CN106482211A - Energy-conservation dual-heated system and its method of work in a kind of residents in rural community process - Google Patents
Energy-conservation dual-heated system and its method of work in a kind of residents in rural community process Download PDFInfo
- Publication number
- CN106482211A CN106482211A CN201610907610.9A CN201610907610A CN106482211A CN 106482211 A CN106482211 A CN 106482211A CN 201610907610 A CN201610907610 A CN 201610907610A CN 106482211 A CN106482211 A CN 106482211A
- Authority
- CN
- China
- Prior art keywords
- temperature steam
- control system
- heating tank
- temperature
- water
- 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.)
- Granted
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24D—DOMESTIC- OR SPACE-HEATING SYSTEMS, e.g. CENTRAL HEATING SYSTEMS; DOMESTIC HOT-WATER SUPPLY SYSTEMS; ELEMENTS OR COMPONENTS THEREFOR
- F24D19/00—Details
- F24D19/10—Arrangement or mounting of control or safety devices
- F24D19/1006—Arrangement or mounting of control or safety devices for water heating systems
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24D—DOMESTIC- OR SPACE-HEATING SYSTEMS, e.g. CENTRAL HEATING SYSTEMS; DOMESTIC HOT-WATER SUPPLY SYSTEMS; ELEMENTS OR COMPONENTS THEREFOR
- F24D15/00—Other domestic- or space-heating systems
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24D—DOMESTIC- OR SPACE-HEATING SYSTEMS, e.g. CENTRAL HEATING SYSTEMS; DOMESTIC HOT-WATER SUPPLY SYSTEMS; ELEMENTS OR COMPONENTS THEREFOR
- F24D3/00—Hot-water central heating systems
- F24D3/08—Hot-water central heating systems in combination with systems for domestic hot-water supply
-
- 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
- Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
- Y02B10/00—Integration of renewable energy sources in buildings
- Y02B10/20—Solar thermal
-
- 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
- Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
- Y02B10/00—Integration of renewable energy sources in buildings
- Y02B10/70—Hybrid systems, e.g. uninterruptible or back-up power supplies integrating renewable energies
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
- Water Supply & Treatment (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
The invention discloses a kind of residents in rural community process in energy-conservation dual-heated system and its method of work, by cold water plastic conveying and plastic pipe, high-temperature steam delivery pipe, high-temperature steam instrument, solar light collecting device, high-temperature steam heating tank, hot water plastic water outlet pipe, control system forms；Described high-temperature steam heating tank side is provided with cold water plastic conveying and plastic pipe, described high-temperature steam heating tank opposite side is provided with hot water plastic water outlet pipe, described high-temperature steam heating tank overhead surface is provided with high-temperature steam instrument, described high-temperature steam instrument both sides are provided with high-temperature steam delivery pipe, described high-temperature steam instrument overhead surface is provided with solar light collecting device, and described control system is located at high-temperature steam heating tank one side position.Energy-conservation dual-heated system and its method of work novel and reasonable structure in a kind of residents in rural community process of the present invention, efficiently, the scope of application is wide for the efficiency of heating surface.
Description
Technical field
The invention belongs to environmental protection class field and in particular to a kind of residents in rural community process in energy-conservation dual-heated system and
Its method of work.
Background technology
Thermal source used by house refuse heating system at present, typically adopts single conventional energy resource, such as gas fired-boiler, grill pan
Stove and oil burning boiler etc..With the anxiety of energy resource structure, the utilization of regenerative resource becomes inexorable trend, and this not only contributes to save
Can reduce discharging, be also beneficial to the sustainable development of the energy.So-called house refuse " solar-heating ", refer to by solar thermal collector with
Heat storage water tank, as solar energy acquisition system, provides the novel energy-conserving heat-supplying mode of heat with hot water or heating for building.
Conventional house refuse solar energy heat distribution system ensures part, low-temperature water heating by solar energy heating part, supplementary energy
A few part composition such as radiant floor heating system and the supply of house refuse hot water.Wherein, house refuse solar heating system by
Solar thermal collector, solar energy water circulating pump and heat storage water tank composition, its effect is by being arranged at the heat collector of lighting surface
Heat is collected on limits ground, and carries out the deposit of heat by heat storage water tank.House refuse auxiliary energy system can be by various types of
The conventional energy resource composition of type, as the supplement of house refuse solar thermal collection system, house refuse aid system can be continuous
When rainy weather or other special heating demands, meet heat supply and house refuse supplying hot water demand.
Under normal circumstances, if house refuse solar heating system is only used for independent hot-water supply or heating, typically set
Put a house refuse heat storage water tank, its effect is storage hot water, also heat is passed to heating terminal for heating system.If
House refuse solar energy system should hot-water supply heat again, then need at least provided with a house refuse heat storage water tank and one
Platform house refuse heat exchanger, this kind of setting takes up an area space greatly, and heat waste also increases.Its height of cylindrical house refuse heat storage water tank
With the ratio generally 0.85～1.15 of diameter, the house refuse water tank of this kind of ratio, its internal hot-water is unable to reach and divides very well
The effect of layer, and this water tank does not have the function of heat exchanger concurrently.
Existing house refuse heating system, complex process, floor space is big, and cold/heat exchange efficiency is low, prior art
House refuse energy requirement cannot be met.
Content of the invention
In order to solve above-mentioned technical problem, the present invention provides energy-conservation dual-heated system in a kind of residents in rural community process
System, including：Cold water plastic conveying and plastic pipe 1, high-temperature steam delivery pipe 2, high-temperature steam instrument 3, solar light collecting device 4, high-temperature steam
Heating tank 5, hot water plastic water outlet pipe 6, control system 7；Described high-temperature steam heating tank 5 side is provided with cold water plastic conveying and plastic pipe 1,
Described high-temperature steam heating tank 5 opposite side is provided with hot water plastic water outlet pipe 6, and described high-temperature steam heating tank 5 overhead surface is provided with
High-temperature steam instrument 3, described high-temperature steam instrument 3 both sides are provided with high-temperature steam delivery pipe 2, and described high-temperature steam instrument 3 overhead surface sets
There is solar light collecting device 4, described control system 7 is located at high-temperature steam heating tank 5 one side position；
On electrically-controlled valve on described cold water plastic conveying and plastic pipe 1, the electrically-controlled valve in high-temperature steam delivery pipe 2, hot water plastic water outlet pipe 6
Electrically-controlled valve, high-temperature steam instrument 3 and solar light collecting device 4 be connected with control system 7 polygon control survey respectively.
