CN107213847A - A kind of water pollution bed mud efficient improver prilling granulator and prilling process - Google Patents
A kind of water pollution bed mud efficient improver prilling granulator and prilling process Download PDFInfo
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- CN107213847A CN107213847A CN201710660481.2A CN201710660481A CN107213847A CN 107213847 A CN107213847 A CN 107213847A CN 201710660481 A CN201710660481 A CN 201710660481A CN 107213847 A CN107213847 A CN 107213847A
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- bed mud
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- 238000003911 water pollution Methods 0.000 title claims abstract description 29
- 238000000034 method Methods 0.000 title claims abstract description 14
- 230000008569 process Effects 0.000 title claims abstract description 13
- 238000001816 cooling Methods 0.000 claims abstract description 73
- 230000007246 mechanism Effects 0.000 claims abstract description 56
- 239000000463 material Substances 0.000 claims abstract description 29
- 238000007599 discharging Methods 0.000 claims abstract description 17
- 239000012809 cooling fluid Substances 0.000 claims abstract description 12
- 238000003825 pressing Methods 0.000 claims abstract description 11
- 238000005520 cutting process Methods 0.000 claims abstract description 10
- 239000012530 fluid Substances 0.000 claims description 50
- 239000002994 raw material Substances 0.000 claims description 40
- 238000003756 stirring Methods 0.000 claims description 38
- 230000005540 biological transmission Effects 0.000 claims description 17
- 238000000605 extraction Methods 0.000 claims description 16
- 238000002156 mixing Methods 0.000 claims description 16
- 238000005469 granulation Methods 0.000 claims description 11
- 230000003179 granulation Effects 0.000 claims description 11
- 239000008187 granular material Substances 0.000 claims description 10
- 238000001125 extrusion Methods 0.000 claims description 9
- 238000006243 chemical reaction Methods 0.000 claims description 7
- 230000007723 transport mechanism Effects 0.000 claims description 6
- 238000002224 dissection Methods 0.000 claims description 3
- 239000002826 coolant Substances 0.000 claims description 2
- 238000004519 manufacturing process Methods 0.000 abstract description 9
- 230000000694 effects Effects 0.000 abstract description 8
- 239000003795 chemical substances by application Substances 0.000 abstract description 7
- 239000002245 particle Substances 0.000 abstract description 6
- 230000001681 protective effect Effects 0.000 description 6
- 230000008859 change Effects 0.000 description 4
- 230000008901 benefit Effects 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000008676 import Effects 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 238000003786 synthesis reaction Methods 0.000 description 2
- 238000010276 construction Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2/00—Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic
- B01J2/20—Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic by expressing the material, e.g. through sieves and fragmenting the extruded length
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/80—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis
- B01F27/90—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis with paddles or arms
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Glanulating (AREA)
Abstract
The invention discloses a kind of water pollution bed mud efficient improver prilling granulator and prilling process, the prilling granulator includes supercharging pressing mechanism, rotary cutting mechanism, cooling body and drive mechanism, supercharging pressing mechanism includes hollow nacelle and the booster pump being coaxially sequentially connected, the inside of hollow nacelle is coaxially arranged with screw rod and swivel nut, rotary cutting mechanism includes rotary-cut cutter head and control grain mould, control grain mould is connected with the discharging opening of booster pump, rotary-cut cutter head is arranged on the discharging opening of control grain mould, cooling body includes a cooling collar, cooling collar is used to fill cooling fluid, cooling collar is twist arranged on the outside of hollow nacelle and booster pump.In the present invention cooling collar is twist provided with the outside of supercharging pressing mechanism, so that the heat produced in the course of the work is quickly distributed, heat is avoided excessively to cause the problem of material changes primary characteristic, the activity of synthetics in modifying agent particle is ensure that, so as to improve the quality of production of modifying agent particle.
Description
Technical field
The present invention relates to the technical field for preparing graininess modifying agent, more particularly to a kind of water pollution bed mud efficiently changes
Good dose of prilling granulator and prilling process.
