CN102384606B - System for recovering total heat of waste damp and hot air and method - Google Patents
System for recovering total heat of waste damp and hot air and method Download PDFInfo
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- CN102384606B CN102384606B CN201110238148.5A CN201110238148A CN102384606B CN 102384606 B CN102384606 B CN 102384606B CN 201110238148 A CN201110238148 A CN 201110238148A CN 102384606 B CN102384606 B CN 102384606B
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- 238000000034 method Methods 0.000 title abstract description 17
- 239000002699 waste material Substances 0.000 title abstract 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 193
- 238000005406 washing Methods 0.000 claims abstract description 14
- 239000008399 tap water Substances 0.000 claims abstract description 5
- 235000020679 tap water Nutrition 0.000 claims abstract description 5
- 239000000498 cooling water Substances 0.000 claims description 15
- 230000009471 action Effects 0.000 claims description 8
- 238000004891 communication Methods 0.000 claims description 6
- 238000001514 detection method Methods 0.000 claims description 6
- 230000002452 interceptive effect Effects 0.000 claims description 3
- 238000012360 testing method Methods 0.000 claims description 3
- 230000000694 effects Effects 0.000 abstract description 12
- 238000001816 cooling Methods 0.000 abstract description 11
- 238000011084 recovery Methods 0.000 abstract description 5
- 238000004043 dyeing Methods 0.000 abstract description 4
- 238000007639 printing Methods 0.000 abstract description 4
- 239000008400 supply water Substances 0.000 description 15
- 238000013461 design Methods 0.000 description 10
- 239000004744 fabric Substances 0.000 description 4
- 238000009434 installation Methods 0.000 description 4
- 238000005070 sampling Methods 0.000 description 4
- 208000034423 Delivery Diseases 0.000 description 3
- 238000004378 air conditioning Methods 0.000 description 3
- 238000007791 dehumidification Methods 0.000 description 3
- 238000001035 drying Methods 0.000 description 3
- 238000000605 extraction Methods 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 238000005457 optimization Methods 0.000 description 3
- 239000010865 sewage Substances 0.000 description 3
- 238000012384 transportation and delivery Methods 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- 230000006835 compression Effects 0.000 description 2
- 238000007906 compression Methods 0.000 description 2
- 230000003111 delayed effect Effects 0.000 description 2
- 238000010304 firing Methods 0.000 description 2
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 2
- 230000003020 moisturizing effect Effects 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 239000003507 refrigerant Substances 0.000 description 2
- 229920006395 saturated elastomer Polymers 0.000 description 2
- 241001269238 Data Species 0.000 description 1
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000001294 propane Substances 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 230000005144 thermotropism Effects 0.000 description 1
- 230000001131 transforming effect Effects 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B30/00—Heat pumps
- F25B30/06—Heat pumps characterised by the source of low potential heat
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24H—FLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
- F24H4/00—Fluid heaters characterised by the use of heat pumps
- F24H4/02—Water heaters
- F24H4/04—Storage heaters
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24H—FLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
- F24H9/00—Details
- F24H9/20—Arrangement or mounting of control or safety devices
- F24H9/2007—Arrangement or mounting of control or safety devices for water heaters
- F24H9/2014—Arrangement or mounting of control or safety devices for water heaters using electrical energy supply
- F24H9/2021—Storage heaters
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D21/00—Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
- F28D21/0001—Recuperative heat exchangers
- F28D21/0014—Recuperative heat exchangers the heat being recuperated from waste air or from vapors
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24D—DOMESTIC- OR SPACE-HEATING SYSTEMS, e.g. CENTRAL HEATING SYSTEMS; DOMESTIC HOT-WATER SUPPLY SYSTEMS; ELEMENTS OR COMPONENTS THEREFOR
- F24D17/00—Domestic hot-water supply systems
- F24D17/02—Domestic hot-water supply systems using heat pumps
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24D—DOMESTIC- OR SPACE-HEATING SYSTEMS, e.g. CENTRAL HEATING SYSTEMS; DOMESTIC HOT-WATER SUPPLY SYSTEMS; ELEMENTS OR COMPONENTS THEREFOR
- F24D2200/00—Heat sources or energy sources
- F24D2200/16—Waste heat
- F24D2200/22—Ventilation air
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Heat-Pump Type And Storage Water Heaters (AREA)
- Drying Of Solid Materials (AREA)
Abstract
The invention discloses a system for recovering the total heat of waste damp and hot air and a method for recovering the total heat of the waste damp and hot air. The system for recovering the total heat of the waste damp and hot air is used for high-temperate and high-humidity work environment which is relatively sealed. The system comprises a heat recovery machine set and heat usage equipment, wherein the heat recovery machine set comprises an evaporator arranged in a work environment, a condenser connected with the evaporator by one pipeline, and a compressor connected with the evaporator and the condenser by the other pipelines; the heat usage equipment comprises a water box connected with the condenser by a circulating pipeline, and water transporting equipment connected in a water outlet pipeline of the water box; and a water inlet pipe and the water outlet pipe which can be connected with a tap water pipeline, are further arranged on the water box. The system and the method can be used for effectively collecting the waste damp and hot air discharged in the work environment such as a hotel washhouse, a printing and dyeing mill and the like as well as recovering the total heat of the waste damp and hot air to heat up the tap water, so that the hot water can be provided to a washing flow path to use, and the effects of energy saving, consumption reducing, and air cooling and dehumidifying of a working space can be achieved.
