WO2006054498A1 - Shoe press belt - Google Patents

Shoe press belt Download PDF

Info

Publication number
WO2006054498A1
WO2006054498A1 PCT/JP2005/020758 JP2005020758W WO2006054498A1 WO 2006054498 A1 WO2006054498 A1 WO 2006054498A1 JP 2005020758 W JP2005020758 W JP 2005020758W WO 2006054498 A1 WO2006054498 A1 WO 2006054498A1
Authority
WO
WIPO (PCT)
Prior art keywords
hardness
shoe press
belt
polyurethane
liquid substance
Prior art date
Application number
PCT/JP2005/020758
Other languages
French (fr)
Inventor
Jun Ishino
Hiroyuki Takamura
Original Assignee
Ichikawa Co., 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 Ichikawa Co., Ltd. filed Critical Ichikawa Co., Ltd.
Publication of WO2006054498A1 publication Critical patent/WO2006054498A1/en

Links

Classifications

    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21FPAPER-MAKING MACHINES; METHODS OF PRODUCING PAPER THEREON
    • D21F3/00Press section of machines for making continuous webs of paper
    • D21F3/02Wet presses
    • D21F3/0209Wet presses with extended press nip
    • D21F3/0218Shoe presses
    • D21F3/0227Belts or sleeves therefor

