CN1050339A - Automatic proportioning device for powder materials - Google Patents
Automatic proportioning device for powder materials Download PDFInfo
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- CN1050339A CN1050339A CN 90102881 CN90102881A CN1050339A CN 1050339 A CN1050339 A CN 1050339A CN 90102881 CN90102881 CN 90102881 CN 90102881 A CN90102881 A CN 90102881A CN 1050339 A CN1050339 A CN 1050339A
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Abstract
Automatic proportioning device for powder materials is a kind of granular material proportioning automatic control equipment.This equipment can be controlled bin-level automatically, automatically abolish feed bin knot arch, automatically control powder flow and the major and minor material proportion of adjusting automatically, improve distributing precision and homogeneity, save equipment investment and energy consumption, it is characterized in that: there is vibratory screening apparatus in feed bin inflow point, Automatic Arch device and material level self-actuated controller are housed on the feed bin, discharging opening below the feed bin is connected to the batcher of rectification definite value batcher or adjustable feed flow, batcher is connected mutually by the impulse flowmeter of aggregate bin with its below, dashes the material flowmeter and links to each other by the stirring conveyor of material blanking tube with its below.
Description
Automatic proportioning device for powder materials is a kind of granular material proportioning automatic control equipment.
The granular material batching has at present: the one, and positive displacement, as the screw reamer tubular type feeding machine of band baffle-box, this mode equipment is many, and power consumption is big, the parts rapid wear, maintenance cost is many, needs manually often to take a sample test actual flow, and distributing precision is lower; The 2nd, intermittently weight-type as blk weigher, needs complicated electric interlock to control and satisfies reliability, and dynamic error is bigger, can not satisfy successional requirement; The 3rd, the continuous and quantitative formula, as powder from feed bin through common impeller discharger, material level reamer, speed governing reamer to spiral metering scale, detect actual flow, with set throughput ratio and regulate the speed governing reamer again after, Control Flow, owing to adopt tubular type reamer charging gear to do flow regulation topworks, it is slower to regulate the speed, proportioning real-Time Tracking Control error is bigger, easily causes bigger error during feed bin knot arch.
The objective of the invention is: the device that a kind of granular material automatic blending is provided, this device can be controlled the material level of feed bin automatically, automatically abolish feed bin knot arch, automatically control granular material flow and the major and minor material proportion of adjusting automatically, improve distributing precision and homogeneity, reduce equipment investment, save energy consumption.
Embodiment of the present invention are as follows:
Principle of the present invention is by regulating the flow of secondary material, the principal goods materials flow amount that it is regulated from the motion tracking definite value.Automatic proportioning device for powder materials is made up of apparatus for feeding, vibratory screening apparatus, feed bin, charge level controller, Arch-Breaking Device, gate, batcher, flowmeter, flow indicator, flow regulator, flow controller, proportioning controller and stirring conveyor.Batcher is connected with the flowmeter that batcher feed flow is measured in its below mutually by the mouth that gathers materials, and flowmeter links to each other by the stirring conveyor of material blanking tube with its below; The vibratory screening apparatus that is used for removing granular material coarse fodder, impurity is equipped with in feed bin inflow point, feed bin Arch-Breaking Device and bin-level controller are housed on the feed bin, be used for unobstructed materials flow, stablize the storehouse and press, improve the batching set-up condition of work, discharging opening joins by the batcher of gate and interface and rectification batcher or adjustable feed flow below the feed bin; Major and minor mass flow score Tong Guo not link to each other with corresponding major and minor mass flow regulator by corresponding flow indicator, be used to produce corresponding mass flow control signal, principal goods materials flow amount indicator also links to each other with proportioning controller, produce the flow setting signal of secondary material, proportioning controller links to each other with secondary material flow amount regulator again, and controls by its ratio that goes to finish between the major and minor mass flow; Major and minor mass flow regulator links to each other with flow controller with corresponding feed bin Arch-Breaking Device respectively simultaneously, and flow controller links to each other with batcher, carries out the task that Automatic Arch and definite value are regulated mass flow.
The flow regulator that the present invention adopts is digital or the simulation formula; The signal that adopts is a voltage signal, or current signal, or frequency signal, or digital signal; The proportioning controller that adopts is a shunt, or voltage divider, or the coefficient adjustable amplifier, or arithmetical operation software.