Description
Technical field
The present invention relates to the full heat recovery system of a kind of air and method, particularly a kind of useless muggy air total heat recovering system and method that can be used for the environment such as laundry, hotel, printing and dyeing mill.
Background technology
Locate in laundry, hotel, printing and dyeing mill etc., because requirements of one's work, often need to carry out by a large amount of vapours the oven dry of clothing, yarn fabric etc., and for the ease of ensureing yarn fabric health, usually will in the environment of a relative closure, carry out, it ventilates, the condition of heat radiation is all undesirable.The process of vapours drying clothes, yarn fabric, makes above-mentioned working environment easily produce the high temperature, the high humidity situation that are unfavorable for staff, need freeze to lower the temperature, dehumidify with air-conditioning unit.In addition, in these working environments, also need to come washing clothes, yarn fabric etc. with hot water in a large number, can cause separately again sizable energy consumption.
Therefore, wish to occur that one both can reclaim useless hot and humid gas, eliminate high temperature, the high humidity of working environment, can utilize again the system of used heat.
Summary of the invention
The present invention is in order to overcome above-mentioned defect of the prior art, and a kind of useless muggy air total heat recovering system and method are provided.This system can effectively be collected in the heat energy in the useless damp-heat air discharging in the working environments such as laundry, hotel, printing and dyeing mill, and it is retrieved running water to heat entirely, and then offer in washing flow and use, play effect energy-saving and cost-reducing and to workplace air cooling, dehumidifying.
For achieving the above object, the invention provides following technical scheme:
A kind of useless muggy air total heat recovering system, be applied to the hot and humid working environment of relative closure, comprise recuperation of heat unit and heat utilization equipment, described recuperation of heat unit comprises the evaporimeter being arranged in working environment, the condenser being connected by pipeline with described evaporimeter, and the compressor being connected by pipeline with condenser with described evaporimeter; Described heat utilization equipment comprises the water tank being connected by circulating line with described condenser, and is connected to the water conveying equipment in the outlet pipeline of described water tank; Wherein, on described water tank, be also provided with water inlet pipe and the outlet pipe that can connect tap water pipe line.
Further, in described recuperation of heat unit, also comprise and be arranged near the circulating fan of described evaporimeter, and the air supply duct being connected with the air outlet of this circulating fan.This evaporimeter carries out heat exchange for the useless damp-heat air that makes environment with the cold-producing medium in this evaporimeter, therefore, need to determine its installation site according to the physical condition in place.Described circulating fan be for make through with evaporimeter heat exchange after air be transported in air supply duct, therefore, the installation of this circulating fan need to be determined a near correct position described evaporimeter according to physical conditions such as the mounting condition on place, air-flow trend, the specification of blower fan and the positions of air supply duct.
Further, described heat utilization equipment also comprises the washing machine that uses equipment as heat, and washing machine itself has water and heats and keep water temperature function, this heat to use the downstream of equipment connection at described water conveying equipment.
Further, in the circulating line between described water tank and described condenser, be provided with heat of cooling water pump.
Further, described water conveying equipment comprises the constant voltage water pump in the outlet pipeline that is connected to described water tank, detect the pressure sensor of pressure in the outlet pipeline of described water tank, detect the temperature sensor of water temperature in the outlet pipeline of described water tank, and control the frequency converter of described constant voltage water pump action.