Background technology
At present, prilling granulator has turned into the important equipment that mixing bulk cargo is prepared as to shaped article, then existing granulation
Extrusion forming device is provided with device, it can produce substantial amounts of heat during extrusion forming, contain chemistry for some
For the raw material of synthetic, produced using existing prilling granulator, it will cause synthetics is heated to change original
Characteristic, and then cause to granulate underproof problem;
Therefore, offer is needed badly a kind of suitable for the raw material prilling granulator containing synthetics.
The content of the invention
Not the problem of present invention is not suitable for granulating the raw material containing synthetics for existing prilling granulator, and
A kind of water pollution bed mud efficient improver prilling granulator and prilling process are provided, be can effectively ensure that former containing synthetics
The granulation quality of material, increases the practical promoted extension of prilling granulator.
To achieve the above object, the invention provides following scheme:
The invention provides a kind of water pollution bed mud efficient improver prilling granulator, including supercharging pressing mechanism, rotary-cut
Mechanism, cooling body and drive mechanism, the supercharging pressing mechanism include hollow nacelle and the booster pump being coaxially sequentially connected, institute
State and charging aperture is provided with hollow nacelle, the inside of the hollow nacelle is coaxially arranged with screw rod and swivel nut, the rotary cutting mechanism
Including rotary-cut cutter head and control grain mould, the control grain mould is connected with the discharging opening of the booster pump, and the rotary-cut cutter head is set
The discharging opening in the control grain mould is put, the cooling body includes a cooling collar, and the cooling collar, which is used to fill, to be cooled down
Fluid, the cooling collar is twist arranged on the outside of the hollow nacelle and the booster pump, the drive mechanism point
It is not connected with the screw rod, the booster pump and the rotary-cut cutter head.
It is preferred that, a numeral is additionally provided with the prilling granulator can control cabinet, and the numeral can control cabinet and the driving machine
Structure is electrically connected.
It is preferred that, a mixing mechanism is additionally provided with the prilling granulator, the mixing mechanism includes stir storehouse and setting
Stirring vane in the stir storehouse, one end of the stir storehouse is provided with a material inlet, the other end of the stir storehouse
Material outlet is provided with, the material outlet above and below the charging aperture of the hollow nacelle with being equipped with, and the stirring vane leads to
An agitating shaft is crossed with the drive mechanism to be connected.
It is preferred that, a transport mechanism is additionally provided with the prilling granulator, the transport mechanism includes transmission support, set
Transfer assembly above the transmission support and the collecting box for being arranged on the transmission support side, the transfer assembly bag
Drive roll, driven voller and conveyer belt are included, one end of the conveyer belt is arranged on the lower section of the control grain mould discharging mouthful, the biography
The other end of band is sent to be arranged on the top of the collecting box, the drive roll is connected with the drive mechanism.
It is preferred that, the drive mechanism includes stirring motor, frequency conversion rotary-cut motor, transmission motor, screw motor and supercharging
Pump motor, the stirring motor is connected with the agitating shaft, and the frequency conversion rotary-cut motor is connected with the rotary-cut cutter head, institute
State transmission motor with the drive roll to be connected, the screw motor is connected with the screw rod, the booster motor and institute
Booster pump is stated to be connected.
It is preferred that, the charging aperture of the hollow nacelle is to be provided with a charging on speed governing charging aperture, the speed governing charging aperture
Adjustable plate.
It is preferred that, a fluid draw-off pump, the fluid extraction pump and the digital energy are additionally provided with the cooling body
Cabinet electrical connection is controlled, the fluid inlet of the fluid extraction pump is connected with the fluid issuing of the cooling collar, and the fluid is taken out
The fluid issuing of pump is taken to be connected with the fluid inlet of the cooling collar.
It is preferred that, a condenser is additionally provided with the cooling body, the condenser is arranged on the fluid extraction pump
Fluid issuing and the cooling collar fluid inlet between.
It is preferred that, temperature sensor is additionally provided with the cooling body, the temperature sensor can be controlled with the numeral
Cabinet is electrically connected, and the temperature sensor is arranged on the inside of the cooling collar.
It is preferred that, the rotary cutting mechanism also includes a protective cover, and the protective cover is arranged on the outside of the rotary-cut cutter head,
The protective cover is used to protect the rotary-cut cutter head.