Further, described high-temperature steam heating tank 5 includes：High-temperature steam thermal treatment zone 5-1, a water temperature detector 5-2,
Secondary electrical heating tank 5-3, stacked heating energising head 5-4, drainage disc 5-5, be energized head rate of heat addition detector 5-6, No. two warm water
Warm detector 5-7；Described high-temperature steam thermal treatment zone 5-1 by cylinder blanket parcel form, high-temperature steam thermal treatment zone 5-1 shell by
Not Heat Conduction Material composition, high-temperature steam thermal treatment zone 5-1 total height is no less than 1.2m；A described water temperature detector 5-2 is located at height
Warm steam thermal treatment zone 5-1 side wall, a water temperature detector 5-2 is connected with control system 7 polygon control survey；Described secondary electrical heating tank
5-3 is located inside the 5-1 of the high-temperature steam thermal treatment zone, secondary electrical heating tank 5-3 and high-temperature steam thermal treatment zone 5-1 central axes,
Away from high-temperature steam thermal treatment zone 5-1 bottom 30cm～45cm, secondary electrical heating tank 5-3 diameter is than high for secondary electrical heating tank 5-3 bottom
Little 5cm～the 15cm of warm steam thermal treatment zone diameter；Described stacked heating energising head 5-4 is located in secondary electrical heating tank 5-3, and stacked adds
Heat energising head 5-4 and secondary electrical heating tank 5-3 central axes；Described drainage disc 5-5 is located at secondary electrical heating tank 5-3 bottom and puts down
Face, drainage disc 5-5 is fixed with secondary electrical heating tank 5-3 baseplane seamless welding, drainage disc 5-5 maximum diameter and secondary electrical heating tank
5-3 diameter is identical；Described energising head rate of heat addition detector 5-6 is located at secondary electrical heating tank 5-3 internal side wall, energising head heating
Speed detector is connected with control system 7 polygon control survey；Described No. two warm water temperature detector 5-7 are located at secondary electrical heating tank 5-3
Internal side wall, No. two warm water temperature detector 5-7 are connected with control system 7 polygon control survey.
Further, described stacked heating energising head 5-4 includes：Vertically blade 5-4-1, horizontal blade 5-4-2, negative electrode is led
Electric post 5-4-3, anode conducting post 5-4-4；The rectangular flake of described vertical blade 5-4-1 profile, multiple vertical blade 5-4-1
Energising head 5-4 its center axis uniform circular arrangement is heated with stacked, vertical blade 5-4-1 quantity is no less than 6 pieces, adjacent two
Vertically 30 °～60 ° of blade 5-4-1 angle；Described horizontal blade 5-4-2 profile is round pie, and horizontal blade 5-4-2 is set in perpendicular
Prismatic blade 5-4-1 surface, horizontal blade 5-4-2 quantity is no less than 2 pieces, and horizontal blade 5-4-2 is parallel evenly distributed up and down, adjacent
Two horizontal blade 5-4-2 spacing 60mm～150mm；Described negative electrode conductive pole 5-4-3 is located at vertical blade 5-4-1 overhead surface,
Negative electrode conductive pole 5-4-3 is connected with the control of control system 7 cathode conductor；Described anode conducting post 5-4-4 is located at vertical blade 5-
4-1 underlying surfaces, anode conducting post 5-4-4 is connected with the control of control system 7 positive wire.
Further, described drainage disc 5-5 includes：" V " type circumferential section 5-5-1, boss through hole 5-5-2；Described " V " type
Circumferential section 5-5-1 wall thickness 3mm～5mm, " V " type circumferential section 5-5-1 is by rotating 360 degrees formation bowl structure, described bowl-shape
Structure external diameter inclined-plane and horizontal plane angle are β, and described β value range is 30 °～65 °；The trapezoidal cylinder of described boss through hole 5-5-2
Hollow body structure, boss through hole 5-5-2 aperture is up-small and down-big, and boss through hole 5-5-2 inclined-plane and horizontal plane angle are α, described α model
Enclose value and be 40 °～70 °.
Further, described stacked heating energising head 5-4 is by macromolecular material pressing mold molding, stacked heating energising head 5-4
Constituent and manufacture process as follows：
First, stacked heating energising head 5-4 constituent：
Count by weight, 53～133 parts of polyallylmethacrylate, 73～133 parts of butyl -2- methyl -2- acrylate,
123～233 parts of Tributyl Tin Methacrylate, 73～183 parts of 2- butyl methacrylate, methacrylic acid triphenylmethyl
63～133 parts, 113～233 parts of 3- tri-chlorination tinbase acrylate, concentration is the ethyl acrylate base front three of 43ppm～83ppm
73～113 parts of ammonium chloride, 63～123 parts of 2- methacrylic acid -3- (methyl dichloro silicon substrate) third (alcohol) ester, acetic acid -3- chlorine third
63～153 parts of alkene ester, 83～153 parts of cross-linking agent, β -43～123 parts of trichlorine tinbase propionic ester, carboxylic acid beta-hydroxy (chlorine) propyl ester 73
～163 parts, 33～63 parts of α-chloro- beta-hydroxyphenyl methyl propionate, β -33～113 parts of alkoxy carbonyl group propyl group tin trichloride；
Described cross-linking agent is beta-hydroxy-alpha-aromatic acrylate, methacrylic acid β hydroxyl ethyl ester, in senecioate-hydroxy methacrylate
Any one；
2nd, the manufacture process of stacked heating energising head 5-4, comprises the steps of：
1st step：Add 513～1103 parts of the ultra-pure water that electrical conductivity is 0.33 μ S/cm～0.63 μ S/cm in a kettle., start
Agitator in reactor, rotating speed is 83rpm～223rpm, starts heat pump, makes reactor temperature rise to 53 DEG C～63 DEG C；
Sequentially add polyallylmethacrylate, butyl -2- methyl -2- acrylate, Tributyl Tin Methacrylate, stir to
It is completely dissolved, adjusting pH value is 1.3～6.3, and agitator speed is adjusted to 113rpm～233rpm, and temperature is 73 DEG C～143 DEG C,
Esterification 13～23 hours；
2nd step：2- butyl methacrylate, methacrylic acid triphenylmethyl is taken to be pulverized, powder diameter is 203～633
Mesh；Plus 3- tri-chlorination tinbase crylic acid ester mixture is uniformly, is laid in pallet, tiling thickness is 13mm～43mm, using dosage
It is the alpha ray irradiation 43～123 minutes of 5.3MeV～13MeV for 1.3kGy～9.3kGy, energy, and the β of Isodose penetrates
Line irradiation 63～153 minutes；
3rd step：It is dissolved in ethylacrylate-trimethylammonium chloride through the mixed-powder that the 2nd step is processed, add reactor, stirring
Device rotating speed be 73rpm～173rpm, temperature be 83 DEG C～133 DEG C, start vacuum pump make the vacuum of reactor reach-
0.73MPa～-0.33MPa, keeps this state response 13～43 hours；Pressure release is simultaneously passed through nitrogen, makes the reacting kettle inner pressure be
0.23MPa～0.63MPa, insulation standing 13～23 hours；Agitator speed is promoted to 103rpm～243rpm, simultaneous reactions kettle
Pressure release is to 0MPa；Sequentially add 2- methacrylic acid -3- (methyl dichloro silicon substrate) third (alcohol) ester, acetic acid-chlorallylene ester complete
After dissolving, add cross-linking agent stirring mixing so that the hydrophile-lipophile balance value of reactor solution is 3.3～6.3, be incubated standing 13
～23 hours；
4th step：When agitator speed is for 123rpm～253rpm, sequentially add β-trichlorine tinbase propionic ester, carboxylic acid beta-hydroxy
(chlorine) propyl ester, α-chloro- beta-hydroxyphenyl methyl propionate, β-alkoxy carbonyl group propyl group tin trichloride, lifting reactor pressure is so as to reach
0.73MPa～1.53MPa, temperature is 123 DEG C～263 DEG C, polyreaction 13～33 hours；After the completion of reaction, reactor is intrinsic pressure
Power is down to 0MPa, is cooled to 23 DEG C～33 DEG C, discharging, enters molding press and can be prepared by stacked heating energising head 5-4.
