US3050299A - Method and apparatus for controlling feed to shaft furnace - Google Patents
Method and apparatus for controlling feed to shaft furnace Download PDFInfo
- Publication number
- US3050299A US3050299A US822298A US82229859A US3050299A US 3050299 A US3050299 A US 3050299A US 822298 A US822298 A US 822298A US 82229859 A US82229859 A US 82229859A US 3050299 A US3050299 A US 3050299A
- Authority
- US
- United States
- Prior art keywords
- temperature
- furnace
- burden
- shaft furnace
- spots
- 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
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21B—MANUFACTURE OF IRON OR STEEL
- C21B5/00—Making pig-iron in the blast furnace
- C21B5/008—Composition or distribution of the charge
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B1/00—Preliminary treatment of ores or scrap
- C22B1/14—Agglomerating; Briquetting; Binding; Granulating
- C22B1/16—Sintering; Agglomerating
- C22B1/214—Sintering; Agglomerating in shaft furnaces
Definitions
- the combustion zone remains at a uniform constant level, but in practice its level tends to deviate non-uniformly.
- the traversing drive for the conveyor commonly is equipped with a speed control device which causes the discharge end of the conveyor to dwell over some spots on the burden and pass quickly over others.
- Previously known means through which the speed control device receives its intelligence include a mechanical feeler, as shown in De Vaney et al. Patents Nos. 2,792,132 and 2,834,484, or a temperature measuring device, as shown in Sisco Patent No. 2,739,800.
- a feeler senses the level of the stockline profile and causes the conveyor to dwell over low spots and pass quickly over high spots.
- a temperature measuring device senses the temperature of combustion gases from different spots on the burden and causes the conveyor to dwell over hot spots and pass quickly over cool spots. Thus the feeler tends to maintain a level stockline, and the temperature measuring device a uniform combustion gas temperature, but I have observed neither afforns exactly the form of control that is needed.
- An object of the present invention is to provide an improved method and apparatus for controlling feed of material to a shaft furnace in which control is effected in accordance with the relative permeability of the furnace burden to fiow of gases.
- a further object is to provide an improved method and apparatus for controlling the traversing drive of a conveyor which feeds a shaft furnace whereby the discharge end of the conveyor dwells over spots in the furnace burden of high permeability and passes quickly over spots of low permeability.
- a more specific object is to provide an improved control method and apparatus of the foregoing type in which the velocity of combustion gas at different spots over the burden is measured with an anemometer or the equivalent, the temperature at these spots is measured with a thermocouple or the equivalent, these measurements are combined to furnish an indication of gas velocity at a standard temperature, and this indication is used to effect control of the traversing drive.
- FIGURE l is a diagrammatic vertical sectional View of the upper portion of a shaft furnace whose feed means is equipped with a control apparatus in accordance with my invention.
- FIGURE 2 is a schematic diagram of an electric circuit suitable for use in my apparatus.
- FIGURE l shows the upper portion of a conventionall shaft furnace 10 for indurating balled iron ore fines.
- the furnace can be either rectangular or circular in cross sec-v tion, and its feed means can lbe of any suitable type for traversing the top, for example as shown in the afore-v mentioned patents.
- the feed means is shown diagrammatically as including a conveyor belt 12, a movable carriage 13 on which the belt is mounted, a fixed support 14 for the carriage, and a. variable speed traversing drive motor 15.
- the furnace has a hood 16 above its feed means and a stack 17 above the hood.
- the furnace wall has a suitably curtained opening for admitting the feed means, as known in the art.
- the feed means feeds balls to the furnace where they form a burden B. Air is introduced to the' and escape through the stack.
- the burden has the usuall combustion zone C.
- carriage 13 ⁇ carries an anemometer 18 and a thermocouple 19 positioned over the burden B adjacent the spot to which con-V veyor 12 discharges balls.
- the anemometer measures the velocity at which combustion gases pass through the burden at each spot and generates a voltage proportionate thereto.
- thermocouple measures the temperature of these gases and generates another voltage proportionate to this temperature. The latter voltage is used to compute the velocity of combustion gases at a standard temperature (32 F.).
- the permeability of the bed below the spot where velocity is measured is of course directly proportional to the velocity at standard temperature.
- Both the anemometer and the thermocouple per se are conventional instruments; hence they are not shown in detail.
- FIGURE 2 shows schematically one form of circuit for accomplishing this computation.
- the anemometer 18 and thermocouple 19 transmit voltages proportionate to the velocity and temperature to conventional voltage amplifiers 20 and 21 respectively. These amplifiers are equipped with volume controls 22 and 23, which are adjusted manually to place the voltage outputs of the two ampliers on scale.
