WO2002049830A2 - Verfahren zur herstellung von blasgeformten hohlkörpern mit mattierten oberflächen - Google Patents
Verfahren zur herstellung von blasgeformten hohlkörpern mit mattierten oberflächen Download PDFInfo
- Publication number
- WO2002049830A2 WO2002049830A2 PCT/EP2001/014433 EP0114433W WO0249830A2 WO 2002049830 A2 WO2002049830 A2 WO 2002049830A2 EP 0114433 W EP0114433 W EP 0114433W WO 0249830 A2 WO0249830 A2 WO 0249830A2
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- blow
- plastic
- blow mold
- hollow body
- mold
- Prior art date
Links
- 238000000034 method Methods 0.000 title claims abstract description 35
- 229920003023 plastic Polymers 0.000 claims abstract description 56
- 239000004033 plastic Substances 0.000 claims abstract description 54
- 239000000654 additive Substances 0.000 claims abstract description 34
- 239000000463 material Substances 0.000 claims abstract description 17
- 230000003746 surface roughness Effects 0.000 claims abstract description 9
- 239000011265 semifinished product Substances 0.000 claims abstract description 3
- 239000002356 single layer Substances 0.000 claims abstract description 3
- 229920001169 thermoplastic Polymers 0.000 claims abstract description 3
- 238000004519 manufacturing process Methods 0.000 claims description 22
- 238000000071 blow moulding Methods 0.000 claims description 19
- 239000010410 layer Substances 0.000 claims description 14
- 238000010101 extrusion blow moulding Methods 0.000 claims description 10
- -1 polyethylene Polymers 0.000 claims description 7
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 6
- 230000000996 additive effect Effects 0.000 claims description 5
- 239000002245 particle Substances 0.000 claims description 5
- 239000000126 substance Substances 0.000 claims description 5
- 239000004952 Polyamide Substances 0.000 claims description 3
- 239000004698 Polyethylene Substances 0.000 claims description 3
- 239000004743 Polypropylene Substances 0.000 claims description 3
- 239000012530 fluid Substances 0.000 claims description 3
- 239000000203 mixture Substances 0.000 claims description 3
- 229920000747 poly(lactic acid) Polymers 0.000 claims description 3
- 229920002647 polyamide Polymers 0.000 claims description 3
- 229920000728 polyester Polymers 0.000 claims description 3
- 229920000573 polyethylene Polymers 0.000 claims description 3
- 239000005020 polyethylene terephthalate Substances 0.000 claims description 3
- 229920000139 polyethylene terephthalate Polymers 0.000 claims description 3
- 239000004626 polylactic acid Substances 0.000 claims description 3
- 229920000098 polyolefin Polymers 0.000 claims description 3
- 229920001155 polypropylene Polymers 0.000 claims description 3
- 229920000915 polyvinyl chloride Polymers 0.000 claims description 3
- 239000004800 polyvinyl chloride Substances 0.000 claims description 3
- 235000012239 silicon dioxide Nutrition 0.000 claims description 3
- 239000000377 silicon dioxide Substances 0.000 claims description 3
- 238000010348 incorporation Methods 0.000 claims 1
- 239000002991 molded plastic Substances 0.000 abstract 1
- 230000000694 effects Effects 0.000 description 8
- 238000002347 injection Methods 0.000 description 5
- 239000007924 injection Substances 0.000 description 5
- 238000001746 injection moulding Methods 0.000 description 4
- 230000001788 irregular Effects 0.000 description 4
- 238000005488 sandblasting Methods 0.000 description 4
- 238000007664 blowing Methods 0.000 description 3
- 239000002537 cosmetic Substances 0.000 description 3
- 238000005530 etching Methods 0.000 description 3
- 238000001125 extrusion Methods 0.000 description 3
- 239000011521 glass Substances 0.000 description 3
- 239000008187 granular material Substances 0.000 description 3
- 239000011324 bead Substances 0.000 description 2
- 235000013361 beverage Nutrition 0.000 description 2
- 230000003628 erosive effect Effects 0.000 description 2
- 238000005498 polishing Methods 0.000 description 2
- 238000005266 casting Methods 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 238000005352 clarification Methods 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 239000003845 household chemical Substances 0.000 description 1
- 239000004922 lacquer Substances 0.000 description 1
- 230000000877 morphologic effect Effects 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 238000004806 packaging method and process Methods 0.000 description 1
- 238000010422 painting Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 230000003678 scratch resistant effect Effects 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 238000005494 tarnishing Methods 0.000 description 1
- 239000012815 thermoplastic material Substances 0.000 description 1
- 239000005028 tinplate Substances 0.000 description 1
- 238000009423 ventilation Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C49/00—Blow-moulding, i.e. blowing a preform or parison to a desired shape within a mould; Apparatus therefor
- B29C49/0005—Blow-moulding, i.e. blowing a preform or parison to a desired shape within a mould; Apparatus therefor characterised by the material