The invention also discloses a kind of residents in rural community process in energy-conservation dual-heated system method of work, the method
Including following step：
1st step：The electrically-controlled valve that control system 7 is opened on cold water plastic conveying and plastic pipe 1 conveys cold into the 5-1 of the high-temperature steam thermal treatment zone
Water, simultaneously control system 7 start solar light collecting device 4 and absorb luminous energy and simultaneously convert it into heat energy, heat energy and then be transitioned into height
Inside warm steam instrument 3, control system 7 starts high-temperature steam instrument 3 and the water heating evaporation of internal reservoir is become vapor, now controls
High-temperature water vapor is delivered to the cold water in the 5-1 of the high-temperature steam thermal treatment zone by the electrically-controlled valve that system 7 is opened in high-temperature steam delivery pipe 2
In, provide thermal source for heating process；In the process, in a water temperature detector 5-2 real-time monitoring high-temperature steam thermal treatment zone 5-1
Water temperature condition, when a water temperature detector 5-2 detects water temperature in the 5-1 of the high-temperature steam thermal treatment zone and is less than 40 DEG C, No. one
The signal of telecommunication is sent to control system 7 by water temperature detector 5-2, and control system 7 controls solar light collecting device 4 increasing to adopt heat；
2nd step：5-1 internal warm water after first heating in the high-temperature steam thermal treatment zone flows into secondary electrical heating by drainage disc 5-5
In tank 5-3, control system 7 starts stacked heating energising head 5-4 and warm water is heated further, in heating process, No. two warm water
Water temperature condition in the secondary electrical heating tank 5-3 of warm detector 5-7 real-time monitoring, when No. two warm water temperature detector 5-7 detect two
When water temperature in secondary electrical heating tank 5-3 reaches 85 DEG C～100 DEG C, the signal of telecommunication is sent to control by No. two warm water temperature detector 5-7
System 7, control system 7 cut-out stacked heating energising head 5-4 power supply stops heating, with save energy；
3rd step：Heat in energising head 5-4 heating process in stacked, energising head rate of heat addition detector 5-6 is carried out to the rate of heat addition
Real-time monitoring, when the head rate of heat addition detector 5-6 that is energized detects the rate of heat addition and is less than 45%, energising head rate of heat addition detection
The signal of telecommunication is sent to control system 7 by instrument 5-6, and control system 7 controls stacked heating energising head 5-4 to increase heat fan-out capability；
4th step：After the completion for the treatment of hot water heating, the electrically-controlled valve on control system 7 unlatching hot water plastic water outlet pipe 6 is by delivery extremely
In each residential building or office building water supply line.
Energy-conservation dual-heated system and its method of work during disclosed in patent of the present invention, a kind of residents in rural community is processed, its
Advantage is：
(1) this device adopts solar light collecting device, and energy saving rate is high；
(2) this apparatus structure is reasonable in design compact, and integrated level is high；
(3) this device stacked heating energising head adopts macromolecular material to prepare, and the lifting of firing rate conservation rate is notable.
In a kind of residents in rural community process of the present invention, energy-conservation dual-heated system and its method of work structure are new
Rationally, efficiently, the scope of application is wide for the efficiency of heating surface for grain husk.
Brief description
Fig. 1 is energy-conservation dual-heated system schematic in a kind of heretofore described residents in rural community process.
Fig. 2 is heretofore described high-temperature steam heating tank internal structure schematic diagram.
Fig. 3 is heretofore described stacked heating energising header structure schematic diagram.
Fig. 4 is heretofore described drainage disc three dimensional structure diagram.
Fig. 5 is heretofore described drainage disc schematic cross-section.
Fig. 6 is stacked heating energising head material of the present invention and firing rate conservation rate graph of a relation.
In figure 1 above～Fig. 5, cold water plastic conveying and plastic pipe 1, high-temperature steam delivery pipe 2, high-temperature steam instrument 3, solar energy light collecting
Device 4, high-temperature steam heating tank 5, high-temperature steam thermal treatment zone 5-1, a water temperature detector 5-2, secondary electrical heating tank 5-3, fold
Formula heating energising head 5-4, vertical blade 5-4-1, horizontal blade 5-4-2, negative electrode conductive pole 5-4-3, anode conducting post 5-4-4,
Drainage disc 5-5, " V " type circumferential section 5-5-1, boss through hole 5-5-2, be energized head rate of heat addition detector 5-6, No. two warm water temperature
Detector 5-7, hot water plastic water outlet pipe 6, control system 7.
Specific embodiment
Energy-conservation dual-heated in reference to the accompanying drawings and examples a kind of residents in rural community that the present invention provides being processed
System is further described.
As shown in figure 1, being the signal of energy-conservation dual-heated system during a kind of residents in rural community that the present invention provides is processed
Figure.In figure is found out, including：Cold water plastic conveying and plastic pipe 1, high-temperature steam delivery pipe 2, high-temperature steam instrument 3, solar light collecting device 4,
High-temperature steam heating tank 5, hot water plastic water outlet pipe 6, control system 7；Described high-temperature steam heating tank 5 side is provided with cold water plastics
Delivery pipe 1, described high-temperature steam heating tank 5 opposite side is provided with hot water plastic water outlet pipe 6, above described high-temperature steam heating tank 5
Surface is provided with high-temperature steam instrument 3, and described high-temperature steam instrument 3 both sides are provided with high-temperature steam delivery pipe 2, on described high-temperature steam instrument 3
Square surface is provided with solar light collecting device 4, and described control system 7 is located at high-temperature steam heating tank 5 one side position；Described cold water is moulded
Electrically-controlled valve on electrically-controlled valve in electrically-controlled valve on material conveying tube 1, high-temperature steam delivery pipe 2, hot water plastic water outlet pipe 6, high temperature
Steam instrument 3 and solar light collecting device 4 are connected with control system 7 polygon control survey respectively.
