CN201807411U - Full-automatic totally-closed continuous material treatment equipment - Google Patents
Full-automatic totally-closed continuous material treatment equipment Download PDFInfo
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- CN201807411U CN201807411U CN2010205421748U CN201020542174U CN201807411U CN 201807411 U CN201807411 U CN 201807411U CN 2010205421748 U CN2010205421748 U CN 2010205421748U CN 201020542174 U CN201020542174 U CN 201020542174U CN 201807411 U CN201807411 U CN 201807411U
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- 239000000109 continuous material Substances 0.000 title claims abstract description 15
- 239000000463 material Substances 0.000 claims abstract description 204
- 238000001035 drying Methods 0.000 claims abstract description 59
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 45
- 229910052799 carbon Inorganic materials 0.000 claims abstract description 45
- 238000003860 storage Methods 0.000 claims abstract description 34
- 230000007704 transition Effects 0.000 claims abstract description 33
- 238000007872 degassing Methods 0.000 claims abstract description 31
- 238000001914 filtration Methods 0.000 claims abstract description 19
- 238000001125 extrusion Methods 0.000 claims description 44
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 31
- 238000007738 vacuum evaporation Methods 0.000 claims description 26
- 239000004576 sand Substances 0.000 claims description 12
- 125000006850 spacer group Chemical group 0.000 claims description 8
- 244000309464 bull Species 0.000 claims description 7
- 238000007599 discharging Methods 0.000 claims description 6
- 230000008676 import Effects 0.000 claims description 6
- 238000010438 heat treatment Methods 0.000 claims description 4
- 238000009434 installation Methods 0.000 claims description 4
- 239000000428 dust Substances 0.000 abstract description 5
- 238000004519 manufacturing process Methods 0.000 abstract description 3
- 238000001704 evaporation Methods 0.000 abstract 3
- 238000004806 packaging method and process Methods 0.000 abstract 1
- 238000000034 method Methods 0.000 description 9
- 230000008569 process Effects 0.000 description 7
- 230000001105 regulatory effect Effects 0.000 description 5
- 238000012946 outsourcing Methods 0.000 description 4
- 238000005469 granulation Methods 0.000 description 3
- 230000003179 granulation Effects 0.000 description 3
- 238000012856 packing Methods 0.000 description 3
- 238000010298 pulverizing process Methods 0.000 description 3
- 239000003082 abrasive agent Substances 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000008187 granular material Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 238000001291 vacuum drying Methods 0.000 description 2
- 241000196324 Embryophyta Species 0.000 description 1
- 235000019013 Viburnum opulus Nutrition 0.000 description 1
- 244000071378 Viburnum opulus Species 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 238000000498 ball milling Methods 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 235000013312 flour Nutrition 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 235000012054 meals Nutrition 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 239000012716 precipitator Substances 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
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Abstract
The utility model relates to a ball mill, in particular to full-automatic totally-closed continuous material treatment equipment. According to the technical scheme provided in the utility model, an extruding conveying device is mutually connected with a lifting machine; the extruding conveying device is mutually connected with a pelleting device; the pelleting device is mutually connected with a vacuum evaporating and drying tower; the vacuum evaporating and drying tower is mutually connected with a ring type airflow drying device; the ring type airflow drying device is mutually connected with a transition storage tank; the transition storage tank is mutually connected with a full-automatic totally-closed continuous ball mill; the full-automatic totally-closed continuous ball mill is mutually connected with a material collector; the material collector is mutually connected with a finished product transition storage tank; the finished product transition storage tank is mutually connected with a finished product conveying and packaging machine; the extruding conveying device, the vacuum evaporating and drying tower and the transition storage tank are respectively and mutually connected with a gas filtering device through moisture-removing pipelines; and the gas filtering device is mutually connected with an active carbon degassing tower through a pipeline. The utility model has the advantages of improving the production efficiency, avoiding the dust escape, and improving the working environment.
