CN103949320B - Three separate type fine-grinding techniques - Google Patents
Three separate type fine-grinding techniques Download PDFInfo
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- CN103949320B CN103949320B CN201410175663.7A CN201410175663A CN103949320B CN 103949320 B CN103949320 B CN 103949320B CN 201410175663 A CN201410175663 A CN 201410175663A CN 103949320 B CN103949320 B CN 103949320B
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- powder
- coarse powder
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- ball mill
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Abstract
The present invention relates to a kind of three separate type fine-grinding techniques, it is characterized in that: include three separate type Vertical Mills, three separation Vertical Mills have material inlet, promotes and expect that import, fine powder outlet, the outlet of middle coarse powder, mixed powder export;The outlet of middle coarse powder connects ball mill, and ball mill outlet connects lifting material import;Mixed powder outlet connects elevator A, and lift outlet connects to promote expects import.The beneficial effects of the present invention is: first, by selecting powder equipment and Vertical Mill equipment to be combined, saved space;The more important thing is: coarse powder and the sorting unit of coarse powder in adding in three separate Vertical Mill, effectively middle coarse powder and coarse powder can be carried out selecting crude drugs with winnower, it is thus possible to carry out a step provides different following process means, reach saving equipment, reduce cost, the advantage lowering energy consumption.
Description
Technical field
The present invention relates to a kind of fine-grinding technique, it is adaptable to grind high thin material, be particularly suited for double closing
Road grinding produces cement, is a kind of novel hierarchical grinding requiring that height is thin, high-strength, multi items blends material cement
Technique.
Background technology
Energy-saving and emission-reduction are the targets that enterprise is pursued, and produce ultra-fine, high-strength, multi items blending material cement, are existing
For recycling economy and the demand of green building material.
More than the 90% of total power consumption is accounted in broken, the grinding of material.Common milling equipment is ball mill
And vertical grinder, wherein ball mill efficiency is low, and power consumption is high, but it has a unrivaled advantage:
The particle diameter shape of ball mill grinding material is good, the feature that cement characteristics is good;And the advantage body of vertical grinder exists
Mill efficiency is high, and power consumption is low, but its material being ground in the form of sheets, strip, particle diameter shape is bad,
And then cause the of low quality of cement.
In order to save the energy, ensureing product quality, present stage commonly used method is through vertical by coarse fodder simultaneously
Middle coarse powder worn in advance by formula grinding machine, be re-fed into ball mill grinding be fine powder for selecting powder, simultaneously vertical grinder,
Ball mill rear end respectively sets one and selects powder equipment, thus makes equipment investment big, takes up an area more, Er Qiecao
Make link loaded down with trivial details, production can bring some inconvenience.
Summary of the invention
It is an object of the invention to provide a kind of three separate type fine-grinding techniques to make up the deficiency of prior art.
The technical scheme is that three separate type fine-grinding techniques, it is characterized in that:
Including three separation Vertical Mills, three separate have on Vertical Mills material inlet, promote material import, fine powder outlet,
The outlet of middle coarse powder, mixed powder outlet;
The outlet of middle coarse powder connects ball mill, and ball mill outlet connects lifting material import;
Mixed powder outlet connects elevator A, and lift outlet connects to promote expects import.
Optimize, between ball mill and lifting material import, have elevator B.
The beneficial effects of the present invention is: first, powder equipment and Vertical Mill equipment will be selected to be combined, save
Space;The more important thing is: coarse powder and the sorting unit of coarse powder in adding in three separate Vertical Mill, can have
Effect middle coarse powder and coarse powder are carried out selecting crude drugs with winnower, it is thus possible to carry out a step provides different following process means,
Reach saving equipment, reduce cost, the advantage lowering energy consumption.
Accompanying drawing explanation
Fig. 1 is conventional operation schematic diagram.
Fig. 2 is this operation schematic diagram.
Fig. 3 is the structure chart of three separation Vertical Mills.
Fig. 4 is the partial enlarged drawing of Fig. 3.
Detailed description of the invention
Embodiment:
Initial material enters coarse powder mill in grinding assembly 26 from material inlet 25, and the material after coarse powder mill contains
Fine powder, middle coarse powder, coarse powder.The advantage of this step is the advantage utilizing Vertical Mill energy-conservation.
Owing to fine powder, middle coarse powder, coarse powder are in admixture, effective method to be utilized three to be separated:
A small amount of fine powder is directly becoming finished product, middle coarse powder sends into ball mill, the most pre-grinding of coarse powder.
Wherein, the separation of fine powder is relatively simple: air-flow is under blower negative pressure effect, through grinding assembly 26
Air inlet 24, vane enter in it, and carry fine powder all the way up, until entering into from product channel 8
Product catcher.The assorting room of above-mentioned fine powder patent in our prior201320198571.1Have detailed
Describe.
Technology before, for middle coarse powder and coarse powder, just cannot realize efficiently separating, and can only be by mixed
Compound all sends into ball mill, then arranges powder concentrator after ball mill, the most substantially makes ball mill hold
Carry on a shoulder pole part pre-grinding task, add energy consumption;On the other hand, the powder concentrator that ball mill is disposed behind,
Increase equipment investment and operating cost.
In this application, just can effectively realize separating by middle coarse powder and coarse powder, thus reach the purpose set,
Details are provided below:
Middle coarse powder after pre-grinding and the mixed powder of coarse powder, the mixed powder outlet 23 entrance elevator from bottom
In A27 more elevated, from promote material import 100 enter in body 1, enter through spreading grading wheel 4
Shed after entering spreading groove box 18, fallen.
