CS267151B1 - A method of reducing the liquid slag from the production of the refining ferochrome - Google Patents
A method of reducing the liquid slag from the production of the refining ferochrome Download PDFInfo
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- CS267151B1 CS267151B1 CS867004A CS700486A CS267151B1 CS 267151 B1 CS267151 B1 CS 267151B1 CS 867004 A CS867004 A CS 867004A CS 700486 A CS700486 A CS 700486A CS 267151 B1 CS267151 B1 CS 267151B1
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Abstract
Riešení sa týká problematiky zvýšenia využitia chrómu pri výrobě rafinačného ferochrómu v elektrickej peci znížením jeho strát v odvalovej troske přibližné o jednu polovicu tak, že sa mimopecne doderudukováva minimálně trojnásobným prebytkom redukovadla - silikochrómu, pričom vznikne odvalová troska s obsahom do 2 % hmot. kysličníka chromítého a medziprodukt silikochróm s obsahom chrómu nad 30 % hmot. Podlá potřeby sa na úpravu vlastností odvalovej trosky móžu počas procesu doredukovávania použiť troskotvorné přísady, najma vápno a suroviny obsahujúoe hliník alebo jeho zlúčeniny.The solution concerns the problem of increasing the utilization of chromium in the production of refined ferrochrome in an electric furnace by reducing its losses in the tailings slag by approximately one half by performing additional reduction outside the furnace with a minimum threefold excess of the reducing agent - silicochrome, resulting in tailings slag with a content of up to 2% by weight of chromium oxide and an intermediate silicochrome with a chromium content of over 30% by weight. If necessary, slag-forming additives, in particular lime and raw materials containing aluminum or its compounds, can be used to adjust the properties of the tailings slag during the additional reduction process.
Description
2 CS 267 151 B12 EN 267 151 B1
Vynález sa týká zníženia obsahu chrómu v odvalových troskách vznikajúclch pri výroběrafipačného ferochrómu v elektrickéj peci s cielom dosiahnutia jeho vyššieho využitia.BACKGROUND OF THE INVENTION The present invention relates to a reduction in the chromium content of the wreckage debris generated by the production of a ferrochromising ferrochrome in an electric furnace in order to make it more useful.
Pri doteraz známých postupoch výroby tohto ferochrómu v elektrickej peci vzniká od-valová troska s obsahom okolo 4 % hmot. kysličníka chromitého, pričom pri jej vysokej kratnosti vznikají! značné 20 až 25 %-né straty chrómu, z toho jedna polovica strát připadá na chrómnachádzajúci sa v troske v kysličníkovej formě. Na výrobu ferochrómu s obsahom uhlíka do0,04 * hmot. sa používají! známe jedno alebo dvojstupňové mimopecné postupy. Princip postupuje, že v elektrickej peci sa nataví špeciálna troska s obsahom kysličníka chromitého 25 až30 % hmot., známa tiež pod názvom rudno-vápenatá zmes, ktorá sa redukuje mimopecne siliko-chrómom v jednom stupni, alebo v dvoch stupňoch, známa pod názvom Perren, kde v druhom stupnisa doredukováva troska z prvého stupňa obsahujiica minimálně 14 až 15 % hmot. kysličníkachromitého. U mimopecných postupov sa dosahuji! lepšie výsledky vo využití chrómu cca o 5 %,ale hlavně vyššie využitie kremíka. Podlá autorského osvedčenia č. 197 396 sa získává nízko-uhlíkatý ferochróm opakovanou mimopecnou rafináciou silikochrómu odvalovou troskou z výrobyrafinačného ferochrómu s obsahom 5 až 15 % hmot. kysličníka chromitého.In the prior art processes for the production of this ferro-chrome in an electric furnace, a waste slag with a content of about 4% by weight is produced. chromium oxide, with its high shorter! significant 20 to 25% chromium loss, one half of which is attributable to chromium present in slag in oxide form. For the production of ferochrome with a carbon content of up to 0.04% by weight. are used! known one- or two-stage in-process procedures. The principle is that a special slag with a chromium oxide content of 25 to 30% by weight is known to be melted in an electric furnace, also known as a red-calcium mixture, which is ultimately reduced by silico-chromium in one or two stages known as Perren wherein in the second stage the slag from the first stage comprises at least 14 to 15 wt. chromium oxide. In the case of out-of-office procedures, I get it! better results in the use of chromium by about 5%, but mainly higher utilization of silicon. According to the Author's Certificate No. 197 396, low-carbon ferro-chromium is obtained by repeatedly refining the silicochrome with a hollow slag from a production refinery ferochrome containing 5 to 15% by weight. chromium oxide.
Nedostatkom uvedených postupov je nízké využitie chrómu, ked vo vzniknutých odvalovýchtroskách se nachádza ešte viac ako 2 % hmot. kysličníka chromitého.The drawbacks of these processes are the low use of chromium when more than 2 wt. chromium oxide.
