WO1997049864A1 - Gasket paper - Google Patents

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Publication number
WO1997049864A1
WO1997049864A1 PCT/GB1997/001587 GB9701587W WO9749864A1 WO 1997049864 A1 WO1997049864 A1 WO 1997049864A1 GB 9701587 W GB9701587 W GB 9701587W WO 9749864 A1 WO9749864 A1 WO 9749864A1
Authority
WO
WIPO (PCT)
Prior art keywords
mixture
added
weight
paper
silicate mineral
Prior art date
Application number
PCT/GB1997/001587
Other languages
French (fr)
Inventor
David Geoffrey Hall
Antony Latkowski
Original Assignee
T & N Technology Limited
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 T & N Technology Limited filed Critical T & N Technology Limited
Priority to JP10502481A priority Critical patent/JP2000513053A/en
Priority to EP97926103A priority patent/EP0916001B1/en
Priority to DE69704947T priority patent/DE69704947T2/en
Priority to BR9709944A priority patent/BR9709944A/en
Priority to AU30990/97A priority patent/AU713243B2/en
Publication of WO1997049864A1 publication Critical patent/WO1997049864A1/en

Links

Classifications

    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H13/00Pulp or paper, comprising synthetic cellulose or non-cellulose fibres or web-forming material
    • D21H13/10Organic non-cellulose fibres
    • D21H13/20Organic non-cellulose fibres from macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
    • D21H13/26Polyamides; Polyimides
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H17/00Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/63Inorganic compounds
    • D21H17/67Water-insoluble compounds, e.g. fillers, pigments
    • D21H17/68Water-insoluble compounds, e.g. fillers, pigments siliceous, e.g. clays

Definitions

  • This invention relates to papers particularly, but not exclusively, suitable for use in fluid sealing applications such as cylinder head gaskets. It is known to make gasket papers from non-asbestos formulations based on other fibres such as glass fibres and/or mineral fibres and including a minor proportion of cellulose as a web-forming agent.
  • GB-A-2138854 and 2138855 disclose cellulose-containing compositions using ball clay as a filler.
  • GB-A-2250302 discloses a gasket material which is cellulose-free and which includes a carefully selected mixture of calcined china clay and ball clay as filler.
  • a method of manufacture of a paper stock for dewatering to paper comprising by weight 4-15% aramid fibre pulp, 60-90% silicate mineral, 4-10% polymeric binder and 2-15% inorganic binder, comprises the steps of mixing the aramid fibres in water to produce a slurry of about 2% solids content by weight, diluting the pulp with water, adding the silicate mineral to the mixture, agitating the mixture, further diluting the mixture with water to produce a slurry of about 4% solids content by weight, adding a 10% solution of papermakers alum such that the dry content is about 1% of the total composition, agitating the mixture, adding to the mixture the inorganic binder, adding to the mixture the polymeric binder having a solids content of about 50% by weight, waiting until the polymeric binder is fully dispersed and adding a further quantity of the papermakers alum solution until the supernatant liquid becomes clear.
  • At least some of the silicate mineral is constituted by attapulgite.
  • the inorganic binder is preferably colloidal silica.
  • the polymeric material is preferably nitrile rubber.
  • a particularly preferred paper produced according to the inventive method comprises by weight, 4-8% aramid fibre pulp, 5-8% polymeric binder, 75-90% silicate mineral and 4-10% colloidal silica. It will be appreciated that in the present context "aramid” is a reference to polyaromatic amide material.
  • the formulations of the present invention may be used in at least two different ways.
  • the use of calcined china clay in combination with colloidal silica lends itself to the product of a paper which can be impregnated with a silicone or other resin such as poiybutadiene in order to enhance resistance to and seaiabilty against fluids such as water-antifreeze mixtures and oil.
  • a paper which can be impregnated with a silicone or other resin such as poiybutadiene in order to enhance resistance to and seaiabilty against fluids such as water-antifreeze mixtures and oil.
  • attapulgite it is possible to produce a paper which swells when exposed to water.
  • Such papers can be used without a resin impregnation treatment.
  • the invention therefore includes a process for producing gaskets from the paper of this invention, both with and without a post-treatment with a resin impregnant.
  • testing was carried out by bonding the test paper to both sides of a plain steel core, blanking out annular samples of inside diameter 14.7mm and outside diameter 34.5mm. These were then tested, again based on ASTM F1276, by applying an initial stress of 58.6 MPa. After 22 hours at 300°C the residual stress was measured, the stress relaxation calculated and then normalised to a paper thickness of 1.0mm, in the usual way. This procedure was used throughout the following Examples, including tests on paper made according to prior art.
  • a paper was made having the following composition:
  • the aramid fibres were dispersed in water to give a slurry of around 2% solids content by weight. This pulp had a freeness of 50°SR. The pulp was transferred to a mixing vessel and further diluted with water at 40°C. The calcined china clay was added and the mixture agitated. Further water was added to give a slurry having a solids content of approximately 4% by weight. A 10% solution of papermakers alum was added such that the dry content was approximately 1 % of the total composition. The mixture was agitated for 2 minutes before adding the colloidal silica as a 30% solids content suspension. The mixture was agitated for a further 5 minutes and nitrile rubber added in latex form, having a solids content of around 50%.
  • the nitrile rubber latex was diluted 5:1 with water before adding to the mix. When fully dispersed the latex was then caused to precipitate onto the fibres and fillers by the addition of a further quantity of papermakers alum solution until the supernatant liquid became clear.
  • a paper was produced from the above stock by the conventional technique of dewatering on a wire mesh, pressing and drying, a polyacrylamide flocculant was used to aid processing.
  • the paper was subsequently calendered to the required density using a conventional 2-bowl calender.
  • the resulting paper had the following properties.
  • a conventional paper made according to GB 2250302 showed a stress relaxation of 42% by the same test method.
  • a paper was prepared largely as described above from the following formulation.
  • the paper had the following properties:
  • a sealing test was carried out as described above and the paper was found to seal an internal pressure of 10 bar without detectable leakage at a sealing stress of 10.3 MPa.
  • the paper also sealed 10 bar fluid pressure at a reduced sealing stress of 3.4 MPa.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Dispersion Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Sealing Material Composition (AREA)
  • Paper (AREA)
  • Materials For Medical Uses (AREA)