As shown in Fig. 2 being heretofore described high-temperature steam heating tank internal structure schematic diagram.From Fig. 2 or Fig. 1
Go out, described high-temperature steam heating tank 5 includes：High-temperature steam thermal treatment zone 5-1, a water temperature detector 5-2, secondary electrical heating tank 5-
3, stacked heating energising head 5-4, drainage disc 5-5, be energized head rate of heat addition detector 5-6, No. two warm water temperature detector 5-7；Institute
State high-temperature steam thermal treatment zone 5-1 to be formed by cylinder blanket parcel, high-temperature steam thermal treatment zone 5-1 shell is by not Heat Conduction Material group
Become, high-temperature steam thermal treatment zone 5-1 total height is no less than 1.2m；A described water temperature detector 5-2 is located at the high-temperature steam thermal treatment zone
5-1 side wall, a water temperature detector 5-2 is connected with control system 7 polygon control survey；Described secondary electrical heating tank 5-3 is located at high temperature
Inside the 5-1 of the steam thermal treatment zone, secondary electrical heating tank 5-3 and high-temperature steam thermal treatment zone 5-1 central axes, secondary electrical heating tank
Away from high-temperature steam thermal treatment zone 5-1 bottom 30cm～45cm, secondary electrical heating tank 5-3 diameter is than the high-temperature steam thermal treatment zone for 5-3 bottom
Little 5cm～the 15cm of diameter；Described stacked heating energising head 5-4 is located in secondary electrical heating tank 5-3, stacked heating energising head 5-4
With secondary electrical heating tank 5-3 central axes；Described drainage disc 5-5 is located at secondary electrical heating tank 5-3 baseplane, drainage disc 5-
5 are fixed with secondary electrical heating tank 5-3 baseplane seamless welding, drainage disc 5-5 maximum diameter and secondary electrical heating tank 5-3 diameter phase
With；Described energising head rate of heat addition detector 5-6 is located at secondary electrical heating tank 5-3 internal side wall, energising head rate of heat addition detection
Instrument is connected with control system 7 polygon control survey；Described No. two warm water temperature detector 5-7 are located at secondary electrical heating tank 5-3 internal side wall,
No. two warm water temperature detector 5-7 are connected with control system 7 polygon control survey.
As shown in figure 3, being heretofore described stacked heating energising header structure schematic diagram.Find out from Fig. 3 or Fig. 2,
Described stacked heating energising head 5-4 includes：Vertically blade 5-4-1, horizontal blade 5-4-2, negative electrode conductive pole 5-4-3, anode is led
Electric post 5-4-4；The rectangular flake of described vertical blade 5-4-1 profile, multiple vertical blade 5-4-1 heat energising head with stacked
5-4 its center axis uniform circular arranges, and vertical blade 5-4-1 quantity is no less than 6 pieces, adjacent two vertical blade 5-4-1 folders
30 °～60 ° of angle；Described horizontal blade 5-4-2 profile is round pie, and horizontal blade 5-4-2 is set in vertical blade 5-4-1 table
Face, horizontal blade 5-4-2 quantity is no less than 2 pieces, and horizontal blade 5-4-2 is parallel evenly distributed up and down, adjacent two horizontal blade 5-
4-2 spacing 60mm～150mm；Described negative electrode conductive pole 5-4-3 is located at vertical blade 5-4-1 overhead surface, negative electrode conductive pole 5-
4-3 is connected with the control of control system 7 cathode conductor；Described anode conducting post 5-4-4 is located at vertical blade 5-4-1 underlying surfaces,
Anode conducting post 5-4-4 is connected with the control of control system 7 positive wire.
As shown in Figure 4, Figure 5, it is heretofore described drainage disc three dimensional structure diagram and schematic cross-section.From Fig. 4
Or find out in Fig. 5, described drainage disc 5-5 includes：" V " type circumferential section 5-5-1, boss through hole 5-5-2；Described " V " type circumference
Section 5-5-1 wall thickness 3mm～5mm, " V " type circumferential section 5-5-1 is by rotating 360 degrees formation bowl structure, described bowl structure
External diameter inclined-plane and horizontal plane angle are β, and described β value range is 30 °～65 °；The trapezoidal cylinder hollow of described boss through hole 5-5-2
Body structure, boss through hole 5-5-2 aperture is up-small and down-big, and boss through hole 5-5-2 inclined-plane and horizontal plane angle are α, described α value range
For 40 °～70 °.
In a kind of residents in rural community process of the present invention, the work process of energy-conservation dual-heated system is：
1st step：The electrically-controlled valve that control system 7 is opened on cold water plastic conveying and plastic pipe 1 conveys cold into the 5-1 of the high-temperature steam thermal treatment zone
Water, simultaneously control system 7 start solar light collecting device 4 and absorb luminous energy and simultaneously convert it into heat energy, heat energy and then be transitioned into height
Inside warm steam instrument 3, control system 7 starts high-temperature steam instrument 3 and the water heating evaporation of internal reservoir is become vapor, now controls
High-temperature water vapor is delivered to the cold water in the 5-1 of the high-temperature steam thermal treatment zone by the electrically-controlled valve that system 7 is opened in high-temperature steam delivery pipe 2
In, provide thermal source for heating process；In the process, in a water temperature detector 5-2 real-time monitoring high-temperature steam thermal treatment zone 5-1
Water temperature condition, when a water temperature detector 5-2 detects water temperature in the 5-1 of the high-temperature steam thermal treatment zone and is less than 40 DEG C, No. one
The signal of telecommunication is sent to control system 7 by water temperature detector 5-2, and control system 7 controls solar light collecting device 4 increasing to adopt heat；
2nd step：5-1 internal warm water after first heating in the high-temperature steam thermal treatment zone flows into secondary electrical heating by drainage disc 5-5
In tank 5-3, control system 7 starts stacked heating energising head 5-4 and warm water is heated further, in heating process, No. two warm water
Water temperature condition in the secondary electrical heating tank 5-3 of warm detector 5-7 real-time monitoring, when No. two warm water temperature detector 5-7 detect two
When water temperature in secondary electrical heating tank 5-3 reaches 85 DEG C～100 DEG C, the signal of telecommunication is sent to control by No. two warm water temperature detector 5-7
System 7, control system 7 cut-out stacked heating energising head 5-4 power supply stops heating, with save energy；
3rd step：Heat in energising head 5-4 heating process in stacked, energising head rate of heat addition detector 5-6 is carried out to the rate of heat addition
Real-time monitoring, when the head rate of heat addition detector 5-6 that is energized detects the rate of heat addition and is less than 45%, energising head rate of heat addition detection
The signal of telecommunication is sent to control system 7 by instrument 5-6, and control system 7 controls stacked heating energising head 5-4 to increase heat fan-out capability；
4th step：After the completion for the treatment of hot water heating, the electrically-controlled valve on control system 7 unlatching hot water plastic water outlet pipe 6 is by delivery extremely
In each residential building or office building water supply line.
In a kind of residents in rural community process of the present invention, energy-conservation dual-heated system and its method of work structure are new
Rationally, efficiently, the scope of application is wide for the efficiency of heating surface for grain husk.
The following is the embodiment of the manufacture process of stacked heating energising head 5-4 of the present invention, embodiment is to enter one
Step explanation present disclosure, but should not be construed as limitation of the present invention.In the situation without departing substantially from present invention spirit and essence
Under, the modification that the inventive method, step or condition are made and replacement, belong to the scope of the present invention.
If not specializing, the conventional meanses that in embodiment, technological means used are well known to those skilled in the art.
