Classifications

• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
  • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
  • B01J20/22—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
  • B01J20/24—Naturally occurring macromolecular compounds, e.g. humic acids or their derivatives
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J3/00—Processes of treating or compounding macromolecular substances
  • C08J3/12—Powdering or granulating
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
  • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
  • B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
  • B01J20/28002—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their physical properties
  • B01J20/28004—Sorbent size or size distribution, e.g. particle size
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
  • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
  • B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
  • B01J20/28014—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their form
  • B01J20/28016—Particle form
  • B01J20/28019—Spherical, ellipsoidal or cylindrical
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
  • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
  • B01J20/30—Processes for preparing, regenerating, or reactivating
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08B—POLYSACCHARIDES; DERIVATIVES THEREOF
  • C08B1/00—Preparatory treatment of cellulose for making derivatives thereof, e.g. pre-treatment, pre-soaking, activation
  • C08B1/003—Preparation of cellulose solutions, i.e. dopes, with different possible solvents, e.g. ionic liquids
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08B—POLYSACCHARIDES; DERIVATIVES THEREOF
  • C08B3/00—Preparation of cellulose esters of organic acids
  • C08B3/16—Preparation of mixed organic cellulose esters, e.g. cellulose aceto-formate or cellulose aceto-propionate
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08B—POLYSACCHARIDES; DERIVATIVES THEREOF
  • C08B3/00—Preparation of cellulose esters of organic acids
  • C08B3/16—Preparation of mixed organic cellulose esters, e.g. cellulose aceto-formate or cellulose aceto-propionate
  • C08B3/18—Aceto-butyrates
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
  • C08K5/00—Use of organic ingredients
  • C08K5/04—Oxygen-containing compounds
  • C08K5/10—Esters; Ether-esters
  • C08K5/11—Esters; Ether-esters of acyclic polycarboxylic acids
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
  • C08K5/00—Use of organic ingredients
  • C08K5/49—Phosphorus-containing compounds
  • C08K5/51—Phosphorus bound to oxygen
  • C08K5/52—Phosphorus bound to oxygen only
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L1/00—Compositions of cellulose, modified cellulose or cellulose derivatives
  • C08L1/08—Cellulose derivatives
  • C08L1/10—Esters of organic acids, i.e. acylates
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L1/00—Compositions of cellulose, modified cellulose or cellulose derivatives
  • C08L1/08—Cellulose derivatives
  • C08L1/10—Esters of organic acids, i.e. acylates
  • C08L1/12—Cellulose acetate
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L1/00—Compositions of cellulose, modified cellulose or cellulose derivatives
  • C08L1/08—Cellulose derivatives
  • C08L1/10—Esters of organic acids, i.e. acylates
  • C08L1/14—Mixed esters, e.g. cellulose acetate-butyrate
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L1/00—Compositions of cellulose, modified cellulose or cellulose derivatives
  • C08L1/08—Cellulose derivatives
  • C08L1/26—Cellulose ethers
  • C08L1/28—Alkyl ethers
• • G—PHYSICS
  • G02—OPTICS
  • G02B—OPTICAL ELEMENTS, SYSTEMS OR APPARATUS
  • G02B1/00—Optical elements characterised by the material of which they are made; Optical coatings for optical elements
  • G02B1/04—Optical elements characterised by the material of which they are made; Optical coatings for optical elements made of organic materials, e.g. plastics
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J2301/00—Characterised by the use of cellulose, modified cellulose or cellulose derivatives
  • C08J2301/08—Cellulose derivatives
  • C08J2301/10—Esters of organic acids
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L2201/00—Properties
  • C08L2201/06—Biodegradable
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L2203/00—Applications
  • C08L2203/20—Applications use in electrical or conductive gadgets
  • C08L2203/206—Applications use in electrical or conductive gadgets use in coating or encapsulating of electronic parts

Definitions

• microplastics In natural environments, conventional non-biodegradable plastics mechanically break down into small pieces of plastics, called microplastics, that persists in the environment.
• Some single use plastics, such as microbeads, used in health and beauty products and lint microfibers from the laundry are other sources of microplastics. Due to their size, these microplastics end up in natural water bodies. To reduce microplastics generation, it is desirable to use plastics that are freshwater biodegradable.
• the present application discloses a biodegradable bead comprising a mixed cellulose ester.
• the biodegradable bead exhibits at least 40 percent biodegradability at 56 days according to the OECD 301 F test method.
• the mixed cellulose ester comprises: (a) an acetyl substituent and an average degree of substitution for acetyl substituents (“DSAc”) of less than 2.3, (b) an average degree of substitution for propionyl substituents (“DSPr”) or an average degree of substitution for butyryl substituents (“DSBu”) of at least 0.1 , and (c) an average degree of substitution for hydroxyl substituents (“DSOH”) of at least 0.6.
• the present application also discloses a biodegradable bead comprising a mixed cellulose ester and an additional biodegradable cellulose ester.
• the biodegradable bead exhibits at least 40 percent biodegradability at 56 days according to the OECD 301 F test method.
• the mixed cellulose ester comprises: (a) an acetyl substituent and an average degree of substitution for acetyl substituents (“DSAc”) of less than 2.3, (b) an average degree of substitution for propionyl substituents (“DSPr”) or an average degree of substitution for butyryl substituents (“DSBu”) of at least 0.1 , and (c) an average degree of substitution for hydroxyl substituents (“DSOH”) of at least 0.6.
• the present application also discloses a process for forming biodegradable beads.
• the process comprises: (a) forming a dope comprising a mixed cellulose ester; (b) contacting at least a portion of the dope with an aqueous mixture under agitation to thereby form a reaction mixture comprising a plurality of biodegradable beads; and (c) recovering at least a portion of the biodegradable beads from the reaction mixture.
• the biodegradable beads exhibit at least 40 percent biodegradability at 56 days according to the OECD 301 F test method.
• the mixed cellulose ester comprises: (a) an acetyl substituent and an average degree of substitution for acetyl substituents (“DSAc”) of less than 2.3, (b) an average degree of substitution for propionyl substituents (“DSPr”) or an average degree of substitution for butyryl substituents (“DSBu”) of at least 0.1 , and (c) an average degree of substitution for hydroxyl substituents (“DSOH”) of at least 0.6.
• MCE mixed cellulose ester
• the CE has a degree of substitution for the acetyl substituents (“DSA C ”) is from 0.6 to 1 .9
• the CE has a degree of substitution for the propionyl substituents (“DS pr ”) is from 0.5 to 0.95
• the CE has a degree of substitution for the hydroxyl substituents (“DS OH ”) is from 0.7 to 1 .4.
• MCE mixed cellulose ester
• the MCE has an average degree of substitution for the acetyl substituents (“DSAC”) is from 0.6 to 1 .2
• the MCE has an average degree of substitution for the propionyl substituents (“DSp r ”) is from 1 .05 to 1 .4
• the MCE has an average degree of substitution for the hydroxyl substituents (“DSOH”) is from 0.7 to 1 .4.
• MCE mixed cellulose ester
• the MCE has an average degree of substitution for the acetyl substituents (“DSAC”) is from 0.9 to 2.4
• the MCE has an average degree of substitution for the butyryl substituents (“DSBU”) is from 0.1 to 1.1
• the MCE has an average degree of substitution for the hydroxyl substituents (“DSOH”) is from 0.6 to 1 .5.
• cellulose ester particles formed from a cellulose ester composition comprising:
• MCE mixed cellulose ester
• the MCE has an average degree of substitution for the acetyl substituents (“DS AC ”) that is from 0.6 to 2.4
• the MCE has an average degree of substitution for the (C2-s)alkyl- CO- substituents (“DS Akco ”) that is from 0.1 to 1.1
• the MCE has an average degree of substitution for the hydroxyl substituents (“DS OH ”) that is from 0.55 to 1 .5;
• CA cellulose acetate
• the CA has an average degree of substitution for the acetyl substituents (“DS AC ”) that is from 1 .5 to 2.6
• the CA has an average degree of substitution for the hydroxyl substituents (“DS OH ”) that is from 0.4 to 1 .5.
• the present application also discloses a dope composition
• a dope composition comprising:
• MCE mixed cellulose ester
• the MCE has an average degree of substitution for the acetyl substituents (“DS AC ”) that is from 0.6 to 2.4
• the MCE has an average degree of substitution for the (C 2- 3 )alkyl-CO- substituents (“DSAkco”) that is from 0.1 to 1.1
• the MCE has an average degree of substitution for the hydroxyl substituents (“DS OH ”) that is from 0.55 to 1 .5
• CA cellulose acetate
• the CA has an average degree of substitution for the acetyl substituents (“DS AC ”) that is from 1 .5 to 2.6, the CA has an average degree of substitution for the hydroxyl substituents (“DS OH ”) that is from 0.4 to 1 .5; and (B) a solvent, wherein the solvent comprises:
• the present disclosure is directed to cellulose acetate propionate and cellulose acetate butyrate polymers that have been designed with the appropriate mix of acetyl, propionyl/butyrate, and hydroxyl content to biodegrade in freshwater environments.
