Litter composition

The litter composition addresses odor control inefficiencies by using a granular malodor adsorbent with specific pore size and surface area, achieving effective malodor reduction and aroma maintenance.

JP7611166B2Active Publication Date: 2025-01-09SOCIETE DES PRODUITS NESTLE SA
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Patent Information

Application Number
JP2021561719
Authority / Receiving Office
JP · JP
Patent Type
Patents
Current Assignee / Owner
Priority Date
2019-04-22
Filing Date
2020-03-30
Publication Date
2025-01-09
Estimated Expiration
2040-03-30

AI Technical Summary

Technical Problem

Existing animal litter compositions face challenges in effectively controlling odors without increasing fragrance intensity, as strong malodor adsorbents like activated carbon preferentially adsorb fragrances rather than malodors, leading to inefficient odor control and aroma reduction.

Method used

A litter composition incorporating a granular malodor adsorbent with a specific pore size and surface area, present in a range of 0.05% to 5.0% by weight, that adsorbs malodor while releasing fragrance, allowing for improved odor control without significantly reducing aroma intensity.

Benefits of technology

The composition achieves a significant reduction in malodor perception by 25-50% while maintaining a similar or increased perceived aroma, compared to controls without the granular adsorbent, through the use of molecular sieves or granular activated carbon.

✦ Generated by Eureka AI based on patent content.

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Abstract

Provided herein are compositions and methods that can be used to remove malodors in animal waste, comprising a fragrance and about 0.5% to about 5.0% by weight of a granular malodor absorber. The granular malodor absorber may be a granular molecular sieve or granular activated carbon, having a pore size of about 0.4 nm to about 2.0 nm and a surface area of ​​about 100 m. 2 / g~about 1500m 2 / g total surface area.
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Description

Detailed Description of the Invention

[0001] CROSS-REFERENCE TO RELATED APPLICATIONS

[0001] This application claims priority to U.S. Provisional Patent Application No. 62 / 836,998, filed April 22, 2019, the disclosure of which is incorporated herein by reference in its entirety.

[0002] [Technical field]

[0002] The present disclosure relates generally to animal litter compositions for odor control, comprising a fragrance and a granular malodor absorbing agent. More specifically, the present disclosure relates to litter compositions comprising a fragrance and a granular malodor absorbing agent having a specific pore size and surface area.

[0003] [Background technology]

[0003] Animal litter boxes are used by pets, such as cats, to eliminate urine and feces. The animal litter box contains a layer of pet litter that receives the urine and feces. Pet litter can be non-clumping or clumping, and can include absorbent and / or adsorbent materials. Clumping pet litter is a litter product in which the particles promote the formation of a clump after the urine and feces are deposited in the litter box. The clump is typically separated from the litter box by using a litter scoop and then discarded. Non-clumping pet litter can absorb urine and eliminate the odor of urine. However, it can be difficult to replace soiled non-clumping pet litter without emptying the entire box of litter. Deodorizers can be added to the pet litter to absorb odors from pet urine and feces.

[0004]

[0004] The addition of fragrances is often used to control malodors in animal litter, such as cat litter. Typically, the greater the amount of fragrance added, the better the malodor control or malodor masking effect. However, for various reasons, strongly scented products, such as cat litter, may not be desirable for pets or pet owners. Therefore, there is a need to further improve the malodor control performance of animal litter without increasing the perceived fragrance intensity.

[0005]

[0005] One way to improve malodor control without adding large amounts of fragrance is to use a strong malodor adsorbent such as activated carbon. However, in general, fragrance cannot be present in concert with a strong adsorbent such as powdered activated carbon, because the adsorbent may preferentially interact with the fragrance rather than the malodor, adsorbing the fragrance. As a result, the malodor intensity may remain unchanged or increase, but the fragrance intensity will decrease.

[0006]

[0006] One method to overcome the incompatibility between the fragrance and the adsorbent material, as described in U.S. Patent No. 5,782,409, is by physically separating the fragrance from the malodor adsorbent. However, such separation is inconvenient to require, uneconomical and inefficient. Another method is by encapsulating or enrobing the fragrance. However, encapsulation can also have challenges with efficient and timely delivery and physical stability.

[0007]

[0007] Accordingly, it is an object of the present disclosure to provide an improved litter composition that overcomes the aforementioned drawbacks and shortcomings associated with existing malodor control technologies.

[0008] [Summary of the Invention]

[0008] The present disclosure generally relates to an animal litter composition comprising a fragrance and a granular malodor adsorbent, the granular malodor adsorbent being present in an amount of about 0.05% to about 5.0% by weight, having a pore size of about 0.4 nm to about 2.0 nm and a molecular weight of about 100 μm. 2 / g~about 1500m 2 The present invention relates to an animal litter composition having a total surface area of ​​1 / g, wherein the granular malodor adsorbent substantially adsorbs malodor and substantially releases fragrance.

[0009] Another aspect of the present disclosure is a method for reducing or eliminating malodors in animal litter while providing a pleasant smelling environment, comprising the steps of contacting the malodors with a composition comprising a fragrance and a granular malodor adsorbent, the granular malodor adsorbent being present in an amount of about 0.05% to about 5.0% by weight, having a pore size of about 0.4 nm to about 2.0 nm and an average molecular weight of about 100 μm. 2 / g~about 1500m 2 The method relates to a method for producing a 100% aqueous solution of 100% cellulose acetate having a total surface area of ​​100 / g.

