METHOD AND DEVICE FOR THE EXTRUSION OF A POLYMERIC SUBSTANCE

Abstract: The polymeric substance delivery method and device, in which the outflow is determined from a first container (5) of a monomeric substance able to polymerize autonomously upon air contact, and eventually, the outflow from a second container (7) is determined of a hardening substance able to accelerate the polymerization of the monomeric substance, by sending the same hardening substance towards a mixing zone of the hardening substance with the same monomeric substance.

Description: METHOD AND DEVICE FOR THE EXTRUSION OF A POLYMERIC SUBSTANCE The present invention is relative to a method for the extrusion of a polymeric substance. As already known, the polymerization of a monomeric substance emission from a container occurs in many cases due to the effect of the mixing of the same substance, before the output from the same container, with a prefixed quantity of a certain liquid, for example, constituted by additived water or at least with other substances or other liquids which are different in dependence from the type of monomeric substance in question. The said liquid, when simple water, is usually supplied from air humidity in the case of single component extruder, that is to say, extruders containing only the monomeric substance inside, or is supplied following the break of a small tank housed in the container in the case of the so called "double-component" extrusion ( obviously, this solution is valid for any type of liquid). This second process should be considered as being of high technical value, as, on the contrary to what occurs with the first process, the liquid contained in the aforementioned container can be intimately mixed with the entire mass of the monomeric substance, assuring the subsequent uniform and simultaneous polymerization in all zones. However, this second procedure has a considerable inconvenience which consists in the fact that after the mixing of the monomeric substance with the liquid, there is only a very brief period of time available ( some minutes), in which the whole mass completes its polymerization. This means that, if for any such reason it has not been possible to proceed to the whole substance extrusion housed in the container, the polymerized quantity left in the same container, hardens and so becomes useless. Therefore, indipendently, from the objective use requirements, in a polymeric substance extrusion container which functions in the above described method, within a few minutes the unextruded mass is no longer able to be used, and constitutes together with its container "special waste" which is complicated and expensive to dispose of. l In order to use the two-component process without encountering the above mentioned inconveniences, the aim of the present invention is to supply a simple and economic invention , and a device which accomplishes such a method , suitable to permit the use, by obtaining an excellent polymerisation, 5 only the quantity of monomeric substance necessary from time to time, without prejudicing at all the substance characteristics which provisionally remain unused in a container, in order to permit the use when necessary. Moreover, the result is that any type of operation including the extrusion of a l o polymeric substance is able to be effected, using the proposed method and the device, with the due care and attention, without the harassement of having to use the whole container load within a prefixed time limit. According to the present invention, a polymerised substance extrusion method is supplied, characterised by the fact of including the phases of output determination, 1 5 from a first container, of a monomeric substance able to polymerise independently once in air contact; and eventually, to determine, the output of a hardening substance from a second container , able to accelerate the polymerization of the said monomeric substance, by sending the same hardening substance towards a mixing zone of the hardening substance with 0 the same monomeric substance. Moreover, the present invention is relative to an extrusion device for a polymeric substance. 25 According to the present invention, a device is realized for a polymeric substance extrusion which is characterised by the fact of including a first container housing within its' internal, a monomeric substance able to autonomously polymerize once put into contact with air;and a second container suitable to house a hardening substance in its internal which is able 30 to accelerate the polymerization of the said monomeric substance, and a first conduit suitable to drive the said monomeric substance towards an output station of the same monomeric substance of said device, and a second conduit suitable to conduct the hardening substance eventually outflowing from said second container towards a mixing zone of the same hardening substance with 35 the said monomeric substance; and the first obstruction means being provided which are suitable to determine, on comand, the outflow of the said monomeric substance from the said device, and the second obstruction means suitable to determine, on comand, the sending of the hardening substance eventually present within the said second container towards the said mixing 40 zone. The invention will now be described with reference to the annexed designs, which represent a preferred form of non limitative accomplishment, in which: ■ figure 1 represents a partially cross-section lateral view, of an extrusion device for the polymeric substance realized in accordance with the present 5 invention; ■ figure 2 represents a schematic lateral view of the extruder device in figure l; ■ figure 3 represents a partial section view of the extruder device of figures 1 and 2; and l o ■ figures from 4 to 7 represent some details of the extruder device of the preceding figures. With reference to figure 1, inl, a device for the polymeric substance extrusion is indicated in its complex. 