• the mixed cellulose esters disclosed herein are useful in preparing films, microbeads, and other articles.
• Values may be expressed as “about” or “approximately” a given number.
• ranges may be expressed herein as from “about” one particular value and/or to “about” or another particular value. When such a range is expressed, another aspect includes from the one particular value and/or to the other particular value.
• values are expressed as approximations, by use of the antecedent “about,” it will be understood that the particular value forms another aspect.
• the term “and/or,” when used in a list of two or more items, means that any one of the listed items can be employed by itself or any combination of two or more of the listed items can be employed. For example, if a composition is described as containing components A, B, and/or C, the composition can contain A alone; B alone; C alone; A and B in combination; A and C in combination, B and C in combination; or A, B, and C in combination.
• the terms “comprising,” “comprises,” and “comprise” are open-ended transition terms used to transition from a subject recited before the term to one or more elements recited after the term, where the element or elements listed after the transition term are not necessarily the only elements that make up the subject.
• a “mixed cellulose ester” shall denote a cellulose ester having at least two different ester substituents on a single cellulose ester polymer chain.
• “Degree of Substitution” is used to describe the average substitution level of the substituents per anhydroglucose unit (“AGU”).
• AGU anhydroglucose unit
• conventional cellulose contains three hydroxyl groups in each AGU that can be substituted. Therefore, the DS can have a value between 0 and 3.
• low molecular weight cellulose mixed esters can have a total degree of substitution slightly above 3 from end group contributions. Low molecular weight cellulose mixed esters are discussed in more detail subsequently in this disclosure. Because DS is a statistical mean value, a value of 1 does not assure that every AGU has a single substituent.
• Total DS is defined as the average number of all of substituents per anhydroglucose unit.
• the degree of substitution per AGU can also refer to a particular substituent, such as, for example, hydroxyl, acetyl, butyryl, or propionyl. Additionally, the degree of substitution can specify a given hydroxyl based on the carbon unit of the anhydroglucose unit.
• the degree of substitution refers to hydroxyl, i.e, DSOH
• the reference is to the average hydroxyl groups per anhydroglucose that are not substituted.
• DSOH is not used in the calculation of the total degree of substitution.
• each specific numerical value provided herein is to be construed as providing literal support for a broad, intermediate, and narrow range.
• the broad range associated with each specific numerical value is the numerical value plus and minus 60 percent of the numerical value, rounded to two significant digits.
• the intermediate range associated with each specific numerical value is the numerical value plus and minus 30 percent of the numerical value, rounded to two significant digits.
• the narrow range associated with each specific numerical value is the numerical value plus and minus 15 percent of the numerical value, rounded to two significant digits.
• the broad, intermediate, and narrow ranges for the pressure difference between these two streams would be 25 to 99 psi, 43 to 81 psi, and 53 to 71 psi, respectively.
• the cellulose esters can be produced by any method known in the art. Examples of processes for producing cellulose esters are taught in Kirk-Othmer, Encyclopedia of Chemical Technology, 5th Edition, Vol. 5, Wiley-lnterscience, New York (2004), pp. 394-444, the disclosure of which is incorporated by reference in its entirety.
• Cellulose the starting material for producing cellulose esters, can be obtained in different grades and from sources such as, for example, cotton linters, softwood pulp, hardwood pulp, corn fiber and other agricultural sources, and bacterial celluloses.
• cellulose esters are by esterification.
• the cellulose is mixed with the appropriate organic acids, acid anhydrides, and catalysts and then converted to a cellulose triester.
• Ester hydrolysis is then performed by adding a water-acid mixture to the cellulose triester, which can be filtered to remove any gel particles or fibers. Water is added to the mixture to precipitate out the cellulose ester.
• the cellulose ester can then be washed with water to remove reaction by-products followed by dewatering and drying.
• Acylating reagents suitable for use herein can include, but are not limited to, alkyl or aryl carboxylic anhydrides, carboxylic acid halides, and/or carboxylic acid esters containing the above-described alkyl or aryl groups suitable for use in the acyl substituents of the substituted cellulose esters described herein.
• suitable carboxylic anhydrides include, but are not limited to, acetic anhydride, propionic anhydride, butyric anhydride, pivaloyl anhydride, benzoic anhydride, and naphthoyl anhydride.
• carboxylic acid halides include, but are not limited to, acetyl, propionyl, butyryl, pivaloyl, benzoyl, and naphthoyl chlorides or bromides.
• carboxylic acid esters include, but are not limited to, acetyl, propionyl, butyryl, pivaloyl, benzoyl and naphthoyl methyl esters.
• the acylating reagent can be one or more carboxylic anhydrides selected from the group consisting of acetic anhydride, propionic anhydride, butyric anhydride, pivaloyl anhydride, benzoyl anhydride, and naphthoyl anhydride.
• the cellulose triesters that are hydrolyzed can have three substituents selected independently from alkanoyls having from 2 to 12 carbon atoms.
• examples of cellulose triesters include cellulose triacetate, cellulose tripropionate, cellulose tributyrate, or mixed triesters of cellulose, such as cellulose acetate propionate and cellulose acetate butyrate.
• These cellulose triesters can be prepared by a number of methods known to those skilled in the art.
• cellulose triesters can be prepared by heterogeneous acylation of cellulose in a mixture of carboxylic acid and anhydride in the presence of a catalyst, such as H2SO4.
• Cellulose triesters can also be prepared by the homogeneous acylation of cellulose dissolved in an appropriate solvent such as LiCI/DMAc or LiCI/NMP.
• acyl substituents After esterification of the cellulose to the triester, part of the acyl substituents can be removed by hydrolysis or by alcoholysis to give a secondary cellulose ester. Secondary cellulose esters can also be prepared directly with no hydrolysis by using a limiting amount of acylating reagent. This process is particularly useful when the reaction is conducted in a solvent that will dissolve cellulose.
• the cellulose esters thus prepared generally comprise the following structure: where R 2 , R 3 , and R 6 are hydrogen (with the proviso that R 2 , R 3 , and R 6 are not hydrogen simultaneously), alkyl-acyl groups, and/or aryl-acyl groups (such as those described above) bound to the cellulose via an ester linkage.
• the degree of polymerization (“DP”) of the cellulose esters prepared by these methods can be at least 10. In other embodiments, the DP of the cellulose esters can be at least 50, at least 100, or at least 250. In other embodiments, the DP of the cellulose esters can be in the range of from about 5 to about 100, or in the range of from about 10 to about 50.
• degree of polymerization when referring to cellulose esters, shall denote the average number of anhydroglucose monomer units per cellulose polymer chain.
• the cellulose esters can have a DP of at least 1 10, at least 120, at least 130, at least 140, at least 150, at least 160, at least 170, at least 180, at least 190, at least 200, at least 210, at least 220, at least 230, at least 240 and/or up to 350, up to 325, or up to 300.
• a mixed cellulose ester comprising: (1 ) a plurality of acetyl substituents; (2) a plurality of propionyl substituents; and (3) a plurality of hydroxyl substituents, wherein: the MCE has an average degree of substitution for the acetyl substituents (“DS AC ”) is from 0.6 to 2.3, the MCE has an average degree of substitution for the propionyl substituents (“DS pr ”) is from 0.1 to 0.95, the MCE has an average degree of substitution for the hydroxyl substituents (“DS OH ”) is from 0.5 to 1.5.
