CN106196913A - Double source enclosed efficient energy-saving drying system - Google Patents
Double source enclosed efficient energy-saving drying system Download PDFInfo
- Publication number
- CN106196913A CN106196913A CN201610536436.1A CN201610536436A CN106196913A CN 106196913 A CN106196913 A CN 106196913A CN 201610536436 A CN201610536436 A CN 201610536436A CN 106196913 A CN106196913 A CN 106196913A
- Authority
- CN
- China
- Prior art keywords
- heat pump
- machine
- air
- drying system
- baking room
- 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
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B9/00—Machines or apparatus for drying solid materials or objects at rest or with only local agitation; Domestic airing cupboards
- F26B9/06—Machines or apparatus for drying solid materials or objects at rest or with only local agitation; Domestic airing cupboards in stationary drums or chambers
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B21/00—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
- F26B21/02—Circulating air or gases in closed cycles, e.g. wholly within the drying enclosure
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B23/00—Heating arrangements
- F26B23/02—Heating arrangements using combustion heating
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B23/00—Heating arrangements
- F26B23/10—Heating arrangements using tubes or passages containing heated fluids, e.g. acting as radiative elements; Closed-loop systems
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B25/00—Details of general application not covered by group F26B21/00 or F26B23/00
- F26B25/005—Treatment of dryer exhaust gases
- F26B25/007—Dust filtering; Exhaust dust filters
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Drying Of Solid Materials (AREA)
Abstract
The invention discloses double source enclosed efficient energy-saving drying system, double source enclosed efficient energy-saving drying system, it is characterized in that, including baking room, combustor, heat pump machine and circulation airduct, circulation airduct includes discharge pipe and blast pipe, and described blast pipe connects the air inlet of baking room, discharge pipe connects the air outlet of baking room, heat pump is arranged on blast pipe, is provided with air heat exchanger between discharge pipe and blast pipe, and described air heat exchanger is connected with combustor and is heated by combustor.This system uses fully-automatic thermostatic height air quantity low humidity stoving process, and combustor and heat pump combine quick heating, reduces drying time；In utilizing heat pump, machine replaces the dehumidifier in tradition drying system, more efficient energy-conservation；Confined space arbitrarily arranges air circulation, bottom wind-guiding and accessory fan formation flow-disturbing and makes to be dried and ensure uniform drying effect without dead angle.Sealing and circulating is dried and is difficult to enter without outside contamination mosquito dust, it is ensured that article quality.High wind convection current without dead angle, article without stirring, Automatic Control.
Description
Technical field
The invention belongs to senior middle school's warm pump drying field, particularly to double source enclosed efficient energy-saving drying system.Application model
Enclose for: senior middle school warm pump drying dehumidification.Being dried the article scope dried is grain, vegetable and fruit, Nicotiana tabacum L., bacon, aquatic products, clothes
Dress cloth, Chinese crude drug, timber, mud coal, various industrial or agricultural raw material and product etc..
Background technology
The category that dry materials is dried is extremely extensively and enormous amount, the energy consumption that the whole society dries for dry materials
The hugest.Having data to show, developed country accounts between the 7%-15% of total energy consumption for the energy consumption that dry materials is dried, averagely
It is 12%.The annual electricity generating capacity of China is about 5,000,000,000,000 degree now, as estimated for electric energy consumption is gross generation 8% dried,
The electric power energy consumption in the whole nation dried for electrical heating the most every year is 400,000,000,000 degree, is equivalent to the generated energy in power station, 5 Yangtze River Gorges；
The fuel such as coal being simultaneously used for drying also is a quantity the hugest.
Traditional dry materials dehumidifying usually electricity consumption or fuel is carried out with mode of heating.General capacity usage ratio all than
Relatively low, the capacity usage ratio of mode of heating greatly below 70%, the most even as low as less than 40%, some occasion such as home laundry
Dry and also need to the damp atmosphere discharged is carried out moisture condensation process again, very inconvenient.1 degree of heat of being converted into of electricity is
3600KJ, the heat needed for 1 kilogram of aqueous water evaporation is about 2400KJ, so electricity consumption heating, drying, entirely without thermal loss
In the case of, 1 degree of electric energy is dehydrated 1.5 kilograms；And actually in drying course, inevitably have substantial amounts of heat to dissipate,
The drying efficiency that electrical heating is dried, typically between 1 degree of electric dehydration 0.6-1.2 kilogram, is averagely about 0.8 kilogram.