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C49/00—Blow-moulding, i.e. blowing a preform or parison to a desired shape within a mould; Apparatus therefor
- B29C49/42—Component parts, details or accessories; Auxiliary operations
- B29C49/48—Moulds
- B29C49/52—Moulds having decorating or printing means
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
- B29K2995/00—Properties of moulding materials, reinforcements, fillers, preformed parts or moulds
- B29K2995/0018—Properties of moulding materials, reinforcements, fillers, preformed parts or moulds having particular optical properties, e.g. fluorescent or phosphorescent
- B29K2995/0024—Matt surface
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
- B29K2995/00—Properties of moulding materials, reinforcements, fillers, preformed parts or moulds
- B29K2995/0037—Other properties
- B29K2995/0072—Roughness, e.g. anti-slip
Definitions
- the invention relates to a method for producing matt surfaces on blow-molded hollow bodies made of plastic, for example on plastic bottles or the like with containers provided with an emptying opening, according to the preamble of claim 1.
- the invention also relates to a hollow body produced according to the method.
- Plastic containers are mainly used in particular for the packaging of fluid substances, for example of beverages, oil, cleaning utensils, personal care products, cosmetics, etc.
- the low weight and the lower costs certainly play a significant role in this substitution.
- the use of recyclable plastic materials and the overall lower overall energy balance in their manufacture also help to promote the acceptance of plastic containers, in particular plastic bottles, by the consumer.
- the introduced low-viscosity plastic is pressed against the walls of the injection mold at pressures of approximately 100 bar to approximately 300 bar.
- the surface roughness of the injection mold is transferred to the surface of the injection molded object. After the object has been removed from the mold, its surface reflects the surface structure of the injection mold.
- the conventional injection molding process is not suitable for the mass production of hollow bodies, such as plastic bottles for drinks or containers for household chemicals, personal care articles or cosmetics.
- a blow molding process in particular a hollow body extrusion blow molding process, is usually used today for the economical mass production of such containers.
- a single or multi-layer extruded preform for example a hose, is introduced into blow molding tools and inflated by means of a blow mandrel by means of excess pressure.
- a preform produced in a separate process is heated and the shape is stretched to the required length in addition to being inflated by the blow mandrel.
- the blow pressure in the stretch blow molding process is generally higher than the blow pressure in the extrusion blow molding process. However, it is still far lower than with injection molding.
- the blow pressure in the extrusion blow molding process is only about 6 bar - about 8 bar.
- the effective pressure with which the preform is pressed against the walls of the blow mold during inflation is even lower.
- the low pressure in connection with the plastics used for the blow molding process, which have a relatively high viscosity, means that roughness of the blow mold walls is only insufficiently transferred to the surface of the hollow body. For this reason, it has not previously been possible to use the blow molding process to produce objects with deliberately matt surfaces that correspond to the desired “frosty finish”.
- the known blow molding process for the production of hollow bodies made of plastic is to be modified to the extent that it is possible to provide blow molded hollow bodies with a desired matt surface within the blow mold during the blow molding process.
- the process should not require any additional process steps. It should be simple and inexpensive to carry out.
- the matt surface should be mechanically stable, especially scratch-resistant.
- a single-layer or multi-layer preform made of a preferably thermoplastic plastic for example a section of a tube or a semi-finished product, is in the wall material of which temperature-resistant, particulate additives are incorporated into a blow mold.
- the preform is then inflated by means of a blow mandrel assigned to the blow mold according to the cavities enclosed by the blow molds, and the surface of the hollow body is provided with a greater surface roughness, at least in some areas.
- materials are used as particulate additives which have a Mohs hardness of at least 5.
- the preform is used in the Inflation is pressed against a blow mold whose blow mold walls have a surface with increased roughness, at least in some areas.
- the escape of the air trapped between the outer wall of the preform and the areas of the blow mold with increased surface roughness is hindered during the inflation process.
- the method according to the invention allows hollow bodies to be partially provided with a partially diffusely reflecting, matt surface during the blow molding process. Subsequent sandblasting, coating or painting can therefore be omitted.
