CN202792879U - Total heat recovery type air source dehumidifying and drying integrated machine - Google Patents
Total heat recovery type air source dehumidifying and drying integrated machine Download PDFInfo
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- CN202792879U CN202792879U CN2012203054461U CN201220305446U CN202792879U CN 202792879 U CN202792879 U CN 202792879U CN 2012203054461 U CN2012203054461 U CN 2012203054461U CN 201220305446 U CN201220305446 U CN 201220305446U CN 202792879 U CN202792879 U CN 202792879U
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- drying
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- dehumidifying
- heat recovery
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
- Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
- Y02B30/52—Heat recovery pumps, i.e. heat pump based systems or units able to transfer the thermal energy from one area of the premises or part of the facilities to a different one, improving the overall efficiency
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/10—Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working
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Abstract
The utility model discloses a total heat recovery type air source dehumidifying and drying integrated machine which comprises a machine housing, a heat recovering device, a compressor, a gas-liquid separator, an electric control box, a dehumidifying system and a drying system. A return-air inlet, a fresh-air inlet and a hot-air outlet are arranged on the machine housing, and the heat recovering device is arranged between the dehumidifying system and the drying system. The dehumidifying system comprises a circulation fan, an evaporator, an electric heating tube and a strong exhaust air cooler, and a cold-air outlet is arranged on the strong exhaust air cooler. The drying system comprises a secondary condenser, a centrifugal fan and a condenser. Compared with the prior art, the total heat recovery type integrated air source dehumidifying and drying machine has the advantages that the device comprising a two-stage total heat recovery and two-stage condensation system is arranged, a dehumidifying function and a drying function are integrated, multistage heating and continuous dehumidification can be achieved, a circulation heating function is achieved, neither frosting nor defrosting is caused, the air resource is fully used for heat exchange, and the total heat recovery type integrated air source dehumidifying and drying machine is energy saving and environmental friendly.
Description
[technical field]
The utility model relates to mechanical field, air-source field and drying field, relates in particular to a kind of full heat-recovery air source dehumidifying drying all-in-one.
[background technology]
Existing air-source drying technology mainly contains two kinds.
The first is that oven dry is independent mutually with dehumidifying, and the air-source oven dry is a cover system, and unit is split type; The independent humidity control machine is adopted in dehumidifying, uses needs to satisfy.There is following defective in this technology: 1, Drying unit itself does not possess dehumidification function, and the dehumidification rate of dehumidifier can and reduce along with the temperature rising, is higher than more than 35 ℃, does not substantially dehumidify.2, outer chance frosting in winter needs defrost, under low temperature condition, and poor effect, indoor temperature does not increase because of frequent defrost; 3, in the circulating-heating process, condensation temperature can uprise along with the rising of indoor temperature, causes the compressor return air temperature to raise, and has a strong impact on the service life of compressor.
Another kind is that the air source drying-machine group is adopted monoblock type, and dehumidifying is by high-power blower that hot and humid Bas Discharged is outdoor under the condition of high temperature, thereby reaches the oven dry purpose.Also there is following defective in this technology: 1, unit itself does not possess dehumidification function, only depends on forced-ventilated under the humid tropical condition, and drying effect can't guarantee.2, outer machine frosting in winter, defrost still fail to solve, and weak effect reaches instructions for use reluctantly after increasing powerful auxiliary electrical heater; Operating cost is high, and is not energy-conservation; 3, in the forced-ventilated hydrofuge process, can cause a large amount of heats to lose in vain, cause the wasting of resources.Simultaneously, drying room must be introduced from the external world new wind, has additionally introduced again the new air that contains a large amount of humidity, has greatly prolonged drying time.
[utility model content]
The utility model provides a kind of full heat-recovery air source dehumidifying drying all-in-one in order to solve the above-mentioned deficiency of prior art.It has realized that dehumidifying drying is integrated, and is reaching under the prerequisite of drying effect, realizes energy-saving and cost-reducing purpose, has greatly promoted user's effectiveness of operation.
Above-mentioned purpose of the present utility model realizes by following technical scheme: a kind of full heat-recovery air source dehumidifying drying all-in-one, comprise casing, heat regenerator, compressor, gas-liquid separator, electric cabinet, dehumidification system and drying system, described casing is provided with the return air entrance, new wind entrance and hot-blast outlet, described heat regenerator is arranged between dehumidification system and the drying system, described dehumidification system comprises circulating fan, evaporimeter, electric heating tube and forced-ventilated air-cooler, the forced-ventilated air-cooler is provided with the cold wind outlet, and described drying system comprises secondary condenser, centrifugal blower and condenser.
