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DETAILED DESCRIPTION OF THE INVENTION

A METHOD OF PRODUCING PLASTIC BAGS tions of layers of film may cross each other during the

.,.ir. ~- TM„„ ... time the resin is extruded. A resin-feeding opening of

BACKGROUND OF THE INVENTION one of ^ djes Js communicated with an extruding ma

It is well known that when heated plastic resin is ex- chine for supplying with low-heat-plastic resin, and the

panded, the material is apt to be oriented in the direc- 5 rotation of this die is stopped when the resin is ex

tion of being stretched to increase its tensile strength truded. The other two resin-feeding openings of the

toward the orientation, so that in case the material is other dies are respectively communicated with one or

stretched in both directions of length and breadth at two extruding machines which is or are supplied with

the same co-efficient of stretch, the strength of the ma- similar or different kinds of heat-plastic-resin. The

terial tends to be increased in any directions. 10 three annular dies are assembled with the annular inner

The packing bags made of polyethylene of low den- die inserted in a space of a middle annular die which in

sity of molecules, for packing heavy fertilizer, are man- turn is inserted in a space of the other annular die.

ufactured by the "method of inflation" which makes a Before the film is pressed and flattened, two kinds of

cylindrical film. For example, to make a bag for fertil- resin are extruded so as to form two kinds of bubbles

izer of 25 Kg., a cylindrical film of 450 to 500 mm in 15 through annular gaps of outer and inner annular dies,

diameter and 0.2 mm in thickness is formed by an an- and both bubbles are formed in cylindrical bubbles,

nular die having a slit whose diameter is 250 mm and both of which are contacted by the method of inflation,

its width is 1.00 mm. The co-efficient of the lengthwise The bubble at the outer side is cooled by a cooling me

stretch of the cylindrical film is 1.0 mm/0.2 mm = 5, dium to a certain degree while the inner one may not

while that of transverse stretch of the film is 2 X (450 20 become solidified. The two kinds of resin are extruded

to 500)mm/3 X 250 -M .3. by the rotation of the annular die for outer layer of film.

Accordingly, it is clear that the former is larger than In a space of the rotatable annular die for the outer the latter, namely, the lengthwise stretch is about four layer of film, another annular die for the inner layer of times as great as the transverse one. For the purpose of film is inserted, of which resin-feeding opening is cornincreasing the transverse stretch of the flattened cylin- 25 municated with an extruding machine in which lowdrical film, it is necessary to form such a film of 0.2 mm heat-plastic resin is supplied, while the annular die for in thickness, by welding two cylindrical films cross- the outer layer of film is also provided with a resinwisely. Thus formed stratified film is well known to be feeding opening which is communicated with an other strong enough for packing any kind of heavy materials. extruding machine in which another kind of heat

30 plastic-resin is supplied.

To manufacture above mentioned strong bags several troublesome steps are necessary such as gluing two flattened cylindrical films crossing in lengthwise directions For a more particular description of the invention, to each other with paste; cutting the films in desired reference is to be had to the accompanying drawings, length; folding back the cut film along its center line; 35 forming a part thereof, in which: sticking the edges opposite the center line so as to form FIG. 1 is a perspective view illustrating stratified film a tube; and forming a bottom to make a bag from the formed by an embodiment of the invention, tube. For the purpose of utilization of the method, our FIG. 2 is a vertical cross sectional view of the apparainvention is to provide a novel method and apparatus. tus for manufacturing the stratified film illustrated in

FIG. 1.

FIG. 3A and FIG. 3B are respectively illustrating dynamically the stretching directions of inner and outer

The object of the invention is to provide a method for layers forming the stratified film shown in FIG. 1.

manufacturing flatten cylindrical film of heat-plastic FIG. 4 is a vertical cross sectional view of another

resin in layers stretched and stuck one over the other. 45 embodiment of the invention for manufacturing the

Before the cylindrical films are flattened and stuck to- stratified film.

gether a bubble of melted plastic resin is expanded by In an example (1) of the first embodiment, polyethylthe "method of inflation" so that the layers of film may ene of high density of molecules is supplied to an exbe contacted or welded with each other. The bubbles truding machine (not shown in drawings) having two are extruded concentrically through annular gaps discharging openings for melted resin with which, the formed between two annular dies when one of the dies apparatus of the invention is communicated, rotates or both dies rotate in reverse directions. As shown in FIG. 2, inside of an annular outer die II One die is inserted in a space of another die and each for forming film of an outer layer is provided a space die is provided with a feeding opening for melted resin 5J into which an annular inner die I for forming film of an and communicated with an extruding machine having inner layer is inserted so as to rotate in reverse directwo extruding openings for the same kind of material, tions with each other.

