|Número de publicación||US20050153084 A1|
|Tipo de publicación||Solicitud|
|Número de solicitud||US 10/754,753|
|Fecha de publicación||14 Jul 2005|
|Fecha de presentación||9 Ene 2004|
|Fecha de prioridad||9 Ene 2004|
|También publicado como||WO2005070996A1|
|Número de publicación||10754753, 754753, US 2005/0153084 A1, US 2005/153084 A1, US 20050153084 A1, US 20050153084A1, US 2005153084 A1, US 2005153084A1, US-A1-20050153084, US-A1-2005153084, US2005/0153084A1, US2005/153084A1, US20050153084 A1, US20050153084A1, US2005153084 A1, US2005153084A1|
|Cesionario original||Yu Shi|
|Exportar cita||BiBTeX, EndNote, RefMan|
|Citas de patentes (34), Citada por (11), Clasificaciones (19), Eventos legales (1)|
|Enlaces externos: USPTO, Cesión de USPTO, Espacenet|
This application relates to poly(ethylene terephthalate)—based compositions and more particularly to stress cracking resistance of articles such as containers made with poly(ethylene terephthalate)—based compositions.
Poly(ethylene terephthalate)-based resins, which are commonly referred to in the industry simply as “PET” even though they may and often do contain minor amounts of additional components, have widely been used to make containers for carbonated soft drink, juice, water and the like due to their excellent combination of mechanical and gas barrier properties. Unfortunately, a phenomenon known as environmental stress cracking (ESC) has been a persistent annoyance in PET containers used for carbonated beverages since the advent of the one-piece container design. The ultimate failure caused by ESC is a rupture in the base of the container resulting in the loss of the container's contents and subsequent contamination of the surroundings. Clean-up is laborious. Product and liability losses can be expensive. Usually 10 to 20 stress crack failure containers per million is considered excessive.
Direct causes for failures are often difficult to determine. The factors affecting ESC of PET containers include, but are not limited to, container production conditions, the stress due to the pressurization of the carbonated beverage, and the conditions in container handling and storage.
Production conditions are critical contributors to the ESC phenomenon. Manufacturing variations can play a significant role in determining the ESC resistance. Minor changes in processing conditions are reported to have significant effect on stress crack resistance. During line conveying and container cleaning stress crack agents in the form of chemicals contact PET container. The origin of a crack in a PET container is normally located at the areas where stress concentration exists. The stress cracking agent can attack the base by many mechanisms, but normally starts from craze development as a result of the cracking agent attack. Crazes can then develop into cracks and failure may occur in forms of a rupture or leakage. Optimum processing conditions, which are difficult to manage consistently, are required to prevent ESC.
ESC can be also caused by excessive stress seen in the carbonation of beverages. Beverages are often over pressurized during the filling process to increase shelf life. However, over pressurization creates added stress to the container and thus a higher possibility for rupture.
Physical aging has been found to be an important contributing factor for ESC of PET containers. Studies have shown that the container ESC resistance decreases exponentially with hours of aging. The physical aging that containers experience before filling may be a primary factor responsible for the increased rate of failures often observed during the hot summer months.
Several methods have been reported to improve ESC resistance of one-piece PET containers for carbonated soft drinks (CSDs). Proper and robust base design of the PET container is one method used to reduce ESC. A well-designed base is required to tolerate manufacturing variations and can protect containers from excess stress. Base design is a critical component in today's container manufacture. However, base design can not protect containers from contact with stress-inducing chemical agents.
Another method for reducing ESC is a modification to the blow molding process. The modification achieves optimal base weight, minimum residual stress, and/or maximum crystallinity in the base. This method, however, has the same problem inherent with all the methods above: the nature of the material is not changed. Therefore, the reduction of stress cracking is just a matter of degree, depending on the nature of the chemical agent, the contact time and other factors.
A third method is the use of special lubricants on container line conveyors. These lubricants have fewer tendencies to attack PET containers as stress cracking agents and thus reduce the stress cracking of PET containers. This method, however, can not solve problems associated with other chemicals such as cleansers, contaminants from water, and the like that can cause stress cracking. So ESC still occurs, just to a lesser degree during filling.
