The present application is a U.S. National Stage of PCT International Patent Application No. PCT/US13/62205, filed Sep. 27, 2013, which claims priority to EP Application No. 12186505.9, filed Sep. 28, 2012, and Ser. No. 13/166,389.0, filed May 3, 2013, all of which are hereby incorporated herein by reference.
The present disclosure relates to a method and apparatus for injection moulding of an elongated hollow article, such as a urinary catheter.
As explained in U.S. Pat. No. 4,750,877 there is a need in the art of moulding plastic products to be able to mould a plastic part having a relatively small diameter hole extending therethrough.
Especially in the field of medical products, such as catheters, it is important to exert great care in maintaining the constant diameters of both the outer surface and the central hole extending through a catheter product since this has the effect of maintaining a substantially straight shank in the finished tubular product. Also, the product must be constructed to have a consistent flex pattern and avoid “kinking” when bent or flexed. Often, such moulded plastic parts are required to have a thin wall of necessarily constant thickness with a longitudinally extending channel extending therethrough.
Previously, especially in the art of injection moulding, when plastic is melted, and forced to flow into a cavity about a fine, small diameter core, the pressure of injection forcing the melt into the mould cavity if not adequately balanced during the moulding operation tends to cause the thin diameter core to be displaced from its substantially centred, straight line configuration relative to the central axis of the mould cavity. This displacement is of course undesirable since a straight line configuration of the central hole as well as the shank portion of the product is required. Such displacement of the core pin relative to the interior surface of the mould cavity is also frequently caused by what may be considered an imbalance in the flow characteristics of the hot melt as it enters the mould cavity and passes along the length thereof in substantially surrounding relation to the core pin. Such imbalance may be caused by a number of factors but also has the tendency to cause uneven forces to be exerted on the core pin tending to cause its displacement from the aforementioned and preferred straight line configuration. For these reasons, the prior art has generally been limited to relatively short tubular lengths in relation to the diameter of the hole through it. If, for example, the tubular product is to be relatively long, which is quite common in the medical industry, a small hole, especially a hole in a thin walled tube is extremely difficult to make with any great degree of accuracy. In addition, different materials provide different problems.
Another problem generally associated with the injection moulding technique of products of the type referred to above is the breakdown in the intensity of the plastic material utilized to form the tubular product when the material is forced to travel along what may be referred to as a circuitous path from the point of leaving the injection nozzle to the point of entering and passing along the length of the mould cavity. This is particularly true when the plastic material, after being melted, is forced to flow along a circuitous path or a path including one or more right angles at a relatively high speed. Attempts to slow the speed of injection of the inflowing melt however have met with little success especially in the formation of thin walled tubular products. This is primarily due to the fact that the melt rapidly cools and therefore solidifies as it flows along the length of the mould cavity especially at slow speeds. Accordingly, when using injection moulding techniques at such slow speeds, attempts have been made to raise the temperature of the plastic material to a somewhat higher than normal temperature, prior to injection to overcome the problems of the prior art. This higher temperature results in a degradation of many plastic materials which has obvious disadvantages in the making of thin walled tubular products.
U.S. Pat. No. 2,443,053 discloses a method and an apparatus for manufacturing hollow cylindrical plastic articles with a moving core, which is moved during the injection of moulding material through an annular inlet in the stationary outer moulding member. However, according to the moulding technique disclosed herein, the first end section of the article is formed whereafter a tubular section of the article is formed. However, there are limitations to which designs the article can have when moulded according to this method as only the front end of the article can be provided with a special design as the rest of the article must have a cylindrical shape.
From U.S. Pat. No. 7,871,261 and U.S. Pat. No. 7,910,044 a method and an injection moulding apparatus for producing profiled elongated articles are disclosed where a moving inlet is provided for a moving moulding core.
From EP 1 116 567 there is known a gas assisted injection moulding technique. However, this technique only allows making short catheters.
