OA19856A - Process for Scratch Masking of Glass Containers. - Google Patents
Process for Scratch Masking of Glass Containers. Download PDFInfo
- Publication number
- OA19856A OA19856A OA1201200271 OA19856A OA 19856 A OA19856 A OA 19856A OA 1201200271 OA1201200271 OA 1201200271 OA 19856 A OA19856 A OA 19856A
- Authority
- OA
- OAPI
- Prior art keywords
- émulsion
- scratch
- masking
- oil
- esters
- Prior art date
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- 239000011521 glass Substances 0.000 title claims abstract description 84
- 238000000034 method Methods 0.000 title claims abstract description 67
- 230000000873 masking Effects 0.000 title abstract description 11
- 238000000576 coating method Methods 0.000 claims abstract description 58
- 239000011248 coating agent Substances 0.000 claims abstract description 56
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 56
- 230000000087 stabilizing Effects 0.000 claims abstract description 43
- 239000000203 mixture Substances 0.000 claims description 47
- 239000003921 oil Substances 0.000 claims description 46
- 239000004094 surface-active agent Substances 0.000 claims description 44
- 238000009472 formulation Methods 0.000 claims description 26
- 230000003134 recirculating Effects 0.000 claims description 18
- JNYAEWCLZODPBN-CTQIIAAMSA-N Sorbitan Chemical class OCC(O)C1OCC(O)[C@@H]1O JNYAEWCLZODPBN-CTQIIAAMSA-N 0.000 claims description 17
- PEDCQBHIVMGVHV-UHFFFAOYSA-N glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 claims description 12
- 239000002253 acid Substances 0.000 claims description 7
- 239000006096 absorbing agent Substances 0.000 claims description 6
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- 150000007513 acids Chemical class 0.000 claims description 4
- 125000004432 carbon atoms Chemical group C* 0.000 claims description 4
- 239000000975 dye Substances 0.000 claims description 4
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- LYCAIKOWRPUZTN-UHFFFAOYSA-N glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 claims description 4
- 229920000223 polyglycerol Polymers 0.000 claims description 4
- 229920000151 polyglycol Polymers 0.000 claims description 4
- 239000010695 polyglycol Substances 0.000 claims description 4
- 239000007921 spray Substances 0.000 claims description 4
- -1 bactéricides Substances 0.000 claims description 3
- 235000014113 dietary fatty acids Nutrition 0.000 claims description 3
- 239000000194 fatty acid Substances 0.000 claims description 3
- 229920000098 polyolefin Polymers 0.000 claims description 3
- IJCWFDPJFXGQBN-BIFNRIDTSA-N Sorbitan tristearate Chemical compound CCCCCCCCCCCCCCCCCC(=O)OCC(OC(=O)CCCCCCCCCCCCCCCCC)[C@H]1OC[C@@H](O)[C@@H]1OC(=O)CCCCCCCCCCCCCCCCC IJCWFDPJFXGQBN-BIFNRIDTSA-N 0.000 claims description 2
- LWZFANDGMFTDAV-BURFUSLBSA-N [(2R)-2-[(2R,3R,4S)-3,4-dihydroxyoxolan-2-yl]-2-hydroxyethyl] dodecanoate Chemical compound CCCCCCCCCCCC(=O)OC[C@@H](O)[C@H]1OC[C@H](O)[C@H]1O LWZFANDGMFTDAV-BURFUSLBSA-N 0.000 claims description 2
- 150000003973 alkyl amines Chemical class 0.000 claims description 2
- 230000003115 biocidal Effects 0.000 claims description 2
- 239000003139 biocide Substances 0.000 claims description 2
- 238000007598 dipping method Methods 0.000 claims description 2
- 150000004665 fatty acids Chemical class 0.000 claims description 2
- 150000002194 fatty esters Chemical class 0.000 claims description 2
- 239000003205 fragrance Substances 0.000 claims description 2
- 150000002314 glycerols Chemical class 0.000 claims description 2
- 239000002304 perfume Substances 0.000 claims description 2
- 125000005359 phenoxyalkyl group Chemical group 0.000 claims description 2
- 150000003138 primary alcohols Chemical class 0.000 claims description 2
- 150000003333 secondary alcohols Chemical class 0.000 claims description 2
- 229940035044 sorbitan monolaurate Drugs 0.000 claims description 2
- 239000001589 sorbitan tristearate Substances 0.000 claims description 2
- 235000011078 sorbitan tristearate Nutrition 0.000 claims description 2
- 229960004129 sorbitan tristearate Drugs 0.000 claims description 2
- 239000000839 emulsion Substances 0.000 abstract description 7
- 230000002708 enhancing Effects 0.000 abstract description 3
- 239000012071 phase Substances 0.000 description 33
- 238000002156 mixing Methods 0.000 description 29
- 238000009833 condensation Methods 0.000 description 12
- 230000005494 condensation Effects 0.000 description 12
- 238000011049 filling Methods 0.000 description 10
- 239000007788 liquid Substances 0.000 description 10
- 238000005406 washing Methods 0.000 description 9
- 238000002372 labelling Methods 0.000 description 6
- 230000000670 limiting Effects 0.000 description 6
- 206010049796 Excoriation Diseases 0.000 description 4
- 230000002411 adverse Effects 0.000 description 4
- 238000005260 corrosion Methods 0.000 description 4
- 239000000314 lubricant Substances 0.000 description 4
- 239000011253 protective coating Substances 0.000 description 4
- 230000000996 additive Effects 0.000 description 3
- 239000008346 aqueous phase Substances 0.000 description 3
- 239000003795 chemical substances by application Substances 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 230000001264 neutralization Effects 0.000 description 3
- 239000002736 nonionic surfactant Substances 0.000 description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- ZQPPMHVWECSIRJ-KTKRTIGZSA-N Oleic acid Chemical compound CCCCCCCC\C=C/CCCCCCCC(O)=O ZQPPMHVWECSIRJ-KTKRTIGZSA-N 0.000 description 2
- IPCSVZSSVZVIGE-UHFFFAOYSA-N Palmitic acid Chemical compound CCCCCCCCCCCCCCCC(O)=O IPCSVZSSVZVIGE-UHFFFAOYSA-N 0.000 description 2
- 238000007792 addition Methods 0.000 description 2
- 125000000129 anionic group Chemical group 0.000 description 2
- 235000013361 beverage Nutrition 0.000 description 2
- 230000015556 catabolic process Effects 0.000 description 2
- 238000004581 coalescence Methods 0.000 description 2
- 239000008199 coating composition Substances 0.000 description 2
- 239000012141 concentrate Substances 0.000 description 2
- 230000001687 destabilization Effects 0.000 description 2
- 230000000368 destabilizing Effects 0.000 description 2
- 239000003995 emulsifying agent Substances 0.000 description 2
