DE10205477A1 - Ring-like packaging profile containing polyethylene foam, a plate slot and an antislip layer useful for packaging glass plates and other similar items - Google Patents

Abstract

Preparation of a packing especially a ring-shaped packing for glass plates and similar items, especially in polyethylene and foam with a slot for receiving the plates, with an antislip layer in the slot of strength less than that of the packing is new.

Description

The invention relates to an annular packaging profile, in particular from Plastic foam and in particular made of polyethylene and in particular for glass panes or similar packaging.

Packing foam has the task of protecting the packaged goods against damage. A shock load should be dampened. Sensitive packaging must be be treated with care. Then there are high acceleration and braking forces undesirable. The sensitive packaging goods include e.g. B. glass panes.

For the packaging of glass panes, US Pat. No. 5,101,976 inter alia suggests multilayered material, the contact surfaces of which are cross-linked with the panes Polyethylene foam is formed. The polyethylene foam is very compliant and prevents damage to the glass.

Another proposal according to the German utility model 90 01 475 has Task: the individual packaging of panes or similar flat products from fragile materials such as glass of any contours, with the help of a To allow foam profile, so that the individually wrapped disc shatterproof is packed. This is said to be achieved by predominantly closed-cell polyolefin-based foam with a bulk density of at least 30 kg per cubic meter up to approx. 70 kg per cubic meter by machining in A groove is cut in the longitudinal direction of the profile. It is preferred highly elastic foams with high compressibility, resilience and Impact elasticity used, which has a high tensile strength of at least 0.2 N per Have square millimeters and an elongation at break of at least 80% and at Deformation build up a high compressive stress. A framing of glass panes should the known profile already achieve such a high cushioning effect that it is already relatively low Protect the glass pane sufficiently.

For the production of the known profiles are preferably foam bodies, such as z. B. block foam is provided. The foam body can Foam sheets of the same or different density exist.

According to another proposal, the foam profiles are to be extruded.

According to another proposal, extruded foam should not be used because extruded foam have limited strength and impact resilience. Also be expensive Tools required to achieve the desired different profile dimensions serve.

Still other suggestions according to EP 621207 B1 see both in the plastic foam in the extruded plastic foam as well as in the block foam fundamental defects in all Strength values (penetration, shearing, tearing, removal). See these suggestions a coating that has greater strength values than the plastic foam. The packaging profiles have a U-shaped or similar cross-section and are preferably placed as a ring on the edge of the glass pane. The profile is at least partially bent apart to move it over the edge of the glass pane. The process reminds of mounting a tire on the rim of a motor vehicle wheel.

The known technology has proven itself. Nevertheless, the invention with the known Technology examined. The invention has come to the conclusion that it is for contemporary foams less on the strength values than on a correct positioning of the packaged goods arrives. The invention has namely recognized that when the ring-shaped packaging the risk of the packaging slipping relative to the Glass pane exists.

According to the invention this is done using conventional or new profiles Plastic foam achieved in that the profiles on the contact surface with the Packaged goods are provided with a hot melt adhesive coating. This glue will melted by appropriate heating and can be applied very advantageously. at In the packaging, the hot melt adhesive prevents the glass panes from slipping on the Plastic and vice versa. The hot melt adhesive is namely the one that occurs Packaging temperature is sufficiently compliant to enclose the glass sheet, and then has sufficient resistance to undesired slipping. at Room temperature of around 20 degrees Celsius, the hot melt adhesive is even a little sticky, so that it adheres very favorably to the disc. At the same time, the hot melt adhesive has the advantage that it can be removed from the glass pane without residue.

Commercial hot-melt adhesives are described in various publications, e.g. B. in US-PS 412535, US-PS 6051652, US-PS 5414039, US-PS 5392592, US-PS 6107430, US-PS 5530054, U.S. Patent 5548014, U.S. Patent 5731384, U.S. Patent 6044625;

The hot melt adhesive is liquefied for application.

Tools such as spray guns, pumps and small extruders are suitable for application.

One of the tools is connected to a reservoir, in which the melt is Hot melt adhesive is held and pull the adhesive out of the container as needed. The other tools only liquefy the hot melt adhesive immediately before discharge. In As a rule, the tools with the storage container are more powerful.

A nozzle is preferably provided on the tool discharge.

