CN106089592B - A kind of double blades wind power generating set with vertical shaft and its working method - Google Patents
A kind of double blades wind power generating set with vertical shaft and its working method Download PDFInfo
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- CN106089592B CN106089592B CN201610638979.4A CN201610638979A CN106089592B CN 106089592 B CN106089592 B CN 106089592B CN 201610638979 A CN201610638979 A CN 201610638979A CN 106089592 B CN106089592 B CN 106089592B
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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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E10/00—Energy generation through renewable energy sources
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Abstract
The invention discloses a kind of double blades wind power generating set with vertical shaft and its working methods, are made of spindle blade, countershaft blade, swivel bearing, variable pitch adjuster, generator control room, upper backup pad, lower supporting plate, main backstop, secondary supporting rack；Spindle blade and countershaft blade rotate under wind-force drive, and in rotary course, gear carries out speedup to its rotary speed, to promote electrical power generators；Electromagnetic brake carries out electromagnetic braking when generator speed is excessively high, to generator, to reduce generator speed.A kind of double blades wind power generating set with vertical shaft of the present invention, the device utilize wind power generation performance, efficiently use new energy, using vertical structure, can generate electricity under breeze conditions, double blades structure effectively improves generating efficiency.
Description
Technical field
The invention belongs to wind energy application fields, and in particular to a kind of double blades wind power generating set with vertical shaft.
Background technology
Wind is a kind of prodigious new energy of potentiality, and perhaps people also remember that 18 beginnings of the century swept away the primary of two countries of Great Britain and France
Violent strong wind has wiped out 400 windmills, 800 houses, 100 churches, 400 a plurality of sailing boats, and have thousands by
To injury, 250,000 plants big tree is uprooped.Only in pulling out tree, wind has been issued by 10,000,000 horsepowers within the several seconds
The power of (i.e. 7,500,000 kilowatts).Someone estimated that can be used to the wind resource to generate electricity on the earth, there are about 10,000,000,000 kilowatts, almost
10 times of present whole world hydroelectric generation amount.Burn the energy that coal is obtained every year in the whole world at present, and only wind-force is in 1 year
The one third of provided energy.Therefore, all take much count of generating electricity using wind-force both at home and abroad, tap a new source of energy.
Now, the resource of non-renewable energy resources is fewer and fewer or even some energy have run out of, therefore, as wave energy, can
Ice, coal bed gas, microorganism are fired, these energy will become the widely applied new energy of the mankind, and this regenerative energy of wind energy exists
It has begun to use in many areas and equipment, technology moving to maturity slowly.Modern wind generator mainly has
Horizontal axis wind-driven generator and vertical axis aerogenerator.Perpendicular axis type it is different from the product of horizontal axial type, in vertical shaft wind
In power generator, shaft is installed on the vertical axis, perpendicular to the ground, not by the shadow of wind direction when vertical axis aerogenerator works
It rings, therefore when change of the wind without adjustment.
Development with social economy and the demand to the energy are also increasing, it has been recognized that destroying intrinsic energy money
Source will threaten the existence of the mankind.It was found that and utilize natural resources, and with environment-friendly function project be people struggle target.
Multi-propeller wind driven generator is that the natural energy resources for being conducive to environmental protection utilize project, and wind power generation plant before is mostly single wind paddle
Group machine, generated output are small.
Invention content
In order to solve the above technical problem, the present invention provides a kind of double blades wind power generating set with vertical shaft, including：Main shaft
Blade 1, countershaft blade 2, swivel bearing 3, variable pitch adjuster 4, generator control room 5, upper backup pad 6, lower supporting plate 7,
Main backstop 8, secondary supporting rack 9；1 shape of the spindle blade is half circle ring surface structure, and 1 number of spindle blade is 4
A, the axis centered on swivel bearing 3 of spindle blade 1 is circumferentially distributed；1 other side of spindle blade is connected with countershaft blade 2；It is described
Upper backup pad 6 and lower supporting plate 7 are rectangular configuration, and size is 1m~1.5m (length) × 0.5m~1m (width) × 0.2m~0.4m
(thickness)；Variable pitch adjuster 4 and generator control room 5 are provided between upper backup pad 6 and lower supporting plate 7, wherein can switch political loyalty
It is fixedly mounted on 5 top of generator control room away from adjuster 4, the variable pitch adjuster 4 is coaxially revolved with 3 lower end of swivel bearing
Turn connection；The main backstop 8 is cylindrical structure, and between 80mm~100mm, main backstop 8 is fixedly welded on diameter
7 bottom center of lower supporting plate；9 quantity of the pair supporting rack is four, and is respectively fixedly connected in 6 bottom surface quadrangle of upper backup pad.
Further, the countershaft blade 2 includes：Rotating vane 2-1, servo motor 2-2, drive shaft 2-3, wind speed measurement
Device 2-4；The wherein described rotating vane 2-1 contour structures are " C " font；The drive shaft 2-3 and rotating vane 2-1 coaxial rotatings
Connection；The upper ends the drive shaft 2-3 are equipped with servo motor 2-2, and servo motor 2-2 is drivingly connected with rotating vane 2-1；It is described
Wind speed measurement device 2-4 is located at rotating vane 2-1 upper sides.
Further, the generator control room 5 includes：Gear 5-1, generator 5-2, electromagnetic brake 5-3,
Microcontroller 5-4, generator-temperature detection inductor 5-5, generator speed inductor 5-6；The wherein described gear 5-1 is located at
Above generator 5-2, gear 5-1 is rotated coaxially with generator 5-2 and is connect, and gear 5-1 is cylindrical structure,
Its outer diameter is between 10cm~15cm；The electromagnetic brake 5-3 is located at below generator 5-2, electromagnetic brake 5-3 and power generation
Machine 5-2 rotates coaxially connection；The microcontroller 5-4 is fixedly mounted on 5 bottom side of generator control room；The generator temperature
Degree inductor 5-5 and generator speed inductor 5-6 is installed on generator 5-2；
The electromagnetic brake 5-3, generator-temperature detection inductor 5-5, generator speed inductor 5-6 pass through conducting wire respectively
It is connected with microcontroller 5-4 controls.
Further, the gear 5-1 includes：Low-speed gear 5-1-1, high gear 5-1-2, ring oiler
5-1-3, fluid concentration detector 5-1-4；The wherein described low-speed gear 5-1-1 is located at the sides gear 5-1, the high speed
Gear 5-1-2 is located at the other sides gear 5-1, and low-speed gear 5-1-1 and high gear 5-1-2 is connected by gear drive
It connects；The ring oiler 5-1-3 is positioned over low-speed gear 5-1-1 and high gear 5-1-2 gear meshing portions position top, high
Degree is higher by 1cm~1.5cm than low-speed gear 5-1-1；The fluid concentration detector 5-1-4 is located at low-speed gear 5-1-1 gears
Edge, fluid concentration detector 5-1-4 is apart from gear side along between 5mm~8mm；
The low-speed gear 5-1-1 is connected by conducting wire and microcontroller 5-4 controls.
