EP0161579A2 - Dryer fabric having warp strands made of melt-extrudable polyphenylene sulphide - Google Patents

Dryer fabric having warp strands made of melt-extrudable polyphenylene sulphide Download PDF

Info

Publication number
EP0161579A2
EP0161579A2 EP85105288A EP85105288A EP0161579A2 EP 0161579 A2 EP0161579 A2 EP 0161579A2 EP 85105288 A EP85105288 A EP 85105288A EP 85105288 A EP85105288 A EP 85105288A EP 0161579 A2 EP0161579 A2 EP 0161579A2
Authority
EP
European Patent Office
Prior art keywords
fabric
polyphenylene sulphide
monofilament
dryer
dryer fabric
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
EP85105288A
Other languages
German (de)
French (fr)
Other versions
EP0161579B1 (en
EP0161579A3 (en
Inventor
Samuel M. Baker
F. Brian Best
Girish M. Bhatt
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Jwi Ltd
Original Assignee
Jwi Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Jwi Ltd filed Critical Jwi Ltd
Publication of EP0161579A2 publication Critical patent/EP0161579A2/en
Publication of EP0161579A3 publication Critical patent/EP0161579A3/en
Application granted granted Critical
Publication of EP0161579B1 publication Critical patent/EP0161579B1/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21FPAPER-MAKING MACHINES; METHODS OF PRODUCING PAPER THEREON
    • D21F1/00Wet end of machines for making continuous webs of paper
    • D21F1/0027Screen-cloths
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21FPAPER-MAKING MACHINES; METHODS OF PRODUCING PAPER THEREON
    • D21F1/00Wet end of machines for making continuous webs of paper
    • D21F1/0027Screen-cloths
    • D21F1/0036Multi-layer screen-cloths
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21FPAPER-MAKING MACHINES; METHODS OF PRODUCING PAPER THEREON
    • D21F1/00Wet end of machines for making continuous webs of paper
    • D21F1/0027Screen-cloths
    • D21F1/0072Link belts