Still another method is to coat the PET container, at least around the base. The coating itself is very inert to chemical agents which are normally strong enough to attack PET. This method, however, requires additional steps in the container making process and thus adds more cost to the container. The method is not applicable in all container making or filling sites either due to space limitations.
Additionally, increasing the molecular weight or intrinsic viscosity (IV) of PET has been found helpful in reducing the occurrence of ESC in PET containers used for carbonated beverage. A minimum IV of 0.80 dL/g is desirable in making a CSD container, with preferred IV's being reported to be 0.82 dL/g or higher. Higher IV or higher molecular weight PET has fewer chain ends and is believed to have less interaction with chemical attacking agents, which is believed to result in less stress cracking. In addition, higher IV PET (above 0.80 dL/g) is believed to have more chain entanglement, which can dissipate more stress than traditionally lower IV PET (below 0.76 dL/g). Normally, when a craze forms in PET during the attack of the chemical agent, stress is localized at the point of craze formation and is transferred through the expansion of crazes to form cracks. A higher IV resin is believed to be able to reduce the effect by transferring the stress partially to the other chains without further expansion of the crazes to form cracks. However, higher IV PET requires longer solid state polymerization (SSP) time, and higher injection molding temperature due to higher melt viscosity. Unfortunately, this means higher IV PET is more expensive to make than lower IV PET. Nevertheless, the general trend in recent years is to use higher IV PET of about 0.84 dL/g to avoid the annoyance of the ESC problem even though higher IV PET costs more to produce and convert from resin to container.
Lower IV PETs, such as 0.72 to 0.76 dL/g, however, have been used for a few container applications, such as still water containers, where stress cracking is seldom an issue. Application of such lower IV PETs in one-piece-CSD containers has been limited solely because of its bad performance in stress cracking resistance. Modifications to PET compositions have been reported in an effort to counter ESC effects so that lower IV PET can be used for CSDs. One example is the addition of a comonomer, such as naphthalene dicarboxylate to enhance the stress cracking resistance. In any case, a higher IV PET has always been used for carbonated beverage applications. Having different resins for packaging different products, however, creates more inventories in the converting facilities. Some facilities do not have enough capability to have so many inventories. Thus, having a lower IV PET that resists stress cracking problems would be greatly desired by the industry so that a lower IV resin can be used for both CSD and water application reducing resin cost as well as inventory cost.
Impact modifiers have been used in amorphous polymer as well as high crystalline polymers to improve the impact resistance of these polymers. For polyesters, impact modifiers are widely used to improve the low temperature or room temperature impact resistance of highly crystallized PET homopolymers (often referred to as “CPET”) or amorphous polyesters made using high levels of glycol modification (more than 10 mole percent of non-ethylene glycol modifiers). The impact stress is normally applied in a rapid movement, such as dropping the article from a high distance or applying a rapid high stress to the article through an external force. These modifiers are believed to form a two-phase morphology in the polymer. The modifiers form a rubber-like phase which can absorb the impact energy and effectively transfers the stress from the CPET or amorphous polyester phase. Although impact modifiers are generally known for the above applications, there has been no attempt of using the same family of chemicals to improve the stress cracking resistance of PET containers for carbonated beverage application, especially those made with lower IV PET.
Although much effort has been made to understand and solve the stress cracking problem, the root causes of the stress cracking are still unknown. Stress cracking can have costly ramifications in terms of clean-up or liability. As can be seen, no one method currently available solves the stress cracking problems of PET containers used for CSDs. Rather, the stress cracking problem of PET containers has been carefully managed through optimized bottle design, bottle making, and product filling processes. Therefore, there remains a need to prevent or decrease environmental stress cracking in PET containers. Accordingly, it is to the provision of such that the present invention is primarily directed.
This invention addresses the foregoing issues in the prior art by providing a preform having an open ended mouth forming portion, an intermediate body forming portion, and a closed base forming portion and being made of a stress cracking resistant polyester composition comprising a poly(ethylene terephthalate) based resin and an impact modifier. This invention also encompasses a container made by blow molding such preform made of the stress cracking resistant polyester composition.