Definitions

  • the present invention relates to a shoe press belt useful for a paper shoe press, and particularly to a shoe press belt useful for a shoe press of closed type. More particularly, the invention relates to a shoe press belt having the resin layers composed of polyurethane having a specific composition and hardness, and having excellent physical properties of crack resistance, abrasion resistance, and bending fatigue resistance.
  • a shoe press mechanism 100 comprising a looped shoe press belt 1 interposed between a press roll 101 and a shoe 102 is employed, a wet paper (not shown) is passed between the press roll 101 and the shoe press belt 1 in a press portion formed by the press roll 101 and the shoe 102 to make dehydration, as shown in Fig. 1.
  • the shoe press belt 1 has the resin layers 5, 6 integrally provided on both sides of a substrate 3, and many concave grooves 7 are formed on the surface of a resin layer 5 on the press roll side, as shown in a cross-sectional view of Fig. 2.
  • Water squeezed from a wet paper at the time of pressing is held in the concave grooves 7, and further held water is transferred out of the press portion by the rotation of the belt itself. Therefore, it is required that the projections 8 provided on the resin layer 5 on the press roll side serve to improve the mechanical characteristics in terms of abrasion, bending fatigue, crack, and compression fatigue caused by a vertical pressing force of the press roll 101 and a friction or bending fatigue of the belt in a shoe press area.
  • polyurethane excellent in the crack resistance is broadly employed (e.g., refer to Japanese Patent Unexamined Publication Nos. JP-A-11-247086 and JP-A-2004-52204. ) .
  • the present invention provides a shoe press belt comprised of polyurethane and a substrate, characterized in that the polyurethane contains a non-reactive polydimethylsiloxane liquid substance and has a JIS A hardness of 93° to 96°.
  • the shoe press belt of the invention is composed of polyurethane forming the resin layers, which contains non-reactive polydimethylsiloxane and has a JIS
  • a hardness of 93° to 96° it has more excellent mechanical characteristics such as abrasion resistance, bending fatigue, crack resistance, and compression fatigue resistance than conventionally and is good for service under severe conditions.
  • Fig. 1 is a schematic view showing a shoe press mechanism.
  • Fig. 2 is a cross-sectional view showing a shoe press belt.
  • Fig. 3 is a schematic view showing an apparatus for measuring the occurrence number of cracks.
  • Fig. 4 is a schematic view showing an apparatus for measuring the abrasion loss. Description of Reference Numerals and Signs 1 shoe press belt 3 base substance
  • a shoe press belt of the invention is integrally formed with the resin layers 5, 6 on both sides of a substrate 3, and provided with many concave grooves 7 on a resin layer 5 on the side of a roll press, as shown in Fig. 2.
  • the resin layers 5, 6 are formed of polyurethane containing a non-reactive polydimethylsiloxane liquid substance and having a JIS A hardness (hereinafter referred to as a hardness) of 93° to 96°.
  • Polyurethane containing the non-reactive polydimethylsiloxane liquid substance and having a hardness of 93° to 96° is prepared from urethane prepolymer, a curing agent, and non-reactive polydimethylsiloxane liquid substance by adjusting their mixture ratio to have a hardness of 93° to 96° when cured (hereinafter referred to as a "hardness 93° to 96° product containing non-reactive polydimethylsiloxane liquid substance”) .
  • polyurethane not containing non- reactive polydimethylsiloxane liquid substance prepared by adjusting the mixture ratio of urethane prepolymer and curing agent to have a hardness of 98° (hereinafter referred to as a "hardness 98° product not containing non- reactive polydimethylsiloxane liquid substance")
  • polyurethane containing non-reactive polydimethylsiloxane liquid substance prepared by adjusting the mixture ratio of urethane prepolymer, curing agent and non-reactive silicone oil liquid substance to have a hardness of 90° to 93° hereinafter referred to as "hardness 90° to 93° product containing non-reactive polydimethylsiloxane liquid substance" may be blended.
  • Urethane prepolymer is prepared by reacting an organic diisocyanate and polyol by a well-known method.
  • organic diisocyanate include paraphenylene diisocyanate (PPDI), triden diisocyanate (TODI), isophorone diisocyanate (IPDI) , 4, 4' -methylene bis (phenylisocyanate) (MDI), toluene-2, 4-diisocyanate (2, 4-TDI), toluene-2, 6-diisocyanate (2, ⁇ -TDI), naphthalene-1, 5-diisocyanate (NDI), diphenyl-4, A' - diisocyanate, dibenzyl-4, 4' -diisocyanate, stilbene-4, 4' -diisocyanate, benzophenone-4, 4' -diisocyanate, 1, 3- and 1, 4-xylene diisocyanate, 1, 6-hexamethylene diiso
