EP1020696B1 - Process and device to inject solid particles in a shaft furnace - Google Patents
Process and device to inject solid particles in a shaft furnace Download PDFInfo
- Publication number
- EP1020696B1 EP1020696B1 EP99124593A EP99124593A EP1020696B1 EP 1020696 B1 EP1020696 B1 EP 1020696B1 EP 99124593 A EP99124593 A EP 99124593A EP 99124593 A EP99124593 A EP 99124593A EP 1020696 B1 EP1020696 B1 EP 1020696B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- pipe
- carrier gas
- solid particles
- pipe section
- injection lance
- 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.)
- Expired - Lifetime
Links
- 239000002245 particle Substances 0.000 title claims abstract description 25
- 239000007787 solid Substances 0.000 title claims abstract description 22
- 238000000034 method Methods 0.000 title claims abstract description 10
- 238000002347 injection Methods 0.000 claims abstract description 15
- 239000007924 injection Substances 0.000 claims abstract description 15
- 239000012159 carrier gas Substances 0.000 claims abstract description 10
- 239000007789 gas Substances 0.000 claims abstract description 5
- 238000011144 upstream manufacturing Methods 0.000 claims description 2
- 239000000446 fuel Substances 0.000 description 15
- 238000007664 blowing Methods 0.000 description 10
- 230000000694 effects Effects 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 229920000426 Microplastic Polymers 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 238000002844 melting Methods 0.000 description 2
- 230000008018 melting Effects 0.000 description 2
- 238000010310 metallurgical process Methods 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 239000004449 solid propellant Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 239000000969 carrier Substances 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 230000007257 malfunction Effects 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21B—MANUFACTURE OF IRON OR STEEL
- C21B5/00—Making pig-iron in the blast furnace
- C21B5/02—Making special pig-iron, e.g. by applying additives, e.g. oxides of other metals
- C21B5/023—Injection of the additives into the melting part
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21B—MANUFACTURE OF IRON OR STEEL
- C21B5/00—Making pig-iron in the blast furnace
- C21B5/001—Injecting additional fuel or reducing agents
- C21B5/003—Injection of pulverulent coal
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27B—FURNACES, KILNS, OVENS OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
- F27B1/00—Shaft or like vertical or substantially vertical furnaces
- F27B1/10—Details, accessories or equipment specially adapted for furnaces of these types
- F27B1/16—Arrangements of tuyeres
Definitions
- the invention relates to a method and a device for blowing in solid particles in a shaft furnace, in particular a blast furnace, in which the solid particles by means of a gaseous flow into the hot wind stream the wind forms are fed.
- additional fuels via the wind forms the metallurgical process supply.
- additional fuels such as. B. heating oil
- suitable pneumatic transport devices Furnace fed.
- These mostly powdered fuels are thereby Actuation of a carrier gas via pipelines from a storage container via discharge chambers and appropriately trained blowing lances added to the hot wind stream and transported into the furnace interior.
- a method for supplying a powdered fuel mixture is for Example described in the publication according to DE 30 50 394. After this The powdered fuel mixture is processed immediately after Discharge from a discharge chamber in each pipe with a gas jet acted on, which is directed against the flow. So that should Eligibility of the fuel particles stored in the conveying gas is ensured become.
- US-A-5 070 797 describes the additional injection of compressed air into a flow of solid fuel particles before entering a hot air stream a hot wind lead to a shaft furnace.
- the object of the invention is to find a method and a device with which additional fuels in the form of solid particles, such as. B. granules from the Processing of old plastics, dusts or other powdery substances and their Mixtures by means of a gaseous flow into the hot wind stream Wind forms of a shaft furnace, in particular a blast furnace, are promoted, that while lowering the usual pressure on the Conveyor system after a discharge chamber of a pneumatic transport device Faults in the supply of the stove with these additional fuels avoided the maintenance and repair work for such Plants reduced and more favorable conditions for a combustion of the solid Particles in the melting zone of the furnace can be guaranteed.
