CN104949496A - High-temperature heat pump drying system with intelligent adjusting function - Google Patents
High-temperature heat pump drying system with intelligent adjusting function Download PDFInfo
- Publication number
- CN104949496A CN104949496A CN201510383802.XA CN201510383802A CN104949496A CN 104949496 A CN104949496 A CN 104949496A CN 201510383802 A CN201510383802 A CN 201510383802A CN 104949496 A CN104949496 A CN 104949496A
- Authority
- CN
- China
- Prior art keywords
- heat pump
- valve
- temperature heat
- blower fan
- air
- Prior art date
Links
- 238000001035 drying Methods 0.000 title claims abstract description 51
- 239000003570 air Substances 0.000 claims abstract description 31
- 239000000463 materials Substances 0.000 claims abstract description 28
- 239000007788 liquids Substances 0.000 claims description 37
- 238000002347 injection Methods 0.000 claims description 29
- 239000007924 injections Substances 0.000 claims description 29
- 238000001914 filtration Methods 0.000 claims description 8
- 239000011521 glasses Substances 0.000 claims description 8
- 239000003921 oils Substances 0.000 claims description 8
- 238000001704 evaporation Methods 0.000 claims description 5
- 238000010438 heat treatment Methods 0.000 claims description 4
- 210000001736 Capillaries Anatomy 0.000 claims description 3
- 238000006243 chemical reactions Methods 0.000 claims description 3
- 230000005520 electrodynamics Effects 0.000 claims description 3
- 229910001220 stainless steel Inorganic materials 0.000 claims description 3
- 239000010935 stainless steel Substances 0.000 claims description 3
- 230000000875 corresponding Effects 0.000 claims description 2
- 238000005516 engineering processes Methods 0.000 abstract description 14
- 239000003205 fragrance Substances 0.000 abstract description 2
- 238000005485 electric heating Methods 0.000 abstract 1
- 238000000034 methods Methods 0.000 description 16
- 239000003507 refrigerants Substances 0.000 description 9
- 230000001105 regulatory Effects 0.000 description 4
- 241001081830 Degeneriaceae Species 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000007789 gases Substances 0.000 description 3
- 238000001816 cooling Methods 0.000 description 2
- 239000000203 mixtures Substances 0.000 description 2
- 238000003825 pressing Methods 0.000 description 2
- 239000000126 substances Substances 0.000 description 2
- 206010020843 Hyperthermia Diseases 0.000 description 1
- 239000005864 Sulphur Substances 0.000 description 1
- 238000003916 acid precipitation Methods 0.000 description 1
- 238000004378 air conditioning Methods 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound 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- 239000011555 saturated liquids Substances 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N sulfur Chemical compound 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[S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 238000004781 supercooling Methods 0.000 description 1
- 239000002912 waste gases Substances 0.000 description 1
- 239000002699 waste materials Substances 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
Abstract
Description
Technical field
The present invention relates to a kind of high-temperature heat pump drying system with Intelligent adjustment function.
Background technology
In China, traditional drying technology mainly produces heat by primary energy such as fuel oil, combustion gas, fire coal or burn wood and carries out product oven dry, not only energy consumption is large, efficiency is low, also can produce the harmful substances such as a large amount of waste gas, waste water, waste residue, dust, cause the disaster such as acid rain, haze, serious environment pollution.Meanwhile, adopt the drying technology of traditional energy, in the drying course of material, there will be pernicious gas and enter baking room, make, containing harmful substances such as sulphur in material, to form secondary pollution.Therefore, traditional stoving process needs to improve.
Current novel drying technology mainly contains two kinds, and one adopts the direct heating technique of electrothermal tube, simple to operate, but efficiency is too low, and operating cost is higher, contrary with the energy saving policy of country; Another kind adopts heat pump drying technology, energy-conserving and environment-protective, existing Some Enterprises is brought into use, but existing heat pump drying technology, systemic-function is too simple, and Intelligent adjustment is poor, cause the temperature of baking room, moisture fluctuation larger, the epidemic disaster that can not meet stoving process regulates requirement, causes heat pump overall efficiency not high, and service life reduces.
Summary of the invention
Object of the present invention just in order to provide a kind of high-temperature heat pump drying system with Intelligent adjustment function, to solve in existing stoving process the outstanding technical problems such as environmental pollution is serious, efficiency is lower, operating cost is high, temperature and humidity regulation is poor.