Definitions

  • the present invention relates to fabrics made of synthetic materials and particularly, but not exclusively, for use in dryer sections of papermaking machines involving high temperature.
  • 4,290,209 discloses the use of rectangular cross-section warp strands having a flattening ratio of about 2:1, whereby the resulting fabric acquires superior properties of distortion resistance and surface smoothness, along with more desirable permeability and elastic modulus. None of these improved fabrics, however, are suitable for high temperature applications, again because of the inherent tendency of the polymers normally used to degrade and lose strength.
  • U.S. 4,359,501 discloses an industrial fabric, for use in applications involving elevated temperatures, comprised of melt-extrudable polyaryletherketone monofilament strands. This material, however, suffers the major disadvantage of being so costly that the woven end product is not economically attractive to the specific paper mill end-users already identified.
  • the present invention is directed towards solving these problems.
  • the present invention provides a dryer fabric for use in a dryer section of a paper machine wherein at least the machine direction components of the fabric are monofilaments made from polyphenylene sulphide or a blend of polyphenylene sulphide with heat-stabilized polyamide 66 with the polyamide 66 being present in the range of up to about 20% by weight.
  • polyphenylene sulphide is blended with about 6% by weight of heat-stabilized polyamide 66.
  • the dryer fabric comprises a plurality of interwoven warp and weft strands wherein at least the warps are monofilaments made from polyphenylene sulphide or a blend of polyphenylene sulphide with heat-stabilized polyamide 66 the warp strands having an essentially rectangular cross-section with the long axis of the rectangle lying in the plane of the fabric.
  • the dryer fabric comprises a multiplicity of helical coils connected together by hinge pins wherein at least the helical coils are made from polyphenylene sulphide or a blend of polyphenylene sulphide with heat-stabilized polyamide 66.
  • the dryer fabric comprises a multiplicity of helical coils connected together by hinge pins wherein at least the helical coils are made from polyphenylene sulphide or a blend of polyphenylene sulphide with heat-stabilized polyamide 66 and wherein the helical coils have an essentially rectangular cross-section when viewed in the machine direction with the long axis of the rectangle lying in the plane of the fabric.
  • Monofilaments of the type described above can also be used to advantage in other industrial applications where hydrolysis is encountered.
  • Fig. 1 there is schematically illustrated a sub-section of a typical dryer section in a papermaking machine (not shown).
  • the top tier dryer cylinders are generally indicated at 10 and the bottom tier at 11.
  • the paper web 13 passes in a serpentine fashion over the top and bottom dryer cylinders as shown.
  • An endless top fabric 14 holds the paper web 13 tightly against the upper cylinders 10 as it passes partially around the first upper cylinder, around a felt roll 15, partially around the remaining top cylinders 10 and around the other intervening felt rolls 15, then around return roll 16, passing over guide and tensioning rolls 24 and 23 respectively, and then over other return rolls 16 before it passes again over the first dryer cylinder to complete the cycle.
  • an endless bottom fabric 18 holds the paper web 13 tightly against the lower dryer cylinders 11 as it passes around these and the intervening bottom felt rolls 19, return rolls 21, tensioning roll 25, guide roll 26, and other return rolls 21, substantially as shown.
  • Polyphenylene sulphide is a linear high molecular weight polymer having the repeating unit and is available commercially under the registered trademark RYTON from Phillips Chemical Corporation. While priced at a fraction of the material of U.S. 4,359,501, pure polyphenylene sulphide of the present invention is difficult to extrude. It is also lacking in "toughness" required for industrial weaving.
  • Table 1 shows the results of a test with the percent retained tensile strength of a polyphenylene sulphide strand exposed to saturated ateam at 130°C in a pressure vessel (24 gauge psi) for a period of eight days, along with a polyester monofilament strand of the same size.
  • Table 2 shows test results for the same materials when exposed to saturated steam at 150°C.
  • the material can only be extruded with difficulty in monofilament form in the size range commonly used in dryer fabrics. Also during weaving the pure material is subject to frequent warp breakages due to its lack of toughness and is prone to scraping in the loom heddles and reed dents, all of which renders pure polyphenylene sulphide difficult for heavy industrial weaving.
  • the means by which the additive improves toughness while preserving hydrolysis resistance is not entirely known, but the successful monofilaments are characterized by having the additive material present in small, discrete, elongated globules with the long axis parallel to the axis of the monofilament. These discrete globules are not connected to each other or to the outer boundaries of the monofilament, and are thus protected from the harsh environment of the end use application of the filament.
  • the melt viscosity of the added material must be higher than the melt viscosity of polyphenylene sulphide at the extrusion temperature and the amount of additive must be limited.
  • Another factor to consider in choosing the additive is that it must not degrade during extrusion when it is temporarily exposed to the temperature required to melt the polyphenylene sulphide, the range being 285°c to 315°C.
  • Some additives which satisfy the above mentioned requirements do not form globules because they are chemically incompatible with polyphenylene sulphide and react in unsuitable ways.
  • heat-stabilized polyamide 66 is the only additive to polyphenylene sulphide which successfully imparts the quality of toughness to the resultant monofilament while preserving hydrolysis resistance.
  • Other materials may be found which can also impart the same quality to the blend.
  • Some factors which are important in choosing additives are: a higher viscosity at extrusion temperature than polyphenylene sulphide, chemical compatibility, resistance to heat degradation during extrusion.
  • Figs. 2 and 2A depict a plain weave dryer fabr: 30 representative of a single-layer dryer fabric used in the papermaking industry.
  • numeral 31 denotes consecutive warp strands made from polyphenylene sulphide or a blend of polyphenylene sulphide and polyam 66 flattened to an essentially rectangular cross-section and numeral 32 represents consecutive weft strands.
  • each warp strand 31 passes over a first weft strand 32, under the second weft strand, over the third and so on.
  • the adjacent warp strand passes under the first weft, over the second, under the third and so on.
  • Figs. 3 and 3A depict a four-shaft eight-repeat duplex-weave dryer fabric 40, which is a type commonly used in the papermaking industry.
  • numerals 41, 42, 43 and 44 are consecutive warp strands, made from polyphenylene sulphide or a blend of polyphenylene sulphide and polyamide 66, flattened to an essentially rectangular cross-section. The weft is paired in two layers and numbered 48 to 57 as shown.
  • a warp strand 41 passes in sequence over a pair of weft strands 50-51, between the next pair 52-53, under the third pair 54-55, between the fourth pair 56-57, and so on.
  • next consecutive warp strand 42 passes between the first pair of weft strands 50-51, over the second pair, between the third pair and under the fourth pair.
  • third and fourth consecutive warp strands 43 and 44 are woven commencing under and between the first pair of weft strands respectively.
  • Fig. 4 depicts the essentially rectangular cross-section of the polyphenylene sulphide or polyphenylene sulphide/polyamide blend warp strands.
  • Such strands may be produced by rolling round monofilament strands, or by slitting film, or, in the preferred embodiment by melt-extruding through a specially shaped die.
  • the flatness ratio a:b of the preferred embodiment shown in Fig. 4 is 2:1 and is preferably between 1.5:1 and 2.5:1 for the woven dryer fabric embodiments.
  • Figs. 5 and 5A depict a spiral construction dryer felt 60 comprising a plurality of helical S-coils 61 joined together with adjacent Z-coils 62 by means of hinge pins 63.
  • the designations 's' and 'Z' indicate the direction of twist, following the convention in the textile industry.
  • the coils 61, 62. are wound using polyphenylene sulphide or polyphenylene sulphide/polyamide blend strand material of essentially rectangular cross-section with a flatness ratio a:b of 2:1 as shown in this preferred embodiment. In this construction a range of flatness ratios between 1.1:1 and 2.5:1 can be used.
  • the woven dryer fabric of the present invention has a warp count preferably in the range of 25 to 80 strands per inch.
  • Warp strands are made from polyphenylene sulphide or a blend of polyphenylene sulphide and polyamide 66.
  • the flattened warp strands of the invention will have major axis measurements in the range of 0.0125" to 0.050". With respect to weft it is not intended to limit the material utilized to monofilaments. Since in the fabric of the invention the weft strands are non- loadbearing, other materials resistant to high temperature and hydrolytic degradation may be utilized, for example composite strands incorporating asbestos or fiberglass.
  • the dryer fabric of spiral construction which is another embodiment of the invention, utilizes helical coils made from polyphenylene sulphide or a blend of polyphenylene sulphide and heat-stabilized polyamide 66 up to 20% by weight of polyamide 66.
  • Hinge pins may be made from the same material or alternatively from other temperature resistant materials such as the composite constructions already mentioned.

