CN106063997A - A kind of heat exchange type exsiccator - Google Patents
A kind of heat exchange type exsiccator Download PDFInfo
- Publication number
- CN106063997A CN106063997A CN201610489471.2A CN201610489471A CN106063997A CN 106063997 A CN106063997 A CN 106063997A CN 201610489471 A CN201610489471 A CN 201610489471A CN 106063997 A CN106063997 A CN 106063997A
- Authority
- CN
- China
- Prior art keywords
- dryer shell
- temperature
- processor
- high speed
- humidity
- 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.)
- Pending
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Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D1/00—Evaporating
- B01D1/16—Evaporating by spraying
- B01D1/18—Evaporating by spraying to obtain dry solids
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D1/00—Evaporating
- B01D1/0011—Heating features
- B01D1/0017—Use of electrical or wave energy
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D1/00—Evaporating
- B01D1/0082—Regulation; Control
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D1/00—Evaporating
- B01D1/30—Accessories for evaporators ; Constructional details thereof
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Drying Of Solid Materials (AREA)
Abstract
The invention discloses a kind of heat exchange type exsiccator, including dryer shell, described dryer shell be arranged above high speed atomisation device;One end of described high speed atomisation device is connected with feed pump;The other end of described high speed atomisation device is connected with electric heater, and one end of described electric heater is connected with vapor heat exchanger, and described vapor heat exchanger is connected with pressure fan A;The lower section of described dryer shell is provided with chamber, and one end of described chamber is connected with pressure fan B;The outside of described dryer shell is provided with temperature indicator and wetness, described temperature indicator is all connected with processor with wetness, described processor is connected with temperature sensor and humidity sensor, described temperature sensor and humidity sensor are arranged at the inside of described dryer shell, and described processor is connected with temperature controller and humidity controller respectively.The present invention is provided by temperature controller and humidity controller, it is possible to be controlled the temperature and humidity within exsiccator.
Description
Technical field
The present invention relates to technical field of drying, particularly relate to a kind of heat exchange type exsiccator.
Background technology
Exsiccator is to make the hygroscopic water (referring generally to moisture or other volatile liquid components) in material vaporize by heating
Effusion, to obtain the plant equipment of the solid material of regulation moisture content.Dry run needs to consume a large amount of heat energy, in order to save energy
Amount, the material that some moisture content is high, the suspension containing solid matter or solution are typically first through mechanical dehydration or heating evaporation, then
It is dried in exsiccator, to obtain the solid done.The purpose being dried is the needs using for material or being processed further.Such as wood
Material is making the dry product deformation that is possible to prevent before wooden model, woodenware, and ceramic batch before calcination dry is possible to prevent finished product
Be full of cracks.The most dried material also allows for transport and storage, as will the grain drying of results to below certain moisture content, in case
Go mouldy.Owing to natural drying is far from meeting the needs of production development, various mechanization exsiccators are answered more and more widely
With.Dry run needs complete heat and the transmission of quality (hygroscopic water), it is ensured that material surface hygroscopic water vapor partial pressure is (dense simultaneously
Degree) higher than the hygroscopic water vapor partial pressure in space outerpace, it is ensured that heat source temperature is higher than temperature of charge.The intellectuality of current exsiccator
Degree is low, it is impossible to be controlled the temperature and humidity within exsiccator.
Summary of the invention
The invention aims to overcome the deficiencies in the prior art, it is provided that a kind of heat exchange type exsiccator.
The present invention is to be achieved through the following technical solutions:
A kind of heat exchange type exsiccator, including dryer shell, described dryer shell be arranged above high speed atomisation device;
One end of described high speed atomisation device is connected with feed pump;The other end of described high speed atomisation device is connected with electric heater, described electricity
One end of heater is connected with vapor heat exchanger, and described vapor heat exchanger is connected with pressure fan A;The lower section of described dryer shell
Being provided with chamber, one end of described chamber is connected with pressure fan B;The outside of described dryer shell be provided with temperature indicator and
Wetness, described temperature indicator is all connected with processor with wetness, described processor and temperature sensor and
Humidity sensor is connected, and described temperature sensor and humidity sensor are arranged at the inside of described dryer shell, and described
Processor is connected with temperature controller and humidity controller respectively.Described whirlwind wind is provided with receipts powder drum from the lower end of device B.Also wrap
Including alarm, described alarm is connected with processor.
As the preferred technical solution of the present invention, described feed pump is screw pump.
Compared with prior art, the invention has the beneficial effects as follows: the present invention is provided by temperature controller and humidity
Controller, it is possible to the temperature and humidity within exsiccator is controlled.
Accompanying drawing explanation
Fig. 1 is the structural representation of the present invention.
Detailed description of the invention
In order to make the purpose of the present invention, technical scheme and advantage clearer, below in conjunction with drawings and Examples, right
The present invention is further elaborated.Should be appreciated that specific embodiment described herein only in order to explain the present invention, and
It is not used in the restriction present invention.
Refer to the structural representation that Fig. 1, Fig. 1 are the present invention.