As explained above, one of the technical factors limiting the use of conventional injection moulding for catheter manufacture is the high injection pressures required to fill the cavity and the difficulty of producing long tubular parts, e.g. up to and in excess of 40 cm, with adequate internal and outer diameter tolerances and good reproducibility. Therefore, it is an object of the disclosure to provide an improved method and apparatus for injection moulding of elongated hollow articles, in particular for the manufacture of urinary catheters.
The disclosure comprises a method and an apparatus for injection moulding of an elongated hollow article, such as a urinary catheter, said apparatus comprising a heated central mould with an inlet opening for entering liquid moulding compound into a substantially tubular cavity formed in said central mould; an elongated central mould core which is provided in the tubular cavity and extends beyond said tubular cavity and into a tip mould cavity of a tip mould part which is aligned with the tubular mould cavity in the longitudinal axis of the central mould core; wherein the tip mould part is moveable in a linear movement in a direction along the longitudinal axis of the elongated central mould core.
Hereby an injection moulding technique with a moving mould is provided. The moving mould provides a drag force to transport a viscous melt of moulding material to fill the elongated cavity and minimizing the injection pressure required to make an article with a predetermined tip design at one end and a predetermined shape at the other end, in particular a tipped urinary catheter, including a funnel connector portion of the opposite end, produced in a single polymer processing operation.
It is preferred that the movable tip mould is movable in a linear direction from a first position where the tip mould is abutting the outer mould with the tip mould cavity aligned with the mould cavity to a second position at a predetermined distance from said first position via a sledge.
In a preferred embodiment, the elongated central mould core is moveable and adapted to be moved in the same direction and together with the tip mould part. In addition, it may be advantageous that the elongated central mould core is moved by being pushed by a second elongated central mould core which will eventually provide the elongated mould core for the subsequent moulding cycle. Accordingly, the elongated mould core is ejected together with the moulded article by the insertion and positioning of the second elongated central mould core. This is advantageous since the elongated mould core acts as a mandrel for the moulded product which facilitates the handling of the product during the subsequent processing steps, such as surface coating, etc.
In an embodiment of the disclosure, the tubular cavity is cylindrical with a circular cross-section. However, it is realised that other cross-sectional shapes may be provided.
Advantageously, the disclosure provides the option of providing at least a section of the inner surface of the outer mould with a predetermined patterning for moulding such patterning on the surface of the article.
In order to assist in ensuring a predetermined inner surface of the article, it is found advantageous in an embodiment that the elongated mould core is provided with a fluid channel, which is in flow connection with a fluid source, such as a pressurised air source providing air through the fluid channel. The fluid channel is in flow communication with the first end of the mould cavity at the distal end mould core, and in connection with the fluid source, such as the pressurised air source and at the second end of the fluid channel.
Using the method and apparatus according to the present disclosure is found particularly advantageous that the elongated hollow article is a catheter with the first end geometry being the proximal tip end of the catheter and the second end being the funnel-shaped connector end of the catheter.
According to a further aspect, there is provided an apparatus and a method for injection moulding of an elongated hollow article, such as a urinary catheter, where said apparatus comprises
The method of injection moulding of an elongated hollow article, such as a urinary catheter, according to this third aspect comprises the steps of:
This embodiment may be advantageous since the moulding apparatus according to this process can be adopted for producing elongated articles, such as urinary catheters, of a variety of lengths, in principle any lengths. This method and apparatus is found particular advantageous that the elongated hollow article is a catheter with the first end geometry being the proximal tip end of the catheter and the second end being the funnel-shaped connector end of the catheter. Hereby, the costs of manufacturing such articles can be reduced since the articles can be produced in a reduced amount of moulding processes, preferably a single moulding process.
The elongated central mould core is preferably temperature controlled for maintaining an elevated temperature, such as a temperature similar to that of the heated central mould. More particularly, the elevated temperature is above the melting temperature of the liquid mould compound, such as between +130° C. and +350° C. depending on the polymer material used for the moulding process.
Similarly, the movable tip mould part is preferably temperature controlled for maintaining a temperature lower than of that the heated central mould. In particular, the temperature of the movable tip mould part is kept below the melting temperature for the mould compound material, such as between +20° C. and +130° C., which is also well below the glass temperature of the polymer materials used for moulding the article.
