PL764B1 - The method of preparing sinter agglomerates in a shaft furnace from a mixture of fine ore, top dust, pyrite prazonkj, etc. with fine fuel. - Google Patents

The method of preparing sinter agglomerates in a shaft furnace from a mixture of fine ore, top dust, pyrite prazonkj, etc. with fine fuel. Download PDF

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Publication number
PL764B1
PL764B1 PL764A PL76420A PL764B1 PL 764 B1 PL764 B1 PL 764B1 PL 764 A PL764 A PL 764A PL 76420 A PL76420 A PL 76420A PL 764 B1 PL764 B1 PL 764B1
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PL
Poland
Prior art keywords
fine
mixture
agglomerates
shaft furnace
fuel
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Application number
PL764A
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Polish (pl)
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Publication of PL764B1 publication Critical patent/PL764B1/en

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Pierwszenstwo: 20 grudnia 1917 r. (Niernc\Tj.Przygotowywanie zlepów z drobnej rudy, pylu gardzielowego, praizonki z pirytu itp., zapomoca spiekania uprzednio sformowanej maisy w pieciu szybowymi, miailo te wade, ze drobne paliwo (np. anial fcolkisowy), doda¬ no do czesci skladowych mlaisy, bylo w ziniaciz- nych ilosciach usuwane z pieca przez prad gazu. Szczególnie szkodliwa byla ta wada przez to,, ze usuwanie nastepowalo nierów¬ nomiernie na wszystkich czesciach, przez co i ogien byl nierównomierny, wskutek czego bieg pracy byl utrudniony. Uzywanie koksu w duzych kawalach usuwalo wprawdzie te niedogodnosc, ale cialo spiekane mialo pod wieloma wzgledami wady w stosunku do otrzymanego przy miale koksowym.Byly czynione przeto próby wprowadza¬ nia do pieca drobnej rudy i t. p. dokladnie zmieszainjeij z d!ro'bnein (piaiHwieim, potrzebnem do spiekania, jako ciala, tloczonego. Ten spo¬ sób byl juz dawniej proponowamy dla za¬ stapienia spiekania w konwertorach.Przytem nastreczaly sie jednak-rózne nie¬ dogodnosci, uniemozliwiajace praktycznie prawidlowa pra.ce pieca, które daja sie.usu¬ nac zadawalniajaco dopiero zapomoca ni¬ niejszego sposobu, stanowiacego przedmiot wynalazku.Stosownie do dotychczasowych pogladów starano sie otrzymac wpierw dosyc twarde brylki, zapomoca wy-ckiego cisnienia w od¬ powiednich prasach, wytrzymujace zarówno przeniesienie do pieca szybowego, jaiko tseft nie rozpadajace sie ani przed, ani przy spie¬ kaniu.Takie prasy pracuja przy niewielkiej Do-scd wody, wedlug t. zw. siposobu prasowa¬ nia na sucho, i dawaly dobre wynikli dla drobn^iziiiarniisitych rud a taJkisei idla cementu.W ptiecu szybowym Jednak brylki lz drobnej rudy i z mialu koksowego rozpadaly sie talk dalece, ze skutkiem tego czysto gasl ogien lub tylko jednostronnie unosil sie wgótre. Do<- danie odpowiednich srodków wiazacych wy¬ wolywalo wprawdzie pewne polepszenie, lecz przez to stawal sie znowu sposób bandziej, klopotliwym i malo ekonomicznym.Jednak sp-rasawlalme na sucho brylki przy ich spiekaniu w piieicu kanalowym lub pier¬ scieniowym, gdzie temperatura podnosi sie raptownie, rozsypuja sie, wobec silnego pa¬ rowania zawartej w brylkach wody. Chociaz wiec dodatek wody przy prasowaniu na su¬ cho jest nieznaczny, to jednak' przy raptow- nem ogrzewaniu wydzielajaca sie para po^ siada zbyt waskie kanaly do ujscia, skut¬ kiem wysokiego cisnienia prasy. Z tego wy¬ jasnienia wynika, ze nawet znacznie wieksza zawartosc wody w brylkach sprasowanych nie wywola rozsypywania sie ich, gdy be¬ dzie dostateczna ilosc otworów lub kaniai- lików do ujscia pary. Dalszo próby z praso¬ waniem na sucho o wyzszej zawartosci wody nie doprowadzily do zadawalajacego rezul¬ tatu, natomiast rezultat byl .'zadawalajacy, gdy jeszcze bardziej powiekszono ilosc do¬ dawanej wody i nastepnie prasowano mie¬ szanine rudy drobnoziarnistej z drobnym koksem w ceglarce prasowej, a wiec wedlug sposobu mokregoi prasowania. Takie brylki z pelna zawartoscia wody bez, wysychania dawaly sie latwo umieszczac w piecu i nie pekaly przy spiekaniu.Zawartosc wody bywa wprawdzie przy prasowaniu na mokro znacznie wyzsza, niz przy prasowaniu na sucho, ale umozliwia wlasnie przez to ujscie pary. Raz nasyca sie mianowicie drobne-paliwo (mialki koks) wo¬ da nawskros i nastepnie osadza sie równielz woda nie wsiaknieta w pory poszczególnych czastek paliwa lub rudy okolo mich i mie¬ dzy niemi. Jezeli wiec wzrasta temperatura w brylce stopniowo 'z zewnatrz, to nie moze ornia w jiakietmkolwiek miejscu wzrosnac po¬ wyzej jak 100° az do cziaisu, kiedy w tem miejscu wszystka woda wyparuje. Przez to znajduje wówczas para wodna dosyc wolnej przestrzeni do ujscia. Wysoka zawartosc wo¬ dy dziala w pewnym stopniu, jak plaszcz wewnetrznego jadr!a.Przy tym sposobie pracy jest wiec szcze¬ gólnie koTzystnem mieszanie paliwa, do drob¬ nej rudy i daje ono lepsze wyniki tez ze wzgledu na wytrzymalosc przeciw skrusza niu sie w piecu, jak gdyby do drobnej rudy, uksztaltowanej w sposób znamy zaipioimioca mokrej prasy, dodawano paliwa w drobnych lub grubych kawalkach miedzy brylkami do spiekania w piecu szybowym. Jezeli np. potrzeba do spiekania 8°/0 mialu koksowego, to stosunek objetosci rudy i koksu wynosi 1 : 0,35. Innemi slowy znaczy to, ze udzial objetosciowy porowatego mialu koksowego wynosi w mieszaninie 25°/0 i, ze znaczna ilosc wody, uchodzaca z mialu koksowego, pozo¬ stawia wiecej kanalików w jeszcze wiekszym stosunku dla uchodzenia], pary wodnej, niz przy brylce rudy bez dodatku mialu kok¬ sowego.Dalsza korzysc, w porównaniu z dotych¬ czasowym sposobem, polega na tem, ze skut¬ kiem znikniecia dosyc .znacznych ilosci wody i wypalenia koksu domieszanego do rudy, pozostaja bardzo porowate zlepy.Sposób ten bywia nip. talk wykonywa ny, ze miesza sie w t. zw. wyralbiaczu gli¬ ny odwaizone ilosci drobnej rudy i mialu koksowego lub innego drobnego paliwa (cd- padki) w stosunku 12:1 z obfitym dodatkiem wody i poddaje sie miekka gniiotina mase dzialaniu ceglarki pasmowej. Wytworzone przez nia krótkie kawalki pasmowe padaja na przyrzad nadawczy pieca szybowego, pro¬ wadzonego z nader wysoko lezacym ogniem, przez co osiaga sie szybkie ogrzanie do tem¬ peratury spiekania, korzystnej dla wyrobu pod wieloma wzgledami. Naturalnie, mozna — 2 —dodawac materjaly, wywolujace odpowied¬ nie reakcje, lub srodki wiazace.Juz dawniej w przemysle cementowym mieisizamo stezaly mul e drofoniein paliwem i z tego przygotowywano brylki dla pieców szybowych do sfpiietoaaiiai. Przyton, umte- sizic!zain'a jednak brylki w piecach dopiero wtedy, gdy one zinawu tracily wode skutkiem szczególnego procesu wysuszania. Przy ni¬ niejszymi jednak spio$obiel unika' sie takiego szczególnego suszenia wraz z jego trudami i kosztami. PL PLPrecedence: on December 20, 1917 (I.e. preparation of lumps of fine ore, throat dust, pyrite fire, etc., by sintering a previously formed maisy in five shafts, it had the disadvantage that fine fuel (e.g. carbon fiber), was added to the components of the melt, it was removed from the furnace in staggered amounts by the gas current. This drawback was particularly harmful because the removal was unevenly carried out on all parts, which made the fire unevenly run Although the use of coke in large chunks eliminated this inconvenience, the sintered body had in many respects disadvantages compared to the coke powder obtained with coke powder, therefore attempts were made to introduce fine ore into the furnace and, for example, thoroughly mix the pieces of wood. (sand, needed for sintering, as a body, pressed. We propose this method for a long time in order to replace sintering in converters. Various inconveniences, which prevent practically the correct operation of the furnace, which can be removed satisfactorily only after the use of this method, which is the subject of the invention. According to the current views, attempts were made to obtain quite hard flakes at first, by avoiding the high pressure in suitable presses, which can withstand both transfer to the shaft furnace, as tseft non-disintegrating either before or during sintering. Such presses operate with little water, according to the so-called In the shaft end, however, the lumps of fine ore and coke dust broke apart the talc to a great extent, with the result that the fire was simply extinguished or only one-sidedly raised in the deep. Admittedly, the addition of appropriate binders brought about a certain improvement, but in this way it was again a slacker, troublesome and not very economical way. However, I dried the flakes dry while sintering them in a canal or ring saw, where the temperature rises. suddenly, they disintegrate due to the strong evaporation of the water contained in the particles. Thus, although the addition of water during dry ironing is slight, nevertheless, on rapid heating, the steam that is released will stick too narrow to the outlet, due to the high pressure of the press. It follows from this explanation that even the much greater water content of the compressed nuggets will not cause them to scatter when there are enough holes or channels for the steam to escape. Further trials with dry pressing with a higher water content did not lead to a satisfactory result, but the result was satisfactory when the amount of added water was increased even more and the mixture of fine ore and fine coke was pressed in a press brick. that is, according to the method of wet ironing. Such nuggets with full water content without drying out were easy to place in the oven and did not crack when sintering. The water content in wet pressing is much higher than in dry pressing, but it allows the steam to escape. One time the fine fuel (fine coke) is saturated with water and then the water that has not penetrated into the pores of individual fuel particles or ore around them and between them is deposited. So if the temperature in the flake rises gradually from the outside, it cannot rise above 100 ° in any place until the time when all the water has evaporated there. As a result, the water vapor finds enough free space for its exit. The high water content acts to some extent like the mantle of the inner core. In this mode of operation, it is therefore particularly costly to mix the fuel into a fine ore, and it gives better results also because of the resistance to crushing in In the furnace, fuel was added in fine or coarse pieces between the sintering flasks in the shaft furnace, as if to the fine ore, shaped in the manner known to the zaipioimioca of a wet press. If, for example, 8% coke fines are required for sintering, the volume ratio of the ore to the coke is 1: 0.35. In other words, the volume fraction of porous coke fines in the mixture is 25/0 and that a significant amount of water that escapes from the coke fines leaves more channels in an even greater proportion of water vapor to escape than in the ore nugget. Without the addition of coke fines. A further advantage compared to the current process is that as a result of the disappearance of quite significant amounts of water and the burning of the coke admixed to the ore, they remain very porous lumps. This method can be nip. talc performed ny that mixes in the so-called In the clay crusher, weighed amounts of fine ore and coke fines or other fine fuel (cont'd) in a ratio of 12: 1 with copious addition of water and subjected the soft mass to the action of a strip brick. The short strip pieces produced by them fall on the transmitting device of a shaft furnace, guided with a very high fire, thereby achieving a rapid heating to the sintering temperature, which is favorable for the product in many respects. Naturally, you can - 2 - add materials that evoke the appropriate reaction, or binders. Already in the past, in the cement industry, mud was stored with fuel in the cement industry, and from this pellets were prepared for shaft furnaces for sfpiietoaaiiai. However, the chimney, umtesizic !, but the flakes in the furnaces only when they lost water as a result of a special drying process. With the following, however, such special drying is avoided with its difficulties and costs. PL PL