- 238000005189 flocculation Methods 0.000 description 2
- 230000016615 flocculation Effects 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 238000007689 inspection Methods 0.000 description 2
- KFZMGEQAYNKOFK-UHFFFAOYSA-N iso-propanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 2
- 239000007791 liquid phase Substances 0.000 description 2
- 239000007764 o/w emulsion Substances 0.000 description 2
- 229920000642 polymer Polymers 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 238000005086 pumping Methods 0.000 description 2
- 238000005507 spraying Methods 0.000 description 2
- WECIKJKLCDCIMY-UHFFFAOYSA-N 2-chloro-N-(2-cyanoethyl)acetamide Chemical compound ClCC(=O)NCCC#N WECIKJKLCDCIMY-UHFFFAOYSA-N 0.000 description 1
- NLXLAEXVIDQMFP-UHFFFAOYSA-N Ammonium chloride Substances [NH4+].[Cl-] NLXLAEXVIDQMFP-UHFFFAOYSA-N 0.000 description 1
- 210000004534 Cecum Anatomy 0.000 description 1
- 239000005642 Oleic acid Substances 0.000 description 1
- 235000021314 Palmitic acid Nutrition 0.000 description 1
- 239000004698 Polyethylene (PE) Substances 0.000 description 1
- 239000004372 Polyvinyl alcohol Substances 0.000 description 1
- 239000004147 Sorbitan trioleate Substances 0.000 description 1
- GLDOVTGHNKAZLK-UHFFFAOYSA-N Stearyl alcohol Chemical class CCCCCCCCCCCCCCCCCCO GLDOVTGHNKAZLK-UHFFFAOYSA-N 0.000 description 1
- 239000004393 Stigmasterol-rich plant sterol Substances 0.000 description 1
- 230000002378 acidificating Effects 0.000 description 1
- 239000000783 alginic acid Substances 0.000 description 1
- 235000019270 ammonium chloride Nutrition 0.000 description 1
- 235000013405 beer Nutrition 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 125000002091 cationic group Chemical group 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
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- 238000007730 finishing process Methods 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
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- 238000009533 lab test Methods 0.000 description 1
- QDHHCQZDFGDHMP-UHFFFAOYSA-N monochloramine Chemical compound ClN QDHHCQZDFGDHMP-UHFFFAOYSA-N 0.000 description 1
- 230000003000 nontoxic Effects 0.000 description 1
- 231100000252 nontoxic Toxicity 0.000 description 1
- 230000003287 optical Effects 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 229920001296 polysiloxane Polymers 0.000 description 1
- 229920002451 polyvinyl alcohol Polymers 0.000 description 1
- 238000006748 scratching Methods 0.000 description 1
- 230000002393 scratching Effects 0.000 description 1
- 230000035807 sensation Effects 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
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Abstract
The present invention relates to a process for applying oil-in-water emulsions for improving the glass surface appearance, particularly the external surfaces of glass containers. More particularly, the present invention relates to a process for applying a scratch masking coating on glass bottles, which enhances appearance, said process comprising the step of maintaining the oilin water emulsion in a stabilizing zone during a few seconds to about 300 minutes.
Description
PROCESS FOR SCRATCH MASKING OF GLASS CONTAINERS
The présent invention relates to a process of applying oil-in-water emulsion(s) onto glass surfaces, particularly the external surfaces of glass containers, in order to improve the appearance of said glass surface(s). More particularly, the présent invention relates to a process for applying a scratch masking coating on glass bottles, which enhances appearance.
ίο Glass articles such as returnable bottles are handled a great number of times during manufacture, inspection, filling, shipping, washing etc. During such handling the bottles corne into contact with various mechanical devices such as conveyors, inspection devices and the like as well as contact with other glass containers (such as bottles, jars, and the like) and surfaces such as boxes, shelves etc. This high degree of contact causes damage either is by breakage, cracking, scratching or other defects of the surface.
The use of scratch- or scuff-masking agents on glass containers is already well known and used. Such masking agents desirably mask scuffs, and exhibit acceptable durability and surface properties. Désirable properties for scuff-masking agents include water résistance and durability while being non-toxic and removable in washing operations, typically alkaline 20 washing operations.
Coatings for glassware can comprise polymeric materials, which cure after application to the bottle surface, either at room température or upon heating. For example, US Patent Number 4,273,834 discloses a spécifie organopolysiloxane and a curing catalyst that are applied to glass articles to mask abrasions. The material is cured on bottle surfaces at room 25 température or under heating. US Patent Number 5,346,544 discloses triglycéride materials and fatty acid esters of isopropyl alcohol as a coating for glass containers which are emulsified in water, applied to glass bottles and dried at room température or with heating.
US Patents Numbers 4,792,494 and 4,834,950 disclose the use of modified polyethylene preferably in the form of an aqueous dispersion to form a protective coating on glass 30 surfaces. The coating is typically applied at the end of a hot end finishing process whereby residual heat of the glass aids drying in a conventional cold end coating process.
US Patent Number 3,296,173 discloses a protective coating for glass comprising a reaction product of polyvinyl alcohol, an emulsified polyolefin and ammonium chloride. The coating is applied and heated whereby the composition reacts to produce a durable coating.
The variety of designs for glass bottle handling, cleaning and filling operations however results in a number of limitations on the applicability of prior art coating methods. Protective coatings are applied to glass containers during manufacture in either a hot end process
ι. , 19856 — 2 — and/or cold end process. In single use glass containers, such protective coatings are sufficient to protect against scuffing during the life of the container.