According to an embodiment, the fluid channel is in controlled flow connection with a pressurised air source providing pressurised air through the fluid channel into the inner volume of the moulded article during the moulding process. This air pressure inside the inner volume of the article stabilises the material of the moulded portion of the article during the moulding process as this portion leaves the inner support of the elongated mould core. This pressurised air helps solidifying the material and ensures the shape of the article even though the material may not yet be solidified immediately after leaving the heated elongated mould core.
According to the moulding in this embodiment, the movable tip mould is movable in a linear direction from a first position where the tip mould is abutting the outer mould with the tip mould cavity aligned with the mould cavity to a second position at a predetermined distance from said first position via a sledge. This ensures the formation of the tubular portion of the article in an extrusion moulding sub-process.
In a preferred embodiment, a set of cooling mould blocks is provided for radially inwardly encompassing and preferably also clamping the moulded portion of the article when the tip mould is approaching said second position. Furthermore, the cooling mould blocks are preferably provided with inner contacting surfaces resembling the shape of the tubular mould cavity. Hereby a rapid cooling of the article as well as the surface outer shape of the article is ensured.
In a further embodiment, the cooling mould blocks are formed with end contacting surfaces having an end section geometry. Particularly, the cooling mould blocks is provided with inner contacting surfaces resembling the shape of the tubular mould cavity and wherein the cooling moulding blocks are formed with end contacting surfaces having an end section geometry and pressurised air is supplied to form said end section geometry. Hereby, a sub-process of blow-moulding the second end shape of the elongated hollow article. This is particularly advantageous when producing a catheter with the first end geometry being the proximal tip end of the catheter and the second end geometry being the funnel-shaped connector end of the catheter.
According to a further embodiment, a gap between the cooling blocks and the outer mould is provided at the second position in which cutting means are provided for cutting the moulded article away from the mould. Hereby the moulded article is easily freed from the mould to complete the moulding cycle.
According to an aspect of the disclosure, the inlet member is preferably moving in the track of the outer mould, preferably in the upper half part, from a first position near the first end section of the cavity to a second position near the second end section of the cavity. Preferably, the movable inlet member is provided with an annular cooling section downstream the inlet opening and a heated section upstream the inlet opening. This is advantageous as it is hereby ensured that as the mould moves the injected polymer material solidifies, helping to support the mould core and hindering its deflection from the long axis of the article due to the injection pressure whereby a good control of the inner and outer diameter of the article during the moulding process is ensured.
Preferably, the limiter insert piston is moved together with the inlet member and the mould core until reaching its second end moulding position at the second end. Hereby the continuous moving injection mould can be finalised with a complex geometry at the second end.
According to an embodiment, the inlet member is moving together with (i.e. stationary relative to) the mould core. Moreover, the outer mould is preferably adapted to be moving during the injection moulding and the central mould core is stationary until the moulding process is finished whereafter the mould core is retracted for ejection of the moulded component.
It may be advantageous that the cavity of the second end is provided with an outer peripheral surface defining an end geometry larger than the outer diameter of the cavity of the cylindrical section of said cavity. This allows for the manufacture of more complex geometry at both ends of the elongated article.
In the following the disclosure is described in more detail with reference to the drawings, in which:
With reference to
A moveable inlet member 4 is provided axially sliding along a track 51 of the outer mould member 1. This movable inlet member 4 is provided with an inlet opening 5 which is in flow communication with a liquid moulding material source 6. The inlet member 4 is adapted to move relative to the outer mould 1 from the start position at the first end 10 (see
In the first embodiment, the inlet member 4 is held stationary by a guide rail 17, which will close the mould downstream, having the shape of the track 51. The outer mould 1 is adapted to move relative to the inlet member 4 as well as the mould core 2 and the piston 16 which are also kept stationary during the moulding process.