• DS AC average degree of substitution for the acetyl substituents
• DS pr average degree of substitution for the propionyl substituents
• DS OH average degree of substitution for the hydroxyl substituents
• class or subclass of this first aspect wherein the DSAC is from 0.6 to 2.2, or 0.6 to 2.1 , or 0.6 to 2.0, or 0.6 to 1 .9, or 0.6 to 1 .8, or 0.7 to 2.3, or 0.7 to 2.2, or 0.7 to 2.1 , or 0.7 to 2.0, or 0.7 to 1 .9, or 0.8 to 2.3, or 0.8 to 2.2, or 0.8 to 2.1 , or 0.8 to 2.0, or 0.8 to 1 .9, or 0.9 to 2.3, or 0.9 to 2.2, or 0.9 to 2.1 , or 0.9 to 2.0, or 0.9 to 1 .9, or 1 .0 to 2.3 or 1 .0 to 2.2, or 1 .0 to 2.1 , or 1 .0 to 2.0, or 1 .0 to 1.9, or 1.1 to 2.3, or 1.1 to 2.2, or 1.1 to 2.1 , or 1.1 to 2.0, or 1.1 to 1.9, or 1.1 to 2.3, or 1.1 to
• class or subclass of this first aspect wherein the DSp r is from 0.1 to 0.9, or 0.1 to 0.85, or 0.1 to 0.8, or 0.1 to 0.75, or 0.1 to 0.7, or 0.1 to 0.6 or 0.1 to 0.5, or 0.1 to 0.4, or 0.15 to 0.95, or 0.15 to 0.9, or 0.15 to 0.85, or 0.15 to 0.8, or 0.15 to 0.75, or 0.15 to 0.7, or 0.15 to 0.65, or 0.2 to 0.95, or 0.2 to 0.9, or 0.2 to 0.85, or 0.2 to 0.8, or 0.2 to 0.75, or 0.2 to 0.7, or 0.2 to 0.65, 0.25 to 0.95, or 0.25 to 0.9, or 0.25 to 0.85, or 0.25 to 0.8, or 0.25 to 0.75, or 0.25 to 0.7, or 0.25 to 0.65, or 0.3 to 0.95, or 0.3 to 0.9, or 0.3 to 0.85, or 0.3 to
• class or subclass of this first aspect wherein the DSOH is from 0.5 to 1 .5, or 0.5 to 1 .45, or 0.5 to 1 .40, or 0.5 to 1 .35, or 0.5 to 1 .30, or 0.5 to 1 .25, or 0.5 to 1 .2, or 0.5 to 1.15, or 0.5 to 1.1 , or 0.5 to 1.05, or 0.5 to 1.0, or 0.5 to 0.95 or 0.5 to 0.9, or 0.55 to 1 .5, or 0.55 to 1 .45, or 0.55 to 1 .40, or 0.55 to 1 .35, or 0.55 to 1 .30, or 0.55 to 1 .25, or 0.55 to 1 .2, or 0.55 to 1 .15, or 0.55 to 1 .1 , or 0.55 to 1 .05, or 0.55 to 1 .0, or 0.55 to 0.95 or 0.55 to 0.9, or 0.6 to 1 .5, or 0.6 to 1 .5, or 0.6 to 1 .5, or
• class or subclass of this first aspect wherein the sum of DSp r and DS AC is from 1 .9 to 2.44, or 1 .9 to 2.0, or 1 .9 to 2.1 , or 1 .9 to 2.2, or 1 .9 to 2.3, or 2.0 to 2.44, or 2.0 to 2.1 , or 2.0 to 2.2, or 2.0 to 2.3, or 2.1 to 2.44, or 2.1 to 2.2, or 2.1 to 2.3, or 2.2 to 2.44, or 2.2 to 2.3.
• class or subclass of this first aspect wherein the MCE exhibits at least 40% biodegradability, at least 45% biodegradability, or at least 50% biodegradability, or at least 55% biodegradability, at least 60% biodegradability, or at least 65% biodegradability, or at least 70% biodegradability, or at least 75% biodegradability, or at least 80% biodegradability, or at least 85% biodegradability, at 56 days according to the OECD 301 F test method.
• the MCE has a weight average molecular weight in the range of from 5,000 to 100,000 Da, or 5,000 to 50,000 Da, or 5,000 to 25,000 Da, or 15,000 to 100,000 Da, or 15,000 to 50,000 Da, or 15,000 to 25,000 Da, or 50,000 to 100,000 Da, or 75,000 to 100,000 Da, or 15,000 to 250,000 Da.
• the present application discloses, in a second aspect, a mixed cellulose ester (“MCE”), comprising: (1 ) a plurality of acetyl substituents; (2) a plurality of propionyl substituents; and (3) a plurality of hydroxyl substituents, wherein: the MCE has an average degree of substitution for the acetyl substituents (“DS AC ”) is from 0.6 to 1 .2, the MCE has an average degree of substitution for the propionyl substituents (“DS pr ”) is from 1 .05 to 1 .4, and the MCE has an average degree of substitution for the hydroxyl substituents (“DS OH ”) is from 0.7 to 1 .4.
• MCE mixed cellulose ester
• class or subclass of this second aspect wherein the DSAC is from 0.6 to 0.7, or 0.6 to 0.8, or 0.6 to 0.9, or 0.6 to 1 .0, or 0.6 to 1 .1 , or 0.7 to 0.9, or 0.7 to 1 .0, or 0.7 to 1.1 , or 0.7 to 1 .2, or 0.8 to 0.9, or 0.8 to 1 .0, or 0.8 to 1.1 , or 0.8 to 1 .2, or 0.9 to 1 .0, or 0.9 to 1 .1 , or 0.9 to 1 .2, or 1 .0 to 1 .1 , or 1 .0 to 1 .2, or 1 .0 to 1 .1 , or 1 .0 to 1 .2, or 1 .1 to
• class or subclass of this second aspect wherein the DSp r is from 1 .05 to 1 .35, or 1.05 to 1.3, or 1.05 to 1.25, or 1.05 to 1.2, or 1.05 to 1.15, or 1.05 to 1.1 , or 1 .1 to 1 .4, or 1 .1 to 1 .35, or 1 .1 to 1 .3, or 1 .1 to 1 .25, or 1.1 to 1 .2, or 1 .1 to 1 .15, or 1 .15 to 1 .4, or 1 .15 to 1 .35, or 1 .15 to 1 .3, or 1 .15 to 1 .25, or 1 .15 to
• class or subclass of this second aspect wherein the DSOH is from 0.7 to 1 .35, or 0.7 to 1 .3, or 0.7 to 1 .25, or 0.7 to 1 .2, or 0.7 to 1 .15, or 0.7 to 1 .1 , or 0.7 to 1 .05, or 0.7 to 1 .0, or 0.7 to 0.95, or 0.7 to 0.9, or 0.7 to 0.85, or 0.7 to 0.8, or 0.7 to 0.75, or 0.75 to 1 .4, or 0.75 to 1 .35, or 0.75 to 1 .3, or 0.75 to 1 .25, or 0.75 to 1 .2, or 0.75 to 1 .15, or 0.75 to 1 .1 , or 0.75 to 1 .05, or 0.75 to 1 .0, or 0.75 to 0.95, or 0.8 to 1 .4, or 0.8 to 1 .35, or 0.8 to 1 .3, or 0.8 to 1 .25, or 0.7 to 1 .2, or 0.8 to 1
• class or subclass of this second aspect wherein the sum of DSp r and DSAC is from 1 .65 to 2.3, or 1 .65 to 2.2, or 1 .65 to 2.1 , or 1 .65 to 2.0, or 1 .65 to 1 .9, or 1 .65 to 1 .8, or 1 .7 to 2.3, or 1 .7 to 2.2, or 1 .7 to 2.1 , or 1 .7 to 2.0, or 1 .7 to 1 .9, or 1 .7 to 1 .8, or 1 .75 to 2.3, or 1 .75 to 2.2, or 1 .75 to 2.1 , or 1 .75 to 2.0, or 1 .75 to 1 .9, or 1 .8 to 2.3, or 1 .8 to 2.2, or 1 .8 to 2.1 , or 1 .8 to 2.0, or 1 .8 to 1 .9, or 1 .9 to 2.3, or 1 .8 to 2.0, or 1 .8 to
• class or subclass of this second aspect wherein the DSOH is from 0.6 to 0.7, or 0.7 to 1 .35, or 0.7 to 1 .3, or 0.7 to 1 .25, or 0.7 to 1 .2, or 0.7 to 1 .15, or 0.7 to 1.1 , or 0.7 to 1 .05, or 0.7 to 1 .0, or 0.7 to 0.95, or 0.7 to 0.9, or 0.7 to 0.85, or 0.7 to 0.8, or 0.7 to 0.75, or 0.75 to 1 .4, or 0.75 to 1 .35, or 0.75 to 1 .3, or 0.75 to 1 .25, or 0.75 to 1 .2, or 0.75 to 1 .15, or 0.75 to 1 .1 , or 0.75 to 1 .05, or 0.75 to 1 .0, or 0.75 to 0.95, or 0.8 to 1 .4, or 0.8 to 1 .35, or 0.8 to 1 .35, or 0.8 to 1 .3, or 0.8 to 1 .3,
• class or subclass of this second aspect wherein the MCE exhibits at least 40% biodegradability, at least 45% biodegradability, or at least 50% biodegradability, or at least 55% biodegradability, at least 60% biodegradability, or at least 65% biodegradability, or at least 70% biodegradability, or at least 75% biodegradability, or at least 80% biodegradability, or at least 85% biodegradability, at 56 days according to the
• the MCE has a weight average molecular weight in the range of from 5,000 to 100,000 Da, or 5,000 to 50,000 Da, or 5,000 to 25,000 Da, or 15,000 to 100,000 Da, or 15,000 to 50,000 Da, or 15,000 to 25,000 Da, or 50,000 to 100,000 Da, or 75,000 to 100,000 Da, or 15,000 to 250,000 Da.
