CN107940805A - Direct-cooling type depth enthalpy takes hot idle air heat pump system - Google Patents
Direct-cooling type depth enthalpy takes hot idle air heat pump system Download PDFInfo
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- CN107940805A CN107940805A CN201711422521.6A CN201711422521A CN107940805A CN 107940805 A CN107940805 A CN 107940805A CN 201711422521 A CN201711422521 A CN 201711422521A CN 107940805 A CN107940805 A CN 107940805A
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- idle air
- heat
- heat pump
- direct
- hot
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- 238000001816 cooling Methods 0.000 title claims abstract description 31
- 239000012530 fluid Substances 0.000 claims abstract description 43
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 38
- 230000002528 anti-freeze Effects 0.000 claims abstract description 29
- 239000007788 liquid Substances 0.000 claims abstract description 27
- 239000003507 refrigerant Substances 0.000 claims abstract description 14
- 238000010521 absorption reaction Methods 0.000 claims abstract description 5
- 239000007921 spray Substances 0.000 claims description 22
- 238000010257 thawing Methods 0.000 claims description 19
- 238000010438 heat treatment Methods 0.000 claims description 17
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 claims description 15
- 239000000498 cooling water Substances 0.000 claims description 10
- 230000008676 import Effects 0.000 claims description 7
- 230000008859 change Effects 0.000 claims description 4
- 238000009833 condensation Methods 0.000 claims description 4
- 230000005494 condensation Effects 0.000 claims description 4
- 238000005507 spraying Methods 0.000 claims description 3
- 235000015110 jellies Nutrition 0.000 claims 1
- 239000008274 jelly Substances 0.000 claims 1
- 239000002918 waste heat Substances 0.000 abstract description 6
- 238000011084 recovery Methods 0.000 abstract description 3
- 238000010025 steaming Methods 0.000 description 9
- 238000005516 engineering process Methods 0.000 description 8
- 238000000034 method Methods 0.000 description 6
- 238000010586 diagram Methods 0.000 description 5
- 239000003245 coal Substances 0.000 description 4
- 238000001704 evaporation Methods 0.000 description 4
- 230000008020 evaporation Effects 0.000 description 4
- 230000014759 maintenance of location Effects 0.000 description 4
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 4
- 238000007710 freezing Methods 0.000 description 3
- 238000012423 maintenance Methods 0.000 description 3
- 230000006835 compression Effects 0.000 description 2
- 238000007906 compression Methods 0.000 description 2
- 239000010725 compressor oil Substances 0.000 description 2
- 230000008014 freezing Effects 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 238000011144 upstream manufacturing Methods 0.000 description 2
- 108010053481 Antifreeze Proteins Proteins 0.000 description 1
- 208000010086 Hypertelorism Diseases 0.000 description 1
- 206010020771 Hypertelorism of orbit Diseases 0.000 description 1
- 238000004378 air conditioning Methods 0.000 description 1
- 238000003287 bathing Methods 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 239000000284 extract Substances 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 230000035800 maturation Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000001681 protective effect Effects 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
- 208000011580 syndromic disease Diseases 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 238000010792 warming Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- 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
- 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
- F25B30/02—Heat pumps of the compression type
-
- 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
- F25B39/00—Evaporators; Condensers
- F25B39/02—Evaporators
-
- 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
- F25B49/00—Arrangement or mounting of control or safety devices
- F25B49/02—Arrangement or mounting of control or safety devices for compression type machines, plants or systems
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
- Heat-Pump Type And Storage Water Heaters (AREA)
Abstract
The invention discloses a kind of direct-cooling type depth enthalpy to take hot idle air heat pump system, it includes idle air and takes hot cell, the idle air takes hot cell to be equipped with least one idle air heat producing box, the idle air heat producing box is connected by antifreeze liquid pipeline with the evaporator of heat pump unit, the antifreeze liquid pipeline is used to flow through anti-icing fluid, circulating pump is installed on the antifreeze liquid pipeline, the anti-icing fluid absorbs the heat in idle air when flowing through idle air heat producing box, the heat in the idle air of absorption is changed to the refrigerant in heat pump unit when the anti-icing fluid flows through the evaporator, condenser in the heat pump unit is used to exchange heat with user's hot water.Direct-cooling type depth enthalpy of the present invention takes hot idle air heat pump system simple in structure, and the idle air waste heat recovery thermal efficiency is high.
Description
Technical field
The present invention relates to a kind of residual neat recovering system, is used to recycle coal mine methane (return air) waste heat more particularly to one kind
System.
Background technology
The characteristics of mine air-lack (return air) has air quantity big, and wind-warm syndrome is stable, relative humidity is big, and continuity is good, is good
Cryogenic waste heat resource, by idle air heat pump techniques, waste heat in idle air is extracted, can meet mine structure heating, bathing
Hot water prepares and the needs of wellhead anti-freezing heat.Summer can utilize idle air heat pump refrigerating to be used for building air conditioning or underground drop at the same time
Temperature.