Further, described useless muggy air total heat recovering system also comprises multiple Temperature Humidity Sensors of temperature and humidity in testing environment, and the control module being connected with described multiple Temperature Humidity Sensor communications; And, described control module is also connected with described pressure sensor and described temperature sensor communication, all be electrically connected with described heat of cooling water pump and described frequency converter, according to the action of heat of cooling water pump described in the detection signal control of described multiple Temperature Humidity Sensors and described temperature sensor, according to the action of frequency converter described in the detection signal control of described temperature sensor and described pressure sensor.
Further, described control module is the one having in man-machine interactive PLC controller, singlechip controller or other computerized control system of touch-screen.
A kind of useless full heat recovery method of damp-heat air, comprises the steps:
1) start, the each status register of system initializes;
2) sampling cistern water level, water tank temperature, and the temperature and humidity of working environment air-conditioning, the each device status register set of system;
3) judge whether the water level of water tank reaches the lowest water level of setting, if start moisturizing operation lower than lowest water level, water level is supplemented to designated water level;
4) environment temperature, humidity reach request cooling, sequence starting heat of cooling water pump, circulating fan, compressor while dehumidifying set definite value;
5) judge respectively the relation of water tank temperature and water supply design temperature, comprising:
5.1) judge the relation of water tank temperature and water supply set water temperature, if be less than the water temperature of setting, use equipment whether to send water request and whether recuperation of heat unit is in running order according to heat, also detect hot use equipment simultaneously and whether have the request of the water of pressure, if recuperation of heat unit is in running order, nothing is forced water request simultaneously, waits for that water temperature is to design temperature row water supply again, if there is the water supply of pressure request to supply water immediately; If recuperation of heat unit is not in running order, supply water immediately or after the delayed time;
5.2), if water request appears in the water temperature of water tank in setting range, supply water immediately;
5.3) if the water temperature of water tank higher than design temperature, and without forcing water request, postpone to supply water, running water pipe water inlet is simultaneously supplied water Water in Water Tank temperature drop to design temperature, when as reached the water level upper limit in water inlet temperature-fall period middle water level, temperature does not drop to design temperature, supply water immediately; If there is the request of supplying water of forcing, no matter in what temperature all supply water immediately;
6) judge the hydraulic pressure of radiator drain, if the pressure that is less than setting frequency converter raising frequency control constant voltage water pump by boost in pressure to setting value, if the pressure of supply water that is greater than setting frequency converter frequency reducing control constant voltage water pump by Pressure Drop to setting value.
Compared with prior art, the present invention has following beneficial effect:
1, evaporimeter can make the cold-producing medium in useless damp-heat air and the evaporimeter in work-yard carry out heat exchange effectively, thereby cooled dose of institute of full heat that high temperature, highly humid air comprise in the process of cooling and dehumidifying absorbed, when reaching to work-yard cooling, dehumidifying, can also reclaim the effect of heat.
2, cold-producing medium enters in condenser after the compression of compressor, discharges the heat that it absorbs from evaporimeter; And condenser is connected by circulating line with water tank, the heat that can utilize easily cold-producing medium to discharge heats the water in water tank, thereby reaches the effect that used heat utilizes.
3, circulating fan and air supply duct can, by be sent to the assigned address of inside, workplace through cool-down dehumidification air after treatment, be realized the effect to working environment cool-down dehumidification effectively.
4, heat of cooling water pump can make the water in water tank be fed to fully condenser place, thus in effectively realizing the heating of water, can also avoid heat in condenser not to be passed away in time and cause overheated.
5, constant voltage water pump can be realized the control to hydraulic pressure in radiator drain road under the control of frequency converter, preset standard hydraulic pressure according to the requirement using, when water tank discharge pressure is during lower than this setting hydraulic pressure, frequency converter can improve discharge pressure to setting hydraulic pressure to control constant voltage water pump by raising frequency; When water tank discharge pressure is during higher than this setting hydraulic pressure, frequency converter frequency reducing reduces discharge pressure to setting hydraulic pressure to control constant voltage water pump, thereby ensures that water tank thermotropism uses the heat hydraulic pressure of supply of equipment constant.
