CN108658421A - A kind of cold air accelerator in sludge dewatering negative pressure High shear device - Google Patents

Abstract

A kind of cold air accelerator in sludge dewatering negative pressure High shear device of disclosure of the invention.It is equipped with controls connecting rod in cold air accelerating chamber hull outside, the airlock that controls connecting rod accelerates wind turbine, two level to accelerate wind turbine respectively at level-one controls connection；The cold air outlet bell shape, port and the seamless perforation connection of two level acceleration wind turbine thereon, the bore of lower port accelerates room housing bore equal with cold air, and seamless welding；Cold air enters cold air accelerating chamber from cold air import, is magnetized by way of electromagnetism ring, in the case where level-one accelerates wind turbine, two level to accelerate the acceleration of wind turbine, is sprayed from cold air outlet；Meanwhile cooling water enters cooling jacket from wind turbine water inlet pipe, accelerates wind turbine, two level that wind turbine is accelerated to cool down for level-one, and flowed out from wind turbine outlet pipe.The device intelligence degree is high, and stability is good, small to whole equipment impact force, high yield rate.

Description

A kind of cold air accelerator in sludge dewatering negative pressure High shear device

Technical field

The invention belongs to device for dehydrating sladge waste fields, and in particular to a kind of in sludge dewatering negative pressure High shear device Cold air accelerator.

Background technology

In the high shear synergistic supersonic wave course of work, need to add the raw materials such as antioxidant in cold air accelerating chamber to improve dirt Material cooling may be implemented using high shear synergistic supersonic wave ancillary equipment under the negative pressure of automation in the performance of mud dehydration, and right Quality of material is accurately added, and human input can also be significantly reduced.Existing structure is complicated, accelerating chamber work is unstable Fixed, cold air blows ineffective, waste of manpower, material resources.

Invention content

In order to solve the above technical problem, the present invention provides a kind of cold air in sludge dewatering negative pressure High shear device Accelerator, the work piece holder 4 are arranged in 5 other side of support platform；The control system 6 is fixedly mounted on fixed frame 2 On；The rolling cutter 7 is located at 3 left side of pushing mechanism, the two connection.

Further, what this section was told about is heretofore described 3 structure of pushing mechanism.The speed regulating motor transmission shaft 3- 10 one end are connect with speed regulating motor 3-4, and the other end passes through fuel tank 3-5, pushes disk brake apparatus 3-9, hydraulic cylinder 3-6 and push disk 3-7 is fixedly connected, and speed regulating motor 3-4, which drives, pushes disk 3-7 rotations；The fuel tank 3-5 is connected to the one end hydraulic cylinder 3-6 conduit； The hydraulic cylinder 3-6 other ends push disk 3-7 to connect with detachable；The promotion disk brake apparatus 3-9 be located at push disk 3-7 with Hydraulic cylinder 3-6 is between the two；The speed regulating motor 3-4, hydraulic cylinder 3-6, disk 3-7 central axis are pushed in the same horizontal line, It pushes disk 3-7 to be connect with rolling cutter 7, pushes disk 3-7 that rolling cutter 7 is driven to rotate；The speed regulating motor 3-4, hydraulic cylinder 3-6 It is connected respectively by conducting wire and the control of control system 6；The slide motor 3-8 is connected by conducting wire and the control of control system 6.

Further, what this section was told about is 7 structure of heretofore described rolling cutter.The peripheries water inlet pipe 7-7 are equipped with heating Pipe 7-5, heating tube 7-5 helical structures, the one end heating tube 7-5 are connected to by conducting wire with transformer 7-2, and transformer 7-2's is another End is electrically connected by conducting wire with external city, and heating tube 7-5 implements heating to water inlet pipe 7-7, and transformer 7-2 implements heating temperature It adjusts；Outside transmission shaft 7-9 be equipped with cutting edge 7-3, cutting edge 7-3 quantity be 4,4 cutting edge 7-3 angularly, center Axial symmetry mode is fixed on transmission shaft 7-9；It is equipped with cutting edge nozzle 7-6, cutting edge nozzle 7-6 mono- in the roots cutting edge 7-3 End open design is simultaneously directed toward cutting edge 7-3 knife faces, and the cutting edge nozzle 7-6 other ends are connected to water inlet pipe 7-7；Driven wheel 7-1 is logical Crossing transmission shaft 7-9 drives cutting edge 7-3 rotations, cutting edge 7-3 to implement equidistant cutting to material；Meanwhile 7-6 pairs of cutting edge nozzle Cutting edge 7-3 knife faces implement cleaning.

Further, what this section was told about is in the present invention for the cooling device structure of slideway 3-2 settings.It is superposed slow Process chamber 3-2-5 is rushed, top is equipped with refrigerant inlet 3-2-6, and the buffered room 3-2-5 and refrigerant inlet 3-2-6 on top connect Logical, buffered room its bottom 3-2-5 for being located at lower part is equipped with refrigerant exit 3-2-9, the buffered room 3-2-5 of lower part and bottom The refrigerant exit 3-2-9 connections in portion；The medicament mixing device 3-2-8 is connected to heat-exchanging chamber 3-2-3；Refrigerant is from refrigerant inlet 3-2-6 enters buffered room 3-2-5, and then enters inside heat-exchange tube 3-2-2, caused by heat-exchange tube 3-2-2 Heat absorption, and flowed out from refrigerant exit 3-2-9；Heat-exchanging chamber 3-2-3 is entered from by coolant liquid entrance 3-2-1 by coolant liquid, Heat-exchange tube 3-2-2 is transferred heat to, and from by coolant liquid outlet 3-2-7 outflows；Meanwhile external agent is mixed by medicament Device 3-2-8 is controllably added to inside heat-exchanging chamber 3-2-3, is reacted with by coolant liquid.

