CN106482211B - Energy saving dual-heated system and its working method in a kind of processing of residents in rural community - Google Patents
Energy saving dual-heated system and its working method in a kind of processing of residents in rural community Download PDFInfo
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- CN106482211B CN106482211B CN201610907610.9A CN201610907610A CN106482211B CN 106482211 B CN106482211 B CN 106482211B CN 201610907610 A CN201610907610 A CN 201610907610A CN 106482211 B CN106482211 B CN 106482211B
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- 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
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- 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
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Abstract
The invention discloses energy saving dual-heated system and its working methods in a kind of processing of residents in rural community, by cold water plastics delivery 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 composition；High-temperature steam heating tank side is equipped with cold water plastics delivery pipe, the high-temperature steam heating tank other side is equipped with hot water plastic water outlet pipe, the high-temperature steam heating tank overhead surface is equipped with high-temperature steam instrument, high-temperature steam instrument two sides are equipped with high-temperature steam delivery pipe, the high-temperature steam instrument overhead surface is equipped with solar light collecting device, and the control system is located at one side position of high-temperature steam heating tank.Energy saving dual-heated system and its working method novel and reasonable structure in a kind of residents in rural community processing of the present invention, heating efficiency is efficient, and the scope of application is wide.
Description
Technical field
The invention belongs to environmentally friendly class fields, and in particular in a kind of processing of residents in rural community energy saving dual-heated system and
Its working method.
Background technique
Heat source used in house refuse heating system at present generally uses single conventional energy resource, such as gas fired-boiler, grill pan
Furnace and oil burning boiler etc..With the anxiety of energy resource structure, the utilization of renewable energy has become inexorable trend, this not only contributes to save
Energy emission reduction, is 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 provides the novel energy-conserving heat-supplying mode of heat as solar energy acquisition system, using hot water or heating as 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 compositions 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, effect is by being set to the heat collector of lighting surface most
Heat is collected to limits, 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 of type forms, and as the supplement of house refuse solar thermal collection system, house refuse auxiliary system can be continuous
When rainy weather or other special heating demands, meet heat supply and house refuse supplying hot water demand.
Under normal conditions, it if house refuse solar heating system is only used for independent hot-water supply or heating, generally sets
A house refuse heat storage water tank is set, effect is storage hot water, and heat is also transmitted to heating terminal for heating system.If
House refuse solar energy system should hot-water supply heat again, then need at least be arranged a house refuse heat storage water tank and one
Platform house refuse heat exchanger, such setting space occupied is big, and heat waste also increases.Its height of the house refuse heat storage water tank of cylinder
It is generally 0.85~1.15 with the ratio of diameter, the house refuse water tank of such ratio, internal hot-water is unable to reach to be divided very well
The effect of layer, and the water tank does not have both the function of heat exchanger.
Existing house refuse heating system, complex process take up a large area, and cold/heat exchange efficiency is low, the prior art
It is unable to satisfy house refuse energy requirement.
Summary of the invention
In order to solve the above technical problem, the present invention provides energy saving dual-heated systems in a kind of processing of residents in rural community
System, comprising: cold water plastics delivery 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；5 side of high-temperature steam heating tank is equipped with cold water plastics delivery pipe 1,
5 other side of high-temperature steam heating tank is equipped with hot water plastic water outlet pipe 6, and 5 overhead surface of high-temperature steam heating tank is equipped with
High-temperature steam instrument 3,3 two sides of high-temperature steam instrument are equipped with high-temperature steam delivery pipe 2, and 3 overhead surface of high-temperature steam instrument is set
There is solar light collecting device 4, the control system 7 is located at 5 one side position of high-temperature steam heating tank；
Electrically-controlled valve in the cold water plastics delivery pipe 1, the electrically-controlled valve in high-temperature steam delivery pipe 2, the water outlet of hot water plastics
Electrically-controlled valve, high-temperature steam instrument 3 and solar light collecting device 4 on pipe 6 are connect with 7 polygon control survey of control system respectively.
Further, the high-temperature steam heating tank 5 includes: high-temperature steam heating zone 5-1, No.1 water temperature detector 5-2,
Secondary electrical heating tank 5-3, stacked heat energization head 5-4, drainage disc 5-5, energization head rate of heat addition detector 5-6, No. two warm water
Warm detector 5-7；The high-temperature steam heating zone 5-1 is wrapped up by cylindrical shell, high-temperature steam heating zone 5-1 shell by
Heat Conduction Material does not form, and high-temperature steam heating zone 5-1 total height is no less than 1.2m；The No.1 water temperature detector 5-2 is located at height
Warm steam heating zone 5-1 side wall, No.1 water temperature detector 5-2 are connect with 7 polygon control survey of control system；The secondary electrical heating tank
5-3 is located inside the 5-1 of high-temperature steam heating zone, and secondary electrical heating tank 5-3 is overlapped with high-temperature steam heating zone 5-1 central axis,
The bottom secondary electrical heating tank 5-3 is away from the high-temperature steam heating zone bottom 5-1 30cm~45cm, and secondary electrical heating tank 5-3 diameter is than high
The warm steam heating zone small 5cm~15cm of diameter；The stacked heating energization head 5-4 is located in secondary electrical heating tank 5-3, and stacked adds
Hot energization head 5-4 is overlapped with secondary electrical heating tank 5-3 central axis；It is flat that the drainage disc 5-5 is located at the bottom secondary electrical heating tank 5-3
Face, the baseplane drainage disc 5-5 and secondary electrical heating tank 5-3 seamless welding are fixed, drainage disc 5-5 maximum diameter and secondary electrical heating tank
5-3 diameter is identical；The energization head rate of heat addition detector 5-6 is located at secondary electrical heating tank 5-3 internal side wall, the heating of energization head
Rate detector is connect with 7 polygon control survey of control system；No. two warm water temperature detector 5-7 is located at secondary electrical heating tank 5-3
Internal side wall, No. two warm water temperature detector 5-7 are connect with 7 polygon control survey of control system.
