CN104534849A - High-temperature heat pump drying machine started with heating and operating in high heating load state - Google Patents
High-temperature heat pump drying machine started with heating and operating in high heating load state Download PDFInfo
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- CN104534849A CN104534849A CN201410416753.0A CN201410416753A CN104534849A CN 104534849 A CN104534849 A CN 104534849A CN 201410416753 A CN201410416753 A CN 201410416753A CN 104534849 A CN104534849 A CN 104534849A
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Abstract
The invention provides a high-temperature heat pump drying machine started with heating and operating in a high heating load state. The machine comprises a heat pump drying system, a wind inlet passage, a wind outlet passage, and a drying chamber for connecting the wind inlet passage with the wind outlet passage; the heat pump drying system comprises a condenser arranged in the wind inlet passage, and an evaporator arranged in the wind outlet passage; a heater is arranged between the condenser and the drying chamber; air enters from a wind inlet of the wind inlet passage, and becomes high-temperature dried air after passing through the condenser and the heater in sequence, and then the high-temperature dried air is conveyed into the drying chamber and is used for drying operation and turned into humid air; the humid air is discharged and is guided onto the evaporator, and after moisture in the humid air is condensed, the air is discharged through the wind outlet passage. The heater is additionally arranged for increasing the drying operation starting speed of the drying system and the temperature of the dried air and improving the heat and mass transfer intensity of the drying operation, so that the heat absorption intensity of the evaporator is improved; moreover, the heat absorption intensity of the evaporator is improved, so that the heat release intensity of the condenser is improved, and the heat pump drying system can enter a high heating load operation state.
Description
Technical field
The present invention relates to drying device design field, particularly relate to a kind of heating starting and the high temperature heat pump drying machine of load operation of reheating.
Background technology
Heat pump, as a kind of handbarrow of heat, improve tow taste heat quality in soil, air, water to obtain the equipment compared with high-grade heat, under the background of energy-saving and emission-reduction as a kind of, in fields such as heating, hot water, dryings, obtain and apply more and more widely.The essence of heat pump energy-conserving, injects a small amount of electric energy exactly to drive compressor, is operated by the suction and discharge of compressor, will absorb the low pressure refrigerant gas of a large amount of tow taste heat in evaporimeter, is compressed into gases at high pressure and enters condenser and realize high-temperature position heat release.
The ratio of the electrical power usually the heat pump condenser heat release power determined under operating mode and compressor sucked, is called the Energy Efficiency Ratio of heat pump.This Energy Efficiency Ratio, generally near 4, namely the electrical power input of 1kw can by the tow taste heat in soil, air, water, and the high-temperature position be transported to required for people is gone, and carries out operations such as heating, dry, and obtains the heating power of about 4kw in high-temperature position.
The characteristics of energy saving of heat pump, makes it, in heating, hot water, drying etc. field, to obtain a wide range of applications.But when heat pump is used for the purposes such as dry materials, also there is obvious problem, specific as follows:
1. the time needed for Analysis of Heat Pump Drying System start-up course is partially long
Because Analysis of Heat Pump Drying System is a vapor compression refrigeration device be made up of evaporimeter, compressor, condenser, choke valve and control unit, during operation, cold-producing medium is at the closing pipe line Inner eycle be made up of evaporimeter, compressor, condenser, choke valve and constantly undergo phase transition to carry out evaporation endothermic and condensation heat release, and condensing pressure is sufficiently high, refrigerant gas can condensation heat release within the condenser, evaporating pressure is sufficiently low, refrigerant liquid can in evaporimeter evaporation endothermic.