Abstract

A non-asbestos gasket paper comprises, by weight, 4-15 % aramid fibre pulp, 4-10 % polymeric binder, 60-90 % silicate mineral and 2-15 % inorganic binder.

Description

Gasket Paper
This invention relates to papers particularly, but not exclusively, suitable for use in fluid sealing applications such as cylinder head gaskets. It is known to make gasket papers from non-asbestos formulations based on other fibres such as glass fibres and/or mineral fibres and including a minor proportion of cellulose as a web-forming agent. For example, GB-A-2138854 and 2138855 disclose cellulose-containing compositions using ball clay as a filler. GB-A-2250302 discloses a gasket material which is cellulose-free and which includes a carefully selected mixture of calcined china clay and ball clay as filler.
Whilst these non-asbestos products containing ball clay have good performance in non- critical applications, it has been observed that their behaviour at elevated temperatures is not adequate as regards stress relaxation (or creep), particularly when tested over an extended period of time to simulate actual use. Stress relaxation or creep results in a loss of loading in a bolted joint and can lead to gasket failure, so that in temperature critical applications, better stress retention is very desirable.
It has now been discovered that replacement of the ball clay component by a layered kaolinitic clay or a fibrous chain silicate, or by a mixture of these results in improved stress relaxation performance.
According to the present invention, a method of manufacture of a paper stock for dewatering to paper, comprising by weight 4-15% aramid fibre pulp, 60-90% silicate mineral, 4-10% polymeric binder and 2-15% inorganic binder, comprises the steps of mixing the aramid fibres in water to produce a slurry of about 2% solids content by weight, diluting the pulp with water, adding the silicate mineral to the mixture, agitating the mixture, further diluting the mixture with water to produce a slurry of about 4% solids content by weight, adding a 10% solution of papermakers alum such that the dry content is about 1% of the total composition, agitating the mixture, adding to the mixture the inorganic binder, adding to the mixture the polymeric binder having a solids content of about 50% by weight, waiting until the polymeric binder is fully dispersed and adding a further quantity of the papermakers alum solution until the supernatant liquid becomes clear.
According to a further aspect of the invention, at least some of the silicate mineral is constituted by attapulgite.
The inorganic binder is preferably colloidal silica. The polymeric material is preferably nitrile rubber.
A particularly preferred paper produced according to the inventive method comprises by weight, 4-8% aramid fibre pulp, 5-8% polymeric binder, 75-90% silicate mineral and 4-10% colloidal silica. It will be appreciated that in the present context "aramid" is a reference to polyaromatic amide material.
The formulations of the present invention may be used in at least two different ways. Firstly, the use of calcined china clay in combination with colloidal silica lends itself to the product of a paper which can be impregnated with a silicone or other resin such as poiybutadiene in order to enhance resistance to and seaiabilty against fluids such as water-antifreeze mixtures and oil. Alternatively, by including attapulgite it is possible to produce a paper which swells when exposed to water. Such papers can be used without a resin impregnation treatment.
The invention therefore includes a process for producing gaskets from the paper of this invention, both with and without a post-treatment with a resin impregnant.
Surprisingly, it has been found that by eliminating ball clay (previously regarded as a critical ingredient) in favour of the formulations of the present invention, it is possible to achieve improved stress relaxation performance at elevated temperatures, without using inorganic fibres.
In order that the invention be better understood, preferred embodiments of it will now be described by way of example with reference to the following Examples.
In the interests of clarity, the stress relaxation performance was determined by a method based on ASTM test F1276, the samples being exposed to 300°C for 22 hours. It will be appreciated that the latter is significantly longer than some other tests, but investigation reveals that stress relaxation is appreciably higher after longer exposures, which more closely approximate actual use.
Thus testing was carried out by bonding the test paper to both sides of a plain steel core, blanking out annular samples of inside diameter 14.7mm and outside diameter 34.5mm. These were then tested, again based on ASTM F1276, by applying an initial stress of 58.6 MPa. After 22 hours at 300°C the residual stress was measured, the stress relaxation calculated and then normalised to a paper thickness of 1.0mm, in the usual way. This procedure was used throughout the following Examples, including tests on paper made according to prior art.