Object of the present invention realizes by following technique measures:
The high-temperature heat pump drying system with Intelligent adjustment function of the present invention comprises high temperature heat pump subsystem, Temperature and Humidity Control regulates subsystem, baking room subsystem, described high temperature heat pump subsystem comprises compressor, throttling arrangement, air-cooled condenser, wind-cooled evaporator, oil eliminator, reservoir, device for drying and filtering, liquid-sighting glass, capacity adjusting valve, liquid injection valve, subcooler, pressure of inspiration(Pi) control valve, septum valve, differential control valve and connecting pipe, the exhaust outlet of described compressor is divided into two interfaces, one of them exhaust port is connected with the import of pressure of inspiration(Pi) control valve by capacity adjusting valve, another exhaust port is connected with differential control valve import with air-cooled condenser import respectively by oil eliminator, described air-cooled condenser outlet is exported with differential control valve respectively by septum valve and is connected with the import of reservoir, the outlet of described reservoir passes through device for drying and filtering successively, liquid-sighting glass and subcooler are connected with liquid injection valve import with throttling arrangement import respectively, wherein throttling arrangement outlet is connected with the import of pressure of inspiration(Pi) control valve by wind-cooled evaporator, liquid injection valve outlet is connected to the corresponding air inlet of compressor by subcooler, and described pressure of inspiration(Pi) control valve outlet is connected with compressor air suction mouth, described Temperature and Humidity Control regulates subsystem comprise capacity adjusting valve, air-cooled condenser blower fan, wind-cooled evaporator blower fan, hydrofuge/exhaust fan, new wind blower fan, electric heater, controller, temperature sensor, humidity sensor and connect wire, in the storeroom that wherein said temperature sensor, humidity sensor are installed on casing respectively and return air inlet place, be connected with the input of controller respectively by connecting wire, the output of described controller is connected with the motor of capacity adjusting valve, the motor of air-cooled condenser blower fan, the motor of wind-cooled evaporator blower fan, the motor of the motor of hydrofuge exhaust fan, newly wind blower fan, electric heater respectively by connecting wire, described baking room subsystem comprises casing, door, return air dividing plate, materials vehicle, hydrofuge exhaust fan, new wind blower fan, screen pack, air-cooled condenser and electric heater, wherein said door is arranged on the right-hand member of casing, hydrofuge exhaust fan, new wind blower fan are installed on the both sides up and down of the left end of casing respectively, wherein screen pack is arranged on the front portion of new wind blower fan, described air-cooled condenser, electric heater are installed on the air inlet of storeroom front end successively, described materials vehicle deposits in storeroom air inlet, described return air dividing plate is installed on storeroom upper end, for the return airway between component material.
The outlet of liquid injection valve described in the present invention is connected with pressing tonifying Qi chamber in compressor by subcooler.
The outlet of liquid injection valve described in the present invention is connected with the air entry of compressor by subcooler, pressure of inspiration(Pi) control valve.Regulated the aperture of liquid injection valve by the temperature sensitive control device being arranged on compressor outlet, and then control the spouting liquid entering subcooler.
Compressor of the present invention be invariable frequency compressor, point gear compressor, frequency-changeable compressor or tonifying Qi increase in enthalpy compressor any one; Described air-cooled condenser, wind-cooled evaporator are any one in fin-tube type, stacked or parallel flow heat exchanger; Described air-cooled condenser blower fan, wind-cooled evaporator blower fan, hydrofuge exhaust fan, new wind blower fan are any one in frequency conversion fan, fixed blower fan frequently or gear shift blower fan; Described throttling arrangement is any one in heating power expansion valve, capillary expansion valve or electric expansion valve; Described liquid injection valve is any one in pressure type liquid injection valve or temp. type liquid injection valve; Described capacity adjusting valve is any one in thermal type capacity adjusting valve, electromagnetic energy control valve or electrodynamic type capacity adjusting valve; Described pressure of inspiration(Pi) control valve is a kind of proportionality control valve controlled by downstream pressure (i.e. suction pressure of compressor); Described septum valve is a kind of proportionality control valve controlled by upstream pressure (i.e. condensing pressure); Described electric heater is any one in PTC electric heater, stainless steel heater, fluid explosion-proof electric heater or electric infrared heater; Described subcooler is any one in plate type heat exchanger, double-tube heat exchanger or flash evaporation.
Principle of the present invention and beneficial effect as follows:
A kind of high-temperature heat pump drying system with Intelligent adjustment function provided by the invention, its structure is ingenious, system Optimized Matching, high temperature heat pump technology, air-conditioning regulation technology and auxiliary electrical heater technology are organically combined, its bake out temperature adjustable range is between 35 DEG C ~ 90 DEG C, widen the application that different material is dried, improve high-temperature heat pump drying system reliability of operation, stability and economy.