Further, stacked heating energization head 5-4 includes: vertical blade 5-4-1, horizontal blade 5-4-2, and cathode is led
Electric column 5-4-3, anode conducting column 5-4-4；The vertical blade 5-4-1 shape is in rectangular sheet, multiple vertical blade 5-4-1
With stacked heating energization head 5-4 center axis uniform circular arrangement, vertical blade 5-4-1 quantity is no less than 6 pieces, and adjacent two
Vertical 30 °~60 ° of angle of blade 5-4-1；The horizontal blade 5-4-2 shape is round pie, and horizontal blade 5-4-2 is set in perpendicular
The surface prismatic blade 5-4-1, horizontal blade 5-4-2 quantity are no less than 2 pieces, and horizontal blade 5-4-2 or more is parallel evenly distributed, adjacent
Two horizontal blade 5-4-2 spacing 60mm~150mm；The cathode conductive column 5-4-3 is located at vertical blade 5-4-1 overhead surface,
Cathode conductive column 5-4-3 and the control of 7 cathode conductor of control system connect；The anode conducting column 5-4-4 is located at vertical blade 5-
4-1 underlying surfaces, anode conducting column 5-4-4 and the control of 7 positive wire of control system connect.
Further, the drainage disc 5-5 includes: " V " type circumferential section 5-5-1, boss through-hole 5-5-2；" V " type
Circumferential section 5-5-1 wall thickness 3mm~5mm, " V " type circumferential section 5-5-1 are described bowl-shape by being rotated by 360 ° to form bowl structure
Structure outer diameter inclined-plane angle with horizontal plane is β, and the β value range is 30 °~65 °；The trapezoidal cylinder of the boss through-hole 5-5-2
Hollow body structure, the aperture boss through-hole 5-5-2 is up-small and down-big, and boss through-hole 5-5-2 inclined-plane angle with horizontal plane is α, the α model
Enclosing value is 40 °~70 °.
Further, the stacked heating energization head 5-4 is formed by high molecular material pressing mold, and stacked heats energization head 5-4
Constituent and manufacturing process it is as follows:
One, stacked heats energization head 5-4 constituent:
According to parts by weight, 53~133 parts of polyallylmethacrylate, butyl -2- methyl -2- acrylate 73~
133 parts, 123~233 parts of Tributyl Tin Methacrylate, 73~183 parts of 2- butyl methacrylate, metering system triphenyl phosphate
63~133 parts of base methyl esters, 113~233 parts of acrylate of 3- tri-chlorination tinbase, concentration is the ethyl acrylate of 43ppm~83ppm
73~113 parts of base trimethyl ammonium chloride, third 63~123 parts of (alcohol) ester of 2- methacrylic acid -3- (methyl dichloro silicon substrate), acetic acid -
63~153 parts of chlorallylene ester, 83~153 parts of crosslinking agent, β -43~123 parts of trichlorine tinbase propionic ester, carboxylic acid beta-hydroxy (chlorine)
73~163 parts of propyl ester, 33~63 parts of the chloro- beta-hydroxyphenyl methyl propionate of α -, β -33~113 parts of alkoxy carbonyl group propyl tin trichloride；
The crosslinking agent is beta-hydroxy-alpha-aromatic acrylate, methacrylic acid β hydroxyl ethyl ester, senecioate-hydroxy methacrylate
In any one；
Two, the manufacturing process of stacked heating energization head 5-4 comprising the steps of:
Step 1: being added 513~1103 parts of ultrapure water that conductivity is 0.33 μ of μ S/cm~0.63 S/cm in a kettle,
Start reaction kettle in blender, revolving speed be 83rpm~223rpm, start heat pump, make reactor temperature rise to 53 DEG C~
63℃；Polyallylmethacrylate, butyl -2- methyl -2- acrylate, Tributyl Tin Methacrylate are sequentially added,
To being completely dissolved, adjusting pH value is 1.3~6.3 for stirring, and agitator speed is adjusted to 113rpm~233rpm, temperature is 73 DEG C~
143 DEG C, esterification 13~23 hours；
Step 2: taking 2- butyl methacrylate, methacrylic acid triphenylmethyl to be crushed, powder diameter be 203~
633 mesh；Add 3- tri-chlorination tinbase crylic acid ester mixture uniform, be laid in pallet, tiles with a thickness of 13mm~43mm, using agent
The alpha ray that amount is 1.3kGy~9.3kGy, energy is 5.3MeV~13MeV irradiates 43~123 minutes and the same dose of β
X ray irradiation x 63~153 minutes；
Step 3: the mixed-powder handled through step 2 is dissolved in ethylacrylate-trimethylammonium chloride, and reaction kettle is added,
Agitator speed be 73rpm~173rpm, temperature be 83 DEG C~133 DEG C, starting vacuum pump make the vacuum degree of reaction kettle reach-
0.73MPa~-0.33MPa, keeps this state response 13~43 hours；Pressure release is simultaneously passed through nitrogen, makes reacting kettle inner pressure
0.23MPa~0.63MPa, heat preservation stand 13~23 hours；Agitator speed is promoted to 103rpm~243rpm, simultaneous reactions kettle
Pressure release is to 0MPa；It is complete to sequentially add third (alcohol) ester of 2- methacrylic acid -3- (methyl dichloro silicon substrate), acetic acid-chlorallylene ester
After dissolution, crosslinking agent is added and is stirred, so that the hydrophilic lipophilic balance of reaction kettle solution is 3.3~6.3, heat preservation stands 13
~23 hours；
Step 4: when agitator speed is 123rpm~253rpm, β-trichlorine tinbase propionic ester, carboxylic acid β-is sequentially added
Hydroxyl (chlorine) propyl ester, the chloro- beta-hydroxyphenyl methyl propionate of α-, β-alkoxy carbonyl group propyl tin trichloride promote reactor pressure, make it
Reach 0.73MPa~1.53MPa, temperature is 123 DEG C~263 DEG C, polymerization reaction 13~33 hours；After the reaction was completed by reaction kettle
Interior pressure is down to 0MPa, is cooled to 23 DEG C~33 DEG C, discharging, entering molding press can be prepared by stacked heating energization head 5-4.
