CN202961947U - Chemical drying device - Google Patents
Chemical drying device Download PDFInfo
- Publication number
- CN202961947U CN202961947U CN 201220651776 CN201220651776U CN202961947U CN 202961947 U CN202961947 U CN 202961947U CN 201220651776 CN201220651776 CN 201220651776 CN 201220651776 U CN201220651776 U CN 201220651776U CN 202961947 U CN202961947 U CN 202961947U
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- drying
- bucket
- controller
- drying crystalline
- tower
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Abstract
The utility model relates to the technical field of drying equipment and particularly relates to a chemical drying device. The chemical drying device comprises a drying and crystallizing barrel, a material generation tower and a drying tower, wherein an outlet of the material generation tower is communicated with a feeding opening of the drying and crystallizing barrel; a discharge opening of the drying and crystallizing barrel is communicated with the drying tower through a pipeline; a material is fed into the material generation tower, so that the material is uniformly and continuously delivered into a material crystallizing barrel under the own gravity of the material; the chemical drying device has the advantages of continuous drying, uniform drying time and uniform crystallizing time; the quality of a product can be ensured; in addition, the chemical drying device further comprises a controller; a position sensor is arranged inside the drying and crystallizing barrel; a feeding electromagnetic valve is arranged at the position of an outlet of the material generation tower; the position sensor and the feeding electromagnetic valve are respectively and electrically connected with the controller; a material level in the drying and crystallizing barrel can be sensed by using the position sensor and is fed back to the controller; and the feeding electromagnetic valve is controlled to be turned on or off through the controller. Therefore, the chemical drying device can be used for automatically feeding; the working efficiency is high; and the labor is saved.
Description
Technical field:
The utility model relates to the drying equipment technical field, refers in particular to dryer for chemical industry.
Background technology:
The method of existing dry chemical material is that material is directly joined in the drying crystalline bucket, is that the material that material is joined of clearance-type joins in the drying crystalline bucket.Determine that the drying crystalline time is to obtain by the material level in the crystallizing tank that sees drying estimation, cause the drying time of material unstable, exist dry not in place, the phenomenon such as moisture content is inhomogeneous in dry run, thus the product rate such as reduction and affect end product quality.
The utility model content:
The purpose of this utility model is exactly the deficiency that exists for prior art and the needs of the continuous drying that a kind of assurance satisfies material and the dryer for chemical industry that drying time is even, drying effect is good are provided.
To achieve these goals, the technical solution adopted in the utility model is: dryer for chemical industry, include the drying crystalline bucket, drying crystalline bucket top is provided with the raw material tower, drying crystalline bucket below is provided with drying tower, and drying crystalline bucket top is provided with charging aperture, and the outlet of raw material tower passes in the charging aperture of drying crystalline bucket, the drying crystalline bottom of the barrel is provided with discharging opening, and the discharging opening of drying crystalline bucket is communicated with drying tower by tilted tube; Also include controller, be provided with the position sensor that the inductor material level is put in the drying crystalline bucket, the exit of raw material tower is provided with the charging magnetic valve, and position sensor and charging magnetic valve are electrically connected to controller respectively.
Described raw material tower bottom sidewall is provided with vibrator, and vibrator is electrically connected to controller.
Be provided with temperature inductor in described drying crystalline bucket, temperature inductor is electrically connected to controller.
Be provided with the air inlet pipe that can upwards blow in the discharging opening of described drying crystalline bucket, drying crystalline bucket upper end offers the gas outlet.
Described air inlet pipe is provided with air inlet electromagnetic valve.
Described gas outlet is provided with exhaust purifier.
Described controller is the PLC Programmable Logic Controller.
The utility model beneficial effect is: the dryer for chemical industry that the utility model provides, include the drying crystalline bucket, drying crystalline bucket top is provided with the raw material tower, drying crystalline bucket below is provided with drying tower, drying crystalline bucket top is provided with charging aperture, the outlet of raw material tower passes in the charging aperture of drying crystalline bucket, and the drying crystalline bottom of the barrel is provided with discharging opening, and the discharging opening of drying crystalline bucket is communicated with drying tower by tilted tube; , material is joined in the raw material tower, by the gravity of material self, just can make evenly continuous being conveyed in the material crystallizing tank of material, have that continuous drying, drying time are even, the uniform advantage of crystallization time, guarantee the quality of product; In addition, the utility model also includes controller, be provided with the position sensor that the inductor material level is put in the drying crystalline bucket, the exit of raw material tower is provided with the charging magnetic valve, and position sensor and charging magnetic valve are electrically connected to controller respectively, can respond to the material level in the drying crystalline bucket and feed back to controller by position sensor, controlling the charging magnetic valve by controller again opens or closes, can self-feeding, high efficiency is saved manpower.
