CN2643989Y - Liguid and solid medicine dispensing and administrating randomly machine - Google Patents
Liguid and solid medicine dispensing and administrating randomly machine Download PDFInfo
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- CN2643989Y CN2643989Y CN 03258491 CN03258491U CN2643989Y CN 2643989 Y CN2643989 Y CN 2643989Y CN 03258491 CN03258491 CN 03258491 CN 03258491 U CN03258491 U CN 03258491U CN 2643989 Y CN2643989 Y CN 2643989Y
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Abstract
The utility model is a liquid and solid material follow-up chemical dosing and feed machine, which is characterized in that: a feeding device, a premixing device, a stirring device and a main controller are arranged on a water tank; the discharge hole of a thruster is fixedly and tightly connected with the feeding hole of a mixing chamber; a plurality of clapboards are fixedly arranged in the water tank in a relatively parallel and alternative manner and divide the water tank into a plurality of stage overflow mechanical flocculation charmers and output buffer charmers; the inlets and outlets of each stage mechanical flocculation charmer and output buffer charmer relatively interlace. The utility model has the advantages of rational design, compact structure, small volume, low use and operation cost, and reducing the manual working strength. The dosing is a continuous technique, which changes the intermittent mode into the continuous mode, completely achieving the fully automatic dosing; moreover, the dosing amount can be adjusted along with the change of the required amount at any time, and has a good homogeneity, thoroughly avoiding the error caused by the batch dosing. By adopting the follow-up controlling technique, the solid high molecular flocculating agent enters continuously the rotational flow premixing device and the mixing chamber in an invariable proportion, forming a continuous dosing technique and achieving a dynamic balance.
Description
Technical field
The utility model relates to a kind of liquid, solid proportioning materials equipment, relates in particular to a kind of liquid, the solid material servo-actuated chemical feed machine that makes up a prescription.
Background technology
At present, domestic and international large-scale sewage-farm is to adopt bioanalysis to carry out sewage disposal mostly, has produced a large amount of mud in processing procedure, and the moisture content of its mud is at 96-98%.When handling mud, carry out by medicine system the high polymer coagulant of liquid state being squeezed in the mixed reaction vessel before the mechanical dehydration, high polymer coagulant is fully mixed with mud.Mud becomes bulky grain by the rapid absorption of subparticle under the effect of high polymer coagulant, form network structure, and the moisture between mud granule is separated out fast, enters thickening in the dewaterer then.In adding the preparing process of flocculant, all be to adopt the technology of intermittently making up a prescription.This method is that timesharing is placed in the mixing bunker and mixes after regularly dry powder flocculating agent and diluent liquid (water) being measured respectively.Through after the mixing slaking of several hrs, be transported in the mud by pump.Making up a prescription of this mode, production efficiency is lower, is easy to generate a batch error, and labor strength is bigger, and the volume ratio in mixing bunker and slaking storehouse is bigger, and capital cost is than higher.
Summary of the invention
Main purpose of the present utility model is to solve the deficiency in the above-mentioned water treatment, and the technology of intermittent mode being changed into the serialization mode is provided, and the amount of making up a prescription is along with a kind of liquid of the amount of making up a prescription, the solid material servo-actuated chemical feed machine that makes up a prescription is adjusted in the variation of requirement at any time.
The technical scheme that its technical problem that solves the utility model adopts is:
One end of storage tank upper end is provided with and adds machine and premixed device, the angle of rake discharging opening of the machine that adds is connected with the dog-house fixing seal of premixed device blending bunker, one side of storage tank is provided with the vacuum feeder tool, the upper end that adds machine is connected with the separator fixing seal of vacuum feeder tool, the vacuum feeder tool is connected with separator by flexible pipe, and the starting switch of vacuum feeder tool is connected with master controller.The middle part of storage tank upper end sets gradually several agitators, and the other end of storage tank upper end is provided with master controller.
Feeding system is made up of vacuum feeder tool and separator, and the vacuum feeder tool is connected with separator by flexible pipe, and the vacuum feeder tool adopts vavuum pump, and the starting switch of vacuum feeder tool is connected with master controller.Master controller starts the vavuum pump of vacuum feeder tool, and solid material is transported to by the vacuum feeder tool and carries out the solid and gas separation in the separator.
The bottom of storage tank one side is provided with evacuation port, and the upper end of storage tank one side is provided with overfall, and the bottom of storage tank opposite side is provided with discharging opening, and the side of storage tank one end is provided with the main water inlet tube road.
One end, main water inlet tube road is provided with stop valve, stop valve is connected with an end of pressure-reducing valve, the other end of pressure-reducing valve is connected with an end of control valve, and the other end of control valve is connected with the premixed device water main inlet port, constitutes the water inlet main line that enters storage tank.