Heat pump drying technology is to utilize the energy of electricity, with heat pump assembly, heat is warm to high temperature heat source conveying from low-temperature heat source
The technology of amount, a electricity can carry several parts of heat, compares general electrical heating and dries the energy consumption that can save more than 50%, simultaneously
Condenser heating and the double effects of vaporizer dehumidifying can be had concurrently, be the developing direction of following drying technology.
Because heat pump drying is an emerging technology, the exploitation application time is shorter, fails to fill to the basic principle of heat pump drying
Deep understanding is divided to grasp, so the potentiality of heat pump drying technology fail to fully play.
Heat pump drying equipment conventional on market can be roughly divided into two classes: A class is open, B class is closed.
A class heat pump drying device approximately as: so-called open, device i.e. has wind pipe or the air-out of a band blower fan
Mouthful, the hot and humid gas in baking oven is constantly drawn out of from wind pipe and enters eventually in air, has equivalent simultaneously
The new wind of air of low temperature and low humidity is inhaled in oven ncavity, and the gas in baking oven constantly swaps with atmospheric air.Heat
Pumping system has the outer vaporizer of a band blower fan outside baking oven, if the hot and humid gas in baking oven without outer vaporizer and changes
Hot device and be directly discharged in air, then the heat being discharged gas is not used, and outer vaporizer is completely from air
Middle draw heat.If, with the heat in the hot and humid gas being discharged, substantially there is following several ways: 1, there is no air
Air flows through outer vaporizer, and the hot and humid gas being only discharged drains emptying into air after flowing through outer vaporizer, showing of gas
Latent heat in heat and gas moisture is absorbed by outer vaporizer and is discharged in baking oven by condenser, a key features of the manner
Being intended to the air themperature in maintenance baking oven and enthalpy does not declines, the leaving air temp of vaporizer must drop to equal to or less than air
Ambient temperature, the evaporator refrigerant temperature that the evaporator refrigerant temperature of vaporizer directly absorbs heat with vaporizer from air is more or less the same；
2, the hot and humid gas being discharged again passes through vaporizer after adding atmospheric air mixing, and vaporizer is from the mixed gas flow through
Draw heat, then mixed gas drains emptying into air, and the manner makes the gas temperature flowing through vaporizer higher than atmospheric temperature, carries
High COP；3, the hot and humid gas wind new with the air being inhaled into being discharged first carries out heat friendship in a sensible heat exchanger
After changing, hot and humid gas again passes through outer vaporizer or directly drains emptying into air, exists completely as directly emptied outer vaporizer
Absorbing heat in air, the new wind of the manner is improved through heat-exchange temperature, the hot and humid gas discharged in having reclaimed baking oven
Partial heat.Above-mentioned several Application way all makes the heat in the hot and humid gas being discharged obtain a certain degree of utilization,
But compared with directly emptying with hot and humid gas, the effect of increase is extremely limited, the heating energy efficiency ratio of heat pump is substantially by greatly
Temperature is restricted, and drying effect is changed by the new wind i.e. humidity of atmospheric air simultaneously is affected.The result caused is: if wanted
Make the i.e. COP of heat pump Energy Efficiency Ratio high, then the high-low temperature difference of coolant can not be big, namely the air themperature in baking oven compares ambient temperature
Can not exceed too many, and the temperature in baking oven is the highest, then the effect of removal moisture drying is the most poor；Or gas temperature in baking oven
Higher, but in case, air themperature is very big with the temperature difference of ambient temperature, then and the coolant high/low temperature temperature difference of heat pump is big, Energy Efficiency Ratio
COP is low.
In a word: the open heat pump drying device of A class compares the electric heating drying machine of routine, energy profit is greatly improved
By rate, fractional energy savings is more than 50%, but general effect is less desirable, is restricted by relatively low ambient temperature, weighs total soma
The SMER of dry effect i.e. consumes the drying and dehydrating amount that often degree electricity obtains, it is impossible to the highest, and (3 is public at 3KGH2O/KWH for general SMER
Jin water/kilowatt-hour) below, SMER is averagely about 2.5, and winter is below 2.
