US2212125A - Control system for pulverizer mills - Google Patents

Control system for pulverizer mills Download PDF

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US2212125A
US2212125A US112935A US11293536A US2212125A US 2212125 A US2212125 A US 2212125A US 112935 A US112935 A US 112935A US 11293536 A US11293536 A US 11293536A US 2212125 A US2212125 A US 2212125A
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regulator
pulverizer
bellows
mill
rate
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US112935A
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Thomas A Peebles
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JOHN M HOPWOOD
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JOHN M HOPWOOD
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B02CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
    • B02CCRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
    • B02C23/00Auxiliary methods or auxiliary devices or accessories specially adapted for crushing or disintegrating not provided for in preceding groups or not specially adapted to apparatus covered by a single preceding group
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B02CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
    • B02CCRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
    • B02C21/00Disintegrating plant with or without drying of the material
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B02CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
    • B02CCRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
    • B02C25/00Control arrangements specially adapted for crushing or disintegrating
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10TTECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T137/00Fluid handling
    • Y10T137/2496Self-proportioning or correlating systems
    • Y10T137/2514Self-proportioning flow systems
    • Y10T137/2521Flow comparison or differential response
    • Y10T137/2529With electrical controller

Definitions

  • This'invention relates to pulverizer mills, such as are used, for example, to pulverize coal for boiler furnaces and more particularly to a control system for regulating the rate of feed of raw coal to the pulverizer mill primarily in accordance with the demand for pulverized fuel and secondarily, controlling the feed in accordance withthe load on the prime mover that drives the mill.
  • An object of this invention is. to provide a control system for pulverizermills that shall be capable of changing the rate of feed. of material to the mills to bepulverized, either automatically or by hand, in accordance with the demand for pulverized material, and of so modifying the rate of feed of unpulverized material that a balance is maintained between the rate of feed to and the amount of pulverized material delivered by the mill for any given rate of demand therefor.
  • Another object of. the invention is to provide a control system that shall be automatic in operation, for example in connection with a steam boiler plant, and adaptable to pulverizer mills that are driven either by steam engines or turbines or electric motors.
  • Figure 1 is a more or less diagrammatic view of a pulverizer mill provided with a control system arranged and constructed in accordance with an embodiment of the invention
  • Fig. 2 is a'view similar to Fig. 1 showing a modified form of control system
  • Fig. 3 is a view of a control system of the type shown in Figs. 1 and 2 but modified for application to pulverized millsdriven by electric motors,
  • Fig. 4 is a sectional view of a regulator embodied in the control system of Fig. 3. and adapted for use where the pulverized mill is driven by an electric motor.
  • the invention herein disclosed is adapted for use with pulverizer mills, that is mills that grind coarse material to such a degree of fineness that the pulverized material may be carried away to the point of use by a carrier such as air, for example.
  • a carrier such as air
  • the system is shown and described in connection with a mill employed to pulverize coal to be conveyed by air to the burners of a furnace, for example a boiler furnace.
  • the rate of feed of coal to the mill is influenced also by the condition of the coal; for example, the state of dryness affects the rate of feed, in that wet coal does not feed as fast as dry coal.
  • a control system embodying one form of the invention is illustrated as applied to a pulverizer mill l driven by ,a. prime mover 2 indicated diagrammatically as a steam turbine.
  • Coal is fed to the pulverizer from a hopper 3 by means of a feeder 4 driven by an adjustable-speed electric motor 5.
  • the speed of the electric motor is controlled by a rheostat 6 connected in circuit with the field winding of the motor, and by adjusting this rheostat, the rate of feed to the pulverizer may be varied to meet varying demands for pulverized fuel.
  • Thisadjustment of the rheostat may be accomplished by hand or automatically by means of a regulator 6', disposed to operate in response to an operative that reflects the demands for combustion.
  • a regulator 6' disposed to operate in response to an operative that reflects the demands for combustion.
  • variations in pressure of the steam indicate either that more or less coal must be burned to maintain the steam pressure at the desired value. vlj or that the load is increasing and that the combustion rate is insuflicient to supply the demand for steam, or if the pressure .is increasing, that indicates that the load and therefore the demand for steam is falling ofi and that the rate of combustion should be reduced.
  • the rate of delivery 'of pulverized fuel to the burners must be increased which means that the pulverizer must grind more coal per unit of time and in order to do that the rate of feed must be increased.- In the other case, the rate of delivery of fuel to the burners must be decreased, requiring therefore, a decreased rate of feed of coal to the pulverizer.
  • the coal as it is pulverized is carriedaway by a stream of air passing through the pulverizer,
  • the air supply is also regulated in accordance with the rate at which the coal is pulverized, all as is well known in this art.
  • the air supply to the pulverizer may be controlled by -a regulator I and this regulator may be adjusted by hand or it may be operated automatically in response to changes in the demands for combustion.
  • the load imposed on the turbine which drives the pulverizer indicates the amount of coal that is being pulverized.
  • the pressure of the steam as delivered to the nozzles will vary with the degree of opening of the governor controlled throttle valve 8.
  • aregulator 9 which responds to a control impulse delivered thereto by a master regulator M. R. in response to variations in the demand for steam on the boiler and to the pressure of the steam at the nozzles of the turbine.
  • Regulator 9 comprises a regulating element, for example, an escapement valve II) that is actuated jointly by a pressure responsive element ii and a pressure responsive element l2 both acting on a lever or beam l3.
  • Beam l3 carries a stem l4 positioned to move the escapement valve I either toward an inlet port l5 and away from an exhaust port it or vice versa, depending upon the relative magnitudes of the impulses or forces acting on elements II and I2.
