CN206996794U - The grinding system of ball mill and roll squeezer composition - Google Patents
The grinding system of ball mill and roll squeezer composition Download PDFInfo
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- CN206996794U CN206996794U CN201720838452.6U CN201720838452U CN206996794U CN 206996794 U CN206996794 U CN 206996794U CN 201720838452 U CN201720838452 U CN 201720838452U CN 206996794 U CN206996794 U CN 206996794U
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Abstract
The utility model discloses the grinding system that a kind of roll squeezer and ball mill form, the grinding system includes the first elevator, roll-in grinding system and ball milling grinding system, wherein the first elevator is connected with roll-in grinding system and ball milling grinding system respectively, and roll-in grinding system is connected with ball milling grinding system.Roll-in grinding system and ball milling grinding system can be with work in tandems, it can also be connected respectively with the first elevator and carry out separate operaton, another can continue operation when being broken down so as to one in roll-in grinding system and ball milling grinding system, and the operating efficiency of overall grinding system greatly improved.
Description
Technical field
A kind of material grinding system is the utility model is related to, is made up of more particularly, to one kind ball mill and roll squeezer
Grinding system.
Background technology
Currently, the diversification grinding system of roll squeezer and ball mill composition be domestic cement production enterprise generally use compared with
Ripe cement grinding process system.Such a cement industry enterprise degree of recognition is high, have high cement output, steady quality and energy consumption compared with
The advantages of low.
However, compared with other cement grinding process, roll squeezer and ball mill Joint grinding system are by roll squeezer and ball milling
Machine milling equipment tandem working, the problem of number of devices is more, and trouble point is more be present, and the failure of its any appliance can be led
Whole system is caused to stop production.
Utility model content
In order to solve the above technical problems, the utility model proposes the grinding system that a kind of roll squeezer and ball mill form,
The grinding system includes：First elevator, roll-in grinding system and ball milling grinding system, wherein：
The entrance of first elevator is connected to material storage device by pipeline；
Roll-in grinding system is connected with the first elevator, and roll-in grinding system includes：
Current stabilization storehouse, the entrance in current stabilization storehouse are connected to the outlet of the first elevator by pipeline；
Roll squeezer, the entrance of roll squeezer are connected to the outlet in current stabilization storehouse by pipeline；
V-type powder concentrator, the entrance of V-type powder concentrator are connected to the outlet of roll squeezer, and the bottom of V-type powder concentrator by pipeline
Discharging opening is connected to current stabilization storehouse by pipeline；
First powder concentrator, the entrance of the first powder concentrator is connected to the air outlet of V-type powder concentrator by pipeline, and first selects powder
The bottom of machine is connected to current stabilization storehouse with fine powder outlet, coarse powder outlet with coarse powder outlet and the outlet of middle powder, top by pipeline
Entrance, the outlet of middle powder is connected respectively to the entrance and ball milling grinding system in current stabilization storehouse by pipeline；With
Cyclone cylinder, the entrance of cyclone cylinder is connected to fine powder by pipeline and exported, and the outlet at bottom of cyclone cylinder is received with powder
Acquisition means are connected, and
Ball milling grinding system includes：
Ball mill, the entrance of ball mill is connected respectively to the outlet of the first elevator by pipeline and middle powder exports, and ball
The entrance of grinding machine is connected to middle powder by pipeline and exported；
Second powder concentrator, the entrance of the second powder concentrator are connected to the discharging opening of ball mill, and the second powder concentrator by pipeline
Bottom discharge mouth the entrance of ball mill is connected to by pipeline；With
Grinding machine dust-precipitator, the entrance of grinding machine dust-precipitator is connected to the air outlet of the second powder concentrator by pipeline, and grinding machine is received
The outlet at bottom of dirt device is connected to powder collection device by pipeline.
In one embodiment, the first elevator is connected with current stabilization storehouse and ball mill respectively by the first triple valve.
In one embodiment, the outlet of roll squeezer is connected to the entrance of V-type powder concentrator by the second elevator.
In one embodiment, roll-in grinding system also includes：
First circulation blower fan, the entrance of first circulation blower fan are connected to the top exit of cyclone cylinder, and first by pipeline
The outlet of circulating fan is connected to the air inlet of V-type powder concentrator by pipeline；
Roll squeezer dust-precipitator, the entrance of roll squeezer dust-precipitator are connected to the outlet of first circulation blower fan, roll-in by pipeline
The outlet at bottom of machine dust-precipitator is connected to powder collection device by pipeline；With
Second circulation blower fan, second circulation blower fan are connected to roll squeezer dust-precipitator by pipeline, are gathered dust with discharging roll squeezer
Air in device.