The rectification batcher that the present invention adopts is by impeller, housing, bearing, the end-cover axle bearing, gland bonnet, bearing shell, shaft joint, reductor is configured to propping up, the impeller shaft of impeller is contained in the end-cover axle bearing by bearing and is contained in the bearing shell, be connected with reductor by shaft joint simultaneously, the V sheave of reductor is connected with buncher by vee belt, reductor is fixed on the support, the end-cover axle bearing links to each other with housing, impeller blade more than 10 is arranged on the impeller, the height of impeller blade is less than or equal to 1/3rd of impeller radius, impeller blade and the welding of impeller beam barrel, the impeller beam barrel passes through left end cap, right end cap and reinforcement and impeller shaft welding, housing is fixed on the support, have square charging aperture above the housing, have discharging opening below the housing.Shape behind the discharging opening planar development is to be to make by the following practice on the rectangle of two impeller blade spacings more than three times or three times growing (vertically) for impeller length and width (laterally): make diagonal line to the lower right corner from the rectangle upper left corner, in rectangle bottom, from 1/3 of summit, rectangle lower right corner intercepting impeller blade height, and be the garden heart with the section, the line segment of intercepting is that radius is made arc in rectangle, the tangent line that remakes arc is parallel with above-mentioned rectangle diagonal line, and prolongs tangent line to the rectangle top; With rectangular top left corner apex is starting point, intercepting is the line segment of length by the cotangent and high the amassing of impeller blade of the angle of repose of material on the rectangle left side, crossing section makes the tangent line of the parallel lines of rectangle top and above-mentioned arc and intersects, crossing this intersection point does the vertical line of tangent line and the rectangle top of arc and intersects, with this intersection point is the garden heart, is radius with the garden heart to the distance between intersection point, and be that starting point is made an arc to the rectangle top with the intersection point, with this camber line, the point of contact of above-mentioned rectangle lower right corner arc and tangent line is the separatrix to the camber line on summit, the lower right corner and the common tangent of two arcs, remove rectangle left-hand component, form feed opening.
Under the bigger situation of diameter of the housing, feed opening by the left side of the feed opening that makes at said method by about oppositely remake the feed opening of same shape, size, and form feed opening with its merging, or above-mentioned separatrix with removal between the line that forms more than three times or three times of these separatrix translation two impeller spacings and the formation feed opening.
The bin-level controller is used to guarantee to remain in the feed bin powder of certain altitude, form by machinery and circuit two parts, mechanical part is made of regulating block, pendulum plate stem, pendulum plate, axle, bearing seat cam, travel switch, the pendulum plate is fixedlyed connected with pendulum plate stem lower end, the pendulum plate stem is fixedlyed connected with an end of axle, the centre of axle is contained in the bearing seat by bearing, the other end of axle is equipped with cam, a travel switch respectively is equipped with on the both sides of cam, regulating block is sleeved on pendulum plate stem top, but up-down adjustment is fixed with nut; Circuit part has main circuit and control circuit; main circuit is by automatic air-break switch; main contacts often left by A.C. contactor; the electrothermal relay of overload protection and feed bin charging motor are formed; control circuit is by the normally opened contact of material level lower limit actuating length switch; the normally closed contact of material level upper limit actuating length switch; ac contactor coil and auxiliary normally opened contact thereof are formed; its course of work is as follows: automatic air-break switch closes; when being lower than under the given material level, bin-level prescribes a time limit; pendulum plate and pendulum plate stem reset under the self gravitation effect; drive axle and cam rotation simultaneously; the normally opened contact of material level lower limit actuating length switch is connected; the coil of A.C. contactor gets; A.C. contactor often open auxiliary contact and Chang Kai main contacts closure; feed bin charging motor gets electric startup; the beginning charging; because charging rate is greater than discharging speed; bin-level constantly rises; the pendulum plate rises with material level and constantly is pushed; drive axle and cam rotation simultaneously; the normally opened contact of material level lower limit actuating length switch is disconnected; but because the self-locking action of the auxiliary contact of A.C. contactor; the charging motor is rotated further feed; when rising on the given material level, bin-level prescribes a time limit; cam disconnects the normally closed contact of material level upper limit actuating length switch; the coil losing electricity of A.C. contactor; A.C. contactor often leaves main contacts and disconnects; the auxiliary contact release; feed bin charging motor dead electricity; stop charging; but the feed bin bottom is constantly discharging still; bin-level constantly descends, and prescribes a time limit when dropping under the given material level, repeats said process again; make feed bin charging motor get electric startup; the beginning charging, so circulation guarantees that bin-level is controlled at certain height repeatedly.
Automatic Arch when the feed bin Arch-Breaking Device is used for feed bin knot arch, form by machinery and automatically controlled two parts, mechanical part is made of suspension rod, bearing support, vibrating motor, cage, stage clip, suspension rod passes stage clip and feed bin upper cover plate, its upper end is fixed on the bearing support with nut and cushion block, and the lower end is connected with cage, and vibrating motor is contained on the bearing support, four stage clips place between bearing support and feed bin upper cover plate, and cage is in feed bin; Automatically controlled part is made up of main circuit and control circuit, main circuit is made up of automatic air-break switch, A.C. contactor normally opened contact, electrothermal relay and vibrating motor, and control circuit is made up of pushbutton switch, potentiometer, resistance, triode, relay and ac contactor coil.Its principle of work is: when feed bin knot arch, feed bin and batcher do not have material and provide, it is zero that flowmeter detects actual flow, and delivery rate is that zero electric signal and the interior flow signal of setting of flow regulator compares, produce very wide minus deviation signal, through the flow regulator integral operation, the flow regulator output signal is very fast surpass its peaked 80%, string is risen in the potentiometer both end voltage of conditioner outlet end, center tap place current potential rises, after the resistance step-down, the transistor base current potential is risen, the triode conduction, relay coil gets, its normally opened contact adhesive, ac contactor coil gets electric, the adhesive of A.C. contactor normally opened contact, and vibrating motor gets, cage and its generation resonance, begin brokenly arch, feed bin and batcher have material output again, and actual flow dwindles with setting flow signal deviation, until overgauge occurring, the flow regulator output signal descends, and potentiometer both end voltage decline transistor base current potential descends, and triode ends, relay electric-loss, its normally opened contact disconnects, the ac contactor coil dead electricity, and the A.C. contactor normally opened contact disconnects, the vibrating motor dead electricity stops brokenly arch.