To coal mine methane UTILIZATION OF VESIDUAL HEAT IN at present based on two kinds of technology paths：One is " water spray type idle air heat pump " technology road
Line, another is " direct steaming type idle air heat pump " technology path.
Water spray type idle air heat pump techniques route principle in return air retention tower mouth as shown in Figure 1, by setting spray equipment, in fact
Existing recirculated water " spray ", makes water directly contact carry out heat and mass with idle air, heat in idle air is replaced in water, recycles water
Source heat pump technology extracts heat from water, for heat supply.The technology includes collection chamber 1 ', collecting-tank 2 ', full-automatic water processor
The capital equipment such as 3 ' and Scrawl wind source heat pump unit 4 '.
Direct steaming type idle air heat pump techniques, its principle take hot cell 5 ' as shown in Fig. 2, building an idle air in return air retention tower mouth,
Hot cell side arrangement idle air heat producing box (evaporator) 6 ' is taken, using low-temperature low-pressure refrigerant liquid in idle air heat producing box heat exchanger
Evaporation endothermic, directly comes out heat extraction in idle air, is changed into gaseous state after refrigerant evaporation endothermic, and gaseous refrigerant enters compression
Further compression is changed into high temperature and high pressure gaseous refrigerant in machine 7 ', and heat is replaced feedwater in condenser 9 ' and used by gaseous refrigerant
It is changed into liquid after heat supply, gaseous refrigerant heat release, the expanded valve 8 ' of liquid refrigerant is again introduced into idle air heat producing box after being depressured
Heat exchanger, so as to complete entirely to circulate.
Water spray type idle air heat pump techniques have the following disadvantages：(1) return air utilization rate is low, and aqueous vapor takes away a large amount of waste heats；(2) system
System is complicated, including spray system, the circulatory system, collecting-tank, filter, heat pump system etc.；(3) it is weary due to being exchanged heat using spray
Foul is fully entered in water in wind, causes filter and unit to be frequently occluded, and inefficiency, maintenance difficulties are big, costly, reliably
Property is low；(4) water circulating pump uses open circulation, and power consumption is higher, and operating cost is high；(5) after idle air takes thermal Finite, idle air to take heat
Not less than 7 DEG C；(6) hot side is taken to use open circulation, idle air takes away a large amount of aqueous vapors, and system water supplement amount is larger.
Direct steaming type idle air heat pump techniques have the following disadvantages：(1) direct steaming type idle air heat pump techniques belong to large-scale split heat pump,
There is no standard unit, it is necessary to which equipment manufacturer's Specialty Design, technical difficulty are big；(2) direct steaming type idle air heat pump and idle air heat producing box it
Between connection using being refrigerant tubing, compressed function power and compressor oil return limitation, distance between unit and idle air heat producing box
It must not be too far away, typically not greater than 200m, hypertelorism, compressor oil return is difficult, and idle air heat pump is not energy efficient, and idle air heat pump can
It is deteriorated by property；(3) height difference is not easy too greatly between idle air heat producing box and idle air heat pump unit, no that compressor will be caused not energy efficient；
(4) when unit number of units is more, every idle air heat pump unit is connected with respective heat producing box by respective refrigerant tubing, causes to freeze
Agent pipeline is very more, system complex and investment is big；(5) idle air takes to defrosting problem below frost point and is difficult to solve, and realizes that twin-stage takes
Hot difficulty is larger.
The content of the invention
The technical problem to be solved in the present invention is to provide a kind of direct-cooling type depth enthalpy that can solve above-mentioned prior art shortcoming
Take hot idle air heat pump system.
Direct-cooling type depth enthalpy of the present invention takes hot idle air heat pump system, including idle air to take hot cell, and the idle air takes hot cell to be equipped with
At least one idle air heat producing box, the idle air heat producing box are connected by antifreeze liquid pipeline with the evaporator of heat pump unit, described anti-
Freeze liquid pipeline to be used to flow through anti-icing fluid, circulating pump is installed, the anti-icing fluid flows through idle air heat producing box on the antifreeze liquid pipeline
When absorb idle air in heat, the heat in the idle air of absorption is changed to heat pump machine when the anti-icing fluid flows through the evaporator
Refrigerant in group, the condenser in the heat pump unit are used to exchange heat with user's hot water.
Direct-cooling type depth enthalpy of the present invention takes hot idle air heat pump system, wherein the idle air heat producing box is including first base and admittedly
The outer framework being scheduled in the first base, at least level-one is provided with the outer framework and takes heat along what idle air flowed through direction arrangement
Heat exchanger, the lower part and top of every grade of heat taking and exchanging device are respectively equipped with and take hot working fluid import and take hot working fluid to export, described to take heat
Working medium import and it is described take hot working fluid outlet connect the antifreeze liquid pipeline respectively, the heat pump unit is arranged at least level-one,
The heat pump unit is corresponded with the heat taking and exchanging device and arranged, the cooling water pipeline of condenser in every grade of heat pump unit
Between be connected in series by communicating pipe.