Further, the ring oiler 5-1-3 includes：Oiling motor 5-1-3-1, piston ring pusher 5-1-3-2,
Oily cylinder 5-1-3-3；The wherein described oily cylinder 5-1-3-3 is columnar structured, and material is chrome-manganese-silicon steel material, oily cylinder 5-1-3-3
Outer diameter is between 3cm~5cm；The piston ring pusher 5-1-3-2 is located inside oily cylinder 5-1-3-3, piston ring pusher 5-
1-3-2 makees compressional movement in oily cylinder 5-1-3-3；The tops piston ring pusher 5-1-3-2 are provided with oiling motor 5-1-
3-1, oiling motor 5-1-3-1 are drivingly connected with piston ring pusher 5-1-3-2；
The oiling motor 5-1-3-1 is connected by conducting wire and microcontroller 5-4 controls.
Further, the rotating vane 2-1 is molded by high molecular material pressing mold, the constituent of rotating vane 2-1 and
Manufacturing process is as follows：
One, rotating vane 2-1 constituents：
It counts in parts by weight, 12~44 parts of (5R) -5- methyl -2- isopropyl -1- cyclohexenyl methoxyl methyls ether, 2,3,5,
Tetra- fluoro- 4- methylbenzyls (Z) of 6--(1R, 3R, 1S, 3S) -3- (the chloro- 3,3,3- trifluoros propyl- 1- alkenyls of 2-) -2,2- diformazan basic rings
32~85 parts of carboxylate, 2- (2- quinoline azo) 105~163 parts of -4- diethylamino Benzoic Acids, (S) alpha-cyano-phenoxy
Benzyl (1R, 3R) -3- (2,2- dibromo vinyl) -53~114 parts of 2,2- dimethyl cyclopropane carboxylic acids ester, 3- (2,2- bis- chloroethenes
Alkenyl) -2,2- dimethyl cyclopropionate -33~78 parts of (1S, 3S)-REL- (R)-cyano (3- phenoxy phenyls) methyl ester, (RS) -
Alpha- cyano -3- phenoxy benzyls (SR) -3- (2,2- dichloroethylenes) -2,2- dimethyl cyclopropane carboxylic acids ester 112~
184 parts, the trans- -3- of 1R- (2,2- dichloroethylene) -2,2- dimethyl cyclopropane carboxylic acids-of a concentration of ppm of 44 ppm~85
(2,3,5,6,-tetrafluoro phenyl) 78~138 parts of methyl ester, d-trans -2,2- dimethyl -3- (2- methyl-1-propylenes base) ring
Amyl- 142~228 parts of the 2- alkenyl esters of propanecarboxylic acid's-S-2- methyl -3- (2- propargyls) -4- oxo rings, cyano-(3- phenoxy group benzene
Base) methyl -3- (2,2- dichloroethylene) -96~155 parts of 2,2- dimethyl cyclopropane carboxylic acids ester, 38~75 parts of crosslinking agent, 2-
(4- acetylaminohydroxyphenylarsonic acid 3- chlorphenyls) 69~146 parts of propionitrile, N- [2- [(2,4- dinitrophenyl) azo] -5- [(2- hydroxyls -3-
Phenoxy propyl) amino] -4- methoxyphenyls] 162~249 parts of acetamide, (E)-N- [2- [(bromo- 6- cyano -4- nitros of 2-
Benzene) azo group] -5- (lignocaine) phenyl] 22~58 parts of propionamide, 2- [[4- [[2- (acetoxyl group) ethyl] butyl ammonia
Base] -2- aminomethyl phenyls] azo] the bromo- 5- nitros of -3- -68~147 parts of benzonitrile；
The crosslinking agent is N- (2- cyanoethyls)-N-ethylaniline, N- butyl-N- cyanoethyl anilines, acetoaceto pair
Any one in chlorine ortho-nitraniline；
Two, the manufacturing process of rotating vane 2-1, comprises the steps of：
1st step：The ultra-pure water 1150~1480 that conductivity is 6.65 μ of μ S/cm~8.26 S/cm is added in a kettle
Part, start blender in reaction kettle, rotating speed is the rpm of 86 rpm~149, starts heat pump, reactor temperature is made to rise to 52
DEG C~84 DEG C；Sequentially add (5R) -5- methyl -2- isopropyl -1- cyclohexenyl methoxyl methyls ether, tetra- fluoro- 4- first of 2,3,5,6-
Base benzyl (Z)-(1R, 3R, 1S, 3S) -3- (the chloro- 3,3,3- trifluoros propyl- 1- alkenyls of 2-) -2,2- dimethyl cyclopropane carboxylic acids ester,
2- (2- quinoline azo) -4- diethylamino Benzoic Acids, to being completely dissolved, it is 2.8~5.7 to adjust pH value, and blender is turned for stirring
Velocity modulation is to the rpm of 108 rpm~182, and temperature is 73 DEG C~152 DEG C, esterification 14~25 hours；
2nd step：Take (S) alpha-cyano-phenoxy benzyl (1R, 3R) -3- (2,2- dibromo vinyls) -2,2- diformazans basic ring third
Alkane carboxylate, 3- (2,2- dichloroethylenes) -2,2- dimethyl cyclopropionate-(1S, 3S)-REL- (R)-cyano (3- phenoxy phenyls)
Methyl ester crushes, and powder diameter is 2100~2800 mesh；(RS)-alpha- cyano -3- phenoxy benzyls (SR)-are added
3- (2,2- dichloroethylene) -2,2- dimethyl cyclopropane carboxylic acid's esters are uniformly mixed, and are laid in pallet, and tiling thickness is 11
The mm of mm~18 use dosage to irradiate 111~154 for the alpha ray that the kGy of 5.5 kGy~10.2, energy are the MeV of 9 MeV~15
Minute and the same dose of β x ray irradiation xs 63~144 minutes；
3rd step：The mixed-powder handled through the 2nd step is dissolved in the trans- -3- of 1R- (2,2- dichloroethylenes) -2,2- dimethyl
In cyclopropane-carboxylic acid-(2,3,5,6 ,-tetrafluoro phenyl) methyl ester, reaction kettle is added, agitator speed is 92 rpm~146
Rpm, temperature are 114 DEG C~168 DEG C, and starting vacuum pump makes the vacuum degree of reaction kettle reach the MPa of -0.68 MPa~1.22, keeps
This state response 15~28 hours；Pressure release is simultaneously passed through radon gas, and it is the MPa of 0.55 MPa~1.47 to make reacting kettle inner pressure, and heat preservation is quiet
It sets 8~12 hours；Agitator speed is promoted to the rpm of 202 rpm~258, simultaneous reactions kettle pressure release to 0MPa；Sequentially add the right side
Revolve trans- -2,2- dimethyl -3- (2- methyl-1-propylenes base) cyclopropane-carboxylic acid-S-2- methyl -3- (2- propargyls) -4- oxos
The amyl- 2- alkenyl esters of ring, cyano-(3- Phenoxyphenyls) methyl -3- (2,2- dichloroethylenes) -2,2- dimethyl cyclopropane carboxylic acids
After ester is completely dissolved, crosslinking agent is added and is stirred so that the hydrophilic lipophilic balance of reaction kettle solution is 4.8~9.2, heat preservation
Stand 11~20 hours；
4th step：When agitator speed is 123 rpm~188 rpm, 2- (4- acetylaminohydroxyphenylarsonic acid 3- chlorobenzenes are sequentially added
Base) propionitrile, N- [2- [(dinitrophenyl group) azo] -5- [(2- hydroxyl -3- phenoxy propyls) amino] -4- methoxybenzenes
Base] acetamide, (E)-N- [2- [(the bromo- 6- cyano -4- nitrobenzenes of 2-) azo group] -5- (lignocaine) phenyl] propionamides and 2-
[[4- [[2- (acetoxyl group) ethyl] butylamino] -2- aminomethyl phenyls] azo] bromo- 5- nitros-benzonitriles of -3- promote reaction
Kettle pressure reaches the MPa of 1.2 MPa~2.5, and temperature is 158 DEG C~214 DEG C, polymerisation 22~30 hours；It has reacted
Reacting kettle inner pressure is down to 0 MPa after, is cooled to 33 DEG C~43 DEG C, discharging enters molding press and can be prepared by rotating vane 2-
1。
Further, the invention also discloses a kind of working method of double blades wind power generating set with vertical shaft, this method
Including following steps：
1st step：Staff opens general supply and master controller, the wind speed measurement device 2-4 being now placed on countershaft blade 2