The automatic control section of the proportioning of mass flow is used to make two or more mass flows and mutual proportioning constant in setting value, be made up of the control of principal goods materials flow amount definite value and secondary material flow amount tracking Control two parts, the control of principal goods materials flow amount definite value is made up of rectification batcher, flowmeter, flow indicator, flow regulator, flow controller; Secondary material flow amount tracking Control is by the batcher of adjustable flow, and flowmeter, flow indicator, proportioning controller, flow regulator, flow controller are formed, and two-part principle of work is as follows:
The control of the rectification batcher delivery rate of principal goods material is the flow that preestablishes the principal goods material by the dial of principal goods materials flow amount regulator, and change into and set the flow electric signal, take into account the flow indicator with flow principal goods material actual flow is detected integrating, convert the actual flow electric signal to, compare with the setting flow electric signal in the principal goods materials flow amount regulator, produce deviation signal, after principal goods materials flow amount regulator carries out the proportional integral computing to deviation signal, produce control signal and be defeated by principal goods materials flow amount controller, the delivery rate of control rectification batcher is stabilized on the preset flow rate principal goods material actual flow.
The batcher delivery rate control of secondary material is that flow is taken into account in the principal goods material actual flow electric signal input proportioning controller of flow indicator detection integrating, in the setting flow signal input secondary material flow amount regulator as secondary material after conversion, take into account electric signal that secondary material actual flow that the flow indicator detects converts to relatively with flow, produce deviation signal, deviation signal is after the computing of secondary material flow amount regulator proportional integral, produce control signal and be defeated by the secondary material flow amount controller, control the delivery rate of secondary material feeder again by the secondary material flow amount controller, regulate the flow of secondary material, make the flow of itself and principal goods material keep certain ratio.
The transformation relation of finishing in the proportioning controller is: the setting flow signal of secondary material equals the actual flow that conversion coefficient multiply by the principal goods material, also the conversion coefficient that multiply by secondary material flow amount meter with regard to the proportioning that equals major and minor material multiply by the actual flow signal of principal goods material again divided by the transformation coefficient of principal goods material flowmeter, and the maximum flow that conversion coefficient equals flowmeter survey is removed the maximum amplitude of signal.
The present invention is further described below in conjunction with drawings and Examples:
Fig. 1: the automatic proportioning device for powder materials block diagram,
Fig. 2: automatic proportioning device for powder materials technological process diagrammatic sketch,
Fig. 3: TB-1 bin-level controller diagrammatic sketch,
The right view of Fig. 4: Fig. 3,
Fig. 5: pG-1 feed bin Automatic Arch device diagrammatic sketch,
The vertical view of Fig. 6: Fig. 5,
The A-A cut-open view of Fig. 7: Fig. 5,
Fig. 8: ZL-1 rectification batcher diagrammatic sketch,
Fig. 9: ZL-1 rectification batcher impeller diagrammatic sketch,
The B-B cut-open view of Figure 10: Fig. 9,
Figure 11: ZL-L rectification batcher housing diagrammatic sketch,
The left view of Figure 12: Figure 11,
The vertical view of Figure 13: Figure 11,
The C-C cut-open view of Figure 14: Figure 11,
Figure 15: the automatic proportioning device for powder materials electrical schematic diagram,
Figure 16: automatic proportioning device for powder materials control circuit figure,
Figure 17: the automatic proportioning device for powder materials main circuit diagram,
Among the figure: 1, secondary material flow amount regulator, 2, secondary material flow amount indicator, 3, the secondary material flow amount controller, 4, pG-1 feed bin Arch-Breaking Device, 5, secondary material impulse flowmeter, 6, the batcher of secondary material, 7, feed bin, 8, apparatus for feeding, 9, TB-1 bin-level controller, 10, stirring conveyor, 11, proportioning controller, 12, TB-1 bin-level controller, 13, principal goods material impulse flowmeter, 14, ZL-1 rectification batcher, 15, feed bin, 16, apparatus for feeding, 17, principal goods materials flow amount indicator, 18, principal goods materials flow amount controller, 19, pG-1 feed bin Arch-Breaking Device, 20, principal goods materials flow amount regulator, 21, vibratory screening apparatus, 22, gate, 23, gate, 24, interface, 25, the mouth that gathers materials, 26, interface, 27, mouth gathers materials, 28, regulating block, 29, nut, 30, saturating lid, 31, bearing, 32, axle, 33, bearing seat, 34, cam, 35, the travel switch base, 36, support, 37, material level upper limit actuating length switch XK
B, 38, the cam fixed screw, 39, material level lower limit actuating length switch XK
A, 40, the pendulum plate stem, 41, the pendulum plate, 42, vibrating motor, 43, bearing support, 44, cushion block, 45, stage clip, 45
A, the feed bin upper cover plate, 46, suspension rod, 46
ACage, 47, bearing shell, 48, lubricating cup, 49, gland bonnet, 50, end-cover axle bearing, 51, impeller, 52, housing, 53, shaft joint, 54, impeller shaft, 55, left end cap, 56, the impeller beam barrel, 57, impeller blade, 58, reinforcement, 59, right end cap, 60, charging aperture, 61, discharging opening, 62, secondary material feed bin charging motor, 63, vibratory screening apparatus electromagnet, 64, the broken arch of principal goods material feed bin motor, 65, the broken arch of secondary material feed bin motor, 66, batcher motor, 67, stirring conveyor motor, 68, principal goods material feed bin charging motor, 69, the vibratory screening apparatus electromagnet.
