CS238409B1 - The method of draining sludge from wet gas treatment plant in steel production, especially in converters - Google Patents
The method of draining sludge from wet gas treatment plant in steel production, especially in converters Download PDFInfo
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- CS238409B1 CS238409B1 CS827466A CS746682A CS238409B1 CS 238409 B1 CS238409 B1 CS 238409B1 CS 827466 A CS827466 A CS 827466A CS 746682 A CS746682 A CS 746682A CS 238409 B1 CS238409 B1 CS 238409B1
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Abstract
Vynález rieši problém odlúčenia nežiadúcich prvkov, ako je zinok a olovo z úletov a ich opátovné použitie do vsádzky alebo iné použitie v hutníckej prevádzke. Podstata vynálezu spočívá v tom, že kalová voda z plynočistiarne sa v prve] etape počas prvých dvoch patin fúkania kyslíka do konvertora, najdlhšie však po dobu štyroch minut odvádza oddelene od kalové) vody z plynočistiarne v druhé) etape výroby ocele v konvertore, pričom sa obe časti kalov spracujú v kalovom hospodárstve odděleno. S výhodou sa kaly z druhé) etapy po zahuštění spracujú do vysokopecnej vsádzkyThe invention solves the problem of separating undesirable elements such as zinc and lead from fly ash and their reuse in the charge or other use in metallurgical operations. The essence of the invention lies in the fact that the sludge water from the gas treatment plant is, in the first stage, during the first two stages of oxygen blowing into the converter, but for a maximum of four minutes, drained separately from the sludge water from the gas treatment plant in the second stage of steel production in the converter, while both parts of the sludge are processed separately in the sludge management. Preferably, the sludge from the second stage is processed into the blast furnace charge after thickening.
Description
Vynález sa týká sposobu . odvádzania a oddelovania kovonosného kalu z mokrej plynočistiarne pri výrobě ocele — najma v konvertoroch a rieši problém odlúčenia nežiadúceho zinku a olova z úletových kalov pre použitie do vysokopecnej vsádzky alebo iné použitie v hutníckom procese.The invention relates to a method. removing and separating the metal sludge from the wet gas treatment plant in steel production - especially in converters and solving the problem of separating unwanted zinc and lead from the waste sludge for use in a blast furnace charge or other use in the metallurgical process.
Pri konvertorovej výrobě ocele sú splodiny čištěné a odlučované najčastejšie v tzv. mokrej plynočistiarni, pričom sú pevné frakcie zo splodín splachované a odvádzané v podobě špinavých kalových vod do usadzovacej nádrže, kde sa kalové vody mechanicky, připadne aj chemicky čistia pre dalšie použitie vody na chladenie a čistenie splodín a zachytený kal sa po zahuštění, například v dalších usadzovacích nádržiach spracúva v kalovom hospodárstve (pre dopravu na skládku ako nepoužitelný odpad). Vzhladom na jeho velký výskyt a vysoký podiel železa v ňom boli a sú pokusy tento úletový kal použiť dalej v hutníckom procese, a to například přečerpáváním do priestoru aglomerácií vysokých pecí, kde by sa spolu s ostatnými zložkami přidával do aglomerátu pre vysokopecnú vsádzku. Oceliarenské kaly však obsahujú zmok a olovo, takže je vylúčená ich použitelnost’ priamo do vysokopecnej vsádzky. Přitom sú známe pokusy s odstraňováním týchto prvkov zo suchých úletov, například priamym predspekaním alebo pri peletizácii a pod., pričom ide o náročnú technológiu, nízko efektívnu. Ide o celosvětový problém, ako maximálně zvýšit podiel efektívnej použitelnosti úletov vzniklých pri oceliarenskej výrobě, najma pri prevažujúcom mokrom čistění z kalov. Vynález přitom zakladá na zistenej skutočnosti, že pri skujňovacom procese v kyslíkových konvertoroch dochádza k spalovaniu zinku a olova už v prvých minutách fúkania kyslíku do konvertorovej vsádzky, čo je až 95 % do druhej minuty. Tým je aj únik týchto prvkov do splodín v tejto etape najvačší, resp. v dalších etapách už nevzniká.In the converter steel production, the waste products are cleaned and separated most often in a so-called wet gas treatment plant, where the solid fractions from the waste products are flushed and discharged in the form of dirty sludge water to a settling tank. and the cleaning of the flue gas and the collected sludge are treated in the sludge management (for transport to landfill as unusable waste), after concentration, for example in other settling tanks. Due to its high incidence and high proportion of iron, there have been attempts to use this drift sludge further in the metallurgical process, for example by pumping it into the blast furnace agglomeration area where it would be added to the blast furnace batch agglomerate. However, steel sludge contains sludge and lead, so it is impossible to use them directly into the blast furnace charge. Attempts have been made to remove these elements from dry debris, for example by direct sintering or pelletizing, and the like, while this is a demanding technology which is not very effective. This is a global problem to maximize the share of the effective usability of wastes generated by steelmaking, especially in the prevailing wet sludge treatment. The invention is based on the found fact that in the milling process in oxygen converters, the combustion of zinc and lead already occurs in the first minutes of oxygen blowing into the converter batch, which is up to 95% in the second minute. Thus, the leakage of these elements into the fumes at this stage is the greatest, respectively. it does not arise in the next stages.