Abstract

A dryer fabric for use in a dryer section of a paper machine wherein at least the machine direction components of the fabric are monofilaments made from polyphenylene sulfide or a blend of polyphenylene sulfide with heat-stabilized polyamide 66 when using a blend of the polyamide 66 is present in the range of up to about 20% by weight.

Description

    BACKGROUND OF INVENTION: (a) Field of the Invention
  • The present invention relates to fabrics made of synthetic materials and particularly, but not exclusively, for use in dryer sections of papermaking machines involving high temperature.
  • (b) Description of Prior Art
  • Increasingly dryer fabrics are being manufactured from monofilament strands because such fabrics are easier to keep clean, thus retaining their drying efficiency, and because they are essentially non-absorptive. These are normally of woven construction, but in recent years an alternative non-woven construction is becoming popular - the so-called "spiral fabrics" - which are assembled from a multiplicity of helical coils connected together by inserted hinge pins. German patent DE2419751 and U.S. 4,481,079 describe this type of fabric. The predominant material used in such fabrics, whether woven or spiral, is polyester, with polyamides used less frequently. Unfortunately both of these classes of materials degrade at high temperature, a shortcoming which precludes their use in high temperature applications on paper machines. High temperature applications are ones that result in operating temperatures of about 150°C or above.
  • Some manufacturers of woven fabrics have resorted to NOMEX* or KBVLAR* in order to cope with the extreme conditions prevalent in such high temperature applications. Because neither polymer is melt-extrudable, monofilaments made from them are not practicable and so these materials are employed in the form of composite multifilaments, often resin coated. U.S. 4,159,618 teaches such a monofilament-like composite strand for this purpose, but even these composites are deficient in that they lose tensile strength when exposed to moist or dry heat (see Tables 1-3 in U.S. 4,159,618).
  • Considering now another property of dryer fabrics, it is highly desirable that such fabrics be distortion resistant, that is, have inherent dimensional stability and retain this property so as to resist skewing throughout their life on the paper machine. Woven fabrics made with monofilament warp of round cross-section, and conventional materials such as polyester while having the desirable advantages of running clean and of non-absorptivity already mentioned, are generally deficient in distortion resistance because of the minimal interlocking contact at the warp and weft cross-overs dictated by the geometry of the respective strands. U.S. 4,290,209 discloses the use of rectangular cross-section warp strands having a flattening ratio of about 2:1, whereby the resulting fabric acquires superior properties of distortion resistance and surface smoothness, along with more desirable permeability and elastic modulus. None of these improved fabrics, however, are suitable for high temperature applications, again because of the inherent tendency of the polymers normally used to degrade and lose strength.
  • * Registered Trademark
  • U.S. 4,359,501 discloses an industrial fabric, for use in applications involving elevated temperatures, comprised of melt-extrudable polyaryletherketone monofilament strands. This material, however, suffers the major disadvantage of being so costly that the woven end product is not economically attractive to the specific paper mill end-users already identified.
  • The present invention is directed towards solving these problems.
  • SUMMARY OF INVENTION:
  • Broadly, the present invention provides a dryer fabric for use in a dryer section of a paper machine wherein at least the machine direction components of the fabric are monofilaments made from polyphenylene sulphide or a blend of polyphenylene sulphide with heat-stabilized polyamide 66 with the polyamide 66 being present in the range of up to about 20% by weight.
  • In a preferred embodiment of the invention the polyphenylene sulphide is blended with about 6% by weight of heat-stabilized polyamide 66.
  • In another preferred embodiment the dryer fabric comprises a plurality of interwoven warp and weft strands wherein at least the warps are monofilaments made from polyphenylene sulphide or a blend of polyphenylene sulphide with heat-stabilized polyamide 66 the warp strands having an essentially rectangular cross-section with the long axis of the rectangle lying in the plane of the fabric.
  • In another preferred embodiment the dryer fabric comprises a multiplicity of helical coils connected together by hinge pins wherein at least the helical coils are made from polyphenylene sulphide or a blend of polyphenylene sulphide with heat-stabilized polyamide 66.
  • In another preferred embodiment the dryer fabric comprises a multiplicity of helical coils connected together by hinge pins wherein at least the helical coils are made from polyphenylene sulphide or a blend of polyphenylene sulphide with heat-stabilized polyamide 66 and wherein the helical coils have an essentially rectangular cross-section when viewed in the machine direction with the long axis of the rectangle lying in the plane of the fabric.
