CN202010573U - Single-cabin ball mill type cement vertical mill grinding device - Google Patents
Single-cabin ball mill type cement vertical mill grinding device Download PDFInfo
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- CN202010573U CN202010573U CN2011200525872U CN201120052587U CN202010573U CN 202010573 U CN202010573 U CN 202010573U CN 2011200525872 U CN2011200525872 U CN 2011200525872U CN 201120052587 U CN201120052587 U CN 201120052587U CN 202010573 U CN202010573 U CN 202010573U
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- mill
- vertical mill
- cement vertical
- cement
- ball mill
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Abstract
The utility model provides a single-cabin ball mill type cement vertical mill grinding device which mainly replaces a multi-cabin ball mill with a single-cabin finely-grinding ball mill and adds a coarse powder circulating device based on an existing grinding device composed of a cement vertical mill and a ball mill. The coarse powder circulating device is in series connection with a cement vertical mill material-discharging port and a single-cabin ball finely-grinding mill material-feeding port and positioned between the cement vertical mill material-discharging port and the single-cabin ball mill material-feeding port. Large material particles which are discharged by the cement vertical mill are enabled to return to an input end of the cement vertical mill and enter into the cement vertical mill to be ground again, accordingly an outer circulation is formed, and the problem that coarse materials enter into the ball mill is totally resolved. The single-cabin ball mill type cement vertical mill grinding device directly adopts a single-cabin finely-grinding ball mill, enables the flow of raw materials which enter into the cement vertical mill to be stable, resolves the problems of vibration caused by the cement vertical mill and the like, can further improve the grinding efficiency of the cement, lowers the grinding power consumption, is convenient in fine powder particle control, and enables the particle grading of cement products to be good.
Description
Technical field
The utility model relates to and a kind of the clinker crushing grinding of bulk is become the device of finished cement, and the cement grinding device that single storehouse ball mill of particularly a kind of Vertical Mill that has additional the meal EGR and fine grinding cooperatively interacts belongs to cement and pulverizes the field.
Background technology
Traditional cement grinding generally adopts ball mill to carry out grinding, and its grinding mechanism is carried out the fragmentation corase grind for adopting big steel ball to material, and small ball carries out fine grinding to material, and average ball diameter is reduced to the mill tail successively by bistrique.Be generally 2～3 storehouses, for 13 meters long 2 storehouse ball mills, the length in corase grind storehouse is 4 meters, the length in fine grinding storehouse is 9 meters, be provided with partition panel between corase grind storehouse and the fine grinding storehouse, the Coarse Aggregate that prevents to roughly grind in the storehouse advances into the fine grinding storehouse at the fines that is not ground to setting, because corase grind and fine grinding are carried out in machine, can't make two storehouses all be operated in optimum state, seriously have defectives such as the low and power consumption height of mill efficiency.
In order to improve the mill efficiency of ball mill, all adopt the way of pre-grinding now, promptly material is carried out entering ball mill again after preliminary fragmentation is roughly ground and carry out whole grinding, can significantly improve the output of grinding system like this, reduce power consumption.Pre-grinding device commonly used at present is roll squeezer and cement vertical mill.Roll squeezer is because structure problem, and the maintenance inconvenience after the roll wear influences system's operation and is eliminated substantially.Though cement vertical mill has avoided the roll squeezer maintenance difficult, the problem that running rate is low, but but exist the bed of material to be not easy control, and grinding machine is easy to generate vibrations, and the material grain size of output is also inhomogeneous, still need the above long ball grinding machine in 2 storehouses to its carry out elder generation roughly grind after fine grinding again.So still do not accomplish at utmost to bring into play the advantage of two kinds of grinding devices, make mill efficiency still not high, and power consumption increase to some extent because of setting up cement vertical mill.
Summary of the invention
The purpose of this utility model is in order to overcome the weak point of above-mentioned existing cement grinding device, design a kind of advantage that can give full play to cement vertical mill and ball mill, further improve the mill efficiency of cement, reduce single storehouse ball milling formula cement vertical mill grinding device of grinding pow consumption.
Single storehouse of the present utility model ball milling formula cement vertical mill grinding device, mainly be at the existing raw material conveyer belt that comprises, tramp iron separator, cement vertical mill, first elevator, pulverized-coal collector, first dust-precipitator, semi-finished product are carried skewed slot, ball mill, second elevator, second dust-precipitator, on the basis of the grinding device that finished product conveying skewed slot is formed, mainly be that many storehouses ball mill is changed into single storehouse fine grinding ball mill and has additional the meal EGR, described meal EGR is serially connected between cement vertical mill discharging opening and the single storehouse fine grinding ball mill charging aperture, its annexation is: the charging aperture of meal EGR connects with the cement vertical mill discharging opening through first elevator, the fine powder discharging opening of meal EGR is carried skewed slot order storehouse fine grinding ball mill charging aperture through semi-finished product, the meal discharging opening of meal EGR connects the raw material belt conveyor through the current stabilization surge bunker, and the air outlet of meal EGR connects the air inlet of pulverized-coal collector.