15 Device (1) comprises a " gun " element indicated in it's complex with (2), of which a handgrip 3 is part and a substantially horizontal extended element 4 (figure 1 and 2) and presenting a portion of the superior end connected to the same handgrip 3. Some components (4) are combined to such extended 20 element, which will be described as follows , and which are suitable to extrude the mentioned polymeric substance. To a superior part of the extended element (4), the outlet nozzle of a first container (5) being essentially cylindric, is positioned in proximity to the 25 handgrip (3) , and connected in a known way, through screw-female thread connection, and internally housing a constituted monomeric substance, for example, by a urethane composition in liquid form, and a certain quantity of a gassy propellent substance having a pressure superior to the atmospheric pressure. The container (5) outlet nozzle is equipped, in a known and not 30 represented way, with a valve element able to hermetically maintain closed the same container (5) until the moment in which it is connected, usually through screwing, to the extended element (4), which permits the outflow from the mentioned outlet nozzle of the housed substance in container (5) after the same container (5) has been connected to the extended element (4). The 35 mentioned monomeric substance housed within the container (5) is able, when exposed into the environment, to polymerize without the addition of hardening substances, combining, for example with the humidity contained in the air; however, such polymerization without the addition of hardening substances, is verified in a relatively long time. To a superior part of the extended element (4) situated essentially in correspondence to a median part of the same extended element (4), a second essentially cylindric container (7) is connected, through a pressure regulator device indicated in it's complex with (6) and preferibly through use of screw- female thread connections , the said second container (7) being suitable to house in it's internal, a preferably liquid hardening substance, preferably constituted by water, being able to, when mixed with the quoted urethane compound, to accelerate the polymerisation of the same compound. According to that which is illustrated in figure 6, the pressure governor (6), of a known type, includes an adjusting block (8) equipped with a closed hollow cylinder (9) at its' axial ends; within such cavity a smooth-sliding, liquidtight slider (19) is installed, placed at right angles at two passages (11) and (12), respectively at the fluid influx and offtake, which pressure must be regulated, being situated at opposite bands with respect to the same slider (10). A conduit (13) leaves from the offtake passage (12), in the adjusting block internal (8), and disembogues in correspondence to an end portion of the mentioned cavity (9). T e adjusting block (10) is defined by two end cylindric parts (14) and (15), (respectively inferior and superior in figure 6) having an approximate diameter less than the cavity diameter (9), the same are connected between themselves by a shaft (16) which has a diameter which is inferior to those of the same end parts (14) and (15). A helicoid spring (16) functioning by compression is coaxially positioned withing the cavity (9), and axially drives the slider (9) towards the cavity (9)end communicating with the conduit (13). The force with which the helicoid spring (16) acts on the slider (10) can be regulated by adjusting an external thread element (17), being screwed in the adjusting block (8) and suitable to push the same hecoidal spring with variable force (16) against the same slider (10). While functioning, the pressure of the liquid flowing out of the offtake passage (12) is regulated to requirement, and is maintained equal to the desired pressure value, after having set the force through the external thread element (17), by which the helicoidal spring (16) presses on the slider (10). Such automatic regulation occurs in virtue of the fact that a part of the liquid flowing through the offtake passage (12) constantly flows into the conduit (13), consequently pressing the end cylindric part (14) facing the same conduit (13) towards the helicoidal spring (16) with a force which is in function to the pressure which the same liquid presents with the offtake passage (12); as a result of that, the end cylindric part (14) obstructs the part of the cavity (9) that