CN2110518U - Micron disintegrator - Google Patents
Micron disintegrator Download PDFInfo
- Publication number
- CN2110518U CN2110518U CN 91221578 CN91221578U CN2110518U CN 2110518 U CN2110518 U CN 2110518U CN 91221578 CN91221578 CN 91221578 CN 91221578 U CN91221578 U CN 91221578U CN 2110518 U CN2110518 U CN 2110518U
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- roll
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- crushing
- coarse crushing
- cylindrical shell
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Abstract
The utility model belongs to a micron disintegrator for processing dry materials, wet materials, moist materials and sheet-shaped materials, comprising a feed port, a crushing chamber, a discharge port, an electric transmission device and a machine base, wherein, the upper part of the crushing chamber is formed into a coarse crushing part by the feed port 12 and a coarse crushing device 1 fixed on the upper end of the a main shaft 4; the lower part of the crushing chamber is formed into a fine grinding part by a barrel body 10 and a set of rollers 2 provided with special spiral grooves; the outside of the barrel body 10 is provided with a cooling chamber. With small volume, light weight, and large material treating quantity, the utility model is mainly suitable for the micron order crushing and processing of non-metal materials, such as chemical industries, medicines, dyestuffs, pigments, agricultural chemicals, cosmetics, foods, ceramics, etc.
Description
The utility model belongs to a kind of size reduction machinery, micron order pulverizer particularly, the decline pulverizing processing of meter level of dry type, wet type, the profit that is applicable to non-metallic materials such as chemical industry, medicine, dyestuff, pigment, agricultural chemicals, cosmetics, grocery trade, pottery.
As everyone knows, current representative micron order size reduction machinery is an airslide disintegrating mill, as: the NQS-25 airslide disintegrating mill that Zhongnan (South Contral) Pharmacentical Machinery Fectory produces, mainly form by spiral air feeder, charging aperture, pulverizing chamber, discharging opening, support; Operation principle or technical process are compressed air (6~8 kilograms per centimeter that come from compressor
2) by the nozzle with pulverizing chamber or certain angle form high velocity air to material suspended body through scissors, collision and grinding, reach the pulverizing purpose, little venthole on the collet circumference of finished product micro mist in pulverizing chamber is together taken out of through discharging opening by gas and is entered in the bag, its production capacity is 20~25 kilograms/hour, feed size≤3~4 millimeter, accounting for more than 75% of smashing fineness≤5 micron, the largest particles≤50 micron, this machine is pulverized in the industry at micron order and has been made very big contribution, but also there is certain problem, 1, user's reflection in use, the blowback phenomenon takes place owing to the venthole of collet is often stopped up by dust, directly influence operator's physical and mental health, need often cleaning maintenance, also influence operating efficiency; 2, this machine can only be processed siccative, so in using certain limitation is arranged; 3, this machine need be equipped with air compressor machine, so it is big to take working space; 4, working ability relative deficiency.
The purpose of this utility model be overcome above-mentioned weak point and provide that a kind of volume is little, efficient is high, relative working ability is big and micron pulverizer that all can process siccative, wet feed and material moistening.
The purpose of this utility model is achieved in that
Micron pulverizer described in the utility model, form by charging aperture, pulverizing chamber, discharging opening, electric transmission machanism and support, the coarse crushing part is formed by feeding mouth 12 and the coarse crushing device 1 that is fixed in main shaft 4 upper ends in the top that it is characterized in that pulverizing chamber, and the broken part of fine powder is formed by cylindrical shell 10 and one group of roll 2 that has special spiral grooves in the bottom.
Pulverizer described in the utility model is characterized in that the outside of cylindrical shell 10 has the cooling chamber of chuck 3 formations to cool off.
