CN101003025A - Biconical double impacting flour mill - Google Patents
Biconical double impacting flour mill Download PDFInfo
- Publication number
- CN101003025A CN101003025A CN 200610008424 CN200610008424A CN101003025A CN 101003025 A CN101003025 A CN 101003025A CN 200610008424 CN200610008424 CN 200610008424 CN 200610008424 A CN200610008424 A CN 200610008424A CN 101003025 A CN101003025 A CN 101003025A
- Authority
- CN
- China
- Prior art keywords
- flour mill
- awl
- awl dish
- opposite directions
- speed
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Images
Landscapes
- Crushing And Grinding (AREA)
Abstract
A dual-cone butt-impact pulverizer able to make the raw material to butt-impact with each other in its pulverizing cavity features that said its pulverizing cavity is composed of two truncated hollow cones, which are coaxially butt-arranged and have same rotation speed but different directions and internal guide slots. Its advantages are high effect, and low energy consumption and abrasion.
Description
Affiliated technical field
The present invention relates to a kind of newly-built pulverizing physical model, and develop material superfine powder grinding machine on this basis with big comminution ratio and obvious energy saving effect.
Background technology
Existing high speed impact flour mill has two big classes with regard to its crushing mechanism, promptly the medium type impacts the gentle power type of flour mill and impacts flour mill.
The basic structure that the medium type impacts flour mill is by Motor Drive, utilizes media such as tup, needle bar to directly act on the material particles under high-speed motion, particle is born repeatedly impact between medium and counterattack liner plate and reaches ultra-fine grinding.Such flour mill version is numerous, and is simplified and traditional different, is widely used.For the production superfine powder, must improve medium velocity, but its maximum permission speed usually is subjected to the restriction of member mechanical strength, impact flour mill as disc type, the limit line speed of tup is no more than 120m/s.In addition, also must in case tup or wear liner cause that the gap increases, will cause mill efficiency greatly to descend the clearance control between tup and the counterattack liner plate in the scope of 1~3mm, product fineness be difficult to meet the demands.Flour mill mill efficiency fluctuation is big because the medium type impacts, and component wear is serious, therefore is only applicable to the brittle material of Mohs' hardness below 3 grades, and product fineness generally can reach 20 μ m.
The aerodynamic force type impacts flour mill and uses compressed air as power source, can be transformed into the speed energy to compression by nozzle, and the high velocity air of ejection drives material particles and quickens, and generation collision mutually becomes crushing energy.The most typical at present airflow milling is that axis is intersected in a bit with several nozzle positioned opposite.Material on the material bed under each nozzle aerodynamic force effect, and pulverize with gas, solid fluidization head-on collision.Nozzle often is designed to subsonic speed or supersonic speed curve, and different jet velocities can obtain corresponding product fineness, generally can reach several microns.In addition, owing to use gas as carrier, medium pollutions such as no metal can be guaranteed product purity.Therefore be applicable to the material superfine grinding that high rigidity and strict control are polluted.At present, the major defect that aerodynamic force type flour mill exists is that the energy consumption of material unit mass is very big, usually needs several Baidu, and even several thousand degree electricity could be produced one ton of superfine powder.This is determined by its grinding mechanism.Promptly at first it is a kind of continuous flow pattern to spray formula aerodynamic model, and the energy that passes to material disperses continuously, and concentration class is not enough, and crush efficiency is low.Secondly, the distance between each nozzle polarizes, and is all shorter, and the static particle that is on the material bed will be very difficult with the interior acquisition of the distance flow velocity identical with air-flow in very short time, often is fully not obtain energy as yet just to bump, and influences crushing effect.The part high velocity air sprays counteracting mutually, causes energy dissipation.
Summary of the invention
1. the bipyramid flour mill that liquidates is pulverized physical model
For impact strength deficiency and the component wear that overcomes the existence of existing mechanical medium type impact flour mill seriously causes problems such as contamination of products, reduce simultaneously existing high energy consumption problem again significantly to spray formula airflow milling, the present invention's newly-built " crushing model ", promptly has discrete boundling, quicken synchronously, the pulverizing physical model of the function that liquidates in opposite directions, its feature is as follows:
1.1 discrete boundling
The moving material stream that enters mill chamber is separated into the boundling unit by distributing device, to strengthen all material particles obtain same order from carrier speed.
Existing mechanical shock is ground and to spray formula airflow milling, material is the fluidization continuous distributed on the material bed, can't guarantee the momentum of all material particles from carrier (tup medium or aerodynamic force stream) the identical magnitude of acquisition.