With returnable glass containers, which can be washed and refilled, for example 20 to 60 times or more, the 'production applied’ coatings are washed off and protection is lost. As the s number of return cycles increases, so does scuffing which results in an undesirable appearance.
In order to provide a better appearance, retumed bottles are treated with an anti-scuff coating during each wash/refill cycle. Known coating Systems, especially those that rely on heat to cure or dry an applied coating, are not effective on lines where the glass bottles are ίο cool, cooled or chilled.
For other coating Systems, such as émulsion based coating Systems, especially oil-in-water émulsions, instability of the émulsion on the glass surface is desired such that the émulsion breaks and the oil phase coating is deposited on the glass surface in order to form the scratch masking coating. Aqueous emulsion-based coating Systems often rely on émulsion is destabilization by breaking due to water phase évaporation.
However moisture on the bottles, such as condensation, can adversely impact such Systems, and with some coatings, long cure times due to moisture, such as condensation, can adversely impact the coating System. Ail current products known to date show poor or not satisfactory performances when applied on wet bottles, or on cold bottles which become 20 wet due to condensation, for example during filling of glass bottles or containers, with cold stuffs, typically cold liquids, such as sparkling liquids, e.g. sparkling water, sodas, beer, and the like.
Indeed, the applied product is diluted by the condensation water on the outside of the container, said dilution mainly resulting in a Tinsing off of the applied coating, said rinsing 25 off meaning no coating at ali.
Solutions to this problem already exist, such as Systems relying on émulsion destabilization through the addition of an émulsion destabilizer, or émulsions with high emulsifier concentration and active ingrédient concentration.
Emulsions based upon high emulsifier concentration consist in using more concentrated 30 émulsions, because the condensation water dilutes said émulsion. However, using more concentrated émulsions results in a not acceptable coating, since the amount of condensation water strongly varies, due to dew-point variations, so that the use of concentrated émulsions is not satisfying.
An example of addition of émulsion destabilizer is disclosed in EP-A-1 731 227. In this document, the émulsion breaker is an acid, and the resuit is an improved performance of the desired coating, even in the presence of condensation on the outer parts of the glass containers.
— 3 —
However the use of émulsion breakers, such as acids, suffer from several disadvantages, and it is now highly désirable to use émulsions with a neutral pH, in order to avoid, among others and to recite, the main drawbacks of acid émulsions:
corrosion issues, for both bottle closure and equipments;
issues with dyes, especially in labels that are pH sensitive;
security issues for local workers and end users;
environmental issues due to acidic effluents that are disposed off.
One other possibility consists in using scratch-masking aqueous émulsions, which can easily break during the coating on the glass containers. Such aqueous émulsions typically are of the oil-in-water type, the oil phase of which may for example contain a low amount of surfactant, say less than 15%, and even less than 10%. Such oil-in-water émulsions with low amount of surfactant that easily brakes in the case of the présent invention are also called “unstable” émulsions or “not too stable” émulsion in the présent invention.
However, depending on layout of filling line(s), a circulation piping, in the sense of piping from the point where the scratch-masking émulsion is prepared toward the application point (i.e. one way flow to applicator), is often created to feed e.g. the spray guns. In these cases, such “unstable” émulsions as discussed in previous paragraph, will lead to phase séparation already in this circulation piping. This results in either overloading of coating if a very oil rich émulsion or only the oil phase is applied in extreme case; or to less or no coating at alljf a too little oil containing émulsion or only the aqueous phase is applied, in the other extreme case.
In brief, ail formulations types, scratch-masking techniques, now available to the skilled artisan, hâve advantages and drawbacks that are summarized here-below:
Formulation type | Advantages | Drawbacks |
“Stable” émulsions | Stability | Rinsing off / overloading |
Emulsions comprising a destabilizer | Stability | Corrosion, security and environmental issues |
“Unstable émulsions | Safety, labelling compatibility | unstability |
Evidently, ali existing techniques are not satisfying and there is still a need for scratchmasking techniques and processes, which can combine ail the advantages without any of the drawbacks outlined here-above.
Now therefore, the main objectives of the présent invention are to provide a process to be used on returnable containers in order to face-lift or mask the white reflecting bands (scuff bands) that appear at the container-to-container (or other container to devices or surfaces) contact zones, because of intense glass to glass contact (or glass to devices and the like, as explained above), mainly during the filling process, after several trips of returnable glass containers.
— 4 —
Another objective of the présent invention is to provide a process for applying a formulation (a ‘masking fluid’), in order to repair the Visual aspect of such containers, since the presence of scuff bands strongly reduces the appearance of containers.
A further objective of the présent invention consists in providing an efficient scratch-masking or scuff-masking process, especially in case of filling conditions in which containers are filled with cold liquids, and water condensation of moisture at the container surface occurs.
Still another objective is to provide a process allowing the use of not too stable scratchmasking émulsions that would simply be rinsed off or strongly diluted, thereby avoiding the presence of significant higher concentration of active ingrédients in the émulsions.
Still another objective of the présent invention is to avoid the use of acid additive, or other type of additive(s), as a destabilizer that would lead to corrosion issues, label issues, as well as security and environmental issues.
The présent inventors hâve now found that the above objectives are met, in whole or in part, with the process of the présent invention, which is now described in more details herein below. Still other objectives will appear in the below description of the présent invention.
By the term émulsion’’ as used is denoted a dispersed system, where one liquid phase (the dispersed phase) is distributed in form of microscopie droplets in another liquid phase (the continuous phase), wherein in the présent invention the continuous phase is water.
By the term “émulsion stability” as used is denoted that no phase séparation occurs over time or more generally to resists change in its properties over time. From a thermodynamic point of view émulsions are not stable, but from a kinetic point of view they can be stable for a long time, which détermines their lifetime. The émulsion stability refers to the ability of the émulsion to resist changes in its properties especially breakdown processes over a certain time. As major breakdown processes known can be cited sedimentaion, creaming, flocculation and coalescence.
By the term stable émulsion” as used in the présent invention is denoted that no phase séparation appears meaning that the émulsion will not separate into its components in a macroscopie scale on a time scale of at least 2 hour when still in the piping system before being fed to applicator of the coating device. It has to be distinguished between the “stability” of the émulsion in the piping and the stability once the émulsion has been applied, latter meaning the émulsion is spread at the surface of a glass container.
