALCOTEX® 78 (manufactured by the Harlow Chemical Co. Ltd. of Templefields, Harlow, Essex, England CM20 2BH) 5.5-6.5 76.0-79.0 ALCOTEX® B72 (manufactured by the Harlow Chemical Co. Ltd. of Templefields, Harlow, Essex, England CM20 2BH) 4.8-5.8 72.0-75.0 ALCOTEX® F80/40 (manufactured by the Harlow Chemical Co. Ltd. of Templefields, Harlow, Essex, England CM20 2BH) 38-42 78.8-82.1 ALCOTEX® F88/4 (manufactured by the Harlow Chemical Co. Ltd. of Templefields, Harlow, Essex, England CM20 2BH) 3.5-4.5 86.7-88.7 ALCOTEX® F88/26 (manufactured by the Harlow Chemical Co. Ltd. of Templefields, Harlow, Essex, England CM20 2BH) 24.5-27.5 86.7-88.7 ALCOTEX® F88/40 (manufactured by the Harlow Chemical Co. Ltd. of Templefields, Harlow, Essex, England CM20 2BH) 38.0-42.0 86.7-88.7 ALCOTEX® F88/47 (manufactured by the Harlow Chemical Co. Ltd. of Templefields, Harlow, Essex, England CM20 2BH) 45.0-49.0 86.7-88.7 MOWIOL® 10-74 (manufactured by American Hoechst Celanese Corp., Building 5200, 77 Center Drive, P.O. Box 1026, Charlotte, North Carolina 28201-1026) 8.5-11.5 71.6-75.2 MOWIOL® 15-79 (manufactured by American Hoechst Celanese Corp., Building 5200, 77 Center Drive, P.O. Box 1026, Charlotte, North Carolina 28201-1026) 13-17 79.3-83.7 MOWIOL® 4-80 (manufactured by American Hoechst Celanese Corp., Building 5200, 77 Center Drive, P.O. Box 1026, Charlotte, North Carolina 28201-1026) 3.5-4.5 78.8-82.0 MOWIOL® 3-83 (manufactured by American Hoechst Celanese Corp., Building 5200, 77 Center Drive, P.O. Box 1026, Charlotte, North Carolina 28201-1026) 2.5-3.5 80.4-84.8 MOWIOL® 18-88 (manufactured by American Hoechst Celanese Corp., Building 5200, 77 Center Drive, P.O. Box 1026, Charlotte, North Carolina 28201-1026) 16.5-19.5 86.7-88.7 MOWIOL® 40-88 (manufactured by American Hoechst Celanese Corp., Building 5200, 77 Center Drive, P.O. Box 1026, Charlotte, North Carolina 28201-1026) 38-42 86.7-88.7 MOWIOL® 3-98 (manufactured by American Hoechst Celanese Corp., Building 5200, 77 Center Drive, P.O. Box 1026, Charlotte, North Carolina 28201-1026) 3.0-4.0 98.0-98.8 MOWIOL® 6-98 (manufactured by American Hoechst Celanese Corp., Building 5200, 77 Center Drive, P.O. Box 1026, Charlotte, North Carolina 28201-1026) 5-7 98.0-98.8 MOWIOL® 66-100 (manufactured by American Hoechst Celanese Corp., Building 5200, 77 Center Drive, P.O. Box 1026, Charlotte, North Carolina 28201-1026) 62-70 98.8-100.0 GOHSENOL® NK-05 (manufactured by Nippon Gohsei K.K. (The Nippon Synthetic Chemical Industry Co., Ltd.) of No. 9-6, Nozaki-Cho, Kita-Ku, Osaka, 530 Japan) 4.5-5.5 71.0-75.0 GOHSENOL® A-300 (manufactured by Nippon Gohsei K.K. (The Nippon Synthetic Chemical Industry Co., Ltd.) of No. 9-6, Nozaki-Cho, Kita-Ku, Osaka, 530 Japan) 25-30 97-98.5 GOHSENOL® AH-22 (manufactured by Nippon Gohsei K.K. (The Nippon Synthetic Chemical Industry Co., Ltd.) of No. 9-6, Nozaki-Cho, Kita-Ku, Osaka, 530 Japan) 50-58 97.7-98.4 GOHSENOL® C-500 (manufactured by Nippon Gohsei K.K. (The Nippon Synthetic Chemical Industry Co., Ltd.) of No. 9-6, Nozaki-Cho, Kita-Ku, Osaka, 530 Japan) 25-27 96-97 GOHSENOL® GH-20 (manufactured by Nippon Gohsei K.K. (The Nippon Synthetic Chemical Industry Co., Ltd.) of No. 9-6, Nozaki-Cho, Kita-Ku, Osaka, 530 Japan) 40-46 87-89 GOHSENOL® GL-03 (manufactured by Nippon Gohsei K.K. (The Nippon Synthetic Chemical Industry Co., Ltd.) of No. 9-6, Nozaki-Cho, Kita-Ku, Osaka, 530 Japan) 3.0-3.7 87-89 GOHSENOL® GM-14L (manufactured by Nippon Gohsei K.K. (The Nippon Synthetic Chemical Industry Co., Ltd.) of No. 9-6, Nozaki-Cho, Kita-Ku, Osaka, 530 Japan) 16-20 87-89 GOHSENOL® KA-20 (manufactured by Nippon Gohsei K.K. (The Nippon Synthetic Chemical Industry Co., Ltd.) of No. 9-6, Nozaki-Cho, Kita-Ku, Osaka, 530 Japan) 5-7 78-82 GOHSENOL® KA-500 (manufactured by Nippon Gohsei K.K. (The Nippon Synthetic Chemical Industry Co., Ltd.) of No. 9-6, Nozaki-Cho, Kita-Ku, Osaka, 530 Japan) 4.5-7.5 70-74 GOHSENOL® KH-20 (manufactured by Nippon Gohsei K.K. (The Nippon Synthetic Chemical Industry Co., Ltd.) of No. 9-6, Nozaki-Cho, Kita-Ku, Osaka, 530 Japan) 44-52 