[0010]

[0010] Many additional features and advantages will become apparent upon consideration of this specification. Furthermore, it should be noted that the language used in this specification has been selected solely for purposes of readability and instruction, and is not intended to limit the scope of the inventive subject matter.

[0011] [Mode for carrying out the invention]

[0011] It must be noted that as used in this disclosure and the appended claims, the singular forms "a," "an," and "the" include plural referents unless the context indicates otherwise. Thus, for example, reference to "a granule" or "the granule" includes two or more granules.

[0012]

[0012] The terms "comprise", "comprises" and "comprising" should be construed as inclusive rather than exclusive. Similarly, the terms "include", "including" and "or" should all be construed as inclusive unless such a construction is clearly prevented by the context.

[0013]

[0013] However, the compositions and methods disclosed herein may be free of any element not specifically disclosed. Thus, disclosure of an embodiment using the term "comprising" includes disclosure of embodiments "consisting essentially of" and "consisting of" the specified components. "Consisting essentially of" means that the embodiment contains more than 50% by weight of the specified components, at least 75% by weight of the specified components, at least 85% by weight of the specified components, at least 95% by weight of the specified components, or at least 99% by weight of the specified components.

[0014]

[0014] The term "and / or" used in the context of "X and / or Y" should be interpreted as "X", or "Y", or "both X and Y". As used herein, the terms "examples" and "such as", especially when followed by a list of terms, are merely exemplary and descriptive and should not be considered exclusive or exhaustive. Unless otherwise stated, any embodiment disclosed herein can be combined with any other embodiment disclosed herein.

[0015]

[0015] All percentages set forth herein are by weight of the total composition unless otherwise indicated. As used herein, "about," "approximately," and "substantially" are understood to refer to numbers within a range of numbers, for example, within -10% to +10% of the referenced number, within -5% to +5% of the referenced number, within -1% to +1% of the referenced number, or within -0.1% to +0.1% of the referenced number. All numerical ranges herein should be understood to include all integers, whole numbers, or fractions within the range. Furthermore, these numerical ranges should be interpreted as supporting claims directed to any number or subset of numbers within the range. For example, a disclosure of 1 to 10 should be interpreted as supporting ranges such as 1 to 8, 3 to 7, 1 to 9, 3.6 to 4.6, 3.5 to 9.9, etc.

[0016]

[0016] The terms "pet" and "animal" are used interchangeably herein and refer to any animal capable of using an animal litter box. Non-limiting examples include cats, dogs, rats, ferrets, hamsters, rabbits, iguanas, pigs, and birds. A pet can be any suitable animal, and the present disclosure is not limited to a particular pet animal.

[0017]

[0017] The term "litter" means any material that has sorption properties for moisture and / or liquids, such as animal urine, and / or reduces odors from animal urine and / or feces. "Clumping litter" or "clumping deodorant" forms clumps when in contact with moisture. In an animal litter box, the clumps are distinct from other litter or deodorants that are not in contact with moisture. "Clumping agents" bind adjacent particles together when wet. Thus, in "clumping" litter, consumers can scoop pet waste using a litter scoop with a specific opening, whereas in "non-clumping" litter, it is impossible or impractical to scoop pet waste. "Non-clumping" litter does not form distinct clumps. The term "deodorant" means any material that adsorbs or absorbs at least a portion of the ambient odors, and may be in a form that is added to the pet litter box in the animal litter box. The term "excrement" means urination and / or defecation by pets.

[0018]

[0018] The term "animal litter" refers to any device capable of holding pet litter. For example, animal litter can be a container with a bottom wall and one or more side walls, and / or any device, such as a mat or grid, configured for litter to be placed on. As a non-limiting example, animal litter can be a rectangular box with side walls that are at least about 6 inches high.

[0019]

[0019] The term "mesh" is defined by the ASTM E-11 USA Standard specifications for sieves. As used herein, the "size" of a particle refers to the length of the particle's widest dimension.

[0020]

[0020] The methods and apparatus and other advances disclosed herein are not limited to the particular methodology, procedures, and reagents, as such may vary as will be recognized by those skilled in the art. Moreover, the terminology used herein is for the purpose of describing particular embodiments only and is not intended to limit the scope of the disclosure or claims.

[0021]

[0021] Unless otherwise defined, all technical and scientific terms, terminology, and acronyms used herein have the meaning commonly understood by one of ordinary skill in the field(s) of the disclosure or in the field(s) in which the term is used. Although any compositions, methods, products, or other procedures or materials similar or equivalent to those described herein can be used, the preferred devices, methods, products, or other procedures or materials are described herein.