A kind of water pollution bed mud efficient improver prilling process is also provided in the present invention, comprised the following steps:
Raw material is put into the stir storehouse of mixing mechanism, while the stirring vane that numeral can be controlled in cabinet control stir storehouse is rotated
Raw material is mixed, mixed material is formed;
After the material outlet outflow in the agitated storehouse of mixed material, enter described hollow by the speed governing charging aperture of hollow nacelle
Inside nacelle, the screw rod and swivel nut being subsequently located inside the hollow nacelle carry out first time extruding to mixed material, are formed
Extruding raw material;Discharging opening of the extruding raw material through the hollow nacelle enters in booster pump, and the booster pump is to the extruding
Raw material carries out second and extruded, and forms secondary extrusion raw material;While first time extruding and second are extruded, numeral can control cabinet
Control fluid draw-off pump is filled with cold into the cooling collar being twist arranged on outside the hollow nacelle and the booster pump
But fluid, and the temperature information detected according to the temperature sensor being arranged on inside the cooling collar, to the cooling collar
The flow velocity of the interior cooling fluid is controlled in real time;
The secondary extrusion raw material is flowed out by being arranged on the control grain mould of the booster pump discharge outlet, while described two
Secondary extruding raw material forms shaped granule under the dissection of rotary-cut cutter head;The shaped granule falls to the control grain mould
On conveyer belt below discharging opening, the shaped granule is delivered in collecting box by the subsequent conveyer belt, completes granulation work.
Had the advantages that relative to prior art:
1st, it is being pressurized pressing mechanism in water pollution bed mud efficient improver prilling granulator of the invention and prilling process
The outside of hollow nacelle and booster pump is twist provided with cooling collar so that hollow nacelle and booster pump are in the course of the work
The heat of generation can be distributed quickly, it is to avoid heat is accumulated in hollow nacelle and booster pump causes hollow nacelle and increasing
The mixed material of press pump is heated the problem of change primary characteristic, and then ensure that chemical in the modifying agent particle containing synthetics
The activity of synthetic, so as to improve the quality of production of modifying agent particle.
2nd, cabinet pair can be controlled by numeral in water pollution bed mud efficient improver prilling granulator of the invention and prilling process
Prilling granulator is controlled, and improves the mechanization degree of prilling granulator, time and labour saving, human cost when reducing production.
3rd, used in water pollution bed mud efficient improver prilling granulator of the invention and prilling process in mixing mechanism
The mode of stirring vane is set so that raw material can carry out sufficient batch mixing, and supercharging can be fed directly to after batch mixing and is squeezed
Granulation work is carried out in press mechanism, production efficiency is not only increased, also improves the mixability of raw material.
4th, in water pollution bed mud efficient improver prilling granulator of the invention and prilling process in order to increase cooling collar
Cooling effect, it is ensured that the activity of synthetics in raw material, using the fluid issuing and the stream of cooling collar in cooling collar
The mode of fluid extraction pump is set between body import so that the flowing velocity of cooling fluid is increased in cooling collar, and then
Improve the cooling performance of cooling collar;Further, also using the fluid issuing and the stream of cooling collar in fluid extraction pump
The mode of condenser is set between body import, and quickly the temperature of reduction cooling fluid, further improves the cooling of cooling collar
Performance.
5th, a transport mechanism is provided with water pollution bed mud efficient improver prilling granulator of the invention and prilling process,
The product produced very easily is collected, the mechanization degree of prilling granulator is further increased, time and labour saving,
Human cost when reducing production.
6th, water pollution bed mud efficient improver prilling granulator of the invention has that the simple in construction, quality of production is high, promote
The big advantage of scope.
Brief description of the drawings
In order to illustrate more clearly about the embodiment of the present invention or technical scheme of the prior art, below will be to institute in embodiment
The accompanying drawing needed to use is briefly described, it is clear that drawings in the following description are only some embodiments of the present invention, for
For those of ordinary skill in the art, on the premise of not paying creative work, other can also be obtained according to these accompanying drawings
Accompanying drawing.
