Bonded fibrous materials

Information

  • Patent Grant
  • 6987076
  • Patent Number
    6,987,076
  • Date Filed
    Tuesday, September 14, 1999
    25 years ago
  • Date Issued
    Tuesday, January 17, 2006
    19 years ago
Abstract
A composite material comprises inorganic-bonded alkaline earth silicate fibers in which any bonding agents or fillers comprise low amounts of aluminum so that the composite material comprises less than 1% by weight aluminum expressed as Al2—O3.
Description

This invention relates to bonded fibrous materials and is particularly applicable to materials comprising saline soluble fibres bonded with a binder.


Refractory ceramic fibres (RCF) are well known materials and typically comprise an alumino-silicate inorganic fibre formed from an oxide melt which is spun, blown, drawn, or otherwise formed into fibres. Such RCF fibres are used in the manufacture of various industrial and domestic articles. Typical uses of RCF are for applications in which resistance to temperatures in excess of 800° C. is required.


Much RCF fibre is used in the form of needled blankets of fibre in which structural integrity is provided by the fibres that are tangled together in the needling process. (Such products are known as “blanket”). Sometimes a binder is used to lock the fibres together subsequent to exposure to high temperature. Blanket can be processed further to form cut shapes or folded to form insulating modules.


RCF fibre is also used in the production of so-called “Converted Products”. Converted products comprise materials in which the RCF is processed further to provide materials in which the RCF is present as either a minor or major constituent. Typical converted products include the following:—

  • “Board”—substantially rigid flat sheets containing inorganic and/or organic binders produced by a wet process (for example made by dehydrating a suspension of RCF and binders);
  • “Paper”—a flexible fibrous insulating material with a thickness of less than or equal to 6 mm, formed on paper making machinery (for example RCF in sheet form with a binder);
  • “Shapes”—substantially rigid shapes made of ceramic fibre with the addition of inorganic and/or organic binder, fired or unfired (for example, RCF formed by vacuum forming into a variety of shapes);
  • “Fire shapes”—RCF formed by a vacuum forming route and used for domestic and industrial fires either as radiant bodies or for decorative appearance;
  • “Castables”—ceramic fibre with inorganic and/or organic binder which may be cast (for example, RCF in the form of cements, concretes and mortars);
  • “Mastics”—A mouldable material containing RCF with binders and which may be trowelled, hand moulded, or dispensed from a pressure gun and which sets upon drying/heating;
  • “Extrusion”—A mastic-like material that may be used in the manufacture of extruded sections and tubes;
  • “Textiles”—ceramic fibre which has been woven with or without the addition of other filaments, wires, or yarns (for example, RCF formed into rope, yarn, mats and the like by textile technology).


In many of the above mentioned applications binders are used. There are two broad classes of binders:—

  • “Organic binders”—which serve to improve the handling characteristics of the product concerned at low temperatures but which burn off at higher temperatures. Organic binders include, for example, such materials as starch.
  • “Inorganic binders”—which may be effective to improve the handling characteristics of the product concerned at low temperatures, but which also give integrity to the product after exposure to high temperatures. Inorganic binders include, for example, such materials as colloidal silicas, aluminas, and clays.


All of the above materials and concepts are well known in the refractory industry.


Although extremely useful, RCF is an inorganic fibrous material. Inorganic fibrous materials can be either glassy or crystalline. Asbestos is an inorganic fibrous material one form of which has been strongly implicated in respiratory disease.


It is still not clear what the causative mechanism is that relates some asbestos with disease but some researchers believe that the mechanism is mechanical and size related. Asbestos of a critical size can pierce cells in the body and so, through long and repeated cell injury, have a bad effect on health. Whether this mechanism is true or not regulatory agencies have indicated a desire to categorise any inorganic fibre product that has a respiratory fraction as hazardous, regardless of whether there is any evidence to support such categorisation. Unfortunately, for many of the applications for which inorganic fibres are used, there are no realistic substitutes.


Accordingly there is an industry and regulatory demand for inorganic fibres that will pose as little risk as possible (if any) and for which there are objective grounds to believe them safe.


A line of study has proposed that if inorganic fibres were made that were sufficiently soluble in physiological fluids that their residence time in the human body was short; then damage would not occur or at least be minimised. As the risk of asbestos linked disease appears to depend very much on the length of exposure this idea appears reasonable. Asbestos is extremely insoluble.