B class heat pump dry device approximately as: so-called closed, i.e. air in baking oven is isolated with outside atmosphere substantially,
Its representative products is domestic heat pump dryer, it is characterized in that, extract heat in the vaporizer of the described device not air from baking oven
Amount；Having a circulation return air pipeline, vaporizer is arranged in return air duct, and condenser, in the downstream of the vaporizer of return air duct, steams
Sending out device and condenser shares a blower fan, evaporation air quantity is equal with condensation air quantity, and the hot and humid gas of oven ncavity is from return air
The import of pipeline flows into, and through vaporizer cool-down dehumidification, again passes through condenser heat temperature raising, returns to oven ncavity.Its advantage is
Being affected relatively small by ambient temperature and humidity, the heat that the aqueous water carburation by evaporation being dried in material is consumed is followed
Ring utilizes, and drying effect is basicly stable.Shortcoming is that atmosphere temperature rising is very slow in baking oven, and the heat that oven ncavity is obtained is heat pump
The heat that converted of energy that device acting consumes, device bring into operation after in baking oven the long-time temperature of air relatively low, also make stream
The gas temperature crossing vaporizer in return air duct is relatively low, and latent heat/sensible heat ratio that vaporizer absorbs in heat is the lowest, and drying removes
Wet weak effect, drying rate is slow.Especially because condenser and vaporizer share a blower fan, condensation air quantity and evaporation air quantity phase
Meanwhile, the latent heat absorbed such as vaporizer more than sensible heat, the air inlet/outlet temperature difference of condenser be 2.5 times of the vaporizer air inlet/outlet temperature difference with
On, the leaving air temp making condenser is the highest thus coolant condensation temperature is the highest causes heat pump Energy Efficiency Ratio to decline；Such as vaporizer
The latent heat absorbed is less than sensible heat, although be avoided that the drawback that condenser leaving air temp is the highest, but latent heat/sensible heat is less than 1, makes baking oven
Conversion ratio between latent heat and the sensible heat of interior air lowers, and causes water removal effect to be deteriorated.Total effect and A class open devices phase
When: the closed heat pump drying device of B class dries energy-conservation more than 50% compared with electrical heating, and SMER is about 2 to 2.5, difficult more than 3,
Especially in winter, being affected by ambient temperature, drying effect is worse.
Summary of the invention
The present invention solves problem above present in prior art, it is provided that double source enclosed efficient energy-saving drying system,
Combustor and heat pump combine quick heating, reduce drying time.Confined space arbitrarily arranges air circulation, bottom wind-guiding and auxiliary wind
Machine forms flow-disturbing and makes to be dried without the uniform drying effect of dead angle guarantee.Sealing and circulating be dried without outside contamination mosquito dust be difficult to into
Enter, it is ensured that article quality.High wind convection current is without dead angle, and article are without stirring.Ease of Use system, unmanned, automatically control.
To achieve these goals, the technical solution used in the present invention is:
Double source enclosed efficient energy-saving drying system, it is characterised in that include baking room, combustor, heat pump and circulated air
Pipe, circulation airduct includes discharge pipe and blast pipe, and described blast pipe connects the air inlet of baking room, and discharge pipe meets going out of baking room
Air port, heat pump includes machine and the outer machine of heat pump in heat pump, and wherein, in heat pump, machine is arranged on blast pipe, and the outer machine of heat pump is arranged on out
On airduct, the position of the outer machine of discharge pipe correspondence heat pump is provided with condensation-water drain, is provided with air and changes between discharge pipe and blast pipe
Hot device, described air heat exchanger is connected with combustor and is heated by combustor.
In such scheme, described heat pump machine includes machine in the outer machine of heat pump and heat pump, in described drying system also includes heat pump
Machine airduct switchs with machine airduct in heat pump, in outside described heat pump, machine is located at heat pump in machine airduct, and machine airduct two ends in described heat pump
Communicate with discharge pipe, machine airduct switch in machine airduct two ends and discharge pipe junction are designed with heat pump in described heat pump.
In such scheme, in baking room, be provided with material table, the blast pipe between heat pump and baking room be divided into main air duct and
Auxiliary air channel, is provided with main air blower in main air duct, auxiliary is provided with accessory fan in air channel, wherein, and main air duct and baking room phase
Being positioned at Lian below material table, auxiliary air channel is positioned at above material table with baking room connecting place.
In such scheme, the connecting place of main air duct and auxiliary air channel and baking room is provided with adjustable wind deflector.
In such scheme, described main air duct is provided with adjustable air-port.
In such scheme, described discharge pipe and described heat pump machine are fitted with dust removal and filtration net；Set above described baking room
The scalable dehumidifying automatically-controlled door put.
In such scheme, the baking room both sides of described system are warming plate, and additionally both sides are can be rolled onto above baking room
Thermal-insulated blind.
In such scheme, described material table is provided with ventilative orifice plate, and described material table connects stock guide, and described stock guide is even
It is connected to automatic stuff-conveying machine, described conveyer is provided with automatic harvester.
In such scheme, described air heat exchanger is externally provided with air heat exchanger fin, and described air heat exchanger is arranged over
Smoke exhaust pipe fin it is provided with outside smoke exhaust pipe described in smoke exhaust pipe.