Direct-cooling type depth enthalpy of the present invention takes hot idle air heat pump system, wherein between the heat exchanger tube of every grade of heat taking and exchanging device
Equipped with defrosting heating tube, the defrosting heating tube is used for the hydrothermal solution that circulates.
Direct-cooling type depth enthalpy of the present invention takes hot idle air heat pump system, is used to adjust idle air flow wherein the outer framework is equipped with
Adjustable air-valve.
Direct-cooling type depth enthalpy of the present invention takes hot idle air heat pump system, wherein the heat taking and exchanging device further includes fin, it is described to change
Heat pipe is arranged on the fin, and the defrosting heating tube is also disposed on the fin.
Direct-cooling type depth enthalpy of the present invention takes hot idle air heat pump system, wherein the outer framework, which is equipped with to be used to spraying, described takes heat
The spray system of heat exchanger outer surface, the spray system include nozzle and the spray tube being connected with the nozzle, the spray
Shower pipe is used for being connected with watering.
Direct-cooling type depth enthalpy of the present invention takes hot idle air heat pump system, wherein the anti-icing fluid is ethylene glycol.
Direct-cooling type depth enthalpy of the present invention takes hot idle air heat pump system, wherein further including second base, is set in the second base
It is equipped with the heat pump unit.
Direct-cooling type depth enthalpy of the present invention takes hot idle air heat pump system, is set wherein the condenser in every grade of heat pump unit is fixed
Put in the second base, the top of the condenser is equipped with the evaporator, between the condenser and the evaporator
The pipeline of connection is equipped with expansion valve, and the top of the evaporator is equipped with compressor.
Direct-cooling type depth enthalpy of the present invention takes hot idle air heat pump system, wherein the condenser is disposed side by side on the second base
On.
Direct-cooling type depth enthalpy of the present invention takes hot idle air heat pump system difference from prior art to be that the present invention sets idle air
Hot cell is taken, idle air takes hot cell to be equipped with least one idle air heat producing box, and idle air heat producing box passes through antifreeze liquid pipeline and heat pump unit
Evaporator connection, absorb the heat in idle air when anti-icing fluid flows through idle air heat producing box, anti-icing fluid will when flowing through the evaporator
Heat in the idle air of absorption is changed to the refrigerant in heat pump unit, the condenser in heat pump unit be used for user's hot water into
Row heat exchange.Whole system is simple, and the idle air waste heat recovery thermal efficiency is high；Circulated using enclosed anti-icing fluid, water consumption is small, while antifreeze
Liquid is not mixed into foul, smaller on unit durability influence, while blockage problem is not present, and reliability is high, and maintenance is small；Anti-icing fluid
Circulation use circulating pump, heat pump computer room and idle air take hot cell between relative position it is more flexible, from heat producing box and idle air heat pump
Unit spacing and height difference restricted problem；Connecting pipe can share between heat producing box and heat pump unit, with direct steaming type idle air heat pump
Compare, reduce number of tubes, system is simpler, reduces investment.
The invention will be further described below in conjunction with the accompanying drawings.
Brief description of the drawings
Fig. 1 is water spray type idle air heat pump system schematic diagram of the prior art；
Fig. 2 is direct steaming type idle air heat pump system schematic diagram of the prior art；
Fig. 3 takes hot idle air heat pump system schematic diagram one for direct-cooling type depth enthalpy of the present invention；
Fig. 4 takes hot idle air heat pump system schematic diagram two for direct-cooling type depth enthalpy of the present invention；
Fig. 5 is the front view of the idle air heat producing box in the present invention；
Fig. 6 is the left view of the idle air heat producing box in the present invention；
Fig. 7 is the schematic diagram of the heat pump unit in the present invention；
Fig. 8 is the front view of the heat pump unit in the present invention；
Fig. 9 is the top view of the heat pump unit in the present invention；
Figure 10 is the left view of the heat pump unit in the present invention.
Embodiment
As shown in figure 3, direct-cooling type depth enthalpy of the present invention takes hot idle air heat pump system, including idle air to take hot cell 25, the idle air
Hot cell 25 is taken to be equipped with least one idle air heat producing box 1, the idle air heat producing box 1 passes through antifreeze liquid pipeline 2 and heat pump unit 28
Evaporator connection, the antifreeze liquid pipeline 2 be used for flow through anti-icing fluid, circulating pump 27, institute are installed on the antifreeze liquid pipeline 2
The heat absorbed when anti-icing fluid flows through idle air heat producing box 1 in idle air is stated, by absorption when the anti-icing fluid flows through the evaporator
Heat in idle air is changed to the refrigerant in heat pump unit 28, and the condenser in the heat pump unit 28 is used for and user's hot water
Exchange heat.
