CN203577945U - Continuous airtight nitrogen-sealed wet material aftertreatment system - Google Patents
Continuous airtight nitrogen-sealed wet material aftertreatment system Download PDFInfo
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- CN203577945U CN203577945U CN201320691140.9U CN201320691140U CN203577945U CN 203577945 U CN203577945 U CN 203577945U CN 201320691140 U CN201320691140 U CN 201320691140U CN 203577945 U CN203577945 U CN 203577945U
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Abstract
The utility model relates to a continuous airtight nitrogen-sealed wet material aftertreatment system which mainly comprises a centrifugal machine, a storage silo, a disc type drier, a sieving machine, a powder storage silo and a racking machine which are sequentially arranged, wherein a discharge auger is arranged between the storage silo and the disc type dryer, a hot air circulation system is arranged beside the disc type dryer, a crusher is connected in parallel between the sieving machine and the powder storage silo, the hot air circulation system mainly comprises a condenser, a fan and a heater, and nitrogen is always led into the centrifugal machine, the storage silo, the discharge auger, the disc type dryer, the hot air circulation system, a pipe chain machine, the sieving machine, the crusher, the powder storage silo and the racking machine. The continuous airtight nitrogen-sealed wet material aftertreatment system has the advantages that the whole process from material centrifuging to packaging is completed inside equipment without manual operation, and the continuous airtight nitrogen-sealed wet material aftertreatment system is sealed by utilizing nitrogen, thus guaranteeing the sealing of equipment.
Description
Technical field
The utility model relates to a kind of wet stock after-treatment system of continuous airtight nitrogen envelope, and a kind of wet stock is from centrifugal to pack the device that can complete continuously whole process under airtight environment specifically.
Background technology
At present, in existing Chemical Manufacture, for wet stock from centrifugal to packing this part of last handling process, its method conventionally adopting is by manually having transported, such as being dried needing after centrifuge is centrifugal when wet stock, now staff can take out material from centrifuge, and re-use transport trolley and be delivered to drying machine place and be dried, the like.In this whole process, need labour intensity larger, and material is when carried by transport trolley by staff again, transport trolley is open type, so material can be directly exposed in air, likely can cause certain pollution to material, affect the quality of product.In addition, if material web is toxic or can give out penetrating odor, can be to environment around, and also staff works for a long time in such environment, also can cause certain harm to health.
Summary of the invention
The technical problems to be solved in the utility model is to provide a kind of wet stock from the centrifugal wet stock after-treatment system to pack the continuous airtight nitrogen envelope that can complete continuously whole process under airtight environment.
In order to solve the problems of the technologies described above, the technical solution of the utility model is: a kind of wet stock after-treatment system of continuous airtight nitrogen envelope, and its innovative point is: mainly comprise centrifuge, storage bin, pan dryer, screening machine, powder storage warehouse and racking machine;
Described centrifuge, storage bin, pan dryer, screening machine, powder storage warehouse and racking machine set gradually, between storage bin and pan dryer, be also provided with discharging auger, side at pan dryer is also provided with hot air circulating system, between screening machine and powder storage warehouse and be connected to pulverizer;
The bottom discharging opening of described centrifuge is connected with the top charging aperture of storage bin, the bottom discharging opening of storage bin is connected with the charging aperture of discharging auger, the discharging opening of discharging auger is connected with the charging aperture of tray drier, the discharging opening of tray drier by pipe chain machine by mass transport the charging aperture place to screening machine, the bottom discharging opening of screening machine is connected with the charging aperture of powder storage warehouse, the charging aperture of pulverizer is connected with screening machine, the discharging opening of pulverizer is connected with the charging aperture of powder storage silo, in powder storage silo, be provided with paddle, described paddle is driven and is rotated by drive motors, the discharging opening of powder storage warehouse is connected with the charging aperture of racking machine, at the discharging opening place of racking machine, cover has packaging bag,
Described hot air circulating system mainly comprises condenser, blower fan and heater, and described condenser, blower fan and heater set gradually from the exhaust ports of tray drier, and the tail end of heater is connected with the air inlet of tray drier;
Described centrifuge, storage bin, discharging auger, pan dryer have passed into nitrogen in hot air circulating system, screening machine, pulverizer, powder storage warehouse and racking machine always.