It starts to work；When wind speed measurement device 2-4 detects that wind speed is less than 1m/s, wind speed measurement device 2-4 is sent to signal is detected always
Controller, master controller start the servo motor 2-2 on countershaft blade 2, and servo motor 2-2 promotes drive shaft 2-3 to do rotation fortune
It is dynamic, to drive rotating vane 2-1 to move in a circle as rotary shaft using drive shaft 2-3；In the band of rotating vane 2-1 motional inertias
Under dynamic, spindle blade 1 is rotated around swivel bearing 3；
2nd step：In 2 rotary course of spindle blade 1 and countershaft blade, the gear 5-1 in generator control room 5
High gear 5-1-2 is driven to improve the rotary speed of spindle blade 1 and countershaft blade 2 by low-speed gear 5-1-1, to promote
Generator 5-2 is set to generate electricity；
3rd step：In generator 5-2 power generation processes, generator-temperature detection inductor 5-5 and generator speed inductor 5-6
The temperature to generator 5-2 and rotating speed monitor in real time respectively；When generator-temperature detection inductor 5-5 detects generator 5-2 temperature
When higher than 110 DEG C, electric signal is sent to microcontroller 5-4 by generator-temperature detection inductor 5-5, and microcontroller 5-4 controls low speed
Gear 5-1-1 reduces rotary speed；When generator speed inductor 5-6 detects that the rotating speed of generator 5-2 is more than 1.5 times of volume
When determining rotating speed, generator speed inductor 5-6 will detect signal and be sent to microcontroller 5-4, and microcontroller 5-4 starts electromagnetic system
The rotating speed of generator 5-2 is reduced to by dynamic device 5-3, electromagnetic brake 5-3 to be allowed in the range of speeds；
4th step：Fluid concentration detector 5-1-4 in gear 5-1 is to low-speed gear 5-1-1 and high gear 5-
Fluid density real-time monitoring between 1-2, when fluid concentration detector 5-1-4 detects that fluid concentration is less than 10 ppm, micro-control
Device 5-4 processed starts oiling motor 5-1-3-1, and oiling motor 5-1-3-1 drives piston ring pusher 5-1-3-2 in oily cylinder 5-1-3-
Compressional movement is done in 3, to which fluid to be injected between low-speed gear 5-1-1 and high gear 5-1-2；It is examined when fluid concentration
When survey device 5-1-4 detects that fluid concentration is higher than 45 ppm, microcontroller 5-4 closes oiling motor 5-1-3-1；
5th step：After the alternating current that generator 5-2 is generated is by rectification, filtering, reversion reaction, it is converted to workable friendship
Galvanic electricity.
A kind of double blades wind power generating set with vertical shaft disclosed by the invention, the advantage is that：
(1) device utilizes wind power generation performance, energy conservation and environmental protection；
(2) device uses vertical electrification structure, is not influenced by wind direction, can be generated electricity under breeze conditions；
(3) device uses double blades structure, and collection wind effect is good, and generated energy significantly improves.
A kind of double blades wind power generating set with vertical shaft of the present invention, the device utilize wind power generation performance, effectively
It can be generated electricity under breeze conditions using vertical structure using new energy, double blades structure effectively improves generating efficiency.
Description of the drawings
Fig. 1 is a kind of heretofore described double blades wind power generating set with vertical shaft schematic diagram.
Fig. 2 is heretofore described countershaft paddle blade structure schematic diagram.
Fig. 3 is heretofore described generator control chamber interior structural schematic diagram.
Fig. 4 is heretofore described gear internal structure schematic diagram.
Fig. 5 is heretofore described ring oiler structural schematic diagram.
Fig. 6 is heretofore described rotating vane material corrosion resistant erosion degree with usage time variation diagram.
In figure 1 above~Fig. 5, spindle blade 1, countershaft blade 2, rotating vane 2-1, servo motor 2-2, drive shaft 2-3,
Wind speed measurement device 2-4, swivel bearing 3, variable pitch adjuster 4, generator control room 5, gear 5-1, low-speed gear
5-1-1, high gear 5-1-2, ring oiler 5-1-3, oiling motor 5-1-3-1, piston ring pusher 5-1-3-2, oily cylinder
5-1-3-3, fluid concentration detector 5-1-4, generator 5-2, electromagnetic brake 5-3, microcontroller 5-4, generator-temperature detection sense
Answer device 5-5, generator speed inductor 5-6, upper backup pad 6, lower supporting plate 7, main backstop 8, secondary supporting rack 9.
Specific implementation mode
With reference to the accompanying drawings and examples to a kind of double blades wind power generating set with vertical shaft provided by the invention into traveling
One step explanation.
As shown in Figure 1, being a kind of heretofore described double blades wind power generating set with vertical shaft schematic diagram.From Fig. 1
Find out, including：Spindle blade 1, countershaft blade 2, swivel bearing 3, variable pitch adjuster 4, generator control room 5, upper support
Plate 6, lower supporting plate 7, main backstop 8, secondary supporting rack 9；1 shape of the spindle blade is half circle ring surface structure, main
1 number of axis blade is 4, and the axis centered on swivel bearing 3 of spindle blade 1 is circumferentially distributed；1 other side of spindle blade is connected with
Countershaft blade 2；The upper backup pad 6 and lower supporting plate 7 are rectangular configuration, and size is 1m~1.5m (length) × 0.5m~1m
(width) × 0.2m~0.4m (thickness)；Variable pitch adjuster 4 and generator control are provided between upper backup pad 6 and lower supporting plate 7
Room 5 processed, wherein variable pitch adjuster 4 are fixedly mounted on 5 top of generator control room, the variable pitch adjuster 4 and rotation
Shaft holds 3 lower end coaxial rotating connections；The main backstop 8 is cylindrical structure, and diameter is main between 80mm~100mm
Supporting rack 8 is fixedly welded on 7 bottom center of lower supporting plate；9 quantity of the pair supporting rack is four, and is respectively fixedly connected with upper
6 bottom surface quadrangle of support plate.
As shown in Fig. 2, being heretofore described countershaft paddle blade structure schematic diagram.As seen from Figure 2, countershaft blade 2 wraps
It includes：Rotating vane 2-1, servo motor 2-2, drive shaft 2-3, wind speed measurement device 2-4；The wherein described rotating vane 2-1 shape knots
Structure is " C " font；The drive shaft 2-3 is connect with rotating vane 2-1 coaxial rotatings；The upper ends the drive shaft 2-3, which are equipped with, to be watched
Motor 2-2 is taken, servo motor 2-2 is drivingly connected with rotating vane 2-1；The wind speed measurement device 2-4 is located on rotating vane 2-1
Portion side.