The idle air takes hot cell 25 to be arranged on coal mine return air retention tower mouth, is provided with fan in drive, idle air is blowed to weary
Wind takes hot cell 25, and the idle air heat producing box 1 is arranged on the side that idle air takes hot cell 25, and idle air takes the opposite side in hot cell 25 to be provided with
Reverse self closing door 26, idle air are flowed out through idle air heat producing box 1.
Direct-cooling type depth enthalpy of the present invention takes hot idle air heat pump system, wherein the idle air heat producing box 1 include first base 15 with
And the outer framework 16 in the first base 15 is fixed on, be provided with least level-one in the outer framework 16 flows through direction along idle air
The heat taking and exchanging device 17 of arrangement, the lower part and top of every grade of heat taking and exchanging device 17, which are respectively equipped with, to be taken hot working fluid import 23 and takes thermal technology
Matter outlet 24, it is described to take hot working fluid import 23 and described take hot working fluid outlet 24 to connect the antifreeze liquid pipeline 2, the heat respectively
Pump assembly 28 is arranged at least level-one, and the heat pump unit 28 is corresponded with the heat taking and exchanging device 17 and arranged, described in every grade
It is connected in series in heat pump unit 28 between the cooling water pipeline of condenser by communicating pipe 14.
An idle air heat producing box 1 is provided with Fig. 3, and level-one heat taking and exchanging device 17 is provided only with the idle air heat producing box 1,
Corresponding, the heat pump unit 28 is also only arranged to level-one.
An idle air heat producing box 1 is provided with Fig. 4, and two-stage heat taking and exchanging device 17 is equipped with the idle air heat producing box 1, with
This is corresponding, and the heat pump unit 28 is also configured as two-stage.
In practical applications, idle air heat producing box 1 can set two or more according to actual condition, idle air heat producing box
Heat taking and exchanging device 17 in 1 can also be set to more than two-stage according to actual condition.
Direct-cooling type depth enthalpy of the present invention takes hot idle air heat pump system, wherein the anti-icing fluid is ethylene glycol.
As shown in figure 5, and with reference to shown in Fig. 6, the idle air heat producing box in the present invention includes first base 15 and being fixed on
Outer framework 16 in the first base 15, at least level-one is provided with the outer framework 16 and flows through taking for direction arrangement along idle air
Heat exchanger 17, the lower part and top of every grade of heat taking and exchanging device 17, which are respectively equipped with, to be taken hot working fluid import 23 and takes hot working fluid to export
24, defrosting heating tube 22 is equipped between the heat exchanger tube of every grade of heat taking and exchanging device 17, the defrosting heating tube 22 is used for the heat that circulates
Liquid, the lower section of the heat taking and exchanging device 17 are equipped with water-collecting tray 18, and the water-collecting tray 18 is built-in with antifreeze coil pipe 19, the antifreeze disk
Pipe 19 is used for the hydrothermal solution that circulates.
Above-mentioned outer framework 16 and the protective device that first base 15 is whole heat producing box, make the structure of heat producing box more
Firmly, can be directly stacked by two heat producing box during installation heat producing box, convenient installation.
For above-mentioned heat taking and exchanging device 17 to take hot systems in the present invention, the heat taking and exchanging device 17 can be according to actual work
Condition sets specific series, and in this embodiment, heat taking and exchanging device 17 is set to two-stage, is respectively that level-one takes hot heat exchange
Device and two level heat taking and exchanging device, level-one heat taking and exchanging device are located at the upstream that idle air flows through direction, and two level heat taking and exchanging device is positioned at weary
The distinguished and admirable downstream through direction.Taking hot systems by the low temperature of every grade of idle air heat pump unit preparation to take hot working fluid, (ethylene glycol etc. is antifreeze
Liquid) respectively enter the heat exchanger tube of level-one heat taking and exchanging device and two level heat taking and exchanging device, idle air passes through every grade of heat taking and exchanging device 17
During heat exchanger tube, the heat in idle air is replaced and is taken in hot working fluid.
Above-mentioned defrosting heating tube 22 is remove defrosting system in the present invention, and during defrosting, closing heat producing box I and II takes heat to change
The valve of hot device 17, realizes that stopping takes heat, while opens the hydrothermal solution valve of defrosting heating tube 22, makes to be passed through in defrosting heating tube 22
Hydrothermal solution, so that the frost on 17 surface of heat taking and exchanging device be removed.
Above-mentioned antifreeze coil pipe is the winterization system in the present invention, and the water that frost becomes after defrosting in order to prevent, which flows into, to catchment
Freeze after disk 18, the built-in antifreeze coil pipe 19 of water-collecting tray 18.By ceaselessly toward hydrothermal solution is passed through in antifreeze coil pipe 19 to prevent from collecting
Water pond 18 freeze it is freezing and defrosting water can not discharge.
