CN208282449U - Integrated Energy recycling system - Google Patents
Integrated Energy recycling system Download PDFInfo
- Publication number
- CN208282449U CN208282449U CN201820931900.1U CN201820931900U CN208282449U CN 208282449 U CN208282449 U CN 208282449U CN 201820931900 U CN201820931900 U CN 201820931900U CN 208282449 U CN208282449 U CN 208282449U
- Authority
- CN
- China
- Prior art keywords
- heat
- energy
- plate
- cold
- accumulation
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 238000004064 recycling Methods 0.000 title claims abstract description 14
- 238000012546 transfer Methods 0.000 claims abstract description 48
- 239000002918 waste heat Substances 0.000 claims abstract description 29
- 230000010354 integration Effects 0.000 claims abstract description 12
- 238000011084 recovery Methods 0.000 claims abstract description 10
- 238000009825 accumulation Methods 0.000 claims description 52
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 38
- 239000004065 semiconductor Substances 0.000 claims description 27
- 230000017525 heat dissipation Effects 0.000 claims description 23
- 238000001816 cooling Methods 0.000 claims description 16
- 239000000872 buffer Substances 0.000 claims description 11
- 230000005611 electricity Effects 0.000 claims description 11
- 238000010521 absorption reaction Methods 0.000 claims description 9
- 230000005855 radiation Effects 0.000 claims description 9
- 239000012530 fluid Substances 0.000 claims description 7
- 230000008676 import Effects 0.000 claims description 7
- 230000003139 buffering effect Effects 0.000 claims description 5
- 230000003321 amplification Effects 0.000 abstract description 4
- 238000003199 nucleic acid amplification method Methods 0.000 abstract description 4
- 230000008901 benefit Effects 0.000 abstract description 3
- 239000003344 environmental pollutant Substances 0.000 abstract description 2
- 238000009434 installation Methods 0.000 abstract description 2
- 231100000719 pollutant Toxicity 0.000 abstract description 2
- 230000000694 effects Effects 0.000 description 9
- 238000010438 heat treatment Methods 0.000 description 9
- 238000005057 refrigeration Methods 0.000 description 9
- 241000196324 Embryophyta Species 0.000 description 8
- 238000003860 storage Methods 0.000 description 8
- 239000007789 gas Substances 0.000 description 7
- 239000000463 material Substances 0.000 description 7
- 230000005540 biological transmission Effects 0.000 description 6
- 238000010586 diagram Methods 0.000 description 4
- 241000209140 Triticum Species 0.000 description 3
- 235000021307 Triticum Nutrition 0.000 description 3
- 230000008859 change Effects 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 239000000498 cooling water Substances 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 235000013312 flour Nutrition 0.000 description 3
- 150000002500 ions Chemical group 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 230000001105 regulatory effect Effects 0.000 description 3
- 230000009466 transformation Effects 0.000 description 3
- 229910001289 Manganese-zinc ferrite Inorganic materials 0.000 description 2
- 229910017629 Sb2Te3 Inorganic materials 0.000 description 2
- JIYIUPFAJUGHNL-UHFFFAOYSA-N [O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[Mn++].[Mn++].[Mn++].[Fe+3].[Fe+3].[Fe+3].[Fe+3].[Fe+3].[Fe+3].[Fe+3].[Fe+3].[Fe+3].[Fe+3].[Zn++].[Zn++] Chemical compound [O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[Mn++].[Mn++].[Mn++].[Fe+3].[Fe+3].[Fe+3].[Fe+3].[Fe+3].[Fe+3].[Fe+3].[Fe+3].[Fe+3].[Fe+3].[Zn++].[Zn++] JIYIUPFAJUGHNL-UHFFFAOYSA-N 0.000 description 2
- 229910045601 alloy Inorganic materials 0.000 description 2
- 239000000956 alloy Substances 0.000 description 2
- 229910052797 bismuth Inorganic materials 0.000 description 2
- JCXGWMGPZLAOME-UHFFFAOYSA-N bismuth atom Chemical compound [Bi] JCXGWMGPZLAOME-UHFFFAOYSA-N 0.000 description 2
- 238000009833 condensation Methods 0.000 description 2
- 230000005494 condensation Effects 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 230000008020 evaporation Effects 0.000 description 2
- 238000009776 industrial production Methods 0.000 description 2
- 230000033001 locomotion Effects 0.000 description 2
- 239000011159 matrix material Substances 0.000 description 2
- 239000007769 metal material Substances 0.000 description 2
- 230000006855 networking Effects 0.000 description 2
- 239000006104 solid solution Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- XSOKHXFFCGXDJZ-UHFFFAOYSA-N telluride(2-) Chemical compound [Te-2] XSOKHXFFCGXDJZ-UHFFFAOYSA-N 0.000 description 2
- 238000010792 warming Methods 0.000 description 2
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 1
- 238000003723 Smelting Methods 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 229910001423 beryllium ion Inorganic materials 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 238000004939 coking Methods 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 230000002045 lasting effect Effects 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
- 230000005619 thermoelectricity Effects 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
- 238000009423 ventilation Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E10/00—Energy generation through renewable energy sources
- Y02E10/40—Solar thermal energy, e.g. solar towers
Landscapes
- Photovoltaic Devices (AREA)
Abstract
The utility model discloses a kind of Integrated Energy recycling systems, including cold-heat-exchanging exchange system, energy integration device, new ionic charge cold-heat-exchanging exchange system, waste heat of plant recovery pipe, wherein energy integration device, new ionic charge cold-heat-exchanging exchange system, waste heat of plant recovery pipe distinguish connection cold-heat-exchanging exchange system, and the cold-heat-exchanging exchange system sends the heat collection of energy integrating device, new ionic charge cold-heat-exchanging exchange system, engineering waste heat pipeline outside；Heat-transfer working medium used in above-mentioned each device is all made of R401A.The system can effectively be recycled environment, air and solar energy and waste heat of plant etc., then uniformly put together to amplify again the energy of amplification is then converted into heat, then heat-exchanger rig be recycled to carry out heat to send utilization outside.Advantage mountable, without any pollutant emission in, convenient transportation small with occupied area, easy for installation, outdoor and computer room.