  • Monofilaments of the type described above can also be used to advantage in other industrial applications where hydrolysis is encountered.
  • BRIEF DESCRIPTION OF DRAWINGS:
    • FIG. 1 is a schematic view of a typical dryer section as used in a papermaking machine;
    • FIG. 2 is an enlarged sectional view of an all-monofilament plain weave dryer fabric utilizing flattened warp strands;
    • FIG. 2A is a fragmented sectional view along section line A-A of Fig. 2;
    • PIG. 3 is an enlarged sectional view of an all-monofilament four-shaft eight-repeat duplex-weave dryer fabric utilizing flattened warp strands;
    • FIG. 3A is a fragmented sectional view along cross-section line A-A of Fig. 3;
    • FIG 4 is an enlarged cross-section view of the flattened warp strand;
    • FIG. 5 is a plan view of a part of a spiral dryer fabric with flattened spirals; and
    • FIG. 5A is an enlarged sectional view, along cross-section line A-A of fig. 5, of the spiral fabric viewed in the machine direction.
    DETAILED DESCRIPTION OF THE INVENTION:
  • Referring to Fig. 1 there is schematically illustrated a sub-section of a typical dryer section in a papermaking machine (not shown). The top tier dryer cylinders are generally indicated at 10 and the bottom tier at 11. The paper web 13 passes in a serpentine fashion over the top and bottom dryer cylinders as shown. An endless top fabric 14 holds the paper web 13 tightly against the upper cylinders 10 as it passes partially around the first upper cylinder, around a felt roll 15, partially around the remaining top cylinders 10 and around the other intervening felt rolls 15, then around return roll 16, passing over guide and tensioning rolls 24 and 23 respectively, and then over other return rolls 16 before it passes again over the first dryer cylinder to complete the cycle. Similarly, an endless bottom fabric 18 holds the paper web 13 tightly against the lower dryer cylinders 11 as it passes around these and the intervening bottom felt rolls 19, return rolls 21, tensioning roll 25, guide roll 26, and other return rolls 21, substantially as shown.
  • Polyphenylene sulphide is a linear high molecular weight polymer having the repeating unit
    Figure imgb0001
    and is available commercially under the registered trademark RYTON from Phillips Chemical Corporation. While priced at a fraction of the material of U.S. 4,359,501, pure polyphenylene sulphide of the present invention is difficult to extrude. It is also lacking in "toughness" required for industrial weaving.
  • We have found that monofilament polyphenylene sulphide has greatly superior resistance to hydrolytic degradation than the polyester strands commonly used in dryer fabrics. Table 1 shows the results of a test with the percent retained tensile strength of a polyphenylene sulphide strand exposed to saturated ateam at 130°C in a pressure vessel (24 gauge psi) for a period of eight days, along with a polyester monofilament strand of the same size.
    Figure imgb0002
  • Table 2 shows test results for the same materials when exposed to saturated steam at 150°C.
    Figure imgb0003
  • It will be observed that in these accelerated tests the strength of the polyphenylene sulphide strand was not only retained but was, in fact, enhanced whereas the polyester strand showed a rapid and catastrophic loss in strength. This extraordinary retention of hydrolysis resistance, even after prolonged exposure, makes polyphenylene sulphide an outstanding candidate material for use in paper machine dryer fabrics, particularly in high-temperature applications.
  • Unfortunately, the material can only be extruded with difficulty in monofilament form in the size range commonly used in dryer fabrics. Also during weaving the pure material is subject to frequent warp breakages due to its lack of toughness and is prone to scraping in the loom heddles and reed dents, all of which renders pure polyphenylene sulphide difficult for heavy industrial weaving.
  • The addition of a heat-stabilized polyamide 66 to the polyphenylene sulphide before extrusion has greatly alleviated these problems. Experiments in a range of blends has confirmed the following important results:
    • 1. the addition of polyamide 66 acts as a processing aid, which makes the commercial extrusion of the blend a more viable process;
    • 2. ''toughness" is significantly enhanced. For example, the addition of 6% by weight of heat-stabilized polyamide 66 increased the measured knot toughness by a factor of seven times. This property is determined by subjecting a strand, which contains a simple overhand knot, to tensile pull and producing a resulting load-elongation diagram. The area under the curve is a measure of knot toughness;
    • 3. full hydrolytic degradation resistance is retained;
      Figure imgb0004
    • 5. subsequent pilot plant and commercial weaving in a wide range of dryer fabric designs, including those requiring high weaving tensions and high pick counts, confirms that the use of the polyphenylene eulphide/6% polyamide blend in warp strands of dryer fabrics reduced warp breakage and scraping to an acceptable level;
    • 6. increasing the polyamide 66 from 6% to 20% increases the toughness of the monofilament, however,

