CA1236667A - Process for producing pourable spherical-segment- shaped packing material particles made of plastic - Google Patents
Process for producing pourable spherical-segment- shaped packing material particles made of plasticInfo
- Publication number
- CA1236667A CA1236667A CA000497629A CA497629A CA1236667A CA 1236667 A CA1236667 A CA 1236667A CA 000497629 A CA000497629 A CA 000497629A CA 497629 A CA497629 A CA 497629A CA 1236667 A CA1236667 A CA 1236667A
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- plastic
- plastic material
- particles
- opening
- extrude
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Abstract
In the case of a process for producing pourable spherical-segment-shaped packing material particles made of plastic which have an external convex and an internal concave surface, the plastic material is mixed with additives, such as bubble forming agents, coloring pigments and similar agents. The plastic material is fed, by means of a feeding funnel into an extruder through an opening in a bush surrounding the extrusion screw The plastic material plasticizes over the course of the extruder and, because of the difference in speed existing over the cross section of the mass, comes out of an opening in the die with a bent surface. The plastic material is cut off directly at the opening of the die and before any considerable expansion has taken place. Before the processing of the plastic granules in the extruder a bubble-forming agent is applied to their surface in a drum.
Description
~36~6~7 This invention relates to a process for producing parboil spherical segment-shaped packing material particles made of a plastic material which have an external convex and an internal concave surface, where the plastic material is mixed with additives such as bubble-forming agents, coloring pigments or similar substances, and by means of a feeding funnel, is fed into an ex~ruder through an opening in a bush surrounding the extrusion screw, where the plastic material is plasticized in the course of the extrude and, because of the difference in speed existing over the cross section of the mass, comes out of an opening in the die with a bent surface, and the extruded plastic material is cut off directly at the opening of the die and before any considerable expansion has taken place.
A process of this type is known from U.S.
Patent No. 3,961,000. In the case of this process, the e~pandible polystyrene (ENS) is mixed with add-lives. The additives consist of bubble-forming-agents-such as bicarbonate of ammonia and sodium bicarbonate or similar substances and coloring pigments Via a supply funnel, the mixture is fed into an extrusion device. An extrusion screw transports the mixture through the extrude, where because of the special design of the extrusion screw, i.e. an inquiry-sing core diameter as well as a suitable temperature .~, ..
~36~6~
program, the plastic material is plasticized in the course of the extrude. Immediately after the plastic material comes out of an opening in the die, it is cut off by means of a cutting device, in which case it is made possible for the cut-off particles to expand in a first expansion process into the special shape with a convex outside and a concave inside surface. The packing material particles are processed to their final condition in several subsequent expanding processes.
Polystyrene is a polymerization product of the Bunsen derivative styrenes and according to the conditions of representation, has polymers of varying chain lengths. The chain length is significantly determined by how many styrenes units were "chained to one another" during the polymerization.
polymerization j CH=cH2 2 OH -monomeric styrenes polystyrene The chain length essentially determines the physical characteristics of the plastic material. In order for the plastic material to be processed in an extrude, it must by "thermoplastic". This means that , . . ... .
. .
~L~3~6~
the plastic material which is firm at a certain temperature (usually at room temperature) becomes plastic (soft, moldable) when the temperature is in-creased and can then be processed to a certain shape and after cooling resumes its firm condition.
For the processing in the extrude, two different basic types of polystyrene are available:
a the so-called standard polystyrene ) a polystyrene containing an expanding agent.
The standard polystyrene is a pure polymer, ire., a pure polystyrene without additives. In the case of the polystyrene containing an expanding agent, an expanding agent is included in the polymer matrix which boils at an increased temperature and foams the polymer. Such expanding agents are prefer rawly low-boiling hydrocarbons, fluorohydro-carbons or water.
Standard polystyrene types as well as polyp styrenes types containing expanding agents are suitable for processing into foamed materials on the extrude.
When standard polystyrene is used, it is necessary to add an expanding agent to the extrude during process sing In that case, one speaks of a so-called direct gassing.
The expanding agent causes the plasticized material to foam after leaving the extrude.
, - 3 _ `' ' ' `
The expanding agent, in the extrude, is released under pressure in gaseous fox in the pies-ticized plastic mass. The plastic mass is supers-turated with gas, i.e., because of the conditions (pressure, temperature existing in the extrude, more gas is released than under normal conditions.
After leaving the extrude, the expanding agent tries to burble down and to expand to normal pressure. The stick plastic mass surrounding the expanding agent prevents the propellant gas from escaping into the atmosphere and therefore results in the foamed structure.
By cooling the plastic material in the indicated shapes, the typical structure of the blocks of foamed material is obtained.
In the case of large-volume blocks of foamed material, such as insulating boards, the size of the foam bubbles is relatively large, and the diameter of these bubbles fluctuates over a considerable range.
In the case of the present process, however, small packing material particles are produced, the diameter of which is about up to three centimeters.
In the case of these small packing particles, the size of the bubbles must naturally be much smaller than in the above-described case in order to ensure the stability of the packing particle material. Only a few large bubbles in these small packing particles Jo ~31~i6~
decrease stability and even under little stress result in a breaking of the particles. Larger bumbles, especially in the edge area of the packing particles having a surface that is convex on the outside and concave on the inside lead to a consider fable danger of "crumbling" in this edge area, so that because of the constant friction during the transport a fine rubbed of snow will be created.
There is also the danger that during the re-expandiny processes, such as they are carried out in the process of the initially mentioned type, if individual larger bubbles are created, these become larger and the packing particles are destroyed during these expanding processes.