Description
Technical field
The invention belongs to comprehensive utilization of energy fields, and specifically one kind can be collected effectively and be produced in nature and industrial production
Raw waste heat, and then the system being used.
Background technique
Current solar energy equipment mostly uses water to run as working medium, and can only work by day, and does not have at night
There is sunlight that can not work, heating efficiency is lower.
Meanwhile component cooling water, especially thermoelectricity, smelting, coking, petrochemical industry, coal used in the interior production of industry at present
The industrial productions such as chemical industry, chemical industry, light industry are equipped its internal recirculated cooling water and are substantially all by cooling tower, water-cooling tower, air cooler
Cooling processing is carried out, there are disadvantage is exactly one, the cooling water opening area that needs to cool down is big, moisture evaporation is high, water resource waste
Seriously need not stop to supplement a large amount of external water resource (underground water etc.).Two, cooling system loss electric energy is big, maintenance period is short,
Especially summer, cooling effect obviously weaken, if recirculated water cannot get excellent cooling in factory, can all bring to whole production
Adverse effect.
Summary of the invention
The object of the invention is that providing a kind of Integrated Energy recycling for above-mentioned the problems of the prior art
Solar energy and waste heat of plant etc. can be carried out in active set, then uniformly put together and converted again by system, the system
The energy of amplification is then converted into heat by heat and mass, then heat-exchanger rig is recycled to carry out heat to send utilization outside.
Its technical solution is as follows: Integrated Energy recycling system, including cold-heat-exchanging exchange system, energy integration dress
It sets, new ionic charge cold-heat-exchanging exchange system, waste heat of plant recovery pipe, wherein energy integration device, the cold and hot friendship of new ionic charge
Changing device, waste heat of plant recovery pipe distinguish connection cold-heat-exchanging exchange system, and the cold-heat-exchanging exchange system is by energy integrating device, new
Ionic charge cold-heat-exchanging exchange system, engineering waste heat pipeline heat collection send outside；Heat-transfer working medium used in above-mentioned each device is all made of
R401A。
The energy integration device includes solar absorption circuit and residual heat collection circuit, the solar absorption circuit packet
Include solar heat radiation evaporative condenser, sheet string type natural induced draft evaporative condenser, waste heat stock buffer tank, backheat self compensation
Device；The residual heat collection circuit includes the enthalpy increasing heat pump being linked in sequence, high efficiency plate cool-heat-exchanger, buffers fluid reservoir, is more
Channel microgap heat-exchanger rig；Wherein waste heat stock buffer tank connection backheat self-compensating device, the backheat self-compensating device with
The multichannel microgap heat-exchanger rig connection；It is cold that the sheet string type natural induced draft evaporative condenser is located at solar radiation evaporation
Above condenser.
Solar heat radiation evaporative condenser and sheet string type natural induced draft evaporative condenser are simultaneously connected to system, above-mentioned
Solar heat radiates evaporative condenser when daytime is sunny, solar energy is absorbed as evaporator, after absorbing solar energy
Working medium enter waste heat stock buffer tank, then enter enthalpy increasing heat pump；When there is no sunlight at night, the solar heat spoke
Evaporative condenser is penetrated as condenser to radiate outward, around hot-air move upwards naturally, thus by the sheet string type above it
The heat of the recycling of natural induced draft evaporative condenser, the recycling of natural induced draft evaporative condenser brings waste heat stock buffer by working medium again
Tank.A part of high temperature and high pressure gas a part of enthalpy increasing heat pump discharge enters backheat self compensation by multichannel microgap heat-exchanger rig
Device, is condensed and is liquefied, and multichannel microgap heat-exchanger rig is then returned to, this be improve the inlet pressure of heat pump with
Temperature prevents the generation of liquid hammer, second is that carrying out more effectively cooling condensation to the discharge gas of high temperature and pressure again, plays more
Good condensation effect.