The other end of main water inlet tube road pressure-reducing valve is connected with an end of mozzle control valve, and the other end of mozzle control valve is connected with mixed flow device premix diversion intake, constitutes the water conservancy diversion inlet pipeline that enters storage tank.
An end that adds machine base is provided with motor, reductor and encoder, and motor is connected with reductor with encoder, and the data message output of the switch of motor and encoder is connected with master controller.
The other end that adds machine base is provided with feeder, and the bottom and the base of feeder are connected to a fixed, and the upper end of feeder and the bottom of feed bin are connected to a fixed, and the upper end of feeder and the bottom of feed bin match.
The middle part opposing parallel of feed bin is provided with the material toggling shaft, and opposing parallel vertically is provided with several material toggling puddlers on the material toggling shaft, and the upper and lower of feed bin is provided with level-sensing device respectively, and the data-signal output of level-sensing device is connected with master controller.
Enter the abundant stirring of the material toggling puddler of various different materials on the material toggling shaft of feed bin, make the material in the feed bin be in the state of waiting to add into storage tank.
The middle part opposing parallel of feeder is provided with propeller, propeller runs through the middle part of feeder, along the propeller opposing parallel conveyer device﹠apos is set in the propeller, one end of conveyer device﹠apos is meshed with the output of reductor, angle of rake the other end is provided with discharging opening, and angle of rake discharging opening is connected with the dog-house fixing seal of premixed device blending bunker.
The middle part that adds machine base fixedly installs reduction gearing mechanism, the transmission input of reduction gearing mechanism is meshed with the output of reductor, the transmission output of reduction gearing mechanism is meshed with an end of material toggling axle, the separator of vacuum feeder tool is connected with the upper end fixing seal of the machine of adding, and adds the base of machine and the top of storage tank and is connected to a fixed.
Discharge in industry spot not only is subjected to the control of the open degree of valve, and the influence of the water pressure that also can be arrived in order to overcome the variation that the variation that comes water pressure causes coming discharge, and causes the inaccurate problem of dilution ratio, has adopted the servo-actuated control principle.At first the instantaneous discharge that enters storage tank is carried out accurate measurement, and with the data-signal of instantaneous discharge input master controller with add in the machine, the machine of adding is an independent closed loop following control system, its independently controller calculate dosage according to the instantaneous discharge size and the proportional meter that adds set, and compare with the detected current instantaneous amount that adds of machine that adds.Add the servo electrical machinery system of machine according to both instantaneous difference control, regulate angle of rake rotating speed and control dosage.
The blending bunker of premixed device is hollow inversed taper platform shape, and top is provided with the diversion intake, and the diversion intake is connected with mozzle.The upper end of blending bunker is provided with blending bunker, on the bulkhead of last blending bunker one side dog-house is set, with the dog-house opposing parallel cylinder is set on the bulkhead of last blending bunker opposite side, the piston rod end of cylinder is provided with valve plate, valve plate and dog-house match, and the open-close on-off of cylinder is connected with master controller.
The bottom of blending bunker is connected with the upper end of premixed device discharging opening, and the bottom and the storage tank of premixed device discharging opening are connected to a fixed, and insert in the casing of storage tank the bottom of premixed device discharging opening.
In order to prevent the solid-state flocculant deliquescence of macromolecule, reduce humid air and enter in the feed bin of the machine of adding, feed bin has adopted hermetically-sealed construction.The method of vacuum material loading is adopted in charging, and the discharging opening that adds machine adopts the method for air rammer sealing, opens piston when adding, closure piston when stopping to add.
Fixedly install some dividing plates and be separated into some grades of overflow-types machinery flocculation storehouses and output surge bunker along the inwall opposing parallel of storage tank is staggered in the storage tank, and the machinery of each grade flocculation storehouse is relative staggered with outlet with the import of output surge bunker, along output surge bunker inwall opposing parallel several liquid level gauges are set equidistantly in the output surge bunker, the data-signal output of liquid level gauge is connected with master controller.
Mixing and slaking mode in the storage tank adopt multistage storehouse overflow structure, after being full of in the previous stage storehouse, enter automatically in the next grade bin by the overflow mode, enter at last in the output surge bunker.The output surge bunker adopts multi-stage liquid level control, controls the soup amount of preparation according to the transformation period gradient of liquid level between adjacent liquid-level switch, real serialization batching.
The output shaft of agitator motor and transmission vertical shaft are connected to a fixed, and the transmission vertical shaft inserts in the machinery flocculation storehouse of storage tank, and the upper end and the bottom of transmission vertical shaft fixedly install paddle, and the middle part of transmission vertical shaft fixedly installs fixed blades.