6, adopt PLC, single-chip microcomputer or computer as control module, timely sampling and the judgement that can realize multiple sensing datas are processed, its sample frequency is high, control is accurate, can ensure the smooth running of whole system, can also come easily the numerical value such as water temperature, hydraulic pressure to be set and adjusted by program prepared in advance simultaneously, thereby improve the adaptability to different operating environment and requirement of the present invention, guarantee that system works is in optimum state.
7, the sewage draining exit being arranged on water tank is closed at ordinary times, need to remove contamination time, opens, can be so that the cleaning of water tank and maintenance.
Brief description of the drawings
Fig. 1 is useless muggy air total heat recovering system structural representation of the present invention;
Fig. 2 is method of operating FB(flow block) of the present invention.
Mark the following drawings mark thereon by reference to the accompanying drawings:
1-steam drying machine, 2-washing machine, 3-recuperation of heat unit, 31-evaporimeter, 32-condenser, 33-compressor, 34-circulating fan, 4-water tank, 41-heat of cooling water pump, 42-water conveying equipment, 421-constant voltage water pump, 422-pressure sensor, 423-temperature sensor, 43-water inlet pipe, 44-outlet pipe, 45-sewage draining exit, 5-air supply duct.
Detailed description of the invention
Below in conjunction with accompanying drawing, preferred embodiment of the present invention is described in detail, but is to be understood that protection scope of the present invention is not subject to the restriction of detailed description of the invention.
A kind of useless muggy air total heat recovering system, is applied to the hot and humid working environment of relative closure, as shown in Figure 1, comprises recuperation of heat unit 3 and heat utilization equipment.Described recuperation of heat unit 3 comprises the evaporimeter 31 being arranged in working environment, the condenser 32 being connected by pipeline with described evaporimeter 31, and the compressor 33 being connected by pipeline with condenser 32 with described evaporimeter 31.In evaporimeter 31, condenser 32 and compressor 33, use cold-producing medium, the materials such as such as common freon, ammonia, propane, ethene, as refrigerant.In described recuperation of heat unit 3, also comprise and be arranged near the circulating fan 34 of described evaporimeter 31, and the pipeline for giving wind for air conditioner 5 to working environment cool-down dehumidification being connected with the air outlet of this circulating fan 34, on this air supply duct 5, be provided with multiple air outlets to blowing in working environment, in Fig. 1, schematically drawn three.Evaporimeter 31 carries out heat exchange for the useless damp-heat air and the cold-producing medium that make environment, therefore, need to determine its installation site according to the physical condition in place, selects to be both conducive to heat exchange, can not affect again the position of arrangement and the operation of other equipment.Described circulating fan 34 be for make with evaporimeter 31 heat exchange after air be transported in air supply duct 5, therefore, the installation of this circulating fan 34 need to be determined a near correct position described evaporimeter 31 according to physical conditions such as the mounting condition on place, air-flow trend, the specification of blower fan and the positions of air supply duct 5, to obtain good air draft effect.
The operation principle of recuperation of heat unit 3 is as follows: compressor 33 is high steam by the refrigerant compression under low-pressure steam state, high steam drains in condenser 32, external cooling surface and the water in water tank 4 of condenser 32 carries out heat exchange (be to condense into highly pressurised liquid after the high steam heat release in condenser 32, the running water heat absorption in water tank 4 simultaneously forms the hot water for heat utilization equipment); Highly pressurised liquid in condenser 32 further enters evaporimeter 31, now evaporimeter 31 with carry out heat exchange from the useless damp-heat air in working environment and (enter evaporation endothermic under aforementioned highly pressurised liquid in evaporimeter 31 low-pressure state in evaporimeter 31, flow through after the useless damp-heat air on evaporimeter 31 surfaces is lowered the temperature, dehumidified simultaneously and enter air supply duct 5 through the effect of circulating fan 34 again, be finally back to working environment).Whole system by useless damp-heat air at the surface cooling of evaporimeter 31, condense into water, again the heat absorbing in whole temperature-fall period heated for the water of heat utilization system, effectively realized the recycling of energy, the temperature and humidity of air all has obvious decline simultaneously.By the specification of each equipment of choose reasonable, and optimal control method and parameter setting on the basis of debugging at the scene, can make air temperature control in above-mentioned working environment at 26~28 degrees Celsius, humidity is controlled at 55%~65%.