As intercellular fluid is saline in nature the importance of fibre solubility in saline solution has long been recognised. If fibres are soluble in physiological saline solution then, provided the dissolved components are not toxic, these fibres should be safer than fibres that are not so soluble. Accordingly, in recent years, a number of different types of fibre have been proposed which are refractory and yet soluble in body fluids. Such fibres comprise alkaline earth silicates (e.g. WO87/05007, WO89/12032, WO93/15028, WO94/15883, WO96/02478, and WO97/49643) which are soluble to varying extent in body fluids.


A problem with saline soluble fibres is that by their nature they are more reactive than RCF and therefore cannot always be used as a direct replacement for RCF. The applicants have found that one aspect of this reactivity is that the performance of materials at temperatures in excess of 1100° C. is extremely adversely affected by the presence of aluminium in the binders and fillers conventionally used with RCF. The applicants speculate that this adverse effect is due to a eutectic composition that has been reported to lie at about 1238° C. in the CaO—Al2O3—MgO—SiO2 phase field.


The applicants have further found that sodium and boron badly affect performance of fibres above 1200° C.


Accordingly the present invention provides a composite material comprising bonded alkaline earth silicate fibres in which any bonding agents or fillers comprise low amounts of aluminium so that the composite material comprises less than 1% aluminium expressed as Al2O3. Preferably the composite material comprises less than 0.5% by weight of aluminium expressed as Al2O3. More preferably the composite material comprises less than 0.1% by weight of aluminium expressed as Al2O3. Yet more preferably the composite material is essentially free of aluminium.


In a further feature the composite material comprises less than 1%, preferably less than 0.5%, more preferably less than 0.1% by weight of sodium expressed as Na2O and is still more preferably essentially free of sodium.


In a still further feature the composite material comprises less than 0.5% by weight of boron, preferably less than 0.1% of boron expressed as B2O3.







Further features of the invention are apparent from the claims and the following description, which refers to various applications in which the invention is applicable.


Insulation Board and Shapes.


The invention can be illustrated in its broadest concept by reference to Table 1 which indicate the results of making board using alkaline earth silicate fibres of the SUPERWOOL™ 612™ composition (available from Thermal Ceramics de France SA or Thermal Ceramics Limited). Such fibres have a nominal composition (by weight) of SiO2 64%, CaO 17%, MgO 13.5%, ZrO2 5%, and impurities <0.5%, and are usable at temperatures in excess of 1200° C. and up to 1250° C.


Boards and some shapes are conventionally made by first formulating a suspension of fibre with a cationic organic binder such as a starch and an anionic inorganic binder such as colloidal silica. The cationic organic binder and anionic inorganic binder flocculate, drawing the fibre into a flocculated suspension.


The suspension is placed in contact with mesh moulds and vacuum is applied to the moulds to vacuum form articles either on the outside of the mesh (male mould) or on the inside of the mesh (female mould). Vacuum is applied to the mould until a sufficient thickness of fibre has built up and the mould is then removed from the suspension, the vacuum remaining on for a little while to promote dewatering. This process produces a wet green article containing about 50%–70% water.


At this stage the product is extremely fragile having the consistency of wet cardboard. The wet green article is dried, for example at a temperature of about 150° C. and the organic binder then gives some handling strength. Relatively low amounts of inorganic binder are used in the formation of such materials. A typical recipe for use in vacuum forming would comprise 100 kg of fibre, 25 kg of colloidal silica (a 30% solution i.e. 7.5 kg dry weight), 6.5 kg starch and 1000 gallons (approximately 4500 liters) water. The silica in this formulation amounts to about 0.16% of the suspension formulation and about 7% of the dry materials.


When first fired by the end user of the shape or board the organic binder burns off and the inorganic binder binds the fibres.


Recipes 1, 2 and 3 of Table 1 were tested in the discontinuous manufacture of special shapes. As can be seen Recipe 1 of Table 1 melts at 1250° C. due to the presence of aluminium in the clay. The aluminium reacts with the CaO, MgO, and SiO2 of the fibre to form a eutectic mixture. Although Recipe 1 failed at temperature Recipes 2 and 3 appear to give similar results. Recipes 4 to 10 were tested in the continuous manufacture of board.


