CN205351964U - Energy -conserving dehumidification drying equipment of air cooling - Google Patents
Energy -conserving dehumidification drying equipment of air cooling Download PDFInfo
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- CN205351964U CN205351964U CN201620021702.2U CN201620021702U CN205351964U CN 205351964 U CN205351964 U CN 205351964U CN 201620021702 U CN201620021702 U CN 201620021702U CN 205351964 U CN205351964 U CN 205351964U
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Abstract
The utility model discloses an energy -conserving dehumidification drying equipment of air cooling, dehumidification drying equipment include except that moist chamber and drying chamber, remove the moist chamber setting and are provided with the plenum chamber at drying chamber one side, drying chamber opposite side, are provided with ventilation holes on the common wall of plenum chamber and drying chamber, except that being provided with dehydrating unit and drying device in the moist chamber. Still including setting up the solar energy air heat collector at the drying chamber top, solar energy air heat collector one side is provided with the heat collector air inlet to dehumidification drying equipment, and the opposite side is provided with the heat collector exhaust pipe who is connected with exhaust pipe B, is provided with the heat collector solenoid valve of the choke amount of wind on heat collector exhaust pipe's the pipeline, and intake stack B still is provided with air condenser on the pipeline that lies in the member of the royal clan that dehumidifies, the utility model discloses a conventional energy is new forms of energy helping hand and wide temperature section automatically regulated in addition, and the removal moisture drying can be carried out to grain, forestry products and the chinese -medicinal material of the different drying temperature's of needs different cultivars to the air cooling dehumidification.
Description
Technical field
This utility model belongs to product dried dehumidifying technology field, is specifically related to the dehumidification equipment that a kind of air cooling is energy-conservation.
Background technology
China is a grain, forestry products and Producing medicinal herbs and consumption big country.Showing according to " national economy and social development statistical communique in 2014 ", within 2014, China's grain obtains good harvest again, it is achieved " 11 even increase ".Annual grain yield 607,100,000 tons；Meanwhile, China is also the processing of maximum in the world wood industry, woodwork production base and topmost woodwork export processing state and one of importation of timber state maximum in the world.The wood-based plate of China, furniture, floor annual production position are at the forefront in the world；One of country that still natural drug kind is the abundantest in the world of China.Showing according to Third National natural resources of Chinese medicinal materials census statistics data, China's natural resources of Chinese medicinal materials has reached 12807 kinds.In natural resources of Chinese medicinal materials, Medicinal plant kind is maximum, reaches 11146 kinds, accounts for the 87.03% of sum；Medicinal animal 1,581 kind, mineral drug 80 kinds.320 kinds of conventional large vegetable drugs and 29 kinds of wild total reserves of conventional animal medical material are 8,500,000 tons, and it is more than 30 ten thousand tons that medical material annual production is planted by family.Along with the continuous growth of China's grain, forestry products and Producing medicinal herbs amount with consumption figure, the dry product population that needs of substantial amounts also constantly increases immediately.
When front because of global warming, extreme weather increases, climate damage takes place frequently, because climate reasons and drying equipment are not enough with practitioner, cause the loss that grain, timber, Chinese crude drug can not dry in time very surprising.Drying equipment is reducing loss, and products quality guarantee aspect is playing more and more important effect.Along with grain, timber, Chinese crude drug increase of production more many, the demand of its drying equipment is also more big.Particularly " operating cost " of grain drying equipment is just, is directly connected to " economic well-being of workers and staff " of kind of grain person and dry practitioner especially.Thus the grain drying equipment of " low operating cost " effect in the grain-production of stable China, Ensuring Food Safety and protection kind grain person with the enthusiasm of dry practitioner is also manifesting day by day.
Make a general survey of China for the equipment that grain, forestry products and Chinese crude drug dry, much there is the defects such as operating cost is higher, temperature controlled section is narrower；Vast plus China region, Middle East Western Economic is uneven, the kind of the energy and Regional Distribution obvious difference and have an urgent demand of energy-saving and emission-reduction, single thermal source to utilize the Local Adaptation of drying equipment is poor, energy-saving and emission-reduction usefulness is also poor, therefore, Local Adaptation scope low in the urgent need to utility model one operating cost is wide, and dry benefit is profitable with energy-saving and emission-reduction.And the technology that can be effectively dried in a variety of weather conditions.