As shown in figure 3, being heretofore described generator control chamber interior structural schematic diagram.As seen from Figure 3, it generates electricity
Machine control room 5 includes：Gear 5-1, generator 5-2, electromagnetic brake 5-3, microcontroller 5-4, generator-temperature detection sense
Answer device 5-5, generator speed inductor 5-6；The wherein described gear 5-1 is located above generator 5-2, gear
5-1 is rotated coaxially with generator 5-2 and is connect, and gear 5-1 is cylindrical structure, and outer diameter is between 10cm~15cm；
The electromagnetic brake 5-3 is located at below generator 5-2, and electromagnetic brake 5-3 is rotated coaxially with generator 5-2 and connect；It is described
Microcontroller 5-4 is fixedly mounted on 5 bottom side of generator control room；The generator-temperature detection inductor 5-5 and generator turn
Fast inductor 5-6 is installed on generator 5-2；
The electromagnetic brake 5-3, generator-temperature detection inductor 5-5, generator speed inductor 5-6 pass through conducting wire respectively
It is connected with microcontroller 5-4 controls.
As shown in figure 4, being heretofore described gear internal structure schematic diagram.Find out from Fig. 4 or Fig. 3,
Gear 5-1 includes：Low-speed gear 5-1-1, high gear 5-1-2, ring oiler 5-1-3, fluid concentration detector
5-1-4；The wherein described low-speed gear 5-1-1 is located at the sides gear 5-1, and the high gear 5-1-2 is located at gear biography
The dynamic other sides case 5-1, low-speed gear 5-1-1 are connect with high gear 5-1-2 by gear drive；The ring oiler 5-1-
3 are positioned over low-speed gear 5-1-1 with above high gear 5-1-2 gear meshing portions position, and height is higher by than low-speed gear 5-1-1
1cm~1.5cm；The fluid concentration detector 5-1-4 is located at low-speed gear 5-1-1 gear sides edge, fluid concentration detector 5-
1-4 is apart from gear side along between 5mm~8mm；
The low-speed gear 5-1-1 is connected by conducting wire and microcontroller 5-4 controls.
As shown in figure 5, being heretofore described ring oiler structural schematic diagram.Find out from Fig. 5 or Fig. 3, oil ring
Oil syringe 5-1-3 includes：Oiling motor 5-1-3-1, piston ring pusher 5-1-3-2, oily cylinder 5-1-3-3；The wherein described oily cylinder
5-1-3-3 is columnar structured, and material is chrome-manganese-silicon steel material, and oily cylinder 5-1-3-3 outer diameters are between 3cm~5cm；The work
Plug ring pusher 5-1-3-2 is located inside oily cylinder 5-1-3-3, and piston ring pusher 5-1-3-2 is squeezed in oily cylinder 5-1-3-3
Movement；The tops piston ring pusher 5-1-3-2 are provided with oiling motor 5-1-3-1, oiling motor 5-1-3-1 and piston ring
Pusher 5-1-3-2 is drivingly connected；
The oiling motor 5-1-3-1 is connected by conducting wire and microcontroller 5-4 controls.
A kind of course of work of double blades wind power generating set with vertical shaft of the present invention is：
1st step：Staff opens general supply and master controller, the wind speed measurement device 2-4 being now placed on countershaft blade 2
It starts to work；When wind speed measurement device 2-4 detects that wind speed is less than 1m/s, wind speed measurement device 2-4 is sent to signal is detected always
Controller, master controller start the servo motor 2-2 on countershaft blade 2, and servo motor 2-2 promotes drive shaft 2-3 to do rotation fortune
It is dynamic, to drive rotating vane 2-1 to move in a circle as rotary shaft using drive shaft 2-3；In the band of rotating vane 2-1 motional inertias
Under dynamic, spindle blade 1 is rotated around swivel bearing 3；
2nd step：In 2 rotary course of spindle blade 1 and countershaft blade, the gear 5-1 in generator control room 5
High gear 5-1-2 is driven to improve the rotary speed of spindle blade 1 and countershaft blade 2 by low-speed gear 5-1-1, to promote
Generator 5-2 is set to generate electricity；
3rd step：In generator 5-2 power generation processes, generator-temperature detection inductor 5-5 and generator speed inductor 5-6
The temperature to generator 5-2 and rotating speed monitor in real time respectively；When generator-temperature detection inductor 5-5 detects generator 5-2 temperature
When higher than 110 DEG C, electric signal is sent to microcontroller 5-4 by generator-temperature detection inductor 5-5, and microcontroller 5-4 controls low speed
Gear 5-1-1 reduces rotary speed；When generator speed inductor 5-6 detects that the rotating speed of generator 5-2 is more than 1.5 times of volume
When determining rotating speed, generator speed inductor 5-6 will detect signal and be sent to microcontroller 5-4, and microcontroller 5-4 starts electromagnetic system
The rotating speed of generator 5-2 is reduced to by dynamic device 5-3, electromagnetic brake 5-3 to be allowed in the range of speeds；
4th step：Fluid concentration detector 5-1-4 in gear 5-1 is to low-speed gear 5-1-1 and high gear 5-
Fluid density real-time monitoring between 1-2, when fluid concentration detector 5-1-4 detects that fluid concentration is less than 10 ppm, micro-control
Device 5-4 processed starts oiling motor 5-1-3-1, and oiling motor 5-1-3-1 drives piston ring pusher 5-1-3-2 in oily cylinder 5-1-3-
Compressional movement is done in 3, to which fluid to be injected between low-speed gear 5-1-1 and high gear 5-1-2；It is examined when fluid concentration
When survey device 5-1-4 detects that fluid concentration is higher than 45 ppm, microcontroller 5-4 closes oiling motor 5-1-3-1；
5th step：After the alternating current that generator 5-2 is generated is by rectification, filtering, reversion reaction, it is converted to workable friendship
Galvanic electricity.
A kind of double blades wind power generating set with vertical shaft of the present invention, the device utilize wind power generation performance, effectively
It can be generated electricity under breeze conditions using vertical structure using new energy, double blades structure effectively improves generating efficiency.