In such scheme, described circulation airduct is provided with scalable new wind wind-supplying mouth, and the wind direction of described main air blower is reversible.
The workflow of the present invention:
A: the operational mode of described system is divided into double source hot-air seasoning pattern, single source hot-air seasoning pattern, removal moisture drying mould
Formula and dedusting pattern；
B: described double source hot-air seasoning pattern is combustor 7 sky of fast lifting baking room 19 inner chamber together with heat pump machine 22
Temperature, the entry condition of described double source hot-air seasoning pattern is the air of baking room 19 inner chamber when described system starts to dry
Temperature is less than the intensification target temperature set；The air that termination condition is baking room 19 inner chamber of described double source hot-air seasoning pattern
Temperature reaches intensification target temperature after described system starts to dry first；
C: described single source hot-air seasoning pattern is the air themperature that heat pump machine 22 individually regulates baking room 19 inner chamber, described double
Source hot-air seasoning pattern terminates to start described single source hot-air seasoning pattern；The termination condition of described single source hot-air seasoning pattern is for drying
The relative humidity of stove room 19 inner chamber is equal to the desired value set；
D: described removal moisture drying pattern is that less than 5 DEG C or relative humidity is more than when the wet-bulb depression in baking room 19
When 70%, in heat pump, machine airduct switch 2 is opened, and machine airduct 14 and blast pipe 1.1 in connection heat pump open scalable dehumidifying simultaneously
Automatically-controlled door 21；Scalable dehumidifying is closed certainly when the wet-bulb depression in baking room 19 reaches 10 DEG C or relative humidity is less than 55%
Dynamic door 21；When the wet-bulb depression in baking room 19 reaches 15 DEG C or relative humidity is less than 40%, machine airduct switch 2 in heat pump
It is closed, cuts off machine airduct 14 and blast pipe 1.1 in heat pump；The relative humidity arranging air according to drying article all aridity comes
Reach the drying time of automatic control system；
E: described dedusting pattern is that after described single source hot-air seasoning pattern terminates 5 minutes, described adjustable air-port 26 is beaten
Opening, adjustable air-port baffle plate 13 blocks described main air duct 1.2.1, and described dedusting pattern includes inverting dedusting and rotating forward de-dusting cycle
Two flow processs, said two flow process wind direction is contrary.
The invention has the beneficial effects as follows:
1) present invention uses fully-automatic thermostatic height air quantity low humidity stoving process, and combustor and heat pump combine quick heating, with
Time can accelerate wind speed and reduce humidity, reduce drying time.Offer equipment service efficiency.
2) present invention uses closed cycle waste heat entirely to reclaim, and in utilizing heat pump, machine replaces removing in tradition drying plant simultaneously
Wet machine, energy consumption is low, and efficiency is high；Native system uses 1 degree of electricity to be equal to conventional heat pump drying system and uses the drying effect of 10 degree of electricity
(refrigeration efficiency EER:1=3, heats efficiency COP:1=4, and waste heat recovery is 1/2).1 degree of electricity can be dehydrated about 8 jin, be dried 10～
30 kilograms of materials.
3) sealing and circulating of the present invention is unrelated with ambient temperature, can adapt to throughout the year, and energy-saving benefit is high；
4) present invention takes removal moisture drying, is not affected by ambient temperature, and ambient temperature is relatively low can also reach fast rapid-curing cutback
Dry effect, 15 DEG C of-70 DEG C of any settings of baking temperature, it is dried humidity 10%～90%, arbitrarily realizes.
5) confined space of the present invention arbitrarily arranges air circulation, bottom wind-guiding and accessory fan formation flow-disturbing and makes dry nothing
Dead angle ensures uniform drying effect.
6) sealing and circulating of the present invention is dried and is difficult to enter without outside contamination mosquito dust, it is ensured that article quality.
7) present invention uses high wind convection current without dead angle, and article are without stirring.
8) ease of Use system of the present invention, unmanned, automatically control.