Utility model content
The purpose of this utility model is in that: for defect and the market demand of above-mentioned existing drying equipment, it is provided that the dehumidification equipment that air cooling is energy-conservation.This utility model emphasis is dried design for the maximum grain of social required quantity, forestry products and Chinese crude drug.By closed cycle and damp and hot recirculation, farthest save energy expenditure and reduce operating cost, to ensure the economic interests of grower and dry practitioner；It is automatically adjusted the different requirements meeting different grain, forestry products and Chinese crude drug to dry humiture by multi-temperature section；Especially by its external tapping by new forms of energy such as the solar energy of different geographical, geothermal energy, biomass energies for drying power-assisted.The local energy condition that utilizes of energy treatment in accordance with local conditions promotes the utilization of drying equipment and reduces carbon emission, reduces the loss that the products such as grain cause because the reasons such as weather can not dry in time as much as possible.
To achieve these goals, the technical solution adopted in the utility model is:
The dehumidification equipment that a kind of air cooling is energy-conservation, including dehumidifying room and hothouse, dehumidifying room is arranged on hothouse side, and hothouse opposite side is provided with plenum chamber, and plenum chamber and the common wall of hothouse are provided with wind pushing hole；Dehumidifying is provided with dehydrating unit and drying device in room；
The air inlet A of dehydrating unit connects into lower end, hothouse side by intake stack A, and exhaust outlet A connects into hothouse opposite side upper end by exhaust duct A, and the casing of dehydrating unit is additionally provided with the air intake mesh for absorption dehumidifying room room air；Dehumidifying upper end, room is additionally provided with dehumidifying room solenoid valve；
Drying device includes housing, and the heater in housing, the exhaust outlet B of drying device connects into plenum chamber lower end by exhaust duct B through hothouse indoor, the air inlet B of drying device connects into above the hothouse indoor of plenum chamber opposite side by intake stack B, and housing upper is provided with blower fan, blower fan is connected with intake stack B；Described housing upper is additionally provided with the dehumidifying mesh for dampness enters dehumidifying room；
Intake stack B is being positioned on the pipeline that dehumidifying room is indoor and is being additionally provided with aerial condenser, is provided with several and is perpendicular in air exhaust passage A the air set pipe of direction of ventilation in aerial condenser, and wherein one end of air set pipe is connected to air exhauster.
Preferably, described heater includes combustor, and some layers that stacked distribution is above combustor add heat pipe heat, adds serpentine-like shape connection between heat pipe heat, and one of them end port connects combustor, another end port connects the exhaust emission tube that waste gas is discharged dehumidifying room；Combustor is also associated with air intake duct, and air intake duct extends the outdoor of dehumidifying room, and the oral area of air intake duct is provided with cleaner.
Preferably, described combustor be burning diesel oil diesel combustion room or burning natural gas combustion of natural gas room.
Preferably, described heater also includes base plate, base plate supports fixed combustion room, connecting adding of combustor is provided with first and is connected box body between the end port of heat pipe heat and combustor, the adding heat pipe heat and arrange second between heat pipe heat be connected box body with adding of serpentine-like shape connection, the end port adding heat pipe heat connecting exhaust emission tube is provided with the 3rd connection box body.
Preferably, described each heat pipe heat that adds forms by the heating tube side-by-side setting of 6-8 root.
Preferably, dehumidification equipment also includes the solar energy air heat collector being arranged on hothouse top, solar energy air heat collector side is provided with heat collector air inlet, opposite side is provided with the heat collector exhaust duct being connected with exhaust duct B, and the pipeline of heat collector exhaust duct is provided with the heat collector solenoid valve regulating exhaust air rate；
Four corners of the indoor top of described hothouse and dehumidifying room are provided with Temperature Humidity Sensor, heater is provided with heating control module, Temperature Humidity Sensor is connected with heating control module, and heating control module is connected with heat collector solenoid valve, dehumidifying room solenoid valve respectively.
Preferably, the air inlet A of described dehydrating unit connects into the lower end, hothouse indoor of dehumidifying side, room by intake stack A, and exhaust outlet A connects into the indoor upper end of the plenum chamber of opposite side by exhaust duct A through hothouse indoor.
Preferably, it is indoor that the suction opeing of described air exhauster is positioned at dehumidifying room.
Preferably, the outlet air end of described dehydrating unit through air exhauster, aerial condenser air set pipe after connect exhaust duct A.
Preferably, it is indoor that the suction opeing of described air exhauster connects dehumidifying room simultaneously.