[0022]

[0022] One aspect of the present disclosure relates to an animal litter composition for odor control comprising a fragrance and about 0.05% to about 5.0% by weight of a granular malodor adsorbent. The adsorbent may have a pore size of about 0.4 nm to about 2.0 nm. The adsorbent may also have a pore size of about 100 nm. 2 / g~about 1500m 2 The granular malodor adsorbent may have a total surface area of ​​about 100 m / g. The granular malodor adsorbent may substantially adsorb malodors and substantially eliminate fragrance. The incorporation and coordination of the two malodor control components, the malodor adsorbent and the fragrance, enhances the overall consumer experience. In some embodiments, the adsorbent has a total surface area of ​​about 100 m / g. 2 / g~approx. 1200m 2 / g, about 100m 2 / g ~ approx. 1100m 2 / g, about 100m 2 / g~about 1000m 2 / g, about 100m 2 / g~about 800m 2 / g, about 100m 2 / g~about 700m 2 / g, or about 100m 2 / g~about 600m 2 / g total surface area. In some embodiments, the granular malodor adsorbent has a pore size of less than about 2.0 nm, less than about 1.0 nm, less than about 0.8 nm, or less than about 0.6 nm.

[0023]

[0023] The litter composition of the present disclosure includes one or more fragrances to provide a sense of freshness and / or deodorization to humans or to act as an attractant to animals. Fragrances are an important part of an animal care system. The fragrances can be natural or synthetic fragrances. Non-limiting examples of fragrance compositions include one or more of esters, linear terpenes, cyclic terpenes, aromatics, amines, alcohols, aldehydes, ketones, lactones, and thiols. Non-limiting examples of specific fragrance compounds include limonene, linalool, β-phenethyl alcohol, and myrcene.

[0024] In some embodiments, the fragrance is present in an amount of about 0.05% to about 1.0% by weight. In other embodiments, the fragrance is present in an amount of about 0.05% to about 0.4% by weight. In one embodiment, the fragrance is present in an amount of about 0.2% or about 0.1% by weight.

[0025] In some embodiments, a majority of the fragrance is not encapsulated, e.g., at least 75% of the fragrance is not encapsulated, at least 80% of the fragrance is not encapsulated, at least 85% of the fragrance is not encapsulated, at least 90% of the fragrance is not encapsulated, or at least 95% of the fragrance is not encapsulated.

[0026] In some embodiments, the granular malodor adsorbent adsorbs more malodor than the fragrance. For example, in one embodiment, the malodor is adsorbed in an amount of about 25% to about 60% and the fragrance is adsorbed less than 40% compared to a control sample that does not include the granular malodor adsorbent. In another embodiment, the malodor is adsorbed in an amount of about 30% to about 60% and the fragrance is adsorbed less than 40% compared to a control sample that does not include the granular malodor adsorbent. In one embodiment, the malodor is adsorbed in an amount of about 30% to about 40% and the fragrance is adsorbed close to 0% compared to a control sample that does not include the granular malodor adsorbent. In some embodiments, the granular malodor adsorbent adsorbs at least 25% of the malodor or at least 30% of the malodor. In some embodiments, the granular malodor adsorbent releases at least about 40%, at least about 50%, at least about 70%, or at least about 75% of the fragrance.

[0027] In some embodiments, the animal litter composition comprising the granular malodor sorbent reduces the perception of malodor by at least 25% or at least 30% compared to a control without the granular sorbent. In some embodiments, the animal litter composition comprising the granular malodor sorbent reduces the perceived aroma by about 25% or at least 30% compared to a control without the granular sorbent. In some embodiments, the animal litter composition comprising the granular malodor sorbent reduces the perceived aroma by about 30% or less, about 40% or less, about 50% or less, or about 60% compared to a control without the granular malodor sorbent.

[0028]

[0028] The litter composition of the present disclosure includes a granular malodor sorbent. In some embodiments, the granular malodor sorbent includes a molecular sieve. A molecular sieve is a solid porous material that separates particles of molecular size. Any material with relatively uniform pore size at the molecular level can be considered a molecular sieve, including zeolites and carbon molecular sieves. Molecular sieves are available in a variety of forms, including powders, pellets, mesh, and beads. Molecular sieves can be natural or synthetic. Zeolites are naturally occurring minerals found in volcanic ash. Zeolites are crystalline aluminosilicates of Group IA and Group IIA elements, such as sodium, potassium, magnesium, and calcium. Pellet, mesh, or bead type molecular sieves may be used in the litter composition of the present disclosure. In some embodiments, the size of the molecular sieve can be from -8 mesh to 60 mesh. In some embodiments, the molecular sieve pellets are gently scraped or crushed to produce granules having a size of about -8 mesh to about 60 mesh.

[0029] In some embodiments, the molecular sieves used in the present disclosure have a large surface area and a small pore size. In some embodiments, the molecular sieve has a pore size of about 200 m. 2 / g~about 800m 2 In another embodiment, the molecular sieve has a surface area of ​​about 300 m 2 / g~about 600m 2 / g of surface area. In some embodiments, the molecular sieve has a pore size of about 0.2 nm to about 1.2 nm. In other embodiments, the molecular sieve has a pore size of about 0.3 nm to about 1.1 nm, or about 0.4 nm to about 1.0 nm. In some embodiments, the molecular sieve has a pore size of about 0.6 nm or about 0.8 nm.