The nozzle is adapted to the desired adhesive discharge.

An adhesive application in the form of a thin adhesive film may be desired. Then owns the nozzle has a narrow slit.

A sausage-shaped adhesive film with a small cross-section may be desired. Then owns the nozzle preferably has a round cross section with a comparatively large cross section, so that the adhesive can easily flow through the nozzle.

Droplet-shaped adhesive application may be desired. Then the nozzle has preferably a round cross section with a comparatively small cross section, so that the adhesive jams in front of the nozzle and at high speed and with a large drop in pressure emerges from the nozzle and spreads, optionally even atomized.

The thin adhesive film is usually a smooth film.

With the drop by drop application, a smooth film can also be produced.

A smooth adhesive layer is preferably not produced, but a restless adhesive layer. A droplet-shaped order is e.g. B. by distance between the individual droplets reached. The distance arises when the tool for glue application with higher Speed is moved and / or the packaging profile at higher speed is moved. The tool is preferably moved.

However, the packaging profile can also be moved or both. One is crucial Relative movement between tool and packaging profile.

In the case of large series of packaging profiles, a tool can also be advantageous which covers entire application area at the same time, so that a single short discharge liquid Glue is sufficient for the complete adhesive application.

A suitable design and distribution of the adhesive droplets can be done with a few attempts be tested.

When creating the restless adhesive layer with a slot die or round die comparatively large cross-section is optionally with profiled nozzle edges and / or a special nozzle movement and / or workpiece movement.

For example, teeth that protrude into the nozzle opening or groove-shaped recesses in the Nozzle edge that groove-shaped depressions or web-shaped elevations in the Adhesive layer arise. The shape of the nozzle is formed in the applied adhesive layer from. The result of this is that the nozzle is reproduced in the shape of the desired adhesive layer can.

The different movement results from a change in the Movement speed and / or from additional movements of the tool.

With periodic acceleration and deceleration of the movement, this is formed in the Apply the adhesive. The order is reduced with a constant flow rate in the Nozzle at higher speed in the amount per unit area. In contrast, the Order quantity at low speed per unit area.

In addition to or instead of the periodic change in speed, a nozzle can be used Swivel movement transverse to the feed direction of the general tool movement be performed. However, there is only a small area available for this movement Available. Controlling this movement is easier if the nozzle is close to the Order area of the profile is arranged. Then there is a larger swivel angle, while there is a smaller swivel angle at a greater distance. The bigger the Is the swivel angle, the easier the control with conventional means.

With the combined movement in the feed direction and transversely to it, one is optionally created snake-shaped adhesive application. Conventional means are e.g. B. servomotors or Stepper motors, which with certain tolerances move one step back and forth cause pivotal movement.

Optionally, in addition to or instead of the above change options for Glue application also changed the flow rate in the nozzle. The course of the Flow volume can be designed as desired. The associated curve can be straight and / or angular and / or rounded and / or continuous or at intervals be interrupted. This is reflected in the adhesive application on the profile. The break is synonymous with the formation of sections of the adhesive application and distances between the sections. Short sections appear as drops or as short ones Order areas or even as points, long sections as lines or as long Application surfaces.

Through the control described above, the adhesive can also be applied in special and even complicated patterns are compulsorily repeated evenly while the above spraying of the adhesive described is less imperatively uniform.

When using electrical, programmable control is also necessary to obtain the described control functions only a small economic effort required. A valve is preferably used to control the flow rate of the adhesive in the nozzle provided in the supply line to the nozzle. Standard valves are suitable. There are valves with two or more closed positions. There are also valves with any closed positions due to similar electrical, programmable control as for the drive. at Using such controls, the course of the changes is equally arbitrary can be designed as in the movement described above.

Optionally, instead of the change options described above for glue application or additionally the use of profiles provided, the contact surface with the Glass panes are provided with grooves across the feared sliding movement. Instead of Grooves can also have knobs or other non-slip, uneven surface shapes be provided.

The grooves can run in the longitudinal direction of the profile and are light by extrusion represented.

According to the invention, an advantageous profile when extruding a thermoplastic Plastic foam (preferably polyethylene) with the contours of the desired profile reached.