In one embodiment, the outlet of middle powder by the second triple valve respectively with the entrance in current stabilization storehouse and the entrance of ball mill
It is connected.
In one embodiment, the outlet of the first elevator is connected to the entrance of ball mill by rubber conveyer.
In one embodiment, ball milling grinding system also includes：
Mill inner ventilation dust-precipitator, the entrance of mill inner ventilation dust-precipitator are connected to the air outlet of ball mill by pipeline, in mill
The bottom discharge mouth of ventilation dust-precipitator is connected to the entrance of the second powder concentrator by pipeline；With
Three-circulation wind machine, three-circulation wind machine are connected to the air outlet of mill inner ventilation dust-precipitator by pipeline, will mill
Gas discharge in interior ventilation dust-precipitator.
In one embodiment, the bottom discharge mouth of the discharging opening of ball mill and mill inner ventilation dust-precipitator carries by the 3rd
The machine of liter is connected to the entrance of the second powder concentrator.
In one embodiment, ball milling grinding system also includes the 4th circulating fan, and the 4th circulating fan is connected to grinding machine
The air outlet of dust-precipitator, the gas in grinding machine dust-precipitator is discharged.
The utility model proposes roll squeezer and ball mill composition grinding system in, roll-in grinding system and ball milling grinding
System can with integration of operation can also separate operaton, when grinding system breaks down wherein, another grinding system is still
It can so run, so as to improve the operational efficiency of overall grinding system, improve yield.
Brief description of the drawings
Fig. 1 is the knot of the grinding system formed according to the ball mill and roll squeezer of one exemplary embodiment of the utility model
Structure schematic diagram.
Embodiment
Illustrative, non-limiting example of the present utility model is described in detail with reference to the accompanying drawings, to new according to this practicality
The grinding system of ball mill and the roll squeezer composition of type is further described.
Reference picture 1, the grinding system formed according to the ball mill of one exemplary embodiment of the utility model and roll squeezer
Including the first elevator 1, roll-in grinding system and ball milling grinding system, wherein the first elevator 1 respectively with roll-in grinding system
It is connected with ball milling grinding system, and roll-in grinding system is connected with ball milling grinding system.So, roll-in grinding system and
Ball milling grinding system can also be connected with work in tandem and be carried out separate operaton with the first elevator 1 respectively, so as in roll-in powder
One in grinding system and ball milling grinding system another can continue operation when breaking down, and overall grinding system greatly improved
The operating efficiency of system.
The entrance of first elevator 1 is connected to material storage device by pipeline, for by the thing in material storage device
Material is lifted and is sent into roll-in grinding system or ball milling grinding system.
Roll-in grinding system is connected with the first elevator 1, and roll-in grinding system includes current stabilization storehouse 3, roll squeezer 4, V
Type powder concentrator 6, the first powder concentrator 7 and cyclone cylinder 8.