Recipe 4 refers to Table 2 to show the effect of aluminium compounds (as aluminium sulphate present in re-cycled wastewater) on high temperature behaviour. This appears to be extremely detrimental.


Recipes 5 and 6 show the effect of adding talc as filler. This appears to improve modulus of rupture and compressive strength. Recipes 5, 7 and 8 allow comparison with other filers, talc giving the best result.


Recipes 5, 9 and 10 allow comparison of the variation of the amount of colloidal silica. Recipe 9 appears the best.



















TABLE 1





Recipe
1
2
3
4
5
6
7
8
9
10

























Fibre
64.0% 
73.3%
76.1%
80.3%
78.1%
75.2%
78.1%
78.1%
76.0%
74.1%


Clay
 24%


Talc


14.2%
15.0%
14.6%
17.5%


13.2%
11.8%


Wollastonite







14.6%


Fumed Silica






14.6%


Colloidal Silica
7.0%
22.8%
6.3%

3.9%
3.9%
3.9%
3.9%
7.6%
11.1%


(30%)


Cationic Starch
5.0%
3.9%
2.8%


Starch



4.1%
2.9%
2.9%
2.9%
2.9%
2.8%
2.7%


Xanthan gum


0.6%
0.6%
0.5%
0.5%
0.5%
0.5%
0.4%
0.3%


Density
313
320
277
303
316
320
304
313
307
296


Modulus of rupture
1.4
0.69
1.2
0.9
0.75
0.87
0.78
0.73
1.26
1.22


by bending (MPa)


M.O.R. at 1150° C.



0.04


M.O.R. at 1200° C.



N.A.
0.2
0.24
0.16
0.11
0.77
0.68


M.O.R. at 1250° C.




0.3
0.39
0.15
N.A.
N.A.
N.A.


Loss on ignition at
5.2
4.5
4.2
3.6
3.6
3.6
3.4
3.4
3.4
3.6


800° C.


Linear shrinkage



see
2.1
2
2.3
1.9
2.6
2.6


24 h-1200° C. (%)



Table


Linear shrinkage
melted
2.1
1.2
2
2.1
2.2
2.5
N.A.
N.A.
N.A.


24 h-1250° C. (%)


Compressive



0.22
0.13
0.15
0.13
0.12
0.22
0.24


strength @ 10%


(MPa)


Compressive



0.1


Strength at 1150° C.


for 10% (MPa)


Compressive



N.A.
0.07
0.09
0.05
0.03
0.20
0.19


Strength at 1200° C.


for 10% (MPa)





















TABLE 2







Al2O3 content
10.2
6.7
6.3
5.1
0.4


(wt %)


Shrinkage at
melted
1.8
1.7
1.6


1150° C. - 24 hours


Shrinkage at
melted
glazed
glazed
glazed
2.3


1200° C. - 24 hours









The recipes of Table 1 resulted in boards having the composition set out in Table 3.



















TABLE 3





Recipe
1
2
3
4
5
6
7
8
9
10

























Fibre
67.3%
87.2%
79.7%
80.3%
80.3%
77.3%
80.3%
80.3%
80.3%
80.3%


Clay
25.2%


Talc


14.8%
15.0%
15.0%
18.0%


13.9%
12.8%


Wollastonite







15.0%


Fumed Silica






15.0%


Colloidal silica
2.2%
8.2%
2.0%

1.2%
1.2%
1.2%
1.2%
2.4%
3.6%


(30%)


Cationic Starch
5.3%
4.6%
2.9%


Starch



4.1%
3.0%
3.0%
3.0%
3.0%
3.0%
3.0%


Xanthan gum


0.6%
0.6%
0.5%
0.5%
0.5%
0.5%
0.4%
0.3%









A typical and useful range of ingredients for making insulating board and shapes by vacuum forming is (in weight percent):—

  • Alkaline earth metal silicate fibre 70–85%
  • Colloidal silica (30% SiO2 by weight) 3–25%
  • Organic binder 1–6%
  • Filler 11–20%


    and from such ingredients typical and useful compositions in the finished board are:—
  • Alkaline earth metal silicate fibre 70–90%
  • Colloidal silica (30% SiO2 by weight) 1–10%
  • Organic binder 1–6%
  • Filler 11–20%


The examples given above have compositions in the range:—

  • Alkaline earth metal silicate fibre 77.3–87.2%
  • Colloidal silica (30% SiO2 by weight) 1.2–8.2%
  • Organic binder 3.3–4.7%
  • Filler 12.8–18%


In all of the above tested compositions the colloidal silica used was Nyacol™ 1430 which has a sodium content of about 0.4% by weight. The amount of colloidal silica binder present was sufficiently low (3.9–22.8% by weight of the colloidal silica translating as approximately 1.2–7 wt % silica binder in the finished product) that the sodium in the binder did not have an appreciable deleterious effect on the properties of the material.


