CN209498542U - Interior circulating dehumidification bulk curing barn based on air energy - Google Patents
Interior circulating dehumidification bulk curing barn based on air energy Download PDFInfo
- Publication number
- CN209498542U CN209498542U CN201821968717.5U CN201821968717U CN209498542U CN 209498542 U CN209498542 U CN 209498542U CN 201821968717 U CN201821968717 U CN 201821968717U CN 209498542 U CN209498542 U CN 209498542U
- Authority
- CN
- China
- Prior art keywords
- heating
- air
- heat pump
- dehumidifying
- pump assembly
- 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
Links
- 238000007791 dehumidification Methods 0.000 title claims abstract description 72
- 238000010438 heat treatment Methods 0.000 claims abstract description 222
- 241000208125 Nicotiana Species 0.000 claims abstract description 92
- 235000002637 Nicotiana tabacum Nutrition 0.000 claims abstract description 92
- 238000011049 filling Methods 0.000 claims abstract description 90
- 238000000034 method Methods 0.000 claims abstract description 57
- 230000008569 process Effects 0.000 claims abstract description 44
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 124
- 239000012224 working solution Substances 0.000 claims description 48
- 238000001816 cooling Methods 0.000 claims description 25
- 230000008676 import Effects 0.000 claims description 18
- 230000005611 electricity Effects 0.000 claims description 15
- 238000005485 electric heating Methods 0.000 claims description 12
- 230000001681 protective effect Effects 0.000 claims description 11
- 238000001035 drying Methods 0.000 claims description 9
- 238000006243 chemical reaction Methods 0.000 claims description 7
- 238000004891 communication Methods 0.000 claims description 6
- 238000009833 condensation Methods 0.000 claims description 6
- 230000005494 condensation Effects 0.000 claims description 6
- 230000018044 dehydration Effects 0.000 claims description 5
- 238000006297 dehydration reaction Methods 0.000 claims description 5
- 239000007788 liquid Substances 0.000 claims description 5
- 238000012544 monitoring process Methods 0.000 claims description 5
- 238000000819 phase cycle Methods 0.000 claims description 5
- 230000001737 promoting effect Effects 0.000 claims description 5
- 241000196324 Embryophyta Species 0.000 claims description 4
- 238000013500 data storage Methods 0.000 claims description 4
- 230000003993 interaction Effects 0.000 claims description 4
- 230000007257 malfunction Effects 0.000 claims description 4
- 230000009897 systematic effect Effects 0.000 claims description 4
- 239000000498 cooling water Substances 0.000 claims description 3
- 238000003780 insertion Methods 0.000 claims description 3
- 230000037431 insertion Effects 0.000 claims description 3
- 238000005507 spraying Methods 0.000 claims description 3
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 claims description 2
- 230000001502 supplementing effect Effects 0.000 claims 1
- 230000009286 beneficial effect Effects 0.000 abstract description 3
- 230000001276 controlling effect Effects 0.000 description 14
- 239000003245 coal Substances 0.000 description 11
- 210000003205 muscle Anatomy 0.000 description 9
- 239000000446 fuel Substances 0.000 description 8
- 239000007789 gas Substances 0.000 description 7
- 238000011161 development Methods 0.000 description 6
- 230000018109 developmental process Effects 0.000 description 6
- 238000010586 diagram Methods 0.000 description 6
- 230000008859 change Effects 0.000 description 5
- 238000006073 displacement reaction Methods 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 238000011160 research Methods 0.000 description 4
- 230000015572 biosynthetic process Effects 0.000 description 3
- 238000005265 energy consumption Methods 0.000 description 3
- 238000012545 processing Methods 0.000 description 3
- 239000013589 supplement Substances 0.000 description 3
- 238000009423 ventilation Methods 0.000 description 3
- 239000002028 Biomass Substances 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 229910002056 binary alloy Inorganic materials 0.000 description 2
- 230000015556 catabolic process Effects 0.000 description 2
- 235000019504 cigarettes Nutrition 0.000 description 2
- 229910052802 copper Inorganic materials 0.000 description 2
- 239000010949 copper Substances 0.000 description 2
- 238000006731 degradation reaction Methods 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 230000008020 evaporation Effects 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 230000000505 pernicious effect Effects 0.000 description 2
- 239000000779 smoke Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 238000003786 synthesis reaction Methods 0.000 description 2
- 238000009825 accumulation Methods 0.000 description 1
- 230000001174 ascending effect Effects 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 239000008280 blood Substances 0.000 description 1
- 210000004369 blood Anatomy 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 239000002283 diesel fuel Substances 0.000 description 1
- 238000009472 formulation Methods 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 230000010354 integration Effects 0.000 description 1
- 238000011031 large-scale manufacturing process Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 239000000178 monomer Substances 0.000 description 1
- 239000003345 natural gas Substances 0.000 description 1
- 239000002304 perfume Substances 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 239000000523 sample Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 238000010025 steaming Methods 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
- 210000003462 vein Anatomy 0.000 description 1
- 238000010792 warming Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Landscapes
- Drying Of Solid Materials (AREA)
Abstract
The utility model discloses a kind of interior circulating dehumidification bulk curing barns based on air energy, including cigarette-filling house, heat pump assembly, controller three parts;There are two connect branch to heat pump assembly with cigarette-filling house, branch one is connected by cigarette-filling house's return air inlet with heat pump assembly heating room, branch two is connected by parallel pipeline with heat pump assembly moist chamber by hydrofuge window, heat pump assembly air outlet introduces hot-air and enters cigarette-filling house for tobacco flue-curing, air stream in cigarette-filling house controls gas flow paths by control electric-powered shutter according to baking process curve and algorithm routine by controller, admits air into heat pump assembly and is internally heated or dehumidifies to realize the interior circulating dehumidification baking of tobacco leaf.The utility model has the beneficial effects that using internal air circulation heat supply and dehumidifying using heat pump assembly as supplying heat source, energy loss and gas discharge can be reduced, the yield rate of sound tobacco can be improved, the judging parameter of tobacco leaf can be improved.
Description
Technical field
The utility model belongs to tobacco leaf baking system, especially a kind of to be used using the tobacco flue-curing of internal air circulation and dehumidifying
Bulk curing barn.
Background technique
Barn is the essential professional equipment of tobacco flue-curing operation.With the constant growth of productivity, China's barn from
The open fire barn of earliest period, the development of natural ventilation type traditional flue-curing barn are heated air circulation type barn, general change close barn.20 end of the centurys
Phase, with China's science and technology and economic progress and the large-scale production of flue-cured tobacco, it is raw that bulk curing barn has gradually adapted to China's flue-cured tobacco
The new situations for producing sustainable development, represent the developing direction of current flue-cured tobacco equipment.The working principle of bulk curing barn baking system is
Forced ventilation is carried out as thrust using blower and hot air circulation mode heats the tobacco leaf in cigarette-filling house, promotes object inside tobacco leaf
Matter conversion, synthesis, dehydration, drying are regulated and controled the degradation of substance in tobacco leaf by temperature and humidity controller and wind-speed adjusting device, closed
At, conversion rate and tobacco leaf appearance coloration.Although bulk curing barn is in terms of dress smoke, baking quality of tobacco, intensive degree
Embody huge advantage.But still there are some problem needs to probe into and solve in application process, though it is on the one hand economic benefit
Promoted compared with traditional baking chamber, but cost is still higher, be mainly reflected in manual operation excessively cause cost of labor excessively high and
Forced-ventilated is wet to cause amount of heat to lose, and causes that energy loss is big, energy consumption cost is high;It on the other hand is baking automatic control equipment and technology
Not mature enough, it is not perfect or unreasonable to be mainly reflected in hardware facility, using fuel such as coal and petroleum as supplying heat source, causes to dry
The poor controllability of temperature in roasted journey, the present Research for being limited by hardware facility also indirectly affect the development of software aspects,
Cause software design too simple, control precision is low, increases manual operation load.This requires the development of China's bulk curing barn to build
Material selection, hardware device transformation, automatic control very well equipped etc. is made to be badly in need of incorporating new blood.
Tobacco flue-curing required time is generally 6 ~ 10 days, therefore must have enough heats to supply in baking process.
External tobacco flue-curing is using diesel oil, natural gas as fuel.And China is limited by the influence of economic development, the fuel that foreign countries use
It is not appropriate for China's national situation, China's tobacco flue-curing is mostly using coal, biomass as fuel, although biomass fuel source is wide and can
Regeneration, but cost is higher compared to coal, machine used in the natural ventilation airflow ascending manner barn to current toast from early stage
Tool divulges information thermal cycle barn generally using coal as main fuel.Since baking system equipment and baking technology backwardness lead to coal energy
Consumption is high, and every kilogram of dry tobacco leaf coal consumption is generally 1.5 ~ 2.0 kg, and utilization efficiency only has 30% or so, and release of burning
A large amount of harmful substance will cause serious pollution to environment, studies have shown that carrying out tobacco flue-curing, every kilogram of tobacco leaf using coal
It will lead to coal and generate NOx 0.0094kg、SO20.0132 kg and CO2 4.302kg.With the whole world for demand for fuel not
Disconnected to increase, cost used in tobacco flue-curing constantly rises.