connects the passages (11) and (12) to the measure that, the higher the pressure is, the higher the pressure tends to be between the offtake passage (12), with the effect of reducing or increasing such pressure till it is carried to the desired value and to maintain it equal to such value. In accordance to the illustration in figure 1, a portion of the container (7) is connected to a known pressure gauge element (18), which is capable of supplying a visual indication relative to the existing pressure in the intemal of the same container (7). A part of the container (7) being axially opposite with respect to the same container outlet nozzle is defined by a cap element (19), coaxially screwed on the body of the container (7) to reclose the part which is principally distanced from the extended element (4). It should be noted that, in alternative, the container (7), may be equiped at any of its points with an opening (not represented) being sealable through a removable tap (not represented). A circular bottom wall (20) of the cap element (19) is equipped with a coaxial circular opening (21), to which a pump element is connected, as indicated in its complex by (22). Said pump element (22) comprising of a cylindric element (23) being partially inserted in the (19) coaxially integral cap element, with its median zone at the mentioned opening(21); within such cylindric element, a smooth sliding piston element is coaxially installed , to which the same cylindric element (23) is externally connected, by a handgrip (25) used to impart to the piston element (24) a convenient number of strokes in the two directions within the cylindric element (23) with the objective of letting into the container (7) higher air pressure than the atmospheric pressure. A known type of non-return valve (26), represented in figure 4 and essentially comprising a small ball (27) and a helicoidal spring (28) able to drive the same small ball (27) and a helicoidal spring against a matching surface of the cylindric element (23), is associated at the end of the same cylindric element (23) placed within the cap element (19). The mentioned containers (5) and (7) are both connected, in correspondence to the respective zones, and conveniently distanced from the extended element (4), by a strip element (29) which encloses and renders them substantially intesral between them. According to what is represented in the figures 1 and 3, in a horizontal threaded hole (30) obtained in a superior part of the handgrip (3) an end portion of the plug element (31) is screwed on. Such plug element by means of a helicoidal spring (32) functioning by compression is placed within the said hole (30) axially pushing an essentially cylindric element (33) to the free end of the hole (30). Coaxially connected to the free end of such element (33) is a liquidtight first conduit or tubular element (34), which extends beyond the free end of the extended element (4) and is coaxially enclosed, starting from an essentially coinciding zone with the free end of the same extended element (4), by a second conduit or tubular element (35), one of which end portion is supported by the free end of the same extended element (4). A portion of the extended element (4) above the handgrip (3) supports, by means of a horizontal pin (36), in a rotating manner, a superior end of a trigger element (37), of which an intermediate portion borders and binds, in a knovvΗ and not represented method, the end of the element (33) turned towards the free end of the extended element (4): when the lower portion of the handgrip element (37) is moved manually towards the plug element (31), the (33) element and the tubular element (34) are axially dragged towards the same plug element (31), with the following consequences which will result clear. The screw element of the plug element (31) determines the force with which the handgrip element (37) resists to the manual traction towards the same plug element (31). In accordance to what is represented, in particular, in figures 3 and 5, the output nozzle of the container (7), communicates with a conduit (38) obtained in the extended element (4), which in turn communicates with a toriodal chamber (39) obtained on the external peripheral surface of a hollow cylindric element coaxially housed within a cylindric cavity (41) of the same extended element (4). Such hollow cylindric element (40) houses the mentioned cylindric element (34), in a sliding manner with a modest gap, within its' internal cavity (42), and it is connected to the extended element (4) in a stable manner by means of two threaded arrest elements (43) (only partially illustrated in figure 5) which borders the axial ends. The intemal cavity (42) of the hollow cylindric element (40) is concerned with a toroidal chamber (44), which encloses a portion of the tubular element (34) equipped with a radial hole (45). The toroidal chambers (39) and (44) are both connected by an essentially conic shaft hole, within which it can bind in variable measures the conic shaft end (47) of a half obstruction made up of a screw element (48) screwed in a threaded hole obtained in the extended element (4). A higher or lower screwing of the external thread element (48) corresponds