- the negative output terminals of both amplifiers are electrically connected to one end of a potentiometer slide wire 24.
- a bias voltage source 28 is connected between the negative output terminal of amplifier 21 and the slide wire to furnish a voltage proportionate to the term 460 of the foregoing ratio.
- the positive output terminal of amplifier 21 is electrically connected to the other end of this slide wire.
- the positive output terminal of amplifier 20 is electrically connected to the arm 25 of the potentiometer through a conventional self-balancing device 26.
- a voltage proportionate t-o the absolute temperature (460-I-T) is applied across the full length of the slide wire 24 and a voltage proportionate to the anemometer reading across a variable portion of the slide wire determined by the position of arm 25.
- FIGURE 2 also shows schematically one form of speed Patented Aug. 21, 1962 ⁇
- This device includes a second potentiometer 27 in the iield circuit of this motor.
- the arm of potentiometer 27 is mechanically linked to arm 25, as indicated by a dotted line 30, whereby potentiometer 27 is automatically adjusted with adjustment of potentiometer 24, 25 and regulates the speed of the traversing drive motor accordingly. For example if the anemometer 18 and the discharge end of conveyor 12 reach a spot where the burden has unduly high permeability, the potentiometer arm 25 moves clockwise to restore balance in the control circuit.
- Potentiometer 27 is adjusted to increase the field strength of motor 15 and thus reduce the speed, whereby the discharge end of the conveyor dwells over this spot. The reverse action occurs when the discharge end of the conveyor reaches a spot of low permeability.
- the potentiometer 27 can automatically be connected in the eld circuit of the appropriate motor through suitable relays, or else each motor can be equipped with its own potentiometer.
- a shaft furnace which includes a feeder adapted to deliver material to the top of the furnace, a traversing drive for said feeder, and a speed control device for said drive
- an apparatus for adjusting said speed control device comprising means for measuring the velocity of combustion gases passing through the furnace burden adjacent the spot where the feeder is delivering material, separate means for measuring the gas temperature at approximately the same spot, computing means operatively connected with said velocity measuring means and said temperature measuring means for determining the gas velocity at a standard temperature and thereby providing an indication of the relative permeability of the burden to ow of gases below this spot, and means operatively connecting said computing means with said speed control device to increase the feed rate over spots of relatively high permeability and decrease the feed rate over spots of relatively low permeability.
- a method of controlling feed to a shaft furnace to which material feeds from a traversing feeder comprising measuring the velocity of combustion gases passing through the burden adjacent the spot where the feeder is delivering material, developing a first voltage proportionate to the velocity measurement, separately measuring the temperature of the combustion gases at approximately the same spot, developing a second voltage proportionate to the absolute temperature measurement, balancing said first voltage against said second voltage to obtain an indication of the gas velocity at a standard temperature and thus of the relative permeability of the burden to flow ⁇ of gases below this spot, and varying the rate of traverse in accordance with said indication to increase the feed rate over spots of relatively high permeability and decrease the rate over spots of relatively low permeability.
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- Life Sciences & Earth Sciences (AREA)
- Geochemistry & Mineralogy (AREA)
- Geology (AREA)
- Mechanical Engineering (AREA)
- Tunnel Furnaces (AREA)
- Manufacture And Refinement Of Metals (AREA)
- Vertical, Hearth, Or Arc Furnaces (AREA)
- Refinement Of Pig-Iron, Manufacture Of Cast Iron, And Steel Manufacture Other Than In Revolving Furnaces (AREA)
Description
T. F. REED Aug. 21, 1962 METHOD AND APPRATUS FOR CONTROLLING FEED T0 SHAFT FURNACE Filed June 23, 1959 N @uw INVENTOR. 77/0/1/45 F. @50
are
3,050,299 METTI-101) AND APPARATUS FOR CNTROLLING FEED Tt) SHAFT FURNACE Thomas F. Reed, Pittsburgh, Pa., assigner to United States Steel Corporation, a corporation of New .ersey Filed .lune 23, 1959, Ser. No. 822,298 2 Claims. (Cl. 263-29) or disk and then heat the balls to the point of incipient fusion in a shaft furnace. The balls feed to the top of the furnace, attain a maximum temperature in a combustion zone a few inches below the stocklne, and discharge from the bottom. The usual feeding means includes a conveyor whose discharge end continually traverses the furnace above the stockline and deposits balls over the whole area. Typical conveyor arrangements for this purpose are shown in Davis Patent No. 2,757,782 and De Vaney et al. Patent No. 2,834,484.