Described heat utilization equipment comprises the water tank 4 being connected by circulating line with described condenser 32, and is connected to the water conveying equipment 42 in the outlet pipeline of described water tank 4; Wherein, the volume of described water tank meets the full heat absorption of per tour and the state without water request, is also provided with water inlet pipe 43, outlet pipe 44 and the sewage draining exit 45 that can connect tap water pipe line on water tank 4.Outside watering equipment in this example is washing machine 2, and washing machine 2 itself has water and heats and keep water temperature function, is connected to the downstream of described water conveying equipment 42.Described circulating line comprises pipeline and a pipeline from water tank 4 to condenser 32 water deliverys from condenser 32 to water tank 4 water deliverys, the pipeline from water tank 4 to condenser 32 water deliverys, is provided with heat of cooling water pump 41.In the time that this heat of cooling water pump 41 is worked, can ensure the output of water tank 4 to condenser 32.Described water conveying equipment 42 comprises the constant voltage water pump 421 in the outlet pipeline that is connected to described water tank 4, detect the pressure sensor 422 of pressure in the outlet pipeline of described water tank 4, detect the temperature sensor 423 of water temperature in the outlet pipeline of described water tank 4, and control the frequency converter (not shown) that described constant voltage water pump 421 moves.This frequency converter can be controlled the output pressure of described constant voltage water pump 421, frequency converter is adjusted frequency and is made the downstream hydraulic pressure of constant voltage water pump 421 in outlet pipeline keep constant according to the numerical value change situation of pressure sensor 422, and the downstream line of this constant voltage water pump 421 is connected with described washing machine 2.The optimum frequency that the numerical value of pressure sensor 422 and best cistern water level, frequency converter are set is corresponding, and in the time that washing machine 2 supplies water to water tank 4 requests, when the SEA LEVEL VARIATION of water tank 4, pressure sensor 422 detects corresponding variation simultaneously.Frequency converter is according to the output of the numerical value change controlled frequency of pressure sensor 422, when hydraulic pressure is lower than when setting value frequency converter raising frequency, when the frequency converter frequency reducing during higher than the setting operating pressure of constant voltage water pump 421 of the hydraulic pressure in outlet pipeline, the water pressure invariableness of exporting to control constant voltage water pump 421.
Described useless muggy air total heat recovering system also comprises multiple Temperature Humidity Sensors (not shown) of temperature and humidity in testing environment, and the control module (not shown) being connected with described multiple Temperature Humidity Sensor communications; And, described control module is also connected with described pressure sensor 422 and 423 communications of described temperature sensor, all be electrically connected with described heat of cooling water pump 41 and described frequency converter, according to the action of heat of cooling water pump 41 described in the detection signal control of described multiple Temperature Humidity Sensors and described temperature sensor 423, according to the action of frequency converter described in the detection signal control of described temperature sensor 423 and described pressure sensor 422.Preferably, described control module is the one having in man-machine interactive PLC controller, singlechip controller or other computerized control system of touch-screen.
In Fig. 2, provide the optimization operation method of useless muggy air total heat recovering system in this example by the form of FB(flow block), i.e. a kind of useless full heat recovery method of damp-heat air.The object that the method can realize the dehumidifying and cooling to working environment and supply constant voltage hot water to washing machine 2, comprises the steps:
1) start, the each status register of system initializes;
2) sampling cistern water level, water tank temperature, and the temperature and humidity of working environment air-conditioning, the each device status register set of system;
3) judge whether the water level of water tank reaches the lowest water level of setting, if start moisturizing operation lower than lowest water level, water level is supplemented to designated water level;
4) environment temperature, humidity reach request cooling, sequence starting heat of cooling water pump, circulating fan, compressor while dehumidifying set definite value, and heat of cooling water pump, circulating fan status register set open state;
5) judge respectively the relation of water tank temperature and water supply design temperature, comprising:
5.1) judge the relation of water tank temperature and water supply set water temperature, if be less than the water temperature of setting, use equipment whether to send water request and whether recuperation of heat unit is in running order according to heat, also detect hot use equipment simultaneously and whether have the request of the water of pressure, if recuperation of heat unit is in running order, nothing is forced water request simultaneously, waits for that water temperature is to design temperature row water supply again, if there is the water supply of pressure request to supply water immediately; If recuperation of heat unit is not in running order, supply water immediately or after delayed time (not shown);
5.2), if water request appears in the water temperature of water tank in setting range, supply water immediately;
5.3) if the water temperature of water tank higher than set output temperature, and without forcing water request, postpone to supply water, running water pipe water inlet is simultaneously supplied water Water in Water Tank temperature drop to design temperature, when as reached the water level upper limit in water inlet temperature-fall period middle water level, temperature does not drop to design temperature, supply water immediately; If there is the request of supplying water of forcing, no matter in what temperature all supply water immediately;
6) judge the hydraulic pressure of radiator drain, if the pressure that is less than setting frequency converter raising frequency control constant voltage water pump by boost in pressure to setting value, if the pressure of supply water that is greater than setting frequency converter frequency reducing control constant voltage water pump by Pressure Drop to setting value.