The mould core 2 is provided with a fluid channel 9 which has an opening to the mould cavity 3 at the distal first end 10 of the mould core 2. At the other end of the fluid channel 9 a pressurised air source (not shown) is provided. As the moulding process gets underway pressurised air is provided through the fluid channel 9 into the cavity 3 and into the hollow portion 3a of the article during the moulding (see
In an alternative to the shown embodiment, it is realised that the disclosure may also be used for the formation of profiles, such as tubes with multiple layers, for example a bi-layer, tri-layer tubes, etc. This may be achieved by providing more than one inlet member. Yet another embodiment allows making catheters with variable stiffness along the catheter length. Variable stiffness catheters facilitate catheter insertion and handling to the user. This embodiment requires injecting more than one polymer material.
The moulding process according to the first embodiment of the disclosure is illustrated in the
The outer mould is moved until its final position which is shown in
After the second end of the article 20 is moulded, the article 20 is ejected from the mould as shown in
It is realised by the disclosure that the method and apparatus allows for adding a predetermined pattern on the catheter surface. For example the inner surface of the outer mould 1 (
With reference to
The initial position of the moulding apparatus is shown in
Liquidised moulding material 20 is advanced into the cavity 3 as shown in
This second embodiment is advantageous as the same mould can be used for manufacturing articles of different lengths without changing any of the components.
In short, the aspects of the first and second embodiments may be summarised in the following items:
With reference to
The elongated mould core 2 is provided with a central axial fluid channel 9 which is connected to a pressurised air supply 9a. The inlet 5 is provided substantially radially to the elongated mould core 2. The elongated mould core 2 is provided with an end section so that the extent of the cavity 3 is limited at the inlet 5 but extends beyond the outer mould 1 and into a tip mould 30. In the tip mould 30 there is provided a tip end cavity 12. The tip mould 30 is in its initial position positioned adjacent the outer mould 1 so that the tubular cavity 3 and the tip end cavity 12 are aligned and the tip of the elongated mould core 2 extends into the tip end cavity 12 (see
The tip mould 30 is kept cool, e.g. at +40° C. for PVC (and +20° C. to +130° C. for other polymers), i.e. well below the melting temperature of the polymer moulding material 20. The moulding material 20 is in a liquidised state in the heated section of the mould but is cooled and thereby solidifies as it leaves the heated mould members. The pressurised air supplied to the inside of the product formed stabilises the moulded portion 20a of the tubular product which is in the process of being moulded. The moulded portion 20a is thereby prevented from collapsing as it is pushed off the elongated mould core 2 by the liquidised moulding material 20, which is continuously being supplied under a predetermined pressure through the inlet 5. This pushing of the moulded product is also assisted by the supply of pressurised air 9a through the fluid channel 9 and into the inner volume 9b of the moulded portion 20a as well as the movement of the tip mould 30 which also assists the advancement of the moulded portion 20a off the elongated mould core 2. The tip mould 30 is arranged on a sledge 34 arranged for a linear movement in the direction D3.
By this movement of the tip mould 30, the tubular form of the moulded portion is extended in length, as indicated in
In this gap 35, a cutting arrangement 31 is then provided, as shown in
When the product has been cut, the cutting arrangement 31 is removed and the tip mould 30 is then moved further whereby the product 20a is held between the two cooling mould blocks 32, 33, as shown in
Although not shown in the figures, it is realised that the cooling mould blocks 32, 33 may be formed with a funnel cavity at the mould facing end so that when the mould blocks 32, 33 are clamped around the tubular moulded product as shown in
The central mould 1 is provided with an inlet 5 which is provided substantially radially to the elongated mould core 2 and through which inlet 5 the liquidised moulding material 6 is fed. The elongated mould core 2 is provided with an end section so that the extent of the cavity 3 is limited at the inlet 5 but extends beyond the outer mould 1 and into a tip mould part 30. In the tip mould part 30 there is provided a tip end cavity 12. The tip mould part 30 is shown in
The tip mould part 30 is kept cool, e.g. at +40° C. for PVC (and +20° C. to +130° C. for other polymers), i.e. well below the melting temperature of the polymer moulding material 20. The moulding material 20 is in a liquidised state in the heated section of the mould but is cooled and thereby solidifies as it leaves the heated mould 1. The moulded portion 20a is prevented from collapsing as it is supported by the elongated mould core 2.