Either curing barn cluster or monomer barn in the barn that current tobacco flue-curing operation uses, fixation hydrofuge phase flue-cured tobacco room
In damp and hot steam and the indoor high temperature air of drying muscle stage flue-cured tobacco be discharged outside flue-cured tobacco room in the form of in line, cause the energy compared with
Big waste.It is found by researches that the heat lost is about the 10% ~ 20% of total energy consumption, and highest is even during forced-ventilated is wet
Reach 25%, moreover, the cigarette perfume that tobacco leaf comes out also has been exhausted during the hydrofuge of tobacco flue-curing.In control technology
It is surely warm in baking process although existing bulk curing barn realizes semi-automation and automates substantially on baking process
Duration, heating rate, hydrofuge opportunity, coal opportunity, coal amount etc. still also rely on artificial experience and go to control, and due to existing
The overall structure and baking process of bulk curing barn baking system are all built upon on the wet dehumidification mode of coal heating, forced-ventilated,
Again because the hysteresis quality and uncontrollability of coal-fired heating make researcher insufficient for the research of control aspect, compares and have progressed
Property research also only achieving some achievements in terms of automatic stoking, automatic hydrofuge, and in intelligent control, intelligence baking, collection
Groupization baking aspect is still relatively backward.
Summary of the invention
In order to overcome problem described above, the utility model discloses a kind of interior circulating dehumidification based on air energy is intensive
Barn.
The technical solution of the utility model is: a kind of interior circulating dehumidification bulk curing barn based on air energy, including cigarette-filling house
Three (1-1), heat pump assembly (1-2), controller (1-3) parts, controller (1-3) are placed on the outside of heat pump assembly (1-2), heat pump
Device (1-2) is placed in bulk curing barn original heating room position, and stream of hot air by heating is from cigarette-filling house's air inlet or heat pump assembly
Air outlet (1-6) enters cigarette-filling house (1-1) and is used for tobacco flue-curing, and air stream after being exchanged heat with tobacco leaf is from cigarette-filling house's air outlet
(1-5) discharge, interior circulating-heating stage air flow through electric-powered shutter (1-7) heating internal back to heat pump assembly (1-2)
Room (1-9), interior circulating dehumidification stage air flow through hydrofuge window (1-4), hydrofuge window outlet air parallel pipeline (1-8), heat pump dress
Put back into air port (1-11) moist chamber (1-10) internal back to heat pump assembly (1-2);It is characterized in that: controller (1-3) passes through
Sensor acquires the running parameter of cigarette-filling house (1-1) internal temperature and humidity, heat pump assembly (1-2) internal electric equipment, through embedded
The main control chip operation of baking process algorithm routine simultaneously exports control instruction, control heat pump assembly (1-2) internal electric equipment with
Realize that the interior circulating dehumidification of tobacco leaf intelligently toasts;Heat pump assembly (1-2) includes heating/dehumidification system, constant temperature system, moist chamber
(1-10), heating room (1-9), moist chamber (1-10) is independent cabinet in heat pump assembly (1-2), and box house, which is integrated with, to be passed through
Condense the dehumidify evaporimeter (2-5) that air removes moisture in air, for by dried Cryogenic air and damp-heat air into
The total-heat exchanger (2-7) of row heat exchange, for filling the U-shaped water pond (2-14) of condensed water, top of the box is provided with for that will fill
Damp-heat air is pumped into the dehumidifying blower (2-9) that moist chamber dehumidifies, dehumidifying blower (2-9) and heat pump assembly return air inlet in smoke-box
(1-11) connection, the bottom of box are provided with the drainpipe (2-15) for the condensed water accumulated in moist chamber to be discharged, body side
It is provided with the moist chamber air outlet (2-16) for being used to introduce the air dried oven heats being connected with heating room;Heating
Room (1-9) is the separate space body for having two return air paths in heat pump assembly (1-2), and a return air path is to be gone out by cigarette-filling house
Air port (1-5) passes through the electric-powered shutter (1-7) being placed at the top of heating room (1-9) and is pumped into the air in cigarette-filling house (1-1)
Heating room (1-9) is internally heated, and another return air path passes through the heating room return air inlet that is connected with moist chamber (1-10)
The air for having exchanged heat dry is introduced in heating room (1-9) and is heated by (2-17), and the heating room bottom (1-9) is equipped with heat pump
Device air outlet (1-6), which is mutually common to for the air of heating to be discharged into cigarette-filling house (1-1) with cigarette-filling house (1-1), carries out tobacco leaf baking
Roasting, heating room (1-9) has been internally integrated circulating fan (2-19), electric heating device (2-18), condenser (2-6), condenser
(2-6) is placed under heating room return air inlet (2-17) for heating the air for flowing through condenser, electric heating device (2-18)
It being placed under condenser (2-6) for assisting heating, circulating fan (2-19) is placed under electric heating device (2-18),
Using the axial flow blower with high, low speed working method, for promoting circulating for baking system inner air;It heats/removes
The wet system integration 3 structures and the consistent heating/dehumidifying subsystem of working principle, for the heat in Tobacco Leaf Curing
Supply and dehydration dehumidifying respectively heat/dehumidify subsystem A, heating/dehumidifying subsystem B, heating/dehumidifying subsystem C, 3 systems
Mutually indepedent between heat/dehumidifying subsystem, each, which heats/dehumidify subsystem, heating mode and dehumidification mode, single son
The heating mode and dehumidification mode of system are interrelated, and the switching of work relationship and mode between 3 subsystems is by controller
The embedded mobile GIS program of (1-3) based on baking process curve carries out intelligent control;Constant temperature system is used in tobacco flue-curing
The dehumidifying stage, which heats/dehumidifies, stablizes real-time dry-bulb temperature and control heating rate when subsystem opens dehumidification mode.
In the present invention, the heating/dehumidifying subsystem include compressor (2-1), dehumidify magnetic valve (2-2),
Heating solenoid valve (2-3), dehumidify evaporimeter (2-5), condenser (2-6), outdoor fan (2-8), is removed outdoor evaporator (2-4)
Wet blower (2-9), electric expansion valve (2-10), the working solution import of the working solution outlet and condenser (2-6) of compressor (2-1)
It is connected, enters the working solution handled by compressor in condenser (2-6) for heating the air for flowing through condenser, condensation
The working solution outlet of device connects the electric expansion valve (2- for adjusting heating capacity according to the temperature requirements of cigarette-filling house (1-1)
10), there are two branches in electric expansion valve (2-10) outlet, and a branch passes through for controlling the system for heating branch and starting or stoping
Thermoelectrical magnetic valve (2-3) is connected with the working solution import of outdoor evaporator (2-4), then by the outlet and pressure of outdoor evaporator (2-4)
Contracting machine (2-1), which is connected, constitutes the heating circulation loop of working solution, along with the outdoor wind being placed on heat pump assembly (1-2) shell
Machine (2-8) forms heating/dehumidifying subsystem heating operating mode, and another branch passes through for controlling dehumidifying branch starting
Or the dehumidify magnetic valve (2-2) stopped being connected with the working solution import of dehumidify evaporimeter (2-5), dehumidify evaporimeter (2-5)
Outlet has been connected to form the dehumidifying circulation loop of working solution with compressor (2-1), along with being placed at the top of moist chamber (1-10)
Dehumidifying blower (2-9) form heating/dehumidifying subsystem dehumidification work mode;Heating/dehumidifying subsystem A, heating/dehumidifying
The work in combination of subsystem B, heating/dehumidifying subsystem C heating mode and dehumidification mode are by controller (1-3) with baking process
Embedded mobile GIS program based on curve carries out intelligent control.