The new ionic charge cold-heat-exchanging exchange system, it includes plasma power supply, electric power core heat transfer piece, heat exchanger plates, storage
Plate can be laid in, the plasma power supply converts alternating current to direct current and supplies electricity to electric power core heat transfer piece offer working power, electric power
Core heat transfer piece is semiconductor chilling plate, and after electric power core heat transfer piece, electric power core heat transfer piece converts electrical energy into electric current
Thermal energy discharges heat to plate face two sides or absorbs heat, and connection heat exchanger plates are in close contact on the upside of electric power core heat transfer piece, and downside is tight
Plate is laid in close contact connectio accumulation of energy, and the heat exchanger plates are provided with water inlet, water outlet, heat exchanging chamber, and heat transferring medium passes through water inlet
It after mouth enters heat exchanging chamber heat exchange, is flowed out from water outlet, plate is laid in accumulation of energy and electric power core heat transfer piece downside exchanges heat, and is stored
Thermal energy or cold energy.
The device further includes preheating table, and preheating table plate face is in close contact connection plasma power supply shell, and preheating table is ion
Power supply cooling heat absorption, the preheating table are provided with the import being sequentially communicated, circulating water pipe, outlet, and outlet is controlled by valve
It is connected to the water inlet of heat exchanger plates, import is connected to water source.
The contact of the heat exchanger plates and electric power core heat transfer piece contact component, accumulation of energy deposit plate and electric power core heat transfer piece
The contact component of component, preheating table and ion power supply shell is the metal material of good heat conductivity, preferably T2.
The heat exchanger plates, the accumulation of energy deposit non-heat transfer/heat exchanging part of plate are provided with insulating, i.e., except transmission of heat by contact
Face, other faces are provided with insulating, guarantee the heat exchange efficiency of heat exchanging part.
The amount of heat exchanger plates be one piece or more, be sequentially connected in series, it is concatenated to be defined as, heat transferring medium be sequentially connected in series by
The heat exchanging chamber of heat exchanger plates exchanges heat.
After the electric power core heat transfer piece uses semiconductor chilling plate, electric current to pass through, one end wheat flour heat of cooling piece, separately
One end wheat flour is cold, and when the galvanic couple that ion-conductance is connected by two kinds of different semiconductor materials, internal charge starts to do height mutually
Frequency movement simultaneously can absorb heat and release heat at the both ends of galvanic couple respectively, and the purpose of cooling and warming, material can be realized
Material is the ternary solid solution alloy using bismuth telluride as matrix, and wherein p-type is Bi2Te3-Sb2Te3, and N-type is Bi2Te3-
Bi2Se3。
High temperature heat transferring medium can be used for heating, high temperature water；Low-temperature heat exchange medium can be used for refrigeration system.
The heat exchanging chamber of the heat exchanger plates include T2 material contact plate and with contact plate thermal column connected vertically, heat dissipation
Column is evenly arranged in heat exchanging chamber, and to increase heat exchange area, contact plate and electric power core heat transfer piece upper surface, which are in close contact, to be connected.
The described accumulation of energy deposit plate includes high wing T2, heat dissipation cavity, heat release hole, air blower, high wing T2 include heat accumulation plate and with
The fin that heat accumulation plate is vertically fixedly connected, fin multiple groups are arranged in parallel, and uniformly distributed multi-group vacuum lumen is provided in heat accumulation plate, use
With accumulation of energy, the avris shell of fin and accumulation of energy deposit plate is provided with heat release hole, and the heat release hole setting of multiple fins is straight in same
Heat dissipation channel is constituted on line, heat dissipation channel is vertical with fin, and heat dissipation channel is that multiple groups are arranged in same level, and air blower is set
It sets and lays in plate lower end in accumulation of energy, outside air introduces heat dissipation cavity by air blower, by heat dissipation channel by the air after heat exchange from storage
The discharge of two avris of plate can be laid in.
The electric power core heat transfer piece further include with semiconductor chilling plate semiconductor temperature differential power generating sheet disposed in parallel, i.e.,
In upside heat exchanger plates and downside accumulation of energy deposit plate contact surface, semiconductor chilling plate and semiconductor temperature differential power generating sheet respectively account for part face
Product, semiconductor chilling plate are connect with plasma power supply, and semiconductor temperature differential power generating sheet is connect with battery, and battery is to supply this
The electricity consumption of device part.
The working principle of the new ionic charge cold-heat-exchanging exchange system are as follows:
Plasma power supply exports normal power supplies 220V/380V transformation for operating current needed for electric power core heat transfer piece,
So that the heating of electric power core heat transfer piece or refrigeration, in the specific implementation, by the output positive and negative anodes for converting plasma power supply
Realize the conversion of heating and refrigeration；
Electric power core heat transfer piece work when, with heat exchanger plates and accumulation of energy deposit plate exchange heat simultaneously, heat exchanger plates will with flow through
The heat transferring medium of its heat exchanging chamber exchanges heat, and accumulation of energy deposit plate absorbs storage energy, excessive heat meeting as storage device
The mode for opening air blower is shed by heat dissipation cavity；
Preheating table effect one, the preheated plate of room temperature heat transferring medium such as water flow then can be to the plasma electric that it is connected
Source carries out heat exchange cooling, and when plasma power supply works, can shed amount of heat, carries out walking guide heat by preheating table, solves electricity
The heat dissipation problem in source；The effect two of preheating table simultaneously, heat transferring medium enter heat exchanger plates after preheating and exchange heat, and improve heat exchange
Efficiency, it is energy saving.