or communicated with two extruding machines for the To the top of an inner shaft 1 of the inner die I, an different kinds of materials. inner member 2 is fixed, around of which is provided Another object of the invention is to provide for 6Q an inner cylinder 3, to the lower portion of which a gear manufacturing flattened cylindrical film of heat-plastic wheel 4 is fixed which is driven through a chain 5 by a resin in layers stretched and connected one over the driving means 6 so as to rotate the inner die I for formother. Before the cylindrical films are flattened bubbles ing film of an inner layer, which inner disc comprises of melted plastic resin are expanded by the "method of the inner member 2 and the inner cylinder 3. To the inflation" so that the layers of film may be contacted 65 bottom of the cylinder 3 is fitted, through a packing 7, or welded with each other. The bubbles are extruded a feeding means 8 for introducing resin. Between the through each annular gap formed in three annular dies, feeding opening 8 and the inner cylinder 3 is arranged two of which are rotated so that the stretched direc- a bearing 9 for rotation. Melted resin supplied from an

40

SUMMARY OF THE INVENTION

3

extruding machine is extruded out of an upper annular gap 12 through the stationary feeding opening 8, a guide aperture 10 which is formed along the axis of the inner cylinder 3 and a guide gap 11 formed between the cylinder 3 and the inner member 2. The fixed feeding opening 8 is provided with an air-tube 13 which is centrally through the inner die I and through the guide aperture 10 and along the axes of the inner shaft and inner member 2.

In the annular outer die II for forming film of an outer layer, around an outer member 14 is provided with an outer cylinder 15 to which a gear wheel 16 is fixed which is driven by a driving means 17 so that the outer die II may be rotated.

With the bottom of the outer member 14 and of the outer cylinder 15 is fitted through a packing 18 a fixed feeding opening 19 for feeding-resin. Between the inner cylinder 3 and the outer member 14 is provided a bearing 20 for supporting the outer die II. Melted resin is extruded out of an upper annular gap 22 through the feeding opening 19 and a guide gap 21 which is formed between the outer cylinder 15 and the outer member 14.

For the purpose of manufacturing the stratified cylindrical film F, feeding openings 8, 19 for feeding resin, of the dies I, II for forming cylindrical stratified film, are communicated with two openings for extruding resin, of the extruding machine. To determine the thickness of film, a proper speed (a) to pull out the film is chosen in accordance with the diameters and the widths of gaps 12, 22 of the dies I, II respectively and by the diameter of screw of the extruding machine. And the air is blown into the air tube 13 by which the diameter of the cylindrical film is made as desired. In case the dies I, II are rotated in reverse directions at the same speed (b) as the speed (a) of pulling out the film by the driving means 6, 17 through the gear wheels 4, 16 fixed to the outer walls of the outer cylinders 3, 15 respectively, the resin extruded from the gap 12 is stretched in the direction (c) at an angle of 45° in rela

4

is crossed. The inner bubble 23 is expanded to a certain size of desired diameter by the air blown thereinto through the air tube 13, so that the outer bubble 24 is pressed outwardly to be also expanded and welded con5 centrically with the outer bubble without leaving any space therebetween so as to form a sheet of stratified film F which seems just like a conventional film of single layer.

In another example 2 of the first embodiment, poly10 ethylene of high density of molecules is supplied by one > extruding machine of which the extruding opening is communicated with the fixed feeding opening 8 of the inner die I for forming the stratified cylindrical film, while polypropylene is supplied by an other extruding • 5 machine of which the extruding opening is communicated with the fixed feeding opening 19 of the outer die II. Similarly to the example 1, the resin of polypropylene extruded in the direction at an angle of 45° in relation to the vertical line of the graph, is formed for an 20 outer layer of film and the resin of polyethylene of high density stretched crosswisely with the outer layer, is formed for inner layer of film so as to be contacted concentrically with each other to make the stratified film (F).

25 In another example 3 of the first embodiment, polyethylene of high density of molecules is supplied by one extruding machine to be extruded through the gap 12 of the inner die I which is held stationarily, so that the material is stretched only in the vertical direction of

30 pulling out, while polypropylene is supplied to the other extruding machine to be extruded through the slit 22 of the outer die II which is rotated in a high speed so that the resin may be stretched in the direction at an angle of 80° in relation to the vertical line of the graph

35 so as to be crossed with the vertically stretched inner layer of film and to form the stratified film (F).

The following list shows the examined values of each product manufactured by the method in two cases of producing a sheet of startified film having a similar

40 thickness of both inner and outer layers of 0.06 mm, comparing the substantial characteristics of each.

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