Description
Technical field
The utility model relates to a kind of ball mill, specifically a kind of full-automatic totally-enclosed continuous material treatment facility.
Background technology
Pulverize after powder that various moistures are higher or granular material need be dried mostly and select materials, in the prior art,, therefore can cause a large amount of flour dust overflows under air-tight state, influence environment because processes such as oven dry, pulverizing are not carried out.
Summary of the invention
The purpose of this utility model provides a kind of full-automatic totally-enclosed continuous material treatment facility, to enhance productivity, avoids dust to escape, and improves working environment.
According to the technical scheme that the utility model provides, the material inlet of extrusion conveying device and the material outlet of elevator interconnect; The material outlet of extrusion conveying device and the material inlet of prilling granulator interconnect; The material inlet of the material outlet of prilling granulator and vacuum evaporation drying tower interconnects; The material inlet of the material outlet of vacuum evaporation drying tower and ring type Pneumatic drying device interconnects; The material inlet of the material outlet of ring type Pneumatic drying device and transition storage tank interconnects; The material inlet of the material outlet of transition storage tank and full-automatic totally-enclosed continous way ball mill interconnects; The material outlet of full-automatic totally-enclosed continous way ball mill and the material inlet of material collector interconnect; The material inlet of the material outlet of material collector and finished product transition storage tank interconnects; The material inlet of the material outlet of finished product transition storage tank and the installation of finished product bull ladle interconnects; On described extrusion conveying device, vacuum evaporation drying tower and transition storage tank, utilize the inlet of hydrofuge pipeline and gas-filtering device to interconnect respectively; The outlet of gas-filtering device utilizes the inlet of pipeline and active carbon degassing tower to interconnect.
In described full-automatic totally-enclosed continous way ball mill, inner fixedly connected rotation pipe at feed pipe, on the wall that rotates pipe, the through hole that the ground material of some permissions passes through is set, described feed pipe is rotationally connected with on the bearing block, feed pipe is communicated with the inner chamber that rotates pipe, in the outside of rotating pipe airtight fixed casing is arranged, discharging opening is arranged below the described casing, described feed pipe is the material inlet of described full-automatic totally-enclosed continous way ball mill.
Between feed pipe and bearing block, tube connector is arranged, utilize self-aligning ball bearing to interconnect between described tube connector and described bearing block; Between tube connector and casing, utilize bearing to interconnect; Two ends at described rotation pipe all are provided with adpting flange; Outer wall in described tube connector outer end is provided with external screw thread, and the round nut with described external thread bolt connection is set in the end of tube connector; Spacer ring and the lasso that plays the role of positioning is set between the inwall of tube connector outer end and tube connector, and the end face of described spacer ring contacts with the inner face of round nut.
The utility model can also adopt such technical scheme, and the material inlet of extrusion conveying device and the material outlet of elevator interconnect; The material outlet of extrusion conveying device and the material inlet of prilling granulator interconnect; The material inlet of the material outlet of prilling granulator and vacuum evaporation drying tower interconnects; The material inlet of the material outlet of vacuum evaporation drying tower and ring type Pneumatic drying device interconnects; The material inlet of the material outlet of ring type Pneumatic drying device and transition storage tank interconnects; The material outlet of transition storage tank is connected with the feeder of material conveyor, the material outlet of material conveyor is connected with the material inlet of airslide disintegrating mill, the material outlet of airslide disintegrating mill utilizes pipeline to be connected with the material inlet of cyclopneumatic separator, the bottom of cyclopneumatic separator has material outlet, top at cyclopneumatic separator is provided with upper outlet, described upper outlet utilizes pipeline to be connected with the import of material collector, and the top outlet of material collector utilizes pipeline to be connected with the inlet of active carbon degassing tower; The material outlet of the material outlet of cyclopneumatic separator bottom and material collector bottom all interconnects with the material inlet that the finished product bull ladle is installed; On described extrusion conveying device, vacuum evaporation drying tower and transition storage tank, utilize the inlet of hydrofuge pipeline and gas-filtering device to interconnect respectively; The outlet of gas-filtering device utilizes the inlet of pipeline and described active carbon degassing tower to interconnect.