By the term “unstable émulsion” as used is denoted that at least the first step of phase séparation occurs by séparation in two liquid layers on a time scale of 10 minutes, meaning that the émulsion is not homogenously anymore.
By the term “homogeneously” as used is denoted that there is no important gradient of distribution in the dispersed system. In case of a homogeneous émulsion the dispersed phase is uniformly distributed in the continuous phase at least from concentration point of view. According to the présent invention this concerns the variation of the concentration of — 5 — the oil phase in the aqueous phase that has a variation less then 20% based on the complété continuous phase.
By the term “stabilizing zone” as used in the present invention is denoted a zone where the scratch mask coating formulation in form of an oil-in-water émulsion is homogenously dispersed.
By the term “dynamic stabilizing zone” as used is denoted in the present invention is denoted a zone where the scratch mask coating formulation in form of an oil-in-water émulsion is homogenous and in movement as flowing.
By the term “HLB” as used is denoted the hydrophilic-lipophilic balance as established by ίο William C. Griffin in the 1950s in order to classify and distinguish non ionic surfactants in arbitrary scale from 1 to 20 (“Nonionic Surfactants”, Ed.: M. J. Schick, Marcel Decker, New York 1966, Chapter 18 Emulsification pages 604-626). Non ionic surfactants having a HLB of 4 and less are usually non dispersible in water and are considered as oils in the present invention.
is Therefore, according to a first aspect, the present invention relates to an improved process for the scratch-masking of containers, under both cold and wet conditions. Both laboratory tests and field expérience showed that several parameters do influence the effïciency of masking, related to the émulsion stability.
More specifically, the present invention relates to a process for applying a scratch-masking 20 aqueous émulsion on returnable glass containers, said process comprising at least the steps of:
preparing an aqueous émulsion of a scratch-masking formulation;
feeding the aqueous émulsion to a stabilizing zone; and feeding the aqueous émulsion from the stabilizing zone to the glass 25 container-coating device.
Step a) comprises, and advantageously consists in, the préparation of an aqueous émulsion, from a scratch-masking formulation and water. The émulsion may be prepared according to any conventional techniques known in the art, and for example by thoroughly mixing water and a scratch-masking formulation.
The so prepared aqueous formulation is then fed to a stabilizing zone (or buffer zone, or waiting zone), so that the prepared émulsion is maintained stable in that zone, ali along the pipes to the coating device.
The stabilizing zone (or buffer zone, or waiting zone) according to the invention comprises at least a tube, a mixing device and a pump, preferably a tube, a mixing device and a variable 35 flow rate pump, more preferably a tube and one unique mixing and pumping device, capable of variable flow rate. The stabilization zone may further comprise a buffer tank.
The stabilizing zone allows for the prepared émulsion to reach a stabilized state meaning a homogenous émulsion that stays in the stabilized state, which is necessary for the scratch19856 — 6 — masking fluid to arrive to the applying device in the émulsion State, said émulsion being unstable and breaks by itself when in contact with the glass container.
The émulsion used in the invention has a limited stability meaning that the émulsion will phase separate on a time scale much longer then 2 hours, however a slight coalescence of s the oil drops or a slight flocculation or a slight creaming might already hâve begun on a microscopie level, but the émulsion is still adapted to supply a homogenously distributed working liquid to the applicator.
The process of the invention therefore allows for the use of an émulsion which is stabilized enough and homogenously in composition throughout the whole piping of the installation ίο before coming to the coating device, and unstable enough so that said émulsion breaks by itself when in contact with the glass container, without the use of a too large amount of surfactant, and without the use of émulsion destabilizer(s) or émulsion breaker(s), or at least with a lesser amount of émulsion destabilizer(s) or émulsion breaker(s) as commonly used in the art.
Accordingly the process of the invention may be qualified as a “physical” stabilizing/destabilizing émulsion process, in opposition to the known “Chemical” stabilizing/destabilizing émulsion processes.
According to a preferred embodiment, the stabilizing zone is a dynamic stabilizing zone, i.e.
the aqueous émulsion is maintained in the stabilizing zone under constant 20 movement/agitation. this means that a shear force is applied to the aqueous émulsion and the émulsion is under constant flow.
The stabilizing zone may therefore consists in any device wherein an amount of freshly prepared émulsion is maintained under constant movement/agitation so that the said émulsion does not break ail along the feeding lines leading to the coating device, and 25 automatically breaks by itself when applied onto the glass container.
Devices for the stabilizing zone are for examples vessels provided with mixing tools, agitating tools, such as anchors, propellers, magnetic stirrers, and the like. According to a preferred embodiment of the invention, the stabilizing zone comprises a recirculating loop wherein the freshly prepared émulsion is circulated at high speed in a pipe-loop. By “high 30 speed is meant that the émulsion is circulated at such speed that it is homogeneously supplied to the coating device, that is to say typically at a speed of between about 10 L/hour and about 100000 L/hour, advantageously between about 100 L/hour and 4000 L/hour, and preferably between about 200 L/hour and about 2500 L/hour.
The pipe-loop may vary in great proportions regarding its shape and size, mainly depending 35 on the nature of the scratch-masking émulsion, the intrinsic stability of said émulsion, and the like. For example, the total volume of the pipe-loop may be comprised between 1 L or less and 500 L, preferably between 5 L to 200 L, although pipe-loops of smaller or larger volumes may be used. In principle the volume can be unlimited as long as the émulsion is circulated at such speed that it is homogeneously supplied to the coating device.
Figure 1 describes a schematic example of a System for implementing the process of the présent invention. Feed line 1 contains a scratch-masking formulation and feed line 2 contains an aqueous or water phase. Both feed lines 1 and 2 arrive into a mixing device 3 so that an émulsion is formed. Alternatively the scratch-masking formulation of feed line 1 is directly injected into the aqueous or water phase of feed line 2 just before entering the mixing device 3 (not shown).
The freshly prepared émulsion enfers the stabilizing zone 4, which is in this example a recirculating loop (circulating pipe) 5, wherein the émulsion is recirculated via a pump 6. The émulsion is then transferred to the out-pipe 7 leading to the coating device. The stabilizing zone 4 may further comprise a buffer tank (not represented) so that a minimum amount of émulsion remains within the stabilizing zone 4 and is ready to be transferred to the out-pipe
7.