The invention also discloses the working method of energy saving dual-heated system in a kind of processing of residents in rural community, this method
Including the following steps:
Step 1: the electrically-controlled valve that control system 7 is opened in cold water plastics delivery pipe 1 is conveyed into high-temperature steam heating zone 5-1
Cold water, while control system 7 starts solar light collecting device 4 and absorbs luminous energy and convert it into thermal energy, thermal energy is transitioned into turn
Inside high-temperature steam instrument 3, control system 7 starts high-temperature steam instrument 3 for the water heating evaporation of internal reservoir into vapor, this time control
High-temperature water vapor is delivered to cold in the 5-1 of high-temperature steam heating zone by the electrically-controlled valve that system 7 processed opens in high-temperature steam delivery pipe 2
In water, heat source is provided for heating process；In the process, No.1 water temperature detector 5-2 real-time monitoring high-temperature steam heating zone 5-1
Interior water temperature condition, when No.1 water temperature detector 5-2 detects the water temperature in the 5-1 of high-temperature steam heating zone lower than 40 DEG C, one
Electric signal is sent to control system 7 by number water temperature detector 5-2, and control system 7 controls the increasing of solar light collecting device 4 and adopts heat
Amount；
Step 2: the warm water inside the 5-1 of high-temperature steam heating zone after heating for the first time flows into secondary electricity by drainage disc 5-5
In heating tank 5-3, control system 7 starts stacked heating energization head 5-4 and further heats to warm water, during heating, No. two
Water temperature condition in the secondary electrical heating tank 5-3 of warm water temperature detector 5-7 real-time monitoring, when No. two warm water temperature detector 5-7 are detected
When reaching 85 DEG C~100 DEG C to the water temperature in secondary electrical heating tank 5-3, electric signal is sent to by No. two warm water temperature detector 5-7
Control system 7, control system 7 cuts off stacked heating energization head 5-4 power supply and stops heating, to save the energy；
Step 3: in stacked heating energization head 5-4 heating process, energization head rate of heat addition detector 5-6 is to the rate of heat addition
Real-time monitoring is carried out, when energization head rate of heat addition detector 5-6 detects the rate of heat addition lower than 45%, the energization head rate of heat addition
Electric signal is sent to control system 7 by detector 5-6, and control system 7 controls stacked heating energization head 5-4 and increases heat output energy
Power；
Step 4: after the completion 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
It send into each residential building or office building water supply line.
Energy saving dual-heated system and its working method in a kind of processing of residents in rural community disclosed in the invention patent,
Advantage is:
(1) device uses solar light collecting device, and energy saving rate is high；
(2) apparatus structure design is rationally compact, and integrated level is high；
(3) device stacked heating energization head is prepared using high molecular material, and heating speed conservation rate is promoted significant.
Energy saving dual-heated system and its working method structure are new in a kind of residents in rural community processing of the present invention
Clever reasonable, heating efficiency is efficient, and the scope of application is wide.
Detailed description of the invention
Fig. 1 is energy saving dual-heated system schematic in a kind of heretofore described residents in rural community processing.
Fig. 2 is heretofore described high-temperature steam heating tank schematic diagram of internal structure.
Fig. 3 is heretofore described stacked heating energization 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 energization head material of the present invention and heating speed conservation rate relational graph.
In figure 1 above~Fig. 5, cold water plastics delivery 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 heating zone 5-1, No.1 water temperature detector 5-2, secondary electrical heating tank 5-3 are folded
Formula heat energization head 5-4, vertical blade 5-4-1, horizontal blade 5-4-2, cathode conductive column 5-4-3, anode conducting column 5-4-4,
Drainage disc 5-5, " V " type circumferential section 5-5-1, boss through-hole 5-5-2, energization 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
With reference to the accompanying drawings and examples to energy saving dual-heated in a kind of residents in rural community processing provided by the invention
System is further described.
As shown in Figure 1, being the signal of energy saving dual-heated system in a kind of residents in rural community processing provided by the invention
Figure.Find out in figure, comprising: cold water plastics delivery 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；5 side of high-temperature steam heating tank is equipped with cold water plastics
Delivery pipe 1,5 other side of high-temperature steam heating tank are equipped with hot water plastic water outlet pipe 6,5 top of high-temperature steam heating tank
Surface is equipped with high-temperature steam instrument 3, and 3 two sides of high-temperature steam instrument are equipped with high-temperature steam delivery pipe 2, on the high-temperature steam instrument 3
Square surface is equipped with solar light collecting device 4, and the control system 7 is located at 5 one side position of high-temperature steam heating tank；The cold water modeling
Electrically-controlled valve on material conveying tube 1, the electrically-controlled valve in high-temperature steam delivery pipe 2, the electrically-controlled valve on hot water plastic water outlet pipe 6, high temperature
Steam instrument 3 and solar light collecting device 4 are connect with 7 polygon control survey of control system respectively.
