CN208983822U - A kind of heat pump drying device that efficient dehumidification module is pre-chilled than air inlet using different area air quantity - Google Patents
A kind of heat pump drying device that efficient dehumidification module is pre-chilled than air inlet using different area air quantity Download PDFInfo
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Abstract
The utility model discloses a kind of heat pump drying device that efficient dehumidification module is pre-chilled than air inlet using different area air quantity, including shell, shell is equipped with air inlet and outlet, is equipped with the first blower at air outlet；At least two sets of dehumidification systems are equipped in shell, dehumidification system includes the compressor for connecting and composing cooling cycle system, condenser, throttling set, evaporator；Evaporator side is equipped with cross-flow heat exchanger, top wind outlet is provided with the second blower；Wherein the area air quantity when cross-flow heat exchanger operation of a set of efficient dehumidifying even distributing wind module of air inlet pre-cooling is than being greater than the area air quantity ratio when cross-flow heat exchanger operation of efficiently dehumidifying even distributing wind module is pre-chilled in another set of air inlet；The condenser of multiple dehumidification systems is arranged sequentially at the air outlet of the case top up and down；Under the action of the first blower, a part air inlet flows separately through after efficient dehumidification module is pre-chilled in each air inlet and passes through all condensers, and another part is entered the wind directly through all condensers, then is discharged from air outlet.
Description
Technical field
The utility model relates to dehumidification device design fields, and in particular to a kind of using different area air quantity ratio air inlet
The heat pump drying device of efficient dehumidification module is pre-chilled.
Background technique
The heat pump drying device of air-flow closed cycle, by the Heat Pump blower fan group and carrying of production high temperature dry air containing wet
The drying spaces union of material forms.
In the heat pump drying device of air-flow closed cycle, high temperature dry air and contain wet stock that heat pump condenser produces
Hot and humid area is carried out, captures containing the moisture in wet stock and becomes warm-humid air and return to evaporator with heat pump, cool down in evaporator
Dehumidifying filters out water vapour, enters condenser heat absorption heating later, and temperature elevated relative humidity reduces and becomes high temperature drying again
Air starts next round circulation, until the drying containing wet stock is completed.
The heat pump drying device of air-flow closed cycle, due to heat closed cycle, not containing the effective component in wet stock
As outer moisture-removing air-flow is discharged, thus dry matter yield rate improves, dry matter quality improves.
But in the operational process of air-flow closed cycle heat pump drying device, with the evaporation of the moisture containing wet stock, cold
Solidifying, relative humidity and the absolute moisture content for drying space air are all lower and lower, drying return air (i.e. the evaporator of drying heat pump into
Wind) temperature is higher and higher, water capacity is lower and lower, and cause the sensible heat load of evaporator (to put for absorbing drying return air cooling
The refrigerating capacity of heat) accounting in evaporator overall refrigerating effect is higher and higher, and damp and hot load (is steamed for absorbing water in drying return air
The refrigerating capacity of vapour condensation heat) accounting is lower and lower, until final damp and hot load accounting is zero, evaporator filter, which is not discharged, to be come；
And in the operational process of air-flow closed cycle heat pump drying device, the water vapour in dry air is constantly filtered out,
The relative humidity and water vapour absolute content in dry air are reduced, promotes the lasting evaporation containing moisture in wet stock, especially
The evaporation for solving a small amount of moisture remained in drying latter stage material is the key problem of air-flow closed cycle drying.
In order to cope with the higher and higher problem of accounting of evaporator this sensible heat load in overall refrigerating effect, people's utility model
Efficient dehumidifying technology is pre-chilled in air inlet, i.e., plate heat exchanger is arranged in evaporator air inlet, makes plate heat exchanger and evaporation
Device constitutes one " air inlet be pre-chilled efficient dehumidification module ", with the low temperature outlet air of evaporator by plate heat exchanger " cold fluid is logical
" pre-cooling " is implemented to the evaporator high temperature air inlet in " zone of heat liberation " of plate heat exchanger in road ", reduces the temperature of evaporator air inlet
Degree, the relative humidity for improving evaporator air inlet, thus reduce accounting of the evaporator sensible heat load in overall refrigerating effect, improve it is damp and hot
Accounting, raising moisture removal of the load in overall refrigerating effect.