Papers


The same principles apply in the manufacture of papers. In the conventional manufacture of refractory paper slurry is made in like manner to vacuum forming and is cast upon a wire former as in paper making machinery.


The normal flocculant used is alum. The applicants have been able to make refractory fibre paper using acrylic latex binders and an organic flocculant. Such papers have been tested to 1250° C. and while collapsing at 1200° C. the fibres remain in place providing some insulating effect. In contrast, if alum is used as a flocculating agent the paper melts.


A typical recipe (by weight percent) for the paper is:—

  • SUPERWOOL™ 612™ 90–95%
  • Acrylic latex (PRIMAL HA8™ from Rohm & Haas) 5–10%
  • Organic flocculants <1%


Suitable organic flocculants comprise the PERCOL L Series™ from Allied Colloids. These are polyacrylamide based products. In particular PERCOL 230L works well.


Fire Beds, Artificial Coals, and Fire Shapes.


Articles that are directly exposed to flames are in an aggressive environment with temperatures in excess of 1000° C. and exposure to combustion products. Use of conventional binders with alkaline earth metal silicate fibres (SUPERWOOL™ 612™) led to cracking of shapes. The applicants tested a series of compositions by making pieces using different colloidal silica binders each present at the same amount (about 6% by weight). These pieces were heated to 1000° C. for one hour and assessed for cracking, friability, and hardness (Shore ‘o’). The results of these tests are given in Table 4 below:—
















TABLE 4








Specific









Surface




Na2O
Area
Silica


Colloid
pH
(wt %)
(m2/g)
(wt %)
Cracking
Friability
Hardness






















Nyacol ™
10.2
0.4
230
30
Bad
Friable
10–17


1430




fracturing


Syton ™
9.9
0.3
250
30
Some
Fibrous
57


X30




fracture


Levasil ™
9.5
0.17
200
30
Minor
Friable
40


200-A-30




fracture


Bindzil ™
9.7
0.42
220
40
Some
Friable
40


40/220




fracture


Bindzil ™
9.5
<0.1
220
30
Some
Fibrous
47


30NH3/220




fracture









From this it was deduced that:—

  • a) Alkaline pHs were associated with fractured pieces and could be indicative of poor thermal shock resistance; and
  • b) A reduction in Na2O content appears to correlate with friability of the product.


Accordingly, and in view of the growing perception that aluminium, sodium and boron are detrimental to the high temperature performances of alkaline earth metal silicate fibres, the applicants requested their suppliers of colloid (Univar of Croydon, England—distributors for Akzo Nobel) to supply colloidal silica meeting the following requirements not usually called for commercially:—

  • a) The colloidal silica should have a slightly acid to roughly neutral pH, preferably in the range 6.5 to 7.5
  • b) The soda content of the colloidal silica should be low, preferably below 0.1 wt %
  • c) The silica should not have appreciable amounts of aluminium present.


A preliminary experimental product supplied under the reference Bindzil 30/220LPN comprised 30 wt % silica, had a pH of 7.0 and comprised 0.08 wt % Na2O. The same trial as above was repeated using this silica and a product was produced which did not crack and remained fibrous with a Shore ‘o’ hardness of 50. Further samples were made and subjected to a 250 hours cycling test (2 hours on and 2 hours off under gas flame) and passed this test.


Preliminary specifications for the typical colloidal silicas usable to achieve these results are:—













TABLE 5









SiO2 content (by weight)
30
25



Viscosity
<10 cP
<10 cP



pH
6.5–8.0
6.5–8.0



Specific Surface Area (m2/g)
220–240
220–240



Density (g/cm3)
1.192–1.199
1.155–1.175



Na2O content (by weight)
<0.1 
<0.1 










Such silicas are obtainable from Akzo Nobel under the reference Bindzil 30/220LPN or the mark THERMSOL™.


