CN207622350U - Drying system - Google Patents
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- CN207622350U CN207622350U CN201721734114.4U CN201721734114U CN207622350U CN 207622350 U CN207622350 U CN 207622350U CN 201721734114 U CN201721734114 U CN 201721734114U CN 207622350 U CN207622350 U CN 207622350U
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Abstract
The utility model discloses a kind of drying system, it is related to dry field.The main technical schemes of the utility model are：A kind of drying system, including：Comminutor, including drying tube and drying section；The drying tube coiling is thermally dried in the drying section for the raw material to the drying section；Heating device, including babinet and heater；The heater is fixedly connected on the babinet, and the babinet forms high-temperature vapor for heating water；Heat-exchanger rig, including desuperheat case and nozzle；The tank outlet is connected to the desuperheat tank inlet, and the desuperheat case outlet is fixedly connected on the desuperheat case, and the nozzle is fixedly connected on the desuperheat case, for the high-temperature water vapor spray cooling into the reduction box；The entrance of condensing unit, the condensing unit is fixedly connected on the drying tube, and the outlet of the condensing unit is fixedly connected on the nozzle and the babinet.
Description
Technical field
The utility model is related to dry field more particularly to a kind of drying systems.
Background technology
In the prior art, it is granulated the offer component that machine heat exchanger is major heat during granulating and drying, drier changes
The superheated steam that heat medium is 0.5 to 0.8MPa in hot coil, 160-260 DEG C of vapor (steam) temperature；But due to superheat steam temperature
Excessively high, material is fallen on drier coil, it may occur that melting again, the situation that causes material collophore, can not be granulated.Comminutor changes at present
Hot device is in superheated steam disconnection, and can not come into operation situation, significantly impact the drying efficiency and production capacity of comminutor.And due to overheat
It needs to transmit between steam manufacturing equipment and heat exchange coil, the superheat steam temperature that superheated steam manufacturing equipment generates is identical
, but superheated steam has thermal losses in transmission process, and thermal losses degree is related to environment temperature, therefore Various Seasonal
Thermal losses is different, causes the superheat steam temperature entered in heat exchange coil extremely unstable.Vapor (steam) temperature difference can reach 100 DEG C, and
Exactly because this larger temperature difference so that the service life of heat exchange coil is greatly reduced, and works as the temperature that heat exchange coil is born
It is larger with pressure change, easily cause cracking or fracture, and then have steam and enter and increase material moisture in material, instead so that
Humidity of materials increases.
Utility model content
In view of this, the utility model embodiment provides a kind of drying system, main purpose is to stablize drying in comminutor
Temperature reduces pipeline pressure, prevents material melts, extends the service life of comminutor component, reduces maintenance cost, recycles simultaneously
Save water resource.
In order to achieve the above objectives, the utility model mainly provides the following technical solutions：
The utility model embodiment provides a kind of drying system, including：
Comminutor, including drying tube and drying section；The drying tube coiling is in the drying section, for the drying section
Raw material be thermally dried；
Heating device, including babinet and heater；The heater is fixedly connected on the babinet, and the babinet is for adding
Hot water forms high-temperature vapor；
Heat-exchanger rig, including desuperheat case and nozzle；The tank outlet is connected to the desuperheat tank inlet, the desuperheat case
Outlet is fixedly connected on the desuperheat case, and the nozzle is fixedly connected on the desuperheat case, for the height into the reduction box
Heated steam spray cooling；
The entrance of condensing unit, the condensing unit is fixedly connected on the drying tube, and the outlet of the condensing unit is solid
Surely the nozzle and the babinet are connected to.