In order to shorten incorporation time, adopted the agitator of the many blades of single shaft, two homodromal blades up and down promptly are set on a transmission vertical shaft, the middle part of transmission vertical shaft is provided with the fixedly paddle of a reverse rotation.
Insert in the hollow inversed taper platform shape blending bunker along hollow inversed taper platform shape blending bunker opposing parallel the diversion intake of hollow inversed taper platform shape blending bunker upper end, the inwall of diversion intake and hollow inversed taper platform shape blending bunker is tangent, and the spiral inner wall along hollow inversed taper platform shape blending bunker in the hollow inversed taper platform shape blending bunker is provided with deflector.
In order to accelerate dissolution velocity, adopt hollow inversed taper platform shape eddy flow blending bunker, dilution with 1/5 is input to the madial wall top of hollow inversed taper platform shape eddy flow blending bunker by the diversion pipeline along continuous straight runs, dilution is done the accelerated motion of circumference spiral along the cone inboard by deflector, the accelerated motion of circumference spiral also can turn clockwise, also can be rotated counterclockwise, solid-state flocculant falls into the conical surface of premixed device and the dilution of motion carries out premixed.
During use, opening the stop valve on main water inlet tube road and water that control valve need be handled enters from water inlet pipe, measure the instantaneous discharge of water outlet by pressure-reducing valve and fluid flowmeter, fluid flowmeter is transferred to master controller with the data-signal of instantaneous discharge, master controller collects behind the data-signal of instantaneous discharge according to the predefined ratio of making up a prescription, and starts the vacuum feeder tool, adds machine, agitator.A part of water of need handling enters the machinery flocculation storehouse of storage tank along main water pipeline by the water main inlet port of premixed device, and another part water that needs to handle enters the machinery flocculation storehouse of storage tank by the premix diversion intake of premixed device along diversion pipeline.The vacuum feeder tool will make up a prescription to carry by flexible pipe and separator and add in the feed bin of machine, drive the material toggling shaft by motor by reduction gearing mechanism, the material toggling puddler of material toggling shaft carries out material toggling and stirs, and batching is carried by feeder, propeller and conveyer device﹠apos.
Cylinder drive valve plate is opened the dog-house batching and is entered blending bunker, and batching enters the machinery flocculation storehouse of storage tank by last blending bunker, blending bunker and premixed device discharging opening.Batching enter another part water that blending bunker and premix diversion intake enter carry out swirl-flow premixed, the machinery that enters storage tank together with a part of water storehouse of flocculating.In storage tank, enter the output surge bunker by machinery flocculation storehouse by dividing plate, the soup after handling from the discharging opening output of output surge bunker through the multi-stage mechanical flocculation.
In the output surge bunker, the multi-stage liquid level meter is set, the data-signal output of liquid level gauge is connected with master controller, master controller calculates the output instantaneous delivery according to adjacent 2 liquid level transformation periods, master controller sends the flow of the control valve control water inlet on instruction adjusting main water inlet tube road, by discharge control dry powder flocculating agent dosage, reach the amount of making up a prescription that control adds machine simultaneously.
The utility model is liquid, the solid material servo-actuated chemical feed machine that makes up a prescription.Reasonable in design, compact conformation, volume is little, and cost of use and operating cost are low, reduce working strength of workers.Making up a prescription is the technology of serialization, and intermittent mode is changed into the serialization mode.Reach full-automation fully and make up a prescription, the amount of making up a prescription is along with the amount of making up a prescription is adjusted in the variation of requirement at any time, and the homogeneity of making up a prescription is good, thoroughly stops batch error of making up a prescription and producing.Adopt following control technical, the solid-state polymer flocculant with a constant ratio, is entered continuously and forms the continous way technology of making up a prescription in swirl-flow premixed device and the mixing bunker.Multistage storehouse overflow structure is adopted in mixing and slaking.In each mixing bunker, use many oars to stir to quicken mixing.The output surge bunker of afterbody adopts multi-stage liquid level control.According to liquid level between adjacent two-stage liquid-level switch the time variable gradient and the instantaneous amount of making up a prescription of the solid-liquid two-phase of prime calculate the instantaneous delivery that is added in the mud, and the flow of data feedback regulation water and the flow of solid-state polymer flocculant according to this, thereby reach the instantaneous amount of preparation of control flocculant, make it to reach fully the purpose of a dynamic equilibrium with demand.
Description of drawings
Below in conjunction with drawings and Examples the utility model is described in detail.
