Classifications

• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L67/00—Compositions of polyesters obtained by reactions forming a carboxylic ester link in the main chain; Compositions of derivatives of such polymers
  • C08L67/04—Polyesters derived from hydroxycarboxylic acids, e.g. lactones
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
  • C08G63/00—Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
  • C08G63/02—Polyesters derived from hydroxycarboxylic acids or from polycarboxylic acids and polyhydroxy compounds
  • C08G63/12—Polyesters derived from hydroxycarboxylic acids or from polycarboxylic acids and polyhydroxy compounds derived from polycarboxylic acids and polyhydroxy compounds
  • C08G63/16—Dicarboxylic acids and dihydroxy compounds
  • C08G63/18—Dicarboxylic acids and dihydroxy compounds the acids or hydroxy compounds containing carbocyclic rings
  • C08G63/181—Acids containing aromatic rings
  • C08G63/183—Terephthalic acids
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B32—LAYERED PRODUCTS
  • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
  • B32B27/00—Layered products comprising a layer of synthetic resin
  • B32B27/36—Layered products comprising a layer of synthetic resin comprising polyesters
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B32—LAYERED PRODUCTS
  • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
  • B32B27/00—Layered products comprising a layer of synthetic resin
  • B32B27/06—Layered products comprising a layer of synthetic resin as the main or only constituent of a layer, which is next to another layer of the same or of a different material
  • B32B27/08—Layered products comprising a layer of synthetic resin as the main or only constituent of a layer, which is next to another layer of the same or of a different material of synthetic resin
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B32—LAYERED PRODUCTS
  • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
  • B32B27/00—Layered products comprising a layer of synthetic resin
  • B32B27/18—Layered products comprising a layer of synthetic resin characterised by the use of special additives
  • B32B27/20—Layered products comprising a layer of synthetic resin characterised by the use of special additives using fillers, pigments, thixotroping agents
• • 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
  • C08K3/00—Use of inorganic substances as compounding ingredients
  • C08K3/01—Use of inorganic substances as compounding ingredients characterized by their specific function
• • 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
  • C08K3/00—Use of inorganic substances as compounding ingredients
  • C08K3/01—Use of inorganic substances as compounding ingredients characterized by their specific function
  • C08K3/013—Fillers, pigments or reinforcing additives
• • 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
  • C08K3/00—Use of inorganic substances as compounding ingredients
  • C08K3/28—Nitrogen-containing compounds
• • 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
  • C08K3/00—Use of inorganic substances as compounding ingredients
  • C08K3/34—Silicon-containing compounds
• • 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
  • C08K5/0008—Organic ingredients according to more than one of the "one dot" groups of C08K5/01 - C08K5/59
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L67/00—Compositions of polyesters obtained by reactions forming a carboxylic ester link in the main chain; Compositions of derivatives of such polymers
  • C08L67/02—Polyesters derived from dicarboxylic acids and dihydroxy compounds
• • C—CHEMISTRY; METALLURGY
  • C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
  • C23F—NON-MECHANICAL REMOVAL OF METALLIC MATERIAL FROM SURFACE; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL; MULTI-STEP PROCESSES FOR SURFACE TREATMENT OF METALLIC MATERIAL INVOLVING AT LEAST ONE PROCESS PROVIDED FOR IN CLASS C23 AND AT LEAST ONE PROCESS COVERED BY SUBCLASS C21D OR C22F OR CLASS C25
  • C23F11/00—Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent
  • C23F11/02—Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent in air or gases by adding vapour phase inhibitors
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B32—LAYERED PRODUCTS
  • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
  • B32B2264/00—Composition or properties of particles which form a particulate layer or are present as additives
  • B32B2264/10—Inorganic particles
  • B32B2264/102—Oxide or hydroxide
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B32—LAYERED PRODUCTS
  • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
  • B32B2264/00—Composition or properties of particles which form a particulate layer or are present as additives
  • B32B2264/10—Inorganic particles
  • B32B2264/104—Oxysalt, e.g. carbonate, sulfate, phosphate or nitrate particles
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B32—LAYERED PRODUCTS
  • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
  • B32B2307/00—Properties of the layers or laminate
