DE247011C - - Google Patents
Info
- Publication number
- DE247011C DE247011C DENDAT247011D DE247011DA DE247011C DE 247011 C DE247011 C DE 247011C DE NDAT247011 D DENDAT247011 D DE NDAT247011D DE 247011D A DE247011D A DE 247011DA DE 247011 C DE247011 C DE 247011C
- Authority
- DE
- Germany
- Prior art keywords
- coal
- gas
- iron
- ores
- water vapor
- Prior art date
- Legal status (The legal status 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 status listed.)
- Active
Links
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 24
- 239000007789 gas Substances 0.000 claims description 23
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 17
- 239000003245 coal Substances 0.000 claims description 17
- 229910052742 iron Inorganic materials 0.000 claims description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 10
- MYMOFIZGZYHOMD-UHFFFAOYSA-N oxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 claims description 9
- BVKZGUZCCUSVTD-UHFFFAOYSA-N Carbonic acid Chemical compound OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 claims description 7
- 239000000446 fuel Substances 0.000 claims description 7
- 238000000034 method Methods 0.000 claims description 7
- 238000004519 manufacturing process Methods 0.000 claims description 6
- 238000002844 melting Methods 0.000 claims description 5
- 239000000203 mixture Substances 0.000 claims description 5
- CURLTUGMZLYLDI-UHFFFAOYSA-N carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims description 4
- IJGRMHOSHXDMSA-UHFFFAOYSA-N nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 4
- 229910002090 carbon oxide Inorganic materials 0.000 claims description 3
- 229910052760 oxygen Inorganic materials 0.000 claims description 3
- 239000001301 oxygen Substances 0.000 claims description 3
- 238000006243 chemical reaction Methods 0.000 claims description 2
- 230000000694 effects Effects 0.000 claims description 2
- 229910052757 nitrogen Inorganic materials 0.000 claims description 2
- 239000000571 coke Substances 0.000 claims 3
- 239000002184 metal Substances 0.000 claims 3
- 229910052751 metal Inorganic materials 0.000 claims 3
- NBIIXXVUZAFLBC-UHFFFAOYSA-N phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 claims 2
- 239000002893 slag Substances 0.000 claims 2
- 239000000654 additive Substances 0.000 claims 1
- 229910000147 aluminium phosphate Inorganic materials 0.000 claims 1
- 229910002092 carbon dioxide Inorganic materials 0.000 claims 1
- 239000001569 carbon dioxide Substances 0.000 claims 1
- 238000003763 carbonization Methods 0.000 claims 1
- 238000011109 contamination Methods 0.000 claims 1
- 238000001816 cooling Methods 0.000 claims 1
- 238000000354 decomposition reaction Methods 0.000 claims 1
- 238000004821 distillation Methods 0.000 claims 1
- 238000010438 heat treatment Methods 0.000 claims 1
- 229910052739 hydrogen Inorganic materials 0.000 claims 1
- 239000001257 hydrogen Substances 0.000 claims 1
- OAICVXFJPJFONN-UHFFFAOYSA-N phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 claims 1
- 229910052698 phosphorus Inorganic materials 0.000 claims 1
- 239000011574 phosphorus Substances 0.000 claims 1
- 239000004449 solid propellant Substances 0.000 claims 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 claims 1
- 229910052717 sulfur Inorganic materials 0.000 claims 1
- 239000011593 sulfur Substances 0.000 claims 1
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- 238000003723 Smelting Methods 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21B—MANUFACTURE OF IRON OR STEEL
- C21B13/00—Making spongy iron or liquid steel, by direct processes
- C21B13/06—Making spongy iron or liquid steel, by direct processes in multi-storied furnaces
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21B—MANUFACTURE OF IRON OR STEEL
- C21B13/00—Making spongy iron or liquid steel, by direct processes
- C21B13/0073—Selection or treatment of the reducing gases
Description
KAISERLICHES A IMPERIAL A
PATENTAMT.PATENT OFFICE.
Der Gegenstand der Erfindung ist ein Verfahren zur Erzeugung von Eisen unmittelbar aus Erzen in der Weise, daß zur Reduktion der Eisenerze und gleichzeitigen Einschmelzung des dabei entstehenden Eisens reiner Sauerstoff gleichzeitig mit einem anderen Gase vermischt oder getrennt in die in einen besonderen Kohlenraum eingetragene Steinkohle eingeblasen und der dabei resultierende Gasstrom dem gesonderten Schmelzraum zugeführt wird.The subject of the invention is a process for producing iron directly from ores in such a way that for the reduction of iron ores and simultaneous smelting the resulting iron is pure oxygen at the same time as another gas mixed or separated into the hard coal entered in a special coal room blown in and the resulting gas stream fed to the separate melting chamber will.
Es sind bereits Verfahren bekannt geworden, bei denen Gasströme zur Reduktion der Erze verwendet werden, und wobei Brennstoff einerseits und Erze und Zuschläge andererseits in getrennten Räumen untergebracht sind.There are already methods known in which gas flows to reduce the Ores are used, and with fuel on the one hand and ores and aggregates on the other are housed in separate rooms.