Owing to have employed technique scheme, the beneficial effects of the utility model are:
1. this utility model adopts conventional energy resource to be automatically adjusted with wide temperature section plus new forms of energy power-assisted, can to needing the different grain of different cultivars of baking temperature, forestry products and Chinese crude drug to carry out removal moisture drying.Treatment in accordance with local conditions make use of local solar energy, geothermal energy, biomass energy equal energy source again, and Local Adaptation is strong；Meanwhile, when heat reaches to dry temperature required, burning diesel oil or combustion of natural gas room quit work, the heat keeping producing mainly by new forms of energy such as external solar energys of later temperature；When outside climatic changes, can integrated use electric energy, diesel oil, natural gas, the various combination of external new forms of energy carrys out the properly functioning of support equipment.
2. drying device absorption dehydration room air of the present utility model, is discharged in hothouse after heating again, is isolated from the outside, and forms closed cycle, and heat not easily runs off, and power consumption is decreased obviously；
3. dehydrating unit of the present utility model is also adopt closed cycle, it is possible to effectively removing the dampness in hothouse, coordinate with drying device, reach better effect on moisture extraction, heat not easily scatters and disappears；
4. the Hot wet air heating produced during drying device of the present utility model heating, after also being dehumidified by dehydrating unit, by dehumidifying, blood circulation enters in hothouse, and heat not easily scatters and disappears；
5. this utility model also utilizes the convection current of heat and conduction between adjacent two drying equipments to reach the purpose of further energy-saving and emission-reduction；
6. the air intake passage of drying device of the present utility model is provided with aerial condenser, it is possible to the condensate moisture in the hot blast entered in drying device got off, effectively removes the dampness in hot blast, and utilize air setting principle, do not need other energy, energy-conservation and environmental protection, and effect on moisture extraction is good；The high-temperature water condensed out may also pass through hothouse, then recycles, through hothouse, it is possible to distributes heat in hothouse, to reach effective utilization of heat；
7. this utility model conventional energy resource further promotes the reduction of drying equipment drying cost plus new forms of energy power-assisted.Wide temperature section is automatically adjusted, and makes again the various product of the grower of grain, forestry products, Chinese crude drug can be dried in time on an equipment；Also the scope promoting the business of the owner of drying equipment further expands；Grower and drying equipment owner can therefrom more interests of capacitation.Thus just drive plant and dry industry more addition.The expansion of plantation and dry working troop, this grain loss that the grain security and minimizing climate reasons that ensure China are caused will produce very positive effect undoubtedly.
To sum up, this utility model has obvious economy, society and environmental benefit.Should widely popularize.
Accompanying drawing explanation
Fig. 1 is the top view of dehumidification equipment of the present utility model.
Fig. 2 is the A-A sectional view of Fig. 1.
Fig. 3 is the B-B sectional view of Fig. 1.
Fig. 4 is the C-C sectional view of Fig. 1.
Fig. 5 is heater structure schematic diagram of the present utility model.
Fig. 6 is that heater of the present utility model is connected block diagram with temperature sensor.
Fig. 7 is aerial condenser structural representation of the present utility model.
Fig. 8 is the application state figure of dehumidification equipment of the present utility model.
Labelling in figure: 10-dehumidifies room, 20-hothouse, 30-plenum chamber, 40-wind pushing hole, 50-drying device, 51-heater, 511-base plate, 512-combustor, 513-first connects box body, 514-second connects box body, 515-adds heat pipe heat, 516-the 3rd connects box body, 517-exhaust emission tube, 518-cleaner, 519-air intake duct, 52-housing, 53-dehumidifying mesh, 54-blower fan, 55-intake stack B, 56-air inlet B, 57-exhaust duct B, 58-exhaust outlet B, 59-heating control module, 60-dehydrating unit, 61-air intake mesh, 62-intake stack A, 63-air inlet A, 64-exhaust duct A, 65-exhaust outlet A, 66-dehumidifying room solenoid valve, 70-temperature sensor, 80-solar energy air heat collector, 81-heat collector air inlet, 82-heat collector exhaust duct, 83-heat collector solenoid valve, 91-aerial condenser, 910-air set pipe, 92-air exhauster, 100-dehumidification equipment.