  • B32B2307/70—Other properties
  • B32B2307/716—Degradable
  • B32B2307/7163—Biodegradable
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B32—LAYERED PRODUCTS
  • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
  • B32B2307/00—Properties of the layers or laminate
  • B32B2307/70—Other properties
  • B32B2307/724—Permeability to gases, adsorption
  • B32B2307/7242—Non-permeable
  • B32B2307/7246—Water vapor barrier
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B32—LAYERED PRODUCTS
  • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
  • B32B2307/00—Properties of the layers or laminate
  • B32B2307/70—Other properties
  • B32B2307/752—Corrosion inhibitor
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B32—LAYERED PRODUCTS
  • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
  • B32B2439/00—Containers; Receptacles
  • B32B2439/40—Closed containers
  • B32B2439/46—Bags
• • 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
  • C08K2201/00—Specific properties of additives
  • C08K2201/014—Additives containing two or more different additives of the same subgroup in C08K
• • 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
  • C08K5/09—Carboxylic acids; Metal salts thereof; Anhydrides thereof
• • 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
  • C08K5/09—Carboxylic acids; Metal salts thereof; Anhydrides thereof
  • C08K5/098—Metal salts of carboxylic 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
  • C08K5/16—Nitrogen-containing compounds
  • C08K5/34—Heterocyclic compounds having nitrogen in the ring
  • C08K5/3467—Heterocyclic compounds having nitrogen in the ring having more than two nitrogen atoms in the ring
  • C08K5/3472—Five-membered rings
  • C08K5/3475—Five-membered rings condensed with carbocyclic rings
• • 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
  • C08L2201/00—Properties
  • C08L2201/08—Stabilised against heat, light or radiation or oxydation

Definitions

• a breathable biodegradable volatile corrosion inhibitor composition comprises a biodegradable polyester composition that comprises one or more homopolymer polyesters and/or one or more random copolymer polyesters with one or more volatile corrosion inhibitors (VCI), and at least one or more fillers that unexpectedly improve various physical properties of the composition.
• the total amount of said one or more VCI is generally from about 0.1 wt.% to about 10 wt.% based upon the total weight of all of the biodegradable polyesters excluding said fillers.
• U.S. Patent 6,028,160 to Cortec Corporation relates to biodegradable resin products consisting essentially of a polymeric resin of polyethylene, starch, polyesters such as polylactic acid, or other suitable polyesters.
• a particulate vapor phase corrosion inhibitor selected from amine salts, ammonium benzoate, triazole derivatives, tall oil imidazolines, alkali metal molybdates, alkali dibasic acid salts, and mixtures thereof, and is present in an amount ranging from between 1 % and 3% by weight of the polymeric resin.
• U.S. Patent 6,156,929 to Cortec Corporation relates to biodegradable resin products consisting essentially of a polymeric resin of starch, polyesters of polylactic acid and polycaprolactone.
• a particulate vapor phase corrosion inhibitor selected from amine salts, ammonium benzoate, triazole derivatives, tall oil imidazolines, alkali metal molybdates, alkali dibasic acid salts, and mixtures thereof, and is present in an amount ranging from between 1 % and 3% by weight of the polymeric resin.
• U.S. Patent 6,617,415 to Cortec Corporation relates to biodegradable resin products consisting essentially of a polymeric resin of starch, polyesters such as polylactic acid, or other suitable polyesters.
• a particulate vapor phase corrosion inhibitor selected from amine salts, triazole derivatives, alkali dibasic acid salts, and mixtures thereof, and is present in an amount ranging from between 1 % and 3% by weight of the polymeric resin and which is shaped into formed articles.
• U.S. Patent 6,984,426 to Cortec Corporation relates to a biodegradable film formable into biodegradable bags which includes the blended product of polylactic acid and a suitable biodegradable polymeric resin.
• the blended product includes from about 5% to about 50% by weight polylactic acid.
• U.S. Publication 2014/0235777 to Purac Biochem B.V. relates to a composition comprising a poly-D-lactic acid (PDLA) polymer and a poly-L-lactic acid (PLLA) polymer. It also relates to a method for the production of a moulded part comprising the steps of heating a mold, and supplying to the mold a composition comprising a poly-D-lactic acid (PDLA) polymer and a poly-L-lactic acid (PLLA) polymer. It further relates to a composition comprising a poly-D-lactic acid (PDLA) polymer and a poly-L-lactic acid (PLLA) polymer for use in injection molding, thermoforming and/or film blowing. It also relates to a composition that can be obtained by heating a composition comprising a poly- D-lactic acid (PDLA) polymer and a poly-L-lactic acid (PLLA) polymer.