Fig. 1 is the overall structure diagram of water pollution bed mud efficient improver prilling granulator of the present invention;
Fig. 2 is the knot of rotary-cut cutter head and control grain mould in water pollution bed mud efficient improver prilling granulator device of the present invention
Structure schematic diagram;
In figure:The hollow nacelles of 1-;2- booster pumps;3- rotary cutting mechanisms;4- cooling collars;5- numerals can control cabinet;6- stir storehouses;
7- stirring vanes;8- transmits support;9- collecting boxs;10- drive rolls, 11- driven vollers, 12- conveyer belts, 13- stirring motors, 14-
Frequency conversion rotary-cut motor, 15- transmission motor, the fluid inlet of 16- cooling collars, the fluid issuing of 17- cooling collars, 18- speed governing
Charging aperture, 19- control grains mould, 20- rotary-cuts cutter head, 21- charging adjustable plates.
Embodiment
Below in conjunction with the accompanying drawing in the embodiment of the present invention, the technical scheme in the embodiment of the present invention is carried out clear, complete
Site preparation is described, it is clear that described embodiment is only a part of embodiment of the invention, rather than whole embodiments.It is based on
Embodiment in the present invention, it is every other that those of ordinary skill in the art are obtained under the premise of creative work is not made
Embodiment, belongs to the scope of protection of the invention.
Not the problem of present invention is not suitable for granulating the raw material containing synthetics for existing prilling granulator, and
A kind of water pollution bed mud efficient improver prilling granulator is provided, the granulation matter containing chemical synthesis raw material is can effectively ensure that
Amount, increases the practical promoted extension of prilling granulator.
In order to facilitate the understanding of the purposes, features and advantages of the present invention, it is below in conjunction with the accompanying drawings and specific real
Applying mode, the present invention is further detailed explanation.
The present invention as shown in Figure 1-2 provides a kind of water pollution bed mud efficient improver prilling granulator, including supercharging is squeezed
Press mechanism, rotary cutting mechanism 3, cooling body and drive mechanism, the supercharging pressing mechanism include the hollow cabin being coaxially sequentially connected
Be provided with charging aperture in body 1 and booster pump 2, the hollow nacelle 1, the inside of the hollow nacelle 1 be coaxially arranged with screw rod and
Swivel nut, the rotary cutting mechanism 3 includes rotary-cut cutter head 20 and control grain mould 19, and the control grain mould 19 goes out with the booster pump 2
Material mouth is connected, and the rotary-cut cutter head 20 is arranged on the discharging opening of the control grain mould 19, and the cooling body includes a cooling
Sleeve pipe 4, the cooling collar 4 is used to fill cooling fluid, and the cooling collar 4 is twist arranged on the hollow nacelle 1
With the outside of the booster pump 2, the drive mechanism respectively with the screw rod, the booster pump 2 and the phase of rotary-cut cutter head 20
Connection.
In the water pollution bed mud efficient improver prilling granulator work of the present invention, operating personnel are by the raw material mixed
Entered by the charging aperture of hollow nacelle 1 inside hollow nacelle 1, while being arranged on the screw rod and swivel nut inside hollow nacelle 1
Extruding work is carried out to raw material, the material after extruding is pushed into booster pump 2 carries out secondary booster to material, after supercharging
Raw material be extruded out by the multiple discharging openings controlled on grain mould 19, while the extruding of 20 pairs of the rotary-cut cutter head of rotary cutting mechanism 3
Raw material out is cut, and completes granulation work;Screw rod and swivel nut and booster pump 2 inside hollow nacelle 1 is to raw material
Carry out that during once supercharging and secondary booster substantial amounts of heat can be produced, hollow nacelle 1 and increasing in supercharging pressing mechanism
The outside of press pump 2 is twist provided with cooling collar 4 so that the heat that hollow nacelle 1 and booster pump 2 are produced in the course of the work
Amount can be distributed quickly, it is to avoid heat is accumulated in hollow nacelle 1 and booster pump 2 causes hollow nacelle 1 and booster pump 2
Mixed material it is heated the problem of change primary characteristic, and then ensure that chemical synthesis in the modifying agent particle containing synthetics
The activity of thing, so as to improve the quality of production of modifying agent particle.Wherein, drive mechanism can be a motor, motor difference
It is connected with screw rod, booster pump 2 and rotary-cut cutter head 20, connected mode can be gear connection, axle connection etc.;Further,
Drive mechanism can also be a motor, and drive mechanism includes stirring motor 13, frequency conversion rotary-cut motor 14, transmission motor 15, spiral shell
Bar motor and booster motor, stirring motor 13 are connected with agitating shaft, and frequency conversion rotary-cut motor 14 is connected with rotary-cut cutter head 20,
Transmission motor 15 is connected with drive roll 10, and screw motor is connected with screw rod, and booster motor is connected with booster pump 2;Its
In, screw motor and booster motor are built in hollow nacelle 1 and booster pump 2 respectively.