The embodiment of the manufacturing process of rotating vane 2-1 of the present invention below, embodiment be in order to further illustrate
Present disclosure, but should not be construed as limiting the invention.Without departing from the spirit and substance of the case in the present invention, to this
It changes and replaces made by inventive method, step or condition, all belong 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
Rotating vane 2-1 of the present invention is manufactured according to the following steps, and is counted in parts by weight：
1st step：1150 parts of the ultra-pure water that conductivity is 6.65 μ S/cm is added in a kettle, starts stirring in reaction kettle
Device, rotating speed are 86 rpm, start heat pump, reactor temperature is made to rise to 52 DEG C；It is different to sequentially add (5R) -5- methyl -2-
12 parts of propyl -1- cyclohexenyl methoxyl methyls ether, 2,3,5,6- tetra- fluoro- 4- methylbenzyls (Z)-(1R, 3R, 1S, 3S) -3- (2-
Chloro- 3,3,3- trifluoro propyl- 1- alkenyls) -32 parts of 2,2- dimethyl cyclopropane carboxylic acids ester, 2- (2- quinoline azo) -4- lignocaines
105 parts of benzoic acid, to being completely dissolved, it is 2.8 to adjust pH value for stirring, and agitator speed is adjusted to 108 rpm, and temperature is 73 DEG C,
Esterification 14 hours；
2nd step：Take (S) alpha-cyano-phenoxy benzyl (1R, 3R) -3- (2,2- dibromo vinyls) -2,2- diformazans basic ring third
53 parts of alkane carboxylate, 3- (2,2- dichloroethylene) -2,2- dimethyl cyclopropionate-(1S, 3S)-REL- (R)-cyano (3- benzene oxygen
Phenyl) 33 parts of methyl ester crushes, and powder diameter is 2100 mesh；(RS)-alpha- cyano -3- phenoxy benzyls are added
(SR) -3- (2,2- dichloroethylene) -112 parts of 2,2- dimethyl cyclopropane carboxylic acids ester is uniformly mixed, and is laid in pallet, is tiled
Thickness is 11 mm, uses dosage to be irradiated 65 minutes and the same dose of β for the alpha ray that 5.5 kGy, energy are 9 MeV and penetrates
Line irradiates 63 minutes；
3rd step：The mixed-powder handled through the 2nd step is dissolved in 1R- trans- -3- (the 2,2- dichloroethylene of a concentration of 44 ppm
Base) in -2,2- dimethyl cyclopropane carboxylic acids-(2,3,5,6,-tetrafluoro phenyl) 78 parts of methyl ester, reaction kettle is added, blender turns
Speed is 92 rpm, and temperature is 114 DEG C, and starting vacuum pump makes the vacuum degree of reaction kettle reach -0.68 MPa, keeps this state response
15 hours；Pressure release is simultaneously passed through radon gas, and it is 0.55 MPa to make reacting kettle inner pressure, and heat preservation stands 8 hours；Agitator speed is promoted to
202 rpm, simultaneous reactions kettle pressure release to 0MPa；Sequentially add d-trans -2,2- dimethyl -3- (2- methyl-1-propylenes base)
Amyl- 142 parts of the 2- alkenyl esters of cyclopropane-carboxylic acid-S-2- methyl -3- (2- propargyls) -4- oxo rings, cyano-(3- Phenoxyphenyls)
After methyl -3- (2,2- dichloroethylene) -96 parts of 2,2- dimethyl cyclopropane carboxylic acids ester is completely dissolved, 38 parts of crosslinking agent is added and stirs
Mix mixing so that the hydrophilic lipophilic balance of reaction kettle solution is 4.8, and heat preservation stands 11 hours；
4th step：When agitator speed is 123 rpm, 2- (4- acetylaminohydroxyphenylarsonic acid 3- chlorphenyls) propionitrile 69 is sequentially added
Part, N- [2- [(2,4- dinitrophenyl) azo] -5- [(2- hydroxyl -3- phenoxy propyls) amino] -4- methoxyphenyls] second
162 parts of amide, (E)-N- [2- [(the bromo- 6- cyano -4- nitrobenzenes of 2-) azo group] -5- (lignocaine) phenyl] propionamide 22
Part, 2- [[4- [[2- (acetoxyl group) ethyl] butylamino] -2- aminomethyl phenyls] azo] bromo- 5- nitros-benzonitriles 68 of -3-
Part, reactor pressure is promoted, 1.2 MPa are reached, temperature is 158 DEG C, polymerisation 22 hours；It will reaction after the completion of reaction
Pressure is down to 0 MPa in kettle, is cooled to 33 DEG C, and discharging enters molding press and can be prepared by rotating vane 2-1；
The crosslinking agent is N- (2- cyanoethyls)-N-ethylaniline.
Embodiment 2
Rotating vane 2-1 of the present invention is manufactured according to the following steps, and is counted in parts by weight：
1st step：1244 parts of the ultra-pure water that conductivity is 7.22 μ S/cm is added in a kettle, starts stirring in reaction kettle
Device, rotating speed are 126 rpm, start heat pump, reactor temperature is made to rise to 67 DEG C；Sequentially add (5R) -5- methyl -2-
27 parts of isopropyl -1- cyclohexenyl methoxyl methyls ether, 2,3,5,6- tetra- fluoro- 4- methylbenzyls (Z)-(1R, 3R, 1S, 3S) -3-
(chloro- 3,3,3- trifluoro propyl- 1- alkenyls of 2-) -55 parts of 2,2- dimethyl cyclopropane carboxylic acids ester, 2- (2- quinoline azo) -4- diethylaminos
138 parts of yl benzoic acid, to being completely dissolved, it is 4.2 to adjust pH value, and agitator speed is adjusted to 148 rpm, temperature 113 for stirring
DEG C, esterification 19 hours；
2nd step：Take (S) alpha-cyano-phenoxy benzyl (1R, 3R) -3- (2,2- dibromo vinyls) -2,2- diformazans basic ring third
83 parts of alkane carboxylate, 3- (2,2- dichloroethylene) -2,2- dimethyl cyclopropionate-(1S, 3S)-REL- (R)-cyano (3- benzene oxygen
Phenyl) 53 parts of methyl ester crushes, and powder diameter is 2500 mesh；(RS)-alpha- cyano -3- phenoxy benzyls are added
(SR) -3- (2,2- dichloroethylene) -148 parts of 2,2- dimethyl cyclopropane carboxylic acids ester is uniformly mixed, and is laid in pallet, is tiled
Thickness is 15 mm, and dosage is used to be irradiated 132 minutes and the same dose of β for the alpha ray that 7.8 kGy, energy are 12 MeV
X ray irradiation x 103 minutes；
3rd step：The mixed-powder handled through the 2nd step is dissolved in 1R- trans- -3- (the 2,2- dichloroethylene of a concentration of 64 ppm
Base) in -2,2- dimethyl cyclopropane carboxylic acids-(2,3,5,6,-tetrafluoro phenyl) 108 parts of methyl ester, reaction kettle is added, blender turns
Speed is 117 rpm, and temperature is 140 DEG C, and starting vacuum pump makes the vacuum degree of reaction kettle reach -0.22 MPa, keeps this state anti-
It answers 21 hours；Pressure release is simultaneously passed through radon gas, and it is 0.96 MPa to make reacting kettle inner pressure, and heat preservation stands 10 hours；Agitator speed carries
Rise to 228 rpm, simultaneous reactions kettle pressure release to 0MPa；Sequentially add d-trans -2,2- dimethyl -3- (2- methyl-1-propylenes
Base) amyl- 182 parts of the 2- alkenyl esters of cyclopropane-carboxylic acid-S-2- methyl -3- (2- propargyls) -4- oxo rings, cyano-(3- phenoxy group benzene
Base) after methyl -3- (2,2- dichloroethylene) -126 parts of 2,2- dimethyl cyclopropane carboxylic acids ester is completely dissolved, crosslinking agent 58 is added
Part is stirred so that the hydrophilic lipophilic balance of reaction kettle solution is 7.1, and heat preservation stands 15 hours；
4th step：When agitator speed is 155 rpm, 2- (4- acetylaminohydroxyphenylarsonic acid 3- chlorphenyls) propionitrile 110 is sequentially added
Part, N- [2- [(2,4- dinitrophenyl) azo] -5- [(2- hydroxyl -3- phenoxy propyls) amino] -4- methoxyphenyls] second
204 parts of amide, (E)-N- [2- [(the bromo- 6- cyano -4- nitrobenzenes of 2-) azo group] -5- (lignocaine) phenyl] propionamide 38
Part, 2- [[4- [[2- (acetoxyl group) ethyl] butylamino] -2- aminomethyl phenyls] azo] bromo- 5- nitros-benzonitriles 108 of -3-
Part, reactor pressure is promoted, 1.8 MPa are reached, temperature is 185 DEG C, polymerisation 26 hours；It will reaction after the completion of reaction
Pressure is down to 0 MPa in kettle, is cooled to 38 DEG C, and discharging enters molding press and can be prepared by rotating vane 2-1；
The crosslinking agent is acetoaceto p-chloro-o-nitroaniline.