In order to achieve a more uniform formation of bubbles, so-called "nucleation agents" may be added. These nucleation agents cause a nucleation ox bubbles in the plasticized plastic material. From a chemical point of view, this takes place by the fact that the solid nucleation agents decompose in the extrude while forming gas.
The released gas has the objective of forming in the plasticized plastic material a larger number of nuclei of bubbles. This resulting gas, as far as the term it concerned, must be clearly separated from the propellant gas, The propellant gas which under pressure is released in the plastic material, diffuses .;,...~.
into the small bubbles and causes the expansion of the nuclei of the bubbles created by the decomposition of the nucleation agent.
In the technique, nucleation agents are preferably used that do no carry harmful gases, decomposing into carbon dioxide, nitrogen or similar gases The raw materials used in the process must correspond to the German Food Law. According to FDA
requirements, all components must be GRAS (GENERALLY
RECOGNIZED AS SAFE). The most often used materials are carbonates, such as carbonate of ammonia or sodium carbonate. Sodium hydrogen carbonate has, for exam-pie, also teen used widely as a propellant in backing powders since at an increased temperature it separates carbon dioxide.
The required quantity of nucleation agent is determined by the decomposition behavior of the nucleation agent at a rising temperature The so-called theoretical gas yield in-this case plays a significant role. The theoretical gas yield is determined by the released quantity of gas (such as carbon dioxide per unit of weight. wince the gas yield increases with rising temperature, small quantities of nucleation agent art required at high processing temperatures.
In the case of relatively low processing .
3~7 temperatures of about 110 - 130C, the conventional nucleation agents cannot be used economically because they have an optimal processing temperature range of 180 - 230C. In addition, the formation of bubbles in regard to their size and their spatial distribution per volume element of plasticized plastic mass is very irregular, which after leaving the extrude results in an irregular cell structure of the expand dyed plastic material.
It is the objective of the invention to improve a process of the initially mentioned type in such a way that in the case of a relatively low processing temperature of the plastic material in the extrude and small additions of nucleation agent, an even format lion of a large number of bubbles is made possible.
This objective is achieved by the fact that on the surface of the plastic granules, before their processing in the extrude, the bubble forming agent (nucleation agent) is applied.
In accordance with the present invention, there is thus provided a process for producing parboil spherical-segment-shaped packing material particles made of plastic and having an external convex and an internal concave surface, in which the plastic-materialis mixed with additives and fed by means of a feeding funnel into an extrude through an opening in a bush "
. .
. . .
surïc)undinq an extrusion screw, where the plastic material is plasticized in the course of extrusion and comes out of an opening in a die with a bent surface, and the extruded plastic material is cut off directly at the opening of the die and before any considerable expansion has taken place. The process according to the invention is characterized in that a bubble-forming agent having a grain size of less than about 40 mu is uniformly distributed on the surface of the plastic particles before their processing in the extrude in an amount less than 0.2 percent by weight based on the weight of said particles.
The finely ground nucleation agent, in a drum, is "drummed" onto the plastic granules. The quantity of the "drummed-on" nucleation agent is preferably about 0.1-0.2 percent by weight with respect to the - pa -~66~
weight of the granules.
The nucleation agent may especially ad van-tageously consist of a carbonate and an acid combo-next n The acid component, in addition to the effect of the heat, by the chemical effect on the carbonate component, makes possible a development of carbon dioxide. the acid component consists of citric acid and there are therefore no reservations based on the food law, Of decisive significance in regard to a uniform quality of the packing material particles produced according to this process is the formation and the expansion of gas bubbles.
The formation ox bubbles takes place by the fact that the nucleation agent releases a gas in the plasticized plastic material. The release of gas, as mentioned before, can take place only by the then-mix splitting-up of the carbonate, or in addition by reactions between the acid component and the carbonate component. Since the carbonates are salts of the weak acid carbonic acid, the carbonic acid can be pushed out o their compounds by stronger acids, in this case citric acids.
The conventional propellants are swilled exothermal systems, during the decomposition of which large quantities ox heat are released. The danger of the formation of heat accumulation, i.e. local over-"
~L~36~
heating, leads to an uneven formation of bubbles.
The propellant used in this process is an endothermally effective system. With an increasing temperature, an even decomposition of the propellant and thus more finely celled and more uniform foamed structures are obtained. The decomposition behavior of the nucleation agent depends essentially on the added quantity of heat (temperature stress through outside heating and inside friction.
The solid nucleation agent must be evenly and finely distributed in the plasticized plastic material so that per volume element potential nuclei exist that are as numerous as possible and as small as possible. It is then ensured that when the for-motion of gas occurs, a uniform fine-celled foam will be created in the extrude.
According to the invention, this it achieved by the tact that the nucleation agent, before the plastic material granules are pulled into the extrude, is distributed on these granules so that it adheres to them evenly, in which case the grain size is of very decisive significance.
The finely ground nucleation agent (grain size about 40 I) is "drummed onto" the granules of plastic material in a drum. The term "drummed onto"
is used here in order to differentiate it clearly from the mixing of the granules of plastic material Jo _ 9 _ ' with the nucleation agent, as it is carried out in the state of the art. This mixing may also take place in mixing drums so that a clear difference must be made between the two processes, as far as the terminology is concerned.
Figuratively, the granules of plastic material, after they have left the drum, are different from one another because of the fact that after the "drumming-on" the granule s of plastic material look like, for example, an apple iced with confectioners sugar, whereas after the mixing, the granules look as if an apple had been sprinkled with sugar crystals.
The adherence of the swigger crystals" in the state of the art is achieved by adding bonding agents, such as talc to the mixture. In the case of the drur~ming-on, no bonding agents are required since the fine "powder"
adheres well to the surface.