- additional fuels in the form of solid particles such as. B. granules from the Processing of old plastics, dusts or other powdery substances and their Mixtures by means of a gaseous flow into the hot wind stream Wind forms of a shaft furnace, in particular a blast furnace
- Fig. 8 9 is in a hot wind pipe leading to a shaft furnace a central pipe for a flow of solid auxiliary fuel and gas is arranged. Before the hot wind pipe opens into the furnace and at an angle to it, oxygen supply lines are arranged, which swirl the additional fuel in a spiral. The swirling takes place in Contrary to the invention only in the wind pipe and not before the flow in the wind pipe.
- EP-A-44 096 describes the supply of solid fuel particles and their swirling in one Hot wind form of a blast furnace by means of branch lines that open at an angle in the wind form connected by a pipe bend. In contrast to the invention, the supply line does not take place before but in the wind form.
- the application of a gaseous medium to the feed stream according to the invention immediately before the solid particles enter a blow-in lance enables the solid particles to be loosened and swirled before entering the hot wind stream of a wind form while increasing the flow rate of the feed stream.
- the additional introduction of a gaseous medium in the direction of the injection lance with a pressure which is several times higher than that of the conveying medium in this pipe section creates a suction effect in the upstream part of the respective pipe, which considerably reduces the risk of blockages in this previously endangered pipe section .
- the spiral introduction of the gaseous medium into the flow immediately before entering the blowing lance enables the flow to be formed in a stable manner, as a result of which the solid particles can be transported far into the melting zone of the furnace.
- the embodiment relates to the injection of solid particles, such as. B. plastic granules or processed components from the shredder light fraction, which are fed to the blast furnace process via the wind molds 5 as part of an environmentally sound recycling.
- the solid particles are conveyed under pressure from a storage container via pipes to the area of the windmills 5 of the blast furnace.
- the usual pressure at the beginning of the conveyor line of 2.2-2.5 bar can be reduced to 1.6-2.0 bar using the method according to the invention and the associated device.
- a pressure of 0.2 - 0.5 bar is set at the end of the conveyor line.
- the solid particles are added to the hot wind stream via blowing lances 6 arranged on the wind molds and are thus fed to the interior of the furnace.
- the respective pipeline is connected via a valve 4 to the device according to the invention directly in front of a blowing lance 6.
- the device is arranged between the blowing lance 6 and the valve 4 and is expediently connected to these by means of screw connections on both sides. It consists of a pipe section 1 and a pipe bend 2 firmly connected to the pipe section 1, which is arranged at an angle of approximately 30 ° to the axis of symmetry of the pipe section 1.
- the pipe section 1 and the two ends of the pipe bend 2 are connected to one another in a gas-tight manner in the region of the openings, preferably by a welded connection as shown in FIG. 3.
- the pipe bend 2 has a connection 3 for a compressed air line.
- the connection 3 is arranged at the upper vertex of the pipe bend 2, the connection being designed so that compressed air can flow into the pipe section 1 via the connection 3 and the pipe bend 2.
- the compressed air is taken from the line network installed at the blast furnace at approximately 5 to 6 bar and fed to the device according to the invention via a non-illustrated check valve.
- the existing pressure difference creates a suction effect in the pipeline for the solid particles, as a result of which deposits or blockages in the rear section of the pipeline are avoided.
- the staggered arrangement of the pipe bend ends on the pipe section 1 can be seen from FIG. 1. It loosens and swirls the solid particles in the area behind the pipe openings in the pipe section 1.
- the arrangement of the pipe bend ends at an angle of 80 ° to the axis of symmetry of the pipe section 1 produces a spiral movement of the solid particles directed in the direction of the lance 6. This configuration is shown in Fig. 2.
- the inner diameter of the pipe section 1 is equal to the inner diameter of the downstream blowing lance 6 in order to avoid negative effects on the flow.
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Furnace Charging Or Discharging (AREA)
- Blast Furnaces (AREA)
- Crucibles And Fluidized-Bed Furnaces (AREA)
- Air Transport Of Granular Materials (AREA)
Abstract
Description
Die Erfindung betrifft ein Verfahren und eine Vorrichtung zum Einblasen von festen Teilchen in einen Schachtofen, insbesondere einen Hochofen, bei dem die festen Teilchen mittels eines gasförmigen Förderstromes in den Heißwindstrom der Windformen zugeführt werden.The invention relates to a method and a device for blowing in solid particles in a shaft furnace, in particular a blast furnace, in which the solid particles by means of a gaseous flow into the hot wind stream the wind forms are fed.