Automatic proportioning device for powder materials (seeing Fig. 1, Fig. 2) is made up of batcher 6, ZL-1 rectification batcher 14, impulse flowmeter 5,13, flow regulator 1,20, flow indicator 2,17, flow controller 3,18, proportioning controller 11, the stirring conveyor 10 of apparatus for feeding 8,16, vibratory screening apparatus 21, feed bin 7,15, TB-1 bin-level controller 9,12, pG-1 feed bin Arch-Breaking Device 4,19, gate 22,23, secondary material.Batcher 14,6 is connected with the impulse flowmeter 13,5 of its below mutually by the mouth 25,27 that gathers materials, and impulse flowmeter links to each other by the stirring conveyor 10 of material blanking tube with its below; Vibratory screening apparatus 21 is equipped with in feed bin inflow point, with removing coarse fodder and impurity, feed bin 7, pG-1 feed bin Arch-Breaking Device 4 is housed on 15,19 and TB-1 bin-level controller 9,12, feed bin 7, discharging opening and gate 22 below 15,23 and interface 26, after 24 connections, be connected to the batcher 6 and the rectification batcher 14 of secondary material, impulse flowmeter 5,13 respectively with flow indicator 2,17 link to each other, principal goods materials flow amount indicator 17 links to each other with proportioning controller 11 with principal goods materials flow amount regulator 20 simultaneously, proportioning controller links to each other with secondary material flow amount regulator 1 again, flow regulator 1,20 difference while and corresponding pG-1 feed bin Arch- Breaking Devices 4,19 and flow controller
3,18 link to each other, and flow controller links to each other with batcher.
Embodiment of the invention lectotype selection is as follows:
Device name principal goods material is used with secondary material
Bin-level controller TB-1 bin-level controller TB-1 bin-level controller
Feed bin Arch-Breaking Device pG feed bin Arch-Breaking Device pG feed bin Arch-Breaking Device
Batcher ZL-1 rectification batcher GZ-1 electro-vibrating feeder
Flowmeter LFD-125 impulse flowmeter LFD-125 impulse flowmeter
0～25 ton/h of 0～25 ton/h
Flow indicator WDZ-III indication integrating instrument WDZ-III indication integrating instrument
Flow regulator DTL-121 regulator DTL-121 regulator
Flow controller DK-2 speed-regulating motor controller ZK-1 scr voltage converter
Proportioning controller Dp-01 ratio biasing device
Signal 0-10mA current signal
The bin-level controller is made up of machinery and circuit two parts.Mechanical part (seeing Fig. 3, Fig. 4) is made of regulating block 28, pendulum plate stem 40, pendulum plate 41, axle 32, bearing seat 33, cam 34, travel switch 37,39.Pendulum plate 41 is fixedlyed connected with the lower end of pendulum plate stem 40, pendulum plate stem 40 is fixedlyed connected with an end of axle 32, the centre of axle 32 is contained in the bearing seat 33 by bearing 31, the other end of axle is equipped with cam 34, a travel switch 37,39 respectively is equipped with on the both sides of cam, regulating block 28 is sleeved on pendulum plate stem 40 tops, but up-down adjustment is fixing with nut 29.Circuit part has main circuit (seeing Figure 17) and control circuit (seeing Figure 16).Major and minor material bin material level control principle is identical, is controlled to be example with the principal goods bin-level, and main circuit is often opened main contacts 1C, commutation diode D by automatic air-break switch 1ZK, A.C. contactor
1Inhale iron 1DZ with vibratory screening apparatus, electrothermal relay 1RJ and feed bin charging motor 1D form.Control circuit by among the man-auto change-over switch 1K(figure for automated location), manually boot and stop button 1QA, 1TA, material level lower limit actuating length switch 1XK
ANormally opened contact, material level upper limit actuating length switch 1XK
BThe normally closed contact 1RJ of normally closed contact, A.C. contactor 1C and auxiliary normally opened contact 1C thereof, electrothermal relay form.Its course of work is as follows: the automatic air-break switch 1ZK that closes, 1K press 1QA and start charging when manual position, stop charging by 1TA; 1K is when automated location, and when bin-level is lower than under the given material level in limited time, pendulum plate 41 and pendulum plate stem 40 reset under the self gravitation effect, drives axle 32 simultaneously and cam 34 rotates, and cam makes material level lower limit actuating length switch 1XK