As the required length of the tubular product is reached (see
As shown in
Number | Date | Country | Kind |
---|---|---|---|
12186505 | Sep 2012 | EP | regional |
13166389 | May 2013 | EP | regional |
Filing Document | Filing Date | Country | Kind |
---|---|---|---|
PCT/US2013/062205 | 9/27/2013 | WO | 00 |
Publishing Document | Publishing Date | Country | Kind |
---|---|---|---|
WO2014/052770 | 4/3/2014 | WO | A |
Number | Name | Date | Kind |
---|---|---|---|
2443053 | Parmelee | Jun 1948 | A |
2801444 | Lorenian | Aug 1957 | A |
2969563 | Hendry | Jan 1961 | A |
3296345 | Dietz | Jan 1967 | A |
3328498 | Cheney | Jun 1967 | A |
3329996 | Marcus | Jul 1967 | A |
3394209 | Cheney | Jul 1968 | A |
3466701 | Cheney | Sep 1969 | A |
3725522 | Sheridan et al. | Apr 1973 | A |
4188179 | Linss | Feb 1980 | A |
4750877 | McFarlane | Jun 1988 | A |
4806093 | Linss | Feb 1989 | A |
5316706 | Muni et al. | May 1994 | A |
5358580 | Miyamura et al. | Oct 1994 | A |
5409644 | Martin et al. | Apr 1995 | A |
5547364 | Wong et al. | Aug 1996 | A |
5558737 | Brown et al. | Sep 1996 | A |
5614136 | Pepin et al. | Mar 1997 | A |
5762631 | Klein | Jun 1998 | A |
5780073 | Chen et al. | Jul 1998 | A |
5851464 | Davila et al. | Dec 1998 | A |
5853518 | Utas | Dec 1998 | A |
6086970 | Ren | Jul 2000 | A |
6280788 | Rakhorst et al. | Aug 2001 | B1 |
7399444 | Skinner et al. | Jul 2008 | B2 |
7431876 | Mejlhede et al. | Oct 2008 | B2 |
7871261 | Steiner et al. | Jan 2011 | B2 |
7910044 | Steiner et al. | Mar 2011 | B2 |
8048058 | Fulford | Nov 2011 | B2 |
8123892 | Morris et al. | Feb 2012 | B2 |
20020084551 | Lee | Jul 2002 | A1 |
20030044484 | Goral et al. | Mar 2003 | A1 |
20040159966 | Yamaguchi | Aug 2004 | A1 |
20040241364 | Zihlmann | Dec 2004 | A1 |
20050104255 | Mejlhede et al. | May 2005 | A1 |
20080027414 | Tanghoj et al. | Jan 2008 | A1 |
20100221500 | Steiner et al. | Sep 2010 | A1 |
20110180969 | Sansoucy | Jul 2011 | A1 |
20120150130 | Triel et al. | Jun 2012 | A1 |
Number | Date | Country |
---|---|---|
1111810 | Jul 1961 | DE |
202008014672 | Feb 2009 | DE |
102008052950 | Apr 2009 | DE |
102008052951 | Apr 2009 | DE |
0371497 | Jun 1990 | EP |
0465660 | Jan 1992 | EP |
0489335 | Jun 1992 | EP |
618059 | Oct 1994 | EP |
662385 | Jul 1995 | EP |
0824930 | Feb 1998 | EP |
0850655 | Jul 1998 | EP |
1034811 | Sep 2000 | EP |
1110711 | Jun 2001 | EP |
1208955 | May 2002 | EP |
1935614 | Jun 2008 | EP |
2335767 | Jun 2011 | EP |
2445565 | May 2012 | EP |
2712721 | Apr 2014 | EP |
2230702 | Oct 1990 | GB |
WO 9114473 | Oct 1991 | WO |
WO 9710940 | Mar 1997 | WO |
WO2004067076 | Aug 2004 | WO |
WO 2009048423 | Apr 2009 | WO |
WO2009117270 | Sep 2009 | WO |
WO2010149175 | Dec 2010 | WO |
WO 2013127718 | Sep 2013 | WO |
WO 2013127725 | Sep 2013 | WO |
Entry |
---|
European Search Report and Opinion, counterpart EP Appl. No. 12186505, dated Feb. 28, 2013. |
International Search Report and Written Opinion, counterpart PCT Appl. No. PCT/US2013/062205, dated Nov. 4, 2013. |