The make up a prescription schematic diagram of chemical feed machine of Fig. 1 liquid, solid material servo-actuated
The make up a prescription side view of chemical feed machine of Fig. 2 liquid, solid material servo-actuated
The make up a prescription schematic diagram of chemical feed machine of Fig. 3 liquid, solid material servo-actuated
The make up a prescription cutaway view of chemical feed machine of Fig. 4 liquid, solid material servo-actuated
The make up a prescription cutaway view of chemical feed machine of Fig. 5 liquid, solid material servo-actuated
1 adds machine, 2 level-sensing devices, 3 overfalls, 4 agitators, 5 storage tanks, 6 master controllers, 7 liquid level gauges, 8 stop valves, 9 pressure-reducing valves, 10 control valves, 11 fluid flowmeters, 12 heaters, 13 premixed devices, 14 discharging openings, 15 evacuation ports, 16 vacuum feeder tools, 17 water inlet pipes, 18 transmission vertical shafts, 19 paddles, 20 fixing paddles, 21 dividing plates, 22 motors, 23 reductors, 24 bases, 25 propellers, 26 feeders, 27 material toggling agitators, 28 material toggling puddlers, 29 feed bins, 30 reduction gearing mechanisms, 31 conveyer device﹠apos, 32 encoders, 33 premixed devices, 34 machinery flocculation storehouses, 35 output surge bunkers, 36 main water inlet tube roads, 37 diversion pipelines, 38 water main inlet ports, 39 premix diversion intakes, 40 premixed device discharging openings, 41 blending bunkers, 42 cylinders, 43 valve plates, blending bunker on 44,45 dog-houses, 46 deflectors, 47 separators
The specific embodiment
One end of storage tank (5) upper end is provided with and adds machine (1) and premixed device (33), the discharging opening that adds machine (1) propeller (25) is connected with dog-house (45) fixing seal of premixed device (33) blending bunker (41), one side of storage tank (5) is provided with vacuum feeder tool (16), the upper end that adds machine (1) is connected with separator (47) fixing seal of vacuum feeder tool (16), vacuum feeder tool (16) is connected with separator (47) by flexible pipe, and the starting switch of vacuum feeder tool (16) is connected with master controller (6); The middle part of storage tank (5) upper end sets gradually several agitators (4), and the other end of storage tank (5) upper end is provided with master controller (6).Feeding system is made up of vacuum feeder tool (16) and separator (47), vacuum feeder tool (16) is connected with separator (47) by flexible pipe, the vacuum feeder tool adopts vavuum pump, and the starting switch of vacuum feeder tool (16) is connected with master controller (6).Master controller (6) starts the vavuum pump of vacuum feeder tool (16), and solid material is transported to by vacuum feeder tool (16) and carries out the solid and gas separation in the separator (47).
The bottom of storage tank (5) one sides is provided with evacuation port (15), and the upper end of storage tank (5) one sides is provided with overfall (3), and the bottom of storage tank (5) opposite side is provided with discharging opening (14), and the side of storage tank (5) one ends is provided with main water inlet tube road (36).(36) one ends, main water inlet tube road are provided with stop valve (8), stop valve (8) is connected with an end of pressure-reducing valve (9), the other end of pressure-reducing valve (9) is connected with an end of control valve (10), the other end of control valve (10) is connected with premixed device (33) water main inlet port (38), constitutes the water inlet main line that enters storage tank (5).The other end of main water inlet tube road (36) pressure-reducing valve (9) is connected with an end of mozzle (37) control valve (10), the other end of mozzle (37) control valve (10) is connected with premixed device (33) premix diversion intake (39), constitute the water conservancy diversion inlet pipeline that enters storage tank (5), as shown in Figure 1 and Figure 2.
An end that adds machine (1) base (24) is provided with motor (22), reductor (23) and encoder (32), motor (22) is connected with reductor (23) with encoder (32), and the data message output of the switch of motor (22) and encoder (32) is connected with master controller (6); The other end that adds machine (1) base (24) is provided with feeder (26), the bottom of feeder (26) and base (24) are connected to a fixed, the bottom of the upper end of feeder (26) and feed bin (29) is connected to a fixed, and the bottom of the upper end of feeder (26) and feed bin (29) matches.The middle part opposing parallel of feed bin (29) is provided with material toggling shaft (27), material toggling shaft (27) is gone up opposing parallel several material toggling puddlers (28) vertically is set, the upper and lower of feed bin (29) is provided with level-sensing device (2) respectively, and the data-signal output of level-sensing device (2) is connected with master controller (6).Enter the abundant stirring of the material toggling puddler of various different materials on the material toggling shaft of feed bin, make the material in the feed bin be in the state of waiting to add into storage tank.The middle part opposing parallel of feeder (26) is provided with propeller (25), propeller (25) runs through the middle part of feeder (26), along propeller (25) opposing parallel conveyer device﹠apos (31) is set in the propeller (25), one end of conveyer device﹠apos (31) is meshed with the output of reductor (23), the other end of propeller (25) is provided with discharging opening, and the discharging opening of propeller (25) is connected with dog-house (45) fixing seal of premixed device (33) blending bunker (41).The middle part that adds machine (1) base (24) fixedly installs reduction gearing mechanism (30), the transmission input of reduction gearing mechanism (30) is meshed with the output of reductor (23), the transmission output of reduction gearing mechanism (30) is meshed with an end of material toggling axle (27), the discharging opening of material loading machinery (16) is connected with the upper end fixing seal of the machine of adding (1), add the base (24) of machine (1) and the top of storage tank (5) and be connected to a fixed, as Fig. 1, Fig. 2, shown in Figure 3.