Above-mentioned meal EGR is selected dynamic powder concentrator for use.Miscellaneous equipment and annexation thereof are identical with existing apparatus.
Single storehouse of the present utility model ball milling formula cement vertical mill grinding device, owing to have additional the meal EGR, the big pellet of particle of cement vertical mill output can be turned back to the cement vertical mill input enters Vertical Mill and mills once more, form outer circulation, stopped the situation generation that coarse fodder enters ball mill fully, make the ball milling function directly select single storehouse fine grinding ball mill for use, both helped controlling cement quality, can increase substantially cement output again, also can shorten the length of ball mill, its length only is equivalent to the length in the fine grinding storehouse of traditional ball mill, cancel the corase grind storehouse of traditional ball mill, can reduce the load of ball mill significantly and use the drive motors of smaller power instead, total power consumption can not increased considerably because setting up cement vertical mill; The big pellet of diameter because of cement vertical mill output separates in the meal EGR after current stabilization surge bunker and raw material belt conveyor turn back to the cement vertical mill input again, by regulating the output flow of current stabilization surge bunker, just can make the material flow that enters cement vertical mill stable, solve because of the material flow shakiness makes the irregular grinding machine that causes of the bed of material and produced problems such as vibrations; Also the big pellet of exporting owing to cement vertical mill of particle can turn back in the cement vertical mill and mill once more, the fine powder that directly meets finished cement is multiplied, can directly carry skewed slot send into warehouse for finished product through finished product after collecting through pulverized-coal collector and first dust-precipitator again, can further reduce ball mill load again and enhance productivity as finished product.Be a kind of advantage that can give full play to cement vertical mill and ball mill, further improve the mill efficiency of cement, reduce grinding pow consumption, the fine particle regulation and control are convenient, the cement grinding device that the cement products grain composition is good.
Description of drawings
Fig. 1 is a kind of structural representation of single storehouse of the present utility model ball milling formula cement vertical mill grinding device.
Among the figure 1 is the raw material conveyer belt, the 2nd, and current stabilization surge bunker, the 3rd, tramp iron separator, 4 is first elevators, the 5th, and meal EGR, the 6th, cement vertical mill, the 7th, pulverized-coal collector, the 8th, semi-finished product are carried skewed slot, and the 9th, circulating fan, 10 is first dust-precipitators, the 11st, single storehouse fine grinding ball mill, 12 is second dust-precipitators, and 13 is second elevators, the 14th, and finished product is carried skewed slot.Solid line among the figure is the material pipe, and dotted line is an airduct.
The specific embodiment
Accompanying drawing is non-limiting to disclose a specific embodiment of the present utility model, is further described as follows in conjunction with the accompanying drawings.
Single storehouse of the present utility model ball milling formula cement vertical mill grinding device, comprise raw material conveyer belt 1, tramp iron separator 3, cement vertical mill 6, first elevator 4, pulverized-coal collector 7, first dust-precipitator 10, semi-finished product are carried skewed slot 8, single storehouse fine grinding ball mill 11, second elevator 13, second dust-precipitator 12, finished product is carried skewed slot 14, also include meal EGR 5, described meal EGR 5 is serially connected between cement vertical mill 6 discharging openings and single storehouse fine grinding ball mill 11 charging apertures, its annexation is: the charging aperture of meal EGR 5 connects with cement vertical mill 6 discharging openings through first elevator 4, the fine powder discharging opening of meal EGR 5 is carried skewed slot 8 order storehouse fine grinding ball mills 11 charging apertures through semi-finished product, the meal discharging opening of meal EGR 5 connects raw material belt conveyor 1 through current stabilization surge bunker 2, and the air outlet of meal EGR 5 connects the air inlet of pulverized-coal collector 7.Described meal EGR 5 is selected dynamic powder concentrator for use.
Other annexation is same as the prior art, air inlet as pulverized-coal collector 7 also is connected with the air outlet of cement vertical mill 6 and the air outlet of first elevator 4, the discharging opening of pulverized-coal collector 7 is carried skewed slot 8 order storehouse fine grinding ball mills 11 charging apertures through lock feeding device and semi-finished product, the air outlet of pulverized-coal collector 7 is connected with first dust-precipitator, 10 air inlets through circulating fan 9, first dust-precipitator, 10 air outlets are through the air inlet and the outside atmosphere of blower fan water receiving mud Vertical Mill 6, the discharging opening of first dust-precipitator 10 is carried skewed slot 14 through the lock feeding device product that are connected into, single storehouse fine grinding ball mill 11 discharging openings are through connecing the charging aperture that flap valve connects second elevator 13, and the discharging opening of second elevator 13 is connected into product and carries skewed slot 14.The air outlet of single storehouse fine grinding ball mill 11 connects the air inlet that connects second dust-precipitator 12 with the air outlet of second elevator 13, the discharging opening of second dust-precipitator 12 is carried skewed slot 14 through the lock feeding device product that are connected into, in order to remove the irony foreign material, can on raw material conveyer belt 1, be provided with tramp iron separator 3.
