WO2001023315A1 - Procedes de formation de fibres anorganiques - Google Patents
Procedes de formation de fibres anorganiques Download PDFInfo
- Publication number
- WO2001023315A1 WO2001023315A1 PCT/GB2000/003590 GB0003590W WO0123315A1 WO 2001023315 A1 WO2001023315 A1 WO 2001023315A1 GB 0003590 W GB0003590 W GB 0003590W WO 0123315 A1 WO0123315 A1 WO 0123315A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- fibres
- fibre
- volatile component
- strontium
- melting
- Prior art date
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03C—CHEMICAL COMPOSITION OF GLASSES, GLAZES OR VITREOUS ENAMELS; SURFACE TREATMENT OF GLASS; SURFACE TREATMENT OF FIBRES OR FILAMENTS MADE FROM GLASS, MINERALS OR SLAGS; JOINING GLASS TO GLASS OR OTHER MATERIALS
- C03C13/00—Fibre or filament compositions
Definitions
- This invention relates to methods of making man-made inorganic oxide fibres containing strontium oxide.
- the invention also relates to products formed by such methods.
- Inorganic fibrous materials are well known and widely used for many purposes (e.g. as thermal or acoustic insulation in bulk, mat, or blanket form, as vacuum formed shapes, as vacuum formed boards and papers, and as ropes, yarns or textiles; as a reinforcing fibre for building materials; as a constituent of brake blocks for vehicles).
- thermal or acoustic insulation in bulk, mat, or blanket form as vacuum formed shapes, as vacuum formed boards and papers, and as ropes, yarns or textiles; as a reinforcing fibre for building materials; as a constituent of brake blocks for vehicles.
- the properties for which inorganic fibrous materials are used require resistance to heat, and often resistance to aggressive chemical environments.
- 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.
- fibres 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, the fibres should be safer than fibres that are not so soluble. The shorter the time a fibre is resident in the body the less damage it can do.
- Refractory fibres generally are formed by the steps of: -
- the disruption can be by many methods but typically a jet of air is used (blowing) or the stream impinges on spinning discs (spinning) although other methods such as centrifugal formation of fibres have been proposed.
- Strontium is found chiefly as the minerals celestite (SrS0 4 ) and strontianite (SrC0 3 ).
- Use of a sulphate such as SrS0 4 would be hazardous since on melting copious amounts of sulphur dioxide would be produced which would be hazardous and corrosive and would require complex and expensive extraction apparatus.
- the present invention provides a method of fo ⁇ ning fibres comprising SrO, A1 2 0 3 , and a fibre-forming additive, the method comprising the steps of a) mixing:- i) a compound of strontium which on heating loses a volatile component ii) A1 2 0 3> and iii) a fibre fo ⁇ ning additive b) calcining the mixture to remove the volatile component c) melting the calcined mixture d) disrupting the melt to form fibres.
- the present invention provides a method of forming fibres comprising SrO, A1 2 0 3 , and a fibre-forming additive, the method comprising the steps of:- a) mixing: - i) a compound of strontium which on heating loses a predominantly non-toxic volatile component ii) A1 2 0 3> and iii) a fibre forming additive b) forming granules from the mixture of a sufficient size to resist ejection from the melt by outgassing c) melting the granules and extracting the predominantly non-toxic volatile component d) disrupting the melt to form fibres
- the first alternative has the advantages that:- a) no additional gas extraction is required at the melting step, evolution of gas taking place primarily or entirely on calcining b) a stable non-irritant intermediate (in the form of the calcined mixture) is produced which is easy to handle and/or transport c) it does not involve significant outgassing at the melting stage d) extraction of gas takes
- the second alternative has the advantages that:- a) a stable non-irritant intermediate (in the form of the granulated mixture) is produced which is easy to handle and/or transport b) although there is significant outgassing at the melting stage the granulated product is sufficiently heavy to resist ejection from the melt c) the granules provide a continuous path between granules by which the gas can escape without causing explosive eruptions in the batch above the melt. but has the disadvantage that an additional processing step is required and gas extraction is required at the melting step. If no localised extraction is present then the amount of toxic volatile components in the predominantly non-toxic volatile component must be kept low to minimise worker exposure. For example, if no extraction is provided and SrC0 3 is used as the strontium compound it must have a low S0 3 content, e.g. of ⁇ 0.1%, preferably ⁇ 0.05%.
- the A1 2 0 3 and/or the fibre forming additive or part thereof may be in the form of compounds with a volatile component that is lost on melting.
- the strontium is in the form of a carbonate.
- compositions plotted in Fig.l include those described in WO96/04214. Such compositions may contain impurities and these should amount to less than 10%, preferably to less than 5%, of the composition so that the compositions comprise more than 90%, preferably more than 95% SrO-Al 2 0 3 -Si0 2 .
- the compositions contain less than 3wt%, more advantageously less than 2wt% and still more advantageously less than lwt% incidental impurities.
- the compositions were tested for shrinkage and the results, normalised to 100% SrO-Al 2 0 3 -Si0 2 , are plotted on the three co-ordinate graph of Fig.1. Contours are drawn around the compositions tested as having shrinkage of less than 3.5% at 1260°C, 1300°C, 1400°C, 1450°C, 1500°C, and 1550°C respectively.
