CN206152941U - Broken system of cement clinker - Google Patents
Broken system of cement clinker Download PDFInfo
- Publication number
- CN206152941U CN206152941U CN201621147913.7U CN201621147913U CN206152941U CN 206152941 U CN206152941 U CN 206152941U CN 201621147913 U CN201621147913 U CN 201621147913U CN 206152941 U CN206152941 U CN 206152941U
- Authority
- CN
- China
- Prior art keywords
- roll squeezer
- elevator
- ball mill
- cement
- deduster
- 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.)
- Expired - Fee Related
Links
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P40/00—Technologies relating to the processing of minerals
- Y02P40/10—Production of cement, e.g. improving or optimising the production methods; Cement grinding
Landscapes
- Disintegrating Or Milling (AREA)
- Crushing And Grinding (AREA)
Abstract
Broken system of cement clinker, it relates to a cement manufacture equipment, concretely relates to broken system of cement clinker device. It contains allotment storehouse (1), preceding lifting machine (2), rubber belt conveyor (3), feed bin (4), V -arrangement selection powder machine (5), roll squeezer (6), cyclone (7), roll squeezer dust remover (8), ball mill dust remover (10), ball mill (11), warehouse entry lifting machine (12), air chute (13), finished stock storage (14), it still contains go back to grey conveying line (9) its characterized in that, the dust removal export of roll squeezer dust remover (8) is connected to the one end of going back to grey conveying line (9), return the other end of grey conveying line (9) and connect warehouse entry lifting machine (12). Grinding efficiency influence to the ball mill is very big. Also can make cement grinding system not increase too many input, do not increase the condition of energy consumption under, rely on the existing equipment, cement increase of production 5 just enables 10%. Thereby play the reduction energy consumption, cost -effective huge effect.
Description
Technical field
The utility model is related to a kind of cement manufacture plant, and in particular to a kind of clinker crashing system device.
Background technology
Now overwhelming majority cement production enterprise, in the cement grinding stage, is all using typical technique at present：Manufacture of cement is former
Material, by conveying equipment, delivers to precrushing (or ball breaks machine, or roll squeezer), the material after crushing Jing after proportioning station matches somebody with somebody honest material
Again Jing conveying equipments are delivered in mill, are milled into finished product.
The shortcoming that this technique has, i.e., not using the thin material after precrushing.In fact, material there are about 28% after precrushing
0.08 μm of finish fineness is reached.This partial material reenters mill, carries out repeating grinding, without in all senses, can only increase
Energy consumption, reduces mill grinding efficiency.And this fine powder easily forms ELECTROSTATIC DUST, the mill efficiency shadow to ball mill in mill
Ring very big.
Utility model content
The purpose of this utility model is the defect and deficiency for prior art, there is provided a kind of broken system of clinker
System, it can not increase too many input, in the case of not increasing energy consumption, by existing equipment, can just make cement output increase 5-
10%.So as to play reducing energy consumption, cost-effective great function.
For achieving the above object, the utility model is employed the following technical solutions is：It includes allotment storehouse, front elevator, glue
Band conveyer, feed bin, V-arrangement powder concentrator, roll squeezer, cyclone dust collectors, roll squeezer deduster, ball mill deduster, ball mill, enter
Storehouse elevator, air flume, warehouse for finished product, it also includes back grey transfer pipeline, and one end connection roll squeezer for returning grey transfer pipeline is removed
The dedusting outlet of dirt device, returns the other end connection warehouse-in elevator of grey transfer pipeline；
Described returns the feeding end that grey transfer pipeline is located at the lower end of warehouse-in elevator with warehouse-in elevator junction；
Described roll squeezer deduster adopts high-power blower.
The exhaust air rate that the utility model passes through increasing roll squeezer deduster, strengthens the absorption affinity to fines, so as to improve receipts
Dirt efficiency.Then ash will be returned and directly is directly sent to put in storage in elevator as finished product material and mixed with the supplied materials in mill.Jing roll squeezers
Material after broken has 28% finish fineness for having reached 0.08 μm, even if this partial material only reclaims wherein 1/3rd.
This partial material reenters mill, carries out repeating grinding, without in all senses, increasing energy consumption, reduces grinding machine grinding
Efficiency.And this fine powder easily forms ELECTROSTATIC DUST in mill, affects very big to the mill efficiency of ball mill.Also cement can be made
Grinding system is not increasing too many input, in the case of not increasing energy consumption, by existing equipment, can just make cement output increase 5-
10%.So as to play reducing energy consumption, cost-effective great function.
Description of the drawings
In order to be illustrated more clearly that the utility model embodiment or technical scheme of the prior art, below will be to embodiment
Or the accompanying drawing to be used needed for description of the prior art is briefly described, it should be apparent that, drawings in the following description are only
It is some embodiments of the present utility model, for those of ordinary skill in the art, before creative labor is not paid
Put, can be with according to these other accompanying drawings of accompanying drawings acquisition.
Fig. 1 is structural representation of the present utility model.
Description of reference numerals：Allotment storehouse 1, front elevator 2, rubber conveyer 3, feed bin 4, V-arrangement powder concentrator 5, roll squeezer 6,
Cyclone dust collectors 7, roll squeezer deduster 8, return grey transfer pipeline 9, ball mill deduster 10, ball mill 11, warehouse-in elevator 12,
Air flume 13, warehouse for finished product 14.