The plasma power supply includes three-phase/two-phase power supply transformer, three-phase bridge rectification of contactor, high leakage reactance
Device/two-phase bridge rectifier, manganese-zinc ferrite high frequency magnetic field coil, control circuit board, output port, shell and protection element
Deng.
The device further includes electrical control part, including controller, remote transmission module, data acquisition module, the part
Assembled using conventional existing capability technical parts, controller is connected by relay and air blower, plasma power supply, water valve
It connects, is acquired by temperature of the data acquisition module to output heat transferring medium, plasma electric is controlled by controller according to data
The working condition in source and then the purpose for realizing temperature control, remotely control for convenience of operator, can remote terminal (mobile phone, computer etc.
Intelligent networking device) by remote transmission module connection controller, realize the purpose of remote control.The device converts electrical energy into
Thermal energy or cold energy are exported, and can be assembled according to actual needs, it is pollution-free, without discharge, it is noiseless, it is easy to operate practical.
The waste heat of plant recovery pipe includes the water inlet pipe and return pipe with cold-heat-exchanging exchange system connection respectively, it is described into
Filter device and circulating pump is arranged in water pipe.
The present invention is respective by energy integration device, new ionic charge cold-heat-exchanging exchange system, waste heat of plant recovery pipe
For heat transmission to cold-heat-exchanging exchange system, this system is using electric energy as the first operation carrier, in conjunction with environment, air and the sun
Energy swap accumulation of heat, then uniformly put together a kind of working principle amplified again, the energy of amplification converted
At heat, then heat-exchanger rig is recycled to send heat outside, circuits sequentially output to reach required purpose.With land occupation face
Advantage mountable, without any pollutant emission in long-pending small, convenient transportation, easy for installation, outdoor and computer room.
Detailed description of the invention
In order to more clearly explain the embodiment of the invention or the technical proposal in the existing technology, to embodiment or will show below
There is attached drawing needed in technical description to be briefly described, it should be apparent that, the accompanying drawings in the following description is only this
Some embodiments of invention for those of ordinary skill in the art without creative efforts, can be with
It obtains other drawings based on these drawings.
Fig. 1 is the principle of the present invention structural schematic diagram.
The layout drawing of Fig. 2 solar heat radiation evaporative condenser and sheet string type natural induced draft evaporative condenser of the present invention.
Fig. 3 is the sectional view of sheet string type natural induced draft evaporative condenser of the present invention.
Fig. 4 is the structural schematic diagram of new ionic charge cold-heat-exchanging exchange system.
Fig. 5 is that plate structural schematic diagram is laid in the accumulation of energy of new ionic charge cold-heat-exchanging exchange system.
Fig. 6 is Fig. 5 schematic cross-sectional view.
Fig. 7 is new 2 structural schematic diagram of ionic charge cold-heat-exchanging exchange system embodiment.
Specific embodiment
The preferred embodiment of the present invention is described in detail with reference to the accompanying drawing, so that advantages and features of the invention energy
It is easier to be readily appreciated by one skilled in the art, so as to make a clearer definition of the protection scope of the present invention.
As shown in Figure 1, the present invention includes cold-heat-exchanging exchange system 1, energy integration device 2, the cold and hot exchange dress of new ionic charge
3, waste heat of plant recovery pipe 4 is set, wherein energy integration device 2, new ionic charge cold-heat-exchanging exchange system 3, waste heat of plant recycling
Pipeline 4 distinguishes connection cold-heat-exchanging exchange system 1, and cold-heat-exchanging exchange system 1 includes water inlet 11 and water outlet 12.The energy integration dress
Setting 2 includes solar absorption circuit 21 and residual heat collection circuit 22, and the solar absorption circuit 21 includes solar heat spoke
Penetrate evaporative condenser 211, sheet string type natural induced draft evaporative condenser 212, waste heat stock buffer tank 213, backheat self-compensating device
214；214 essence of backheat self-compensating device is also a heat-exchange device.The residual heat collection circuit 22 includes that sequence connects
Enthalpy increasing heat pump 221, high efficiency plate cool-heat-exchanger 222, the buffering fluid reservoir 223, multichannel microgap heat-exchanger rig 224 connect；
Wherein waste heat stock buffer tank 213 and backheat self-compensating device 214 and 224 connection of multichannel microgap heat-exchanger rig.
The sheet string type natural induced draft evaporative condenser 212 as shown in Figure 2 is located on solar radiation evaporative condenser 211
Side, in this way when not having sunlight at night, solar heat radiation evaporative condenser 211 radiates outward, around heat it is empty
Gas moves upwards naturally, to be recycled by sheet string type natural induced draft evaporative condenser 212.As shown in figure 3, sheet string type natural induced draft
The outside of the working medium passage 215 of evaporative condenser 212 is provided with fin 216.
Circulating pump 41 and filter device 42 are provided in waste heat of plant recovery pipe 4.
