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
Application number
NO154171A
Other languages
Norwegian (no)
Inventor
H Flood
A Seltveit
Original Assignee
Elkem Spigerverket As
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 Elkem Spigerverket As filed Critical Elkem Spigerverket As
Priority to NO154171A priority Critical patent/NO127571B/no
Priority to ZA722159A priority patent/ZA722159B/en
Priority to CH471272A priority patent/CH585672A5/xx
Priority to IT2267572A priority patent/IT950961B/en
Priority to GB1762272A priority patent/GB1344761A/en
Priority to DE19722219098 priority patent/DE2219098A1/en
Priority to AU41482/72A priority patent/AU479616B2/en
Priority to CA140,403A priority patent/CA967727A/en
Priority to ES402064A priority patent/ES402064A1/en
Priority to SE7205422A priority patent/SE376374B/xx
Priority to FR7214702A priority patent/FR2134510B1/fr
Priority to BR2546/72A priority patent/BR7202546D0/en
Priority to US00294274A priority patent/US3832434A/en
Publication of NO127571B publication Critical patent/NO127571B/no

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  • 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)

Fremgangsmåte til behandling av det SK^-støv som kan utfelles fraProcedure for treating the SK^ dust that can be precipitated from gassen fra ovner som produserer metallisk silisium eller, silisiumhpldige legeringer i den hensikt å gjøre støvet egnet for pakking pg transport, og hvor støvet agiteres i nærvær av vann, slik at man får en grøtaktig masse,karakterisert ved at agitasjonen fortsettes under tilsats av mere støv, inntil massen går over i et nodulært produkt..........the gas from furnaces that produce metallic silicon or, silicon-rich alloys with the intention of making the dust suitable for packing for transport, and where the dust is agitated in the presence of water, so that a mushy mass is obtained, characterized by the agitation being continued while adding more dust , until the mass turns into a nodular product..........
NO154171A 1971-04-26 1971-04-26 NO127571B (en)

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)

Also Published As

Publication number Publication date
ES402064A1 (en) 1975-03-16
IT950961B (en) 1973-06-20

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