Embodiment 1
Manufacture stacked heating energising head 5-4 of the present invention according to following steps, and fraction meter by weight：
1st step：Add 513 parts of the ultra-pure water that electrical conductivity is 0.33 μ S/cm in a kettle., start agitator in reactor, turn
Speed is 83rpm, starts heat pump, makes reactor temperature rise to 53 DEG C；Sequentially add 53 parts of polyallylmethacrylate,
73 parts of butyl -2- methyl -2- acrylate, 123 parts of Tributyl Tin Methacrylate, stir to being completely dissolved, adjust pH value
For 1.3, agitator speed is adjusted to 113rpm, temperature is 73 DEG C, esterification 13 hours；
2nd step：73 parts of 2- butyl methacrylate, 63 parts of methacrylic acid triphenylmethyl is taken to be pulverized, powder diameter is
203 mesh；Plus 3- 113 parts of mix homogeneously of tri-chlorination tinbase acrylate, it is laid in pallet, tiling thickness is 13mm, using agent
Measuring as 1.3kGy, energy is the alpha ray irradiation 43 minutes of 5.3MeV, and the β x ray irradiation x of Isodose 63 minutes；
3rd step：It is dissolved in 73 parts of the ethylacrylate-trimethylammonium chloride that concentration is 43ppm through the mixed-powder that the 2nd step is processed
In, add reactor, agitator speed be 73rpm, temperature be 83 DEG C, start vacuum pump make the vacuum of reactor reach-
0.73MPa, keeps this state response 13 hours；Pressure release is simultaneously passed through nitrogen, makes reacting kettle inner pressure be 0.23MPa, insulation standing
13 hours；Agitator speed is promoted to 103rpm, simultaneous reactions kettle pressure release to 0MPa；Sequentially add 2- methacrylic acid -3- (first
Base dichloro silicon substrate) after 63 parts of third (alcohol) ester, acetic acid -63 parts of chlorallylene ester be completely dissolved, add 83 parts of stirring mixing of cross-linking agent,
The hydrophile-lipophile balance value making reactor solution is 3.3, insulation standing 13 hours；
4th step：When agitator speed is for 123rpm, sequentially add β -43 parts of trichlorine tinbase propionic ester, carboxylic acid beta-hydroxy (chlorine)
33 parts of 73 parts of propyl ester, α-chloro- beta-hydroxyphenyl methyl propionate, β -33 parts of alkoxy carbonyl group propyl group tin trichloride, lift reactor pressure,
Reach 0.73MPa, temperature is 123 DEG C, polyreaction 13 hours；After the completion of reaction, reacting kettle inner pressure is down to 0MPa,
It is cooled to 23 DEG C, discharging, enter molding press and can be prepared by stacked heating energising head 5-4；
Described cross-linking agent is beta-hydroxy-alpha-aromatic acrylate.
Embodiment 2
Manufacture stacked heating energising head 5-4 of the present invention according to following steps, and fraction meter by weight：
1st step：Add 1103 parts of the ultra-pure water that electrical conductivity is 0.63 μ S/cm in a kettle., start agitator in reactor, turn
Speed is 223rpm, starts heat pump, makes reactor temperature rise to 63 DEG C；Sequentially add polyallylmethacrylate 133
Part, 133 parts of butyl -2- methyl -2- acrylate, 233 parts of Tributyl Tin Methacrylate, stir to being completely dissolved, adjust
PH value is 6.3, and agitator speed is adjusted to 233rpm, and temperature is 143 DEG C, esterification 23 hours；
2nd step：183 parts of 2- butyl methacrylate, 133 parts of methacrylic acid triphenylmethyl is taken to be pulverized, powder diameter
For 633 mesh；Plus 3- 233 parts of mix homogeneously of tri-chlorination tinbase acrylate, it is laid in pallet, tiling thickness is 43mm, adopts
Dosage is 9.3kGy, energy is the alpha ray irradiation 123 minutes of 13MeV, and the β x ray irradiation x of Isodose 153 minutes；
3rd step：It is dissolved in 113 parts of the ethylacrylate-trimethylammonium chloride that concentration is 83ppm through the mixed-powder that the 2nd step is processed
In, add reactor, agitator speed be 173rpm, temperature be 133 DEG C, start vacuum pump make the vacuum of reactor reach-
0.33MPa, keeps this state response 43 hours；Pressure release is simultaneously passed through nitrogen, makes reacting kettle inner pressure be 0.63MPa, insulation standing
23 hours；Agitator speed is promoted to 243rpm, simultaneous reactions kettle pressure release to 0MPa；Sequentially add 2- methacrylic acid -3- (first
Base dichloro silicon substrate) after 123 parts of third (alcohol) ester, acetic acid -153 parts of chlorallylene ester be completely dissolved, add 153 parts of stirrings of cross-linking agent mixed
Close so that the hydrophile-lipophile balance value of reactor solution is 6.3, insulation standing 23 hours；
4th step：When agitator speed is for 253rpm, sequentially add β -123 parts of trichlorine tinbase propionic ester, carboxylic acid beta-hydroxy (chlorine)
63 parts of 163 parts of propyl ester, α-chloro- beta-hydroxyphenyl methyl propionate, β -113 parts of alkoxy carbonyl group propyl group tin trichloride, lift reactor pressure
So as to reach 1.53MPa, temperature is 263 DEG C to power, polyreaction 33 hours；After the completion of reaction, reacting kettle inner pressure is down to
0MPa, is cooled to 33 DEG C, discharging, enters molding press and can be prepared by stacked heating energising head 5-4；
Described cross-linking agent is senecioate-hydroxy methacrylate.
Embodiment 3
Manufacture stacked heating energising head 5-4 of the present invention according to following steps, and fraction meter by weight：
1st step：Add 703 parts of the ultra-pure water that electrical conductivity is 0.43 μ S/cm in a kettle., start agitator in reactor, turn
Speed is 123rpm, starts heat pump, makes reactor temperature rise to 59 DEG C；Sequentially add polyallylmethacrylate 83
Part, 93 parts of butyl -2- methyl -2- acrylate, 153 parts of Tributyl Tin Methacrylate, stir to being completely dissolved, adjust pH
It is worth for 4.3, agitator speed is adjusted to 183rpm, temperature is 93 DEG C, esterification 17 hours；
2nd step：113 parts of 2- butyl methacrylate, 83 parts of methacrylic acid triphenylmethyl is taken to be pulverized, powder diameter is
433 mesh；Plus 3- 183 parts of mix homogeneously of tri-chlorination tinbase acrylate, it is laid in pallet, tiling thickness is 33mm, using agent
Measuring as 6.3kGy, energy is the alpha ray irradiation 83 minutes of 10MeV, and the β x ray irradiation x of Isodose 93 minutes；
3rd step：It is dissolved in 93 parts of the ethylacrylate-trimethylammonium chloride that concentration is 73ppm through the mixed-powder that the 2nd step is processed
In, add reactor, agitator speed be 123rpm, temperature be 103 DEG C, start vacuum pump make the vacuum of reactor reach-
0.53MPa, keeps this state response 33 hours；Pressure release is simultaneously passed through nitrogen, makes reacting kettle inner pressure be 0.43MPa, insulation standing
17 hours；Agitator speed is promoted to 143rpm, simultaneous reactions kettle pressure release to 0MPa；Sequentially add 2- methacrylic acid -3- (first
Base dichloro silicon substrate) after 93 parts of third (alcohol) ester, acetic acid -93 parts of chlorallylene ester be completely dissolved, add 113 parts of stirrings of cross-linking agent mixed
Close so that the hydrophile-lipophile balance value of reactor solution is 5.3, insulation standing 17 hours；
4th step：When agitator speed is for 153rpm, sequentially add β -83 parts of trichlorine tinbase propionic ester, carboxylic acid beta-hydroxy (chlorine)
53 parts of 113 parts of propyl ester, α-chloro- beta-hydroxyphenyl methyl propionate, β -73 parts of alkoxy carbonyl group propyl group tin trichloride, lift reactor pressure
So as to reach 1.13MPa, temperature is 163 DEG C to power, polyreaction 23 hours；After the completion of reaction, reacting kettle inner pressure is down to
0MPa, is cooled to 26 DEG C, discharging, enters molding press and can be prepared by stacked heating energising head 5-4；
Described cross-linking agent is methacrylic acid β hydroxyl ethyl ester.