A numeral is additionally provided with heretofore described prilling granulator can control cabinet 5, and the numeral can control cabinet 5 and the driving
Mechanism is electrically connected;Cabinet 5 can be controlled by numeral to be controlled prilling granulator, improve the mechanization degree of prilling granulator, it is time saving
Saving of labor, human cost when reducing production.
A mixing mechanism is additionally provided with heretofore described prilling granulator, the mixing mechanism includes stir storehouse 6 and set
The stirring vane 7 in the stir storehouse 6 is put, one end of the stir storehouse 6 is provided with a material inlet, the stir storehouse 6
The other end is provided with material outlet, and the material outlet above and below the charging aperture of the hollow nacelle 1 with being equipped with, the stirring
Blade 7 is connected by an agitating shaft with the drive mechanism;Using the setting stirring vane 7 in mixing mechanism in the present invention
Mode so that raw material can carry out sufficient batch mixing, and can be fed directly to be made in supercharging pressing mechanism after batch mixing
Grain work, not only increases production efficiency, also improves the mixability of raw material.
It is collected for convenience to producing product, a transport mechanism is additionally provided with prilling granulator of the invention, is passed
Mechanism is sent to include transmission support 8, the transfer assembly for being arranged on the top of transmission support 8 and be arranged on the transmitted side of support 8
Collecting box 9, transfer assembly includes drive roll 10, driven voller 11 and conveyer belt 12, and one end of conveyer belt 12 is arranged on control grain mould
The lower section of 19 discharging openings, the other end of conveyer belt 12 is arranged on the top of collecting box 9, and drive roll 10 is connected with drive mechanism.
In order to ensure uniform, the stability of charging, it is to avoid due to material cross mostly occur suppress machine phenomenon, in the present invention will in
The charging aperture of empty nacelle 1 is designed as on speed governing charging aperture 18, speed governing charging aperture 18 being provided with a charging adjustable plate 21.
In order to increase the cooling effect of cooling collar 4, it is ensured that the activity of synthetics in raw material, cooler in the present invention
A fluid draw-off pump is additionally provided with structure, the fluid extraction pump can control cabinet 5 with the numeral and electrically connect, the fluid extraction pump
Fluid inlet be connected with the fluid issuing 17 of the cooling collar, the fluid issuing of the fluid extraction pump and the cooling
The fluid inlet 16 of sleeve pipe is connected, i.e., using between the fluid issuing 17 of cooling collar and the fluid inlet 16 of cooling collar
The mode of fluid extraction pump is set so that the flowing velocity of cooling fluid is increased in cooling collar 4, and then improves coolant jacket
The cooling performance of pipe 4.Further, a condenser is additionally provided with the present invention in cooling body, the condenser is set
Between the fluid issuing of the fluid extraction pump and the fluid inlet 16 of the cooling collar, i.e., using in fluid extraction pump
The mode of condenser is set between the fluid inlet 16 of fluid issuing and cooling collar, quickly the temperature of reduction cooling fluid,
Further improve the cooling performance of cooling collar 4.