The utilization of efficient dehumidification module is pre-chilled in air inlet, change air-flow closed cycle heat pump drying device drying rate and
Drying effect, but new problem comes one after another:
In the early metaphase of air-flow closed cycle heat pump drying device operation, return air temperature is less high, relative humidity is relatively high,
Compared with the plate heat exchanger of small area evaporator can just entered the wind in the configuration of evaporator air inlet to be passed through by evaporator low temperature outlet air
Plate heat exchanger is pre-chilled to " saturation " (relative humidity 100%) state, and it is equally important that can guarantee that evaporator is entered the wind
Dew-point temperature is high, evaporator thermic load is high, refrigerant evaporating pressure is high, refrigerant mass fluxes are big, refrigerating capacity is big, moisture removal
Greatly；
And in the later period of air-flow closed cycle heat pump drying device operation, since drying return air temperature is raised, relative humidity
Reduce, dew-point temperature reduces, originally just seemed power in the plate heat exchanger of that " smaller " area of evaporator air inlet configuration
Not from the heart, evaporator air inlet can not be made by the outlet air of evaporator low temperature to be effectively pre-chilled to " saturation " state or close to saturation state,
To repeat again, " accounting of the sensible heat load of evaporator in evaporator overall refrigerating effect be higher and higher, damp and hot load accounting is got over
Come lower, until final damp and hot load accounting is zero, evaporator filter, which is not discharged, to be come, and the last one kilometer of drying course is not complete
At " old problem.
Utility model content
The technical issues of for proposing in background technique, the utility model are wrong with the air inlet pre-cooling for being in evaporator air inlet
Flow the heat exchange area of heat exchanger and ratio (" area air quantity ratio " when i.e. the heat exchanger is run) conduct of the heat exchanger ventilation quantity
The core index of efficient dehumidification module design is pre-chilled in air inlet, provides a kind of using the dehumidifying efficiently than air inlet pre-cooling of different area air quantity
The heat pump drying device of module includes shell, and the shell is equipped with air inlet and outlet, and is arranged at the air outlet
There is the first blower；
At least two sets of dehumidification systems are provided in the shell, the dehumidification system includes compressor, condenser, throttling
Device, evaporator, the compressor, condenser, throttling set, evaporator be linked in sequence constitute one for refrigerant circulation closing
System；The evaporator side is equipped with cross-flow heat exchanger, and the air inlet and the outlet of the evaporator are passed through described respectively by air duct
Zone of heat liberation, the cold fluid pass of cross-flow heat exchanger, cross-flow heat exchanger top wind outlet is provided with the second blower, described
Evaporator, cross-flow heat exchanger, the second blower and connection air duct constitute air inlet pre-cooling efficiently dehumidifying even distributing wind module；It is wherein a set of
Area air quantity ratio when the cross-flow heat exchanger operation of the efficient dehumidifying even distributing wind module of air inlet pre-cooling, is greater than another set of air inlet and is pre-chilled
The efficiently area air quantity ratio when cross-flow heat exchanger operation of dehumidifying even distributing wind module；Wherein the area air quantity is than being cross-flow
Heat exchange area/air quantity of heat exchanger.
Efficient dehumidification module sequence arranged is pre-chilled in the shell in multiple air inlets, multiple dehumidification systems
Condenser up and down be arranged sequentially at the air outlet of the case top；
Under the action of first blower, part air inlet flows separately through each air inlet and the uniform cloth that efficiently dehumidifies is pre-chilled
All condensers are passed through after wind module, part air inlet is directly through all condensers, finally from the air outlet
Discharge.
Preferably, two air inlet pre-coolings efficiently dehumidify, air quantity is equal when the cross-flow heat exchanger operation of even distributing wind module, area
Heat exchange area of the air quantity than big cross-flow heat exchanger, heat exchange area greater than area air quantity than small cross-flow heat exchanger.
Preferably, heat exchange area of the area air quantity than big cross-flow heat exchanger, exchanges heat greater than area air quantity than small cross-flow
The heat exchange area of device；Area air quantity than big cross-flow heat exchanger operation when air quantity, changed less than area air quantity than small cross-flow
The air quantity when operation of hot device.
Preferably, when the volume of two cross-flow heat exchangers is equal, heat exchange plate spacing is small, the mistake more than amount of heat exchanger plates
The heat exchange area for flowing heat exchanger is big.
It is selected preferably, the air quantity when operation of the efficient dehumidifying even distributing wind module of air inlet pre-cooling of big blower is selected to be greater than
The air quantity when operation of the efficient dehumidifying even distributing wind module of air inlet pre-cooling of small blower.
Preferably, area air quantity uses small compressor than the compressor of dehumidification system corresponding to big cross-flow heat exchanger,
Area air quantity uses big compressor than the compressor of dehumidification system corresponding to small cross-flow heat exchanger.