• the present application in a third aspect, also discloses a mixed cellulose ester (“MCE”), comprising: (1 ) a plurality of acetyl substituents; (2) a plurality of butyryl substituents; and (3) a plurality of hydroxyl substituents, wherein: the MCE has an average degree of substitution for the acetyl substituents (“DS AC ”) is from 0.9 to 2.4, the MCE has an average degree of substitution for the butyryl substituents (“DS BU ”) is from 0.1 to 1.1 , the MCE has an average degree of substitution for the hydroxyl substituents (“DS OH ”) is from 0.6 to 1.5.
• MCE mixed cellulose ester
• class or subclass of this third aspect wherein the DSAC is from 0.9 to 2.4, 0.9 to 2.3, or 0.9 to 2.2, or 0.9 to 2.1 , or 0.9 to 2.0, or 0.9 to 1 .9, or 0.9 to 1 .8, or 0.9 to 1 .7, or 0.9 to 1 .6, or 0.9 to 1 .4, 0.9 to 1 .3, or 0.9 to 1 .2, or 0.9 to 1 .1 , or 0.9 to
• 2.2 or 1.1 to 2.1 , or 1.1 to 2.0, or 1.1 to 1.9, or 1.1 to 1.8, or 1.1 to 1.7, or 1.1 to 1 .6, 1 .1 to 1 .4, or 1 .1 to 1 .3, or 1 .1 to 1 .2, or 1 .2 to 2.4, or 1 .2 to 2.3, or 1 .2 to 2.2, or 1 .2 to 2.1 , or 1 .2 to 2.0, or 1 .2 to 1 .9, or 1 .2 to 1 .8, or 1 .2 to 1 .7, or
• class or subclass of this third aspect wherein the DSBU is from 0.1 to 1 .35, or 0.1 to 1 .3, or 0.1 to 1 .25, or 0.1 to 1 .2, or 0.1 to 1.15, or 0.1 to 1 .1 , or 0.1 to 1 .0, or 0.1 to 0.8, or 0.1 to 0.6, or 0.2 to 1 .35, or 0.2 to 1 .3, or 0.2 to 1 .25, or 0.2 to
• class or subclass of this third aspect wherein the DSOH is from 0.5 to 1 .0, or 0.5 to 0.95, or 0.5 to 0.9, or 0.5 to 0.85, or 0.5 to 0.8, or 0.5 to 0.75, or 0.5 to 0.7, or 0.5 to 0.65, or 0.5 to 0.6, or 0.5 to 0.55, or 0.55 to 1 .0, or 0.55 to 0.95, or 0.55 to 0.9, or 0.55 to 0.85, or 0.55 to 0.8, or 0.55 to 0.75, or 0.55 to 0.7, or 0.55 or 0.65, or 0.55 to 0.6, or 0.6 to 0.65, or 0.6 to 0.7, or 0.6 to 0.75, or 0.6 to 0.8, or 0.6 to 0.85, or 0.6 to 0.9, or 0.6 to 0.95, or 0.6 to 1 .0, or 0.65 to 0.7, or 0.65 to 0.75, or 0.65 to 0.8, or 0.65 to 0.85, or 0.6 to 0.9, or 0.6 to 0.95, or
• class or subclass of this third aspect wherein the sum of DS BU and DS AC is from 1 .65 to 2.3, or 1 .65 to 2.2, or 1 .65 to 2.1 , or 1 .65 to 2.0, or 1 .65 to 1 .9, or 1 .65 to 1 .8, or 1 .7 to 2.3, or 1 .7 to 2.2, or 1 .7 to 2.1 , or 1 .7 to 2.0, or 1 .7 to 1 .9, or 1 .7 to 1 .8, or 1 .75 to 2.3, or 1 .75 to 2.2, or 1 .75 to 2.1 , or 1 .75 to 2.0, or 1 .75 to 1 .9, or 1 .8 to 2.3, or 1 .8 to 2.2, or 1 .8 to 2.1 , or 1 .8 to 2.0, or 1 .8 to 1 .9, or 1 .9 to 2.3, or 1 .
• class or subclass of this third aspect wherein the MCE exhibits at least 40% biodegradability, at least 45% biodegradability, or at least 50% biodegradability, or at least 55% biodegradability, at least 60% biodegradability, or at least 65% biodegradability, or at least 70% biodegradability, or at least 75% biodegradability, or at least 80% biodegradability, or at least 85% biodegradability, at 56 days according to the OECD 301 F test method.
• the MCE has a weight average molecular weight in the range of from 5,000 to 100,000 Da, or 5,000 to 50,000 Da, or 5,000 to 25,000 Da, or 15,000 to 100,000 Da, or 15,000 to 50,000 Da, or 15,000 to 25,000 Da, or 50,000 to 100,000 Da, or 75,000 to 100,000 Da, or 15,000 to 250,000 Da.
• the present application also discloses, in a fourth aspect, a composition comprising any of the previously disclosed mixed cellulose esters.
• the compositions may comprise at least 55, at least 60, at least 65, at least 70, at least 75, at least 80, at least 85, at least 90, at least 95, or at least 99 wt% of one or more of the biodegradable mixed cellulose esters described herein, based on the total weight of the cellulose ester composition. Additionally, or in the alternative, the compositions may comprise less than 99, less than 95, less than 90, less than 85, less than 80, less than 75, or less than 70 wt% of one or more of the biodegradable mixed cellulose esters described herein, based on the total weight of the cellulose ester composition.
• composition further comprises a plasticizer.
• the plasticizer reduces the melt temperature, the Tg, and/or the melt viscosity of the MCE.
• the plasticizer is triacetin, triethyl citrate, polyethylene glycol), Benzoflex, propylene glycol, polysorbatemsucrose octaacetate, acetylated triethyl citrate, acetyl tributyl citrate, Admex, tripropionin, Scandiflex, poloxamer copolymers, polyethylene glycol succinate, diisobutyl adipate, polyvinyl pyrollidone, and glycol tribenzoate.
• the plasticizer is present in an amount of from 1 to 40 wt%, or 1 to 30 wt%, or 1 to 20 wt%, or 1 to 10 wt%, or 1 to 5 wt%, or 5 to 40 wt%, or 5 to 30 wt%, or 5 to 20 wt%, or 5 to 10 wt%, or 5 to 5 wt%, or 10 to 40 wt%, or 10 to 30 wt%, or 10 to 20 wt%, or 10 to 10 wt%, or 10 to 5 wt%, 15 to 40 wt%, or 15 to 30 wt%, or 15 to 20 wt%, or 15 to 10 wt%, or 15 to 5 wt%, based on the weight of the cellulose ester composition.
• the plasticizer is a biodegradable plasticizer.
• biodegradable plasticizers include triacetin, triethyl citrate, acetyl triethyl citrate, polyethylene glycol, the benzoate- containing plasticizers such as the BenzoflexTM plasticizer series, poly (alkyl succinates) such as poly (butylene succinate), polyethersulfones, adipate- based plasticizers, soybean oil epoxides such as the ParaplexTM plasticizer series, sucrose-based plasticizers, dibutyl sebacate, tributyrin, sucrose acetate isobutyrate, the ResolflexTM series of plasticizers, triphenyl phosphate, glycolates, polyethylene glycol), 2,2,4-trimethylpentane-1 ,3-diyl bis(2-methylpropanoate), and polycaprolactones.
• the composition further comprises at least one biodegradable polymer that is different than the MCE.
• the biodegradable polymer is chosen from polyhydroxyalkanoates (PHAs and PHBs), poly(lactic acid) (PLA), polycaprolactone polymers (PCL), poly(butylene adipate coterephthalate) (PBAT), polyethylene succinate) (PES), poly(vinyl acetates) (PVAs), poly(butylene succinate) (PBS) and copolymers [such as poly(butylene succinate-co-adipate) (PBSA)], other cellulose esters, cellulose ethers, starch, proteins, derivatives thereof, and combinations thereof.
• the biodegradable polymer is a biodegradable cellulose ester that is different from the biodegradable mixed cellulose ester described herein, such as a cellulose acetate.
• the composition comprises two or more biodegradable polymers.
• the composition comprises a biodegradable polymer in an amount from 0.1 to 60 wt%, 0.1 to 50 wt%, or 0.1 to 40wt%, or 0.1 to 30wt%, or 0.1 to 20wt%, or 0.1 to 15wt%, or 0.1 to 10wt%, or 0.1 to 5 wt%, or 1 to 40 wt%, or 1 to 30 wt%, or 1 to 25 wt%, or 1 to 20 wt%, or 1 to 10 wt%, or 1 to 5wt%, or 5 to 40 wt%, or 5 to 30 wt%, or 5 to 25 wt%, or 5 to 20 wt%, or 5 to 10 wt%, based on the total weight of the composition.
• class or subclass of this fourth aspect wherein the composition further comprises at least one of a filler, an additive, a stabilizer, and/or odor modifier.
• the filler is of a type and present in an amount to enhance biodegradability and/or compostability.