A kind of high-temperature heat pump drying system with Intelligent adjustment function provided by the invention, by the Intelligent adjustment of controller PLC and relevant executing agency, for the requirement of drying materials technique, adopt Temperature and Humidity Control strategy at times, temperature control precision can reach within 0.2 DEG C, and humid control precision can reach within 0.5%, realizes the Automatic Control of drying course, improve the quality of material drying, quality and fragrance simultaneously, ensure that the quality of material drying.
A kind of high-temperature heat pump drying system with Intelligent adjustment function provided by the invention, cost performance is high, energy-conserving and environment-protective, solve the defect of existing hyperthermia drying technology, therefore, it has market application foreground and huge market potential widely, is applicable to apply on a large scale.
Accompanying drawing explanation
Fig. 1 is the johning knot composition of the first embodiment of the present invention.
Fig. 2 is the johning knot composition of the second embodiment of the present invention.
Sequence number in figure: 1 compressor, 2 throttling arrangements, 3 air-cooled condensers, 3-1 air-cooled condenser blower fan, 4 wind-cooled evaporators, 4-1 wind-cooled evaporator blower fan, 5 oil eliminators, 6 reservoirs, 7 devices for drying and filtering, 8 liquid-sighting glass, 9-1 capacity adjusting valve, 9-2 controller (Programmable Logic Controller), 9-3 temperature sensor, 9-4 humidity sensor, 10 liquid injection valves, 11 subcoolers, 12 pressure of inspiration(Pi) control valves, 13 septum valves, 14 differential control valves, 15 casings, 16 doors, 17 return air dividing plates, 18 materials vehicles, 19 hydrofuge exhaust fans, 20 new wind blower fans, 21 screen packs, 22 electric heaters.
Detailed description of the invention
The present invention is further described below with reference to embodiment (accompanying drawing):
Embodiment 1
As shown in Figure 1, the present embodiment comprises high temperature heat pump subsystem, Temperature and Humidity Control regulates subsystem, baking room subsystem, wherein said high temperature heat pump subsystem is made up of compressor 1, throttling arrangement 2, air-cooled condenser 3, wind-cooled evaporator 4, oil eliminator 5, reservoir 6, device for drying and filtering 7, liquid-sighting glass 8, capacity adjusting valve 9-1, liquid injection valve 10, subcooler 11, pressure of inspiration(Pi) control valve 12, septum valve 13, differential control valve 14 and connecting pipe, its concrete annexation is that the exhaust outlet of compressor 1 is divided into two interfaces, one of them interface is connected with pressure of inspiration(Pi) control valve 12 import by capacity adjusting valve 9-1, another interface is connected with the import of differential control valve 14 with air-cooled condenser 3 import respectively by oil eliminator 5, and air-cooled condenser 3 is exported to be exported with differential control valve 14 respectively by septum valve 13 and is connected with the import of reservoir 6, then the outlet of reservoir 6 is successively by device for drying and filtering 7, liquid-sighting glass 8 and subcooler 11 are connected with liquid injection valve 10 import with throttling arrangement 2 import respectively, wherein throttling arrangement 2 is exported and is connected with pressure of inspiration(Pi) control valve 12 import by wind-cooled evaporator 4, liquid injection valve 10 is exported and is also connected with pressure of inspiration(Pi) control valve 12 import by subcooler 11, described pressure of inspiration(Pi) control valve 12 outlet is connected with compressor air suction mouth, described Temperature and Humidity Control regulates subsystem by capacity adjusting valve 9-1, air-cooled condenser blower fan 3-1, wind-cooled evaporator blower fan 4-1, hydrofuge/exhaust fan 19, new wind blower fan 20, electric heater 22, the preferred Programmable Logic Controller of controller 9-2(), temperature sensor 9-3, humidity sensor 9-4 and connect wire and form, in the storeroom that wherein said temperature sensor 9-3, humidity sensor 9-4 are installed on casing 15 respectively and return air inlet place, be connected with the input of controller 9-2 respectively by connecting wire, the output of described controller 9-2 is connected with the motor of capacity adjusting valve 9-1, the motor of air-cooled condenser blower fan 3-1, the motor of wind-cooled evaporator blower fan 4-1, the motor of hydrofuge exhaust fan 19, the motor of new wind blower fan 20, electric heater 22 respectively by connecting wire, described baking room subsystem is made up of casing 15, door 16, return air dividing plate 17, materials vehicle 18, hydrofuge exhaust fan 19, new wind blower fan 20, screen pack 21, air-cooled condenser 3 and electric heater 22, wherein said door 16 is arranged on the right-hand member of casing 15, hydrofuge exhaust fan 19, new wind blower fan 20 are installed on the both sides up and down of the left end of casing 15 respectively, wherein screen pack 21 is arranged on the front portion of new wind blower fan 20, described air-cooled condenser 3, electric heater 22 are installed on the air inlet of storeroom front end successively, described materials vehicle 18 deposits in storeroom air inlet, described return air dividing plate 17 is installed on storeroom upper end, for the return airway between component material.