Preferably, two sets of dehumidification systems are set in the shell, the two efficient dehumidifying even distributing wind modules of air inlet pre-cooling
Left and right is arranged side by side in the shell；
It is efficiently removed without the humid air of the efficient dehumidifying even distributing wind module of air inlet pre-cooling around air inlet pre-cooling
Wet even distributing wind module surrounding is delivered up.
Preferably, second blower uses centrifugal blower.
Preferably, being provided with drip tray below the evaporator.
Preferably, the evaporator, condenser use finned tube exchanger.
The utility model due to using the technology described above, is allowed to compared with prior art, have the following advantages that and accumulate
Pole effect:
1, a kind of heat pump drying device that efficient dehumidification module is pre-chilled than air inlet using different area air quantity of the utility model,
Under the high temperature low humidity conditions in air-flow closed cycle drying latter stage, there is brilliant effect on moisture extraction, it is " last to solve heat pump drying
One kilometer " problem: dehumidification module is pre-chilled in the air inlet of " big " area air quantity ratio by the utility model, for handling the height in drying later period
Warm low humidity return air has brilliant effect on moisture extraction, by the height containing a small amount of water vapour of the later stage of drying under high temperature low humidity conditions
The dry return air of temperature, carries out " depth pre-cooling " by the cross flow plate type heat exchanger of " big " area air quantity ratio with the outlet air of evaporator low temperature,
To more greatly reduce the temperature of evaporator air inlet, improve relative humidity, the humidity load accounting of evaporator is improved, raising removes
Wet efficiency and drying efficiency, solve the problems, such as heat pump drying " last one kilometer "；
2, a kind of heat pump drying device that efficient dehumidification module is pre-chilled than air inlet using different area air quantity of the utility model,
A part of humid air directly flows through condenser, and another humid air first flows through air inlet and be pre-chilled after efficiently dehumidifying even distributing wind module again
Condenser is flowed through, so that the ventilation quantity of condenser is greater than evaporator air mover amount, reduces the condensation of refrigerant gas in condenser
Pressure, to reduce the pressure difference of refrigerant dehumidification system condensing pressure and evaporating pressure, the power consumption of compressor, compressor compresses
Than dehumidifying Energy Efficiency Ratio greatly improved；
Meanwhile air inlet pre-cooling provided by the utility model efficiently dehumidifies even distributing wind module by board-like cross-flow heat exchanger, steaming
Send out device, the second blower and corresponding air duct composition；The module has the pre-cooling of evaporator high temperature air inlet, evaporator low temperature outlet air reheating
Dual function；Moreover, by the setting of the second blower so that the dry air for filtering out moisture being discharged by cross-flow heat exchanger with not
It sufficiently collides, spread, mix by the humid air that efficiently dehumidifying even distributing wind module is pre-chilled in air inlet, to improve condenser air inlet temperature
The uniformity of humidity, using discharge after condenser heating, so that there is the uniformity of temperature humidity on air-flow section, thus
Bring the uniformity of the drying containing wet stock.
Detailed description of the invention
The above-mentioned and other feature of the utility model can be more clearly understood that by detailed description below in conjunction with attached drawing
And advantage, in which:
Fig. 1 is provided by the utility model using different area air quantity dehumidification module more efficient than air inlet pre-cooling in embodiment 1
Heat pump drying device structural schematic diagram；
Fig. 2 is provided by the utility model using different area air quantity dehumidification module more efficient than air inlet pre-cooling in embodiment 2
Heat pump drying device structural schematic diagram.
Specific embodiment
Referring to the attached drawing for showing the utility model embodiment, the utility model is described in more detail.However, this reality
It can be realized in many different forms with novel, and should not be construed as being limited by the embodiment herein proposed.On the contrary, proposing
These embodiments be in order to reach sufficiently and complete disclosure, and make those skilled in the art understands completely this it is practical newly
The range of type.In these attached drawings, for clarity, the size and relative size in layer and region may be exaggerated.
The utility model provides a kind of heat pump drying that efficient dehumidification module is pre-chilled than air inlet using different area air quantity
Device includes a shell, and air inlet and air outlet are provided on shell, and the first blower 18 is provided at air outlet；In shell 1
At least two sets of dehumidification systems are provided with, every set dehumidification system includes compressor, condenser, throttling set, evaporator, and is pressed
Contracting machine, condenser, throttling set, evaporator be linked in sequence constitute one for refrigerant circulation closed-circuit system.Wherein, every set dehumidifying
Evaporator side in system, which is arranged side by side, a cross-flow heat exchanger, and cross-flow heat exchanger has two groups of heat exchanger channels of interlaced arrangement,
Two groups of heat exchanger channels of cross-flow heat exchanger, and wind outlet setting at the top of cross-flow heat exchanger are passed through in the air inlet and the outlet of evaporator respectively
There is the second blower, evaporator, cross-flow heat exchanger, the second blower and corresponding air duct constitute air inlet pre-cooling efficiently dehumidifying even distributing wind mould
Block；Wherein the area air quantity ratio when cross-flow heat exchanger operation of a set of dehumidification system, the cross-flow greater than another set of dehumidification system are changed
Area air quantity ratio when hot device is run.