Accompanying drawing explanation
Fig. 1 is to erect during double source enclosed efficient energy-saving drying system heating, drying in the present invention to cut open structural representation；
Fig. 2 is to erect during double source enclosed efficient energy-saving drying system dehumidification in the present invention to cut open structural representation；
Fig. 3 is the cross-sectional structural representation of double source enclosed efficient energy-saving drying system in the present invention；
Labelling in figure: labelling in figure: 1, circulation airduct (1.1, discharge pipe, 1.2, blast pipe (1.2.1, main air duct, 1.2.2
Auxiliary air channel)), 2, machine airduct switch in heat pump, 3, air outlet, 4, smoke exhaust pipe, 5, smoke exhaust pipe fin, 6, the new wind of scalable mend wind
Mouthful, 7, combustor, 8, air heat exchanger, 9, air heat exchanger fin, 10, dust removal and filtration net, 11, air inlet, 12, main air blower,
13, adjustable air-port baffle plate, 14, machine airduct in heat pump, 15, adjustable wind deflector, 16, ventilative orifice plate, 17, material table, 18, protect
Temperature plate, 19, baking room, 20, thermal-insulated blind, 21, scalable dehumidifying automatically-controlled door, 22, heat pump machine (22.1, machine in heat pump, 22.2,
The outer machine of heat pump), 23, cool air hose, 25, accessory fan, 26, adjustable air-port, 27, stock guide, 28, automatic stuff-conveying machine, 29, automatically
Cutting machine.
Detailed description of the invention
For making the object, technical solutions and advantages of the present invention clearer, below in conjunction with accompanying drawing, the present invention is made into one
Step ground describes in detail.
See Fig. 1-3, double source enclosed efficient energy-saving drying system, it is characterised in that include baking room 19, combustor 7, heat
Pump 22 and circulation airduct 1, circulation airduct 1 includes that discharge pipe 1.1 and blast pipe 1.2, described blast pipe 1.2 connect baking room 19
Air inlet 11, discharge pipe 1.1 connects the air outlet 3 of baking room, and heat pump 22 includes machine and the outer machine of heat pump in heat pump, wherein, heat pump
Interior machine is arranged on blast pipe 1.2, and the outer machine of heat pump is arranged on discharge pipe, and the position of the outer machine of discharge pipe correspondence heat pump is provided with cold
Solidifying water out, is provided with air heat exchanger 8 between discharge pipe 1.1 and blast pipe 1.2, described air heat exchanger 8 is connected with combustor 7
And heated by combustor 7.Described heat pump machine 22 includes machine 22.2 in the outer machine 22.1 of heat pump and heat pump, and described drying system is also wrapped
Include machine airduct 14 and machine airduct switch 2 in heat pump in heat pump, in outside described heat pump, machine 22.1 is located at heat pump in machine airduct 14, described
In heat pump, machine airduct 14 two ends communicate with discharge pipe 1.1, and in described heat pump, machine airduct 14 two ends all set with discharge pipe 1.1 junction
There is machine airduct switch 2 in heat pump.Material table 17 it is provided with, the blast pipe between heat pump 22 and baking room 19 1.2 points in baking room
For main air duct 1.2.1 and auxiliary air channel 1.2.2, it is provided with main air blower 12 in main air duct 1.2.1, arranges in auxiliary air channel 1.2.1
Having accessory fan 25, wherein, main air duct 1.2.1 and baking room 19 connecting place are positioned at below material table, auxiliary air channel 1.2.1 and baking
Stove room 19 connecting place is positioned at above material table.Main air duct 1.2.1 and auxiliary air channel 1.2.1 is respectively provided with the connecting place of baking room 19
There is adjustable wind deflector.Described main air duct 1.2.1 is provided with adjustable air-port 26.Described discharge pipe 1.1 and described heat pump machine 22
It is fitted with dust removal and filtration net 10；The scalable dehumidifying automatically-controlled door 21 that described baking room 19 is provided above.The drying of described system
Both sides, room 19 are warming plate 18, and additionally both sides are to be rolled onto the thermal-insulated blind 20 above baking room.Described material table 17 is provided with
Spiracular plate 16, described material table 17 connects stock guide 27, and described stock guide 27 connects automatic stuff-conveying machine 28, described conveyer
Automatic harvester 29 is installed on 28.Described air heat exchanger 8 is externally provided with air heat exchanger fin 9, on described air heat exchanger 8
Side is provided with smoke exhaust pipe 4 outside described in smoke exhaust pipe 4 and is provided with smoke exhaust pipe fin 5.Described circulation airduct 1 is provided with scalable new wind wind-supplying mouth
6, the wind direction of described main air blower 12 is reversible.
