WO2001065008A1 - Method of making fibre-based products and their use - Google Patents

Method of making fibre-based products and their use Download PDF

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Publication number
WO2001065008A1
WO2001065008A1 PCT/GB2001/000839 GB0100839W WO0165008A1 WO 2001065008 A1 WO2001065008 A1 WO 2001065008A1 GB 0100839 W GB0100839 W GB 0100839W WO 0165008 A1 WO0165008 A1 WO 0165008A1
Authority
WO
WIPO (PCT)
Prior art keywords
fibres
thermoplastic
refractory
preform
binder
Prior art date
Application number
PCT/GB2001/000839
Other languages
French (fr)
Inventor
John Dinwoodie
Kathleen Elizabeth Wade
Stella Margaret Young
Original Assignee
Saffil 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 Saffil Limited filed Critical Saffil Limited
Priority to AU35786/01A priority Critical patent/AU3578601A/en
Priority to JP2001563689A priority patent/JP2004500495A/en
Priority to US10/220,047 priority patent/US6733628B2/en
Priority to DE60120392T priority patent/DE60120392T2/en
Priority to EP01907919A priority patent/EP1276929B1/en
Publication of WO2001065008A1 publication Critical patent/WO2001065008A1/en

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B26/00Compositions of mortars, concrete or artificial stone, containing only organic binders, e.g. polymer or resin concrete
    • C04B26/02Macromolecular compounds
    • C04B26/04Macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • C04B26/06Acrylates
    • B01J35/58
    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B16/00Use of organic materials as fillers, e.g. pigments, for mortars, concrete or artificial stone; Treatment of organic materials specially adapted to enhance their filling properties in mortars, concrete or artificial stone
    • C04B16/04Macromolecular compounds
    • C04B16/06Macromolecular compounds fibrous
    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B30/00Compositions for artificial stone, not containing binders
    • C04B30/02Compositions for artificial stone, not containing binders containing fibrous materials
    • 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
    • D21H13/36Inorganic fibres or flakes
    • D21H13/46Non-siliceous fibres, e.g. from metal oxides
    • D21H13/48Metal or metallised fibres
    • 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
    • D21H15/00Pulp or paper, comprising fibres or web-forming material characterised by features other than their chemical constitution
    • D21H15/02Pulp or paper, comprising fibres or web-forming material characterised by features other than their chemical constitution characterised by configuration
    • D21H15/10Composite fibres

