US3895785A - Method and apparatus for controlling the operation of a steel refining converter - Google Patents

Method and apparatus for controlling the operation of a steel refining converter Download PDF

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Publication number
US3895785A
US3895785A US312173A US31217372A US3895785A US 3895785 A US3895785 A US 3895785A US 312173 A US312173 A US 312173A US 31217372 A US31217372 A US 31217372A US 3895785 A US3895785 A US 3895785A
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United States
Prior art keywords
flow
tuyere
fluid
annulus
center
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US312173A
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English (en)
Inventor
William A Kolb
Pete Vignovich
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United States Steel Corp
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United States Steel Corp
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Application filed by United States Steel Corp filed Critical United States Steel Corp
Priority to US312173A priority Critical patent/US3895785A/en
Priority to GB3288973A priority patent/GB1447642A/en
Priority to AU57985/73A priority patent/AU480299B2/en
Priority to YU01943/73A priority patent/YU194373A/xx
Priority to DE2337846A priority patent/DE2337846C2/de
Priority to LU68107A priority patent/LU68107A1/xx
Priority to NL7310523A priority patent/NL7310523A/xx
Priority to IT69319/73A priority patent/IT991926B/it
Priority to AT671573A priority patent/ATA671573A/de
Priority to ES417414A priority patent/ES417414A1/es
Priority to FR7328267A priority patent/FR2194785B1/fr
Priority to US05/574,838 priority patent/US4047937A/en
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Publication of US3895785A publication Critical patent/US3895785A/en
Priority to ES442692A priority patent/ES442692A1/es
Assigned to USX CORPORATION, A CORP. OF DE reassignment USX CORPORATION, A CORP. OF DE MERGER (SEE DOCUMENT FOR DETAILS). Assignors: UNITED STATES STEEL CORPORATION (MERGED INTO)
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    • C—CHEMISTRY; METALLURGY
    • C21—METALLURGY OF IRON
    • C21C—PROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
    • C21C5/00—Manufacture of carbon-steel, e.g. plain mild steel, medium carbon steel or cast steel or stainless steel
    • C21C5/28—Manufacture of steel in the converter
    • C21C5/30—Regulating or controlling the blowing
    • C—CHEMISTRY; METALLURGY
    • C21—METALLURGY OF IRON
    • C21C—PROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
    • C21C5/00—Manufacture of carbon-steel, e.g. plain mild steel, medium carbon steel or cast steel or stainless steel
    • C21C5/28—Manufacture of steel in the converter
    • C21C5/30—Regulating or controlling the blowing
    • C21C5/34—Blowing through the bath