ANormally opened contact connect, the coil of A.C. contactor 1C gets, A.C. contactor 1C often leaves main contacts and Chang Kai auxiliary contact closure, feed bin charging motor gets electric startup, and the beginning charging is because charging rate is greater than discharging speed, bin-level constantly rises, pendulum plate 41 rises with material level and constantly is pushed, and drives axle 32 and cam 34 rotations simultaneously, makes material level lower limit actuating length switch 1XK
ANormally opened contact disconnect, but because the self-locking action of often driving auxiliary contact of A.C. contactor, the charging motor is rotated further feed, when bin-level rises on the given material level in limited time, cam 32 makes material level upper limit actuating length switch 1XK
BNormally closed contact disconnect, the coil losing electricity of A.C. contactor 1C, the main contacts of often opening of A.C. contactor disconnects, the auxiliary contact release, feed bin charging motor 1D dead electricity stops charging, but the feed bin bottom is constantly discharging still, bin-level constantly descends, and prescribes a time limit when dropping under the given material level, repeats said process again, make feed bin charging motor get electric startup, the beginning charging, so circulation guarantees that bin-level is controlled at certain height repeatedly.
The feed bin Arch-Breaking Device is made up of machinery and automatically controlled two parts.Mechanical part (seeing Fig. 5, Fig. 6, Fig. 7) is by suspension rod 46, bearing support 43, vibrating motor 42, cage 46
A, stage clip 45 constitutes, suspension rod 46 passes stage clip 45 and feed bin upper cover plate 45
A, its upper end is fixed on the bearing support 43 lower end and cage 46 with nut and cushion block 44
AConnect, vibrating motor 42 is contained on the bearing support 43, and four stage clips 45 place bearing support 43 and feed bin upper cover plate 45
ABetween, cage is in feed bin.Automatically controlled part is made up of main circuit and control circuit, main, the broken arch of secondary material bin control principle is identical, be controlled to be example with the broken arch of principal goods feed bin, main circuit (seeing Figure 17) is by automatic air-break switch 3ZK, A.C. contactor normally opened contact 3C, electrothermal relay 3RJ and vibrating motor 3D form, control circuit (seeing Figure 16) is by potentiometer 1W, resistance 1R, triode 1T, relay 1J, hand push button switch 3QA, the normally opened contact 1J of relay, ac contactor coil 3C, the normally closed contact 3RJ of electrothermal relay forms, its principle of work is: when feed bin knot arch, feed bin and batcher do not have material and provide, it is zero that impulse flowmeter 13 detects actual flow, delivery rate is that zero electric signal and the flow regulator 20 interior flow electric signal of setting compare, produce the deviation electric signal, through flow regulator 20 integral operationes, the flow regulator output signal is very fast surpass its peaked 80%, the both end voltage of potentiometer 1W is risen, the current potential at center tap place rises, after resistance 1R step-down, triode 1T base potential is risen, triode 1T conducting, relay 1J coil gets, its normally opened contact adhesive, A.C. contactor 3C gets, the adhesive of A.C. contactor normally opened contact, vibrating motor 3D gets electric, cage 46
AWith its generation resonance, begin brokenly arch; Broken arch back batcher has material output again, actual flow increases sharply, dwindle immediately with the deviation of setting the flow electric signal, and overgauge appears, flow regulator 20 output electric signal descend, and potentiometer 1W both end voltage descends, and triode 1T base potential descends, triode 1T ends, relay 1J dead electricity, its normally opened contact disconnects, the coil losing electricity of A.C. contactor 3C, the A.C. contactor normally opened contact disconnects, vibrating motor 3D dead electricity stops brokenly arch, so, the every knot of feed bin encircles once, and Arch-Breaking Device is just pressed the said process action once.The working current of triode 1T is by transformer B, and rectifier bridge is piled QL, capacitor C
1, C
2, the circuit that integrated stable voltage circuit 1C forms provides.