  • High molecular weight polyol having long chain for example, having a molecular weight (MW) of more than 250, is typically employed to form prepolymer.
  • the high molecular weight polyol having long chain provides the rein flexibility and elastomer property.
  • the high molecular weight polyol typically polyether polyol, polyester polyol, or hydrocarbon polyol having a number average molecular weight of at least 250, is often employed to prepare prepolymer.
  • the molecular weight is preferably from about 500 to 6000, but more preferably in a range from about 650 to about 3000.
  • the high molecular weight polyol has a high molecular weight of about 10,000, and a low molecular weight of about 250.
  • the low molecular weight glycol and triol having a molecular weight of 60 to 250 may be contained.
  • Suitable polyalkyleneetherpolyol is represented by a general formula "HO(RO) n H", where R is alkylene radical, and n is an integer in which polyether polyol has a number average molecular weight of at least 250.
  • Polyalkylene ether polyol is well-known polyurethane product component and prepared by polymerizing cyclic ether, for example, alkylene oxide, glycol, and dihydroxy ether by a well-known method.
  • the average functional group number is from about 2 to about 8, preferably from about 2 to about 3, or more preferably from about 2 to about 2.5.
  • Polyester polyol is typically prepared by reacting dibasic acid (usually adipic acid, but other components, for example, glutaric acid, succinic acid, azelaic acid, sebacic acid, or phthalic anhydride may exist) with diol, for example, ethylene glycol, 1, 2-propylene glycol, 1, 4-butylene glycol, 1, 6-hexylene glycol, diethylene glycol, or polytetramethyleneetherglycol) . If the chain is branched or ultimately bridged, polyol, for example, glycerol, trimethylolpropane, penthaerythritol, or sorbitol can be employed. Diester may be employed instead of dibasic acid. Some of polyester polyol is produced employing caprolactam, or dimerization unsaturated fatty acid.
  • dibasic acid usually adipic acid, but other components, for example, glutaric acid, succinic acid, azelaic acid, sebacic acid, or phthal
  • Hydrocarbon polyol is prepared from ethylene unsaturated polymer, for example, ethylene, isobutylene, and 1, 3-butadiene.
  • polybutadienpolyol is employed, such as "Poly-bd R-45HT” made by Atochem, "DIFOL” made by Amoco Corp., and "Kratone” L polyol” made by Shell Chemical CO.
  • Polycarbonate polyol is also usable, and prepared by reacting glycol (e.g., 1, 6-hexyline glycol) and organic carbonate (e.g., diphenylcarbonate, diethylecarbonate, or ethylenecarbonate) .
  • glycol e.g., 1, 6-hexyline glycol
  • organic carbonate e.g., diphenylcarbonate, diethylecarbonate, or ethylenecarbonate
  • a curing agent or chain elongation agent for use with prepolymer is selected from various kinds of organic diamine or polyol materials which are usually used and well known.
  • Preferable material is solid or liquid having a low melting point.
  • diamine, polyol, and a blend thereof, having a melting point of below 140°C are preferred.
  • diamine or polyol is currently employed as the curing agent for polyurethane in this industry.
  • the curing agent is generally selected on the basis of the required reactivity, required property needed in specific uses, required processing conditions, and a desired pot life.
  • a well-known catalyst may be employed in combination with the curing agent .
  • the curing agent may be aliphatic diol or aromatic diamine.
  • aliphatic diol include 1, 4-butadiendiol, 1, 3-propanediol and 1, 6-hexanediol .
  • aromatic diamine include dimethyl thio toluene diamine (DMTDA), and 3, 3'-dichrolo 4, 4' -diaminodiphenylmethane (MBOCA) .
  • DMTDA and MBOCA are preferable.
  • various isomers of DMTDA exist depending on the substitution position of dimethylthio group and amino group, but may be employed in the form of isomer mixture and is available as "(ETHACURE) 300" made by Albemarle Corporation in United States.
  • the use percentage of urethane prepolymer and the curing agent is adjusted depending on the hardness, but it is preferable that the equivalent ratio of active hydrogen group of curing agent and isocyanate group of urethane prepolymer is from 0.9 to 1.10.
  • the non-reactive polydimethyl siloxane liquid substance is preferably high molecular compound containing siloxane, such as silicone oil, silicone rubber and silicone elastomer.
  • silicone oils such as silicone oil, silicone rubber and silicone elastomer.
  • silicones may be commercially available from Wacker Silicones Corporation with a tradename "Silicone Fluids SWS-101", belonging to the silicone fluids, and "KF96” made by Shinetsu Chemical .