  • bellows 24 When the steam pressure rises, bellows 24 is compressed and moves the push rod upwardly against the tension of spring 29 thereby causing the escapement valve to move away from its inlet port and to allow an increased pressure to be transmitted to the housing in which the bellows Ii is disposed. 'If the steam pressure is failing, the bellows expands whereby the valve is moved towards its inlet port and away from the exhaust port thereby decreasing the pressure imposed on bellows II. In other words, with increasing load on the boiler, the pressure acting on bellows Ii decreases, and with decreasing load on the boiler the pressure on this bellows increases.
  • a dash-pot 34 acts on beam l3 in such manner as to avoid excessive and sudden movements .Justments and bring matters under their control to somewhere near the proper point before requiring further adjustment if any is necessary.
  • Lever i3 is connected by a yoke 3
  • the dash-pot comprises a cylindrical member 35 having a reservoir 36 at its upper end and a variable volume chamber 31 communicating with the lower end of the cylinder. Chamber 3'! is defined by a bellows 38 which is urged towards its maximum volume position by means of a spring 38'.
  • This bellows is disposed within a chamber or housing 39 to which pressure impulses are delivered by the escapement valve ID. If the pressures delivered to housing 39 are increasing, bellows 38 is compressed whereby fluid is displaced causing piston 33 to move upwardly thereby compressing spring 32 and yieldingly opposing downward movement of lever l3.
  • a needle valve ll associated with a bypass 42 which is connected at its lower end to cylinder 35 at a point below piston 33 and at its upper end to the reservoir at a point above the piston, allows fluid to escape from the space below the piston to the space above the piston. The adjustment of this needle valve thereby determines the length of time the dash-pot is effective in checking movement of lever i3.
  • the eii'ect of the dash-pot is nullified. If the pressure delivered to housing 39 is decreasing, the bellows tends to expand and increase the volume of chamber 3'! so that the tendency is to pull the dashpot piston downwardly. The expansion of the bellows allows fluid to flow from the reservoir above the piston through the needle valve into the space below the piston and the efl'ect oi the dash-pot on the regulator is therefore gradually and finally nullified.
  • eflectiveness of the dash-pot is made proportional to the pressuredelivered to it.
  • valve Ill This would disturb the equilibrium between bellows I2 and II and cause valve Ill to transmit increased impulses to regulators 6' and 1, thereby reducing the rate of feed of coal to the pulverizer and the rate of air delivery thereto to a value corresponding to that determined by the demand for coal on the pulver-.
  • the rateof fuel feed to the pulverizer is caused to bear such a relation to the demand for pulverized fuel that the feed of fuelto the pulverizer is caused to bear a fixed or substantially fixed relation to the amount of pulverized fuel delivered by the pulverizer to the furnace.
  • Any change in the duty imposed on the pulverizer is primarily controlled by the master regulator acting through regulator 5' and secondarily by the unbalance between the loading pressure sent from master regulator M. R. to regulator 9 and the steam pressure at the nozzles of the steam turbine acting on bellows I2.
  • regulator 9 indicated only schematically, and regulators 6' and l which control the feed of fuel to the pulverizer and the air pulled through the pulverizer are directly responsive to impulses sent out from the master regulator M. R. Feed control regulator 6' is also controlled by regulator 9.
  • steam turbine 2 drives the pulverizer and a suction fan 46 pulls air through the pulverizer, the air carrying with it pulverized coal through duct 41 into the fan from which it is discharged through a pipe 48 to the furnace (not shown)
  • Regulator 6' operating rheostat 6 is controlled by a dual pressure responsive mechanism 49.
  • This impulse from the master regulator also acts immediately on bellows 50 associated with regulator 6' causing that regulator to immediately respond and shift the rheostat to a point corresponding to the speed required of the coal feed motor 5.
  • the loading pressure sent out by the master regulator also acts on bellows II of regulator 9 to effect an unbalance between the turbine steam pressure responsive bellows I2 and bellows II, whereby a change is produced in the magnitude of the impulses sent out from this regulator to bellows 52 of the feed controlling regulator.
  • This change in pressure acts to operate regulator 6' and cause it to further increase or decrease, as the case may be, the speed setting of the rheostat 6.
  • Fig. 3 of the drawings I have illustrated regulator 9 in a form modified to be operable in the case where the pulverizer mill is driven by an electric motor as indicated at 53.
  • a plurality of coil windings 55 and 56 have been substituted for bellows I2 of regulator 9.
  • One of these coils is stationarily mounted and the other movably mounted.
  • One coil is arranged to be energized in accordance with the voltage of the power supply for the mill motor 53.
  • the other coil is traversed by the current delivered to the motor or by a current whose value is proportional to the current delivered to the motor.
  • These coils are so disposed with respect to each other that they move towards each other with increasing load on the motor and away from each other when the load on the motor decreases.
  • Regulators 6 and l, of Figs. 1 and 2 may be of any suitable type. As illustrated, these are of the pneumatic cylinder type, that is a type having a cylinder in which a reciprocating piston is disposed and provided with a piston rod 59 carrying aframe 60 connected to the element to be regulated. Movement of the piston in either direction is controlled by a pilot valve 6
  • a regulator of this type is shown and described in United States Letters Patent No. 2,044,936 to Robert R. Donaldson and dated June 23, 1936. These regulators as described in the patent, are compensated in their action, i. e. the piston comes to rest when it has moved a predetermined distance in either direction depending on the extent to which the pilot valve is opened, and if, when in such position of rest,
  • these regulators are capable of operating step-by-step in either direction, slowly in small increments or faster in larger increments-or they are capable of making a full stroke in either direction in one motion provided the pilot valve is held open by its actuating device because a condition undergoing regulation requires it. Since the operation and construction of these regulators are fully disclosed in the patent just referred to further detailed description thereof herein is believed unnecessary in that no claim is made to these regulators per se.