As shown in Fig. 2, being heretofore described high-temperature steam heating tank schematic diagram of internal structure.From Fig. 2 or Fig. 1
Out, the high-temperature steam heating tank 5 includes: high-temperature steam heating zone 5-1, No.1 water temperature detector 5-2, secondary electrical heating tank 5-
3, stacked heats energization head 5-4, drainage disc 5-5, the energization head rate of heat addition detector 5-6, No. two warm water temperature detector 5-7；Institute
It states high-temperature steam heating zone 5-1 to be wrapped up by cylindrical shell, high-temperature steam heating zone 5-1 shell is by not Heat Conduction Material group
At high-temperature steam heating zone 5-1 total height is no less than 1.2m；The No.1 water temperature detector 5-2 is located at high-temperature steam heating zone
5-1 side wall, No.1 water temperature detector 5-2 are connect with 7 polygon control survey of control system；The secondary electrical heating tank 5-3 is located at high temperature
Inside the 5-1 of steam heating zone, secondary electrical heating tank 5-3 is overlapped with high-temperature steam heating zone 5-1 central axis, secondary electrical heating tank
The bottom 5-3 is away from the high-temperature steam heating zone bottom 5-1 30cm~45cm, and secondary electrical heating tank 5-3 diameter is than high-temperature steam heating zone
Small 5cm~the 15cm of diameter；The stacked heating energization head 5-4 is located in secondary electrical heating tank 5-3, and stacked heats energization head 5-4
It is overlapped with secondary electrical heating tank 5-3 central axis；The drainage disc 5-5 is located at the baseplane secondary electrical heating tank 5-3, drainage disc 5-
5 fix with the baseplane secondary electrical heating tank 5-3 seamless welding, drainage disc 5-5 maximum diameter and secondary electrical heating tank 5-3 diameter phase
Together；The energization head rate of heat addition detector 5-6 is located at secondary electrical heating tank 5-3 internal side wall, the detection of the energization head rate of heat addition
Instrument is connect with 7 polygon control survey of control system；No. two warm water temperature detector 5-7 is located at secondary electrical heating tank 5-3 internal side wall,
No. two warm water temperature detector 5-7 are connect with 7 polygon control survey of control system.
As shown in figure 3, being heretofore described stacked heating energization header structure schematic diagram.Find out from Fig. 3 or Fig. 2,
The stacked heating energization head 5-4 includes: vertical blade 5-4-1, horizontal blade 5-4-2, cathode conductive column 5-4-3, and anode is led
Electric column 5-4-4；The vertical blade 5-4-1 shape is in rectangular sheet, and multiple vertical blade 5-4-1 heat energization head with stacked
The arrangement of 5-4 center axis uniform circular, vertical blade 5-4-1 quantity are no less than 6 pieces, adjacent two vertical blade 5-4-1 folder
30 °~60 ° of angle；The horizontal blade 5-4-2 shape 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 are no less than 2 pieces, parallel evenly distributed, the adjacent two horizontal blades 5- of horizontal blade 5-4-2 or more
4-2 spacing 60mm~150mm；The cathode conductive column 5-4-3 is located at vertical blade 5-4-1 overhead surface, cathode conductive column 5-
4-3 and the control of 7 cathode conductor of control system connect；The anode conducting column 5-4-4 is located at vertical blade 5-4-1 underlying surfaces,
Anode conducting column 5-4-4 and the control of 7 positive wire of control system connect.
It as shown in Figure 4, Figure 5, is heretofore described drainage disc three dimensional structure diagram and schematic cross-section.From Fig. 4
Or find out in Fig. 5, the drainage disc 5-5 includes: " V " type circumferential section 5-5-1, boss through-hole 5-5-2；" V " the type circumference
Section 5-5-1 wall thickness 3mm~5mm, " V " type circumferential section 5-5-1 are by being rotated by 360 ° to form bowl structure, the bowl structure
Outer diameter inclined-plane angle with horizontal plane is β, and the β value range is 30 °~65 °；The trapezoidal cylinder hollow of the boss through-hole 5-5-2
Body structure, the aperture boss through-hole 5-5-2 is up-small and down-big, and boss through-hole 5-5-2 inclined-plane angle with horizontal plane is α, the α value range
It is 40 °~70 °.
The course of work of energy saving dual-heated system is in a kind of residents in rural community processing of the present invention:
Step 1: the electrically-controlled valve that control system 7 is opened in cold water plastics delivery pipe 1 is conveyed into high-temperature steam heating zone 5-1
Cold water, while control system 7 starts solar light collecting device 4 and absorbs luminous energy and convert it into thermal energy, thermal energy is transitioned into turn
Inside high-temperature steam instrument 3, control system 7 starts high-temperature steam instrument 3 for the water heating evaporation of internal reservoir into vapor, this time control
High-temperature water vapor is delivered to cold in the 5-1 of high-temperature steam heating zone by the electrically-controlled valve that system 7 processed opens in high-temperature steam delivery pipe 2
In water, heat source is provided for heating process；In the process, No.1 water temperature detector 5-2 real-time monitoring high-temperature steam heating zone 5-1
Interior water temperature condition, when No.1 water temperature detector 5-2 detects the water temperature in the 5-1 of high-temperature steam heating zone lower than 40 DEG C, one
Electric signal is sent to control system 7 by number water temperature detector 5-2, and control system 7 controls the increasing of solar light collecting device 4 and adopts heat
Amount；
Step 2: the warm water inside the 5-1 of high-temperature steam heating zone after heating for the first time flows into secondary electricity by drainage disc 5-5
In heating tank 5-3, control system 7 starts stacked heating energization head 5-4 and further heats to warm water, during heating, No. two
Water temperature condition in the secondary electrical heating tank 5-3 of warm water temperature detector 5-7 real-time monitoring, when No. two warm water temperature detector 5-7 are detected
When reaching 85 DEG C~100 DEG C to the water temperature in secondary electrical heating tank 5-3, electric signal is sent to by No. two warm water temperature detector 5-7
Control system 7, control system 7 cuts off stacked heating energization head 5-4 power supply and stops heating, to save the energy；
Step 3: in stacked heating energization head 5-4 heating process, energization head rate of heat addition detector 5-6 is to the rate of heat addition
Real-time monitoring is carried out, when energization head rate of heat addition detector 5-6 detects the rate of heat addition lower than 45%, the energization head rate of heat addition
Electric signal is sent to control system 7 by detector 5-6, and control system 7 controls stacked heating energization head 5-4 and increases heat output energy
Power；
Step 4: after the completion 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
It send into each residential building or office building water supply line.