    the abrasion resistance decreases.
  • The means by which the additive improves toughness while preserving hydrolysis resistance is not entirely known, but the successful monofilaments are characterized by having the additive material present in small, discrete, elongated globules with the long axis parallel to the axis of the monofilament. These discrete globules are not connected to each other or to the outer boundaries of the monofilament, and are thus protected from the harsh environment of the end use application of the filament. In order to preserve the additive as discrete globules we have found that the melt viscosity of the added material must be higher than the melt viscosity of polyphenylene sulphide at the extrusion temperature and the amount of additive must be limited. Another factor to consider in choosing the additive is that it must not degrade during extrusion when it is temporarily exposed to the temperature required to melt the polyphenylene sulphide, the range being 285°c to 315°C. Some additives which satisfy the above mentioned requirements do not form globules because they are chemically incompatible with polyphenylene sulphide and react in unsuitable ways.
  • In our experiments in blending to date, we have found that heat-stabilized polyamide 66 is the only additive to polyphenylene sulphide which successfully imparts the quality of toughness to the resultant monofilament while preserving hydrolysis resistance. Other materials may be found which can also impart the same quality to the blend. Some factors which are important in choosing additives are: a higher viscosity at extrusion temperature than polyphenylene sulphide, chemical compatibility, resistance to heat degradation during extrusion.
  • All types of dryer fabrics having monofilament: in the machine direction will benefit in resistance to hydrolysis from this invention. Three preferred construc tions utilizing rectangular machine direction components are described below but the invention is not limited to these constructions.
  • Figs. 2 and 2A depict a plain weave dryer fabr: 30 representative of a single-layer dryer fabric used in the papermaking industry. In Figs. 2 and 2A numeral 31 denotes consecutive warp strands made from polyphenylene sulphide or a blend of polyphenylene sulphide and polyam 66 flattened to an essentially rectangular cross-section and numeral 32 represents consecutive weft strands. In this structure each warp strand 31 passes over a first weft strand 32, under the second weft strand, over the third and so on. Similarly, the adjacent warp strand passes under the first weft, over the second, under the third and so on.
  • Figs. 3 and 3A depict a four-shaft eight-repeat duplex-weave dryer fabric 40, which is a type commonly used in the papermaking industry. In Figs. 3 and 3A numerals 41, 42, 43 and 44 are consecutive warp strands, made from polyphenylene sulphide or a blend of polyphenylene sulphide and polyamide 66, flattened to an essentially rectangular cross-section. The weft is paired in two layers and numbered 48 to 57 as shown. In this woven structure a warp strand 41 passes in sequence over a pair of weft strands 50-51, between the next pair 52-53, under the third pair 54-55, between the fourth pair 56-57, and so on. The next consecutive warp strand 42 passes between the first pair of weft strands 50-51, over the second pair, between the third pair and under the fourth pair. Similarly, the third and fourth consecutive warp strands 43 and 44 are woven commencing under and between the first pair of weft strands respectively.
  • Fig. 4 depicts the essentially rectangular cross-section of the polyphenylene sulphide or polyphenylene sulphide/polyamide blend warp strands. Such strands may be produced by rolling round monofilament strands, or by slitting film, or, in the preferred embodiment by melt-extruding through a specially shaped die. The flatness ratio a:b of the preferred embodiment shown in Fig. 4 is 2:1 and is preferably between 1.5:1 and 2.5:1 for the woven dryer fabric embodiments.
  • Figs. 5 and 5A depict a spiral construction dryer felt 60 comprising a plurality of helical S-coils 61 joined together with adjacent Z-coils 62 by means of hinge pins 63. The designations 's' and 'Z' indicate the direction of twist, following the convention in the textile industry. The coils 61, 62. are wound using polyphenylene sulphide or polyphenylene sulphide/polyamide blend strand material of essentially rectangular cross-section with a flatness ratio a:b of 2:1 as shown in this preferred embodiment. In this construction a range of flatness ratios between 1.1:1 and 2.5:1 can be used.
  • The woven dryer fabric of the present invention has a warp count preferably in the range of 25 to 80 strands per inch. Warp strands are made from polyphenylene sulphide or a blend of polyphenylene sulphide and polyamide 66. The flattened warp strands of the invention will have major axis measurements in the range of 0.0125" to 0.050". With respect to weft it is not intended to limit the material utilized to monofilaments. Since in the fabric of the invention the weft strands are non- loadbearing, other materials resistant to high temperature and hydrolytic degradation may be utilized, for example composite strands incorporating asbestos or fiberglass.
  • The dryer fabric of spiral construction, which is another embodiment of the invention, utilizes helical coils made from polyphenylene sulphide or a blend of polyphenylene sulphide and heat-stabilized polyamide 66 up to 20% by weight of polyamide 66. Hinge pins may be made from the same material or alternatively from other temperature resistant materials such as the composite constructions already mentioned.
  • In the preferred embodiments above, rectangular shaped monofilaments have been used, but round monofilaments and other cross-sectional shapes may also be used provided they are made from the material of this invention. We have found that woven fabrics made with rectangular warp strands of pure polyphenylene sulphide, and in a different test with warp strands made from a 6% blend of polyamide 66 and polyphenylene sulphide have superior resistance to distortion compared to equivalent fabrics made with monofilament polyester warp material. Thus, the invention can be used to improve the distortion resistance of fabrics made with round monofilaments which is normally troublesome.
  • It is within the ambit of the present invention to cover any obvious modifications of the examples of the preferred embodiment described herein provided such modifications fall within the,scope of the appended claims.