- the procedure differs from the known blow molding process in that when the preform is inflated in the blow mold, the air surrounding the preform is prevented from escaping in the areas of the blow mold with increased surface roughness. While normally the blow molding process ensures that the air can escape from the blow mold as quickly and completely as possible, in the method according to the invention the air is prevented from escaping in those areas in which the matt surface is to be produced.
- temperature-resistant, particulate additives which have a Mohs hardness of at least 5 are incorporated into the wall material of the preform.
- additives with the specified Mohs hardness also have the desired property from a morphological point of view, in conjunction with the increased surface roughness of the blow mold wall, to prevent the air from escaping quickly.
- the enclosed air bubbles are compressed when the preform is inflated and form a rough structure on selective areas of the surface of the container. This partially reflects the incident light diffusely and thereby leads to the desired “frosty-finsh” effect.
- the method according to the invention does not require any additional method steps and can be carried out during the inflation process.
- blow molds have proven to be expedient, the blow mold walls of which have a roughness depth of> 0.5 ⁇ m to approximately 20 ⁇ m in the desired areas.
- the production of the blow mold walls with The desired roughness is achieved, for example, by line polishing, glass beads, sandblasting, eroding or etching.
- the particulate additives in the wall material of the preform have a grain size of approximately 1 ⁇ m to approximately 400 ⁇ m, preferably approximately 4 ⁇ m to approximately Have 12 ⁇ m.
- the preform lies against the blow mold walls, where it solidifies by cooling and thus retains its shape.
- a part of the particulate additives is located on the surface of the preform and at least partially closes the small channels remaining between the preform and the structured wall areas of the blow mold. As a result, the air can no longer escape completely to ventilation slots in the blow mold.
- the remaining, enclosed air is compressed when the preform is further inflated and imaged on the surface.
- the granularity of the structure depicted on the surface of the blow-molded container is significantly greater than the roughness specifically formed in the blow mold on certain wall areas.
- the particulate additives When inflated, the particulate additives are at least partially on the surface of the preform and protrude from the surface thereof.
- the proportion by weight of the additives in the plastic is selected to be about 20 ppm to about 2%, preferably about 0.1% to about 0.8%.
- Materials which are inert to the plastic are advantageously used as particulate additives. For example, particles based on natural or artificial silicon dioxide or similar substances whose refractive index difference is small compared to plastic are used. In this way it is ensured that the additives which are applied over the surface of the preform are divided, with transparent plastics do not impair the transparency of the manufactured container in the other areas.
- the extrusion blow molding process is particularly preferred, in which the preform is produced as a plastic tube only immediately before the actual inflation process. This is then clamped between two mold halves and inflated and shaped using the blow mandrel.
- the extrusion blow molding process has the advantage that containers of various shapes and sizes can be produced with it.
- the containers can have volumes of a few ml up to 5000 liters and more.
- the process is suitable for the production of asymmetrical articles, for the production of hollow bodies with several openings and / or handle sections, as well as for containers with insert parts.
- the preform produced immediately before the inflation is advantageously produced from a plastic to which about 20 ppm to about 2% of the temperature-resistant, particulate additive is added. The addition of the particulate additive does not change the initial situation of the manufacturing process, since the plastic is also presented in granulate form. The actual manufacturing process of the preform then does not differ from the known and proven manufacturing processes.
- the hose can be made in one or more layers.
- the additives are advantageously introduced into the outermost layer so that they are largely present on the surface of the preform when inflated.
- the hollow body made of polyester, for. B. PET, polyvinyl chloride, polyamide, made from a polyolefin, for example polyethylene or polypropylene, or from PLA or a similar plastic or plastic mixture.
- Hollow bodies produced by the method according to the invention for receiving fluid substances can be provided in their entirety or only partially with structured surface areas which have changed reflection properties compared to the rest of the material.
- the hollow body can have areas with different degrees of transparency as well as areas with different matting in order to achieve different surface effects, in particular a “frosty finish” effect, as required.
- the structural roughness is of the order of magnitude of approximately 50 ⁇ m to approximately 200 ⁇ m ,
- FIG. 2 shows a section of a blow mold provided with a roughened surface in section
- FIG. 3 shows the area of the blow mold according to FIG. 2 with the norform in contact
- FIG. 5 shows a detail of the plastic bottle from FIG. 4 on an enlarged scale.
- the blow molding process is used for the mass production of thin-walled hollow bodies, such as bottles, canisters, drums, but also watering cans, tanks for motor vehicles and similar containers made of thermoplastic materials.