The operation of described system is completed by control panel, and control model is as follows:
A: the operational mode of described system is divided into double source hot-air seasoning pattern, single source hot-air seasoning pattern, removal moisture drying mould
Formula and dedusting pattern；
B: described double source hot-air seasoning pattern is combustor 7 sky of fast lifting baking room 19 inner chamber together with heat pump machine 22
Temperature, the entry condition of described double source hot-air seasoning pattern is the air of baking room 19 inner chamber when described system starts to dry
Temperature is less than the intensification target temperature set；The air that termination condition is baking room 19 inner chamber of described double source hot-air seasoning pattern
Temperature reaches intensification target temperature after described system starts to dry first；
C: described single source hot-air seasoning pattern is the air themperature that heat pump machine 22 individually regulates baking room 19 inner chamber, described double
Source hot-air seasoning pattern terminates to start described single source hot-air seasoning pattern；The termination condition of described single source hot-air seasoning pattern is for drying
The relative humidity of stove room 19 inner chamber is equal to the desired value set；
D: described removal moisture drying pattern is that less than 5 DEG C or relative humidity is more than when the wet-bulb depression in baking room 19
When 70%, in heat pump, machine airduct switch 2 is opened, and machine airduct 14 and blast pipe 1.1 in connection heat pump open scalable dehumidifying simultaneously
Automatically-controlled door 21；Scalable dehumidifying is closed certainly when the wet-bulb depression in baking room 19 reaches 10 DEG C or relative humidity is less than 55%
Dynamic door 21；When the wet-bulb depression in baking room 19 reaches 15 DEG C or relative humidity is less than 40%, machine airduct switch 2 in heat pump
It is closed, cuts off machine airduct 14 and blast pipe 1.1 in heat pump；The relative humidity arranging air according to drying article all aridity comes
Reach the drying time of automatic control system；
E: described dedusting pattern is that after described single source hot-air seasoning pattern terminates 5 minutes, described adjustable air-port 26 is beaten
Opening, adjustable air-port baffle plate 13 blocks described main air duct 1.2.1, and described dedusting pattern includes inverting dedusting and rotating forward de-dusting cycle
Two flow processs, said two flow process wind direction is contrary.
The foregoing is only presently preferred embodiments of the present invention, not in order to limit the present invention, all spirit in the present invention and
Within principle, any modification, equivalent substitution and improvement etc. made, should be included within the scope of the present invention.
Claims (10)
1. double source enclosed efficient energy-saving drying system, it is characterised in that include baking room (19), combustor (7), heat pump (22),
And circulation airduct (1), circulation airduct (1) includes discharge pipe (1.1) and blast pipe (1.2), and described blast pipe (1.2) connects dries
The air inlet (11) in room (19), discharge pipe (1.1) connects the air outlet (3) of baking room, and heat pump (22) includes machine and heat pump in heat pump
Outer machine, wherein, in heat pump, machine is arranged on blast pipe (1.2), and the outer machine of heat pump is arranged on discharge pipe, outside discharge pipe correspondence heat pump
The position of machine is provided with condensation-water drain, is provided with air heat exchanger (8), described sky between discharge pipe (1.1) and blast pipe (1.2)
Gas heat exchanger (8) is connected with combustor (7) and passes through combustor (7) heating.
Double source enclosed efficient energy-saving drying system the most according to claim 1, it is characterised in that described heat pump machine (22) wraps
Including machine (22.2) in the outer machine (22.1) of heat pump and heat pump, described drying system also includes machine airduct (14) and machine in heat pump in heat pump
Airduct switch (2), in the outer machine (22.1) of described heat pump is located at heat pump, machine airduct (14) is interior, machine airduct (14) two ends in described heat pump
Communicating with discharge pipe (1.1), in described heat pump, machine airduct (14) two ends and discharge pipe (1.1) junction are designed with machine wind in heat pump
Pipe switch (2).
Double source enclosed efficient energy-saving drying system the most according to claim 1, it is characterised in that be provided with thing in baking room
Material platform (17), the blast pipe (1.2) between heat pump (22) and baking room (19) is divided into main air duct (1.2.1) and auxiliary air channel
(1.2.2), it is provided with main air blower (12) in main air duct (1.2.1), in auxiliary air channel (1.2.1), is provided with accessory fan (25),
Wherein, main air duct (1.2.1) and baking room (19) connecting place are positioned at below material table, auxiliary air channel (1.2.1) and baking room
(19) connecting place is positioned at above material table.
Double source enclosed efficient energy-saving drying system the most according to claim 2, it is characterised in that main air duct (1.2.1) and
Auxiliary air channel (1.2.1) is provided with adjustable wind deflector with the connecting place of baking room (19).
Double source enclosed efficient energy-saving drying system the most according to claim 3, it is characterised in that described main air duct
(1.2.1) adjustable air-port (26) is installed.
Double source enclosed efficient energy-saving drying system the most according to claim 1, it is characterised in that described discharge pipe (1.1)
It is fitted with dust removal and filtration net (10) with described heat pump machine (22)；The scalable dehumidifying that described baking room (19) is provided above is automatically
Door (21).