Top at the active carbon degassing tower is provided with gas vent, below the active carbon degassing tower water tank is set; Described ring type Pneumatic drying device is one and is wound into the device that ring-type forms by pipeline; Outer wall at extrusion conveying device is provided with the electric heater that several are used to heat material in the extrusion conveying device.
Material outlet at prilling granulator is provided with tubaeform extrusion head, at the port of export of tubaeform extrusion head web plate with holes is set, and in the outside of web plate with holes movable blade is arranged, and described movable blade is installed in the rotating shaft of extrusion conveying device.Be provided for heating the electric heater of material in the extrusion conveying device at the outer wall of vacuum evaporation drying tower, material outlet at the vacuum evaporation drying tower utilizes pipeline to be connected with the material inlet of ring type Pneumatic drying device, and on described pipeline cold and hot wind apparatus is set.
Bottom at water tank is provided with water pump, the delivery port of described water pump utilizes pipeline to be connected with the import of sand filter, the delivery port of sand filter utilizes pipeline to be connected with the water inlet of active carbon filter, and the delivery port of active carbon filter utilizes pipeline to be connected with the water inlet of accurate filter.On the pipeline that the material inlet with the active carbon degassing tower is connected blower fan is set, the outlet of described blower fan utilizes described pipeline to be communicated with the inlet of described active carbon degassing tower.On the pipeline that the material inlet with the active carbon degassing tower is connected blower fan is set, the outlet of described blower fan utilizes described pipeline to be communicated with the inlet of described active carbon degassing tower.
The utility model has the advantages that, carry out, therefore, the situation that dust escapes can not take place because the processing procedure of all materials all is under the air-tight state.Owing to adopted full-automatic totally-enclosed continous way ball mill, make whole process of production all carry out continuously simultaneously, therefore, improved production efficiency effectively.
Description of drawings
Fig. 1 is a structure chart of the present utility model.
Fig. 2 is the enlarged drawing of A among Fig. 1.
Fig. 3 is the structure chart of full-automatic totally-enclosed continous way ball mill.
Fig. 4 is the left view of Fig. 3.
The specific embodiment
Among the figure: 1, the first infinitely variable speeds decelerator, 2, the duplex chain wheel transmission device, 3, extruder drive, 4, elevator, 5, electric heater unit, 6, extrusion conveying device, can be a kind of screw conveyer; 7, prilling granulator, 8, vavuum pump, 9, first control valve, 10, ring type Pneumatic drying device, 11, hydrofuge pipeline, 12, gas bag, 13, material collector, it can be a kind of fiber bag precipitator, but this collection be material, 14, second control valve, 15, gas-filtering device, be similar to the air filter that a kind of automobile engine is used, the inner filter screen that gathers.16, active carbon degassing tower has the spout of shower water on the top of tower, be active carbon layer below the spout, and gas, is discharged at the top of active carbon degassing tower 16 through shower water spray back earlier through active carbon layer from following again; 17, cold and hot wind apparatus here can external hot blast official or cool air hose; 18, vacuum drier can outsourcing, as Changzhou space drying equipment far away Co., Ltd, also can make by oneself; 19, transition storage tank is exactly a kind of holding vessel; 20, the 3rd control valve, 21, full-automatic totally-enclosed continous way ball mill, 22, the second infinitely variable speeds decelerator, 23, the 4th control valve, 24, finished product transition storage tank, be exactly a kind of holding vessel, 25, finished product bull ladle installation can outsourcing, creates precious package packing machine Co., Ltd as the Foshan City, 26, the 5th control valve, 27, blower fan, 28, water tank, 29, water pump, 30, sand filter, be water treatment facilities, the sand that filtration is arranged in this equipment, water filters through obtaining behind the layer of sand; 31, active carbon filter, a kind of water treatment facilities have active carbon layer in this