- the plastic which is usually in the form of granules, is melted and a preform is produced from it.
- the preform can be in different forms. For example, it can be designed as a hose or have an elongated, cylindrical shape.
- the preform is then immediately after its manufacture or also introduced into the cavity of a blow mold at a later point in time and inflated in accordance with the mold cavity and thereby shaped into its final shape.
- An extrusion blow molding machine provided with the reference number 1 is composed of an extruder 2 with an extrusion head 4 for the production of a preform 5 and a blow molding unit which immediately adjoins and which has a blow mandrel 7 which projects from a blow mandrel bar and which usually consists of two halves in the cavity 10 Blow mold 9 is retractable.
- the preform 5 is produced immediately before being introduced into the blow mold 9.
- a plastic P which is usually in the form of granules, is fed to the extruder 2 via a funnel 3, melted and conveyed to the extrusion head 4 in the molten state.
- the extrusion head 4 there is a tube-like preform 5 which is introduced into the cavity 10 of the blow mold 9 essentially immediately after its production.
- the preform 5 can be extruded or co-extruded in one or more layers as required.
- the blow mandrel 7 is introduced in order to inflate the preform ring 5 to the shape predetermined by the cavity 10 in the blow mold 9.
- the preform 5, which is inflated into its final shape cools down through the contact with the wall of the blow mold 9 and through the blowing medium, for example air, and can be removed as a fully formed container 13.
- the slug pieces on the bottom and on the neck of the container 13 are separated by a punch indicated by the reference numeral 8. Thereafter, the container 13 is usually still checked for leaks.
- the method according to the invention differs from the known extrusion blow molding method in that a certain amount of a particulate additive A is added to the plastic P for producing the preform 5.
- additives A solid, temperature-resistant particles of regular or irregular shape are suitable which are not soluble in plastic P and are advantageously completely inert to the plastic P used.
- particles are based natural or artificial silicon dioxide or similar substances, whose refractive index difference is small compared to the plastic used, used as additives.
- Their grain size is approximately 1 ⁇ m to approximately 400 ⁇ m.
- the particles preferably have an equivalent diameter of approximately 4 ⁇ m to approximately 12 ⁇ m.
- the proportion by weight of the particulate additives A added to the plastic P is about 20 pp to about 2%, preferably about 0.1% to about 0.8%.
- suitable plastics are polyesters, for example PET, polyvinyl chloride, polyamide, polyolefins, for example polyethylene or polypropylene, or PLA or similar plastics or plastic mixtures.
- FIG. 2 shows a sectional illustration of a section of a blow mold 9 used in the method according to the invention.
- the cavity of the blow mold 9 is indicated by reference number 10.
- the blow mold 9 is provided with a structure 12 in those areas of its wall 11 where the manufactured container is supposed to have reflective properties that differ from the other areas, in particular a matt surface.
- the structuring 12 is produced, for example, by line polishing, glass beads, sandblasting, eroding or etching and has a roughness depth> 0.5 ⁇ m to approximately 20 ⁇ m.
- FIG. 3 shows an illustration analogous to FIG. 2 with a preform 5 arranged inside the blow mold 9.
- the same reference numerals therefore also denote the same elements.
- the preform 5 can be, for example, a tube extruded immediately before the blow molding process. However, the preform 5 can also be in the form of an elongated, cylindrical container which was produced in a work step that is completely separate in terms of space and time.
- the preform is taken over by the blow mold and inflated by the retracted blow mandrel.
- the preform 5 has, for example, a two-layer wall 15. For clarification, only the inner wall 17 is hatched in FIG. 3.
- the wall 16 of the preform 5 facing the blow mold wall 11 has the particulate additives A.
- the surface concentration of the particulate additives A corresponds approximately to the proportion by weight of the additive in the plastic and is approximately 20 ppm to approximately 2%, preferably approximately 0.1% to approximately 0.8%.
- the blowing pressure measured at the inlet of the blowing mandrel is about 6 bar to about 8 bar when the preform 5 is inflated.
- the wall 15 of the preform 5 is pressed against the blow mold wall 11 by the inflation.
- the particulate additives protruding from the surface partially close the channels formed by the structuring 12 of the blow mold wall 11. As a result, the air located between the outer wall of the preform 5 and the blow mold wall 11 is prevented from escaping.
- the remaining, enclosed gas bubbles are compressed during further inflation and form an irregular structure on the plastic surface.
- a plastic bottle produced by the method according to the invention is shown schematically and provided with the reference number 13 as a whole.