Reference examples
Reference examples are the service condition for heating process for the stacked heating energising head of certain brand commercially available.
Embodiment 4
Stacked heating energising head described in the stacked heating energising head 5-4 that prepare embodiment 1～3 and reference examples is used for adding
The service condition of thermal process is contrasted, and with bulk density value, using duration, high temperature strength enhancing rate, corrosion-resistant
Degree enhancing rate is counted for technical specification, and result is as shown in table 1：
Table 1 is the contrast for the parameters in heating process for the stacked heating energising head described in embodiment 1～3 and reference examples
As a result, as seen from Table 1, stacked of the present invention heating energising head 5-4, its bulk density value, using duration, high temperature resistant
Strength enhancing rate, corrosion resistant erosion degree enhancing rate are above the product of prior art production.
Additionally, as shown in fig. 6, being that stacked heating energising head 5-4 material of the present invention is closed with firing rate conservation rate
System's figure.In figure is found out, used by embodiment 1～3, macromolecule stacked heating energising head 5-4, is better than in terms of firing rate conservation rate
Existing product.
Claims (6)
1. energy-conservation dual-heated system during a kind of residents in rural community is processed, including：Cold water plastic conveying and plastic pipe (1), high-temperature steam
Delivery pipe (2), high-temperature steam instrument (3), solar light collecting device (4), high-temperature steam heating tank (5), hot water plastic water outlet pipe
(6), control system (7)；It is characterized in that, described high-temperature steam heating tank (5) side is provided with cold water plastic conveying and plastic pipe (1), institute
State high-temperature steam heating tank (5) opposite side and be provided with hot water plastic water outlet pipe (6), described high-temperature steam heating tank (5) overhead surface
It is provided with high-temperature steam instrument (3), described high-temperature steam instrument (3) both sides are provided with high-temperature steam delivery pipe (2), described high-temperature steam instrument
(3) overhead surface is provided with solar light collecting device (4), and described control system (7) is located at high-temperature steam heating tank (5) side position
Put；
Electrically-controlled valve in electrically-controlled valve on described cold water plastic conveying and plastic pipe (1), high-temperature steam delivery pipe (2), hot water plastics water outlet
Electrically-controlled valve on pipe (6), high-temperature steam instrument (3) and solar light collecting device (4) are respectively with control system (7) polygon control survey even
Connect.
2. energy-conservation dual-heated system during a kind of residents in rural community according to claim 1 is processed is it is characterised in that institute
State high-temperature steam heating tank (5) to include：The high-temperature steam thermal treatment zone (5-1), a water temperature detector (5-2), secondary electrical heating tank
(5-3), stacked heating energising head (5-4), drainage disc (5-5), energising head rate of heat addition detector (5-6), No. two warm water temperature detectors
Survey instrument (5-7)；The described high-temperature steam thermal treatment zone (5-1) is formed by cylinder blanket parcel, the high-temperature steam thermal treatment zone (5-1) shell
It is made up of not Heat Conduction Material, the high-temperature steam thermal treatment zone (5-1) total height is no less than 1.2m；A described water temperature detector (5-2)
Positioned at the high-temperature steam thermal treatment zone (5-1) side wall, a water temperature detector (5-2) is connected with control system (7) polygon control survey；Described
Secondary electrical heating tank (5-3) is located at the high-temperature steam thermal treatment zone (5-1) inside, and secondary electrical heating tank (5-3) is heated with high-temperature steam
Area (5-1) central axes, secondary electrical heating tank (5-3) bottom away from the high-temperature steam thermal treatment zone (5-1) bottom 30cm～45cm,
Secondary electrical heating tank (5-3) diameter 5cm～15cm less than high-temperature steam thermal treatment zone diameter；Described stacked heating energising head (5-4)
In secondary electrical heating tank (5-3), stacked heats energising head (5-4) and secondary electrical heating tank (5-3) central axes；Institute
State drainage disc (5-5) and be located at secondary electrical heating tank (5-3) baseplane, drainage disc (5-5) and secondary electrical heating tank (5-3) baseplane
Seamless welding is fixed, and drainage disc (5-5) maximum diameter is identical with secondary electrical heating tank (5-3) diameter；The described energising head rate of heat addition
Detector (5-6) is located at secondary electrical heating tank (5-3) internal side wall, and energising head rate of heat addition detector is led with control system (7)
Line traffic control connects；Described No. two warm water temperature detector (5-7) are located at secondary electrical heating tank (5-3) internal side wall, No. two warm water temperature
Detector (5-7) is connected with control system (7) polygon control survey.
3. energy-conservation dual-heated system during a kind of residents in rural community according to claim 2 is processed is it is characterised in that institute
State stacked heating energising head (5-4) to include：Vertically blade (5-4-1), horizontal blade (5-4-2), negative electrode conductive pole (5-4-3),
Anode conducting post (5-4-4)；The rectangular flake of described vertical blade (5-4-1) profile, multiple vertical blades (5-4-1) are with folded
Formula heating energising head (5-4) its center axis uniform circular arrangement, vertical blade (5-4-1) quantity is no less than 6 pieces, and adjacent two
Vertically 30 °～60 ° of blade (5-4-1) angle；Described horizontal blade (5-4-2) profile is round pie, and horizontal blade (5-4-2) covers
It is located at vertical blade (5-4-1) surface, horizontal blade (5-4-2) quantity is no less than 2 pieces, and horizontal blade (5-4-2) is parallel up and down
Evenly distributed, adjacent two horizontal blades (5-4-2) spacing 60mm～150mm；Described negative electrode conductive pole (5-4-3) is located at vertical leaf
Piece (5-4-1) overhead surface, negative electrode conductive pole (5-4-3) is connected with the control of control system (7) cathode conductor；Described anode conducting
Post (5-4-4) is located at vertical blade (5-4-1) underlying surfaces, anode conducting post (5-4-4) and control system (7) positive wire control
System connects.