After enthalpy increasing heat pump 221 powers on, high temperature and high pressure gas is transported to high efficiency plate cool-heat-exchanger 222 and is passed
High temperature and high pressure gas after hot mass transfer, release heat enters buffering fluid reservoir 223, before entering, and there are also one to shunt more than warp
Heat utilization circuit 225 is entering the pipeline between multichannel microgap heat-exchanger rig 224 and heat pump import with low-temp low-pressure therein
Gas carries out heat and mass, and the condensate liquid of lower temperature enters buffering fluid reservoir 223, while also improving the intake air temperature of heat pump
And better condensed fluid has been obtained simultaneously and (wherein UTILIZATION OF VESIDUAL HEAT IN loop apparatus while pressure-equalizing pipe is set has prevented pressure difference pressure
Drop), the liquid of buffering fluid reservoir 223 enters regulating valve, it is multinomial to enter multichannel microgap heat-exchanger rig 224 by regulating valve and carry out
It shunts and the R410A of vaporization is transported to solar heat radiation evaporative condenser 211 and sheet string type with heat and mass, converted valve
It is slow that the low temperature low pressure gas that natural induced draft evaporative condenser 212 carries out after the abundant release of cold energy, release enters back into waste heat deposit
Tank 213 is rushed, buffered and is shunted, wherein also enter backheat self-compensating device 214, the present apparatus is sharp simultaneously using unit waste heat
With the heat and mass of multichannel microgap heat-exchanger rig, come the temperature and pressure of adjusting heat pump low-temp low-pressure R410A, guarantees heat pump
It can continue efficiently to work, when the efficient operating condition of heat pump is not achieved in external environment, by waste heat stock buffer tank 213, return
Hot self-compensating device 214, multichannel microgap heat-exchanger rig 224, residual heat collection circuit 22 etc. are completed jointly, by cold and hot conversion
Direct-through valve put down it is horizontal adjust, such heat pump is just also able to maintain a kind of efficient working condition under rugged environment at last.
The inherently a kind of free energy in residual heat collection circuit 22, by residual heat collection it is latter be ensure the normal operating temperature of unit,
Second is that providing a kind of energy that can be utilized to whole device again, has reached and save the purpose that efficiency improves work quality.
Solar heat radiates evaporative condenser 211 and does not use forced ventilation, but the efficient and rational heat exchange side passed through
Cold energy is taken away, has saved electric energy to whole device again due to carrying out air blast without using blower by formula, while also improving work effect
Rate.
Sheet string type natural induced draft evaporative condenser 212 is to be increased heat exchange area using the heat transfer form of string piece, due to changing
Heat area, which increases, has saved device space, he and waste heat stock buffer tank etc. again and has been used cooperatively, more the stabilization work of guarantee heat pump
Make.
The new ionic charge cold-heat-exchanging exchange system include plasma power supply 51, electric power core heat transfer piece 52, heat exchanger plates 53,
Plate 54 is laid in accumulation of energy, and the plasma power supply 51 converts alternating current to direct current and supplies electricity to the offer work electricity of electric power core heat transfer piece 52
Source, electric power core heat transfer piece 52 are semiconductor chilling plate, and for electric current after electric power core heat transfer piece, electric power core heat transfer piece 52 will
Electric energy is converted into thermal energy and discharges heat to plate face two sides or absorb heat, is in close contact connection on the upside of electric power core heat transfer piece 52 and changes
Hot plate 53, downside are in close contact connection accumulation of energy and lay in plate 54, and the heat exchanger plates 53 are provided with water inlet 55, water outlet 56, change
Hot chamber flows out after heat transferring medium enters heat exchanging chamber heat exchange by water inlet 5 from water outlet 56, and plate 54 and electric power core are laid in accumulation of energy
It exchanges heat on the downside of heart heat transfer piece, and stores thermal energy or cold energy.
The device further includes preheating table 58, and 58 plate face of preheating table is in close contact connection 51 shell of plasma power supply, preheating table
58 be ion power supply cooling heat absorption, and the preheating table is provided with the import being sequentially communicated, circulating water pipe, outlet, and outlet passes through
Valve F3 control is connected to the water inlet 5 of heat exchanger plates, and import is connected to water source, when the embodiment carries out heating operation, valve
F1, F2 are closed, and F3 is opened, it is ensured that and water source first passes through preheating table 58 and flows into heat exchanger plates 3 again, and the preheating table 8 is two pieces of series connection,
The packet of plasma power supply 51 is clipped in the middle, the heat transfer effect of preheating table 8 is improved.
Contact component, accumulation of energy deposit plate 54 and the electric power core of the heat exchanger plates 53 and electric power core heat transfer piece 52 are conducted heat
The contact component of the contact component of part 2, preheating table 58 and ion power supply shell 1 is the metal material of good heat conductivity, preferably
T2。
The heat exchanger plates 53, the accumulation of energy deposit non-heat transfer/heat exchanging part of plate 4 are provided with insulating, i.e., except contact
Heat-transfer area, other faces are provided with insulating, guarantee the heat exchange efficiency of heat exchanging part.