Desirably the combustion zone remains at a uniform constant level, but in practice its level tends to deviate non-uniformly. To correct such deviations the traversing drive for the conveyor commonly is equipped with a speed control device which causes the discharge end of the conveyor to dwell over some spots on the burden and pass quickly over others. Previously known means through which the speed control device receives its intelligence include a mechanical feeler, as shown in De Vaney et al. Patents Nos. 2,792,132 and 2,834,484, or a temperature measuring device, as shown in Sisco Patent No. 2,739,800. A feeler senses the level of the stockline profile and causes the conveyor to dwell over low spots and pass quickly over high spots. A temperature measuring device senses the temperature of combustion gases from different spots on the burden and causes the conveyor to dwell over hot spots and pass quickly over cool spots. Thus the feeler tends to maintain a level stockline, and the temperature measuring device a uniform combustion gas temperature, but I have observed neither afforns exactly the form of control that is needed.
An object of the present invention is to provide an improved method and apparatus for controlling feed of material to a shaft furnace in which control is effected in accordance with the relative permeability of the furnace burden to fiow of gases.
A further object is to provide an improved method and apparatus for controlling the traversing drive of a conveyor which feeds a shaft furnace whereby the discharge end of the conveyor dwells over spots in the furnace burden of high permeability and passes quickly over spots of low permeability.
A more specific object is to provide an improved control method and apparatus of the foregoing type in which the velocity of combustion gas at different spots over the burden is measured with an anemometer or the equivalent, the temperature at these spots is measured with a thermocouple or the equivalent, these measurements are combined to furnish an indication of gas velocity at a standard temperature, and this indication is used to effect control of the traversing drive.
In the drawing:
FIGURE l is a diagrammatic vertical sectional View of the upper portion of a shaft furnace whose feed means is equipped with a control apparatus in accordance with my invention; and
FIGURE 2 is a schematic diagram of an electric circuit suitable for use in my apparatus.
FIGURE l shows the upper portion of a conventionall shaft furnace 10 for indurating balled iron ore fines. The
furnace can be either rectangular or circular in cross sec-v tion, and its feed means can lbe of any suitable type for traversing the top, for example as shown in the afore-v mentioned patents. For purposes of illustration, the feed means is shown diagrammatically as including a conveyor belt 12, a movable carriage 13 on which the belt is mounted, a fixed support 14 for the carriage, and a. variable speed traversing drive motor 15. Preferably the furnace has a hood 16 above its feed means and a stack 17 above the hood. The furnace wall has a suitably curtained opening for admitting the feed means, as known in the art. The feed means feeds balls to the furnace where they form a burden B. Air is introduced to the' and escape through the stack. The burden has the usuall combustion zone C.
ln accordance with the present invention, carriage 13` carries an anemometer 18 and a thermocouple 19 positioned over the burden B adjacent the spot to which con-V veyor 12 discharges balls. As the conveyor traverses the furnace, the anemometer measures the velocity at which combustion gases pass through the burden at each spot and generates a voltage proportionate thereto. thermocouple measures the temperature of these gases and generates another voltage proportionate to this temperature. The latter voltage is used to compute the velocity of combustion gases at a standard temperature (32 F.). The permeability of the bed below the spot where velocity is measured is of course directly proportional to the velocity at standard temperature. Both the anemometer and the thermocouple per se are conventional instruments; hence they are not shown in detail.
' The gas velocity at standard temperature can be computed by multiplying the anemometer reading lby the ratio where Tis the temperature indicated by the thermocouple. FIGURE 2 shows schematically one form of circuit for accomplishing this computation. The anemometer 18 and thermocouple 19 transmit voltages proportionate to the velocity and temperature to conventional voltage amplifiers 20 and 21 respectively. These amplifiers are equipped with volume controls 22 and 23, which are adjusted manually to place the voltage outputs of the two ampliers on scale. The negative output terminals of both amplifiers are electrically connected to one end of a potentiometer slide wire 24. A bias voltage source 28 is connected between the negative output terminal of amplifier 21 and the slide wire to furnish a voltage proportionate to the term 460 of the foregoing ratio. The positive output terminal of amplifier 21 is electrically connected to the other end of this slide wire. The positive output terminal of amplifier 20 is electrically connected to the arm 25 of the potentiometer through a conventional self-balancing device 26. Thus a voltage proportionate t-o the absolute temperature (460-I-T) is applied across the full length of the slide wire 24 and a voltage proportionate to the anemometer reading across a variable portion of the slide wire determined by the position of arm 25. When the circuit balances, no current flows from amplifier 20. The self-balancing device 26 and arm 25 are mechanically connected as indicated by a dotted line 29, whereby the self-balancing device automatically positions arm 25 to balance the circuit in this way. With proper calibration, the position of the arm when the circuit is in balance indicates the relative permeability of the burden.