Further, what this section was told about is heretofore described medicament mixing device 3-2-8 structures.The agitation ball 3- 2-8-5 is located on the right side of buffer subsystem 3-2-8-4, and agitation ball 3-2-8-5 is macromolecule thin-walled hollow structure, stirs ball 3-2-8-5 materials Matter density is less than the density of water, and agitation ball 3-2-8-5 quantity is 50~100, and the single ball 3-2-8-5 mass that stirs is less than 10 Gram, between multiple agitation ball 3-2-8-5 are limited at buffer subsystem 3-2-8-4 and stablize net 3-2-8-6, the agitation ball 3-2-8- 5 be scattered distribution, and gap mutual agitation ball 3-2-8-5 is more than 5cm；The stable net 3-2-8-6 is located at agitation ball 3- On the right side of 2-8-5, it is holey, vertical display to stablize net 3-2-8-6；Medicament enters from medicament inlet 3-2-8-1, with diluent The diluent sprayed into pipe 3-2-8-9 meets, will be dilute under the action of decentralized network 3-2-8-8, diffusion horn mouth 3-2-8-7 Agent is released further to disperse and mix with medicament；Diffusant enters pipe 3-2-8-3 by diffusant and is sprayed from diffusant jet pipe 3-2-8-2 Go out, buffer subsystem 3-2-8-4 implements buffering to the diffusant of ejection, and enters together with medicament, diluent and be located at buffer subsystem 3-2- Agitation ball 3-2-8-5 action spaces between 8-4 and stable net 3-2-8-6, in the case where stirring ball 3-2-8-5 agitaions, diffusion Agent, diluent, medicament are sufficiently mixed, and mixture is discharged from agent outlet 3-2-8-10.

Further, what this section was told about is heretofore described promotion disk brake apparatus 3-9 structures.Brake hauling rope 3- The other end of 9-3 is connect with haulage gear 3-9-2；It is equipped with brake cooling system 3-9-1, the two on the tops brake caliper 3-9-4 It is connected by conduit；Haulage gear 3-9-2 rotations, tightening braking hauling rope 3-9-3, and then by brake caliper 3-9-4 by 4 Friction plate 3-9-6 is tightly attached on speed regulating motor transmission shaft 3-10, and speed regulating motor transmission shaft 3-10 is made to stop operating；At the same time, The heat that friction plate 3-9-6 is generated by friction, is taken away by the brake cooling system 3-9-1 being connect with brake caliper 3-9-4.

Further, what this section was told about is heretofore described brake cooling system 3-9-1 structures.Butterfly plate 3-9-1- 1 sets there are two arc side wing, two arc side wing central symmetries, and two arc side wings pass through butterfly ventilating hole plate 3-9-1- 2 connections, butterfly ventilating hole plate 3-9-1-2 promote air-flow to form turbulent flow in its both sides；Barrier board is equipped on the left of oscillating deck 3-9-1-8 3-9-1-7, barrier board 3-9-1-7 are placed vertically, and barrier board 3-9-1-7 is internally provided with a large amount of horizontal grates, barrier board 3-9-1-7 Left and right is penetrating；Lower open mouth wing plate 3-9-1-6 is equipped on the left of barrier board 3-9-1-7, between the two away from for 10cm, lower open mouth wing plate 3- 9-1-6 is vertically arranged；Lower open mouth wing plate 3-9-1-6 is set there are two facing side wing directly, and two are faced directly side wing central symmetry, two Face open design between side wing directly, two face side wing directly between hard cable wire be fixedly connected；In brake cooling system 3-9-1 Side is equipped with oily atomizer 3-9-1-10；The cool room gas outlet lower parts 3-9-1-9 be equipped with oil collection box 3-9-1-11, the two it Between be equipped with certain distance；The deep fat sprayed from oily atomizer 3-9-1-10 is cold with cool room in brake cooling system 3-9-1 The cold air that gas import 3-9-1-4 is generated carries out heat exchange, and oil after cooling converges in oil collection box 3-9-1-11；It is cold in cool room The tops gas import 3-9-1-4 are equipped with cold air accelerating chamber 3-9-1-12.

Further, what this section was told about is heretofore described cold air accelerating chamber 3-9-1-12 structures.Accelerate in cold air Controls connecting rod 3-9-1-12-9 is equipped with outside room housing 3-9-1-12-2, controls connecting rod 3-9-1-12-9 accelerates wind respectively at level-one Machine 3-9-1-12-6, two level accelerate the airlock control connection of wind turbine 3-9-1-12-4；The cold air outlet 3-9-1-12-1 loudspeakers Mouth-shaped, port and the seamless perforation connections of two level acceleration wind turbine 3-9-1-12-4 thereon, bore and the cold air of lower port add Fast room housing 3-9-1-12-2 bores are equal, and seamless welding；Cold air enters cold air accelerating chamber from cold air import 3-9-1-12-10 3-9-1-12 is magnetized by way of electromagnetism ring 3-9-1-12-8, accelerates wind turbine 3-9-1-12-6, two level to accelerate wind turbine 3-9- in level-one Under the acceleration of 1-12-4, sprayed from cold air outlet 3-9-1-12-1；Meanwhile cooling water is from wind turbine water inlet pipe 3-9-1-12-3 Into cooling jacket, accelerate wind turbine 3-9-1-12-6, two level that wind turbine 3-9-1-12-4 is accelerated to cool down for level-one, and from wind turbine Outlet pipe 3-9-1-12-5 outflows.

Further, what this section was told about is heretofore described 4 structure of work piece holder.The electric rotating machine 4-1 is fixed Mounted on the sides service chamber 4-2, electric rotating machine 4-1 is drivingly connected with central gear 4-5；The workpiece handgrip 4-3 is arranged in inspection The other sides case 4-2 are repaiied, workpiece one end handgrip 4-3 is fixedly connected with handgrip gear 4-6；The lap count 4-7 is fixedly connected On electric rotating machine 4-1 turntables；The electric rotating machine 4-1, lap count 4-7 are controlled by conducting wire and control system 6 respectively Connection；Electric rotating machine 4-1 driving central gear 4-5 rotations, and then drive three, periphery handgrip gear 4-6 along gear wheel 4-4 Interior tooth does revolution motion, while three handgrip gear 4-6 are also done rotation movement, and handgrip gear 4-6 is driven by workpiece handgrip 4-3 Workpiece revolves round the sun and rotation.