Embodiment 3
Rotating vane 2-1 of the present invention is manufactured according to the following steps, and is counted in parts by weight：
1st step：1480 parts of the ultra-pure water that conductivity is 8.26 μ S/cm is added in a kettle, starts stirring in reaction kettle
Device, rotating speed are 149 rpm, start heat pump, reactor temperature is made to rise to 84 DEG C；Sequentially add (5R) -5- methyl -2-
44 parts of isopropyl -1- cyclohexenyl methoxyl methyls ether, 2,3,5,6- tetra- fluoro- 4- methylbenzyls (Z)-(1R, 3R, 1S, 3S) -3-
(chloro- 3,3,3- trifluoro propyl- 1- alkenyls of 2-) -85 parts of 2,2- dimethyl cyclopropane carboxylic acids ester, 2- (2- quinoline azo) -4- diethylaminos
163 parts of yl benzoic acid, to being completely dissolved, it is 5.7 to adjust pH value, and agitator speed is adjusted to 182 rpm, temperature 152 for stirring
DEG C, esterification 25 hours；
2nd step：Take (S) alpha-cyano-phenoxy benzyl (1R, 3R) -3- (2,2- dibromo vinyls) -2,2- diformazans basic ring third
114 parts of alkane carboxylate, 3- (2,2- dichloroethylene) -2,2- dimethyl cyclopropionate-(1S, 3S)-REL- (R)-cyano (3- benzene oxygen
Phenyl) 78 parts of methyl ester crushes, and powder diameter is 2800 mesh；(RS)-alpha- cyano -3- phenoxy benzyls are added
(SR) -3- (2,2- dichloroethylene) -184 parts of 2,2- dimethyl cyclopropane carboxylic acids ester is uniformly mixed, and is laid in pallet, is tiled
Thickness is 18 mm, and dosage is used to be irradiated 154 minutes and the same dose of β for the alpha ray that 10.2 kGy, energy are 15 MeV
X ray irradiation x 144 minutes；
3rd step：The mixed-powder handled through the 2nd step is dissolved in 1R- trans- -3- (the 2,2- dichloroethylene of a concentration of 85 ppm
Base) in -2,2- dimethyl cyclopropane carboxylic acids-(2,3,5,6,-tetrafluoro phenyl) 138 parts of methyl ester, reaction kettle is added, blender turns
Speed is 146 rpm, and temperature is 168 DEG C, and starting vacuum pump makes the vacuum degree of reaction kettle reach 1.22 MPa, keeps this state response
28 hours；Pressure release is simultaneously passed through radon gas, and it is 1.47 MPa to make reacting kettle inner pressure, and heat preservation stands 12 hours；Agitator speed is promoted
To 258 rpm, simultaneous reactions kettle pressure release to 0MPa；Sequentially add d-trans -2,2- dimethyl -3- (2- methyl-1-propylenes
Base) amyl- 228 parts of the 2- alkenyl esters of cyclopropane-carboxylic acid-S-2- methyl -3- (2- propargyls) -4- oxo rings, cyano-(3- phenoxy group benzene
Base) after methyl -3- (2,2- dichloroethylene) -155 parts of 2,2- dimethyl cyclopropane carboxylic acids ester is completely dissolved, crosslinking agent 75 is added
Part is stirred so that the hydrophilic lipophilic balance of reaction kettle solution is 9.2, and heat preservation stands 20 hours；
4th step：When agitator speed is 188 rpm, 2- (4- acetylaminohydroxyphenylarsonic acid 3- chlorphenyls) propionitrile 146 is sequentially added
Part, N- [2- [(2,4- dinitrophenyl) azo] -5- [(2- hydroxyl -3- phenoxy propyls) amino] -4- methoxyphenyls] second
249 parts of amide, (E)-N- [2- [(the bromo- 6- cyano -4- nitrobenzenes of 2-) azo group] -5- (lignocaine) phenyl] propionamide 58
Part, 2- [[4- [[2- (acetoxyl group) ethyl] butylamino] -2- aminomethyl phenyls] azo] bromo- 5- nitros-benzonitriles 147 of -3-
Part, reactor pressure is promoted, 1.2 MPa are reached, temperature is 214 DEG C, polymerisation 30 hours；It will reaction after the completion of reaction
Pressure is down to 0 MPa in kettle, is cooled to 43 DEG C, and discharging enters molding press and can be prepared by rotating vane 2-1；
The crosslinking agent is N- butyl-N- cyanoethyl anilines.
Reference examples
Reference examples are the rotating vane of certain commercially available brand.
Embodiment 4
Rotating vane described in the rotating vane 2-1 and reference examples that Examples 1 to 3 is prepared carries out using effect pair
Than.The two Unit Weight, collection airspeed, material compression strength, wind sweeping area are counted, the results are shown in Table 1.
As seen from Table 1, rotating vane 2-1 of the present invention, Unit Weight, material compression strength, are swept collection airspeed
The indexs such as wind area are superior to the product of prior art production.
In addition, as shown in fig. 6, being heretofore described rotating vane material corrosion resistant erosion degree with usage time variation diagram.
It can be seen from the figure that rotating vane 2-1 used in Examples 1 to 3, material corrosion resistant erosion degree with usage time variation degree substantially
Better than existing product.
Claims (7)
1. a kind of double blades wind power generating set with vertical shaft, including：Spindle blade（1）, countershaft blade（2）, swivel bearing（3）,
Variable pitch adjuster（4）, generator control room（5）, upper backup pad（6）, lower supporting plate（7）, main backstop（8）, pair support
Frame（9）；It is characterized in that, the spindle blade（1）Shape is half circle ring surface structure, spindle blade（1）Number is 4
It is a, spindle blade（1）With swivel bearing（3）Centered on axis be circumferentially distributed；Spindle blade（1）The other side is connected with countershaft blade
（2）；The upper backup pad（6）And lower supporting plate（7）For rectangular configuration, size is 1m~1.5m (length) × 0.5m~1m (width)
× 0.2m~0.4m (thickness)；Upper backup pad（6）With lower supporting plate（7）Between be provided with variable pitch adjuster（4）And generator
Control room（5）, wherein variable pitch adjuster（4）It is fixedly mounted on generator control room（5）Top, the variable pitch are adjusted
Device（4）With swivel bearing（3）Lower end coaxial rotating connection；The main backstop（8）For cylindrical structure, diameter 80mm~
Between 100mm, main backstop（8）It is fixedly welded on lower supporting plate（7）Bottom center；The pair supporting rack（9）Quantity is four,
And it is respectively fixedly connected in upper backup pad（6）Bottom surface quadrangle.