When one follows the path of the differently treated (mixed or drurmmed-on) granules from the mixing drum through the extrude, the difference can be made particularly clear using the "apple example'`.
The granules (apples) in the tunnel are in a constant movement and in the pull-in zone of the extrude, where they are not yet plasticized, are turned into different directions and rubbed against one another. The granule (apple first carries out an essentially vertical movement through the funnel ,; , , I
and subsequently in the extrude, by the propelling sides of the extrusion screw, is moved into a direct lion that can be divided into two components. One movement is the axial movement through the extrude and the other movement is the circular movement around the axis of the extrude.
Over the course of the extrude, because of the increase of the core diameter of toe screw, the space for the granules (apples decreases continuously.
Through the rubbing-against-one-another of the individual granules (apples) because of the advancing and rotating movement and because of the increasing densification. a relatively extensive rubbing-off takes place on the granules with the coarse nucleation agent (apples with sugar crystals), the rubbed-off material collecting especially in the hollow spaces between the granules.
In the case of the granules with the drummed-on nucleation agent (apples with confectioners sugar icing), a layer exists that adheres firmly because of the adhesive forces and is distributed evenly over the surface. The rubbing-off of nucleation agent on the path of the granule (apple) through the funnel and the material pull-in zone is much less, and therefore hardly any material is collected in the spaces between the granules (apples).
,,.~
I
In the plasticizing zone of the extrude, i.e., in the zone where the granules become sot, the granules no longer rub against one another but are squeezed together or kneaded together. However, this kneading-through in the extrude is only a rough mixing of components.
In the microscopic range, a certain "close order" is still maintained despite this mixing.
In the case of the drummed-on granules of plastic material, after the collapse of the solid phase by plasticizing, the spatial distribution of the still firm nucleation agent it very regular. This means that in any volume element, numerous very fine nuclei of bubbles are evenly distributed.
In contrast, in the cave of the originally only mixed granules (i.e., the plastic material and the nucleation agent are only mixed and not drummed on), there are in certain areas many and relatively large solid matter particles of the bubble nuclei present, whereas in other areas there are almost no bubble nuclei present, but only much plasticized plastic material with the propellant released in said material.
Because of the small grain size and the fine distribution, even at low processing temperatures of about 110 130~C - thus far below the processing range of 180 _ 230C considered as optimal in the I
state of the art - a sufficient decomposition of the nucleation agent takes place with the formation of numerous and very small bubbles.
The first phase, i.e., the formation of the nuclei and thus of the bubbles, is improved decisively by the drumming-on of the nucleation agent, and con-siderable costs are saved because of the low process sing temperature.
The second important aspect concerning the quality of the end product is the increase in the size of the gas bubbles. In the initial phase, the increase in size of the gas bubbles still takes place by means of the occurring gas of the nucleation agent. However, the further increase in size, espy-Shelley during the re-expanding processes, takes place by means of the propellant released in the plastic material.
Decisive for the growth of the bubbles is the pressure within the bubbles and the pressure of the released agent in the extrude and the pressure in the extrude itself. The relationship between these pressures can be described by means of the following reaction equations UP Pi Pi (1) UP = 2 OR I
_ 13 -~36~6~
In these equations, Pi is the existing pressure on the inside of the bubble, Pi is the partial pressure of the released propellant gas in the melted plastic material, UP is the difference in pressure (ire. the "driving pharisee, is the surface tension of the burble, R is the radius of the bubble.
While the bubble grows, the pressure in the bubble decreases, while the radius increases keynote-nuzzle. At the beginning" it grows very fast until a large part of the excessive released gas was used up in the adjacent area to expand the polymer.
The growth of the bubbles is influenced by the diffusion rate of the released propellant in the melted plastic material in the direction of the bubble as well as by the degree of supersaturation and the viscosity of the melted mass. In the state of equip librium, the balance of forces exists that is desert-bed by equations (1) and (2).
In the case of a starting material that is only mixed (apple with sugar crystals), uneven growth rates of the bubbles exist because of the irregular spatial distribution. Zones with a lot of plastic material and muck released propellant alternated with other zones which contained relatively large amounts ,:
.
~36~7 of nucleation agent and where gas bubbles were created that are relatively large and grew rapidly end in regard to the pressure of the propellant have no vacuum in the gas bubbles. They cause an inquiry-sod diffusion of the propellant into the bubble no-suiting in an increased rate of growth of these already large bubbles. The mixing or the "fraction-lion" taking place in the extrude my means of the screw, to e. a milling-through of the plasticized mass with an occasional cell collapse of the foam struck lure is not sufficient for controlling an uneven foam structure in regard to arrangement and size.
Further features and advantages of the invention will become more readily apparent from the following description of preferred embodiments, with reference to the appended drawings, in which Figure 1 is a diagrammatic side view of a device for producing packing material particles.
The device required to carry out the process is shown in diagram form in Figure 1 and has a drum 5 provided with openings 6 and 7 through which the plastic material and the finely ground nucleation agent are added. From the drum 5, the drummed-on plastic granules, by means of a conveying device 8 and a conveying pipe 9, are fed into an extrusion device 10.
The extrusion device 10 consists of a drip , - 15 -" :, .. ^
~66~
vying motor 11, a gear 12, a material pull-in zone 13 and an extrude 14. A cutting device 16 it arranged directly in front of an opening 15 of the die of the extrude 14.
The drummed-on granules, via a feeding funnel 17, reach the extrude 14 through the material entrance zone 13.