equipment, and water is further filtered through behind this active carbon layer; 32, accurate filter, a kind of filter plant, the centre is a filter stick, dense fiber-like object is twined in the filter stick outside, gas permeation fiber-like object, and granular material then is filtered, 33, drive mechanism can be a motor, 34, feeder, can be a kind of hopper, 35, material conveyor can be a kind of screw rod conveyor, 36, airslide disintegrating mill can outsourcing, as Weifang elite powder technology equipment Co., Ltd, 37, cyclone separator, can outsourcing, 38, material collector can be a kind of sack cleaner, 39, movable blade, 40, and cap, 41, web plate, 42, extrusion head, 43, the 6th control valve, 44, the 7th control valve.51, feed pipe, 52, round nut, 53, spacer ring, 54, lasso, 55, spacer ring, 57, the left shaft holder left end cap, 58, self-aligning ball bearing, 59, left shaft holder, 60, left shaft holder right end cap, 61, rubber oil seal with reinforce, 62, seal receptacle, 63, tube connector, 64, casing, 65, rotate pipe, 66, adpting flange, 67, right bearing left end cap, 69, taper roll bearing, 70, the right bearing right end cap, 71, nut, 72, rubber oil seal with reinforce, 73, flat key.
As shown in the figure: the material outlet of the material inlet of extrusion conveying device 6 and elevator 4 interconnects; The material inlet of the material outlet of extrusion conveying device 6 and prilling granulator 7 interconnects; The material inlet of the material outlet of prilling granulator 7 and vacuum evaporation drying tower 18 interconnects; The material inlet of the material outlet of vacuum evaporation drying tower 18 and ring type Pneumatic drying device 10 interconnects; The material inlet of the material outlet of ring type Pneumatic drying device 10 and transition storage tank 19 interconnects; The material inlet of the material outlet of transition storage tank 19 and full-automatic totally-enclosed continous way ball mill 21 interconnects; The material inlet of the material outlet of full-automatic totally-enclosed continous way ball mill 21 and material collector 13 interconnects; The material inlet of the material outlet of material collector 13 and finished product transition storage tank 24 interconnects; The material inlet of the material outlet of finished product transition storage tank 24 and finished product bull ladle installation 25 interconnects; On described extrusion conveying device 6, vacuum evaporation drying tower 18 and transition storage tank 19, utilize the hydrofuge pipeline 11 and the inlet of gas-filtering device 15 to interconnect respectively; The outlet of gas-filtering device 15 utilizes the inlet of pipeline and active carbon degassing tower 16 to interconnect.
Top at active carbon degassing tower 16 is provided with gas vent, and water tank 28 is set below active carbon degassing tower 16, with the water that produces in the collection and treatment process; Described ring type Pneumatic drying device 10 is one and is wound into the device that forms after the ring-type by pipeline, the length of ring type Pneumatic drying device 10 should be determined according to the moisture content of material, when moisture content when higher, then answer the length of proper extension ring type Pneumatic drying device 10, utilize the preheating and drying material of 6 pairs of materials generations of extrusion conveying device at ring type Pneumatic drying device 10; Outer wall at extrusion conveying device 6 is provided with the electric heater 5 that several are used to heat material in the extrusion conveying device 6, simultaneously material is heated in the process of carrying.
Material outlet at prilling granulator 7 is provided with tubaeform extrusion head 42, the port of export at tubaeform extrusion head 42 is provided with web plate 41 with holes, in the outside of web plate 41 with holes movable blade 39 is set, described movable blade 39 is installed in the rotating shaft of extrusion conveying device 6, can rotate with the rotation of rotating shaft.Material is compressed under the effect of extrusion conveying device 6 in the tubaeform extrusion head 42, and is extruded the hole on the web plate 41 with holes, utilizes 39 pairs of material cuttings of movable blade again in the outside of web plate 41 with holes, and material is pulverized.When needs are adjusted the granularity of material, can realize by the quantity of adjustment movable blade 39 and the size in the hole on the web plate with holes 41.