  • the non-reactive polydimethylsiloxane liquid substance may have any viscosity (used as a criterion of chain length in this specification) as far as it is effective to improve the abrasion resistance of the product without losing the friction characteristic of the product containing it. Accordingly, the viscosity is 200,000cst or more, and preferably in a range from 5,000 to 100,000cst.
  • non-reactive polydimethylsiloxane liquid substance is blended at a percentage of 0.5 to 25mass% to the total amount of urethane prepolymer and the curing agent .
  • the shoe press belt is produced by applying and impregnating a mixture of hardness 93° to 96° product containing non-reactive polydimethylsiloxane liquid substance or hardness 93° product containing non-reactive polydimethylsiloxane liquid substance and hardness 98° product not containing non-reactive polydimethylsiloxane liquid substance onto the substrate, curing the mixture by heating, then polishing the surface to have a predetermined thickness, and forming the concave grooves on one surface in the same manner as conventionally, as shown in Fig. 2.
  • the curing conditions are appropriately selected depending on the kind of used product, the heating temperature is from 20 to 150°C, preferably from 90 to 140°C, and the heating time is 30 minutes or longer.
  • the substrate may be a film or knit, narrow strip made of polyamide, polyester, aromatic polyamide, aromatic polyimide, or high strength polyethylene, and wound like spiral, for example.
  • adiprenestream X ⁇ 493" made by Uniroyal hardness 93° product not containing non-reactive polydimethylsiloxane liquid substance (adiprene LF930A made by Uniroyal) , and hardness 98° product not containing non-reactive polydimethylsiloxane liquid substance (adiprene LF600D made by Uniroyal), a mixture of them is applied on both the surfaces of a substrate made from polyester fabric, and cured by heating, whereby the concave grooves (0.5 to 4mm wide, 0.5 to 5mm deep) are formed with the land part interval between adjacent waterways being 2 to 3mm on one surface to produce a belt sample.
  • polyurethane contains no non-reactive polydimethylsiloxane liquid substance.
  • the hardness was measured employing a JIS A durometer.
  • Both ends of a belt sample 51 were pinched by the clamp hands 52, 52, and the clamp hands 52, 52 were linked and reciprocated in the left and right direction in the figure, as shown in Fig. 3.
  • the tension applied on the belt sample 51 was 3kg/cm, and the reciprocation speed was 40cm/sec.
  • the belt sample 51 was carried by a rotary roll 53 and a press shoe 54, and the press shoe 54 was moved in a direction of the rotary roll to pressurize the belt sample 51 with a pressure of 36kg/cm 2 .
  • a lubricant oil was sprayed from the press shoe side onto the belt sample 51 during the reciprocating movement to suppress generation of heat.
  • the belt sample 51 was reciprocated in this way, whereby the number of reciprocations was measured until a crack occurred on a face of the belt sample 51 opposed to the rotary roll.
  • the belt sample 51 was attached on the lower part of a press board 55, and rotated with a rotary roll 56 having a rubber 57 on the outer circumference pressed against a lower face (measurement object face) thereof.
  • the pressure with the rotary roll 56 was 3kg/cm, and the rotation rate of the rotary roll 56 was lOOm/min, whereby the belt sample was rotated for ten minutes. After rotation, a decrease amount in the thickness of the belt sample 51 was measured.
  • Uncured silicone resin (before curing) was filled in the concave grooves of another belt sample, scraped smoothly over the belt grooves by a scoop, and cured under a pressure of 40kg. After curing, resin was taken out of the concave grooves of each belt sample, and the groove sizes (groove width, groove height, groove length) were measured by a microscope, whereby the W reduction ratio under pressure was calculated from the following expression.
  • the belt sample made of polyurethane containing non-reactive polydimethylsiloxane liquid substance and having a hardness of 93° to 96° was more excellent in the crack resistance and the abrasion resistance and had less deformation in the concave grooves than any other belt sample.
  • the shoe press belt of the invention is composed of polyurethane forming the resin layers, which contains non-reactive polydimethylsiloxane and has a JIS
  • a hardness of 93° to 96° it has more excellent mechanical characteristics such as abrasion resistance, bending fatigue, crack resistance, and compression fatigue resistance than conventionally and is good for service under severe conditions .