The plastic material is plasticized over the longitudinal course of the extrude: the nucleation agent decomposes while forming gas, and the plastic material comes out of the opening 15 in the form of a mass of melted foam. Because of the difference in speed existing over the mass cross section, the pies-tic foam squeezes out of the inside area of the open nine 15 of the die with a bent surface.
The extruded plastic is cut off by means of the cutting device 16 directly at the opening 15.
The cut-off plastic particles expand in the free fall in a first expanded condition, already taking their shape of having a surface that is concave on the inside an convex on the outside A collecting container 19 collects the solidified and cooled plastic particles 18.
The initially expanded foamed particles by means of a blower 20 are transported through a pipe I into a storage container 22.
After a certain storage period, the initially I, eye expanded plastic particles 18 are conveyed from the storage container 22 into a re-expansion unit 23 where the plastic particles are re-expanded.
After leaving the re-expansion unit 23, the re-expanded plastic particles 18 are conveyed to a storage container 24. This storage container 24 preferably consists of a sieve material or any other open mesh material permitting a free circulation of air and thus an easier drying of the newly expanded plastic particles 18.
The plastic packing particles that are expanded to their final condition have an even and uniform cell structure. The particles have such stability that the pressure affecting the packing material during transport does not result in a breaking of the packing material particles. In addition, the individual particles are closed off in themselves by a relatively smooth surface so that not much "crumb formation" takes place when the individual packing material particles rub against one another.
When carrying out this process, the nuclear lion agent is first ground to a grain size of 40 p.
The nucleation agent is based on the multi-component nucleation agent that is known under the trademark of "Hydrocerol". The acid component consists either of water-repellent anhydrocitric acid or of citric acid MindWrite. The acid component is treated or coated I
in such a way that it is water-repellent and can thus be mixed with the carbonate component (sodium hydrogen carbonate) and can be stored for long periods without drawing humidity from the environment.
The nucleation agent OF 0556 is a fine, odorless, white, free-flowing, non-dusty powder.
According to FDA requirements, all components of OF
0556 are GRAS (Generally Recognized As Safe). CF0556 can be stored well without clotting or sticking-to-getter because of moisture absorption.
The plastic granules consisting of expandable polystyrene (ENS), i.e., polystyrene with incorporated propellant (for example, pontoon) are fed into the drum 5.
For each 70 kg ENS granules, 100 g CF0~56 nucleation agent are drummed on. In the case of this process which must not be confused with a pure mixing, an evenly distributed layer of the fine nucleation agent places itself on the plastic granules. The addition of so-called bonding agents in the form of talc or similar substances is not necessary, because the very fine coating adheres well to the granules.
The proportion of nucleation agent is 0.14 percent by weight.
The drummed-on granules, by means of the conveying advice 8, via conveying pipe 9, are fed into the feeding funnel 17. Coloring pigments or Jo, I
6~6~
other desirable additives may be added to the feeding funnel. The mixture is pulled into the material pull in zone 13 of the extrude 14 by means of the extrusion screw. Over the course of the ox-truer 14, the material, because of an increase of the core diameter of the extrude screw, is plastic cited by the friction and by heat supplied cores-pondingly from the outside.
The drummed-on granules, on their surface, lo have the evenly distributed about 40 large solid matter particles of the nucleation agent. In the transition phase from the solid to the plasticized condition, the granules are squeezed against one another, without significantly destroying the close order of the particles arranged on the surface. When the plastic particles are squeezed and sheared, the overall mixing is still somewhat improved. This can be remonstrated by imagining that a softly chewed piece of chewing gum is made into a ball and this ball is then pulled apart between two fingers. The strut-eking will take place so evenly that the regularity of particles on-the surface will be maintained -The processing temperature of the plastic material is approximately between 110 - 130C. Even at these low temperatures, the nucleation agent OF
0~56 develops carbon dioxide Because of the fine distribution, considering the overall volume, an -- :19 --I
evenly distributed formation of bumbles that increases at a uniform speed is achieved The size of the hubbies also depends on the dimensions of the extrude and the speed of the extrude screw. Immediately after the extruded plastic comes out and is cut elf, a rapid expansion of the plastic particles will take place because the compressed gasses in the bubbles can expand to almost normal pressure.
At the same time, the plastic particles are colored and are maintained in a first expanded shape, In this first expanded shape, the initially expanded packing material particles have a bulk density of about 22 kgJm3. They have an extremely fine-celled structure making the surface of the packing material particles very smooth. the packing material part-ales, after a rest, will then be re-expanded.
During this rest period, the propellant existing in the plastic material diffuses from the plastic material into the bubbles. The inside pressure within the bubbles, because of the rapid expansion after leaving the extrusion screw, is much less than the partial pressure of the released pro-pollinate in the plastic material, in which case this difference in pressure is the driving force for the diffusion and also determines the direction.
The further expansion processes are carried out in such a way that the packing particles are ~L~3Ç~6~7 exposed to a vapor atmosphere, pausing the propellant that had diffused into the bubbles to expand and expanding the plastic particle. The storage periods between the individual expanding processes become continuously longer, because less and less propellant gas is released in the plastic material and less can therefore diffuse into the bubbles. After several expanding processes, the packing particles have a bulk density of only about 4.5 kg/m3.
Despite the numerous expanding processes, the packing material particles have a relatively smooth surface and, because of the fine-celled struck lure have sufficient stability. Especially at the edge zones, the packing particles are smooth and round so that there is no danger of a crumb formation between the parts that are stacked into one another under stress.
By means of the drumming-on of the 40 nucleation particles on the plastic granules, the basis is created for the quality of the end product.