Embodiment 3
The blending bunker (41) of premixed device (33) is hollow inversed taper platform shape, and top is provided with diversion intake (39), and diversion intake (39) are connected with mozzle (37).The upper end of blending bunker (41) is provided with blending bunker (44), dog-house (45) is set on the bulkhead of last blending bunker (44) one sides, with dog-house (45) opposing parallel cylinder (42) is set on the bulkhead of last blending bunker (44) opposite side, the piston rod end of cylinder (42) is provided with valve plate (43), valve plate (43) matches with dog-house (45), and the open-close on-off of cylinder (42) is connected with master controller (6).
The bottom of blending bunker (41) is connected with the upper end of premixed device discharging opening (40), the bottom of premixed device discharging opening (40) and storage tank (5) are connected to a fixed, and insert in the casing of storage tank (5), as Fig. 2, shown in Figure 4 the bottom of premixed device discharging opening (40).
Be separated into some grades of overflow-type machinery flocculation storehouses (34) and output surge bunker (35) along the staggered some dividing plates (21) that fixedly install of the inwall opposing parallel of storage tank (5) in the storage tank (5), and the import of the machinery of each grade flocculation storehouse (34) and output surge bunker (35) is relative staggered with outlet, along output surge bunker (35) inwall opposing parallel several liquid level gauges (7) are set equidistantly in the output surge bunker (35), the data-signal output of liquid level gauge (7) is connected with master controller (6), as shown in Figure 1.
The output shaft of agitator (4) motor (22) and transmission vertical shaft (18) are connected to a fixed, transmission vertical shaft (18) inserts in the machinery flocculation storehouse (34) of storage tank (5), the upper end of transmission vertical shaft (18) and bottom fixedly install paddle (19), the middle part of transmission vertical shaft (18) fixedly installs fixedly paddle (20), as shown in Figure 1.
Insert in the hollow inversed taper platform shape blending bunker (41) along hollow inversed taper platform shape blending bunker (41) opposing parallel the diversion intake (39) of hollow inversed taper platform shape blending bunker (41) upper end, diversion intake (39) is tangent with the inwall of hollow inversed taper platform shape blending bunker (41), and the spiral inner wall along hollow inversed taper platform shape blending bunker (41) in the hollow inversed taper platform shape blending bunker (41) is provided with deflector (46).
In order to accelerate dissolution velocity, adopt hollow inversed taper platform shape eddy flow blending bunker, dilution with 1/5 is input to the madial wall top of hollow inversed taper platform shape eddy flow blending bunker by the diversion pipeline along continuous straight runs, dilution is done the accelerated motion of circumference spiral along the cone inboard by deflector, the accelerated motion of circumference spiral is by turning clockwise, solid-state flocculant falls into the conical surface of premixed device and the dilution of motion carries out premixed, as Fig. 4, shown in Figure 5.
Insert in the hollow inversed taper platform shape blending bunker (41) along hollow inversed taper platform shape blending bunker (41) opposing parallel the diversion intake (39) of hollow inversed taper platform shape blending bunker (41) upper end, diversion intake (39) is tangent with the inwall of hollow inversed taper platform shape blending bunker (41), and the spiral inner wall along hollow inversed taper platform shape blending bunker (41) in the hollow inversed taper platform shape blending bunker (41) is provided with deflector (46).
In order to accelerate dissolution velocity, adopt hollow inversed taper platform shape eddy flow blending bunker, dilution with 1/5 is input to the madial wall top of hollow inversed taper platform shape eddy flow blending bunker by the diversion pipeline along continuous straight runs, dilution is done the accelerated motion of circumference spiral along the cone inboard by deflector, the accelerated motion of circumference spiral is by being rotated counterclockwise, solid-state flocculant falls into the conical surface of premixed device and the dilution of motion carries out premixed, as Fig. 4, shown in Figure 5.