Without wishing to be bound by theory, the impact modifier is believed to improve the relaxation phenomenon of the poly(ethylene terephthalate) based resin such that a lower molecular weight (i.e. lower intrinsic viscosity) poly(ethylene terephthalate) based resin behaves as a higher molecular weight resin and resists stress cracking. In preferred embodiments the poly(ethylene terephthalate) based resin has an IV of from about 0.65 to about 0.90 dL/g, more preferably from about 0.65 to about 0.86 dL/g, even more preferably from about 0.65 to about 0.80 dL/g and still even more preferably from about 0.68 to about 0.76 dL/g. Thus, as a result of this invention, less expensive, lower IV poly(ethylene terephthalate) based resin when combined with the impact modifier can be used to make such preforms and containers. Further the same preform and container can be used for a variety of applications including CSD and bottled water containers.
Other objects, features, and advantages of this invention and the preferred embodiments will be appreciated from the following drawings, detailed description of embodiments, and claims.
The present invention encompasses a preform and a container made by blow molding the preform, both having an open ended mouth forming portion, an intermediate body forming portion, and a closed base forming portion and comprising a stress cracking resistant polyester composition comprising a poly(ethylene terephthalate) (PET) based resin and at least one impact modifier. Preferably, the PET based resin has a low intrinsic viscosity (IV), that is below about 0.76 dL/g. The impact modifier surprisingly enhances the stress cracking resistance of the low IV PET based resin such that the low IV PET based resin behaves as a higher IV resin. Thus, the container made utilizing this invention is particularly suited for use as a carbonated soft drink (CSD) container. The use of the impact modifier makes it possible to use a cheaper low IV PET based resin for the CSD container, and use the same container for other applications such as bottled water, alcoholic beverages, juices, and the like.
Conventionally, impact modifiers have been used in thermal formed high crystallinity PET (CPET) articles to improve the low temperature impact resistance. Such articles include amorphous polyester films or thermal formed high crystallinity PET trays used in low temperature freezer storage and high temperature oven-able applications. The high crystallinity is normally achieved through thermal crystallization. Therefore, a PET homopolymer is normally used to enhance the thermal crystallization rate. The high crystalline PET homopolymers used for such application normally also have high IVs of above 0.80 dL/g and preferably above 0.90 dL/g to achieve the good impact resistance in low temperature applications. Further, in order to improve the impact resistance, normally a loading level of 10 weight percent or more of the impact modifier has to be incorporated into CPET. In this invention, the same family of chemicals that are used as impact modifiers improves the stress cracking resistance of low IV PET based resins at much lower loading, preferably lower than 10 weight percent, such that the low IV PET based resin can perform similar to that of high IV PET materials in applications including, but not limited to CSD containers. The containers are made through injection blow molding processes, where the thermal crystallization is minimized in the injection molding to obtain clear preforms and the crystallinity is achieved through strain induced crystallization during the blow molding process.
Suitable impact modifiers for use in this invention include any impact modifier compatible with PET based resins. Preferred impact modifiers include elastomers. Still more preferred suitable impact modifiers include elastomers based on polyethylene, butadiene or isoprene, such as polybutadiene, polyisoprene, natural rubber, styrene-butadiene (SBR), acrylonytrile-butadiene, styrene-butadiene-styrene or hydrogenated SBS block copolymers, or acrylonytrile-butadiene-styrene polymers containing high levels of butadiene.
The impact modifiers that are especially useful are the ones modified to enhance the compatibility with PET based resins, such as polyethylene based elastomers. Examples of desirable polyethylene based elastomers include ethylene-acrylate copolymers such as ethylene/methylacrylate, ethylene/ethyl acrylate, ethylene/butyl acrylate and ethylene/methylacrylate/glycidyl methacrylate, or ethylene/vinyl acetate copolymers, or the copolymers of butadiene/MMA/styrene. U.S. Pat. Nos. 5,409,967 and 5,652,306 and PCT application WO00/15717 disclose the composition of such impact modifiers, and the specifications thereof are expressly incorporated herein by reference.