Energy saving dual-heated system and its working method structure are new in a kind of residents in rural community processing of the present invention
Clever reasonable, heating efficiency is efficient, and the scope of application is wide.
It is the embodiment of the manufacturing process of stacked of the present invention heating energization head 5-4 below, embodiment is in order into one
Step illustrates the contents of the present invention, but should not be construed as limiting the invention.In the situation without departing substantially from spirit of that invention and essence
Under, it to modification made by the method for the present invention, step or condition and replaces, all belongs to the scope of the present invention.
Unless otherwise specified, the conventional means that technological means used in embodiment is well known to those skilled in the art.
Embodiment 1
Stacked heating energization head 5-4 of the present invention, and score meter by weight are manufactured according to the following steps:
Step 1: 513 parts of ultrapure water that conductivity is 0.33 μ S/cm, stirring in starting reaction kettle are added in a kettle
Device, revolving speed 83rpm start heat pump, reactor temperature are made to rise to 53 DEG C；Sequentially add polyallylmethacrylate
53 parts, 73 parts, 123 parts of Tributyl Tin Methacrylate of butyl -2- methyl -2- acrylate, stirring are adjusted to being completely dissolved
PH value is 1.3, agitator speed is adjusted to 113rpm, temperature is 73 DEG C, esterification 13 hours；
Step 2: take 73 parts of 2- butyl methacrylate, 63 parts of methacrylic acid triphenylmethyl crushed, powder grain
Diameter is 203 mesh；Add 113 parts of acrylate of 3- tri-chlorination tinbase to be uniformly mixed, be laid in pallet, tiles with a thickness of 13mm, adopt
It is irradiated 43 minutes and the same dose of β x ray irradiation xs 63 minutes with the alpha ray that dosage is 1.3kGy, energy is 5.3MeV；
Step 3: the mixed-powder handled through step 2 is dissolved in the ethylacrylate-trimethylammonium chloride that concentration is 43ppm
In 73 parts, reaction kettle, agitator speed 73rpm is added, temperature is 83 DEG C, and starting vacuum pump reaches the vacuum degree of reaction kettle
To -0.73MPa, this state response is kept 13 hours；Pressure release is simultaneously passed through nitrogen, makes reacting kettle inner pressure 0.23MPa, keeps the temperature quiet
It sets 13 hours；Agitator speed is promoted to 103rpm, simultaneous reactions kettle pressure release to 0MPa；Sequentially add 2- methacrylic acid -3-
After 63 parts of (methyl dichloro silicon substrate) third (alcohol) ester, acetic acid -63 parts of chlorallylene ester are completely dissolved, it is mixed that 83 parts of crosslinking agent stirrings are added
It closes, so that the hydrophilic lipophilic balance of reaction kettle solution is 3.3, heat preservation stands 13 hours；
Step 4: when agitator speed is 123rpm, β -43 parts of trichlorine tinbase propionic ester, carboxylic acid beta-hydroxy is sequentially added
33 parts of the chloro- beta-hydroxyphenyl methyl propionate of 73 parts of (chlorine) propyl ester, α -, β -33 parts of alkoxy carbonyl group propyl tin trichloride promote reaction kettle
Pressure, reaches 0.73MPa, and temperature is 123 DEG C, polymerization reaction 13 hours；Reacting kettle inner pressure is down to after the reaction was completed
0MPa is cooled to 23 DEG C, and discharging, entering molding press can be prepared by stacked heating energization head 5-4；
The crosslinking agent is beta-hydroxy-alpha-aromatic acrylate.
Embodiment 2
Stacked heating energization head 5-4 of the present invention, and score meter by weight are manufactured according to the following steps:
Step 1: 1103 parts of ultrapure water that conductivity is 0.63 μ S/cm, stirring in starting reaction kettle are added in a kettle
Device, revolving speed 223rpm start heat pump, reactor temperature are made to rise to 63 DEG C；Sequentially add polymethylacrylic acid allyl
133 parts of ester, 133 parts, 233 parts of Tributyl Tin Methacrylate of butyl -2- methyl -2- acrylate, stirring to being completely dissolved,
Adjusting pH value is 6.3, agitator speed is adjusted to 233rpm, temperature is 143 DEG C, esterification 23 hours；
Step 2: take 183 parts of 2- butyl methacrylate, 133 parts of methacrylic acid triphenylmethyl crushed, powder
Partial size is 633 mesh；Add 233 parts of acrylate of 3- tri-chlorination tinbase to be uniformly mixed, be laid in pallet, tiles with a thickness of 43mm,
The alpha ray for using dosage to be 13MeV for 9.3kGy, energy irradiates 123 minutes and the same dose of β x ray irradiation xs 153 divide
Clock；
Step 3: the mixed-powder handled through step 2 is dissolved in the ethylacrylate-trimethylammonium chloride that concentration is 83ppm
In 113 parts, reaction kettle, agitator speed 173rpm is added, temperature is 133 DEG C, and starting vacuum pump makes the vacuum degree of reaction kettle
Reach -0.33MPa, keeps this state response 43 hours；Pressure release is simultaneously passed through nitrogen, makes reacting kettle inner pressure 0.63MPa, heat preservation
Stand 23 hours；Agitator speed is promoted to 243rpm, simultaneous reactions kettle pressure release to 0MPa；Sequentially add 2- methacrylic acid-
After third 123 parts of (alcohol) ester of 3- (methyl dichloro silicon substrate), acetic acid -153 parts of chlorallylene ester are completely dissolved, it is added 153 parts of crosslinking agent
It is stirred, so that the hydrophilic lipophilic balance of reaction kettle solution is 6.3, heat preservation stands 23 hours；
Step 4: when agitator speed is 253rpm, β -123 parts of trichlorine tinbase propionic ester, carboxylic acid beta-hydroxy is sequentially added
63 parts of the chloro- beta-hydroxyphenyl methyl propionate of 163 parts of (chlorine) propyl ester, α -, β -113 parts of alkoxy carbonyl group propyl tin trichloride promote reaction
Kettle pressure, reaches 1.53MPa, and temperature is 263 DEG C, polymerization reaction 33 hours；Reacting kettle inner pressure is dropped after the reaction was completed
To 0MPa, 33 DEG C are cooled to, discharging, entering molding press can be prepared by stacked heating energization head 5-4；
The crosslinking agent is senecioate-hydroxy methacrylate.