The usual U-shaped profile can - starting from a full surface Profile cross-section - be created by means of a groove in which the glass pane is accommodated becomes. The groove can have any shape, e.g. B. in cross-section a precisely rectangular shape or a round shape or a combination of rectangular and round shape or one wedge shape with an extension towards the groove base. Furthermore, the groove in cross section partially have a shape as described above, e.g. B. in cross section the shape of a Quadrant.

According to the invention, the groove is preferably created during the extrusion of the profile. An extruder is used for the extrusion, which is the initially granular plastic plasticized and mixed with aggregates and optionally fillers. When manufacturing plastic foam is either given a blowing agent with the plastic granulate and / or after plasticizing, a blowing agent is added to the extruder and in the melt finely divided.

The extruder presses the melt out through an extrusion nozzle.

The extrusion die has an outer cross section of the desired cross section simulated passage channel, in whose passage opening a web protrudes. The jetty has the contour of the desired groove.

In a further embodiment of the invention, an open-cell plastic foam for the profile used.

The terms "open cell" and "closed cell" cannot be seen absolutely. On open-cell foam regularly also has closed cells; vice versa closed-cell foam regularly also open cells. So much for an open cell Foam is started, the foam has a large part or largely open Cells. With closed-cell foam, the foam has a large part or largely closed cells.

The assembly of closed-cell foam strands is more or less tedious because that Deforming such foams requires increasing force. The difficulties will be without further recognizable if, for example, a foam strand with a diameter of 15 mm should be compressed to a diameter of 10 mm and beyond.

An open-cell foam behaves differently. With an open-cell foam, this can happen Gas in the cells not only diffuse out, but also through openings in the Flowing out of cell walls. Such open-cell foams have so far been made of PUR or Polyvinyl chloride (PVC) or made of synthetic rubber. However, must be taken into account that PUR is not very weather-resistant. The weather resistance should be by a bitumen impregnation or by other impregnation of the foam can be achieved. However, bitumen is not stable. The bitumen evaporates in the course of Most of the time. The impregnation is through moisture and heat discharged.

PVC foams are less from the point of view of disposal and for other reasons he wishes.

• a) an sich bekannte Verwendung eines thermoplastischen Kunststoffes, vorzugsweise von PE, und
• b) Extrusion des Kunststoffes zu einem offenzelligen Schaum unter Erzeugung einer Außenhaut an dem Schaumstrang
• c) wobei die Außenhaut wasserundurchlässig, reißfest und elastisch ist
• d) wobei die Offenzelligkeit so groß gewählt ist, daß der Schaum eine verzögerte Rückstellung besitzt.

Rubber profiles regularly have a high density, which is not always desirable. According to the invention, an easily manageable, weather-resistant foam strand is achieved by

• a) known use of a thermoplastic, preferably PE, and
• b) extrusion of the plastic into an open-cell foam to produce an outer skin on the foam strand
• c) the outer skin being impermeable to water, tear-resistant and elastic
• d) the open cell is chosen so large that the foam has a delayed reset.

The open cell structure arises during extrusion, not through subsequent mechanical Destruction of the cell structure due to excessive compression.

• a) einer Länge von 10 cm, einer Dicke von 1 cm und einer Breite von 3 cm, der an der Mitte im flach liegenden Zustand bei einer Raumtemperatur von 20 Grad Celsius auf einer Länge von 3 cm über seiner Breite mit einem flachen Stempel in einer Zeit von 1 sec mit möglichst gleichbleibender Geschwindigkeit um 80% auf 2 mm Dicke eingedrückt und dort eine weitere Sekunde gehalten und anschließend schlagartig entlastet wird.
• b) nach der Entlastung soll der Prüfkörper mindestens 3 sec, vorzugsweise mindestens 5 sec und noch weiter bevorzugt mindestens 10 sec benötigen, um im Wege der Rückstellung 100% seiner ursprünglichen Form (10 mm Dicke) wieder zu erreichen.

The standard for the open cell / delay is a test specimen made from the respective foam

• a) a length of 10 cm, a thickness of 1 cm and a width of 3 cm, lying flat in the middle at a room temperature of 20 degrees Celsius over a length of 3 cm above its width with a flat stamp in one Time of 1 sec pressed in at a constant speed by 80% to a thickness of 2 mm and held there for a further second and then suddenly relieved.
• b) after the relief, the test specimen should need at least 3 seconds, preferably at least 5 seconds and even more preferably at least 10 seconds, in order to return to 100% of its original shape (10 mm thickness).