, yo-yo Jo
A process of this type is known from U.S.
Patent No. 3,961,000. In the case of this process, the e~pandible polystyrene (ENS) is mixed with add-lives. The additives consist of bubble-forming-agents-such as bicarbonate of ammonia and sodium bicarbonate or similar substances and coloring pigments Via a supply funnel, the mixture is fed into an extrusion device. An extrusion screw transports the mixture through the extrude, where because of the special design of the extrusion screw, i.e. an inquiry-sing core diameter as well as a suitable temperature .~, ..
~36~6~
program, the plastic material is plasticized in the course of the extrude. Immediately after the plastic material comes out of an opening in the die, it is cut off by means of a cutting device, in which case it is made possible for the cut-off particles to expand in a first expansion process into the special shape with a convex outside and a concave inside surface. The packing material particles are processed to their final condition in several subsequent expanding processes.
Polystyrene is a polymerization product of the Bunsen derivative styrenes and according to the conditions of representation, has polymers of varying chain lengths. The chain length is significantly determined by how many styrenes units were "chained to one another" during the polymerization.
polymerization j CH=cH2 2 OH -monomeric styrenes polystyrene The chain length essentially determines the physical characteristics of the plastic material. In order for the plastic material to be processed in an extrude, it must by "thermoplastic". This means that , . . ... .
. .
~L~3~6~
the plastic material which is firm at a certain temperature (usually at room temperature) becomes plastic (soft, moldable) when the temperature is in-creased and can then be processed to a certain shape and after cooling resumes its firm condition.
For the processing in the extrude, two different basic types of polystyrene are available:
a the so-called standard polystyrene ) a polystyrene containing an expanding agent.
The standard polystyrene is a pure polymer, ire., a pure polystyrene without additives. In the case of the polystyrene containing an expanding agent, an expanding agent is included in the polymer matrix which boils at an increased temperature and foams the polymer. Such expanding agents are prefer rawly low-boiling hydrocarbons, fluorohydro-carbons or water.
Standard polystyrene types as well as polyp styrenes types containing expanding agents are suitable for processing into foamed materials on the extrude.
When standard polystyrene is used, it is necessary to add an expanding agent to the extrude during process sing In that case, one speaks of a so-called direct gassing.
The expanding agent causes the plasticized material to foam after leaving the extrude.
, - 3 _ `' ' ' `
The expanding agent, in the extrude, is released under pressure in gaseous fox in the pies-ticized plastic mass. The plastic mass is supers-turated with gas, i.e., because of the conditions (pressure, temperature existing in the extrude, more gas is released than under normal conditions.
After leaving the extrude, the expanding agent tries to burble down and to expand to normal pressure. The stick plastic mass surrounding the expanding agent prevents the propellant gas from escaping into the atmosphere and therefore results in the foamed structure.
By cooling the plastic material in the indicated shapes, the typical structure of the blocks of foamed material is obtained.
In the case of large-volume blocks of foamed material, such as insulating boards, the size of the foam bubbles is relatively large, and the diameter of these bubbles fluctuates over a considerable range.
In the case of the present process, however, small packing material particles are produced, the diameter of which is about up to three centimeters.
In the case of these small packing particles, the size of the bubbles must naturally be much smaller than in the above-described case in order to ensure the stability of the packing particle material. Only a few large bubbles in these small packing particles Jo ~31~i6~
decrease stability and even under little stress result in a breaking of the particles. Larger bumbles, especially in the edge area of the packing particles having a surface that is convex on the outside and concave on the inside lead to a consider fable danger of "crumbling" in this edge area, so that because of the constant friction during the transport a fine rubbed of snow will be created.
There is also the danger that during the re-expandiny processes, such as they are carried out in the process of the initially mentioned type, if individual larger bubbles are created, these become larger and the packing particles are destroyed during these expanding processes.
In order to achieve a more uniform formation of bubbles, so-called "nucleation agents" may be added. These nucleation agents cause a nucleation ox bubbles in the plasticized plastic material. From a chemical point of view, this takes place by the fact that the solid nucleation agents decompose in the extrude while forming gas.
The released gas has the objective of forming in the plasticized plastic material a larger number of nuclei of bubbles. This resulting gas, as far as the term it concerned, must be clearly separated from the propellant gas, The propellant gas which under pressure is released in the plastic material, diffuses .;,...~.
into the small bubbles and causes the expansion of the nuclei of the bubbles created by the decomposition of the nucleation agent.
In the technique, nucleation agents are preferably used that do no carry harmful gases, decomposing into carbon dioxide, nitrogen or similar gases The raw materials used in the process must correspond to the German Food Law. According to FDA
requirements, all components must be GRAS (GENERALLY
RECOGNIZED AS SAFE). The most often used materials are carbonates, such as carbonate of ammonia or sodium carbonate. Sodium hydrogen carbonate has, for exam-pie, also teen used widely as a propellant in backing powders since at an increased temperature it separates carbon dioxide.
The required quantity of nucleation agent is determined by the decomposition behavior of the nucleation agent at a rising temperature The so-called theoretical gas yield in-this case plays a significant role. The theoretical gas yield is determined by the released quantity of gas (such as carbon dioxide per unit of weight. wince the gas yield increases with rising temperature, small quantities of nucleation agent art required at high processing temperatures.
In the case of relatively low processing .
3~7 temperatures of about 110 - 130C, the conventional nucleation agents cannot be used economically because they have an optimal processing temperature range of 180 - 230C. In addition, the formation of bubbles in regard to their size and their spatial distribution per volume element of plasticized plastic mass is very irregular, which after leaving the extrude results in an irregular cell structure of the expand dyed plastic material.