78.5-81.5 GOHSENOL® KP-06 (manufactured by Nippon Gohsei K.K. (The Nippon Synthetic Chemical Industry Co., Ltd.) of No. 9-6, Nozaki-Cho, Kita-Ku, Osaka, 530 Japan) 5-7 71-75 GOHSENOL® N-300 (manufactured by Nippon Gohsei K.K. (The Nippon Synthetic Chemical Industry Co., Ltd.) of No. 9-6, Nozaki-Cho, Kita-Ku, Osaka, 530 Japan) 25-30 98-99 GOHSENOL® NH-26 (manufactured by Nippon Gohsei K.K. (The Nippon Synthetic Chemical Industry Co., Ltd.) of No. 9-6, Nozaki-Cho, Kita-Ku, Osaka, 530 Japan) 60-68 99.4-100 GOHSENOL® NM-11Q (manufactured by Nippon Gohsei K.K. (The Nippon Synthetic Chemical Industry Co., Ltd.) of No. 9-6, Nozaki-Cho, Kita-Ku, Osaka, 530 Japan) 13-16 99-100 GOHSENOL® KZ-06 (manufactured by Nippon Gohsei K.K. (The Nippon Synthetic Chemical Industry Co., Ltd.) of No. 9-6, Nozaki-Cho, Kita-Ku, Osaka, 530 Japan); molecular weight = 42,200; melting point = 140-160°C 69.0-72.5 Since the VINEX® materials are "preplasticized", no additional plasticizer need be added, however, plasticizer can be added up to an amount of about 13% by weight. On the other hand, the AIRVOL® 205 may be combined with additional plasticizer, for example, glycerine or any of the plasticizers set forth, supra. However, AIRVOL® 205 and polyvinyl alcohol materials similar thereto need not be plasticized to be useful for the purposes of the invention. The following materials are both foaming agents and are also detergents useful in the practice of the invention: STANDAPOL® 7023 (an anhydrous blend of Cocamide DEA and DEA-Myreth Sulfate detergent); WITCONATE® AOK (manufactured by Witco Chemical Comapany (solid anionic alpha sulfonate)); and WITCONATE® 90 FLAKE (manufactured by Witco Chemical Company (solid anionic alpha sulfonate)). The following materials are useful as secondary detergents but cannot be depended on for their foaming properties: PLURONIC® F88 (a block copolymer of ethylene oxide and propylene oxide manufactured by BASF); PLURONIC® F77 (a block copolymer of ethylene oxide and propylene oxide manufactured by BASF); and WITCONATE® 90. Additional examples of detergents which are also foaming agents are alkyl benzene sulfonates such as n-octyl benzene sulfonate (sodium salt). An example of a foam booster (which is not a detergent) is: INCROMIDE® CA (Cocamide DEA) manufactured by Croda, Inc.. Another example of a foam booster is a mixture of 1:1 Neodol 45-13:INCROMIDE® CA (Neodol 45-13 being a C 14 -C 15 linear primary alcohol ethoxylate) (manufactured by the Shell Chemical Company). Another example of a foaming agent that is also a detergent that is preferred for the practice of the invention is sodium lauryl sulfate. In carrying out the process of the invention, polyvinyl alcohol or partially hydrolyzed polyvinyl alcohol is combined with plasticizer and added to an extruder, compatible fragrance or compatible fragrance combined with hydrophobic silica is simultaneously fed into the extruder downstream from the addition of the polyvinyl alcohol or partially hydrolyzed polyvinyl acetate/plasticizer mix, and liquid detergent is optionally fed into the extruder upstream from the feeding of the compatible fragrance and downstream from the feeding of the polyvinyl alcohol/plasticizer mix or partially hydrolyzed polyvinyl acetate/plasticizer mix. The extruded tow is cooled (without being immersed in water) and then pelletized. The pelletized product may be marketed as is or it may be formed into toilet rim blocks, for example. In practicing the process of this invention to form a particulate polyvinyl alcohol/compatible fragrance composition or particulate partially hydrolyzed polyvinyl acetate/compatible fragrance composition, single screw or double screw extruders can be utilized. Some of the extruders that can be used are shown at pages 2416-267 and 332-349 of the Modern Plastics Encyclopedia 1982-1983. More specifically, examples of extruders which are desirable for carrying out the process of the invention include: 1. The Krauss-Maffei twin screw extruder manufactured by the Krauss-Maffei Corporation/Extruder Division, 