Further, what this section was told about is heretofore described lap count 4-7 structures.In conversion head 4-7-2 water It square pops one's head in 4-7-11 to equipped with spare Laser Measuring circle, quantity is 4, spare Laser Measuring circle probe 4-7-11 and Laser Measuring circle 4-7-1 structures of popping one's head in are identical, and Laser Measuring circle probe 4-7-1 and spare Laser Measuring circle probe 4-7-11 are Demountable；Institute State the tops rotary shaft 4-7-7 and be equipped with gearbox 4-7-5, gearbox 4-7-5 is internally provided with deboost axle 4-7-3, deboost axle 4-7-3 with The engagement connection of rotary shaft 4-7-7 gears；The tops gearbox 4-7-5 be equipped with electric rotating machine 4-7-10, electric rotating machine 4-7-10 with subtract Fast axis 4-7-3 gears engagement connection；The bottoms gearbox 4-7-5 are equipped with temperature sensor 4-7-4, velocity sensor 4-7-6；Rotation Motor 4-7-10 drives the probe 4-7-1 rotations of Laser Measuring circle by deboost axle 4-7-3, rotary shaft 4-7-7, to exchange Laser Measuring circle The operating angle of probe 4-7-1；At the same time, it is located at temperature sensor 4-7-4, the velocity sensor of the bottoms gearbox 4-7-5 4-7-6 is in real time monitored the object state on workbench 4.

Further, what this section was told about is heretofore described workpiece handgrip 4-3 structures.Banjo traction splint 4-3-3 drives Dynamic motor, workpiece clamp tightness inductor 4-3-4 are connected by conducting wire and the control of control system 6 respectively.It is set in the control system 6 It is equipped with timer, the timer is connect with speed regulating motor 3-4 actuating coil polygon control surveys.

Further, the wind turbine water inlet pipe 3-9-1-12-3 is molded by high molecular material pressing mold, wind turbine water inlet pipe 3-9- The constituent and manufacturing process of 1-12-3 is as follows：

One, wind turbine water inlet pipe 3-9-1-12-3 constituents：

339.2~564.8 parts of lake water of meter purification in parts by weight, N- methyl-1s, 1,2,2,3,3,4,4,5,5,5- ten one fluoro- 131.5~173.6 parts of 1- pentanes sulfonamide, 134.2~243.1 parts of 1- (methoxy) -4- methylbenzenes, 4- (methyl mercapto) fourth 130.4~147.4 parts of aldehyde, 133.1~190.3 parts of rutile, bis- [2- (2- the acrylic)] phenol of 4,4'- (1- methyl ethylidene) With 136.9~197.5 parts of the polymer of (chloromethyl) ethylene oxide, 138.7~193.3 parts of silver nano-particle, polymerization oxidation 1,1,2,3,3,3,131.1~173.6 parts of-hexafluoro -1- propylene, the polymer of formaldehyde and dicyanodiamide and ethylenediamine sulfate 133.6~173.5 parts, 133.9~156.6 parts of alkali formula aphthenic acids zinc salt, methyl ethyl ketoxime sealing end [2,4,6- tri- oxygen triazine -1, 3,5 (2H, 4H, 6H)-three base] three 122.5~158.8 parts of (cyclohexyl) isocyanates, 121.2~164.8 parts of 7- methyl octanals, 130.8~175.4 parts of (2E)-formic acid -2- hexen-1-ols ester, 140.3~184.3 parts of the polymer of polyurethane, mass concentration are 163.4~217.8 parts of the rosolic acid cetyl ester of 130mg/L~397mg/L；

Two, the manufacturing process of wind turbine water inlet pipe 3-9-1-12-3, comprises the steps of：

1st step：In tower reactor is found in stirring, it is added and purifies lake water and N- methyl-1s, 1,2,2,3,3,4,4,5,5,5- ten One fluoro -1- pentane sulfonamide starts the blender in the vertical tower reactor of stirring, and setting speed is 132rpm~178rpm, Start the steam oil heater in the vertical tower reactor of stirring, so that temperature is risen to 147.2 DEG C~148.8 DEG C, 1- (methoxies are added Ylmethyl) -4- methylbenzenes stir evenly, and carry out reaction 124.5~135.6 minutes, and 4- (methyl mercapto) butyraldehyde is added, is passed through flow For 123.5m³/ min~164.4m³The helium of/min 124.5~135.6 minutes；It is added in tower reactor is found in stirring later Rutile, the steam oil heater being again started up in the vertical tower reactor of stirring, makes temperature rise to 164.2 DEG C~197.1 DEG C, 4,4'- (1- methyl ethylidene) bis- [2- (2- acrylic)] phenol and (chloromethyl) ring is added in heat preservation 124.4~135.4 minutes The polymer of oxidative ethane, the pH value that solution in tower reactor is found in adjustment stirring are 4.1~8.3, keep the temperature 124.1~364.1 points Clock；