[0030] In some embodiments, the molecular sieve is present in an amount of about 0.05% to about 5.0% by weight of the total litter composition. In another embodiment, the molecular sieve is present in an amount of about 0.1% to about 4.0% by weight. In one embodiment, the molecular sieve is present in an amount of about 1.0% to about 3.0% by weight. In one embodiment, the molecular sieve is present in an amount of about 2.0% by weight.

[0031] In some embodiments, the granular malodor adsorbent comprises granular activated carbon. Granular activated carbon is composed of particles that are larger than those found in powdered activated carbon. Granular activated carbon is typically classified as a material that is too large to pass through an 80-mesh sieve. Granular activated carbon is available in a variety of sizes. In some embodiments, the granular activated carbon has a size of about -12 mesh to about 60 mesh. In some embodiments, the granular activated carbon has a size of about -12 mesh to about 40 mesh. In some embodiments, the granular activated carbon has a size of about 100 mesh to about 200 mesh. 2 / g~about 1500m 2 / g, about 100m 2 / g~approx. 1200m 2 / g, about 100m 2 / g ~ approx. 1100m 2 / g, about 100m 2 / g~about 1000m 2 / g, about 100m 2 / g~about 800m 2 / g, about 100m 2 / g~about 700m 2 / g, or about 100m 2 / g~about 600m 2 / g surface area. In some embodiments, the granular activated carbon has a pore size of about 0.4 nm to about 2.0 nm. In some embodiments, the granular activated carbon has a pore size of less than about 2.0 nm. In some embodiments, the adsorbent comprises a carbon molecular sieve.

[0032] In some embodiments, the granular activated carbon is present in an amount of about 0.05% to about 5.0% by weight. In other embodiments, the granular activated carbon is present in an amount of about 0.1% to about 4.0% by weight. In one embodiment, the granular activated carbon is present in an amount of about 1% to about 3.0% by weight. In one embodiment, the granular activated carbon is present in an amount of about 2.0% by weight.

[0033] In some embodiments, the litter composition further comprises an absorbent substrate, hi some embodiments, the absorbent substrate comprises absorbent granules, each of which comprises an absorbent core and a separate layer surrounding the absorbent core.

[0034] In some embodiments, compositions comprising the granular malodor sorbent of the present disclosure can be obtained by dry mixing the granular malodor sorbent with an absorbent substrate to form a blended litter composition, which has the ability to absorb moisture and / or liquid and reduce or eliminate malodor while providing a fragrance to the surrounding environment.

[0035]

[0035] In some embodiments, the absorbent substrate comprises a flocculating agent, which comprises bentonite, guar gum, starch, xanthan gum, gum arabic, acacia gum, silica gel, and mixtures thereof.

[0036] In some embodiments, the flocculant comprises bentonite. In one embodiment, the bentonite is sodium bentonite.

[0037]

[0037] In some embodiments, the absorbent substrate comprises absorbent granules comprising an absorbent core, the absorbent core comprising at least one of clay, expanded perlite, quartz, feldspar, calcium bentonite, calcite, illite, calcium carbonate, carbon, mica, Georgia white clay, hectorite, zeolite, smectite, opal, kaolinite, pumice, tobermorite, slate, gypsum, vermiculite, halloysite, sepiolite, marl, diatomaceous earth, dolomite, attapulgite, montmorillonite, Monterey shale, fuller's earth, silica, fossilized plant material, perlite, perlite particulates, and mixtures thereof.

[0038]

[0038] In some embodiments, the absorbent substrate further comprises an additive selected from the group consisting of antimicrobial agents, anti-adherents, agents for pH control, dyes, colorants, dust removal agents, disinfectants, additional odor control agents, and combinations thereof.

[0039] In some embodiments, the absorbent substrate has a capacity of about 50 kg / m 3 ~About 2000kg / m 3 has a density of

[0040]

[0040] Non-limiting examples of absorbent substrates include non-swelling clays agglomerated into clay particles coated with a flocculant, such as swelling clay. The non-swelling clays used in the agglomeration process can be about 0.3 mm or less in size and are sometimes referred to as seed materials. In an exemplary embodiment, the clay particles range in size from about 0.15 mm or less.

[0041] One specific embodiment involves recycling waste fines containing calcium-montmorillonite. The calcium-montmorillonite fines can be agglomerated in a pin mixer using water as a binder. The agglomerated fines have a moisture content of about 20% to about 40%. In another embodiment, the fines have a moisture content of about 28% to about 34%. The agglomerated fines can then be coated with bentonite powder having a particle size of about 0.15 mm or less using a centrifugal coater or a rotary coater / dryer system.

[0042] In an exemplary embodiment, the non-swelling clay can be agglomerated using a pin mixer. A swelling clay can be applied to the agglomerated particles to form a coating. A non-limiting example of a swelling clay includes sodium bentonite powder. In some embodiments, the swelling clay can be blended with guar gum. In some embodiments, the coating can be further enhanced with either or both of a malodor control agent and an antimicrobial agent.

[0043] In one embodiment, the non-swelling clay is fed to a pin mixer using a screw extruder. Moisture (e.g. water) is added as a binder. The clay and moisture form a cake-like material as it enters the pin mixer. The pin mixer is equipped with a shaft with a series of pins that break up the cake, resulting in the formation of small spherical particles that are separated from the cake-like material using a shaker screen. Other methods are contemplated, including using a binder comprising guar gum and water, or starch and water.