Rectification batcher (see figure 8) is by impeller 51, housing 52, bearing, end-cover axle bearing 50, O-ring seal 49, bearing shell 47, shaft joint 53, reductor is configured to propping up, the impeller shaft 54(of impeller 51 sees Fig. 9) be contained in the end-cover axle bearing 50 and in the bearing shell 47 by bearing, be connected with reductor by shaft joint 53 simultaneously, the V sheave of reductor is connected with buncher by vee belt, end-cover axle bearing 50 is connected with housing 52,16 impeller blades 57 are arranged on the impeller 51, impeller shaft 54 is by left end cap 55, right end cap 59 and reinforcement 58 and 56 welding of impeller beam barrel, impeller blade 57 and 56 welding of impeller beam barrel, the top of housing 52 has square charging aperture 60, the housing below has discharging opening 61(and sees Figure 11, Figure 12), shape behind the discharging opening planar development is to be the length of impeller growing (vertically), wide (laterally) is to make by the following practice on the rectangle of two impeller blade spacings more than three times: make diagonal line from the rectangle upper left corner to the lower right corner, in rectangle bottom, from 1/3 of rectangle lower right corner intercepting impeller blade height, and be the center of circle with the section, the line segment of intercepting is that radius is made arc in rectangle, the tangent line that remakes arc is parallel with above-mentioned rectangle diagonal line, and prolongs tangent line to the rectangle top; With rectangular top left corner apex is starting point, intercepting is the line segment of length by the cotangent and the amassing of impeller blade height of material angle of repose on the rectangle left side, crossing section makes the tangent line of the parallel lines of rectangle top and above-mentioned arc and intersects, crossing this intersection point does the vertical line of tangent line and the rectangle top of arc and intersects, with this intersection point is the center of circle, is radius with the center of circle to the distance between intersection point, and be that starting point is made an arc to the rectangle top with the intersection point, with this camber line, the point of contact of above-mentioned rectangle lower right corner arc and tangent line is the separatrix to the camber line on summit, the lower right corner and the common tangent of two arcs, remove rectangle left-hand component, form feed opening.
The flow control of principal goods material at first preestablishes the flow (referring to Fig. 1, Figure 15) of principal goods material by the dial of principal goods materials flow amount regulator 20, and be transformed into and set the flow electric signal, if it is 0～25 ton/hour that flow regulator 20 is set flow adjustment range, the setting voltage range of adjustment is 0～2V, scale on the dial is 0～10, be that each scale is corresponding to 2.5 tons of/hour flows, 0.2V voltage, now setting principal goods materials flow amount is 20 tons/hour, just dial is pushed on the scale 8, promptly in flow regulator 20, form 1.6V setting voltage signal; The principal goods material actual flow that next ZL-1 type rectification batcher 14 provides detects integratings through impulse flowmeter 13 and flow indicator 17, convert current signal to, if established standards current signal scope is 0～10mA, every milliampere corresponding to 25 tons of/hour materials flow amounts, the actual flow that now detects the principal goods material is 5 tons/hour, promptly convert the current signal of 2mA to, this current signal converts the voltage signal of 0.4V to by the resistance of 20 Ω at the input end of flow regulator 20, compare with above-mentioned 1.6V setting voltage signal, produce deviation voltage signal 1.2V, the deviation voltage signal of 20 couples of 1.2V of flow regulator carries out the proportional integral computing, according to bias direction, change the output signal of flow regulator 20, when comparative result is minus deviation, increase output, reduce output when being overgauge, it is constant to keep output when deviation is zero, make the output voltage of flow controller 18 do corresponding the increase, reduce or remain unchanged, thereby make rectification batcher 14 delivery rates also do corresponding increase, reduce or remain unchanged, the actual flow of finally controlling the principal goods material is stabilized in to be set on the flow value.
The control and the principal goods materials flow amount control principle of secondary material feeder 6 delivery rates are basic identical, main difference is: impulse flowmeter 13 and flow indicator 17 detected in the actual flow electric signal input proportioning controller 11 of principal goods material of integratings, after conversion, producing secondary material sets in the flow electric signal input secondary material flow amount regulator 1, the electric signal that the secondary material actual flow that detects with secondary material impulse flowmeter 5 and secondary material flow amount indicator 2 converts to relatively, produce the deviation electric signal, the deviation electric signal is after flow regulator 1 proportional integral computing, produce the Control current signal and be defeated by secondary material flow amount controller 3, go to control the delivery rate of batcher 6 again, regulate the flow of secondary material, make it keep proportional with principal goods materials flow amount.The conversion of carrying out in proportioning controller 11 is: the setting flow signal of secondary material equals the actual flow signal of principal goods material and takes advantage of proportioning to set coefficient, proportioning is set coefficient and is equaled to set measurement conversion coefficient that proportioning takes advantage of secondary material flow amount meter 5 again divided by the measurement conversion coefficient of principal goods material flowmeter 13, setting proportioning as two kinds of materials is 10%, signal is that the measurement range of the major and minor mass flow meter of the electric current of 0～10mA is respectively 0～25 ton/hour and 0～5 ton/hour, and then proportioning is set coefficient and equaled 10% and multiply by the 10mA/5 ton and also just equal 0.5 divided by the 10mA/25 ton.
Adopt the present invention to two or more granular material proportionings, distributing precision height, good evenness, adaptability is strong, and is stable and reliable for performance, easy to operate, the automaticity height, save the labour, save equipment investment and energy consumption, reduce the maintenance cost of equipment, the present invention is used for the cement mill coal blending, not only can improve output, and can improve the quality of product effectively, cellar for storing things condition abnormal occurrence significantly reduces.