Definitions

  • ABSTRACT A method and apparatus for controlling the operation of a steel refining converter of the type having bottom tuyeres, each tuyere consisting of a center jet surrounded by annulus jets is disclosed. Controls are provided for blowing oxygen through the center jets and a fuel gas, such as propane, through the annulus jets during the refining step. Gases, such as nitrogen and compressed air, are blown through the jets during other parts of the steel making process.
  • a fuel gas such as propane
  • the disclosed apparatus en 1,953.53] 5/934 Kennico 2 35 sures that molten metal will not enter or damage the 3,212,879 10/1965 Cordier 1 1 4 266/ X tuyeres thereby preventing severe damage to the 3,343,826 9/1967 Manny et a1. 1 i 266/41 X equipment and possible hazards to operating person- 3,70e,549 12/1972 Knuppel et al. 75/60 81.
  • This invention relates to a method and apparatus for controlling the operation of a steel refining converter and, in particular, to a method and apparatus for controlling a converter of the type wherein a combination of gases is blown into the melt through tuyeres located at the bottom of the converter.
  • An improved process for refining steel employs oxygen blown from below the surface of the melt resulting in better mixing, higher efficiency and less smoke generation than the conventional method.
  • the improved process may also include the use of side tuyeres mounted above the melt as an additional means of introducing oxygen.
  • a converter employed in carrying out this improved method comprises a tiltable vessel having a refractory lining and a bottom member provided with a plurality of nozzles, or tuyeres, extending through the bottom member.
  • Each tuyere consists of a center jet through which oxygen flows during the refining portion of the process and an annulus jet concentrically surrounding the center jet through which a fuel gas flows to provide cooling for the center jet. Apparatus of this type is disclosed in copending U.S. patent application Ser. No. 800,892, filed Feb. 20, 1969, now U.S. Pat. No. 3,706,549, issued Dec. 19, 1972.
  • oxygen is used in the center jet during the refining operation, various combinations of gases are required for purging, cooling the tuyeres and during other parts of the process such as charging the converter, sampling the resulting melt, tapping the converter after the iron has been refined and during the transition periods when the converter is being rotated to a position in which the next operation can take place.
  • the tuyeres may be protected from melting by the introduction of gases such as compressed air at the center jets and low pressure nitrogen at the annulus jets.
  • the pressure at the jets must be increased to assure that the molten metal will not enter the tuyeres thereby blocking the openings and allowing them to come into contact with the steel and highly corrosive slag.
  • Nitrogen at a relatively high pressure, may be substituted for the compressed air during this portion of the cycle.
  • the refining operation is carried out by substituting oxygen for the nitrogen at the center jet and a fuel for the nitrogen at the annulus jet.
  • the pressure during refining must be high enough to prevent the nozzles from becoming blocked or damaged by contact with the melt.
  • high pressure nitrogen is substituted for the oxygen and the converter tilted downward to permit drawing a sample or removing the completed charge.
  • compressed air or low pressure nitrogen is substituted for the high pressure nitrogen at the center jets in order to prevent contamination of the surrounding area since the mouth of the converter is no longer under the hood.
  • apparatus for controlling the operation of a tiltable steel refining converter of the type having at least one tuyere at the bottom consisting of a center jet positioned within an annulus jet.
  • At least first, second and third fluid sources may be coupled to the converter, fluid control means being provided for selectively coupling first and second sets of the fluid sources to the tuyere in response to the setting of a selector switch coupled to the fluid control means by a switching network.
  • the first fluid source may be coupled to both the center and annulus jets to comprise the first set of fluid sources and in another position of the selector switch the second and third fluids may be coupled to the center and annulus jets to comprise the second set of fluid sources.
  • Means are also provided for detecting if inadequate pressure is present at the center or annulus jet or if the flow rate of any of the fluids is inadequate.
  • the second and third fluids are substituted in the center and annulus jet respectively. If the flow rate of the first fluid to the center jet decreases below a predetermined value without a reduction in pressure, the second set of fluids is provided to the tuyere together with the first set of fluids. When the second set of fluids is being provided to the tuyere and it is detected that the pressure or flow rates are below a predetermined value, the first set of fluids is substituted in the center and annulus jet.
  • the first fluid source is coupled to the center jet through a first flow control means and a first valve means and to the annulus jet through a second flow control means and a second valve means.
  • the second fluid source is coupled to the center jet through a third flow control means and a third valve means
  • a third fluid source is coupled to the annulus jet through a fourth flow control means and a fourth valve means.
  • the first fluid may be nitrogen gas, the second fluid oxygen gas and the third fluid selected from the group consisting of natural gas, propane and butane.
  • a fourth fluid which is coupled to the center jet through a fifth flow control means and a fifth valve means may be provided, the fourth fluid being selected from the group consisting of compressed air, synthetic air (a mixture of nitrogen gas and oxygen gas), nitrogen and argon.
  • first and second pressure measuring means are coupled respectively to these jets.
  • the rate of flow of the first, second, third and fourth fluids is established by flow measuring devices located in the first, third, fourth and fifth flow control means respectively, flow switches being actu' ated in the first, third and fourth flow control means whenever the flow rate of the corresponding fluids falls below a predetermined value.
  • Means are provided for actuating selectively the appropriate valve means whenever inadequate pressure or flow conditions are detected in order to prevent the melt from entering the tuyeres.
  • the third and fourth control valves are opened to permit flow of the second and third fluids to the center and annulus jets respectively and to close the first and second valves after a predetermined time delay.
  • means are provided for opening the first and second valves to permit flow of the first fluid to the center and annulus jets and, after a time delay, close the third and fourth valves thereby stopping the flow of the second and third fluids.
  • the means for coupling the pressure and flow rate measuring devices to the valves is preferably electrical but pneumatic, mechanical, hydraulic or combinations of such may be used.
  • a selector switch having first, second and third positions. In the first position, the selector switch is electrically connected to the second and fifth valve means which, when energized, couple the first and fourth fluid sources to the annulus and center jets respectively. In the second position of the switch, the first and second valve means are actuated coupling the first fluid source to the center and annulus jets and in the third position the third and fourth valve means are actuated coupling the second and third fluid sources to the center and annulus jets respectively.
  • means are provided to maintain flow of a first selected set of fluids until flow of a second selected second set of fluids has been established.
  • the first set of fluid is shut off only after a predetermined time delay and after adequate flow of the selected fluid to the center jet has been measured.
  • means are provided to prevent tilting of the converter to its upright position in the event the pressure at the center or annulus jets is below a predetermined value. Additional control means are also provided to ensure safe and proper operation of the converter and these will be explained in detail hereinafter.
  • FIGS. IA-IC are diagrams showing the orientation of the converter for various positions of the selector switch
  • FIG. 2 is a block diagram of the system for controlling the operation of the steel refining converter
  • FIGS. 3 and 3A show portions of the apparatus for controlling the flow of nitrogen
  • FIGS. 4 and 4A illustrate the apparatus for controlling the flow of oxygen and fuel to the bottom tuyeres
  • FIG. 5 shows apparatus for controlling the flow of oxygen and fuel to the side tuyeres
  • FIG. 6 depicts apparatus for control of the air supply to the bottom tuyeres
  • FIG. 7 is a schematic control diagram showing operation of the system
  • FIG. 8 is a schematic diagram of the motor drive for tilting the converter
  • FIG. 9 is a vertical sectional view of a bottom blown oxygen converter showing a pair of submerged bottom tuyeres, a pair of side submerged tuyeres, and a pair of side tuyeres directed toward the carbon monoxide zone of the furnace;
  • FIG. 10 is a vertical sectional view of an electric-arc steelmaking furnace showing a bottom vertical and bottom inclined submerged tuyere, a pair of side submerged tuyeres and a side tuyere directed toward the carbon monoxide zone of the furnace;
  • FIG. 11 is a vertical sectional view of an open hearth furnace utilizing a vertical and inclined bottom submerged tuyere, a side submerged tuyere and another side tuyere directed toward the carbon monoxide zone of the furnace;
  • FIG. 12 is a vertical sectional view of a tiltable open hearth furnace having a vertical and an inclined bottom submerged tuyere, a side submerged tuyere and side tuyere directed toward the carbon monoxide zone of the furnace;