Operation principle of the present utility model: the return air entrance is connected with drying room with hot-blast outlet, High Temperature Moist Air enters unit through the return air entrance in the drying room, through the heat regenerator cooling, pressurizes by circulating fan afterwards, enter the evaporimeter cool-down dehumidification and become the low temperature dry air, dehumidification process finishes; The low temperature dry air heats up through heat regenerator; pass through again the secondary condenser secondary temperature elevation; by the air-supply centrifugal blower; after entering condenser and again heating up; become high temperature dry air, enter drying room by hot-blast outlet, high temperature dry air becomes again High Temperature Moist Air and enters unit through the return air entrance again; begin next circulation, until drying requirement is shut down.
The utility model advantage compared with prior art is: the system and device with two-stage total heat recovery, condensed in two stages, integrate dehumidifying drying, possessed stepped heating, the lasting ability that dehumidifies, also possessed hydronic function, frost-free, without defrost, take full advantage of the air-source heat exchange, energy-conserving and environment-protective.
Be specially:
1, two-stage total heat recovery
High Temperature Moist Air in the drying room through warm and humid air in becoming after the heat regenerator heat exchange, heats up to opposite side low temperature dry air simultaneously, realizes the one-level recuperation of heat; Again with enter evaporimeter after new wind mixes and become the low temperature dry air, realize the secondary recuperation of heat.By these two full recuperations of heat of process implementation.
2, condensed in two stages technology
In condenser dry air temperature-rise period, adopt the condensed in two stages technology, widen on the one hand air intake and the air-out temperature difference, improve leaving air temp, improve the drying efficiency of unit; Reduce on the other hand the refrigerant temperature that enters expansion valve, improve the condensation efficiency of equipment, thereby the efficiency of unit is provided; The 3rd, breeze fan can be placed between the condenser, when satisfying air current composition, guarantees the working environment of blower motor, improves the service life of motor.
3, dehumidifying drying one
Two-stage total heat recovery has guaranteed required heat in the evaporator evaporation process, has also realized simultaneously dehumidification function, after heating up through heat regenerator, secondary condenser, condenser, reaches the oven dry purpose, realizes the dehumidifying drying one fully.
4, stepped heating technology
Low temperature dry air after the flash-pot dehumidifying directly being heated under the condition that does not adopt any auxiliary thermal source more than 60 ℃, has promoted the drying efficiency of unit through heat regenerator, secondary condenser, three grades of intensifications of condenser greatly.
5, continue dehumidifying effect
The unit temperature-rise period is a lasting cyclic process, circulated air all must be through entering the evaporimeter dehumidifying again after the heat regenerator cooling, avoided having guaranteed dehumidification rate and the continuous service of evaporimeter because High Temperature Moist Air excess Temperature in the drying room affects dehumidification rate even unit operation.
6, heating tech
Unit first through heating up after twice cooling, has avoided condensation temperature too high and affect the equipment operation even can not work in the dehumidifying drying process again, can realize continuing circulating-heating, stable operation.
7, frost-free is without defrost
In the winter time between algid stage; the required heat of the inadequate evaporimeter of warm and humid airborne heat in after lowering the temperature through heat regenerator replenishes by the auxiliary electrical heater pipe, guarantees that frost does not appear in unit operation; guarantee that unit is in oven-dried condition always, improve serviceability.
8, utilize the air-source heat exchange
Between non-algid stage in winter, during through the required heat of the inadequate evaporimeter of warm and humid airborne heat in after the heat regenerator cooling, replenish by introducing the new wind-heat amount in outside, too much low temperature dry air is discharged by strong board air-cooler, realize the air-source heat exchange, reduce power consumption, improve the efficiency of unit, improve energy-saving benefit.
[
Description of drawings]
Fig. 1 is structural representation of the present utility model.
Wherein, 1-evaporimeter; 2-forced-ventilated air-cooler; 3-heat regenerator; 4-secondary condenser; 5-centrifugal blower; 6-condenser; 7-electric cabinet; 8-gas-liquid separator; 9-compressor; 10-circulating fan; 11-casing; 12-electric heating tube; 13-return air entrance; 14-new wind entrance; 15-hot-blast outlet; The outlet of 16-cold wind.
[specific embodiment]
Below in conjunction with accompanying drawing the utility model is described in further detail:
As shown in Figure 1, a kind of full heat-recovery air source dehumidifying drying all-in-one, comprise casing 11, heat regenerator 3, compressor 9, gas-liquid separator 8, electric cabinet 7, dehumidification system and drying system, described casing 11 is provided with return air entrance 13, new wind entrance 14 and hot-blast outlet 15, described heat regenerator 3 is arranged between dehumidification system and the drying system, described dehumidification system comprises circulating fan 10, evaporimeter 1, electric heating tube 12 and forced-ventilated air-cooler 2, forced-ventilated air-cooler 2 is provided with cold wind outlet 16, and described drying system comprises secondary condenser 4, centrifugal blower 5 and condenser 6.
