Patent Grant
7077933
This application is a 371 of application PCT/JP01/01465 filed 27 Feb. 2001.
This application is based upon and claims the benefit of priority under 35 U.s.c. §120 from application No. PCT/JP01/01465, filed Feb. 27, 2001, and under 35 U.S.C. §119 from Japanese Patent Application No. 2000-056537, filed Mar. 1, 2000.
The present invention relates to a pulp molded article which has a threaded part and assures a good seal with a cap. More particularly, it relates to a pulp molded article with a threaded part which part is an accurate reproduction of a molding surface of a mold. The present invention also relates to a method of producing the pulp molded article.
Pulp containers with a threaded part which are prepared by forming a thread on a paper cylinder by a calender press are known. However, the shapes of the threads and containers formed by a calender press are limited in nature of the method adopted only to provide a poor seal with a cap, allowing the contents to leak during use. In addition, the paper cylinder itself is not strong enough to assure durability for repeated capping and uncapping.
JP-A-8-302600 discloses a pulp molded article having on its surface a projection such as a thread. The projection is attached with an adhesive, etc. in a separate step or formed in the step of drying a molded article. The method of forming a projection in the step of drying is advantageous for efficient production of molded articles since the step of making a projection and the step of attaching the projection are carried out on the same molding line. Where a projection is formed in a drying step, however, cases are met with, while depending on the shape of the projection, in which the depression on the molding surface of a mold is not accurately transferred only to make a rounded projection or a projection with a rough surface, or the resulting projection fails to have an increased density for securing sufficient strength.
Accordingly, an object of the present invention is to provide a pulp molded article with a threaded part which assures a good seal with a cap.
Another object of the present invention is to provide a pulp molded article with a threaded part which has high durability for repeated capping and uncapping.
Still another object of the present invention is to provide a pulp molded article with a threaded part which part is an accurate reproduction of a depression on the molding surface of a mold and has sufficient strength.
The present invention accomplishes the above objects by providing a pulp molded article comprising a neck portion and a thread provided on an outer surface of the neck portion, and having an overrun torque of 1 N·m or higher between the neck portion and a threaded cap screwed on the neck portion.
The present invention provides a preferred method for producing a pulp molded article having a thread at the neck portion thereof. In the method of the present invention, a papermaking mold having a threaded part at the region corresponding to the neck portion of the above pulp molded article is employed. The method comprises the step of papermaking with the above papermaking mold to form a pulp molded article comprising a neck portion and a thread provided on the outer surface of the neck portion.
a) shows the step of pouring a pulp slurry;
a) shows the step of inserting a pressing member.
The present invention will be described based on its preferred embodiments with reference to the accompanying drawings.
The molded articles 1 and 1′ form right angles between their bodies 3 and 3′ and bottoms 4 and 4′. That is, the bodies 3 and 3′ have a taper angle of 0°. The molded articles 1 and 1′ are at least 50 mm high, preferably at least 100 mm high. For some uses of the molded articles 1 and 1′, the bodies 3 and 3′ do not need to make right angles with their bottoms 4 and 4′.
The molded articles 1 and 1′ have no seams nor thicker-walled parts which might have resulted from joining and therefore ensure sufficient strength and a good appearance.
In the molded article 1 shown in
In the molded article 1 shown in
The molded articles 1 and 1′ are made mainly of pulp. They can be made solely of pulp. Where pulp is used in combination with other materials, the proportion of the other materials is preferably 1 to 70% by weight, still preferably 5 to 50% by weight. Other materials that can be used include inorganic substances such as talc and kaolinite, inorganic fibers such as glass fiber and carbon fiber, powder or fiber of synthetic resins such as polyolefins, non-wood or vegetable fibers, and polysaccharides.