Example 1
A paper was made having the following composition:
% by dry weight
Fibrillated Aramid Fibre Pulp 8
Calcined China Clay 76
Nitrile Rubber 6
Colloidal Silica 10
Stock Preparation
The aramid fibres were dispersed in water to give a slurry of around 2% solids content by weight. This pulp had a freeness of 50°SR. The pulp was transferred to a mixing vessel and further diluted with water at 40°C. The calcined china clay was added and the mixture agitated. Further water was added to give a slurry having a solids content of approximately 4% by weight. A 10% solution of papermakers alum was added such that the dry content was approximately 1 % of the total composition. The mixture was agitated for 2 minutes before adding the colloidal silica as a 30% solids content suspension. The mixture was agitated for a further 5 minutes and nitrile rubber added in latex form, having a solids content of around 50%. The nitrile rubber latex was diluted 5:1 with water before adding to the mix. When fully dispersed the latex was then caused to precipitate onto the fibres and fillers by the addition of a further quantity of papermakers alum solution until the supernatant liquid became clear.
Paper Manufacture
A paper was produced from the above stock by the conventional technique of dewatering on a wire mesh, pressing and drying, a polyacrylamide flocculant was used to aid processing. The paper was subsequently calendered to the required density using a conventional 2-bowl calender.
The resulting paper had the following properties.
Thickness 0.83mm
Substance 920gm 2
Density 1100kgm'3
Tensile Strength 4.2 MPa
Compression at 34.5 MPa 14.3%
Stress Relaxation 24.8%
A conventional paper made according to GB 2250302 showed a stress relaxation of 42% by the same test method.
In additional to the above properties the ability of the paper to seal against a mixture of 50% water and 50% antifreeze (w/w) was measured. A sealing stress of 10.3 MPa was applied to an annular sample of the paper and the internal pressure of the water/antifreeze mixture increased in steps of 1 bar. Each pressure was held for a period of 5 minutes and the pressure at which leakage occurred was noted. Samples of the above paper were found to leak at an internal pressure of 2 bar. It was found that the sealing performance of the paper could be dramatically improved by impregnation of the paper with a silicone resin, such that a fluid pressure of 10 bar was sealed.
Example 2
A paper was prepared largely as described above from the following formulation.
% by dry weight
Fibrillated Aramid Fibre Pulp 4
Calcined China Clay 30
Attapulgite 50
Colloidal Silica 10
Nitrile Rubber 6
The paper had the following properties:
Thickness 0.65mm
Substance 860gm'2
Density 1330kgm'3
Tensile Strength 7.0 MPa
Compression at 34.5 MPa 15.3%
Stress Relaxation 29.8%
A sealing test was carried out as described above and the paper was found to seal an internal pressure of 10 bar without detectable leakage at a sealing stress of 10.3 MPa. The paper also sealed 10 bar fluid pressure at a reduced sealing stress of 3.4 MPa.

Claims

1. A method of manufacture of a paper stock for dewatering to paper, comprising by weight 4-15% aramid fibre pulp, 60-90% silicate mineral, 4-10% polymeric binder and 2-15% inorganic binder, comprising the steps of mixing the aramid fibres in water to produce a slurry of about 2% solids content by weight diluting the pulp with water adding the silicate mineral to the mixture agitating the mixture further diluting the mixture with water to produce a slurry of about 4% solids content by weight adding a 10% solution of papermakers alum such that the dry content is about 1% of the total composition agitating the mixture adding to the mixture the inorganic binder adding to the mixture the polymeric binder having a solids content of about 50% by weight waiting until the polymeric binder is fully dispersed and adding a further quantity of the papermakers alum solution until the supernatant liquid becomes clear.
2. A method according to claim 1 in which at least some of the silicate mineral added is constituted by a fibrous chain silicate.
3. A method according to claim 2 in which said added fibrous chain silicate is attapulgite.
4. A method according to any of claims 1-3 in which the silicate mineral added comprises a layered kaoiinitic clay.
5. A method according to claim 4 wherein the added clay comprises calcined china clay.
6. A method according to claim 5 wherein said added chain clay has been calcined at over 800°C.
7. A method according to any of claims 1-6 wherein the inorganic binder added is colloidal silica.
8. A method according to any preceding claim wherein the polymeric binder added is nitrile rubber.
9. A method according to any preceding claim comprising by weight 4-8% aramid fibre pulp, 5-8% polymeric binder, 75-90% silicate mineral, 4-10% inorganic binder.
PCT/GB1997/001587 1996-06-27 1997-06-12 Gasket paper WO1997049864A1 (en)