- its wall has two layers 16 and 17.
- the layer 17 lies in the interior of the bottle 13.
- the additives A are contained in the outer layer 16.
- an irregular structure 18 is formed on the areas of the outer surface 14 of the plastic bottle 13 that correspond to the structured areas of the blow mold.
- the structural roughness is approximately 50 ⁇ m to approximately 200 ⁇ m.
- the structured areas 18 on the surface 14 of the plastic bottle 13 diffusely reflect the light in an exaggerated manner and lead to the desired matt appearance, in particular to the desired “frosty finish” effect.
Landscapes
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Mechanical Engineering (AREA)
- Blow-Moulding Or Thermoforming Of Plastics Or The Like (AREA)
- Moulds For Moulding Plastics Or The Like (AREA)
Abstract
Description
Claims
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AU2002231680A AU2002231680A1 (en) | 2000-12-20 | 2001-12-08 | Method of producing matted surfaces on blow-molded hollow bodies |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CH24822000 | 2000-12-20 | ||
CH2482/00 | 2000-12-20 |
Publications (2)
Publication Number | Publication Date |
---|---|
WO2002049830A2 true WO2002049830A2 (de) | 2002-06-27 |
WO2002049830A3 WO2002049830A3 (de) | 2002-09-26 |
Family
ID=4569548
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/EP2001/014433 WO2002049830A2 (de) | 2000-12-20 | 2001-12-08 | Verfahren zur herstellung von blasgeformten hohlkörpern mit mattierten oberflächen |
Country Status (2)
Country | Link |
---|---|
AU (1) | AU2002231680A1 (de) |
WO (1) | WO2002049830A2 (de) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102005010273A1 (de) * | 2005-03-03 | 2006-09-07 | Siemens Ag | Vermeidung von Quietschgeräuschen an Kunststoffteilen |
CH699237A1 (de) * | 2008-07-24 | 2010-01-29 | Alpla Werke | Kunststoffformulierung und Verfahren zur Herstellung von Kunststoffflaschen in einem Zweistufen-Streckblasprozess. |
Family Cites Families (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
NL73078C (de) * | 1949-08-02 | |||
DE2520229A1 (de) * | 1975-05-07 | 1976-11-18 | Solvay Werke Gmbh | Verfahren zur herstellung von hohlkoerpern, behaeltern u.dgl. |
AU538516B2 (en) * | 1979-01-26 | 1984-08-16 | Yoshino Kogyosho Co., Ltd. | Crystallised surface of blow moulding |
JPS5770154A (en) * | 1980-10-22 | 1982-04-30 | Teijin Ltd | Ground glass-like polyester container |
JPH02160862A (ja) * | 1988-12-14 | 1990-06-20 | Diafoil Co Ltd | セラミックス粒子含有ポリエステル中空成形体 |
JP2982274B2 (ja) * | 1990-07-05 | 1999-11-22 | 東洋製罐株式会社 | フロスト状多層プラスチック容器及びその製法 |
JP2643745B2 (ja) * | 1992-12-22 | 1997-08-20 | 東洋製罐株式会社 | フロスト状プラスチック容器及びその製法 |
JPH07266343A (ja) * | 1994-03-30 | 1995-10-17 | Asahi Chem Ind Co Ltd | 艶消し状表面を有する合成樹脂成形品 |
JPH08309835A (ja) * | 1995-05-23 | 1996-11-26 | Toppan Printing Co Ltd | 多層ブローボトル |
-
2001
- 2001-12-08 AU AU2002231680A patent/AU2002231680A1/en not_active Abandoned
- 2001-12-08 WO PCT/EP2001/014433 patent/WO2002049830A2/de not_active Application Discontinuation
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102005010273A1 (de) * | 2005-03-03 | 2006-09-07 | Siemens Ag | Vermeidung von Quietschgeräuschen an Kunststoffteilen |
DE102005010273B4 (de) * | 2005-03-03 | 2008-08-07 | Siemens Ag | Baugruppe aus miteinander verbundenen Kunststoffteilen zur Vermeidung von Quietschgeräuschen |
CH699237A1 (de) * | 2008-07-24 | 2010-01-29 | Alpla Werke | Kunststoffformulierung und Verfahren zur Herstellung von Kunststoffflaschen in einem Zweistufen-Streckblasprozess. |
Also Published As
Publication number | Publication date |
---|---|
WO2002049830A3 (de) | 2002-09-26 |
AU2002231680A1 (en) | 2002-07-01 |
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