The characteristics of micron pulverizer described in the utility model are that compact conformation, production capacity are big, and maximum 300 kilograms/hour, 10 microns of finish fineness ∠ all can process for siccative, wet feed, material moistening or sheet material.Pulverization principle is that material enters in the pulverization cylinder body after the coarse crushing of coarse crushing device in charging aperture, the roll that one group of band particular channel is arranged in the cylindrical shell, and it is minimum with the gap of barrel, roll is made the air-flow that high speed rotating produces rotation under the gear drive of main shaft, in the future be filled in the groove of roll and the gap of roll and barrel as for the material after the coarse crushing, material continues to be turned round roll crown and the grinding of pulverizing barrel like this, the shearing of revolution roll lead angle and barrel, the impulsive force of moving about between the revolution roll, material itself in the roll spiral grooves reach and barrel between comprehensive function such as extrusion friction and reach the pulverizing purpose, afterwards generated heat because of cylindrical shell rubs, carry out liquid cools so set up chuck formation cooling chamber in the cylindrical shell outside.
Below in conjunction with accompanying drawing the utility model is described in further detail;
Fig. 1 is a structural representation of the present utility model;
Fig. 2 is the intention of executing of the utility model coarse crushing device;
Fig. 3 is the vertical view of the utility model meal device;
Fig. 4 is the schematic diagram of the utility model roll;
Above Fig. 1~Fig. 4 also is a most preferred embodiment of the present utility model;
Sequence number is represented among the figure: meal device 1, roll 2, chuck 3, main shaft 4, gear train assembly 5, discharging opening 6, receiving hopper 7, electric transmission machanism 8, support 9, cylindrical shell 10, material channel 11, charging aperture 12.
Fig. 1 shows the overall structure of pulverizer, the upper end of pulverizer is a taper charging aperture 12, be positioned at the coarse crushing device 1 coaxial upper end of being fixed in main shaft 4 of charging aperture 12, the below that is positioned at charging aperture 12 is a cylindrical shell 10, the outside of cylindrical shell 10 has chuck 3 to constitute cooling chamber so that the water flowing cooling, be positioned at roll 2 that three of cylindrical shell 10 have an identical thread groove on the uniform location-plate that is positioned cylindrical shell 10 two ends of main shaft 4, roll 2 is minimum with the barrel gap of cylindrical shell 10, gear train assembly 5 is all formed by the gear on travelling gear and the main shaft 4 in the lower end of roll 2, the lower end of cylindrical shell 10 is fixed as one by location-plate and support 9, between the receiving hopper 7 of between charging aperture 12 and the cylindrical shell 10 and cylindrical shell 10 and its underpart the material channel 11 that communicates is arranged, there is discharging opening 6 side of receiving hopper 7, its lower end also has blanking port temporary cover closure, the lower end of main shaft 4 is formed electric transmission machanism 8 by belt wheel by belt and motor, belt wheel preferably adopts the polywedge bet wheel, by changing rotating speed and the fineness of different belt wheels to this machine of adjustment; Fig. 2 or Fig. 3 show the dnockout rod that coarse crushing device 1 has three layers of four symmetry;
The bottom land that Fig. 4 shows the spiral grooves of roll 2 is a circular arc, and notch is a rectangle.Its whole working is that motor makes main shaft 4 together with coarse crushing device and roll work high speed rotary motion by electric transmission machanism 8 and gear train assembly 5, material carries out entering in the broken cylindrical shell of fine powder by material channel 11 after the first step coarse crushing under the effect of coarse crushing device 1 by charging aperture 12, under the air-flow effect of the roll that rotates at a high speed, material after the coarse crushing continuously is filled in the groove of roll 2 and the wall gap of roll 2 and cylindrical shell 10, material continues to be turned round the grinding of the roll surface and the barrel of roll 2 like this, shear between the roll lead angle barrel, the impact of moving about between the revolution roll 2, material self in the roll spiral grooves and and barrel between comprehensive function such as extrusion friction and reach the broken fineness of micron order grain, finished product materials enters in the receiving hopper 7 by material channel 11, contain in the bag through discharging opening 6 suctions or the eliminating of receiving hopper lower end blanking port, the logical cooling water of chuck 3 domestic demands in the crushing process is with the temperature rise of control cylindrical shell 10.