The second neck portion 2b of the molded article 1 shown in
The contour of the thread 5 (5′) may be trapezoidal, triangular, squared, rounded, etc. A proper thread contour is chosen according to the strength of the neck 2 (2′) and productivity of the molded article 1 (1′) (e.g., drying capability or shaping capability of the thread 5 (5′)). For example, a rounded thread or a triangular thread is preferred where ease of screwing a cap on and off is of importance or where a cap is screwed on and off frequently. A trapezoidal thread is preferred where a cap is screwed tight with a great torque, where a cap is required to hardly loosen, or where a cap is required to be hardly pulled out. The threads used in the molded articles I and 1′ are trapezoidal threads whose contour is a trapezoid as shown in
With a threaded cap screwed on the neck 2 (2′) of the molded article 1 (1′), the overrun torque exerted between the neck 2 (2′) and the cap is 1N·m or more, preferably 1.2 N·m or more, still preferably 5 N·m or more. Such designing provides a good seal of the neck 2 (2′) with the cap so that the cap hardly loosens even by vibrations during transportation, effectively preventing leakage of the contents contained in the molded article 1 (1′). In particular, the molded article 1 shown in
It is preferred for the profile of the threads 5 and 5′ to satisfy relationships (1) and (2) or (3) shown below, taking the length of the contour line of the thread observed via a cross-section along its width direction as S (mm), the width of the thread as viewed via a plan as W (mm), and the thickness of the molded articles 1 and 1′ (the thickness of the neck in the present embodiment) as t (mm) as illustrated in FIG. 5.
1<S/W≦1.5 (1)
0<W≦10 t (mm) (2)
0<W≦10 mm (3)
If S/W in relationship (1) exceeds 1.5, the thread 5 is liable to be broken during dewatering or drying, or the thread 5 (5′) tends to fail to have a smooth surface or an increased density. If W exceeds 10 t (mm) or 10 mm in relationships (2) or (3), it is not easy to accumulate pulp fiber along the depression of a papermaking mold from the viewpoint of available space, considering that a papermaking net is fitted on the papermaking mold. Further, it is not easy to put the preform taken out of the papermaking mold into a heating mold with a good registration.
Relationship (1) is preferably represented by relationship (1′) in order to accurately form thread 5 (5′) in conformity to the depression of a mold, to prevent the thread 5 (5′) from being broken, to improve the surface smoothness of the thread 5 (5′), or to increase the density of the thread 5 (5′).
1<S/W≦1.3 (1′)
In the present embodiment the width W of the thread (i.e., the length of the bottom side of the trapezoid) is preferably 0.5 to 10 mm, still preferably 2 to 6 mm, for exerting a sufficient clamping force and enjoying freedom of design (e.g., size and shape) of the molded article 1.
The thickness t (mm) of the molded article 1 (1′) (i.e., the thickness of the neck 2 (2′)) is determined appropriately according to the use, etc. of the molded article 1 (1′) but, in general, preferably ranges from 0.2 to 10 mm, particularly 0.4 to 2 mm. Within this range, the neck 2 (2′) will make a better seal with a cap, and durability against frequent opening and closing will be improved further.
The flank angle θ of the thread 5′ (see
If the flank angle exceeds 90°, shaping by expansion of a pressing member hereinafter described is insufficient, and pressing of the preform by the pressing member is insufficient.
Corners 5a (see
The height H of the thread 5 (5′) from the base plane B is appropriately determined taking into account ease of molding the thread 5 (5′), the clamping force between the thread 5 (5′) and the cap, etc. In general, the thread 5 (5′) preferably has a height H of 0.3 mm or more, particularly 0.3 to 10 mm, especially 0.5 to 4 mm, for producing a sufficient clamping force and assuring ease of opening and closing.
While pulp molded articles having a threaded part of the above-mentioned shape and dimensions have been difficult to produce by conventional methods, they can be produced easily by the preferred method described hereunder.
The effective number of turns of the threaded part is preferably 0.75 or more. With an effective number of turns less than 0.75, a cap screwed on has reduced pull-out strength and a reduced clamping force, tending to fail to provide a sufficient seal. Further, with this preferred effective number of turns, the difference between clamping torque in screwing a cap on the neck 2 (2′) and opening torque in screwing the cap off the neck is smaller than that obtained with the neck of a plastic container and a plastic cap measured under the same conditions (as to, for example, the shape and dimensions of the container and the cap). In short, so-called loss of torque is smaller. This means that a cap screwed on a pulp molded container even with a small clamping torque hardly becomes loose and that a pulp molded container can be sealed with a cap with a smaller force without spilling the contents thereby assuring safety as compared with a plastic container.