Zum Betreiben von Hochöfen oder anderen vergleichbaren Schachtöfen ist es bekannt, Zusatzbrennstoffe über die Windformen dem metallurgischen Prozeß zuzuführen. Neben flüssigen Zusatzbrennstoffen, wie z. B. Heizöl, werden auch feste Energieträger über geeignete pneumatische Transporteinrichtungen dem Ofen zugeführt. Diese zumeist pulverförmigen Brennstoffe werden dabei durch Beaufschlagung mit einem Trägergas über Rohrleitungen von einem Vorratsbehälter über Ausgabekammern und entsprechend ausgebildete Einblaslanzen dem Heißwindstrom zugesetzt und in das Ofeninnere befördert.It is for operating blast furnaces or other comparable shaft furnaces known, additional fuels via the wind forms the metallurgical process supply. In addition to liquid additional fuels, such as. B. heating oil, too solid energy carriers via suitable pneumatic transport devices Furnace fed. These mostly powdered fuels are thereby Actuation of a carrier gas via pipelines from a storage container via discharge chambers and appropriately trained blowing lances added to the hot wind stream and transported into the furnace interior.
Ein Verfahren zum Zuführen eines pulverförmigen Brennstoffgemisches ist zum Beispiel in der Veröffentlichung gemäß DE 30 50 394 beschrieben. Nach diesem Verfahren wird das pulverförmige Brennstoffgemisch unmittelbar nach dem Austrag aus einer Ausgabekammer in jeder Rohrleitung mit einem Gasstrahl beaufschlagt, der entgegen dem Förderstrom gerichtet ist. Damit soll die Förderfähigkeit der im Fördergas eingelagerten Brennstoffteilchen gesichert werden.A method for supplying a powdered fuel mixture is for Example described in the publication according to DE 30 50 394. After this The powdered fuel mixture is processed immediately after Discharge from a discharge chamber in each pipe with a gas jet acted on, which is directed against the flow. So that should Eligibility of the fuel particles stored in the conveying gas is ensured become.
US-A-5 070 797 beschreibt das zusätzliche Einblasen von Druckluft in einen Förderstrom fester Brennstoffteilchen vor dessen Eintreten in einen Heißluftstrom einer Heißwindzuleitung zu einem Schachtofen.US-A-5 070 797 describes the additional injection of compressed air into a flow of solid fuel particles before entering a hot air stream a hot wind lead to a shaft furnace.
Neben dem Einsatz von pulverförmigen Zusatzbrennstoffen in Form von Kohlenoder Koksstäuben ist es bekannt, Plastegranulate oder Abprodukte aus der Altautoverwertung, wie z. B. die Shredderleichtfraktion nach entsprechender Aufbereitung als Zusatzbrennstoff in einem Hochofen einzusetzen. Diese Stoffe neigen jedoch stärker als normale pulverförmige Brennstoffe zu Verstopfungen in den Rohrleitungen und verursachen Störungen bei der Versorgung der einzelnen Einblaslanzen mit Zusatzbrennstoff. Diesem Zustand wird durch eine Erhöhung der Strömungsgeschwindigkeit des Förderstromes begegnet. Trotz dieser Maßnahmen sind Störungen beim Betrieb derartiger Anlagen nicht zu vermeiden. Durch die Erhöhung der Strömungsgeschwindigkeit des Förderstromes tritt in den Rohrleitungen ein verstärkter Verschleiß auf, der zu einem erhöhten Instandhaltungsaufwand für die Anlage führt. Weiterhin führen auftretende Verstopfungen im pneumatischen Transportsystem verstärkt zu Ausfällen an den Einblaslanzen, da eine Kühlung der Einblaslanzen durch den Förderstrom dann nicht mehr gegeben ist. Darüber hinaus hat eine instabile Versorgung der einzelnen Windformen mit Zusatzbrennstoff Auswirkungen auf einen kontinuierlichen Ablauf der metallurgischen Prozesse im Hochofen.In addition to the use of powdered additional fuels in the form of coal or Coke dust is known, plastic granules or waste products from the recycling of used cars, such as B. the shredder light fraction after the corresponding Processing used as additional fuel in a blast furnace. These substances however, they tend to clog more than normal powdered fuels in the pipes and cause malfunctions in the supply of the individual blowing lances with additional fuel. This condition is confirmed by a Countered increasing flow rate of the flow. Despite these measures, there are no disruptions in the operation of such systems to avoid. By increasing the flow rate of the Flow occurs in the pipes, increased wear, which leads to increased maintenance costs for the system. Continue to lead blockages occurring in the pneumatic transport system are increased Failures on the blowing lances because the blowing lances are cooled by the Flow is then no longer given. It also has an unstable Supplying the individual wind forms with additional fuel affects a continuous flow of the metallurgical processes in the blast furnace.