It is the objective of the invention to improve a process of the initially mentioned type in such a way that in the case of a relatively low processing temperature of the plastic material in the extrude and small additions of nucleation agent, an even format lion of a large number of bubbles is made possible.
This objective is achieved by the fact that on the surface of the plastic granules, before their processing in the extrude, the bubble forming agent (nucleation agent) is applied.
In accordance with the present invention, there is thus provided a process for producing parboil spherical-segment-shaped packing material particles made of plastic and having an external convex and an internal concave surface, in which the plastic-materialis mixed with additives and fed by means of a feeding funnel into an extrude through an opening in a bush "
. .
. . .
surïc)undinq an extrusion screw, where the plastic material is plasticized in the course of extrusion and comes out of an opening in a die with a bent surface, and the extruded plastic material is cut off directly at the opening of the die and before any considerable expansion has taken place. The process according to the invention is characterized in that a bubble-forming agent having a grain size of less than about 40 mu is uniformly distributed on the surface of the plastic particles before their processing in the extrude in an amount less than 0.2 percent by weight based on the weight of said particles.
The finely ground nucleation agent, in a drum, is "drummed" onto the plastic granules. The quantity of the "drummed-on" nucleation agent is preferably about 0.1-0.2 percent by weight with respect to the - pa -~66~
weight of the granules.
The nucleation agent may especially ad van-tageously consist of a carbonate and an acid combo-next n The acid component, in addition to the effect of the heat, by the chemical effect on the carbonate component, makes possible a development of carbon dioxide. the acid component consists of citric acid and there are therefore no reservations based on the food law, Of decisive significance in regard to a uniform quality of the packing material particles produced according to this process is the formation and the expansion of gas bubbles.
The formation ox bubbles takes place by the fact that the nucleation agent releases a gas in the plasticized plastic material. The release of gas, as mentioned before, can take place only by the then-mix splitting-up of the carbonate, or in addition by reactions between the acid component and the carbonate component. Since the carbonates are salts of the weak acid carbonic acid, the carbonic acid can be pushed out o their compounds by stronger acids, in this case citric acids.
The conventional propellants are swilled exothermal systems, during the decomposition of which large quantities ox heat are released. The danger of the formation of heat accumulation, i.e. local over-"
~L~36~
heating, leads to an uneven formation of bubbles.
The propellant used in this process is an endothermally effective system. With an increasing temperature, an even decomposition of the propellant and thus more finely celled and more uniform foamed structures are obtained. The decomposition behavior of the nucleation agent depends essentially on the added quantity of heat (temperature stress through outside heating and inside friction.
The solid nucleation agent must be evenly and finely distributed in the plasticized plastic material so that per volume element potential nuclei exist that are as numerous as possible and as small as possible. It is then ensured that when the for-motion of gas occurs, a uniform fine-celled foam will be created in the extrude.
According to the invention, this it achieved by the tact that the nucleation agent, before the plastic material granules are pulled into the extrude, is distributed on these granules so that it adheres to them evenly, in which case the grain size is of very decisive significance.
The finely ground nucleation agent (grain size about 40 I) is "drummed onto" the granules of plastic material in a drum. The term "drummed onto"
is used here in order to differentiate it clearly from the mixing of the granules of plastic material Jo _ 9 _ ' with the nucleation agent, as it is carried out in the state of the art. This mixing may also take place in mixing drums so that a clear difference must be made between the two processes, as far as the terminology is concerned.
Figuratively, the granules of plastic material, after they have left the drum, are different from one another because of the fact that after the "drumming-on" the granule s of plastic material look like, for example, an apple iced with confectioners sugar, whereas after the mixing, the granules look as if an apple had been sprinkled with sugar crystals.
The adherence of the swigger crystals" in the state of the art is achieved by adding bonding agents, such as talc to the mixture. In the case of the drur~ming-on, no bonding agents are required since the fine "powder"
adheres well to the surface.
When one follows the path of the differently treated (mixed or drurmmed-on) granules from the mixing drum through the extrude, the difference can be made particularly clear using the "apple example'`.
The granules (apples) in the tunnel are in a constant movement and in the pull-in zone of the extrude, where they are not yet plasticized, are turned into different directions and rubbed against one another. The granule (apple first carries out an essentially vertical movement through the funnel ,; , , I
and subsequently in the extrude, by the propelling sides of the extrusion screw, is moved into a direct lion that can be divided into two components. One movement is the axial movement through the extrude and the other movement is the circular movement around the axis of the extrude.
Over the course of the extrude, because of the increase of the core diameter of toe screw, the space for the granules (apples decreases continuously.
Through the rubbing-against-one-another of the individual granules (apples) because of the advancing and rotating movement and because of the increasing densification. a relatively extensive rubbing-off takes place on the granules with the coarse nucleation agent (apples with sugar crystals), the rubbed-off material collecting especially in the hollow spaces between the granules.
In the case of the granules with the drummed-on nucleation agent (apples with confectioners sugar icing), a layer exists that adheres firmly because of the adhesive forces and is distributed evenly over the surface. The rubbing-off of nucleation agent on the path of the granule (apple) through the funnel and the material pull-in zone is much less, and therefore hardly any material is collected in the spaces between the granules (apples).
,,.~
I
In the plasticizing zone of the extrude, i.e., in the zone where the granules become sot, the granules no longer rub against one another but are squeezed together or kneaded together. However, this kneading-through in the extrude is only a rough mixing of components.
In the microscopic range, a certain "close order" is still maintained despite this mixing.