Landscapes

  • Paper (AREA)
  • Polyurethanes Or Polyureas (AREA)

Abstract

To provide a shoe press belt that is more excellent in the properties such as abrasion resistance, bending fatigue, crack resistance, and compression fatigue resistance, the shoe press belt comprised of polyurethane and a substrate, characterized in that the polyurethane contains a non-reactive polydimethylsiloxane liquid substance and has a JIS A hardness of 93° to 96°.

Description

DESCRIPTION
SHOE PRESS BELT
Technical Field
The present invention relates to a shoe press belt useful for a paper shoe press, and particularly to a shoe press belt useful for a shoe press of closed type. More particularly, the invention relates to a shoe press belt having the resin layers composed of polyurethane having a specific composition and hardness, and having excellent physical properties of crack resistance, abrasion resistance, and bending fatigue resistance.
Background Art
In a shoe press process, a shoe press mechanism 100 comprising a looped shoe press belt 1 interposed between a press roll 101 and a shoe 102 is employed, a wet paper (not shown) is passed between the press roll 101 and the shoe press belt 1 in a press portion formed by the press roll 101 and the shoe 102 to make dehydration, as shown in Fig. 1.
Also, the shoe press belt 1 has the resin layers 5, 6 integrally provided on both sides of a substrate 3, and many concave grooves 7 are formed on the surface of a resin layer 5 on the press roll side, as shown in a cross-sectional view of Fig. 2. Water squeezed from a wet paper at the time of pressing is held in the concave grooves 7, and further held water is transferred out of the press portion by the rotation of the belt itself. Therefore, it is required that the projections 8 provided on the resin layer 5 on the press roll side serve to improve the mechanical characteristics in terms of abrasion, bending fatigue, crack, and compression fatigue caused by a vertical pressing force of the press roll 101 and a friction or bending fatigue of the belt in a shoe press area.
From these reasons, as the material forming the resin layers 5, 6 of the shoe press belt 1, polyurethane excellent in the crack resistance is broadly employed (e.g., refer to Japanese Patent Unexamined Publication Nos. JP-A-11-247086 and JP-A-2004-52204. ) .
However, in recent years, the service environments of the shoe press belt 1 are increasingly severe as the operation speed or the pressure of the press portion is increased owing to higher productivity of paper. Therefore, it is required that various mechanical characteristics are further improved.
Disclosure of the Invention Accordingly, it is an object of the invention to provide a shoe press belt having the excellent properties such as abrasion resistance, bending fatigue resistance, crack resistance, and compression fatigue resistance.
In order to achieve the above object, the present invention provides a shoe press belt comprised of polyurethane and a substrate, characterized in that the polyurethane contains a non-reactive polydimethylsiloxane liquid substance and has a JIS A hardness of 93° to 96°.
Since the shoe press belt of the invention is composed of polyurethane forming the resin layers, which contains non-reactive polydimethylsiloxane and has a JIS
A hardness of 93° to 96°, it has more excellent mechanical characteristics such as abrasion resistance, bending fatigue, crack resistance, and compression fatigue resistance than conventionally and is good for service under severe conditions.
Brief Description of the Drawing
Fig. 1 is a schematic view showing a shoe press mechanism.
Fig. 2 is a cross-sectional view showing a shoe press belt.
Fig. 3 is a schematic view showing an apparatus for measuring the occurrence number of cracks. Fig. 4 is a schematic view showing an apparatus for measuring the abrasion loss. Description of Reference Numerals and Signs 1 shoe press belt 3 base substance
5 resin layer
6 resin layer
7 concave groove
8 projection
Best Mode For Carrying Out the Invention
The present invention will be described below with reference to the accompanying drawings.
A shoe press belt of the invention is integrally formed with the resin layers 5, 6 on both sides of a substrate 3, and provided with many concave grooves 7 on a resin layer 5 on the side of a roll press, as shown in Fig. 2. The resin layers 5, 6 are formed of polyurethane containing a non-reactive polydimethylsiloxane liquid substance and having a JIS A hardness (hereinafter referred to as a hardness) of 93° to 96°.
Polyurethane containing the non-reactive polydimethylsiloxane liquid substance and having a hardness of 93° to 96° is prepared from urethane prepolymer, a curing agent, and non-reactive polydimethylsiloxane liquid substance by adjusting their mixture ratio to have a hardness of 93° to 96° when cured (hereinafter referred to as a "hardness 93° to 96° product containing non-reactive polydimethylsiloxane liquid substance") . Also, polyurethane not containing non- reactive polydimethylsiloxane liquid substance prepared by adjusting the mixture ratio of urethane prepolymer and curing agent to have a hardness of 98° (hereinafter referred to as a "hardness 98° product not containing non- reactive polydimethylsiloxane liquid substance") , and polyurethane containing non-reactive polydimethylsiloxane liquid substance prepared by adjusting the mixture ratio of urethane prepolymer, curing agent and non-reactive silicone oil liquid substance to have a hardness of 90° to 93° (hereinafter referred to as "hardness 90° to 93° product containing non-reactive polydimethylsiloxane liquid substance") may be blended.