Single storehouse of the present utility model ball milling formula cement vertical mill grinding device, can also effectively control the grain composition of cement, make the grain composition of cement more reasonable, because of finished product carries finished product in the skewed slot 14 from three blanking points, be respectively first dust-precipitator 11, second dust-precipitator 12 and second elevator 13, wherein the fine powder of first dust-precipitator, 10 collections by regulating wind-force and the cement vertical mill 6 and meal EGR 5 intakes of circulating fan 9, can make the fine powder specific area be controlled at 400m
2/ kg～450m
2/ kg, 0.08mm tails over less than 1%.The fine powder that second dust-precipitator 12 is collected is regulated its wind-force, can make the fine powder specific area be controlled at 350m
2/ kg～400m
2/ kg, 0.08mm tails over less than 1%.The fine powder that second elevator 13 is carried by regulating single storehouse fine grinding ball mill, can make the fine powder specific area be controlled at 320m
2/ kg～360m
2/ kg, 0.08mm tails over less than 2%.The finished cement material that mixes through the three reaches specific area greater than 320m when arriving the finished cement sampler
2/ kg, 0.08mm tail over the qualified finished product requirement less than 2%.
Claims (2)
1. single storehouse ball milling formula cement vertical mill grinding device, comprise the raw material conveyer belt, tramp iron separator, cement vertical mill, first elevator, pulverized-coal collector, first dust-precipitator, semi-finished product are carried skewed slot, ball mill, second elevator, second dust-precipitator, finished product is carried skewed slot, it is characterized in that described ball mill is single storehouse fine grinding ball mill and has additional the meal EGR, described meal EGR is serially connected between cement vertical mill discharging opening and the single storehouse fine grinding ball mill charging aperture, its annexation is: the charging aperture of meal EGR connects with the cement vertical mill discharging opening through first elevator, the fine powder discharging opening of meal EGR is carried skewed slot order storehouse fine grinding ball mill charging aperture through semi-finished product, the meal discharging opening of meal EGR connects the raw material belt conveyor through the current stabilization surge bunker, and the air outlet of meal EGR connects the air inlet of pulverized-coal collector.
2. single storehouse as claimed in claim 1 ball milling formula cement vertical mill grinding device is characterized in that described meal EGR selects dynamic powder concentrator for use.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011200525872U CN202010573U (en) | 2011-03-02 | 2011-03-02 | Single-cabin ball mill type cement vertical mill grinding device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011200525872U CN202010573U (en) | 2011-03-02 | 2011-03-02 | Single-cabin ball mill type cement vertical mill grinding device |
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| Publication Number | Publication Date |
|---|---|
| CN202010573U true CN202010573U (en) | 2011-10-19 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011200525872U Expired - Lifetime CN202010573U (en) | 2011-03-02 | 2011-03-02 | Single-cabin ball mill type cement vertical mill grinding device |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102179285A (en) * | 2011-03-02 | 2011-09-14 | 江苏羚羊水泥工程技术有限公司 | Single-compartment ball mill type cement vertical mill grinding device |
| CN102950057A (en) * | 2012-11-28 | 2013-03-06 | 四川省川威集团有限公司 | Continuous converting method for mutually converting clinker and slag powder |
| CN103084259A (en) * | 2013-02-27 | 2013-05-08 | 南京凯盛国际工程有限公司 | Outer circulation type vertical mill system |
| CN104668075A (en) * | 2015-03-10 | 2015-06-03 | 江苏飞鹏重型设备有限公司 | Pre-grinding circle-flow grinding system adopting FPP grinder |
| CN107716077A (en) * | 2017-11-02 | 2018-02-23 | 江苏吉能达环境能源科技有限公司 | A kind of multilevel grinding superfine powder production-process systems |
-
2011
- 2011-03-02 CN CN2011200525872U patent/CN202010573U/en not_active Expired - Lifetime
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102179285A (en) * | 2011-03-02 | 2011-09-14 | 江苏羚羊水泥工程技术有限公司 | Single-compartment ball mill type cement vertical mill grinding device |
| CN102950057A (en) * | 2012-11-28 | 2013-03-06 | 四川省川威集团有限公司 | Continuous converting method for mutually converting clinker and slag powder |
| CN103084259A (en) * | 2013-02-27 | 2013-05-08 | 南京凯盛国际工程有限公司 | Outer circulation type vertical mill system |
| CN104668075A (en) * | 2015-03-10 | 2015-06-03 | 江苏飞鹏重型设备有限公司 | Pre-grinding circle-flow grinding system adopting FPP grinder |
| CN107716077A (en) * | 2017-11-02 | 2018-02-23 | 江苏吉能达环境能源科技有限公司 | A kind of multilevel grinding superfine powder production-process systems |
| CN107716077B (en) * | 2017-11-02 | 2023-10-31 | 江苏吉能达环境能源科技有限公司 | Multistage grinding superfine powder production process system |
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|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20111019 |