2nd step：Separately take silver nano-particle, by silver nano-particle power be 6.64KW~12.08KW under ultrasonication 0.130 After~1.197 hours；Silver nano-particle is added to another stirring to stand in tower reactor, addition mass concentration is 134mg/ The 1 of the polymerization oxidation of L~364mg/L, 1,2,3,3,3,-hexafluoro -1- propylene disperses silver nano-particle, and it is vertical tower anti-to start stirring The steam oil heater in device is answered, makes solution temperature between 45 DEG C~89 DEG C, starts stirring and stands stirring in tower reactor Machine is mixed, and with 4 × 10²Rpm~8 × 10²The speed of rpm stirs, and adjusts pH value between 4.5~8.8, and insulated and stirred 130~ 197 minutes；Stop reaction later and stand 6.64 × 10~12.08 × 10 minutes, removes impurity；Formaldehyde and two is added in suspension The polymer of cyano diamides and ethylenediamine sulfate, adjustment pH value form sediment and are washed with purification lake water between 1.5~2.8 It is de-, by centrifuge in rotating speed 4.192 × 10³Rpm~9.643 × 10³Solid content is obtained under rpm, 2.407 × 10²DEG C~ 3.642×10²It is dry at a temperature of DEG C, 0.192 × 10 is crossed after grinding³~1.643 × 10³Mesh sieves, spare；

3rd step：Another silver nano-particle after taking alkali formula aphthenic acids zinc salt and the processing of the 2nd step, uses the small angle of glancing incidence after mixing Gamma-rays diffusing reflection irradiation is spent, the energy of glancing incidence low-angle gamma-rays diffusing reflection irradiation is 121.2MeV~149.8MeV, agent Amount is 169.2kGy~209.8kGy, irradiation time is 133.2~158.8 minutes, obtains the alkali formula zinc naphthenate of character change Salt and silver nano-particle mixture；Alkali formula aphthenic acids zinc salt and silver nano-particle mixture are placed in another stirring and stand tower reaction In device, start the steam oil heater in the vertical tower reactor of stirring, 132.8 DEG C~178.4 DEG C of set temperature starts stirring Blender in vertical tower reactor, rotating speed are 124rpm~519rpm, and pH is adjusted between 4.3~8.3, dehydration 133.3~ 147.3 minute, spare；

4th step：The alkali formula aphthenic acids zinc salt and silver nano-particle mixture that the character that 3rd step is obtained changes, it is dense to add to quality [- three base of tri- oxygen triazines -1,3,5 (2H, 4H, 6H) of 2,4,6-] three that the methyl ethyl ketoxime that degree is 134mg/L~364mg/L blocks In (cyclohexyl) isocyanates, cocurrent add to the 1st step stirring stand tower reactor in, flow acceleration be 269mL/min~ 997mL/min；Start stirring and found tower reactor blender, setting speed is 138rpm~178rpm；Stirring 4~8 minutes；Again 7- methyl octanals are added, starts the steam oil heater in the vertical tower reactor of stirring, is warming up to 168.4 DEG C~205.8 DEG C, PH is adjusted between 4.4~8.8, and it is 123.118m to be passed through helium ventilatory capacity³/ min~164.273m³/ min, heat preservation are stood 158.2~188.8 minutes；It is again started up stirring and founds tower reactor blender, rotating speed is 133rpm~178rpm, is added (2E)-formic acid -2- hexen-1-ol esters, and pH is adjusted between 4.4~8.8, heat preservation stands 157.5~197.6 minutes；

5th step：Start the blender in the vertical tower reactor of stirring, setting speed is 130rpm~197rpm, and it is vertical to start stirring Steam oil heater in tower reactor sets stirring and founds temperature in tower reactor as 1.287 × 10²DEG C~2.32 ×10²DEG C, the polymer of polyurethane is added, reacts 124.2~135.1 minutes；Rosolic acid cetyl ester is added later, starts The steam oil heater in tower reactor is found in stirring, set temperature in the vertical tower reactor of stirring as 208.4 DEG C~ 264.4 DEG C, pH is adjusted between 4.1~8.1, and pressure is 1.3MPa~1.31MPa, and the reaction time is 0.4~0.9 hour；It After be depressurized to normal pressure, be cooled to 124.2 DEG C~135.1 DEG C and discharge into molding press to get to wind turbine water inlet pipe 3-9-1-12-3；Institute The grain size for stating silver nano-particle is 138 μm~148 μm.

Further, a kind of working method for the cold air accelerator in sludge dewatering negative pressure High shear device, should Method includes following steps：

1st step：Object to be cut is encased in the workpiece slot 4-3-2 on workpiece handgrip 4-3 by treatment process, control system 6 Banjo traction splint 4-3-3 work is controlled, process object is clamped；Workpiece clamp tightness inductor 4-3-4 monitors process object in real time Clamping degree, when workpiece clamp tightness inductor 4-3-4 detects that process object clamping degree reaches default value M, Workpiece clamping Feedback signal is sent to control system 6 by degree inductor 4-3-4, and control system 6 controls banjo traction splint 4-3-3 and is stopped；

2nd step：At the same time, control system 6 starts the slide motor 3-8 of the ends sliding block 3-3, in the case where slide motor 3-8 drives, Sliding block 3-3 does sliding motion along slideway 3-2, pushes disk 3-7 to be leaned on to the workpiece for being fixed on the ends workpiece handgrip 4-3 to drive Closely；When pushing disk 3-7 apart from workpiece 3cm~5cm, control system 6 stops slide motor 3-8 work, while controlling hydraulic cylinder 3-6 works；Under hydraulic cylinder 3-6 drivings, push disk 3-7 slowly close to workpiece, until pushing disk 3-7 front end blades and processing Object end face is in contact；

3rd step：Control system 6 starts the electric rotating machine 4- in speed regulating motor 3-4 and work piece holder 4 in pushing mechanism 3 simultaneously 1；Under speed regulating motor 3-4 drivings, disk 3-7 is pushed to do circular motion clockwise；Under the driving of electric rotating machine 4-1 motors, workpiece Handgrip 4-3 does counterclockwise circular motion by handgrip gear 4-6；

4th step：In electric rotating machine 4-1 rotary courses, lap count 4-7 monitors electric rotating machine 4-1 rotating cycles in real time；When When lap count 4-7 detects that electric rotating machine 4-1 rotating cycles reach default value R, lap count 4-7 is by feedback letter It number is sent to control system 6, control system 6 controls electric rotating machine 4-1 and is stopped；

5th step：In the speed regulating motor 3-4 courses of work, when the timer in control system 6 works to speed regulating motor 3-4 Between carry out timing；When timer, which adds up timing time, reaches default value T, control system 6 stops speed regulating motor 3-4；

6th step：Control system 6 controls banjo traction splint 4-3-3 and unclamps, and the workpiece handled well enters subsequent processing.