Be provided for heating the electric heater 5 of material in the extrusion conveying device 6 at the outer wall of vacuum evaporation drying tower 18, material outlet at vacuum evaporation drying tower 18 utilizes pipeline to be connected with the material inlet of ring type Pneumatic drying device 10, and cold and hot wind apparatus 17 is set on described pipeline, utilize cold and hot wind apparatus 17 to regulate material temperature, when needs are dry, with regard to blowing hot-air, make material in long ring type Pneumatic drying device 10, obtain further drying, when needs reduce material temperature, then can blow a cold wind over.
In described full-automatic totally-enclosed continous way ball mill 21, inner fixedly connected rotation pipe 65 at feed pipe 51, on the wall that rotates pipe 65, the through hole that the ground material of some permissions passes through is set, described feed pipe 51 is rotationally connected with on the bearing block, feed pipe 51 is communicated with the inner chamber that rotates pipe 65, in the outside of rotating pipe 65 airtight fixed casing 64 is arranged, below the described casing 64 discharging opening is arranged, described feed pipe 51 is the material inlet of described full-automatic totally-enclosed continous way ball mill 21.During work, material enters continuously from feed pipe 51 and rotates in the pipe 65, in rotating pipe 65, abrasive material is arranged, when rotating pipe 65 when rotating with feed pipe 51, abrasive material grinds material, make the material grinding that constantly is broken, some through holes of setting size are set on the wall that rotates pipe 65, when material is milled to can be when the through hole, the granularity that material is described meets the requirements, intransitable material is then continued to grind in rotating pipe 65, all can be by till the described through hole up to all materials.Therefore in whole process of lapping, advancing and going out of material is continuous.In the outside of rotating pipe 65 airtight casing 64 is arranged, when coming out in the through hole of material on rotating pipe 65, can guarantee can dust from flying.Discharging opening in the bottom of casing 64 utilizes pipeline to connect negative suction system, ground material is inhaled delivered to next process.
In the bottom of water tank 28 water pump 29 is set, the delivery port of described water pump 29 utilizes pipeline to be connected with the import of sand filter 30, the delivery port of sand filter 30 utilizes pipeline to be connected with the water inlet of active carbon filter 31, and the delivery port of active carbon filter 31 utilizes pipeline to be connected with the water inlet of accurate filter 32.The water that utilizes sand filter 30, active carbon filter 31 and 32 pairs of accurate filters to be collected in the water tank 28 is handled, and can meet emission request to guarantee water.
The material inlet that another kind of implementation of the present utility model is an extrusion conveying device 6 and the material outlet of elevator 4 interconnect; The material inlet of the material outlet of extrusion conveying device 6 and prilling granulator 7 interconnects; The material inlet of the material outlet of prilling granulator 7 and vacuum evaporation drying tower 18 interconnects; The material inlet of the material outlet of vacuum evaporation drying tower 18 and ring type Pneumatic drying device 10 interconnects; The material inlet of the material outlet of ring type Pneumatic drying device 10 and transition storage tank 19 interconnects; The material outlet of transition storage tank 19 is connected with the feeder 34 of material conveyor 35, the material outlet of material conveyor 35 is connected with the material inlet of airslide disintegrating mill 36, the material outlet of airslide disintegrating mill 36 utilizes pipeline to be connected with the material inlet of cyclopneumatic separator 37, the bottom of cyclopneumatic separator 37 has material outlet, top at cyclopneumatic separator is provided with upper outlet, described upper outlet utilizes pipeline to be connected with the import of material collector 38, and the top outlet of material collector 38 utilizes pipeline to be connected with the inlet of active carbon degassing tower 16; The material outlet of the material outlet of cyclopneumatic separator 37 bottoms and material collector 38 bottoms all interconnects with the material inlet that the finished product bull ladle is installed; On described extrusion conveying device 6, vacuum evaporation drying tower 18 and transition storage tank 19, utilize the hydrofuge pipeline 11 and the inlet of gas-filtering device 15 to interconnect respectively; The outlet of gas-filtering device 15 utilizes the inlet of pipeline and described active carbon degassing tower 16 to interconnect.At this time just need not pass through full-automatic totally-enclosed continous way ball mill 21, but utilize 36 pairs of materials of airslide disintegrating mill to pulverize, the material after the pulverizing after cyclopneumatic separator 37 and material collector 38 bi-level treatment, is sent to packing again.Gas then is admitted in the active carbon degassing tower 16 and handles, and the water that produces in the processing procedure then need be handled through sand filter 30 and active carbon filter 31 and accurate filter 32 equally.