Suitable impact modifiers also include those with a core-shell structure which are described in U.S. Pat. No. 5,409,967 and PCT application WO00/15717. These core-shell modifiers normally contain a hard shell from methylmethacrylate copolymers and a core made from either butadiene methcrylate/butadiene-styrene copolymer or butyl acrylate copolymers. Examples of suitable core-shell impact modifiers include those available from Rohm & Haas Company under the trade name Paraloid.
Impact modifiers can contain added or reacted-to-the-chain compatibilizers. The compatibilizers are those functional groups that can enhance the compatibility or the miscibility of the impact modifiers with PET based resin. These modifiers include those described in PCT application WO 00/15717.
Normal impact modifiers have a different reflective index than that of PET based resins, and the resultant container is white or hazy. One way to solve this is to use modified impact modifiers. Impact modifiers can be modified to match the reflective index of the impact modifiers to that of PET based resins so that the resultant container is clear. The impact modifiers can also be modified with core-shell technology such that the compatibility as well as the reflective index is matched with PET based resins. Further, the impact modifiers can be modified by manipulating the particle sizes of the modifiers such that they are below the visible light wave length, normally below 0.1 microns. All these modifications can be achieved by those skilled in the art.
The impact modifier is present in the stress cracking resistant polyester composition in an amount effective to enhance the stress cracking resistance thereof relative to a polyester composition not including the impact modifier. Preferably, the impact modifier is present in the stress cracking resistant polyester composition in an amount from about 1 to about 10 weight percent of the stress cracking resistant polyester composition. More desirably, the impact modifier is present in an amount from about 3 to about 10 weight percent and even more preferably in an amount from about 3 to about 6 weight percent.
The PET based resin preferably comprises a diacid component having repeat units from terephthalic acid with less than about 5 mole percent modification and a diol component having repeat units from ethylene glycol with less than about 5 mole percent diol modification based on 100 mole percent diacid component and 100 mole percent diol component. The diacid modification can be a comonomer from any of a number of diacids, including adipic acid, succinic acid, isophthalic acid, phthalic acid, 4,4′-biphenyl dicarboxylic acid, 2,6-naphthalenedicarboxylic acid, and the like. The diol modification can be a comonomer such as cyclohexanedimethanol, diethylene glycol, 1,2-propanediol, neopentylene glycol, 1,3-propanediol, and 1,4-butanediol, and the like. The PET base resin preferably further comprises a comonomer for reducing the thermal crystallization rate thereby allowing for the manufacture of relatively clear containers.
In preferred embodiments, the IV of the PET based resin, as measured according to ASTM D4603-96, is from about 0.65 to about 0.90 dL/g, more preferably from about 0.65 to about 0.86 dL/g, still more preferably from 0.65 to 0.80 and further more preferably from about 0.68 to about 0.76 dL/g. According to ASTM D4603-96, the IV of PET based resin was measured at 30° C. with 0.5 weight percent concentration in a 60/40 (by weight fraction) phenol/1,1,2,2-tetrachloroethane solution.
As is well known to those skilled in the art, containers can be made by blow molding an injection molded preform. Examples of suitable preform and container structures and methods for making the same are disclosed in U.S. Pat. No. 5,888,598, the disclosure of which is expressly incorporated herein by reference in its entirety.
The preform 10 illustrated in
The preform 10, container 22, and packaged beverage 38 are but examples of applications using the stress cracking resistant compositions of the present invention. It should be understood that the compositions of the present invention can be used to make preforms and containers having a variety of configurations.
Embodiments of the present invention are further illustrated below by way of examples, which are not to be construed in any way as imposing limitations upon the scope of the invention.
Sample container preforms were injection molded using two different PET based resins and different stress crack resistance modifiers. Sample 1 was made with a first PET resin (R1), a commercially available CSD grade PET copolymer resin with an IV of 0.83, and Samples 2-6 were made with a second PET resin (R2), a commercially available water grade PET copolymer resin with an IV of 0.74. The compositions of the Sample preforms are set forth in Table 1.
Each preform was injection molded using 500 mL Contour design 28 g preforms under conditions that were set to produce molded samples with no crystallinity, haze or other visual imperfections based on the control resin variable. The PET resins R1 and R2 were dried overnight at 280° F. to a moisture level below 50 ppm. The stress crack resistance additives, poly[ethylene-co-butyl acrylate] (PBA, Aldrich #43,077-3) and poly[ethylene-co-methyl acrylate] (PMA, Aldrich #43,266-0), were dried over the weekend in a vacuum oven with no heat applied to avoid the sticking of additives. An Arburg 320H was used for the injection molding trial.
The preforms were blow molded into containers using a Sidel SBO1/2 machine. The blow molding process conditions that produced an acceptable container with appropriate section weights was established for each variable.
The intrinsic viscosity (IV) of each Sample was measured according to ASTM D4603-96 and the results are shown in Table 1.
TABLE 1 Resin/Additive Variables Actual % IV Sample Resin Additive Additive Added (dL/g) 1 R1 Control-None N/A 0.795 2 R2 Control-None N/A 0.696 3 R2 PBA 3.0 0.681 4 R2 PBA 5.0 0.670 5 R2 PMA 3.0 0.689 6 R2 PMA 5.0 0.679
The stress cracking resistance of the containers made from Samples 1-6 was measured and the results are shown in Table 2 measured by caustic stress cracking method. In the test, twenty-five containers were randomly selected. Due to the limited number of containers, the number of containers tested varied from 8 to 25 in different cases. The relative comparison was therefore used. The samples were carbonated to about 56 psi of CO2 and stored for 24 hours in an environment of 72° F. and 50% RH. The base of each sample container was immersed in a 0.1% NaOH solution. The % pass indicates the % of containers that passed the test and did not exhibit stress cracking.
TABLE 2 Caustic Stress Crack Results Average Minimum Maximum Failure Time Failure Time Failure Sample (min.) σ (min.) Time (min.) % Passed 1 180 0 180 180 100% 2 123 49 26 180 9% 3 180 0 180 180 100% 4 180 0 180 180 100% 5 175 11 150 180 75% 6 180 0 180 180 100%
The results in Table 2 clearly showed that the addition of the stress cracking resistance modifiers dramatically improved the stress cracking resistance of the containers made from low IV PET resins. The low IV resins with stress cracking resistance modifiers performed similarly to that of higher IV resins. In this case, the IV of the low molecular weight PET container is 0.68 and the IV of the high molecular weight PET container is 0.80, but their stress cracking performance is the same. Sample 2, the low IV resin without the modifier, could not pass the stress cracking test.
Sample container preforms were injection molded using two different PET based resins and different stress crack resistance modifiers. Sample 1 was made with a first PET resin (R3), a commercially available CSD grade PET copolyester resin with an IV of 0.84, and Samples 2-4 were made with a second PET resin (R4), a commercially available water grade PET copolyester resin with an IV of 0.74. The composition of the Sample preforms is set forth in Table 3.
The stress cracking resistance additive used was a commercially available Paraloid EXL core-shell impact modifier supplied by Rohm & Haas. The preforms were injection and blow molded according to Example 1. The containers were then subjected to the same tests and the results are shown in Table 4.
TABLE 3 Resin/Additive Variables Actual % IV Sample Resin Additive Additive Added (dL/g) 1 R3 Control-None 0 0.782 2 R4 Control-None 0 0.674 3 R4 EXL 3.0 0.651 4 R4 EXL 6.0 0.638
The stress cracking test was performed the same as in the Example 2. All variables had 25 containers for testing. The absolute failure time was thus used for the comparison. The average failure time for different variables is shown in the table 4. The longer the failure time, the better the stress cracking resistance. It is seen that both 3 and 6 wt % of the Paraloid EXL additive improved the stress cracking resistance of the low IV resin. For 6 wt %, it was very similar to that of the high IV resin.
TABLE 4 Stress Cracking Test Results Average failure Standard deviation Sample time (minutes) (minutes) 1 168.0 11.3 2 27.0 34.2 3 112.8 39.5 4 137.4 7.7
It should be understood that the foregoing relates to particular embodiments of the present invention, and that numerous changes may be made therein without departing from the scope of the invention as defined by the following claims.
|Patente citada||Fecha de presentación||Fecha de publicación||Solicitante||Título|
|US3960807 *||30 Sep 1974||1 Jun 1976||Minnesota Mining And Manufacturing Company||Thermoformed polyester articles having impact resistance and high temperature dimensional stability|
|US4820795 *||4 Dic 1987||11 Abr 1989||Toyo Seikan Kaisha, Ltd.||Polyester vessel and package|
|US4929375 *||14 Jul 1988||29 May 1990||Diversey Corporation||Conveyor lubricant containing alkyl amine coupling agents|
|US5001935 *||27 Feb 1990||26 Mar 1991||Hoover Universal, Inc.||Method and apparatus for determining the environmental stress crack resistance of plastic articles|
|US5009801 *||25 Ago 1989||23 Abr 1991||Diversey Corporation||Compositions for preventing stress cracks in poly(alkylene terephthalate) articles and methods of use therefor|
|US5073280 *||8 Jun 1990||17 Dic 1991||Diversey Corporation||Composition for inhibiting stress cracks in plastic articles and methods of use therefor|
|US5280066 *||18 Sep 1991||18 Ene 1994||Globe-Union Inc.||Polyester-polyolefin blends containing a functionalized elastomer|
|US5281387 *||7 Jul 1992||25 Ene 1994||Continental Pet Technologies, Inc.||Method of forming a container having a low crystallinity|
|US5300334 *||16 Dic 1992||5 Abr 1994||Ppg Industries, Inc.||Pressurizable thermoplastic container having an exterior polyurethane layer and its method of making|
|US5409967 *||22 Mar 1994||25 Abr 1995||Rohm And Haas Company||Amorphous, aromatic polyester containing impact modifier|
|US5439718 *||21 Jul 1993||8 Ago 1995||General Electric Company||Multilayer container of polycarbonate and amorphous polyamide of improved barrier and stress crack resistant properties|
|US5520877 *||30 Jun 1993||28 May 1996||Continental Pet Technologies, Inc.||Method of forming container with high-crystallinity sidewall and low-crystallinity base|
|US5602227 *||30 Ago 1995||11 Feb 1997||The Procter & Gamble Company||Biodegradable copolymers|
|US5652306 *||27 Mar 1996||29 Jul 1997||Rohm And Haas Company||Impact modifier combination for aromatic polyesters|
|US5681628 *||27 Dic 1993||28 Oct 1997||Ppg Industries, Inc.||Pressurizable thermoplastic container having an exterior polyurethane layer and its method of making|
|US5804617 *||20 Feb 1997||8 Sep 1998||Eastman Chemical Company||Poly(cyclohexylenedimethylene terephthalate) copolyester molding compositions|
|US5829614 *||24 May 1996||3 Nov 1998||Continental Pet Technologies, Inc.||Method of forming container with high-crystallinity sidewall and low-crystallinity base|
|US5859073 *||17 May 1995||12 Ene 1999||Ciba Specialty Chemicals Corportation||Polyester/polycarbonate blends having enhanced properties|
|US5880241 *||24 Ene 1996||9 Mar 1999||E. I. Du Pont De Nemours And Company||Olefin polymers|
|US5988416 *||10 Jul 1998||23 Nov 1999||Crown Cork & Seal Technologies Corporation||Footed container and base therefor|
|US5989661 *||27 Nov 1996||23 Nov 1999||Continental Pet Technologies, Inc.||Pressurized refill container resistant to sprue cracking|
|US6077904 *||17 Jul 1992||20 Jun 2000||Lawson Mardon Thermaplate Corporation||Elevated temperature dimensionally stable, impact modified polyester with low gas permeability|
|US6174990 *||21 Dic 1998||16 Ene 2001||The Procter & Gamble Company||Films comprising biodegradable PHA copolymers|
|US6207622 *||16 Jun 2000||27 Mar 2001||Ecolab||Water-resistant conveyor lubricant and method for transporting articles on a conveyor system|