Definitions

  • the invention relates to a method of making fibre-based products and their use.
  • One particular application of the invention is the manufacture of a mat like article to hold a catalytic converter inside a can at high temperature.
  • a fibre- based article comprising:
  • thermoplastic fibres which comprises fibres having two different melting points, one lower than the other;
  • thermomoulding the preform then cooling under pressure to form the article in another aspect there is provided a dry preform article comprising a major proportion of refractory fibres having a mean length of about 4 cm and a mean diameter of up to about 6 micron, held together by melted thermoplastic fibres and having a substantially uniform density over its area
  • the fibres making up the major proportion are relatively short, say up to 4 cm in length and up to say 6 micron in diameter
  • the fibres are preferably inorganic fibres such as alumina, mullite, silica, zirconia, graphite they may be used alone or with other materials such as intumenescent plate materials, particulates, or any materials like these Combinations may be used
  • the fibres are the ones available under the registered trade mark SAFFIL
  • thermoplastic fibres may be selected from a wide variety of suitable materials having different melting points The choice is determined by compatabihty with the other fibres and the temperature at which the fibres melt The function of this lower melting component is to bond the refractory fibres and hold them together until they are exposed to the temperature at which the thermoplastic fibres are decomposed
  • suitable fibres are olefins such as polyethylene and polypropylene, polyesters polyamines
  • bicomponent fibres which have having a core and a sheath made of different plastics Suitable materials are available from different suppliers, e g "Trevira 255" available from Trevira Fasem, Hartmann Huth, Frankfurt, Germany and "Adhesion C special" fibres available from Fibrevisions Denmark
  • concentration of thermoplastic fibres in the final product may vary, generally we prefer about 10% by weight
  • the binder is preferably a latex
  • the flocculating agent is preferably a polyelectrolyte
  • thermoplastic When the deposited body of wet fibres is heated the water is removed and the lower melting point thermoplastic material melts to bind the fibres to form a substantially self- supporting body The refractory fibres are anchored in the solidified thermoplastic Because of the way in which the article has been made it has substantially the same consistency and density throughout The thermoplastic gives the mat integrity making it easier to handle and process
  • thermoulding under compression provides a dense inorganic fibre mat of bulk density suitable for use, e g in the monolith in the application
  • the process may be batch or continuous
  • the article may be used as a support between the inner surface of a catalytic convertor can and the convertor itself
  • the article may be in the form of mat up to say 8 mm thick which can be used in number of known "canning" techniques
  • the thermoplastic will burn away to provide a porous resilient structure which holds and supports the catalytic body in place over a prolonged period despite the vibration and fluctuations in temperature
  • the resulting composition of fibres or fibres (and mtrumescent particulates if present) exerts a pressure which supports the delicate convertor during its life
  • An advantage of the invention is that because it is so self- supporting and resistant to high temperature it is possible to use a mat of the invention in a high temperature environment, for example in a close coupled application, e g near an engine exhaust manifold
  • the mat may be used in vehicles having gasoline, Diesel engines or the like
  • Alumina fibres measuring about 3 micron in diameter and having a mean length of about 4 cm were added to water in a concentration of about 0 1% by weight to form a slurry
  • the solids were prevented from settling by gentle agitation
  • Bicomponent fibres having a core of polypropylene and a sheath of polyethylene and of a size compatible with the alumina fibres were added in a concentration of 0 01 % by weight
  • a standard acrylate latex was added and dispersed, followed by a flocculating agent The mix was added to a vessel having a perforate floor, and the water was allowed to flow through leaving a pad-like deposit on the floor This was allowed to dry and removed to an oven and heated to about 130°C to fully dry the deposit and to melt the thermoplastic sheath of the bicomponent fibres to bond the alumina fibres together
  • the dry mat was then heated to 150°C and cooled under compression to a thickness of about 5 mm
  • the formed mat was found to be of substantially
  • Portions of the mat were cut into shapes for an infill for a monolith support
  • the shapes were mounted in a can which was positioned in the style of a close coupled catalyst When the catalyst was heated by the exhaust gases the thermoplastic reached its decomposition temperature and burned out, giving the mat a resilient porous fibre structure
  • the support mat was well able to hold the catalyst in the can, despite vibration and variation in temperature
  • Alumina fibres measuring about 3 micron in diameter and having a mean length of about 4 cm were added to water in concentration of about 0 1% by weight to form a slurry
  • the solids were prevented from settling by gentle agitation
  • Bicomponent fibres having a core of polyethylene terphthalate and a sheath of polyethylene and of a size compatible with alumina fibres were added in a concentration of 0 01% by weight
  • a standard acrylate latex was added and dispersed followed by a flocculating polyelectrolyte agent
  • the mix was added to a vessel having a perforate floor and the water was allowed to flow through leaving a pad-like deposit on the floor This was allowed to dry and removed to an oven and heated to about 130°C to fully dry the deposit and to melt the thermoplastic sheath of the fibres to bond the alumina fibres together
  • the dry mat was then heated to 150°C and cooled under compression to a thickness of about 5 mm
  • the formed mat was found to be
  • Portions of the mat were cut into shapes for an infill for a monolith support
  • the shapes were mounted in a can which was positioned in the style of a close coupled catalyst
  • the thermoplastic reached its decomposition temperature and burned out giving the mat a resilient porous fibre structure
  • the support mat was well able to hold the catalyst in the can, despite vibration and variation in temperature