Wherein, " area air quantity ratio " be cross-flow heat exchanger heat exchange area and the heat exchanger ventilation quantity ratio wherein,
Efficient dehumidification module sequence arranged is pre-chilled in shell in multiple air inlets, and the condenser of multiple dehumidification systems is sequentially arranged up and down
At the air outlet of case top.
When heat pump drying device is run, under the action of the first blower, humid air enters in shell from air inlet, part
Air first flows separately through each air inlet pre-cooling efficiently dehumidifying even distributing wind module, flows through process are as follows: the hot-fluid of cross-flow heat exchanger
Body channel, evaporator, the cold fluid pass of crossflow regenerator, the second blower；Then under the action of the second blower, by cross-flow
The dry air for filtering out water vapour and peripheral part of the cold fluid pass output of formula heat exchanger are directly entered the wet sky in shell 1
After gas uniformly mixes, then followed by the condenser of each set dehumidification system, the final dry air that obtains is discharged from air outlet.
Heat pump drying device provided by the utility model has the advantage that
1, for a part of humid air directly through condenser, it is high that another humid air first flows through air inlet pre-cooling in the utility model
Condenser is passed through after effect dehumidifying even distributing wind module, so that the ventilation quantity of condenser is greater than evaporator air mover amount, is reduced
The condensing pressure of refrigerant gas in condenser, to reduce the pressure of refrigerant dehumidification system condensing pressure and evaporating pressure
Difference, the power consumption of compressor, compressor pressure ratios, greatly improved dehumidifying Energy Efficiency Ratio；
2, air inlet provided by the utility model pre-cooling efficiently dehumidifying even distributing wind module by cross-flow heat exchanger, evaporator, the
Two blowers and corresponding air duct composition；The module has the dual function of the pre-cooling of evaporator high temperature air inlet, evaporator low temperature outlet air reheating
Energy；Moreover, passing through the setting of the second blower, so that being pre-chilled efficiently by the dry air that cross-flow heat exchanger is discharged with without air inlet
The humid air of dehumidifying even distributing wind module is sufficiently collided, spreads, is mixed, using being discharged after condenser heating, to have
The uniformity of temperature humidity on air-flow section, to bring the uniformity of the drying containing wet stock；It is particularly conducive to stoving process
Demanding drying course, such as the drying course of tobacco leaf, fragrance, Chinese herbal medicine；
3, heat pump drying device provided by the utility model includes at least two sets of dehumidification system, and further restriction
Wherein the heat exchange area of the cross-flow heat exchanger of a set of dehumidification system is greater than the heat exchange of the cross-flow heat exchanger of another set of dehumidification system
The heat exchange area of area, heat exchanger is big, and the air quantity of the passage of heat and cold passage is relatively small, area air quantity than this index with regard to big,
The heat exchange efficiency of hot and cold gas is just high；Conversely, the heat exchange area of heat exchanger is small, the air quantity of the passage of heat and cold passage is big, area wind
Amount is than this index with regard to small, and the heat exchange efficiency of hot and cold gas is with regard to low；The utility model is by the restriction of above structure, in practical fortune
In row, by being equipped with corresponding control system, control is with air inlet pre-cooling dehumidification module (the i.e. configuration heat-transfer surface of small area air quantity ratio
Small, the larger blower of air quantity the efficient dehumidifying even distributing wind module of air inlet pre-cooling of product) it is the dehumidifying task that the main force undertakes drying early stage,
With the air inlet pre-cooling dehumidification module of large area air quantity ratio, (i.e. configuration heat exchange area is larger, the air inlet of the smaller blower of air quantity is pre- for control
Cold efficient dehumidifying even distributing wind module) it is the dehumidifying task that the main force undertakes the drying later period；
The key problem in technology problem of air-flow closed cycle heat pump drying device is to make there be not heat type (sensible heat, latent heat)
There is the evaporator with heat pump of differentiation and selective power, absorbs the condensation heat of water vapor in air as much as possible, inhale as few as possible
Receive the sensible heat of air.The water vapour continually escaped from containing wet stock is destroyed continuously high-intensitively, drying space
Water vapour in air is reduced to water, reduces the relative humidity of drying space air, is only air-flow closed cycle heat pump drying
Key problem in technology is only " absolute principle " of air-flow closed cycle heat pump drying.