Embodiment 2
As shown in Figure 2, this embodiment its difference compared with embodiment 1 is: described subcooler 11 is no longer connected with pressure of inspiration(Pi) control valve 12 import, but is connected with pressing tonifying Qi chamber in compressor.
Compressor 1 of the present invention is any one form in invariable frequency compressor, point gear compressor, frequency-changeable compressor, tonifying Qi increasing enthalpy compressor; Described air-cooled condenser 3, wind-cooled evaporator 4 are any one version in fin-tube type, stacked, parallel flow heat exchanger; Described air-cooled condenser blower fan 3-1, wind-cooled evaporator blower fan 4-1, hydrofuge exhaust fan 19, new wind blower fan 20 are any one form in frequency conversion fan, fixed blower fan, gear shift blower fan frequently; Described throttling arrangement 2 is any one version in heating power expansion valve, capillary expansion valve or electric expansion valve; Described liquid injection valve 10 is any one version in pressure type liquid injection valve, temp. type liquid injection valve; Described capacity adjusting valve 9-1 is any one form in thermal type capacity adjusting valve, electromagnetic energy control valve, electrodynamic type capacity adjusting valve; Described pressure of inspiration(Pi) control valve 12 is a kind of proportionality control valve controlled by downstream pressure (i.e. suction pressure of compressor); Described septum valve 13 is a kind of proportionality control valve controlled by upstream pressure (i.e. condensing pressure); Described electric heater 22 is any one form in PTC electric heater, stainless steel heater, fluid explosion-proof electric heater, electric infrared heater; Described subcooler 11 is any one version in plate type heat exchanger, double-tube heat exchanger, flash evaporation; Described air-cooled condenser 3, wind-cooled evaporator 4 are any one version in fin-tube type, stacked, parallel flow heat exchanger.
Combined by the Optimized Matching of above-mentioned three subsystems, controller PLC Intelligent adjustment, workflow of the present invention is as follows:
(1) basic energy level mode of operation
When drying materials technique just starts, when high-temperature heat pump drying system does not need energy, temperature and humidity regulation, this mode of operation can be adopted.The flow process of Temperature and Humidity Control adjustment subsystem is: the information that controller 9-2 inputs according to temperature sensor 9-3 and humidity sensor 9-4, open air-cooled condenser blower fan 3-1, wind-cooled evaporator blower fan 4-1, and be adjusted to maximum wind velocity, close capacity adjusting valve 9-1, hydrofuge exhaust fan 19, new wind blower fan 20 and electric heater 22.The flow process of high temperature heat pump subsystem is: pressure of inspiration(Pi) control valve 12 and septum valve 13 standard-sized sheet, liquid injection valve 10 and differential control valve 14 are closed, the refrigerant vapour of the HTHP that compressor is discharged becomes the cold or saturated liquid refrigerant of the mistake of high pressure by air-cooled condenser 3 release heat that oil eliminator 5 enters in casing 15, then successively through septum valve 13, reservoir 6, device for drying and filtering 7, liquid-sighting glass 8, subcooler 11 enters throttling arrangement 2, cross the gas-liquid two-phase cold-producing medium that cold liquid refrigerant becomes low-temp low-pressure after the flow restriction control of throttling arrangement 2, enter the superheated refrigerant steam becoming low pressure after wind-cooled evaporator 4 absorbs heat, then enter compressor 1 by pressure of inspiration(Pi) control valve 12 and carry out next cyclic process.Baking room subsystem flow process is: the air in casing 15 absorbs after heat intensification through air-cooled condenser 3, storeroom is entered through electric heater 22, after material on the air heat materials vehicle 18 of high temperature, releases heat is lowered the temperature, the simultaneously stability moisture of material, humidity increases, and the return airway then on the upside of return air dividing plate 17 enters air-cooled condenser 3, enters next circulation.