• the composition comprises at least one filler chosen from: carbohydrates (sugars and salts), cellulosic and organic fillers (wood flour, wood fibers, hemp, carbon, coal particles, graphite, and starches), mineral and inorganic fillers (calcium carbonate, talc, silica, titanium dioxide, glass fibers, glass spheres, boronitride, aluminum trihydrate, magnesium hydroxide, calcium hydroxide, alumina, and clays), food wastes or byproduct (eggshells, distillers grain, and coffee grounds), desiccants (e.g. calcium sulfate, magnesium sulfate, magnesium oxide, calcium oxide), alkaline fillers (e.g., Na2CC>3, MgCOa), or combinations (e.g., mixtures) of these fillers.
• carbohydrates sacgars and salts
• cellulosic and organic fillers wood flour, wood fibers, hemp, carbon, coal particles, graphite, and starches
• mineral and inorganic fillers calcium carbonate,
• the composition can include at least one filler that also functions as a colorant additive.
• the colorant additive filler can be chosen from: carbon, graphite, titanium dioxide, opacifiers, dyes, pigments, toners and combinations thereof.
• the composition can include at least one filler that also functions as a stabilizer or flame retardant.
• the composition further comprises at least one filler in an amount from 1 to 60 wt%, or 5 to 55 wt%, or 5 to 50 wt%, or 5 to 45 wt%, or 5 to 40 wt%, or 5 to 35 wt%, or 5 to 30 wt%, or 5 to 25 wt%, or 10 to 55 wt%, or 10 to 50 wt%, or 10 to 45 wt%, or 10 to 40 wt%, or 10 to 35 wt%, or 10 to 30 wt%, or 10 to 25 wt%, or 15 to 55 wt%, or 15 to 50 wt%, or 15 to 45 wt%, or 15 to 40 wt%, or 15 to 35 wt%, or 15 to 30 wt%, or 15 to 25 wt%, or 20 to 55 wt%, or 20 to 50 wt%, or 20 to 45
• the stabilizer is at least one of a UV absorber, an antioxidant (e.g., ascorbic acid, BHT, BHA, etc), acid or radical scavengers, epoxidized oils (e.g., epoxidized soybean oil), or combinations thereof.
• an antioxidant e.g., ascorbic acid, BHT, BHA, etc
• acid or radical scavengers e.g., ascorbic acid, BHT, BHA, etc
• epoxidized oils e.g., epoxidized soybean oil
• the stabilizer comprises one or more secondary antioxidants.
• the stabilizer comprises a first stabilizer component chosen from one or more secondary antioxidants and a second stabilizer component chosen from one or more primary antioxidants, citric acid or a combination thereof.
• the additive is an organic acid, a salt, a wax, a compatibilizer, a biodegradation promoter, a dye, a pigment, a colorant, a luster control agent, a lubricant, an antioxidant, a viscosity modifier, an antifungal agent, an anti-fogging agent, an impact modifier, an antibacterial agent, a softening agent, a mold release agent, or combinations thereof. It should be noted that the same type of compounds or materials can be identified for or included in multiple categories of components in the compositions.
• polyethylene glycol could function as a plasticizer or as an additive that does not function as a plasticizer, such as a hydrophilic polymer or biodegradation promotor, e.g., where a lower molecular weight PEG has a plasticizing effect and a higher molecular weight PEG functions as a hydrophilic polymer but without plasticizing effect.
• a plasticizer such as a hydrophilic polymer or biodegradation promotor, e.g., where a lower molecular weight PEG has a plasticizing effect and a higher molecular weight PEG functions as a hydrophilic polymer but without plasticizing effect.
• Antioxidants can be classified into several classes, including primary antioxidant, and secondary antioxidant.
• Primary antioxidants a generally known to function essentially as free radical terminators (scavengers).
• Secondary antioxidants are generally known to decompose hydroperoxides (ROOH) into nonreactive products before they decompose into alkoxy and hydroxy radicals.
• Secondary antioxidants are often used in combination with free radical scavengers (primary antioxidants) to achieve a synergistic inhibition effect and secondary AOs are used to extend the life of phenolic type primary AOs.
• Primary antioxidants are antioxidants that act by reacting with peroxide radicals via a hydrogen transfer to quench the radicals.
• Primary antioxidants generally contain reactive hydroxy or amino groups such as in hindered phenols and secondary aromatic amines. Examples of primary antioxidants include BHT, IrganoxTM 1010, 1076, 1726, 245, 1098, 259, and 1425; EthanoxTM 310, 376, 314, and 330; EvernoxTM 10, 76, 1335, 1330, 3114, MD 1024, 1098, 1726, 120.
• Secondary antioxidants are often called hydroperoxide decomposers. They act by reacting with hydroperoxides to decompose them into nonreactive and thermally stable products that are not radicals. They are often used in conjunction with primary antioxidants. Examples of secondary antioxidants include the organophosphorous (e.g., phosphites, phosphonites) and organosulfur classes of compounds. The phosphorous and sulfur atoms of these compounds react with peroxides to convert the peroxides into alcohols.
• secondary antioxidants include Ultranox 626, EthanoxTM 368, 326, and 327; Doverphos TM LPG11 , LPG12, DP S-680, 4, 10, S480, S-9228, S-9228T; Evernox TM 168 and 626; IrgafosTM 126 and 168; WestonTM DPDP, DPP, EHDP, PDDP, TDP, TLP, and TPP; MarkTM CH 302, CH 55, TNPP, CH66, CH 300, CH 301 , CH 302, CH 304, and CH 305; ADK Stab 2112, HP- 10, PEP-8, PEP-36, 1178, 135A, 1500, 3010, C, and TPP; Weston 439, DHOP, DPDP, DPP, DPTDP, EHDP, PDDP, PNPG, PTP, PTP, TDP, TLP, TPP, 398, 399, 430, 705, 705T, TLTTP, and TN
• the odor modifier can be chosen from: vanillin, Pennyroyal M-1178, almond, cinnamyl, spices, spice extracts, volatile organic compounds or small molecules, and Plastidor.
• the odor modifier is vanillin.
• the odor modifier is present in an amount from 0.01 to 1 wt%, or 0.1 to 0.5 wt%, or 0.1 to 0.25 wt%, or 0.1 to 0.2 wt%, based on the total weight of the composition.
• Mechanisms for the odor modifying additives can include masking, capturing, complementing or combinations of these.
• the compatibilizer is a non-reactive compatibilizer or a reactive compatibilizer.
• the compatibilizer can enhance the ability of the MCE or another component to reach a desired small particle size to improve the dispersion of the chosen component in the composition.
• the compatibilizer is present in an amount from about 1 to about 40 wt%, or about 1 to about 30 wt%, or about 1 to about 20 wt%, or about 1 to about 10 wt%, or about 5 to about 20 wt%, or about 5 to about 10 wt%, or about 10 to about 30 wt%, or about 10 to about 20 wt%, based on the weight of the composition.
• the salt is an alkaline earth metal oxide, an alkaline earth metal hydroxide, an alkaline earth metal carbonate, an alkali metal carbonate, an alkali metal bicarbonate, ZnO, and basic A12O3.
• the salt is MgO, Mg(OH) 2 , MgCO 3 , CaO, Ca(OH) 2 , CaCO 3 , NaHCO 3 , Na 2 CO 3 , K 2 CO 3 , ZnO KHCO 3 or basic AI 2 O 3 .
• the organic acid is acetic acid, propionic acid, butyric acid, valeric acid, citric acid, tartaric acid, oxalic acid, malic acid, benzoic acid, formate, acetate, propionate, butyrate, valerate citrate, tartarate, oxalate, malate, maleic acid, maleate, phthalic acid, phthalate, benzoate, and combinations thereof.
• the biodegradation promoter may include glycols, polyglycols, polyethers, and polyalcohols or other biodegradable polymers such as poly(glycolic acid), poly(lactic acid), polyethylene glycol, polypropylene glycol, polydioxanes, polyoxalates, polyphydroxy esters), polycarbonates, polyanhydrides, polyacetals, polycaprolactones, poly(orthoesters), polyamino acids, aliphatic polyesters such as poly(butylene)succinate, poly(ethylene)succinate, starch, regenerated cellulose, or aliphatic-aromatic polyesters such as PBAT.
• biodegradation promoter may include glycols, polyglycols, polyethers, and polyalcohols or other biodegradable polymers such as poly(glycolic acid), poly(lactic acid), polyethylene glycol, polypropylene glycol, polydioxanes, polyoxalates, polyphydroxy est
• the colorant can include carbon black, iron oxides such as red or blue iron oxides, titanium dioxide, silicon dioxide, cadmium red, calcium carbonate, kaolin clay, aluminum hydroxide, barium sulfate, zinc oxide, aluminum oxide, and organic pigments such as azo and diazo and triazo pigments, condensed azo, azo lakes, naphthol pigments, anthrapyrimidine, benzimidazolone, carbazole, diketopyrrolopyrrole, flavanthrone, indigoid pigments, isoindolinone, isoindoline, isoviolanthrone, metal complex pigments, oxazine, perylene, perinone, pyranthrone, pyrazoloquinazolone, quinophthalone, triarylcarbonium pigments, triphendioxazine, xanthene, thioindi
• iron oxides such as red or blue iron oxides, titanium dioxide, silicon dioxide, cadmi
• the luster control agent can include silica, talc, clay, barium sulfate, barium carbonate, calcium sulfate, calcium carbonate, magnesium carbonate, and the like.