Aufgabe der Erfindung ist es, ein Verfahren und eine Vorrichtung zu finden, mit denen Zusatzbrennstoffe in Form von festen Teilchen, wie z. B. Granulate aus der Altplasteaufbereitung, Stäube oder andere pulverförmige Stoffe und deren Gemische mittels eines gasförmigen Förderstromes so in den Heißwindstrom der Windformen eines Schachtofens, insbesondere eines Hochofens, gefördert werden, daß unter Absenkung der bisher üblichen Druckbeaufschlagung des Fördersystems nach einer Ausgabekammer einer pneumatischen Transporteinrichtung Störungen bei der Versorgung des Ofens mit diesen Zusatzbrennstoffen vermieden, der Wartungs- und Instandhaltungsaufwand für derartige Anlagen vermindert und günstigere Bedingungen für eine Verbrennung der festen Teilchen in der Schmelzzone des Ofens gewährleistet werden können.The object of the invention is to find a method and a device with which additional fuels in the form of solid particles, such as. B. granules from the Processing of old plastics, dusts or other powdery substances and their Mixtures by means of a gaseous flow into the hot wind stream Wind forms of a shaft furnace, in particular a blast furnace, are promoted, that while lowering the usual pressure on the Conveyor system after a discharge chamber of a pneumatic transport device Faults in the supply of the stove with these additional fuels avoided the maintenance and repair work for such Plants reduced and more favorable conditions for a combustion of the solid Particles in the melting zone of the furnace can be guaranteed.
Erfindungsgemäß wird die Aufgabe entsprechend den Ansprüchen 1 bis 6 gelöst.According to the invention the object is achieved according to claims 1 to 6.
Gemäß FR-A-2 681 417, Fig. 8, 9, ist in einer zu einem Schachtofen führenden Heißwindleitung ein Zentralrohr für einen Förderstrom von festem Zusatzbrennstoff und Gas angeordnet. Vor der Mündung der Heißwindleitung in den Ofen und hierzu schräg angeordnet sind Sauerstoffzuleitungen, welche der Zusatzbrennstoff spiralförmig verwirbeln. Die Verwirbelung erfolgt in Gegensatz zur Erfindung erst in der Windleitung und nicht vor dem Eintreten des Förderstroms in die Windleitung.According to FR-A-2 681 417, Fig. 8, 9, is in a hot wind pipe leading to a shaft furnace a central pipe for a flow of solid auxiliary fuel and gas is arranged. Before the hot wind pipe opens into the furnace and at an angle to it, oxygen supply lines are arranged, which swirl the additional fuel in a spiral. The swirling takes place in Contrary to the invention only in the wind pipe and not before the flow in the wind pipe.
EP-A-44 096 beschreibt die Zuleitung fester Brennstoffteilchen und deren Verwirbelung in einer Heißwindform eines Hochofens mittels in der Windform schräg einmündender Zweigleitungen, die über einen Rohrbogen verbunden, sind. Anders als erfindungsgemäß erfolgt die Zuleitung nicht vor sondern in der Windform.EP-A-44 096 describes the supply of solid fuel particles and their swirling in one Hot wind form of a blast furnace by means of branch lines that open at an angle in the wind form connected by a pipe bend. In contrast to the invention, the supply line does not take place before but in the wind form.