The outer framework 16 is equipped with the adjustable air-valve 20 for being used for adjusting idle air flow.Above-mentioned adjustable air-valve 20 is this hair
Tune wind system in bright, the adjustable air-valve 20 are installed at the air outlet of heat producing box.When multiple heat producing box are arranged, by
It is different in the distance apart from air port, cause also to differ by the air quantity of each heat producing box, by each heat producing box
Setting the adjustable air-valve 20 for carrying out air quantity adjusting, the air quantity that is, multiple heat producing box pass through is roughly the same to achieve the purpose that equal wind.
If necessary, adjustable air-valve 20 can also be closed, to prevent idle air from passing through heat producing box.
The heat taking and exchanging device further includes fin, and the heat exchanger tube is arranged on the fin, the defrosting heating tube 22
It is also disposed on the fin.
The outer framework 16 is equipped with the spray system for being used for spraying 17 outer surface of heat taking and exchanging device, the spray system
System includes nozzle 21 and the spray tube being connected with the nozzle 21, and the spray tube is used for being connected with watering.
Spray system can prevent the booty in idle air from concentrating at the surface of heat taking and exchanging device 17, by detect heat producing box into
Wind side and the pressure difference of air side, when pressure difference is higher than setting value, starts spray system and are sprayed, so as to remove heat taking and exchanging device
The booty on 17 surfaces, keeps heat producing box surface clean.
Separate unit heat producing box in the present invention can be achieved twin-stage even multistage and take heat, and idle air takes heat big, realizes deep enthalpy
Take heat；The built-in defrosting heating tube 22 of heat producing box heat exchanger, has achieveed the purpose that heat producing box defrosts；Heat producing box water-collecting tray is provided with
Winterization system, solves the problems, such as the antifreeze of water-collecting tray.
Idle air heat producing box in the present invention has the characteristics that：(1) heat producing box can realize that twin-stage even multistage takes heat, make
Idle air takes the temperature after heat to reduce step by step, is down to subzero；(2) idle air heat producing box can realize automatic defrosting；(3) defrost with
Afterwards, frost becomes water, flows into water-collecting tray, and water-collecting tray itself is equipped with defroster, will not be freezing.
As shown in fig. 7, the heat pump unit in the present invention sets at least to level-one, every grade of heat pump unit includes evaporation
Device, compressor, condenser and expansion valve, are each connected in series between the cooling water pipeline of the condenser by communicating pipe 14,
The evaporator is used to exchange heat with flowing through the anti-icing fluid after heat producing box 1, and the condenser is used to be changed with user's hot water
Heat.Connected between heat producing box and evaporator by antifreeze liquid pipe 2, anti-icing fluid is by the antifreeze liquid pipe 2 in heat producing box and evaporation
Reciprocation cycle between device.
In present embodiment, two-stage heat pump unit, respectively level-one heat pump unit and two level heat pump unit, institute are set
Stating level-one heat pump unit includes level-one evaporator 3, stage compressor 4, first-stage condenser 5 and one-stage expansion valve 6, the two level heat
Pump assembly includes secondary evaporimeter 7, split-compressor 9, secondary condenser 10 and compound expansion valve 8, evaporator, compressor, cold
Connection mode between condenser and expansion valve is the prior art, and it will not be described here.
First-stage condenser 5 is with the mode that secondary condenser 10 is connected：Cooling water is equipped with I and II condenser 5,10
Pipeline, the outlet of 10 cooling water pipeline of secondary condenser and the entrance of 5 cooling water pipeline of first-stage condenser are connected by communicating pipe 14
Connect.The entrance 12 of user's hot water from 10 cooling water pipe of secondary condenser enters, cold through secondary condenser 10, communicating pipe 14, level-one
Flowed out after condenser 5 from the outlet 13 of 5 cooling water pipe of first-stage condenser, the hot water of outflow returns to user.
The anti-icing fluid of level-one evaporator 3 is flowed through when flowing through heat producing box 1, positioned at the upstream of idle air flow direction；Flow through two level steaming
The anti-icing fluid of device 7 is sent out when flowing through heat producing box 1, positioned at the downstream of idle air flow direction, step is completed and takes heat.Hot water used by a user
First pass through secondary condenser 10 to exchange heat, water temperature rises to 45 DEG C by 40 DEG C, and then 45 DEG C of hot water passes through first-stage condenser again
5, water temperature rises to 50 DEG C by 45 DEG C, completes the step heating of user's hot water.
As shown in figure 8, and with reference to shown in Fig. 9 and Figure 10, present invention additionally comprises second base 11, in the second base 11
It is provided with the heat pump unit.
Condenser in every grade of heat pump unit is fixed in the second base 11, the top of the condenser
Equipped with the evaporator, the pipeline connected between the condenser and evaporator is equipped with the expansion valve, the evaporator
Top is equipped with the compressor.The condenser is disposed side by side in the second base 11.