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Ceramic Engineering (AREA)
  • Structural Engineering (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Inorganic Chemistry (AREA)
  • Exhaust Gas After Treatment (AREA)
  • Nonwoven Fabrics (AREA)
  • Yarns And Mechanical Finishing Of Yarns Or Ropes (AREA)
  • Paper (AREA)
  • Preliminary Treatment Of Fibers (AREA)

Abstract

Thermoplastic fibres of different melting points are present in an aqueous slurry of refractory fibres, binder and flocculant. The slurry is passed through a screen to form a wet body which is heated to dry the body and melt the thermoplastic fibres to bind the refractory fibres together.

Description

METHOD OF MAKING FIBRE-BASED PRODUCTS AND THEIR USE
The invention relates to a method of making fibre-based products and their use. One particular application of the invention is the manufacture of a mat like article to hold a catalytic converter inside a can at high temperature.
According to one aspect of the invention there is provided a method of making a fibre- based article, the method comprising:
• forming an aqueous slurry containing a major proportion of refractory fibres and a minor proportion of thermoplastic fibres which comprises fibres having two different melting points, one lower than the other;
• adding a binder and a flocculating agent;
• passing the slurry containing the refractory fibres, thermoplastic fibres, binder and flocculating agent through a perforate screen to deposit a body of wet fibres on the screen;
• heating the body to remove the water and to melt the lower melting point thermoplastic fibres to bind the refractory fibres to form a preform; and
• thermomoulding the preform then cooling under pressure to form the article. In another aspect there is provided a dry preform article comprising a major proportion of refractory fibres having a mean length of about 4 cm and a mean diameter of up to about 6 micron, held together by melted thermoplastic fibres and having a substantially uniform density over its area
Preferably the fibres making up the major proportion are relatively short, say up to 4 cm in length and up to say 6 micron in diameter The fibres are preferably inorganic fibres such as alumina, mullite, silica, zirconia, graphite they may be used alone or with other materials such as intumenescent plate materials, particulates, or any materials like these Combinations may be used Most preferably the fibres are the ones available under the registered trade mark SAFFIL
The thermoplastic fibres may be selected from a wide variety of suitable materials having different melting points The choice is determined by compatabihty with the other fibres and the temperature at which the fibres melt The function of this lower melting component is to bond the refractory fibres and hold them together until they are exposed to the temperature at which the thermoplastic fibres are decomposed Typically suitable fibres are olefins such as polyethylene and polypropylene, polyesters polyamines It is preferred to use bicomponent fibres which have having a core and a sheath made of different plastics Suitable materials are available from different suppliers, e g "Trevira 255" available from Trevira Fasem, Hartmann Huth, Frankfurt, Germany and "Adhesion C special" fibres available from Fibrevisions Denmark The concentration of thermoplastic fibres in the final product may vary, generally we prefer about 10% by weight The binder is preferably a latex, the flocculating agent is preferably a polyelectrolyte
When the deposited body of wet fibres is heated the water is removed and the lower melting point thermoplastic material melts to bind the fibres to form a substantially self- supporting body The refractory fibres are anchored in the solidified thermoplastic Because of the way in which the article has been made it has substantially the same consistency and density throughout The thermoplastic gives the mat integrity making it easier to handle and process
A further step of thermoulding under compression provides a dense inorganic fibre mat of bulk density suitable for use, e g in the monolith in the application
The process may be batch or continuous
The article may be used as a support between the inner surface of a catalytic convertor can and the convertor itself The article may be in the form of mat up to say 8 mm thick which can be used in number of known "canning" techniques When the convertor is first heated the thermoplastic will burn away to provide a porous resilient structure which holds and supports the catalytic body in place over a prolonged period despite the vibration and fluctuations in temperature The resulting composition of fibres or fibres (and mtrumescent particulates if present) exerts a pressure which supports the delicate convertor during its life An advantage of the invention is that because it is so self- supporting and resistant to high temperature it is possible to use a mat of the invention in a high temperature environment, for example in a close coupled application, e g near an engine exhaust manifold The mat may be used in vehicles having gasoline, Diesel engines or the like
In order that the invention may be well understood it will now be described by way of illustration only with reference to the following examples
Example 1
Alumina fibres measuring about 3 micron in diameter and having a mean length of about 4 cm were added to water in a concentration of about 0 1% by weight to form a slurry The solids were prevented from settling by gentle agitation Bicomponent fibres having a core of polypropylene and a sheath of polyethylene and of a size compatible with the alumina fibres were added in a concentration of 0 01 % by weight A standard acrylate latex was added and dispersed, followed by a flocculating agent The mix was added to a vessel having a perforate floor, and the water was allowed to flow through leaving a pad-like deposit on the floor This was allowed to dry and removed to an oven and heated to about 130°C to fully dry the deposit and to melt the thermoplastic sheath of the bicomponent fibres to bond the alumina fibres together The dry mat was then heated to 150°C and cooled under compression to a thickness of about 5 mm The formed mat was found to be of substantially uniform density across its area
Portions of the mat were cut into shapes for an infill for a monolith support The shapes were mounted in a can which was positioned in the style of a close coupled catalyst When the catalyst was heated by the exhaust gases the thermoplastic reached its decomposition temperature and burned out, giving the mat a resilient porous fibre structure The support mat was well able to hold the catalyst in the can, despite vibration and variation in temperature
Example 2
Alumina fibres measuring about 3 micron in diameter and having a mean length of about 4 cm were added to water in concentration of about 0 1% by weight to form a slurry The solids were prevented from settling by gentle agitation Bicomponent fibres having a core of polyethylene terphthalate and a sheath of polyethylene and of a size compatible with alumina fibres were added in a concentration of 0 01% by weight A standard acrylate latex was added and dispersed followed by a flocculating polyelectrolyte agent The mix was added to a vessel having a perforate floor and the water was allowed to flow through leaving a pad-like deposit on the floor This was allowed to dry and removed to an oven and heated to about 130°C to fully dry the deposit and to melt the thermoplastic sheath of the fibres to bond the alumina fibres together The dry mat was then heated to 150°C and cooled under compression to a thickness of about 5 mm The formed mat was found to be of substantially uniform density across its area
Portions of the mat were cut into shapes for an infill for a monolith support The shapes were mounted in a can which was positioned in the style of a close coupled catalyst When the catalyst was heated by the exhaust gases, the thermoplastic reached its decomposition temperature and burned out giving the mat a resilient porous fibre structure The support mat was well able to hold the catalyst in the can, despite vibration and variation in temperature