Claims (5)
1, automatic proportioning device for powder materials has apparatus for feeding, vibratory screening apparatus, feed bin, charge level controller, Arch-Breaking Device, gate, batcher, flowmeter, the flow indicator, flow regulator, flow controller, proportioning controller and stirring conveyor are formed, batcher is connected with the flowmeter of its below mutually by the mouth that gathers materials, flowmeter links to each other by the stirring conveyor of material blanking tube with its below, it is characterized in that: vibratory screening apparatus is equipped with in feed bin inflow point, feed bin Arch-Breaking Device and bin-level controller are housed on the feed bin, discharging opening joins by the batcher of gate and interface and rectification batcher or adjustable feed flow below the feed bin, main, secondary material flow amount score Tong Guo corresponding flow indicator and corresponding master, secondary material flow amount regulator links to each other, principal goods materials flow amount indicator also links to each other with proportioning controller, proportioning controller links to each other with secondary material flow amount regulator again, main, secondary material flow amount regulator links to each other with flow controller with corresponding feed bin Arch-Breaking Device respectively simultaneously, and flow controller links to each other with batcher.
2; according to the described automatic proportioning device for powder materials of claim 1; it is characterized in that: the bin-level controller is made up of machinery and circuit two parts; mechanical part is by regulating block; the pendulum plate stem; the pendulum plate; axle; bearing seat; cam; travel switch constitutes; circuit part has main circuit and control circuit; main circuit is by automatic air-break switch; main contacts often left by A.C. contactor; the electrothermal relay of overload protection and feed bin charging motor are formed, and control circuit is by the normally opened contact of material level lower limit actuating length switch; the normally closed contact of material level upper limit actuating length switch; ac contactor coil and auxiliary normally opened contact thereof are formed.
3, according to the described automatic proportioning device for powder materials of claim 1, it is characterized in that: the feed bin Arch-Breaking Device is made up of machinery and automatically controlled two parts, mechanical part is made of suspension rod, bearing support, vibrating motor, cage, stage clip, automatically controlled part is made up of main circuit and control circuit, main circuit is made up of automatic air-break switch, A.C. contactor normally opened contact, electrothermal relay and vibrating motor, and control circuit is made up of pushbutton switch, potentiometer, resistance, triode, relay, alternating-current controller coil.
4, according to the described automatic proportioning device for powder materials of claim 1, it is characterized in that: the rectification batcher is by impeller, housing, bearing, the end-cover axle bearing, gland bonnet, bearing shell, shaft joint, reductor is configured to propping up, the impeller shaft of impeller is contained in the end-cover axle bearing by bearing and is contained in the bearing shell, reductor is fixed on the support, the end-cover axle bearing links to each other with housing, 10 above impeller blades are arranged on the impeller, impeller shaft passes through left end cap, right end cap and reinforcement and the welding of impeller beam barrel, impeller blade and the welding of impeller beam barrel, housing is fixed on the support, have square charging aperture above the housing, have discharging opening below the housing.
5, according to the described rectification batcher of claim 4, it is characterized in that: the shape behind the discharging opening planar development that housing has below is to be the length of impeller growing (vertically), wide (laterally) is to make by the following practice on the rectangle of two impeller blade spacings more than three times or three times, make diagonal line from the rectangle upper left corner to the lower right corner, in rectangle bottom, from 1/3 of summit, rectangle lower right corner intercepting impeller blade height, and be the garden heart with the section, the line segment of intercepting is that radius is made arc in rectangle, the tangent line that remakes arc is parallel with above-mentioned rectangle diagonal line, and prolongs tangent line to the rectangle top; With rectangular top left corner apex is starting point, intercepting is the line segment of length by the cotangent and the amassing of impeller blade height of the angle of repose of material on the rectangle left side, crossing section makes the tangent line of the parallel lines of rectangle top and above-mentioned arc and intersects, crossing this intersection point does the vertical line of tangent line and the rectangle top of arc and intersects, with this intersection point is the garden heart, is radius with the garden heart to the distance between intersection point, and be that starting point is made an arc to the rectangle top with the intersection point, with this camber line, the point of contact of above-mentioned rectangle lower right corner arc and tangent line is the separatrix to the camber line on summit, the lower right corner and the common tangent of two arcs, remove rectangle left-hand component, form feed opening; Or the left side of the feed opening that said method makes by about oppositely remake the feed opening of same shape, size, and form feed opening with its merging; Or removing and the formation feed opening between above-mentioned separatrix and the line that forms more than three times or three times with these separatrix translation two impeller blade spacings.