1.2 quicken synchronously
Specific track---spiral of Archimedes is done motion with uniform acceleration to each material particles along one, and material obtains identical speed in the mode of vehicle-mounted type from carrier, its momentum with
ω linear increment (wherein: m-granular mass, r-particle radius of living in, ω-awl dish angular speed).
Existing mechanical shock is ground and to spray formula airflow milling, material particles obtains the speed energy in the air swept mode from carrier, and there are speed difference in material and carrier, and at the same order of magnitude, random is not strong for the momentum of each particle, poor synchronization.
1.3 liquidate in opposite directions
When the boundling unit of all materials is pulverized near the district through quickening to reach, momentum with linear increment reaches extreme value, and discharged suddenly, moment has very strong whipping effect, bumps with the relative velocity that doubles throwing speed with the material particles that comes in opposite directions and impacts and pulverize.
Existing mechanical shock mill and to spray formula airflow milling, material disperses continuously, and concentration is poor, even the part airflow kinetic energy cancels each other, and causes energy waste, and crush efficiency is low.
2 bipyramids liquidate flour mill structural design and performance evaluation
The technical solution adopted for the present invention to solve the technical problems is: empty frustum of a cone in adopting two, hold in opposite directions horizontally disposed grinding chamber greatly.On the angled direction of inner cavity surface and bus abundant stock guide is set.Two awls are to equate rotating speed, the rightabout rotation.Material enters mill chamber by feed arrangement from the conelet end, moves rapidly to big end along deflector chute.Its tangential velocity is strict to be consistent with cone, and momentum is linear increment.When reaching the auger end, with maximum tangential velocity throwing, with material Shu Xiangxiang from opposed circular cone throwing liquidate take place broken.Smashing fineness does not reach before the requirement, can repeatedly collide repeatedly in mill chamber.The grinding time, then can control by mill chamber inner and outer air pressure difference, after satisfying fineness requirement, get rid of from slit between awl.Gap between two awl dishes should guarantee that material has enough big impact energy when liquidating in opposite directions in pulverizing the district, and can smooth and easy discharge.
Beneficial effect of the present invention is summarized as follows:
Performance, feature are relatively
Sequence number | Project | This case | The disk hammer impacts flour mill | To spray formula airflow milling |
1 | Have or not whipping effect (discharging suddenly when energy constantly gathers certain extreme value) | Have | Do not have | Do not have |
2 | The Changing Pattern of particle momentum increment | Linear increment | Irregular | Irregular |
3 | Pulverize in the district, whether each particle has the momentum of same order | Have | Do not have | Do not have |
4 | Material particles from carrier obtain speed form, whether quicken synchronously | Vehicle-mounted type, synchronously, it is poor not have speed | Air swept, asynchronous, there is speed poor | |
5 | The maximum comminution ratio that the single grinding may reach | ≥1000 | 200 | 20 |
6 | The feeding coal fluctuation is to the influence of mill efficiency | Little | Greatly | Little |
7 | Material is to the degree of wear of medium, carrier | Little | Greatly | Little |
8 | Under the condition of identical production capacity, the institutional investment cost | Low | In | High |
9 | The material hardness (Mohs' hardness) that is suitable for | Below 8 grades | Below 3 grades | 10 grades |
10 | The complete machine physical dimension | Little | Greatly | In |
Description of drawings
The invention will be further described below in conjunction with drawings and Examples:
Fig. 1 is vertical section, an embodiment of the invention grinding chamber schematic diagram;
Fig. 2 is the A-A cutaway view among Fig. 1;
Fig. 3 is that material is pulverized physical model;
Fig. 4 is that particle is pulverized relative impact principle figure in the district.
Among the figure: 1-awl dish, the left and right sides is opposed; The 2-stock guide; The 3-feed pipe; The 4-power transmission shaft; 5-grinding district; The 6-material particles quickens track---spiral of Archimedes
Among Fig. 4: m
1, m
2-granular mass; v
t-the velocity of following; v
r-relative velocity; V-particle throwing speed.
The specific embodiment
In Fig. 1, the big end of two awl dishes (1) is opposed in opposite directions, is on the same horizontal axis, and both ends of the surface are parallel, and both gaps are generally several millimeters.The cone angle size designs according to material characteristic, generally gets 60 °~90 °.Present embodiment is 90 °.Two awl dishes are supported on the power transmission shaft (4) separately by spoke, the axle other end by two independently transmission device and drive motors link, rotating speed can be regulated by electrical system.The present embodiment rotating speed is 2950r/min.
