NO127571B - - Google Patents
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- Publication number
- NO127571B NO127571B NO154171A NO154171A NO127571B NO 127571 B NO127571 B NO 127571B NO 154171 A NO154171 A NO 154171A NO 154171 A NO154171 A NO 154171A NO 127571 B NO127571 B NO 127571B
- Authority
- NO
- Norway
- Prior art keywords
- dust
- water
- agitation
- silicon
- product
- Prior art date
Links
- 239000000428 dust Substances 0.000 claims description 20
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 6
- 238000013019 agitation Methods 0.000 claims description 5
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 claims description 4
- 238000000034 method Methods 0.000 claims description 4
- 229910052710 silicon Inorganic materials 0.000 claims description 4
- 239000010703 silicon Substances 0.000 claims description 4
- 229910045601 alloy Inorganic materials 0.000 claims description 2
- 239000000956 alloy Substances 0.000 claims description 2
- 238000012856 packing Methods 0.000 claims 1
- 239000000725 suspension Substances 0.000 description 3
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000004806 packaging method and process Methods 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 238000005054 agglomeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 239000004566 building material Substances 0.000 description 1
- 238000005056 compaction Methods 0.000 description 1
- 239000003337 fertilizer Substances 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000000049 pigment Substances 0.000 description 1
- 239000011214 refractory ceramic Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 230000009974 thixotropic effect Effects 0.000 description 1
Landscapes
- Silicon Compounds (AREA)
- Manufacture And Refinement Of Metals (AREA)
- Processing Of Solid Wastes (AREA)
Description
Fremgangsmåte for behandling av SiC^-støv. Method for treating SiC^ dust.
Oppfinnelsen angår en fremgangsmåte for behandling av SiC^-støv som kan utfelles fra gassene fra ovner som produserer metallisk silisium eller sili-siumholdige legeringer. The invention relates to a method for treating SiC₂ dust that can be precipitated from the gases from furnaces that produce metallic silicon or silicon-containing alloys.
Dette støv som er meget finfordelt (kolloidalt) kan anvendes for en rekke for-mål, som komponent i ildfaste keramiske masser, som pigmentmateriale, som filler i bygningsmateriale, gummi etc. samt som pudringsstoff i gjødningsindu-strien. Støvet er meget lett og voluminøst, og man har derfor visse problemer med såvel pakking som forsendelse av støvet. Hittil har man vanligvis fylt det tørre støv i sekker e. 1. , men såvel ifyllingen som tømmingen av sekkene med-fører store støvplager som kan være ubehagelige for omgivelsene for dem som håndterer stoffet^ Transportomkostningene for slik voluminøst materiale blir også uforholdsmessig høye. Det er kjent å agglomerere SiO^-partikler med vann og brenne de dannede agglomerater som derpå knuses til pulver, som så presses Bammén tii nye agglomerater. Det er også kjent å vibreré sedimen-tert støv for kompakterning. Dette er imidlertid kompliserte og tungvinte metoder for agglomerering. This dust, which is very finely divided (colloidal), can be used for a number of purposes, as a component in refractory ceramic masses, as a pigment material, as filler in building material, rubber etc. and as a powder in the fertilizer industry. The dust is very light and bulky, and there are therefore certain problems with both packaging and shipping of the dust. Until now, the dry dust has usually been filled in sacks e. 1. , but both the filling and the emptying of the sacks entail large dust nuisances which can be unpleasant for the surroundings for those who handle the substance^ The transport costs for such voluminous material are also disproportionately high. It is known to agglomerate SiO^ particles with water and burn the formed agglomerates which are then crushed into powder, which is then pressed into new agglomerates. It is also known to vibrate sedimented dust for compaction. However, these are complicated and cumbersome methods of agglomeration.
Oppfinnerne har nå funnet at den grøtaktige mas se som oppstår hår silikastøv agiteres med vann, går over i et nodulært produkt når agitasjonen fortsettes under tilsats av mere støv, samt at dette trekk kan utnyttes ved forpakning og forsendelse. The inventors have now found that the mushy mass that occurs when silica dust is agitated with water turns into a nodular product when the agitation is continued with the addition of more dust, and that this feature can be used for packaging and shipping.