4. energy-conservation dual-heated system during a kind of residents in rural community according to claim 2 is processed is it is characterised in that institute
State drainage disc (5-5) to include：" V " type circumferential section (5-5-1), boss through hole (5-5-2)；Described " V " type circumferential section (5-5-
1) wall thickness 3mm～5mm, " V " type circumferential section (5-5-1) is by rotating 360 degrees formation bowl structure, described bowl structure external diameter
Inclined-plane and horizontal plane angle are β, and described β value range is 30 °～65 °；The trapezoidal hollow cylindrical body of described boss through hole (5-5-2)
Structure, boss through hole (5-5-2) aperture is up-small and down-big, and boss through hole (5-5-2) inclined-plane and horizontal plane angle are α, described α scope
It is worth for 40 °～70 °.
5. energy-conservation dual-heated system during a kind of residents in rural community according to claim 2 is processed is it is characterised in that institute
State stacked heating energising head (5-4) by macromolecular material pressing mold molding, the constituent of stacked heating energising head (5-4) and manufacture
Process is as follows：
First, stacked heating energising head (5-4) constituent：
Count by weight, 53～133 parts of polyallylmethacrylate, 73～133 parts of butyl -2- methyl -2- acrylate,
123～233 parts of Tributyl Tin Methacrylate, 73～183 parts of 2- butyl methacrylate, methacrylic acid triphenylmethyl
63～133 parts, 113～233 parts of 3- tri-chlorination tinbase acrylate, concentration is the ethyl acrylate base front three of 43ppm～83ppm
73～113 parts of ammonium chloride, 63～123 parts of 2- methacrylic acid -3- (methyl dichloro silicon substrate) third (alcohol) ester, acetic acid -3- chlorine third
63～153 parts of alkene ester, 83～153 parts of cross-linking agent, β -43～123 parts of trichlorine tinbase propionic ester, carboxylic acid beta-hydroxy (chlorine) propyl ester 73
～163 parts, 33～63 parts of α-chloro- beta-hydroxyphenyl methyl propionate, β -33～113 parts of alkoxy carbonyl group propyl group tin trichloride；
Described cross-linking agent is beta-hydroxy-alpha-aromatic acrylate, methacrylic acid β hydroxyl ethyl ester, in senecioate-hydroxy methacrylate
Any one；
2nd, the manufacture process of stacked heating energising head (5-4), comprises the steps of：
1st step：Add 513～1103 parts of the ultra-pure water that electrical conductivity is 0.33 μ S/cm～0.63 μ S/cm in a kettle., start
Agitator in reactor, rotating speed is 83rpm～223rpm, starts heat pump, makes reactor temperature rise to 53 DEG C～63 DEG C；
Sequentially add polyallylmethacrylate, butyl -2- methyl -2- acrylate, Tributyl Tin Methacrylate, stir to
It is completely dissolved, adjusting pH value is 1.3～6.3, and agitator speed is adjusted to 113rpm～233rpm, and temperature is 73 DEG C～143 DEG C,
Esterification 13～23 hours；
2nd step：2- butyl methacrylate, methacrylic acid triphenylmethyl is taken to be pulverized, powder diameter is 203～633
Mesh；Plus 3- tri-chlorination tinbase crylic acid ester mixture is uniformly, is laid in pallet, tiling thickness is 13mm～43mm, using dosage
It is the alpha ray irradiation 43～123 minutes of 5.3MeV～13MeV for 1.3kGy～9.3kGy, energy, and the β of Isodose penetrates
Line irradiation 63～153 minutes；
3rd step：It is dissolved in ethylacrylate-trimethylammonium chloride through the mixed-powder that the 2nd step is processed, add reactor, stirring
Device rotating speed be 73rpm～173rpm, temperature be 83 DEG C～133 DEG C, start vacuum pump make the vacuum of reactor reach-
0.73MPa～-0.33MPa, keeps this state response 13～43 hours；Pressure release is simultaneously passed through nitrogen, makes the reacting kettle inner pressure be
0.23MPa～0.63MPa, insulation standing 13～23 hours；Agitator speed is promoted to 103rpm～243rpm, simultaneous reactions kettle
Pressure release is to 0MPa；Sequentially add 2- methacrylic acid -3- (methyl dichloro silicon substrate) third (alcohol) ester, acetic acid-chlorallylene ester complete
After dissolving, add cross-linking agent stirring mixing so that the hydrophile-lipophile balance value of reactor solution is 3.3～6.3, be incubated standing 13
～23 hours；
4th step：When agitator speed is for 123rpm～253rpm, sequentially add β-trichlorine tinbase propionic ester, carboxylic acid beta-hydroxy
(chlorine) propyl ester, α-chloro- beta-hydroxyphenyl methyl propionate, β-alkoxy carbonyl group propyl group tin trichloride, lifting reactor pressure is so as to reach
0.73MPa～1.53MPa, temperature is 123 DEG C～263 DEG C, polyreaction 13～33 hours；After the completion of reaction, reactor is intrinsic pressure
Power is down to 0MPa, is cooled to 23 DEG C～33 DEG C, discharging, enters molding press and can be prepared by stacked heating energising head (5-4).