to a higher or lower obstruction of the hole (46) from the end part (47) of the same screw element (48), with a consequent lower or higher free flow of the liquid housed in the container (7) from the conduit (38) to the toroidal chamber (44). An essentially completed screwing of the external thread element (48), represented in figure 5, corresponds to the elimination of the communication between the conduit (38) and the toroidal chamber (44), and therefore of the container (7) with the intemal cavity of the tubular element (34). In consequence of what has been said, the end (47) of the screw element (48) and the hole (46) constitute regulating means of the rate of flow of the hardening substance coming from the container (7). According to what has been represented, in particular, in figure 3, the outlet nozzle of the container (5) comunicates with a conduit (49) obtained in the extended element (4), which comunicates in turn with the liquidtight end of the tubular element (35) connected to the same extended element (4). In accordance to the representation in figure (7), the free end (50) of the tubular element (34) internally presents an essentially truncated cone form with the crest arranged on the outside of the same tubular element (34); the end (51) of the tubular element (35) externally presents a substantially truncated cone form, able to follow axial movements of the tubular elements (34) of which it can be said, as follows, to conjugate itself in a liquidtight manner with the (50) essentially tmncated cone end of the tubular element (34). In use, the device (1) could be used to deliver the monomeric substance contained within the container (5) without adding any hardening substance to the same monomeric substance. In such case, the container (7) may not not be filled with water or other hardening substance; in alternative, the container (7) could contain the hardening substance, but the screw element (48) could be arranged in its' highest screwed condition, with consequent impossible passage of the same hardening substance from the toroidal chamber (39) to the toroidal chamber (44) and from the latter to the intemal tubular element cavity (34). The emission of the monomeric substance for the device (1) occurs in consequence of a stoppage effected manually, of the lower portion of the trigger element (37); at such stoppage, as previously mentioned, follows a traverse of the tubular element (34) towards the handgrip (3), with consequent distancing of the end (50) of the same tubular element (34) from mentioned end (51) of the tubular element (35), and consequent free outflow, between the same two ends (50) and (51), of the monomer coming from the container (5) through the intemal cavity of the tubular element (35). The mentioned ends (50) and (51), therefore, act on obstructing means able to regulate the outflow of the monomeric substance housed within the container (5). Such monomer, as soon as it discharges from the device (1), it begins to polimerize even in absence of the added hardening substance, for example, due to the contact with the air humidity, it completes the polimerization in a relatively long time. In the case in which one desires to add to the mentioned monomer a hardening substance in a liquid form, it is necessary to fill the container (7) at least partially with such hardening substance. Such filling, in accordance to what has been previously mentioned and with the illustration represented in figure 1, is effected by removing, by means of screwing off the mentioned cap element (19) from the body of the container (7). The cap element (19) is then reapplied to the container body (7), and the pump element (22) is repeatedly actuated, acting on the handgrip (3), to generate in the internal of the same container (7), a higher pressure to the atmospheric pressure. The pressure gauge (18) element indicates the value of such pressure, and permits value verification at any moment during device use (1). During such operations, and more generally, while the trigger element (37) is not actuated, the tubular element (34) is positioned, under the action of the spring (32), in its' maximum forward position towards the end (51) of the tubular element (35). In such conditions, the mentioned hole (45) is found outside the toroidal chamber (44), and is not in a condition to receive liquid from the container (7). The hollow cylindric element (40) and the hole (45), as a consequence of the aforementioned, act as a obstructing means able to regulate the influx, within the tubular element (34) of the hardening substance housed within the container (7). As soon as the lower portion of the trigger element (37) is pulled back, the tubular element (34) is moved to a certain tract towards the handgrip (3), as mentioned, allowing the free passage of the monomer coming from the container (5) between the mentioned ends (50) and (51) and carrying the hole (45) within the toroidal chamber (44). In the case in which the screw element (48) does not obstruct the hole (46), the liquid contained in the container (7) begins to flow from the same contianer (7) towards the toroidal chamber (39) to then enter into the toroidal chamber (44) and pass from it, across