53 quantity of heat exchanger plates, 52 size of electric power core heat transfer piece, the watt level of plasma power supply are according to reality
Demand is assembled, and the quantity of heat exchanger plates 3 is one piece or more, is sequentially connected in series, concatenated to be defined as, heat transferring medium be sequentially connected in series through
The heat exchanging chamber for crossing heat exchanger plates exchanges heat.
After the electric power core heat transfer piece 52 uses semiconductor chilling plate, electric current to pass through, one end wheat flour heat of cooling piece,
Other end refrigeration, when the galvanic couple that ion-conductance is connected by two kinds of different semiconductor materials, internal charge starts to do mutually
High-frequency motion simultaneously can absorb heat and release heat at the both ends of galvanic couple respectively, and the purpose of cooling and warming can be realized,
Material is the ternary solid solution alloy using bismuth telluride as matrix, and wherein p-type is Bi2Te3-Sb2Te3, and N-type is Bi2Te3-
Bi2Se3。
When the device is run using heating mode, output high temperature heat transferring medium can be used for heating, high temperature water；Refrigeration output
When, heat transferring medium can be used for refrigeration system.
The heat exchanging chamber of the heat exchanger plates 53 include T2 material contact plate and with contact plate thermal column connected vertically, dissipate
Plume is evenly arranged in heat exchanging chamber, and to increase heat exchange area, contact plate and electric power core heat transfer piece upper surface, which are in close contact, to be connected.
The accumulation of energy deposit plate 54 includes high wing T2, heat dissipation cavity 514, heat release hole 511, air blower 513, and high wing T2 includes
Heat accumulation plate 59 and the fin 512 being fixedly connected vertical with heat accumulation plate 59,512 multiple groups of fin are arranged in parallel, setting in heat accumulation plate 59
There is uniformly distributed multi-group vacuum lumen 510, to accumulation of energy, the avris shell of fin 512 and accumulation of energy deposit plate is provided with heat release hole 11,
The heat release hole setting of multiple fins constitutes heat dissipation channel on same straight line, and heat dissipation channel is vertical with fin 512, heat dissipation channel
It is arranged in same level for multiple groups, the setting of air blower 513 lays in plate lower end in accumulation of energy, and air blower, which introduces outside air, to be dissipated
Air after heat exchange is laid in 54 liang of avris discharges of plate from accumulation of energy by heat dissipation channel by hot chamber 514.
Plasma power supply flies the 500W low-temperature plasma high-voltage electricity of ozone devices Co., Ltd production using the double Long Tengs in Beijing
Source, frequency 5-20KHZ；Input voltage 220V, continuous work electric current 2.5A；Power amplification: IGBT power tube, 50A/600V-2
Only；Export high pressure: 10-40KVP-P.Plasma power supply exports normal power supplies 220V/380V transformation for electric power core heat transfer piece
Required operating current, so that the heating of electric power core heat transfer piece or refrigeration pass through transformation plasma power supply in the specific implementation
Heating and the conversion of refrigeration can be realized in output positive and negative anodes, and when the device is used for refrigeration mode, valve F1, F2 is open-minded, and F3 is closed
It closes, water source is directly entered heat exchanger plates, and preheating table walks other circulation waterway and cools down to plasma power supply；
Electric power core heat transfer piece work when, with heat exchanger plates and accumulation of energy deposit plate exchange heat simultaneously, heat exchanger plates will with flow through
The heat transferring medium of its heat exchanging chamber exchanges heat, and accumulation of energy deposit plate absorbs storage energy, excessive heat meeting as storage device
The mode for opening air blower is shed by heat dissipation cavity；
The effect of preheating table 58 one, the preheated plate of room temperature heat transferring medium such as water flow then can be to the plasma that it is connected
Power supply carries out heat exchange cooling, and when plasma power supply works, can shed amount of heat, carries out walking guide heat by preheating table, solves
The heat dissipation problem of power supply；The effect two of preheating table simultaneously, heat transferring medium enter heat exchanger plates after preheating and exchange heat, and raising is changed
The thermal efficiency, it is energy saving.
The plasma power supply includes three-phase/two-phase power supply transformer, three-phase bridge rectification of contactor, high leakage reactance
Device/two-phase bridge rectifier, manganese-zinc ferrite high frequency magnetic field coil, control circuit board, output port, shell and protection element
Deng.
The device further includes electrical control part, including controller, remote transmission module, data acquisition module, controller
Using KG317T three phase mains intelligent controller, the functional component of the electrical control part is using conventional existing capability technology department
Part, controller are connect by relay with air blower, plasma power supply, water valve, are situated between by data acquisition module to output heat exchange
Matter, accumulation of energy deposit plate temperature be acquired, according to data by controller control plasma power supply, air blower working condition into
And realize the purpose of temperature control, remotely controlled for convenience of operator, can remote terminal (intelligent networking devices such as mobile phone, computer) it is logical
Long-range transmission module connection controller is crossed, realizes the purpose of remote control.