The entrance in current stabilization storehouse 3 is connected to the outlet of the first elevator 1 by pipeline.The material of first elevator 1 enters steady
After flowing storehouse 3, the different material particles of particle diameter are well mixed by current stabilization storehouse 3.The entrance of roll squeezer 4 is connected to current stabilization storehouse by pipeline
3 outlet, to receive material from current stabilization storehouse 3 and carry out roll operation.The entrance of V-type powder concentrator 6 is connected to roll-in by pipeline
The outlet of machine 4, and the bottom discharge mouth of V-type powder concentrator 6 is connected to the entrance in current stabilization storehouse 3 by pipeline, V-type powder concentrator 6 goes out
Air port is connected to the entrance of the first powder concentrator 7 by pipeline.In one embodiment, the outlet of roll squeezer 4 passes through the second lifting
Machine 5 is connected to the entrance of V-type powder concentrator 6.The material received out of roll squeezer 4 is dispersed as in V-type powder concentrator 6 as powder,
And wherein the less powder of granularity is larger into the first powder concentrator 7, granularity with air-flow by the air outlet of V-type powder concentrator 6
Powder returns to current stabilization storehouse 3 by the discharging opening of the bottom of V-type powder concentrator 6 and enters roll squeezer 4 with by further roll-in.First choosing
The bottom of powder machine 7 is connected to current stabilization with fine powder outlet, coarse powder outlet with coarse powder outlet and the outlet of middle powder, top by pipeline
The entrance in storehouse 3, middle powder outlet are connected respectively to the entrance and ball milling grinding system in current stabilization storehouse 3 by pipeline.So, through the first choosing
The coarse powder that the particle diameter of the separation of powder machine 7 is larger returns to current stabilization storehouse 3 through coarse powder outlet, and travels further into roll squeezer 4 and carry out further
Grinding；Powder outlet enters current stabilization storehouse 3 and ball milling grinding system at random in the less middle powder warp of particle diameter separated through the first powder concentrator 7
System, to carry out roll-in or ball milling.The entrance of cyclone cylinder 8 by pipeline be connected to fine powder export, and the outlet at bottom of cyclone cylinder 8 with
Powder collection device 21 is connected.The smaller fine powder of particle diameter through the separation of the first powder concentrator 7 enters follow-up cyclone cylinder 8, through rotation
Air duct 8 enters powder collection device 21 after separating and completes grinding operation.So, even if ball milling grinding system breaks down, roll-in
Grinding system still can be with complete independently grinding operation.
Ball milling grinding system includes ball mill 13, the second powder concentrator 15 and grinding machine dust-precipitator 16.
The entrance of ball mill 13 is connected respectively to the outlet and the bottom of the first powder concentrator 7 of the first elevator 1 by pipeline
Middle powder outlet.So, when roll-in grinding system and the equal normal operation of ball milling grinding system, the ball mill in ball milling grinding system
13 export powder in reception from the middle powder of the first powder concentrator 7 in roll-in grinding system, to perform further grinding, realizes joint
Grinding；When roll-in grinding system breaks down, the material transmitted by the first elevator 1 is transferred directly to ball mill by pipeline
13, so as to individually complete the grinding operation of material by ball milling grinding system.In one embodiment, the entrance of ball mill 13 passes through
Rubber conveyer 12 is connected to the outlet of the first elevator 1.The entrance of second powder concentrator 15 is connected to ball mill 13 by pipeline
Discharging opening with the powder after receiving grinding from ball mill 13, and the bottom discharge mouth of the second powder concentrator 15 is connected to by pipeline
The entrance of ball mill 13 by the larger material of particle diameter to return to 13 further grinding of ball mill.The entrance of grinding machine dust-precipitator 16 leads to
The air outlet that pipeline is connected to the second powder concentrator 15 is crossed, and the outlet at bottom of grinding machine dust-precipitator 16 is connected to powder by pipeline and received
Acquisition means 21, for the powder received from the second powder concentrator 15 to be collected into powder collection device 21 and by gas discharge system.
By described above it is recognised that the utility model proposes the grinding system that forms of roll squeezer and ball mill in, when
When roll-in grinding system and the equal normal operation of ball milling grinding system, ball mill 13 in ball milling grinding system is from roll-in grinding system
In the first powder concentrator 7 middle powder outlet receive in powder to perform further grinding, realize combination grinding；When ball milling grinding system
When system breaks down, connection, the connection of the first elevator 1 and ball mill 13 of the first powder concentrator 7 and ball mill 13 are disconnected, individually
Grinding operation is performed using roll-in grinding system；When roll-in grinding system breaks down, the material that is transmitted by the first elevator 1
Ball mill 13 is transferred directly to by pipeline, so as to individually complete the grinding operation of material by ball milling grinding system.So, increase
The availability of system, can greatly improve operating efficiency.
In one embodiment, the first elevator 1 is connected with current stabilization storehouse 3 and ball mill 13 respectively by the first triple valve 2
Connect.So, by controlling the first triple valve 2 to close roll-in grinding system or ball milling grinding system.
In one embodiment, the bottom of the first powder concentrator 7 middle powder outlet by the second triple valve 9 respectively with current stabilization storehouse 3
Entrance be connected with the entrance of ball mill 13, so when the device fails in ball milling grinding system, by close with
The valve that ball mill 13 connects can disable ball milling grinding system.