In the present invention, the constant temperature system include 3 water cooling heat exchangers (2-13), water circulating pump (2-11),
Water tank (2-12), tank drains pipe (2-20), cold water inlet (2-21), 3 water cooling heat exchanger (2-13) settings are filled in heat pump
It sets (1-2) box house to be wrapped in one section of working liquid pipe before dehumidify magnetic valve (2-2) wherein, is used for flowing through pipe
Working solution cool down, the outlet of 3 water cooling heat exchangers (2-13) is parallel-connected to water tank (2-12), water tank by water pipe
The outlet of (2-12) is connected to water circulating pump (2-11) water inlet, and the water outlet of water circulating pump (2-11) passes through water pipe connection in parallel
To the water inlet of 3 water cooling heat exchangers (2-13), one is formed for controlling 3 heatings/dehumidifying subsystem and opens dehumidification mode
When the heating rate of the real-time dry-bulb temperature and cooling water circulation loop of temperature fluctuation range;Use is additionally provided on water tank (2-12)
In the tank drains pipe (2-20) of cold water inlet (2-21) He Huanshui of supplement cold water, cold water inlet (2-21) and water tank row
Water pipe (2-20) is designed with manual switch, and constant temperature system is opened or closed by controller (1-3) according to baking process curve, reality
When the rate of temperature fall of wet-bulb temperature, the displacement for the discharge outlet that dehumidifies and real-time dry-bulb temperature and target temperature temperature difference it is common
It determines, whole process carries out intelligent control by the embedded mobile GIS program in controller (1-3) based on baking process curve.
In the present invention, the controller (1-3) includes main control chip minimum systematic module, power circuit, temperature
Spend acquisition module, numeral input and protective module, relay and its drive module, ULN2003 driving circuit, warning circuit, LCD
Touch display screen module, program and data memory module, communication interface circuit module;Main control chip minimum systematic module is used for root
According to the real time humiture of each stage Temperature Humidity Sensor acquisition of tobacco flue-curing, calculated by the insertion based on baking process curve
Method program controls 3 heatings/dehumidifying subsystem time for starting or stoping, running, heating mode or dehumidification mode respectively
Switching with combine;Power circuit includes rectification circuit and voltage conversion circuit, for 220V alternating current to be converted into each electricity
DC voltage required for the module of road;Temperature collecting module is used to monitor the compressor of temperature and humidity and heat pump unit in cigarette-filling house
Hydrojet temperature;Numeral input and protective module are used to guarantee the normal work of each electrical equipment, including phase sequence, blower overload
Protection, compressor high voltage protective, compressor low-voltage variation, the auxiliary hot overtemperature prote of electricity;Relay and its drive module are according to master control
The control instruction that chip is sent open or close the high low speed switching of solenoid valve, circulating fan, control A.C. contactor connects
It is logical to obtain disconnection;ULN2003 driving circuit is used for according to the real time humiture variation in method for flue-curing tobacco leaves curve and cigarette-filling house certainly
The dynamic aperture for adjusting electric-powered shutter and electric expansion valve;Warning circuit is used to prompt staff whole in Tobacco Leaf Curing
The malfunction of a roasting plant;LCD touch display screen is used to carry out numerical value and the equipment operation of human-computer interaction and display monitoring
State;The data that program and data storage are used for storage system working procedure, record and save each tobacco flue-curing;Communication connects
Mouth circuit module is carried out telecommunication for carrying out telecommunication with host computer with mobile phone terminal;By temperature collecting module acquisition
Input of the real time data as the embedded mobile GIS program based on baking process curve carries out operation in main control chip, determines
Control output quantity is obtained after plan, each performer is sent in the form of binary instruction, realizes circulating dehumidification intelligence in tobacco leaf
It can baking.
The utility model has the beneficial effects that: carrying out heat supply using three heatings/dehumidification system, it can reduce and petrochemical industry is fired
The burning of material, the discharge of Litter and pernicious gas can reduce the loss of heat using the interior circulation heating and dehumidifying of multipath,
The judging parameter of tobacco leaf can be improved in the yield rate that sound tobacco can be improved, and the control based on baking process curve is used to calculate
Method can reduce human interference, labor intensity, can reduce baking cost.
Detailed description of the invention
Fig. 1 is the overall system diagram of the utility model;
In figure: 1-1-cigarette-filling house, 1-2-heat pump assembly, 1-3-controller, 1-4-hydrofuge window, 1-5-cigarette-filling house
Air outlet, 1-6-cigarette-filling house's air inlet or heat pump assembly air outlet, 1-7-electric-powered shutter, 1-8-moistureproof window outlet air are in parallel
Pipeline, 1-9-heating room, 1-10-moist chamber, 1-11-heat pump assembly return air inlet.
Fig. 2 is the heat pump assembly embodiment block diagram of the utility model;
In figure: 2-1-compressor A, compressor B, compressor C, 2-2-dehumidify magnetic valve A, dehumidify magnetic valve B, dehumidifying electricity
Magnet valve C, 2-3-heating solenoid valve A, heating solenoid valve B, heating solenoid valve C, 2-4-outdoor evaporator, 2-5-dehumidifying evaporation
Device, 2-6-condenser, 2-7-total-heat exchanger, 2-8-outdoor fan, 2-9-dehumidifying blower 2-10-electric expansion valve A,
Electric expansion valve B, electric expansion valve C, 2-11 water circulating pump, 2-12-water tank, 2-13-water cooling heat exchanger A, water cooling heat exchanger,
The U-shaped water pond of water cooling heat exchanger C, 2-14-, 2-15-moist chamber drainpipe, 2-16-moist chamber air outlet, 2-17-heating room
Return air inlet, 2-18-electric heating device, 2-19-circulating fan, 2-20-tank drains pipe, 2-21-tank inlet pipe.
Fig. 3 is the controller embodiment block diagram of the utility model.
Specific embodiment
The following will be combined with the drawings in the embodiments of the present invention, carries out the technical scheme in the embodiment of the utility model
Clearly and completely describe, it is clear that the described embodiments are only a part of the embodiments of the utility model, rather than whole
Embodiment.Based on the embodiments of the present invention, those of ordinary skill in the art are without making creative work
Every other embodiment obtained, fall within the protection scope of the utility model.
Referring to attached drawing, Fig. 1 is the overall system diagram of the utility model.A kind of interior circulating dehumidification based on air energy is intensive
Barn, including three cigarette-filling house (1-1), heat pump assembly (1-2), controller (1-3) parts, controller (1-3) place heat pump dress
It sets on the outside of (1-2), heat pump assembly (1-2) is placed in bulk curing barn original heating room position;It is characterized in that: the heat for tobacco flue-curing is empty
Air-flow enters cigarette-filling house (1-1) from cigarette-filling house's air inlet or heat pump assembly air outlet (1-6), the air after being exchanged heat with tobacco leaf
Stream is discharged from cigarette-filling house's air outlet (1-5), and interior circulating-heating stage air flows through electric-powered shutter (1-7) back to heat pump assembly
(1-2) internal heating room (1-9), interior circulating dehumidification stage air flow through hydrofuge window (1-4), hydrofuge window outlet air parallel transistor
Road (1-8), heat pump assembly return air inlet (1-11) moist chamber (1-10) internal back to heat pump assembly (1-2);Controller (1-3)
Pass through the running parameter of the internal temperature and humidity of sensor acquisition cigarette-filling house (1-1), heat pump assembly (1-2) internal electric equipment, warp
The main control chip operation of embedded baking process algorithm routine simultaneously exports control instruction, and control heat pump assembly (1-2) internal electric is set
It is standby intelligently to be toasted with the interior circulating dehumidification for realizing tobacco leaf.Cigarette-filling house (1-1) and heat pump assembly (1-2) have two connection branch conducts
Inlet air flow path, branch one is connected by cigarette-filling house's air outlet (1-5) with the heating room (1-9) inside heat pump assembly will be from dress
Smoke-box is drained into the air heating of heating room, is placed with electric-powered shutter (1-7) between the two for controlling inside baking system
Inlet air flow path, according to the real-time dry and wet in tobacco leaf variation and positioned baking stage and cigarette-filling house in baking process
Ball temperature controls the path that baking system inner air flows to control the aperture of electric-powered shutter, avoids since air flows
Path it is too long and caused by energy loss, branch two by hydrofuge window (1-4) by hydrofuge window outlet air parallel pipeline (1-8) with
Heat pump assembly return air inlet (1-11), which is connected for cigarette-filling house's moist inside air to be drained into heat pump assembly moist chamber (1-10), to carry out
Exchange heat drying, and dried air is internally heated in heat pump assembly, then from heat pump assembly air outlet (1-6) by heating
Air stream discharges into cigarette-filling house and carries out tobacco flue-curing, and the air stream after being exchanged heat in cigarette-filling house with tobacco leaf is again from cigarette-filling house's outlet air
Mouth (1-5) or hydrofuge window (1-4) are again introduced into heat pump assembly and are heated, dehumidified, the air stream in Tobacco Leaf Curing
No gas is circulated between cigarette-filling house and heat pump assembly and is discharged into outdoor, and is not used using heat pump assembly heating air
Any fuel is discharged without polluted gas;Controller (1-3) is placed on the outside of heat pump assembly, is filled with the temperature acquisition in cigarette-filling house
It sets, the electrical equipment in heat pump assembly, digital protection device are connected, the signal inside controller and cigarette-filling house and heat pump assembly
Acquisition device, electrical control equipment are connected, the signal and heat pump dress of the temperature sensor acquisition in heat pump assembly and cigarette-filling house
The digital input signals of interior protection equipment are set as the defeated of the algorithm routine being embedded in based on baking process curve in controller
Enter value, carries out operation by the main control chip inside controller and obtain output control instruction, the actuator being transferred on controller
Part is controlled the electrical equipment in heat pump assembly by performer and is toasted with the interior circulating dehumidification for realizing tobacco leaf.