Embodiment 3
Stacked heating energization head 5-4 of the present invention, and score meter by weight are manufactured according to the following steps:
Step 1: 703 parts of ultrapure water that conductivity is 0.43 μ S/cm, stirring in starting reaction kettle are added in a kettle
Device, revolving speed 123rpm start heat pump, reactor temperature are made to rise to 59 DEG C；Sequentially add polymethylacrylic acid allyl
83 parts of ester, 93 parts, 153 parts of Tributyl Tin Methacrylate of butyl -2- methyl -2- acrylate, stirring are adjusted to being completely dissolved
Saving pH value is 4.3, agitator speed is adjusted to 183rpm, temperature is 93 DEG C, esterification 17 hours；
Step 2: take 113 parts of 2- butyl methacrylate, 83 parts of methacrylic acid triphenylmethyl crushed, powder grain
Diameter is 433 mesh；Add 183 parts of acrylate of 3- tri-chlorination tinbase to be uniformly mixed, be laid in pallet, tiles with a thickness of 33mm, adopt
It is irradiated 83 minutes and the same dose of β x ray irradiation xs 93 minutes with the alpha ray that dosage is 6.3kGy, energy is 10MeV；
Step 3: the mixed-powder handled through step 2 is dissolved in the ethylacrylate-trimethylammonium chloride that concentration is 73ppm
In 93 parts, reaction kettle, agitator speed 123rpm is added, temperature is 103 DEG C, and starting vacuum pump reaches the vacuum degree of reaction kettle
To -0.53MPa, this state response is kept 33 hours；Pressure release is simultaneously passed through nitrogen, makes reacting kettle inner pressure 0.43MPa, keeps the temperature quiet
It sets 17 hours；Agitator speed is promoted to 143rpm, simultaneous reactions kettle pressure release to 0MPa；Sequentially add 2- methacrylic acid -3-
After 93 parts of (methyl dichloro silicon substrate) third (alcohol) ester, acetic acid -93 parts of chlorallylene ester are completely dissolved, 113 parts of crosslinking agent stirrings are added
Mixing, so that the hydrophilic lipophilic balance of reaction kettle solution is 5.3, heat preservation stands 17 hours；
Step 4: when agitator speed is 153rpm, β -83 parts of trichlorine tinbase propionic ester, carboxylic acid beta-hydroxy is sequentially added
53 parts of the chloro- beta-hydroxyphenyl methyl propionate of 113 parts of (chlorine) propyl ester, α -, β -73 parts of alkoxy carbonyl group propyl tin trichloride promote reaction kettle
Pressure, reaches 1.13MPa, and temperature is 163 DEG C, polymerization reaction 23 hours；Reacting kettle inner pressure is down to after the reaction was completed
0MPa is cooled to 26 DEG C, and discharging, entering molding press can be prepared by stacked heating energization head 5-4；
The crosslinking agent is methacrylic acid β hydroxyl ethyl ester.
Reference examples
Reference examples are that the stacked of certain commercially available brand heats the service condition that energization head is used for heating process.
Embodiment 4
Stacked heating energization head described in the stacked heating energization head 5-4 and reference examples that Examples 1 to 3 is prepared is used
Compared in the service condition of heating process, and with bulk density value, use duration, high temperature strength enhancing rate, resistance to
Degree of corrosion enhancing rate is that technical indicator is counted, and the results are shown in Table 1:
Table 1 is that stacked described in Examples 1 to 3 and reference examples heats energization head for the parameters in heating process
Comparing result, as seen from Table 1, stacked of the present invention heat energization head 5-4, and bulk density value uses duration, resistance to
Elevated temperature strength enhancing rate, corrosion resistant erosion degree enhancing rate are above the product of prior art production.
In addition, as shown in fig. 6, being that stacked heating energization head 5-4 material and heating speed conservation rate of the present invention close
System's figure.Find out in figure, macromolecule stacked used in Examples 1 to 3 heats energization head 5-4, is better than in terms of heating speed conservation rate
Existing product.