• a) aus dem zur Prüfung anstehenden Material die oben beschriebenen Prüfkörper herauszuschneiden, wenn das zur Prüfung anstehende Material größere Abmessungen als die oben beschriebenen Prüfkörper hat
• b) oder aus einem Prüfkörper bekannten Materials einen Vergleich-Prüfkörper mit den relevanten Abmessung des zur Prüfung anstehenden Materials herauszuschneiden, wenn die Abmessungen des zur Prüfung anstehenden Materials kleiner als der oben beschriebene Prüfkörper ist.
  Die Werte des gewonnen Vergleichsprüfkörpers lassen sich dann mit dem zur Prüfung anstehenden Material vergleichen. Wahlweise können die daraus gewonnenen Ergebnisse anschließend auf einen Vergleich mit dem unter g) beschriebenen Prüfkörper hoch gerechnet werden.

Instead of the test specimen described, any other test specimen can also be used or deviating samples can be examined. The specified delay must then be calculated down or up to the dimensions of the other test specimens. For other test specimens, it is recommended to either

• a) cut out the test specimens described above from the material to be tested if the material to be tested has larger dimensions than the test specimens described above
• b) or cut out a reference test specimen with the relevant dimensions of the material to be tested from a test specimen of known material if the dimensions of the material to be tested are smaller than the test specimen described above.
  The values of the comparison test piece obtained can then be compared with the material to be tested. The results obtained can then optionally be extrapolated to a comparison with the test specimen described under g).

The skin resulting from the incorporation of the groove on or in the profile according to the invention can be checked.

The examination of the skin is carried out optionally on test pieces, which are from the invention Foam to be cut out. Preferably on a 3 mm thick top layer (skin and underlying cells), which is separated from the foam.

The profile to be machined is optionally as in the known utility model from one Bloch foam obtained. It can also be produced by extrusion without the Groove is generated.

Different types of extruders are available. The most common are Single screw extruder and the twin screw extruder / twin screw extruder. With Single-screw and twin-screw / twin-screw is the number of screws. The screws feed the feed material into the extruder, build up pressure, cause warming, so that the plastic changes into a melt.

It is common to cause the melt to form by heating it over the extruder barrel support. After the melt has formed, the aggregates in the melt become fine distributed, dispersed. In this phase, blowing agents are used in modern extruders liquid / gaseous form injected into the extruder. Then finds another Homogenization and cooling of the melt to the extrusion temperature instead. For the Production of foam is important that there is sufficient pressure in front of the extrusion die is built up, which prevents foaming of the melt in the extruder. If the If foam escapes into the surrounding atmosphere, the one surrounding the melt strand falls Strong pressure and the enclosed, finely divided and gaseous blowing agent expands suddenly under the pressure prevailing in the melt. Since the blowing agent in the If the melt is finely distributed, a large number of small cells are created.

The open cell structure arises when foaming, if the compliance of the cell walls is not is enough to adapt the cell walls to the cell growth. Then they tear Cell walls.

The open cell is determined by the choice of the plastic, the blowing agent and the Process parameters determined during extrusion. According to the invention Obviousness of the resulting foam is evident in that air and other gases in Longitudinal direction through the resulting foam strand without diffusion processes can be pushed through. Evidence of open cells can also be provided with water or other liquids. As with gas, water can be used with a Apply the test pressure to the foam and then measure the gas passage. For the measurement it is also possible to compress and in the plastic foam To lay fluidity. After squeezing, the foam sucks during the subsequent one Provision like a sponge liquid on. For the evidence of open cell or It is an advantage to always use the same evidence of the same open cell same test specimen always the same compression of z. B. 50% of Select output volume and measure the amount of liquid sucked up. Optionally, the open cell can also be checked by means of a DIN test Closed cells occur. If the size of the closed cell is available this also determines the degree of open cell.

The foam according to the invention preferably has a density of 20 to 80 kg per Cubic meters, more preferably from 30 to 40 kg per cubic meter

The foam according to the invention can absorb shock loads particularly well. ever The more sensitive the goods to be packaged, the more carefully the shock load must be be counteracted. Traditionally, closed-cell polystyrene foam is used closed cell PE foam used for shock absorption. The conventional one Foam is more resilient and has a hard stroke.