Brown, S. et al., Extrusion of Precision Small-Diameter Plastic Tubing for Medical Applications, Medical Device Technology, 3 (7), pp. 34-40 (1992). |
Callari, J., Dies Easy to Adjust, Plastics World, 53 (2), p. 14 (1995). |
Colbert, J., Concepts of Precision Tube Extrusion for Medical and Healthcare Applications, Antec 95, vol. III, pp. 3375-3382 (1995). |
Dowler, B. et al., How Low Can You Go? Optimising Cooling of Small Injection Moulded Parts, Antec 97, vol. 1, pp. 946-953 (1997). |
Ferrandino, M., Tubing Extrusion Made Easier, Part 1, Medical Device Technology, 15 (8), pp. 12-15 (2004). |
Gupta, A. et al., Influence of a Rotating Tip on the Properties of Tubing Made Using a Crosshead Tubing Die, International Polymer Processing, 14 (1), pp. 51-56 (1999). |
Kirkland, C., Nanomoulding Meets the Medical Catheter Tip, Injection Molding, 9 (10), pp. 79-80 (Oct. 2001). |
Machado, A., Multi Lumen Die Design and Techniques, Conference Medical Manufacturing, Paper 2.2.3 (1990). |
Martini, L. G. et al., Manufacturing High Quality Urinary Catheters, Medical Device Technology, 20 (1), pp. 18-19 (2009). |
Mori, K. et al., Development of Polymer-Molding-Releasing Metal Mold Surfaces with Perfluorinated-Group-Containing Polymer Plating, Journal of Applied Polymer Science, 90 (9), pp. 2549-2556 (2003). |
O'Neil, C., Selecting Materials for Mission-Critical Catheters, European Medical Device Technology, 1 (9), pp. 48-55 (2010). |
Person, T. J. et al., The Effect of Die Materials and Pressure-Dependent Slip on the Extrusion of Linear Low-Density Polyethylene, Journal of Rheology, 41 (2), pp. 249-265 (1997). |
Schut, J. H., Moving Die Parts Change Profile Shapes “On The Fly”, Plastics Technology, 52 (4), pp. 45, 47 (2006). |
Schut, J. H., Medical Tubing: Tinier Than Ever and Much More Complex, Plastics Technology, 53 (4), pp. 70-73 (2007). |
Stein, O., Extrusion of Medical Tubing, Plastics in Medical Technique, pp. 179-191 (2002). |
No Author, Cool Small Mold Cores Faster with New Water Transfer System, Plastics Technology, 24 (8), pp. 48-49 (1978). |
No Author, One-Piece Catheter, Plastics and Rubber Weekly, 1264, p. 8 (1988). |
No Author, One-Piece Catheter Cuts Manufacturing Costs, Biomedical Materials, pp. 4-5 (1990). |
No Author, New Dies Fine-Tune Tiniest Medical Tubes, Plastics Technology, 48 (9), p. 17 (2002). |
No Author, Medical Tubing Can Be Configured on the Fly, British Plastics and Rubber, p. 10 (2006). |
Colbert, J., High Quality Tube Extrusion for the Medical Device Industry, Polymers for the Medical Industry, paper 4 (1999). |
Comim, L. M. et al., Effect of the Extrusion Process on the Bactericidal Performance of Biocidal Polypropylene Catheters, Polymer-Plastics Technology and Engineering, 51(3), pp. 289-295 (2012). |
Kazmierska, K. et al., Determination of Urethral Catheter Surface Lubricity, Journal of Materials Science, Materials in Medicine, 19(6), pp. 2301-2306 (2008). |
Zhao, Danyang et al., Numerical Simulation and Experimental Study of Polymer Micro Extrusion Flow, IEEE International Conference on Mechatronics and Automation, pp. 3155-3160 ( 2009). |