  • FIG. 13 is a vertical sectional view of oscillatable hot metal mixer having an inclined bottom and vertical bottom submerged tuyeres, a pair of side submerged tuyeres and a side tuyere directed toward the carbon monoxide zone of the mixer.
  • FIGS. 1A, 1B, 1C and 2 a converter 10 is shown oriented for the various operations required in the process of refining pig iron into steel.
  • FIG. 1A shows the position of converter 10 for the charging and tapping operations
  • FIG. 1B the position of the converter during the actual refining step
  • FIG. 1C the converter position during sampling and test of the refined iron.
  • the converter 10 is provided with a steel shell 12 having a brick refractory lining l4 and a refractory bottom plug 16 positioned on a steel bottom plate 18.
  • Bottom tuyeres 20 (FIGS.
  • each having a center jet 22 and an annulus jet 24 concentric with and surrounding the center jet 22 are preferably located to one side of the bottom plug 16 and perpendicular to the axis A-A (FIG. 2) of trunnions 26 about which the converter 10 is tilted.
  • side tuyeres 28 may be provided in the wall of the converter 10 to accelerate conversion of carbon monoxide above the level of the melt to carbon dioxide.
  • the sequence of steps during a normal refining operation begins with the converter in the orientation shown in FIG. Ia and a selector switch 32 (FIG. 7) placed in position A.
  • compressed air or low pressure nitrogen
  • the pressure of the gases at the center 22 and annulus jets 24 are in the ranges 10 to 20 pounds per square inch and 60 to 90 pounds per square inch respectively.
  • the vessel 10 is heated by a suitable source (not shown) and a scrap and pig iron charge placed therein while it is in the tilted position shown in FIG. 1a.
  • Selector switch 32 (FIG. 7) is next moved to position B causing nitrogen at a pressure in the range 60 to I 10 pounds per square inch to be substituted for the compressed air in the bottom center jet 22 and the converter 10 is rotated about trunnions 26 by a motor 30 (F IG. 8) to the upright position shown in FIG. 1b where its mouth is under hood 34.
  • the higher pressure on the center jet 22 pevents the charge from entering and possibly blocking or otherwise damaging the bottom tuyeres 20.
  • Oxygen is not introduced into the converter 10 prior to attaining the upright position of FIG. lb because, when the vessel 10 is on its side and not under hood 34, fumes may be blown into the area surrounding the converter 10 due to the reaction of the oxygen with the melt.
  • selector switch 32 (FIG. 7) is moved to position C and pure oxygen substituted for the nitrogen in the bottom center jets 22 and a fuel, such as propane, substituted for the nitrogen in the surrounding annulus jets 24.
  • a fuel such as propane
  • the fuel acts as an encasing gas to retard melting of bottom tuyeres 20 and premature wear of the converter bottom 16.
  • oxygen and fuel are also fed to the center jets 36 and annulus jets 38 of the side tuyeres 28.
  • switch 32 (FIG. 7) is moved back to position B replacing the gases in the bottom tuyeres 20 with nitrogen and cutting off the flow of oxygen and fuel to the side tuyeres 28.
  • Converter 10 is then rotated down to the position shown in FIG. 1c and switch 32 (FIG. 7) moved to position A substituting lower pressure nitrogen or compressed air for the high pressure nitrogen in the bottom center jets 20.
  • selector switch 32 (FIG. 7) is moved to position B and the converter 10 rotated to the orientation shown in FIG.
  • FIG. 2 a schematic block diagram showing how the various gases used in operation of converter 10 are coupled to the tuyeres 20 and 28 of the converter 10, a nitrogen source 42 is coupled through a nitrogen flow measurement and control unit 44 (FIGS. 2, 3) and a valve 46 (FIG. 2) actuated by a solenoid R (FIGS. 2, 7) to the center jets 22 of bottom tuyeres 20.
  • Source 42 is also connected by a restricting orifice 48 (FIG. 2), which acts as a flow control means, and a valve 50 actuated by solenoid R (FIGS. 2, 7) to the annulus jets 24 of bottom tuyeres 20.
  • An oxygen source 52 (FIG.
  • a fuel source 60 (FIG. 2) is connected via a fuel flow measurement and control unit 62 (FIGS. 2, 4) and valve 64 (FIG. 2) actuated by solenoid R (FIGS. 2, 7) to the bottom annulus jets 24 and through a fuel flow measurement and control unit 66 (FIGS. 2, 5) to side tuyeres 28.
  • a compressed air source 68 (FIG.
  • the fuel source 60 may be any fluid that can provide adequate cooling such as propane, natural gas or fuel oil. Further, low pressure nitrogen may be substituted for the compressed air source, if desired.
  • a pressure switch 74 (FIG. 2) having electrical contacts PS-l and PS-Z (FIGS. 2, 7) is connected to the side annulus jets 24 through piping 76 (FIG. 2), and a pressure switch 78 having contacts PS-3 and PS4 (FIGS. 2, 7) is coupled to the bottom center jets 22 through piping 80.
  • Contacts PS-l and PS-3 are open under normal pressure but close when the pressure is below a predetermined value.
  • Contacts PS2 and PS4 are closed under normal pressure but open when the pressure is below a predetermined value.
  • the nitrogen flow measurement and control unit 44 (FIGS. 2, 3) is shown in detail in FIG. 3 wherein cylindrical conduit 82 is a portion of the piping connecting the nitrogen source 42 to solenoid valve 46.
  • Orifice 84 (FIG. 3) is provided at the upstream end of pipe section 82 and a conventional flow measuring unit 86, having a voltage output proportional to the rate of flow of nitrogen through orifice 84, is connected to the orifice 84.
  • Such units are commercially available and, therefore, need not be further described.
  • the output of flow measuring unit 86 is connected to one input of an amplifier 88 (FIG. 3), the other input of amplifier 88 being connected to ground through a normally open contact R -l of a relay R (FIG. 3a)
  • a normally open contact of a relay shall be defined as a contact which is open when the relay is deenergized and illustrated by two parallel spaced vertical lines and a normally closed contact is one which is closed when the relay is deenergized and is illustrated by two parallel spaced vertical lines with a diagonal line through the parallel lines.
  • the pick up coil of each relay and the relay, per se, shall be designed by the letter R and a subscript to identify the relay. Each contact of the relay will be identified by the relay designation followed by a number unique to that contact.
  • Potentiometer 92 (FIG. 3) is connected between a source of reference potential +E and ground and nitrogen flow switch 94 having a contact FS-l which is closed when the flow of nitrogen is normal and open when the flow is below a predetermined amount is connected to the output of flow measuring device 86.
  • Flow switch 94 (FIG. 3) is provided with an adjustment knob 96 which may be set to the flow rate at which it is desired that contact FS-l (FIGS. 3, 7) close.
  • the function of flow relay 94 and contact FS-1 will be explained hereinafter.
  • the output of amplifier 88 is connected to a motor-operated valve 98 (FIG. 3) which provides a continuous control of the rate of flow of nitrogen through pipe 82 to the center jet 22 of bottom tuyeres 20 in response to the signals at its input.
  • FIG. 3a is a control circuit for the operation of relay R As shown, relay R is coupled to a source of voltage B through either a first path consisting of a normally open contact R -l ofa relay R (FIG. 7) or a second path comprising in series normally closed contact R -l (FIG. 3). normally closed contact R -l or normally open contact R -l, and normally open contact R -l. The operation of this circuit will be described in greater detail in connection with FIG. 7. For present purposes, when relay R (FIG. 3a) is deenergized, the reference potential at the arm 90 (FIG. 3) of potentiometer 92 is compared with the actual flow measurement indicated by the output of flow measuring unit 86.
  • Arm 90 of potentiometer 92 is set to a value corresponding to the desired flow rate of nitrogen to bottom center jets 22 and, when the desired. and actual flow rates are the same. the motor-operated valve 98 (FIG. 3) remains fixed in position. If the operator wishes to change the rate of flow of nitrogen through pipe 82, he adjusts arm 90 on potentiometer 92 to produce a voltage difference between the inputs to amplifier 88 causing valve 98 to open or close thereby changing the rate of flow of nitrogen to jets 22. When relay R (FIG. 3a) is energized an input of amplifier 88 is grounded through contact R -I (FIG. 3) causing amplifier 88 to drive motor-operated valve 98 to its closed position.
  • FIG. 4 shows details of the oxygen flow measurement and control unit 54 and the fuel flow measurement and control unit 62.
  • conduit 100 is a portion of the piping connecting oxygen source 52 and solenoid valve 56.
  • An orifice 102 (FIG. 4) is interposed in the upstream end of conduit 100 and an oxygen flow measuring device 104 coupled to the orifice 102.
  • the oxygen flow measuring device 104 Analogous to the nitrogen flow measuring device 86, the oxygen flow measuring device 104 generates a voltage having an output which is proportional to the rate of oxygen flow through orifice 102.
  • conduit 106 (FIGS. 2, 4). which connects fuel source 60 (FIG. 2) to solenoid valve 64 has an orifice 108 connected to fuel flow measuring device 110.
  • the oxygen flow measuring device 104 and fuel flow measuring device 110 are conventional.
  • the output of the oxygen flow measuring device 104 is coupled to one input of an amplifier 112 (FIG. 4), to one end of a potentiometer 113 and to an oxygen flow switch 114 having an adjustment knob 116 and a pair of normally open contacts FS-2 and FS-3 (FIGS. 4, 7) which close when the flow rate set by knob 116 is reached.