It is heretofore described in order to which the temperature to cooling fluid in cooling collar 4 is monitored in real time, it is ensured that cooling effect
Temperature sensor is additionally provided with cooling body, temperature sensor can control cabinet 5 with numeral and electrically connect, and temperature sensor is arranged on cold
But the inside of sleeve pipe 4.In the course of the work, numeral can control cabinet 5 according to temperature sensor transmission come real time temperature signal, to cold
But mechanism is controlled in real time.
Cooling fluid is water or liquid nitrogen in the present invention.
Rotary cutting mechanism 3 also includes a protective cover in the present invention, and protective cover is arranged on the outside of rotary-cut cutter head 20, and protective cover is used
In protection rotary-cut cutter head 20.
A kind of water pollution bed mud efficient improver prilling process of application said apparatus is also provided in the present invention, including such as
Lower step:
Raw material is put into the stir storehouse 6 of mixing mechanism, while numeral can control the stirring vane 7 in the control stir storehouse 6 of cabinet 5
Rotation is mixed to raw material, forms mixed material;
After the material outlet outflow in the agitated storehouse 6 of mixed material, enter described by the speed governing charging aperture 18 of hollow nacelle 1
Inside hollow nacelle 1, the screw rod and swivel nut being subsequently located inside the hollow nacelle 1 carry out squeezing for the first time to mixed material
Pressure, forms extruding raw material;Discharging opening of the extruding raw material through the hollow nacelle 1 enters in booster pump 2, the booster pump 2
Second is carried out to the extruding raw material to extrude, and forms secondary extrusion raw material;While first time extruding and second are extruded,
Numeral can control cabinet 5 and control fluid draw-off pump to the cooling being twist arranged on outside the hollow nacelle 1 and the booster pump 2
Cooling fluid, and the temperature information detected according to the temperature sensor being arranged on inside the cooling collar 4 are filled with sleeve pipe 4,
The flow velocity of the cooling fluid in the cooling collar 4 is controlled in real time;
The secondary extrusion raw material is flowed out by being arranged on the control grain mould 19 of the discharge outlet of booster pump 2, while institute
Secondary extrusion raw material is stated under the dissection of rotary-cut cutter head 20, shaped granule is formed;The shaped granule falls to the control
On conveyer belt 12 below the grain discharging opening of mould 19, the shaped granule is delivered in collecting box 9 by the subsequent conveyer belt 12,
Complete granulation work.
Apply specific case in this specification to be set forth the principle and embodiment of the present invention, above example
Explanation be only intended to help to understand the method and its core concept of the present invention;Simultaneously for those of ordinary skill in the art,
According to the thought of the present invention, it will change in specific embodiments and applications.In summary, in this specification
Appearance should not be construed as limiting the invention.
Claims (10)
1. a kind of water pollution bed mud efficient improver prilling granulator, it is characterised in that:Including supercharging pressing mechanism, peeler
Structure, cooling body and drive mechanism, the supercharging pressing mechanism include hollow nacelle and the booster pump being coaxially sequentially connected, described
Charging aperture is provided with hollow nacelle, the inside of the hollow nacelle is coaxially arranged with screw rod and swivel nut, the rotary cutting mechanism bag
Rotary-cut cutter head and control grain mould are included, the control grain mould is connected with the discharging opening of the booster pump, and the rotary-cut cutter head is set
In the discharging opening of the control grain mould, the cooling body includes a cooling collar, and the cooling collar is used to fill cooling stream
Body, the cooling collar is twist arranged on the outside of the hollow nacelle and the booster pump, the drive mechanism difference
It is connected with the screw rod, the booster pump and the rotary-cut cutter head.
2. water pollution bed mud efficient improver prilling granulator according to claim 1, it is characterised in that:The granulation dress
A numeral is additionally provided with putting can control cabinet, and the numeral can control cabinet and be electrically connected with the drive mechanism.
3. water pollution bed mud efficient improver prilling granulator according to claim 2, it is characterised in that:The granulation dress
A mixing mechanism is additionally provided with putting, the mixing mechanism includes stir storehouse and the stirring vane being arranged in the stir storehouse,
One end of the stir storehouse is provided with a material inlet, and the other end of the stir storehouse is provided with material outlet, and the raw material goes out
Mouth above and below the charging aperture of the hollow nacelle with being equipped with, and the stirring vane passes through an agitating shaft and the drive mechanism phase
Connection.