(2) energy level mode of operation is regulated
A, air-breathing throttling energy adjustment
When summer, outdoor temperature was higher, compressor 1 pressure of inspiration(Pi) is too high, motor load can be caused excessive, now pressure of inspiration(Pi) control valve 12 controls the pressure of inspiration(Pi) of compressor 1 according to downstream pressure (i.e. suction pressure of compressor), when pressure of inspiration(Pi) raises, pressure of inspiration(Pi) control valve 12 turns down, and the refrigerant superheat steam throttling that wind-cooled evaporator 4 is exported, enters compressor with lower pressure of inspiration(Pi).Other workflows are identical with basic energy level mode of operation.
B, Liquid injection cooling energy adjustment
When winter outdoor temperature lower, evaporating pressure and evaporating temperature lower time, or in drying materials technical process, condensing pressure and condensation temperature too high time, or when causing the degree of superheat excessive in energy adjustment process, compressor 1 excessive discharge temperature may be caused, liquid injection valve 10 can according to the delivery temperature of compressor 1, regulate the spouting liquid before entering pressure of inspiration(Pi) control valve 12, reduce the suction superheat of compressor, prevent compressor 1 excessive discharge temperature, simultaneously, in order to prevent the liquid refrigerant shwoot before throttling arrangement 2, through the gas-liquid two-phase cold-producing medium of liquid injection valve 10 throttling, first by subcooler 11, before entering pressure of inspiration(Pi) control valve 12 again after absorbing the heat of a part of liquid refrigerant, this ensure that the degree of supercooling of cold-producing medium before throttling arrangement 2, improve refrigerating effect per unit swept volume and the compressor efficiency of evaporimeter.Other workflows are identical with basic energy level mode of operation.
C, hot-gas bypass energy adjustment
When in drying materials technical process, when the temperature rise of storeroom is too fast, the information that controller 9-2 inputs according to temperature sensor 9-3, open capacity adjusting valve 9-1, the refrigerant vapour part bypass of the HTHP that compressor 1 is discharged is through capacity adjusting valve 9-1, enter compressor air suction mouth after reducing pressure by regulating flow, reduce the thermal discharge of air-cooled condenser 3, run under preventing the lower pressure of inspiration(Pi) of compressor 1.Other workflows are identical with basic energy level mode of operation.
D, condenser reflux method energy adjustment
When winter outdoor temperature very low, when high temperature heat pump system just starts, when condensing pressure is too low, before and after throttling arrangement 2, pressure reduction is too little, feed flow is short of power, cannot provide enough liquid supply rates to wind-cooled evaporator 4, by regulating air-cooled condenser blower fan 3-1, wind-cooled evaporator blower fan 4-1 is not when still having an effect, can adopt this control method.After start, septum valve 13 is closed, and differential pressure control valve 14 is opened, and compressor 1 is vented a part and is bypassed to reservoir 6, and pressure in reservoir 6 is raised.When condensing pressure be elevated to septum valve 13 unlatching value above time, septum valve 13 is slightly opened, along with the rising of storeroom temperature, when maintaining normal condensing pressure balance, the aperture of septum valve 13 increases to standard-sized sheet, the aperture of differential pressure control valve 14 diminishes to complete shut-down, and heat pump refrigerant walks normal circulation path.Other workflows are identical with basic energy level mode of operation.
E, heat extraction energy adjustment
When system adopts hot-gas bypass+Liquid injection cooling energy adjustment, when the temperature rise of storeroom is still too fast, the information that controller 9-2 inputs according to temperature sensor 9-3, open hydrofuge/exhaust fan 19, new wind blower fan 20, by the discharge with a part of high temperature return air that enters of the new wind of a part of low temperature, ensure the temperature rise rate of storeroom.Other workflows are identical with basic energy level mode of operation.
F, hydrofuge mode of operation
When in drying materials technical process, when storeroom humidity is excessive, the information that controller 9-2 inputs according to humidity sensor 9-4, opens hydrofuge exhaust fan 19, new wind blower fan 20, by the discharge with a part of high temperature return air that enters of the new wind of a part of low temperature, ensure the humidity of storeroom.Other workflows are identical with basic energy level mode of operation.
G, auxiliary electrical heater energy adjustment
When in drying materials technical process, the temperature rise rate of storeroom is excessively slow, when the energy adjustment of high temperature heat pump unit itself can't meet the demands, the information that controller 9-2 inputs according to temperature sensor 9-3, open electrical auxiliary heater 22, post bake is carried out to the air through air-cooled condenser 3, for meeting the requirement of the temperature rise rate of storeroom.Other workflows are identical with basic energy level mode of operation.
Claims (10)
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