  • the regulator which adjusts the rheostat of Fig; 2 is similar to the regulators 6 and! and differs therefrom only in the mechanism which operates the pilot valve 6
  • This pilot valve is operated by bellows 50 and 52 each of which is provided with a push rod 63 to which a floating beam 64 is pivotally connected at its opposite ends. At some point between the connection of this floating beam to the push rods, a
  • link 65 is connected and this link is in turn connected to a lever 66 that operates the pilot valve 6
  • the direction of movement in this case would be such as to decrease the speed of the motor as a reduction in. the rate of supply of fuel is required.
  • Fig. 2 the operation is somewhat the same, except that the loading pressure sent out by master regulator acts directly on regulators 6' and 1 as well as on bellows ll of regulator 9.
  • Regulator 9 acts only on regulator 5 but the regulating position of regulator l is finally determined by a state of balance being maintained between the loading pressure and the steam pressure of the turbine nozzles acting respectively on bellows H and I2. And since this loading pressure also acts on regulator 1, the required amount of air is supplied to the pulverizer and a balance is maintained between the amount of coal delivered to the pulverizer and the amount of pulverized coal delivered to the furnaces for a given demand therefor.
  • the regulator of Fig. 3 operates on the same principle as the regulator 9 of Figs. 1 and 2 operates, but differs therefrom in that the power delivered to the motor is measured by coils 55 and 56 and utilized to balance spring l8 for the various loading pressures on bellows ll, any unbalancebetween them resulting in a change in feed of coal to the pulverizer and in the rate of air supply thereto until a balance is restored between them.
  • a control system for regulating the output of a pulverizer mill disposed to deliver pulverized fuel to a furnace, and provided with a prime mover for driving the mill and a feeder for delivering unpulverized fuel to the mill, said control system comprising a regulator responsive to a condition reflecting the demand for pulverized fuel for causing the feeder to deliver unpulverized fuel to the mill at -a rate approximating the demand for pulverized fuel, and means responsive to the load imposed on the prime mover for so modifying the action of said regulator that the feeder is caused to deliver unpulverized fuel to the mill at substantially the same rate that pul- 'verlzed fuel is delivered by said mill to the furnace.
  • a regulator for controlling the operation of a mill for pulverizing coal said mill being driven by a prime mover'and provided with a feeder for delivering coal to the mill and a regulator for controlling said feeder, said regulator having a control element for governing the operation of the feeder regulator, an actuating element for sponsive tothe load on the prime mover disposed to be normally in balance with said actuating element, said load responsive and actuating ele-- ments mutually cooperating with said control element to so adjust the rate of feed that a balance is maintained between them.
  • a system for controlling the operation of a pulverizer mill driven by a prime mover and provided with a feeder and regulator for adjusting the rate of delivery of material by the feeder to the mill said system including a' regulator having a control mechanism for controlling the feeder regulator, a spring yieldingly urging said mechanism inonedirection, means for variably loading said spring in accordance with the demand for p l erizedmaterial to cause said control mechanism to function and change the rate of feed of material to the mill, and means responsive to the load on said prime mover and acting in opposition to the pull of said spring on said control mechanism to effect such a modification of the rate of feed that a balance is established between the load responsive means and the loading imposed on the spring by said loading means.
  • a control system for pulverizer mills driven by a prime mover and provided with a motor driven feeder and a source of supply of air for carryin pulverized material out of the mill to a boiler furnace comprising a master regulator responsive to the demand for steam and means under the control of said master regulator for regulating the air supply. and a second regulator having means responsive to the operation of the master regulator for adjusting the speed of the feeder motor to establish a rate of feed required by the demand for pulverized material, and means responsive to the load on' the prime mover and cooperating with said regulator responsive means to so modify the speed of the feeder motor that a balance is maintained between the output of the mill and the rate of feed of unpulverized material to the mill.
  • the master regulator embodies means for establishing control impulses whose magnitudes are dependent upon the demand for pulverized material and that said second regulator includes a control element for adjusting the speed of the feeder motor, an actuating element including a spring for actuating said control element, means responsive to the master regulator impulse for adjusting said spring to cause the control'element to regulate thefeeder motor in accordance with the demand for pulverized material as indicated by the magnitude of the master regulator impulse, and means responsive to the load on the prime mover and acting in opposition to said spring arranged to so modify the action of said control element that a balance is maintained between the output of the mill and the rate of feed thereto for any rate of demand as indicated by said master'regulator.
  • said second regulator comprises a regulating element for controlling said feeder motor, a spring operatively connected to said regulating element and tending to move the same in one direction, means under the control of the master regulator for applying a variable loading force to said spring, and means actuated in accordance with the load on the prime mover for balancing the loading force on said spring, whereby when an unbalance occurs the regulating element is actuated to modify the speed of the feeder motor until the spring loading is again balanced.
  • a control system for pulverizer mills adapted to supply powdered fuel to boiler furnaces, and provided with an adjustable speed motor for driving the mill, means for feeding unpulverized fuel to the mill at controllable rates, and an adjustable supply of air for carrying powdered fuel out of the mill to the furnace, said system comprising a master regulator responsive to steam demand for developing a first control force that is a measure of steam demand, a second regulator responsive to said first control force and to a condition that varies with the load on the mo tor for establishing a second control force whose magnitude varies with the value of said first mentioned control force and the extent of response of said second regulator to the load on the motor, and means responsive to said second cont-rol force for so controlling the unpulverized fuel feeding means that said regulator is maintained substantially in a state of balance between said first control force and the effect of the motor load thereon.