Claims (16)

1. A dryer fabric for use in a dryer section of a paper machine wherein at least the machine direction components of the fabric are monofilaments made from polyphenylene sulfide or a blend of polyphenylene sulfide with heat-stabilized polyamide 66, said polyamide 66 being present in the range of up to about 20% by weight.
2. A dryer fabric as claimed in claim 1 wherein said polyphenylene sulphide is blended with about 6% by weight of heat stabilized polyamide 66.
3. A dryer fabric as claimed in claim 1 wherein said machine direction components are warp strands in a woven dryer fabric.
4. A dryer fabric as claimed in claim 3 wherein said warp strands are flattened warp strands having an essentially rectangular cross-section with the long axis of the rectangle lying in the plane of said fabric.
5. A dryer fabric as claimed in claim 4 wherein said woven dryer fabric has flattened warp strands having an essentially rectangular cross-section with a flatness ratio between 1.5:1 and 2.5:1.
6. A dryer fabric as claimed in claim 1 wherein said machine direction components comprise a plurality of helical coils connected together by hinge pins.
7. A dryer fabric as claimed in claim 6 wherein the monofilament of said helical coils has an essentially rectangular cross-section when viewed in the machine direction with the long axis of the.rectangle lying in the plane of said fabric.
8. A dryer fabric as claimed in claim 7 wherein said rectangular cross-section has a flatness ratio between 1.1:1 and 2.5:1.
9. A dryer fabric for use in a dryer section wherein at least the machine direction components of the fabric are made from monofilaments composed of a blend of polyphenylene sulphide and an additive which imparts toughness to the monofilament while preserving the hydrolysis resistance inherent in polyphenylene sulphide, said additive having characteristics of a higher melt viscosity than the polyphenylene sulphide at extrusion temperatures, resistance to thermal degradation at extrusion temperatures, and chemical compatibility with the polyphenylene sulphide.
10. A synthetic industrial fabric comprising a plurality of interwoven warp and weft monofilament strands made from polyphenylene sulfide.
11. A synthetic industrial fabric as claimed in claim 10 wherein said polyphenylene sulfide is blended with heat stabilized polyamide 66, said polyamide 66 being present in the range of up to about 20% by weight.
12 . A monofilament made from a blend of polyphenylene sulphide and an additive, said additive imparting improved toughness to the resultant monofilament without substantially reducing its hydrolysis resistance, said additive being added to the polyphenylene sulphide in the range of 1% to 20% by weight and having the characteristics of,
- higher viscosity at extrusion temperatures than polyphenylene sulphide;
- resistance to degradation during extrusion;
- chemical compatibility with polyphenylene sulphide.
13. A monofilament as in claim 12 wherein the additive ie heat-stabilized polyamide 66.
14. A monofilament as in claim 13 wherein the heat-stabilized polyamide 66 comprises about 6% by weight of the polyphenylene sulphide.
15. A monofilament as in claim 12 having a flattened essentially rectangular cross-section with an axis ratio between 1.1 to 1 and 3 to 1.
16. A monofilament as in claim 15 with an axis ratio of about 2 to 1.
EP19850105288 1984-05-01 1985-04-30 Dryer fabric having warp strands made of melt-extrudable polyphenylene sulphide Expired - Lifetime EP0161579B1 (en)

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
US60582584A 1984-05-01 1984-05-01
US72766585A 1985-04-26 1985-04-26
US727665 1985-04-26
US605825 2009-10-26

Publications (3)

Publication Number Publication Date
EP0161579A2 true EP0161579A2 (en) 1985-11-21
EP0161579A3 EP0161579A3 (en) 1986-08-13
EP0161579B1 EP0161579B1 (en) 1990-02-07

Family

ID=27085066

Family Applications (1)

Application Number Title Priority Date Filing Date
EP19850105288 Expired - Lifetime EP0161579B1 (en) 1984-05-01 1985-04-30 Dryer fabric having warp strands made of melt-extrudable polyphenylene sulphide

Country Status (4)