Description of drawings:
Fig. 1 is structural representation of the present utility model.
Fig. 2 is control principle drawing of the present utility model.
The specific embodiment:
Below in conjunction with accompanying drawing, the utility model is further described, see shown in Fig. 1 ~ 2, the utility model includes drying crystalline bucket 1, drying crystalline bucket 1 top is provided with raw material tower 2, drying crystalline bucket 1 below is provided with drying tower 3, and drying crystalline bucket 1 top is provided with charging aperture 11, and the outlet of raw material tower 2 passes in the charging aperture 11 of drying crystalline bucket 1, drying crystalline bucket 1 bottom is provided with discharging opening 12, and the discharging opening 12 of drying crystalline bucket 1 is communicated with drying tower 3 by tilted tube 4.
During use, material is joined in raw material tower 2, by the gravity of material self, just can make evenly continuous being conveyed in the material crystallizing tank of material, have continuous drying, drying time is even, crystallization time is even, dry after the uniform advantage of material water ratio, guarantee the quality of product.
The utility model also includes controller 7, controller 7 is the PLC Programmable Logic Controller, be provided with the position sensor 71 that the inductor material level is put in drying crystalline bucket 1, the exit of raw material tower 2 is provided with charging magnetic valve 72, and position sensor 71 and charging magnetic valve 72 are electrically connected to controller 7 respectively.Can respond to the material level in drying crystalline bucket 1 and feed back to controller 7 by position sensor 71, automatically determine the drying crystalline time by material level, then control charging magnetic valves 72 by controller 7 and open or close, can self-feeding, high efficiency is saved manpower.
Raw material tower 2 bottom sidewalls are provided with vibrator 8, and vibrator 8 is electrically connected to controller 7, and vibrator 8 falls the material in raw material tower 2 by effect of vibration, can effectively solve material blanking hard problem, and blanking is even, is conducive to improve the quality of production.
Be provided with temperature inductor 73 in drying crystalline bucket 1, temperature inductor 73 is electrically connected to controller 7, and temperature inductor 73 can detect in real time the temperature in drying crystalline bucket 1 and feed back to controller 7, is convenient to control the temperature in drying crystalline bucket 1.
In addition, be provided with the air inlet pipe 5 that can upwards blow in the discharging opening 12 of drying crystalline bucket 1, drying crystalline bucket 1 upper end offers gas outlet 13, and air inlet pipe 5 is provided with air inlet electromagnetic valve 74, air inlet electromagnetic valve 74 is electrically connected to controller 7, controls opening or closing of air inlet electromagnetic valve 74 by controller 7.Can blow out dry air-flow by air inlet pipe 5 and contact with material is reverse, control material water ratio in certain scope, improve the spinnability of product, simple in structure, the material after drying is completed is discharged by discharging opening 12.Gas outlet 13 is provided with exhaust purifier 9, reduces air pollution, environmental protection.
Certainly, the above is only better embodiment of the present utility model, therefore all equivalences of doing according to the described structure of the utility model patent claim, feature and principle change or modify, is included in the utility model patent claim.
Claims (7)
1. dryer for chemical industry, include drying crystalline bucket (1), drying crystalline bucket (1) top is provided with raw material tower (2), it is characterized in that: be provided with drying tower (3) below described drying crystalline bucket (1), drying crystalline bucket (1) top is provided with charging aperture (11), the outlet of raw material tower (2) passes in the charging aperture (11) of drying crystalline bucket (1), drying crystalline bucket (1) bottom is provided with discharging opening (12), and the discharging opening (12) of drying crystalline bucket (1) is communicated with drying tower (3) by tilted tube (4); Also include controller (7), be provided with the position sensor (71) that the inductor material level is put in drying crystalline bucket (1), the exit of raw material tower (2) is provided with charging magnetic valve (72), and position sensor (71) and charging magnetic valve (72) are electrically connected to controller (7) respectively.