In one embodiment of the present utility model, roll-in grinding system also includes first circulation blower fan 10, roll squeezer is received
Dirt device 11 and second circulation blower fan 18.The entrance of first circulation blower fan 10 is connected to the top exit of cyclone cylinder 8 by pipeline, and
The outlet of first circulation blower fan 10 is connected to the air inlet of V-type powder concentrator 6 by pipeline.The entrance of roll squeezer dust-precipitator 11 passes through
Pipeline is connected to the outlet of first circulation blower fan 10, and the outlet at bottom of roll squeezer dust-precipitator 11 is connected to powder by pipeline and collected
Device 21.Second circulation blower fan 18 is connected to roll squeezer dust-precipitator 11 by pipeline.So, through the thin of the first powder concentrator 7 separation
After powder enters cyclone cylinder 8, the bottom discharge mouth of cyclone cylinder 8 discharges finished powder, and in the presence of first circulation blower fan 10
The air-flow for carrying powder is discharged from the top exit of cyclone cylinder 8, and fraction returns to V-type powder concentrator 6, partly enters roll squeezer
Dust-precipitator 11 is simultaneously collected in roll squeezer dust-precipitator 11, into roll squeezer dust-precipitator 11 gas then in second circulation blower fan 18
The lower discharge roll squeezer dust-precipitator 11 of effect.
In one embodiment, ball milling grinding system also includes mill inner ventilation dust-precipitator 17 and three-circulation wind machine 19.Mill
The entrance of interior ventilation dust-precipitator 17 is connected to the air outlet of ball mill 13 by pipeline, and the bottom of mill inner ventilation dust-precipitator 17 goes out
Material mouth is connected to the entrance of the 3rd elevator 14 by pipeline.Three-circulation wind machine 19 is connected to mill inner ventilation by pipeline and gathered dust
The air outlet of device 17, the gas in mill inner ventilation dust-precipitator 17 is discharged.Mill inner ventilation dust-precipitator 17 is collecting ball mill
Powder material in the air-flow of 13 discharges, improves utilization of materials.
In one embodiment, the bottom discharge mouth of the discharging opening of ball mill 13 and mill inner ventilation dust-precipitator 17 passes through
Three elevators 14 are connected to the entrance of the second powder concentrator 15.
In one embodiment, ball milling grinding system also includes the 4th circulating fan 20, and the 4th circulating fan 20 is connected to
The air outlet of grinding machine dust-precipitator 16, the gas in grinding machine dust-precipitator 16 is discharged.
Illustrate the work of the grinding system of roll squeezer 4 disclosed in the utility model and the composition of ball mill 13 with reference to Fig. 1
Flow：Material enters the He of current stabilization storehouse 3 at random from outside material storage device by the first elevator 1 and by the first triple valve 2
Rubber conveyer 12；Into current stabilization storehouse 3 material in current stabilization storehouse 3 be well mixed after enter roll squeezer 4, it is complete in roll squeezer 4
Into roll operation；The material that roll-in is completed enters V-type powder concentrator 6 by the second elevator 5, and is disperseed in V-type powder concentrator 6
Into powder；The larger material of particle diameter returns to current stabilization storehouse 3 by the discharging opening of the bottom of V-type powder concentrator 6 and is further returned to roller
Press 4 carries out roll-in again, and the less material of particle diameter enters the first powder concentrator 7 in the presence of air-flow；In the first powder concentrator 7
Interior, the larger powder of particle diameter returns to current stabilization storehouse 3 by the coarse powder outlet of the bottom of the first powder concentrator 7 and is further returned to roll-in
Machine 4 carries out roll-in again, the less powder of particle diameter exported by the middle powder of the bottom of the first powder concentrator 7 and pass through the second triple valve with
Machine enters current stabilization storehouse 3 and ball mill 13, and the smaller powder of particle diameter enters cyclone cylinder 8 by the air outlet of the first powder concentrator 7；Powder
Enter powder collection device 21 from the discharging opening of the bottom of cyclone cylinder 8；The air-flow gone out from the air outlet of cyclone cylinder 8 passes through first
Circulating fan 10 returns to V-type powder concentrator 6, or enters roll squeezer dust-precipitator 11, and the fine powder powder in air-flow is received through roll squeezer
The discharging opening of the bottom of dirt device 11 enters powder collection device 21, and the gas in roll squeezer dust-precipitator 11 is in second circulation blower fan 18
Air outlet discharge through roll squeezer dust-precipitator 11 under effect；Enter ball mill 13 by the first triple valve 2 and the second triple valve 9
Material and powder complete ball milling operation in ball mill 13；The powder discharged from the discharging opening of ball mill 13 enters the 3rd elevator
14 entrance, the powder discharged from the air outlet of ball mill 13 enters dust-precipitator of being divulged information in goal, through dust-precipitator recovery of being divulged information in ball
Powder divulged information out of ball dust-precipitator bottom discharging opening enter the 3rd elevator 14 entrance；Powder enters through the 3rd elevator 14
Enter the second powder concentrator 15, through the second powder concentrator 15, the larger powder of particle diameter returns to from the discharging opening of the bottom of the second powder concentrator 15
Again ball milling, air outlet of the less powder of particle diameter through the second powder concentrator 15 enter grinding machine dust-precipitator 16 to ball mill 13；Through grinding machine
The recovery of dust-precipitator 16, discharging opening of the powder through the bottom of grinding machine dust-precipitator 16 enter powder collection device 21, and grinding machine dust-precipitator
Gas in 16 is discharged in the presence of three-circulation wind machine 19 from the air outlet of grinding machine dust-precipitator 16.When roll-in grinding system and
During the equal normal operation of ball milling grinding system, the first triple valve 2 and the second triple valve 9 are in the state opened；When ball milling grinding
When equipment in system breaks down, close respectively in the first triple valve 2 and the second triple valve 9 with rubber conveyer 12 and ball milling
The switch that machine 13 connects；When the equipment in roll-in grinding system breaks down, close the first triple valve 2 and connected with current stabilization storehouse 3
Switch.
Claims (9)
1. a kind of ball mill and roll squeezer composition grinding system, it is characterised in that the grinding system include the first elevator,
Roll-in grinding system and ball milling grinding system, wherein：
The entrance of first elevator is connected to material storage device by pipeline；
The roll-in grinding system is connected with first elevator, and the roll-in grinding system includes：
Current stabilization storehouse, the entrance in the current stabilization storehouse are connected to the outlet of first elevator by pipeline；
Roll squeezer, the entrance of the roll squeezer are connected to the outlet in the current stabilization storehouse by pipeline；
V-type powder concentrator, the entrance of the V-type powder concentrator is connected to the outlet of the roll squeezer by pipeline, and the V-type selects powder
The bottom discharge mouth of machine is connected to the current stabilization storehouse by pipeline；
First powder concentrator, the entrance of first powder concentrator are connected to the air outlet of the V-type powder concentrator by pipeline, and described
The bottom of first powder concentrator passes through pipeline with coarse powder outlet and the outlet of middle powder, top with fine powder outlet, the coarse powder outlet
The entrance in the current stabilization storehouse is connected to, the middle powder outlet is connected respectively to the entrance in the current stabilization storehouse and the ball by pipeline
Be milled grinding system；With
Cyclone cylinder, the entrance of the cyclone cylinder is connected to the fine powder by pipeline and exported, and the outlet at bottom of the cyclone cylinder
It is connected with powder collection device, and
The ball milling grinding system includes：
Ball mill, the entrance of the ball mill is connected respectively to the outlet of first elevator by pipeline and the middle powder goes out
Mouthful, and the entrance of the ball mill is connected to the middle powder by pipeline and exported；
Second powder concentrator, the entrance of second powder concentrator are connected to the discharging opening of the ball mill, and described by pipeline
The bottom discharge mouth of two powder concentrators is connected to the entrance of the ball mill by pipeline；With
Grinding machine dust-precipitator, the entrance of the grinding machine dust-precipitator are connected to the air outlet of second powder concentrator, and institute by pipeline
The outlet at bottom for stating grinding machine dust-precipitator is connected to powder collection device by pipeline.
2. grinding system according to claim 1, it is characterised in that first elevator is distinguished by the first triple valve
It is connected with the current stabilization storehouse and the ball mill.
3. grinding system according to claim 1, it is characterised in that the outlet of the roll squeezer is connected by the second elevator
It is connected to the entrance of the V-type powder concentrator.