• PDLA poly-D-lactic acid
• PLLA poly-L-lactic acid
• U.S. Patent 8,008,373 to Norihern Technologies International Corporation relates to a biodegradable thermoplastic polymer masterbatch composition
• a biodegradable thermoplastic polymer masterbatch composition comprising a blend of at least one biodegradable thermoplastic polymer containing high loading of a particulate filler uniformly dispersed therein.
• the amount of the biodegradable thermoplastic polymer is generally from about 25% to about 50% by weight and the amount of the filler is from about 75% to about 50% by weight, based upon the total amount of one biodegradable polymer and the at least one filler.
• the uniform dispersion of the fillers is obtained by adding small particles of the filler to a melt of the biodegradable polymer and blending using high shear equipment with special screw geometry.
• the masterbatch composition is then physically blended with additional biodegradable thermoplastic polymer and extrusion processed into final articles such as blown and cast films, molded products, and the like.
• the masterbatch multi-stage approach results in a product that has improved physical properties and lower costs over that of a one-step blend of the same amount of a biodegradable thermoplastic polymer and a filler that is subsequently heat formed into a final product
• An aspect of the present invention is to alleviate the above-noted pollution and/or toxic problems. Another aspect is providing a composition that is in the form of a film that can pass EN 13432 and ASTM D6400 which evaluates timely composability of the material in industrial composting facilities.
• the composition has superior mechanical properties and volatile corrosion inhibition properties compared to PE, unlike the above mention products, so it can truly replace PE based material in the field of corrosion mitigation.
• Another important aspect of the present invention is to provide a biodegradable VCI packaging composition that effectively prevents corrosion of various items including machines, tools, and metal parts.
• VCI packaging composition such as packaging material containing a VCI
• WVTR water-vapor transmission rates
• biodegradable compositions such as in the form of biodegradable polyester plastic bags perform better than polyethylene (PE) bags when containing the same amounts of VCIs therein, despite higher WVTR of the biodegradable bags than PE bags.
• VCI chemistries like sodium nitrite, salts of carboxylic acids, or ammonium salts react with water to release the VCI and therefore, if more moisture is permeated through the bag faster, more VCI chemistry is activated in a shorter period and the chemistry would reach the surface of metal sooner than in a bag with a lower water vapor transmission rate.
• the VC I packaging compositions of the present invention containing fillers have improved breathability, showed increased water vapor transmission rates (WVTR), improved process-ability in extrusion equipment, less blocking which allows the bags made with this material to be opened more easily, lower cost without sacrificing the mechanical properties of the product, and better corrosion resistance than compositions containing the same amounts and types of VCIs therein but no fillers.
• WVTR water vapor transmission rates
• a biodegradable volatile corrosion inhibitor polyester composition comprises one or more biodegradable random copolymer polyesters and/or one or more biodegradable homopolymer polyesters; from about 0.1 wt.% to about 10 wt.% of one or more volatile corrosion inhibitors based upon 100 total parts by weight of said one or more biodegradable random copolymer polyesters and/or said one or more biodegradable homopolymer polyesters; and from about 3 to about 53 parts by weight of at least one filler based upon 100 parts by weight of said one or more biodegradable random copolymer polyesters and/or said one or more biodegradable homopolymer polyesters.
• the present invention relates to biodegradable VCI compositions that are desirable for many uses including packaging of various items, apparatus, machines, parts, and the like. Such items are contained within, encased, wrapped, or otherwise exist within the biodegradable VCI packaging compositions of the present invention.
• the packaging material preferably is in the form of a sheet or film that can be used to form a container, enclosure, or box for the above-noted items to be protected against corrosion.
• An essential component of the biodegradable VCI composition is one or more biodegradable homopolymer polyesters or one or more random copolymer polyesters, or both.