So after Analysis of Heat Pump Drying System startup, under the promotion of compressor, condenser inner refrigerant gas pressure progressively raise until the refrigerant gas condensation temperature corresponding to condensing pressure higher than condenser place surrounding air temperature thus can to the effective heat release of surrounding air; The pressure of evaporimeter inner refrigerant gas progressively reduce until the refrigerant liquid evaporating temperature corresponding to evaporating pressure lower than evaporimeter place surrounding medium temperature thus effectively can absorb heat from surrounding medium; At this moment, Analysis of Heat Pump Drying System just starts to enter drying regime; And stable dry operating mode will be reached, also will first to be dried be heated containing wet stock, this also needs the regular hour.Time needed for Analysis of Heat Pump Drying System start-up course is partially long.
2. heat pump condenser leaving air temp is on the low side, and hot humidity load is on the low side, and drying capacity is on the weak side
The functions/drying of Analysis of Heat Pump Drying System adds hot-air by condenser heat rejection, improves the temperature of air, reduces the relative humidity of air, namely improve the wettability power of air, realize.
With reference to Fig. 1, for the saturated water capacity of different temperatures air and the wettability power table of different temperatures nonsaturated air, wherein saturation of the air humidity and saturated water capacity, the drying capacity of air and wettability power, with the temperature direct correlation of air: temperature is higher, and saturated humidity and saturated water capacity, drying capacity and the wettability power of air are also higher.From in Fig. 1,6.3 times that 80 DEG C, the maximum moisture absorption ability of the unsaturated air of 30% reaches 381.5 g water vapour/kg dry air is 50 DEG C, the maximum moisture absorption ability of the unsaturated air of 30% reaches 60.34 g water vapour/kg dry air.
Present industry and civilian heat pump drier, condenser leaving air temp is on the low side, generally only has about 50 DEG C, and hot humidity load is obviously on the low side, and drying capacity is obviously on the weak side.And heat pump condenser leaving air temp is on the low side, heat load intensity is not enough, and basic reason is that the evaporating temperature of evaporimeter, evaporating pressure are on the low side, because in heat pump condenser liberated heat, derive from the work done during compression of compressor on a small quantity, main body still comes from the heat that evaporimeter absorbs from low-temperature heat source.
With reference to Fig. 2-4, if the evaporating pressure of evaporator with heat pump, evaporating temperature reduce, then will there is comprehensive decline in the evaporation convection composite heat-exchange coefficient inside the refrigerant flow of Analysis of Heat Pump Drying System, evaporator pipeline, evaporimeter caloric receptivity; Conversely, if the evaporating pressure of evaporator with heat pump, evaporating temperature raise, to there is comprehensive rising in the evaporation convection composite heat-exchange coefficient then inside the refrigerant flow of Analysis of Heat Pump Drying System, evaporator pipeline, evaporimeter caloric receptivity, the condensation convection current composite heat-exchange coefficient inside condenser pipe, condenser heat rejection amount, condensation temperature, condensing pressure also will raise thereupon comprehensively.
Summary of the invention
In order to solve the problem, the invention provides a kind of heating starting and the high temperature heat pump drying machine of load operation of reheating, comprise air intake passage, air-out passage, hothouse and Analysis of Heat Pump Drying System, described air intake passage is all connected with described hothouse with described air-out passage;
Described Analysis of Heat Pump Drying System includes condenser and evaporimeter, and described condenser is arranged in described air intake passage, and described evaporimeter is arranged in described air-out passage, is provided with heater between described condenser and hothouse;
Air enters from the air inlet of described air intake passage, becomes high temperature dry air successively and be transported in described hothouse after described condenser and heater, carries out hot and humid area become humid air with needing dried object; Humid air is expelled on described evaporimeter, separates out after moisture discharge described air-out passage through described evaporator condensation.
Preferably, blower fan is provided with in the air inlet of described air intake passage.
Preferably, the air inlet of described air intake passage is provided with the first filter screen.
Preferably, the second filter screen is provided with between the air outlet of described hothouse and described evaporimeter.