• the antifungal and/or antibacterial agents include polyene antifungals (e.g., natamycin, rimocidin, filipin, nystatin, amphotericin B, candicin, and hamycin), imidazole antifungals such as miconazole (available as MICATIN® from WellSpring Pharmaceutical Corporation), ketoconazole (commercially available as NIZORAL® from McNeil consumer Healthcare), clotrimazole (commercially available as LOTRAMIN® and LOTRAMIN AF® available from Merck and CANESTEN® available from Bayer), econazole, omoconazole, bifonazole, butoconazole, fenticonazole, isoconazole, oxiconazole, sertaconazole (commercially available as ERTACZO® from OrthoDematologics), sulconazole, and tioconazo
• polyene antifungals e.g., natamycin, rimo
• viscosity modifiers having the purpose of modifying the melt flow index or viscosity of the composition that can be used include polyethylene glycols and polypropylene glycols, and glycerin.
• the mold release agent or lubricant e.g. fatty acids, ethylene glycol distearate
• anti-block or slip agents e.g. fatty acid esters, metal stearate salts (for example, zinc stearate), and waxes
• antifogging agents e.g. surfactants
• thermal stabilizers e.g. epoxy stabilizers, derivatives of epoxidized soybean oil (ESBO), linseed oil, and sunflower oil
• anti-static agents foaming agents, biocides, impact modifiers, or reinforcing fibers.
• DOC dissolved organic carbon
• CO2 dissolved organic carbon
• oxygen uptake There are three main methods for testing the biodegradation of a material: the Sturm method, respirometry method, and the radio-labeled 14 C atom test method.
• the Sturm method precisely measures carbon dioxide production through a change in pressure.
• the respirometry test precisely measures the oxygen consumption over 60 days.
• the radio-labeled 14C atom test determines 14 C conversion to 14 CO 2 . All three methods can be used under aquatic or composting conditions if the right equipment is used.
• Freshwater Modified Sturm Test (OECD 301 B) - The amount of carbon dioxide (CO2) produced as a percentage of theoretical yield (based on total organic carbon analysis) is used as a basis for assessing whether the material biodegrades. CO2 is measured by way of a sodium hydroxide trap. The study is run for a minimum of 28 days and may be continued if the yield of CO2 is showing signs of increase towards the end of the 28-day period.
• Biodegradation Test - O2 Consumption may be used to monitor biodegradation of polymeric materials.
• OECD 301 F is an aquatic aerobic biodegradation test that determines the biodegradability of a material by measuring oxygen consumption.
• OECD 301 F is most often used for insoluble and volatile materials that are challenged by OECD 301 B testing.
• the purity or proportions of major components of the test material is important for calculating the Theoretical Oxygen Demand (ThOD).
• the standard test duration for OECD 301 F is a minimum of 28 days and can measure ready or inherent biodegradability.
• a solution or suspension, of the test substance in a mineral medium is inoculated and incubated under aerobic conditions in the dark or in diffuse light.
• a reference compound typically sodium acetate or sodium benzoate
• biodegradability there are three classifications of biodegradability: readily biodegradable, inherently biodegradable, and not biodegradable.
• a material is readily biodegradable if it reaches ⁇ 60% of its theoretical oxygen demand within 28 days.
• Inherently biodegradable materials also reach the 60% level, but only after the 28-day window has passed. Normally, the test for materials that are readily biodegradable lasts for 28 days, while a prolonged test period may be used to classify materials as inherently biodegradable.
• the OxiTop method is a modified Sturm method to analyze biodegradation while reporting biodegradability as oxygen consumption, converting the pressure from the CO 2 produced during the test to BOD, biological oxygen demand.
• OxiTop provides precise measurement in an easy- to-use format for aquatic biodegradation.
• Biological Oxygen Demand [BOD] was measured over time using an OxiTop® Control OC 110 Respirometer system. This is accomplished by measuring the negative pressure that develops when oxygen is consumed in the closed bottle system. NaOH tablets are added to the system to collect the CO 2 given off when O 2 is consumed. The CO 2 and NaOH react to form Na 2 CO 3 , which pulls CO 2 out of the gas phase and causes a measurable negative pressure.
• the OxiTop measuring heads record this negative pressure value and relay the information wirelessly to a controller, which converts CO 2 produced into BOD due to the 1 :1 ratio.
• the measured biological oxygen demand can be compared to the theoretical oxygen demand of each test material to determine the percentage of biodegradation.
• the OxiTop can be used to screen materials for ready or inherent biodegradability. Beads and Articles Formed from the Mixed Cellulose Ester Compositions
• the present application also discloses, of a fifth aspect, an article comprising any one of the previously disclosed mixed cellulose esters.
• the present application also discloses, of a sixth aspect, a biodegradable bead comprising any one of the previously disclosed mixed cellulose esters (i.e., the first aspect, second aspect, and/or the third aspect) or cellulose ester compositions (i.e., the fourth aspect).
• the biodegradable beads may be produced by: (i) forming a dope comprising any one of the previously disclosed mixed cellulose esters and/or mixed cellulose ester compositions; (ii) contacting at least a portion of the dope with an aqueous mixture under agitation to thereby form a reaction mixture comprising a plurality of biodegradable beads; and (iii) recovering at least a portion of the biodegradable beads from the reaction mixture.
• An exemplary bead forming procedure is described in EP0750007A1 , the disclosure of which is incorporated by reference in its entirety.
• the dope may further comprise an alkanol (e.g., methanol, ethanol, and/or propanol).
• alkanol e.g., methanol, ethanol, and/or propanol
• the dope may further comprise a compound comprising a carboxyl, a first C1 -C3 alkyl, and a second C1 -C2 alkyl.
• this compound may be an alkyl acetate.
• the dope may further comprise an alkyl acetate, such as methyl acetate.
• the dope may further comprise water, an alkanol, and an alkyl acetate, such as ethyl acetate.
• the aqueous mixture may comprise an alkyl acetate (e.g., ethyl acetate) and/or methyl cellulose.
• the aqueous mixture may comprise water, an alkyl acetate (e.g., ethyl acetate), a surfactant, and methyl cellulose.
• an alkyl acetate e.g., ethyl acetate
• a surfactant e.g., methyl cellulose
• the biodegradable beads may be recovered from the reaction mixture via one or more centrifugal steps and/or one or more filtration steps.
• the forming and contacting steps can occur at temperatures in the range of 5 to 40 °C (e.g., room temperature) and at a pressure of less than 3 atm (e.g., atmospheric pressure).
• the formed beads may be subjected to a drying treatment at a temperature range of 75 to 150 °C for 4 to 24 hours after the recovery steps.
• the biodegradable beads exhibit at least 40% biodegradability at 56 days according to the OECD 301 F test method.
• the biodegradable beads exhibit at least 40% biodegradability, at least 45% biodegradability, or at least 50% biodegradability, or at least 55% biodegradability, at least 60% biodegradability, or at least 65% biodegradability, or at least 70% biodegradability, or at least 75% biodegradability, or at least 80% biodegradability, or at least 85% biodegradability, at 56 days according to the OECD 301 F test method.
• the biodegradable beads may comprise at least 55, at least 60, at least 65, at least 70, at least 75, at least 80, at least 85, at least 90, at least 95, or at least 99 wt% of one or more of the biodegradable mixed cellulose esters described herein, based on the total weight of the bead. Additionally, or in the alternative, the biodegradable beads may comprise less than 99, less than 95, less than 90, less than 85, less than 80, less than 75, or less than 70 wt% of one or more of the biodegradable mixed cellulose esters described herein, based on the total weight of the bead.
• the biodegradable beads may comprise from 60 wt% to 99 wt% of one or more of the biodegradable mixed cellulose esters described herein, based on the total weight of the bead.
• the biodegradable beads may comprise at least 55, at least 60, at least 65, at least 70, at least 75, at least 80, at least 85, at least 90, at least 95, or at least 99 wt% of the biodegradable mixed cellulose ester compositions described herein, based on the total weight of the bead. Additionally, or in the alternative, the biodegradable beads may comprise less than 99, less than 95, less than 90, less than 85, less than 80, less than 75, or less than 70 wt% of one or more of the biodegradable mixed cellulose ester compositions described herein, based on the total weight of the bead.
• the biodegradable beads may comprise from 60 wt% to 99 wt% of one or more of the biodegradable mixed cellulose ester compositions described herein, based on the total weight of the bead.