The utility model has the advantage of: wet stock from rotary process to packaging process, whole process all completes at device interior, and carried by conveying equipments such as discharging auger, pipe chain machines, without manual operation, greatly reduce hand labor intensity, guarantee the continuous production of material simultaneously, in addition all equipment has all been passed into nitrogen, guaranteed the airtight of equipment.
Accompanying drawing explanation
Fig. 1 is the schematic diagram of the wet stock after-treatment system of continuous airtight nitrogen envelope of the present utility model.
The specific embodiment
Schematic diagram is as shown in Figure 1 known, and the wet stock after-treatment system of continuous airtight nitrogen envelope of the present utility model mainly comprises centrifuge 1, storage bin 2, pan dryer 8, screening machine 12, powder storage warehouse 14 and racking machine 16.
Centrifuge 1, storage bin 2, pan dryer 8, screening machine 12, powder storage warehouse 14 and racking machine 16 set gradually, between storage bin 2 and pan dryer 8, be also provided with discharging auger 4, side at pan dryer 8 is also provided with hot air circulating system, between screening machine 12 and powder storage warehouse 14 and be connected to pulverizer 13.
Hot air circulating system mainly comprises condenser 7, blower fan 10 and heater 9, and condenser 7, blower fan 10 and heater 9 set gradually from the exhaust ports of tray drier 8, and the tail end of heater 9 is connected with the air inlet of tray drier 8.At circulation time, hot blast in tray drier 8 first passes through condenser 7 condensations, solvent gas process condenser 7 condensations in hot blast are reclaimed, again utilize, through the condensed hot blast of condenser 7, by blower fan 10, deliver to again tray drier 8, so circulation, simultaneously because hot blast is after condenser 7 condensations, temperature decreases, therefore at blower fan 10 wind, deliver to before tray drier 8, need to by heater 9, heat again, to reach, deliver to again tray drier 8 after the temperature needing and recycle.
The bottom discharging opening of centrifuge 1 is connected with the top charging aperture of storage bin 2, the bottom discharging opening of storage bin 2 is connected with the charging aperture of discharging auger 4, discharging auger 4 is driven and is turned round by the drive motors A3 that is arranged on discharging auger 4 sides, the discharging opening of discharging auger 4 is connected with the charging aperture of tray drier 8, tray drier 8 is driven and to be turned round by the drive motors B5 that is arranged on tray drier 8 upper ends, the discharging opening of tray drier 8 by pipe chain machine 11 by mass transport the charging aperture place to screening machine 12.
The bottom discharging opening of screening machine 12 is connected with the charging aperture of powder storage warehouse 14, the charging aperture of pulverizer 13 is connected with screening machine 12, the discharging opening of pulverizer 13 is connected with the charging aperture of powder storage silo 14, in powder storage silo 14, be provided with paddle 15, paddle 15 is driven and is rotated by drive motors, the discharging opening of powder storage warehouse 14 is connected with the charging aperture of racking machine 16, and at the discharging opening place of racking machine 16, cover has packaging bag.Screening machine 12 is in screening, the small particles material filtering out directly enters powder storage silo 14, the large granular materials filtering out is introduced into pulverizer 13 and pulverizes and be small particles material, at the material after pulverizer 13 is pulverized, enter again powder storage silo 14, and then stir by the interior paddle 15 of powder storage silo 14, after the material stirring of two kinds of separate sources is mixed, enter again racking machine 16 and carry out packing.
In described centrifuge, storage bin, discharging auger, pan dryer, hot air circulating system, pipe chain machine, screening machine, pulverizer, powder storage warehouse and racking machine, passed into nitrogen always.