Preferably, described Analysis of Heat Pump Drying System comprises compressor, and described evaporimeter is connected with the pipeline in described condenser and forms with described compressor the circulation canal that supplies flow of refrigerant warp; Described cold-producing medium flows through the pipeline in described condenser and described evaporimeter successively from described compressor starts.
Preferably, throttling arrangement is provided with before the entrance of the refrigerant tubing of described evaporimeter.
Preferably, the bottom of described evaporimeter is provided with a water leg, and described water leg is connected with a return water tank or sewer by a water pipe.
Preferably, be provided with a rotation hopper in described hothouse, described rotation hopper is tubbiness, and the sidewall of described rotation hopper is provided with some through holes.
The present invention, owing to adopting above technical scheme, makes it compared with prior art, has following advantage and good effect:
A kind of heating starting provided by the invention and the high temperature heat pump drying machine of load operation of reheating, heater is installed additional at condenser air outlet, improve temperature and the drying capacity of dry air, accelerate the dried pre-heating temperature elevation containing wet stock and moisture evaporation, significantly improve the evaporating temperature of evaporimeter, evaporating pressure and thermic load, thus significantly improve the condensation temperature of condenser, condensing pressure and heating strength, the heat load intensity defining evaporimeter and condenser promotes mutually, " positive feedback " situation competitively improved, " heating power+compressor compresses merit of heater " and " enthalpy difference+Analysis of Heat Pump Drying System of evaporimeter air-out and condenser air intake leaks heat " is made to reach balance, Analysis of Heat Pump Drying System is Effec-tive Function under " load of reheating " state, solve " time needed for Analysis of Heat Pump Drying System start-up course is partially long " particularly " present industry and civilian heat pump drier at all, condenser leaving air temp is on the low side, hot humidity load is obviously on the low side, drying capacity is obviously on the weak side " problem.
Accompanying drawing explanation
By reference to the accompanying drawings, by hereafter state detailed description, more clearly can understand above-mentioned and other feature and advantage of the present invention, wherein:
Fig. 1 is the saturated water capacity of different temperatures air and the wettability power table of different temperatures nonsaturated air;
Fig. 2 be in heat pump refrigerant mass fluxes with the variation diagram of evaporating temperature;
Fig. 3 be in heat pump evaporimeter refrigerant pipe tube internal heat exchange coefficient with the variation diagram of evaporating temperature;
Fig. 4 is the variation diagram of heat pump evaporimeter caloric receptivity with evaporating temperature;
Fig. 5 is heating starting of the present invention and the structural representation of the high temperature heat pump drying machine of load operation of reheating;
Fig. 6 is the structural representation rotating hopper;
Fig. 7 be on psychrometric chart heating starting reheat load heat pump drying air open-circuit circulating path figure (heating starting constant rate drying period air open-circuit circulating path figure 1. → 2. → 3. → 4. → 5.);
Fig. 8 is that on pressure-enthalpy chart, heating starting load heat pump drying of reheating heats circular chart.
Symbol description:
1-air intake passage
101-air inlet
2-air-out passage
201-air outlet
3-hothouse
4-first filter screen
5-blower fan
6-condenser
7-heater
8-second filter screen
9-evaporimeter
10-return water tank
11-rotates hopper
1101-through hole
12-compressor
13-throttling arrangement.
Detailed description of the invention
See the accompanying drawing that the embodiment of the present invention is shown, hereafter in more detail the present invention will be described.But the present invention can realize in many different forms, and should not be construed as by the restriction in the embodiment of this proposition.On the contrary, it is abundant and complete open in order to reach for proposing these embodiments, and makes those skilled in the art understand scope of the present invention completely.In these accompanying drawings, for clarity sake, may be exaggerated size and the relative size in layer and region.
The invention provides a kind of heating starting and the high temperature heat pump drying machine of load operation of reheating, the mode of production can be batch (-type), and namely dry object quilt " cage one cage " putting into high temperature dry air carries out desiccant dehumidification; Drying medium is that air or nitrogen etc. have the gaseous material of very high wettability power in the condition of high temperature, is not all restricted herein.
Concrete, with reference to Fig. 5-6, this heating starting and the high temperature heat pump drying machine of load operation of reheating comprises air intake passage 1, air-out ventilating duct 2, hothouse 3 and Analysis of Heat Pump Drying System.Wherein, need dried damp item to be positioned in hothouse 3, one end of hothouse 3 air intake passage 1 is the air inlet 101 be connected with the external world, and the other end is connected with hothouse 3; One end of air-out passage 2 is the air outlet 201 communicated with the external world, and the other end is connected with hothouse 3.Be provided with blower fan 5 in air intake passage 1, blower fan 5 is arranged near air inlet 101 place, and blower fan 5 can adopt centrifugal blower, is not restricted herein; Under the effect of blower fan 5, outside air enters into air intake passage 1 from air inlet 101, enters air-out passage 2 after hothouse 3, finally discharges drying machine from the air outlet 201 of air-out passage 2.
In the present embodiment, Analysis of Heat Pump Drying System comprises condenser 6, evaporimeter 9 and compressor 12, wherein evaporimeter 9 and condenser 6 include pipeline and are arranged on the fin outside pipeline, condenser 6, between evaporimeter 9 and compressor 12, form one for the circulation canal of flow of refrigerant warp by pipeline sequential communication, and be filled with cold-producing medium in this circulation canal; This circulation canal is still provided with throttling arrangement 13, throttling arrangement 13 is positioned on the entrance point of the pipeline of evaporimeter 9, for reducing the pressure of the cold-producing medium flow in evaporimeter 9, throttling arrangement 13 can adopt choke valve, capillary, electric expansion valve etc., is not restricted herein.Start cold-producing medium from compressor 12 and flow through condenser 6 → throttling arrangement 13 → evaporimeter 9 successively, finally get back to again in compressor 12.
Wherein, the periodic duty principle of cold-producing medium is specific as follows:
High temperature refrigerant gas after compressor 12 out pressurized, flows through the pipeline of condenser 6, realizes heat release cooling, transfers heat to the air flowing through condenser 6, and the refrigerant liquid that high temperature refrigerant condensation of gas is liquefied as low temperature simultaneously exports; The refrigerant liquid of low temperature, after throttling arrangement 13 reduces pressure, is imported in the pipeline of evaporimeter 9, and absorb after flowing through the heat of the air of evaporimeter 9, evaporation becomes low pressure refrigerant gas; Compressor 12 flows to condenser 6 after pressurizeing to the low pressure refrigerant gas of being come by evaporimeter 9 again, thus forms a complete refrigerant circulation.
In the present embodiment, condenser 6 to be arranged in air intake passage and between blower fan 5 and the import of hothouse 3; Evaporimeter 9 is arranged in air-out passage 2, and the bottom of evaporimeter 9 is provided with a water leg, and water leg is connected with a return water tank 10 or sewer by a water pipe.In the present embodiment, be also provided with heater 7 in air intake passage 1, heater 7 is between condenser 6 and the import of hothouse 3, and wherein heater 7 can be electrical heating or Steam Heating, also can be fuel gas buring heating, not be restricted herein.Air, after condenser 6 heats, heats through heater 7 again again; The present invention after condenser 6 air outlet, install a heater 7 before drying operation additional, to improve the drying operation toggle speed of Analysis of Heat Pump Drying System and the temperature of dry air, improve the heat and mass intensity of drying operation; By improving the heat and mass intensity of drying operation, improve evaporimeter 9 heat absorption intensity; Again by the raising of evaporimeter 9 heat absorption intensity, improve condenser 6 heating strength, thus make Analysis of Heat Pump Drying System enter load operating region of reheating.
In the present embodiment, the air inlet of air intake passage 1 is provided with the first filter screen, prevents extraneous dust, impurity etc. from entering in drying machine with air; Be provided with the second filter screen 8 between the air outlet of hothouse 3 and evaporimeter 9, for preventing the chip of the partial material in hothouse 3 with air flow evaporimeter 9, thus affect evaporimeter 9 and normally run.
In the present embodiment, in hothouse 3, be provided with a rotation hopper 11, rotate hopper 11 in barrel-like structure, one circle sidewall is provided with several through holes 1101; Rotate hopper 11 to be connected with power set, power set provide power to make it around central axis for rotating hopper 11.Being placed in needing dried material rotates in hopper 11, through the high temperature dry air that condenser 6 and heater 7 obtain, the moist material of rotating hopper 11 inside is flowed through by some through holes 1101, carry out hot and humid area with moist material and complete drying operation, rotate hopper 11 ceaselessly to rotate, the effect ceaselessly changing dry materials face can be reached, thus accelerate drying efficiency effectively.
This law invents a kind of heating starting and the high temperature heat pump drying machine of load operation of reheating that provide, and the dry air used adopts open circuit circulation mode, and its dry run is:
Air in dryer outer environment is sucked by blower fan 5, flows through the dry air that condenser 6 is heated to form high-temperature, low humidity, flows through heater 7 and is further heated; Flow through from the dry air of heater 7 outflow and carry out drying operation containing wet stock, now dry air does " constant enthalpy " change, the enthalpy (energy density) of air is constant, but drying air temperature declines to a great extent, relative humidity and absolute moisture content increase fast, the sensible heat of dry air is transformed to the latent heat of water vapour, and the humidity load of air increases fast; After completing drying operation containing wet stock, the damp-heat air carrying a large amount of humidity load (water vapour) flows to evaporimeter 9, heat release cooling in evaporimeter 9, when damp-heat air temperature drops to below corresponding dew-point temperature, the exothermic condensation on evaporimeter 9 of the water vapour in air is separated out; Separated out the saturated air of most of water vapor through evaporator 9, temperature and absolute moisture content all greatly reduce, and enthalpy greatly reduces, and finally discharge machine from the air outlet 201 of air-out passage 2.
A kind of heating starting provided by the invention and the high temperature heat pump drying machine of load operation of reheating, by after condenser air outlet, install heater additional before drying operation, to improve the drying operation toggle speed of Analysis of Heat Pump Drying System and the temperature of dry air, wherein heater is specific as follows in the ruuning situation in each stage of dry run:
One, when Analysis of Heat Pump Drying System starts and the commitment of desiccant dehumidification, heater is devoted oneself to work:
1. heater 7 is devoted oneself to work, and its liberated heat superposes with the thermal discharge of condenser 6, improves the temperature of dry air, heating efficiency and dry wettability power significantly, rapidly;
2. improve the dry air of temperature, heating efficiency and dry wettability power significantly, rapidly, pass through dry object (such as wet clothes), accelerate the programming rate of dry object and evaporation to dry speed, exchange heat is carried out between dry air and dry object, humid air psychrometric chart shows as constant enthalpy humidification process, the temperature of dry air reduces humidity to be increased, but the enthalpy of air (i.e. the energy density of air) is constant, with reference to shown in Fig. 7;
3. the air lowered the temperature, be humidified, its enthalpy does not change; This Hot wet air heating flows to evaporimeter, compared with ambient air, significantly improve the temperature and humidity of evaporimeter 9 air intake, namely significantly add the thermic load of evaporimeter 9, comprise air and to lower the temperature the latent heat load that the sensible heat load that discharges and water vapor in air discharge through evaporator 9 condensation through evaporator 9.The superposition of this sensible heat and latent heat, significantly adds the thermic load of evaporator air side; This evaporator air side thermic load significantly increased, significantly improves again the evaporation convection composite heat-exchange coefficient inside the evaporating temperature of cold-producing medium in evaporator pipeline, evaporating pressure, evaporator pipeline, evaporimeter caloric receptivity;
4. the significantly increase of the thermic load of evaporimeter 9, significantly improve the evaporation convection composite heat-exchange coefficient inside the evaporating temperature of cold-producing medium in evaporimeter 9 pipeline, evaporating pressure, evaporimeter 9 pipeline, evaporimeter caloric receptivity, and this fundamentally improves the density of the refrigerant gas that compressor 12 sucks, significantly improve the mass flow of Analysis of Heat Pump Drying System inner refrigerant, from and the condensation convection current composite heat-exchange coefficient that improves further inside the condensing pressure of condenser 9, condensation temperature, condenser pipe and refrigerant gas condensation heating strength.
So, when Analysis of Heat Pump Drying System starts and the commitment of drying operation, coming into operation of heater 7, enhance dry run, add evaporimeter thermic load, and then add the thermic load of condenser, define " positive feedback " situation that evaporimeter 9 promotes mutually with the heat load intensity of condenser 6, competitively improves, until " heating power+compressor compresses power of heater " and " enthalpy difference+Analysis of Heat Pump Drying System of evaporimeter air-out and condenser air intake leaks heat " progressively reaches balance, Analysis of Heat Pump Drying System is Effec-tive Function under " load of reheating " state.
Two, in stage middle and later periods of Analysis of Heat Pump Drying System desiccant dehumidification, heater works on:
1. heater is devoted oneself to work, and its liberated heat superposes with the thermal discharge of heat pump condenser, improves the temperature of dry air, heating efficiency and dry wettability power significantly, rapidly;
2. in stage middle and later periods of Analysis of Heat Pump Drying System desiccant dehumidification, because the free moisture on dry object (such as wet clothes) surface evaporates, enter falling rate drying period, exchange heat is proceeded between high temperature dry air after condenser 6 and heater 7 and dry object, humid air psychrometric chart still shows as constant enthalpy humidification process, its enthalpy does not change, but the decline of its temperature is less, water capacity increases less, with reference to shown in Fig. 8; This high temperature air flows to evaporimeter 9, compared with ambient air, significantly improves the temperature of evaporimeter 9 air intake, namely significantly adds the thermic load of evaporimeter 9.This evaporimeter 9 air side thermic load significantly increased, significantly improves again the evaporation convection composite heat-exchange coefficient inside the evaporating temperature of cold-producing medium in evaporimeter 9 pipeline, evaporating pressure, evaporator pipeline, evaporimeter caloric receptivity;
3. the significantly increase of the thermic load of evaporimeter 9, significantly improve the evaporation convection composite heat-exchange coefficient inside the evaporating temperature of cold-producing medium in evaporimeter 9 pipeline, evaporating pressure, evaporimeter 9 pipeline, evaporimeter caloric receptivity, and this fundamentally improves the density of the refrigerant gas that compressor sucks, significantly improve the mass flow of Analysis of Heat Pump Drying System inner refrigerant, thus the condensation convection current composite heat-exchange coefficient continuing to improve further inside the condensing pressure of condenser, condensation temperature, condenser pipe and refrigerant gas condensation heating strength.
So, at the later stage that Analysis of Heat Pump Drying System runs, the use of heater, still dry run is enhanced, add evaporimeter thermic load, and then add the thermic load of condenser, " positive feedback " situation that the heat load intensity defining evaporimeter and condenser promotes mutually, competitively improve, make " heating power+compressor compresses merit of heater " and " enthalpy difference+Analysis of Heat Pump Drying System of evaporimeter air-out and condenser air intake leaks heat ", reach balance, Analysis of Heat Pump Drying System continues Effec-tive Function under " load of reheating " state.