[0044] Another embodiment utilizes a blend of non-swelling clay and bentonite with water as binder to produce particles by pin mixing process. Yet another embodiment utilizes sodium bentonite with water as binder to produce particles of about 0.25 mm to about 3 mm size using pin mixer process. Agglomerated particles made by any of the above methods can be coated with bentonite powder of about 0.15 mm or less using centrifugal coater or rotary coater / dryer system to improve the agglomeration ability.

[0045] In an alternative embodiment, the method of coating the outer surface of the non-swelling clay particles with the flocculant includes utilizing at least one of a fluidized bed dryer, a semi-continuous centrifugal coater, or a rotary coating and drying system. In a rotary system, the clay particles and the flocculant are tumbled in a drum and mixed for about 60 seconds. The litter is then removed from the drum and the drum is heated to about 300°F to about 400°F, and the litter is returned to the drum and dried to a moisture content of about 8%.

[0046] The resulting coated litter typically has a moisture content of about 5% to about 15% and a mesh size range of -8 to 50. In some embodiments, the moisture content is about 8%.

[0047] In one embodiment, the bentonite coating is about 20% to about 40% by weight of the coated particle. In an alternative embodiment, the bentonite coating is about 25% to about 35% by weight of the coated particle. In a further alternative embodiment, the bentonite coating is about 30% by weight of the coated particle.

[0048] In an alternative method for producing litter, the agglomerated particulates are placed in a fluidized bed and sprayed with a bentonite coating from a dilute solution.

[0049]

[0049] The litter resulting from the above described compositions and methods has excellent clumping properties due to the active clumping agent being maintained on the particle surface where the clumping interactions occur. Furthermore, due to the formation of a shell around the agglomerated particles as a result of the above described coating process, the litter has a lower dust content than other known clumping litter, resulting in less tracking. Furthermore, because the litter described herein is less likely to adhere to animal litter, the litter is easier to remove from animal litter than known clumping litter.

[0050] In another aspect of the present disclosure, the composition further comprises an absorbent substrate comprising relatively low density absorbent granules. The relatively low density absorbent granules can be non-agglomerated particles comprising perlite and an outer particle surface coating comprising a flocculating agent. In one embodiment, the flocculating agent comprises bentonite.

[0051] In some embodiments, the low density absorbent granules include particles consisting essentially of expanded perlite and a coating on the outer surface of the particles. In one embodiment, the coating includes a flocculating agent including bentonite. In another embodiment, the flocculating agent includes sodium bentonite and guar gum.

[0052]

[0052] In some embodiments, the flocculants that make up the coating of perlite or expanded perlite can be bentonite, guar gum, starch, xanthan gum, gum arabic, acacia gum, silica gel, and other minerals, and mixtures thereof.

[0053]

[0053] When sodium bentonite is used as or in the cohesive layer, it refers to bentonite clay having a high percentage of sodium, but it should be understood that it may also contain other clays or minerals, including calcium bentonite. Sodium bentonite can be sourced directly from mining operations (natural sodium bentonite) or can be obtained from the conversion of calcium bentonite by an ion exchange process. When sodium bentonite is used as or in the cohesive layer, the bulk density of the bentonite is typically from about 600 to about 1125 kg / m 3 In some embodiments, the density of the sodium bentonite is in the range of about 600 kg / m 3 , about 700kg / m 3 , about 800kg / m 3 , about 900kg / m 3 , 1000kg / m 3 , or about 1100 kg / m 3 It is.

[0054]

[0054] In one embodiment, the moisture content of the sodium bentonite is about 6% to about 7%.

[0055]

[0055] Bentonite may be provided as a powder or "particulate" having a size of 0.2 mm or less. In an exemplary embodiment, the sodium bentonite particles have a size of about 0.15 mm or less.

[0056]

[0056] Various particle sizes can be used in the low density coated absorbent granules described herein. In some embodiments, the particles have a size of about -8 to +30 mesh (US standard sieve) of expanded perlite. In other embodiments, the particle size of the expanded perlite is about -6 to +40 mesh. In some embodiments, the expanded perlite particles are not uniformly distributed within the size range.

[0057] Typically, at least some moisture is present to facilitate the coating process, but the moisture content of the low density absorbent granules is relatively low. In one embodiment, the moisture content of the expanded perlite in the low density coated litter is between 0% and 3%. In another embodiment, the moisture content is about 0.5%.

[0058]

[0058] Generally, the method of preparing a litter composition according to the present disclosure includes coating perlite and / or expanded perlite with a flocculating agent. In one embodiment, the perlite is screened to select particles of a predetermined size. For example, the expanded perlite may be screened to remove particles smaller than a 50 mesh US standard sieve. In some embodiments, the perlite is screened to remove particles smaller than a 40 mesh US standard sieve or smaller than a 30 mesh US standard sieve.