Die erfindungsgemäße Beaufschlagung des Förderstromes mit einem gasförmigen
Medium unmittelbar vor Eintritt der festen Teilchen in eine Einblaslanze ermöglicht
eine Auflockerung und Verwirbelung der festen Teilchen vor Eintritt in den
Heißwindstrom einer Windform bei gleichzeitiger Erhöhung der Fließgeschwindigkeit
des Förderstromes. Die zusätzliche Einleitung eines gasförmigen
Mediums in Richtung der Einblaslanze mit einem Druck, der um ein mehrfaches
über dem des Fördermediums in diesem Rohrabschnitt liegt, wird im
vorgeordneten Teil der jeweiligen Rohrleitung eine Sogwirkung erzeugt, die die
Gefahr von Verstopfungen in diesem bisher gefährdeten Rohrabschnitt erheblich
vermindert. Die spiralförmige Einleitung des gasförmigen Mediums in den
Förderstrom unmittelbar vor Eintritt in die Einblaslanze ermöglicht eine stabile
Ausbildung des Förderstromes, wodurch ein Transport der festen Teilchen bis
weit in die Schmelzzone des Ofens möglich ist.
Durch die Beaufschlagung des Förderstromes mit einem zusätzlichen gasförmigen
Medium vor einer Einblaslanze ist sichergestellt, daß bei einer
auftretenden Verstopfung in den zu jeder Einblaslanze führenden Rohrleitung
ein Verbrennen der Lanzen nicht mehr möglich ist, da die Kühlung der
Einblaslanze mit dem zusätzlichen gasförmigen Medium gewährleistet wird.The application of a gaseous medium to the feed stream according to the invention immediately before the solid particles enter a blow-in lance enables the solid particles to be loosened and swirled before entering the hot wind stream of a wind form while increasing the flow rate of the feed stream. The additional introduction of a gaseous medium in the direction of the injection lance with a pressure which is several times higher than that of the conveying medium in this pipe section creates a suction effect in the upstream part of the respective pipe, which considerably reduces the risk of blockages in this previously endangered pipe section , The spiral introduction of the gaseous medium into the flow immediately before entering the blowing lance enables the flow to be formed in a stable manner, as a result of which the solid particles can be transported far into the melting zone of the furnace.
By supplying the flow with an additional gaseous medium in front of an injection lance, it is ensured that if there is a blockage in the pipeline leading to each injection lance, it is no longer possible to burn the lances, since the cooling of the injection lance is ensured with the additional gaseous medium.
Das erfindungsgemäße Verfahren und die dazugehörende Vorrichtung sollen nachfolgend an einem Ausführungsbeispiel näher erläutert werden. In den dazugehörenden Zeichnungen zeigen
- Fig. 1 :
- Seitenansicht der Vorrichtung
- Fig. 2 :
- Draufsicht der Vorrichtung
- Fig. 3 :
- Verbindung Rohrbogen mit Rohrabschnitt
- Fig. 4 :
- Vorrichtung im eingebauten Zustand
- Fig. 1:
- Side view of the device
- Fig. 2:
- Top view of the device
- Fig. 3:
- Connection pipe bend with pipe section
- Fig. 4:
- Device when installed
Das Ausführungsbeispiel bezieht sich auf das Einblasen von festen Teilchen, wie
z. B. Plastegranulat oder aufbereitete Bestandteile aus der Shredderleichtfraktion,
die im Rahmen einer umweltgerechten Verwertung als Energieträger dem
Hochofenprozeß über die Windformen 5 zugeführt werden. Die festen Teilchen
werden dabei unter Druckbeaufschlagung von einem Vorratsbehälter über
Rohrleitungen bis in den Bereich der Windformen 5 des Hochofens gefördert.
Der übliche Druck am Anfang der Förderstrecke von 2,2 - 2,5 bar kann unter
Anwendung des erfindungsgemäßen Verfahrens sowie der dazugehörenden
Vorrichtung auf 1,6 - 2,0 bar abgesenkt werden. In Abhängigkeit von der
Förderstrecke, die je nach Ofengröße und Anzahl der Vorratsbehälter unterschiedlich
sein kann, stellt sich am Ende der Förderstrecke ein Druck von 0,2 -
0,5 bar ein. Die festen Teilchen werden über an den Windformen angeordnete
Einblaslanzen 6 dem Heißwindstrom zugesetzt und so dem Ofeninneren zugeführt.
Dazu ist unmittelbar vor einer Einblaslanze 6 die jeweilige Rohrleitung über
ein Ventil 4 mit der erfindungsgemäßen Vorrichtung verbunden. Die Vorrichtung
ist zwischen Einblaslanze 6 und Ventil 4 angeordnet und zweckmäßigerweise
mittels beidseitiger Schraubverbindungen mit diesen verbunden.