Detailed description of the invention
With reference to Fig. 1-8, the dehumidification equipment that a kind of air cooling of the present utility model is energy-conservation, including dehumidifying room 10 and hothouse 20, dehumidifying room 10 is arranged on hothouse 20 side, hothouse 20 opposite side is provided with plenum chamber 30, and plenum chamber 30 and the common wall of hothouse 20 are provided with wind pushing hole 40.Dehumidifying is provided with, in room 10, the dehydrating unit 60 and drying device 50 that are arranged side by side.
Wherein, dehydrating unit 60 adopts electric power heat pump as core parts, remove the dampness in air, the air inlet A63 of dehydrating unit 60 connects into lower end, hothouse 20 side by intake stack A62, exhaust outlet A65 connects into hothouse 20 opposite side upper end by exhaust duct A64, and the casing of dehydrating unit 60 is additionally provided with the air intake mesh 61 for absorption dehumidifying room 10 room air.In order to the inlet and outlet of the inlet and outlet of dehydrating unit 60 and drying device 50 is staggered, to reach better effect on moisture extraction, the air inlet A63 of dehydrating unit 60 connects into the indoor lower end of hothouse 20 of dehumidifying side, room 10 by intake stack A62, and exhaust outlet A65 connects into the indoor upper end of plenum chamber 30 of opposite side by exhaust duct A64 through hothouse 20 indoor.
Drying device 50 includes housing 52, and the heater 51 in housing 52, the exhaust outlet B58 of drying device 50 connects into plenum chamber 30 lower end by exhaust duct B57 through hothouse 20 indoor, the air inlet B56 of drying device 50 connects into the indoor top of hothouse 20 of plenum chamber 30 opposite side by intake stack B55, and housing 52 top is provided with blower fan 54, blower fan 54 is connected with intake stack B55.Blower fan 54 is preferably induced-draught fan, can by the housing 52 of the indoor continuous suction drying device 50 of air by induced-draught fan 54, and air is after adding heat pipe heat 515 and be heated, then enters in hothouse 20.Housing 52 top is additionally provided with the dehumidifying mesh 53 for dampness enters dehumidifying room 10.
Heater 51 includes combustor 512, and some layers that stacked distribution is above combustor 512 add heat pipe heat 515, adding serpentine-like shape connection between heat pipe heat 515, and one of them end port connects combustor 512, another end port connects the exhaust emission tube 517 that waste gas is discharged dehumidifying room 10.Combustor 512 is also associated with air intake duct 519, and air intake duct 519 extends the outdoor of dehumidifying room 10, and the oral area of air intake duct 519 is provided with cleaner 518.
Dehumidification equipment 100 also includes the solar energy air heat collector 80 being arranged on hothouse 20 top, solar energy air heat collector 80 side is provided with heat collector air inlet 81, opposite side is provided with the heat collector exhaust duct 82 being connected with exhaust duct B57, and the pipeline of heat collector exhaust duct 82 is provided with the heat collector solenoid valve 85 regulating exhaust air rate.
Being provided with temperature sensor 70 in four corners of the indoor top of hothouse 20 and dehumidifying room 10, heater 51 is provided with heating control module 59, and temperature sensor 70 is connected with heating control module 59.
Preferably, combustor 512 be burning diesel oil diesel combustion room 512 or burning natural gas combustion of natural gas room 512, by combustor 512 burning can produce huge heat, be then passed to add in heat pipe heat 515.Heater 51 also includes base plate 511, base plate 511 supports fixed combustion room 512, it is provided with first between the end port adding heat pipe heat 515 and the combustor 512 of connection combustor 512 and is connected box body 513, the adding heat pipe heat 515 and be connected box body 514 with adding heat pipe heat between 515 and arranging second of serpentine-like shape connection, the end port adding heat pipe heat 515 connecting exhaust emission tube 517 is provided with the 3rd connection box body 516.The steam of combustor 512 burning flows into after flowing through the first connection box body 513 and adds in heat pipe heat 515, then pass through the second connection connection box body inflow next one and add in heat pipe heat 515, heat pipe heat 515 is added by what be arranged to snakelike circulation, heat can be flowed through endlessly and add heat pipe heat 515, it is ensured that add heat pipe heat 515 and there is enough heating-up temperatures.Last waste gas then flows into the 3rd connection box body 516, and is discharged by exhaust emission tube 517.Each heat pipe heat 515 that adds forms by the heating tube side-by-side setting of 6-8 root.