Embodiment 8
During use, opening the stop valve (8) of main water inlet tube road (36) and water that control valve (10) need be handled enters from water inlet pipe (17), measure the instantaneous discharge of water outlet by pressure-reducing valve (9) and fluid flowmeter (11), fluid flowmeter (11) is transferred to master controller (6) with the data-signal of instantaneous discharge, master controller (6) collects behind the data-signal of instantaneous discharge according to the predefined ratio of making up a prescription, and starts vacuum feeder tool (16), adds machine (1), agitator (4).A part of water of need handling enters the machinery flocculation storehouse (34) of storage tank (5) along main water pipeline (36) by the water main inlet port (38) of premixed device (33), the machinery that needs another part water of handling to enter storage tank (5) along the premix diversion intake (39) of diversion pipeline (37) by premixed device (33) storehouse (34) of flocculating.Vacuum feeder tool (16) will make up a prescription to carry by flexible pipe and separator (47) and add in the feed bin (29) of machine (1), drive material toggling shaft (27) by motor (22) by reduction gearing mechanism (30), the material toggling puddler (28) of material toggling shaft (27) carries out material toggling and stirs, and batching is carried by feeder (26), propeller (25) and conveyer device﹠apos (31).Cylinder (42) drive valve plate (43) is opened dog-house (45) batching and is entered blending bunker (44), and batching enters the machinery flocculation storehouse (34) of storage tank (5) by last blending bunker (44), blending bunker (41) and premixed device discharging opening (40).Batching enters another part water that blending bunker (41) and premix diversion intake (39) enter and carries out swirl-flow premixedly, enters the machinery flocculation storehouse (34) of storage tank (5) together with a part of water.In storage tank (5), enter output surge bunker (35) by machinery flocculation storehouse (34) by dividing plate (21), the soup after handling from discharging opening (14) output of output surge bunker (35) through the multi-stage mechanical flocculation.In output surge bunker (35), multi-stage liquid level meter (7) is set, the data-signal output of liquid level gauge (7) is connected with master controller (6), master controller (6) calculates the output instantaneous delivery according to adjacent 2 liquid level transformation periods, master controller (6) sends the flow of control valve (10) the control water inlet on instruction adjusting main water inlet tube road (36), simultaneously by discharge control dry powder flocculating agent dosage, reach the amount of making up a prescription that control adds machine (1), as Fig. 1, Fig. 2, Fig. 3, Fig. 4, shown in Figure 5.
Claims (4)
1, a kind of liquid, the chemical feed machine Gu the material servo-actuated is made up a prescription, the end setting that it is characterized in that storage tank (5) upper end adds machine (1) and premixed device (33), the discharging opening that adds machine (1) propeller (25) is connected with dog-house (45) fixing seal of premixed device (33) blending bunker (41), one side of storage tank (5) is provided with vacuum feeder tool (16), the upper end that adds machine (1) is connected with separator (47) fixing seal of vacuum feeder tool (16), vacuum feeder tool (16) is connected with separator (47) by flexible pipe, and the starting switch of vacuum feeder tool (16) is connected with master controller (6); The middle part of storage tank (5) upper end sets gradually several agitators (4), and the other end of storage tank (5) upper end is provided with master controller (6); The bottom of storage tank (5) one sides is provided with evacuation port (15), and the upper end of storage tank (5) one sides is provided with overfall (3), and the bottom of storage tank (5) opposite side is provided with discharging opening (14), and the side of storage tank (5) one ends is provided with main water inlet tube road (36); (36) one ends, main water inlet tube road are provided with stop valve (8), stop valve (8) is connected with an end of pressure-reducing valve (9), the other end of pressure-reducing valve (9) is connected with an end of control valve (10), the other end of control valve (10) is connected with premixed device (33) water main inlet port (38), constitutes the water inlet main line that enters storage tank (5); The other end of main water inlet tube road (36) pressure-reducing valve (9) is connected with an end of mozzle (37) control valve (10), the other end of mozzle (37) control valve (10) is connected with mixed flow device (33) premix diversion intake (39), constitutes the water conservancy diversion inlet pipeline that enters storage tank (5); An end that adds machine (1) base (24) is provided with motor (22), reductor (23) and encoder (32), motor (22) is connected with reductor (23) with encoder (32), and the data message output of the