  • the other input of amplifier 112 (FIG. 4) is connected to ground through a normally closed contact R -l of a relay R (FIG. 4a) and to the adjustable arm 118 (FIG. 4) of a potentiometer 120 through a normally open contact R -Z of relay R
  • the output of fuel flow measuring device 110 is connected to an input of an amplifier 122 (FIG.
  • a fuel flow switch 123 having an adjustment knob 125 and a normally open contact FS-4 (FIGS. 4, 7), which closes when the flow rate set by knob 125 is reached.
  • the other input of amplifier 122 is connected to ground through a normally closed contact R -3 (FIG. 4) and to the adjustable arm 118' of potentiometer 113 through normally open contact R -4.
  • the output of amplifier 112 is connected to a motoroperated valve 124 (FIG. 4) in conduit 100 and the output of amplifier 122 is connected to a motoroperated valve 126 in conduit 106.
  • RELAY R Relay coil R (FIG. 4a) is connected to the voltage source E through a normally closed contact R,2 connected in series with a network consisting of seriesconnecting normally closed contact R,-l and R l connected in parallel with normally open contacts R -2 and R -l.
  • the purpose of these contacts will be discussed in connection with the schematic control diagram of FIG. 7 but, for the purpose of explaining the operation of the oxygen and fuel flow measurement and control units 54 and 62, it is sufficient to state that relay R is energized to remove the inputs of amplifiers 112 and 122 (FIG. 4) from ground and connect them to the arms of potentiometers 120 and 113 respectively whenever it is desired that oxygen and fuel be delivered to tuyeres 20.
  • the adjustable arms 118, 118' of potentiometers 120 and 113 are set to provide the desired flow rates.
  • potentiometer 120 may be set to provide a flow of oxygen at the rate of 30,00035,000 cubic feet per minute and potentiometer 113 a flow of fuel which is 8% of the oxygen flow rate.
  • control valves 124 and 126 are actuated to change the flow rates.
  • the operation of the oxygen and fuel flow measurement and control units 54 and 62 is the same in this respect as the previously described operation of the nitrogen flow measurement and control unit 44.
  • OXYGEN FLOW MEASUREMENT AND CONTROL UNIT 58 AND FUEL FLOW MEASUREMENT AND CONTROL UNIT 66 FOR SIDE TUYERES 28 Referring to FIG. 5, it is seen that the components and operation of the oxygen flow measurement and control unit 58 and fuel flow measurment and control unit 66 with supply oxygen and fuel to the side tuyeres 28 is quite similar to that of units 54 and 62.
  • a conduit 128 (FIG. having an orifice 130 in its upstream end and a motor-operated control valve 132 at its downstream end is part of the piping connecting the oxygen source 52 and the center jets 36 of side tuyeres 28.
  • conduit 134 (FIG.
  • oxygen flow measuring device 140 having an orifice 136 at its upstream end and a motor-operated valve 138 at its downstream end is part of the piping connecting the fuel source 60 with the annulus jets 38 of side tuyeres 28.
  • An oxygen flow measuring device 140 and a fuel flow measuring device 142 are connected to orifices 130 and 136 to provide voltages proportional to the rate of flow of oxygen and fuel respectively through conduits 128 and 134.
  • the output of oxygen flow measuring device 140 (FIG. 5) is coupled to one input of amplifier 144 and to the end of a potentiometer 146 having its other end connected to ground.
  • the other input of amplifier 144 is connected to ground through a normally closed relay contact R -2 and to the adjustable arm 143 of a potentiometer 148 through a normally open relay contact R -3 (FIG. 5), potentiometer 148 being connected across the voltage source +E.
  • the output of fuel flow measurement device 142 is connected to one input of an amplifier 150, the other input being connected to ground through the normally closed contact R -4 (FIG. 5) and to an adjustable arm 145 on potentiometer 146 through a normally open contact R -S.
  • the outputs of amplifiers 144 and 150 (FIG. 5) are connected to valves 132 and 138 respectively, these valves being controlled in the same manner as valves 124 and 126 of FIG. 4.
  • relay contacts R -2 to R -5 will be explained hereinafter in connection with FIG. 7 but, for the purposes of understanding the operation of FIG. 5, it can be stated that the contacts of relay R (FIG. 7) are in the position shown in FIG. 5 only when selector switch 32 (FIG. 7) is in position A or B and it is desired that valves 132 and 138 (FIGS. 5) be closed to prevent the flow of oxygen or fuel to side tuyeres 28. With switch 32 (FIG. 7) in position C, oxygen and fuel flow to the center jets 36 and annulus jets 38 of side tuyeres 28 at rates determined by the settings of arms 143 and 145 (FIG. 5) of potentiometers 148 and 146 respectively.
  • FIG. 6 The air flow measurement and control unit 70 is illustrated in FIG. 6 wherein conduit 152 having an orifice 154 at its upstream end and a motor-operated control valve 156 and its downstream end is part of the piping connecting compressed air source 68 to solenoidactuated valve 72.
  • Measurement and control unit 70 (FIG. 6) comprises an air flow measuring device 157 and amplifier 158, the desired rate of air flow in conduit 152 being set by adjusting the arm 160 of a potentiometer 162 connected across the voltage source +E. Arm 160 (FIG.
  • valve 156 is connected to one input of amplifier 158, the other input of the amplifier being coupled to the output of air flow measuring device 157 and the output of the amplifier 158 being connected to the motor-operated valve 156. Since amplifier 158 is connected directly to potentiometer 162, valve 156 will be set to provide an air flow through conduit 152 which corresponds to the setting of potentiometer 162.
  • relay coil R (FIG. 7) is connected across the voltage source E.
  • Energizing relay R (FIG. 7) closes contact R -3 picking up the coil of relay R Relay R, (FIG. 7) is designed to pick up without intentional delay but, when deenergized, drops out only after a finite predetermined delay as indicated in FIG. 7 by the legend TD- OFF.
  • contact R -1 closes causing solenoid R (FIGS. 2, 7) in valve 72 (FIG.
  • valve 72 opening valve 72 and permitting compressed air from source 68 to flow to the center jets 22 of bottom tuyeres 20 in accordance with the setting of arm 160 (FIG. 6) on potentiometer 161 of the air flow measurement and control unit (FIG. 6).
  • contact R,-2 (FIG. 7) is opened, deenergizing solenoid R (FIGS. 2, 7) to open valve 50 (FIG. 2) and permit nitrogen to flow from source 42 through the restricting orifice 48 (FIG. 2) to the bottom annulus jets 24.
  • Solenoid valves 50 and 46 (FIG.
  • solenoid valves 72, 56 and 64 which are closed when deenergized
  • valves 46 and 50 would immediately open maintaining pressure on bottom tuyeres 20 by substituting nitrogen for the oxygen and fuel.
  • Motor-operated valve 98 in nitrogen flow measurement and control unit 44 is closed when selector switch 32 (FIG. 7) is in position A because relay RH (FIG. 3a) is picked up through closed contact R -l thereby grounding the amplifier input through contact R -l (FIG. 3).
  • Motor-operated valves 124 and 126 in oxygen and fuel flow measurement and control units 54 and 62 (FIG. 4) are also closed since the inputs of amplifiers 112 and 122 are grounded through contacts R, -2 and R, -,-3 respectively of deenergized relay R (FIG. 4a), relay R being deenergized because contact R,-2 is open and neither contacts R -l or R -l are closed.
  • relay R (FIGS. 7) is energized closing contact R -2 and energizing relay R through the normally closed contact R -3 of relay coil R Relay R (FIG. 7), like relay R picks up instantaneously but drops out when deenergized only after a time delay.
  • the energization of coil R opens contacts R -l and R -2 (FIG. 7) dropping out solenoids R and R (FIGS. 2, 7) respectively causing valves 50 and 46 (FIG. 2) to open and permit nitrogen to flow to the annulus 24 and center jets 22 respectively of bottom tuyeres 20.
  • the compressed air from source 68 (FIG. 2) is cut off by the closing, after a delay, of valve 72 upon the opening of contact R,-l (FIG. 7) due to the deenergization of time delay relay R, by the opening of contact R -3.
  • motor-operated valve 98 is opened by an amount determined by the setting of arm 90 on potentiometer 92 by the dropping out of relay R (FIG. 3a) and the consequent opening of contact R, -l (FIG. 3) and closing of contact R,.,-2.
  • Relay R (FIG. 3a) is deenergized because in position B under normal operation contacts R,-l, R -l and R -l are open.
  • motor-operated valve 98 (FIGS. 3, 3a) is closed when switch 32 (FIG. 7) is moved to position C because relay R (FIG. 3a) is energized grounding the input to amplifier 88 (FIG. 3) through contact R -l and disconnecting it from potentiometer 92 by the opening of contact R,,-2.
  • Relay R (FIG. 3a) is energized because adequate oxygen and fuel flow and pressure are present (this being indicated because contacts R,,-l and R -1 are closed as will be explained hereinafter) and contact Rg'l is closed upon the transfer of switch 32 (FIG. 7) from position 8 to position C. Further, with selector switch 32 (FIG. 7) in position C, relay R (FIGS.
  • 4a is also energized through contacts R -l, R -2 and R,,-2 (FIG. 4a) to open oxygen and fuel valves 124 and 126 (FIG. 4) by connecting the inputs of amplifiers I12 and 122 to potentiometers 120 and 113.
  • POSITION B That is, if nitrogen is called for by moving selector switch 32 (FIG. 4) to position B and the flow is inadequate as indicated by the opening of contact FS-l (FIG. 3), the oxygen valves 124 (FIG. 4), 56 (FIG. 2) and fuel valves 126 (FIG. 4), 64 (FIG. 2) will remain open if switch 32 (FIG. 7) was previously in position C or will automatically move from closed to open if switch 32 was previously in position A. Similarly, if oxygen and fuel are called for by moving selector switch 32 (FIG. 7) to position C and the oxygen flow is inadequate as indicated by the opening of contact FS-3 (FIG. 4). the nitrogen valves 98 (FIG. 3), 46 (FIG.