The energy and loss in efficiency of drying course, occur mainly in the later period of drying: containing wet stock, the phase contains after the drying
Water rate has already decreased to very low level, after moisture is primarily present in the deep-level location containing wet stock, such as tobacco leaf drying process
Moisture in the cigarette muscle of phase, the waist of trousers in clothes drying later period, pocket, the moisture in collar, it is slow that these moisture diffuse to the surface speed,
Evaporation capacity very little；
The utility model has brilliant effect on moisture extraction under the high temperature low humidity conditions in air-flow closed cycle drying latter stage,
Solve the problems, such as heat pump drying " last one kilometer ": dehumidification module is pre-chilled in the air inlet of " big " area air quantity ratio by the utility model,
For handling the high temperature low humidity return air in drying later period, there is brilliant effect on moisture extraction under high temperature low humidity conditions, by the later stage of drying
The high temperature drying return air containing a small amount of water vapour, is changed with evaporator low temperature outlet air by the way that the cross-flow of " big " area air quantity ratio is board-like
Hot device carries out " depth pre-cooling ", to more greatly reduce the temperature of evaporator air inlet, improve relative humidity, improves evaporator
Humidity load accounting, improve dehumidifying efficiency and drying efficiency, solve the problems, such as heat pump drying " last one kilometer ".
Specific embodiment is further described below:
Embodiment 1
Referring to Fig.1, heat pump drying device includes shell 1 in the present embodiment, and 1 upper end of shell is provided with air outlet 102,
Lower end is provided with air inlet 101.
In the present embodiment, two sets of dehumidification systems are provided in shell 1, respectively by compressor 10, evaporator 6, cross-flow
The first set dehumidification system that heat exchanger 7, the second blower 5, throttling set 4, condenser 2 are constituted, and by compressor 11, evaporator
13, second set of dehumidification system that cross-flow heat exchanger 14, the second blower 16, throttling set 17, condenser 3 are constituted；Wherein, evaporator
6, cross-flow heat exchanger 7, the second blower 5, the first efficient dehumidifying even distributing wind module of air inlet pre-cooling constituted, evaporator 13, cross-flow
Heat exchanger 14, the second blower 16 constitute the second air inlet pre-cooling efficiently dehumidifying even distributing wind module, the first air inlet pre-cooling efficiently dehumidifying
The interposition of shell 1 is arranged in even distributing wind module and second efficient dehumidifying even distributing wind module of air inlet pre-cooling or so spacing side by side
It sets；Condenser 2, condenser 3 are setting up and down.
Certainly, the tricks of dehumidification system can be adjusted as the case may be in other embodiments, herein with no restrictions.
In the present embodiment, cross-flow heat exchanger 7, cross-flow heat exchanger 14 are all made of board-like cross-flow heat exchanger, by multiple friendships
The lateral passage of heat and vertical cold passage composition of mistake arrangement.
In the present embodiment, the heat exchange area for being less than cross-flow heat exchanger 14 by limiting the heat exchange area of cross-flow heat exchanger 7,
To limit area air quantity when cross-flow heat exchanger 7 is run than being less than area air quantity ratio when cross-flow heat exchanger 14 is run.
Further, by leading in cross-flow heat exchanger 7, the identical situation of 14 volume of cross-flow heat exchanger in the present embodiment
Between the heat exchanger plates for the heat exchanger channels that the heat exchange plate spacing 8 for crossing the heat exchanger channels of control cross-flow heat exchanger 7 is greater than cross-flow heat exchanger 14
Away from 15, so that the heat exchange area for realizing cross-flow heat exchanger 7 is less than the function of the heat exchange area of cross-flow heat exchanger 14；Certainly, exist
Cross-flow heat exchanger 7,14 heat exchange amount of cross-flow heat exchanger can also control size by other means in other embodiments, not do herein
Limitation.
Further, in the present embodiment, the ventilation quantity of the second blower 5 is greater than the ventilation quantity of the second blower 16；Further
, realize area air quantity when cross-flow heat exchanger 7 is run than being less than area air quantity ratio when cross-flow heat exchanger 14 is run.Specifically
, as shown in fig. 1, the second blower 5 selects large fan, the second blower 16 to select small-sized fan, to realize the second blower 5
Ventilation quantity be greater than the second blower 16 ventilation quantity purpose.
Certainly, it can also realize by other means to the adjustment of the second fan delivery, not do herein in other embodiments
Limitation.
Certainly, in other embodiments the second blower 5, the second blower 16 also can be selected same size blower, herein not
It is limited.