Heat pump assembly is spaced with cigarette-filling house by a face wall close to cigarette-filling house side, and the upper and lower ends of wall respectively have one to open
Mouthful, the opening of upper end is as return air inlet, and as air outlet, two air ports will heat room and connect with cigarette-filling house the opening of lower end
Come, an electric-powered shutter is placed at the top of the heat pump assembly under return air inlet, when tobacco flue-curing is not when needing the dehumidifying stage
It opens the electric-powered shutter heating room that is directly entered the air in cigarette-filling house in heat pump assembly to be heated, when needing to dehumidify
When, closing electric-powered shutter makes the air stream being discharged from cigarette-filling house all return heat pump assembly after heat pump assembly dehumidifies
It is heated heating room;Air stream in heat pump assembly heating room, cigarette-filling house, follow between the moist chamber three on heat pump assembly
Circulation is dynamic, does not have gas to be discharged into outdoor in entire Tobacco Leaf Curing, temperature sensor in cigarette-filling house and heat pump assembly plus
The indoor heating equipment of heat and circulating fan, heating/dehumidifying unit are connected with controller, temperature sensor temperature collection signal,
By the algorithm routine that the main control chip of preset baking process combination controller is internally embedded obtain output control two into
Control instruction is transferred to performer, is started by performer or close electrical equipment with reality by system instruction, main control chip
The interior circulating dehumidification baking of existing tobacco leaf.
Attached drawing 2 is the heat pump assembly embodiment block diagram of the utility model.Heat pump assembly (1-2) include heating/dehumidification system,
Constant temperature system, moist chamber (1-10), heating room (1-9);Moist chamber (1-10) is independent cabinet in heat pump assembly (1-2), case
Internal portion is integrated with the dehumidify evaporimeter (2-5) that moisture in air is removed by condensation air, is used for dried low temperature
Air and damp-heat air carry out the total-heat exchanger (2-7) of heat exchange, for filling the U-shaped water pond (2-14) of condensed water, cabinet top
Portion is provided with for damp-heat air in cigarette-filling house to be pumped into the dehumidifying blower (2-9) that moist chamber dehumidifies, and is dehumidified blower (2-9)
It is connect with heat pump assembly return air inlet (1-11), the bottom of box is provided with the drainpipe for the condensed water accumulated in moist chamber to be discharged
(2-15), body side are provided with the air introducing heating room for being used to dry being connected with the return air inlet (2-17) of heating room
The moist chamber air outlet (2-16) of heating;Heating room (1-9) is that have the independent empty of two return air paths in heat pump assembly (1-2)
Mesosome, a return air path are to pass through the electric-powered shutter being placed at the top of heating room (1-9) by cigarette-filling house's air outlet (1-5)
(1-7) by cigarette-filling house (1-1) air be pumped into heating room (1-9) be internally heated, another return air path by with remove
The heating room return air inlet (2-17) that moist chamber (1-10) is connected, by the air for having exchanged heat dry introduce heating room (1-9) in into
Row heating, the heating room bottom (1-9) are equipped with heat pump assembly air outlet (1-6) and are mutually common to cigarette-filling house (1-1) by the sky of heating
Gas is discharged into the interior progress tobacco flue-curing of cigarette-filling house (1-1), and heating room (1-9) has been internally integrated circulating fan (2-19), electricity auxiliary adds
Hot device (2-18), condenser (2-6), condenser (2-6) be placed in heating room return air inlet (2-17) under for heat flow through it is cold
The air of condenser, electric heating device (2-18) are placed under condenser (2-6) for assisting heating, circulating fan (2-19)
It is placed under electricity auxiliary heating (2-18), using the axial flow blower with high, low speed working method, for promoting baking system
Inner air circulates;Heating/dehumidification system is integrated with the consistent heating/dehumidifying subsystem of 3 structures and working principle
System respectively heats/dehumidifies subsystem A, heating/dehumidifying for the heat supply and dehydration dehumidifying in Tobacco Leaf Curing
System B, heating/dehumidifying subsystem C, mutually indepedent between 3 heatings/dehumidifying subsystem, each heats/dehumidifies subsystem
There are heating mode and dehumidification mode, the heating mode and dehumidification mode of single subsystem are interrelated, the work between 3 subsystems
The switching for making relationship and mode carries out intelligent control by embedded mobile GIS program of the controller (1-3) based on baking process curve
System;Constant temperature system, which is used to heat/dehumidify when subsystem opens dehumidification mode in the dehumidifying stage of tobacco flue-curing, stablizes real-time dry bulb
Temperature and control heating rate.Moist chamber (1-10) is integrated with as independent cabinet in heat pump assembly and is removed by condensation air
The dehumidify evaporimeter (2-5) of moisture in air, dehumidify evaporimeter are integrated with 3 as 3 heatings/dehumidifying subsystem public module
Working solution inlet-outlet connector is covered, 3 sets of working solution inlet-outlet connectors are mutually indepedent, and dehumidify evaporimeter is placed in the bottom moist chamber (1-10)
Portion is vertically-mounted, and the damp-heat air for being pumped into moist chamber from cigarette-filling house is dehydrated, and total-heat exchanger (2-7), which is placed in, to be removed
Above wet evaporator (2-5), for dried Cryogenic air and damp-heat air to be carried out heat exchange, total-heat exchanger (2-
7) there are an inlet side and an air side, inlet side is opposite with dehumidifying blower, and dehumidifying blower (2-9) is used for will be empty in cigarette-filling house
Gas is pumped into moist chamber, and relatively, heat pump assembly return air inlet (1-11) is logical by dehumidifying blower (2-9) and heat pump assembly return air inlet (1-11)
It crosses moistureproof window outlet air parallel pipeline to be connected with cigarette-filling house two hydrofuge windows (1-4), air side and dehumidifying air outlet (2-16)
Relatively, dehumidifying air outlet (2-16) is connected with heating room return air inlet (2-17) by dried air is discharged into moist chamber
Heating interior is heated, and is placed with the U-shaped water for filling the condensed water for passing through dehumidify evaporimeter dehumidification by condensation in dehumidifying bottom
Disk (2-14), U-shaped water pond are equipped with moist chamber drainpipe (2-15) and are used to that the condensed water accumulated in moist chamber to be discharged, avoid dehumidifying
The interior excessive water of accumulation, which is mixed into be again passed in cigarette-filling house in dried air, causes dehumidification efficiency to decline, and causes in cigarette-filling house
Humidity is excessively high to bake bad tobacco leaf;Heating room (1-9) is integrated with circulating fan (2- as independent spatial volume in heat pump assembly
19), electric heating device (2-18), condenser (2-6), heating room (2-36) have two return air paths, and a return air path is
The electric-powered shutter (1-7) for passing through the heating ceiling portion that is placed in (also at the top of heat pump assembly) by cigarette-filling house's air outlet (1-5) will
Air in cigarette-filling house is pumped into heating chamber and is heated, and cigarette-filling house's air outlet (1-5) is for introducing air in cigarette-filling house
Into heat pump assembly, electric-powered shutter (1-7) is used to control the path of baking system inner air flowing and directly from cigarette-filling house
The air capacity for flowing into heating room does not need the flavescence preliminary stage of dehumidifying or the dry muscle of moisture removal very little when tobacco flue-curing is in
The progress of heating room is directly entered without moist chamber by air in cigarette-filling house by fully opening electric-powered shutter when later stage
Heating, avoid as inlet air flow path is too long and caused by energy loss, when need dehumidify but moisture removal it is small when flavescence
Mid-term and dry muscle early period, adjust electric-powered shutter opening angle make portion of air directly pass through return air inlet one return to heating room into
Row heating, portion of air is heated by returning heating room after moist chamber progress removal moisture drying, when moisture removal is very big
When closure electric-powered shutter make the air in cigarette-filling house all pass through moist chamber carry out air heat humidity, wherein the size of moisture removal by
It fills smoke and displacement hourly determines, another is connected by heating room return air inlet (2-17) with dehumidifying, heats room return air inlet
(2-17), which is arranged between electric-powered shutter (1-7) and condenser (2-6), introduces heating room for the air Jing Guo removal moisture drying
Make that air flows through condenser (2-6) and electric heating device (2-18) is heated, heating room bottom be equipped with air outlet (1-6) with
Cigarette-filling house be mutually common to will be heated after air introduce cigarette-filling house carry out tobacco flue-curing, heat indoor condenser (2-6) and put
Be placed under electric-powered shutter (1-7) for heating the air for flowing through condenser, also have on condenser (2-6) 3 sets of working solutions into
Outlet connection, 3 sets of working solution inlet-outlet connectors are used as 3 heatings/dehumidifying subsystem, one module independently of each other, and electricity auxiliary adds
It is unlatching when reaching fast rapid-curing cutback muscle that hot device (2-18), which was placed under condenser (2-6) for the tobacco flue-curing dry muscle later period, can be contracted
The duration of short drying muscle stage, circulating fan (2-19) are placed under electric heating device (2-18), using axial flow blower and adopt
With the control of high low speed for promoting baking system inner air to flow, by circulating fan tune before tobacco flue-curing is in drying muscle stage
Whole is low or first gear, and the wind speed in gap promotes degradation, synthesis and the conversion of tobacco leaf inner material between the tobacco leaf leaf in reduction cigarette-filling house,
Open top gear after tobacco flue-curing is in drying muscle stage, avoid after the wilting dry plate of tobacco leaf due between tobacco leaf leaf gap cause greatly very much
Path short circuit causes front and back dry-bulb temperature error in cigarette-filling house to occur blue veins greatly or bake red cigarette;Heating/dehumidification system is integrated with 3
A heating/dehumidifying subsystem respectively heats/dehumidifies subsystem for the heat supply and dehydration dehumidifying in Tobacco Leaf Curing
Unite A, heating/dehumidifying subsystem B, heating/dehumidifying subsystem C, mutually indepedent between 3 heatings/dehumidifying subsystem, each system
Heat/dehumidifying subsystem has heating mode and dehumidification mode, and the heating mode and dehumidification mode of single subsystem are interrelated, and three
The switching of work relationship and mode between a subsystem is embedded in main control chip based on baking process curve by controller
Interior algorithm routine carries out intelligent control;Constant temperature system heats/dehumidifies subsystem unlatching in the dehumidifying stage for tobacco flue-curing and removes
Stablize real-time dry-bulb temperature and control heating rate when wet model.