For obtaining a good seal by screw cap engagement and securing thread durability, the threads per inch as measured according to JIS basic dimensions is preferably 2 to 64/25.4 mm, still preferably 4 to 12/25.4 mm. While an increased number of threads could provide an improved seal, too many turns for clamping reduces convenience in screwing a cap on and off.
Screw blocking projections 6 are provided near the junction between the second neck portion 2b and the second step 7b of the molded article 1 shown in
It is preferred for the neck 2 (2′) inclusive of the thread 5 (5′) to have a center-line average roughness Ra (JIS B0601) of 50 μm or less, particularly 25 μm or less, especially 10 μm or less, which favors a better seal of the neck 2 (2′) with a cap. The neck 2 (2′) with such surface smoothness can be formed by, for example, a prescribed polishing processing technique, but the production method hereinafter described is successful in making the neck 2 (2′) with high smoothness without involving such polishing. The smaller the center-line average roughness, the better the seal of the neck 2 (2′) with a cap. A minimum center-line average roughness that could be achievable by the state-of-the-art techniques is about 0.1 μm. For the same reason, the largest height Ry (JIS B0601) of the neck 2 (2′) inclusive of the thread 5 (5′) is preferably 500 μm or less.
The neck 2 (2′) inclusive of the thread 5 (5′) preferably has a wax pick grade of 5A or higher, particularly 10A or higher, especially 16A or higher, which is a measure of surface strength characteristics (resistance to picking, resistance to fiber rising during use, and resistance to strength reduction of the neck) measured according to the wax pick method (JIS P8129). With this preferred surface strength, the neck exhibits improved durability against repeated capping and uncapping so that pulp fiber rising, surface picking, paper dust fall-off, and like surface disturbances can be prevented to maintain the appearance of the molded article 1 (1′).
In order to obtain the above-recited surface hardness as graded by the wax pick method, a method by adding a synthetic resin or a natural resin either externally or internally can be adopted. Methods of externally adding the resin include laminating the neck 2 (2′) inclusive of the thread 5 (5′) with a resin film, coating the neck 2 (2′) with a resin liquid, and impregnating the neck 2 (2′) with a resin liquid, and the like. Methods of internally adding the resin include previous addition of a resin to a pulp slurry as a stock for making the molding article 1 (1′). The resin film includes polyolefin films and polyester films, with polyester shrinkable films being preferred. The resin liquids which can be used for coating or impregnation or the resins which can be previously added to a pulp slurry include liquids containing acrylic resins, styrene resins, polyester resins, polyolefin resins, synthetic rubber resins, vinyl acetate resins, polyvinyl alcohol resins, wax resins, polyacrylamide resins, polyamide epichlorohydrin resins, starch resins, gum resins, viscous resins, epoxy resins, melamine resins, phenolic resins, urea resins, polyurethane resins, fluorine resins, silicone resins, etc. These resin liquids may be used either individually or as a mixture of two or more thereof.
The engagement of the neck 2 (2′) of the molded article 1 (1′) with a cap is preferably such that the pull-out strength of the cap is 5 N or greater, particularly 10 N or greater, especially 20 N or greater, when the amount of engagement between the screw thread of the neck 2 (2′) and that of the cap is 0.5 mm, and the cap is given one turn. With this preferred pull-out strength, the neck 2 (2′) secures a better seal with the cap to prevent the contents in the molded article 1 (1′) from leaking more effectively. Further, even when the molded article 1 (1′) is lifted by the cap, the cap does not come off, and the contents are prevented from leaking. Similarly to the aforementioned overrun torque, the greater the pull-out strength, the better the seal between the neck 2 (2′) and the cap. The upper limit of the pull-out strength, which is sufficient for the practical use, is about 700 N, while depending on the method of producing the molded article 1 (1′), the composition of the molded article 1 (1′), and the like. The details of the method of measuring pull-out strength will be described in Examples hereinafter given.
It is preferred that the neck 2 (2′) inclusive of the thread 5 (5′) has a density of 0.4 to 2.0 g/cm3, particularly 0.6 to 1.5 g/cm3, for assuring durability and sealing properties. The density is calculated from the weight of a cut piece of arbitrary size sliced off the neck 2 (2′) and the volume of the piece measured from the size (area) and the thickness.