Oloha bola vyrřešená a nevýhoda doterajších technologií bola odstránená doredukovanímtrosky s použitím vysokého, minimálně trojnásobného přebytku silikochrómu oproti stechio-metrickej spotrebe až do zníženia obsahu kysličníka chromitého v odvalových troskách pod2 % hmot., pričom sa získává medziprodukt vo formě silikochrómu s obsahom chrómu nad 30 %hmot. Na úpravu fyzikálnych vlastností a chemického zloženia odvalovej trdsky sa móžu priprocese doredukovania přidávat do 20 % troskotvorné přísady najma vápno a suroviny obsahujúce'hliník alebo jeho zlúčeniny.The problem has been solved and the disadvantage of the prior art has been eliminated by reducting the slag using a high, at least three times excess of silicochrome over stoichiometric consumption until the chromium oxide content in the wreckage is below 2% by weight, yielding a silicochrome intermediate with a chromium content of over 30% wt. In order to adjust the physical properties and chemical composition of the hull, it is possible to add up to 20% of the wax-forming additives, especially lime and aluminum-containing raw materials or its compounds.
Postup oproti doteraz známým postupom je jednoduchý, menej náročný na kontrolu kvalityvýsledku rafinácie, pričom získané materiály - o chróm ochudobnená troska a o chróm obohatenýsilikochróm majú vhodnejšie chemické zloženie pre dalšie použitie. Troska s obsahom kyslič-níka chromitého do 2 % hmot. sa rýchlejšie rozpadává, čo zlepšuje jej dalšie spracovaniea stává sa vhodnou ako vápenatohorečnaté hnojivo v polnohospodárstve. Silikochróm s obsahomchrómu nad 30 i hmot. ktorý sa ako redukovadlo používá pri výrobě rafinačného ferochrómu,zvyšuje efektivnost výroby. Příklad 1Compared to previously known processes, the process is simple, less demanding to control the quality of the refining result, whereby the materials obtained - chromium-depleted slag and chromium-enriched silicochrome - have a more suitable chemical composition for further use. Slag containing chromium oxide up to 2% by weight it disintegrates more quickly, which improves its further processing and becomes suitable as calcium fertilizer in agriculture. Silicochrome with chromium content over 30% by weight which is used as a reducing agent in the production of refining ferochrome, increases production efficiency. Example 1
Pri výrobě ferochrómu s obsahom do 0,1 % uhlíku v elektrickej oblúkovej peci vzniklatekutá odvalová troska obsahujúca v % hmotnosti 8 % oxidu chromitého, 42,5 % oxidu vápenaté-ho, 23,2 % oxidu křemičitého, 1,8 % oxidu železnatého, zbytok do 100 % hmot. oxid horečnatý a hlinitý. Troska sa doredukovala v reakčnej nádobě mimo pec silikochrómom s obsahom 26 % hmot. chrómu. V nalsedujúcej tabulke je prehlad dosažených výsledkov.In the production of ferochrome containing up to 0.1% carbon in an electric arc furnace, a liquid heap slag containing 8% chromium oxide, 42.5% calcium oxide, 23.2% silica, 1.8% iron oxide, is produced. a residue of up to 100 wt. magnesium and aluminum oxide. The slag was reduced in a reaction vessel outside the furnace with a silicochrome containing 26% by weight. chromium. The following table shows an overview of the results achieved.
Tabulka 1 Č. SpotřebakgTable 1 Spotřebakg
Hliník troska SiCr 1 5 000 1 360 2 5 000 1 100 3 3 900 2 300 4 4 500 1 700 5 4 500 1 750 6 4 500 1 600 15 Vápno Prebytok SiCrskutočná spo- ,třeba teoretic.spotřeba Obsah Cr2O3 v troskef% hmot .7 před po doredukovaní - 7,9 krát 6,1 1,1 - 4,9 krát 6,4 2,0 - 9,3 krát 9,8 0,6 - 7,8 krát 7,8 0,2 100 8,6 krát 8,1 0,6 200 5,7 krát 8,4 0,3Aluminum slag SiCr 1 5 000 1 360 2 5 000 1 100 3 3 900 2 300 4 4 500 1 700 5 4 500 1 750 6 4 500 1 600 15 Lime Excess SiCrecial sp. .7 before doreduction - 7.9 times 6.1 1.1 - 4.9 times 6.4 2.0 - 9.3 times 9.8 0.6 - 7.8 times 7.8 0.2 100 8.6 times 8.1 0.6 200 5.7 times 8.4 0.3
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Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CS867004A CS267151B1 (en) | 1986-09-30 | 1986-09-30 | A method of reducing the liquid slag from the production of the refining ferochrome |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CS867004A CS267151B1 (en) | 1986-09-30 | 1986-09-30 | A method of reducing the liquid slag from the production of the refining ferochrome |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CS700486A1 CS700486A1 (en) | 1989-06-13 |
| CS267151B1 true CS267151B1 (en) | 1990-02-12 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CS867004A CS267151B1 (en) | 1986-09-30 | 1986-09-30 | A method of reducing the liquid slag from the production of the refining ferochrome |
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| Country | Link |
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| CS (1) | CS267151B1 (en) |
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1986
- 1986-09-30 CS CS867004A patent/CS267151B1/en unknown
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| Publication number | Publication date |
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| CS700486A1 (en) | 1989-06-13 |
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