The operation principle of dehumidification equipment of the present utility model:
The article needing removal moisture drying are put in hothouse 20, run dehydrating unit 60 and drying device 50, wherein, drying device 50 is under the effect of blower fan 54, by in the intake stack B55 air suction casing 52 by hothouse 20 indoor, the heat of combustor 512 burning of heater 51, it is sent to and adds in heat pipe heat 515, enter the air of housing 52 by heated after adding heat pipe heat 515, then pass through exhaust duct B57 and be sent in plenum chamber 30, the heat that external solar energy air heat collector 80 produces passes through heat collector exhaust duct 82 through exhaust duct B57 also into plenum chamber 30.Hot blast is sent in hothouse 20 by the wind pushing hole 40 on the common wall of plenum chamber 30 and hothouse 20, and the air of hothouse 20 indoor is by after circulating-heating, and temperature rises, and the article being placed in hothouse 20 are dried.The air inlet B56 of drying device 50 is provided in the indoor top of hothouse 20 of plenum chamber 30 opposite side, exhaust outlet B58 is then provided in plenum chamber 30, air intake position and air-out position in hothouse 20 is made to be in diagonal position, thus forming convection current so that the article of each position of hothouse 20 can obtain better drying effect.Meanwhile, drying device 50 is the air in absorption dehydration room 20, then sends back in hothouse 20 again after heating, forms a dry cycle system closed, and heat loss is few, energy-saving and cost-reducing.
The air of hothouse 20 indoor is sucked in dehydrating unit 60 by intake stack A62 by dehydrating unit 60, after dehumidifying, is sent back to the indoor of plenum chamber 30 by exhaust duct A64 and exhaust outlet A65, forms a circulation dehumidification system closed.
Drying device 50 can produce certain Hot wet air heating when heating, in order to remove this part Hot wet air heating, on housing 52 top of drying device 50, dehumidifying mesh 53 is set, the Hot wet air heating dehumidifying mesh 53 through housing 52 top enters in dehumidifying room 10, then dehumidified device 60 sucks through air intake mesh 61, enters dehumidification system, sends the indoor of plenum chamber 30 back to finally by exhaust duct A64 and exhaust outlet A65, heat recovery, not easily scatters and disappears.
The air inlet B56 and exhaust outlet B58 of drying device 50 forms the convection current at a diagonal angle in hothouse 20, and the convection current at another diagonal angle that the air inlet A63 and exhaust outlet A65 of dehydrating unit 60 intersect therewith in the indoor formation of plenum chamber 30, enhance desiccant dehumidification effect.
Owing to hothouse 20 and dehumidifying room 10 being designed with temperature sensor 70, hothouse 20 and the temperature in dehumidifying room 10 can be detected in real time, when hothouse 20 exceedes setting value with the temperature in dehumidifying room 10, temperature sensor 70 transmits a signal to heating control module 59 in heater 51, heating control module 59 stops combustor 512 and works, and it is located at the dehumidifying room solenoid valve 66 on dehumidifying top, room 10 and the dual regulation of the heat collector solenoid valve 83 of external new forms of energy by what be controlled by, to regulate and control baking temperature in the temperature range set, blower fan 54 works on simultaneously, proceed dry and dehumidifying circulation.
For ensureing that the hothouse 20 temperature energy long period maintains in set temperature range, this utility model utilizes the heat collector solenoid valve 83 of the external new forms of energy of the waste heat adding heat pipe heat 515 and heating control module 59 control, the entrance heat of regulation and control solar energy air heat collector 80.When the heat that external solar energy produces can maintain always dry temperature required time, combustor 512 is not restarted；Because outside climatic condition changes.When the heat that external new forms of energy produce can not maintain dry temperature required time, combustor 512 restarts.
In order to reach better effect on moisture extraction, intake stack B55 of the present utility model is additionally provided with aerial condenser 91 on the pipeline being positioned at dehumidifying indoor, room 10, being provided with several air set pipes 910 being perpendicular to direction of ventilation in exhaust duct A64 in aerial condenser 91, wherein one end of air set pipe 910 is connected to air exhauster 92.
It is indoor that the suction opeing of air exhauster 92 is positioned at dehumidifying room 10, the air in dehumidifying room 10 is directly extracted by air exhauster 92, when cold air is constantly by the pipe of air setting 910, and the steam pre-cooling outside air set pipe 910 pipe, condensate moisture in hot blast is got off, and the bottom of aerial condenser 91 it is flow to along the tube wall of air set pipe 910, one osculum (not shown) is set in the bottom of aerial condenser 91, Water Sproading can be utilized, achieve and the hot blast in intake stack B55 is effectively dehumidified, hot blast after dehumidifying enters back into drying device 50, it is dried process.