  • both sets of fluids, nitrogennitrogen and oxygen-fuel, will be provided to the bottom tuyeres 20 to maintain adequate pressure and prevent molten metal from entering them in the event a low rate of gas flow is detected for the selected gas at the bottom center jets 22.
  • valves associated with the gases When proper gas flow is restored, the valves associated with the gases not selected automatically close and the selected valves remain open. For example, if switch 32 (FIG. 7) is in position B and nitrogen flow increases sufficiently to close contact FS-l (FIG. 3) relay R (FIG. 7) is energized opening contact R,,-2 thereby deenergizing solenoids R and R (FIG. 2) allowing 13 valves 56 and 64 to close. Also, relay R (FIG. 4a) is deenergized by the opening of contact R -l thereby grounding the inputs to amplifiers 112 and 122 (FIG. 4) through contacts R 4 and R -3 and causing valves 124 and 126 to close.
  • relay R (FIG. 7) is energized opening contact R -2 thereby deenergizing relay R and energizing solenoids R and R (FIGS. 2, 7) through contacts R -2 and R -I (FIG. 7) allowing valves 46 and 50 (FIG. 2) to close.
  • Relay R (FIG. 3a) is energized by the closing of contact R -l grounding the input to amplifier 88 (FIG. 3) through contact R,,-] and closing valve 98.
  • the control system for operating the tilt motor 30 (FIG. 8) to rotate the converter 10 about trunnions 26 is shown at the bottom of FIG. 7 and in FIG. 8. It comprises an AUTO-MANUAL switch 163 (FIG. 7) which energizes a relay coil R (FIG. 7) having a contact R -l (FIG. 8) in series with a FORWARD-OFF- REVERSE switch 164.
  • a relay coil R (FIG. 8) having a contact R -l connected between the positive terminal of the voltage source and tilt motor 30 and a contact R -2 between the grounded terminal of the voltage source and motor 30, is coupled to the FOR- WARD position of switch 164.
  • a relay coil R (FIG.
  • switch 164 having a contact R -l connected between the junction of contact R -l and motor 30 and ground and a contact R -2 connected between the junction of contact R -2 and motor 30 and the positive sides of the voltage source, is coupled to the REVERSE position of switch 164.
  • switch 163 (FIG. 7) is in the MAN- UAL position, relay R is energized and the tilt motor 30 operated in the forward direction by turning switch 164 (FIG. 8) to FORWARD thereby energizing relay R and contacts R -l and R -2.
  • the forward direction of converter motion may be defined as rotation from the orientation shown in FIGS. 10-10, for example.
  • switch 164 (FIG.
  • switch 163 (FIG. 7) is used only when the converter 10 is being prepared for the refining operation and there is no molten charge in the vessel. Thus, for normal operation switch 163 (FIG. 7) is is kept in the AUTO position.
  • the converter 10 must never be tilted upright when selector switch 32 (FIG. 7) is in position A and there is a molten charge in the vessel 10 since the compressed air being fed to the center jets 22 of the bottom tuyeres 20 is at reduced pressure. Accordingly, a normally closed contact R -4 (FIG. 7) of relay R is connected in series with coil R when switch 163 is in the AUTO position thereby preventing operation of the tilt motor 30 (FIG. 8) when selector switch 32 (FIG. 7) is in position A. When switch 32 (FIG. 7) is moved to position B, sufficient pressure must be applied from nitrogen source 42 to the center 22 and annulus jets 24 of bottom tuyeres 20 to permit the converter 10 to be moved to an upright position (FIG.
  • contacts PS-Z and PS-4 (FIGS. 2, 7) of pressure switches 74 and 78 (FIG. 2) are connected in series with a relay coil R (FIG. 7).
  • Contacts PS-2 and PS-4 (FIGS. 2, 7) close only when the pressure required for converter operation in the upright position of FIG. lb is present at the annulus 24 and center jets 22 respectively of bottom tuyeres 20 and, therefore, relay R (FIG. 7) is energized only under these conditions.
  • contact R -l closes energizing coil R through the closed contact R -3 of relay R Contact R -2 (FIG.
  • relay R also closes preventing relay R from dropping out in the event the pressure should subsequently decrease at the bottom tuyeres 20 thereby deenergizing relay R This is essential since it would be necessary to quickly tilt the converter 10 onto its side if pressure were lost at the bottom tuyeres 20, and it is desirable that this be possible without moving switch 163 (FIG. 7) to the MANUAL position. Also, contact R -7 (FIG. 7) is connected in parallel with contact R -3 to permit lowering of the converter 10 when switch 32 (FIG. 7) is in position C.
  • the fourth function that of making certain that adequate pressure is maintained on the bottom tuyeres 20 at all times, is provided by circuits which automatically connect nitrogen to the center 22 and annulus jets 24 if fuel and oxygen are being used and the pressure of one of these should drop below a predetermined value. Further, the circuits automatically connect fuel to the annulus jet 24 and oxygen to the center jet 22 if nitrogen is being used and the pressure at either the annulus 24 or center jets 22 drops below a predetermined value.
  • the circuit may be reset by turning selector switch 32 (FIG. 7) to position C thereby dropping out relay R (FIG. 7) while maintaining flow of oxygen and nitrogen to bottom tuyeres 20.
  • Valves I24 and 126 (FIG. 4) in the oxygen and fuel flow measurement and control units 54 and 62 are opened by the energization of relay R (FIG. 4a) which couples the inputs of amplifiers 112 and 122 (FIG. 4) to Potentiometers I and 113 through contacts R -2 and Il -4.
  • Relay R (FIG. 4a) is energized through contacts R -2 and Il -2 and remains energized when the circuit is reset by turning switch 32 (FIG. 7) to position C through contact R -1 (FIG. 4).
  • Valve 98 (FIG. 3) in the nitrogen flow measurement and control unit 44 is closed by the energization of relay R (FIG. 3a) through contacts Rg'l, R -I and R -l (indicating adequate oxygen flow) and through contacts Rg'l, R -1 and R -1 after switch 32 (FIG. 7) has been moved in position C.
  • selector switch 32 (FIG. 7) is in position C, oxygen and fuel are being supplied to the bottom tuyeres 20 and one or both the contacts PS-l and PS-3 (FIGS. 2, 7) closes, relay R (FIG. 7) will be picked up through contact R 8 of relay R and contact It -6 of relay R Energization of relay R (FIG. 7) causes contact R -5 to close, picking up relay R which, results in the deenergization of solenoids R and R (FIGS. 2, 7) thereby connecting nitrogen source 42 (FIG. 2) to the bottom tuyeres 20.
  • Contact R,,3 (FIG.
  • Relay R (FIG. 7) is sealed in through contacts 11 -6 and R -9 to prevent the system from automatically switching back to oxygen and fuel after operating pressure has been restored by the substitution of nitrogen source 42 (FIG. 2) for the oxygen and fuel sources 60 and 52. Also, contacts R -6 and R -4 (FIG. 7) prevent either relay R or R, from being energized if the other relay has been picked up.
  • the circuit may be reset by turning selector switch 32 (FIG. 7) to position B thereby dropping out relay R while maintaining flow of nitrogen to bottom tuyeres 20.
  • Valve 98 (FIG. 3) in the nitrogen flow measurement and control unit 44 is opened by the deenergization of relay R (FIG. when contact Rg-l opens thereby connecting the input of amplifier 88 (FIG. 3) to potentiometer 92.
  • Relay R (FIG. 3a) remains deenergized after the circuit is reset by the opening of contact R -1.
  • Valves I24 and 126 (FIG. 4) in the oxygen and fuel flow measurement and control units 54 and 62 are closed, as previously described, by the deenergization of relay R (FIG. when contact R -2 opens.
  • Relay R (FIG. 40) remains deenergized and valves 124 and 126 (FIG. 4) remain closed after the circuit has been reset by moving switch 32 (FIG.
  • FUNCTION 5 Damage may be caused to the bottom tuyeres 20 when oxygen and fuel are being delivered, even though the pressure is adequate, if the oxygen or fuel flow rates should drop below values which will permit burning of the bottom annulus 24 and center jets 22.
  • the system automatically switches to nitrogen in bottom tuyeres 20 until the vessel 10 can be tilted and the condition corrected.
  • selector switch 32 (FIG. 7) is in position C thereby causing relays R R R (FIG. 7) and solenoids R and R (FIGS. 2, 7) to be energized. If the flow rate of either the oxygen, fuel or both should drop below a predetermined value, one or both of the contacts FS-2 (FIGS.
  • Relay R (FIG. 7) seals in through contacts R -9 and R 6 and remains energized until selector switch 32 (FIG. 7) is moved to position B corresponding to nitrogen flow to the bottom tuyeres 20.
  • Relay R (FIG. 7) has a delay characteristic which permits it to be energized only after a predeter mined interval has elapsed. This is to prevent energization of relay R (FIG. 7) when switch 32 (FIG. 7) is first moved to position C and there has been insufficient time for the flow of oxygen and fuel to be established.
  • a cam switch 166 (FIG. 7) on converter 10 which closes when the converter 10 is intermediate the position shown in FIGS. 1A and 1C.
  • Switch 166 (FIG. 7) is connected in series with contact R,-5 of relay R, to energize relay R, in the event the converter 10 is upright (FIG. 1B) and switch 32 (FIG. 7) is moved to position A.
  • solenoid R (FIGS. 2, 7) would be deenergized opening valve 46 (FIG. 2) to add nitrogen to the compressed air supplied through valve 72 in position A and thereby provide sufficient pressure at the bottom center jets 22 to prevent the molten metal from entering the bottom tuyeres 20.
  • ALTERN ATIVE EMBODIMENTS From a consideration of FIG. 9, it will be apparent that the present invention may be employed with a bottom blown converter 210 having bottom submerged tuyeres 212, the side submerged tuyeres 214 and side tuyeres 216 directed toward the carbon monoxide zone (CO zone) of the converter 210.
  • This bottom blown converter 210 has a shell 218 provided with a refractory lining 220 and a mouth 222 and is rotatable on trunnions 224.