2. a kind of double blades wind power generating set with vertical shaft according to claim 1, which is characterized in that the countershaft blade
（2）Including：Rotating vane（2-1）, servo motor（2-2）, drive shaft（2-3）, wind speed measurement device（2-4）；The wherein described rotation
Blade（2-1）Contour structures are " C " font；The drive shaft（2-3）With rotating vane（2-1）Coaxial rotating connects；The drive
Moving axis（2-3）Upper end is equipped with servo motor（2-2）, servo motor（2-2）With rotating vane（2-1）It is drivingly connected；The wind
Fast detector（2-4）Positioned at rotating vane（2-1）Upper side.
3. a kind of double blades wind power generating set with vertical shaft according to claim 1, which is characterized in that the generator control
Room processed（5）Including：Gear（5-1）, generator（5-2）, electromagnetic brake（5-3）, microcontroller（5-4）, generator
Temperature inductor（5-5）, generator speed inductor（5-6）；The wherein described gear（5-1）Positioned at generator（5-2）
Top, gear（5-1）With generator（5-2）Rotate coaxially connection, gear（5-1）For cylindrical structure,
Outer diameter is between 10cm~15cm；The electromagnetic brake（5-3）Positioned at generator（5-2）Lower section, electromagnetic brake（5-3）With
Generator（5-2）Rotate coaxially connection；The microcontroller（5-4）It is fixedly mounted on generator control room（5）Bottom side；Institute
State generator-temperature detection inductor（5-5）And generator speed inductor（5-6）It is installed in generator（5-2）On；
The electromagnetic brake（5-3）, generator-temperature detection inductor（5-5）, generator speed inductor（5-6）Respectively by leading
Line and microcontroller（5-4）Control connection.
4. a kind of double blades wind power generating set with vertical shaft according to claim 3, which is characterized in that the gear drive
Case（5-1）Including：Low-speed gear（5-1-1）, high gear（5-1-2）, ring oiler（5-1-3）, fluid concentration detector
（5-1-4）；The wherein described low-speed gear（5-1-1）Positioned at gear（5-1）Side, the high gear（5-1-2）Position
In gear（5-1）The other side, low-speed gear（5-1-1）With high gear（5-1-2）It is connected by gear drive；It is described
Ring oiler（5-1-3）It is positioned over low-speed gear（5-1-1）With high gear（5-1-2）It is high above gear meshing portions position
Degree compares low-speed gear（5-1-1）It is higher by 1cm~1.5cm；The fluid concentration detector（5-1-4）Positioned at low-speed gear（5-1-
1）Gear side edge, fluid concentration detector（5-1-4）Apart from gear side along between 5mm~8mm；
The low-speed gear（5-1-1）Pass through conducting wire and microcontroller（5-4）Control connection.
5. a kind of double blades wind power generating set with vertical shaft according to claim 4, which is characterized in that the ring oiling
Device（5-1-3）Including：Oiling motor（5-1-3-1）, piston ring pusher（5-1-3-2）, oily cylinder（5-1-3-3）；It is wherein described
Oily cylinder（5-1-3-3）To be columnar structured, material is chrome-manganese-silicon steel material, oily cylinder（5-1-3-3）Outer diameter 3cm~5cm it
Between；The piston ring pusher（5-1-3-2）Positioned at oily cylinder（5-1-3-3）Inside, piston ring pusher（5-1-3-2）In oily cylinder
（5-1-3-3）Inside make compressional movement；The piston ring pusher（5-1-3-2）Top is provided with oiling motor（5-1-3-1）, note
Oily motor（5-1-3-1）With piston ring pusher（5-1-3-2）It is drivingly connected；
The oiling motor（5-1-3-1）Pass through conducting wire and microcontroller（5-4）Control connection.
6. a kind of double blades wind power generating set with vertical shaft according to claim 2, which is characterized in that the rotating vane
（2-1）It is molded by high molecular material pressing mold, rotating vane（2-1）Constituent and manufacturing process it is as follows：
One, rotating vane（2-1）Constituent：
It counts in parts by weight, 12~44 parts of (5R) -5- methyl -2- isopropyl -1- cyclohexenyl methoxyl methyls ether, 2,3,5,6- tetra-
Fluoro- 4- methylbenzyls (Z)-(1R, 3R, 1S, 3S) -3- (the chloro- 3,3,3- trifluoros propyl- 1- alkenyls of 2-) -2,2- dimethylcyclopropanes
32~85 parts of carboxylate, 2- (2- quinoline azo) 105~163 parts of -4- diethylamino Benzoic Acids, (S) alpha-cyano-phenoxy benzyl
(1R, 3R) -3- (2,2- dibromo vinyl) -53~114 parts of 2,2- dimethyl cyclopropane carboxylic acids ester, 3- (2,2- dichloroethylene
Base) -2,2- dimethyl cyclopropionate -33~78 parts of (1S, 3S)-REL- (R)-cyano (3- phenoxy phenyls) methyl ester, (RS) -
Alpha- cyano -3- phenoxy benzyls (SR) -3- (2,2- dichloroethylenes) -2,2- dimethyl cyclopropane carboxylic acids ester 112~
184 parts, the trans- -3- of 1R- (2,2- dichloroethylene) -2,2- dimethyl cyclopropane carboxylic acids-of a concentration of ppm of 44 ppm~85
(2,3,5,6,-tetrafluoro phenyl) 78~138 parts of methyl ester, d-trans -2,2- dimethyl -3- (2- methyl-1-propylenes base) ring
Amyl- 142~228 parts of the 2- alkenyl esters of propanecarboxylic acid's-S-2- methyl -3- (2- propargyls) -4- oxo rings, cyano-(3- phenoxy group benzene
Base) methyl -3- (2,2- dichloroethylene) -96~155 parts of 2,2- dimethyl cyclopropane carboxylic acids ester, 38~75 parts of crosslinking agent, 2-
(4- acetylaminohydroxyphenylarsonic acid 3- chlorphenyls) 69~146 parts of propionitrile, N- [2- [(2,4- dinitrophenyl) azo] -5- [(2- hydroxyls -3-
Phenoxy propyl) amino] -4- methoxyphenyls] 162~249 parts of acetamide, (E)-N- [2- [(bromo- 6- cyano -4- nitros of 2-
Benzene) azo group] -5- (lignocaine) phenyl] 22~58 parts of propionamide, 2- [[4- [[2- (acetoxyl group) ethyl] butyl ammonia
Base] -2- aminomethyl phenyls] azo] the bromo- 5- nitros of -3- -68~147 parts of benzonitrile；
The crosslinking agent is N- (2- cyanoethyls)-N-ethylaniline, N- butyl-N- cyanoethyl anilines, acetoaceto to chlorine neighbour
Any one in nitroaniline；
Two, rotating vane（2-1）Manufacturing process, comprise the steps of：
1st step：1150~1480 parts of the ultra-pure water that conductivity is 6.65 μ of μ S/cm~8.26 S/cm is added in a kettle, opens
Blender in dynamic reaction kettle, rotating speed are the rpm of 86 rpm~149, start heat pump, make reactor temperature rise to 52 DEG C~
84 ℃；Sequentially add (5R) -5- methyl -2- isopropyl -1- cyclohexenyl methoxyl methyls ether, tetra- fluoro- 4- methyl benzyls of 2,3,5,6-
Base (Z)-(1R, 3R, 1S, 3S) -3- (the chloro- 3,3,3- trifluoros propyl- 1- alkenyls of 2-) -2,2- dimethyl cyclopropane carboxylic acids ester, 2-