Ahmed, N. et al., A Hydrophilic Technology for Intermittent Urinary Catheters, Medical Device Technology, 19 (1), pp. 17-19 (2008). |
Bales, S. J., Know Your Mold Coatings, Plastics Technology, 50 (12), pp. 52-57 (2004). |
Baumeister, C., et al., Excellent Catheter Coupling. Raumedic Develops and Produces a Component of 2K Injection Moldings for Medicinal Applications, Kunststoffberater, 50 (5), pp. 38-40 (2005). |
Beddus, D., Extruder Theory and Die Design for Medical Tubing, Conference Medical Manufacturing, Paper 2.2.1 (1990). |
Berg, G. et al., Chrome Nitride Coatings for Applications in Plastics Processing, International Polymer Processing, 14 (2), pp. 122-127 (1999). |
Callari, J. J., Precision Processing: It's All in the Details, Plastics World, 53 (2), pp. 35-38 (1995). |
Chen, S. C. et al., Efficiencies of Various Mold Surface Temperature Controls and Their Effects on the Qualities of Injection Molded Parts, ANTEC 2006, 64th SPE Annual Conference, pp. 1280-1284 (2006). |
Daniels, U. et al., How Injection Moulding Tool Coating Affects the Demoulding Force, Kunststoffe/German Plastics, 79 (1), pp. 42-44 (1989). |
Fallon, M., Resins Flow Better in TiN-Coated Molds, Plastics Technology, 36 (6), pp. 41-43 (1990). |
Farzaneh, S. et al., Critical Factors in Extruding Catheter Tubing From Polyamide, Medical Device & Diagnostic Industry, 24 (11), pp. 54-60 (2002). |
Kaiser, W. et al., Injection Moulds. Titanium Nitride Coating Improves Injection Moulding of Thermoplastics, Plastverarbeiter, 40 (10), pp. 81-91 (1989). |
Navabpour, P. et al., Evaluation of Non-Stick Properties of Magnetron-Sputtered Coatings for Moulds Used for the Processing of Polymers, Surface & Coatings Technology, 201 (6), pp. 3802-3809 (2006). |
Reilly, J. F., Fast Fourier Transform Analysis of Melt Fractured Extrudate, Conference Polymer Rheology 99, paper 6 (1999). |
Shearer, G., et al., Extrusion of LLDPE Through Polypropylene Coated Dies, Annual Technical Conference, vol. I, pp. 73-77 (1999). |
No Author, BM Equips Catheter Facility, Plastics and Rubber Weekly, 1817, p. 9 (1999). |
No Author, Enhancing the Economic Efficiency in the Production of Catheter Hoses, Kunststoffe-Synthetics, 50 (1), pp. 14-15 (2003). |
No Author, Extrusion Plants for Continuous Hollow Profile Manufacture, Plastverarbeiter, 49 (10), p. 152 (1998). |
No Author, High-Tech Plant for High Precision Flexible Tube Extrusion for Cardiac Catheters Application, Plastverarbeiter, 49 (7), pp. 26-27 (1998). |
No Author, Manufacturing Medical Catheter Tubes, Extrusion, 10 (5), pp. 18-19 (2004). |
No Author, Surface Treatments Extend Tool Life, Plastics Technology, 43 (3), p. 29 (1997). |
International Preliminary Report on Patentability, counterpart PCT Appl. No. PCT/US2013/062205, dated Mar. 31, 2015. |
Examination Report, counterpart Australian Appl. No. 2013323339, dated Nov. 26, 2015. |
Office Action, counterpart Canadian Appl. No. 2,889,820, dated Mar. 10, 2016. |
Office Action, counterpart Canadian Appl. No. 2,889,820, dated Sep. 29, 2016. |
Number | Date | Country | |
---|---|---|---|
20150273747 A1 | Oct 2015 | US |