Description

Aug. 2091940. 1'. A. PEEBLES 7 CONTROL SYSTEM FOR PULVERIZER MILLS Filed Nov. 27, 1936 2 sheets-Sheet 1 2 8 I: a /17 i 2e 5 INVENTOR Y E1 7 20, 1940- T. A. PEEBLES 2,212,125
I CONTROL SYSTEM FOR PULVERIZER MILLS Filed Nov. 27, 1956 2 Sheets-Sheet 2 Bai/er 5 HIE, Sfeam Header- Patented Aug. 20, 1940 PATENT OFFICE 2,212,125 con'mor. SYSTEM son PULVERIZER -MILLS Thomas A. Peebles, Pittsburgh, Pa.,
John' M. Hopwood, Mt. Lebanon,
assignor to Application November 27, 1936, Serial No. 112,935
9v Claims.
This'invention relates to pulverizer mills, such as are used, for example, to pulverize coal for boiler furnaces and more particularly to a control system for regulating the rate of feed of raw coal to the pulverizer mill primarily in accordance with the demand for pulverized fuel and secondarily, controlling the feed in accordance withthe load on the prime mover that drives the mill.
An object of this invention is. to provide a control system for pulverizermills that shall be capable of changing the rate of feed. of material to the mills to bepulverized, either automatically or by hand, in accordance with the demand for pulverized material, and of so modifying the rate of feed of unpulverized material that a balance is maintained between the rate of feed to and the amount of pulverized material delivered by the mill for any given rate of demand therefor.
Another object of. the invention is to provide a control system that shall be automatic in operation, for example in connection with a steam boiler plant, and adaptable to pulverizer mills that are driven either by steam engines or turbines or electric motors.
The above stated objects and other objects of the invention will. be apparent to those skilled in this art, from the following description taken in conjunction with the accompanying drawings, in which: Figure 1 is a more or less diagrammatic view of a pulverizer mill provided with a control system arranged and constructed in accordance with an embodiment of the invention;
Fig. 2 is a'view similar to Fig. 1 showing a modified form of control system;
Fig. 3 is a view of a control system of the type shown in Figs. 1 and 2 but modified for application to pulverized millsdriven by electric motors,
m the mills of Figs. 1 and 2 being driven by steam turbines; I
Fig. 4 is a sectional view of a regulator embodied in the control system of Fig. 3. and adapted for use where the pulverized mill is driven by an electric motor.
Throughout the drawings and the specifica-v tion, like reference characters indicate like parts. I
The invention herein disclosed is adapted for use with pulverizer mills, that is mills that grind coarse material to such a degree of fineness that the pulverized material may be carried away to the point of use by a carrier such as air, for example. Speciflcally, the system is shown and described in connection with a mill employed to pulverize coal to be conveyed by air to the burners of a furnace, for example a boiler furnace.
In the operation of a pulverizer mill, for furnace operation, the coal at a rate corresponding to the rate at which it is burned, and that the coal be fed to the pulverizer mill at a rate corresponding to the rate atwhich it is ground in the mill and carried therefrom by an air blast to the burners. If coal is fed too fast to the mill, the mill grinds more coal than is necessary for a given demand,
or if the coal is fed too slowly, not enough coal is ground to supply the demand. The rate of feed of coal to the mill is influenced also by the condition of the coal; for example, the state of dryness affects the rate of feed, in that wet coal does not feed as fast as dry coal.
In Fig. l of the drawings, a control system embodying one form of the invention is illustrated as applied to a pulverizer mill l driven by ,a. prime mover 2 indicated diagrammatically as a steam turbine. Coal is fed to the pulverizer from a hopper 3 by means of a feeder 4 driven by an adjustable-speed electric motor 5. The speed of the electric motor is controlled by a rheostat 6 connected in circuit with the field winding of the motor, and by adjusting this rheostat, the rate of feed to the pulverizer may be varied to meet varying demands for pulverized fuel. Thisadjustment of the rheostat may be accomplished by hand or automatically by means of a regulator 6', disposed to operate in response to an operative that reflects the demands for combustion. In the case of a steamboiler, variations in pressure of the steam indicate either that more or less coal must be burned to maintain the steam pressure at the desired value. vlj or that the load is increasing and that the combustion rate is insuflicient to supply the demand for steam, or if the pressure .is increasing, that indicates that the load and therefore the demand for steam is falling ofi and that the rate of combustion should be reduced. In, the one case, the rate of delivery 'of pulverized fuel to the burners must be increased which means that the pulverizer must grind more coal per unit of time and in order to do that the rate of feed must be increased.- In the other case, the rate of delivery of fuel to the burners must be decreased, requiring therefore, a decreased rate of feed of coal to the pulverizer.
The coal as it is pulverized is carriedaway by a stream of air passing through the pulverizer,
it is desirable that the mill grind 5 to the burners of the furnace. The air supply is also regulated in accordance with the rate at which the coal is pulverized, all as is well known in this art.
The air supply to the pulverizer may be controlled by -a regulator I and this regulator may be adjusted by hand or it may be operated automatically in response to changes in the demands for combustion.
If the condition of the coal to be pulverized always remained fixed and constant, the feed of coal to the pulverizer as controlled by rheost'at 6 would be sufficient to meet the. demands. But in practical operation the condition of the coal varies so that, insome cases, for a.given demand for powdered coal, the coal would be delivered to the pulverizer at a rate higher than required. At other times, not sufiicient coal would be delivered to meet the demand.