[0059] Dust mitigation can be facilitated by placing perlite particles in an enrobing machine and agitating the particles to aid in particulate reduction. In one embodiment, the expanded perlite particles are weighed and sprayed with water prior to or upon entry into the enrober. Generally, the amount of water added depends on the weight of the expanded perlite particles in the enrober. In some embodiments, the weight of the water added is about 20% to about 90% of the weight of the expanded perlite. In other embodiments, the weight of the water added is about 50% to about 85% of the weight of the expanded perlite. In one particular embodiment, the weight of the water added is about 65% of the weight of the expanded perlite particles.

[0060]

[0060] The perlite particles are coated with a flocculant (e.g., sodium bentonite) in the coater. In one example, a centrifugal coating method can be used. For example, a batch of perlite particles is metered by volume onto a feed belt and fed into the coater while the coater is rotating. The perlite particles roll in the coater chamber in the direction of rotation. In an optional preconditioning step, the perlite particles are spun in the coater for a period of time (e.g., 30-60 seconds) before coating.

[0061]

[0061] Water can be added to the coater while it is spinning. The water added may be based on the weight of the flocculant added to the coater. The weight of the water added is typically about 10-100% (e.g., 10%, 15%, 20%, 25%, 30%, 35%, 40%, 45%, 50%, 55%, 60%, 65%, 70%, 75%, 80%, 85%, 90%, 95%, or 100%) of the weight of the flocculant. In one embodiment, for example, the weight of the water added is about 10-60% (e.g., 10%, 15%, 20%, 25%, 30%, 35%, 40%, 45%, 50%, 55%, or 60%) of the weight of the flocculant. In another embodiment, for example, the weight of water added is approximately 10-40% (e.g., 10%, 15%, 20%, 25%, 30%, 35%, or 40%) of the weight of the flocculant. Alternatively, water addition can occur in the enrober or both the enrober and coater.

[0062] A flocculant (e.g., sodium bentonite) is metered into the coater. Generally, the amount of flocculant added to the coater is based on the volume of the perlite particles. In one embodiment, for example, about 5 to about 45 pounds (e.g., 5 pounds, 10 pounds, 12 pounds, 14 pounds, 20 pounds, 30 pounds, 35 pounds, 40 pounds, or 45 pounds) of sodium bentonite is added per cubic foot of expanded perlite. In another embodiment, for example, about 20 to about 35 pounds (e.g., 20 pounds, 25 pounds, 30 pounds, or 35 pounds) of sodium bentonite is added per cubic foot of expanded perlite. In yet another embodiment, about 20 to about 30 pounds (e.g., 20 pounds, 25 pounds, 27 pounds, 29 pounds, or 30 pounds) of sodium bentonite is added per cubic foot of expanded perlite. In one particular embodiment, approximately 30 pounds of sodium bentonite is added per cubic foot of expanded perlite.

[0063] In addition to or instead of the bentonite-based flocculant, other coating materials such as guar gum may be included in the coater. Such materials may be added as a mixture with the bentonite or may be added in a separate step. When the bentonite (or other coating material) is metered into the chamber of the coater, it combines with the expanded perlite, which is being spun wet, to form a coating on the expanded perlite.

[0064]

[0064] The coated perlite (e.g., expanded perlite) particles can optionally be further contacted with water (e.g., misted or sprayed with water). Generally, the water added is added based on the weight of the flocculant in the coater. In an exemplary embodiment, the weight of the water added is about 1 to about 5% (e.g., 1%, 2%, 3%, 4%, or 5%) of the weight of the flocculant. In another exemplary embodiment, the weight of the water added is about 5 to about 10% (e.g., 5%, 6%, 7%, 8%, 9%, or 10%) of the weight of the flocculant. In a further exemplary embodiment, the weight of the water added is about 1 to about 3% (e.g., 1%, 2%, or 3%) of the weight of the flocculant. In one particular embodiment, the weight of the water added is approximately 2% of the weight of the flocculant. In another particular embodiment, the weight of the water added is approximately 5% of the weight of the flocculant. In another particular embodiment, the weight of the water added is approximately 9% of the weight of the flocculant.

[0065] In alternative embodiments, water may be added in an amount appropriate to achieve a particular target moisture content after coating. In one embodiment, water is added in an amount appropriate to achieve a target moisture content of, for example, about 20 to about 40% (e.g., 20%, 21%, 22%, 23%, 24%, 25%, 26%, 27%, 28%, 29%, 30%, 31%, 32%, 33%, 34%, 35%, 36%, 37%, 38%, 39%, or 40%). In another embodiment, water is added in an amount appropriate to achieve a target moisture content of, for example, about 25 to about 30%. In one embodiment, a rolling system is utilized to coat the perlite particles with bentonite.

[0066]

[0066] The coated particles are transferred to a dryer. Drying removes moisture from the coated particles without substantially removing the coating or substantially damaging the final product. A fluidized bed dryer is utilized in certain embodiments. Typically, the coated particles are dried to have a moisture content in the range of about 1.5% to about 20%. In one embodiment, for example, the coated particles are dried to a moisture content in the range of about 5% to about 15% (e.g., about 5%, about 7%, about 9%, about 11%, about 13%, or about 15%). In another embodiment, for example, the coated particles are dried to a moisture content in the range of about 7% to about 10% (e.g., about 7%, about 8%, about 9%, or about 10%). In one particular embodiment, for example, the final moisture content of the coated litter product is approximately 10%. In another particular embodiment, the coated particles are dried to a moisture content sufficient to provide a relatively uniform appearance to the coated particles.