Further, further include temperature sensor, flow sensor and the first PLC；The temperature sensor is two, point
It Wei not the first temperature sensor, second temperature sensor and third temperature sensor；First temperature sensor is arranged in institute
Desuperheat tank inlet is stated, the second temperature sensor is arranged in the nozzle entrance；The flow sensor is two, respectively
First flow sensor and second flow sensor, first flow sensor setting is in the desuperheat tank inlet, and described the
Two flow sensings go to be arranged in the nozzle entrance；First temperature sensor, the second temperature sensor, described first
Flow sensor and the second flow sensor are all connected to the first PLC；First PLC is connected to the nozzle；
First PLC adjusts the capacity of sprinkler according to the temperature and flow information of reception.
Further, further include third temperature sensor and the 2nd PLC；The third temperature sensor setting subtracts described
Incubator exports, and is connected to the desuperheat case outlet valve；2nd PLC is connected to the desuperheat case imported valve, described
Nozzle and the third temperature sensor；When the Temperature of Warm Case that subtracts is in the preset range of the third temperature sensor
When, the desuperheat case outlet valve is opened；When outside the preset range in the third temperature sensor, the desuperheat case outlet
Valve is closed, and the 2nd PLC adjusts the desuperheat case imported valve and the nozzle.
Further, further include humidity sensor and alarm, the humidity sensor is arranged in the drying section simultaneously
It is connected to the alarm；When the drying section humidity is more than the humidity sensor preset value, the alarm sounds.
Further, the nozzle is multiple, uniform to be arranged in the desuperheat case.
Further, it is equipped between the drying tube and the desuperheat case, between the condensing unit and the nozzle
Pressurizing valve or pressure reducing valve.
A kind of drying system that the utility model embodiment proposes, including：Comminutor, heating device, heat-exchanger rig and cold
Solidifying device；Comminutor includes drying tube and drying section；Drying tube is coiled in drying section, is heated for the raw material to drying section
It is dry；Heating device includes babinet and heater；Heater is fixedly connected on babinet, and babinet forms high-temperature water for heating water
Steam；Heat-exchanger rig includes desuperheat case and nozzle；Tank outlet is connected to desuperheat tank inlet, and the outlet of desuperheat case, which is fixedly connected on, to be subtracted
Incubator, nozzle are fixedly connected on desuperheat case, for the high-temperature water vapor spray cooling into reduction box；The entrance of condensing unit is solid
Surely it is connected to drying tube, the outlet of condensing unit is fixedly connected on nozzle and babinet.In the prior art due to superheated steam temperature
Height is spent, material is fallen on drier coil, it may occur that melting again, the situation that causes material collophore, can not be granulated.Comminutor at present
Heat exchanger is in superheated steam disconnection, and can not come into operation situation, significantly impact the drying efficiency and production capacity of comminutor.And due to mistake
It needs to transmit between hot steam manufacturing equipment and heat exchange coil, the superheat steam temperature that superheated steam manufacturing equipment generates is identical
, but superheated steam has thermal losses in transmission process, and thermal losses degree is related to environment temperature, therefore Various Seasonal
Thermal losses is different, causes the superheat steam temperature entered in heat exchange coil extremely unstable.Vapor (steam) temperature difference can reach 100 DEG C, and
Exactly because this larger temperature difference so that the service life of heat exchange coil is greatly reduced, and works as the temperature that heat exchange coil is born
It is larger with pressure change, easily cause cracking or fracture, and then have steam and enter and increase material moisture in material, instead so that
Humidity of materials increases.And the utility model carries out cooling to the superheated steam for entering drying tube by heat-exchanger rig and is done to reduce
Vapor (steam) temperature in dry pipe, temperature reduction also reduces pressure in drying tube, so that the service life of drying tube effectively extends,
It enables to enter the superheated steam in drying tube simultaneously more to stablize, and the drying tube after cooling down is unable to reach raw material melting temperature
Degree so that raw material drying can be normally carried out, and ensure that working efficiency, reduce frequency and the time of maintenance shut-downs.And it uses cold
Solidifying device connects nozzle, realizes the recycling of water resource, has reached water-saving purpose.
Description of the drawings
Fig. 1 is a kind of structural schematic diagram for drying system that the utility model embodiment provides.