Priority Applications (5)

Application Number Priority Date Filing Date Title
JP10502481A JP2000513053A (en) 1996-06-27 1997-06-12 Gasket paper
EP97926103A EP0916001B1 (en) 1996-06-27 1997-06-12 Gasket paper
DE69704947T DE69704947T2 (en) 1996-06-27 1997-06-12 SEALING PAPER
BR9709944A BR9709944A (en) 1996-06-27 1997-06-12 Process of making a paper mass to form paper by removing water
AU30990/97A AU713243B2 (en) 1996-06-27 1997-06-12 Gasket paper

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GB9613456A GB2314569B (en) 1996-06-27 1996-06-27 Gasket paper
GB9613456.4 1996-06-27

Publications (1)

Publication Number Publication Date
WO1997049864A1 true WO1997049864A1 (en) 1997-12-31

Family

ID=10795958

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/GB1997/001587 WO1997049864A1 (en) 1996-06-27 1997-06-12 Gasket paper

Country Status (9)

Country Link
EP (1) EP0916001B1 (en)
JP (1) JP2000513053A (en)
KR (1) KR20000015807A (en)
AU (1) AU713243B2 (en)
BR (1) BR9709944A (en)
DE (1) DE69704947T2 (en)
GB (1) GB2314569B (en)
WO (1) WO1997049864A1 (en)
ZA (1) ZA975620B (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102011053389A1 (en) * 2011-09-08 2013-03-14 Elringklinger Ag Sealing arrangement for use in control plate of automatic transmission, has sealing contour elements made of sealing paper and including height profile with height, which varies between minimum height regions and maximum height regions

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2093474A (en) * 1981-02-10 1982-09-02 Texon Inc High Temperature Resistant Gasketing Material Incorporating Organic Fibers
GB2138855A (en) * 1983-04-27 1984-10-31 T & N Materials Res Ltd Gasket paper
GB2138854A (en) * 1983-04-27 1984-10-31 T & N Materials Res Ltd Gasket paper
GB2250302A (en) * 1990-11-29 1992-06-03 T & N Technology Ltd Gasket paper
EP0522441A2 (en) * 1991-07-10 1993-01-13 Akzo N.V. Composition based on aramid staple fibers

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4271228A (en) * 1980-02-04 1981-06-02 Hollingsworth & Vose Company Sheet material containing exfoliated vermiculite
US4330442A (en) * 1980-05-07 1982-05-18 Armstrong World Industries, Inc. Asbestos free gasket forming compositions
US4786670A (en) * 1987-01-09 1988-11-22 Lydall, Inc. Compressible non-asbestos high-temperature sheet material usable for gaskets
GB9106806D0 (en) * 1991-04-02 1991-05-22 T & N Technology Ltd Non-asbestos flexible sheet material
DE4113153A1 (en) * 1991-04-23 1992-10-29 Du Pont Int INDUSTRIAL SEAL FOR USE WITH STEAM

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2093474A (en) * 1981-02-10 1982-09-02 Texon Inc High Temperature Resistant Gasketing Material Incorporating Organic Fibers
GB2138855A (en) * 1983-04-27 1984-10-31 T & N Materials Res Ltd Gasket paper
GB2138854A (en) * 1983-04-27 1984-10-31 T & N Materials Res Ltd Gasket paper
GB2250302A (en) * 1990-11-29 1992-06-03 T & N Technology Ltd Gasket paper
EP0522441A2 (en) * 1991-07-10 1993-01-13 Akzo N.V. Composition based on aramid staple fibers

Also Published As

Publication number Publication date
GB2314569A (en) 1998-01-07
AU3099097A (en) 1998-01-14
AU713243B2 (en) 1999-11-25
BR9709944A (en) 1999-08-10
KR20000015807A (en) 2000-03-15
GB2314569B (en) 2000-01-26
DE69704947T2 (en) 2001-09-06
DE69704947D1 (en) 2001-06-28
JP2000513053A (en) 2000-10-03
GB9613456D0 (en) 1996-08-28
EP0916001A1 (en) 1999-05-19
ZA975620B (en) 1997-12-29
EP0916001B1 (en) 2001-05-23

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