One group of performance parameter enumerating most preferred embodiment below sees Table 1
Table 1
Pulverize cylindrical shell | Diameter of phi 160mm material 9Cr18M 0 | ||
Roll (3) | Diameter of phi 64mm material 9Cr18M 0 | ||
Motor | 2.2 rpm kilowatt rotating speed 1000(1500) | ||
Pulley diameters | 50mm/50mm | 75mm/50mm | 100mm/50mm |
Coarse crushing device rotating speed | 1000(1500)rpm | 1500(2250)rpm | 2000(3000)rpm |
Roll rotational speed | 1300(1950)rpm | 1500(2925)rpm | 2600(3900)rpm |
Drop into the material diameter | ≤Φ3mm | ||
Finish fineness | ∠ | ||
Grindability | |||
1~300Kg/h | |||
Appearance and size | 310×540×750(mm) | ||
Machine is heavy | About 100Kg |
The utlity model has following advantage:
1, compact conformation, volume are little, in light weight;
2, grindability is big relatively, the efficient height;
3, adaptability is extensive, all can process for siccative, wet feed, material moistening and sheet material;
4, there are not dust pollution, noise slight;
5, discharge method is flexible, unimpeded.
Claims (2)
1, a kind of micron pulverizer, form by charging aperture, pulverizing chamber, discharging opening, electric transmission machanism and support, the coarse crushing part is formed by feeding mouth 12 and the coarse crushing device 1 that is fixed in main shaft 4 upper ends in the top that it is characterized in that pulverizing chamber, and the broken part of fine powder is formed by cylindrical shell 10 and one group of roll 2 that has special spiral grooves in the bottom.
2, pulverizer according to claim 1 is characterized in that the outside of cylindrical shell 10 has the cooling chamber of chuck 3 formations to cool off.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 91221578 CN2110518U (en) | 1991-08-23 | 1991-08-23 | Micron disintegrator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 91221578 CN2110518U (en) | 1991-08-23 | 1991-08-23 | Micron disintegrator |
Publications (1)
Publication Number | Publication Date |
---|---|
CN2110518U true CN2110518U (en) | 1992-07-22 |
Family
ID=4928551
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN 91221578 Granted CN2110518U (en) | 1991-08-23 | 1991-08-23 | Micron disintegrator |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN2110518U (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN100435958C (en) * | 2007-02-08 | 2008-11-26 | 武汉理工大学 | Inside-outside double-cold impact crusher |
CN103301904A (en) * | 2013-05-30 | 2013-09-18 | 中华人民共和国北海出入境检验检疫局 | Safe and explosion-proof pyrotechnic composition milling device |
CN105735083A (en) * | 2016-02-22 | 2016-07-06 | 三峡大学 | Ground rainwater comprehensive utilization system and rainwater purification method |
CN110315659A (en) * | 2019-07-05 | 2019-10-11 | 郁林斌 | A kind of amino Moulding powder processing and fabricating device |
CN113484083A (en) * | 2021-07-14 | 2021-10-08 | 马世留 | Quick sampling device of food detection breakage degree |
-
1991
- 1991-08-23 CN CN 91221578 patent/CN2110518U/en active Granted
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN100435958C (en) * | 2007-02-08 | 2008-11-26 | 武汉理工大学 | Inside-outside double-cold impact crusher |
CN103301904A (en) * | 2013-05-30 | 2013-09-18 | 中华人民共和国北海出入境检验检疫局 | Safe and explosion-proof pyrotechnic composition milling device |
CN103301904B (en) * | 2013-05-30 | 2015-04-15 | 中华人民共和国北海出入境检验检疫局 | Safe and explosion-proof pyrotechnic composition milling device |
CN105735083A (en) * | 2016-02-22 | 2016-07-06 | 三峡大学 | Ground rainwater comprehensive utilization system and rainwater purification method |
CN110315659A (en) * | 2019-07-05 | 2019-10-11 | 郁林斌 | A kind of amino Moulding powder processing and fabricating device |
CN113484083A (en) * | 2021-07-14 | 2021-10-08 | 马世留 | Quick sampling device of food detection breakage degree |
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Legal Events
Date | Code | Title | Description |
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C06 | Publication | ||
PB01 | Publication | ||
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C19 | Lapse of patent right due to non-payment of the annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |