CN212468244U - Raw material roller press final grinding double-fan system - Google Patents
Raw material roller press final grinding double-fan system Download PDFInfo
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- CN212468244U CN212468244U CN202020894129.2U CN202020894129U CN212468244U CN 212468244 U CN212468244 U CN 212468244U CN 202020894129 U CN202020894129 U CN 202020894129U CN 212468244 U CN212468244 U CN 212468244U
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- powder concentrator
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Abstract
The utility model discloses a raw material roller press final grinding double-fan system, which comprises a kiln tail high-temperature fan and a kiln tail exhaust fan; the air outlet of the kiln tail high-temperature fan is respectively connected with the air inlet of the V-shaped powder concentrator and the air inlet of the kiln tail bag dust collector; the air outlet of the V-shaped powder concentrator is connected with the air inlet of the dynamic powder concentrator; the air outlet of the dynamic powder concentrator is connected with the air inlet of the kiln tail bag dust collector; the air outlet of the kiln tail bag dust collector is connected with the air inlet of a kiln tail exhaust fan; and the air outlet of the kiln tail exhaust fan is connected with the air inlet of the V-shaped powder concentrator and a kiln tail chimney. The utility model discloses cancelled the grinding system circulating fan among the traditional system, simplified the flow, reduced the system resistance, reduced the equipment trouble point, can reduce the capital construction investment effectively, reduce the system power consumption, reduce the plant maintenance work load.
Description
Technical Field
The utility model relates to a raw material grinding and exhaust-gas treatment system especially relate to a raw material roller press finish grinding double fan system.
Background
At present, a raw material roller press final grinding system is a relatively mature grinding process commonly adopted by domestic cement production enterprises, and a raw material roller press final grinding waste gas treatment system in the related technology is generally a three-fan system (a high-temperature fan, a grinding system circulating fan and a kiln tail exhaust fan), and is mainly characterized in that the grinding system is relatively independent of air, the grinding system is specially provided with the grinding system circulating fan, and the interference between the raw material grinding and the waste gas treatment system is relatively small in operation; however, the system has the problems of complex process flow, large floor area, high engineering investment, large quantity of process equipment (multiple fault points), blade dust formation, abrasion, vibration and the like when the circulating fan of the grinding system operates in a high-dust environment.
SUMMERY OF THE UTILITY MODEL
Utility model purpose: the utility model provides a raw meal grinding and exhaust-gas treatment system who only contains the simplified process flow of two fans.
The technical scheme is as follows: the raw material roller press final grinding double-fan system comprises a kiln tail high-temperature fan 13 and a kiln tail exhaust fan 15; the air outlet of the kiln tail high-temperature fan 13 is respectively connected with the air inlet of the V-shaped powder concentrator 05 and the air inlet of the kiln tail bag dust collector 14; the air outlet of the V-shaped powder concentrator 05 is connected with the air inlet of the dynamic powder concentrator 11; the air outlet of the dynamic powder concentrator 11 is connected with the air inlet of the kiln tail bag dust collector 14; the air outlet of the kiln tail bag dust collector 14 is connected with the air inlet of a kiln tail exhaust fan 15; and the air outlet of the kiln tail exhaust fan 15 is connected with the air inlet of the V-shaped powder concentrator 05 and a kiln tail chimney 16.
The air outlet of the dynamic powder concentrator 11 is directly connected with the air inlet of the kiln tail bag dust collector 14, and a circulating fan of a grinding system is omitted, so that the flow can be simplified, the system resistance is reduced, and the equipment fault points are reduced. The air outlet of the kiln tail exhaust fan 15 is connected with the air inlet of the V-shaped powder concentrator 05, so that the mixing proportion of fresh air can be reduced, and the system balance is achieved by adjusting the amount of circulating air.
Further, the system also comprises a first shutter 17 which is arranged on an air inlet pipe of the V-shaped powder concentrator 05 and is used for adjusting the temperature and the air quantity of the air entering the V-shaped powder concentrator 05.
Further, the kiln tail high-temperature fan 13 is connected with an air inlet of the V-shaped powder concentrator 05 through a second louver valve 18 and a hot air pipeline.
Further, the kiln tail high-temperature fan 13 is connected with an air inlet of the kiln tail bag dust collector 14 through a third louver valve 19 and a hot air pipeline.
Further, the system also comprises a fourth louver valve 20 which is arranged on the air inlet pipe of the kiln tail bag dust collector 14 and is used for adjusting the temperature of the waste gas entering the kiln tail bag dust collector 14.
Further, the kiln tail exhaust fan 15 is connected with an air inlet of the V-shaped powder concentrator 05 through a sixth louver valve 22 and a hot air pipeline.
Further, the kiln tail exhaust fan 15 is connected to the kiln tail chimney 16 through a fifth louver valve 21 and a hot air pipeline.
Further, the system also comprises a raw material conveying device connected with the V-shaped powder concentrator 05.
Further, raw materials conveyor includes raw materials conveyer 01, install metal detector 02 on the raw materials conveyer 01, detect that the material that does not satisfy the requirement discharges through three-way valve 03, detect that the material that satisfies the requirement passes through three-way valve 03 and first weight airlock valve 04 and send to V type selection powder machine 05 feed inlet.
Further, the system also comprises a roller press device, wherein the roller press device comprises a first bucket elevator 06, a steady flow bin 07, a pneumatic gate valve 08, a roller press 09 and a second bucket elevator 10; the discharge pipe of the V-shaped powder concentrator 05 is connected to the feed inlet of the first bucket elevator 06; the feed inlet of the steady flow bin 07 is connected with the discharge outlet of the first bucket elevator 06, the discharge outlet of the steady flow bin 07 is connected with the feed inlet of the roller press 09 through a pneumatic gate valve 08, and the discharge outlet of the roller press 09 is connected into the feed inlet of the V-shaped powder concentrator 05 through a second bucket elevator 10; and the dynamic powder concentrator 11 is connected with a feed inlet of the steady flow bin 07 through a second heavy hammer air locking valve 12.
Has the advantages that: the utility model cancels the circulating fan of the grinding system in the traditional system, simplifies the flow, reduces the system resistance, reduces the equipment fault points, can effectively reduce the power consumption of the system and reduce the equipment maintenance workload; meanwhile, the fresh air mixing proportion is reduced, and the system balance of the grinding system is achieved by adjusting the circulating air quantity.
Drawings
Fig. 1 is the structural schematic diagram of the final grinding double-fan system of the roller press.
Detailed Description
The technical solution of the present invention will be further explained with reference to the accompanying drawings and examples.
The concrete technical implementation conditions of the utility model lie in:
1. the raw material roller press final grinding system has the obvious advantage of smaller resistance of a grinding system;
2. at present, a waste heat power generation system is basically configured in the domestic cement clinker production line, the temperature of waste gas at the outlet of a high-temperature fan at the tail of a kiln is lower, the temperature of the waste gas can be adjusted according to the moisture condition of raw materials, and the situation that when a raw material mill runs, the waste gas at the tail of the kiln is completely sent to a raw material grinding system for drying the raw materials can be basically realized, so that the consumption of circulating air and fresh air is reduced as much as;
3. with the rapid development of the centrifugal induced draft fan technology, the performance curve of the induced draft fan can be designed and manufactured according to the actual requirement, so that the high operation efficiency of the kiln tail exhaust fan is ensured to be kept when raw materials are ground;
4. with the development of the bag dust collector technology, the high-concentration bag dust collector is widely applied, and the problems of sealing performance, environmental-friendly emission and the like are well solved.
Based on the 4 points, the circulating fan and the cyclone cylinder of the grinding system are eliminated on the basis of the traditional three-fan system (the high-temperature fan, the circulating fan of the grinding system and the kiln tail exhaust fan), and the system is simplified into a double-fan system (the high-temperature fan and the kiln tail exhaust fan) and has great advantages.
As shown in fig. 1, the raw material roller press final grinding double-fan system has the advantages of simple working flow, less equipment (fewer fault points), small occupied area, small engineering investment, small system resistance (small total installed capacity), less wear and faults of large fans and the like, can effectively reduce capital investment, reduce system power consumption and reduce equipment maintenance workload.
The raw material roller press final grinding double-fan system comprises a roller press final grinding system and a waste gas treatment system, wherein the roller press final grinding system comprises: the device comprises a raw material belt conveyor 01, a metal detector 02, a three-way valve 03, a first heavy hammer air locking valve 04, a V-shaped powder concentrator 05, a first bucket elevator 06, a steady flow bin 07, a pneumatic gate valve 08, a roller press 09, a second bucket elevator 10, a dynamic powder concentrator 11, a second heavy hammer air locking valve 12, a first shutter valve 17 and a second shutter valve 18; the exhaust gas treatment system includes: the kiln tail high-temperature fan 13, the kiln tail bag dust collector 14, the kiln tail exhaust fan 15, the kiln tail chimney 16, the third louver valve 19, the fourth louver valve 20, the fifth louver valve 21 and the sixth louver valve 22.
According to the material flow schematic of fig. 1, feed inlets of a raw material belt conveyor 01, a three-way valve 03, a first heavy hammer air lock valve 04, a V-shaped powder concentrator 05, a first bucket elevator 06, a steady flow bin 07, a pneumatic gate valve 08, a roller press 09, a second bucket elevator 10 and the V-shaped powder concentrator 05 are sequentially connected through a chute; the coarse material outlet of the dynamic powder concentrator 11, the second heavy hammer air locking valve 12 and the feed inlet of the steady flow bin 07 are connected in sequence through a chute.
According to the airflow schematic of fig. 1, a kiln tail high-temperature fan 13, a V-shaped powder concentrator 05, a dynamic powder concentrator 11, a kiln tail bag dust collector 14, a kiln tail exhaust fan 15 and a kiln tail chimney 16 are sequentially connected through a hot air pipeline; the first louver valve 17, the second louver valve 18, the third louver valve 19, the fourth louver valve 20, the fifth louver valve 21 and the sixth louver valve 22 are installed on the hot air pipeline.
When the raw material roller press final grinding double-fan system operates, the roller press final grinding system utilizes waste gas (after being processed and cooled by an SP (SP) furnace) of a preheater as a drying heat source of raw materials, the raw materials which are controlled to be proportioned according to quality requirements pass through a raw material belt conveyor 01, and are output from a discharge hole of the raw material belt conveyor 01 after being detected by a metal detector 02, wherein the metal detector 02 is installed on an intermediate frame of the raw material belt conveyor 01 and is used for detecting iron pieces. The detected unsatisfactory materials are discharged through the three-way valve 03, and the materials meeting the requirements are delivered to the feeding port of the V-shaped powder concentrator 05 through the three-way valve 03 and the air locking of the first heavy hammer air locking valve 04. The material extruded by the roller press 09 is sent to the V-type powder concentrator 05 by the second bucket elevator 10 for primary separation. The large and coarse materials are discharged from a discharge port of the V-shaped powder concentrator 05 and are lifted to the steady flow bin 07 by the first bucket elevator 06, and then are stably fed into the roller press 09 for extrusion and crushing again. The air current discharged outside the air outlet of the V-shaped powder concentrator 05 carries the pulverized material to enter the dynamic powder concentrator 11, the classified coarse material returns to the roller press 09 to be circularly extruded and pulverized, the fine powder meeting the requirements of the raw material is brought into the kiln tail bag dust collector 14 along with the classified air current, after being purified by the kiln tail bag dust collector 14, part of the clean waste gas circulates to the air inlet of the V-shaped powder concentrator 05 through the kiln tail exhaust fan 15 to supplement the classified air current, and the other part of the clean waste gas is discharged into the atmosphere through the kiln tail chimney 16.
When the final grinding double-fan system of the raw material roller press stops operating, waste gas from the firing kiln tail (and/or after being treated by the SP furnace) is discharged through a kiln tail high-temperature fan 13, directly enters a kiln tail bag dust collector 14, is purified through the kiln tail bag dust collector 14, and is discharged into the atmosphere through a kiln tail chimney 16 through a kiln tail exhaust fan 15.
The kiln dust and/or raw materials collected by the kiln tail bag dust collector 14 are conveyed to a raw material homogenizing warehouse or a raw material kiln entering system through a raw material kiln dust conveying device.
And the first shutter 17 is installed on an air inlet air pipe of the V-shaped powder concentrator 05 and used for controlling the fresh air mixing amount of the roller press system so as to adjust the temperature and the air volume of the air entering the V-shaped powder concentrator 05.
And the second louver valve 18 is arranged on a pipeline communicated with an air outlet of the kiln tail high-temperature fan 13 and an air inlet of the V-shaped powder concentrator 05 and is used for controlling the air quantity of the kiln tail high-temperature fan 13 entering the V-shaped powder concentrator 05.
And the third louver valve 19 is arranged on a communicating pipeline which is connected with the kiln tail bag dust collector 14 at the air outlet of the kiln tail high-temperature fan 13 and is used for controlling the air quantity of the kiln tail high-temperature fan 13 entering the kiln tail bag dust collector 14.
The fourth louver valve 20 is installed on the air inlet pipe of the kiln tail bag dust collector 14 and used for adjusting air volume and controlling the amount of cold air mixed into the kiln tail bag dust collector 14 so as to adjust the temperature of the waste gas entering the kiln tail bag dust collector 14.
The fifth louver valve 21 is installed on an air outlet of the kiln tail exhaust fan 15 and a hot air pipeline of the kiln tail chimney 16 and used for controlling the air volume of the exhausted waste gas.
The sixth louver valve 22 is installed on a hot air pipeline between the air outlet of the kiln tail exhaust fan 15 and the air inlet of the V-shaped powder concentrator 05, and is used for controlling air volume, so as to achieve system balance of the final grinding system of the roller press by adjusting the air volume of circulating air.
Claims (10)
1. A raw material roller press final grinding double-fan system is characterized by comprising a kiln tail high-temperature fan (13) and a kiln tail exhaust fan (15); the air outlet of the kiln tail high-temperature fan (13) is respectively connected with the air inlet of the V-shaped powder concentrator (05) and the air inlet of the kiln tail bag dust collector (14); the air outlet of the V-shaped powder concentrator (05) is connected with the air inlet of the dynamic powder concentrator (11); the air outlet of the dynamic powder concentrator (11) is connected with the air inlet of the kiln tail bag dust collector (14); the air outlet of the kiln tail bag dust collector (14) is connected with the air inlet of a kiln tail exhaust fan (15); and the air outlet of the kiln tail exhaust fan (15) is connected with the air inlet of the V-shaped powder concentrator (05) and a kiln tail chimney (16).
2. The raw mill finishing double-fan system according to claim 1, characterized in that the system further comprises a first shutter (17) installed on the air inlet pipe of the V-shaped powder concentrator (05) for adjusting the temperature and air volume of the air fed into the V-shaped powder concentrator (05).
3. The raw meal roller press final grinding double-fan system according to claim 1, wherein the kiln tail high-temperature fan (13) is connected with an air inlet of the V-shaped powder concentrator (05) through a second louver valve (18) and a hot air pipeline.
4. The raw meal roller press final grinding double-fan system according to claim 1, wherein the kiln tail high-temperature fan (13) is connected with a kiln tail bag dust collector (14) through a third louver valve (19) and a hot air pipeline.
5. The raw meal roller press final grinding double-fan system according to claim 1, characterized in that: the system also comprises a fourth louver valve (20) which is arranged on an air inlet pipe of the kiln tail bag dust collector (14) and is used for adjusting the temperature of the waste gas entering the kiln tail bag dust collector (14).
6. The raw meal roller press final grinding double-fan system according to claim 1, wherein the kiln tail exhaust fan (15) is connected with an air inlet of the V-shaped powder concentrator (05) through a sixth louver valve (22) and a hot air pipeline.
7. The raw mill finishing double-fan system according to claim 1, characterized in that the kiln tail exhaust fan (15) is connected to a kiln tail chimney (16) through a fifth louver valve (21) and a hot air pipeline.
8. The raw meal roller press final grinding double-fan system according to claim 1, characterized in that the system further comprises a raw material conveying device connected with the V-shaped powder concentrator (05).
9. The raw meal roller press final grinding double-fan system according to claim 8, wherein the raw meal conveying device comprises a raw meal conveyor (01), a metal detector (02) is mounted on the raw meal conveyor (01), and when the raw meal conveyor detects the materials which do not meet the requirements, the materials are discharged through a three-way valve (03); when detecting the materials meeting the requirements, the materials are sent to a feeding hole of the V-shaped powder concentrator (05) through the three-way valve (03) and the first heavy hammer air locking valve (04).
10. The raw meal roller press final grinding double-fan system according to claim 1, characterized in that the system further comprises a roller press device, wherein the roller press device comprises a first bucket elevator (06), a steady flow bin (07), a pneumatic gate valve (08), a roller press (09) and a second bucket elevator (10); the discharge pipe of the V-shaped powder concentrator (05) is connected to the feed inlet of the first bucket elevator (06); the feed inlet of the steady flow bin (07) is connected with the discharge outlet of the first bucket elevator (06), the discharge outlet of the steady flow bin (07) is connected with the feed inlet of the roller press (09) through a pneumatic gate valve (08), and the discharge outlet of the roller press (09) is connected into the feed inlet of the V-shaped powder concentrator (05) through a second bucket elevator (10) and a chute; and the dynamic powder concentrator (11) is connected with a feed inlet of the steady flow bin (07) through a second heavy hammer air lock valve (12).
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| Application Number | Priority Date | Filing Date | Title |
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| CN202020894129.2U CN212468244U (en) | 2020-05-25 | 2020-05-25 | Raw material roller press final grinding double-fan system |
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| CN202020894129.2U CN212468244U (en) | 2020-05-25 | 2020-05-25 | Raw material roller press final grinding double-fan system |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111569994A (en) * | 2020-05-25 | 2020-08-25 | 中国中材国际工程股份有限公司 | Raw material roller press final grinding double-fan system and rolling method |
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- 2020-05-25 CN CN202020894129.2U patent/CN212468244U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111569994A (en) * | 2020-05-25 | 2020-08-25 | 中国中材国际工程股份有限公司 | Raw material roller press final grinding double-fan system and rolling method |
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