Specific implementation mode
Further to illustrate that the utility model is to reach the technological means and effect that predetermined purpose of utility model is taken,
Below in conjunction with attached drawing and preferred embodiment, to according to the utility model proposes drying system specific implementation mode, structure, feature
And its effect, it is described in detail as after.
As shown in Figure 1, a kind of drying system, including：
Comminutor, including drying tube 11 and drying section 12；The coiling of above-mentioned drying tube 11 in above-mentioned drying section 12, for
The raw material for stating drying section 12 is thermally dried；In practical operation, the superheat steam temperature of above-mentioned drying tube 11 is actually entered
Between 160 DEG C to 260 DEG C, and after the cooling of above-mentioned desuperheat case 31, can by superheated steam stability contorting at 100 DEG C extremely
Between 150 DEG C, cool down to superheated steam so that the service life is longer for equipment, also so that the temperature to superheated steam controls more
Add precisely.And in order to reach preferable drying effect, it should be by above-mentioned 11 density of drying tube of increase, or increase above-mentioned dry
The modes such as 12 volume of dry portion, the drying time appropriate for increasing raw material.
Heating device, including babinet 21 and heater 22；Above-mentioned heater 22 is fixedly connected on above-mentioned babinet 21, above-mentioned case
Body 21 forms high-temperature vapor for heating water；Due to above-mentioned babinet 21 between above-mentioned drying tube 11 have transmission range,
In this section of transmission process, superheated steam has a thermal loss, therefore by this thermal losses meter when above-mentioned heater 22 designs
It calculates in the middle, heated at constant temperature higher so that environment temperature that in actual use can be because of different regions and different overheats
The service condition of the transportation range of steam etc. and lead to different effects.
Heat-exchanger rig 3, including desuperheat case 31 and nozzle 32；The outlet of above-mentioned babinet 21 is connected to above-mentioned 31 entrance of desuperheat case,
The above-mentioned outlet of desuperheat case 31 is fixedly connected on above-mentioned desuperheat case 31, and above-mentioned nozzle 32 is fixedly connected on above-mentioned desuperheat case 31, is used for
High-temperature water vapor spray cooling into above-mentioned reduction box；Since the combination of every group of equipment is different, above-mentioned babinet 21 is exported to
It is also different to state the distance between 31 entrance of desuperheat case, therefore the thermal losses of every group of equipment is variant, and for same group of equipment
For, environment temperature caused by different weather is different, and thermal losses is also variant, and uses above-mentioned desuperheat case 31 and 32 energy of nozzle
It is enough to cool down before superheated steam enters above-mentioned drying tube 11, so that temperature will not be excessively high in above-mentioned drying tube 11,
Prevent raw material from being melted when dry because releasing drying tube 11, while the cooling of superheated steam makes gas pressure reduce so that
The pressure that above-mentioned drying tube 11 is born becomes smaller, and can effectively improve the service life of above-mentioned drying tube 11.The water of above-mentioned nozzle 32
So that while high temperature super heated steam cooling, also so that the water meeting that above-mentioned nozzle 32 sprays is because heat transmission causes to vaporize, to
Supplement in above-mentioned babinet 21 pressure to decline, prevent pressure from declining excessive and so that above-mentioned babinet 21 damages, effectively reduce repair at
This.
The entrance of condensing unit 4, above-mentioned condensing unit 4 is fixedly connected on above-mentioned drying tube 11, and above-mentioned condensing unit 4 goes out
Mouth is fixedly connected on above-mentioned nozzle 32 and above-mentioned babinet 21.Above-mentioned condensing unit 4 by used superheated steam condensing recovery, and
It is mixed and is cooled down with superheated steam by above-mentioned nozzle 32 so that water resource recycles, effectively save water resource, while mistake
Hot steam is condensed into distilled water, and degree of purity is high, without impurity so that above-mentioned nozzle 32 does not tend to have incrustation scale or other impurities are led
It causes to block so that maintenance shut-downs number is few, and then reduces failure rate and maintain cost.