A kind of cold air accelerator in sludge dewatering negative pressure High shear device of the present invention, device intelligence Change degree is high, and time intelligence is controllable, and cooling quality is substantially improved, and stability is high, and the speed of service is fast, to other equipment impact force Small, work efficiency is high.

Description of the drawings

Fig. 1 is that a kind of heretofore described cold air accelerator in sludge dewatering negative pressure High shear device is illustrated Figure.

Fig. 2 is heretofore described 3 structural schematic diagram of pushing mechanism.

Fig. 3 is 7 structural schematic diagram of heretofore described rolling cutter.

Fig. 4 is in the present invention for the cooling device structural schematic diagram of slideway 3-2 settings.

Fig. 5 is heretofore described medicament mixing device 3-2-8 structural schematic diagrams.

Fig. 6 is heretofore described promotion disk brake apparatus 3-9 structural schematic diagrams.

Fig. 7 is heretofore described brake cooling system 3-9-1 structural schematic diagrams.

Fig. 8 is heretofore described cold air accelerating chamber 3-9-1-12 structural schematic diagrams.

Fig. 9 is heretofore described 4 structural schematic diagram of work piece holder.

Figure 10 is heretofore described lap count 4-7 structural schematic diagrams.

Figure 11 is heretofore described workpiece handgrip 4-3 structural schematic diagrams.

Figure 12 is heretofore described wind turbine water inlet pipe 3-9-1-12-3 material wear-resistant rates with usage time variation diagram.

Specific implementation mode

With reference to the accompanying drawings and examples to provided by the invention a kind of in sludge dewatering negative pressure High shear device Cold air accelerator is further described.

As shown in Figure 1, being that a kind of heretofore described cold air in sludge dewatering negative pressure High shear device accelerates Schematic device.The fixed frame 2 is stainless steel rectangular structure, and thickness is between 3cm~4cm；The shock-absorbing foot pad 1 counts Amount is four, is respectively and fixedly installed to 2 bottom four corners of fixed frame；The support platform 5 is rectangle galvanized sheet, support platform 5 It is fixedly mounted on 2 top of fixed frame；The pushing mechanism 3 is arranged in 5 side of support platform.

As shown in Fig. 2, being heretofore described 3 structural schematic diagram of pushing mechanism.The slideway 3-2 is fixed by slideway Block 3-1 is fixedly connected with support platform 5；The cross sections the slideway 3-2 are in " Ω " shape, and slideway 3-2 quantity is 2；The cunning Block 3-3 is slidably connected with slideway 3-2, and the ends sliding block 3-3 are provided with slide motor 3-8, and slide motor 3-8 drivings sliding block 3-3 exists It is slided on slideway 3-2；The speed regulating motor 3-4 is variable-frequency motor, and speed regulating motor 3-4 pedestals are welded and fixed with sliding block 3-3.

As shown in figure 3, being 7 structural schematic diagram of heretofore described rolling cutter.Driven wheel 7-1 positioned at one end, with External cutter motor connection, meanwhile, driven wheel 7-1 is fixedly connected with transmission shaft 7-9；Support is equipped on the inside of driven wheel 7-1 Roller bearing holds 7-4, and the back-up roller bearing 7-4 quantity is 2, is located at the both ends of transmission shaft 7-9；In the transmission shaft 7-9 Hollow structure is internally provided with transformer 7-2, heating tube 7-5, water inlet pipe 7-7；Water inlet pipe 7-7 is parallel to transmission shaft 7-9, water inlet pipe The quantity of 7-7 is 3, and water inlet pipe 7-7 is connected to water inlet port 7-8, and water inlet port 7-8 is connected to external pump.

As shown in figure 4, being the cooling device structural schematic diagram being arranged for slideway 3-2 in the present invention.Positioned at the cold of side But liquid entrance 3-2-1 is connected to heat-exchanging chamber 3-2-3, and is located at lower parts heat-exchanging chamber 3-2-3, low by coolant liquid entrance 3-2-1 Position；It is described that the tops heat-exchanging chamber 3-2-3, a high position are located at by coolant liquid outlet 3-2-7, and handed over heat by coolant liquid outlet 3-2-7 Change room 3-2-3 connections；The heat-exchange tube 3-2-2 is located in the middle part of heat-exchanging chamber 3-2-3, heat-exchange tube 3-2-2 hollow structures, heat The quantity for exchanging pipe 3-2-2 is 20, the more vertical equidistant arrangements of heat-exchange tube 3-2-2；The both ends heat-exchange tube 3-2-2 are set respectively There are buffered room 3-2-5, the both ends heat-exchange tube 3-2-2 to be connected to respectively with the buffered room 3-2-5 for being located at its upper and lower ends； The buffered room 3-2-5 is separated by the partition board 3-2-4 and buffered room 3-2-5 of upper and lower ends.

As shown in figure 5, being heretofore described medicament mixing device 3-2-8 structural schematic diagrams.The medicament mixing dress It is L-type pipe structure, both ends perforation to set 3-2-8, is located at the medicament inlet 3-2-8-1 of one end, is equipped on the right side of medicament inlet 3-2-8-1 Diluent enters pipe 3-2-8-9, and diluent enters the one end pipe 3-2-8-9 and is connected to external diluent bottle, and diluent enters pipe The 3-2-8-9 other ends are open, and are inserted into inside diffusion horn mouth 3-2-8-7；It is equipped in the middle part of diffusion horn mouth 3-2-8-7 Decentralized network 3-2-8-8 is holey, vertical display；It is flared structure, heavy caliber end to spread horn mouth 3-2-8-7 Towards right side, the diameter ratio for spreading horn mouth 3-2-8-7 heavy calibers end and small-caliber end is 3:1；The diffusant jet pipe 3-2- 8-2 is located on the right side of diffusion horn mouth 3-2-8-7, is hollow ring pipe structure, the ring pipe right side of diffusant jet pipe 3-2-8-2 Surface is equipped with a large amount of through-holes, and diffusant one end jet pipe 3-2-8-2 enters pipe 3-2-8-3 with diffusant and is connected to；The buffer subsystem 3-2- 8-4 is located at diffusant and enters on the right side of pipe 3-2-8-3, and buffer subsystem 3-2-8-4 is holey, vertical display.