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 90102881 CN1023380C (en) | 1990-06-13 | 1990-06-13 | Automatic proportioning device for powder materials |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 90102881 CN1023380C (en) | 1990-06-13 | 1990-06-13 | Automatic proportioning device for powder materials |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1050339A true CN1050339A (en) | 1991-04-03 |
| CN1023380C CN1023380C (en) | 1994-01-05 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 90102881 Expired - Fee Related CN1023380C (en) | 1990-06-13 | 1990-06-13 | Automatic proportioning device for powder materials |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1023380C (en) |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100398419C (en) * | 2004-12-30 | 2008-07-02 | 黄世荣 | Solid raw material storing and mixing technology |
| CN100450950C (en) * | 2007-07-16 | 2009-01-14 | 缪建通 | Warehouse bottom material-flushing resisting method and control device |
| CN102008919A (en) * | 2010-10-11 | 2011-04-13 | 章志华 | Composite material automatic stirring system |
| CN102079555A (en) * | 2009-11-26 | 2011-06-01 | 江苏瀚深水业科技发展有限公司 | Manual material feeding assistor for mixing drum in powdered activated carbon wet type feeding device |
| CN102424261A (en) * | 2011-08-15 | 2012-04-25 | 鞍钢集团矿业公司 | High-precision continuous feeding system |
| CN102830722A (en) * | 2012-09-20 | 2012-12-19 | 江苏新美星包装机械股份有限公司 | Drink mixing control method |
| CN103612844A (en) * | 2013-11-22 | 2014-03-05 | 山东工大中能科技有限公司 | Method and device for automatically clearing blockage at discharge outlets of fine ore bin of mine |
| CN104874584A (en) * | 2015-05-12 | 2015-09-02 | 浙江大学 | Feed preparation system and method suitable for a worm biological reactor |
| CN104925862A (en) * | 2015-07-15 | 2015-09-23 | 攀钢集团攀枝花钢铁研究院有限公司 | Method for processing large particles produced during continuous acidolysis of titanium-containing raw materials |
| CN105854696A (en) * | 2016-06-16 | 2016-08-17 | 张家港宇新羊毛工业有限公司 | Wool cleansing thermonatrite powder stirring and mixing device |
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| CN106925419A (en) * | 2017-03-24 | 2017-07-07 | 茂名粤桥集团矿业有限公司 | A kind of titanium zirconium ore shaking table wet separation feed control system |
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1990
- 1990-06-13 CN CN 90102881 patent/CN1023380C/en not_active Expired - Fee Related
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| CN100398419C (en) * | 2004-12-30 | 2008-07-02 | 黄世荣 | Solid raw material storing and mixing technology |
| CN100450950C (en) * | 2007-07-16 | 2009-01-14 | 缪建通 | Warehouse bottom material-flushing resisting method and control device |
| CN102079555A (en) * | 2009-11-26 | 2011-06-01 | 江苏瀚深水业科技发展有限公司 | Manual material feeding assistor for mixing drum in powdered activated carbon wet type feeding device |
| CN102008919A (en) * | 2010-10-11 | 2011-04-13 | 章志华 | Composite material automatic stirring system |
| CN102424261A (en) * | 2011-08-15 | 2012-04-25 | 鞍钢集团矿业公司 | High-precision continuous feeding system |
| CN102830722A (en) * | 2012-09-20 | 2012-12-19 | 江苏新美星包装机械股份有限公司 | Drink mixing control method |
| CN103612844B (en) * | 2013-11-22 | 2016-03-23 | 山东工大中能科技有限公司 | The automatic block clearing method and apparatus of mine fine ore bin feed opening blocking |
| CN103612844A (en) * | 2013-11-22 | 2014-03-05 | 山东工大中能科技有限公司 | Method and device for automatically clearing blockage at discharge outlets of fine ore bin of mine |
| CN104874584B (en) * | 2015-05-12 | 2017-04-26 | 浙江大学 | Feed preparation system and method suitable for a worm biological reactor |
| CN104874584A (en) * | 2015-05-12 | 2015-09-02 | 浙江大学 | Feed preparation system and method suitable for a worm biological reactor |
| CN104925862A (en) * | 2015-07-15 | 2015-09-23 | 攀钢集团攀枝花钢铁研究院有限公司 | Method for processing large particles produced during continuous acidolysis of titanium-containing raw materials |
| CN105854696A (en) * | 2016-06-16 | 2016-08-17 | 张家港宇新羊毛工业有限公司 | Wool cleansing thermonatrite powder stirring and mixing device |
| CN106242244A (en) * | 2016-08-31 | 2016-12-21 | 四川中科玻璃有限公司 | Glass production feed proportioning system |
| CN106925419A (en) * | 2017-03-24 | 2017-07-07 | 茂名粤桥集团矿业有限公司 | A kind of titanium zirconium ore shaking table wet separation feed control system |
| CN109634235A (en) * | 2018-12-11 | 2019-04-16 | 成都航天科工大数据研究院有限公司 | A kind of energy consumption analysis method based on smelting furnace management |
| CN110652926A (en) * | 2019-09-19 | 2020-01-07 | 长兴众利耐火器材有限公司 | Automatic material proportioning device for refractory bricks |
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| Publication number | Publication date |
|---|---|
| CN1023380C (en) | 1994-01-05 |
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