In the present invention, heating/dehumidifying subsystem includes compressor (2-1), dehumidify magnetic valve (2-2), heating electricity
Magnet valve (2-3), outdoor evaporator (2-4), dehumidify evaporimeter (2-5), condenser (2-6), outdoor fan (2-8), dehumidifying blower
The working solution outlet of (2-9), electric expansion valve (2-10), compressor (2-1) is connected with the working solution import of condenser (2-6)
It connects, enters the working solution handled by compressor for heating the air for flowing through condenser in condenser (2-6), condenser
Working solution outlet connects the electric expansion valve (2-10) for adjusting heating capacity according to the temperature requirements of cigarette-filling house (1-1), electricity
There are two branches in sub- expansion valve (2-10) outlet, and a branch passes through for controlling the heating electromagnetism for heating branch and starting or stoping
Valve (2-3) is connected with the working solution import of outdoor evaporator (2-4), then outlet and compressor (2- by outdoor evaporator (2-4)
1) it is connected and constitutes the heating circulation loop of working solution, along with the outdoor fan (2-8) being placed on heat pump assembly (1-2) shell
Heating/dehumidifying subsystem heating operating mode is formd, another branch for controlling dehumidifying branch by starting or stoping
Dehumidify magnetic valve (2-2) be connected with the working solution import of dehumidify evaporimeter (2-5), the outlet of dehumidify evaporimeter (2-5) with
Compressor (2-1) has been connected to form the dehumidifying circulation loop of working solution, along with the dehumidifying being placed at the top of moist chamber (1-10)
Blower (2-9) forms heating/dehumidifying subsystem dehumidification work mode;Heating/dehumidifying subsystem A, heating/dehumidifying subsystem
B, the work in combination of heating/dehumidifying subsystem C heating mode and dehumidification mode is with baking process curve by controller (1-3)
The embedded mobile GIS program on basis carries out intelligent control.Heating/dehumidifying subsystem A includes compressor A(2-1), dehumidify magnetic valve A
(2-2), heating solenoid valve A(2-3), outdoor evaporator (2-4), dehumidify evaporimeter (2-5), condenser (2-6), outdoor fan
(2-8), dehumidifying blower (2-9), electric expansion valve A(2-10), compressor A(2-1) working solution outlet and condenser (2-6)
Working solution import I, which is connected, makes the high temperature and pressure working solution formed by compressor A(2-1) processing enter condenser and flow through cold
The air stream of condenser carries out heat exchange, and the working solution outlet I of condenser is connected with electric expansion valve A(2-10), when heating/remove
Heating load is automatically adjusted according to the heat demand of cigarette-filling house and real-time dry-bulb temperature rate of change when wet subsystem A is opened, electricity
Sub- expansion valve A(2-10) outlet You Liangtiao branch, a branch, which passes through, heats the heating that starts or stops of branch A for control
Solenoid valve A(2-3) it is connected with the working solution import I of outdoor evaporator (2-4), then outlet I and compressor I by outdoor evaporator
(2-1), which is connected, constitutes heating branch loop body, along with the outdoor fan (2-8) being placed on heat pump assembly constitutes system
The heating mode circuit heat/dehumidifying subsystem A, the dehumidifying that another branch is started or stoped by being used to control dehumidifying branch A
Solenoid valve A(2-2) it is connected with the working solution import I of dehumidify evaporimeter (2-5), the outlet I of dehumidify evaporimeter and compressor A
(2-1) has been connected to form dehumidifying branch loop body, along with the dehumidifying blower (2-9) for being placed in heating ceiling portion constitutes system
The dehumidification mode circuit heat/dehumidifying subsystem A;The heating/dehumidifying subsystem B includes compressor B(2-1), dehumidifying electromagnetism
Valve B(2-2), heating solenoid valve B(2-3), outdoor evaporator (2-4), dehumidify evaporimeter (2-5), condenser (2-6), outdoor wind
Machine (2-8), dehumidifying blower (2-9), electric expansion valve B(2-10), compressor B(2-1) working solution outlet with condenser (2-6)
Working solution import II be connected make by compressor B(2-1) processing formed high temperature and pressure working solution enter condenser and stream
The air stream for crossing condenser carries out heat exchange, and the working solution outlet II of condenser is connected with electric expansion valve B(2-10), works as system
Heat supply is automatically adjusted according to the heat demand of cigarette-filling house and real-time dry-bulb temperature rate of change when heat/dehumidifying subsystem B is opened
Amount, electric expansion valve B(2-10) outlet have two branches, a branch passes through to be heated branch B and starts or stops for controlling
Heating solenoid valve B(2-3) be connected with the working solution import II of outdoor evaporator (2-4), then by the outlet II of outdoor evaporator
It is connected with compressor B(2-1) and constitutes heating loop body branch, along with the outdoor fan (2-8) being placed on heat pump assembly
The heating mode circuit heating/dehumidifying subsystem B is constituted, another branch passes through for controlling dehumidifying branch B starting or stopping
Dehumidify magnetic valve B(2-2 only) it is connected with the working solution import II of dehumidify evaporimeter (2-5), the outlet II of dehumidify evaporimeter
It is connected to form dehumidifying loop body branch with compressor B(2-1), along with the dehumidifying blower (2- for being placed in heating ceiling portion
9) the dehumidification mode circuit heating/dehumidifying subsystem B is constituted;The heating/dehumidifying subsystem C includes compressor C(2-
1), dehumidify magnetic valve C(2-2), heating solenoid valve C(2-3), outdoor evaporator (2-4), dehumidify evaporimeter (2-5), work condensation
Device (2-6), outdoor fan (2-8), dehumidifying blower (2-9), electric expansion valve C(2-10), compressor C(2-1) working solution go out
Mouth be connected with the working solution import III of condenser (2-6) make by compressor C(2-1) processing formation high temperature and pressure working solution
Heat exchange, the working solution outlet III and electric expansion valve C(2- of condenser are carried out into condenser and the air stream for flowing through condenser
10) it is connected, heat demand and real-time dry-bulb temperature rate of change when heating/dehumidifying subsystem C is opened according to cigarette-filling house
To automatically adjust heating load, electric expansion valve C(2-10) outlet have two branches, a branch passes through for controlling heating branch
The heating solenoid valve C(2-3 that road C is started or stoped) it is connected with the working solution import III of outdoor evaporator (2-4), then by outdoor steaming
The outlet III of hair device is connected with compressor C(2-1) constitutes heating loop body branch, along with the room being placed on heat pump assembly
Outer blower (2-8) constitutes the heating mode circuit heating/dehumidifying subsystem C, and another branch passes through for controlling dehumidifying branch
The dehumidify magnetic valve C(2-2 that road C is started or stoped) it is connected with the working solution import III of dehumidify evaporimeter (2-5), dehumidifying evaporation
The outlet III of device and compressor C(2-1) it has been connected to form dehumidifying loop body branch, removing for ceiling portion is heated along with being placed in
Wet blower (2-9) constitutes the dehumidification mode circuit heating/dehumidifying subsystem C;Heating/dehumidifying subsystem A, B, C heating mould
The combination of formula and dehumidification mode is controlled by the algorithm routine that controller is embedded in based on baking process curve, when tobacco leaf dries
It bakes in the dry muscle stage, since heat demand amount is big and moisture removal hour, 3 heatings/dehumidifying subsystem can be made to be switched on heating mould
Formula, when the real time temperature of cigarette-filling house can be warming up to often within 5 minutes by the heating capacity of two subsystems or a subsystem again
The target temperature being raised to required for a hour, while the positioned baking stage needs to dehumidify, and can only open a heating/dehumidifying
The heating of subsystem or two heatings/dehumidifying subsystem heating, while other subsystems open dehumidification mode, work as two subsystems
Moisture removal when not being able to satisfy the dehumidification requirements in locating baking stage (rate that both dehumidified is slow, moisture removal is few), by three subsystems
It is both configured to dehumidification mode, while opening constant temperature mode and avoiding causing under dehumidification mode since real-time dry-bulb temperature is uncontrollable
Bad tobacco leaf is baked, when tobacco flue-curing is when turning yellow early period, can only open the heating mode of a subsystem.