The present invention sets at least level-one heat pump unit, and the cooling water pipeline of the condenser in every grade of heat pump unit passes through connection
Pipe 14 is connected in series, and is illustrated exemplified by setting two-stage heat pump unit, and two heat pump units of A, B are combined, and make one
Platform unit, while the condenser in two heat pump units of A, B realizes series connection, the i.e. hot water after the heating of heat pump unit B condensers
Enter back into heat pump unit A condensers to heat again, realize that step heats, it is assumed that heat pump unit B condenser water temperatures are by 40 DEG C of heatings
To 45 DEG C, enter back into heat pump unit A condensers and realize that water temperature is warming up to 50 DEG C by 45 DEG C, the condensation temperature of such heat pump unit B
Degree can be designed as 48 DEG C, and the condensation temperature of heat pump unit A can be designed as 53 DEG C, in this way,
Theoretical COPA=(273+53)/[(273+53)-(273-13)]=4.94
Theoretical COPB=(273+48)/[(273+48)-(273-20)]=4.72
Two heat pump units are averaged COP=(COPA+COPB)/2=4.83
As it can be seen that the present invention can improve the synthesis COP values of whole system, that is, improve the efficiency of system.At the same time so
The condensation temperature of heat pump unit B is reduced, optimizes the operating condition of unit, improves the stability of unit.
As shown in figure 3, and with reference to shown in Fig. 4, build an idle air in coal mine return air retention tower mouth and take hot cell, idle air takes hot cell
Side arrangement idle air heat producing box, circulatory mediator is using anti-icing fluid such as ethylene glycol.Low-temperature antifreeze liquid enters idle air heat producing box heat exchanger tube
Interior, idle air is flowed through outside idle air heat producing box Tube Sheet of Heat Exchanger, is replaced heat in idle air into anti-icing fluid, anti-icing fluid temperature liter by exchanging heat
Height, enters (water source) heat pump unit, heat pump unit is extracted in anti-icing fluid after heat, and anti-icing fluid temperature reduces, and becomes by circulating pump
For low-temperature antifreeze liquid, low temperature is antifreeze to be again introduced into idle air heat producing box, completes whole circulation.
Advantages of the present invention is as follows：
1st, idle air takes difference in enthalpy big, it is possible to achieve twin-stage takes heat, and idle air takes after heat temperature to reach -10 DEG C, even lower；
2nd, simple system, the idle air waste heat recovery thermal efficiency are high；
3rd, using enclosed anti-icing fluid circulate, water consumption is small, while anti-icing fluid is not mixed into foul, on unit durability influence compared with
It is small, while blockage problem is not present, reliability is high, and maintenance is small；
4th, anti-icing fluid circulation use circulating pump, heat pump computer room and idle air take hot cell between relative position it is more flexible, from
Heat producing box and idle air heat pump unit spacing and height difference restricted problem；
5th, unit can use water source heat pump units, and technology maturation is reliable and stable；
6th, connecting pipe can share between heat producing box and idle air heat pump, compared with direct steaming type idle air heat pump, reduce pipe
Road quantity, system is simpler, reduces investment.
Embodiment described above is only that the preferred embodiment of the present invention is described, not to the model of the present invention
Enclose and be defined, on the premise of design spirit of the present invention is not departed from, technical side of the those of ordinary skill in the art to the present invention
The various modifications and improvement that case is made, should all fall into the protection domain that claims of the present invention determines.
Claims (10)
1. a kind of direct-cooling type depth enthalpy takes hot idle air heat pump system, it is characterised in that：Hot cell is taken including idle air, the idle air takes hot cell
At least one idle air heat producing box is equipped with, the idle air heat producing box is connected by antifreeze liquid pipeline with the evaporator of heat pump unit,
The antifreeze liquid pipeline is used to flow through anti-icing fluid, circulating pump is provided with the antifreeze liquid pipeline, the anti-icing fluid flows through idle air
During heat producing box absorb idle air in heat, when the anti-icing fluid flows through the evaporator by the heat in the idle air of absorption change to
Refrigerant in heat pump unit, the condenser in the heat pump unit are used to exchange heat with user's hot water.
2. direct-cooling type depth enthalpy according to claim 1 takes hot idle air heat pump system, it is characterised in that：The idle air heat producing box
Including first base and the outer framework being fixed in the first base, at least level-one is installed along idle air in the outer framework
Flow through the heat taking and exchanging device of direction arrangement, the lower part and top of every grade of heat taking and exchanging device, which are respectively equipped with, to be taken hot working fluid import and take heat
Sender property outlet, it is described take hot working fluid import and it is described take hot working fluid outlet connect the antifreeze liquid pipeline, the heat pump machine respectively
Group is arranged at least level-one, and the heat pump unit is corresponded with the heat taking and exchanging device and arranged, in every grade of heat pump unit
It is connected in series between the cooling water pipeline of condenser by communicating pipe.