En suspensjon av vann og støv bestående av f. eks. 1 del vann til 2-4 deler støv, avhengig av støvkvaliteten, vil under agitasjon forholde seg som en. væske.. Til-settes så mere 6tøv i små porsjoner under sterk agitasjon, vil den tixotropisk grøtaktige masse gå over til et produkt,av faste nøtteaktige noduler som er velegnet for forsendelse. En enkel nodul kan ha en volumvekt på ca. 1, 8 kg/l, svarende til ca. 1,45 kg/l silika-støv. Litervekten av nodulproduktet er 1, 1 kg hvilket tilsvarer ca. 0, 9 kg støv i Litervekten av ubehandlet støv er ca. 0, 2 - 0,3 kg. Det oppnås således betydelig volumbesparelser ved overføring av støvet til noduler. A suspension of water and dust consisting of e.g. 1 part water to 2-4 parts dust, depending on the dust quality, will behave as one during agitation. liquid.. If more silk is then added in small portions under strong agitation, the thixotropic mushy mass will change to a product of solid nut-like nodules which is suitable for shipping. A simple nodule can have a volumetric weight of approx. 1.8 kg/l, corresponding to approx. 1.45 kg/l silica dust. The liter weight of the nodule product is 1.1 kg, which corresponds to approx. 0.9 kg of dust in The liter weight of untreated dust is approx. 0.2 - 0.3 kg. Significant volume savings are thus achieved by transferring the dust to nodules.
Større tetthet kan oppnås ved at nodulene presses til briketter eller blokker som eventuelt kan kuttes opp i ønsket størrelse. Greater density can be achieved by pressing the nodules into briquettes or blocks which can possibly be cut into the desired size.
Ved tilsetning av vann og mekanisk agitasjon blir nodulproduktet atter overført til suspensjon. Denne suspensjon kan så benyttes direkte til mange av de for-mål hvor man hittil har anvendt tørt støv. By adding water and mechanical agitation, the nodule product is transferred back into suspension. This suspension can then be used directly for many of the purposes where dry dust has hitherto been used.
Claims (1)
Priority Applications (13)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
NO154171A NO127571B (en) | 1971-04-26 | 1971-04-26 | |
ZA722159A ZA722159B (en) | 1971-04-26 | 1972-03-29 | Method of treating sio2-dust |
CH471272A CH585672A5 (en) | 1971-04-26 | 1972-03-29 | |
IT2267572A IT950961B (en) | 1971-04-26 | 1972-03-31 | METHOD OF TREATMENT OF SILICA DUST |
GB1762272A GB1344761A (en) | 1971-04-26 | 1972-04-17 | Method of treating sio2-dust |
DE19722219098 DE2219098A1 (en) | 1971-04-26 | 1972-04-19 | Silica tixotrope and its further processed product |
AU41482/72A AU479616B2 (en) | 1971-04-26 | 1972-04-21 | METHOD OF INCREASING BULK DENSITY OF FINELY DIVIDED SiO2-DUST |
CA140,403A CA967727A (en) | 1971-04-26 | 1972-04-24 | Method of nodulizing silicon dioxide dust |
ES402064A ES402064A1 (en) | 1971-04-26 | 1972-04-25 | A method for the powder treatment of si o2. (Machine-translation by Google Translate, not legally binding) |
SE7205422A SE376374B (en) | 1971-04-26 | 1972-04-25 | |
FR7214702A FR2134510B1 (en) | 1971-04-26 | 1972-04-25 | |
BR2546/72A BR7202546D0 (en) | 1971-04-26 | 1972-04-26 | A PROCESS FOR THE TREATMENT OF SIO2 OP |
US00294274A US3832434A (en) | 1971-04-26 | 1972-10-02 | Method of treating silicon dioxide dust |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
NO154171A NO127571B (en) | 1971-04-26 | 1971-04-26 |
Publications (1)
Publication Number | Publication Date |
---|---|
NO127571B true NO127571B (en) | 1973-07-16 |
Family
ID=19878265
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
NO154171A NO127571B (en) | 1971-04-26 | 1971-04-26 |
Country Status (3)
Country | Link |
---|---|
ES (1) | ES402064A1 (en) |
IT (1) | IT950961B (en) |
NO (1) | NO127571B (en) |
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1971
- 1971-04-26 NO NO154171A patent/NO127571B/no unknown
-
1972
- 1972-03-31 IT IT2267572A patent/IT950961B/en active
- 1972-04-25 ES ES402064A patent/ES402064A1/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
ES402064A1 (en) | 1975-03-16 |
IT950961B (en) | 1973-06-20 |
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