(2- quinoline azo) -4- diethylamino Benzoic Acids, stirring is to being completely dissolved, and it is 2.8~5.7 to adjust pH value, by agitator speed
The rpm of 108 rpm~182 are adjusted to, temperature is 73 DEG C~152 DEG C, esterification 14~25 hours；
2nd step：Take (S) alpha-cyano-phenoxy benzyl (1R, 3R) -3- (2,2- dibromo vinyls) -2,2- dimethylcyclopropane carboxylics
Acid esters, 3- (2,2- dichloroethylenes) -2,2- dimethyl cyclopropionate-(1S, 3S)-REL- (R)-cyano (3- phenoxy phenyls) methyl
Ester crushes, and powder diameter is 2100~2800 mesh；Addition (RS)-alpha- cyano -3- phenoxy benzyls (SR) -3- (2,
2- dichloroethylenes) -2,2- dimethyl cyclopropane carboxylic acid's esters be uniformly mixed, be laid in pallet, tiling thickness be 11 mm~18
Mm uses dosage to be irradiated 111~154 minutes for the alpha ray that the kGy of 5.5 kGy~10.2, energy are the MeV of 9 MeV~15, with
And the same dose of β x ray irradiation xs 63~144 minutes；
3rd step：The mixed-powder handled through the 2nd step is dissolved in the trans- -3- of 1R- (2,2- dichloroethylenes) -2,2- diformazans basic ring third
In alkane carboxylic acid-(2,3,5,6 ,-tetrafluoro phenyl) methyl ester, reaction kettle is added, agitator speed is the rpm of 92 rpm~146, temperature
Degree is 114 DEG C~168 DEG C, and starting vacuum pump makes the vacuum degree of reaction kettle reach the MPa of -0.68 MPa~1.22, keeps this state
Reaction 15~28 hours；Pressure release is simultaneously passed through radon gas, makes reacting kettle inner pressure for the MPa of 0.55 MPa~1.47, and heat preservation standing 8~
12 hours；Agitator speed is promoted to the rpm of 202 rpm~258, simultaneous reactions kettle pressure release to 0MPa；It is anti-to sequentially add dextrorotation
Formula -2,2- dimethyl -3- (2- methyl-1-propylenes base) cyclopropane-carboxylic acid-S-2- methyl -3- (2- propargyls) -4- oxo rings are amyl-
2- alkenyl esters, cyano-(3- Phenoxyphenyls) methyl -3- (2,2- dichloroethylenes) -2,2- dimethyl cyclopropane carboxylic acid's esters are complete
After fully dissolved, crosslinking agent is added and is stirred so that the hydrophilic lipophilic balance of reaction kettle solution is 4.8~9.2, and heat preservation is stood
11~20 hours；
4th step：When agitator speed is 123 rpm~188 rpm, 2- (4- acetylaminohydroxyphenylarsonic acid 3- chlorphenyls) third is sequentially added
Nitrile, N- [2- [(dinitrophenyl group) azo] -5- [(2- hydroxyl -3- phenoxy propyls) amino] -4- methoxyphenyls] second
Amide, (E)-N- [2- [(the bromo- 6- cyano -4- nitrobenzenes of 2-) azo group] -5- (lignocaine) phenyl] propionamides and 2- [[4-
[[2- (acetoxyl group) ethyl] butylamino] -2- aminomethyl phenyls] azo] the bromo- 5- nitros-benzonitriles of -3-, promote reaction kettle pressure
Power reaches the MPa of 1.2 MPa~2.5, and temperature is 158 DEG C~214 DEG C, polymerisation 22~30 hours；After the completion of reaction
Reacting kettle inner pressure is down to 0 MPa, is cooled to 33 DEG C~43 DEG C, discharging enters molding press and can be prepared by rotating vane（2-
1）.
7. a kind of working method of double blades wind power generating set with vertical shaft, which is characterized in that this method includes following step
Suddenly：
1st step：Staff opens general supply and master controller, is now placed in countershaft blade（2）On wind speed measurement device（2-4）
It starts to work；When wind speed measurement device（2-4）When detecting that wind speed is less than 1m/s, wind speed measurement device（2-4）Detection signal is sent
To master controller, master controller starts countershaft blade（2）On servo motor（2-2）, servo motor（2-2）Promote drive shaft
（2-3）It rotates, to drive rotating vane（2-1）With drive shaft（2-3）It moves in a circle for rotary shaft；In pivoting leaf
Piece（2-1）Under the drive of motional inertia, spindle blade（1）Around swivel bearing（3）Rotation；
2nd step：In spindle blade（1）And countershaft blade（2）In rotary course, generator control room（5）Interior gear
（5-1）Pass through low-speed gear（5-1-1）Drive high gear（5-1-2）By spindle blade（1）With countershaft blade（2）Rotation speed
Degree improves, to promote generator（5-2）Power generation；
3rd step：In generator（5-2）In power generation process, generator-temperature detection inductor（5-5）And generator speed inductor（5-
6）Respectively to generator（5-2）Temperature and rotating speed monitor in real time；When generator-temperature detection inductor（5-5）Detect generator
（5-2）When temperature is higher than 110 DEG C, generator-temperature detection inductor（5-5）Electric signal is sent to microcontroller（5-4）, microcontroller
Device（5-4）Control low-speed gear（5-1-1）Reduce rotary speed；When generator speed inductor（5-6）Detect generator（5-
2）Rotating speed when being more than 1.5 times of rated speed, generator speed inductor（5-6）Detection signal is sent to microcontroller
（5-4）, microcontroller（5-4）Start electromagnetic brake（5-3）, electromagnetic brake（5-3）By generator（5-2）Rotating speed reduce
To the permission range of speeds；
4th step：Gear（5-1）In fluid concentration detector（5-1-4）To low-speed gear（5-1-1）With high gear
（5-1-2）Between fluid density real-time monitoring, when fluid concentration detector（5-1-4）Detect that fluid concentration is less than 10 ppm
When, microcontroller（5-4）Start oiling motor（5-1-3-1）, oiling motor（5-1-3-1）Drive piston ring pusher（5-1-
3-2）In oily cylinder（5-1-3-3）Compressional movement is inside done, to which fluid is injected in low-speed gear（5-1-1）With high gear（5-
1-2）Between；When fluid concentration detector（5-1-4）When detecting that fluid concentration is higher than 45 ppm, microcontroller（5-4）It closes
Oiling motor（5-1-3-1）；
5th step：Generator（5-2）After the alternating current of generation is by rectification, filtering, reversion reaction, it is converted to workable exchange
Electricity.
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| CN101487445A (en) * | 2009-02-25 | 2009-07-22 | 陈小兵 | Rotary-vane vertical wind energy engine |
| US8303249B2 (en) * | 2009-06-17 | 2012-11-06 | General Electric Company | Wind turbine and method for optimizing energy production therein |
| CN202756176U (en) * | 2012-05-08 | 2013-02-27 | 李�杰 | Vertical-axis wind turbine with speed-adjustable wind turbine blades |
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