switch of motor (22) and encoder (32) is connected with master controller (6); The other end that adds machine (1) base (24) is provided with feeder (26), the bottom of feeder (26) and base (24) are connected to a fixed, the bottom of the upper end of feeder (26) and feed bin (29) is connected to a fixed, and the bottom of the upper end of feeder (26) and feed bin (29) matches; The middle part opposing parallel of feed bin (29) is provided with material toggling shaft (27), material toggling shaft (27) is gone up opposing parallel several material toggling puddlers (28) vertically is set, the upper and lower of feed bin (29) is provided with level-sensing device (2) respectively, and the data-signal output of level-sensing device (2) is connected with master controller (6); The middle part opposing parallel of feeder (26) is provided with propeller (25), propeller (25) runs through the middle part of feeder (26), along propeller (25) opposing parallel conveyer device﹠apos (31) is set in the propeller (25), one end of conveyer device﹠apos (31) is meshed with the output of reductor (23), the other end of propeller (25) is provided with discharging opening, and the discharging opening of propeller (25) is connected with dog-house (45) fixing seal of premixed device (33) blending bunker (41); The middle part that adds machine (1) base (24) fixedly installs reduction gearing mechanism (30), the transmission input of reduction gearing mechanism (30) is meshed with the output of reductor (23), the transmission output of reduction gearing mechanism (30) is meshed with an end of material toggling axle (27), the separator (47) of vacuum feeder tool (16) is connected with the upper end fixing seal of the machine of adding (1), adds the base (24) of machine (1) and the top of storage tank (5) and is connected to a fixed; The blending bunker (41) of premixed device (33) is hollow inversed taper platform shape, and top is provided with diversion intake (39), and diversion intake (39) are connected with mozzle (37); The upper end of blending bunker (41) is provided with blending bunker (44), dog-house (45) is set on the bulkhead of last blending bunker (44) one sides, with dog-house (45) opposing parallel cylinder (42) is set on the bulkhead of last blending bunker (44) opposite side, the piston rod end of cylinder (42) is provided with valve plate (43), valve plate (43) matches with dog-house (45), and the open-close on-off of cylinder (42) is connected with master controller (6); The bottom of blending bunker (41) is connected with the upper end of premixed device discharging opening (40), and the bottom of premixed device discharging opening (40) and storage tank (5) are connected to a fixed, and insert in the casing of storage tank (5) bottom of premixed device discharging opening (40).
2, liquid according to claim 1, the chemical feed machine Gu the material servo-actuated is made up a prescription, it is characterized in that being separated into some grades of overflow-type machinery flocculation storehouses (34) and output surge bunker (35) along the staggered some dividing plates (21) that fixedly install of the inwall opposing parallel of storage tank (5) in the described storage tank (5), and the import of the machinery of each grade flocculation storehouse (34) and output surge bunker (35) is relative staggered with outlet, along output surge bunker (35) inwall opposing parallel several liquid level gauges (7) are set equidistantly in the output surge bunker (35), the data-signal output of liquid level gauge (7) is connected with master controller (6).
3, liquid according to claim 1, the solid material servo-actuated chemical feed machine that makes up a prescription, the output shaft and the transmission vertical shaft (18) that it is characterized in that described agitator (4) motor (22) are connected to a fixed, transmission vertical shaft (18) inserts in the machinery flocculation storehouse (34) of storage tank (5), the upper end of transmission vertical shaft (18) and bottom fixedly install paddle (19), and the middle part of transmission vertical shaft (18) fixedly installs fixedly paddle (20).
4, liquid according to claim 1, the solid material servo-actuated chemical feed machine that makes up a prescription, insert in the hollow inversed taper platform shape blending bunker (41) along hollow inversed taper platform shape blending bunker (41) opposing parallel the diversion intake (39) that it is characterized in that described hollow inversed taper platform shape blending bunker (41) upper end, diversion intake (39) is tangent with the inwall of hollow inversed taper platform shape blending bunker (41), and the spiral inner wall along hollow inversed taper platform shape blending bunker (41) in the hollow inversed taper platform shape blending bunker (41) is provided with deflector (46).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 03258491 CN2643989Y (en) | 2003-09-22 | 2003-09-22 | Liguid and solid medicine dispensing and administrating randomly machine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 03258491 CN2643989Y (en) | 2003-09-22 | 2003-09-22 | Liguid and solid medicine dispensing and administrating randomly machine |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2643989Y true CN2643989Y (en) | 2004-09-29 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 03258491 Expired - Fee Related CN2643989Y (en) | 2003-09-22 | 2003-09-22 | Liguid and solid medicine dispensing and administrating randomly machine |