Blower fan 27 is set on the pipeline that the material inlet with active carbon degassing tower 16 is connected, and the outlet of described blower fan 27 utilizes described pipeline to be communicated with the inlet of described active carbon degassing tower 16.
During work, can regulate feeding speed by the running speed of regulating first buncher 1, to regulate oven dry and pulverizing time according to the moisture content of material.In the process that material is transferred in extrusion conveying device 6, the 5 pairs of materials of electric heater unit that are installed on the extrusion conveying device 6 carry out heating, drying, when needs are regulated bake out temperature, can realize by the power of regulating electric heater unit 5; Material after the oven dry enters and carries out granulation in the prilling granulator 7, when granulation, the granularity of material can be regulated by the movable blade in the prilling granulator 7 39, during adjusting, and can be by the size that increases or the spacing of 41 of the quantity of the cutter that takes in sail and movable blade and web plates with holes is regulated particle.Material after granulation is finished enters and carries out vacuum drying in the vacuum evaporation drying tower 18; Simultaneously to carrying out sample analysis, so that in time adjust the size of granularity.After the vacuum drying, enter again in the ring type Pneumatic drying device 10, to material do, wet, hot and cold stability adjustment.Adjustment finishes, and material enters in the transition storage tank 19 again, further improves the stability of material.Material is entered in the full-automatic totally-enclosed continous way ball mill 21, under totally enclosed state, continuously material is carried out ball milling, so that obtain the raw meal particle size of requirement, satisfactory material utilizes the principle discharging of vacuum pressure conveying from the discharging opening that is arranged at full-automatic totally-enclosed continous way ball mill 21 bottoms, send in the cloth-bag type material collector 13, satisfactory material collection is delivered on the packing machine through closed conveying equipment 25 and packs in finished product storage tank 24.On extrusion conveying device 6, vacuum evaporation drying tower 18 and transition storage tank 19, be provided with hydrofuge pipeline 11, the moisture that produces in the course of work can be collected in the gas-filtering device 15, moisture is after filtering sent in the active carbon degassing tower 16 again and is discharged after the treatment and purification.The water elder generation structure sand filter 30 that produces in the active carbon degassing tower 16 filters, and discharges after the filtration through active carbon filter 31 and accurate filter 32, for recycling again.
Claims (10)
1. full-automatic totally-enclosed continuous material treatment facility is characterized in that: the material outlet of the material inlet of extrusion conveying device (6) and elevator (4) interconnects; The material inlet of the material outlet of extrusion conveying device (6) and prilling granulator (7) interconnects; The material inlet of the material outlet of prilling granulator (7) and vacuum evaporation drying tower (18) interconnects; The material inlet of the material outlet of vacuum evaporation drying tower (18) and ring type Pneumatic drying device (10) interconnects; The material inlet of the material outlet of ring type Pneumatic drying device (10) and transition storage tank (19) interconnects; The material inlet of the material outlet of transition storage tank (19) and full-automatic totally-enclosed continous way ball mill (21) interconnects; The material inlet of the material outlet of full-automatic totally-enclosed continous way ball mill (21) and material collector (13) interconnects; The material inlet of the material outlet of material collector (13) and finished product transition storage tank (24) interconnects; The material inlet of the material outlet of finished product transition storage tank (24) and finished product bull ladle installation (25) interconnects; On described extrusion conveying device (6), vacuum evaporation drying tower (18) and transition storage tank (19), utilize the hydrofuge pipeline (11) and the inlet of gas-filtering device (15) to interconnect respectively; The outlet of gas-filtering device (15) utilizes the inlet of pipeline and active carbon degassing tower (16) to interconnect.