[0067]

[0067] Alternative screening processes can be used. A vibratory screener may be used to remove coated expanded perlite particles larger than about a mesh size of 8 and smaller than about a mesh size of 40. Any excess coated expanded perlite separated in the screening process may, for example, be crushed and added to other litter products or used in other odor or moisture control products.

[0068]

[0068] Various additives may be optionally applied to the animal litter composition. The additives may include, for example, odor control agents, fragrances, antimicrobial agents, anti-sticking agents, agents for pH control, coloring powders, dyes, colorants and / or colored particles, dusting agents, disinfectants, or combinations thereof. In one embodiment, for example, at least a portion of the coated particles are further coated with a colorant. Various characteristics of the coated litter product of the present invention represent significant improvements over existing litter products.

[0069]

[0069] For example, the density of the low density coated litter product is relatively low compared to other litter products. Typically, for example, the density of the coated litter product is about 200 to about 600 kg / m 3 In one embodiment, the density of the coated litter product is from about 300 to about 500 kg / m 3 (For example, 300 kg / m 3 , 350kg / m 3 , 400kg / m 3 , 450kg / m 3 , or 500 kg / m 3 In another embodiment, the density of the coated litter product is from about 350 to about 450 kg / m 3 (For example, 350 kg / m 3 , 400kg / m 3 , 450kg / m 3 In one particular embodiment, the density of the coated litter product is approximately 350 kg / m 3 In another particular embodiment, the density of the coated litter product is approximately 400 kg / m 3 In another particular embodiment, the density of the coated litter product is approximately 450 kg / m 3 It is.

[0070] Generally, the perlite particles are substantially coated with the flocculating agent. In one embodiment, for example, the particles are coated to greater than 75%. In other embodiments, for example, the particles are coated to greater than 85%, greater than 95%, or greater than 99%. Preferably, the coating material completely surrounds or enrobes the particles. In some embodiments, agglomerated particles composed primarily of expanded perlite can also be used.

[0071] Another aspect of the present disclosure relates to a method for reducing or eliminating malodors in animal litter while providing a pleasant aroma to the surrounding environment. The method includes contacting the malodors with a composition comprising a fragrance and about 0.05 weight percent to about 5.0 weight percent of a granular malodor adsorbent. The granular malodor adsorbent has a pore size of about 0.4 nm to about 2.0 nm and a molecular weight of about 100 μm. 2 / g~about 1500m 2 / g total surface area.

[0072] In some embodiments, the method comprises the steps of: 2 / g~approx. 1200m 2 / g, about 100m 2 / g ~ approx. 1100m 2 / g, about 100m 2 / g~about 1000m 2 / g, about 100m 2 / g~about 800m 2 / g, about 100m 2 / g~about 700m 2 / g, or about 100m 2 / g~about 600m 2 / g of granular malodor adsorbent.

[0073] [Example] Example 1 A series of litter samples was prepared containing various amounts and types of adsorbent material in addition to the base litter. The base litter was a scented engineered litter containing a non-cohesive core and a cohesive outer layer containing sodium bentonite.

[0074] Table 1 details the properties of the adsorbent materials used in the following examples. Activated Carbon A and Activated Carbon B were commercially available. Aluminosilicate Molecular Sieve C and Aluminosilicate Molecular Sieve D were commercially available extruded pellets having a diameter of 1 / 16 inch. Aluminosilicate Molecular Sieve C and Aluminosilicate Molecular Sieve D were gently crushed to produce granular molecular sieves having mesh sizes of about -8 to about 60 mesh.

[0075] [Table 1]

[0076]

[0075] The powdered activated carbon containing litter samples in Table 2 (Test 1 and Test 2) were prepared by incorporating the powdered activated carbon as a layer between a non-cohesive core and a cohesive outer layer containing sodium bentonite. In a typical sample preparation, 1.14 g of high viscosity sodium carboxymethyl cellulose (CMC) was gradually added to 568 g of water in a blender with vigorous stirring until a uniform clear solution was formed. Then, 68.1 g of coconut-based activated carbon powder was gradually added to the CMC solution with vigorous stirring until a uniform carbon slurry or suspension was formed. Next, 1.25 lbs of expanded perlite core was added in a rotary coater rotating at about 500 RPM, followed by the prepared carbon slurry or suspension, followed by 3.75 lbs of dried sodium bentonite powder. The prepared litter material was then dried in a fluid bed dryer to a moisture content of 6-12% and produced to a size of -8 to 30 US mesh size. The carbon content in this litter sample was 3% by weight.

[0077]

[0076] The litter samples containing granular activated carbon in Table 2 (Test 3, Test 4, and Test 5) were prepared by drying the granular activated carbon at 120° Celsius for 4 hours, cooling to room temperature, and then uniformly mixing the dried granular activated carbon with the clumping litter.

[0078] The fragrance in the litter samples prepared as above was present in an amount of 0.15% by weight. For Tests 1 and 2, the fragrance was added as a liquid to a final concentration of about 0.15% by weight, mixed and allowed to equilibrate for one week. For Tests 3, 4, and 5, commercially available scented litter was purchased and used.