The load imposed on the turbine which drives the pulverizer indicates the amount of coal that is being pulverized. Thus for example, if the turbine operates at variable loads, it will be apparent that the pressure of the steam as delivered to the nozzles will vary with the degree of opening of the governor controlled throttle valve 8.
In order to obtain a proper balance between the demand for pulverized fueland the rate of feed of fuel to the pulverizer, aregulator 9 is provided which responds to a control impulse delivered thereto by a master regulator M. R. in response to variations in the demand for steam on the boiler and to the pressure of the steam at the nozzles of the turbine. I
Regulator 9 comprises a regulating element, for example, an escapement valve II) that is actuated jointly by a pressure responsive element ii and a pressure responsive element l2 both acting on a lever or beam l3. Beam l3 carries a stem l4 positioned to move the escapement valve I either toward an inlet port l5 and away from an exhaust port it or vice versa, depending upon the relative magnitudes of the impulses or forces acting on elements II and I2.
Beam I3 is fulcrumed at one end on a knife edge I! and connected at the other end by means of a tension spring i8 to element ll illustrated as comprising a bellows. If bellows ll moves upwardly in response to a. decreasing impulse delivered to a housing I 9 within which it is disposed, spring l8 tends to elongate and move beam l3 upwardly, shifting the valve I 0 towards its inlet port and away from its exhaust port. When moving in this direction the pressure within valve body 20 and which is transmitted to a sending line 2|, to regulators 6' and 1, is also reduced. The minimum pressure occurs in line 2| when inlet port i5 is closed and the exhaust port I6 is open. If thebeam is moved downwardly either as the result of increasing pressure in housing I9 01'' of an increasing pressure acting on element l2 disposed within a housing 22, the valve moves towards exhaust port 16 and away from inlet port' I5 whereby the pressure within the valve body.
header 23. The steam pressure acts on a pressure.
responsive .element, such as a bellows 24 disposed within a pressure tight chamber 25 and this bellows is connected by a stem or push rod 26 to a lever 21 fulcruined between knife edges 28 atone of this lever actuates an escapement valve 30 like the valve Hi just described in connection with regulator 9.
When the steam pressure rises, bellows 24 is compressed and moves the push rod upwardly against the tension of spring 29 thereby causing the escapement valve to move away from its inlet port and to allow an increased pressure to be transmitted to the housing in which the bellows Ii is disposed. 'If the steam pressure is failing, the bellows expands whereby the valve is moved towards its inlet port and away from the exhaust port thereby decreasing the pressure imposed on bellows II. In other words, with increasing load on the boiler, the pressure acting on bellows Ii decreases, and with decreasing load on the boiler the pressure on this bellows increases.
In order to stabilize regulator 9, a dash-pot 34 is provided that acts on beam l3 in such manner as to avoid excessive and sudden movements .Justments and bring matters under their control to somewhere near the proper point before requiring further adjustment if any is necessary. Lever i3 is connected by a yoke 3| to bellows l2 and the yoke is connected by means of a spring 32 to the movable element or piston 33 of the dashpot 34. The dash-pot comprises a cylindrical member 35 having a reservoir 36 at its upper end and a variable volume chamber 31 communicating with the lower end of the cylinder. Chamber 3'! is defined by a bellows 38 which is urged towards its maximum volume position by means of a spring 38'. This bellows is disposed within a chamber or housing 39 to which pressure impulses are delivered by the escapement valve ID. If the pressures delivered to housing 39 are increasing, bellows 38 is compressed whereby fluid is displaced causing piston 33 to move upwardly thereby compressing spring 32 and yieldingly opposing downward movement of lever l3. A needle valve ll associated with a bypass 42 which is connected at its lower end to cylinder 35 at a point below piston 33 and at its upper end to the reservoir at a point above the piston, allows fluid to escape from the space below the piston to the space above the piston. The adjustment of this needle valve thereby determines the length of time the dash-pot is effective in checking movement of lever i3. As soon as the liquid has been transferred to the reservoir above the piston, the eii'ect of the dash-pot is nullified. If the pressure delivered to housing 39 is decreasing, the bellows tends to expand and increase the volume of chamber 3'! so that the tendency is to pull the dashpot piston downwardly. The expansion of the bellows allows fluid to flow from the reservoir above the piston through the needle valve into the space below the piston and the efl'ect oi the dash-pot on the regulator is therefore gradually and finally nullified.
In any case, whether the pressures delivered to housing 39 are increasing or decreasing, the
. eflectiveness of the dash-pot is made proportional to the pressuredelivered to it.
Assuming that the boiler is operating at a point where sufiicient fuel is supplied to maintain the steam pressure in the steam header at the desired value, and that an increased demand for steam takes place, then the steam pressure will be reduced whereby regulator MfR. reduces the mitted to bellows I2.
pressure imposed on bellows II. This causes the bellows to expand and increase the tension in spring I8 whereby the left hand end of beam I3 is moved upwardly, causing valve III to move towards its inlet port and reduce the pressure delivered to the dash-pot chamber 39 and to the sending line 2I. This reduced pressure in the sending'line is communicated to regulators 8' and I. In response to this reduced pressure impulse, regulator 6' adjusts rheostat 6 in a direction to increase the speed of motor 5 and the rate of feed of coal to the pulverizer mill, and regulator 1 moves in a. direction to open a damper 43 to increase the amount of air delivered to the pulverizer mill.