2. full-automatic totally-enclosed continuous material treatment facility as claimed in claim 1, it is characterized in that: in described full-automatic totally-enclosed continous way ball mill (21), inner fixedly connected rotation pipe (65) at feed pipe (51), on the wall that rotates pipe (65), the through hole that the ground material of some permissions passes through is set, described feed pipe (51) is rotationally connected with on the bearing block, feed pipe (51) is communicated with the inner chamber that rotates pipe (65), in the outside of rotating pipe (65) airtight fixed casing (64) is arranged, below the described casing (64) discharging opening is arranged, described feed pipe (51) is the material inlet of described full-automatic totally-enclosed continous way ball mill (21).
3. full-automatic totally-enclosed continuous material treatment facility as claimed in claim 2 is characterized in that: tube connector (63) is arranged between feed pipe (51) and bearing block, utilize self-aligning ball bearing (58) to interconnect between described tube connector (63) and described bearing block; Between tube connector (63) and casing (64), utilize bearing to interconnect; At the two ends of described rotation pipe (65) adpting flange (66) is set all; Outer wall in described tube connector (63) outer end is provided with external screw thread, and the round nut (5) with described external thread bolt connection is set in the end of tube connector (63); Spacer ring and the lasso that plays the role of positioning is set between the inwall of tube connector (63) outer end and tube connector (63), and the end face of described spacer ring contacts with the inner face of round nut (52).
4. full-automatic totally-enclosed continuous material treatment facility, it is characterized in that: the material outlet of the material inlet of extrusion conveying device (6) and elevator (4) interconnects; The material inlet of the material outlet of extrusion conveying device (6) and prilling granulator (7) interconnects; The material inlet of the material outlet of prilling granulator (7) and vacuum evaporation drying tower (18) interconnects; The material inlet of the material outlet of vacuum evaporation drying tower (18) and ring type Pneumatic drying device (10) interconnects; The material inlet of the material outlet of ring type Pneumatic drying device (10) and transition storage tank (19) interconnects; The material outlet of transition storage tank (19) is connected with the feeder (34) of material conveyor (35), the material outlet of material conveyor (35) is connected with the material inlet of airslide disintegrating mill (36), the material outlet of airslide disintegrating mill (36) utilizes pipeline to be connected with the material inlet of cyclopneumatic separator (37), the bottom of cyclopneumatic separator (37) has material outlet, top at cyclopneumatic separator is provided with upper outlet, described upper outlet utilizes pipeline to be connected with the import of material collector (38), and the top outlet of material collector (38) utilizes pipeline to be connected with the inlet of active carbon degassing tower (16); The material outlet of the material outlet of cyclopneumatic separator (37) bottom and material collector (38) bottom all interconnects with the material inlet that the finished product bull ladle is installed; On described extrusion conveying device (6), vacuum evaporation drying tower (18) and transition storage tank (19), utilize the hydrofuge pipeline (11) and the inlet of gas-filtering device (15) to interconnect respectively; The outlet of gas-filtering device (15) utilizes the inlet of pipeline and described active carbon degassing tower (16) to interconnect.
5. as claim 1 or 4 described full-automatic totally-enclosed continuous material treatment facilities, it is characterized in that: the top at active carbon degassing tower (16) is provided with gas vent, and water tank (28) is set below active carbon degassing tower (16); Described ring type Pneumatic drying device (10) is one and is wound into the device that ring-type forms by pipeline; Outer wall at extrusion conveying device (6) is provided with the electric heater (5) that several are used to heat material in the extrusion conveying device (6).