4. grinding system according to claim 1, it is characterised in that the roll-in grinding system also includes：
First circulation blower fan, the entrance of the first circulation blower fan are connected to the top exit of the cyclone cylinder by pipeline, and
The outlet of the first circulation blower fan is connected to the air inlet of the V-type powder concentrator by pipeline；
Roll squeezer dust-precipitator, the entrance of the roll squeezer dust-precipitator are connected to the outlet of the first circulation blower fan by pipeline,
The outlet at bottom of the roll squeezer dust-precipitator is connected to powder collection device by pipeline；With
Second circulation blower fan, the second circulation blower fan are connected to the roll squeezer dust-precipitator by pipeline, to discharge the roller
Air in press dust-precipitator.
5. grinding system according to claim 1, wherein, the middle powder outlet by the second triple valve respectively with it is described steady
The entrance in stream storehouse is connected with the entrance of the ball mill.
6. grinding system according to claim 1, wherein, the outlet of first elevator is connected by rubber conveyer
To the entrance of the ball mill.
7. grinding system according to claim 1, wherein, the ball milling grinding system also includes：
Mill inner ventilation dust-precipitator, the entrance of the mill inner ventilation dust-precipitator are connected to the air outlet of the ball mill by pipeline,
The bottom discharge mouth of the mill inner ventilation dust-precipitator is connected to the entrance of second powder concentrator by pipeline；With
Three-circulation wind machine, the three-circulation wind machine are connected to the air outlet of the mill inner ventilation dust-precipitator by pipeline, with
Gas in the mill inner ventilation dust-precipitator is discharged.
8. grinding system according to claim 7, wherein, the discharging opening of the ball mill and the mill inner ventilation dust-precipitator
Bottom discharge mouth the entrance of second powder concentrator is connected to by the 3rd elevator.
9. grinding system according to claim 1, wherein, the ball milling grinding system also includes the 4th circulating fan, institute
The air outlet that the 4th circulating fan is connected to the grinding machine dust-precipitator is stated, the gas in the grinding machine dust-precipitator is discharged.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720838452.6U CN206996794U (en) | 2017-07-12 | 2017-07-12 | The grinding system of ball mill and roll squeezer composition |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720838452.6U CN206996794U (en) | 2017-07-12 | 2017-07-12 | The grinding system of ball mill and roll squeezer composition |
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| Publication Number | Publication Date |
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| CN206996794U true CN206996794U (en) | 2018-02-13 |
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ID=61452237
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| Application Number | Title | Priority Date | Filing Date |
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| CN201720838452.6U Active CN206996794U (en) | 2017-07-12 | 2017-07-12 | The grinding system of ball mill and roll squeezer composition |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109513515A (en) * | 2019-01-08 | 2019-03-26 | 中建材（合肥）粉体科技装备有限公司 | A kind of system being used to prepare desulfurization mountain flour |
| CN109569853A (en) * | 2019-01-18 | 2019-04-05 | 中材海外工程有限公司 | Combined grinding system composed of ball mill and roller press |
| CN111701698A (en) * | 2020-05-26 | 2020-09-25 | 上海万澄环保科技有限公司 | Cement mill system and automatic optimization control system and method thereof |
-
2017
- 2017-07-12 CN CN201720838452.6U patent/CN206996794U/en active Active
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109513515A (en) * | 2019-01-08 | 2019-03-26 | 中建材（合肥）粉体科技装备有限公司 | A kind of system being used to prepare desulfurization mountain flour |
| CN109513515B (en) * | 2019-01-08 | 2024-06-28 | 中建材（合肥）粉体科技装备有限公司 | System for preparing desulphurized stone powder |
| CN109569853A (en) * | 2019-01-18 | 2019-04-05 | 中材海外工程有限公司 | Combined grinding system composed of ball mill and roller press |
| CN111701698A (en) * | 2020-05-26 | 2020-09-25 | 上海万澄环保科技有限公司 | Cement mill system and automatic optimization control system and method thereof |
| CN111701698B (en) * | 2020-05-26 | 2022-02-22 | 上海万澄环保科技有限公司 | Cement mill system and automatic optimization control system and method thereof |
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Effective date of registration: 20220601 Address after: 100000 room 1201, Ganjiakou building, No. 17, Sanlihe Road, Haidian District, Beijing Patentee after: Sinoma overseas technology development Co.,Ltd. Address before: 100037 floor 12, Ganjiakou building, 17 Sanlihe Road, Haidian District, Beijing Patentee before: SINOMA OVERSEAS DEVELOPMENT CO.,LTD. |
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