  • the tuyeres 212, 214, 216 are adapted to carry in an inner pipe 213 either a fluid alone, such as oxygen, air, argon, or mixtures thereof, or entrained pulverized additives therein, such as a fluxing agent (burned lime (CaO) or the like), a Iiquefying agent (fluorspar (CaF or the like), or a blocking or deoxidizing agent (ferro manganese or the like), and in an outer pipe 215 a shroud gas, such as propane, natural gas, light fuel oil or the like.
  • a fluxing agent burned lime (CaO) or the like
  • Iiquefying agent fluorspar (CaF or the like)
  • a blocking or deoxidizing agent ferrro manganese or the like
  • a shroud gas such as propane, natural gas, light fuel oil or the like.
  • the present invention is also applicable to a Heroult Type electric-arc steelmaking furnace 2100 provided with a vertical and inclined bottom submerged tuyere 212a and 212a, side submerged tuyeres 214a, and a side tuyere 216a directed toward the carbon monoxide zone (CO zone) of the furnace 210a.
  • This electric arc steelmaking furnace 210a has a shell 218a provided with a refractory lining 2200, a side door 226, a refractory roof 228 provided with electrode holes 230, a tap hole 232, and a pouring spout 234 extending from the tap hole 232.
  • the tuyeres 212 and 2120', 214a, 2160 are adapted to carry in an inner pipe 213 either a fluid alone, such as oxygen, air, argon, or mixtures thereof, or entrained pulverized additives therein, such as a fluxing agent (burned lime (CaO) or the like), a liquefying agent (fluorspar (CaF or the like), or a blocking or deoxidizing agent (ferro manganese or the like), and in an outer pipe 215, a shroud gas, such as propane, natural gas, light fuel oil or the like.
  • a fluxing agent burned lime (CaO) or the like
  • fluorspar fluorspar
  • ferro manganese or the like a blocking or deoxidizing agent
  • the present invention may be employed as shown in FIG. 11 with the open hearth furnace 210b having the vertical and inclined bottom submerged tuyeres 212b and 212b', the side submerged tuyere 214b, and the side tuyere 216b directed toward the carbon monoxide zone (CO zone) of the furnace 2111b.
  • This open hearth furnace 2101) includes a refractory lined bottom 236, a refractory lined sloping back wall 238, a refractory lined front wall 240, a charging door 242 in the wall 240, and a refractory lined roof 244.
  • a tap hole 232b opposite the charging door 242 leads to a pouring spout 234b.
  • the tuyeres 212b, 2121;, 214b, 21612 are adapted to carry in an inner pipe 213 either a fluid alone, such as oxygen, air, argon, or mixtures thereof, or entrained pulverized additives therein, such as a fluxing agent (burned lime (CaO) or the like), a liquefying agent (fluorspar can or the like), or a blocking or deoxidizing agent (ferro manganese or the like) and in an outer pipe 215, a shroud gas, such as propane, natural gas, light fuel oil or the like.
  • the present invention may be employed with a tilting open hearth furnace 210C mounted on rollers 246 arranged in a circular path for providing rotation on the longitudinal axis of the furnace 210C for pouring the refined steel through a tap hole 232C and a pouring spout 2346.
  • the tiltable open hearth furnace 2100 has vertical and inclined bottom submerged tuyeres 212C and 212C connected through a blast box 248 to the lines 76 and 80 shown in FIG. 2.
  • a submerged side tuyere 214c and a side tuyere 2166 directed toward the carbon monoxide zone (CO zone) of the furnace 210C are employed.
  • the tiltable open hearth furnace 2100 has a refractory lined bottom 236C, refractory lined back wall 238e, refractory lined front wall 240C (provided with a charging door 2420) and a refractory lined roof 244C.
  • the tuyeres 212C, 212C, 214C, 2166 are adapted to carry in an inner pipe 213 either a fluid alone, such as oxygen, air, argon, or mixtures thereof, or entrained pulverized additives therein, such as a fluxing agent (burned lime (CaO) or the like), a liquefying agent (fluorspar (CaF or the like), or a blocking or deoxidizing agent (ferro manganese or the like), and in an outer pipe 215, a shroud gas, such as propane, natural gas, light fuel oil or the like.
  • a fluxing agent burned lime (CaO) or the like
  • fluorspar fluorspar
  • a blocking or deoxidizing agent ferrro manganese or the like
  • a shroud gas such as propane, natural gas, light fuel oil or the like.
  • the present invention is employed with a hot metal mixer 210d having a shell 218d provided with a refractory lining 220d, and having also an inlet mouth 222d and a pouring spout 234d.
  • the mixer 210d is oscillatable on rollers 246d between the charging and discharging positions.
  • Such mixer 210d has vertical and inclined bottom submerged tuyeres 212d, 212d, side submerged tuyeres 214d and side tuyere 216d directed toward the carbon monoxide zone (CO zone) of the mixer 210d.
  • the tuyeres 212d, 212d, 2l4d, 2l6d are adapted to carry in an inner pipe 213 either a fluid alone, such as oxygen, air, argon, or mixtures thereof, or entrained pulverized additives therein, such as a fluxing agent (burned lime (CaO) or the like), a liquefying agent (fluorspar (CaF- or the like), or a blocking or deoxidizing agent (ferro manganese or the like), and in an outer pipe 215, a shroud gas, such as propane. natural gas, light fuel oil or the like.
  • a fluxing agent burned lime (CaO) or the like
  • fluorspar fluorspar
  • ferro manganese or the like a blocking or deoxidizing agent
  • a shroud gas such as propane. natural gas, light fuel oil or the like.
  • a discharge tuyere or tuyeres 32 (FIGS. 9, 10, 11, l2, 13) is disposed adjacent a discharge opening such as the mouth 222 (FIG. 9); the pouring spouts 234 (FIG. 10); 234b (FIG. 11); 234C (FIG. 12); and 234d (FIG. 13) to prevent the formation of skulls adjacent or on the discharge opening during the pouring operation particularly those chromium-nickel skulls produced during the refining of stainless steel.
  • fluid control means for coupling sources of said first and second sets of fluids to said tuyere
  • switching means connecting said selector means to said fluid control means for selectively coupling said first or second sets of fluids to said tuyere in accordance with the position of said selector switch, said switching means including fluid transfer control means for maintaining flow of one of said first and second sets of fluids after the other of said sets of fluids has been selected until flow of said other set of fluids has been established, said apparatus preventing a molten charge in said converter from entering said tuyere and causing damage thereto.
  • tip paratus is an open hearth furnace.
  • tuyere is a tuyere disposed adjacent a pour opening of said apparatus to prevent the formation of skulls adjacent said pour opening during pouring of said molten metal.
  • Apparatus for controlling the operation of a steel refining converter as defined by claim 16 wherein said first fluid source is coupled to said center jet through a first flow control means and a first valve means and to said annulus jet through a second flow control means and a second valve means, said second fluid source is coupled to said center jet through a third flow control means and a third valve means, and said third fluid source is coupled to said annulus jet through a fourth flow control means and a fourth valve means.
  • Apparatus for controlling the operation of a steel refining converter as defined by claim 17 wherein the means for detecting a condition wherein the flow rate of said first or second fluids is inadequate comprises first and second flow switches in said first and third flow control means.
  • Apparatus for controlling the operation of a steel refining converter as defined by claim 18 wherein said means for adding said second and third fluids to said center and annulus jets respectively when the flow of the selected first fluid is inadequate comprises means connecting said first flow switch to said third and fourth valve means, said third and fourth valve means opening to permit flow of said second and third fluids respec tively when the flow measured by said first flow switch is below a predetermined value.
  • Apparatus for controlling the operation of a steel refining converter as defined by claim 18 wherein said means for adding said first fluid to said center and an nulus jets respectively when the flow rate of the second fluid is inadequate comprises means connecting said second flow switch to said first and second valve means, said first and second valve means opening to permit flow of said first fluid when the flow measured by said second flow switch is below a predetermined value.
  • Apparatus for controlling the operation of a steel refining converter as defined by claim 18 which further comprises means for detecting inadequate flow of said third fluid comprising a third flow switch in said fourth flow control means, and means coupling said second and third flow switches to said first and second valve means for substituting said first fluid at said center and annulus jets when the flow rate of said second or third fluids is inadequate, said first and second valve means opening to permit flow of said first fluid when the flow measured by said second or third flow switch is below a predetermined value.
  • Apparatus for controlling the operation of a steel refining converter as defined by claim 23 wherein means are provided for substituting said second and third fluids to said center and annulus jets respectively when the pressure of the selected first fluid is inadequate said means comprising means connecting said first and second pressure measuring means to said third and fourth valve means, said third and fourth valve means opening to permit flow of said second and third fluids respectively when the pressure measured by either of said first and second pressure means is below a predetermined value.
  • first delay means is further provided for coupling said first and second pressure measuring means to said first and second valve means, said first and second valve means closing after a predetermined delay to prevent flow of