FIGURE 2 also shows schematically one form of speed Patented Aug. 21, 1962` The control device for the traversing drive motor 15. This device includes a second potentiometer 27 in the iield circuit of this motor. The arm of potentiometer 27 is mechanically linked to arm 25, as indicated by a dotted line 30, whereby potentiometer 27 is automatically adjusted with adjustment of potentiometer 24, 25 and regulates the speed of the traversing drive motor accordingly. For example if the anemometer 18 and the discharge end of conveyor 12 reach a spot where the burden has unduly high permeability, the potentiometer arm 25 moves clockwise to restore balance in the control circuit. Potentiometer 27 is adjusted to increase the field strength of motor 15 and thus reduce the speed, whereby the discharge end of the conveyor dwells over this spot. The reverse action occurs when the discharge end of the conveyor reaches a spot of low permeability. In feed devices which employ more than one traversing drive motor (for example De Vaney Patent No. 2,834,484), the potentiometer 27 can automatically be connected in the eld circuit of the appropriate motor through suitable relays, or else each motor can be equipped with its own potentiometer.
I have observed that the combustion zone of the furnace remains more accurately at the desired location when feeding is controlled in accordance with permeability than with either the stockline profile or the gas temperature. The difficulty with a control based on prole is that the usual balls are not uniform and some tend to compact. Consequently there is no direct relation between the depth of burden and its permeability. I have found it is questionable whether temperature varies predictably with permeability.
While I have shown and described only a single embodiment of my invention, it is apparent that modifications may arise. Therefore, I do not wish to be limited to the disclosure set forth but only by the scope of the appended claims.
I claim:
1. In a shaft furnace which includes a feeder adapted to deliver material to the top of the furnace, a traversing drive for said feeder, and a speed control device for said drive, the combination therewith of an apparatus for adjusting said speed control device comprising means for measuring the velocity of combustion gases passing through the furnace burden adjacent the spot where the feeder is delivering material, separate means for measuring the gas temperature at approximately the same spot, computing means operatively connected with said velocity measuring means and said temperature measuring means for determining the gas velocity at a standard temperature and thereby providing an indication of the relative permeability of the burden to ow of gases below this spot, and means operatively connecting said computing means with said speed control device to increase the feed rate over spots of relatively high permeability and decrease the feed rate over spots of relatively low permeability.
2. A method of controlling feed to a shaft furnace to which material feeds from a traversing feeder, said method comprising measuring the velocity of combustion gases passing through the burden adjacent the spot where the feeder is delivering material, developing a first voltage proportionate to the velocity measurement, separately measuring the temperature of the combustion gases at approximately the same spot, developing a second voltage proportionate to the absolute temperature measurement, balancing said first voltage against said second voltage to obtain an indication of the gas velocity at a standard temperature and thus of the relative permeability of the burden to flow `of gases below this spot, and varying the rate of traverse in accordance with said indication to increase the feed rate over spots of relatively high permeability and decrease the rate over spots of relatively low permeability.
