CN205127426U - Drier - Google Patents
Drier Download PDFInfo
- Publication number
- CN205127426U CN205127426U CN201520841742.7U CN201520841742U CN205127426U CN 205127426 U CN205127426 U CN 205127426U CN 201520841742 U CN201520841742 U CN 201520841742U CN 205127426 U CN205127426 U CN 205127426U
- Authority
- CN
- China
- Prior art keywords
- drying tower
- heater
- liquid material
- cyclone
- sprayer
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
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- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
- Drying Of Solid Materials (AREA)
Abstract
The utility model discloses a drier, including liquid material pump (2), atomizer (3), drying tower (4), heater (8), primary cyclone (10) and secondary cyclone (11), the one end of liquid material pump (2) is connected with liquid workbin (1), liquid expect the other end of pump (2) connect in atomizer (3), atomizer (3) set up in the top of drying tower (4), the air inlet and the blower connection of heater (8), the gas outlet of heater (8) with atomizer (3) are connected, be provided with temperature sensor (6) and humidity transducer (7) in drying tower (3). The utility model discloses drying effect is good.
Description
Technical field
The utility model relates to a kind of drier.
Background technology
Drier by heating, the hygroscopic water in material (referring generally to moisture or other volatile liquid components) is vaporized to overflow, to obtain the plant equipment of the solid material of regulation moisture content.The rate of drying of material depends on the diffusion rate of surface vaporization speed and inner hygroscopic water.The rate of drying of usual the early stage of drying controls by surface vaporization speed; In dry run, need the transmission simultaneously completing heat and quality (hygroscopic water), ensure that material surface hygroscopic water vapor partial pressure (concentration) is higher than the hygroscopic water vapor partial pressure in space outerpace, ensure that heat source temperature is higher than temperature of charge.Current drying device, rate of drying is slow, weak effect, and its structure need to improve.
Utility model content
For the defect of prior art, the utility model provides a kind of drier.
A kind of drier, comprise liquid material pump 2, sprayer 3, drying tower 4, heater 8, primary cyclone 10 and secondary cyclone 11, one end of described liquid material pump 2 is connected with liquid tank 1, the other end of liquid material pump 2 is connected to described sprayer 3, described sprayer 3 is arranged at the top of described drying tower 4, the air inlet of described heater 8 is connected with air blast, the gas outlet of heater 8 is connected with described sprayer 3, temperature sensor 6 and humidity sensor 7 is provided with in described drying tower 3, the middle part of drying tower 3 is provided with exhaust tube 5, the bottom of described drying tower 4 is connected by the charging aperture of pipeline with described secondary cyclone 11, described exhaust tube 5 is connected with the charging aperture of described primary cyclone 10, the discharging opening of described primary cyclone 10 is also connected by the charging aperture of pipeline with described secondary cyclone 11, described primary cyclone 10 is all connected with exhaust fan 12 by pipeline with the exhaust outlet of secondary cyclone 11.
Optionally, also include PLC, described temperature sensor 6 is connected with the input of PLC with humidity sensor 7, and an output of described PLC is connected with described liquid material pump 2 by frequency converter, and another output connects the heating wire 9 in heater 8.
The beneficial effects of the utility model are: wet stock can be made dry rapidly by hot-air, and carry out one, two two-stage drying process to material, make feed separation more thorough, drying effect of the present utility model is good.
Accompanying drawing explanation
Fig. 1 is the structural representation of the utility model drier;
Fig. 2 is the utility model control principle drawing.
Detailed description of the invention
For enabling above-mentioned purpose of the present utility model, feature and advantage become apparent more, are described in detail detailed description of the invention of the present utility model below in conjunction with accompanying drawing, make above-mentioned and other object of the present utility model, Characteristics and advantages will be more clear.Reference numeral identical in whole accompanying drawing indicates identical part.Deliberately do not draw accompanying drawing in proportion, focus on purport of the present utility model is shown.
As shown in Figure 1, drier of the present utility model comprises liquid material pump 2, sprayer 3, drying tower 4, heater 8, primary cyclone 10 and secondary cyclone 11, one end of described liquid material pump 2 is connected with liquid tank 1, the other end of liquid material pump 2 is connected to described sprayer 3, described sprayer 3 is arranged at the top of described drying tower 4, the air inlet of described heater 8 is connected with air blast, the gas outlet of heater 8 is connected with described sprayer 3, temperature sensor 6 and humidity sensor 7 is provided with in described drying tower 3, the middle part of drying tower is provided with exhaust tube 5, the bottom of described drying tower 4 is connected by the charging aperture of pipeline with described secondary cyclone 11, described exhaust tube 5 is connected with the charging aperture of described primary cyclone 10, the discharging opening of described primary cyclone 10 is also connected by the charging aperture of pipeline with described secondary cyclone 11, described primary cyclone 10 is all connected with exhaust fan 12 by pipeline with the exhaust outlet of secondary cyclone 11.Refer to Fig. 2, also include PLC, described temperature sensor 6 is connected with the input of PLC with humidity sensor 7, and an output of described PLC is connected with described liquid material pump 2 by frequency converter, and another output connects the heating wire 9 in heater 8.
Operation principle: wet liquid material is sent in sprayer 3 by liquid material pump 2, heater 8 is for heating air, hot-air also enters sprayer 3, wet liquid material is sprayed into droplet dispersion in thermal current by sprayer 3, make wet liquid material dry rapidly in drying tower 3, exhaust tube is by wet steam suction primary cyclone 10, primary cyclone 10 is by steam and feed separation, fall into material that the material bottom drying tower is separated with through primary cyclone 10 all to enter secondary cyclone 11 and do and be further separated, dried material after separation is discharged from the discharging opening of secondary cyclone 11, the waste gas that primary cyclone 10 and secondary cyclone 11 produce is discharged by exhaust fan, in the course of work, PLC obtains the temperature and humidity of drying tower inside in real time by temperature sensor and humidity sensor, the temperature of hot-air is controlled by the power controlling heating wire, thus the temperature in adjustment drying tower, temperature in drying tower is made to maintain setting value, PLC is by the rotating speed of Frequency Converter Control liquid material pump, thus control to enter liquid material in drying tower number, and then control the humidity in drying tower, make drying tower humidity maintain setting value.