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| Country | Link |
|---|---|
| CN (1) | CN2643989Y (en) |
Cited By (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102614795A (en) * | 2011-01-27 | 2012-08-01 | 宜兴协联生物化学有限公司 | Blending tank |
| CN102807282A (en) * | 2012-08-17 | 2012-12-05 | 甘肃银光化学工业集团有限公司 | Wet type raw material feeding device and method for feeding multiple raw materials |
| CN102908917A (en) * | 2011-07-31 | 2013-02-06 | 扬州清溢环保科技有限公司 | Novel integral dosing device |
| CN104174312A (en) * | 2014-08-28 | 2014-12-03 | 青岛恒昌泰橡塑机械有限公司 | Automatic batching, high-speed stirring and cold-mixing system |
| CN105350602A (en) * | 2015-11-30 | 2016-02-24 | 牛占华 | Domestic wastewater regeneration treatment system |
| CN106608675A (en) * | 2015-10-23 | 2017-05-03 | 中国石油化工股份有限公司 | Active carbon-activated sludge coupling process |
| CN106745381A (en) * | 2016-12-15 | 2017-05-31 | 中国科学院海洋研究所 | A kind of devices and methods therefor that red tide is administered using modified clay |
| CN108147513A (en) * | 2017-12-13 | 2018-06-12 | 宁波清智环保科技有限公司 | A kind of method of sewage disposal |
| CN108554217A (en) * | 2017-12-07 | 2018-09-21 | 滁州恒通磁电科技有限公司 | A kind of agitating device of neodymium iron boron powder |
| CN108636276A (en) * | 2018-07-19 | 2018-10-12 | 江苏博环保科技有限公司 | A kind of Intellectualized sewage water processing automatic medicament feeding system |
| CN108640244A (en) * | 2018-07-19 | 2018-10-12 | 江苏博环保科技有限公司 | A kind of medicament automatic feeder weighed |
| CN110180430A (en) * | 2019-05-17 | 2019-08-30 | 天津国投津能发电有限公司 | A kind of universal automatic preparing device of mushy stage medicament |
| CN111056728A (en) * | 2019-12-17 | 2020-04-24 | 中交（天津）生态环保设计研究院有限公司 | Combined dosing and dissolving system for river and lake bottom mud dehydration |
| CN114028843A (en) * | 2021-11-08 | 2022-02-11 | 长沙矿山研究院有限责任公司 | Vertical sand silo overflow water solid content regulation and control system and regulation and control method |
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2003
- 2003-09-22 CN CN 03258491 patent/CN2643989Y/en not_active Expired - Fee Related
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102614795A (en) * | 2011-01-27 | 2012-08-01 | 宜兴协联生物化学有限公司 | Blending tank |
| CN102908917A (en) * | 2011-07-31 | 2013-02-06 | 扬州清溢环保科技有限公司 | Novel integral dosing device |
| CN102807282A (en) * | 2012-08-17 | 2012-12-05 | 甘肃银光化学工业集团有限公司 | Wet type raw material feeding device and method for feeding multiple raw materials |
| CN102807282B (en) * | 2012-08-17 | 2013-12-18 | 甘肃银光化学工业集团有限公司 | Wet type raw material feeding device and method for feeding multiple raw materials |
| CN104174312A (en) * | 2014-08-28 | 2014-12-03 | 青岛恒昌泰橡塑机械有限公司 | Automatic batching, high-speed stirring and cold-mixing system |
| CN106608675A (en) * | 2015-10-23 | 2017-05-03 | 中国石油化工股份有限公司 | Active carbon-activated sludge coupling process |
| CN105350602B (en) * | 2015-11-30 | 2018-01-09 | 广州绿竹环保科技有限公司 | Sanitary wastewater regeneration treatment system |
| CN105350602A (en) * | 2015-11-30 | 2016-02-24 | 牛占华 | Domestic wastewater regeneration treatment system |
| CN106745381A (en) * | 2016-12-15 | 2017-05-31 | 中国科学院海洋研究所 | A kind of devices and methods therefor that red tide is administered using modified clay |
| CN108554217A (en) * | 2017-12-07 | 2018-09-21 | 滁州恒通磁电科技有限公司 | A kind of agitating device of neodymium iron boron powder |
| CN108147513A (en) * | 2017-12-13 | 2018-06-12 | 宁波清智环保科技有限公司 | A kind of method of sewage disposal |
| CN108147513B (en) * | 2017-12-13 | 2020-01-31 | 宁波清智环保科技有限公司 | sewage treatment method |
| CN108636276A (en) * | 2018-07-19 | 2018-10-12 | 江苏博环保科技有限公司 | A kind of Intellectualized sewage water processing automatic medicament feeding system |
| CN108640244A (en) * | 2018-07-19 | 2018-10-12 | 江苏博环保科技有限公司 | A kind of medicament automatic feeder weighed |
| CN110180430A (en) * | 2019-05-17 | 2019-08-30 | 天津国投津能发电有限公司 | A kind of universal automatic preparing device of mushy stage medicament |
| CN111056728A (en) * | 2019-12-17 | 2020-04-24 | 中交（天津）生态环保设计研究院有限公司 | Combined dosing and dissolving system for river and lake bottom mud dehydration |
| CN111056728B (en) * | 2019-12-17 | 2023-10-20 | 中交（天津）生态环保设计研究院有限公司 | Combined dosing and dissolving system for dewatering river and lake sediment |
| CN114028843A (en) * | 2021-11-08 | 2022-02-11 | 长沙矿山研究院有限责任公司 | Vertical sand silo overflow water solid content regulation and control system and regulation and control method |
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