The increased rate of feed of coal to the pulverizer mill imposes greater load on turbine 2. This tends to decrease the speed of the turbine causing the governor operated valve 8 in the steam line to the'turbine to open wider. Asthis governor operated valve opens the steam pressure at the steam nozzles (not shown) of theturbine increases and this increased pressure is communicated to housing 22 within which bellows I2 is disposed causing this bellows to be compressed and to pulldownwardly on lever I3 thereby tending to-move valve III away from its inlet port. This increases the pressure impulses delivered to the rheostat operating regulator 6' and the air control regulator I. 7
When the forces imposed by bellows II an I2 on lever I3 are in equilibrium, the lever comes to rest but this results in such a i e-adjustment of the positions of the movable elements of. regulators 6' and I that the' rate of feed of fuel to the pulverizer is caused to correspond to the rate at which it is delivered from the pulverizer to the furnace. If for some reason the rate of feed to the pulverizer should increase without any change in demand for steam or without any change in loading pressure on bellows I I, the load imposed on turbine 2 would increase whereby an increased steam pressure would be. trans- This would disturb the equilibrium between bellows I2 and II and cause valve Ill to transmit increased impulses to regulators 6' and 1, thereby reducing the rate of feed of coal to the pulverizer and the rate of air delivery thereto to a value corresponding to that determined by the demand for coal on the pulver-.
izerl When this condition is attained the bellows II and I2 are in equilibrium. On the other hand,
should the rate of feed decrease the load on the turbine would decrease thereby causing the steam pressure acting on bellows I2 to decrease, and unbalance the forces exerted by bellows II and I2 on beam I3. Such an unbalance results in regulator 9 sending out impulses to regulators 6' and I that would cause the one to increase the rate of fuel feed and the other to open damper 43 and increase the rate of air supply to the pulverizer. As soon as balance has been restored between bellows II and I2 the rate of feed of coal to the pulverizer mill will remain fixed until the master regulator changes the loading pressure on bellows II, in response to a change in steam demand. d
From the above it is seen that the rateof fuel feed to the pulverizer is caused to bear such a relation to the demand for pulverized fuel that the feed of fuelto the pulverizer is caused to bear a fixed or substantially fixed relation to the amount of pulverized fuel delivered by the pulverizer to the furnace. Any change in the duty imposed on the pulverizer is primarily controlled by the master regulator acting through regulator 5' and secondarily by the unbalance between the loading pressure sent from master regulator M. R. to regulator 9 and the steam pressure at the nozzles of the steam turbine acting on bellows I2.
In Fig. 2 of the drawings, regulator 9, indicated only schematically, and regulators 6' and l which control the feed of fuel to the pulverizer and the air pulled through the pulverizer are directly responsive to impulses sent out from the master regulator M. R. Feed control regulator 6' is also controlled by regulator 9. In the system shown in Fig. 2 steam turbine 2 drives the pulverizer and a suction fan 46 pulls air through the pulverizer, the air carrying with it pulverized coal through duct 41 into the fan from which it is discharged through a pipe 48 to the furnace (not shown) Regulator 6' operating rheostat 6 is controlled by a dual pressure responsive mechanism 49. This mechanism includes a bellows 50 or other pressure responsive element disposed in a housing 5| to which a pressure is transmitted by the master regulator. It also includes another bellows 52 disposed within a housing 53 to which pressure impulses are transmitted from valve III of regulator 9. Whenever a change in the pressure impulse sent out from the master regulator occurs, the air control regulator I responds irrnnediately to effect an adjustment in the rate of flow of air through the pulverizer. This impulse from the master regulator also acts immediately on bellows 50 associated with regulator 6' causing that regulator to immediately respond and shift the rheostat to a point corresponding to the speed required of the coal feed motor 5.- The loading pressure sent out by the master regulator also acts on bellows II of regulator 9 to effect an unbalance between the turbine steam pressure responsive bellows I2 and bellows II, whereby a change is produced in the magnitude of the impulses sent out from this regulator to bellows 52 of the feed controlling regulator. This change in pressure acts to operate regulator 6' and cause it to further increase or decrease, as the case may be, the speed setting of the rheostat 6. These adjustments continue until bellows II and I2 of regulator 9 are in balance at which time the rates of feed of fuel and of air flow to the pulverizer will be such that the proper amount of pulverized fuel is delivered to the furnace and that the amount of raw coal fed to the pulverizer will correspond to the amount of pulverized fuel delivered by the pulverizer to the furnace. n
In Fig. 3 of the drawings, I have illustrated regulator 9 in a form modified to be operable in the case where the pulverizer mill is driven by an electric motor as indicated at 53. For this purpose a plurality of coil windings 55 and 56 have been substituted for bellows I2 of regulator 9. One of these coils is stationarily mounted and the other movably mounted. One coil is arranged to be energized in accordance with the voltage of the power supply for the mill motor 53. The other coil is traversed by the current delivered to the motor or by a current whose value is proportional to the current delivered to the motor. These coils are so disposed with respect to each other that they move towards each other with increasing load on the motor and away from each other when the load on the motor decreases. One coil, for example coil 55, is carried by a yoke 51 connected to lever I3 of the regulator 9'. This yoke is also connected by spring 32 to piston 33 of dash-pot 34 described in connection with regulator 9 of Fig. 1. In other respects the regulator in Fig. 3 operates in subcontrol system would be as shown and described in connection with Figs. 1 and 2.