2. dryer for chemical industry according to claim 1 is characterized in that: described raw material tower (2) bottom sidewall is provided with vibrator (8), and vibrator (8) is electrically connected to controller (7).
3. dryer for chemical industry according to claim 1, it is characterized in that: be provided with temperature inductor (73) in described drying crystalline bucket (1), temperature inductor (73) is electrically connected to controller (7).
4. dryer for chemical industry according to claim 1 is characterized in that: be provided with the air inlet pipe (5) that can upwards blow in the discharging opening (12) of described drying crystalline bucket (1), drying crystalline bucket (1) upper end offers gas outlet (13).
5. dryer for chemical industry according to claim 4, it is characterized in that: described air inlet pipe (5) is provided with air inlet electromagnetic valve (74).
6. dryer for chemical industry according to claim 4, it is characterized in that: described gas outlet (13) are provided with exhaust purifier (9).
7. according to claim 1 ~ 6 described dryer for chemical industries of any one, it is characterized in that: described controller (7) is the PLC Programmable Logic Controller.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220651776 CN202961947U (en) | 2012-11-30 | 2012-11-30 | Chemical drying device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220651776 CN202961947U (en) | 2012-11-30 | 2012-11-30 | Chemical drying device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202961947U true CN202961947U (en) | 2013-06-05 |
Family
ID=48503078
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201220651776 Expired - Fee Related CN202961947U (en) | 2012-11-30 | 2012-11-30 | Chemical drying device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202961947U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104874200A (en) * | 2015-05-28 | 2015-09-02 | 山西长林环保机械设备有限公司 | Crystallizing device for treating coking and desulfurizing waste liquid |
| CN106477504A (en) * | 2015-08-31 | 2017-03-08 | 山东天富非织造材料有限公司 | A kind of liquid gravity charging equipment and liquid gravity charging method |
| CN106669216A (en) * | 2017-01-19 | 2017-05-17 | 张家港市新贝机械有限公司 | Dehumidification and crystallization system |
| CN106669218A (en) * | 2017-01-19 | 2017-05-17 | 张家港市新贝机械有限公司 | Feed device of dehumidification crystallization system |
-
2012
- 2012-11-30 CN CN 201220651776 patent/CN202961947U/en not_active Expired - Fee Related
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104874200A (en) * | 2015-05-28 | 2015-09-02 | 山西长林环保机械设备有限公司 | Crystallizing device for treating coking and desulfurizing waste liquid |
| CN106477504A (en) * | 2015-08-31 | 2017-03-08 | 山东天富非织造材料有限公司 | A kind of liquid gravity charging equipment and liquid gravity charging method |
| CN106669216A (en) * | 2017-01-19 | 2017-05-17 | 张家港市新贝机械有限公司 | Dehumidification and crystallization system |
| CN106669218A (en) * | 2017-01-19 | 2017-05-17 | 张家港市新贝机械有限公司 | Feed device of dehumidification crystallization system |
| CN115350496A (en) * | 2017-01-19 | 2022-11-18 | 张家港市新贝机械有限公司 | Integrated equipment for dedusting, dehumidifying and crystallizing shredded sheets |
| CN115350497A (en) * | 2017-01-19 | 2022-11-18 | 张家港市新贝机械有限公司 | Dehumidification crystallization system of shredding sheet |
| CN115364511A (en) * | 2017-01-19 | 2022-11-22 | 张家港市新贝机械有限公司 | Dust collector that shredded sheet dehumidification crystallization was used |
| CN115364511B (en) * | 2017-01-19 | 2024-06-07 | 张家港市新贝机械有限公司 | Dust collector that piece material dehumidification crystallization was used tears |
| CN115350496B (en) * | 2017-01-19 | 2024-06-11 | 张家港市新贝机械有限公司 | Dedusting, dehumidifying and crystallizing integrated equipment for shredding sheet |
| CN115350497B (en) * | 2017-01-19 | 2024-06-11 | 张家港市新贝机械有限公司 | Dehumidification crystallization system for shredding sheets |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| 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: 20130605 Termination date: 20141130 |
|
| EXPY | Termination of patent right or utility model |