Particularly, in above-mentioned steps 2) in sampling cistern water level, refer to that level sensor measures automatically.In step 3) in operation be to realize by the electric valve of automatic control.In step 4) in, if need to dehumidify separately, can compressor 33 be rear that compressor 33 is carried out to intermittent on off control starting, so that the heat exchange on evaporimeter 31 surfaces is intermittently carried out, can make so airborne a part of steam condensation is aqueous water, reduce air humidity, can also avoid temperature to reduce amplitude simultaneously excessive.The time interval of compressor 33 intermittent starts is longer, temperature reduce more not obvious, but also variation correspondingly of effect on moisture extraction; The time interval is shorter, and cooling-down effect and effect on moisture extraction all can improve.In actual use, the start and stop interval that need to debug compressor 33 according to on-the-spot air humidity with to the requirement of dehumidifying, to obtain a suitable effect on moisture extraction.If need cooling or cooling and dehumidifying carry out simultaneously, directly make compressor 33 keeps always turn round both can, until reach suitable temperature.In step 5.1) in, to heated speed determine according to the water in water tank 4 described time delay, firing rate is faster, and delay time is shorter, on the contrary delay time is longer.Because the parameter such as water temperature, the caliber of outlet pipe 44 of the water level in performance, the water tank 4 of the heat exchanger effectiveness of humiture, evaporimeter 31 and the condenser 32 of the useless damp-heat air in environment, compressor 33 and the water yield, running water all has impact to the firing rate of the water in water tank 4, therefore, this delay time needs could determine optimal values after the debugging of ground on the scene.
It will be appreciated that, the related determining step of temperature, humidity and pressure is all being carried out at any time in the running of whole system in said method, instead of once after judgement, just stop.The judgement of continuation like this, its benefit is to detect in time that the operating parameters of system changes, and control module is responded in time, thereby makes the water that water tank 4 is exported can keep water temperature, hydraulic pressure approximately constant.Any in employing PLC controller, singlechip controller or computerized control system can be by programming to meet this technical requirement of carrying out at any time parameter judgement as control module.
Through measuring and calculating, the system and method for the present embodiment is combined with following effect: the above-mentioned recuperation of heat unit 3 required power consumption of working is about 1/3rd to 1/5th of heat energy that evaporimeter 31 absorbs, and Optimization Work point absorbs 1/4th left and right of heat about evaporimeter; Described useless damp-heat air source is steam drying machine 1, and the temperature range of the useless hot and humid gas of its discharge is at 70~90 degrees Celsius, and the recyclable scope of the heat of recuperation of heat unit 3 contains this temperature range, and Optimization Work o'clock is corresponding to the damp-heat air of 80 degrees Celsius.The hot water scope that washing machine 2 uses is greatly about 30~60 degrees Celsius, optimum temperature is at 55 degrees Celsius, running water temperature before heating is generally lower than room temperature, and common is 10~25 degrees Celsius, and the maximum temperature after condenser 32 heating can be elevated to more than 60 degrees Celsius.According to actual using amount of hot water, remain on best 55 degrees Celsius by the parameters such as the design temperature of selection control system and the specification of compressor 33 water temperature that just can make easily to supply water.The reference data of relevant energy exchange is as follows: the ratio enthalpy of vaporization of every kilogram of saturated vapor: 2675.71kJ/kg; Specific heat of water holds: 4.186kJ/ (kg. DEG C); It is 766.48kW that 1000 kilograms of saturated steam phase transformings are cooled to 80 degrees Celsius of energy that discharge after for the aqueous water of 100 degrees Celsius again.
Disclosed is above only preferably specific embodiment of the present invention, and still, the present invention is not limited thereto, and the changes that any person skilled in the art can think of all should fall into protection scope of the present invention.