3629 West 30th Street, Wichita, Kansas 67277; 2. The CRT ("Counter-Rotating Tangential") Twin Screw Extruder manufactured by Welding Engineers, Inc., King of Prussia, Pennsylvania 19406; 3. The Leistritz Twin Screw Dispersion Compounder manufactured by the American Leistritz Extruder Corporation, 198 U.S. Route 206 South, Sommerville, New Jersey 08876; 4. The ZSK Twin Screw Co-Rotating Extruder manufactured by the Werner & Pfeiderer Corporation, 663 East Crescent Avenue, Ramsey, New Jersey 07446; 5. The MPC/V Baker Perkins Twin Screw Extruder manufactured by the Baker Perkins Inc. Chemical Machinery Division, Saginaw, Michigan 48601; 6. The Berstorff twin screw or foam extrusion equipment manufactured by Berstorff Corporation, P.O. Box 240357, 8200-A Arrowridge Boulevard, Charlotte, North Carolina 28224; and 7. The Theysohn TSK Co-Rotating Extruder manufactured by the Theysohn Corporation of 2 Corporate Drive, Suite F, Radford, Virginia 24141. Generally, in certain preferred embodiments, twin screw extruders such as those set forth above are used to mix the polyvinyl alcohol or partially hydrolyzed polyvinyl acetate with the perfume, silica (if needed), plasticizer, colorant and detergent (if needed) as well as foaming agent (if needed). Such extruders comprise an inner shaft member to which an outer screw member is affixed coaxially. In a double-screw machine, there are two shafts, each of which drives an outer screw member. The screws are intermeshed so that they subject the material being extruded to high-shear conditions, which contribute to dispersing the silica/perfume within the polyvinyl alcohol or partially hydrolyzed polyvinyl alcohol polymers. These extruders also comprise an outer barrel member which encloses the screw or screws. Such extruders over their length can be fitted with different screws on the shaft and with different barrels surrounding the screws. Thus, over the length of the extruder various types and amounts of shear action can be used. The variation is carried out along the length of the extruder so that as various ingredients are initially introduced into the interior of the extruder, as the ingredients are initially mixed, and as the components become more highly mixed or dispersed, the mixing and the shear action can be varied to obtain the particle size and amount of various materials to be dispersed entities in the matrix. After the extrusion, the extrudate is usually cooled. This can be accomplished by suitable means such as belts, blowers and the like. The cooled extrudate comprises a matrix with dispersed entities. This extrudate is then comminuted to provide the finished particles by means known in the art. In addition to the use of a single extruder, it will be apparent from this description that a series of extruders can be used to form extrudate. Thus, a perfume can be added in a small percentage in a first extruder followed by additional perfume and silica in a second extruder. Furthermore, detergent and compatible fragrance can be added in a first extruder followed by detergent, silica and perfume in a second extruder with the detergent being added separately from the silica and perfume. The extrusion and subsequent comminution enable the facile control of the size of the dispersed entities and the overall size of the particulate fragrancing polymers. This, in turn, provides control over the ultimate properties of the particulate fragranced polymers as taught herein. EXAMPLE I The following "compatible" rose fragrance formulation is used in carrying out Example II below. Ingredient Parts by Weight Geraniol ex Palmarosa Oil 0.5 Nerol 2.0 L-Citronellol 3.1 D-Citronellol 3.8 Beta Phenyl Ethyl Alcohol 2.0 o-(2-hydroxy-1-ethyl)-methylbenzene 4.0 5-phenyl-3-methyl-1-pentanol 5.6 It should be noted that each of the ingredients of this example is a highly polar primary organic alcohol. Thus, preferably, the "compatible fragrances" of the invention are mixtures of highly polar primary organic alcohols. EXAMPLE II VINEX® 2144 is fed at 17.24 Kg (38 pounds) per hour