Embodiment 2, as shown in Fig. 7, structure composition is same as Example 1, and distinctive points one, the device is only applied to make
Thermal output, the electric power core heat transfer piece further include with semiconductor chilling plate semiconductor temperature differential power generating sheet disposed in parallel, i.e.,
In upside heat exchanger plates 53 and downside accumulation of energy deposit 54 contact surface of plate, semiconductor chilling plate and semiconductor temperature differential power generating sheet respectively account for one
Half area, semiconductor chilling plate are connect with plasma power supply 51, and semiconductor temperature differential power generating sheet is connect with battery, and battery is used
To supply the device part electricity consumption, when electric power core heat transfer piece works, exchanges heat, change simultaneously with heat exchanger plates and accumulation of energy deposit plate
Hot plate will exchange heat with the heat transferring medium for flowing through its heat exchanging chamber, and accumulation of energy deposit plate absorbs storage energy as storage device,
The mode that excessive heat can open air blower is shed by heat dissipation cavity, when semiconductor chilling plate power-off, semiconductor temperature difference hair
Electric sector-meeting work, issues electricity a part to battery, part electricity generates heat in a manner of directly loading, persistently changes to heat exchanger plates
Heat, it is ensured that the lasting heat exchange of exchange heat pipe in the short time.
Two accumulation of energy of distinctive points is laid in the design of 54 length dimension of plate and is lengthened, and preheating table 58 is arranged in 51 upside of plasma power supply,
51 downside of plasma power supply is in close contact with accumulation of energy deposit plate 54 and connects, and rationally using heat exchange resource, lays in plate 54 by accumulation of energy
Cool down to plasma power supply 51, increases the accumulation of energy and heat-sinking capability for improving accumulation of energy deposit plate.
The present invention, which couples, can be set as needed switching valve and regulating valve on the pipeline of each device, to adjust work in pipeline
The flow direction and flow of matter.
It should be pointed out that the above description is merely a specific embodiment, the above-mentioned technology contents that do not address are equal
It can be used or use for reference the prior art, scope of protection of the present invention is not limited thereto, any to expect without creative work
Change or replacement should be covered by the protection scope of the present invention.
Claims (6)
1. Integrated Energy recycling system, including the cold and hot exchange dress of cold-heat-exchanging exchange system, energy integration device, new ionic charge
It sets, waste heat of plant recovery pipe, wherein energy integration device, new ionic charge cold-heat-exchanging exchange system, waste heat of plant recovery pipe
Respectively connection cold-heat-exchanging exchange system, the cold-heat-exchanging exchange system by energy integrating device, new ionic charge cold-heat-exchanging exchange system,
The heat collection of engineering waste heat pipeline is sent outside；Heat-transfer working medium used in above-mentioned each device is all made of R401A.
2. Integrated Energy recycling system according to claim 1, it is characterised in that: the energy integration device includes
Solar absorption circuit and residual heat collection circuit, the solar absorption circuit include solar heat radiation evaporative condenser,
Sheet string type natural induced draft evaporative condenser, waste heat stock buffer tank, backheat self-compensating device；The residual heat collection circuit includes suitable
Enthalpy increasing heat pump, high efficiency plate cool-heat-exchanger, the buffering fluid reservoir, multichannel microgap heat-exchanger rig of sequence connection；Wherein waste heat
Stock buffer tank connection backheat self-compensating device, the backheat self-compensating device and multichannel microgap heat-exchanger rig join
It is logical；The sheet string type natural induced draft evaporative condenser is located above solar radiation evaporative condenser.
3. Integrated Energy recycling system according to claim 1 or 2, it is characterised in that: the new ionic charge is cold
Heat-exchange device, it includes plasma power supply, electric power core heat transfer piece, heat exchanger plates, accumulation of energy deposit plate, and the plasma power supply will
Alternating current is converted to direct current and supplies electricity to electric power core heat transfer piece offer working power, and electric power core heat transfer piece is semiconductor chilling plate,
After electric power core heat transfer piece, electric power core heat transfer piece converts electrical energy into thermal energy and discharges heat or suction to plate face two sides electric current
Heat is received, connection heat exchanger plates are in close contact on the upside of electric power core heat transfer piece, downside is in close contact connection accumulation of energy and lays in plate, described
Heat exchanger plates are provided with water inlet, water outlet, heat exchanging chamber, after heat transferring medium enters heat exchanging chamber heat exchange by water inlet, from water outlet
Outflow, accumulation of energy lays in and exchanges heat on the downside of plate and electric power core heat transfer piece, and stores thermal energy or cold energy.
4. Integrated Energy recycling system according to claim 3, it is characterised in that: the new cold and hot friendship of ionic charge
Changing device further includes preheating table, and preheating table plate face is in close contact connection plasma power supply shell, and preheating table is ion power supply cooling
Heat absorption, the preheating table are provided with the import being sequentially communicated, circulating water pipe, outlet, and outlet passes through valve control and heat exchanger plates
Water inlet connection, import is connected to water source.
5. Integrated Energy recycling system according to claim 3, it is characterised in that: the accumulation of energy lays in plate and includes
High wing T2, heat dissipation cavity, heat release hole, air blower, high wing T2 include heat accumulation plate and the fin being fixedly connected vertical with heat accumulation plate, fin
Multiple groups are arranged in parallel, and uniformly distributed multi-group vacuum lumen is provided in heat accumulation plate, to accumulation of energy, the avris of fin and accumulation of energy deposit plate
Shell is provided with heat release hole, and the heat release hole setting of multiple fins constitutes heat dissipation channel, heat dissipation channel and wing on same straight line
Piece is vertical, and heat dissipation channel is that multiple groups are arranged in same level, and air blower setting lays in plate lower end in accumulation of energy, and air blower will be outer
Portion's air introduces heat dissipation cavity, and the air after heat exchange is laid in the discharge of two avris of plate from accumulation of energy by heat dissipation channel.