In the case of the drummed-on granules of plastic material, after the collapse of the solid phase by plasticizing, the spatial distribution of the still firm nucleation agent it very regular. This means that in any volume element, numerous very fine nuclei of bubbles are evenly distributed.
In contrast, in the cave of the originally only mixed granules (i.e., the plastic material and the nucleation agent are only mixed and not drummed on), there are in certain areas many and relatively large solid matter particles of the bubble nuclei present, whereas in other areas there are almost no bubble nuclei present, but only much plasticized plastic material with the propellant released in said material.
Because of the small grain size and the fine distribution, even at low processing temperatures of about 110 130~C - thus far below the processing range of 180 _ 230C considered as optimal in the I
state of the art - a sufficient decomposition of the nucleation agent takes place with the formation of numerous and very small bubbles.
The first phase, i.e., the formation of the nuclei and thus of the bubbles, is improved decisively by the drumming-on of the nucleation agent, and con-siderable costs are saved because of the low process sing temperature.
The second important aspect concerning the quality of the end product is the increase in the size of the gas bubbles. In the initial phase, the increase in size of the gas bubbles still takes place by means of the occurring gas of the nucleation agent. However, the further increase in size, espy-Shelley during the re-expanding processes, takes place by means of the propellant released in the plastic material.
Decisive for the growth of the bubbles is the pressure within the bubbles and the pressure of the released agent in the extrude and the pressure in the extrude itself. The relationship between these pressures can be described by means of the following reaction equations UP Pi Pi (1) UP = 2 OR I
_ 13 -~36~6~
In these equations, Pi is the existing pressure on the inside of the bubble, Pi is the partial pressure of the released propellant gas in the melted plastic material, UP is the difference in pressure (ire. the "driving pharisee, is the surface tension of the burble, R is the radius of the bubble.
While the bubble grows, the pressure in the bubble decreases, while the radius increases keynote-nuzzle. At the beginning" it grows very fast until a large part of the excessive released gas was used up in the adjacent area to expand the polymer.
The growth of the bubbles is influenced by the diffusion rate of the released propellant in the melted plastic material in the direction of the bubble as well as by the degree of supersaturation and the viscosity of the melted mass. In the state of equip librium, the balance of forces exists that is desert-bed by equations (1) and (2).
In the case of a starting material that is only mixed (apple with sugar crystals), uneven growth rates of the bubbles exist because of the irregular spatial distribution. Zones with a lot of plastic material and muck released propellant alternated with other zones which contained relatively large amounts ,:
.
~36~7 of nucleation agent and where gas bubbles were created that are relatively large and grew rapidly end in regard to the pressure of the propellant have no vacuum in the gas bubbles. They cause an inquiry-sod diffusion of the propellant into the bubble no-suiting in an increased rate of growth of these already large bubbles. The mixing or the "fraction-lion" taking place in the extrude my means of the screw, to e. a milling-through of the plasticized mass with an occasional cell collapse of the foam struck lure is not sufficient for controlling an uneven foam structure in regard to arrangement and size.
Further features and advantages of the invention will become more readily apparent from the following description of preferred embodiments, with reference to the appended drawings, in which Figure 1 is a diagrammatic side view of a device for producing packing material particles.
The device required to carry out the process is shown in diagram form in Figure 1 and has a drum 5 provided with openings 6 and 7 through which the plastic material and the finely ground nucleation agent are added. From the drum 5, the drummed-on plastic granules, by means of a conveying device 8 and a conveying pipe 9, are fed into an extrusion device 10.
The extrusion device 10 consists of a drip , - 15 -" :, .. ^
~66~
vying motor 11, a gear 12, a material pull-in zone 13 and an extrude 14. A cutting device 16 it arranged directly in front of an opening 15 of the die of the extrude 14.
The drummed-on granules, via a feeding funnel 17, reach the extrude 14 through the material entrance zone 13.
The plastic material is plasticized over the longitudinal course of the extrude: the nucleation agent decomposes while forming gas, and the plastic material comes out of the opening 15 in the form of a mass of melted foam. Because of the difference in speed existing over the mass cross section, the pies-tic foam squeezes out of the inside area of the open nine 15 of the die with a bent surface.
The extruded plastic is cut off by means of the cutting device 16 directly at the opening 15.
The cut-off plastic particles expand in the free fall in a first expanded condition, already taking their shape of having a surface that is concave on the inside an convex on the outside A collecting container 19 collects the solidified and cooled plastic particles 18.
The initially expanded foamed particles by means of a blower 20 are transported through a pipe I into a storage container 22.
After a certain storage period, the initially I, eye expanded plastic particles 18 are conveyed from the storage container 22 into a re-expansion unit 23 where the plastic particles are re-expanded.
After leaving the re-expansion unit 23, the re-expanded plastic particles 18 are conveyed to a storage container 24. This storage container 24 preferably consists of a sieve material or any other open mesh material permitting a free circulation of air and thus an easier drying of the newly expanded plastic particles 18.
The plastic packing particles that are expanded to their final condition have an even and uniform cell structure. The particles have such stability that the pressure affecting the packing material during transport does not result in a breaking of the packing material particles. In addition, the individual particles are closed off in themselves by a relatively smooth surface so that not much "crumb formation" takes place when the individual packing material particles rub against one another.
When carrying out this process, the nuclear lion agent is first ground to a grain size of 40 p.
The nucleation agent is based on the multi-component nucleation agent that is known under the trademark of "Hydrocerol". The acid component consists either of water-repellent anhydrocitric acid or of citric acid MindWrite. The acid component is treated or coated I
in such a way that it is water-repellent and can thus be mixed with the carbonate component (sodium hydrogen carbonate) and can be stored for long periods without drawing humidity from the environment.
The nucleation agent OF 0556 is a fine, odorless, white, free-flowing, non-dusty powder.
According to FDA requirements, all components of OF
0556 are GRAS (Generally Recognized As Safe). CF0556 can be stored well without clotting or sticking-to-getter because of moisture absorption.
The plastic granules consisting of expandable polystyrene (ENS), i.e., polystyrene with incorporated propellant (for example, pontoon) are fed into the drum 5.
For each 70 kg ENS granules, 100 g CF0~56 nucleation agent are drummed on. In the case of this process which must not be confused with a pure mixing, an evenly distributed layer of the fine nucleation agent places itself on the plastic granules. The addition of so-called bonding agents in the form of talc or similar substances is not necessary, because the very fine coating adheres well to the granules.
The proportion of nucleation agent is 0.14 percent by weight.
The drummed-on granules, by means of the conveying advice 8, via conveying pipe 9, are fed into the feeding funnel 17. Coloring pigments or Jo, I
6~6~
other desirable additives may be added to the feeding funnel. The mixture is pulled into the material pull in zone 13 of the extrude 14 by means of the extrusion screw. Over the course of the ox-truer 14, the material, because of an increase of the core diameter of the extrude screw, is plastic cited by the friction and by heat supplied cores-pondingly from the outside.
The drummed-on granules, on their surface, lo have the evenly distributed about 40 large solid matter particles of the nucleation agent. In the transition phase from the solid to the plasticized condition, the granules are squeezed against one another, without significantly destroying the close order of the particles arranged on the surface. When the plastic particles are squeezed and sheared, the overall mixing is still somewhat improved. This can be remonstrated by imagining that a softly chewed piece of chewing gum is made into a ball and this ball is then pulled apart between two fingers. The strut-eking will take place so evenly that the regularity of particles on-the surface will be maintained -The processing temperature of the plastic material is approximately between 110 - 130C. Even at these low temperatures, the nucleation agent OF
0~56 develops carbon dioxide Because of the fine distribution, considering the overall volume, an -- :19 --I
evenly distributed formation of bumbles that increases at a uniform speed is achieved The size of the hubbies also depends on the dimensions of the extrude and the speed of the extrude screw. Immediately after the extruded plastic comes out and is cut elf, a rapid expansion of the plastic particles will take place because the compressed gasses in the bubbles can expand to almost normal pressure.
At the same time, the plastic particles are colored and are maintained in a first expanded shape, In this first expanded shape, the initially expanded packing material particles have a bulk density of about 22 kgJm3. They have an extremely fine-celled structure making the surface of the packing material particles very smooth. the packing material part-ales, after a rest, will then be re-expanded.
During this rest period, the propellant existing in the plastic material diffuses from the plastic material into the bubbles. The inside pressure within the bubbles, because of the rapid expansion after leaving the extrusion screw, is much less than the partial pressure of the released pro-pollinate in the plastic material, in which case this difference in pressure is the driving force for the diffusion and also determines the direction.
The further expansion processes are carried out in such a way that the packing particles are ~L~3Ç~6~7 exposed to a vapor atmosphere, pausing the propellant that had diffused into the bubbles to expand and expanding the plastic particle. The storage periods between the individual expanding processes become continuously longer, because less and less propellant gas is released in the plastic material and less can therefore diffuse into the bubbles. After several expanding processes, the packing particles have a bulk density of only about 4.5 kg/m3.
Despite the numerous expanding processes, the packing material particles have a relatively smooth surface and, because of the fine-celled struck lure have sufficient stability. Especially at the edge zones, the packing particles are smooth and round so that there is no danger of a crumb formation between the parts that are stacked into one another under stress.
By means of the drumming-on of the 40 nucleation particles on the plastic granules, the basis is created for the quality of the end product.
, yo-yo Jo
Claims (4)
1. A process for producing pourable spherical-segment-shaped packing material particles made of plastic and having an external convex and an internal concave surface, in which the plastic material is mixed with additives and fed by means of a feeding funnel into an extruder through an opening in a bush surround-ing an extrusion screw, where the plastic material is plasticized in the course of extrusion and comes out of an opening in a die with a bent surface, and the extruded plastic material is cut off directly at the opening of the die and before any considerable ex-pansion has taken place, characterized in that a bubble-forming agent having a grain size of less than about 40 µ is uniformly distributed on the surface of the plastic particles before their processing in the ex-truder in an amount less than 0.2 percent by weight based on the weight of said particles.
2. A process according to claim 1, characterized in that the processing temperature in the extruder is about 110°C - 130°C.
3. A process according to claim 1, characterized in that the bubble-forming agent consists of a carbonate component and of an acid component.
4. A plastic granule for carrying out the pro-cess according to claims 1, 2 or 3, made of expandable polystyrene (EPS).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CA000497629A CA1236667A (en) | 1985-12-13 | 1985-12-13 | Process for producing pourable spherical-segment- shaped packing material particles made of plastic |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CA000497629A CA1236667A (en) | 1985-12-13 | 1985-12-13 | Process for producing pourable spherical-segment- shaped packing material particles made of plastic |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CA1236667A true CA1236667A (en) | 1988-05-17 |
Family
ID=4132076
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA000497629A Expired CA1236667A (en) | 1985-12-13 | 1985-12-13 | Process for producing pourable spherical-segment- shaped packing material particles made of plastic |
Country Status (1)
| Country | Link |
|---|---|
| CA (1) | CA1236667A (en) |
-
1985
- 1985-12-13 CA CA000497629A patent/CA1236667A/en not_active Expired
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