The inner surface of awl dish (1) is equipped with the stock guide (2) of sufficient amount, and its effect is that material is separated into the boundling unit, and directing material moves to big end from small end, to obtain and the synchronous movement velocity of awl dish tangential velocity.The material movement track is spiral of Archimedes shown in (6) among Fig. 3, material momentum increment thereon is
ω (in the formula: r-particle moment radius of living in, ω-awl dish angular speed, ω=const).The maximum momentum that particle has when reaching the stock guide end is mR ω (m-granular mass, the big end radius of R-, ω-awl dish angular speed), and is released suddenly in the end, produces whipping effect, has extremely strong impact energy.The about 80m/s of throwing speed of present embodiment material, the relative impact velocity of particle reaches 160m/s, considerably beyond existing machinery impact flour mill limit velocity (<120m/s).Model machine and existing high speed impact grinding machine below in conjunction with this case development give comparison with regard to its economic effect.Wherein:
" this case " is the bipyramid flour mill that liquidates.
" 315ZPS " is the impact grinding of disk hammer.
" AFG630 " is to spray formula airflow milling.
Test material: lime stone (calcite), 2.7T/m
3
Economic indicator relatively
Index | This case | 315ZPS | AFG630 |
The maximum ratio of reduction output of product fineness feeding granularity Kg/h specific energy consumption Kwh/T | d 95=22 μ m, 600 order 15mm 〉=1,000 2,400 12 | d 95=25 μ m, 500 orders, 150 μ m, 100 orders 200 400 75 | d 98=20 μ m, 625 orders, 75 μ m, 300 orders 20 700 380 |
Annotate: the parameter of 315ZPS, AFG630 is all from " the Handbook of Mechanical Processing Technology " of German Alpine company.
Claims (4)
1. flour mill, form by the interior empty frustum of a cone that a pair of structure is identical, it is characterized in that: the big end of two awl dishes is opposed in opposite directions, be in same horizontal axis, rotating speed equates, switched in opposite, and material enters in the awl dish from small end respectively, produce when moving near the big end and liquidate in opposite directions, discharged from two awl dish gaps by comminuting matter.
2. flour mill according to claim 1 is characterized in that: two awl dish inner surfaces are provided with the stock guide of some along generatrix direction, make material be separated into the boundling unit, and move to fire end from small end, during the momentum m that obtains
ω (wherein: m-granular mass, r-particle radius of living in, ω-awl dish angular speed) increases with linearity.
3. according to claim 1 and 2 described flour mills, it is characterized in that: material is a spiral of Archimedes at the movement locus of awl dish inner surface.
4. flour mill according to claim 1 is characterized in that: the gap of two awl dishes should guarantee that material has enough big impact energy when liquidating in opposite directions in pulverizing the district, and can smooth and easy discharge.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 200610008424 CN101003025A (en) | 2006-01-21 | 2006-01-21 | Biconical double impacting flour mill |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 200610008424 CN101003025A (en) | 2006-01-21 | 2006-01-21 | Biconical double impacting flour mill |
Publications (1)
Publication Number | Publication Date |
---|---|
CN101003025A true CN101003025A (en) | 2007-07-25 |
Family
ID=38702537
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN 200610008424 Pending CN101003025A (en) | 2006-01-21 | 2006-01-21 | Biconical double impacting flour mill |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN101003025A (en) |
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102554751A (en) * | 2012-02-25 | 2012-07-11 | 何德裕 | Double-cone reverse-drive surface layer grinder for crushed waste stones of buildings |
CN102989747A (en) * | 2011-12-21 | 2013-03-27 | 何德裕 | Solid construction waste processing and treating system |
CN105833969A (en) * | 2016-05-15 | 2016-08-10 | 苏继忠 | Pulverizer |
CN107266598A (en) * | 2017-05-17 | 2017-10-20 | 宁波拜尔玛生物科技有限公司 | The functional sugar prepared based on nanometer technology and its application in field of medicaments |
CN107790266A (en) * | 2017-11-09 | 2018-03-13 | 成都建筑材料工业设计研究院有限公司 | A kind of roll squeezer cement finish grinding system using entrained particle shaping |