into a 30 mm Werner and Pfleiderer twin screw corotating twin screw extruder. The VINEX® 2144 (produced by Air Products & Chemicals, Inc. of Allentown, Pennsylvania) is melted in the first stage of the screws and fragrance oil is then injected at 0.91 Kg (2 pounds) per hour to yield 95% polyvinyl alcohol-5% fragrance. The melt exits the extruder as two strands are dropped onto a 6.1 m (20') long Sandvik water cooled belt to solidify the melt. The strands are then pelletized with a Conair pelletizer. The Summary of the Extrusion Conditions is set forth in the following Table I: RPM 350 % Torque 45-60 Rate Kg per hour (pounds per hour) 18.14 (40) Melt Temperature 103-89°C (219°F) Set/Actual Barrel 1 Temperature 87.78/87.78°C (190/190°F) Set/Actual Barrel 2 Temperature 93.33/93.33°C (200/200°F) Set/Actual Barrel 3 Temperature 98.89/98.89°C (210/210°F) Set/Actual Barrel 4 Temperature 98.89/98.33°C (210/209°F) Set/Actual Barrel 5 Temperature 98.89/98.89°C (210/210°F) Set/Actual Die Temperature 98.89/98.33°C (210/209°F) Melt Pressure Kg/cm 2 (psi) 22.5 (320) These pellets were extruded into 152.4 mm (6'') width-by 0.076 mm (0.003'') thick cast film with a 19.05 mm (0.75'') diameter Haake single screw extruder. Various molded shapes were made with a 40,640 Kg (40 ton) Nissei injection molding machine. 76.2 mm x 127 mm x 3.175 mm (3'' x 5'' x 0.125'') cards were made on the injection molding machine with the following conditions: RPM 250 Secondary Pressure 0.039 Kg/cm 2 (0.5 600 psi) Shot Size 4.5 Injection Speed 21.0 Rotation Speed 34.0 Nozzle Temperature 193.33°C (380°F) Front Temperature 187.78°C (370°F) Middle Temperature 182.22°C (360°F) Rear Temperature 176.67°C (350°F) Eject 1.1 Decompress 0.2 Cycle Start 0.5 Injection Time (seconds) 12 Curing Time (seconds) 13 Clamp Pressure 140.6 Kg/cm 2 (2,000 psi) Pump Pressure 140.6 Kg/cm 2 (2,000 psi) EXAMPLE III GOHSENOL® KZ-06 is fed at either 26.3, 30.84 or 33.11 Kg (58, 68 or 73 pounds) per hour into a 30 mm Werner and Pfleiderer twin screw corotating twin screw extruder. The GOHSENOL® KZ-06 (produced by Nippon Gohsei K.K. of Osaka, Japan) is melted in the first stage of the screws and fragrance oil (of Example I) is then injected at 9.07 Kg (20 pounds) per hour simultaneously with the injection of 9.07, 4.54 or 2.27 Kg (20, 10 or 5 pounds) per hour of WITCONATE® 90 and 0.91 Kg (2 pounds) per hour of foam booster. The melt exits the extruder as two strands which are dropped onto a 6.1 m (20') long Sandvik water cooled belt to solidify the melt. The strands are then pelletized with a Conair pelletizer. The following Table IV sets forth the materials added to the extruder at GOHSENOL® KZ-06 rates of 26.3, 30.84 or 33.11 Kg (58, 68 and 73 pounds) per hour: Ingredients Parts By Weight Example IIIA Example IIIB Example IIIC GOHSENOL® KZ-06 58 68 73 WITCONATE® 90 20 10 5 Fragrance Oil (Example I) 20 20 20 Foam Booster (INCROMIDE® CA) 2 2 2 The rim block formed with 20% surfactant lasts for 300 flushes. The rim block formed with 10% surfactant lasts through 400 flushes. The rim block formed with 5% surfactant lasts with 450 flushes. The molded rim blocks are made as follows: the pellets are extruded into 152.4 mm (6") width by 0.076 mm (0.003'') thick cast film with a 19.05 mm (0.75'') diameter Haake single screw extruder. The molded rim blocks are made with a 40,640 Kg (40 ton) Nissei injection molding machine to form blocks having dimensions of 76.2 mm (3'') width x 127 mm (5'') length x 19.05 mm (0.75'') thickness. In each of the foregoing Examples I, II and III, in addition to the fragrance of Example I, other "compatible" fragrances of a deodorancy type can be used. An example is the Schiff base of helional and methyl anthranilate. "HELIONAL®" is a registered trademark of International Flavors & Fragrances for Piperonyl Propanal. The features disclosed in the foregoing description, in the following claims and/or in the accompanying drawings may, both separately and in any combination thereof, be material for realising the invention in diverse forms thereof.

Claims: A composition of matter consisting of: (a) polyvinyl alcohol or partially hydrolyzed polyvinyl acetate with a maximum mole ratio of acetyl moiety:hydroxyl moiety being 3:1 having a number average molecular weight of from 15,000 up to 68,000 containing from 0 up to 15% by weight of an added polar plasticizer; (b) from 1 up to 20% by weight of compatible fragrance contained within the polyvinyl alcohol or partially hydrolyzed polyvinyl acetate; (c) from 0 up to 20% by weight of foaming agent contained within the polyvinyl alcohol or partially hydrolyzed polyvinyl acetate; (d) from 0 up to 20% by weight of hydrophobic silica contained within the polyvinyl alcohol or partially hydrolyzed polyvinyl acetate; (e) from 0 up to 20% by weight of at least one surfactant in addition to the said foaming agent; (f) from 0 up to 5% by weight of water-soluble dye; and (g) from 0 up to 4% by weight of foam booster, wherein the polyvinyl alcohol or partially hydrolyzed polyvinyl acetate is extruded. A toilet rim block molded using the composition of matter of Claim 1. The composition of matter of Claim 1 containing from 1 up to 5% by weight of compatible fragrance and 0% silica. The composition of matter of Claim 1 containing from 1 up to 20% by weight of compatible fragrance and 0% silica. The composition of matter of Claim 1 containing from 5 up to 20% by weight of compatible fragrance and from 2½ up to 20% by weight of hydrophobic silica. The composition of matter of Claim 5 wherein the ratio of hydrophobic silica:compatible fragrance varies from 1:1 up to 1:2. A toilet rim block molded using the composition of matter of Claim 3. A toilet rim block molded using the composition of matter of Claim 4. A toilet rim block molded using the composition of matter of Claim 5. A toilet rim block molded using the composition of matter of Claim 6. A process for forming a fragrance-containing polyvinyl alcohol or partially hydrolyzed polyvinyl acetate product according to claim 1, which process comprises the step of introducing into an extruder polyvinyl alcohol containing a plasticizer or partially hydrolyzed polyvinyl acetate containing a plasticizer simultaneously with introducing into the extruder a compatible fragrance. The process of Claim 11 further characterized in that the compatible fragrance is combined with hydrophobic silica. The process of Claim 11 further characterized in that in addition to the introduction of the fragrance into the extruder, there is also introduced into the extruder detergent or foaming agent. The process of Claim 12 further characterized in that in addition to the introduction of the fragrance into the extruder, there is also introduced into the extruder detergent or foaming agent.

Inventors: BECK CHARLES E J, GREENE DAVID A, MCDERMOTT KEITH J, SHEFER SHMUEL DAVID, SMITH LESLIE C, TEFFENHART JOHN M, BECK, CHARLES E.J., GREENE, DAVID A., MCDERMOTT, KEITH J., SHEFER, SHMUEL DAVID, SMITH, LESLIE C., TEFFENHART, JOHN M.
Applicants: INT FLAVORS & FRAGRANCES INC, INTERNATIONAL FLAVORS & FRAGRANCES INC.
Application year: 1995
Main classification: C08K5
IPC codes: C08K5, C11D3, A61L9, C11D17