Urethane prepolymer is prepared by reacting an organic diisocyanate and polyol by a well-known method. Suitable examples of organic diisocyanate include paraphenylene diisocyanate (PPDI), triden diisocyanate (TODI), isophorone diisocyanate (IPDI) , 4, 4' -methylene bis (phenylisocyanate) (MDI), toluene-2, 4-diisocyanate (2, 4-TDI), toluene-2, 6-diisocyanate (2, β-TDI), naphthalene-1, 5-diisocyanate (NDI), diphenyl-4, A' - diisocyanate, dibenzyl-4, 4' -diisocyanate, stilbene-4, 4' -diisocyanate, benzophenone-4, 4' -diisocyanate, 1, 3- and 1, 4-xylene diisocyanate, 1, 6-hexamethylene diisocyanate, 1, 3-cyclohexyl diisocyanate, 1, 4- cyclohexyl diisocyanate (CHDI), 1, 1' -methylene-bis (4- isocyanate hexamethylene) , three geometrical isomers (abbreviated collectively as Hi2MDI) and their mixtures.
High molecular weight polyol having long chain, for example, having a molecular weight (MW) of more than 250, is typically employed to form prepolymer. The high molecular weight polyol having long chain provides the rein flexibility and elastomer property. The high molecular weight polyol, typically polyether polyol, polyester polyol, or hydrocarbon polyol having a number average molecular weight of at least 250, is often employed to prepare prepolymer. The molecular weight is preferably from about 500 to 6000, but more preferably in a range from about 650 to about 3000. However, the high molecular weight polyol has a high molecular weight of about 10,000, and a low molecular weight of about 250. Moreover, the low molecular weight glycol and triol having a molecular weight of 60 to 250 may be contained.
Suitable polyalkyleneetherpolyol is represented by a general formula "HO(RO)nH", where R is alkylene radical, and n is an integer in which polyether polyol has a number average molecular weight of at least 250. Polyalkylene ether polyol is well-known polyurethane product component and prepared by polymerizing cyclic ether, for example, alkylene oxide, glycol, and dihydroxy ether by a well-known method. The average functional group number is from about 2 to about 8, preferably from about 2 to about 3, or more preferably from about 2 to about 2.5.
Polyester polyol is typically prepared by reacting dibasic acid (usually adipic acid, but other components, for example, glutaric acid, succinic acid, azelaic acid, sebacic acid, or phthalic anhydride may exist) with diol, for example, ethylene glycol, 1, 2-propylene glycol, 1, 4-butylene glycol, 1, 6-hexylene glycol, diethylene glycol, or polytetramethyleneetherglycol) . If the chain is branched or ultimately bridged, polyol, for example, glycerol, trimethylolpropane, penthaerythritol, or sorbitol can be employed. Diester may be employed instead of dibasic acid. Some of polyester polyol is produced employing caprolactam, or dimerization unsaturated fatty acid.
Hydrocarbon polyol is prepared from ethylene unsaturated polymer, for example, ethylene, isobutylene, and 1, 3-butadiene. For example, polybutadienpolyol is employed, such as "Poly-bd R-45HT" made by Atochem, "DIFOL" made by Amoco Corp., and "Kratone" L polyol" made by Shell Chemical CO.
Polycarbonate polyol is also usable, and prepared by reacting glycol (e.g., 1, 6-hexyline glycol) and organic carbonate (e.g., diphenylcarbonate, diethylecarbonate, or ethylenecarbonate) .
A curing agent or chain elongation agent for use with prepolymer is selected from various kinds of organic diamine or polyol materials which are usually used and well known. Preferable material is solid or liquid having a low melting point. Particularly, diamine, polyol, and a blend thereof, having a melting point of below 140°C are preferred. Generally, diamine or polyol is currently employed as the curing agent for polyurethane in this industry. The curing agent is generally selected on the basis of the required reactivity, required property needed in specific uses, required processing conditions, and a desired pot life. A well-known catalyst may be employed in combination with the curing agent .
The curing agent may be aliphatic diol or aromatic diamine. Suitable examples of aliphatic diol include 1, 4-butadiendiol, 1, 3-propanediol and 1, 6-hexanediol . Also, suitable examples of aromatic diamine include dimethyl thio toluene diamine (DMTDA), and 3, 3'-dichrolo 4, 4' -diaminodiphenylmethane (MBOCA) . Among others, DMTDA and MBOCA are preferable. Also, various isomers of DMTDA exist depending on the substitution position of dimethylthio group and amino group, but may be employed in the form of isomer mixture and is available as "(ETHACURE) 300" made by Albemarle Corporation in United States.
The use percentage of urethane prepolymer and the curing agent is adjusted depending on the hardness, but it is preferable that the equivalent ratio of active hydrogen group of curing agent and isocyanate group of urethane prepolymer is from 0.9 to 1.10.
The non-reactive polydimethyl siloxane liquid substance is preferably high molecular compound containing siloxane, such as silicone oil, silicone rubber and silicone elastomer. Those silicones may be commercially available from Wacker Silicones Corporation with a tradename "Silicone Fluids SWS-101", belonging to the silicone fluids, and "KF96" made by Shinetsu Chemical .
The non-reactive polydimethylsiloxane liquid substance may have any viscosity (used as a criterion of chain length in this specification) as far as it is effective to improve the abrasion resistance of the product without losing the friction characteristic of the product containing it. Accordingly, the viscosity is 200,000cst or more, and preferably in a range from 5,000 to 100,000cst.