Country Link
EP (1) EP0161579B1 (en)
CA (1) CA1261989A (en)
DE (1) DE3575960D1 (en)
FI (1) FI85738C (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0230228A2 (en) * 1986-01-21 1987-07-29 Bayer Ag Method for producing spiral fabric and spiral fabric produced by this method
EP0292186A2 (en) * 1987-05-19 1988-11-23 Shakespeare Company Novel monofilaments, process for the preparation thereof and fabrics thereof
EP0364066A1 (en) * 1988-10-14 1990-04-18 Asten Group Inc. Seam construction for papermakers fabric
EP0425641A1 (en) * 1989-05-12 1991-05-08 Asten Group Inc. Dimensionally stable papermakers fabric
EP0520162A1 (en) * 1991-06-26 1992-12-30 Wangner Systems Corporation Papermaking fabric containing polypropylene terephthalate monofilaments and fibers
US5464685A (en) * 1994-03-25 1995-11-07 Asten, Inc. Textile dryer apparatus having an improved textile dryer fabric
WO2013023276A1 (en) * 2011-08-15 2013-02-21 Astenjohnson, Inc. Embossing fabric including warp yarn sets
CN107988669A (en) * 2018-01-15 2018-05-04 苏州耐德新材料科技有限公司 A kind of modified polyphenyl thioether sewing thread preparation method and its compound filter bag sewing thread

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE4141139C2 (en) * 1991-12-13 1995-08-31 Voith Gmbh J M Screen cloth for a paper machine

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2418826A1 (en) * 1978-03-03 1979-09-28 Huyck Corp FABRICS FOR PAPER MANUFACTURING
US4267227A (en) * 1980-01-11 1981-05-12 Albany International Corp. Press fabric resistant to wad burning
US4290209A (en) * 1978-05-17 1981-09-22 Jwi Ltd. Dryer fabric
EP0063380A2 (en) * 1981-04-20 1982-10-27 E.I. Du Pont De Nemours And Company Abrasion-resistant monofilament with molybdenum disulfide
EP0070708A2 (en) * 1981-07-17 1983-01-26 E.I. Du Pont De Nemours And Company Paper-making belts of fused polymeric filaments

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2418826A1 (en) * 1978-03-03 1979-09-28 Huyck Corp FABRICS FOR PAPER MANUFACTURING
US4290209A (en) * 1978-05-17 1981-09-22 Jwi Ltd. Dryer fabric
US4267227A (en) * 1980-01-11 1981-05-12 Albany International Corp. Press fabric resistant to wad burning
EP0063380A2 (en) * 1981-04-20 1982-10-27 E.I. Du Pont De Nemours And Company Abrasion-resistant monofilament with molybdenum disulfide
EP0070708A2 (en) * 1981-07-17 1983-01-26 E.I. Du Pont De Nemours And Company Paper-making belts of fused polymeric filaments

Cited By (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0230228A3 (en) * 1986-01-21 1989-07-26 Bayer Ag Method for producing spiral fabric and spiral fabric produced by this method
EP0230228A2 (en) * 1986-01-21 1987-07-29 Bayer Ag Method for producing spiral fabric and spiral fabric produced by this method
EP0292186B1 (en) * 1987-05-19 1994-03-23 Shakespeare Company Novel monofilaments, process for the preparation thereof and fabrics thereof
EP0292186A2 (en) * 1987-05-19 1988-11-23 Shakespeare Company Novel monofilaments, process for the preparation thereof and fabrics thereof
EP0364066A1 (en) * 1988-10-14 1990-04-18 Asten Group Inc. Seam construction for papermakers fabric
EP0425641A1 (en) * 1989-05-12 1991-05-08 Asten Group Inc. Dimensionally stable papermakers fabric
EP0425641A4 (en) * 1989-05-12 1991-10-16 Asten Group Inc. Dimensionally stable papermakers fabric
US5240763A (en) * 1989-05-12 1993-08-31 Asten Group, Inc. Dimensionally stable papermakers fabric
EP0520162A1 (en) * 1991-06-26 1992-12-30 Wangner Systems Corporation Papermaking fabric containing polypropylene terephthalate monofilaments and fibers
US5464685A (en) * 1994-03-25 1995-11-07 Asten, Inc. Textile dryer apparatus having an improved textile dryer fabric
US5562968A (en) * 1994-03-25 1996-10-08 Asten, Inc. Textile dryer fabric
WO2013023276A1 (en) * 2011-08-15 2013-02-21 Astenjohnson, Inc. Embossing fabric including warp yarn sets
CN107988669A (en) * 2018-01-15 2018-05-04 苏州耐德新材料科技有限公司 A kind of modified polyphenyl thioether sewing thread preparation method and its compound filter bag sewing thread

Also Published As

Publication number Publication date
FI85738B (en) 1992-02-14
EP0161579B1 (en) 1990-02-07
FI85738C (en) 1992-05-25
DE3575960D1 (en) 1990-03-15
CA1261989A (en) 1989-09-26
EP0161579A3 (en) 1986-08-13
FI851691L (en) 1985-11-02
FI851691A0 (en) 1985-04-29

