CN204079794U - A kind of separate compiling prepares the system of cement - Google Patents
A kind of separate compiling prepares the system of cement Download PDFInfo
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- CN204079794U CN204079794U CN201420543894.4U CN201420543894U CN204079794U CN 204079794 U CN204079794 U CN 204079794U CN 201420543894 U CN201420543894 U CN 201420543894U CN 204079794 U CN204079794 U CN 204079794U
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- 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
Abstract
The utility model relates to the system that a kind of separate compiling prepares cement, comprise Vertical Mill b, lift b, deironing device of pipeline, static rank machine b, dust-precipitator b, exhaust blower b, ball mill, dust-precipitator c, exhaust blower c, also comprise difficult mill class ingredient powder mill apparatus, difficult mill class auxiliary material finished product storing unit and batch mixing homogenization device; Can different grinding systems and equipment be adopted respectively to carry out grinding the auxiliary material (as slag, slag etc.) etc. of cement clinker and difficult mill class, the material after separate compiling obtains qualified product after batch mixing homogenizing.The utility model has the advantages such as grinding pow consumption is low, good product quality when preparing cement.
Description
Technical field
The utility model relates to a kind of cement preparation system, particularly relates to the implementation system that a kind of separate compiling prepares cement.
Background technology
In the production of Cement industry, powder-grinding process is big power consumer.And under the market competition and urgent economizer pressure of fierceness, grinding power-saving technology, conservation measures are constantly brought forth new ideas development.In field of cement preparation, the grinding technology of roller mill particularly Vertical Mill has succeeded and Rapid Popularization.But, under existing milling equipment condition, how to weed out the old and bring forth the new from grinding process, realize further energy-conservation, become current powder-grinding process problem demanding prompt solution.
Current domestic cement grinding mostly adopts combined grinding technique, is about to prepare cement different material used: grog and blended material intergrinding prepare cement.This grinding process, at cement granules gradation adjustment, gives full play to the aspects such as waste residue activity, still there are some problems.
First, the grindability for the different components of pulverizing cement differs greatly, intergrinding after batching, to some difficult mill class materials, as slag, slag etc., its grindability, than cement clinker difference about 30%, certainly leads to selective grinding, causes the size distribution of two class materials in finished product different.The hydration reaction time of cement compares slag, flyash will shift to an earlier date, want to make the hydration reaction time of cement and slag synchronous, just must control their optimum fineness different separately to give full play to their activity, and slag, the hardness of flyash and grindability are compared with cement clinker larger difference, in existing combined grinding technique, if slag, slag does not reach desirable fineness, slag will be caused, slag is crossed thick and can not give full play to its potential hydraulicity, cause the early strength of cement products low, development potentiality is little, slag and slag can not give full play to activity, waste resource, simultaneously, f-CaO in slag also may have an impact to soundness of cement.As reached the desirable fineness of slag, that must cause cement clinker crosses grinding, and make the early strength of cement products large, but development potentiality is little, 28d intensity is low.
Secondly, current cement grinding system adopts the Joint grinding system of roller mill and cement ball mill mostly, makes full use of the advantage of the efficient grinding of roller mill and ball mill superior prod performance.And the mill efficiency of ball mill is low; when difficulty mill class auxiliary material and grog combined grinding; difficult mill class material particles grinding is levigate to being difficult to during certain fineness again; open-circuit grinding system; part difficult-to-grind materials particle productive set is in ball milling; worsen the grinding operating mode of ball mill, and to closed circuit grinding system, increase Ball Mill System circulating load.
Utility model content
Provide for above problem the utility model that a kind of grinding pow consumption is low, the separate compiling of good product quality prepares the system of cement.The auxiliary material (as slag, slag etc.) etc. of cement clinker and difficult mill class can adopt different grinding systems and equipment to carry out grinding by the utility model system respectively, and the material after separate compiling obtains qualified product after batch mixing homogenizing.
The system that a kind of separate compiling prepares cement is provided in order to overcome the above problems the utility model, comprise Vertical Mill b, lift b, deironing device of pipeline, static rank machine b, dust-precipitator b, exhaust blower b, ball mill, dust-precipitator c, exhaust blower c, it is characterized in that: also comprise difficult mill class ingredient powder mill apparatus, difficult mill class auxiliary material finished product storing unit and batch mixing homogenization device.
Described difficulty mill class ingredient powder mill apparatus comprises Vertical Mill a, endless belt conveyor, belt-type tramp iron separator, lift a, static rank machine a, dynamic classification machine, dust-precipitator a, exhaust blower a and transport pipe; Described difficulty mill class auxiliary material finished product storing unit comprises storage vault, high pressure blower a, weigher and transport pipe; Described batch mixing homogenization device comprises combined type mixer, high pressure blower b.
Vertical Mill a11 discharge port is connected with conveyor 12 opening for feed, belt-type tramp iron separator 13 is set above conveyor, conveyor 12 discharge port is connected with lift a14 opening for feed, lift a14 discharge port is connected with static rank machine a15 opening for feed, static rank machine a15 fine powder discharge port is connected with the import of dynamic classification machine a16, static rank machine a15 meal discharge port is connected with Vertical Mill a11 opening for feed, the fine powder discharge port of dynamic classification machine a16 is connected with dust-precipitator a17 entrance, the meal discharge port of dynamic classification machine a16 is connected with Vertical Mill a11 entrance, the waste gas outlet of dust-precipitator a17 is connected with exhaust blower a18 entrance, the opening for feed that discharge port and the difficulty of dust-precipitator a17 grind the storage vault 31 of class auxiliary material finished product storing unit 3 is connected,
The dust-precipitator a17 discharge port that opening for feed and the difficulty of storage vault 31 grind class ingredient powder mill apparatus 1 is connected, storage vault 31 discharge port is connected with weigher 33 opening for feed, storage vault 31 bottom of the reservior is provided with described inflation system, inflation system is by high pressure blower a32 air feed, and weighing balance 33 discharge port is connected with combined type mixer 41 opening for feed of batch mixing homogenization device 4;
The outlet of high pressure blower b42 is connected with combined type mixer 41 inlet mouth;
Combined type mixer 41 opening for feed and ball mill 27, the bag of the described batch mixing homogenization device 4 c28 discharge port that gathers dust is connected.
Grog and gypsum carry out pre-grinding by delivering to Vertical Mill b after designing proportion ingredient, material after pre-grinding is delivered to after deironing device of pipeline deironing through lift b, static rank machine b sorting is delivered to through transport pipe, after sorting, meal returns Vertical Mill b continuation grinding, fine powder is delivered to ball mill after then being collected by dust-precipitator b and is completed last grinding, dust-precipitator b outlet exhaust is discharged through exhaust blower b, compound material mixer delivered to by material after ball mill grinding, grinding of ball grinder tail dusty gas, after dust-precipitator c dedusting, is discharged through exhaust blower c;
After combined type mixer mixing homogenizing, qualified finished cement is namely obtained from weigher difficulty mill class auxiliary material finished product with from the material after ball mill grinding, wherein combined type mixer adopts strength and mechanical composite power batch mixing homogenizing, and mixing homogenizing air is by high pressure blower b air feed.
Described Vertical Mill a and Vertical Mill b is outer circulation Vertical Mill, and Vertical Mill body is not with powder separating machine, and material admission port is arranged on Vertical Mill upper center, and discharge opening is arranged on Vertical Mill side-lower.Material, from the charging of Vertical Mill upper center, from the discharging of Vertical Mill side-lower after grinding, and is connected with the import of static rank machine a and static rank machine b by mechanical transport equipment and pipeline.
As further improvement of the utility model, described Vertical Mill a and Vertical Mill b is the Vertical Mill of adjustable grinding pressure type, when grinding difficulty mill class auxiliary material, adopts high grinding pressure, when clinker grinding, adopts medium grinding pressure.
Described static rank machine a and static rank machine b is high material-gas ratio grading machine.
Described static rank machine a and static rank machine b material-gas ratio are at 4.5 ~ 5.5kg/m
3interior adjustable.
Described static rank machine a inlet duct is merged by hot air duct and cold air duct, in static rank machine, the material of a provides oven dry thermal source; Static rank machine b inlet duct is cold air duct.
Described storage vault bottom of the reservior is provided with inflation system, and rise material in storehouse and help stream and homogenizing, inflation system is by high pressure blower a air feed.
Described combined type mixer adopts strength and mechanical composite power batch mixing homogenizing, and described mixing homogenizing air is by high pressure blower b air feed.
Vertical Mill selected by the utility model is outer circulation Vertical Mill, Vertical Mill body is not with powder separating machine, powder after grinding is by the independent powder selection device arranged of gravity lift technique feeding, this powder separating machine is different from the built-in powder separating machine of Vertical Mill, external the reducing of powder selection device selects powder resistance and part air quantity, the blower fan that powder selection device is arranged below reduces all to some extent on pressure head and air quantity, thus reduces the power consumption of system blower fan used, makes system more energy-conservation.
Beneficial effect:
1, material separate compiling grindability differed greatly prepares cement, is conducive to the grog that makes and difficult mill class auxiliary material all obtains fineness and the size-grade distribution of respective relative ideal as slag, slag etc., gives full play to the lateral reactivity of slag, slag; Avoid the grinding excessively of grog in intergrinding technique simultaneously, each age strength of prepared cement is developed even more ideal, improve grog utilization ratio, reduce grinding pow consumption.
2, adopted by the material that grindability differs greatly different grinding system separate compiling to prepare cement, be more conducive to regulation and control cement size-grade distribution, and can grinding pow consumption be reduced, obtain the finished cement of high-quality.
3, adopt outer circulation Vertical Mill to prepare cement as main milling equipment, can obtain higher mill efficiency, meanwhile, the operating parameterss such as vertical mill grinding pressure can regulate and control according to material grindability feature, are more conducive to realizing that prepared by cement is energy-conservation.Further, powder selection device is placed in outside Vertical Mill body by outer circulation Vertical Mill, goes out grind materials by the airlift of mechanical lifting Substitute For Partial, greatly reduces Vertical Mill body drag losses and mass transport energy consumption, can reach certain energy-saving effect.
4, adopt outer circulation Vertical Mill as main milling equipment, powder selection device is placed in outside Vertical Mill body, and the material going out Vertical Mill is loose shape, can realize good dispersion at static rank machine, thus grading machine can adopt higher material-gas ratio, and its material-gas ratio can at 4.5 ~ 5.5kg/m
3interior adjustable, be conducive to reduction and select powder air quantity, reduce and select powder operation power consumption.
Accompanying drawing explanation
Fig. 1 is process flow diagram of the present utility model.
1-difficulty mill class ingredient powder mill apparatus, 2-chamotte powder mill apparatus, 3-difficulty mill class auxiliary material finished product storing unit, 4-batch mixing homogenization device, 11-Vertical Mill a, 12-endless belt conveyor, 13-belt-type tramp iron separator, 14-lift a, 15-static rank machine a, 16-dynamic classification machine, 17-dust-precipitator a, 18-exhaust blower a, 21-Vertical Mill b, 22-lift b, 23-deironing device of pipeline, 24-static rank machine b, 25-dust-precipitator b, 26-exhaust blower b, 27-ball mill, 28-dust-precipitator c, 29-exhaust blower c, 31-storage vault, 32-high pressure blower a, 33-weigher, 41-combined type mixer, 42-and high pressure blower b.
Embodiment
Below in conjunction with accompanying drawing, the utility model is described in further detail.
As shown in Figure 1, the utility model provides the system that a kind of separate compiling prepares cement, comprises difficult mill class ingredient powder mill apparatus 1, chamotte powder mill apparatus 2, difficult mill class auxiliary material finished product storing unit 3 and batch mixing homogenization device 4;
Described difficulty mill class ingredient powder mill apparatus 1 comprises Vertical Mill a11, endless belt conveyor 12, belt-type tramp iron separator 13, lift a14, static rank machine a15, dynamic classification machine 16, dust-precipitator a17, exhaust blower a18 and transport pipe; Described chamotte powder mill apparatus 2 comprises Vertical Mill b21, lift b22, deironing device of pipeline 23, static rank machine b24, dust-precipitator b25, exhaust blower b26, ball mill 27, dust-precipitator c28, exhaust blower c29; Described difficulty mill class auxiliary material finished product storing unit 3 comprises storage vault 31, high pressure blower a32, weigher 33 and transport pipe; Described batch mixing homogenization device 4 comprises combined type mixer 41, high pressure blower b42;
Vertical Mill a11 discharge port is connected with conveyor 12 opening for feed, belt-type tramp iron separator 13 is set above conveyor, conveyor 12 discharge port is connected with lift a14 opening for feed, lift a14 discharge port is connected with static rank machine a15 opening for feed, static rank machine a15 fine powder discharge port is connected with the import of dynamic classification machine a16, static rank machine a15 meal discharge port is connected with Vertical Mill a11 opening for feed, the fine powder discharge port of dynamic classification machine a16 is connected with dust-precipitator a17 entrance, the meal discharge port of dynamic classification machine a16 is connected with Vertical Mill a11 entrance, the waste gas outlet of dust-precipitator a17 is connected with exhaust blower a18 entrance, the opening for feed that discharge port and the difficulty of dust-precipitator a17 grind the storage vault 31 of class auxiliary material finished product storing unit 3 is connected,
The dust-precipitator a17 discharge port that opening for feed and the difficulty of storage vault 31 grind class ingredient powder mill apparatus 1 is connected, storage vault 31 discharge port is connected with weigher 33 opening for feed, storage vault 31 bottom of the reservior is provided with described inflation system, inflation system is by high pressure blower a32 air feed, and weighing balance 33 discharge port is connected with combined type mixer 41 opening for feed of batch mixing homogenization device 4;
The outlet of high pressure blower b42 is connected with combined type mixer 41 inlet mouth;
Combined type mixer 41 opening for feed and ball mill 27, the bag of the described batch mixing homogenization device 4 c28 discharge port that gathers dust is connected.
As slag in difficult mill class auxiliary material, the materials such as slag first deliver to static rank machine a15 by after design proportion ingredient, after static rank machine a15 tentatively dries sorting, feed Vertical Mill a11 again carry out grinding, endless belt conveyor 12 delivered to by material after Vertical Mill a11 grinding, the belt-type tramp iron separator 13 arranged above it is utilized to remove magnetic substance in material, material is through endless belt conveyor 12, lift a14 and transport pipe are delivered to static rank machine a15 and are carried out roughly selecting classification, after sorting, fine powder feeding dynamic classification machine 16 carries out selected classification, the meal of static rank machine a15 and dynamic classification machine 16 returns Vertical Mill a11 and continues grinding, dynamic classification machine 16 fine powder is after dust-precipitator a17 collects, deliver to storage vault 31 to store, storage vault 31 bottom of the reservior is provided with inflation system, material in storehouse is risen and helps stream and homogenizing, inflation system is by high pressure blower a32 air feed, difficulty mill class auxiliary material finished product in storage vault 31 according to design proportioning after weigher 33 weighs through Cemented filling to combined type mixer 41,
Grog and gypsum etc. carry out pre-grinding by delivering to Vertical Mill b21 after design proportion ingredient, material after pre-grinding is delivered to after deironing device of pipeline 23 deironing through lift b22, static rank machine b24 sorting is delivered to through transport pipe, after sorting, meal returns Vertical Mill b21 continuation grinding, fine powder is delivered to ball mill 27 after then being collected by dust-precipitator b25 and is completed last grinding, dust-precipitator b25 outlet exhaust is discharged through exhaust blower b26, compound material mixer 41 delivered to by material after ball mill 27 grinding, ball mill 27 grinds tail dusty gas after dust-precipitator c28 dedusting, discharges through exhaust blower c29;
From weigher 33 difficulty mill class auxiliary material finished product with to mix after homogenizing through combined type mixer 41 from the material after ball mill 27 grinding and namely obtain qualified finished cement, combined type mixer 41 strength and mechanical composite power batch mixing homogenizing, its mixing homogenizing air is by high pressure blower b42 air feed.
Described Vertical Mill a11 and Vertical Mill b21 is outer circulation Vertical Mill, Vertical Mill body is not with powder separating machine, material, from the charging of Vertical Mill upper center, from the discharging of Vertical Mill side-lower after grinding, and is connected with the import of static rank machine a15 and static rank machine b24 by mechanical transport equipment and pipeline.
Described Vertical Mill a11 and Vertical Mill b21 is the Vertical Mill of adjustable grinding pressure type, when grinding difficulty mill class auxiliary material, adopts high grinding pressure, when clinker grinding, adopts medium grinding pressure.
Described static rank machine a15 and static rank machine b24 is high material-gas ratio grading machine; Described static rank machine a15 and static rank machine b24 material-gas ratio are at 4.5 ~ 5.5kg/m
3interior adjustable.
Described static rank machine a15 inlet duct is merged by hot air duct and cold air duct, in static rank machine, the material of a15 provides oven dry thermal source; Static rank machine b24 inlet duct is cold air duct.
Described storage vault 31 bottom of the reservior is provided with inflation system, and rise material in storehouse and help stream and homogenizing, inflation system is by high pressure blower a32 air feed.
Described combined type mixer 41 adopts strength and mechanical composite power batch mixing homogenizing, and described mixing homogenizing air is by high pressure blower b42 air feed.
Implementation system prepared by cement described in the utility model, the material of different grindability difference can be separated grinding effectively to reduce the material particles occurred in intergrinding and cross thick or meticulous phenomenon, effectively can adjust the size distribution of cement simultaneously, to raising cement quality, it is significant that power consumption prepared by reduction cement.
The foregoing is only preferred embodiment of the present utility model, be not restricted to the utility model, for a person skilled in the art, the utility model can have various modifications and variations.All within spirit of the present utility model and principle, any amendment done, equivalent replacement, improvement etc., all should be included within right of the present utility model.
Claims (5)
1. a separate compiling prepares the system of cement, comprise chamotte powder mill apparatus (2), wherein chamotte powder mill apparatus (2) comprises Vertical Mill b (21), lift b (22), deironing device of pipeline (23), static rank machine b (24), dust-precipitator b (25), exhaust blower b (26), ball mill (27), dust-precipitator c (28), exhaust blower c (29), it is characterized in that: also comprise difficult mill class ingredient powder mill apparatus (1), difficult mill class auxiliary material finished product storing unit (3) and batch mixing homogenization device (4);
Described difficulty mill class ingredient powder mill apparatus (1) comprises Vertical Mill a (11), endless belt conveyor (12), belt-type tramp iron separator (13), lift a (14), static rank machine a (15), dynamic classification machine (16), dust-precipitator a (17), exhaust blower a (18) and transport pipe; Described difficulty mill class auxiliary material finished product storing unit (3) comprises storage vault (31), high pressure blower a (32), weigher (33) and transport pipe; Described batch mixing homogenization device (4) comprises combined type mixer (41), high pressure blower b (42);
Vertical Mill a (11) discharge port is connected with conveyor (12) opening for feed, belt-type tramp iron separator (13) is set above conveyor, conveyor (12) discharge port is connected with lift a (14) opening for feed, lift a (14) discharge port is connected with static rank machine a (15) opening for feed, static rank machine a (15) fine powder discharge port is connected with the import of dynamic classification machine a (16), static rank machine a (15) meal discharge port is connected with Vertical Mill a (11) opening for feed, the fine powder discharge port of dynamic classification machine a (16) is connected with dust-precipitator a (17) entrance, the meal discharge port of dynamic classification machine a (16) is connected with Vertical Mill a (11) entrance, the waste gas outlet of dust-precipitator a (17) is connected with exhaust blower a (18) entrance, the opening for feed that discharge port and the difficulty of dust-precipitator a (17) grind the storage vault (31) of class auxiliary material finished product storing unit (3) is connected,
Dust-precipitator a (17) discharge port that opening for feed and the difficulty of storage vault (31) grind class ingredient powder mill apparatus (1) is connected, storage vault (31) discharge port is connected with weigher (33) opening for feed, storage vault (31) bottom of the reservior is provided with inflation system, inflation system is by high pressure blower a(32) air feed, weighing balance (33) discharge port is connected with combined type mixer (41) opening for feed of batch mixing homogenization device (4);
The outlet of high pressure blower b (42) is connected with combined type mixer (41) inlet mouth;
Combined type mixer (41) opening for feed and ball mill (27), the bag of described batch mixing homogenization device (4) c (28) discharge port that gathers dust is connected.
2. a kind of separate compiling according to claim 1 prepares the system of cement, it is characterized in that, described Vertical Mill a (11) and Vertical Mill b (21) is outer circulation Vertical Mill, Vertical Mill body is not with powder separating machine, material admission port is arranged on Vertical Mill upper center, and discharge opening is arranged on Vertical Mill side-lower.
3. a kind of separate compiling according to claim 1 prepares the system of cement, it is characterized in that, described Vertical Mill a (11) and Vertical Mill b (21) is the Vertical Mill of adjustable grinding pressure type.
4. a kind of separate compiling according to claim 1 and 2 prepares the system of cement, it is characterized in that, described static rank machine a (15) and static rank machine b (24) is high material-gas ratio grading machine.
5. a kind of separate compiling according to claim 1 and 2 prepares the system of cement, it is characterized in that, described static rank machine a (15) inlet duct is merged by hot air duct and cold air duct; Static rank machine b (24) inlet duct is cold air duct.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420543894.4U CN204079794U (en) | 2014-09-19 | 2014-09-19 | A kind of separate compiling prepares the system of cement |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420543894.4U CN204079794U (en) | 2014-09-19 | 2014-09-19 | A kind of separate compiling prepares the system of cement |
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| Publication Number | Publication Date |
|---|---|
| CN204079794U true CN204079794U (en) | 2015-01-07 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420543894.4U Expired - Fee Related CN204079794U (en) | 2014-09-19 | 2014-09-19 | A kind of separate compiling prepares the system of cement |
Country Status (1)
| Country | Link |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104193207A (en) * | 2014-09-19 | 2014-12-10 | 南京凯盛国际工程有限公司 | System for preparing cement through separately grinding |
| CN111729728A (en) * | 2020-07-09 | 2020-10-02 | 天津水泥工业设计研究院有限公司 | Novel dry method white cement raw material preparation device and process |
-
2014
- 2014-09-19 CN CN201420543894.4U patent/CN204079794U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104193207A (en) * | 2014-09-19 | 2014-12-10 | 南京凯盛国际工程有限公司 | System for preparing cement through separately grinding |
| CN104193207B (en) * | 2014-09-19 | 2015-11-18 | 南京凯盛国际工程有限公司 | A kind of separate compiling prepares the device of cement |
| CN111729728A (en) * | 2020-07-09 | 2020-10-02 | 天津水泥工业设计研究院有限公司 | Novel dry method white cement raw material preparation device and process |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150107 Termination date: 20170919 |
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| CF01 | Termination of patent right due to non-payment of annual fee |