The dry system in the present embodiment is illustrated below by way of the working process and principle of drying system in the present embodiment
System：
Above-mentioned heater 22 heats the water in above-mentioned babinet 21 so that water becomes the superheated steam of high temperature, conveying
In to above-mentioned desuperheat case 31, the water spray of above-mentioned nozzle 32 carries out cooling processing, and the superheated steam after cooling inputs above-mentioned drying tube 11
The raw material of above-mentioned drying section 12 is thermally dried, the superheated steam flowed out from above-mentioned drying tube 11 enters above-mentioned condensing unit
4 become liquid water, then are conveyed into above-mentioned nozzle 32 and carry out spray cooling to the high temperature super heated steam in above-mentioned desuperheat case 31.
A kind of drying system that the utility model embodiment proposes, including：Comminutor, heating device, heat-exchanger rig 3 and cold
Solidifying device 4；Comminutor includes drying tube 11 and drying section 12；The coiling of drying tube 11 is in drying section 12, for drying section 12
Raw material is thermally dried；Heating device includes babinet 21 and heater 22；Heater 22 is fixedly connected on babinet 21, babinet 21
For heating water, high-temperature vapor is formed；Heat-exchanger rig 3 includes desuperheat case 31 and nozzle 32；The outlet of babinet 21 is connected to desuperheat
31 entrance of case, the outlet of desuperheat case 31 are fixedly connected on desuperheat case 31, and nozzle 32 is fixedly connected on desuperheat case 31, is used for reduction box
Interior high-temperature water vapor spray cooling；The entrance of condensing unit 4 is fixedly connected on drying tube 11, and the outlet of condensing unit 4 is fixed
It is connected to nozzle 32 and babinet 21.In the prior art since superheat steam temperature is excessively high, material is fallen on drier coil, can be sent out
Raw melting again, the situation that causes material collophore, can not be granulated.It is granulated machine heat exchanger at present and is in superheated steam disconnection, can not throw
With situation, the drying efficiency and production capacity of comminutor are significantly impacted.And due between superheated steam manufacturing equipment and heat exchange coil
It needs to transmit, the superheat steam temperature that superheated steam manufacturing equipment generates is identical, but the superheated steam meeting in transmission process
There is thermal losses, and thermal losses degree is related to environment temperature, therefore the thermal losses of Various Seasonal is different, causes to enter heat exchange coil
In superheat steam temperature it is extremely unstable.Vapor (steam) temperature difference can reach 100 DEG C, exactly because and this larger temperature difference so that
The service life of heat exchange coil is greatly reduced, and works as the temperature and pressure that heat exchange coil is born and change greatly, and easily causes cracking
Or fracture, and then have steam and enter and increase material moisture in material, instead so that humidity of materials increases.And the utility model is logical
Heat-exchanger rig 3 is crossed to cool down to reduce vapor (steam) temperature in drying tube 11, temperature drop to the superheated steam for entering drying tube 11
It is low to also reduce pressure in drying tube 11, so that the service life of drying tube 11 effectively extends, while enabling to enter
Superheated steam in drying tube 11 is more stablized, and the drying tube 11 after cooling down is unable to reach raw material melting temperature so that raw material
Drying can be normally carried out, and ensure that working efficiency, reduce frequency and the time of maintenance shut-downs.And it is connected using condensing unit 4
Nozzle 32 realizes the recycling of water resource, has reached water-saving purpose.
The utility model is described in further detail with reference to the accompanying drawings and examples.