3. direct-cooling type depth enthalpy according to claim 2 takes hot idle air heat pump system, it is characterised in that：Heat is taken to change described in every grade
Defrosting heating tube is equipped between the heat exchanger tube of hot device, the defrosting heating tube is used for the hydrothermal solution that circulates.
4. direct-cooling type depth enthalpy according to claim 3 takes hot idle air heat pump system, it is characterised in that：Set on the outer framework
It is useful for adjusting the adjustable air-valve of idle air flow.
5. direct-cooling type depth enthalpy according to claim 4 takes hot idle air heat pump system, it is characterised in that：The heat taking and exchanging device
Fin is further included, the heat exchanger tube is arranged on the fin, and the defrosting heating tube is also disposed on the fin.
6. direct-cooling type depth enthalpy according to claim 5 takes hot idle air heat pump system, it is characterised in that：Set on the outer framework
It is useful for spraying the spray system of the heat taking and exchanging device outer surface, the spray system includes nozzle and connects with the nozzle
The spray tube connect, the spray tube are used for being connected with watering.
7. hot idle air heat pump system is taken according to claim 1-6 any one of them direct-cooling type depth enthalpys, it is characterised in that：It is described anti-
Jelly liquid is ethylene glycol.
8. direct-cooling type depth enthalpy according to claim 7 takes hot idle air heat pump system, it is characterised in that：Further include the second bottom
, it is provided with the heat pump unit in the second base.
9. direct-cooling type depth enthalpy according to claim 8 takes hot idle air heat pump system, it is characterised in that：Every grade of heat pump machine
Condenser in group is fixed in the second base, and the top of the condenser is equipped with the evaporator, the condensation
The pipeline connected between device and the evaporator is equipped with expansion valve, and the top of the evaporator is equipped with compressor.
10. direct-cooling type depth enthalpy according to claim 9 takes hot idle air heat pump system, it is characterised in that：The condenser is simultaneously
Row is arranged in the second base.
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| Application Number | Priority Date | Filing Date | Title |
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| CN202410373025.XA CN118066737A (en) | 2017-12-25 | 2017-12-25 | Partition heat pump system and heat box |
| CN201711422521.6A CN107940805A (en) | 2017-12-25 | 2017-12-25 | Direct-cooling type depth enthalpy takes hot idle air heat pump system |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201711422521.6A CN107940805A (en) | 2017-12-25 | 2017-12-25 | Direct-cooling type depth enthalpy takes hot idle air heat pump system |
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| Application Number | Title | Priority Date | Filing Date |
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| CN202410373025.XA Division CN118066737A (en) | 2017-12-25 | 2017-12-25 | Partition heat pump system and heat box |
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| CN107940805A true CN107940805A (en) | 2018-04-20 |
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| CN201711422521.6A Pending CN107940805A (en) | 2017-12-25 | 2017-12-25 | Direct-cooling type depth enthalpy takes hot idle air heat pump system |
| CN202410373025.XA Pending CN118066737A (en) | 2017-12-25 | 2017-12-25 | Partition heat pump system and heat box |
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Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108709332A (en) * | 2018-07-14 | 2018-10-26 | 侴雨宏 | The big Wen Sheng of antifreezing agent multipaths takes hot air draft source vapor cascade heat pump |
| CN110081747A (en) * | 2018-09-25 | 2019-08-02 | 北京中矿赛力贝特节能科技有限公司 | The residual neat recovering system that a kind of mine return air heat pipe and ethylene glycol combine |
| CN111102869A (en) * | 2019-12-31 | 2020-05-05 | 北京中矿博能节能科技有限公司 | Ventilation air methane heat-taking platform |
| CN111578354A (en) * | 2020-06-17 | 2020-08-25 | 卡林热泵技术有限公司 | Heating system of mining parallel compression type step ventilation air methane heat pump |
| CN112503613A (en) * | 2019-09-16 | 2021-03-16 | 卡林热泵技术有限公司 | Modular gradient heat-taking ventilation air heat pump unit |
| CN112524717A (en) * | 2020-11-20 | 2021-03-19 | 武汉万居隆电器有限公司 | Internally-switched large-scale screw type water-ground source heat pump unit |