In other embodiments, area air quantity ratio when cross-flow heat exchanger 7 is run is limited to run less than cross-flow heat exchanger 14
When area air quantity ratio mode be not limited to it is illustrated above, can be by suitably adjusting itself ventilation quantity and heat exchange area two
Adjustment of the area air quantity than size can be realized, herein with no restrictions in a numerical value.
In the present embodiment, the lower section of evaporator 7 is provided with drip tray 9, and the lower section of evaporator 13 is provided with drip tray 12,
The moisture being precipitated on an evaporator is flowed into drip tray, is collected discharge.
In the present embodiment, condenser, evaporator are all made of finned tube exchanger.
Below with regard to the heat pump drying provided in this embodiment that efficient dehumidification module is pre-chilled than air inlet using different area air quantity
The working principle of device is further described:
Under the action of the first blower 18, High Temperature Moist Air enters in shell 1 from air inlet 101, is divided into three tunnels；
Air-flow all the way, around the first air inlet pre-cooling, efficiently efficiently dehumidifying is equal for dehumidifying even distributing wind module, the second air inlet pre-cooling
Even cloth wind module is delivered up；
In addition two-way air-flow, flowing separately through the pre-cooling of the first air inlet, efficiently dehumidifying even distributing wind module, the second air inlet pre-cooling are high
It is delivered up again after effect dehumidifying even distributing wind module；Illustrate by taking the first air inlet pre-cooling efficiently dehumidifying even distributing wind module as an example,
High temperature low-humidity air, which enters in the passage of heat of the first cross-flow heat exchanger, cools down " pre-cooling " by the low temperature outlet air in cold passage,
Gas flow temperature after being pre-chilled reduces, relative humidity increases, and enters back into the further cool-down dehumidification of evaporator 6, filters out water vapour；
The low temperature outlet air for leaving evaporator 6 is heated into the cold passage of board-like cross-flow heat exchanger 7 by the high temperature air inlet of the passage of heat, at
It is dry air again by the sucking of the second blower 7, boosting, discharge, 360 ° are thrown to four sides, the humid air conveyed straight up with surrounding
It intersects vertically, mutual collision, reflection of the gas molecule to wall surface of gas molecule occurs, generate air-flow vortex and mutually expand strongly
It dissipates, to obtain the air-flow of temperature, humidity homogenization, which passes through condenser 2,3, high temperature dry air is obtained, the
It is discharged under the action of one blower 18 from air outlet 102.
Using the tobacco leaf heat pump drying device of the air inlet pre-cooling dehumidification module of different area air quantity ratio, with intensive flue-cured tobacco room
To dry space, heat pump unit is equipped with two kinds " area air quantity ratios ", and there is the air inlet of notable difference dehumidification module is pre-chilled, and generate
Apparent otherness effect:
1. dehumidification module is pre-chilled in the air inlet of small area air quantity ratio, there is brilliant effect on moisture extraction under medium temperature super-humid conditions
For example, dehumidification module is pre-chilled in the air inlet of small area air quantity ratio, using cross flow plate type heat exchanger, heat exchanger aluminium foil away from
4.0mm, exchange heat gross area 90m2, handle air quantity 2200m3/ h, area air quantity ratio is in 0.04h/m or so；Using 7HP compressor,
R134a refrigerant, evaporating temperature is at 9~19 DEG C, and refrigerating capacity is in 13.5~26kw；Under 35 DEG C of 80% return air operating condition, evaporation temperature
17 DEG C, refrigerating capacity 24kw, moisture removal 32kg/h of degree；Under 60 DEG C of 10% return air operating condition, 9.5 DEG C of evaporating temperature, refrigerating capacity
13.6kw, moisture removal 5.5kg/h；
Under 35 DEG C of 80% return air operating condition, 17 DEG C of evaporating temperature, refrigerating capacity 24kw, moisture removal 32kg/h, unit refrigeration
Measuring corresponding moisture removal is 1.33kg/kwh；If unit power moisture removal is about in 4kg/ using heat pump electrical power as denominator
kwh；This index is very brilliant！
And under 60 DEG C of 10% return air operating condition, 9.5 DEG C of evaporating temperature, refrigerating capacity 13.6kw, moisture removal 5.5kg/h, unit
It is 0.4kg/kwh that evaporator capacity, which corresponds to moisture removal,；If unit power moisture removal is about using heat pump electrical power as denominator
In 1kg/kwh, this index is difficult to receive；
2. dehumidification module is pre-chilled in the air inlet of large area air quantity ratio, there is brilliant effect on moisture extraction under high temperature low humidity conditions
For example, dehumidification module is pre-chilled in the air inlet of large area air quantity ratio, using cross flow plate type heat exchanger, heat exchanger aluminium foil away from
2.5mm, exchange heat gross area 80m2, handle air quantity 900m3/ h, area air quantity ratio is in 0.09h/m or so；Using 5HP compressor,
R134a refrigerant, evaporating temperature is at 4~14 DEG C, and refrigerating capacity is in 7~14kw；Under 35 DEG C of 80% return air operating condition, evaporating temperature 13