In order to the more accurate and automation for the control that will cool down, specifically, further including temperature sensor, flow sensing
Device and the first PLC；Above-mentioned temperature sensor is two, respectively the first temperature sensor, second temperature sensor and third temperature
Spend sensor；In above-mentioned 31 entrance of desuperheat case, above-mentioned second temperature sensor is arranged upper for above-mentioned first temperature sensor setting
State 32 entrance of nozzle；Above-mentioned flow sensor is two, respectively first flow sensor and second flow sensor, above-mentioned the
The setting of one flow sensor goes to be arranged in 32 entrance of above-mentioned nozzle in above-mentioned 31 entrance of desuperheat case, above-mentioned second flow sensing；On
It is equal to state the first temperature sensor, above-mentioned second temperature sensor, above-mentioned first flow sensor and above-mentioned second flow sensor
It is connected to above-mentioned first PLC；First PLC is connected to the nozzle 32；Above-mentioned first PLC is according to the temperature and flow of reception
Information adjusts above-mentioned 32 flow of nozzle.The flow and temperature for measuring the high temperature super heated steam for entering above-mentioned desuperheat case 31, measure into
Enter the temperature of the water of above-mentioned nozzle 32, and these data transmissions are entered into above-mentioned first PLC, passes through the calculating of above-mentioned first PLC, control
Make the water spray of above-mentioned nozzle 32, and by above-mentioned second flow sensor to above-mentioned first PLC fed back to ensure into
The superheat steam temperature for entering above-mentioned drying tube 11 is suitable.
Specifically, further including third temperature sensor and the 2nd PLC；Above-mentioned third temperature sensor is arranged in above-mentioned desuperheat
Case 31 exports, and is connected to above-mentioned 31 outlet valve of desuperheat case；Above-mentioned 2nd PLC be connected to above-mentioned 31 imported valve of desuperheat case,
Above-mentioned nozzle 32 and above-mentioned third temperature sensor；When above-mentioned 31 temperature of desuperheat case is in the default of above-mentioned third temperature sensor
When in range, above-mentioned 31 outlet valve of desuperheat case is opened；It is above-mentioned to subtract when outside the preset range in above-mentioned third temperature sensor
31 outlet valve of incubator is closed, and above-mentioned 2nd PLC adjusts above-mentioned 31 imported valve of desuperheat case and above-mentioned nozzle 32.Pass through above-mentioned
The feedback of three-temperature sensor, above-mentioned 2nd PLC information can be analyzed and control above-mentioned 31 imported valve of desuperheat case and
The flow of above-mentioned nozzle 32 so that the temperature of superheated steam is reduced to the pre- of above-mentioned third temperature sensor in above-mentioned desuperheat case 31
If when in range, above-mentioned 31 outlet valve of desuperheat case is opened at this time, it is ensured that is suitably overheated to 11 input temp of above-mentioned drying tube
Steam.
To find that above-mentioned drying tube 11 ruptures in time, specifically, further including humidity sensor and alarm, above-mentioned humidity passes
Sensor is arranged in above-mentioned drying section 12 and is connected to above-mentioned alarm；When 12 humidity of above-mentioned drying section is more than above-mentioned humidity sensor
When device preset value, above-mentioned alarm sounds.Due to being superheated steam in above-mentioned drying tube 11, throughout the year in moist, high temperature
The even working environment of high pressure, therefore the service life of above-mentioned drying tube 11 is often below other pipelines.And above-mentioned drying
Pipe 11 is arranged inside above-mentioned comminutor, can not observed in actual work, and staff is waited to find above-mentioned drying tube 11
When rupture, the influence to raw material or other equipment may be larger, and more times, manpower or money is needed to go to safeguard.And
After above-mentioned humidity sensor and above-mentioned alarm, when above-mentioned drying tube 11 ruptures, superheated steam can leak, and necessarily cause
Its ambient humidity increases, and can replace manually observing by the real-time monitoring of above-mentioned humidity sensor, precision and feedback speed
Degree all highers, and above-mentioned alarm then can notify staff to arrive rapidly.
In order to accelerate cooling rate, specifically, above-mentioned nozzle 32 is multiple, it is uniform to be arranged in above-mentioned desuperheat case 31.