Specific embodiment
Referring to shown in Fig. 1, the technical scheme that this specific embodiment is adopted is：
It is by allocating storehouse 1, front elevator 2, rubber conveyer 3, feed bin 4, V-arrangement powder concentrator 5, roll squeezer 6, cyclone dust collectors
7th, roll squeezer deduster 8, time grey transfer pipeline 9, ball mill deduster 10, ball mill 11, warehouse-in elevator 12, air flume
13rd, warehouse for finished product 14 is constituted, and the one end for returning grey transfer pipeline 9 connects the dedusting outlet of roll squeezer deduster 8, returns grey transfer pipeline 9
The other end connection warehouse-in elevator 12；The raw material in allotment storehouse 1 is sent to front elevator 2 and is sent to V-arrangement and selects powder by rubber conveyer 3
Machine 5, what Jing V-arrangements powder concentrator 5 went out is sent to cyclone dust collectors 7 into material, Jing after the unqualified material that V-arrangement powder concentrator 5 goes out is sent to roll squeezer 6
Return to front elevator 2 and be sent to V-arrangement powder concentrator 5 again, then through roll squeezer deduster 8, through the high-power blower of roll squeezer 8
The ash that returns for having reached 0.08 μm is directly sent to into the warehouse-in elevator 12 after air flume 13.
Described returns the pan feeding that grey transfer pipeline 9 is located at the lower end of warehouse-in elevator 12 with warehouse-in elevator 12 junction
End；
Described roll squeezer deduster 8 adopts high-power blower.
The utility model strengthens the absorption affinity to fines, so as to improve receipts by the exhaust air rate of increasing roll squeezer deduster 8
Dirt efficiency.Then ash will be returned and directly is directly sent to put in storage in elevator 12 as finished product material and mixed with the supplied materials in mill.Jing roll-ins
Material after crusher machine has 28% finish fineness for having reached 0.08 μm, though this partial material only reclaim wherein three/
One.
This partial material reenters mill, carries out repeating grinding, without in all senses, increasing energy consumption, reduces grinding machine grinding
Efficiency.And this fine powder easily forms ELECTROSTATIC DUST in mill, affects very big to the mill efficiency of ball mill.Also cement can be made
Grinding system is not increasing too many input, in the case of not increasing energy consumption, by existing equipment, can just make cement output increase 5-
10%.So as to play reducing energy consumption, cost-effective great function.
The above, only to illustrate the technical solution of the utility model and unrestricted, those of ordinary skill in the art couple
Other modifications or equivalent that the technical solution of the utility model is made, without departing from technical solutions of the utility model
Spirit and scope, all should cover in the middle of right of the present utility model.
Claims (3)
1. clinker crushing system, it includes allotment storehouse (1), front elevator (2), rubber conveyer (3), feed bin (4), V-arrangement
Powder concentrator (5), roll squeezer (6), cyclone dust collectors (7), roll squeezer deduster (8), ball mill deduster (10), ball mill
(11), elevator (12), air flume (13), warehouse for finished product (14) are put in storage, it is characterised in that it also includes back grey transfer pipeline
(9) the dedusting outlet of one end connection roll squeezer deduster (8) of grey transfer pipeline (9), is returned, the another of grey transfer pipeline (9) is returned
End connection warehouse-in elevator (12).
2. clinker crushing system according to claim 1, it is characterised in that described to return grey transfer pipeline (9) and enter
Storehouse elevator (12) junction is located at the feeding end of the lower end of warehouse-in elevator (12).
3. clinker crushing system according to claim 1, it is characterised in that described roll squeezer deduster (8) is adopted
High-power blower.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621147913.7U CN206152941U (en) | 2016-10-25 | 2016-10-25 | Broken system of cement clinker |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621147913.7U CN206152941U (en) | 2016-10-25 | 2016-10-25 | Broken system of cement clinker |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206152941U true CN206152941U (en) | 2017-05-10 |
Family
ID=58655605
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621147913.7U Expired - Fee Related CN206152941U (en) | 2016-10-25 | 2016-10-25 | Broken system of cement clinker |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206152941U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107930822A (en) * | 2017-11-13 | 2018-04-20 | 盐城吉达环保设备有限公司 | A kind of more particle diameter cement separation systems |
| CN108114798A (en) * | 2017-11-13 | 2018-06-05 | 盐城吉达环保设备有限公司 | Twin shaft birotor multichannel charging grinding system technique is shared before and after one kind |
| CN108126811A (en) * | 2017-11-13 | 2018-06-08 | 盐城吉达环保设备有限公司 | A kind of iron ore by dry method fine grinding system |
| CN108262131A (en) * | 2017-11-13 | 2018-07-10 | 盐城吉达环保设备有限公司 | A kind of twin shaft Double-rotor powder selector Joint grinding system technique |
-
2016
- 2016-10-25 CN CN201621147913.7U patent/CN206152941U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107930822A (en) * | 2017-11-13 | 2018-04-20 | 盐城吉达环保设备有限公司 | A kind of more particle diameter cement separation systems |
| CN108114798A (en) * | 2017-11-13 | 2018-06-05 | 盐城吉达环保设备有限公司 | Twin shaft birotor multichannel charging grinding system technique is shared before and after one kind |
| CN108126811A (en) * | 2017-11-13 | 2018-06-08 | 盐城吉达环保设备有限公司 | A kind of iron ore by dry method fine grinding system |
| CN108262131A (en) * | 2017-11-13 | 2018-07-10 | 盐城吉达环保设备有限公司 | A kind of twin shaft Double-rotor powder selector Joint grinding system technique |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170510 Termination date: 20181025 |