DEG C, refrigerating capacity 14kw, moisture removal 20kg/h；Under 60 DEG C of 10% return air operating condition, 4 DEG C of evaporating temperature, refrigerating capacity 7kw, dehumidifying
Measure 6.5kg/h；
Under 35 DEG C of 80% return air operating condition, 13 DEG C of evaporating temperature, refrigerating capacity 14kw, moisture removal 20kg/h, flat evaporator
It is 1.43kg/kwh that device refrigerating capacity, which corresponds to moisture removal,；If unit power moisture removal about exists using heat pump electrical power as denominator
4.3kg/kwh, this index are very brilliant；
Under 60 DEG C of 10% return air operating condition, 4 DEG C of evaporating temperature, refrigerating capacity 7kw, moisture removal 6.5kg/h；Specific refrigerating effect pair
Answering moisture removal is 0.93kg/kwh；If using heat pump electrical power as denominator, unit power moisture removal about in 2.3kg/kwh,
Compared with the 1kg/kwh of the air inlet pre-cooling dehumidification module of bottom surface product air quantity ratio, it is substantially higher by 130%, this index is very brilliant；
Embodiment 2
The present embodiment is the further adjustment carried out on the basis of embodiment 1.
Referring to Fig. 2, in the present embodiment, the compressor of the big corresponding dehumidification system of cross-flow heat exchanger of heat exchange area is used
The compressor of small compressor, the small corresponding dehumidification system of cross-flow heat exchanger of heat exchange area uses big compressor；That is compressor 10
Using big compressor, compressor 11 uses small compressor.
Further instruction, the big compressor, that is, big compressor of cylinder capacity, the small compressor, that is, small compressor of cylinder capacity.
The present embodiment is dried using the tobacco leaf heat pump of different compressors, the air inlet pre-cooling dehumidification module of different area air quantity ratio
Equipment for drying, is drying space with intensive flue-cured tobacco room, and heat pump unit is equipped with the different compressor of two kinds of refrigerating capacitys, two kinds of " areas
There is air quantity ratio " air inlet of notable difference dehumidification module is pre-chilled, and generate apparent otherness effect:
1. in the case where drying early metaphase, that is, medium temperature super-humid conditions, the air inlet pre-cooling dehumidifying mould of big compressor, small area air quantity ratio
Block has brilliant effect on moisture extraction；
2. after the drying under phase, that is, high temperature low humidity conditions, the air inlet pre-cooling dehumidification module of small compressor, large area air quantity ratio,
With brilliant effect on moisture extraction；Tobacco leaf enters drying muscle stage at this time, and water capacity is low, moisture removal is smaller, the system with baby compressor
Cooling capacity just matches.
Those skilled in the art should be understood that the utility model can be realized with many other concrete forms without de-
Spirit or scope from itself.Although the case study on implementation of the utility model has been described, it should be understood that the utility model should not limit
Be made as these embodiments, those skilled in the art can as defined by the following claims the spirit of the utility model and
Within the scope of make change and modification.
Claims (10)
1. a kind of heat pump drying device that efficient dehumidification module is pre-chilled than air inlet using different area air quantity, which is characterized in that packet
Shell is included, the shell is equipped with air inlet and outlet, and the first blower is provided at the air outlet；
At least two sets of dehumidification systems are provided in the shell, the dehumidification system includes compressor, condenser, throttling dress
Set, evaporator, the compressor, condenser, throttling set, evaporator be linked in sequence constitute one for refrigerant circulation closing system
System；The evaporator side is equipped with cross-flow heat exchanger, and the air inlet and the outlet of the evaporator pass through the mistake by air duct respectively
Zone of heat liberation, the cold fluid pass of heat exchanger are flowed, wind outlet is provided with the second blower, the steaming at the top of the cross-flow heat exchanger
It sends out device, cross-flow heat exchanger, the second blower and connection air duct and constitutes air inlet pre-cooling efficiently dehumidifying even distributing wind module；Wherein one pack into
Area air quantity ratio when the cross-flow heat exchanger operation of the efficient dehumidifying even distributing wind module of wind pre-cooling is greater than another set of air inlet pre-cooling height
Area air quantity ratio when the cross-flow heat exchanger operation of effect dehumidifying even distributing wind module；Wherein the area air quantity is than being that cross-flow is changed
Heat exchange area/air quantity of hot device；
Efficient dehumidification module sequence arranged is pre-chilled in the shell in multiple air inlets, multiple dehumidification systems it is cold
Condenser is arranged sequentially at the air outlet of the case top up and down；
Under the action of first blower, part air inlet flows separately through each air inlet pre-cooling efficiently dehumidifying even distributing wind mould
All condensers are passed through after block, part air inlet is finally discharged from the air outlet directly through all condensers.