As shown in fig. 6, being heretofore described promotion disk brake apparatus 3-9 structural schematic diagrams.On central axes Speed regulating motor transmission shaft 3-10 is surrounded by friction plate 3-9-6, and friction plate 3-9-6 quantity is 4,4 friction plate 3-9-6 Wherein by speed regulating motor transmission shaft 3-10 packages, the periphery of friction plate 3-9-6 is equipped with brake caliper 3-9-4, brake caliper 3- 9-4 is cyclic annular, is divided into pintongs, and friction plate 3-9-6 is fixed on the inside of brake caliper 3-9-4；It is equipped with and dissipates on the left of brake caliper 3-9-4 Hot-air fan 3-9-5, radiator fan 3-9-5 are brake caliper 3-9-4 coolings；The peripheries brake caliper 3-9-4 are equipped with braking hauling rope 3-9-3, braking hauling rope 3-9-3 are around brake caliper 3-9-4 surroundings, and the two is hinged.

As shown in fig. 7, being heretofore described brake cooling system 3-9-1 structural schematic diagrams.Refrigeration positioned at top Room cold air import 3-9-1-4, up and down with the cool room gas outlet 3-9-1-9 positioned at bottom；In cool room cold air import 3- 9-1-4 vertical pivots center is equipped with cool room agitating shaft 3-9-1-5, and cool room one end agitating shaft 3-9-1-5 is stirred with external refrigeration room Motor connects, and the other end is fixedly connected with cool room paddle 3-9-1-3；It is equipped in the lower parts cool room paddle 3-9-1-3 Oscillating deck 3-9-1-8, the oscillating deck 3-9-1-8 thin-slab structures, single oscillating deck 3-9-1-8 are placed vertically, oscillating deck 3-9- 1-8 quantity is 20,20 oscillating deck 3-9-1-8 be divided to for two groups, be vertically arranged, with group oscillating deck 3-9-1-8 between each other away from From for 10cm, with organizing soft rope chain concatenation between oscillating deck 3-9-1-8, and with it is fixed at the top of brake cooling system 3-9-1, with group pendulum Vacantly at the central axes brake cooling system 3-9-1, oscillating deck 3-9-1-8's movable plate 3-9-1-8 swings with air-flow；It is swinging Butterfly plate 3-9-1-1 is equipped on the right side of plate 3-9-1-8, butterfly plate 3-9-1-1 thin-slab structures, single butterfly plate 3-9-1-1 are put vertically It sets, butterfly plate 3-9-1-1 quantity is 20, and 20 butterfly plate 3-9-1-1 are vertically arranged.

As shown in figure 8, being heretofore described cold air accelerating chamber 3-9-1-12 structural schematic diagrams.In cold air accelerating chamber shell It is equipped with cold air import 3-9-1-12-10 at the top of body 3-9-1-12-2, accelerates the bottoms room housing 3-9-1-12-2 to be equipped in cold air cold Gas exports 3-9-1-12-1, cold air import 3-9-1-12-10 and cold air outlet 3-9-1-12-1 up and down；In cold air import 3- The lower parts 9-1-12-10 are equipped with electromagnetism ring 3-9-1-12-8, and electromagnetism ring 3-9-1-12-8 is connect by conducting wire with control system 6； The lower parts electromagnetism ring 3-9-1-12-8 be equipped with cold air sucting inlet 3-9-1-12-7, cold air sucting inlet 3-9-1-12-7 funnel-forms, thereon Port diameter is more than lower end bore, and the lower parts cold air sucting inlet 3-9-1-12-7 are equipped with level-one and wind turbine 3-9-1-12-6, cold air is accelerated to inhale Entrance 3-9-1-12-7 accelerates the seamless perforations of both wind turbine 3-9-1-12-6 to connect with level-one；Level-one accelerates wind turbine 3-9-1-12-6 Lower part is equipped with two level and accelerates wind turbine 3-9-1-12-4, level-one that wind turbine 3-9-1-12-6 is accelerated to accelerate wind turbine 3-9-1-12-4 with two level Perforation that the two is seamless connects；Wind turbine 3-9-1-12-6 and two level is accelerated to accelerate to be equipped with cooling outside wind turbine 3-9-1-12-4 in level-one Chuck, cooling jacket one end are connected to wind turbine outlet pipe 3-9-1-12-5, the other end and the wind turbine water inlet pipe 3-9- of cooling jacket 1-12-3 is connected to.

As shown in figure 9, being heretofore described 4 structural schematic diagram of work piece holder.The gear wheel 4-4 is arranged in maintenance Inside case 4-2, gear wheel 4-4 is interior tooth type hollow structure, and interior teeth are located in gear wheel 4-4 internal circumferences, gear wheel 4-4 The interior central gear 4-5 and handgrip gear 4-6, central gear 4-5, handgrip gear 4-6 of being equipped with is outer toothing；The central gear 4-5 is located at the central axes gear wheel 4-4, and handgrip gear 4-6, gear wheel 4-4, central gear are surrounded by central gear 4-5 4-5, handgrip gear 4-6 three engage connection；The handgrip gear 4-6 quantity is three, circumferentially right around central gear 4-5 Claim distribution.