6. as claim 1 or 4 described full-automatic totally-enclosed continuous material treatment facilities, it is characterized in that: the material outlet at prilling granulator (7) is provided with tubaeform extrusion head (42), the port of export at tubaeform extrusion head (42) is provided with web plate with holes (41), in the outside of web plate with holes (41) movable blade (39) is arranged, described movable blade (39) is installed in the rotating shaft of extrusion conveying device (6).
7. as claim 1 or 4 described full-automatic totally-enclosed continuous material treatment facilities, it is characterized in that: be provided for heating the electric heater (5) of material in the extrusion conveying device (6) at the outer wall of vacuum evaporation drying tower (18), material outlet at vacuum evaporation drying tower (18) utilizes pipeline to be connected with the material inlet of ring type Pneumatic drying device (10), and cold and hot wind apparatus (17) is set on described pipeline.
8. full-automatic totally-enclosed continuous material treatment facility as claimed in claim 5, it is characterized in that: water pump (29) is set in the bottom of water tank (28), the delivery port of described water pump (29) utilizes pipeline to be connected with the import of sand filter (30), the delivery port of sand filter (30) utilizes pipeline to be connected with the water inlet of active carbon filter (31), and the delivery port of active carbon filter (31) utilizes pipeline to be connected with the water inlet of accurate filter (32).
9. as claim 1 or 4 described full-automatic totally-enclosed continuous material treatment facilities, it is characterized in that: blower fan (27) is set on the pipeline that the material inlet with active carbon degassing tower (16) is connected, and the outlet of described blower fan (27) utilizes described pipeline to be communicated with the inlet of described active carbon degassing tower (16).
10. full-automatic totally-enclosed continuous material treatment facility as claimed in claim 5, it is characterized in that: blower fan (27) is set on the pipeline that the material inlet with active carbon degassing tower (16) is connected, and the outlet of described blower fan (27) utilizes described pipeline to be communicated with the inlet of described active carbon degassing tower (16).
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| Application Number | Priority Date | Filing Date | Title |
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| CN2010205421748U CN201807411U (en) | 2010-09-26 | 2010-09-26 | Full-automatic totally-closed continuous material treatment equipment |
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| CN2010205421748U CN201807411U (en) | 2010-09-26 | 2010-09-26 | Full-automatic totally-closed continuous material treatment equipment |
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| CN201807411U true CN201807411U (en) | 2011-04-27 |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101954304A (en) * | 2010-09-26 | 2011-01-26 | 无锡市明洲机械环保设备厂 | Fully-automatic totally-enclosed continuous material handling equipment |
| CN103157532A (en) * | 2013-02-21 | 2013-06-19 | 江苏浦士达环保科技有限公司 | Ball grinding dust removal integrated device |
| CN106422124A (en) * | 2016-09-26 | 2017-02-22 | 济南康和消防技术有限公司 | Dry powder machining process using fire extinguisher dry powder reuse machining system |
-
2010
- 2010-09-26 CN CN2010205421748U patent/CN201807411U/en not_active Expired - Lifetime
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101954304A (en) * | 2010-09-26 | 2011-01-26 | 无锡市明洲机械环保设备厂 | Fully-automatic totally-enclosed continuous material handling equipment |
| CN101954304B (en) * | 2010-09-26 | 2012-01-18 | 无锡市明洲机械环保设备厂 | Fully-automatic totally-enclosed continuous material handling equipment |
| CN103157532A (en) * | 2013-02-21 | 2013-06-19 | 江苏浦士达环保科技有限公司 | Ball grinding dust removal integrated device |
| CN103157532B (en) * | 2013-02-21 | 2015-07-08 | 江苏浦士达环保科技有限公司 | Ball grinding dust removal integrated device |
| CN106422124A (en) * | 2016-09-26 | 2017-02-22 | 济南康和消防技术有限公司 | Dry powder machining process using fire extinguisher dry powder reuse machining system |
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|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20110427 Effective date of abandoning: 20120118 |