The water condensed out through aerial condenser 91 is hot water, hot water is when osculum is collected, osculum connects collection conduit, can also by the collection conduit indoor through hothouse 20, the heat making hot water can be dispersed in hothouse 20, to reach effective utilization of heat, finally just this part Recovery of the hot water is utilized.
So that aerial condenser 91 reaches better condensation effect, this utility model also provides for another embodiment to realize the air cooling of aerial condenser 91.The outlet air end of described dehydrating unit 60 through air exhauster 92, aerial condenser 91 air set pipe 910 after connect exhaust duct A64.So, the Cryogenic air after being processed by dehydrating unit 60 is incorporated in aerial condenser 91, and this Cryogenic air is the air after electric power heat pump processes, and temperature is lower than room temperature, and condensation effect is more preferably.In order to ensure that aerial condenser 91 has enough intakes, it is indoor that the suction opeing of described air exhauster 92 connects dehumidifying room 10 simultaneously, can the intake of aerial condenser 91 effectively be supplemented by extracting the air of indoor.
With reference to Fig. 7, the dehumidification equipment 100 of the present invention is when multiple stage uses simultaneously, it is possible to is dehumidified and is interconnected between room 10, thus realizing sharing of heat.
Above the dehumidification equipment of a kind of new forms of energy power-assisted width temperature section provided by the utility model regulation and control is carried out exhaustive presentation, structure of the present utility model and implementation are set forth by specific case used herein, and the explanation of above example is only intended to help to understand structure of the present utility model and core concept thereof；Simultaneously for one of ordinary skill in the art, according to thought of the present utility model, all will change in specific embodiments and applications, in sum, this specification content should not be construed as restriction of the present utility model.To be possible to change of the present utility model and improvement, without the design that could dictate that beyond accessory claim and scope.
Claims (10)
1. the dehumidification equipment that an air cooling is energy-conservation, it is characterized in that, including dehumidifying room (10) and hothouse (20), dehumidifying room (10) is arranged on hothouse (20) side, hothouse (20) opposite side is provided with plenum chamber (30), and plenum chamber (30) and the common wall of hothouse (20) are provided with wind pushing hole (40)；Dehumidifying room (10) is provided with dehydrating unit (60) and drying device (50)；
The air inlet A (63) of dehydrating unit (60) connects into hothouse (20) lower end, side by intake stack A (62), exhaust outlet A (65) connects into hothouse (20) opposite side upper end by exhaust duct A (64), and the casing of dehydrating unit (60) is additionally provided with the air intake mesh (61) for absorption dehumidifying room (10) room air；Dehumidifying room (10) upper end is additionally provided with dehumidifying room solenoid valve (66)；
Drying device (50) includes housing (52), and the heater (51) in housing (52), the exhaust outlet B (58) of drying device (50) connects into plenum chamber (30) lower end by exhaust duct B (57) through hothouse (20) indoor, the air inlet B (56) of drying device (50) connects into the indoor top of hothouse (20) of plenum chamber (30) opposite side by intake stack B (55), and housing (52) top is provided with blower fan (54), blower fan (54) is connected with intake stack B (55)；Described housing (52) top is additionally provided with the dehumidifying mesh (53) for dampness enters dehumidifying room (10)；
Intake stack B (55) is being positioned on the pipeline that dehumidifying room (10) is indoor and is being additionally provided with aerial condenser (91), being provided with several air set pipes (910) being perpendicular to direction of ventilation in exhaust duct A (64) in aerial condenser (91), wherein one end of air set pipe (910) is connected to air exhauster (92).
2. the dehumidification equipment that air cooling according to claim 1 is energy-conservation, it is characterized in that, described heater (51) includes combustor (512), and some layers that stacked distribution is in combustor (512) top add heat pipe heat (515), add serpentine-like shape connection between heat pipe heat (515), and one of them end port connects combustor (512), another end port connects the exhaust emission tube (517) that waste gas is discharged dehumidifying room (10)；Combustor (512) is also associated with air intake duct (519), air intake duct (519) extends the outdoor of dehumidifying room (10), and the oral area of air intake duct (519) is provided with cleaner (518).