[0079] Example 2 Scented litter samples containing granular or powdered sorbents prepared as described above, and a control sample containing no additional granular or powdered sorbent, were tested for their ability to control malodors and maintain a pleasant scent. Each sample was treated with cat urine and / or cat feces. After five days, the waste pellets were removed from the litter and each sample was rated on a scale of 0 to 100 by a sensory panel trained in identifying scents associated with feces, urine, ammonia, and fragrance, utilizing industry-accepted methodology. The results are shown in Table 2.

[0080] [Table 2]

[0081]

[0078] The litter samples containing powdered activated carbon adsorbent showed a reduction in odor intensity of 58% or more compared to the control. In contrast, two of the three litter samples containing granular activated carbon showed a lesser reduction in odor intensity. The litter samples containing powdered adsorbent showed a significant increase in malodor intensity compared to the control. Meanwhile, the litter samples containing granular malodor adsorbent showed a reduction in malodor, in some cases by as much as 50%.

[0082] Example 3

[0079] Litter samples containing granular molecular sieve were prepared by uniformly mixing molecular sieve granules with scented clumping litter. The moisture content of the composition was about 6% to about 12% by weight. The fragrance content was about 0.15% by weight.

[0083] Litter samples containing molecular sieves prepared as described above, and a control sample containing no additional adsorbent, were tested for their ability to control malodors and maintain a pleasant scent. Each sample was treated with cat urine and / or cat feces. After 5 days, the waste pellets were removed from the litter and each pellet was rated on a scale of 0 to 100 by a sensory panel trained in identifying scents associated with feces, urine, ammonia, and fragrance, utilizing industry accepted methodology. The results are shown in Table 3. The experiment was repeated using the same experimental design. The results are shown in Table 4.

[0084] [Table 3]

[0085] [Table 4]

[0086]

[0081] Each sample containing granular molecular sieve reduced malodor by more than 30%. The two samples containing molecular sieve C reduced the perceived aroma by less than about 31%, and the two samples containing granular molecular sieve D increased the perceived aroma.

[0087]

[0082] It should be understood that various changes and modifications to the embodiments described herein will be apparent to those skilled in the art. Such changes and modifications can be made without departing from the spirit and scope of the subject matter of the present invention and without diminishing its intended advantages. It is therefore intended that such changes and modifications be covered by the appended claims.

[0088]

[0083] Furthermore, the present embodiments are not therefore limited to the exact details of the methodology or configuration described above, since such changes and modifications are intended to be within the scope of the present disclosure. Furthermore, unless otherwise specified, any use of the terms "first", "second", etc. does not denote any order or importance, but rather the terms "first", "second", etc. are merely used to distinguish one element from another.

Claims

1. 1. An animal litter composition for controlling malodor comprising a fragrance and a granular malodor adsorbent, said granular malodor adsorbent being present in an amount of 0.05% to 5.0% by weight and having a pore size of 0.4 nm to 2.0 nm and a pore size of 100 mm. 2 / g~1500m 2 / g total surface area, said granular malodor adsorbent substantially adsorbing malodor and substantially releasing said fragrance; the granular malodor adsorbent is a zeolite molecular sieve granule, The zeolite molecular sieve granules have a mesh size of -8 to 60. An animal litter composition.

2. The composition of claim 1, wherein the fragrance is present in an amount of from 0.05% to 0.4% by weight.

3. The composition of claim 1 , wherein the fragrance is not encapsulated.

4. The composition of claim 1 further comprising an absorbent substrate.

5. The composition of claim 4 , wherein the absorbent substrate comprises absorbent granules comprising an absorbent core and a separate layer surrounding the absorbent core.

6. The composition of claim 4 , wherein the absorbent substrate comprises clay.

7. The composition of claim 4, wherein the absorbent substrate comprises a non-swelling clay core coated with a swelling clay.

8. The composition of claim 4, wherein the absorbent substrate comprises an expanded perlite core coated with an expanding clay.

9. 9. The composition of claim 7 or 8, wherein the swelling clay is sodium bentonite.

10. 10. The composition of claim 1, wherein said granular malodor adsorbent has a higher affinity for malodor than said fragrance.

11. 10. The composition of claim 1, wherein said granular malodor adsorbent adsorbs at least 25% of said malodor.

12. 10. The composition of claim 1, wherein said granular malodor adsorbent releases at least 40% of said fragrance.

13. 1. A method for reducing or eliminating malodors while providing a pleasant smell to an ambient environment comprising contacting said malodors with a composition comprising a fragrance and a granular malodor adsorbent, said granular malodor adsorbent being present in an amount of 0.05% to 5.0% by weight, having a pore size of 0.4 nm to 2.0 nm and a pore size of 100 mm. 2 / g~1500m 2 / g total surface area, the granular malodor adsorbent is a zeolite molecular sieve granule, The method of claim 1, wherein the zeolite molecular sieve granules have a mesh size of from -8 to 60.

14. 14. The method of claim 13, wherein the composition has the same level of perceived aroma, an increase in perceived aroma, or less than a 60% reduction in perceived aroma compared to a control composition that does not contain a granular malodor adsorbent.

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