6. Integrated Energy recycling system according to claim 3, it is characterised in that: the electric power core heat transfer piece
Further include with semiconductor chilling plate semiconductor temperature differential power generating sheet disposed in parallel, i.e., lay in plate with upside heat exchanger plates and downside accumulation of energy
In contact surface, semiconductor chilling plate and semiconductor temperature differential power generating sheet respectively account for area, semiconductor chilling plate and plasma power supply
Connection, semiconductor temperature differential power generating sheet are connect with battery, and battery is to supply the device part electricity consumption.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820931900.1U CN208282449U (en) | 2018-06-15 | 2018-06-15 | Integrated Energy recycling system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820931900.1U CN208282449U (en) | 2018-06-15 | 2018-06-15 | Integrated Energy recycling system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208282449U true CN208282449U (en) | 2018-12-25 |
Family
ID=64698685
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820931900.1U Expired - Fee Related CN208282449U (en) | 2018-06-15 | 2018-06-15 | Integrated Energy recycling system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208282449U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108507230A (en) * | 2018-06-15 | 2018-09-07 | 山东源源新能源有限公司 | Integrated Energy recycling system |
| CN110332619A (en) * | 2019-07-01 | 2019-10-15 | 江苏盖德冷冻机有限公司 | A kind of air-conditioning condenser energy-saving control device and its control method |
-
2018
- 2018-06-15 CN CN201820931900.1U patent/CN208282449U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108507230A (en) * | 2018-06-15 | 2018-09-07 | 山东源源新能源有限公司 | Integrated Energy recycling system |
| CN108507230B (en) * | 2018-06-15 | 2023-12-12 | 兴鼎工程(深圳)有限公司 | Comprehensive energy recycling system |
| CN110332619A (en) * | 2019-07-01 | 2019-10-15 | 江苏盖德冷冻机有限公司 | A kind of air-conditioning condenser energy-saving control device and its control method |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US10001326B2 (en) | Electric power peak-shaving and combined heat and power waste heat recovery device and operation method thereof | |
| CN110345549B (en) | Liquid cooling data center waste heat recovery system | |
| CN102767880B (en) | A kind of heat pipe hot pump hybrid system | |
| CN102798184B (en) | A kind of heat pipe hot pump hybrid system | |
| CN103307803B (en) | Cold and hot water supply device by compositely utilizing energy | |
| CN111076266B (en) | Multifunctional heat pipe type photovoltaic photo-thermal hot water heating system and heating method | |
| CN103940020B (en) | Superconductive heat storage type solar air conditioner and achieving method thereof | |
| CN110145796B (en) | Micro-energy net supported by solar energy | |
| CN208282449U (en) | Integrated Energy recycling system | |
| CN102759159B (en) | A kind of heat pipe hot pump composite system | |
| CN203068701U (en) | Multifunctional single-effect ammonia water absorption type solar energy air conditioner | |
| CN203336874U (en) | Cold and hot water supply device capable of compositing and utilizing energy | |
| CN110878957A (en) | Urban heat energy comprehensive utilization system and method | |
| CN109595859A (en) | A kind of distributed photovoltaic refrigeration storage system of freezer the library cold-storage | |
| CN109814385A (en) | It is a kind of based on the distributing of Active Disturbance Rejection Control with electric heating system and its method | |
| CN210425244U (en) | Waste heat recovery system of liquid cooling data center | |
| CN201662278U (en) | Device capable of improving energy utilization rate of tri-generation system | |
| CN114135954B (en) | Heat pipe heat exchange air conditioning system | |
| CN102494439A (en) | Photovoltaic photo-thermal energy-storage heat pump system | |
| CN106382767B (en) | The underground heat utilization system in the poor region of groundwater run off | |
| CN108507230A (en) | Integrated Energy recycling system | |
| CN213656920U (en) | Heat pipe type photovoltaic photo-thermal module-heat pump-phase change floor coupling system | |
| CN208282446U (en) | A kind of novel cold-heat-exchanging exchange system | |
| CN211316299U (en) | Urban heat energy comprehensive utilization system | |
| WO2021135297A1 (en) | Geothermal-thermoelectrical cooperative air-conditioning system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20190212 Address after: 271000 Room 311, Enlightenment Star, 396 Development Avenue, Xintai Economic Development Zone, Tai'an City, Shandong Province Patentee after: SHANDONG YUANYUAN INNOVATION INDUSTRIAL PARK MANAGEMENT Co.,Ltd. Address before: 271000 Room 311, Enlightenment Star, 396 Development Avenue, Xintai Economic Development Zone, Tai'an City, Shandong Province Patentee before: SHANDONG YUANYUAN NEW ENERGY Co.,Ltd. |
|
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20181225 |