Claims

A method of making a mat having a substantially consistent density across its area, the method comprising
• forming an aqueous slurry containing a major proportion of refractory fibres and a minor proportion of thermoplastic fibres which comprise fibres having two different melting points, one lower than the other,
• adding a binder and a flocculating agent,
• passing the slurry containing the refractory fibres, thermoplastic fibres, binder and flocculating agent through a perforate screen to deposit a body of wet fibres on the screen,
• heating the body to remove the water and melt the lower melting point fibres to form a preform, and
• thermoforming the preform under pressure to form the article
A method according to Claim 1 , wherein the thermoplastic fibres comprise bicomponent fibres comprising a core and a sheath A method according to Claim 2, wherein the core is polypropylene or polyethylene terephthalate and the sheath is polyethylene
A method according to any preceding Claim, wherein the refractory fibres range up to 4 cm in length and up to 6 micron in diameter
A method according to any preceding Claim, wherein the binder is a latex
A method according to any preceding Claim, wherein the flocculating agent is a polyelectrolyte
A method according to any preceding Claim, wherein the refractory fibres are present in a concentration of about 0 1% by weight in the slurry
A method according to any preceding Claim, wherein the thermoplastic fibres are present in a concentration of about 0 01% by weight in the slurry
A method according to any preceding Claim, wherein the preform is heated to 150°C and cooled under compression
A dry preform article comprising a major proportion of refractory fibres having a mean length of about 4 cm and a mean diameter of about 6 micron, held together by melted thermoplastic fibres and having a substantially uniform density over its area
PCT/GB2001/000839 2000-02-28 2001-02-27 Method of making fibre-based products and their use WO2001065008A1 (en)