Uvedené nedostatky odstraňuje spósob odvádzania kalu z mokrej plynočistiarne pri výrobě ocele, najma v konvertoroch, s čistěním obehovej vody a usadzovaním kalov v kalovom hospodárstve, podlá vynálezu. Podstata vynálezu spočívá v tom, že kalová vodá z plynočistiarne sa v prvej etape počas prvých dvoch patin fúkania kyslíka v konvertore, najdlhšie po dobu štyroch minút, odvádza oddelene od kalovej vody z plynočistiarne v druhej etape výroby ocele v konvertore, pričom sa obe časti kalov spracujú v kalovom hospodárstve oddelene. Kaly z druhej etapy sa po zahuštění s výhodou spracujú do vysokopecnej vsádzky.The above drawbacks are overcome by the method of sludge removal from a wet gas treatment plant in the production of steel, in particular in converters, with purification of circulating water and sludge settling in the sludge management according to the invention. SUMMARY OF THE INVENTION The first step of the invention is to separate the sludge water from the gas treatment plant in the first stage during the first two patina of blowing oxygen in the converter for a maximum of four minutes separately from the sludge water from the gas treatment plant. processed separately in sludge management. The sludges from the second stage are preferably processed into a blast furnace batch after concentration.
Výhoda vynálezu je v tom, že sa umožní využitie výše polovice výskytu oceliarenskych úletov, ktoré neobsahujú zinok a olovo a ktoré sa móžu, bez náročného odlučovania týchto prvkov, použiť pri výrobě surového železa, pričom sa podstatné zvýši podiel kovonosnej vsádzky vysokej pece. Zníži sa množstvo kalov odvázaných na haldu, resp. vytvárajú sa předpoklady pre ich účinnú likvidáciu, resp. spracovanie v budúcnostl pri odstraňovaní týchto prvkov alebo pre ich využitie pre iný účel.An advantage of the invention is that it is possible to utilize half the incidence of zinc and lead-free steel fumes, which can be used in the production of pig iron without complicated separation of these elements, while substantially increasing the proportion of the blast furnace charge. The amount of sludge bound to the heap is reduced. conditions are created for their effective disposal, respectively. future processing to remove these elements or to use them for other purposes.
Podfa příkladného prevedenia vynálezu bolo uskutočnené odvádzanie kalu z mokrej plynočistiarni pri 44 tavbách za deň v 160 t kyslíkovom konvertore. Spálené a vypařené prvky zachytené vo vodě z prvej etapy výroby ocele, t. j. v prvej až tretej minúte fúkania kyslíku do konvertora boli zastúpené predovšetkým zinkom a olovom. Preto tieto dve patiny kalovej vody boli přečerpané na mokrú haldu ako nežiadúci odpad. Tým sa oddělili nežiadúce prvky od ďalšej, spracovatelnej časti kalu, ktoré sa získali v ďalšej etape výroby ocele, t. j. po štvrtej minúte od začiatku fúkania kyslíku do konvertoru.According to an exemplary embodiment of the invention, sludge was removed from a wet gas treatment plant at 44 melts per day in a 160 t oxygen converter. The burnt and vaporized elements trapped in the water from the first stage of steel production, i.e. in the first to third minutes of blowing oxygen into the converter, were mainly represented by zinc and lead. Therefore, these two patina sludge water were pumped to the wet heap as undesirable waste. This separated the unwanted elements from the next, workable sludge portion that was obtained in the next stage of steel production, i.e. after four minutes from the start of oxygen blowing into the converter.
Kaly z tejto druhej etapy boli odvedené do zvláštnej kalovej nádrže. Po zahuštění boli kaly zo zahusťovacej- nádoby přečerpané do vysokopecnej prevádzky k využitiu do vsádzky pre vysokú pec. V případe výpadku'čerpacej stanice na vysokých peciach bolí tieto zhodnotené kaly dopravované do aglomeračnej prevádzky. Postupom podfa vynálezu znížili sa náklady na výrobu surového železa alebo aglomerátu, znížilo sa množstvo nezpracovatelného odpadu, připadne jeho nežiadúceho vlivu na výmurovku technologického zariadenia, znížili sa škodlivé exhalácie olova a zinku, zlepšilo sa pracovně prostredie.The sludge from this second stage was led to a separate sludge tank. After concentration, the sludge from the thickening vessel was pumped to a blast furnace plant for use in a blast furnace charge. In the event of a failure of the blast furnace pumping station, the recovered sludge is transported to the sinter plant. The process of the present invention has reduced the cost of production of pig iron or agglomerate, reduced the amount of unprocessed waste, or its adverse effect on the lining of the process equipment, reduced the harmful lead and zinc inhalations, and improved the working environment.
Claims (2)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CS827466A CS238409B1 (en) | 1982-10-21 | 1982-10-21 | The method of draining sludge from wet gas treatment plant in steel production, especially in converters |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CS827466A CS238409B1 (en) | 1982-10-21 | 1982-10-21 | The method of draining sludge from wet gas treatment plant in steel production, especially in converters |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CS746682A1 CS746682A1 (en) | 1985-04-16 |
| CS238409B1 true CS238409B1 (en) | 1985-11-13 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CS827466A CS238409B1 (en) | 1982-10-21 | 1982-10-21 | The method of draining sludge from wet gas treatment plant in steel production, especially in converters |
Country Status (1)
| Country | Link |
|---|---|
| CS (1) | CS238409B1 (en) |
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1982
- 1982-10-21 CS CS827466A patent/CS238409B1/en unknown
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| Publication number | Publication date |
|---|---|
| CS746682A1 (en) | 1985-04-16 |
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