Also, the non-reactive polydimethylsiloxane liquid substance is blended at a percentage of 0.5 to 25mass% to the total amount of urethane prepolymer and the curing agent .
The shoe press belt is produced by applying and impregnating a mixture of hardness 93° to 96° product containing non-reactive polydimethylsiloxane liquid substance or hardness 93° product containing non-reactive polydimethylsiloxane liquid substance and hardness 98° product not containing non-reactive polydimethylsiloxane liquid substance onto the substrate, curing the mixture by heating, then polishing the surface to have a predetermined thickness, and forming the concave grooves on one surface in the same manner as conventionally, as shown in Fig. 2. Though the curing conditions are appropriately selected depending on the kind of used product, the heating temperature is from 20 to 150°C, preferably from 90 to 140°C, and the heating time is 30 minutes or longer.
The substrate may be a film or knit, narrow strip made of polyamide, polyester, aromatic polyamide, aromatic polyimide, or high strength polyethylene, and wound like spiral, for example.
Examples
This invention will be described below by way of example, but is not limited to those examples.
Examples 1 to 8 and comparative examples 1 to 12
Employing hardness 93° product containing non- reactive polydimethylsiloxane liquid substance
(adiprenestream XΕ493" made by Uniroyal) , hardness 93° product not containing non-reactive polydimethylsiloxane liquid substance (adiprene LF930A made by Uniroyal) , and hardness 98° product not containing non-reactive polydimethylsiloxane liquid substance (adiprene LF600D made by Uniroyal), a mixture of them is applied on both the surfaces of a substrate made from polyester fabric, and cured by heating, whereby the concave grooves (0.5 to 4mm wide, 0.5 to 5mm deep) are formed with the land part interval between adjacent waterways being 2 to 3mm on one surface to produce a belt sample. In the comparative examples 1 to 12, polyurethane contains no non-reactive polydimethylsiloxane liquid substance.
And for each belt sample, (1) hardness, (2) occurrence number of cracks, (3) abrasion loss and (4) W reduction ratio under pressure were measured. A measuring method is as follows, and the results are listed in the table. ( 1 ) Hardness
The hardness was measured employing a JIS A durometer.
(2) Occurrence number of cracks
Both ends of a belt sample 51 were pinched by the clamp hands 52, 52, and the clamp hands 52, 52 were linked and reciprocated in the left and right direction in the figure, as shown in Fig. 3. At this time, the tension applied on the belt sample 51 was 3kg/cm, and the reciprocation speed was 40cm/sec. Also, the belt sample 51 was carried by a rotary roll 53 and a press shoe 54, and the press shoe 54 was moved in a direction of the rotary roll to pressurize the belt sample 51 with a pressure of 36kg/cm2. A lubricant oil was sprayed from the press shoe side onto the belt sample 51 during the reciprocating movement to suppress generation of heat. The belt sample 51 was reciprocated in this way, whereby the number of reciprocations was measured until a crack occurred on a face of the belt sample 51 opposed to the rotary roll.
(3) Abrasion loss
Employing an apparatus as shown in Fig. 4, the belt sample 51 was attached on the lower part of a press board 55, and rotated with a rotary roll 56 having a rubber 57 on the outer circumference pressed against a lower face (measurement object face) thereof. At this time, the pressure with the rotary roll 56 was 3kg/cm, and the rotation rate of the rotary roll 56 was lOOm/min, whereby the belt sample was rotated for ten minutes. After rotation, a decrease amount in the thickness of the belt sample 51 was measured.
(4) W reduction ratio under pressure
Two belt samples were prepared, uncured silicone resin (before curing) was filled in the concave grooves of one belt sample, scraped smoothly over the belt grooves by a scoop, and cured without pressure.
Uncured silicone resin (before curing) was filled in the concave grooves of another belt sample, scraped smoothly over the belt grooves by a scoop, and cured under a pressure of 40kg. After curing, resin was taken out of the concave grooves of each belt sample, and the groove sizes (groove width, groove height, groove length) were measured by a microscope, whereby the W reduction ratio under pressure was calculated from the following expression.
[ (W without pressure - W under pressure) /W without pressure] xlOO%
Figure imgf000015_0001
As seen from the table, the belt sample made of polyurethane containing non-reactive polydimethylsiloxane liquid substance and having a hardness of 93° to 96° was more excellent in the crack resistance and the abrasion resistance and had less deformation in the concave grooves than any other belt sample.
While there has been described in connection with the preferred embodiments of the present invention, it will be obvious to those skilled in the art that various changes and modification may be made therein without departing from the present invention, and it is aimed, therefore, to cover in the appended claim all such changes and modifications as fall within the true spirit and scope of the present invention.
Industrial Applicability
Since the shoe press belt of the invention is composed of polyurethane forming the resin layers, which contains non-reactive polydimethylsiloxane and has a JIS
A hardness of 93° to 96°, it has more excellent mechanical characteristics such as abrasion resistance, bending fatigue, crack resistance, and compression fatigue resistance than conventionally and is good for service under severe conditions .