• Polymers that can be used as one or more homopolymer polyesters such as a polylactide, polycaprolactone, a blend of PLA and polycaprolactone, a polyglycolide, or polyhydroxyalkanoates (PHA), or any combination thereof, that desirably is relatively pure, that is contains no contaminates or polymers therein.
• it generally contains less than about 3 or about 1 wt.% of any contaminate, desirably less than about 0.5 wt.%, and preferably less than about 0.1 wt.% or nil, has no contaminates whatsoever that exist.
• Typical molecular weights of commercial polyiactide homopolymers or other homopolymer polyesters can be utilized wherein the weight average molecular weight thereof is from about 100,000 to about 175,000, desirably from about 1 10,000 to about 150,000, and preferably from about 125,000 to about 140,000 g/mol.
• One or more polylactides can be utilized that differ in molecular weight, and/or are obtained from a different manufacturer.
• a suitable polyiactide that can be used in the present invention is PLA 3052D, made by Natureworks.
• one or more random copolymer polyesters such as an aliphatic-aromatic random copolyester or a random aliphatic copolyester can be utilized.
• the number and type of random copolyesters are large and generally have the formula:
• R 1 independently comprises
• x independently, is an integer from about 2 to about 10, or about 34 (dimer fatty acid), wherein, y, independently, is an integer of from 2 to about 8.
• -can be derived from an adipic acid, sebacic acid, or azelaic acid, and - can be derived from 1 ,4-butanediol or ethylene glycol.
• suitable compostable random copolymer polyesters include polybutylene sebacate-co-terephthalate (PBST), with polybutylene adipate-co- terephthalate (PBAT) being preferred.
• the weight average molecular weight of the one or more random copolymer polyesters independently, can range from about 80,000 to about 175, 000 with a desirable weight average molecular weight being from about 90,000 to about 150,000, and preferably from about 100,000 to about 130,000.
• the weight average molecular weight of the above-noted polylactide homopolymer polyesters as well as the random copolymer polyesters was determined by gel permeation chromatography (GPC) wherein the polymer was dissolved in chloroform, the solvent for GPC was tetrahydrofuran and the temperature was 23°C.
• GPC gel permeation chromatography
• random copolyesters not contain any repeat units derived from succinic acid.
• Such compositions have generally been found to have poor physical properties such as low tear resistance as well as low transparency, both of which are important properties for corrosion inhibiting compositions.
• generally aliphatic-copolyesters such as PBS (poly) (butylene succinate) have poor mechanical properties and are/or also expensive.
• the amount of any repeat units derived from succinic acid is very small such as less than about 10%, and desirably less than 2% based upon the total number of repeat groups in the copolymer.
• nil that is no copolyesters derived from a succinic acid are utilized whatsoever based upon the total weight of the one or more biodegradable polyesters of the present invention.
• the amount thereof is from about 50 wt.% to about 95 wt.%, desirably from about 60 wt.% to about 90 wt.%, and preferably from about 70 wt.% to about 85 wt.% based upon 100 total parts by weight of all of the biodegradable polyesters.
• the amount of one or more homopolymer- polyester is from about 5 wt.% to about 50 wt.%; desirably from about 10 wt.% to about 40 wt.%, and preferably from about 15 wt.% to about 30 wt.% based on 100 total parts by weight of all of the biodegradable polyesters. If the polyester inhibitor composition is not a blend, the amount of the homopolymer or the random copolymer is of course, 100 wt.%. [0022] As an example, it has been found that high ratios of the one or more random copolyesters to the amount of the one or more homopolyesters such as PLA is important with regard to increasing the mechanical performance of the product and shelf life.
• biodegradable VCI packaging compositions can be made from one or more homopolymers as noted above, or from one or more copolymers as noted above, or from a blend containing one or more homopolymers with one or more copolymers.
• one or more fillers are generally always utilized with any of the three above-noted blends since they unexpectedly have been found to improve properties thereof as set forth hereinbelow.
• One or more volatile corrosion inhibitors of the present invention comprise of various triazoles and derivatives thereof such as benzotriazole and tolytriazole; various benzoates such as ammonium benzoate; various ammonium salts; various carbamates; various phosphates; and various alkali acid salts such as set forth in U.S. Patents 4,973,448; 5,139,700; 5,715,945; 6,028,160; 6,156,929; 6,617,415; and 6,787,065, hereby fully incorporated by reference.