It is preferred for the neck 2 (2′) inclusive of the thread 5 (5′) to have a transverse compressive strength of 20 N or higher, particularly 30 N or higher, for preventing the neck 2 (2′) from being buckled. The upper limit of the transverse compressive strength, which is sufficient for practical use, is about 500N. For the same effect, it is preferred for the neck 2 (2′) to have a vertical compressive strength of 100 N or higher, particularly 300 N or higher. The upper limit of the vertical compressive strength, which is sufficient for practical use, is about 700N. These compressive strengths are measured by using a Tensilon tensile tester at a compression rate of 20 mm/min. It is preferred for the neck 2 (2′) to have such drop strength that it does not develop a crack or deformation when dropped once from a height of 1.2 m (JIS Z1703). In measuring the drop strength, the molded article 1 (1′) is dropped to land on its neck 2 (2′).
It is preferred for the neck 2 (2′) inclusive of the thread 5 (5′) to have a water vapor transmission rate (JIS Z0208) of 100 g/(m2·24 hrs) or lower, particularly 50 g/(m2·24 hrs) or lower, for assuring preservability of the contents, for example, for preventing a powdered detergent from absorbing moisture and caking.
It is preferred for the molded article 1 (1′) according to the present embodiment to have a vertical compressive strength of 100 N or higher, particularly 300 N or higher, for preventing the molded article 1 (1′) from being buckled. The upper limit of the vertical compressive strength, which is sufficient for practical use, is about 700 N. The vertical compressive strength is measured in the same manner as described above. It is preferred for the molded article 1 (1′) to have such drop strength that it does not develop a crack or deformation when dropped once from a height of 1.2 m (JIS Z1703) to land on its base, neck or side. In measuring the drop strength, the molded article 1 (1′) is filled with contents (basically full of water, or filled with a prescribed amount of a commercially available product), and the neck 2 (2′) is sealed with a cap.
The preferred method of producing a molded article according to the present invention will then be described with particular reference to the production of the molded article 1′ shown in
According to the method, a papermaking mold having a threaded part in the portion mating with the threaded part of a molded article 1′ is used to make a molded article 1′ having a threaded part on the outer side of the neck 2′.
In more detail, a papermaking mold 10 is prepared. The papermaking mold 10 is made up of two splits 11 and 11, the splits providing a cavity 12 of prescribed shape on joining. The papermaking mold 10 has a thread 16 on its cavity wall in the portion mating with the thread 5′ of the molded article 1′ (hereinafter referred to as a mating thread 16). It is desirable for the mating thread 16 to satisfy relationships (4) and (5) described later.
The cavity 12 of the papermaking mold 10 is connected to the outside via a slurry pouring gate 15 open to the outside. The inner side of the cavity 12 is covered with papermaking net having a prescribed mesh size (not shown). Each split 11 has a plurality of interconnecting passageways 13 which connect the inside (i.e., the inner surface of the cavity 12) to the outside. Each interconnecting passageway 13 is connected to a suction means, such as a suction pump (not shown).
In this situation, a feed nozzle 17 is inserted through the slurry pouring gate 15, and a predetermined amount of a pulp slurry is poured into the cavity 12 through the feed nozzle 17. The pulp slurry concentration is usually 0.1 to 5 % by weight. The pulp slurry is either heated or not. Specifically, the temperature of the pulp slurry can range from 0 to 90° C., preferably 10 to 70° C., still preferably 20 to 40° C. To heat the pulp sluny to an elevated temperature is preferred for increasing dewatering efficiency. Simultaneously with pouring the pulp slurry, the cavity 12 is evacuated by suction through the interconnecting passageways 13 toward the outside of the paper making mold 10, whereby the water content of the pulp slurry is sucked up, and pulp fiber is built up on the papermaking net covering the inner wall of the cavity 12. As a result, there is formed a water-containing preform 1′ as a deposit of pulp fiber on the papermaking net. A predetermined amount of water (diluent water) can be injected into the cavity 12 in the initial stage and/or the final stage of forming the preform l′ to thin the pulp slurry in the cavity 12 so as to prevent thickness unevenness of the preform 1′ effectively. The initial stage of forming is the stage when the amount of pulp having been fed into the cavity 12 is not more than 30 %, particularly not more than 20 %, of the total amount of pulp necessary for preform formation. The final stage of forming is the stage when the amount of pulp having been fed into the cavity 12 is at least 70 %, particularly 80 % or more, of the total amount of pulp necessary for preform formation. The amount of diluent water to be fed is preferably such that the concentration of the pulp slurry is reduced to 80 % or lower, particularly 20 to 60 %.