According to a preferred embodiment, pump 6 is variable flow rate pump allowing for the variation of the circulation speed of the émulsion within the recirculating loop 5, so that the stability of said émulsion may be finely tuned, as required by the giass coating conditions (coating on wet or dry giass ware, containing hot or warm liquids, important levels of scratches, scratch-masking efficiency of the scratch-masking formulation, and the like).
According to a further prefeσed embodiment, the mixing device 3, and the pump 6, which is preferably a variable flow rate pump, are one unique mixing and pumping device, that is to say the mixing device 3 allows for the préparation of the émulsion as well as the circulation of the freshly prepared émulsion ail along within the stabilizing zone 4.
Depending on the characteristics of the stabilizing zone (for example where the stabilizing zone is a recirculating loop: circulating speed, length of the recirculating loop, diameter of the recirculating pipe), the freshly prepared aqueous émulsion is maintained in said stabilizing zone during a few seconds to about 300 minutes, preferably during about 30 seconds to about 100 minutes, more preferably during about 1 minute to about 20 minutes.
As discussed herein-above, the process of the présent invention relies on the fact that the stabilizing zone allows to maintain the stability of the freshly prepared émulsion ail along the feeding pipes, so that the émulsion is still stable and homogenously when it reaches the coating device.
The coating device may be any coating device known by the skilled in the art for applying scratch-masking aqueous émulsions onto retumable giass containers, such as devices appropriate for spray application (e.g. spray-guns), dipping or any other contact method (sponge, and the like), and the like. Spray-coating is the préférable method of application in the présent invention.
— 8 —
According to an advantageous embodiment, the overload (e.g. overspray) and rinse down of the scratch-masking aqueous émulsion applied on the glass containers may be collected with any collecting means known in the art (e.g. such as collecting bins, funnels, and the like). According to a further advantageous embodiment, said collected overload/rinse down may be re-injected back into the stabilizing zone, preferably after filtration and/or quality checking according to methods well known in the art.
The process of the présent invention provides for enhanced control of émulsion based glass surface masking coatings that is applicable in many types of application Systems, such as those where the glass containers are warm as well as those where the glass containers are cold.
The process of the présent invention can be employed in a variety of bottle handling operations, warm as well as cold application températures, as well as be adapted to changing conditions such as water variations or changes in condensation due to variation in humidity in the surrounding area.
Thanks to the presence of the stabilizing zone in the process of the présent invention, it is possible to use oil-in-water émulsions that comprise a low amount of surfactant, said émulsions being known to be too unstable for use in conventional processes for applying scratch-masking émulsions.
Contrary to the currently used émulsions that generally comprise a high amount of surfactant, especially more than 20 weight%, the use of less than 15weight%, preferably less than 10 weight%, still more preferably less than 8 weight%, of surfactant in the scratchmasking formulation provides excellent results, both in cold and wet conditions.
According to a preferred embodiment, the formulation used in the process of the invention comprises less than 15wt%, more precisely from 0.1 wt% to 15wt% of at least one surfactant and from 85 wt% to 99.9 wt% of at least one oil.
According to a further preferred embodiment, the above formulation comprises from 1 wt% to 10 wt% of at least one surfactant and from 90 wt% to 99 wt% of at least one oil. Still more preferably, the above formulation comprises from 1.5 wt% to 8wt% of at least one surfactant and from 92 wt% to 98.5 wt% of at least one oil.
In the above formulations, any surfactant(s) and any oil(s) can be mixed together, provided that they are miscible the one in the other, and typically are able to form an aqueous oil-inwater émulsion. Moreover, preferred formulations to be used as oil-in-water émulsions are liquid formulations, solid formulations being not convenient as scratch-masking coatings.
The surfactants can be non-ionic, anionic, cationic or zwitterionic. Preferably, the surfactant(s) are non-ionic in order to avoid mixing problems with the oil(s), and, when anionic, to prevent sait formation when emulsified with ion-containing water. '
According to a preferred aspect, the surfactant(s) used in the présent invention may be chosen from among:
— 9 — alkoxylated (preferably ethoxylated and/or propoxylated) phenoxy alkyls;
optionally alkoxylated (preferably ethoxylated and/or propoxylated) primary or secondary alcohols, such as, by way of non limiting examples, oleyl- or stearyl-alcohols;
alkoxylated (preferably ethoxylated and/or propoxylated) alkylamines, such as, by way of non limiting examples, surfactants sold by CECA S.A., under the name Noramax®, preferably Noramax® S2, and Noramax® S5;
alkoxylated (preferably ethoxylated and/or propoxylated) acids, such as, by way of non limiting examples, oleic acid and palmitic acid;
alkoxylated (preferably ethoxylated and/or propoxylated) esters, preferably glycerol esters, sorbitan esters or alkoxylated (preferably ethoxylated and/or propoxylated) sorbitan esters preferably with a HLB value of more then 4 and more preferably chosen from sorbitan monooelate, sorbitan mono stéarate and sorbitan monolaurate and mixtures therof.
polyglycol or glycol, mono-, and/or and di-esters; preferably with a HLB value of more then 4; and polyglycerol or glycerol, mono- and/or di- and/or tri-esters, preferably with a HLB value of more then 4 and more preferably chosen from polyglyceryl-oleates
When ethoxylated, the surfactants preferably comprise an average of up to 15 EO units per mole.
When the formulations are used in the process of the présent invention for coating of glass containers in the food and beverage industry, the surfactant(s) are preferably chosen from among those listed in the European food additive list E numbers, more preferably from sections E400 to E499, and still more preferably from among the group of sorbitan esters, sections E491 to E496.
Mixtures of two or more surfactant(s) may be used.
Besides the surfactant(s), the formulation for use in the process of the présent invention comprises at least one oil, which may be of any type known in the art. By “oil” is meant any compound, oil or polymer, that is miscible with the surfactant(s) but not miscible with water and capable of forming an oil-in-water émulsion, that is to say an oil or polymer discontinuous phase in an aqueous or water continuous phase.