Priority Applications (5)

Application Number Priority Date Filing Date Title
AU35786/01A AU3578601A (en) 2000-02-28 2001-02-27 Method of making fibre-based products and their use
JP2001563689A JP2004500495A (en) 2000-02-28 2001-02-27 Process for producing fiber-based products and their use
US10/220,047 US6733628B2 (en) 2000-02-28 2001-02-27 Method of making fibre-based products and their use
DE60120392T DE60120392T2 (en) 2000-02-28 2001-02-27 METHOD FOR PRODUCING FIBER-OPERATED PRODUCTS AND THEIR USE
EP01907919A EP1276929B1 (en) 2000-02-28 2001-02-27 Method of making fibre-based products and their use

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GB0004681.3 2000-02-28
GBGB0004681.3A GB0004681D0 (en) 2000-02-28 2000-02-28 Method of making fibre-based products and their use

Publications (1)

Publication Number Publication Date
WO2001065008A1 true WO2001065008A1 (en) 2001-09-07

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PCT/GB2001/000839 WO2001065008A1 (en) 2000-02-28 2001-02-27 Method of making fibre-based products and their use

Country Status (9)

Country Link
US (1) US6733628B2 (en)
EP (1) EP1276929B1 (en)
JP (1) JP2004500495A (en)
AT (1) ATE329084T1 (en)
AU (1) AU3578601A (en)
DE (1) DE60120392T2 (en)
ES (1) ES2266162T3 (en)
GB (1) GB0004681D0 (en)
WO (1) WO2001065008A1 (en)

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US8182752B2 (en) 2004-06-29 2012-05-22 Unifrax I Llc Exhaust gas treatment device
US8211373B2 (en) 2008-08-29 2012-07-03 Unifrax I Llc Mounting mat with flexible edge protection and exhaust gas treatment device incorporating the mounting mat
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US8349265B2 (en) 2010-08-13 2013-01-08 Unifrax I Llc Mounting mat with flexible edge protection and exhaust gas treatment device incorporating the mounting mat
US8524161B2 (en) 2007-08-31 2013-09-03 Unifrax I Llc Multiple layer substrate support and exhaust gas treatment device
US8679415B2 (en) 2009-08-10 2014-03-25 Unifrax I Llc Variable basis weight mounting mat or pre-form and exhaust gas treatment device
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US8765069B2 (en) 2010-08-12 2014-07-01 Unifrax I Llc Exhaust gas treatment device
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US8951323B2 (en) 2009-09-24 2015-02-10 Unifrax I Llc Multiple layer mat and exhaust gas treatment device
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US8182752B2 (en) 2004-06-29 2012-05-22 Unifrax I Llc Exhaust gas treatment device
US8524161B2 (en) 2007-08-31 2013-09-03 Unifrax I Llc Multiple layer substrate support and exhaust gas treatment device
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US6733628B2 (en) 2004-05-11
ATE329084T1 (en) 2006-06-15
GB0004681D0 (en) 2000-04-19
EP1276929B1 (en) 2006-06-07
DE60120392T2 (en) 2007-05-10
US20030121631A1 (en) 2003-07-03
AU3578601A (en) 2001-09-12
EP1276929A1 (en) 2003-01-22
DE60120392D1 (en) 2006-07-20
JP2004500495A (en) 2004-01-08
ES2266162T3 (en) 2007-03-01

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