References Cited in the file of this patent UNITED STATES PATENTS 2,175,541 Probert Oct. l0, 1939 2,306,811 Kennedy Dec. 29, 1942 2,310,924 Becker Feb. 16, 1943 2,711,837 Henry et al Iune 28, 1955 2,739,800 Sisco Mar. 27, 1956 2,752,231 Bearer June 26, 1956
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US822298A US3050299A (en) | 1959-06-23 | 1959-06-23 | Method and apparatus for controlling feed to shaft furnace |
GB21685/60A GB939602A (en) | 1959-06-23 | 1960-06-21 | Method of operating a shaft furnace and apparatus for use in the method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US822298A US3050299A (en) | 1959-06-23 | 1959-06-23 | Method and apparatus for controlling feed to shaft furnace |
Publications (1)
Publication Number | Publication Date |
---|---|
US3050299A true US3050299A (en) | 1962-08-21 |
Family
ID=25235680
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US822298A Expired - Lifetime US3050299A (en) | 1959-06-23 | 1959-06-23 | Method and apparatus for controlling feed to shaft furnace |
Country Status (2)
Country | Link |
---|---|
US (1) | US3050299A (en) |
GB (1) | GB939602A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3211441A (en) * | 1958-07-31 | 1965-10-12 | Yawata Iron & Steel Co | Method of and apparatus for automatically controlling sintering machine |
US3265377A (en) * | 1963-06-21 | 1966-08-09 | Dravo Corp | Method of and apparatus for regulating the speed of sintering strands |
US4529374A (en) * | 1981-10-06 | 1985-07-16 | The British Petroleum Company P.L.C. | Gas particulate solid system |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2175541A (en) * | 1936-09-29 | 1939-10-10 | Woodall Duckham 1920 Ltd | Material discharge device |
US2306811A (en) * | 1941-08-04 | 1942-12-29 | Nat Tube Co | Method of charging blast furnaces |
US2310924A (en) * | 1939-11-10 | 1943-02-16 | Koppers Co Inc | Coke oven apparatus |
US2711837A (en) * | 1946-06-22 | 1955-06-28 | Henry Georges | Method for putting a glass composition in oven pots |
US2739800A (en) * | 1952-06-13 | 1956-03-27 | Erie Mining Co | Controls for pelletizing furnace |
US2752231A (en) * | 1951-07-20 | 1956-06-26 | Phillips Petroleum Co | Means for converting hydrocarbons |
-
1959
- 1959-06-23 US US822298A patent/US3050299A/en not_active Expired - Lifetime
-
1960
- 1960-06-21 GB GB21685/60A patent/GB939602A/en not_active Expired
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2175541A (en) * | 1936-09-29 | 1939-10-10 | Woodall Duckham 1920 Ltd | Material discharge device |
US2310924A (en) * | 1939-11-10 | 1943-02-16 | Koppers Co Inc | Coke oven apparatus |
US2306811A (en) * | 1941-08-04 | 1942-12-29 | Nat Tube Co | Method of charging blast furnaces |
US2711837A (en) * | 1946-06-22 | 1955-06-28 | Henry Georges | Method for putting a glass composition in oven pots |
US2752231A (en) * | 1951-07-20 | 1956-06-26 | Phillips Petroleum Co | Means for converting hydrocarbons |
US2739800A (en) * | 1952-06-13 | 1956-03-27 | Erie Mining Co | Controls for pelletizing furnace |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3211441A (en) * | 1958-07-31 | 1965-10-12 | Yawata Iron & Steel Co | Method of and apparatus for automatically controlling sintering machine |
US3265377A (en) * | 1963-06-21 | 1966-08-09 | Dravo Corp | Method of and apparatus for regulating the speed of sintering strands |
US4529374A (en) * | 1981-10-06 | 1985-07-16 | The British Petroleum Company P.L.C. | Gas particulate solid system |
Also Published As
Publication number | Publication date |
---|---|
GB939602A (en) | 1963-10-16 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US2787904A (en) | Constituent potential measuring apparatus | |
US2321605A (en) | Measuring system | |
US2276816A (en) | Measuring apparatus | |
US2448199A (en) | Control system for blast furnace air | |
US3050299A (en) | Method and apparatus for controlling feed to shaft furnace | |
US2892347A (en) | Instrument for measuring the flow of a fluid | |
US2962150A (en) | Magnetic material feed control | |
US3597679A (en) | Device for measuring magnetic field strength using a hall probe and comprising means for suppressing alterations of the hall voltage due to temperature fluctuations | |
US3528479A (en) | Control system for regulating flow of molten metal into a continuously rotated casting wheel | |
US3802677A (en) | Device for the permeability control of the layer of material to be sintered in plants for sintering ores, in particular iron ores | |
US3236358A (en) | Means for controlling conveyer | |
US3011873A (en) | Measurement and control of constituent potentials | |
US3700412A (en) | Crystal pulling apparatus having means for maintaining liquid solid crystal interface at a constant temperature | |
US3075756A (en) | Control system for automatically regulating cement kilns and auxiliary apparatus | |
US2909303A (en) | Ratio control of binder to concentrate | |
US2879142A (en) | Combustible gas detector | |
US3497803A (en) | Temperature compensated moisture meter having bridge zero varying potentiometer and ganged rheostats | |
US3376877A (en) | Moist feed mix air permeability control | |
US3746537A (en) | Process and apparatus for the control of the speed of movement of sinter strand | |
US2395385A (en) | Method and apparatus for controlling reduction furnaces | |
US2458947A (en) | Method and means for improving blast furnace operations | |
US2326853A (en) | Measuring and control apparatus | |
US2302036A (en) | Gas analysis apparatus | |
GB1351472A (en) | Electrical apparatus for measuring compensated temperature variations | |
GB1294201A (en) | Improvements in and relating to the casting of deoxidized copper |