Patent Application
20150299902
The invention relates to the field of quench tubes used in polymer fiber or polymer filament extrusion, and to a method to manufacture such quench tubes.
The use of quench tubes in polymer fiber extrusion is known, e.g. in the extrusion process for producing POY (Partially Oriented Yarn) or FDY (Fully Drawn Yarn) polyester multifilament yarns. After extrusion, the fibers or filaments pass through a quench zone which comprises one or more quench tubes. Through the walls of the quench tube, from the inside out or from the outside in—air is led that cools and sometimes also draws the fibers or filaments.
Different types of quench tubes exist and have been described.
GB1382499 mentions quench tubes made of a porous material, such as ceramic or sintered metal powder. Sintered bronze powder is indicated as a specific example for quench tubes.
EP1491663 lists quench tubes manufactured from multilayer cellulose, multilayer wire netting, sintered metal powder or ceramics, and multilayer perforated plate.
CN2861195 describes a quench tube consisting out of an outer layer of a perforated metal tube and an inner layer of a twill weave metal wire mesh.
CN2528783Y describes a quench tube consisting out of an inner layer of a perforated stainless steel sheet of porosity 12-15%, a number of layers of woven stainless steel wire meshes of porosity 25-35%, and an outer layer of a perforated stainless steel sheet of porosity 22-30%.
An example of a commercially available quench tube is made of a helically wound cellulose paper or nonwoven ribbon impregnated with phenolic resin which is heat cured to form a paper quench tube. The air distribution occurs through the innumerable minute gaps formed between the layers of helically wound ribbon. The numerous distributed pores run straight from the outer circumference to the inner core of the quench tube.
Quench tubes have to allow uniform distribution of air over their full surface. It is a problem of the quench tubes of the prior art that the quench tubes are not optimal in terms of uniformity of distribution of air.
The primary object of the invention is to provide an improved quench tube. It is a specific objective to provide a quench tube that provides an improved and excellent uniformity of the flow distribution over its full outflow surface.
A first aspect of the invention is a quench tube for quenching polymer fibers in fiber extrusion. Such polymer fibers can be filaments or staple fibers. The quench tube comprises a cylindrical wall through which quenching air flows when the quench tube is in use. The cylindrical wall can have a circular cross section, or another cross sectional shape such as elliptical. The cylindrical wall comprises metal fibers in a nonwoven fiber structure. The metal fibers are bonded to each other at contacting points by means of metallurgical bonds thereby forming a three dimensionally bonded fiber structure.
Quench tubes according to the invention have the benefit that they have an excellent uniformity of the quench flow over the full outflow surface of the quench tube, in combination with a low pressure drop. It is possible to make quench tubes that are shorter than the quench tubes of the prior art. Quench tubes with metal wire meshes and/or perforated metal sheets have less pores and the pores are of higher sizes. Such quench tubes also have an important discontinuity at joining edges of the metal wire meshes and/or perforated metal sheets; both aspects result in a non-uniform quench flow compared to the quench tube of the invention.
It is a further benefit that the quench tubes of the invention can be cleaned while maintaining after cleaning the excellent uniformity of quench flow distribution. Quench tubes with metal wire meshes and/or perforated metal sheets can also be cleaned, however, after cleaning, the quench flow is even less uniform than before cleaning. This is believed to be because of the different size of number of pores in the quench tube of the prior art compared to the quench tube of the invention. The quench tube of the invention has a large number of small pores, therefore a remaining soil particle after cleaning has less effect on the flow distribution as the quench air flow can find more easily a path around the pore with the remaining soil particle.
It is a further benefit of quench tubes of the invention that they are inflammable. Quench tubes made of a helically wound cellulose paper or nonwoven ribbon impregnated with phenolic resin which is heat cured are flammable.
For the invention, preferred are metallurgical bonding techniques in which no additional bonding material or bonding agent is added, but where only the metal fibers are used to create the bonding. Examples of such metallurgical bonds are sinter bonds (in which a bond is created by means of diffusion between contacting fibers in a sintering process) or welded bonds (where contacting fibers are bonded by means of local melting and re-solidifying). An example of an appropriate welding technique is capacity discharge welding (CDW).
Preferred are metal fibers with an equivalent fiber diameter between 2 and 40 micrometer, more preferred are metal fibers with an equivalent fiber diameter between 12 and 40 micrometer, even more preferred are metal fibers with an equivalent fiber diameter between 18 and 25 micrometer. Such quench tubes have even better quenching results, in terms of distribution of quenching air.
With equivalent diameter of a fiber is meant the diameter of a circle that is having the same area as the cross section of the fiber.
In a preferred embodiment, a majority of the metal fibers at least partially encircle the axis of the quench tube. Preferably at least 50 percent, and more preferably at least 85 percent of the fibers at least partially encircling the axis.
With a metal fiber at least partially encircles the axis of the quench tube is meant that it passes partially around this axis. This can be seen and measured by making a cross section perpendicular to the axis of the cross section and observing the projection line of the fibers on a plane perpendicular to the axis of the quench tube. A metal fiber is at least partially encircling the axis when the projection line of the fiber on the plane perpendicular to the axis of the cross section is concave towards the axis; and when the projection line is for 360° degrees encircling the axis and/or when the projection line is longer than half of the length of the fiber in case of staple fibers.
Preferred are stainless steel fibers. Even more preferred are stainless steel fibers according to AISI 304 or AISI 316.
The metal fibers can e.g. have a circular or a polygonal cross section, e.g. a rectangular or a hexagonal cross section.