The feed nozzle 17 is used as a means for feeding the pulp slurry and also a pressurizing fluid described later. The feed nozzle 17 has a fitting plate 17a, a nozzle 17b vertically piercing the fitting plate, a three-way valve 17c attached to the upper end of the nozzle 17b, and a slurry feed pipe 17d and a pressurizing fluid feed pipe 17e both connected to the three-way valve 17c. On switching the three-way valve 17c, the nozzle 17b is connected to either the slurry feed pipe 17d or the pressurizing fluid feed pipe 17e. While the pulp slurry is being poured into the cavity 12, the nozzle 17b is connected to the slurry feed pipe 17d. The fitting plate 17a is fitted into the slurry pouring gate 15 to close the slurry pouring gate 15.
The resulting preform 1′ is subjected to a dewatering step. As shown in
Pressurizing fluids which can be used include steam and superheated steam (hereinafter inclusively referred to as steam). It is particularly preferred to use superheated steam. By blowing steam, the temperature of water present in the preform 1′ rises instantaneously by the heat transfer in condensation of steam thereby to reduce the viscosity and the surface tension of water. As a result, the water content in the preform 1′ is blown off instantaneously and very efficiently thereby achieving improved dewatering efficiency. Not relying chiefly on heat exchange, this dewatering technique is extremely energically advantageous. Moreover dewatering completes instantaneously, providing a reduction of dewatering time. Because an elastic pressing member, which is used in the heat drying step hereinafter described, is not used for dewatering, the time for mechanical operations involved in using a pressing member, such as insertion into the cavity, is omitted, resulting in a reduction of the time for mechanical operations. Further, because the blowing pressure is lower than the pressure applied in press dewatering, there is obtained an additional advantage that the papermaking net hardly leaves its marks on the surface of the resulting preform 1′ to provide a molded article with a good appearance.
Steam is preferably introduced to increase the inner pressure of the cavity 12 to 98 kPa or greater, particularly 196 kPa or greater, especially 294 kPa or greater. While better results are obtained with a higher inner pressure of the cavity 12, the upper limit of the pressure that pays is about 980 kPa because the water removal efficiency gradually approaches saturation with a pressure increase. The term “(inner) pressure in the cavity 12” as used herein means a difference between the steam pressure at the inlet and that at the outlet of the cavity 12.
It is preferable to start introducing steam while the slurry stays in the cavity 12 or while the diluent water, which has been fed into the cavity 12 in the final stage of forming the preform 1′, stays in the cavity 12, whereby the water content in the cavity 12 is expelled out of the mold to shorten the dewatering time. Steam is preferably blown for about 2 to 20 seconds, particularly about 3 to 15 seconds. Dewatering completes in an extremely short time. By this dewatering step, the preform that has had a water content of 75 to 80 % by weight before dewatering is dewatered to a water content of about 40 to 70 % by weight.
Where superheated steam is used, a sufficient degree of superheating is such that the inner pressure of the mold is increased to or above the above-specified value and that the steam is not condensed before being blown into the mold. Steam may be overheated sufficiently, but the dewatering effect is not improved correspondingly.
In addition to the above-mentioned steam, compressed air is also useful as a pressurizing fluid for dewatering the preform 1′. By blowing compressed air, a physical mechanism which does not chiefly rely on heat exchange works to remove the water content from the wet preform 1′ instantaneously. Compressed air is preferably blown to increase the pressure of the cavity 12 to 196 kPa or higher, particularly 294 kPa or higher. The upper limit of the pressure is about 1471 kPa for the same reasons as with steam. The time for blowing compressed air is preferably 10 to 60 seconds, particularly 15 to 40 seconds. The pressure (initial pressure) of compressed air is not particularly limited as long as the mold inner pressure may be increased to or above the above-recited level. The detailed description concerning steam appropriately applies to the particulars of compressed air that are not described here.