Similar Documents

Publication Publication Date Title
US4755420A (en) Dryer fabric having warp strands made of melt-extrudable polyphenylene sulphide
CA1117799A (en) Fabrics for papermaking machines
US4481079A (en) Spiral fabric papermakers felt formed from non-circular cross section yarns
US3915202A (en) Fourdrinier papermaking belts
EP0077901B1 (en) Hydrolysis resistant fabric for paper making and like uses
USRE33195E (en) Fabrics for papermaking machines
US20080169040A1 (en) Machine side layer weave design for composite forming fabrics
CN1732293B (en) Grooved-shape monofilaments and the fabrics made thereof
JPH0350037B2 (en)
JP4440085B2 (en) Industrial two-layer fabric
US4820571A (en) High temperature industrial fabrics
MXPA97001552A (en) Fabric of paper manufacturer having ideal pairs in the direction of the machine that are as a s
JPH0583678B2 (en)
US4829681A (en) Paper machine clothing
CA1248799A (en) Abrasion and hydrolysis resistant joining wire and coil material for fabric seams
CA2060972C (en) Dryer fabric
EP0161579B1 (en) Dryer fabric having warp strands made of melt-extrudable polyphenylene sulphide
US4786554A (en) Dryer fabric having warp strands made of melt-extrudable polyphenylene sulphide
CA2527135C (en) Polyamide filament and industrial fabric using the polyamide filament
US7935225B2 (en) Papermaker's forming fabrics including monofilaments comprised of a blend of poly(ethylene naphthalate) and poly(ethylene terephthalate)
EP0387395B1 (en) Stabilized polyurethane modified polyester forming fabric
US4421819A (en) Wear resistant paper machine fabric
US5297590A (en) Papermaking fabric of blended monofilaments
RU2384662C1 (en) Shaping wire of papermaking machine
GB2157328A (en) Improved multilayer forming fabric

Legal Events

Date Code Title Description
PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

AK Designated contracting states

Designated state(s): CH DE FR GB IT LI NL SE

PUAL Search report despatched

Free format text: ORIGINAL CODE: 0009013

AK Designated contracting states

Kind code of ref document: A3

Designated state(s): CH DE FR GB IT LI NL SE

17P Request for examination filed

Effective date: 19870127

17Q First examination report despatched

Effective date: 19880418

GRAA (expected) grant

Free format text: ORIGINAL CODE: 0009210

AK Designated contracting states

Kind code of ref document: B1

Designated state(s): CH DE FR GB IT LI NL SE

ITF It: translation for a ep patent filed

Owner name: BARZANO' E ZANARDO MILANO S.P.A.

REF Corresponds to:

Ref document number: 3575960

Country of ref document: DE

Date of ref document: 19900315

ET Fr: translation filed
PLBI Opposition filed

Free format text: ORIGINAL CODE: 0009260

PLAB Opposition data, opponent's data or that of the opponent's representative modified

Free format text: ORIGINAL CODE: 0009299OPPO

26 Opposition filed

Opponent name: HOECHST AKTIENGESELLSCHAFT, FRANKFURT

Effective date: 19901027

Opponent name: FILZTUCHVERWALTUNGS GMBH

Effective date: 19901107

R26 Opposition filed (corrected)

Opponent name: FILZTUCHVERWALTUNGS GMBH * 901027 HOECHST AKTIENGE

Effective date: 19901107

NLR1 Nl: opposition has been filed with the epo

Opponent name: HOECHST AG

Opponent name: FILZTUCHVERWALTUNGS GMBH

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: LU

Payment date: 19910403

Year of fee payment: 7

ITTA It: last paid annual fee
EPTA Lu: last paid annual fee
PLBM Termination of opposition procedure: date of legal effect published

Free format text: ORIGINAL CODE: 0009276

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: OPPOSITION PROCEDURE CLOSED

27C Opposition proceedings terminated

Effective date: 19911219

NLR2 Nl: decision of opposition
EAL Se: european patent in force in sweden

Ref document number: 85105288.6

REG Reference to a national code

Ref country code: GB

Ref legal event code: IF02

REG Reference to a national code

Ref country code: GB

Ref legal event code: 732E

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: GB

Payment date: 20040220

Year of fee payment: 20

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: FR

Payment date: 20040330

Year of fee payment: 20

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: NL

Payment date: 20040415

Year of fee payment: 20

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: SE

Payment date: 20040416

Year of fee payment: 20

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: CH

Payment date: 20040426

Year of fee payment: 20

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: DE

Payment date: 20040525

Year of fee payment: 20

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: GB

Free format text: LAPSE BECAUSE OF EXPIRATION OF PROTECTION

Effective date: 20050429

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: NL

Free format text: LAPSE BECAUSE OF EXPIRATION OF PROTECTION

Effective date: 20050430

REG Reference to a national code

Ref country code: GB

Ref legal event code: PE20

REG Reference to a national code

Ref country code: CH

Ref legal event code: PL

NLV7 Nl: ceased due to reaching the maximum lifetime of a patent

Effective date: 20050430

EUG Se: european patent has lapsed