• the biodegradable beads may comprise: (1 ) any of the mixed cellulose esters described herein and (2) a biodegradable cellulose acetate having an average degree of substitution for the acetyl substituents (“DS AC ”) from 1 .5 to 2.6 and an average degree of substitution for the hydroxyl substituents (“DS OH ”) from 0.4 to 1.5.
• the biodegradable beads may comprise from 55 wt% to 99 wt%, 60 wt% to 99 wt%, 65 wt% to 99 wt%, 70 wt% to 99 wt%, 75 wt% to 99 wt%, 80 wt% to 99 wt%, or 85 wt% to 99 wt% of one or more mixed cellulose esters described herein and 1 wt% to 15 wt%, 1 wt% to 20 wt%, 1 wt% to 25 wt%, 1 wt% to 30 wt%, 1 wt% to 35 wt%, 1 wt% to 40 wt%, or 1 wt% to 45 wt% of the biodegradable cellulose acetate, based on the total weight of the bead.
• the bead has a diameter of from 0.5 to 100 microns, or 0.5 to 50 microns, or 0.5 to 40 microns, or 0.5 to 30 microns, or 0.5 to 20 microns, or 0.5 to 10 microns, or 1 to 100 microns, or 1 to 70 microns, or 1 to 60 microns, or 1 to 50 microns, 1 to 52 microns, or 1 to 40 microns, or 1 to 30 microns, or 1 to 20 microns, or 1 to 10 microns.
• the bead exhibits a sphericity of from 50 to 100%, or 60 to 100%, or 70 to 100%, or 80 to 100%, or 90 to 100%, or 50 to 90%, or 50 to 80%, or 50 to 70%, or 60 to 90%, or 60 to 80%, or 60 to 70%, or 70 to 90%, or 70 to 80%, or 80 to 90%, or at least 70%, or at least 80%, or at least 90%.
• the sphericity can be determined according to the procedure disclosed in U.S. Pat. Pub. No. 2020/0299488.
• the bead exhibits an oil absorption of at least 30 mL per 100 g or 35 mL per 100 g, or 40 mL per 100 g, or 45 mL per 100 g, or 50 mL per 100 g, or 55 mL per 100 g, or 60 mL per 100 g as measured using test method ASTM D281 , wherein mineral oil is used instead of castor oil.
• the biodegradable beads have a bulk density in the range of 0.2 to 0.7, 0.2 to 0.6, 0.3 to 0.6, or 0.3 to 0.7.
• the biodegradable beads have an average surface area of at least 0.1 , at least 0.5, at least 1 , at least 2, at least 3, at least 4, at least 5, at least 6, at least 7, at least 8, at least 9, at least 10 m 2 /g. Additionally, or in the alternative, the biodegradable beads may have an average surface area of less than 20, less than 19, less than 18, less than 17, less than 16, less than 15, less than 14, less than 13, less than 12, less than 1 1 , or less than 10 m 2 /g.
• the biodegradable beads exhibit at least one of the following: (i) an average particle size of from 1 micron to 60 microns, (ii) a bulk density of from 0.2 to 0.7, (iii) an average surface area of 0.1 m 2 /g to 10 m 2 /g, or (iv) a sphericity of from 70% to 100%.
• the bead further comprises a cellulose acetate, wherein the cellulose acetate has an average degree of substitution for the acetyl substituents (“DSAC”) of from 1 .5 to 2.6.
• the DSAC is from 1 .8 to 2.2, or 1 .5 to 2.0, or 1 .8 to 2.0, or 2.0 to 2.2.
• the bead exhibits an oil absorption of at least 30 mL per 100 g or 35 mL per 100 g, or 40 mL per 100 g, or 45 mL per 100 g, or 50 mL per 100 g, or 55 mL per 100 g, or 60 mL per 100 g as measured using test method ASTM D281 , wherein mineral oil is used instead of castor oil.
• the present application also discloses, of a seventh aspect, a composition comprising a plurality of the beads previously disclosed herein.
• the present application also discloses, of an eighth aspect, a film comprising any one of the previously disclosed mixed cellulose esters.
• the present application also discloses, of a ninth aspect, a film prepared from any one of the previously disclosed compositions or mixed cellulose esters.
• the composition further comprises 1 to 40 wt% of a cellulose acetate, wherein the cellulose acetate exhibits an average degree of substitution for the acetyl substituents of from 1 .5 to 2.6.
• the DSAC is from 1 .8 to 2.2, or 1 .5 to 2.0, or 1 .8 to 2.0, or 2.0 to 2.2.
• cellulose ester particles formed from a cellulose ester composition comprising: (I) a mixed cellulose ester (“MCE”) comprising: (1 ) a plurality of acetyl substituents; (2) a plurality of (C 2-3 )alkyl-CO- substituents; and (3) a plurality of hydroxyl substituents, wherein: the MCE has an average degree of substitution for the acetyl substituents (“DS AC ”) that is from 0.6 to 2.4, the MCE has an average degree of substitution for the (C 2-3 )alkyl-CO- substituents (“DSAkco”) that is from 0.1 to 1 .1 , the MCE has an average degree of substitution for the hydroxyl substituents (“DSOH”) that is from 0.55 to 1 .5; and (II) a cellulose acetate (“CA”), comprising: a plurality of acetyl substituents; and a plurality of hydroxyl substituents
• the (C 2-3 )alkyl-CO- is propionyl. In one embodiment or in combination with any other embodiment, class or subclass of this tenth aspect, the (C 2-3 )alkyl-CO- is butyryl.
• the MCE is present at from 60 wt% to 99 wt%, and the CA is present at from 1 wt% to 40 wt%, based on the total weight of the cellulose ester composition. In one embodiment or in combination with any other embodiment, class or subclass of this tenth aspect, the MCE is present at from 55 wt% to 99 wt%, and the CA is present at from 1 wt% to 45 wt%, based on the total weight of the cellulose ester composition.
• the MCE is present at from 65 wt% to 99 wt%, and the CA is present at from 1 wt% to 35 wt%, based on the total weight of the cellulose ester composition. In one embodiment or in combination with any other embodiment, class or subclass of this tenth aspect, the MCE is present at from 70 wt% to 99 wt%, and the CA is present at from 1 wt% to 30 wt%, based on the total weight of the cellulose ester composition.
• the MCE is present at from 75 wt% to 99 wt%, and the CA is present at from 1 wt% to 25 wt%, based on the total weight of the cellulose ester composition. In one embodiment or in combination with any other embodiment, class or subclass of this tenth aspect, the MCE is present at from 80 wt% to 99 wt%, and the CA is present at from 1 wt% to 20 wt%, based on the total weight of the cellulose ester composition.
• the MCE is present at from 85 wt% to 99 wt%
• the CA is present at from 1 wt% to 25 wt%, based on the total weight of the cellulose ester composition.
• the cellulose ester particles exhibit at least one of the following: (i) an average particle size of from 1 micron to 60 microns, (ii) a bulk density of from 0.2 to 0.7, (iii) an average surface area of 0.1 m 2 /g to 10 m 2 /g, or (iv) a sphericity of from 70% to 100%.
• a dope composition comprising: (A) a cellulose ester composition: (I) a mixed cellulose ester (“MCE”) comprising: (1 ) a plurality of acetyl substituents; (2) a plurality of (C 2-3 )alkyl-CO- substituents; and (3) a plurality of hydroxyl substituents, wherein: the MCE has an average degree of substitution for the acetyl substituents (“DSAC”) that is from 0.6 to 2.4, the MCE has an average degree of substitution for the (C 2-3 )alkyl-CO- substituents (“DSAkco”) that is from 0.1 to 1 .1 , the MCE has an average degree of substitution for the hydroxyl substituents (“DSOH”) that is from 0.55 to 1 .5, and (II) a cellulose acetate (“CA”), comprising: a plurality of acetyl substituents; and a plurality of hydroxyl substituents
• the (C 2-3 )alkyl-CO- is propionyl. In one embodiment or in combination with any other embodiment, class or subclass of this eleventh aspect, the (C 2-3 )alkyl-CO- is butyryl.
• the MCE is present at from 60 wt% to 99 wt%, and the CA is present at from 1 wt% to 40 wt%, based on the total weight of the cellulose ester composition. In one embodiment or in combination with any other embodiment, class or subclass of this eleventh aspect, the MCE is present at from 55 wt% to 99 wt%, and the CA is present at from 1 wt% to 45 wt%, based on the total weight of the cellulose ester composition.
• the MCE is present at from 65 wt% to 99 wt%, and the CA is present at from 1 wt% to 35 wt%, based on the total weight of the cellulose ester composition. In one embodiment or in combination with any other embodiment, class or subclass of this eleventh aspect, the MCE is present at from 70 wt% to 99 wt%, and the CA is present at from 1 wt% to 30 wt%, based on the total weight of the cellulose ester composition.