In the present invention, the constant temperature system include 3 water cooling heat exchangers (2-13), water circulating pump (2-11),
Water tank (2-12), tank drains pipe (2-20), cold water inlet (2-21), 3 water cooling heat exchanger (2-13) settings are filled in heat pump
It sets (1-2) box house to be wrapped in one section of working liquid pipe before dehumidify magnetic valve (2-2) wherein, is used for flowing through pipe
Working solution cool down, the outlet of 3 water cooling heat exchangers (2-13) is parallel-connected to water tank (2-12), water tank by water pipe
The outlet of (2-12) is connected to water circulating pump (2-11) water inlet, and the water outlet of water circulating pump (2-11) passes through water pipe connection in parallel
To the water inlet of 3 water cooling heat exchangers (2-13), one is formed for controlling 3 heatings/dehumidifying subsystem and opens dehumidification mode
When the heating rate of the real-time dry-bulb temperature and cooling water circulation loop of temperature fluctuation range;Use is additionally provided on water tank (2-12)
In the tank drains pipe (2-20) of cold water inlet (2-21) He Huanshui of supplement cold water, cold water inlet (2-21) and water tank row
Water pipe (2-20) is designed with manual switch, and constant temperature system is opened or closed by controller (1-3) according to baking process curve, reality
When the rate of temperature fall of wet-bulb temperature, the displacement for the discharge outlet that dehumidifies and real-time dry-bulb temperature and target temperature temperature difference it is common
It determines, whole process carries out intelligent control by the embedded mobile GIS program in controller (1-3) based on baking process curve.It is permanent
Warm system includes water cooling heat exchanger A(2-13), water cooling heat exchanger B(2-13), water cooling heat exchanger C(2-13), water circulating pump (2-
11), water tank (2-12), tank drains pipe (2-20), cold water inlet (2-21), three water cooling heat exchangers are placed in heat pump assembly
The copper pipe in three heatings/dehumidifying subsystem dehumidification mode circuit is encased the work being used for copper pipe is flowed through respectively by box house
Liquid cools down, water cooling heat exchanger A(2-13), water cooling heat exchanger B(2-13), water cooling heat exchanger C(2-13) outlet pass through public affairs
Water pipe head altogether is connected to water tank (2-12), and water tank is used to store water when constant temperature system work, and water circulating pump (2-11) is by controlling
Device processed is controlled for promoting circulating for constant temperature system internal water, and cold water inlet (2-20) and row are additionally provided on water tank
Water pipe (2-21), cold water inlet (2-20) are equipped with manual switch and inject cold water in water tank for toasting initial stage for dehumidifying rank
Duan Kaiqi thermostatic type provides sufficient water and except wet spell supplements cold water when water temperature over-high in water tank exhausts, avoid due to
Cold water water shortage and cause dehumidification efficiency low, drainpipe (2-21) also be provided with manual switch for the megathermal period dehumidifying when by water cooling
The water temperature over-high of heat exchanger discharge and so that the interior water temperature over-high of water tank (2-12) is influenced dehumidification efficiency and heating rate, water tank (2-
12) one outlet is connected to the water inlet of water circulating pump, and the water outlet of water circulating pump (2-11) is connected to water by common end
Cold heat exchanger A(2-13), water cooling heat exchanger B(2-13), water cooling heat exchanger C(2-13) water inlet constitute loop body and use
The heating rate and temperature fluctuation range of real-time dry-bulb temperature when controlling three subsystems and opening dehumidification mode;Constant temperature system
Open and close by controller according to baking process curve, real-time wet-bulb temperature rate of temperature fall, dehumidify discharge outlet displacement
And the temperature difference of dry-bulb temperature and target temperature codetermines whole process by controller using baking process curve as base in real time
The algorithm routine of plinth insertion is controlled.
Attached drawing 3 is the controller embodiment block diagram of the utility model.Controller (1-3) includes main control chip minimum system mould
Block, power circuit, temperature collecting module, numeral input and protective module, relay and its drive module, ULN2003 driving electricity
Road, warning circuit, LCD touch display screen module, program and data memory module, communication interface circuit module;Main control chip is most
Mini system module is used for the real time humiture according to each stage Temperature Humidity Sensor acquisition of tobacco flue-curing, by with baking process song
Embedded mobile GIS program based on line controls 3 heatings/dehumidifying subsystem time for starting or stoping, running, heating respectively
The switching of mode or dehumidification mode with combine;Power circuit includes rectification circuit and voltage conversion circuit, for handing over 220V
Galvanic electricity is converted into DC voltage required for each circuit module;Temperature collecting module be used to monitor temperature and humidity in cigarette-filling house and
The compressor liquid-spraying temperature of heat pump unit;Numeral input and protective module are used to guarantee the normal work of each electrical equipment, including
Phase sequence, blower overload protection, compressor high voltage protective, compressor low-voltage variation, the auxiliary hot overtemperature prote of electricity;Relay and its
Drive module opens or closes the switching of high low speed, the control of solenoid valve, circulating fan according to the control instruction that main control chip is sent
The connection of A.C. contactor processed obtains disconnection;ULN2003 driving circuit is used for according in method for flue-curing tobacco leaves curve and cigarette-filling house
The aperture of real time humiture variation automatic adjustment electric-powered shutter and electric expansion valve;Warning circuit is used in Tobacco Leaf Curing
The malfunction of the middle prompt entire roasting plant of staff;LCD touch display screen is for carrying out human-computer interaction and display monitoring
Numerical value and equipment running status;Program and data storage are used for storage system working procedure, record and save every hypo-tobacco leaf
The data of baking;Communication interface circuit module is carried out telecommunication for carrying out telecommunication with host computer with mobile phone terminal;It will
Input of the real time data of temperature collecting module acquisition as the embedded mobile GIS program based on baking process curve, in master control
Control output quantity is obtained after carrying out operation, decision in chip, each performer is sent in the form of binary instruction, is realized
Circulating dehumidification intelligently toasts in tobacco leaf.The main control chip minimum system, for according to tobacco flue-curing stage, temperature sensor
The real time temperature of acquisition, the number of three heatings/dehumidification system operation time automatic start-stop heating subsystem, dehumidifying subsystem
Number and select suitable combination;The power circuit includes rectification circuit and voltage conversion circuit, and being used for will
220V alternating current is converted into direct current required for other circuit modules;The temperature collecting module includes being placed in cigarette-filling house
As Tobacco Leaf Curing temperature reference value part and be placed on heat pump compressor for monitoring compressor liquid-spraying temperature portion
Point;The numeral input and protective module include phase sequence part, blower overload protection portion, heat pump compressor height
Pressure protection part, electric heating overtemperature prote part, work in the normal range for controlling electrical equipment, avoid changing due to phase sequence
Become, load is excessive that electric equipment overload is caused to burn electrical equipment, when numeral input and protective module work act, phase
The reset setting state answered can also change, and when the equipment protected can work normally, restore to reset setting to be to be in just
Beginning state;The control termination of the monostatic relay drive module is microcontroller, according to the two of microcontroller transmission
Contact is cut off or be closed to system control instruction, and then the starting or closing of the connection equipment of control output end, output interface connect
By 220V AC voltage as power supply include three section solenoid valve parts, the high low speed control part of circulating fan,
A.C. contactor part, wherein high low speed control is used to come automatically according to method for flue-curing tobacco leaves or manually adjust rotation speed of fan
Tobacco flue-curing demand, the output end of the control terminal order steady-state relay drive module of A.C. contactor part, output are met
It is auxiliary that end is connected to 3 heat pump compressors, two dehumidifying blowers, water circulating pump, electricity by 380V alternating voltage respectively as power supply
Heater, two outdoor fans are helped, can directly initiate or close electromagnetism according to the binary system control instruction that microcontroller is sent
The high low speed control of valve circulating fan, and electrical equipment is controlled by switching on and off for control A.C. contactor
Start and stop;The ULN2003 driving circuit is used to be changed according to the real time temperature in method for flue-curing tobacco leaves curve and cigarette-filling house automatic
Adjust the aperture of electric-powered shutter and electric expansion valve;The warning circuit is in Tobacco Leaf Curing for prompting work people
The malfunction of the entire roasting plant of member;LCD touch display screen is for carrying out human-computer interaction and display monitoring numerical value, being presently in
The baking stage, the duration of current generation, tobacco flue-curing duration, 3 heating/dehumidification system runing times, 3
The mode and number, equipment running status of the unlatching of a heating/dehumidification system;The program is with data storage for recording
And save the data of each tobacco flue-curing, on the one hand can for toast same kind later, reference data is provided with position tobacco leaf and
So that baking process is met the tobacco variety currently toasted to improve used baking process, keep method for flue-curing tobacco leaves more specific and
It is detailed-oriented, on the other hand can be used as toast next time same kind, same position tobacco leaf setting value, avoid due to tobacco leaf dry
Roasted journey causes baking sound tobacco rate low due to artificially changing setting value;The communication interface is used to carry out with host computer
Telecommunication and mobile phone terminal carry out telecommunication, and are convenient for tobacco flue-curing to clustering and intelligent development;Main control chip passes through
The real time data of temperature collecting module acquisition and the input signal of digital input module are as embedding based on baking process curve
The input value of the algorithm routine entered is carried out operation within the microcontroller and obtained a result, then referred to operation result with binary system
The form of order is sent to each performer, controls electrical equipment by each performer, makes each equipment according to setting
Baking process curve carries out tobacco flue-curing, thus circulating dehumidification baking in realizing.