In sum, the invention provides a kind of heating starting and the high temperature heat pump drying machine of load operation of reheating, comprise the hothouse of Analysis of Heat Pump Drying System, air intake passage, air-out passage, connection air intake passage and air-out passage; Analysis of Heat Pump Drying System comprises the condenser be arranged in air intake passage and the evaporimeter be arranged in air-out passage, is also provided with heater between condenser and hothouse; Air enters from the air inlet of air intake passage, obtains high temperature dry air successively and is transported in hothouse, carry out drying operation and become humid air after condenser and heater; Humid air is expelled to after condensation on evaporimeter goes out moisture and discharges air-out passage.The present invention adds a heater, for the temperature of the drying operation toggle speed and dry air that improve drying system, improves the heat and mass intensity of drying operation, thus improves evaporimeter heat absorption intensity; Again by the raising of evaporimeter heat absorption intensity, improve condenser heat rejection intensity, thus make Analysis of Heat Pump Drying System enter load operating region of reheating.
Those skilled in the art should be understood that the present invention can realize with other concrete forms many and not depart from the spirit or scope of the present invention.Although describe embodiments of the invention, the present invention should be understood and should not be restricted to these embodiments, within the spirit and scope of the invention that those skilled in the art can define as appended claims, make change and amendment.
Claims (8)
1. heating starting and a high temperature heat pump drying machine for load operation of reheating, it is characterized in that, comprise air intake passage, air-out passage, hothouse and Analysis of Heat Pump Drying System, described air intake passage is all connected with described hothouse with described air-out passage;
Described Analysis of Heat Pump Drying System includes condenser and evaporimeter, and described condenser is arranged in described air intake passage, and described evaporimeter is arranged in described air-out passage;
Heater is provided with between described condenser and hothouse;
Air enters from the air inlet of described air intake passage, becomes high temperature dry air successively and be transported in described hothouse after described condenser and heater, carries out hot and humid area become humid air with needing dried object; Humid air is expelled on described evaporimeter, separates out after moisture discharge described air-out passage through described evaporator condensation.
2., according to heating starting according to claim 1 and the high temperature heat pump drying machine of load operation of reheating, it is characterized in that, in the air inlet of described air intake passage, be provided with blower fan.
3., according to heating starting according to claim 2 and the high temperature heat pump drying machine of load operation of reheating, it is characterized in that, the air inlet of described air intake passage is provided with the first filter screen.
4., according to heating starting according to claim 1 and the high temperature heat pump drying machine of load operation of reheating, it is characterized in that, between the air outlet of described hothouse and described evaporimeter, be provided with the second filter screen.
5. according to heating starting according to claim 1 and the high temperature heat pump drying machine of load operation of reheating, it is characterized in that, described Analysis of Heat Pump Drying System comprises compressor, and described evaporimeter is connected with the pipeline in described condenser and forms with described compressor the circulation canal that supplies flow of refrigerant warp; Described cold-producing medium flows through the pipeline in described condenser and described evaporimeter successively from described compressor starts.
6., according to heating starting according to claim 5 and the high temperature heat pump drying machine of load operation of reheating, it is characterized in that, before the entrance of the refrigerant tubing of described evaporimeter, be provided with throttling arrangement.
7., according to heating starting according to claim 5 and the high temperature heat pump drying machine of load operation of reheating, it is characterized in that, the bottom of described evaporimeter is provided with a water leg, and described water leg is connected with a return water tank or sewer by a water pipe.
8., according to heating starting according to claim 1 and the high temperature heat pump drying machine of load operation of reheating, it is characterized in that, be provided with a rotation hopper in described hothouse, described rotation hopper is tubbiness, and the sidewall of described rotation hopper is provided with some through holes.