When using above-mentioned second temperature sensor and second flow sensor, above-mentioned second temperature sensor and second flow sensor are answered
It is arranged on total waterline of multiple above-mentioned nozzles 32, consequently facilitating control.And when stating two PLC in use, can both it make
It states the 2nd PLC to be connected on total waterline of multiple above-mentioned nozzles 32, each above-mentioned nozzle 32 can be also separately connected, with specific reference to reality
Depending on the service condition of border.
Since superheated steam pressure has variation after cooling, to keep superheated steam pressure relatively stable, specifically, above-mentioned dry
It is equipped with pressurizing valve or pressure reducing valve between dry pipe 11 and above-mentioned desuperheat case 31, between above-mentioned condensing unit 4 and above-mentioned nozzle 32.Tool
The pressure requirements of body according to the actual conditions such as bearing capacity, above-mentioned 31 output pressure of desuperheat case of above-mentioned drying tube 11 determine, into
And it determines to use above-mentioned pressurizing valve or above-mentioned pressure reducing valve.Using enabling to above-mentioned drying after above-mentioned pressurizing valve or above-mentioned pressure reducing valve
Pipe 11 is in more suitably working environment, effectively improves service life, reduces frequency of maintenance.
A kind of drying system that the utility model embodiment proposes, including：Comminutor, heating device, heat-exchanger rig and cold
Solidifying device；Comminutor includes drying tube and drying section；Drying tube is coiled in drying section, is heated for the raw material to drying section
It is dry；Heating device includes babinet and heater；Heater is fixedly connected on babinet, and babinet forms high-temperature water for heating water
Steam；Heat-exchanger rig includes desuperheat case and nozzle；Tank outlet is connected to desuperheat tank inlet, and the outlet of desuperheat case, which is fixedly connected on, to be subtracted
Incubator, nozzle are fixedly connected on desuperheat case, for the high-temperature water vapor spray cooling into reduction box；The entrance of condensing unit is solid
Surely it is connected to drying tube, the outlet of condensing unit is fixedly connected on nozzle and babinet.In the prior art due to superheated steam temperature
Height is spent, material is fallen on drier coil, it may occur that melting again, the situation that causes material collophore, can not be granulated.Comminutor at present
Heat exchanger is in superheated steam disconnection, and can not come into operation situation, significantly impact the drying efficiency and production capacity of comminutor.And due to mistake
It needs to transmit between hot steam manufacturing equipment and heat exchange coil, the superheat steam temperature that superheated steam manufacturing equipment generates is identical
, but superheated steam has thermal losses in transmission process, and thermal losses degree is related to environment temperature, therefore Various Seasonal
Thermal losses is different, causes the superheat steam temperature entered in heat exchange coil extremely unstable.Vapor (steam) temperature difference can reach 100 DEG C, and
Exactly because this larger temperature difference so that the service life of heat exchange coil is greatly reduced, and works as the temperature that heat exchange coil is born
It is larger with pressure change, easily cause cracking or fracture, and then have steam and enter and increase material moisture in material, instead so that
Humidity of materials increases.And the utility model carries out cooling to the superheated steam for entering drying tube by heat-exchanger rig and is done to reduce
Vapor (steam) temperature in dry pipe, temperature reduction also reduces pressure in drying tube, so that the service life of drying tube effectively extends,
It enables to enter the superheated steam in drying tube simultaneously more to stablize, and the drying tube after cooling down is unable to reach raw material melting temperature
Degree so that raw material drying can be normally carried out, and ensure that working efficiency, reduce frequency and the time of maintenance shut-downs.And it uses cold
Solidifying device connects nozzle, realizes the recycling of water resource, has reached water-saving purpose.
Above description is only a specific implementation of the present invention, but the scope of protection of the utility model is not limited to
In this, any one skilled in the art within the technical scope disclosed by the utility model, can readily occur in variation
Or replace, it should be covered within the scope of the utility model.Therefore, the scope of protection of the utility model should be with the power
Subject to the protection domain that profit requires.