Claims (5)
1. energy saving dual-heated system in a kind of residents in rural community processing, comprising: cold water plastics delivery 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, high-temperature steam heating tank (5) side is equipped with cold water plastics delivery pipe (1), institute
High-temperature steam heating tank (5) other side is stated equipped with hot water plastic water outlet pipe (6), high-temperature steam heating tank (5) overhead surface
Equipped with high-temperature steam instrument (3), high-temperature steam instrument (3) two sides are equipped with high-temperature steam delivery pipe (2), the high-temperature steam instrument
(3) overhead surface is equipped with solar light collecting device (4), and the control system (7) is located at high-temperature steam heating tank (5) side position
It sets；
Electrically-controlled valve on the cold water plastics delivery pipe (1), the electrically-controlled valve in high-temperature steam delivery pipe (2), the water outlet of hot water plastics
Electrically-controlled valve, high-temperature steam instrument (3) and the solar light collecting device (4) managed on (6) connect with control system (7) polygon control survey respectively
It connects；
The high-temperature steam heating tank (5) includes: high-temperature steam heating zone (5-1), No.1 water temperature detector (5-2), secondary electricity
Heating tank (5-3), stacked heat energization head (5-4), drainage disc (5-5), energization head rate of heat addition detector (5-6), No. two water
Warm detector (5-7)；The high-temperature steam heating zone (5-1) is wrapped up by cylindrical shell, high-temperature steam heating zone (5-1)
Shell is made of not Heat Conduction Material, and high-temperature steam heating zone (5-1) total height is no less than 1.2 m；The No.1 water temperature detector
(5-2) is located at high-temperature steam heating zone (5-1) side wall, and No.1 water temperature detector (5-2) and control system (7) polygon control survey connect
It connects；The secondary electrical heating tank (5-3) is located at high-temperature steam heating zone (5-1) inside, and secondary electrical heating tank (5-3) and high temperature steam
Vapour heating zone (5-1) central axis is overlapped, and the secondary electrical heating tank bottom (5-3) is away from 30 cm of the bottom high-temperature steam heating zone (5-1)
~45 cm, secondary electrical heating tank (5-3) diameter are the cm of 5 cm~15 smaller than high-temperature steam heating zone diameter；The stacked heating is logical
Dateline (5-4) is located in secondary electrical heating tank (5-3), and stacked heats energization head (5-4) and secondary electrical heating tank (5-3) central axis
Line is overlapped；The drainage disc (5-5) is located at the baseplane secondary electrical heating tank (5-3), drainage disc (5-5) and secondary electrical heating tank
The baseplane (5-3) seamless welding is fixed, and drainage disc (5-5) maximum diameter is identical as secondary electrical heating tank (5-3) diameter；The energization
Head rate of heat addition detector (5-6) is located at secondary electrical heating tank (5-3) internal side wall, energization head rate of heat addition detector and control
The connection of system (7) polygon control survey；No. two water temperature detectors (5-7) are located at secondary electrical heating tank (5-3) internal side wall, and No. two
Water temperature detector (5-7) is connect with control system (7) polygon control survey.
2. energy saving dual-heated system in a kind of residents in rural community processing according to claim 1, which is characterized in that institute
Stating stacked heating energization head (5-4) includes: vertical blade (5-4-1), horizontal blade (5-4-2), cathode conductive column (5-4-3),
Anode conducting column (5-4-4)；Vertical blade (5-4-1) shape is in rectangular sheet, and multiple vertical blades (5-4-1) are with folded
Formula heats the arrangement of energization head (5-4) center axis uniform circular, and vertical blade (5-4-1) quantity is no less than 6 pieces, and adjacent two
Vertical 30 °~60 ° of blade (5-4-1) angle；Horizontal blade (5-4-2) shape is round pie, horizontal blade (5-4-2)
It is set in the surface vertical blade (5-4-1), horizontal blade (5-4-2) quantity is no less than 2 pieces, and horizontal blade (5-4-2) is put down up and down
Evenly distributed, adjacent two horizontal blade (5-4-2) spacing, 60 mm of mm~150 of row；The cathode conductive column (5-4-3) is located at perpendicular
Prismatic blade (5-4-1) overhead surface, cathode conductive column (5-4-3) and the control of control system (7) cathode conductor connect；The anode
Conductive column (5-4-4) is located at vertical blade (5-4-1) underlying surfaces, and anode conducting column (5-4-4) is led with control system (7) anode
Line traffic control connection.
3. energy saving dual-heated system in a kind of residents in rural community processing according to claim 2, which is characterized in that institute
Stating drainage disc (5-5) includes: " V " type circumferential section (5-5-1), boss through-hole (5-5-2)；" V " type circumferential section (5-5-
1) wall thickness 3 mm~5 mm, " V " type circumferential section (5-5-1), which passes through, rotates 360 ° of formation bowl structures, outside the bowl structure
Diameter inclined-plane angle with horizontal plane is β, and the β value range is 30 °~65 °；The trapezoidal cylinder of boss through-hole (5-5-2) is empty
Heart body structure, the aperture boss through-hole (5-5-2) is up-small and down-big, and boss through-hole (5-5-2) inclined-plane angle with horizontal plane is α, the α
Value range is 40 °~70 °.