CN112354651A (en) * | 2020-11-16 | 2021-02-12 | 南昌大学 | Jet impact grinding equipment and method for food full-component pulping |
CN113000173A (en) * | 2021-03-29 | 2021-06-22 | 南京工程学院 | Horizontal hydraulic bidirectional hedging high-speed turbulent mill for superhard nano crushing |
CN114887736A (en) * | 2022-06-02 | 2022-08-12 | 江苏百泰制药装备科技有限公司 | Medicament crushing apparatus for preparing superfine biological pharmaceutical powder |
-
2006
- 2006-01-21 CN CN 200610008424 patent/CN101003025A/en active Pending
Cited By (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102989747A (en) * | 2011-12-21 | 2013-03-27 | 何德裕 | Solid construction waste processing and treating system |
CN102989747B (en) * | 2011-12-21 | 2014-09-24 | 何德裕 | Solid construction waste processing and treating system |
CN102554751A (en) * | 2012-02-25 | 2012-07-11 | 何德裕 | Double-cone reverse-drive surface layer grinder for crushed waste stones of buildings |
CN105833969B (en) * | 2016-05-15 | 2018-05-22 | 苏继忠 | A kind of pulverizer |
CN105833969A (en) * | 2016-05-15 | 2016-08-10 | 苏继忠 | Pulverizer |
CN107266598A (en) * | 2017-05-17 | 2017-10-20 | 宁波拜尔玛生物科技有限公司 | The functional sugar prepared based on nanometer technology and its application in field of medicaments |
CN107266598B (en) * | 2017-05-17 | 2020-06-05 | 宁波拜尔玛生物科技有限公司 | Functional sugar prepared based on nanotechnology and application thereof in medical field |
CN107790266A (en) * | 2017-11-09 | 2018-03-13 | 成都建筑材料工业设计研究院有限公司 | A kind of roll squeezer cement finish grinding system using entrained particle shaping |
CN112354651A (en) * | 2020-11-16 | 2021-02-12 | 南昌大学 | Jet impact grinding equipment and method for food full-component pulping |
CN112354651B (en) * | 2020-11-16 | 2022-03-11 | 南昌大学 | Jet impact grinding equipment and method for food full-component pulping |
CN113000173A (en) * | 2021-03-29 | 2021-06-22 | 南京工程学院 | Horizontal hydraulic bidirectional hedging high-speed turbulent mill for superhard nano crushing |
CN113000173B (en) * | 2021-03-29 | 2022-08-05 | 南京工程学院 | Horizontal hydraulic bidirectional hedging high-speed turbulent mill for superhard nano crushing |
CN114887736A (en) * | 2022-06-02 | 2022-08-12 | 江苏百泰制药装备科技有限公司 | Medicament crushing apparatus for preparing superfine biological pharmaceutical powder |
CN114887736B (en) * | 2022-06-02 | 2023-08-25 | 江苏百泰制药装备科技有限公司 | Medicament crushing equipment for preparing superfine biopharmaceutical powder |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN101003025A (en) | Biconical double impacting flour mill | |
CN100484635C (en) | Micronizing impact grinder and the powder processing system thereof | |
CN203355834U (en) | Fluidized bed jet mill for biological pesticide production | |
CN103167912A (en) | Device for micronization of solid materials and its use | |
CN104941769B (en) | A kind of solid material Ginding process and solid material grinder | |
KR20130100986A (en) | Jet mill | |
JPH1170340A (en) | Method and apparatus for fluidized layer/jet grinding | |
CN204448220U (en) | A kind of Cefixime tablets bulk drug air flow crushing device | |
CN202983811U (en) | Device capable of preparing superfine molybdenum disulfide | |
CN105728147B (en) | Counter-impact flow pulverizer structure and pulverizer | |
US7992816B2 (en) | Crushing and milling device | |
CN105833969B (en) | A kind of pulverizer | |
KR20170055831A (en) | Hybrid jettmill | |
CN117258956A (en) | Jet mill | |
CN102441474A (en) | Cyclonic jet mill | |
CN207478753U (en) | A kind of fluidized bed air flow crusher of controllable grain fineness | |
CN201067702Y (en) | Pulse blowing type crushing machine | |
CN202377042U (en) | Mechanical pulverizing machine | |
CN201701997U (en) | Detachable classifier wheel | |
CN115672511A (en) | Superfine grinding system of rhizome class traditional chinese medicine | |
CN202162052U (en) | Vortex kinetic energy airflow flour mill | |
CN204170811U (en) | A kind of novel vapour powder machine | |
CN208146153U (en) | A kind of flywheel and centrifugal bump pulverizer for centrifugal bump pulverizer | |
CN201064724Y (en) | Micro mist impact grinding machine and powder body processing system thereof | |
CN210279412U (en) | Fluidized bed collision type jet mill |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C12 | Rejection of a patent application after its publication | ||
RJ01 | Rejection of invention patent application after publication |