The foam according to the invention has a viscoelastic braking effect. The stop is softer. The braking distance / damping distance is longer.

Foam pieces of material according to the invention are optionally made with foam pieces conventional closed cell material combined. The foam pieces have the task of quicker resetting from conventional material.

The use is as plastic for the production of the foam strand according to the invention a PE produced catalytically with the help of metallocene (hereinafter referred to as metallocene PE) is particularly advantageous. This PE forms at an extrusion temperature of 110 up to 116 degrees Celsius, preferably from 111 to 115 degrees Celsius, with a plastic foam all desired properties.

• a) Isobutan oder Propan als Treibmittel
• b) mit einem Treibmittelanteil von 6 bis 14 Gew.-%, bezogen auf die Menge des Materialeinsatzes im Extruder
• c) einem Schaum-Raumgewicht von 20 bis 80 kg pro Kubikmeter, gegebenenfalls bis 120 kg pro Kubikmeter, wobei die Treibmittelmenge für ein Schaum- Raumgewicht von 25 bis 35 kg pro Kubikmeter 12 Gew.-% plus/minus 2 Gew.-%, bezogen auf die Menge des Materialeinsatzes beträgt der Extrusionsdruck gegenüber einer herkömmlichen PE-Schaumextrusion (bei etwa 30 bar) nach dem erfindungsgemäßen Verfahren wesentlich höher ist, nämlich bezogen auf einen Profil-Querschnitt von 5 Quadratzentimeter 48 bis 50 bar. Nach der Erfindung kann der Druck unter Reduzierung der Schmelzetemperatur erhöht werden. Der Schmelze steht dann ein wesentlich höherer Strömungswiderstand in der Düse entgegen.

The other extrusion conditions are:

• a) Isobutane or propane as a blowing agent
• b) with a blowing agent content of 6 to 14 wt .-%, based on the amount of material used in the extruder
• c) a foam density of 20 to 80 kg per cubic meter, optionally up to 120 kg per cubic meter, the amount of blowing agent for a foam density of 25 to 35 kg per cubic meter being 12% by weight plus / minus 2% by weight, based on the amount of material used, the extrusion pressure compared to a conventional PE foam extrusion (at about 30 bar) according to the method of the invention is significantly higher, namely based on a profile cross section of 5 square centimeters 48 to 50 bar. According to the invention, the pressure can be increased while reducing the melt temperature. The melt is then opposed to a significantly higher flow resistance in the nozzle.

The invention has also experimentally PE for producing an open-cell foam used, which has been produced using metallocene catalysts. The invention has found that the DSC curve according to two Shows temperature peaks, one at 111 degrees Celsius and one at 122 degrees Celsius. To The temperature peak at 111 degrees Celsius includes a wide hump that is already at 100 degrees Celsius is of considerable size. In comparison, a PE standard has only one Temperature peak, which is 113 degrees Celsius.

At an extrusion temperature of the test material of 116 degrees Celsius is a largely open-cell foam

The invention assumes that at the extrusion temperature of 116 degrees Celsius low melting material is extreme and therefore not worth mentioning Melt tension can unfold. While another high-melting material content is still very tough, d. H. has a high melt tension.

When the foam leaves the extrusion die / nozzle and enters the ambient air and the propellant takes action due to the drop in pressure, cells form. The however, a highly liquid enamel component is not able to limit cell growth. It must inevitably lead to the destruction of the liquid melt at the points Cell walls are coming. Permeable openings are formed.

With regard to the proportion of material belonging to the high temperature peak, the invention goes assume that this melt content is close to the crystallization point and an extremely high Shows melt tension. The high melt tension causes, moreover, stable Cell walls with sufficient restoring force are created. Nevertheless, holes form in the cell walls Conventional PE foams look different with open-cell production. The cells burst under excessive load. However, the cell walls have one uniform appearance.

The air permeability of the metallocene PE foam is compared to conventional PE foam much larger. The open-cell metallocene PE foam is about twice that permeable like the open-cell foam made of conventional PE.

The foam according to the invention is used with densities of 20 to 120 kg per cubic meter, preferably produced from 25 to 35 kg per cubic meter. The open cell results in the production according to the invention without difficulty even with high densities.