|US6213325 *||22 Nov 1999||10 Abr 2001||Crown Cork & Seal Technologies Corporation||Footed container and base therefor|
|US6214777 *||24 Sep 1999||10 Abr 2001||Ecolab, Inc.||Antimicrobial lubricants useful for lubricating containers, such as beverage containers, and conveyors therefor|
|US6223683 *||14 Mar 1997||1 May 2001||The Coca-Cola Company||Hollow plastic containers with an external very thin coating of low permeability to gases and vapors through plasma-assisted deposition of inorganic substances and method and system for making the coating|
|US6262220 *||31 Jul 2000||17 Jul 2001||Bp Amoco Corporation||Polyester compositions|
|US6372318 *||30 Oct 1998||16 Abr 2002||Continental Pet Technologies, Inc.||Method of forming container with high-crystallinity sidewall and low-crystallinity base|
|US6426128 *||6 Ene 1998||30 Jul 2002||Hna Holdings, Inc.||Co-processable multi-layer laminates for forming high strength, haze-free, transparent articles and methods of producing same|
|US6427826 *||16 Jun 2000||6 Ago 2002||Ecolab Inc.||Container, such as a food or beverage container, lubrication method|
|US6485794 *||27 Jun 2000||26 Nov 2002||Ecolab Inc.||Beverage container and beverage conveyor lubricated with a coating that is thermally or radiation cured|
|US6495494 *||16 Jun 2000||17 Dic 2002||Ecolab Inc.||Conveyor lubricant and method for transporting articles on a conveyor system|
|US20020119267 *||19 Dic 2001||29 Ago 2002||Degussa Ag||Molding composition with good capability for blow molding|
|Patente citante||Fecha de presentación||Fecha de publicación||Solicitante||Título|
|US7553441||1 Oct 2004||30 Jun 2009||The Coca-Cola Company||Polyester composition for hot fill applications, containers made therewith, and methods|
|US7572493||11 May 2005||11 Ago 2009||The Coca-Cola Company||Low IV pet based copolymer preform with enhanced mechanical properties and cycle time, container made therewith and methods|
|US7790077||5 Sep 2007||7 Sep 2010||The Coca-Cola Company||Pressurized tooling for injection molding and method of using|
|US7820257||11 May 2005||26 Oct 2010||The Coca-Cola Company||Preforms for preparing lightweight stretch blow molded PET copolymer containers and methods for making and using same|
|US7820258||15 Sep 2006||26 Oct 2010||The Coca-Cola Company||Container and composition for enhanced gas barrier properties|
|US8124202||5 Sep 2007||28 Feb 2012||The Coca-Cola Company||Multilayer container for enhanced gas barrier properties|
|US8247049||18 Dic 2009||21 Ago 2012||The Coca-Cola Company||Preforms for preparing lightweight stretch blow molded pet copolymer containers and methods for making and using same|
|US8545952||14 Nov 2005||1 Oct 2013||The Coca-Cola Company||Polyester container with enhanced gas barrier and method|
|US20050100696 *||1 Oct 2004||12 May 2005||Yu Shi||Polyester composition for hot fill applications, containers made therewith, and methods|
|US20050118371 *||18 Oct 2004||2 Jun 2005||The Coca-Cola Company||PET copolymer composition with enhanced mechanical properties and stretch ratio, articles made therewith, and methods|
|US20070088133 *||6 Oct 2006||19 Abr 2007||Paul Heater||Process to Make Polyesters With An Interfacial Tension Reducing Agent for Blending with Polyamides|
|Clasificación de EE.UU.||428/35.7|
|Clasificación internacional||C08L55/02, C08L67/02, C08L9/00, C08L53/02, C08G63/00, C08L51/04, C08L23/08, C08G63/183|
|Clasificación cooperativa||C08L23/0853, C08L53/025, C08L9/00, C08L51/04, Y10T428/1352, C08L23/0869, C08L67/02, C08L53/02, C08L55/02|
|9 Ene 2004||AS||Assignment|
Owner name: COCA-COLA COMPANY, THE, GEORGIA
Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:SHI, YU;REEL/FRAME:014889/0857
Effective date: 20040109