Claims (4)
1. a useless muggy air total heat recovering system, be applied to the hot and humid working environment of relative closure, comprise recuperation of heat unit and heat utilization equipment, it is characterized in that: described recuperation of heat unit comprises the evaporimeter being arranged in working environment, the condenser being connected by pipeline with described evaporimeter, and the compressor being connected by pipeline with condenser with described evaporimeter;
Described heat utilization equipment comprises the water tank being connected by circulating line with described condenser, and be connected to the water conveying equipment in the outlet pipeline of described water tank, described water conveying equipment comprises the constant voltage water pump in the outlet pipeline that is connected to described water tank, detect the pressure sensor of pressure in the outlet pipeline of described water tank, detect the temperature sensor of water temperature in the outlet pipeline of described water tank, and control the frequency converter of described constant voltage water pump action; Wherein,
In circulating line between described water tank and described condenser, be provided with heat of cooling water pump;
On described water tank, be also provided with water inlet pipe and the outlet pipe that can connect tap water pipe line;
Above-mentioned useless muggy air total heat recovering system also comprises: multiple Temperature Humidity Sensors of temperature and humidity in testing environment, and the control module being connected with above-mentioned multiple Temperature Humidity Sensor communications; Described control module is also connected with described pressure sensor and described temperature sensor communication, all be electrically connected with described heat of cooling water pump and described frequency converter, according to the action of heat of cooling water pump described in the detection signal control of described multiple Temperature Humidity Sensors and described temperature sensor, according to the action of frequency converter described in the detection signal control of described temperature sensor and described pressure sensor.
2. useless muggy air total heat recovering system according to claim 1, is characterized in that: in described recuperation of heat unit, also comprises and is arranged near the circulating fan of described evaporimeter, and the air supply duct being connected with the air outlet of this circulating fan.
3. useless muggy air total heat recovering system according to claim 1 and 2, it is characterized in that: described heat utilization equipment also comprises the washing machine that uses equipment as heat, washing machine itself has water and heats and keep water temperature function, this heat to use the downstream of equipment connection at described water conveying equipment.
4. useless muggy air total heat recovering system according to claim 1, is characterized in that: described control module is the one having in man-machine interactive PLC controller, singlechip controller or other computerized control system of touch-screen.
Priority Applications (2)
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CN201110238148.5A CN102384606B (en) | 2011-08-18 | 2011-08-18 | System for recovering total heat of waste damp and hot air and method |
PCT/CN2012/074714 WO2013023459A1 (en) | 2011-08-18 | 2012-04-26 | Total heat recovery system of waste-wet-hot air and heat recovery method therefor |
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CN201110238148.5A CN102384606B (en) | 2011-08-18 | 2011-08-18 | System for recovering total heat of waste damp and hot air and method |
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CN102384606B true CN102384606B (en) | 2014-08-13 |
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Families Citing this family (12)
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CN102384606B (en) * | 2011-08-18 | 2014-08-13 | 宁波惠康实业有限公司 | System for recovering total heat of waste damp and hot air and method |
CN104596006B (en) * | 2015-01-15 | 2017-06-20 | 王全龄 | A kind of domestic hot-water and swimming pool residual heat integrative heating system |
US10285562B2 (en) * | 2015-07-31 | 2019-05-14 | Illinois Tool Works Inc. | Warewasher with heat recovery system |
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CN109579182A (en) * | 2018-12-04 | 2019-04-05 | 珠海格力电器股份有限公司 | Household electrical appliance |
CN111797525B (en) * | 2020-06-03 | 2021-07-30 | 中国南方电网有限责任公司超高压输电公司广州局 | Pipeline pressure control method and system |
CN111998575A (en) * | 2020-09-16 | 2020-11-27 | 中煤科工(天津)清洁能源研究院有限公司 | Bathing wastewater waste heat recovery system |
CN113183791A (en) * | 2021-04-01 | 2021-07-30 | 南京能瑞电力科技有限公司 | Heat dissipation management system control method and heat dissipation management system of charging pile |
CN114150466B (en) * | 2021-11-17 | 2023-10-20 | 江苏弗莱明恩环境科技有限公司 | Energy-saving and environment-friendly integrated equipment for cleaning, ironing and drying |
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WO2013023459A1 (en) | 2013-02-21 |
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