Preferred oils may be for example chosen from among:
polyolefins such as paraffins oils;
fatty acids;
fatty esters, preferably mono esters, having more than 10 carbon atoms, and preferably up to 40 carbon atoms;
sorbitan esters or alkoxylated (preferably ethoxylated and/or propoxylated) sorbitan esters advantageously with a HLB value of equal or less then 4 and very advantageously chosen from sorbitan trioelate, sorbitan tristearate and sorbitan trilaurate and mixtures therof, — 10 —
Polyglycol or glycol, mono-, and/or and di-esters, advantageously with a HLB value of equal or less then 4; and
Polyglycerol or glycerol, mono- and/or di- and/or tri-esters, advantageously with a HLB value of equal or less then 4.
Mixtures of two or more oil(s) may be used.
When necessary and/or when desired, the above-described formulations comprising at least one surfactant and at least one oil, may also comprise one or more additives usually used and known in the art, such as, for example, those chosen from among:
biocides, bactéricides;
dyes;
émulsion destabilizers, such as acids;
perfumes, odorants;
UV absorbers, light absorbers, impact absorbers; and the like.
Such additives may be added in the formulation oii(s) + surfactant(s) and/or in the oil-inwater ready-to-use émulsion and/or in the aqueous phase or water used for forming the émulsion. According to a preferred embodiment the formulation for use in the présent invention does not contain any additive, and preferably consists in a mixture of at least one oil and at least one surfactant, such as those described above.
As previously described, the formulation (oil(s) + surfactant(s)) is used as an oil-in-water émulsion, that is to say a water continuous phase having dispersed, or emulsified therein, an oil phase, wherein the oil phase is the scratch-masking coating.
The émulsion is typically prepared by mixing an oil phase-containing surfactant(s) with an aqueous or water phase. The oil phase and surfactant can be supplied as a concentrate to be mixed with water by the end user to form the treatment émulsion or supplied as a readyto-use émulsion.
According to an alternative, the émulsion may be prepared by mixing water and at least one of the above-defined surfactants, then adding and mixing at least one of the above-defined oils, or prepared by mixing water and at least one of the above-defined oils, then adding and mixing at least one of the above-defined surfactants.
In other words, the scratch-masking émulsion to be fed into the stabilizing zone before being applied on the glass surface, may be prepared by mixing at least one oil, at least one surfactant and water, in any order, so as to obtained the desired oil-in-water émulsion.
The preferred concentrations of the oil phase in the as applied émulsions are from about 2% to 20% by weight, preferably from about 2.5% to 15% by weight, more preferably from about
3% to 10% by weight of the total weight of the oil-in-water émulsion. Variations in water — 11 — quality such as pH or hardness can impact the quality and stability of the final treatment émulsion when supplied as a concentrate for mixing with local water.
The formulations for use in the process of the présent invention, although comprising a relatively low amount of surfactant(s), surprisingly show outstanding results even when used in spray-coating cabinets presenting complex layout of filling lines (i.e. cabinets with a number of valves, fittings, long feed pipes, and the like).
Such low-containing surfactant émulsions would generally be too unstable and would break before being applied on the glass surfaces. The stabilizing zone, which is part of the process of the présent invention, allows such low-containing surfactant émulsions to remain stable until their use as scratch-masking émulsions.
The émulsion to be fed into the stabilizing zone is obtained by thoroughly mixing water, at least one surfactant, and at least one oil, as described above. Any mixing device known in the art is appropriate, provided that, depending on parameters and layout, the amount of mixing energy is set in such a way that homogeneous émulsion is supplied to the applicator but of limited émulsion stability.
The mixing energy devoted to the préparation of the above described oil-in-water émulsion should be set so that the émulsion is stable for a period time ranging from a few seconds to a few hours, and preferably for period of time that is adapted so as to supply a homogenous working liquid to the applicator. This period of time therefore dépends on the flow lines, application devices, and the like.
Any mixing means may be used to achieve an oil-in water-emulsion from water and the above-described formulation. Typical mixers or emulsifying devices are those known in the art, and as non limiting examples, mention may be made of dynamic mixers, static mixers, ultra-sonie mixing devices, pumps, and the like.
As described above, the présent invention provides a process for applying a coating, typically a scratch-masking coating, to a glass container surface, such as bottles, that is adaptable to a variety of glass surface and application conditions.
The coating provides for masking of scratches and abrasions on the glass container surface, which adversely impact its commercial value. For examples, scratches or abrasions on glass bottles, especially on returnable glass bottles used for beverages, resuit in an undesirable haze or white appearance, which decreases the value of the bottle. The process of the présent invention provides a coating for glass containers that masks such scratches or abrasions. In addition, the coating can enhance the lubricity of the container surface.
Moreover, and thanks to the process of the présent invention comprising a step of allowing the émulsion in a stabilizing zone, preferably under dynamic conditions, the low amount of surfactant(s), as well as the neutral or almost neutral pH of the émulsion, leads to less, or even no, corrosion, security or environmental issues. Additionally, dyes in labels, which are — 12 — generally known to be surfactant sensitive, are far much less affected, while using low oil-inwater émulsion as described in the présent invention.
According to another feature, the process of the présent invention further comprises a step d) wherein the scratch-maskirig coating émulsion is applied to a glass surface, more specifically to a glass container surface, such as bottles, onto at least one part of, or onto the entire, outer surface of said glass container.
Still further steps may be présent along the process of the présent invention, such as, and in a non limiting way:
washing of the glass container;
applying a lubricant onto the outer surface of said glass container;
filling and capping the glass container; and labelling the glass container.
The washing of the glass container may be realised according to any method well known in the art, and for example using water, preferably hot water, more preferably together with one or more detergent, for example a base, such as sodium hydroxide.
At least one lubricant can also be applied onto the outer surface of the glass container after washing. Such lubricants are known in the field, such as for example Tegoglass® 3000 Plus provided by Arkema.
The glass containers are then filled and capped, again according to known methods, with cold, tepid, or even warm liquids. As evidenced by the annexed examples, the efficiency of the scratch-masking coating applied according to the process of the présent invention is not adversely affected by the condensation that may appear on the outer surface of the glass container, because of différences of températures between the glass container, the filled liquid, and/or the outer température and relative humidity of the environment.