The utility model has the beneficial effects that: carrying out heat supply using three heatings/dehumidification system, it can reduce and petrochemical industry is fired
The burning of material, the discharge of Litter and pernicious gas can reduce the loss of heat using the interior circulation heating and dehumidifying of multipath,
The judging parameter of tobacco leaf can be improved in the yield rate that sound tobacco can be improved, and the control based on baking process curve is used to calculate
Method can reduce human interference, labor intensity, can reduce baking cost.
The above is only the preferred embodiment of the present invention and oneself, be not intended to limit the utility model, it is all this
Within the spirit and principle of utility model, any modification, equivalent replacement, improvement and so on should be included in the utility model
Protection scope within.
Claims (4)
1. a kind of interior circulating dehumidification bulk curing barn based on air energy, including cigarette-filling house (1-1), heat pump assembly (1-2), controller
Three parts (1-3), controller (1-3) are placed on the outside of heat pump assembly (1-2), and heat pump assembly (1-2) is placed in bulk curing barn original and adds
Hot cell position, the stream of hot air by heating enter cigarette-filling house (1-1) from cigarette-filling house's air inlet or heat pump assembly air outlet (1-6)
For tobacco flue-curing, the air stream after being exchanged heat with tobacco leaf is discharged from cigarette-filling house's air outlet (1-5), and the interior circulating-heating stage is empty
The air-flow heating room (1-9) internal back to heat pump assembly (1-2) through electric-powered shutter (1-7), interior circulating dehumidification stage air
Hydrofuge window (1-4), hydrofuge window outlet air parallel pipeline (1-8), heat pump assembly return air inlet (1-11) is flowed through to fill back to heat pump
Set (1-2) internal moist chamber (1-10);It is characterized in that: controller (1-3) passes through sensor acquisition cigarette-filling house (1-1) inside
The running parameter of temperature and humidity, heat pump assembly (1-2) internal electric equipment, the main control chip for being embedded baking process algorithm routine are transported
Control instruction is calculated and exported, heat pump assembly (1-2) internal electric equipment is controlled and is intelligently toasted with the interior circulating dehumidification for realizing tobacco leaf;
Heat pump assembly (1-2) includes heating/dehumidification system, constant temperature system, moist chamber (1-10), heating room (1-9), moist chamber (1-10)
It is independent cabinet in heat pump assembly (1-2), box house is integrated with to be steamed by the dehumidifying that condensation air removes moisture in air
It sends out device (2-5), for dried Cryogenic air and damp-heat air to be carried out to the total-heat exchanger (2-7) of heat exchange, is used for
The U-shaped water pond (2-14) of condensed water is filled, top of the box is provided with removes for damp-heat air in cigarette-filling house to be pumped into moist chamber
Wet dehumidifying blower (2-9), dehumidifying blower (2-9) are connect with heat pump assembly return air inlet (1-11), and the bottom of box, which is provided with, to be used for
Be discharged moist chamber in accumulate condensed water drainpipe (2-15), body side be provided with heating room be connected be used for will do
Dry air introduces the moist chamber air outlet (2-16) of oven heats;Heating room (1-9) is to have two in heat pump assembly (1-2)
The separate space body of return air path, a return air path are by cigarette-filling house's air outlet (1-5) by being placed in heating room (1-9)
Air in cigarette-filling house (1-1) is pumped into heating room (1-9) and is internally heated by the electric-powered shutter (1-7) at top, and another
Return air path is introduced the air for having exchanged heat dry by the heating room return air inlet (2-17) being connected with moist chamber (1-10)
It is heated in heating room (1-9), the heating room bottom (1-9) is equipped with heat pump assembly air outlet (1-6) and communicates with cigarette-filling house (1-1)
Tobacco flue-curing is carried out for the air of heating to be discharged into cigarette-filling house (1-1), heating room (1-9) has been internally integrated circulating fan
(2-19), electric heating device (2-18), condenser (2-6), condenser (2-6) are placed under heating room return air inlet (2-17)
For heating the air for flowing through condenser, electric heating device (2-18) is placed under condenser (2-6) for assisting heating,
Circulating fan (2-19) is placed under electric heating device (2-18), using the axial flow blower with high, low speed working method,
For promoting circulating for baking system inner air;It is consistent with working principle that heating/dehumidification system is integrated with 3 structures
Heating/dehumidifying subsystem, in Tobacco Leaf Curing heat supply and dehydration dehumidifying, respectively heat/dehumidify subsystem
Unite A, heating/dehumidifying subsystem B, heating/dehumidifying subsystem C, mutually indepedent between 3 heatings/dehumidifying subsystem, each system
Heat/dehumidifying subsystem has heating mode and dehumidification mode, and the heating mode and dehumidification mode of single subsystem are interrelated, and 3
Embedded mobile GIS of the switching of work relationship and mode between a subsystem by controller (1-3) based on baking process curve
Program carries out intelligent control;Constant temperature system, which is used to heat/dehumidify subsystem in the dehumidifying stage of tobacco flue-curing, opens dehumidification mode
The real-time dry-bulb temperature of Shi Wending and control heating rate.
2. the interior circulating dehumidification bulk curing barn according to claim 1 based on air energy, it is characterized in that: the heating/
Dehumidifying subsystem includes compressor (2-1), dehumidify magnetic valve (2-2), heating solenoid valve (2-3), outdoor evaporator (2-4), removes
Wet evaporator (2-5), condenser (2-6), outdoor fan (2-8), dehumidifying blower (2-9), electric expansion valve (2-10), compressor
The working solution outlet of (2-1) is connected with the working solution import of condenser (2-6), makes to enter by the working solution that compressor is handled
For heating the air for flowing through condenser in condenser (2-6), the working solution outlet connection of condenser is for according to cigarette-filling house (1-
1) temperature requirements adjust the electric expansion valve (2-10) of heating capacity, and there are two branches in electric expansion valve (2-10) outlet, and one
Branch passes through the work for control heating solenoid valve (2-3) and outdoor evaporator (2-4) that heating branch starts or stops
Liquid import is connected, then is connected with compressor (2-1) by the outlet of outdoor evaporator (2-4) and to constitute the heating of working solution and be recycled back to
Road, along with the outdoor fan (2-8) being placed on heat pump assembly (1-2) shell forms heating/dehumidifying subsystem heating work
Operation mode, the dehumidify magnetic valve (2-2) and dehumidify evaporimeter that another branch is started or stoped by being used to control dehumidifying branch
The working solution import of (2-5) is connected, and the outlet of dehumidify evaporimeter (2-5) and compressor (2-1) have been connected to form working solution
Dehumidifying circulation loop, along with the dehumidifying blower (2-9) being placed at the top of moist chamber (1-10) forms heating/dehumidifying subsystem
Dehumidification work mode;Heating/dehumidifying subsystem A, heating/dehumidifying subsystem B, heating/dehumidifying subsystem C heating mode and
The work in combination of dehumidification mode carries out intelligent control by embedded mobile GIS program of the controller (1-3) based on baking process curve
System.