A typical mixture for use in the manufacture of fire shapes comprises:—











TABLE 6







Fibre (e.g. SUPER WOOL 612 ™)
60
parts by weight


Colloidal silica (e.g. THERMSOL ™ =
12–14
parts by weight


Bindzil 30/220 LPN [30% by weight SiO2])


Starch (e.g. PLV available from Avebe,
2.5
parts by weight


Netherlands)









The amount of water used in forming the slurry varies according to application but may for example range from 2700–4500 liters (600–1000 gallons). The fibre typically represents about 0.5–4% by weight of fibre in water. Not all of the ingredients will be incorporated into a vacuum formed product formed from this mixture but typically such a mixture leads to a product comprising approximately 6% by weight colloidal silica, 3.5–5% starch with the balance fibre. The tolerable range for colloidal silica is usually from about 4% to about 9% by weight in the finished product.


Alternative compositions excluding organic binders (useful for such high temperature applications as cooker rings) may be made for example from slurry compositions 1 and 2 below:—











TABLE 7





Component
COMPOSITION 1
COMPOSITION 2







“White water”
50–80% by volume of
90–100% by volume of


component
30% solids
30% solids THERMSOL ™ =



THERMSOL ™ =
Bindzil 30/220 LPN with



Bindzil 30/220 LPN with
10–0% by volume mains



20–50% by volume
water



mains water


Fibre (SUPER-
0.5–4% by weight of
2–3% by weight of solids to


WOOL ™
solids to white water
white water component


612)
component









“White water” is the industry term for a mixture of water and colloidal silica. Such slurry compositions lead to products comprising 15–30% by weight silica with the balance fibre.


Typical ring slurry compositions are, in parts by weight:—


Ring Slurry Composition 1




  • THERMSOL colloidal silica 355

  • Fibre (SUPERWOOL™ 612) 3–5

  • Fresh water 95


    Ring Slurry Composition 2

  • LEVASIL 200-A-40 colloidal silica 750

  • Fibre (spun and chopped SUPERWOOL™ 612) 30

  • Fresh water 250



LEVASIL 200-A-40 differs from LEVASIL 200-A-30, mentioned in Table 4 above, in that in proportion to the amount of silica present LEVASIL 200-A-40 has a lower amount of sodium. Additionally, and very importantly, LEVASIL 200-A-30 is aluminate modified whereas LEVASIL 200-A-40 avoids alumina. LEVASIL 200-A-40 has the characteristics:—

  • Silica content (wt %) 40–41.5
  • Na2O content (wt %) 0.16–0.24
  • Specific Surface Area (m2/g) 180–220
  • pH 8.5–9.5.


The applicants find no deleterious effects in cooker ring production or performance in using LEVASIL 200-A-40. Suitable slurry compositions for rings using a 40% colloidal silica are:—









TABLE 8





Component
















“White water”
65–100% by volume of 40% solids low sodium con-


component
tent colloidal silica having a pH of less than 10 with



35%–0% by volume mains water


Alkaline earth metal
2–3 wt % by weight of solids to white water


silicate fibres, for
component


example chopped


spun fibre









The materials described above under the heading “fire beds, artificial coals, and fire shapes” (see Table 6) can also be used in wider applications such as boards and shapes.


A typical composition for forming boards and shapes is, in parts by weight:—

  • Starch (Solvitose PLV) 4.8
  • THERMSOL colloidal silica 32
  • Fibre (SUPERWOOL™ 612) 80


Generally, the fibre content should preferably be between 0.5 and 5% of the weight of the water. Selection of particular compositions for the wide variety of applications that such bonded fibrous materials are used in is a matter of experiment.


From the above results it can be seen that where the amount of binder used is high the amount of sodium in the binder is best kept low. Similar considerations apply for boron. It should be noted that some colloidal silicas contain aluminium as a counter-ion and such colloidal silicas should be avoided.