Despite the high flexibility, the foams according to the invention have a Resilience adapted to the respective application.

In addition, the resilience of the foam profile by a partial or complete encasement of the profile can be significantly affected.

The greater the resilience, the greater the resilience.

So that the air trapped in the open cells can escape, it will Sealing profile with open ends installed. Where no open ends are possible optionally provide the sealing profile with openings at a suitable point. This happens preferably on the inside, which are not sealing surfaces at the same time. The opening is created by mechanically removing the outer skin. Perforations or are advantageous elongated slit-shaped openings in the skin. The openings can be regular or have irregular distances from each other, but also over the entire profile length extend. In the case of long slots, their width can be small.

The openings can be made with nails, knives or milling cutters.

The profiles according to the invention can have any cross-sectional shape

The profiles are preferably in a width of 10 to 200 mm and a thickness of 10 manufactured up to 30 mm.

Several exemplary embodiments of the invention are shown in the drawing:

In Fig. 1, the glass sheet is shown in dash-dotted lines and designated 1. The edge of the pane is enclosed by a U-shaped extruded PE foam profile 2 . The foam profile 2 forms a profile ring which completely surrounds the glass pane 1 . The glass pane 1 rests in the foam profile 2 on a layer 3 of hot melt adhesive. Various procedures are possible for assembling the foam profile 2 . In a more craft-oriented procedure, the pane 1 is first placed with a corner in the profile ring or the profile ring is first placed on a pane corner. The profile ring is then forced onto the disc edge by hand in a circumferential direction of the ring or in the opposite circumferential direction. This is done with more or less large lateral unfolding or angling of the profile leg that stands in the way of assembly. With this assembly, layer 3 ensures sufficient adhesion between the glass and the profile ring. This prevents slipping.

The handling described can also be automated.

Another assembly provides that the profile ring is held in a device and at the same time a profile leg on the entire ring length or on the entire ring circumference is unfolded or angled. After that, the glass pane can be immediately and completely be used. After loosening the angled or unfolded profile leg and Detach from the device, the profile ring is mounted on all sides. The necessary Device is simple. The assembly takes place in a very short time.

After assembly, layer 3 prevents slipping.

In Figs. 2 to 5 show different skid-resistant layers are shown.

According to FIG. 2, the profile ring is provided with knobs 9 on the part 8 corresponding to the layer 10 . With a uniform coating 10 , the knobs 9 also form in the layer 10 .

According to Fig. 3, the part 5 is flat and the anti-slip layer 6 provided with knobs.

Fig. 4 shows another embodiment of a profile ring 13 with studs 14. The knobs 14 have a selected distance from one another.

Fig. 5 shows an embodiment of a profile ring with a profile extending in the longitudinal direction of grooves 17. Elevations 18 are located between the grooves 17 . The grooves and elevations are also coated.

Fig. 6 shows an embodiment of a profile ring 20 having a serpentine extending line 21. coating. However, the coating line has the same width everywhere.

Fig. 11 shows an embodiment of a profile ring 22 having a coating line 23 comprising periodically repeating larger widths 24th

Fig. 7 shows an embodiment with a profile ring 26. The ring 26 differs from the ring according to FIG. 1 by a groove 27 which opens into a wider recess 28 . At the foot of the depression 28 there is a non-slip layer 29 .

The embodiment of FIG. 9 differs from the embodiment of FIG. 7 in that the profile ring is a slotted plastic hose / tube 31 . The slot is designated 33; the inner layer is designated 32.

Fig. 8 shows a ring profile 40 for a glass disc 42. The ring profile 40 has a circular cross section, which is missing a quarter circle, so that the ring profile can be placed on a corner of the packaged goods.

The contact surface of the profile ring 40 with the packaging material 41 is formed by a non-slip layer 41 .

All non-slip layers are formed by hot-melt glue, which in the Embodiments are sprayed after appropriate liquefaction.