Sie besteht aus einem Rohrabschnitt 1 und einem mit dem Rohrabschnitt 1
festverbundenen Rohrbogen 2, der unter einem Winkel von ca. 30° zur
Symmetrieachse des Rohrabschnittes 1 angeordnet ist. Am Umfang des Rohrabschnittes
1 sind in vertikaler Ebene zur Symmetrieachse des Rohrabschnittes 1
zwei zueinander versetzt angeordnete Öffnungen angebracht, deren Größe dem
Innendurchmesser des Rohrbogens 2 entspricht. Der Rohrabschnitt 1 und die
beiden Enden des Rohrbogens 2 sind im Bereich der Öffnungen gasdicht,
vorzugsweise durch eine Schweißverbindung wie aus Fig. 3 ersichtlich,
miteinander verbunden. Der Rohrbogen 2 weist einen Anschluß 3 für eine
Druckluftleitung auf. Der Anschluß 3 ist am oberen Scheitelpunkt des
Rohrbogens 2 angeordnet, wobei die Verbindung so ausgebildet ist, daß
Druckluft über den Anschluß 3 und dem Rohrbogen 2 in den Rohrabschnitt 1
strömen kann. Die Druckluft wird mit ca. 5 bis 6 bar aus dem am Hochofen
installierten Leitungsnetz entnommen und über ein nicht näher dargestelltes
Rückschlagventil der erfindungsgemäßen Vorrichtung zugeführt. Durch die
vorhandene Druckdifferenz entsteht eine Sogwirkung in der Rohrleitung für die
festen Teilchen, wodurch Ansatzbildungen bzw. Verstopfungen im hinteren
Abschnitt der Rohrleitung vermieden werden. Die versetzte Anordnung der
Rohrbogenenden am Rohrabschnitt 1 ist aus Fig. 1 ersichtlich. Sie bewirkt eine
Auflockerung und Verwirbelung der festen Teilchen im Bereich hinter den
Rohreinmündungen im Rohrabschnitt 1. Die Anordnung der Rohrbogenenden in
einem Winkel von 80° zur Symmetrieachse des Rohrabschnittes 1 erzeugt eine in
Richtung der Lanze 6 gerichtete, spiralförmige Bewegung der festen Teilchen.
Diese Ausgestaltung ist in Fig. 2 dargestellt. Der Innendurchmesser des Rohrabschnittes
1 ist gleich dem Innendurchmesser der nachgeordneten Einblaslanze 6,
um negative Einwirkungen auf den Förderstrom zu vermeiden. The embodiment relates to the injection of solid particles, such as. B. plastic granules or processed components from the shredder light fraction, which are fed to the blast furnace process via the
The usual pressure at the beginning of the conveyor line of 2.2-2.5 bar can be reduced to 1.6-2.0 bar using the method according to the invention and the associated device. Depending on the conveyor line, which can vary depending on the size of the furnace and the number of storage containers, a pressure of 0.2 - 0.5 bar is set at the end of the conveyor line. The solid particles are added to the hot wind stream via blowing
It consists of a pipe section 1 and a
- 11
- Rohrabschnittpipe section
- 22
- RohrbogenElbows
- 33
- AnschlußConnection
- 44
- VentilValve
- 55
- WindformWindform
- 66
- Einblaslanzeinjection lance
Claims (6)
- A process to inject solid particles into a shaft furnace, in particular a blast furnace, wherein solid particles are conveyed into hot blast flow within a blast tyuere (5) by a carrier gas flow through an injection lance (6), the carrier gas flow directly before its entry into the injection lance being impinged on with a gaseous medium which at this point is at a pressure in excess of that existing in the carrier gas flow, characterised in that the gaseous medium is introduced into the carrier gas flow in a manner such that due to increase in the flow velocity the solid particles contained in the carrier gas flow are fluidised and set into a spirallike motion directed towards the injection lance discharge end.
- A device to carry out the process of claim 1 comprising an injection lance (6) opening into a blast tyuere (5) and intended to conduct a flow of carrier gas containing solid particles and a pipe section (1) upstream of the injection lance (6) having at least two opposite mutually offset pipe junctions for receiving gas, characterised in that said pipe junctions are in communication with each other via an arcuate pipe (2) provided with a connection piece (3) for a gaseous medium.