Claims
  • 1. A composite material comprising colloidal silica-bonded alkaline earth silicate fibers in which any bonding agents or fillers comprise low amounts of alumina so that the composite material comprises less than 1% by weight aluminium expressed as Al2O3.
  • 2. A composite material as claimed in claim 1 in which the composite material comprises less than 0.5% by weight of aluminium expressed as Al2O3.
  • 3. A composite material as claimed in claim 2 in which the composite material comprises less than 0.1% by weight of aluminium expressed as Al2O3.
  • 4. A composite material as claimed in claim 1 in which the composite material is essentially free of aluminium.
  • 5. A composite material as claimed in claim 1 and comprising less than 1% by weight sodium expressed as Na2O.
  • 6. A composite material as claimed in claim 5 and comprising less than 0.5% by weight sodium expressed as Na2O.
  • 7. A composite material as claimed in claim 6 and comprising less than 0.1% by weight sodium expressed as Na2O.
  • 8. A composite material as claimed in claim 1 in which the composite material is essentially free of sodium.
  • 9. A composite material as claimed in claim 1 and comprising less than 0.5% by weight boron expressed as B2O3.
  • 10. A composite material as claimed in claim 9 and comprising less than 0.1% by weight boron expressed as B2O3.
  • 11. A composite material as claimed in claim 1 in which the alkaline earth silicate fibre is itself adapted for use without excessive shrinkage at temperatures in excess of 1200° C.
  • 12. A composite material as claimed in claim 1 in which the material is obtainable by vacuum forming from a slurry containing the following ingredients in weight %:— Alkaline earth metal silicate fibres 70–85%Colloidal silica (30% SiO2 by weight) 3–25%Organic binder 1–6%Filler 11–20%.
  • 13. A composite material as claimed in claim 1 comprising:— Alkaline earth metal silicate fibres 70–90%Silica binder from colloidal silica (30% SiO2 by weight) 1–10%Organic binder 1–6%Filler 11–20%.
  • 14. A composite material as claimed in claim 13 comprising:— Alkaline earth metal silicate fibres 77.3–87.2%Silica binder from colloidal silica (30% SiO2 by weight) 1.2–8.2%Organic binder 3.3–4.7%Filler 12.8–18%.
  • 15. A composite material as claimed in claim 1 in which the material is a paper comprising:— Alkaline earth metal silicate fibre 90–95%Organic binder 5–10%Organic flocculants <1%.
  • 16. A composite material as claimed in claim 15 in which the organic binder is an acrylic latex.
  • 17. A composite material as claimed in claim 1 in which the material is a material obtained by vacuum forming from a slurry comprising the ingredients: Alkaline earth metal silicate fibre 60 parts by weightColloidal silica (30% by weight SiO2) 12–14 parts by weightStarch 2.5 parts by weight
  • 18. A composite material comprising 4–12% by weight colloidal silica, 3–6.5% starch, balance alkaline earth silicate fibre, to total 100% based on the weight of composite material.
  • 19. A composite material as claimed in claim 18 and comprising 4–9% by weight colloidal silica, 3.5–5% starch, balance alkaline earth silicate fibre, to total 100% based on the weight of composite material.
  • 20. A composite material as claimed in claim 18 comprising about 6% colloidal silica.