Show and described basic principle of the present utility model and principal character and advantage of the present utility model.The technical staff of the industry should understand; the utility model is not restricted to the described embodiments; that in above-described embodiment and description, describes just illustrates principle of the present utility model; do not departing under the prerequisite of the utility model spirit and scope; the utility model also has various changes and modifications, and these changes and improvements all fall within the scope of claimed the utility model.The claimed scope of the utility model is defined by appending claims and equivalent thereof.
Claims (1)
1. a wet stock after-treatment system for continuous airtight nitrogen envelope, is characterized in that: mainly comprise centrifuge, storage bin, pan dryer, screening machine, powder storage warehouse and racking machine;
Described centrifuge, storage bin, pan dryer, screening machine, powder storage warehouse and racking machine set gradually, between storage bin and pan dryer, be also provided with discharging auger, side at pan dryer is also provided with hot air circulating system, between screening machine and powder storage warehouse and be connected to pulverizer;
The bottom discharging opening of described centrifuge is connected with the top charging aperture of storage bin, the bottom discharging opening of storage bin is connected with the charging aperture of discharging auger, the discharging opening of discharging auger is connected with the charging aperture of tray drier, the discharging opening of tray drier by pipe chain machine by mass transport the charging aperture place to screening machine, the bottom discharging opening of screening machine is connected with the charging aperture of powder storage warehouse, the charging aperture of pulverizer is connected with screening machine, the discharging opening of pulverizer is connected with the charging aperture of powder storage silo, in powder storage silo, be provided with paddle, described paddle is driven and is rotated by drive motors, the discharging opening of powder storage warehouse is connected with the charging aperture of racking machine, at the discharging opening place of racking machine, cover has packaging bag,
Described hot air circulating system mainly comprises condenser, blower fan and heater, and described condenser, blower fan and heater set gradually from the exhaust ports of tray drier, and the tail end of heater is connected with the air inlet of tray drier;
In described centrifuge, storage bin, discharging auger, pan dryer, hot air circulating system, pipe chain machine, screening machine, pulverizer, powder storage warehouse and racking machine, passed into nitrogen always.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320691140.9U CN203577945U (en) | 2013-11-05 | 2013-11-05 | Continuous airtight nitrogen-sealed wet material aftertreatment system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320691140.9U CN203577945U (en) | 2013-11-05 | 2013-11-05 | Continuous airtight nitrogen-sealed wet material aftertreatment system |
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| Publication Number | Publication Date |
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| CN203577945U true CN203577945U (en) | 2014-05-07 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201320691140.9U Withdrawn - After Issue CN203577945U (en) | 2013-11-05 | 2013-11-05 | Continuous airtight nitrogen-sealed wet material aftertreatment system |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103551236A (en) * | 2013-11-05 | 2014-02-05 | 江苏宝众宝达药业有限公司 | Continuous airtight nitrogen sealed wet material post-processing system |
| CN110762961A (en) * | 2019-11-26 | 2020-02-07 | 河北云瑞化工设备有限公司 | Anhydrous lithium hydroxide production device and use method thereof |
-
2013
- 2013-11-05 CN CN201320691140.9U patent/CN203577945U/en not_active Withdrawn - After Issue
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103551236A (en) * | 2013-11-05 | 2014-02-05 | 江苏宝众宝达药业有限公司 | Continuous airtight nitrogen sealed wet material post-processing system |
| CN103551236B (en) * | 2013-11-05 | 2015-07-08 | 江苏宝众宝达药业有限公司 | Continuous airtight nitrogen sealed wet material post-processing system |
| CN110762961A (en) * | 2019-11-26 | 2020-02-07 | 河北云瑞化工设备有限公司 | Anhydrous lithium hydroxide production device and use method thereof |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20140507 Effective date of abandoning: 20150708 |
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| RGAV | Abandon patent right to avoid regrant |