Claims (26)

1. Production of a package, in particular annular profiles and for glass panes or the like and in particular made of polyethylene and in particular of foam, and with a groove for receiving the packaging material, characterized in that a non-slip layer is provided in the groove, the strength of which is less than the strength the packaging is. 2. Production according to claim 1, characterized in that the non-slip layer through Hot melt adhesive is formed. 3. Production according to claim 2, characterized in that the hot-melt adhesive is applied with a nozzle, wherein a) An adhesive strand emerges b) the adhesive is sprayed or sprayed out 4. Production according to claim 3, characterized in that the adhesive is continuous or intermittent exits. 5. Production according to claim 4, characterized in that the adhesive flow is uniform is applied thickly and / or evenly or periodically evenly changed in width or unevenly changed in width and / or even changed in thickness and / or unevenly changed in thickness is applied. 6. Production according to one of claims 3 to 5, characterized by a additional nozzle movement transverse to the direction of advance of the nozzle or the workpiece. 7. Production according to one of claims 1 to 6, characterized by the use of programmable actuators for the feed movement and / or the nozzle movement and / or a control valve for the adhesive flow. 8. Production according to one of claims 2 to 4, characterized by points and / or Grooves on the non-slip groove and / or serpentine course of the adhesive application and / or an adhesive application of constant width or non-uniform width. 9. Production according to one of claims 1 to 8, characterized in that the Contact surface for the non-slip layer with elevations and / or depressions, in particular in the form of dots and / or grooves. 10. Production according to one of claims 1 to 9, characterized by extruded profiles with molded groove or extruded and slotted tubular or tubular Profiles. 11. Production according to one of claims 1 to 10, characterized by the use an open-cell plastic foam and / or by using a partial preformed profile. 12. Production according to claim 11, characterized by the a) the extrusion of an open-cell foam made of thermoplastic, in particular PE, with an outer skin on the extrusion strand b) the outer skin being waterproof, elastic / stretchable and tear-resistant, c) wherein the open cell during the extrusion is set such that a test specimen made of the foam at 80% compression, briefly holding the compression and sudden relief has at least a reset time of 3 seconds, preferably 5 seconds, more preferably 10 seconds, for which Reaching 100% of the original shape,
the test specimen having a thickness of 1 cm, a length of 10 cm and a width of 3 cm and being compressed in the flat state in the middle over a length of 3 cm over its entire width,
the holding time is 1 sec,
with an ambient temperature of 20 degrees Celsius 13. Production according to claim 12, characterized by the use of PE, which in Softening curve with increasing temperature at least two peaks having at least 5, preferably at least 9, and even more preferred are at least 13 degrees Celsius apart, especially with at least one hump-like course at one tip and one for open-cell production usable course of more than 5, preferably of more than 9 and even further preferably of more than 13 degrees Celsius. 14. Production according to claim 12 or 13, characterized by the use of a PE from a catalytic PE production with a metallocene as catalyst. 15. Production according to one of claims 12 to 14, characterized by the use a mixture of PE and other polymers. 16. Production according to claim 15, characterized in that the proportion of PE in Mixture with other polymers at least 50 wt .-%, based on the total amount is. 17. Production according to one of claims 12 to 16, characterized in that the Plastic foam is extruded and the extrusion temperature below the higher Temperature peak. 18. Production according to claims 1 to 17, characterized in that the extrusion temperature is 111 to 120 , preferably 114 to 118 degrees Celsius. 19. Production according to one of claims 1 to 18, characterized by the use of isobutane or propane as a blowing agent in the plastic melt. 20. Production according to one of claims 1 to 19, characterized in that the Amount of blowing agent for foam density from 20 to 100 kg per cubic meter 6 to 14 wt .-%, based on the amount of material used in the extruder. 21. Production according to claim 20, characterized in that the amount of blowing agent for a foam with a density of 25 to 35 kg per cubic meter 12% by weight, plus / minus 2 wt .-%, based on the amount of material used in the extruder 22. Production according to one of claims 12 to 21, characterized by a Extrusion pressure at the extrusion die for a strand cross section of 5 Square centimeters is 46 to 52 bar, preferably 48 to 50 bar. 23. Production according to one of claims 1 to 22, characterized by the production of profiles with partial or full skin and / or with open ends and / or openings in the outer skin. 24. Production according to claim 23, characterized by perforations or slit-shaped Openings in the outer skin. 25. Production according to one of claims 1 to 24, characterized in that the profile partly from the open-cell plastic foam and partly from closed-cell There is foam that causes the packaged goods to return quickly. 26. Production according to one of claims 1 to 25, characterized by the extrusion of Profiles with a width of 10 to 200 mm and a thickness of 10 to 30 mm