3. the interior circulating dehumidification bulk curing barn according to claim 1 based on air energy, it is characterized in that: the constant temperature system
System includes 3 water cooling heat exchangers (2-13), water circulating pump (2-11), water tank (2-12), tank drains pipe (2-20), cold water water inlet
It manages (2-21), 3 water cooling heat exchangers (2-13) are arranged before heat pump assembly (1-2) box house is by dehumidify magnetic valve (2-2)
One section of working liquid pipe be wrapped in wherein, the working solution for flowing through pipe cools down, 3 water cooling heat exchangers (2-13)
Outlet be parallel-connected to water tank (2-12) by water pipe, the outlet of water tank (2-12) be connected to water circulating pump (2-11) water inlet
Mouthful, the water outlet of water circulating pump (2-11) is connected to the water inlet of 3 water cooling heat exchangers (2-13) by water pipe in parallel, forms one
It is a to be used to control heating rate and temperature fluctuation model that 3 heatings/dehumidifying subsystem opens real-time dry-bulb temperature when dehumidification mode
The cooling water circulation loop enclosed;It is additionally provided with cold water inlet (2-21) He Huanshui's for supplementing cold water on water tank (2-12)
Tank drains pipe (2-20), tank drains pipe (2-20) and cold water inlet (2-21) are designed with manual switch, constant temperature system
Open or close by controller (1-3) according to baking process curve, real-time wet-bulb temperature rate of temperature fall, dehumidify discharge outlet row
Water and the temperature difference of real-time dry-bulb temperature and target temperature codetermine, and whole process is by controller (1-3) with Roaster
Embedded mobile GIS program based on skill curve carries out intelligent control.
4. the interior circulating dehumidification bulk curing barn according to claim 1 based on air energy, it is characterized in that: the controller
(1-3) includes main control chip minimum systematic module, power circuit, temperature collecting module, numeral input and protective module, relay
And its it is drive module, ULN2003 driving circuit, warning circuit, LCD touch display screen module, program and data memory module, logical
Believe interface module;Main control chip minimum systematic module is used for the reality according to each stage Temperature Humidity Sensor acquisition of tobacco flue-curing
When temperature and humidity, 3 heatings/dehumidifying subsystem is controlled by the embedded mobile GIS program based on baking process curve respectively and is opened
It is dynamic or stop, the time of operation, heating mode or dehumidification mode switching with combine;Power circuit includes rectification circuit and electricity
Voltage conversion circuit, for 220V alternating current to be converted into direct current required for each circuit module;Temperature collecting module is used for
Monitor the compressor liquid-spraying temperature of the temperature and humidity and heat pump unit in cigarette-filling house;Numeral input and protective module are for guaranteeing each use
The normal work of electric equipment, including phase sequence, blower overload protection, compressor high voltage protective, compressor low-voltage variation, electricity are auxiliary
Hot overtemperature prote;Relay and its drive module open or close solenoid valve according to the control instruction that main control chip is sent, follow
The high low speed switching of ring blower controls being switched on or switched off for A.C. contactor;ULN2003 driving circuit according to tobacco leaf for drying
The aperture of real time humiture variation automatic adjustment electric-powered shutter and electric expansion valve in curing process curve and cigarette-filling house;Alarm
Circuit in Tobacco Leaf Curing for prompting the malfunction of the entire roasting plant of staff;LCD touch display screen is used for
Carry out the numerical value and equipment running status of human-computer interaction and display monitoring;Program and data storage are for storage system work journey
Sequence, the data for recording and saving each tobacco flue-curing;Communication interface circuit module is used to carry out telecommunication with host computer and hand
Machine terminal carries out telecommunication;Using the real time data of temperature collecting module acquisition as the insertion based on baking process curve
The input of algorithm routine is obtained control output quantity after carrying out operation, decision in main control chip, is sent out in the form of binary instruction
Each performer is given, realizes that circulating dehumidification intelligently toasts in tobacco leaf.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201821968717.5U CN209498542U (en) | 2018-11-28 | 2018-11-28 | Interior circulating dehumidification bulk curing barn based on air energy |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201821968717.5U CN209498542U (en) | 2018-11-28 | 2018-11-28 | Interior circulating dehumidification bulk curing barn based on air energy |
Publications (1)
Publication Number | Publication Date |
---|---|
CN209498542U true CN209498542U (en) | 2019-10-18 |
Family
ID=68190509
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201821968717.5U Expired - Fee Related CN209498542U (en) | 2018-11-28 | 2018-11-28 | Interior circulating dehumidification bulk curing barn based on air energy |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN209498542U (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109588755A (en) * | 2018-11-28 | 2019-04-09 | 湖南科技大学 | Interior circulating dehumidification bulk curing barn baking system |
CN114343218A (en) * | 2022-02-10 | 2022-04-15 | 云南省烟草农业科学研究院 | Novel heating system and heating method for cigar airing house |
CN115307419A (en) * | 2022-07-18 | 2022-11-08 | 青岛海尔空调电子有限公司 | Integrated drying system and control method for integrated drying system |
WO2023024635A1 (en) * | 2021-08-25 | 2023-03-02 | 青岛海尔空调电子有限公司 | Drying unit control method, readable storage medium, and drying unit |
-
2018
- 2018-11-28 CN CN201821968717.5U patent/CN209498542U/en not_active Expired - Fee Related
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109588755A (en) * | 2018-11-28 | 2019-04-09 | 湖南科技大学 | Interior circulating dehumidification bulk curing barn baking system |
WO2023024635A1 (en) * | 2021-08-25 | 2023-03-02 | 青岛海尔空调电子有限公司 | Drying unit control method, readable storage medium, and drying unit |
CN114343218A (en) * | 2022-02-10 | 2022-04-15 | 云南省烟草农业科学研究院 | Novel heating system and heating method for cigar airing house |
CN115307419A (en) * | 2022-07-18 | 2022-11-08 | 青岛海尔空调电子有限公司 | Integrated drying system and control method for integrated drying system |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN209498542U (en) | Interior circulating dehumidification bulk curing barn based on air energy | |
CN109588755A (en) | Interior circulating dehumidification bulk curing barn baking system | |
CN109588754A (en) | Interior circulating-heating dehumidification device for bulk curing barn transformation | |
CN110477433A (en) | Flow-circulating type bulk curing barn air energy heating and dehumidifying system | |
CN108477659B (en) | Multi-energy complementary internal circulation bulk curing barn | |
CN101342006B (en) | Method for baking tobacco leaf of intelligentized miniature compact tobacco flue-curing house | |
CN106643107B (en) | A kind of heat-pump-type Two-way Cycle hot air drying system control method and its control device | |
CN207963345U (en) | Based on the drying corps device recycled in clean energy | |
CN110506972A (en) | Bulk curing barn heating and dehumidification device based on airflow circulating control | |
CN106766837B (en) | A kind of frequency conversion capability-variable heat pump hot air drying system control method and its control device | |
CN108185501A (en) | Clean bulk curing barn heat supply dehumidification device that can be complementary | |
CN203378549U (en) | Novel efficient energy-saving tobacco leaf curing equipment | |
CN106500495A (en) | A kind of frequency conversion capability-variable heat pump hot air drying system and its control method | |
CN108185500A (en) | Circulation condensed roasting room baking system in clean energy | |
CN105433424A (en) | Numerical control automatic air energy tobacco leaf curing complete equipment | |
CN206330408U (en) | A kind of heat-pump-type Two-way Cycle hot air drying system | |
CN112515226B (en) | Energy-saving low-temperature-modulation tobacco curing house and curing method | |
CN209498543U (en) | Bulk curing barn heating and dehumidification internal circulation apparatus | |
CN202476421U (en) | Double heat source drying device applied to tobacco flue-curing | |
CN103836725B (en) | sensible heat recovery type fresh air humidity control unit | |
CN202286270U (en) | Tobacco flue-curing house | |
CN208336375U (en) | A kind of lead-acid accumulator humidogene plate high temperature and pressure curing and drying device | |
CN207784255U (en) | The barn that electric heat supply and combustion heat supplying are combined | |
CN208387868U (en) | Energy saving and environment friendly intelligent compact barn | |
CN206330409U (en) | A kind of frequency conversion capability-variable heat pump hot air drying system |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
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: 20191018 |