While steam and compressed air may be used individually, a combined use of both is preferred for dewatering efficiency. It is particularly preferred to introduce steam followed by compressed air for the following reason. If the steam blowing time is long, there can result a large water content variation in the vertical direction of the preform 1′. In order to avoid this, it is effective to first blow steam to sufficiently elevate the temperature of water contained in the preform and then blow compressed air. When steam and compressed air are blown in this order, steam are preferably blown at a pressure of 98 kPa or higher, particularly 196 kPa or higher, especially 294 kPa or higher, for 2 to 20 seconds, particularly 3 to 15 seconds, and compressed air is preferably blown at a pressure of 196 kPa or higher, particularly 294 kPa or higher, for 2 to 25 seconds, particularly 5 to 20 seconds. It is preferred for dewatering efficiency that blowing steam be continuously followed by blowing compressed air.
After the preform 1′ is dewatered to a prescribed water content, the feed of the pressurizing fluid is stopped, and the feed nozzle 17 is taken out of the papermaking mold 10 as shown in
The preform 1′ taken out is then subjected to the step of heat drying.
A heating mold 20 which is made up of a pair of split pieces 21 and 21 is separately prepared, the pieces 21 being joined together to form a cavity 22 having a shape in conformity to the contour of a molded article 1′ to be produced. The heating mold is previously heated to a prescribed temperature. In this embodiment, the cavity shape of the heating mold is the same as that of the papermaking mold. The water-containing preform 1′ having been dewatered to the prescribed water content is fitted into the cavity of the heated heating mold by means of a prescribed handling unit.
There is not a net on the inner surface of the cavity 22. Each of the split pieces 21 has a plurality of interconnecting passageways 23 which connect the inside thereof (the inner wall of the cavity 22) and the outside. Each interconnecting passageway 23 is connected to a suction means (not shown), such as a suction pump.
The heating mold has a thread 26 satisfying relationships (4) and (5) shown below formed on its cavity wall in the portion mating with the thread 5′ of the preform 1′ (hereinafter referred to as a mating thread).
The mating thread 26 satisfy the following relationships (4) and (5), where the length of the contour line of the mating thread observed via a cross-section along its width direction is taken as s (mm), and the width of the thread as viewed via a plane is taken as w (mm). By use of the heating mold 20 having the mating thread 26 satisfying these relationships, the thread 5′ can be formed in accurate conformity with the shape of the mating thread 26, the thread 5′ is prevented from breaking, the thread 5′ can be formed with a smooth surface, and the density of the thread 5′ is increased.
1<s/w≦1.5 (4)
0<w≦10mm (5)
It is still preferred for the mating thread 26 to satisfy relationship (4′):
1≦s/w≦1.3 (4′)
The flank angle θ′ of the mating thread 26, which is equivalent to the flank angle θ of the thread 5′ is preferably greater than 0° and smaller than 90°. The angle of the mating thread 26 facing the corner 5a of the thread 5′ (i.e., the angle made by the mold inner surface facing the base plane B of the neck 2′ of the molded article and the flank of the mating thread 26) preferably has a radius curvature R′ of 0.1 mm or more, particularly 0.3 to 5 mm.
An expandable hollow pressing member 24 is inserted in its shrunken state into the preform 1′ while evacuating the heating mold 20 as shown in
As shown in
The pressurizing fluid which can be used to expand the pressing member 24 includes air (pressurizing air), hot air (heated pressurizing air), superheated steam, oil (heated oil), and other various liquids. From the standpoint of operating convenience, it is preferable to use air, hot air or superheated steam. The pressurizing fluid is preferably fed under a pressure of 0.01 to 5 MPa, particularly 0.1 to 3 MPa.
It is effective for forming the thread 5′ with excellent sealing properties and other characteristics that the heating mold 20 has satisfactory capability of liberating air (steam generated on heating) particularly in the portion corresponding to the neck.
After the preform (molded article) 1′ has been dried sufficiently, the fluid is withdrawn from the pressing member 24, and the pressing member 24 is let to shrink and taken out as shown in
Another preferred method of producing the molded article according to the present invention will then be described. The method will be described only with regard to differences from the above-described one. The detailed description about the foregoing method appropriately applies to the same particulars The method comprises feeding a pulp slurry to a cavity of a papermaking mold composed of a set of split pieces, which are joined together to form a cavity of prescribed shape, to form a water-containing preform on the cavity wall (molding surface of the cavity), inserting an expandable hollow pressing member into the preform, and feeding a prescribed fluid into the pressing member to expand the pressing member thereby pressing the preform by the expanded preform toward the cavity wall (molding surface) to carry out dewatering.