3. the dehumidification equipment that air cooling according to claim 2 is energy-conservation, it is characterised in that the combustion of natural gas room of diesel combustion room that described combustor (512) is burning diesel oil or burning natural gas.
4. the dehumidification equipment that air cooling according to claim 2 is energy-conservation, it is characterized in that, described heater (51) also includes base plate (511), base plate (511) is upper supports fixed combustion room (512), it is provided with first between the end port adding heat pipe heat (515) and the combustor (512) of connection combustor (512) and is connected box body (513), the adding heat pipe heat (515) and arrange second between heat pipe heat (515) be connected box body (514) with adding of serpentine-like shape connection, the end port adding heat pipe heat (515) connecting exhaust emission tube (517) is provided with the 3rd connection box body (516).
5. the dehumidification equipment that air cooling according to claim 2 is energy-conservation, it is characterised in that described each heat pipe heat (515) that adds forms by the heating tube side-by-side setting of 6-8 root.
6. the dehumidification equipment that air cooling according to claim 1 is energy-conservation, it is characterized in that, dehumidification equipment (100) also includes the solar energy air heat collector (80) being arranged on hothouse (20) top, solar energy air heat collector (80) side is provided with heat collector air inlet (81), opposite side is provided with the heat collector exhaust duct (82) being connected with exhaust duct B (57), and the pipeline of heat collector exhaust duct (82) is provided with the heat collector solenoid valve (83) regulating exhaust air rate；
Four corners of indoor top of described hothouse (20) and dehumidifying room (10) are provided with Temperature Humidity Sensor (70), heater (51) is provided with heating control module (59), Temperature Humidity Sensor (70) is connected with heating control module (59), and heating control module (59) is connected with heat collector solenoid valve, dehumidifying room solenoid valve respectively.
7. the dehumidification equipment that air cooling according to claim 1 is energy-conservation, it is characterized in that, the air inlet A (63) of described dehydrating unit (60) connects into the indoor lower end of hothouse (20) of dehumidifying room (10) side by intake stack A (62), and exhaust outlet A (65) connects into the indoor upper end of the plenum chamber (30) of opposite side by exhaust duct A (64) through hothouse (20) indoor.
8. the dehumidification equipment that air cooling according to claim 1 is energy-conservation, it is characterised in that it is indoor that the suction opeing of described air exhauster (92) is positioned at dehumidifying room (10).
9. the dehumidification equipment that air cooling according to claim 1 is energy-conservation, it is characterized in that, the outlet air end of described dehydrating unit (60) through air exhauster (92), aerial condenser (91) air set pipe (910) after connect exhaust duct A (64).
10. the dehumidification equipment that air cooling according to claim 9 is energy-conservation, it is characterised in that it is indoor that the suction opeing of described air exhauster (92) connects dehumidifying room (10) simultaneously.
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| CN201620021702.2U CN205351964U (en) | 2016-01-11 | 2016-01-11 | Energy -conserving dehumidification drying equipment of air cooling |
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| CN201620021702.2U CN205351964U (en) | 2016-01-11 | 2016-01-11 | Energy -conserving dehumidification drying equipment of air cooling |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN107300301A (en) * | 2017-06-13 | 2017-10-27 | 徐州蕴康农业科技有限公司 | The fresh-keeping all-in-one of multi-function drying |
| CN108180754A (en) * | 2018-02-10 | 2018-06-19 | 西南大学 | A kind of chamber typed drying-machine humid air dehydration device |
| CN109066425A (en) * | 2018-09-26 | 2018-12-21 | 国网山东省电力公司海阳市供电公司 | Electric power overhaul system and repair method |
| CN110367330A (en) * | 2019-06-21 | 2019-10-25 | 江苏盐渎百鸣农业有限公司 | A kind of fruit and vegetable dryness equipment |
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| CN108180754A (en) * | 2018-02-10 | 2018-06-19 | 西南大学 | A kind of chamber typed drying-machine humid air dehydration device |
| CN109066425A (en) * | 2018-09-26 | 2018-12-21 | 国网山东省电力公司海阳市供电公司 | Electric power overhaul system and repair method |
| CN109066425B (en) * | 2018-09-26 | 2020-05-05 | 国网山东省电力公司海阳市供电公司 | Electric power overhaul system |
| CN110367330A (en) * | 2019-06-21 | 2019-10-25 | 江苏盐渎百鸣农业有限公司 | A kind of fruit and vegetable dryness equipment |
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