the hole (45), into the intemal cavity of the tubular element (34) ; from said tubular element (34), finally, the liquid flows in the external environment, immediately after being mixed , essentially in correspondence to the said ends (50) and (51), with the monomeric substances coming from the container (5). The rate of flow of the hardening substance coming from the container (7) can be regulated at any moment, by acting on the screw element (17) of the pressure governor device (6) and/or on the mentioned screw element (48), such regulation can be effected without any restraint on the rate of flow of the monomer coming from the container (5) It is important to note that, according to a variant which is not illustrated in the present invention, the described container (7) could be substituted by a prepacked pressurised bottle containing a hardening substance, constituted, for example by water; obviously, in this case, such a bottle would not be used with the described pump element (22) and the hardening substance, especially in this case, could be nebulized towards the monomer in outflow from the tubular element (35) with a dispersive "crown" effect, that is to say, through an expansion which carries the same hardening substance to gradually draw away from both the tubular element end (35) and the axis of the terminal portion of the same tubular element (35). Moreover, it should be noted that, according to a variant not illustrated in device (1), the container (7) could present in its intemal a pressure equal to the atmospheric pressure, and the hardening substance contained therein could reach the toroidal chamber (44) simply under the action of the force of gravity. Furthermore, it should be noted that, the mixing of said monomer with the hardening substance could be effected in a different zone to that described, in an obvious way for the technical expert in this sector, in view of what has been previously said, and this is in a zone distanced form the said ends (50) and (51) or immediately on the outside of the tubular element (35); in particular, the tubular elements (34) and (35) could be shaped and reciprocally arranged in such a way as to assist the hardening substance extraction out of the tubular element (34) on the part of the outflowing monomer from the tubular element (35), by the depression and or in virtue of the moving effect due to the outflow speed difference of the products outflowing from the same tubular elements (34) and (35). Finally, it should be noted that, the described device 1, completely achieves the prefixed objectives, from the moment in which it allows the use of only the necessary quantity of the monomeric substance each time, without prejudicing at all the characteristics of the substance which temporarily remains unused in the container. Moreover, the described device 1, is able to , with the aim of permitting the user to choose whether the polimerization of the said monomer must occur in a short time or can occur in a relativly long period of time, to deliver only the monomeric substance housed in the container (5),or to mix a hardening substance to the same monomeric substance housed in the container (7).

Claims: CLAIMS 1. The polymeric substance extmsion method, being characterized by the fact of including the phases of determining the outflow, from a first container (5) of a monomeric substance able to autonomally polymerize upon air contact; and eventually to determine, the second container outflow (7) of a hardening substance able to accelerate the polymerization of the said monomeric substance, sending the same hardening substance towards a mixing zone of the hardening substance with the same monomeric substance. 2. The polymeric substance extmsion method according to claim 1, characterized by the fact of including the outflow regulating phase of said hardening substance. 3. The polymeric substance extmsion method according to claim 1 or 2, characterized by the fact of including the further phase of pumping air pressure superior to the atmospheric pressure within the said second container (7). 4. The polymeric substance extrusion method according to claim 1 or 2, characterized by the fact that the said second container (7) is constituted by a bottle containing the said hardening substance at a higher pressure to that of the atmospheric pressure. 5. The polymeric substance extmsion method according to any of the claims from 1 to 4 characterized by the fact of including the pressure regulating phase of the said hardening substance. 6. The polymeric substance extrusion method according to any of the claims from 1 to 5, characterized by the fact that both tubular elements ends (35 & 34) of respective outflow of the said monomeric substance and said hardening substance, are essentially situtated next to the said mixing zone. 7. The polymeric substance extmsion method according to claim 6, characterized by the fact that the said tubular elements (34 & 35) are coaxial. 8. The polymeric substance extmsion method according to any of the claims 1,2.6 when dependent on the claims 1 or 2 or 7, characterized by the fact that the said second container (7) internally presents a pressure which is essentially equal to the atmospheric pressure, the said hardening substance reaching the said mixing zone under the effect of the force of gravity. 