4. water pollution bed mud efficient improver prilling granulator according to claim 3, it is characterised in that:The granulation dress
A transport mechanism is additionally provided with putting, the transport mechanism includes transmission support, the transmission being arranged on above the transmission support
Component and the collecting box for being arranged on the transmission support side, the transfer assembly include drive roll, driven voller and conveyer belt,
One end of the conveyer belt is arranged on the lower section of the control grain mould discharging mouthful, and the other end of the conveyer belt is arranged on the receipts
The top of header, the drive roll is connected with the drive mechanism.
5. water pollution bed mud efficient improver prilling granulator according to claim 4, it is characterised in that:The driving machine
Structure includes stirring motor, frequency conversion rotary-cut motor, transmission motor, screw motor and booster motor, the stirring motor with it is described
Agitating shaft is connected, and the frequency conversion rotary-cut motor is connected with the rotary-cut cutter head, the transmission motor and the drive roll phase
Connection, the screw motor is connected with the screw rod, and the booster motor is connected with the booster pump.
6. water pollution bed mud efficient improver prilling granulator according to claim 1, it is characterised in that:The hollow cabin
The charging aperture of body is to be provided with a charging adjustable plate on speed governing charging aperture, the speed governing charging aperture.
7. water pollution bed mud efficient improver prilling granulator according to claim 2, it is characterised in that:The cooler
A fluid draw-off pump is additionally provided with structure, the fluid extraction pump can control cabinet with the numeral and electrically connect, the fluid extraction pump
Fluid inlet be connected with the fluid issuing of the cooling collar, the fluid issuing of the fluid extraction pump and the coolant jacket
The fluid inlet of pipe is connected.
8. water pollution bed mud efficient improver prilling granulator according to claim 7, it is characterised in that:The cooler
A condenser is additionally provided with structure, the condenser is arranged on the fluid issuing and the cooling collar of the fluid extraction pump
Between fluid inlet.
9. water pollution bed mud efficient improver prilling granulator according to claim 8, it is characterised in that:The cooler
Temperature sensor is additionally provided with structure, the temperature sensor can control cabinet with the numeral and electrically connect, and the temperature sensor is set
Put in the inside of the cooling collar.
10. a kind of water pollution bed mud efficient improver prilling process, it is characterised in that comprise the following steps:
Raw material is put into the stir storehouse of mixing mechanism, while the stirring vane that numeral can be controlled in cabinet control stir storehouse is rotated to original
Material is mixed, and forms mixed material;
After the material outlet outflow in the agitated storehouse of mixed material, the hollow nacelle is entered by the speed governing charging aperture of hollow nacelle
Inside, the screw rod and swivel nut being subsequently located inside the hollow nacelle carries out first time extruding to mixed material, forms extruding
Raw material;Discharging opening of the extruding raw material through the hollow nacelle enters in booster pump, and the booster pump is to the extruding raw material
Carry out second to extrude, form secondary extrusion raw material;While first time extruding and second are extruded, numeral can control cabinet control
Fluid extraction pump is filled with cooling stream into the cooling collar being twist arranged on outside the hollow nacelle and the booster pump
Body, and the temperature information detected according to the temperature sensor being arranged on inside the cooling collar, to institute in the cooling collar
The flow velocity for stating cooling fluid is controlled in real time;
The secondary extrusion raw material is flowed out by being arranged on the control grain mould of the booster pump discharge outlet, while described secondary crowded
Press raw material under the dissection of rotary-cut cutter head, form shaped granule;The shaped granule falls to the control grain mould discharging
On conveyer belt below mouthful, the shaped granule is delivered in collecting box by the subsequent conveyer belt, completes granulation work.
Priority Applications (1)
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CN201710660481.2A CN107213847A (en) | 2017-08-04 | 2017-08-04 | A kind of water pollution bed mud efficient improver prilling granulator and prilling process |
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CN201710660481.2A CN107213847A (en) | 2017-08-04 | 2017-08-04 | A kind of water pollution bed mud efficient improver prilling granulator and prilling process |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
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