Claims (6)
1. a kind of drying system, which is characterized in that including：
Comminutor, including drying tube and drying section；The drying tube coiling is in the drying section, for the original to the drying section
Material is thermally dried；
Heating device, including babinet and heater；The heater is fixedly connected on the babinet, and the babinet is for heating
Water forms high-temperature vapor；
Heat-exchanger rig, including desuperheat case and nozzle；The tank outlet is connected to the desuperheat tank inlet, the desuperheat case outlet
It is fixedly connected on the desuperheat case, the nozzle is fixedly connected on the desuperheat case, for the high-temperature water into the desuperheat case
Steam spray cooling；
The entrance of condensing unit, the condensing unit is fixedly connected on the drying tube, and the outlet of the condensing unit, which is fixed, to be connected
It is connected to the nozzle and the babinet.
2. drying system according to claim 1, which is characterized in that further include temperature sensor, flow sensor and
One PLC；The temperature sensor is two, respectively the first temperature sensor and second temperature sensor；First temperature
Sensor setting is arranged in the desuperheat tank inlet, the second temperature sensor in the nozzle entrance；The flow sensing
Device is two, respectively first flow sensor and second flow sensor, and the first flow sensor setting subtracts described
Incubator entrance, the second flow sensing go to be arranged in the nozzle entrance；First temperature sensor, the second temperature
Sensor, the first flow sensor and the second flow sensor are all connected to the first PLC；First PLC
It is connected to the nozzle；First PLC adjusts the capacity of sprinkler according to the temperature and flow information of reception.
3. drying system according to claim 1, which is characterized in that further include third temperature sensor and the 2nd PLC；Institute
It states the setting of third temperature sensor to export in the desuperheat case, and is connected to the desuperheat case outlet valve；2nd PLC connects
It is connected to the desuperheat case imported valve, the nozzle and the third temperature sensor；When the Temperature of Warm Case that subtracts is in described
When in the preset range of third temperature sensor, the desuperheat case outlet valve is opened；In the third temperature sensor
When outside preset range, the desuperheat case outlet valve is closed, and the 2nd PLC adjusts the desuperheat case imported valve and the spray
Head.
4. drying system according to any one of claim 1-3, which is characterized in that further include humidity sensor and alarm
Device, the humidity sensor are arranged in the drying section and are connected to the alarm；When the drying section humidity is more than institute
When stating humidity sensor preset value, the alarm sounds.
5. drying system according to claim 4, which is characterized in that the nozzle is multiple, and uniform setting is described
Desuperheat case.
6. drying system according to claim 5, which is characterized in that between the drying tube and the desuperheat case, described
Pressurizing valve or pressure reducing valve are equipped between condensing unit and the nozzle.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721734114.4U CN207622350U (en) | 2017-12-13 | 2017-12-13 | Drying system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721734114.4U CN207622350U (en) | 2017-12-13 | 2017-12-13 | Drying system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207622350U true CN207622350U (en) | 2018-07-17 |
Family
ID=62823557
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721734114.4U Active CN207622350U (en) | 2017-12-13 | 2017-12-13 | Drying system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207622350U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115432314A (en) * | 2022-10-10 | 2022-12-06 | 江西中烟工业有限责任公司 | Automatic heating constant-temperature system and method for liquid in tank body |
-
2017
- 2017-12-13 CN CN201721734114.4U patent/CN207622350U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115432314A (en) * | 2022-10-10 | 2022-12-06 | 江西中烟工业有限责任公司 | Automatic heating constant-temperature system and method for liquid in tank body |
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Effective date of registration: 20230801 Address after: 831100 Room 208, Floor 2, Building 41, Niuquanzi Huqiu, Agricultural Park, Changji Hui Autonomous Prefecture, Changji City, Xinjiang Patentee after: Changji Huier Zhilian Ecological Co.,Ltd. Address before: 831100 floor 1, building 18, niuquanhuqiu, agricultural park, Changji City, Changji Hui Autonomous Prefecture, Xinjiang Uygur Autonomous Region Patentee before: XINJIANG HUIER AGRICULTURE GROUP CO.,LTD. |
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