Operation principle of the present utility model: the return air entrance 13 on the casing 11 is connected with hot-blast outlet and is connected with drying room, High Temperature Moist Air enters the utility model through return air entrance 13 in the drying room, through heat regenerator 3 coolings, rear by circulating fan 10 pressurizations, enter evaporimeter 1 cool-down dehumidification and become the low temperature dry air, dehumidification process finishes; The low temperature dry air heats up through heat regenerator 3; pass through again secondary condenser 4 secondary temperature elevations; by air-supply centrifugal blower 5; after entering condenser 6 and again heating up; become high temperature dry air, enter drying room by the hot-blast outlet 15 on the casing 11, high temperature dry air becomes again the return air entrance 13 of High Temperature Moist Air on casing 11 and enters the utility model again; begin next circulation, until drying requirement is shut down.
It should be noted that at last: above-described embodiment only is for the utility model example clearly is described; and be not restriction to embodiment; for those of ordinary skill in the field; can also make other changes in different forms on the basis of the above description; here need not also can't give all embodiments exhaustive, and the apparent variation of being amplified out thus or the change still be among the protection domain of the present utility model.
Claims (1)
1. full heat-recovery air source dehumidifying drying all-in-one, comprise casing, heat regenerator, compressor, gas-liquid separator, electric cabinet, dehumidification system and drying system, described casing is provided with return air entrance, new wind entrance and hot-blast outlet, described heat regenerator is arranged between dehumidification system and the drying system, described dehumidification system comprises circulating fan, evaporimeter, electric heating tube and forced-ventilated air-cooler, the forced-ventilated air-cooler is provided with the cold wind outlet, and described drying system comprises secondary condenser, centrifugal blower and condenser.
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CN2012203054461U CN202792879U (en) | 2012-06-28 | 2012-06-28 | Total heat recovery type air source dehumidifying and drying integrated machine |
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CN2012203054461U CN202792879U (en) | 2012-06-28 | 2012-06-28 | Total heat recovery type air source dehumidifying and drying integrated machine |
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Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104359221A (en) * | 2014-12-03 | 2015-02-18 | 湖南省浏阳市择明热工器材有限公司 | Air-source heat-pump air heater for reducing defrosting temperature |
CN104441953A (en) * | 2014-10-10 | 2015-03-25 | 山东丽鹏股份有限公司 | Gold stamping and mark pressing technique for aluminum cap and bottle cap positioning device for gold stamping and mark pressing technique |
CN104482749A (en) * | 2014-12-03 | 2015-04-01 | 湖南省浏阳市择明热工器材有限公司 | Drying system lowering defrosting temperature of air source heat pump |
CN105222566A (en) * | 2015-10-30 | 2016-01-06 | 江门市达能环保节能科技有限公司 | A kind of heat pump drying system with dehumidifier and Waste Heat Reuse |
CN106524583A (en) * | 2016-12-22 | 2017-03-22 | 广东申菱环境***股份有限公司 | Household dehumidify and drying integrated machine |
CN108759141A (en) * | 2018-04-25 | 2018-11-06 | 四川鸿旺同宇能源科技有限公司 | The energy conserving system that freezing is recycled with drying energy |
-
2012
- 2012-06-28 CN CN2012203054461U patent/CN202792879U/en not_active Expired - Fee Related
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104441953A (en) * | 2014-10-10 | 2015-03-25 | 山东丽鹏股份有限公司 | Gold stamping and mark pressing technique for aluminum cap and bottle cap positioning device for gold stamping and mark pressing technique |
CN104359221A (en) * | 2014-12-03 | 2015-02-18 | 湖南省浏阳市择明热工器材有限公司 | Air-source heat-pump air heater for reducing defrosting temperature |
CN104482749A (en) * | 2014-12-03 | 2015-04-01 | 湖南省浏阳市择明热工器材有限公司 | Drying system lowering defrosting temperature of air source heat pump |
CN104359221B (en) * | 2014-12-03 | 2017-12-22 | 湖南省浏阳市择明热工器材有限公司 | A kind of air-source heat-pump air heater for reducing defrost temperature |
CN105222566A (en) * | 2015-10-30 | 2016-01-06 | 江门市达能环保节能科技有限公司 | A kind of heat pump drying system with dehumidifier and Waste Heat Reuse |
CN106524583A (en) * | 2016-12-22 | 2017-03-22 | 广东申菱环境***股份有限公司 | Household dehumidify and drying integrated machine |
CN108759141A (en) * | 2018-04-25 | 2018-11-06 | 四川鸿旺同宇能源科技有限公司 | The energy conserving system that freezing is recycled with drying energy |
CN108759141B (en) * | 2018-04-25 | 2020-10-09 | 四川鸿旺同宇能源科技有限公司 | Energy-saving system for recycling freezing and drying energy |
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130313 Termination date: 20150628 |
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EXPY | Termination of patent right or utility model |