2. the heat pump drying according to claim 1 that efficient dehumidification module is pre-chilled than air inlet using different area air quantity fills
It sets, which is characterized in that air quantity is equal when the cross-flow heat exchanger operation of the two efficient dehumidifying even distributing wind modules of air inlet pre-cooling, area wind
Measure the heat exchange area than big cross-flow heat exchanger, the heat exchange area greater than area air quantity than small cross-flow heat exchanger.
3. the heat pump drying according to claim 1 that efficient dehumidification module is pre-chilled than air inlet using different area air quantity fills
Set, which is characterized in that area air quantity than big cross-flow heat exchanger heat exchange area, greater than area air quantity than small cross-flow heat exchanger
Heat exchange area；Area air quantity than big cross-flow heat exchanger operation when air quantity, exchange heat less than area air quantity than small cross-flow
The air quantity when operation of device.
4. the heat pump drying according to claim 2 or 3 that efficient dehumidification module is pre-chilled than air inlet using different area air quantity
Device, which is characterized in that when the volume of two cross-flow heat exchangers is equal, plate spacing is small for heat exchange, more than amount of heat exchanger plates
The heat exchange area of cross-flow heat exchanger is big.
5. the heat pump drying according to claim 2 or 3 that efficient dehumidification module is pre-chilled than air inlet using different area air quantity
Device, which is characterized in that the air quantity when operation of the efficient dehumidifying even distributing wind module of air inlet pre-cooling of big blower is selected to be greater than choosing
Air quantity when the efficiently operation of dehumidifying even distributing wind module is pre-chilled with the air inlet of small blower.
6. the heat pump drying according to claim 1 or 2 that efficient dehumidification module is pre-chilled than air inlet using different area air quantity
Device, which is characterized in that area air quantity uses small compressor than the compressor of dehumidification system corresponding to big cross-flow heat exchanger,
Area air quantity uses big compressor than the compressor of dehumidification system corresponding to small cross-flow heat exchanger.
7. the heat pump drying according to claim 1 that efficient dehumidification module is pre-chilled than air inlet using different area air quantity fills
It sets, which is characterized in that two sets of dehumidification systems are set in the shell, and efficiently dehumidifying even distributing wind module is left for two air inlet pre-coolings
The right side is arranged side by side in the shell；
It efficiently dehumidifies without the humid air of the efficient even distributing wind module that dehumidifies of the air inlet pre-cooling around air inlet pre-cooling
Even cloth wind module surrounding is delivered up.
8. the heat pump drying according to claim 1 that efficient dehumidification module is pre-chilled than air inlet using different area air quantity fills
It sets, which is characterized in that second blower uses centrifugal blower.
9. the heat pump drying according to claim 1 that efficient dehumidification module is pre-chilled than air inlet using different area air quantity fills
It sets, which is characterized in that be provided with drip tray below the evaporator.
10. the heat pump drying according to claim 1 that efficient dehumidification module is pre-chilled than air inlet using different area air quantity fills
It sets, which is characterized in that the evaporator, condenser use finned tube exchanger.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821220573.5U CN208983822U (en) | 2018-07-30 | 2018-07-30 | A kind of heat pump drying device that efficient dehumidification module is pre-chilled than air inlet using different area air quantity |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821220573.5U CN208983822U (en) | 2018-07-30 | 2018-07-30 | A kind of heat pump drying device that efficient dehumidification module is pre-chilled than air inlet using different area air quantity |
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| CN208983822U true CN208983822U (en) | 2019-06-14 |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109028916A (en) * | 2018-07-30 | 2018-12-18 | 上海伯涵热能科技有限公司 | A kind of heat pump drying device that efficient dehumidification module is pre-chilled than air inlet using different area air quantity |
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2018
- 2018-07-30 CN CN201821220573.5U patent/CN208983822U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109028916A (en) * | 2018-07-30 | 2018-12-18 | 上海伯涵热能科技有限公司 | A kind of heat pump drying device that efficient dehumidification module is pre-chilled than air inlet using different area air quantity |
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