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  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Carbon Steel Or Casting Steel Manufacturing (AREA)
  • Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
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US312173A 1972-08-01 1972-12-04 Method and apparatus for controlling the operation of a steel refining converter Expired - Lifetime US3895785A (en)

Priority Applications (13)

Application Number Priority Date Filing Date Title
US312173A US3895785A (en) 1972-08-01 1972-12-04 Method and apparatus for controlling the operation of a steel refining converter
GB3288973A GB1447642A (en) 1972-08-01 1973-07-10 Method and apparatus for controlling the operation of a steel refining converter
AU57985/73A AU480299B2 (en) 1972-08-01 1973-07-11 Method and apparatus for controlling the operation ofa bottom-blown steel refining converter
YU01943/73A YU194373A (en) 1972-08-01 1973-07-17 Device for the oxidation of raw iron into steel
DE2337846A DE2337846C2 (de) 1972-08-01 1973-07-25 Vorrichtung und Verfahren zum Regeln eines Gas-Einblasprozesses in ein Stahlwerksgefäß
LU68107A LU68107A1 (en, 2012) 1972-08-01 1973-07-27
NL7310523A NL7310523A (en, 2012) 1972-08-01 1973-07-30
IT69319/73A IT991926B (it) 1972-08-01 1973-07-31 Procedimento e dispositivo per l esercizio di un convertitore di affinazione dell acciaio
AT671573A ATA671573A (de) 1972-08-01 1973-07-31 Verfahren zum frischen von roheisen zu stahl in einem frischgefaess mit wenigstens einer aus einer mittelduese und einer diese umgebenden ringduese bestehenden blasform sowie einrichtungen zum durchfuehren des verfahrens
ES417414A ES417414A1 (es) 1972-08-01 1973-07-31 Un aparato para controlar el funcionamiento de un converti-dor de afino de acero.
FR7328267A FR2194785B1 (en, 2012) 1972-08-01 1973-08-01
US05/574,838 US4047937A (en) 1972-12-04 1975-05-05 Method for controlling the operation of a steel refining converter
ES442692A ES442692A1 (es) 1972-08-01 1975-11-17 Un metodo de hacer funcionar un convertidor basculante de a-fino de acero.