Claims (1)

1. Zastrzezenie patentowe. Sposób wytwarzania zlepów do spieka¬ nia w piecach szybowych z mieszaniny drob¬ nej rudy, pylu gardzielowego, prazonki z pi¬ rytu i t. p. z drobnem paliwem (mialem), tem znaniienny, .ze miesizlainina, izwilzota do¬ statecznie woda, przerabia sie w ceglarce pasmowej i ze wytworzone w ten sposób zlepy umieszcza sie jeszcze wilgotne w piecu szybowym. Carl Giesecke. Zastepca: M. Brokimam, rzecznik patentowy. ZAKLGRAF.K0ZIANSK1CH W KRAKIW1E PL PL1. Patent claim. The method of producing sintering agglomerates in shaft furnaces from a mixture of fine ore, throat dust, pyrethrum, etc. with fine fuel (fines), so well known, that fleshy flesh, water is moist enough, and is processed into brick kiln and that the clumps produced in this way are placed in the shaft furnace while still wet. Carl Giesecke. Deputy: M. Brokimam, patent attorney. ZAKLGRAF.K0ZIANSK1CH IN KRAKIW1E PL PL
PL764A 1920-03-03 The method of preparing sinter agglomerates in a shaft furnace from a mixture of fine ore, top dust, pyrite prazonkj, etc. with fine fuel. PL764B1 (en)

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PL764B1 true PL764B1 (en) 1924-10-31

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