When mixed powder enters into the whereabouts of the annular of the material of the taper being made up of reflection circle 12 and drip circle 10
After mouth 101, continue to fall, due to the upright projection position on baffle liner 11 top, setting in whereabouts mouth 101
Outside, so, whole mixed powders all can fall in baffle liner 11.
Herein, from whereabouts mouth 101 to this segment space of baffle liner 11, it is simply that our sorting mouth 102.
Air-flow through grinding assembly 26 upwards, rolled over by the reflection circle 12 arranged through spreader 13 and declivity
Returning, the mixed powder that blows to obliquely to fall (after adjusting parameter, blowing mode obliquely, is
Good energy efficient, selects the mode that powder effect is best), coarse powder continues to fall, and drops in baffle liner 11
Coarse powder droping space 103, enters back into grinding assembly 26, carries out the most pre-grinding;Middle coarse powder is blown to water conservancy diversion
The outer space of circle 11, owing to this space is relatively big, wind speed slows down rapidly, and middle coarse powder can not continue to go up with the wind
Raise, and settle, fall into middle coarse powder droping space 104, more therefrom body 1 is left in coarse powder outlet 7,
Deliver to ball mill 28 and carry out levigation mill.
The powder of ball mill 28 milled, then by elevator B105, enter body 1 from promoting material import 100
In, a large amount of fine powders wherein contained are carried by wind and upwards select, and a small amount of middle fine powder falls again to be selected.
As seen from the above, this technique substantially saves on expense and the energy consumption of a powder concentrator.
Claims (1)
1. three separate type fine-grinding technique, is characterized in that:
Including three separate type Vertical Mills, three separate type Vertical Mills have material inlet, promote material import, fine powder outlet, in
Coarse powder outlet, mixed powder outlet;
The outlet of middle coarse powder connects ball mill, and ball mill outlet connects lifting material import;
Mixed powder outlet connects elevator A, elevator A outlet and connects lifting material import, and mixed powder is in three separate types
Coarse powder and middle coarse powder it is divided in Vertical Mill;
Elevator B is had between ball mill outlet and lifting material import.
Priority Applications (1)
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CN201410175663.7A CN103949320B (en) | 2014-04-29 | 2014-04-29 | Three separate type fine-grinding techniques |
Applications Claiming Priority (1)
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CN201410175663.7A CN103949320B (en) | 2014-04-29 | 2014-04-29 | Three separate type fine-grinding techniques |
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CN103949320A CN103949320A (en) | 2014-07-30 |
CN103949320B true CN103949320B (en) | 2016-10-12 |
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Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
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CN105498927B (en) * | 2015-12-15 | 2019-05-21 | 莱歇研磨机械制造(上海)有限公司 | A kind of half whole formula grinding system |
CN106238188B (en) * | 2016-08-31 | 2019-04-09 | 宜宾市天顺建材集团股份有限公司 | Respective grinding process at times |
CN107570302A (en) * | 2017-07-13 | 2018-01-12 | 北方重工集团有限公司 | A kind of portable grinding station system and technique |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0801987A2 (en) * | 1996-04-18 | 1997-10-22 | Kawasaki Jukogyo Kabushiki Kaisha | Cement clinker grinding apparatus using vertical roller mill and its method |
JP2004188368A (en) * | 2002-12-13 | 2004-07-08 | Ube Machinery Corporation Ltd | Grinding method |
CN202137014U (en) * | 2011-05-15 | 2012-02-08 | 盐城吉达环保设备有限公司 | Outer circulation deironing grinding equipment |
CN102784690A (en) * | 2011-05-15 | 2012-11-21 | 盐城吉达环保设备有限公司 | External-circulation iron-removing grinding technology |
CN102784702A (en) * | 2011-05-15 | 2012-11-21 | 盐城吉达机械制造有限公司 | Parallelly-connected grinding technology and equipment thereof |
-
2014
- 2014-04-29 CN CN201410175663.7A patent/CN103949320B/en active Active
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0801987A2 (en) * | 1996-04-18 | 1997-10-22 | Kawasaki Jukogyo Kabushiki Kaisha | Cement clinker grinding apparatus using vertical roller mill and its method |
JP2004188368A (en) * | 2002-12-13 | 2004-07-08 | Ube Machinery Corporation Ltd | Grinding method |
CN202137014U (en) * | 2011-05-15 | 2012-02-08 | 盐城吉达环保设备有限公司 | Outer circulation deironing grinding equipment |
CN102784690A (en) * | 2011-05-15 | 2012-11-21 | 盐城吉达环保设备有限公司 | External-circulation iron-removing grinding technology |
CN102784702A (en) * | 2011-05-15 | 2012-11-21 | 盐城吉达机械制造有限公司 | Parallelly-connected grinding technology and equipment thereof |
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Address after: 645152 group 1, moding village, Yuejiang Town, Gaoxian County, Yibin City, Sichuan Province Co-patentee after: Luo Hejian Patentee after: YIBIN TIANSHUN BUILDING MATERIAL GROUP STOCK Co.,Ltd. Address before: 644000 Yibin City High County of Sichuan Province Yue Jiang Zhen Co-patentee before: Luo Hejian Patentee before: GAOXIAN TIANSHUN BUILDING MATERIALS Co.,Ltd. |
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