9. The polymeric substance extmsion method according to the claim 6 or 7, characterized by the fact that the said tubular elements (34 and 35) are shaped and reciprocally arranged in such a way as to facilitate the extraction of the said hardening substance from the relative tubular element (34) from the part of the monomeric substance outflow from the relative tubular element (35) by depression and/or in virtue of the pulling effect due to the outflow speed difference of the outflowing substances from the same tubular elements (34 & 35). 10. The polymeric substance extmsion method according to any claim from 1 to 9, characterized by the fact that, in operation, the said second container (7) can be empty. 11. The polymeric substance extrusion method according to any claim from 1 to 9, characterized by the fact that, in operation, the rate of flow of said hardening substance, can be nil. 12. The polymeric substance extmsion method according to any of the claims from 6 to 1 1, characterized by the fact that the said hardening substance is nebulized towards the said monomeric substance in output from the said relative tubular element (35) with a dispersive "crown" effect . 13. The polymeric substance extmsion device characterized by the fact of comprising a first container (5) housing a monomeric substance internally, able to autonomously polymerize once in air contact, a second container (7) suitable for housing a monomeric substance internally, able to accelerate the polymerization of said monomeric substance , a first conduit (35) suitable to conduct the said monomeric substance towards the output station of the same monomeric substance of the said device 1, and a second conduit (34) suitable to conduct the eventually outflowing hardening substance from the said second container (7) towards a mixing zone of the same hardening substance with the said monomeric substance; the first obstruction means foreseen (50 & 51) suitable to determine, on command, the outflow of the said monomeric substance from said device 1. and second obstruction means (40, 45, 48) suitable to determine , on command, the sending of the hardening substance eventually present within the said second container (7) towards the said mixing zone. 14. The polymeric substance extmsion device according to the claim 13, characterized by the fact of comprising the rate of flow regulating means (46 & 47) of the said hardening substance interposed between the said second container (7) and the said mixing zone. 15. The polymeric substance extmsion device according to the claims 13 or 14, characterized by the fact of comprising regulating means (6) of the pressure of said hardening substance interposed between the said second container (7) and the said mixing zone. 16. The polymeric substance extmsion device according to any of the claims from 13 to 15, characterized by the fact that both ends (50,51) of two tubular elements (34,35) respectively defined as said second and first outflow conduit of the said respective monomeric substance and said hardening substance are essentially situated next to the said mixing zone. 17. The polymeric substance extmsion device according to claim 16, characterized by the fact that said tubular elements (34,35) are coaxial. 18. The polymeric substance extmsion device according to any claims from 13 to 17, characterized by the fact of including measuring means (18) of said hardening substance pressure. 19. The polymeric substance extrusion device according to any claim from 13 to 18, characterized by the fact of containing pump means (22) for the immission, in operation, of air pressure superior to the atmospheric pressure within the said second container (7). 20. The polymeric substance extmsion device according to any claim from 13 to 18, characterized by the fact that the said second container (7) is made up of a bottle containing the said hardening substance with pressure superior to atmospheric pressure. 21. The polymeric substance extmsion device according to the claims 19 or 20, characterized by the fact that the said hardening substance is nebulized towards the said monomeric substance in output from the relative said tubular element (35) with the dispersive "crown" effect. 22. The polymeric substance extmsion device according to any claims from 13 to 19, characterized by the fact that, in operation, the said second container (7) may be empty. 23. The polymeric substance extrusion device according to any claims from 14 to 21, characterized by the fact that the said rate of flow regulating means (46, 47) are suitable to render the rate of flow of said hardening substance nil. 24. The polymeric substance extrusion method is essentially as described with reference to the figures of annexed designs. 25. The polymeric substance extrusion device is essentially as described with reference to the figures of annexed designs.

Inventors: PLASMATI-LUECHINGER MARIA TERE, PLASMATI-LUECHINGER, MARIA, TERESA
Applicants: CHEMING AG, PLASMATI LUECHINGER MARIA TERE, PLASMATI-LUECHINGER, MARIA, TERESA
Application year: 1998
Main classification: B29B7
IPC codes: B29B7