Regulators 6 and l, of Figs. 1 and 2, may be of any suitable type. As illustrated, these are of the pneumatic cylinder type, that is a type having a cylinder in which a reciprocating piston is disposed and provided with a piston rod 59 carrying aframe 60 connected to the element to be regulated. Movement of the piston in either direction is controlled by a pilot valve 6| actuated by a diaphragm to which the impulses from a sending line 2i of Fig. 1 are transmitted or from the sending line 2| of the master regulator of Fig. 2. A regulator of this type is shown and described in United States Letters Patent No. 2,044,936 to Robert R. Donaldson and dated June 23, 1936. These regulators as described in the patent, are compensated in their action, i. e. the piston comes to rest when it has moved a predetermined distance in either direction depending on the extent to which the pilot valve is opened, and if, when in such position of rest,
more regulation is required, the piston moves to another position and so on until the proper position is attained. Thus these regulators are capable of operating step-by-step in either direction, slowly in small increments or faster in larger increments-or they are capable of making a full stroke in either direction in one motion provided the pilot valve is held open by its actuating device because a condition undergoing regulation requires it. Since the operation and construction of these regulators are fully disclosed in the patent just referred to further detailed description thereof herein is believed unnecessary in that no claim is made to these regulators per se.
The regulator which adjusts the rheostat of Fig; 2 is similar to the regulators 6 and! and differs therefrom only in the mechanism which operates the pilot valve 6| thereof. This pilot valve is operated by bellows 50 and 52 each of which is provided with a push rod 63 to which a floating beam 64 is pivotally connected at its opposite ends. At some point between the connection of this floating beam to the push rods, a
link 65 is connected and this link is in turn connected to a lever 66 that operates the pilot valve 6|. -If either one or both of these bellows are subjected to an increasing pressure, the push rods thereof move upwardly causing the regulator to move in one direction to adjust thejrheostat.
The direction of movement in this case would be such as to decrease the speed of the motor as a reduction in. the rate of supply of fuel is required.
forces exerted by bellows l l and spring l8 and bellows l2 on lever I3 are in equilibrium. If now the loading pressure imposed by master regulator M. R. on bellows I I of regulator 9, is changed, regulator 9 is unbalanced causing regulators 6' and 1 to make a change in the rate of feed of coal to the pulverizer and in the rate of air supply thereto. The pressure imposed by the pressure of the steam at the nozzles of the turbine on bellows l2 then changes in a direction to place spring l8 and bellows II and I2 in equilibrium. Likewise, a. change in load on the turbine results in a change in pressure on bellows I2 which unbalances the regulator to effect a change in feed of coal and the air supply whereby the steam pressure on bellows I2 is changed until it is in balance with the loading pressure on bellows II.
In Fig. 2, the operation is somewhat the same, except that the loading pressure sent out by master regulator acts directly on regulators 6' and 1 as well as on bellows ll of regulator 9. Regulator 9 acts only on regulator 5 but the regulating position of regulator l is finally determined by a state of balance being maintained between the loading pressure and the steam pressure of the turbine nozzles acting respectively on bellows H and I2. And since this loading pressure also acts on regulator 1, the required amount of air is supplied to the pulverizer and a balance is maintained between the amount of coal delivered to the pulverizer and the amount of pulverized coal delivered to the furnaces for a given demand therefor.
The regulator of Fig. 3 operates on the same principle as the regulator 9 of Figs. 1 and 2 operates, but differs therefrom in that the power delivered to the motor is measured by coils 55 and 56 and utilized to balance spring l8 for the various loading pressures on bellows ll, any unbalancebetween them resulting in a change in feed of coal to the pulverizer and in the rate of air supply thereto until a balance is restored between them.
Having thus described the invention, what I desire to claim and secure by Letters Patent is:
1. A control system for regulating the output of a pulverizer mill disposed to deliver pulverized fuel to a furnace, and provided with a prime mover for driving the mill and a feeder for delivering unpulverized fuel to the mill, said control system comprising a regulator responsive to a condition reflecting the demand for pulverized fuel for causing the feeder to deliver unpulverized fuel to the mill at -a rate approximating the demand for pulverized fuel, and means responsive to the load imposed on the prime mover for so modifying the action of said regulator that the feeder is caused to deliver unpulverized fuel to the mill at substantially the same rate that pul- 'verlzed fuel is delivered by said mill to the furnace.
2. A regulator for controlling the operation of a mill for pulverizing coal, said mill being driven by a prime mover'and provided with a feeder for delivering coal to the mill and a regulator for controlling said feeder, said regulator having a control element for governing the operation of the feeder regulator, an actuating element for sponsive tothe load on the prime mover disposed to be normally in balance with said actuating element, said load responsive and actuating ele-- ments mutually cooperating with said control element to so adjust the rate of feed that a balance is maintained between them.
. 3. A system for controlling the operation of a pulverizer mill driven by a prime mover and provided with a feeder and regulator for adjusting the rate of delivery of material by the feeder to the mill, said system including a' regulator having a control mechanism for controlling the feeder regulator, a spring yieldingly urging said mechanism inonedirection, means for variably loading said spring in accordance with the demand for p l erizedmaterial to cause said control mechanism to function and change the rate of feed of material to the mill, and means responsive to the load on said prime mover and acting in opposition to the pull of said spring on said control mechanism to effect such a modification of the rate of feed that a balance is established between the load responsive means and the loading imposed on the spring by said loading means.
4. A control system for pulverizer mills driven by a prime mover and provided with a motor driven feeder and a source of supply of air for carryin pulverized material out of the mill to a boiler furnace, said system comprising a master regulator responsive to the demand for steam and means under the control of said master regulator for regulating the air supply. and a second regulator having means responsive to the operation of the master regulator for adjusting the speed of the feeder motor to establish a rate of feed required by the demand for pulverized material, and means responsive to the load on' the prime mover and cooperating with said regulator responsive means to so modify the speed of the feeder motor that a balance is maintained between the output of the mill and the rate of feed of unpulverized material to the mill.