Claims

1. A shoe press belt comprised of polyurethane and a substrate, characterized in that said polyurethane contains a non-reactive polydimethylsiloxane liquid substance and has a JIS A hardness of 93° to 96°.
2. The shoe press belt according to claim 1, characterized in that said polyurethane is a mixture of polyurethane having a JIS A hardness of 90° to 93° and containing a non-reactive polydimethylsiloxane liquid substance, and polyurethane having a JIS A hardness of 98C and not containing a non-reactive polydimethylsiloxane liquid substance.
PCT/JP2005/020758 2004-11-16 2005-11-07 Shoe press belt WO2006054498A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP2004332179A JP2006144139A (en) 2004-11-16 2004-11-16 Belt for shoe press
JP2004-332179 2004-11-16

Publications (1)

Publication Number Publication Date
WO2006054498A1 true WO2006054498A1 (en) 2006-05-26

Family

ID=35532546

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/JP2005/020758 WO2006054498A1 (en) 2004-11-16 2005-11-07 Shoe press belt

Country Status (2)

Country Link
JP (1) JP2006144139A (en)
WO (1) WO2006054498A1 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7955475B2 (en) 2009-07-21 2011-06-07 Ichikawa Co., Ltd. Papermaking shoe press belt
WO2014037268A1 (en) * 2012-09-04 2014-03-13 Voith Patent Gmbh Pressing strip in a paper machine
EP4159917A1 (en) * 2021-09-30 2023-04-05 Valmet Technologies Oy Belt

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009057641A (en) * 2005-12-26 2009-03-19 Ichikawa Co Ltd Belt for transporting wet paper
JP4516584B2 (en) * 2006-10-03 2010-08-04 イチカワ株式会社 Shoe press belt for papermaking
JP4516583B2 (en) 2007-05-18 2010-08-04 イチカワ株式会社 Shoe press belt
US7943013B2 (en) 2007-06-25 2011-05-17 Ichikawa Co., Ltd. Shoe press belt for paper making
JP4516610B2 (en) 2008-02-08 2010-08-04 イチカワ株式会社 Shoe press belt
WO2014200095A1 (en) 2013-06-14 2014-12-18 イチカワ株式会社 Shoe press belt for papermaking

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0576115A1 (en) * 1992-06-11 1993-12-29 Albany International Corp. Transfer belt
EP0939162A2 (en) * 1998-02-26 1999-09-01 Ichikawa Co.,Ltd. Shoe press belt and method of manufacture
EP1382738A1 (en) * 2002-07-19 2004-01-21 Ichikawa Co.,Ltd. Belt for paper making machine and manufacturing method therefor

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0576115A1 (en) * 1992-06-11 1993-12-29 Albany International Corp. Transfer belt
EP0939162A2 (en) * 1998-02-26 1999-09-01 Ichikawa Co.,Ltd. Shoe press belt and method of manufacture
EP1382738A1 (en) * 2002-07-19 2004-01-21 Ichikawa Co.,Ltd. Belt for paper making machine and manufacturing method therefor

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7955475B2 (en) 2009-07-21 2011-06-07 Ichikawa Co., Ltd. Papermaking shoe press belt
WO2014037268A1 (en) * 2012-09-04 2014-03-13 Voith Patent Gmbh Pressing strip in a paper machine
EP4159917A1 (en) * 2021-09-30 2023-04-05 Valmet Technologies Oy Belt

Also Published As

Publication number Publication date
JP2006144139A (en) 2006-06-08

Similar Documents

Publication Publication Date Title
WO2006054498A1 (en) Shoe press belt
JP4516610B2 (en) Shoe press belt
WO2016163350A1 (en) Shoe press belt
US7955475B2 (en) Papermaking shoe press belt
EP1609905A1 (en) Papermaking machine belt and method for manufacturing a papermaking machine belt
CA2687552C (en) Shoe press belt
RU2513406C2 (en) Shoe press belt
US20060118261A1 (en) Shoe press belt
JP2008111220A (en) Shoe press belt for papermaking
EP2623667B1 (en) Paper making shoe press belt
EP1574536A1 (en) Papermaking machine belt and method for producing the same
EP2623668A1 (en) Paper making shoe press belt
CN1712636A (en) Papermaking machine belt
CN111527260B (en) Shoe press belt
EP4124628B1 (en) Papermaking device and method for producing papermaking device

Legal Events

Date Code Title Description
AK Designated states

Kind code of ref document: A1

Designated state(s): AE AG AL AM AT AU AZ BA BB BG BR BW BY BZ CA CH CN CO CR CU CZ DE DK DM DZ EC EE EG ES FI GB GD GE GH GM HR HU ID IL IN IS KE KG KM KN KP KR KZ LC LK LR LS LT LU LV LY MA MD MG MK MN MW MX MZ NA NG NI NO NZ OM PG PH PL PT RO RU SC SD SE SG SK SL SM SY TJ TM TN TR TT TZ UA UG UZ VC VN YU ZA ZM ZW

AL Designated countries for regional patents

Kind code of ref document: A1

Designated state(s): BW GH GM KE LS MW MZ NA SD SL SZ TZ UG ZM ZW AM AZ BY KG KZ MD RU TJ TM AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HU IE IS IT LT LU LV MC NL PL PT RO SE SI SK TR BF BJ CF CG CI CM GA GN GQ GW ML MR NE SN TD TG

121 Ep: the epo has been informed by wipo that ep was designated in this application
NENP Non-entry into the national phase

Ref country code: DE

122 Ep: pct application non-entry in european phase

Ref document number: 05805891

Country of ref document: EP

Kind code of ref document: A1

WWW Wipo information: withdrawn in national office

Ref document number: 5805891

Country of ref document: EP