  • 21. A composite material as claimed in claim 1 in which the material is a material obtainable by vacuum forming from the ingredients:— White water component 50–80% by volume of 30% solids colloidal silica with 20–50% by volume waterAlkaline earth metal silicate fibre 0.5–4% by weight of fibre, calculated as the weight of the fibre solids per weight of white water component
  • 22. A composite material as claimed in claim 1 in which the material is a material obtainable by vacuum forming from the ingredients:— White water component 90–100% by volume of 30% solids colloidal silica with 10–0% by volume waterAlkaline earth metal silicate fibre 2–3% by weight of fibre, calculated as the weight of the fibre solids per weight of white water component
  • 23. A composite material as claimed in claim 21 and which comprises 15–30% by weight silica binder formed from colloidal silica, balance fibre.
  • 24. A composite material as claimed in claim 17 in which the fibre is present in amounts comprising 0.5–5% by weight of the water in the slurry.
  • 25. A composite material as claimed in claim 1 in which the material is a material obtainable by vacuum forming from the ingredients White water component 65–100% by volume of 40% solids colloidal silica having a pH of less than 10 with 35–0% by volume waterAlkaline earth metal silicate fibre 2–3% by weight of fibre, calculated as weight of fibre solids per weight of white water component
  • 26. A composite material as claimed in claim 22 and which comprises 15–30% by weight colloidal silica, balance fibre.
Priority Claims (1)
Number Date Country Kind
9820124 Sep 1998 GB national
PCT Information
Filing Document Filing Date Country Kind 371c Date
PCT/GB99/03085 9/14/1999 WO 00 3/22/2001
Publishing Document Publishing Date Country Kind
WO00/15574 3/23/2000 WO A
US Referenced Citations (80)
Number Name Date Kind
2051279 Thorndyke Aug 1936 A
2116303 Coss May 1938 A
2155107 Tyler et al. Apr 1939 A
2308857 Bowes Jan 1943 A
2428810 Powell Oct 1947 A
2520168 Powell Aug 1950 A
2520169 Powell Aug 1950 A
2576312 Minnick Nov 1951 A
2577431 Powell Dec 1951 A
2823416 Powell Feb 1958 A
3348956 Ekdahl Oct 1967 A
3449137 Ekdahl Jun 1969 A
3799836 Rogers et al. Mar 1974 A
3835054 Olewinski et al. Sep 1974 A
3887386 Majumdar Jun 1975 A
3969121 Atkinson Jul 1976 A
4014704 Miller Mar 1977 A
4036654 Yale et al. Jul 1977 A
4041199 Cartwright Aug 1977 A
4047965 Karst et al. Sep 1977 A
4054472 Kondo et al. Oct 1977 A
4055434 Chen et al. Oct 1977 A
4153439 Tomic et al. May 1979 A
4205992 Mogensen et al. Jun 1980 A
4238213 Pallo et al. Dec 1980 A
4251279 Ekdahl Feb 1981 A
4274881 Langton et al. Jun 1981 A
4325724 Froberg Apr 1982 A
4342581 Neubauer et al. Aug 1982 A
4351054 Olds Sep 1982 A
4366251 Rapp Dec 1982 A
4377415 Johnson et al. Mar 1983 A
4430369 Payne Feb 1984 A
4437192 Fujiu et al. Mar 1984 A
4443550 Kume et al. Apr 1984 A
4482541 Telfer et al. Nov 1984 A
4555492 Ekdahl et al. Nov 1985 A
4615988 Le Moigne et al. Oct 1986 A
4661134 Hartung Apr 1987 A
4678659 Drake et al. Jul 1987 A
4693740 Noiret et al. Sep 1987 A
4857489 Bearden Aug 1989 A
4873209 Gnyra Oct 1989 A
4957559 Tiesler et al. Sep 1990 A
5032552 Nonami et al. Jul 1991 A
5055428 Porter Oct 1991 A
5108957 Cohen et al. Apr 1992 A
5121748 Ditz et al. Jun 1992 A
5135893 Dohi et al. Aug 1992 A