• Useful VCI’s of the present invention preferably include various inorganic nitrites or alkali metal nitrites with potassium nitrite and sodium nitrite being preferred, as well as various sodium salts such as sodium octanoate, sodium benzoate, various benzoate acid derivatives such as 2 or 3 or 4- hydroxy-benzoic acid, ammonium benzoate and various alkali metal salts (e.g. sodium or potassium) of aliphatic carboxylic acids such as sorbic acid or a dicarboxylic acid. Such acids have from about 5 to about 18 carbon atoms.
• Fillers are an important aspect of the present invention to provide ease of processing, e.g. extruding the resin and anti-blocking effect for the bags made with such material, cost reduction, retention of tensile strength, reduced density of the end product, and higher stiffness. It has also been found that various one or more fillers such as talc, calcium carbonate, sodium carbonate, silicates, clay, and barites, or any combination thereof, help adjust the WVTR rates. That is, mixing the same into the overall biodegradable VCI packaging compositions improved the porosity and thus promote a desired access of more water molecules to various one or more VCI compounds.
• the higher water vapor transmission rate (WVTR) of biodegradable polyester films than that of polyethylene (PE) based films allows for lower loadings of VCI compounds for short-term applications of the biodegradable VC I packaging compositions of the present invention.
• Talc is a preferred filler.
• the total amount of the one or more fillers is generally from about 3 to about 53 parts by weight, desirably from about 5 to about 33 parts by weight, and preferably from about 5 to about 18 parts by weight based upon 100 total parts by weight of the one or more homopolymer polyesters and/or one or more random copolymer polyesters.
• the present invention is free of starch as a filler, that is, it has no starch.
• a unique advantage of the present invention due to the various factors that contribute to a high WVTR of the present invention is that only low amounts of such VCI compounds need be utilized. That is, the various one or more VCI’s compounds range from about 0.1 wt.% to about 10wt.%, desirably from about 0.3 wt.% to about 5 wt.%, and preferably from about 0.5 wt.% to about 2 or about 0.9 wt.% based on the total weight, e.g. 100 total parts by weight, of the one or more homopolymer polyesters and/or the one or more random copolymer polyesters. In other words, the total amount of one or more VCI’s utilized in the present invention can vary widely.
• the preparation of the various different formulations of the biodegradable VCI packaging composition of the present invention can generally be carried out in any manner known to the art and to the literature.
• various pre-masterbatches are initially prepared and then subsequently all are mixed together at a temperature above the melting point biodegradable compounds such as the various types of polyesters disclosed herein above.
• biodegradable compounds such as the various types of polyesters disclosed herein above.
• from about 1 to about 10 parts by weight of one or more VCI's are added to about 20 parts by weight of one or more random polyesters and/or one or more of the homopolymer polyester polymers of the present invention to form a VCI masterbatch.
• the amount of VCI masterbatch is subsequently added to an existing fair amount of biodegradable polyesters to yield a biodegradable polyester composition having, as noted above, that is from about 0.1 wt.% to about 10 wt.%, desirably from about 0.3 wt.% to about 5 wt.%, and preferably from about 0.5 wt.% to about 2 wt.% of a VC I therein based on the total weight of only said polyesters.
• the preparation of the VCI masterbatch can generally be carried out in any heating and mixing device, such as an extruder, an internal mixer, or preferably a twin-screw extruder, wherein the mixing temperatures are above the melting point of the random copolyesters.
• any heating and mixing device such as an extruder, an internal mixer, or preferably a twin-screw extruder, wherein the mixing temperatures are above the melting point of the random copolyesters.
• a filler masterbatch is generally made in the same manner wherein small amounts by weight of the filler are added to a large amount of the one or more random copolyesters, and/or one or more homopolymer polyester polymers. Subsequently, a small amount of the filler masterbatch is added to a larger amount of the biodegradable polyesters to form an end composition having the desired amount of filler therein.
• the blending temperature of the one or more fillers to form the filler masterbatch is a temperature above the melting point of the one or more random copolyesters.
• a composition is made containing 100 parts by weight of the one or more homopolymer polyesters and/or one or more random copolymer polyesters.