Labelling may be realised before or after applying the scratch-masking émulsion. Washing, applying the lubricant, filling and capping the containers are preferably operated before applying the scratch-masking émulsion.
Should the labelling step be realised before the scratch-masking coating step, the step consisting in applying the scratch-masking émulsion may thus be the last step before the newly washed, refilled and labelled glass containers are once again put on the market, and sold to the customers.
The process of the présent invention is therefore well adapted to existing equipments for refilling returnable glass containers, such as equipments where the returnable glass containers are placed on conveyer belts and undergo ail or parts of the above described washing, refilling, capping, scratch-masking, and labelling steps.
In one embodiment of the process the scratch-masking aqueous émulsion is applied at the returnable glass containers at a température equal or less then the dew point.
— 13 —
Apart from the “stabilizing zone” device, no spécifie equipment is required for carrying out the process of the invention, this meaning that any and ail known equipments in the art are convenient for the use and process of the invention.
The application equipment typically includes mixing and storage vessels, pumps, transfer and feed lines, spray apparatus and control and monitoring equipment.
The equipment may also comprise controlling means aiming at monitoring the flow rates in the feeding lines, the conditions in the stabilizing zone (mixing speed, recirculation speed, résidence time, and the like), the process of applying the scratch-masking émulsion. Such controlling means may be for example optical means detecting the presence or the absence io of a container in front of the applying means, and/or detecting the presence and the quantity of seuff bands or scratches, so that the minimum amount of émulsion is applied on the containers to obtain the best efficiency. According to a preferred aspect, the controlling means are monitored via a computer that may interact with the dosing pump(s), valves, mixing speed and applying means.
is Still according to a preferred embodiment, the above described equipment may be encased within a “scratch-masking” cabinet that can be easily adapted to existing bottling lines, comprising the necessary equipment for washing, filling, capping and labelling glass containers, typically retumable glass bottles.
As described herein-before, the equipment for applying a scratch-masking coating onto 20 retumable glass containers comprises a stabilizing zone, preferably a dynamic stabilizing zone, which forms the very subject matter of the présent invention.
A particularly well adapted “stabilizing zone” device is a recirculating loop when using scratch-masking coatings in the form of oil-in-water émulsion wherein the oil phase comprises at least one surfactant at low concentration, typically from 0.1 wt% to 15wt%, 25 preferably from 1 wt% to 10wt%, and more preferably from 1.5 wt% to 8wt%. Such a recirculating loop comprising a scratch-masking oil-in-water émulsion is also part of the présent invention.
According to still a further object, the présent invention also encompasses the use of such a recirculating loop in a process for applying a scratch-masking coating on retumable glass 30 containers.
According to still another object the présent invention encompasses an apparatus containing a recirculating loop comprising a scratch-masking formulation in form of an oil-inwater émulsion, wherein the concentration of the oil phase is from about 2% to 20% by weight, preferably from about 2.5% to 15% by weight, more preferably from about 3% to 35 10% by weight of the total weight of the oil-in-water émulsion.
According to still another object the présent invention concerns the use of the apparatus containing a recirculating loop in a process for applying a scratch-masking coating on retumable glass containers.
— 14 —
In one embodiment the used apparatus contains a recirculating loop and the scratchmasking coating is applied on returnable giass containers at a température equal or less then the dew point..
The dew point (or dew point température) is the particular température to which humid air has to be cooled, at constant pressure, in order to become saturated with water vapour; i.e. the relative humidity gets 100% at said température. As a conséquence, when the température of air is lowered to its dew point and beyond, water vapour will condensate to produce dew. Similarly, when the température of an object is at or below the dew point of the surrounding air, water will condensate on this object. The dew point is a saturation température that is associated with température and relative humidity, as shown in the table 1 below.
Table 1 -
Température °C | Relative humidity % | Dew point température °C |
10 | 70 | 4.8 |
20 | 70 | 14.4 |
30 | 70 | 23.9 |
40 | 70 | 33.5 |
The présent invention is illustrated in more detail in the following non-limiting examples.
Examples
Various tests are conducted with various scratch-masking formulations in a System as shown in Figure 1, equipped with a buffer tank. To this tank is added a water stream in which the scratch-masking formulation is injected to give an émulsion with a set concentration.
The émulsion is circulated through the circulating pipe at approximately 2000 L/h, while the applied amount is between about 2 L/h and 50 L/h, or even higher, depending on bottle size, and line speed, say for example 500 mL bottle size, running at a speed of about 10000 bottles per hour to 50000 bottles per hour.
The diameter ofthe circulating pipe is such that pressure drop overthe circulating pipe is minimized. The circulating pipe has the spécifications shown in Table 2 below:
Table 2 -
Total circulating pipe length (m) | Internai diameter ofthe circulating pipe (mm) |
10 | 25 |
50 | 35 |
100 | 42 |
220 | 48 |
— 15 —
Emulsions prepared with formulations having more than 20 wt% of surfactant(s) are stable enough, so that the use of the circulating pipe is not necessary. However, when applied on cold bottles (10°C to 12°C), condensation forms on the outside of the glass containers and the applied émulsion is rinsed off, and the scratch-masking appearance is not satisfactory. Emulsions prepared from scratch-masking formulations with less than 15 wt%, and even with less than 8 wt% of surfactants in the oil phase hâve limited stability. Such émulsions are fed into a recirculating loop, as described herein before, having a total length of 50 meters or of 100 meters, at a speed rate of between 1500 L/h and 2000 L/h. The total volume of the recirculating loop is between 100 L and 200 L.
The émulsions are recirculated during about 4 minutes to 10 minutes. Longer résidence times may be applied, however 10 minutes are generally sufficient to obtain a suitable stability of the émulsions until they reach the coating device and the glass containers. Such émulsions are sprayed on cold (10°C to 12°C) and wet (due to condensation) bottles, at for example a rate of about 0.01 mL/bottle to about 10 mL/bottle, preferably of about 0.1 mL/bottle to about 1 mL/bottle, these figures being based on a 500 mL bottle size.