Set forth a lot of detail in the above description so that fully understand the utility model.But above description is only preferred embodiment of the present utility model, the utility model can be much different from alternate manner described here to implement, and therefore the utility model is not by the disclosed concrete restriction implemented above.Any those skilled in the art are not departing under technical solutions of the utility model ambit simultaneously, the Method and Technology content of above-mentioned announcement all can be utilized to make many possible variations and modification to technical solutions of the utility model, or be revised as the Equivalent embodiments of equivalent variations.Every content not departing from technical solutions of the utility model, according to technical spirit of the present utility model to any simple modification made for any of the above embodiments, equivalent variations and modification, all still belongs in the scope of technical solutions of the utility model protection.
Claims (2)
1. a drier, it is characterized in that comprising liquid material pump (2), sprayer (3), drying tower (4), heater (8), primary cyclone (10) and secondary cyclone (11), one end of described liquid material pump (2) is connected with liquid tank (1), the other end of liquid material pump (2) is connected to described sprayer (3), described sprayer (3) is arranged at the top of described drying tower (4), the air inlet of described heater (8) is connected with air blast, the gas outlet of heater (8) is connected with described sprayer (3), temperature sensor (6) and humidity sensor (7) is provided with in described drying tower (4), the middle part of drying tower (4) is provided with exhaust tube (5), the bottom of described drying tower (4) is connected by the charging aperture of pipeline with described secondary cyclone (11), described exhaust tube (5) is connected with the charging aperture of described primary cyclone (10), the discharging opening of described primary cyclone (10) is also connected by the charging aperture of pipeline with described secondary cyclone (11), described primary cyclone (10) is all connected with exhaust fan (12) by pipeline with the exhaust outlet of secondary cyclone (11).
2. drier according to claim 1, characterized by further comprising PLC, described temperature sensor (6) is connected with the input of PLC with humidity sensor (7), one output of described PLC is connected with described liquid material pump (2) by frequency converter, and another output connects the heating wire (9) in heater (8).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520841742.7U CN205127426U (en) | 2015-10-28 | 2015-10-28 | Drier |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520841742.7U CN205127426U (en) | 2015-10-28 | 2015-10-28 | Drier |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205127426U true CN205127426U (en) | 2016-04-06 |
Family
ID=55613252
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520841742.7U Expired - Fee Related CN205127426U (en) | 2015-10-28 | 2015-10-28 | Drier |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205127426U (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105833553A (en) * | 2016-04-26 | 2016-08-10 | 刘湘静 | Intelligent high-speed centrifugal spray dryer |
| CN106063997A (en) * | 2016-06-27 | 2016-11-02 | 安庆市微知著电器有限公司 | A kind of heat exchange type exsiccator |
| CN106110693A (en) * | 2016-06-27 | 2016-11-16 | 安庆市微知著电器有限公司 | A kind of automatic dryer |
| CN106139625A (en) * | 2016-06-27 | 2016-11-23 | 安庆市微知著电器有限公司 | A kind of intelligence exsiccator |
| CN106482489A (en) * | 2016-12-13 | 2017-03-08 | 宜春银锂新能源有限责任公司 | A kind of fine work lithium carbonate production drying device |
| CN110812865A (en) * | 2019-11-28 | 2020-02-21 | 山东滨州智源生物科技有限公司 | Accurate temperature control drying system for cyclodextrin and derivatives |
| CN111420416A (en) * | 2020-04-30 | 2020-07-17 | 清远市鑫辉化工有限公司 | Drying equipment for processing silicon dioxide and using method thereof |
| CN114632341A (en) * | 2022-04-18 | 2022-06-17 | 内蒙古圣龙大地科技有限公司 | Mercury-free catalyst vertical drying tower |
-
2015
- 2015-10-28 CN CN201520841742.7U patent/CN205127426U/en not_active Expired - Fee Related
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105833553A (en) * | 2016-04-26 | 2016-08-10 | 刘湘静 | Intelligent high-speed centrifugal spray dryer |
| CN106063997A (en) * | 2016-06-27 | 2016-11-02 | 安庆市微知著电器有限公司 | A kind of heat exchange type exsiccator |
| CN106110693A (en) * | 2016-06-27 | 2016-11-16 | 安庆市微知著电器有限公司 | A kind of automatic dryer |
| CN106139625A (en) * | 2016-06-27 | 2016-11-23 | 安庆市微知著电器有限公司 | A kind of intelligence exsiccator |
| CN106482489A (en) * | 2016-12-13 | 2017-03-08 | 宜春银锂新能源有限责任公司 | A kind of fine work lithium carbonate production drying device |
| CN110812865A (en) * | 2019-11-28 | 2020-02-21 | 山东滨州智源生物科技有限公司 | Accurate temperature control drying system for cyclodextrin and derivatives |
| CN111420416A (en) * | 2020-04-30 | 2020-07-17 | 清远市鑫辉化工有限公司 | Drying equipment for processing silicon dioxide and using method thereof |
| CN114632341A (en) * | 2022-04-18 | 2022-06-17 | 内蒙古圣龙大地科技有限公司 | Mercury-free catalyst vertical drying tower |
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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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160406 Termination date: 20161028 |