5217529 Tiesler et al. Jun 1993 A
5248637 Taneda et al. Sep 1993 A
5250488 Thelohan et al. Oct 1993 A
5290350 Besnard et al. Mar 1994 A
5312806 Mogensen May 1994 A
5332699 Olds et al. Jul 1994 A
5346868 Eschner Sep 1994 A
5401693 Bauer et al. Mar 1995 A
5407872 Komori et al. Apr 1995 A
5552213 Eschner Sep 1996 A
5583080 Guldberg et al. Dec 1996 A
5614449 Jensen Mar 1997 A
RE35557 Thelohan et al. Jul 1997 E
5691255 Jensen et al. Nov 1997 A
5714421 Olds et al. Feb 1998 A
5811360 Jubb Sep 1998 A
5821183 Jubb Oct 1998 A
5843854 Karppinen et al. Dec 1998 A
5880046 Delvaux et al. Mar 1999 A
5912201 Couture et al. Jun 1999 A
5928975 Jubb Jul 1999 A
5955389 Jubb Sep 1999 A
5994247 Jubb et al. Nov 1999 A
5997247 Arraitz et al. Dec 1999 A
6037284 Holstein et al. Mar 2000 A
6043172 Hart Mar 2000 A
6043173 Hart Mar 2000 A
6060414 Holstein et al. May 2000 A
6180546 Jubb et al. Jan 2001 B1
6214102 Vandermeer Apr 2001 B1
6287994 Hart Sep 2001 B1
Foreign Referenced Citations (106)
Number Date Country
255803 Jul 1963 AU
2017344 Nov 1990 CA
1 94 2 991 Mar 1970 DE
27 48 127 May 1978 DE
2732 387 Nov 1978 DE
34 44 397 Jun 1986 DE
39 05 394 Sep 1989 DE
44 17 230 Nov 1995 DE
44 17 231 Nov 1995 DE
44 21 120 Dec 1995 DE
44 47 576 May 1996 DE
44 47 577 May 1996 DE
0 019 600 Nov 1980 EP
0 076 677 Apr 1983 EP
0 135 449 Mar 1985 EP
0 144 349 Jun 1985 EP
0 399 320 Nov 1990 EP
0 399 652 Nov 1990 EP
0 412 878 Feb 1991 EP
0 459 897 Dec 1991 EP
0 546 984 Jun 1993 EP
0 091 866 Oct 1993 EP
0 585 547 Mar 1994 EP
0 588 251 Mar 1994 EP
0 591 696 Apr 1994 EP
0 586 797 Jun 1994 EP
0 685 434 Dec 1995 EP
0 710 628 May 1996 EP
0 936 199 Aug 1999 EP
0 115 673 Jul 2001 EP
63007 Dec 1982 FI
1 149 289 Dec 1957 FR
1 165 275 Oct 1958 FR
1 589 410 Mar 1970 FR
2 118 026 Jul 1972 FR
2 662 687 Dec 1991 FR
2 662 688 Dec 1991 FR
520247 Apr 1940 GB
790397 Feb 1958 GB
810773 Mar 1959 GB
1 045 848 Oct 1966 GB
1 204 472 Sep 1970 GB
1 209 244 Oct 1970 GB
1 273 205 May 1972 GB
1 399 556 Jul 1975 GB
1 446 910 Aug 1976 GB
1 462 173 Jan 1977 GB
1 473 908 May 1977 GB
1 532 612 Nov 1978 GB
2 011 379 Jul 1979 GB
2 081 703 Feb 1982 GB
2 083 017 Mar 1982 GB
2 122 537 Jan 1984 GB
2 150 553 Jul 1985 GB
2 164 557 Mar 1986 GB
2 259 700 Mar 1993 GB
49-27620 Mar 1974 JP
51-13819 Feb 1976 JP
51-43429 Apr 1976 JP
51-133311 Nov 1976 JP
52-4519 Jan 1977 JP
52-139113 Nov 1977 JP
56-54252 May 1981 JP
104380 Apr 1942 SE
276349 Jul 1970 SU
259337 Aug 1970 SU
607807 May 1978 SU
WO 8502394 Jun 1985 WO
WO 8604807 Aug 1986 WO
WO 8705007 Aug 1987 WO
WO 8905007 Aug 1987 WO
WO 9002713 Mar 1990 WO
WO 9011756 Oct 1990 WO
WO 9111403 Aug 1991 WO
WO 9207801 May 1992 WO
WO 9309536 Jun 1992 WO
WO 9315028 Aug 1993 WO
WO 9315208 Aug 1993 WO
WO 9319596 Oct 1993 WO
WO 9322251 Nov 1993 WO
WO 9414717 Jul 1994 WO
WO 9414718 Jul 1994 WO
WO 9415883 Jul 1994 WO
WO 9423801 Oct 1994 WO
WO 9521799 Aug 1995 WO
WO 9529135 Nov 1995 WO
WO 9531410 Nov 1995 WO
WO 9531411 Nov 1995 WO
WO 9532925 Dec 1995 WO
WO 9532926 Dec 1995 WO
WO 9532927 Dec 1995 WO
WO 9535265 Dec 1995 WO
WO 9601793 Jan 1996 WO
WO 9602478 Feb 1996 WO
WO 9604213 Feb 1996 WO
WO 04214 Feb 1996 WO
WO 9614274 May 1996 WO
WO 9616913 Jun 1996 WO
WO 9630314 Oct 1996 WO
WO 9716386 May 1997 WO
WO 9720782 Jun 1997 WO
WO 9721636 Jun 1997 WO
WO 9729057 Aug 1997 WO
WO 9730002 Aug 1997 WO
WO 9749643 Dec 1997 WO
WO 9802394 Jan 1998 WO