6. during a kind of residents in rural community is processed, the method for work of energy-conservation dual-heated system is it is characterised in that the method includes
Following step：
1st step：Control system (7) opens electrically-controlled valve on cold water plastic conveying and plastic pipe (1) to defeated in the high-temperature steam thermal treatment zone (5-1)
Send cold water, control system (7) starts solar light collecting device (4) and absorbs luminous energy convert it into heat energy simultaneously, heat energy and then
It is transitioned into high-temperature steam instrument (3) inside, control system (7) starts high-temperature steam instrument (3) and becomes the water heating evaporation of internal reservoir
Vapor, high-temperature water vapor is delivered to high temperature and steams by the electrically-controlled valve that now control system (7) is opened in high-temperature steam delivery pipe (2)
In cold water in the vapour thermal treatment zone (5-1), provide thermal source for heating process；In the process, a water temperature detector (5-2) is real-time
Water temperature condition in the monitoring high-temperature steam thermal treatment zone (5-1), when a water temperature detector (5-2) detects the high-temperature steam thermal treatment zone
(5-1), when the water temperature in is less than 40 DEG C, the signal of telecommunication is sent to control system (7), control system by a water temperature detector (5-2)
(7) control solar light collecting device (4) to increase and adopt heat；
2nd step：The internal warm water after first heating in the high-temperature steam thermal treatment zone (5-1) flows into secondary electricity by drainage disc (5-5)
In heating tank (5-3), control system (7) starts stacked heating energising head (5-4) and warm water is heated further, in heating process
In, water temperature condition in the secondary electrical heating tank (5-3) of No. two warm water temperature detector (5-7) real-time monitorings, when No. two warm water temperature detectors
When the water temperature that survey instrument (5-7) detects in secondary electrical heating tank (5-3) reaches 85 DEG C～100 DEG C, No. two warm water temperature detector (5-
7) signal of telecommunication is sent to control system (7), control system (7) cut-out stacked heating energising head (5-4) power supply stops heating, with
Save energy；
3rd step：Heat in energising head (5-4) heating process in stacked, energising head rate of heat addition detector (5-6) is to the rate of heat addition
Carry out real-time monitoring, when head rate of heat addition detector (5-6) that is energized detects the rate of heat addition and is less than 45%, energising head heating speed
The signal of telecommunication is sent to control system (7) by rate detector (5-6), and control system (7) controls stacked heating energising head (5-4) to increase
Heat fan-out capability；
4th step：After the completion for the treatment of hot water heating, the electrically-controlled valve that control system (7) is opened on hot water plastic water outlet pipe (6) is defeated by hot water
Deliver in each residential building or office building water supply line.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610907610.9A CN106482211B (en) | 2016-10-18 | 2016-10-18 | Energy saving dual-heated system and its working method in a kind of processing of residents in rural community |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610907610.9A CN106482211B (en) | 2016-10-18 | 2016-10-18 | Energy saving dual-heated system and its working method in a kind of processing of residents in rural community |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN106482211A true CN106482211A (en) | 2017-03-08 |
| CN106482211B CN106482211B (en) | 2019-03-15 |
Family
ID=58270213
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610907610.9A Active CN106482211B (en) | 2016-10-18 | 2016-10-18 | Energy saving dual-heated system and its working method in a kind of processing of residents in rural community |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106482211B (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112361621A (en) * | 2020-11-09 | 2021-02-12 | 东营市富宏光热石油工程有限公司 | Phase-change energy storage heat exchange device |
Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2807136Y (en) * | 2005-06-24 | 2006-08-16 | 王发明 | Solar water heater |
| GB2491568A (en) * | 2011-05-31 | 2012-12-12 | Edmund Atkinson | Solar water heating system having a drain back |
| CN102887556A (en) * | 2012-03-06 | 2013-01-23 | 吴宣湖 | Solar seawater desalinization machine, water distillator and solar boiler |
| CN203478162U (en) * | 2013-08-12 | 2014-03-12 | 王文杰 | Solar steam generator |
| CN203619312U (en) * | 2013-12-20 | 2014-06-04 | 欧光辉 | Solar steam kettle |
| CN203656882U (en) * | 2013-12-20 | 2014-06-18 | 欧光辉 | Solar heat exchange continuous steam supply system |
| CN204301330U (en) * | 2014-11-26 | 2015-04-29 | 王文杰 | A kind of dual intensity solar concentrator |
| CN204854437U (en) * | 2015-08-05 | 2015-12-09 | 南京星环能源科技有限公司 | Heat -retaining formula heat exchanger |
-
2016
- 2016-10-18 CN CN201610907610.9A patent/CN106482211B/en active Active
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2807136Y (en) * | 2005-06-24 | 2006-08-16 | 王发明 | Solar water heater |
| GB2491568A (en) * | 2011-05-31 | 2012-12-12 | Edmund Atkinson | Solar water heating system having a drain back |
| CN102887556A (en) * | 2012-03-06 | 2013-01-23 | 吴宣湖 | Solar seawater desalinization machine, water distillator and solar boiler |
| CN203478162U (en) * | 2013-08-12 | 2014-03-12 | 王文杰 | Solar steam generator |
| CN203619312U (en) * | 2013-12-20 | 2014-06-04 | 欧光辉 | Solar steam kettle |
| CN203656882U (en) * | 2013-12-20 | 2014-06-18 | 欧光辉 | Solar heat exchange continuous steam supply system |
| CN204301330U (en) * | 2014-11-26 | 2015-04-29 | 王文杰 | A kind of dual intensity solar concentrator |
| CN204854437U (en) * | 2015-08-05 | 2015-12-09 | 南京星环能源科技有限公司 | Heat -retaining formula heat exchanger |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112361621A (en) * | 2020-11-09 | 2021-02-12 | 东营市富宏光热石油工程有限公司 | Phase-change energy storage heat exchange device |
| CN112361621B (en) * | 2020-11-09 | 2022-03-22 | 东营市富宏光热石油工程有限公司 | Phase-change energy storage heat exchange device |
Also Published As
| Publication number | Publication date |
|---|---|
| CN106482211B (en) | 2019-03-15 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN106482211A (en) | Energy-conservation dual-heated system and its method of work in a kind of residents in rural community process | |
| CN206266544U (en) | A kind of automatic distillation Brewing equipment | |
| CN205119209U (en) | Heating system is united to production and use of marsh gas biological energy source and solar energy | |
| CN207065534U (en) | A kind of electrode type steam boiler | |
| CN205655507U (en) | Vacuum tube type solar water heater | |
| CN110260336A (en) | A kind of farm's distributed energy utilization system | |
| CN105462830B (en) | A kind of methane-generating pit for farm household temperature-increasing system with diaphragm type heat-transfer pipe | |
| CN201032225Y (en) | Heating and bathing dual-purpose solar water heater | |
| CN107759046A (en) | A kind of domestic birds and animals excrement installation for fermenting | |
| CN207143064U (en) | A kind of solar energy auxiliary heating type pigsty biogas fermentation device | |
| CN209144142U (en) | Biogas comprehensive utilization system | |
| CN207299564U (en) | A kind of calking corrugated plate type solar energy air heat collector | |
| CN106066098B (en) | A kind of megastore's dedicated full-automatic drinking water heating automatic control system and its self-con-tained unit | |
| CN207299563U (en) | A kind of wavy metal screen mesh type solar energy air heat collector | |
| CN206410338U (en) | A kind of retractable solar heat collector | |
| CN206428807U (en) | A kind of environment-friendly novel building | |
| CN205641609U (en) | Solar water heater's water tank structure | |
| CN205939740U (en) | Energy -efficient combination formula solar heat pump hot water unit | |
| CN108559706A (en) | A kind of methane-generating pit heats regulating device | |
| CN207918848U (en) | A kind of biomass energy solar energy composite utilizes heating system | |
| CN203687398U (en) | Non-bearing balcony wall-mounted solar water heater | |
| CN109405042A (en) | A kind of biomass energy radiant type heat supply stove | |
| CN213603693U (en) | Automatic spraying device for livestock | |
| CN214664753U (en) | Solar steam-water heat collection multipurpose heating system | |
| CN216557716U (en) | Auxiliary heater with good heating effect for solar water heater |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| TA01 | Transfer of patent application right | ||
| TA01 | Transfer of patent application right |
Effective date of registration: 20190219 Address after: 221000 Jiangsu Xuzhou hi tech Industrial Development Zone Subdistrict Office -119 31 Applicant after: Xuzhou Tengrui Intelligent Equipment Co., Ltd. Address before: 221018 Xuzhou Institute of technology, 2 Lishui Road, new town, Xuzhou, Jiangsu Applicant before: Xuzhou Institute of Technology |
|
| GR01 | Patent grant | ||
| GR01 | Patent grant |