The émulsions generally hâve a stability limit of about 10 minutes. Depending on the coating conditions (température of the containers, ambient humidity, amount of scratch-masking composition to be coated, length of the pipes till the coating device, and the like), this stability limit may be lengthened or shortened by varying the mixing means (préparation of the émulsions), by varying the mixing speed, by varying the speed rate into the stabilizing zone, and/or by varying the length of the circulating pipe of the stabilizing zone.
The process of the invention therefore présents the advantage of an easy optimising of the émulsion stability for each situation.
Using the process according to the présent invention, and an aqueous émulsion comprising from 2 wt% to 20 wt% of an oil phase, wherein the oil phase comprises less than 8 wt% surfactant (based on the total weight of the oil phase), excellent masking of scratches can be obtained on wet and cold bottles, under the above-indicated conditions: scuff are masked, the glass containers hâve a “new glass” appearance, while still presenting a normal touch sensation.
The process of the présent invention is also perfectly suitable with such “low-stability” émulsions (having a low level of surfactant) for scratch-masking of glass containers/bottles under dry and hot conditions.
Claims (15)
1. Process for applying a scratch-masking aqueous émulsion on returnable glass containers, said process comprising at least the steps of:
a) preparing an aqueous émulsion of a scratch-masking formulation;
b) feeding the aqueous émulsion to a stabilizing zone; and
c) feeding the aqueous émulsion from the stabilizing zone to the glass container-coating device.
2. Process according to claim 1, wherein the stabilizing zone is a dynamic stabilizing zone.
3, Process according to claim 1, wherein the stabilizing zone comprises a recirculating loop wherein the émulsion prepared at step a) is circulated at high speed in a pipe-loop, typically at a speed of between about 10 L/hour and about 100000 L/hour, advantageously between about 100 L/hour and 4000 L/hour, and preferably between about 200 L/hour and about 2500 L/hour.
4; and polyglycerol or glycerol, mono- and/or di- and/or tri-esters, preferably with a HLB value of more then 4 and more preferably chosen from polyglyceryl-oleates.
4. Process according to claim 1, wherein the émulsion is maintained in said stabilizing zone during a few seconds to about 300 minutes, preferably during about 30 seconds to about 100 minutes, more preferably during about 1 minute to about 20 minutes.
5. Process according to claim 1, wherein the scratch-masking formulation comprises from 0.1 wt% to 15 wt% of at least one surfactant and from 85 wt% to 99.9 wt% of at least one oil, preferably from 1 wt% to 10 wt% of àt least one surfactant and from 90 wt% to 99 wt% of at least one oil, and more preferably, from 1.5 wt% to 8 wt% of at least one surfactant and from 92 wt% to 98.5 wt% of at least one oil.
6. Process according to claim 1, wherein the scratch-masking formulation comprises at least one surfactant chosen from among:
• alkoxylated (preferably ethoxylated and/or propoxylated) phenoxy alkyls;
• optionally alkoxylated (preferably ethoxylated and/or propoxylated) primary or secondary alcohols;
• alkoxylated (preferably ethoxylated and/or propoxylated) alkylamines;
• alkoxylated (preferably ethoxylated and/or propoxylated) acids;
• alkoxylated (preferably ethoxylated and/or propoxylated) esters, preferably glycerol esters;
— 17 — • sorbitan esters or alkoxylated (preferably ethoxylated and/or propoxylated) sorbitan esters, preferably with a HLB value of more then 4 and more preferably chosen from sorbitan monooeiate, sorbitan mono stéarate and sorbitan monolaurate and mixtures therof;
• polyglycol or glycol, mono-, and/or and di-esters; preferably with a HLB value of more then
7. Process according to claim 1, wherein the scratch-masking formulation comprises at least one oil chosen from among:
• polyolefins such as paraffins oils;
• fatty acids;
• fatty esters, preferably mono esters, having more than 10 carbon atoms, and preferably up to 40 carbon atoms;
• sorbitan esters or alkoxylated (preferably ethoxylated and/or propoxylated) sorbitan esters, advantageously with a HLB value of equal or less then 4 and very advantageously chosen from sorbitan trioelate, sorbitan tristearate and sorbitan trilaurate and mixtures therof, • Polyglycol or glycol, mono-, and/or and di-esters, advantageously with a HLB value of equal or less then 4; and ...... ............. ..... ...... - ............
• Polyglycerol or glycerol, mono- and/or di- and/or tri-esters, advantageously with a HLB value of equal or less then 4..
8. Process according to claim 1, wherein the scratch-masking formulation further comprises one or more additives chosen from among biocides, bactéricides, dyes, émulsion destabilizers, perfumes, odorants, UV absorbers, light absorbers, impact absorbers, and the like.
9. Process according to claim 1, wherein the concentration of the oil phase in the scratchmasking émulsion is from about 2% to 20% by weight, preferably from about 2.5% to 15% by weight, more preferably from about 3% to 10% by weight of the total weight of the oilin-water émulsion.
10. Process according to claim 1 further comprising a step d) wherein the scratch-masking coating émulsion is applied to a glass surface, more specifically to a glass container surface, such as bottles, onto at least one part of, or onto the entire, outer surface of said glass container, by means of a coating device, such as devices appropriate for spray application, dipping or any other contact method, and the like.
— 18 —
11. Process according to any of claims 1 to 10, wherein the scratch-masking aqueous émulsion is applied at the returnable glass containers at a température equal or less then the dew point.
12. Apparatus containing a recirculating loop comprising a scratch-masking formulation in form of an oil-in-water émulsion, wherein the concentration of the oil phase is from about 2% to 20% by weight, preferably from about 2.5% to 15% by weight, more preferably from about 3% to 10% by weight of the total weight of the oil-in-water émulsion.
13. Apparatus containing a recirculating loop according to claim 12, wherein the oil phase of said oil-in-water émulsion comprises at least one surfactant in an amount of from 0.1 wt% to 15 wt%, preferably from 1 wt% to 10 wt%, and more preferably from 1.5 wt% to 8 wt%.
14. Use of the apparatus containing a recirculating loop according to any of claims 12 or 13 in a process for applying a scratch-masking coating on returnable glass containers.
15. Use according to claim 14, wherein the glass containers are at a température equal or less then the dew point..
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP09179148.3 | 2009-12-14 |
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Publication Number | Publication Date |
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OA19856A true OA19856A (en) | 2021-06-23 |
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