• the MCE is present at from 75 wt% to 99 wt%, and the CA is present at from 1 wt% to 25 wt%, based on the total weight of the cellulose ester composition. In one embodiment or in combination with any other embodiment, class or subclass of this eleventh aspect, the MCE is present at from 80 wt% to 99 wt%, and the CA is present at from 1 wt% to 20 wt%, based on the total weight of the cellulose ester composition.
• the MCE is present at from 85 wt% to 99 wt%
• the CA is present at from 1 wt% to 25 wt%, based on the total weight of the cellulose ester composition.
• the cellulose ester composition is present at from 5 wt% to 20 wt%, and the solvent is present at from 80 wt% to 95 wt% based on the total weight of the dope composition. In one embodiment or in combination with any other embodiment, class or subclass of this eleventh aspect, the cellulose ester composition is present at from 5 wt% to 15 wt%, and the solvent is present at from 85 wt% to 95 wt% based on the total weight of the dope composition.
• the cellulose ester composition is present at from 5 wt% to 10 wt%, and the solvent is present at from 90 wt% to 95 wt% based on the total weight of the dope composition.
• AC 2 O is acetic anhydride; AcOH is acetic acid; Biodeg is biodegradation; CA-398-3 is Eastman Cellulose Acetate 398-3; CA-398-6 is Eastman Cellulose Acetate 398-6; CA-398-10 is Eastman Cellulose Acetate 398-10; CA-398-30 is Eastman Cellulose Acetate 398-30; CA-394-60LF is Eastman Cellulose Acetate 394-60LF; CE is cellulose ester; CEx is comparative example; °C is degrees Celsius; CAB is cellulose acetate butyrate; CA is cellulose acetate; DS is average degree of substitution; Ex is example(s); DSA C is the average degree of substitution for acetyl; DSBU is the average degree of substitution for butyryl; DSOH is average degree of substitution for hydroxyl; g is gram(s); h is hour(s); kg is kilogram(s); Mg(OAc) 2 is magnesium acetate; min is minute(s); mL is milli
• Activated cellulose mixture [cellulose (7.1 parts) and PrOH (1 1 .0 parts)] was cooled to 15°C in a vessel with overhead stirring. Following, a solution of sulfuric acid (0.2 parts), AC2O (11 .3 parts), and Pr20 (13.3 parts) (acylation solution) cooled to 15°C was added to the cooled activated cellulose mixture with stirring. The resulting reaction mixture was warmed to 23°C and stirred at 23°C for 60 min. Then the reaction mixture was heated to 63°C over 45 min, at which point a soln of PrOH (32.3 parts) and H 2 O (11 .3 parts) was added. The mixture was then stirred at 71 °C for 600 min.
• the mixture is treated with a solution of Mg(OAc) 2 .4H 2 O (0.45 parts) in AcOH (7.3 parts) and H 2 O (5.6 parts) and the mixture was stirred for 30 min and cooled to rt.
• the mixture was filtered.
• the cellulose ester was precipitated from the filtrate with water and agitated in a commercial blender, and the cellulose ester was filtered, collected, the solids were washed with running water and dried in a vacuum oven set at 60°C until dry to give the desired product.
• Table 1 Preparation conditions for Ex 2-5, 7-8, and CEx 5.
• Table 2 provides properties for the cellulose esters prepared above.
• Activated cellulose mixture [cellulose (5.4 parts) and AcOH (21 .5 parts)] with some amount of sulfuric acid was cooled to 32°C in an agitated reactor. Following, a mixture of AC 2 O (11 .3 parts) and BU 2 O (7.3 parts) was added and the mixture cooled to around 9°C with agitation. Additional sulfuric acid was added to a total of 0.4 parts and the resulting reaction mixture was warmed to 55°C. To this reaction mixture was added a mixture of AcOH (23.3 parts) and H 2 O (9.0 parts).
• the biodegradation of CEs was evaluated in an aqueous aerobic biodegradation test according to ISO 14851 or OECD 301 F method. The total test duration was around 56 days. The tests were performed at 21 °C ⁇ 2°C. The biodegradation tests were performed using Eastman wastewater treatment sludge as inoculum.
• CEs were dispersed in a chemically defined mineral media free of other organic carbon sources and inoculated with micro-organisms from wastewater sludge.
• oxygen is consumed by the microbes and carbon from the test material is converted into CO 2 .
• Carbon dioxide produced in the process was trapped by NaOH inside the bottle (NaOH placed in the quiver inside the closed test bottles) and that causes pressure drop in the headspace. This pressure drop corresponds directly to oxygen being consumed and hence to the biodegradation of the test material.
• the biodegradation is calculated from the Oxygen consumption as ratio of BOD (biological oxygen demand) after correcting for the control to the theoretical oxygen demand of the test item.
• a material is considered biodegradable if it has reach at least 90% or 90% of the reference material (according to ISO 14851 ) by 56 days. And according to ECHA microplastic proposal if the material has reached at least 60% biodegradation by 60 days it is considered biodegradable.
• Procedure 1 is based on the procedures disclosed in EP0750007 (“EP’007”).
• Cellulose Acetate Butyrate Microbeads 7 Providedure 1
• Ex 6 40 g
• EtOAc 185 g
• EtOH 25 g
• Benecel A4M 1 .5 g
• Tween 28 4.5 g
• water 350 g
• EtOAc 50 mL
• the aqueous phase was premixed using a roto-stator at 9000 rpm for 5 min and then the oil phase was added to the aqueous phase over 20 min.
• the formed oil emulsion was stirred for 50 min and the emulsion was filtered through a 200 mesh sieve into water (2500 mL) over five min under stirring. The resulting mixture was stirred for 1 h. The formed microparticles were filtered. The resulting microparticles were washed with water and centrifuged at 10,000 for 10 min to separate the particles from the aqueous phase (repeated 3x). The final microparticles exhibited a Dio of 1 .21 microns, D 50 of 4.96 microns, D 90 of 12 microns, and polydispersity of 0.646, which was determined by light scattering. D10, or D50, or D 90 , are the particle size value below which 10%, or 50%, or 90% of the material is contained.
• Cellulose acetate butyrate microbeads 17 was synthesized by adapting the procedure for the preparation of cellulose butyrate microbeads 7. Ex 10 was used instead of Ex 6. Benecel was replaced with carboxymethylcellulose, and Tween 28 was replaced with a 1 :0.5:0.5 ratio of Tergitol 15 S-40, glycerol stearate and PEG-100 stearate. Cellulose acetate butyrate microbeads 17 have a particle size of 11 microns and a bulk density of 0.296 g/mL.
• a dope of the cellulose ester mixture was prepared by adding the cellulose ester mixture (90 g) to a ethyl acetate, (C 2-3 )alkanol, water mixture (547.7 g, 80:13:7) while stirring at 250 rpm. The resulting mixture was stirred at rt ( ⁇ 30min).
• Table 4 provides the cellulose acetate used to prepare representative dopes with Ex 6.
• Table 5 shows which cellulose acetate butyrate/cellulose acetate dopes are possible from an ethyl acetate, ethanol, and water solution system.
• the dopes were prepared by mixing CAB/CA (6.0 g) in a solvent
• Table 7 provides dopes made from either Ex 6, various cellulose acetates, or blends of Ex 6 and various cellulose acetates according to the Dope Procedure in Preparation Procedure 2. Only certain cellulose acetates could be blended with Ex 6 to form dopes in the EA:EtOH:Water solvent system, and none of the cellulose acetates used were able to form dopes in the EA:EtOH:Water solvent system. Ex 6 readily formed a dope in the EA:EtOH:Water solvent system
• the aqueous mixture used to prepare the emulsion is prepared by mixing ethyl acetate (124.6 g) with methyl cellulose (6.8g) with a 2-stage pitched bladed agitator (250 rpm) until a dispersion is formed. Then water (1280 g) and Tween-28 (13.5g) is added. The resulting aqueous mixture is agitated for ⁇ 30 min at which time a solution is formed
• the dope (637.7 g) is charged to the aqueous mixture (1424.3 g) at a rate of 15 mL/min ( ⁇ 45 min) while agitating (250 rpm). Afterwards, the resulting mixture was agitated at 250 rpm and recirculating the mixture through a MagicLab inline high-sheer mixer (6000 rpm) at 200 mL/min for 30 min.
• the absorption or oil uptake properties were measured using the test method of ASTM D281 “Standard Test Method for Oil Absorption of Pigments by Spatula Rub-out,” instead of castor oil, mineral oil was used.
• the mineral oil (Item No. ELL-MIOL-01 ) was obtained from MakingCosmetics.com, Inc. The mineral oil is added dropwise to a known amount of neat powder and stirred with a spatula until a solid dry paste is formed. When the solid dry paste is formed, no more mineral oil is absorbed. Once the amount of oil is determined, the oil take calculated using the following formula:

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