Described a kind of heat exchange type exsiccator, including dryer shell 1, being arranged above at a high speed of described dryer shell 1
Nebulizer 2;One end of described high speed atomisation device 2 is connected with feed pump 3;The other end of described high speed atomisation device 2 and electric heater 4
Being connected, one end of described electric heater 4 is connected with vapor heat exchanger 5, and described vapor heat exchanger 5 is connected with pressure fan A6;Described
The lower section of dryer shell 1 is provided with chamber 8, and one end of described chamber 8 is connected with pressure fan B9;Described dryer shell 1
Outside is provided with temperature indicator 21 and wetness 22, and described temperature indicator 21 and wetness 22 are all and processor
23 are connected, and described processor 23 is connected with temperature sensor and humidity sensor, and described temperature sensor and humidity sensor are equal
It is arranged on the inside of described dryer shell 1, and described processor 23 is connected with temperature controller and humidity controller respectively, also
Including alarm, described alarm is connected with processor 23.Described temperature controller and humidity controller respectively with heater and
Humidifier is connected, and it is internal that described heater and humidifier are arranged at described dryer shell 1, described temperature indicator 21 and wet
Degree display 22 is liquid crystal display.
The lower end of described chamber 8 is provided with air chamber 10, and trachea is passed through with whirlwind wind from device 13 phase in one end of described air chamber 10
Even, described whirlwind wind is connected with air exhauster 14 from one end of device 13, and described whirlwind wind is provided with cyclone from the lower end of device A13
15, one end of described cyclone 15 is connected with air dehumidifier 16, and the other end of described cyclone 15 and whirlwind wind are from device B18's
Upper end is connected with reclaiming blower fan 19, and described recovery blower fan 19 is connected with dryer shell 1;One end of described air dehumidifier 16 with
Air filter B17 is connected, and described whirlwind wind is provided with receipts powder drum 20 from the lower end of device B18.
In use, use and be spray-dried principle, heat sensitive material is sprayed in aerosol apparatus fine drop, and passes through
Electric heater heats, and drop is during declining, and moisture is reached drying purpose by rapid vaporization, thus obtains graininess
Product.The dry run of material is divided into constant speed stage and falling-rate period.In the constant speed stage, the moisture diffusion rate by granule
More than boil-off rate, moisture vaporization is to occur on drop surface, and the constant speed stage is also called surface vaporization and controls the stage.When moisture leads to
When crossing the diffusion rate reduction of granule and can not maintain the abundant moistening of particle surface, boil-off rate starts to slow down, and is dried and enters
Falling-rate period, falling-rate period is also called internal migration and controls the stage.
The foregoing is only presently preferred embodiments of the present invention, not in order to limit the present invention, all essences in the present invention
Any amendment, equivalent and the improvement etc. made within god and principle, should be included within the scope of the present invention.
Claims (2)
1. a heat exchange type exsiccator, it is characterised in that: include dryer shell (1), the top peace of described dryer shell (1)
Equipped with high speed atomisation device (2);One end of described high speed atomisation device (2) is connected with feed pump (3);Described high speed atomisation device (2)
The other end is connected with electric heater (4), and one end of described electric heater (4) is connected with vapor heat exchanger (5), described steam heat-exchanging
Device (5) is connected with pressure fan A (6);The lower section of described dryer shell (1) is provided with chamber (8), one end of described chamber (8)
It is connected with pressure fan B (9);The outside of described dryer shell (1) is provided with temperature indicator (21) and wetness (22),
Described temperature indicator (21) is all connected with processor (23) with wetness (22), described processor (23) and temperature sensing
Device is connected with humidity sensor, and described temperature sensor and humidity sensor are arranged at the inside of described dryer shell (1),
And described processor (23) is connected with temperature controller and humidity controller respectively;
Described whirlwind wind is provided with receipts powder drum (20) from the lower end of device B (18);Also include alarm, described alarm and processor
(23) it is connected.
A kind of heat exchange type exsiccator the most according to claim 1, it is characterised in that: described feed pump (3) is screw pump.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201610489471.2A CN106063997A (en) | 2016-06-27 | 2016-06-27 | A kind of heat exchange type exsiccator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201610489471.2A CN106063997A (en) | 2016-06-27 | 2016-06-27 | A kind of heat exchange type exsiccator |
Publications (1)
Publication Number | Publication Date |
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CN106063997A true CN106063997A (en) | 2016-11-02 |
Family
ID=57421130
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN201610489471.2A Pending CN106063997A (en) | 2016-06-27 | 2016-06-27 | A kind of heat exchange type exsiccator |
Country Status (1)
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CN (1) | CN106063997A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112044106A (en) * | 2020-09-04 | 2020-12-08 | 上海大川原干燥设备有限公司 | Spray drying equipment for online controlling powder moisture and powder moisture control method |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101787397A (en) * | 2010-02-06 | 2010-07-28 | 山东丰源中科生态科技有限公司 | Icing sugar spray drying system with high DE value |
CN201578868U (en) * | 2009-10-26 | 2010-09-15 | 东莞市天益生物工程有限公司 | Spray drying device |
CN201969369U (en) * | 2010-12-13 | 2011-09-14 | 林松 | Spray drying machine |
CN205127426U (en) * | 2015-10-28 | 2016-04-06 | 赵铭鑫 | Drier |
-
2016
- 2016-06-27 CN CN201610489471.2A patent/CN106063997A/en active Pending
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN201578868U (en) * | 2009-10-26 | 2010-09-15 | 东莞市天益生物工程有限公司 | Spray drying device |
CN101787397A (en) * | 2010-02-06 | 2010-07-28 | 山东丰源中科生态科技有限公司 | Icing sugar spray drying system with high DE value |
CN201969369U (en) * | 2010-12-13 | 2011-09-14 | 林松 | Spray drying machine |
CN205127426U (en) * | 2015-10-28 | 2016-04-06 | 赵铭鑫 | Drier |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112044106A (en) * | 2020-09-04 | 2020-12-08 | 上海大川原干燥设备有限公司 | Spray drying equipment for online controlling powder moisture and powder moisture control method |
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WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20161102 |
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