• an appropriate amount of the VCI so that based upon a final total amount of 100 parts by weight of the desired biodegradable polyesters, the amount of VCI is, as noted above, from about 0.1 wt.% to about 10 wt.% thereof.
• the filler masterbatch added in appropriate amounts so that the total final amount of the one or more biodegradable polyesters is 100 parts by weight and the amount of the one or more fillers is within the above-noted weight ranges.
• the one or more filler compounds all of the necessary masterbatches are mixed together with additional amounts of biodegradable random copolyesters and/or a desired amount of a one or more biodegradable homopolyesters to form the final biodegradable VCI packaging composition.
• the mixing can be carried out in any desired mixing device such as calender, an extruder, and so forth and shaped either into pellets, granulars, and the like, or directly formed into the end product such as a sheet, bag or wrapper having a desired thickness.
• the packaging composition of the present invention can be one or more laminates having one or more sheets therein.
• a first sheet can comprise the one or more homopolymer polyester polymers and the above noted one or more random copolymer polyesters that contain a VCI therein and one of the above noted fillers therein.
• a second sheet of the laminate can comprise only said one or more biodegradable random copolymer polyesters optionally comprising a filler and optionally comprising a VCI. It should be obvious that many other different types of laminates can be made from the biodegradable volatile corrosion inhibitor polyester compositions of the present invention.
• breathable biodegradable volatile corrosion inhibitor packaging compositions can be prepared having a broad range of WVTR such as from about 100 to about 2000, desirably from about 300 to about 1000, and preferably from about 400 to about 600[g/(m2 d)] at 38°C/90% RH, normalized to 1 mil according to ASTM F1249.
• EXAMPLE 1 PBAT pellets were dried at 50°C., for minimum of 2 hours and mixed with grinded sodium nitrite powder (VCI#1) at 70 to 30 ratio. The mixture was then fed to the feed port of a twin-screw counter-rotating LabTech ® extruder having L/D of 44 and screw diameter of 26 mm, in which most of the zones were controlled at temperatures in the range from about 270°F to 290°F. The die temperature was maintained at 300°F. The motor speed was about 150 rpm and generates a“strand” which was cooled in a water bath, pelletized into pellets about 3.18 mm (0.125 in) and dried.
• VCI#1 grinded sodium nitrite powder
• VCI MB was then mixed with similarly dried PBAT and PBAT/filler pellets and/or PLA at stated in Table 1 and extruded into a film via blown film line, run at 5 ft/min at 60 micron thickness.
• a control sample was made with a blend of LDPE and LLDPE with comparable level of VCI in it for comparison.
• the panel inside the PE based resin which have lower WVTR showed several corrosion areas along the edges and more than three spots on the panels’ body when tested according to I EC 68-2-30 Cyclic Chamber Testing.
• the panels in PE bags which would be the control received grade 3, while the panels in this example with biodegradable resins, PBAT/filler, and PBAT/PLA/filler blend, showed no corrosion and were graded at 5, after 7 cycles.
• VCI testing according to NACE Standard TM0208 showed grade 3 for the biodegradable sample for the present invention and grade 2 for the PE based control sample with comparable VCI content.
• the NACE Standard TM0208 test showed grade 3 for the first formulation and grade 1 for the second set.
• the VCI#2 was added at similar loading PBAT/filler in one case, and to LDPE/LLDPE blend in another case as the control.
• the PBAT/VCI film showed no corrosion (grade 5) while quite a few spot (grade 3) was observed in control, LDPE/LLDPE film with comparable VCI concentration after 1 week of testing, 7 cycles of (I EC 68-2-30).
• the set with higher filler level showed better protection in the cyclic chamber test running according to (IEC 68-2-30) after two weeks (14 cycles).
• the rating for the higher filler was 4-5 while it was 3-4 for lower filler samples.
• the water vapor transmission rate of the higher filler film was 412 [g/(m2 d)] versus the WVTR of the lower loading being 323 [g/(m2 d)] (normalized) tested at 38°C/90% RH.
• VCI#3 that showed weaker result in example #2, however, when used with higher filler level, showed improved result. While lower filler containing sample showed grade 2 after 14 cycles of (I EC 68-2-30) test, higher filler sample showed grade 3.

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