| CN114322345A (en) * | 2020-11-30 | 2022-04-12 | 华为数字能源技术有限公司 | Heat dissipation system, heat management equipment and working method of heat dissipation system |
Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201037719Y (en) * | 2007-05-25 | 2008-03-19 | 清华大学 | Hot-water heat pump set for gradual increasing water temperature |
| CN101210761A (en) * | 2007-12-25 | 2008-07-02 | 美的集团电冰箱制造（合肥）有限公司 | Refrigerator defrosting heater and controlling method thereof |
| CN102494442A (en) * | 2011-12-08 | 2012-06-13 | 北京矿大节能科技有限公司 | Direct expansion type mine return air source heat pump system and operation method thereof |
| WO2012152199A1 (en) * | 2011-05-06 | 2012-11-15 | Rong Guohua | Air conditioning unit for heat recovery from heat pump |
| CN203629140U (en) * | 2013-11-26 | 2014-06-04 | 北京中矿博能节能科技有限公司 | Heat pump device for providing hot water with large temperature difference through gradient utilization of ventilation air methane heat energy |
| CN104677181A (en) * | 2013-11-26 | 2015-06-03 | 北京中矿博能节能科技有限公司 | Ventilation air methane heat exchange device having automatic cleaning device |
| CN105464694A (en) * | 2016-01-05 | 2016-04-06 | 北京矿大节能科技有限公司 | Energy-saving type mine air return indirect heat exchanger and heat exchange device |
| CN105486104A (en) * | 2016-01-05 | 2016-04-13 | 北京矿大节能科技有限公司 | Mine return air heat energy gradient utilization system and operation mode thereof |
| CN207797456U (en) * | 2017-12-25 | 2018-08-31 | 北京中矿博能节能科技有限公司 | Direct-cooling type depth enthalpy takes hot idle air heat pump system |
-
2017
- 2017-12-25 CN CN201711422521.6A patent/CN107940805A/en active Pending
- 2017-12-25 CN CN202410373025.XA patent/CN118066737A/en active Pending
Patent Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201037719Y (en) * | 2007-05-25 | 2008-03-19 | 清华大学 | Hot-water heat pump set for gradual increasing water temperature |
| CN101210761A (en) * | 2007-12-25 | 2008-07-02 | 美的集团电冰箱制造（合肥）有限公司 | Refrigerator defrosting heater and controlling method thereof |
| WO2012152199A1 (en) * | 2011-05-06 | 2012-11-15 | Rong Guohua | Air conditioning unit for heat recovery from heat pump |
| CN102494442A (en) * | 2011-12-08 | 2012-06-13 | 北京矿大节能科技有限公司 | Direct expansion type mine return air source heat pump system and operation method thereof |
| CN203629140U (en) * | 2013-11-26 | 2014-06-04 | 北京中矿博能节能科技有限公司 | Heat pump device for providing hot water with large temperature difference through gradient utilization of ventilation air methane heat energy |
| CN104677181A (en) * | 2013-11-26 | 2015-06-03 | 北京中矿博能节能科技有限公司 | Ventilation air methane heat exchange device having automatic cleaning device |
| CN105464694A (en) * | 2016-01-05 | 2016-04-06 | 北京矿大节能科技有限公司 | Energy-saving type mine air return indirect heat exchanger and heat exchange device |
| CN105486104A (en) * | 2016-01-05 | 2016-04-13 | 北京矿大节能科技有限公司 | Mine return air heat energy gradient utilization system and operation mode thereof |
| CN207797456U (en) * | 2017-12-25 | 2018-08-31 | 北京中矿博能节能科技有限公司 | Direct-cooling type depth enthalpy takes hot idle air heat pump system |
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108709332A (en) * | 2018-07-14 | 2018-10-26 | 侴雨宏 | The big Wen Sheng of antifreezing agent multipaths takes hot air draft source vapor cascade heat pump |
| CN110081747A (en) * | 2018-09-25 | 2019-08-02 | 北京中矿赛力贝特节能科技有限公司 | The residual neat recovering system that a kind of mine return air heat pipe and ethylene glycol combine |
| CN112503613A (en) * | 2019-09-16 | 2021-03-16 | 卡林热泵技术有限公司 | Modular gradient heat-taking ventilation air heat pump unit |
| CN111102869A (en) * | 2019-12-31 | 2020-05-05 | 北京中矿博能节能科技有限公司 | Ventilation air methane heat-taking platform |
| CN111578354A (en) * | 2020-06-17 | 2020-08-25 | 卡林热泵技术有限公司 | Heating system of mining parallel compression type step ventilation air methane heat pump |
| CN112524717A (en) * | 2020-11-20 | 2021-03-19 | 武汉万居隆电器有限公司 | Internally-switched large-scale screw type water-ground source heat pump unit |
| CN112524717B (en) * | 2020-11-20 | 2022-04-12 | 武汉万居隆电器有限公司 | Internally-switched large-scale screw type water-ground source heat pump unit |
| CN114322345A (en) * | 2020-11-30 | 2022-04-12 | 华为数字能源技术有限公司 | Heat dissipation system, heat management equipment and working method of heat dissipation system |
| WO2022110745A1 (en) * | 2020-11-30 | 2022-06-02 | 华为数字能源技术有限公司 | Heat dissipation system, heat management apparatus, and working method thereof |
| CN114322345B (en) * | 2020-11-30 | 2022-11-11 | 华为数字能源技术有限公司 | Heat dissipation system, heat management equipment and working method of heat dissipation system |
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