Bei diesen bekannten Verfahren bestand jedoch die Schwierigkeit, die Dicke der Brennmaterialschicht so zu bemessen, daß sich Kohlenoxyd und Kohlenwassersoff einerseits und Kohlensäure andererseits in einem richtigen Verhältnis zueinander befinden und zugleich eine genügend hohe Temperatur erzeugt wird, um eine vollständige Reduktion der Erze zu sichern.In these known methods, however, there was a problem with the thickness of the fuel layer to be measured in such a way that carbon oxide and hydrocarbon on the one hand and carbonic acid on the other hand are in a correct one Relationship to each other and at the same time generates a sufficiently high temperature is to ensure a complete reduction in ores.
Diese Schwierigkeit wird bei der Erfindung dadurch beseitigt, daß nicht Luft, sondern reiner Sauerstoff Verwendung findet, um durch die energische Verbrennung der Kohle bei Abwesenheit von Stickstoff und Kohlensäure eine kräftige Reduktion der Eisenerze zu erzielen.This difficulty is eliminated in the invention in that not air, but Pure oxygen is used by the vigorous burning of the coal in the absence of nitrogen and carbonic acid, a strong reduction in iron ores to achieve.
Zur Vermeidung der bei Anwendung reinen Sauerstoffs leicht auftretenden Übertemperatur, die nicht nur eine Schmelzung der Erze, sondern auch des Ofens selbst herbeiführen würde, wird nach dem neuen Verfahren gleichzeitig mit dem reinen Sauerstoff noch ein anderes, stickstofffreies Gas eingeführt, welches entweder nur durch seine niedrige Temperatur oder auch durch Umsetzung mit dem vorhandenen Brennmaterial die Temperatur, die durch die Verbrennung der Brennmaterialien in reinem Sauerstoff entsteht, so weit herabsetzt, um schädliche Einwirkungen auszu- schließen und nur die Durchführung der gewollten Reaktion zuzulassen.To avoid the overtemperature that can easily occur when using pure oxygen, which would melt not only the ores but also the furnace itself, according to the new process, another, nitrogen-free gas was introduced, either only because of its low temperature or by reacting with the existing fuel, the temperature generated by the combustion of the fuel is produced in pure oxygen, reduced to such an extent as to have harmful effects. close and only allow the desired reaction to take place.
Es sind bereits ähnliche Verfahren, die ein möglichst stickstofffreies Gas erstreben, be- , kannt, doch scheitert ihre Anwendung in der Praxis daran, daß die Erreichung der erfor-' derlichen hohen Temperaturen, wenn überhaupt, so doch nur unter solchen Umständen möglich ist, daß die gesamten Anlagen in kurzer Zeit zerstört werden. Es sind auch bereits Verfahren zur Herstellung von Wassergas vorgeschlagen, die zur Verbrennung des Brennmaterials sehr sauerstoffreiche Luft gleichzeitig mit Wasserdampf einführen wollen. Von einer Anwendung des so gewonnenen Gasgemisches für die Zwecke der Eisenerzeugung ist aber niemals die Rede gewesen.There are similar methods that seek a nitrogen-free as possible gas loading, stripped, but their application fails in practice because the achievement of the require 'sary high temperatures, if at all, yet is only possible under such circumstances, that the entire system will be destroyed in a short time. Processes for the production of water gas have also already been proposed, which want to introduce very oxygen-rich air at the same time as water vapor in order to burn the fuel. However, there was never any question of using the gas mixture obtained in this way for the purposes of iron production.
Der Apparat, in welchem das neue Verfahren ausgeführt wird, ist bekannt; er besteht im wesentlichen aus folgenden Teilen:The apparatus in which the new process is carried out is known; it consists in essential from the following parts:
1. dem Kohlenraum a mit durch Schieber b, b1 dicht verschließbarem Füllapparat c und Öffnungen zum Eintritt des Gasgemisches sowie zum Austritt der erzeugten Reduktionsgase, 1. the coal chamber a with the filling apparatus c which can be tightly closed by slides b, b 1 and openings for the inlet of the gas mixture and for the outlet of the reducing gases produced,
2. dem daran stoßenden Erzraum d mit öder ohne Gasfang, .'.·'.,2. the adjoining ore space d with or without gas trap,. '. ·'.,
Claims (1)
Publications (1)
Publication Number | Publication Date |
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DE247011C true DE247011C (en) |
Family
ID=505844
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DENDAT247011D Active DE247011C (en) |
Country Status (1)
Country | Link |
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DE (1) | DE247011C (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1047446B (en) * | 1951-02-08 | 1958-12-24 | Texaco Development Corp | Process for reducing reducible metal oxides |
DE1234749B (en) * | 1963-07-04 | 1967-02-23 | E H Hermann Schenck Dr Ing Dr | Method and device for the production of liquid iron from iron ores using oil or natural gas as reducing agent |
DE1285487B (en) * | 1964-02-13 | 1968-12-19 | Rheinische Stahlwerke | Process for the production of pig iron in a fixed hearth furnace |
-
0
- DE DENDAT247011D patent/DE247011C/de active Active
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1047446B (en) * | 1951-02-08 | 1958-12-24 | Texaco Development Corp | Process for reducing reducible metal oxides |
DE1234749B (en) * | 1963-07-04 | 1967-02-23 | E H Hermann Schenck Dr Ing Dr | Method and device for the production of liquid iron from iron ores using oil or natural gas as reducing agent |
DE1285487B (en) * | 1964-02-13 | 1968-12-19 | Rheinische Stahlwerke | Process for the production of pig iron in a fixed hearth furnace |
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