5. Asystm according to claim '7 characterized by the fact that the master regulator embodies means for establishing control impulses whose magnitudes are dependent upon the demand for pulverized material and that said second regulator includes a control element for adjusting the speed of the feeder motor, an actuating element including a spring for actuating said control element, means responsive to the master regulator impulse for adjusting said spring to cause the control'element to regulate thefeeder motor in accordance with the demand for pulverized material as indicated by the magnitude of the master regulator impulse, and means responsive to the load on the prime mover and acting in opposition to said spring arranged to so modify the action of said control element that a balance is maintained between the output of the mill and the rate of feed thereto for any rate of demand as indicated by said master'regulator.
6. A system according to claim '7 characterized by the fact that said second regulator-comprises a regulating element for controlling said feeder motor, a spring operatively connected to said regulating element and tending to move the same in one direction, means under the control of the master regulator for applying a variable loading force to said spring, and means actuated in accordance with the load on the prime mover for balancing the loading force on said spring, whereby when an unbalance occurs the regulating element is actuated to modify the speed of the feeder motor until the spring loading is again balanced.
7. A control system for pulverizer mills adapted to supply powdered fuel to boiler furnaces, and provided with an adjustable speed motor for driving the mill, means for feeding unpulverized fuel to the mill at controllable rates, and an adjustable supply of air for carrying powdered fuel out of the mill to the furnace, said system comprising a master regulator responsive to steam demand for developing a first control force that is a measure of steam demand, a second regulator responsive to said first control force and to a condition that varies with the load on the mo tor for establishing a second control force whose magnitude varies with the value of said first mentioned control force and the extent of response of said second regulator to the load on the motor, and means responsive to said second cont-rol force for so controlling the unpulverized fuel feeding means that said regulator is maintained substantially in a state of balance between said first control force and the effect of the motor load thereon.
8. The combination with a pulverizer mill, a steam actuated prime mover for driving the mill, and means for feeding material to be pulverized to the mill at regulatable rates, of means for developing a control force that varies with a condition reflecting the demand for pulverized material, means responsiveto said control force for controlling the operation of the feeding means to effect different rates of feed to the mill in ac cordance with the demand for pulverized material, and means responsive to the load on the steam actuated prime mover for so modifying the operation of the feed. controlling means that a substantially balanced relationship is maintained between the rate of feed to the mill and the load on the prime mover for each rate of feed to the mill.
9. The combination with a pulverizer mill, an electric motor for driving the mill, and means for feeding material to be pulverized to the mill at regulatable rates, of means for developing-a control force that varies with a condition reflecting the demand for pulverized material, means responsive to said control force for controlling the operation of the feeding means to effect different rates of feed to the mill in accordance with the demand for pulverizedmaterial, and means responsive to the load on the electric motor for so modifying the operation of the feed controlling means that a substantially balanced relationship is maintained between the rate of feed to the mill and the load' on the prime mover for each rate of -feed to the mill.
moms A. PEEBLES.
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Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2439721A (en) * 1941-04-22 1948-04-13 Bailey Meter Co Control system for feeding fuel to furnaces
US2530117A (en) * 1948-04-12 1950-11-14 Bailey Meter Co Furnace fuel feeder control system
US2547339A (en) * 1951-04-03 Locomotive combustion control
US2780186A (en) * 1950-04-14 1957-02-05 Riley Stoker Corp Feeding pulverized fuel for combustion
US2783947A (en) * 1951-05-22 1957-03-05 Babcock & Wilcox Co Pressure responsive mechanical electrical ratio controller for air swept pulverizer feed
US2804350A (en) * 1946-08-07 1957-08-27 Vastine Engineering Company In Fluid current conveyor system for sawdust-like material
US2990898A (en) * 1959-03-30 1961-07-04 Streeter Amet Co Feeding and weighing apparatus
US3078048A (en) * 1959-11-12 1963-02-19 Hardinge Co Inc Means and methods of supplying heat to grinding mills
US4518123A (en) * 1983-02-02 1985-05-21 Kobe Steel, Limited Method for controlling the pulverization and dryness of flammable materials passing through a pulverizer, and method of controlling the pulverizing rate of the pulverizer

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2547339A (en) * 1951-04-03 Locomotive combustion control
US2439721A (en) * 1941-04-22 1948-04-13 Bailey Meter Co Control system for feeding fuel to furnaces
US2804350A (en) * 1946-08-07 1957-08-27 Vastine Engineering Company In Fluid current conveyor system for sawdust-like material
US2530117A (en) * 1948-04-12 1950-11-14 Bailey Meter Co Furnace fuel feeder control system
US2780186A (en) * 1950-04-14 1957-02-05 Riley Stoker Corp Feeding pulverized fuel for combustion
US2783947A (en) * 1951-05-22 1957-03-05 Babcock & Wilcox Co Pressure responsive mechanical electrical ratio controller for air swept pulverizer feed
US2990898A (en) * 1959-03-30 1961-07-04 Streeter Amet Co Feeding and weighing apparatus
US3078048A (en) * 1959-11-12 1963-02-19 Hardinge Co Inc Means and methods of supplying heat to grinding mills
US4518123A (en) * 1983-02-02 1985-05-21 Kobe Steel, Limited Method for controlling the pulverization and dryness of flammable materials passing through a pulverizer, and method of controlling the pulverizing rate of the pulverizer

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