Double source enclosed efficient energy-saving drying system the most according to claim 2, it is characterised in that the baking room of described system
(19) both sides are warming plate (18), and additionally both sides are to be rolled onto the thermal-insulated blind (20) above baking room.
Double source enclosed efficient energy-saving drying system the most according to claim 2, it is characterised in that described material table (17) sets
Having ventilative orifice plate (16), described material table (17) connects stock guide (27), and described stock guide (27) connects automatic stuff-conveying machine
(28), described conveyer (28) is provided with automatic harvester (29).
Double source enclosed efficient energy-saving drying system the most according to claim 1, it is characterised in that described air heat exchanger
(8) being externally provided with air heat exchanger fin (9), described air heat exchanger (8) is arranged over smoke exhaust pipe (4) described smoke exhaust pipe (4) outward
Portion is provided with smoke exhaust pipe fin (5).
Double source enclosed efficient energy-saving drying system the most according to claim 1, it is characterised in that described circulation airduct (1)
Being provided with scalable new wind wind-supplying mouth (6), the wind direction of described main air blower (12) is reversible.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610536436.1A CN106196913A (en) | 2016-07-08 | 2016-07-08 | Double source enclosed efficient energy-saving drying system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610536436.1A CN106196913A (en) | 2016-07-08 | 2016-07-08 | Double source enclosed efficient energy-saving drying system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106196913A true CN106196913A (en) | 2016-12-07 |
Family
ID=57472928
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610536436.1A Pending CN106196913A (en) | 2016-07-08 | 2016-07-08 | Double source enclosed efficient energy-saving drying system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106196913A (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106989572A (en) * | 2017-05-27 | 2017-07-28 | 江苏省农业科学院 | A kind of soil batch Quick-air-drying device |
| CN108317851A (en) * | 2018-04-09 | 2018-07-24 | 成都朗博旺科技发展有限公司 | A kind of commutation drying grain storage apparatus |
| CN108332550A (en) * | 2018-03-30 | 2018-07-27 | 成都朗博旺科技发展有限公司 | A kind of bidirectional ventilated drying equipment of grain |
| CN109387043A (en) * | 2018-11-25 | 2019-02-26 | 四川美立方门业有限公司 | Interior circulation townhouse formula anti-fire door core board heat drying device |
| CN112856950A (en) * | 2021-01-20 | 2021-05-28 | 广东纽恩泰新能源科技发展有限公司 | Efficient energy-saving heat pump drying system capable of heating in stages |
| CN113639531A (en) * | 2021-08-25 | 2021-11-12 | 安徽金锡机械科技有限公司 | Hot air supply system for grain drying machine and grain drying machine |
| CN113847794A (en) * | 2021-09-13 | 2021-12-28 | 益阳味芝元食品有限公司 | Circulating drying method for processing spicy fish blocks |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2593142Y (en) * | 2003-01-06 | 2003-12-17 | 张璧光 | Multifunctional heat pump drier |
| CN200965390Y (en) * | 2006-06-30 | 2007-10-24 | 江西省科学院食品工程创新中心 | Dryer integrated with the heat pump and hot air |
| CN103175382A (en) * | 2011-12-26 | 2013-06-26 | 中国科学院理化技术研究所 | Heat pump drying system |
| CN103604288A (en) * | 2013-11-20 | 2014-02-26 | 四川双亿实业有限公司 | Totally-enclosed double-effect heat recycling double-source ultrahigh-temperature heat pump dryer and method for implementing same |
| CN203758201U (en) * | 2014-01-07 | 2014-08-06 | 天津商业大学 | Fully-automatic sealed type heat pump drying system |
| CN105222566A (en) * | 2015-10-30 | 2016-01-06 | 江门市达能环保节能科技有限公司 | A kind of heat pump drying system with dehumidifier and Waste Heat Reuse |
| CN206001814U (en) * | 2016-07-08 | 2017-03-08 | 四川自然道节能科技有限公司 | Double source closed recovery drying system |
-
2016
- 2016-07-08 CN CN201610536436.1A patent/CN106196913A/en active Pending
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2593142Y (en) * | 2003-01-06 | 2003-12-17 | 张璧光 | Multifunctional heat pump drier |
| CN200965390Y (en) * | 2006-06-30 | 2007-10-24 | 江西省科学院食品工程创新中心 | Dryer integrated with the heat pump and hot air |
| CN103175382A (en) * | 2011-12-26 | 2013-06-26 | 中国科学院理化技术研究所 | Heat pump drying system |