4. energy saving dual-heated system in a kind of residents in rural community processing according to claim 2, which is characterized in that institute
It states stacked heating energization head (5-4) to be formed by high molecular material pressing mold, stacked heats the constituent and manufacture of energization head (5-4)
Process is as follows:
One, stacked heats energization head (5-4) constituent:
According to parts by weight, 53~133 parts of polyallylmethacrylate, 73~133 parts of acrylate of butyl -2- methyl -2-,
123~233 parts of Tributyl Tin Methacrylate, 73~183 parts of 2- butyl methacrylate, methacrylic acid triphenylmethyl
63~133 parts, 113~233 parts of acrylate of 3- tri-chlorination tinbase, concentration is the ethyl acrylate base three of the ppm of 43 ppm~83
73~113 parts of ammonio methacrylate, third 63~123 parts of (alcohol) ester of 2- methacrylic acid -3- (methyl dichloro silicon substrate), acetic acid -3- chlorine
63~153 parts of acrylic ester, 83~153 parts of crosslinking agent, β -43~123 parts of trichlorine tinbase propionic ester, carboxylic acid beta-hydroxy (chlorine) propyl ester
73~163 parts, 33~63 parts of the chloro- beta-hydroxyphenyl methyl propionate of α -, β -33~113 parts of alkoxy carbonyl group propyl tin trichloride；
The crosslinking agent is beta-hydroxy-alpha-aromatic acrylate, in methacrylic acid β hydroxyl ethyl ester, senecioate-hydroxy methacrylate
Any one；
Two, the manufacturing process of stacked heating energization head (5-4) comprising the steps of:
Step 1: 513~1103 parts of ultrapure water that conductivity is 0.33 μ of μ S/cm~0.63 S/cm are added in a kettle, open
Blender in dynamic reaction kettle, revolving speed are the rpm of 83 rpm~223, start heat pump, make reactor temperature rise to 53 DEG C~
63 ℃；Polyallylmethacrylate, butyl -2- methyl -2- acrylate, Tributyl Tin Methacrylate are sequentially added,
To being completely dissolved, adjusting pH value is 1.3~6.3 for stirring, and agitator speed is adjusted to the rpm of 113 rpm~233, temperature 73
DEG C~143 DEG C, esterification 13~23 hours；
Step 2: taking 2- butyl methacrylate, methacrylic acid triphenylmethyl to be crushed, and powder diameter is 203~633
Mesh；Add 3- tri-chlorination tinbase crylic acid ester mixture uniform, be laid in pallet, tiles with a thickness of the mm of 13 mm~43, using agent
The alpha ray that amount is the kGy of 1.3 kGy~9.3, energy is the MeV of 5.3 MeV~13 irradiates 43~123 minutes and Isodose
β x ray irradiation x 63~153 minutes；
Step 3: the mixed-powder handled through step 2 is dissolved in ethylacrylate-trimethylammonium chloride, and reaction kettle, stirring is added
Device revolving speed be the rpm of 73 rpm~173, temperature be 83 DEG C~133 DEG C, starting vacuum pump make the vacuum degree of reaction kettle reach-
0.33 MPa of MPa~-0.73, keeps this state response 13~43 hours；Pressure release is simultaneously passed through nitrogen, makes reacting kettle inner pressure
The MPa of 0.23 MPa~0.63, heat preservation stand 13~23 hours；Agitator speed is promoted to the rpm of 103 rpm~243, while anti-
Answer kettle pressure release to 0MPa；Sequentially add third (alcohol) ester of 2- methacrylic acid -3- (methyl dichloro silicon substrate), acetic acid-chlorallylene ester
After being completely dissolved, crosslinking agent is added and is stirred, so that the hydrophilic lipophilic balance of reaction kettle solution is 3.3~6.3, keeps the temperature quiet
It sets 13~23 hours；
Step 4: when agitator speed is 123 rpm~253 rpm, β-trichlorine tinbase propionic ester, carboxylic acid β-hydroxyl are sequentially added
Base (chlorine) propyl ester, the chloro- beta-hydroxyphenyl methyl propionate of α-, β-alkoxy carbonyl group propyl tin trichloride promote reactor pressure, reach it
To the MPa of 0.73 MPa~1.53, temperature is 123 DEG C~263 DEG C, polymerization reaction 13~33 hours；It after the reaction was completed will reaction
Pressure is down to 0 MPa in kettle, is cooled to 23 DEG C~33 DEG C, discharging, entering molding press can be prepared by stacked heating energization head (5-
4).
5. the working method of energy saving dual-heated system in a kind of processing of residents in rural community, which is characterized in that this method includes
Following steps:
Step 1: the electrically-controlled valve that control system (7) is opened on cold water plastics delivery pipe (1) is defeated into high-temperature steam heating zone (5-1)
Cold water is sent, while control system (7) starting solar light collecting device (4) absorbs luminous energy and converts it into thermal energy, thermal energy is in turn
It is internal to be transitioned into high-temperature steam instrument (3), control system (7) start high-temperature steam instrument (3) by the water heating evaporation of internal reservoir at
Vapor, control system (7) opens the electrically-controlled valve on high-temperature steam delivery pipe (2) and high-temperature water vapor is delivered to high temperature steaming at this time
In cold water in vapour heating zone (5-1), heat source is provided for heating process；In the process, No.1 water temperature detector (5-2) is real-time
The water temperature condition in high-temperature steam heating zone (5-1) is monitored, when No.1 water temperature detector (5-2) detects high-temperature steam heating zone
When water temperature in (5-1) is lower than 40 DEG C, electric signal is sent to control system (7) by No.1 water temperature detector (5-2), control system
System (7) control solar light collecting device (4) increases and adopts heat；
Step 2: high-temperature steam heating zone (5-1) internal warm water after heating for the first time flows into secondary electricity by drainage disc (5-5)
In heating tank (5-3), warm water is further heated in control system (7) starting stacked heating energization head (5-4), in heating process
In, the water temperature condition in No. two secondary electrical heating tanks of water temperature detector (5-7) real-time monitoring (5-3), when No. two water temperature detectors
When (5-7) detects that the water temperature in secondary electrical heating tank (5-3) reaches 85 DEG C~100 DEG C, No. two water temperature detectors (5-7) will
Electric signal is sent to control system (7), and control system (7) cuts off stacked heating energization head (5-4) power supply and stops heating, to save
The energy；
Step 3: in stacked heating energization head (5-4) heating process, energization head rate of heat addition detector (5-6) is to the rate of heat addition
Real-time monitoring is carried out, when energization head rate of heat addition detector (5-6) detects the rate of heat addition lower than 45 %, energization head heating speed
Electric signal is sent to control system (7) by rate detector (5-6), and control system (7) controls stacked heating energization head (5-4) and increases
Heat fan-out capability；
Step 4: after the completion 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
It send into each residential building or office building water supply line.
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| 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 |
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