The papermaking mold used in this method has the same structure as shown in
After the preform is dewatered to a prescribed water content, and the shape of the cavity wall is sufficiently transferred to the preform, the fluid is withdrawn from the pressing member to let the pressing member to shrink. The shrunken pressing member is removed from the preform. The papermaking mold is opened, and the wet preform having the prescribed water content is taken out by means of a prescribed handling unit. The resulting preform has a thread formed on its neck.
The preform thus taken out is then subjected to a heat drying step. The heat drying step is carried out almost in the same manner as for the aforementioned press dewatering step using a pressing member, except that papermaking and dewatering are not conducted, and a heating mold heated to a prescribed temperature is used. That is, a heating mold made up of a set of split pieces is separately prepared, the split pieces being joined together to form a cavity having a shape in conformity to the contour of a molded article to be produced. The heating mold is previously heated to a prescribed temperature. The wet preform having been dewatered to a prescribed water content is fitted into the cavity of the heated heating mold by means of a prescribed handling unit.
A pressing member which is different from that used in the press dewatering step in shape and/or material, etc. is inserted into the preform. A fluid is fed into the pressing member to expand it. The expanded pressing member presses the preform onto the cavity inner wall. The material of the pressing member and the fluid feed pressure can be the same as those used in the press dewatering step. In this state, the preform is dried by the heat. Thereafter, the same operations as in the aforementioned method are followed.
The present invention is not limited to the above-mentioned embodiments. For example, a pulp molded article satisfying relationships (1) and (2) or (3) can be produced by methods other than the aforementioned ones. For example, while in the above-described methods the screw thread is formed by completely filling the grooves of a mating thread satisfying relationships (4) and (5) with pulp fiber by pressing with a pressing member, it is possible to use a heating mold having a mating thread which satisfies relationship (5) but has deeper grooves than the mating thread used in the aforesaid embodiments. In this case, a molded article having a thread satisfying relationships (1) and (2) or (3) can be produced by appropriately adjusting the degree of pressing pulp fiber so that a thread may be formed with the grooves of the mating thread not being completely filled with pulp fiber.
The present invention will now be illustrated in greater detail by way of Examples, but it is a matter of course that the scope of the present invention is not limited thereto.
A pulp molded article was produced by the method shown in
Pulp molded articles were produced in the same manner as in Example 1 with 15 the following exception. In Example 2, the neck of the molded article was laminated with a polyester shrink film. In Example 3, the neck of the molded article was coated with an acrylic resin emulsion. In Example 4, the neck of the molded article was impregnated with a 50 wt %/50 wt % mixture of an acrylic resin emulsion and a melamine resin emulsion. In Example 5, a pulp slurry containing 30 wt % polyethylene fiber was used. The contour and dimensions of the thread on the neck of the resulting molded articles are shown in Table 1.
A paper cylinder (available from Shofudo; outer diameter: 70 mm; number of turns: 1.25; number of threads: 6.23 mm/inch; thread width: 3.5 mm) was used.
The resulting molded articles were evaluated for overrun torque, pull-out strength, center-line average roughness of the neck, surface strength of the neck by the wax pick method, and durometer hardness of the neck in accordance with the following methods. The transverse compressive strength and the density were measured according to the previously described methods. The seal between the neck and a cap and the degree of fiber rising on the neck after repeated capping and uncapping were measured by the following methods. The results obtained are shown in Table 1.
1. Overrun torque
Measurement was made with a torque gauge (Mechanical Torque Meter 2-TM75, supplied by TOHNICHI). The cap of “Wide Hiter” available from Kao Corp. was used. The cap was screwed on by hand, and the overrun torque (clamping torque) of the cap was measured.
2. Pull-out strength
A jig attachable to a tensile tester was attached to the cap. The cap was screwed on the molded article to a clamping torque of 3 N·m measured with the above-described torque gauge and pulled by the tensile tester at a speed of 20 mm/min. The force when the cap was pulled apart the molded article was measured.
3. Center-line average roughness of neck
Measured with a surface profilometer (Surfcom 120A, available from Tokyo Seimitsu Co., Ltd.).