As shown in Figure 10, it is heretofore described lap count 4-7 structural schematic diagrams.Laser Measuring circle positioned at bottom Pop one's head in 4-7-1, and surface further includes secondary light source 4-7-8 and Laser emission receiver 4-7-9, the Laser emission receiver 4- 7-9 is located at Laser Measuring circle probe 4-7-1 bottom centre, direction is aimed downwardly, and Laser emission receiver 4-7-9 is surrounded by auxiliary Light source 4-7-8, secondary light source 4-7-8 are 12, and secondary light source 4-7-8 is LE light sources；The conversion head 4-7-2 is located at Laser Measuring The rotary shaft 4-7-7 on the top of circle probe 4-7-1, conversion head 4-7-2 and top is rotatablely connected, meanwhile, Laser Measuring circle probe 4- 7-1 is fixedly connected with the rotary shaft 4-7-7 on top.

As shown in figure 11, it is heretofore described workpiece handgrip 4-3 structural schematic diagrams.The workpiece slot 4-3-2 arrangements In the tops arm 4-3-1, workpiece slot 4-3-2 is circular groove, and diameter is 8cm~12cm；The banjo traction splint 4- 3-3 quantity is three, and circumference is equally distributed on around workpiece slot 4-3-2, and the ends banjo traction splint 4-3-3 are equipped with anti-skidding protection Pad and workpiece clamp tightness inductor 4-3-4.

The content that following embodiment further illustrates the present invention, as wind turbine water inlet pipe 3-9-1-12-3, it is the present invention Significant components the service life of integral device is increased due to its presence, it is the safety of integral device, even running Play key effect.For this purpose, by it is following be embodiment, further verify wind turbine water inlet pipe 3-9-1- of the present invention 12-3, the physical characteristic higher than other related patents shown.

Embodiment 1

Wind turbine water inlet pipe 3-9-1-12-3 of the present invention is prepared according to the following steps, and is counted in parts by weight：

1st step：In tower reactor is found in stirring, it is added and purifies 339.2 parts of lake water and N- methyl-1s, 1,2,2,3,3,4,4,5, 5,5- ten one 131.5 parts of fluoro -1- pentanes sulfonamide start stirring and found blender in tower reactor, and setting speed is 132rpm starts the steam oil heater in the vertical tower reactor of stirring, so that temperature is risen to 147.2 DEG C, 1- (methoxyl groups are added Methyl) 134.2 parts of -4- methylbenzenes stir evenly, and carry out reaction 124.5 minutes, and 130.4 parts of 4- (methyl mercapto) butyraldehyde is added, lead to Inbound traffics are 123.5m³The helium of/min 124.5 minutes；133.1 parts of rutile is added in tower reactor is found in stirring later, The steam oil heater being again started up in the vertical tower reactor of stirring, makes temperature rise to 164.2 DEG C, keeps the temperature 124.4 minutes, add Enter 136.9 parts of the polymer of 4,4'- (1- methyl ethylidene) bis- [2- (2- acrylic)] phenol and (chloromethyl) ethylene oxide, adjusts The pH value that solution in tower reactor is found in whole stirring is 4.1, keeps the temperature 124.1 minutes；

2nd step：138.7 parts of silver nano-particle separately is taken, ultrasonication 0.130 is small in the case where power is 6.64KW by silver nano-particle Shi Hou；Silver nano-particle is added to another stirring to stand in tower reactor, the polymeric oxygen that mass concentration is 134mg/L is added 1,1,2,3,3,3 changed, 131.1 parts of dispersion silver nano-particles of-hexafluoro -1- propylene, starts the steaming in the vertical tower reactor of stirring Vapour formula oil heater makes solution temperature at 45 DEG C, starts the blender in the vertical tower reactor of stirring, and with 4 × 10²Rpm's Speed stirs, and adjustment pH value is 4.5, insulated and stirred 130 minutes；Stop reaction later and stand 6.64 × 10 minutes, removes impurity； Suspension is added to 133.6 parts of the polymer of formaldehyde and dicyanodiamide and ethylenediamine sulfate, adjustment pH value is formed 1.5 Sediment purification lake water elution, by centrifuge in rotating speed 4.192 × 10³Solid content is obtained under rpm, 2.407 × 10²℃ At a temperature of it is dry, 0.192 × 10 is crossed after grinding³Mesh sieves, spare；

3rd step：Another silver nano-particle after taking alkali formula aphthenic acids zinc salt 133.9 and the processing of the 2nd step, uses glancing incidence after mixing Low-angle gamma-rays diffusing reflection irradiates, and the energy of glancing incidence low-angle gamma-rays diffusing reflection irradiation is 121.2MeV, dosage is 169.2kGy, irradiation time are 133.2 minutes, obtain the alkali formula aphthenic acids zinc salt and silver nano-particle mixture of character change； Alkali formula aphthenic acids zinc salt and silver nano-particle mixture are placed in another stirring to stand in tower reactor, it is vertical tower anti-to start stirring The steam oil heater in device, 132.8 DEG C of set temperature is answered to start the blender in the vertical tower reactor of stirring, rotating speed is 124rpm, pH are adjusted to 4.3, are dehydrated 133.3 minutes, spare；

4th step：The alkali formula aphthenic acids zinc salt and silver nano-particle mixture that the character that 3rd step is obtained changes, it is dense to add to quality [- three base of tri- oxygen triazines -1,3,5 (2H, 4H, 6H) of 2,4,6-] three (cyclohexyl) that the methyl ethyl ketoxime that degree is 134mg/L blocks are different In 122.5 parts of cyanate, the stirring that cocurrent adds to the 1st step is stood in tower reactor, flow acceleration 269mL/min；Startup is stirred Mix vertical tower reactor blender, setting speed 138rpm；Stirring 4 minutes；121.2 parts of 7- methyl octanals are added, are started The steam oil heater in tower reactor is found in stirring, is warming up to 168.4 DEG C, pH is adjusted to 4.4, is passed through helium ventilatory capacity and is 123.118m³/ min, heat preservation stand 158.2 minutes；It is again started up to stir and founds tower reactor blender, rotating speed 133rpm, 130.8 parts of (2E)-formic acid -2- hexen-1-ols ester is added, and pH is made to be adjusted to 4.4, heat preservation stands 157.5 minutes；