- The device of claim 2, characterised in that the arcuate pipe (2) is mounted at an angle of 20° to 40° with respect to the axis of symmetry of the pipe section (1).
- The device according to claims 2 and 3, characterised in that the pipe junctions of the pipe section (1) are offset equidistantly with respect to the axis of symmetry of the pipe section (1).
- The device according to claims 2 to 4, characterised in that the pipe junctions are mounted at an angle less than 90°, preferably from 80° to 70°, with respect to the axis of symmetry of the pipe section (1).
- The device according to claims 2 to 5, characterised in that the inner diameter of the pipe section (1) is equal to that of the injection lance (6).
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19857306 | 1998-12-14 | ||
DE19857306A DE19857306C2 (en) | 1998-12-14 | 1998-12-14 | Method and device for blowing solid particles into a shaft furnace |
Publications (3)
Publication Number | Publication Date |
---|---|
EP1020696A2 EP1020696A2 (en) | 2000-07-19 |
EP1020696A3 EP1020696A3 (en) | 2003-01-02 |
EP1020696B1 true EP1020696B1 (en) | 2003-10-29 |
Family
ID=7890815
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP99124593A Expired - Lifetime EP1020696B1 (en) | 1998-12-14 | 1999-12-10 | Process and device to inject solid particles in a shaft furnace |
Country Status (4)
Country | Link |
---|---|
EP (1) | EP1020696B1 (en) |
AT (1) | ATE253210T1 (en) |
DE (2) | DE19857306C2 (en) |
ES (1) | ES2210951T3 (en) |
Family Cites Families (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2120474A7 (en) * | 1971-01-05 | 1972-08-18 | Siderurgie Fse Inst Rech | Fuel oil injector for blast furnaces - avoids formation of carbon black inside the furnace |
DE2702422A1 (en) * | 1976-01-26 | 1977-07-28 | Exxon France | Fuel injector lance, esp. for blast furnace blower - has inclined high speed atomising ducts and radial outlets |
GB2087058B (en) * | 1980-05-22 | 1984-03-21 | Do Politekh Inst | Method of feeding powder-like fuel mixture to blast furnace tuyeres |
LU82622A1 (en) * | 1980-07-14 | 1982-02-17 | Wurth Anciens Ets Paul | METHOD AND DEVICE FOR INJECTING SOLID FUELS INTO A HOT WIND DUCT FROM A TANK OVEN |
DE3603078C1 (en) * | 1986-02-01 | 1987-10-22 | Kuettner Gmbh & Co Kg Dr | Method and device for the metered introduction of fine-grained solids into an industrial furnace, in particular a blast furnace or cupola furnace |
CH674567A5 (en) * | 1986-12-24 | 1990-06-15 | Fischer Ag Georg | |
DE4026876C2 (en) * | 1990-08-25 | 1994-09-29 | Guswerk Waltenhofen | Device on a shaft furnace to form a mixture of combustion air and industrial dust intended for blowing into the oxidation zone of the shaft furnace |
FR2681417B1 (en) * | 1991-09-17 | 1998-01-30 | Air Liquide | DEVICE AND METHOD FOR INJECTING GAS AND COAL IN A METAL MELTING OVEN. |
-
1998
- 1998-12-14 DE DE19857306A patent/DE19857306C2/en not_active Expired - Fee Related
-
1999
- 1999-12-10 EP EP99124593A patent/EP1020696B1/en not_active Expired - Lifetime
- 1999-12-10 ES ES99124593T patent/ES2210951T3/en not_active Expired - Lifetime
- 1999-12-10 AT AT99124593T patent/ATE253210T1/en active
- 1999-12-10 DE DE59907537T patent/DE59907537D1/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
ATE253210T1 (en) | 2003-11-15 |
DE19857306C2 (en) | 2003-05-28 |
DE59907537D1 (en) | 2003-12-04 |
EP1020696A2 (en) | 2000-07-19 |
ES2210951T3 (en) | 2004-07-01 |
EP1020696A3 (en) | 2003-01-02 |
DE19857306A1 (en) | 2000-06-15 |
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