- Provision of high capacity gas extraction in a commercial fibre forming plant would add considerably to the cost and complexity of the plant. Loss of powder from the melting chamber would not only create a mess in a commercial fibre forming plant it would also make it difficult to form fibres of a consistent quality.
- one method of producing fibre includes the step of providing an initial charge of calcined or granulated material, melting these materials to form a melt pool, and adding un-calcined or un-granulated material to the melt pool at a sufficiently low rate not to produce explosive evolution of gas.
- a prefe ⁇ ed range of compositions specified in WO96/04214 was that the fibres comprise at least 90%, preferably at least 95%, by weight SrO, A1 2 0 3 , and a fibre forming additive, and had a composition comprising: - SrO 41.2wt% - 63.8wt%
- the applicant's cu ⁇ ently prefe ⁇ ed range is that formed by the >1400°C contour of Fig.l and in particular the composition:-
- incidental impurities ⁇ 3wt% preferably less than 2wt%, more preferably less than lwt%.
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Geochemistry & Mineralogy (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Inorganic Fibers (AREA)
Abstract
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AU73017/00A AU7301700A (en) | 1999-09-27 | 2000-09-19 | Methods of making inorganic fibres |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB9922834.8 | 1999-09-27 | ||
GB9922834A GB2353996B (en) | 1999-09-27 | 1999-09-27 | Methods of making inorganic fibres |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2001023315A1 true WO2001023315A1 (fr) | 2001-04-05 |
Family
ID=10861680
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/GB2000/003590 WO2001023315A1 (fr) | 1999-09-27 | 2000-09-19 | Procedes de formation de fibres anorganiques |
Country Status (3)
Country | Link |
---|---|
AU (1) | AU7301700A (fr) |
GB (1) | GB2353996B (fr) |
WO (1) | WO2001023315A1 (fr) |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4287142A (en) * | 1967-07-02 | 1981-09-01 | Rockwool International A/S | Process for the production of mineral wool products |
WO1993015028A1 (fr) | 1992-01-17 | 1993-08-05 | The Morgan Crucible Company Plc | Fibres inorganiques, solubles en solution saline |
WO1994015883A1 (fr) | 1993-01-15 | 1994-07-21 | The Morgan Crucible Company Plc | Fibres solubres inorganiques salines |
US5338709A (en) * | 1992-09-08 | 1994-08-16 | Solvay Barium Strontium Gmbh | Process for producing granulated strontium carbonate with a strontium-containing binder |
WO1996002478A1 (fr) * | 1994-07-13 | 1996-02-01 | The Morgan Crucible Company Plc | Fibres inorganiques solubles en solution saline |
WO1996004214A1 (fr) | 1994-08-02 | 1996-02-15 | The Morgan Crucible Company Plc | Fibres organiques |
EP0754652A1 (fr) * | 1995-07-12 | 1997-01-22 | Nitto Boseki Co., Ltd. | Laine de roche à haute résistance et son procédé de fabrication |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR745566A (fr) * | 1932-01-22 | 1933-05-12 | ||
DE1154215B (de) * | 1962-02-08 | 1963-09-12 | Patra Patent Treuhand | Anorganischer Leuchtstoff und Verfahren zu seiner Herstellung |
-
1999
- 1999-09-27 GB GB9922834A patent/GB2353996B/en not_active Expired - Fee Related
-
2000
- 2000-09-19 WO PCT/GB2000/003590 patent/WO2001023315A1/fr active Application Filing
- 2000-09-19 AU AU73017/00A patent/AU7301700A/en not_active Abandoned
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4287142A (en) * | 1967-07-02 | 1981-09-01 | Rockwool International A/S | Process for the production of mineral wool products |
WO1993015028A1 (fr) | 1992-01-17 | 1993-08-05 | The Morgan Crucible Company Plc | Fibres inorganiques, solubles en solution saline |
US5338709A (en) * | 1992-09-08 | 1994-08-16 | Solvay Barium Strontium Gmbh | Process for producing granulated strontium carbonate with a strontium-containing binder |
WO1994015883A1 (fr) | 1993-01-15 | 1994-07-21 | The Morgan Crucible Company Plc | Fibres solubres inorganiques salines |
WO1996002478A1 (fr) * | 1994-07-13 | 1996-02-01 | The Morgan Crucible Company Plc | Fibres inorganiques solubles en solution saline |
WO1996004214A1 (fr) | 1994-08-02 | 1996-02-15 | The Morgan Crucible Company Plc | Fibres organiques |
EP0754652A1 (fr) * | 1995-07-12 | 1997-01-22 | Nitto Boseki Co., Ltd. | Laine de roche à haute résistance et son procédé de fabrication |
Also Published As
Publication number | Publication date |
---|---|
GB2353996A (en) | 2001-03-14 |
AU7301700A (en) | 2001-04-30 |
GB9922834D0 (en) | 1999-11-24 |
GB2353996B (en) | 2001-07-25 |
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