| CN103604288A (en) * | 2013-11-20 | 2014-02-26 | 四川双亿实业有限公司 | Totally-enclosed double-effect heat recycling double-source ultrahigh-temperature heat pump dryer and method for implementing same |
| CN203758201U (en) * | 2014-01-07 | 2014-08-06 | 天津商业大学 | Fully-automatic sealed type heat pump drying system |
| CN105222566A (en) * | 2015-10-30 | 2016-01-06 | 江门市达能环保节能科技有限公司 | A kind of heat pump drying system with dehumidifier and Waste Heat Reuse |
| CN206001814U (en) * | 2016-07-08 | 2017-03-08 | 四川自然道节能科技有限公司 | Double source closed recovery drying system |
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106989572A (en) * | 2017-05-27 | 2017-07-28 | 江苏省农业科学院 | A kind of soil batch Quick-air-drying device |
| CN108332550A (en) * | 2018-03-30 | 2018-07-27 | 成都朗博旺科技发展有限公司 | A kind of bidirectional ventilated drying equipment of grain |
| CN108332550B (en) * | 2018-03-30 | 2023-11-10 | 成都朗博旺科技发展有限公司 | Grain bidirectional ventilation drying equipment |
| CN108317851A (en) * | 2018-04-09 | 2018-07-24 | 成都朗博旺科技发展有限公司 | A kind of commutation drying grain storage apparatus |
| CN108317851B (en) * | 2018-04-09 | 2023-11-21 | 成都朗博旺科技发展有限公司 | Reversing drying grain storage device |
| CN109387043A (en) * | 2018-11-25 | 2019-02-26 | 四川美立方门业有限公司 | Interior circulation townhouse formula anti-fire door core board heat drying device |
| CN109387043B (en) * | 2018-11-25 | 2023-07-04 | 四川美立方门业有限公司 | Internal circulation combined fireproof door core board heating and drying device |
| CN112856950A (en) * | 2021-01-20 | 2021-05-28 | 广东纽恩泰新能源科技发展有限公司 | Efficient energy-saving heat pump drying system capable of heating in stages |
| CN113639531A (en) * | 2021-08-25 | 2021-11-12 | 安徽金锡机械科技有限公司 | Hot air supply system for grain drying machine and grain drying machine |
| CN113847794A (en) * | 2021-09-13 | 2021-12-28 | 益阳味芝元食品有限公司 | Circulating drying method for processing spicy fish blocks |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN105605910B (en) | A kind of operational mode and structure of recycle heat formula heat pump drying device | |
| CN106196913A (en) | Double source enclosed efficient energy-saving drying system | |
| CN106855353A (en) | Heat pump drying equipment and drying means with dehumidification type Yu hydrofuge type handoff functionality | |
| CN204830702U (en) | Air source heat pump bakes room | |
| CN203443301U (en) | Integrated heat pump drying unit for heating and dehumidifying air source and recovering heat | |
| CN205843311U (en) | A kind of Novel multifunctional heat pump drying all-in-one | |
| CN205561498U (en) | Joint hot air drying device of full -automatic high -efficient low temperature dehumidification | |
| CN104776691B (en) | A kind of multi-functional dry fruit dries constant-temperature house | |
| CN206001814U (en) | Double source closed recovery drying system | |
| CN105029655A (en) | Energy-saving type garden staff heat pump drying device | |
| CN204994577U (en) | Energy -saving fruit vegetables heat pump drying device | |
| CN104482748B (en) | Air source heat pump hot-air fan with combined operating modes | |
| CN107036428A (en) | Solar energy and air source heat pump double source joint drying system | |
| CN209763716U (en) | Energy-saving drying system | |
| CN208430020U (en) | A kind of air heat circulation formula sludge drying system | |
| CN105486037B (en) | The heat pump drying equipment of solar energy heating and convertible wind direction | |
| CN209415908U (en) | A kind of combined heat pump dehumidifying integrated machine of the dual heat recovery function of band | |
| CN104896882B (en) | A kind of combined dryer | |
| CN201095705Y (en) | Heat pump type clothes drying closet | |
| CN209165936U (en) | A kind of energy-saving heat pump dryer | |
| CN204902523U (en) | Super high temperature heat pump drying system | |
| CN208536530U (en) | A kind of energy-saving and environment-friendly hot air circulation air energy heat pump dryer | |
| CN206989605U (en) | Integral type high temperature drying dehumidification machine | |
| CN107036407A (en) | Natural dehumidifying drying system | |
| CN106562466A (en) | Intensive type curing barn capable of realizing afterheat recycling and zero pollutant emission |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20161207 |
|
| RJ01 | Rejection of invention patent application after publication |