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US27701772A 1972-08-01 1972-08-01
US312173A US3895785A (en) 1972-08-01 1972-12-04 Method and apparatus for controlling the operation of a steel refining converter

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DE (1) DE2337846C2 (en, 2012)
ES (2) ES417414A1 (en, 2012)
FR (1) FR2194785B1 (en, 2012)
GB (1) GB1447642A (en, 2012)
IT (1) IT991926B (en, 2012)
LU (1) LU68107A1 (en, 2012)
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US3985350A (en) * 1974-09-20 1976-10-12 Emile Sprunck Converter
US4050681A (en) * 1973-05-25 1977-09-27 Eisenwerk-Gesellschaft Maximilianshutte Mbh Apparatus for the controlled feeding of a refining gas and of a fluid protective medium
US4093190A (en) * 1975-06-25 1978-06-06 Creusot-Loire Process for the protection of a refractory wall in service
US4097028A (en) * 1975-02-06 1978-06-27 Klockner-Werke Ag Method of melting and apparatus therefor

Families Citing this family (4)

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Publication number Priority date Publication date Assignee Title
DE2834737A1 (de) * 1977-08-26 1979-03-08 British Steel Corp Stahlherstellungsverfahren
EP0045658A1 (en) * 1980-08-06 1982-02-10 British Steel Corporation Gas inlet orifice monitoring
DE3143795C2 (de) * 1981-11-04 1983-10-20 Klöckner Stahlforschung GmbH, 8458 Sulzbach-Rosenberg "Ventil zur Strömungsmittelzufuhr"
SE8702338L (sv) * 1987-06-05 1988-12-06 Aga Ab Gasspolning av smaelta i skaenk

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US33090A (en) * 1861-08-20 Marcus Lane Improvement in treating metals
US707776A (en) * 1901-08-21 1902-08-26 Electro Metallurg Francaise Soc Oscillating electric furnace.
US1958581A (en) * 1932-04-18 1934-05-15 Cass L Kennicott Ore treatment
US3212879A (en) * 1961-10-13 1965-10-19 Siderurgie Fse Inst Rech Process and apparatus for controlling shaft furnaces
US3343826A (en) * 1960-06-27 1967-09-26 Exxon Research Engineering Co Fluid fuel control system and apparatus for furnaces
US3706549A (en) * 1968-02-24 1972-12-19 Maximilianshuette Eisenwerk Method for refining pig-iron into steel

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DE1758816C2 (de) * 1968-08-13 1975-11-20 Eisenwerk-Gesellschaft Maximilianshuette Mbh, 8458 Sulzbach-Rosenberg Verfahren zum Frischen von Roheisen zu Stahl

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Publication number Priority date Publication date Assignee Title
US33090A (en) * 1861-08-20 Marcus Lane Improvement in treating metals
US707776A (en) * 1901-08-21 1902-08-26 Electro Metallurg Francaise Soc Oscillating electric furnace.
US1958581A (en) * 1932-04-18 1934-05-15 Cass L Kennicott Ore treatment
US3343826A (en) * 1960-06-27 1967-09-26 Exxon Research Engineering Co Fluid fuel control system and apparatus for furnaces
US3212879A (en) * 1961-10-13 1965-10-19 Siderurgie Fse Inst Rech Process and apparatus for controlling shaft furnaces
US3706549A (en) * 1968-02-24 1972-12-19 Maximilianshuette Eisenwerk Method for refining pig-iron into steel

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4050681A (en) * 1973-05-25 1977-09-27 Eisenwerk-Gesellschaft Maximilianshutte Mbh Apparatus for the controlled feeding of a refining gas and of a fluid protective medium
US3985350A (en) * 1974-09-20 1976-10-12 Emile Sprunck Converter
US4097028A (en) * 1975-02-06 1978-06-27 Klockner-Werke Ag Method of melting and apparatus therefor
US4093190A (en) * 1975-06-25 1978-06-06 Creusot-Loire Process for the protection of a refractory wall in service

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ES442692A1 (es) 1977-04-16
ATA671573A (de) 1980-03-15
FR2194785B1 (en, 2012) 1978-05-05
GB1447642A (en) 1976-08-25
DE2337846C2 (de) 1984-11-29
FR2194785A1 (en, 2012) 1974-03-01
AU5798573A (en) 1975-01-16
YU194373A (en) 1982-02-28
ES417414A1 (es) 1976-06-16
NL7310523A (en, 2012) 1974-02-05
LU68107A1 (en, 2012) 1973-10-03
IT991926B (it) 1975-08-30
DE2337846A1 (de) 1974-02-14

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