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107621129A (en) * | 2017-08-24 | 2018-01-23 | 上海伯涵热能科技有限公司 | A kind of drying unit of outer thermal starting and depth dehumidifying |
| CN108183573A (en) * | 2017-12-29 | 2018-06-19 | 南京钢铁股份有限公司 | Large-size machine anti-gray dampproof method |
| CN109708330A (en) * | 2018-11-30 | 2019-05-03 | 安徽欧瑞达电器科技有限公司 | A kind of cell liquid recycling unit |
| CN112857022A (en) * | 2021-03-29 | 2021-05-28 | 河北博志热能设备有限公司 | Heating assembly device for improving air outlet temperature of heat pump drying unit and control method thereof |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2009213531A (en) * | 2008-03-07 | 2009-09-24 | Panasonic Corp | Dehumidifying and heating device and drying apparatus using the same |
| JP2012057935A (en) * | 2008-11-28 | 2012-03-22 | Chubu Electric Power Co Inc | Coating drying device |
| CN202511591U (en) * | 2012-03-26 | 2012-10-31 | 东南大学 | Heat pump drying device |
| CN203464650U (en) * | 2013-09-03 | 2014-03-05 | 湖南城建职业技术学院 | Carbon dioxide heat pump dryer |
| CN103629912A (en) * | 2012-08-20 | 2014-03-12 | 王震 | Ground source heat pump drying device |
| CN203629253U (en) * | 2013-11-15 | 2014-06-04 | 西安博昱新能源有限公司 | High-temperature variable frequency heat pump heating-based drying system |
| CN204329542U (en) * | 2014-08-22 | 2015-05-13 | 上海伯涵热能科技有限公司 | A kind of heating starting and the high temperature heat pump drying machine of load operation of reheating |
-
2014
- 2014-08-22 CN CN201410416753.0A patent/CN104534849A/en active Pending
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2009213531A (en) * | 2008-03-07 | 2009-09-24 | Panasonic Corp | Dehumidifying and heating device and drying apparatus using the same |
| JP2012057935A (en) * | 2008-11-28 | 2012-03-22 | Chubu Electric Power Co Inc | Coating drying device |
| CN202511591U (en) * | 2012-03-26 | 2012-10-31 | 东南大学 | Heat pump drying device |
| CN103629912A (en) * | 2012-08-20 | 2014-03-12 | 王震 | Ground source heat pump drying device |
| CN203464650U (en) * | 2013-09-03 | 2014-03-05 | 湖南城建职业技术学院 | Carbon dioxide heat pump dryer |
| CN203629253U (en) * | 2013-11-15 | 2014-06-04 | 西安博昱新能源有限公司 | High-temperature variable frequency heat pump heating-based drying system |
| CN204329542U (en) * | 2014-08-22 | 2015-05-13 | 上海伯涵热能科技有限公司 | A kind of heating starting and the high temperature heat pump drying machine of load operation of reheating |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107621129A (en) * | 2017-08-24 | 2018-01-23 | 上海伯涵热能科技有限公司 | A kind of drying unit of outer thermal starting and depth dehumidifying |
| CN107621129B (en) * | 2017-08-24 | 2023-08-25 | 广州万二二麦工程技术有限公司 | Drying device with external hot start and deep dehumidification |
| CN108183573A (en) * | 2017-12-29 | 2018-06-19 | 南京钢铁股份有限公司 | Large-size machine anti-gray dampproof method |
| CN109708330A (en) * | 2018-11-30 | 2019-05-03 | 安徽欧瑞达电器科技有限公司 | A kind of cell liquid recycling unit |
| CN112857022A (en) * | 2021-03-29 | 2021-05-28 | 河北博志热能设备有限公司 | Heating assembly device for improving air outlet temperature of heat pump drying unit and control method thereof |
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Effective date of registration: 20160328 Address after: Hangzhou City, Zhejiang province 311612 large hangtou town in the city of Jiande Industrial Zone Applicant after: Zhejiang PRINTRONICS Eyre electrical appliance industry company Address before: 200237 Shanghai, Hongmei South Road, No. 777, the bottom floor, room 53, 2101 Applicant before: Shanghai Bohan Thermal Energy Technology Co., Ltd. |
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Application publication date: 20150422 |
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