4. Surface strength of neck by wax pick method
The surface strength was measured in accordance with JIS P8129. Wax (rated 2A to 20A) was applied by fusion to the surface of the neck and pulled off when cool. The highest number wax that did not disturb the surface of the neck was taken as a surface strength grade. A higher wax number indicates higher surface strength. However, this method is unapplicable to molded articles coated with a thermoplastic resin or impregnated with a large amount of a thermoplastic resin.
5. Durometer hardness of neck
Durometer hardness is a measure of resistance to collapse of the part under test. Here, it is used as a measure of resistance to strength reduction of the neck. Durometer hardness was measured in accordance with JIS K7215. A rubber hardness tester (GS-809 available from Teclock Corp.; Shore A type) was used. The hardness was calculated from formula (A):
100−40×h (A)
where h represents the depth (mm) of penetration.
The molded article was set vertical. The indentor of the rubber hardness tester held by hand was pressed horizontally to the outer peripheral surface of the threaded neck. The depth (mm) of penetration in one second pressing was measured. An average depth of penetration in 10 measurements (n=10) as calculated by formula (A) was taken as a durometer hardness. In case where the molded article had a thin and soft wall, the indentor was pressed onto a specimen cut out of the molded article and placed on a glass plate. If necessary, a D type tester was used, or where the test piece is too thin for measurement, a stack of several thicknesses was measured.
6. Seal between neck and cap
The molded article was filled with Wide Hiter (a trade name of a bleaching powder available from Kao Corp.), and the cap was screwed on to a clamping torque of about 1.47 N·m (15 kgf·cm) measured with the torque gauge. The molded article held upside down was given ten vertical shakings and placed on its base. The cap was screwed off, and adhesion of powder to the outer surface of the neck of the molded article, the threaded part of the inner surface of the cap, and the like was observed with the naked eye.
7. Degree of fiber rising on neck after repeated capping and uncapping
The cap was screwed on and off repeatedly, and the degree of fiber rising on the neck was observed with the naked eye.
As is apparent from the results shown in Table 1, the pulp molded articles of Examples 1 to 5 (the products of the present invention) exhibit a good seal between the neck and the cap. It is seen, in particular, that the molded articles of Examples 2 to 5 having a resin added externally or internally to their neck are prevented from being raised on their neck after repetition of capping and uncapping.
A plastic molded article of the same shape and size as the container of Example 1 was prepared. A plastic cap (the one used in Wide Hiter available from Kao Corp.) was screwed on each of the pulp molded article of Example 1 and the plastic molded article to a clamping torque of 2.0 N·m (20 kgf·cm) with the torque gauge. Immediately thereafter, the opening torque was measured.
The opening torque of the pulp molded article of Example 1 was 1.96 to 2.45 N·m, indicating a torque loss of 0.49 to 0.98 N·m (16 to 30%), whereas the opening torque of the plastic molded article was 0.98 to 1.47 N·m, indicating a torque loss of 1.47 to 1.96 N·m (50 to 66%).
The pulp molded article according to the present invention secures a good seal with a cap. The pulp molded article of the present invention exhibits improved durability against repeated capping and uncapping.
The pulp molded article of the present invention assures an accurate reproduction of the depressions on the molding surface of a mold and exhibits sufficiently high strength in the threaded part thereof
| Number | Date | Country | Kind |
|---|---|---|---|
| 2000-056537 | Mar 2000 | JP | national |
| Filing Document | Filing Date | Country | Kind | 371c Date |
|---|---|---|---|---|
| PCT/JP01/01465 | 2/27/2001 | WO | 00 | 8/26/2002 |
| Publishing Document | Publishing Date | Country | Kind |
|---|---|---|---|
| WO01/64527 | 9/7/2001 | WO | A |
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| 2961043 | Hicks | Nov 1960 | A |
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| 6454906 | Nonomura et al. | Sep 2002 | B1 |
| 6461480 | Otakura et al. | Oct 2002 | B1 |
| 6468398 | Kumamoto et al. | Oct 2002 | B1 |
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|---|---|---|
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| 8-302600 | Nov 1996 | JP |
| 2000-25733 | Jan 2000 | JP |
| Number | Date | Country | |
|---|---|---|---|
| 20030029591 A1 | Feb 2003 | US |