The metal fibers can e.g. be produced via single end drawing, via bundled drawing (see e.g. in U.S. Pat. No. 2,050,298, U.S. Pat. No. 3,277,564 and in U.S. Pat. No. 3,394,213)—particularly interesting for producing stainless steel fibers, via shaving (see e.g. in U.S. Pat. No. 4,930,199), via machining or via extrusion from a melt. A hexagonal cross section of the fibers is preferred. Metal fibers, and especially stainless steel fibers, with hexagonal cross section can be obtained via the bundled drawing production technology.
In a preferred embodiment, the metal fibers are part of a fiber structure which is coiled around the central axis of the quench tube.
Preferably such fiber bundle is a combination of metal fibers all oriented substantially in the length direction of the fiber bundle. An example is a bundle of crimped metal filaments (fibers of virtually infinite length). Preferably the coiling is performed building up a number of layers over the wall thickness of the quench tube, e.g. 10 to 100 layers, preferably 20 to 45 layers, more preferably 20 to 40 layers.
Such coiling contributes to the improvement of the uniformity of quench air distribution over the outflow surface of the quench tube.
When using staple fibers for the different embodiments of the invention, preferred staple fibers have an average length ranging from 0.6 cm to 6 cm.
A preferred porosity range of the quench tube of the invention in order to obtain a quench tube with excellent quench air distribution is within the range of 60% to 95%; more preferably 85 to 95%.
In an even more preferred embodiment, the cylindrical wall of the quench tube is over its full wall thickness consisting out of the metal fibers in a nonwoven fiber structure. Such a quench tube has shown to provide the best results in terms of uniformity of the quench air distribution.
A preferred wall thickness range of the quench tube is 5 to 25 mm, more preferred 5 to 10 mm.
A second aspect of the invention is a method to make a quench tube as in the first aspect of the invention. The method comprises the steps of
The method is an economic way of making a quench tube of good uniformity of quench flow. Such coiling contributes to the improvement of the uniformity of quench air distribution over the outflow surface of the quench tube.
In a specific embodiment of the method, the method comprises the steps of
In a specific embodiment of the method, the elongated metal fiber structure is a metal fiber nonwoven web having at least a leading edge; and the metal fiber nonwoven web is cylindrically wound, parallel to said leading edge, until the predetermined diameter is obtained. Preferred is when the width of the web is equal or larger than the quench tube that is to be made.
E.g. 10 to 100, preferably 20 to 50, more preferably 20 to 45 layers, more preferably 20 to 40 can be obtained in the quench tube in coiling the metal fiber nonwoven web.
The metal fiber nonwoven web can e.g. comprise staple metal fibers or metal fiber filaments.
In another specific embodiment of the method the metal fiber structure is comprising a metal fiber bundle or is a metal fiber bundle. Preferably such a fiber bundle is a combination of metal fibers all oriented substantially in the length direction of the fiber bundle. An example is a bundle of crimped metal filaments (fibers of virtually infinite length).
The fiber bundle or fiber bundles can be wrapped around the core, whereby the wrapping is moved along the axis of the core in order to build up the quench tube.
A third aspect of the invention is a polymer fiber extrusion apparatus, comprising a quench tube as in the first aspect of the invention, installed at the extrusion die of the extrusion apparatus, in order to quench the polymer fibers or polymer filaments after their extrusion. The polymer fiber extrusion apparatus can have a flow of the quenching air inside out the quench tube or outside in the quench tube.
For use in extrusion apparatuses that have an inside-out flow of the quench air, internal diameters of the quench tube in the range of 60 to 165 mm are preferred, even more preferably 60 to 100 mm. For use in extrusion apparatus that have an outside-in flow of the quench air, internal diameters of the quench tube in the range of 200 to 350 mm are preferred.
Quench tubes with a wall thickness of 10 mm have been made. Using a stainless steel fiber web with a weight of 300 g/m2, when coiling 27 layers and to a wall thickness of 10 mm; a porosity of the quench tube of 90% was obtained.
Using a stainless steel fiber web with a weight of 300 g/m2, when coiling 21 layers and to a wall thickness of 10 mm; a porosity of the quench tube of 92% was obtained.
Using a stainless steel fiber web with a weight of 300 g/m2, when coiling 40 layers and to a wall thickness of 10 mm; a porosity of the quench tube of 85% was obtained.
An example is a quench tube with internal diameter 86 mm and outer diameter D 106 mm.
The uniformity of quench air flow has been tested using a pressure sensor at the exit of the quench tube. The pressure sensor was located at different positions along the length of the quench tube and along the circumference of the cross section and measurements of the air pressure were performed.
The quench tubes of the invention have shown to provide a remarkable uniform distribution of air over their full surface, along the length of the quench tube as well as along the circumference of cross sections perpendicular to the axis of the quench tube. The remarkably uniform distribution of air was maintained after cleaning by treatment in hot solvent to remove impurities from the quench tube trapped in it during its use.
Other tests showed that compared to a quench tube made of a helically wound cellulose paper or nonwoven ribbon impregnated with phenolic resin which is heat cured afterwards, the uniform distribution of quench air flow could be obtained at a lower air pressure.
By removing the quench tube 210 out of the extrusion apparatus 200 and removing the end cap 250, it is possible to clean the quench tube 210 of the invention, e.g. by washing in a solvent at elevated temperatures which can be in the range of 280-400° C.
| Number | Date | Country | Kind |
|---|---|---|---|
| 13153817.5 | Feb 2013 | EP | regional |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/EP2014/051337 | 1/23/2014 | WO | 00 |