5th step：Start the blender in the vertical tower reactor of stirring, setting speed 130rpm starts stirring and stands tower reaction Steam oil heater in device sets stirring and founds temperature in tower reactor as 1.287 × 10²DEG C, polyurethane is added 140.3 parts of polymer reacts 124.2 minutes；The rosolic acid cetyl ester 163.4 that mass concentration is 130mg/L is added later Part, start stirring and found steam oil heater in tower reactor, set temperature in the vertical tower reactor of stirring as 208.4 DEG C, pH is adjusted to 4.1, and pressure 1.3MPa, the reaction time is 0.4 hour；It is depressurized to normal pressure later, is cooled to 124.2 DEG C and goes out Expect into molding press to get to wind turbine water inlet pipe 3-9-1-12-3；

The grain size of the silver nano-particle is 138 μm.

Embodiment 2

Wind turbine water inlet pipe 3-9-1-12-3 of the present invention is prepared according to the following steps, and is counted in parts by weight：

1st step：In tower reactor is found in stirring, it is added and purifies 564.8 parts of lake water and N- methyl-1s, 1,2,2,3,3,4,4,5, 5,5- ten one 173.6 parts of fluoro -1- pentanes sulfonamide start stirring and found blender in tower reactor, and setting speed is 178rpm starts the steam oil heater in the vertical tower reactor of stirring, so that temperature is risen to 148.8 DEG C, 1- (methoxyl groups are added Methyl) 243.1 parts of -4- methylbenzenes stir evenly, and carry out reaction 135.6 minutes, and 147.4 parts of 4- (methyl mercapto) butyraldehyde is added, lead to Inbound traffics are 164.4m³The helium of/min 135.6 minutes；190.3 parts of rutile is added in tower reactor is found in stirring later, The steam oil heater being again started up in the vertical tower reactor of stirring, makes temperature rise to 197.1 DEG C, keeps the temperature 135.4 minutes, add Enter 197.5 parts of the polymer of 4,4'- (1- methyl ethylidene) bis- [2- (2- acrylic)] phenol and (chloromethyl) ethylene oxide, adjusts The pH value that solution in tower reactor is found in whole stirring is 8.3, keeps the temperature 364.1 minutes；

2nd step：Separately take 193.3 parts of silver nano-particle, by silver nano-particle power be 12.08KW under ultrasonication 1.197 After hour；Silver nano-particle is added to another stirring to stand in tower reactor, the polymerization that mass concentration is 364mg/L is added The 1,1,2,3,3,3 of oxidation, 173.6 parts of dispersion silver nano-particles of-hexafluoro -1- propylene, starts stirring and stands in tower reactor Steam oil heater makes solution temperature between 89 DEG C, starts stirring and founds blender in tower reactor, and with 8 × 10²The speed of rpm stirs, and adjustment pH value is 8.8, insulated and stirred 197 minutes；Stop reaction later and stand 12.08 × 10 minutes, Remove impurity；Suspension is added to 173.5 parts of the polymer of formaldehyde and dicyanodiamide and ethylenediamine sulfate, adjustment pH value exists 2.8, sediment purification lake water elution is formed, solid content is obtained at 9.643 × 103rpm of rotating speed by centrifuge, 3.642×10²It is dry at a temperature of DEG C, 1.643 × 103 mesh sieve is crossed after grinding, it is spare；

3rd step：It is another take 156.6 parts of alkali formula aphthenic acids zinc salt and the 2nd step to handle after silver nano-particle, after mixing use plunder into Low-angle gamma-rays diffusing reflection irradiation is penetrated, the energy of glancing incidence low-angle gamma-rays diffusing reflection irradiation is 149.8MeV, dosage is 209.8kGy, irradiation time are 158.8 minutes, obtain the alkali formula aphthenic acids zinc salt and silver nano-particle mixture of character change； Alkali formula aphthenic acids zinc salt and silver nano-particle mixture are placed in another stirring to stand in tower reactor, it is vertical tower anti-to start stirring The steam oil heater in device, 178.4 DEG C of set temperature is answered to start the blender in the vertical tower reactor of stirring, rotating speed is 519rpm, pH are adjusted to 8.3, are dehydrated 147.3 minutes, spare；

4th step：The alkali formula aphthenic acids zinc salt and silver nano-particle mixture that the character that 3rd step is obtained changes, it is dense to add to quality [- three base of tri- oxygen triazines -1,3,5 (2H, 4H, 6H) of 2,4,6-] three (cyclohexyl) that the methyl ethyl ketoxime that degree is 364mg/L blocks are different In 158.8 parts of cyanate, the stirring that cocurrent adds to the 1st step is stood in tower reactor, flow acceleration 997mL/min；Startup is stirred Mix vertical tower reactor blender, setting speed 178rpm；Stirring 8 minutes；164.8 parts of 7- methyl octanals are added, are started The steam oil heater in tower reactor is found in stirring, is warming up to 205.8 DEG C, pH is adjusted to 8.8, is passed through helium ventilatory capacity and is 164.273m3/min heat preservation stands 188.8 minutes；It is again started up to stir and founds tower reactor blender, rotating speed 178rpm, 175.4 parts of (2E)-formic acid -2- hexen-1-ols ester is added, and pH is made to be adjusted to 8.8, heat preservation stands 197.6 minutes；

5th step：Start the blender in the vertical tower reactor of stirring, setting speed 197rpm starts stirring and stands tower reaction Steam oil heater in device sets stirring and founds temperature in tower reactor as 2.32 × 10²DEG C, the poly- of polyurethane is added 184.3 parts of object is closed, is reacted 135.1 minutes；217.8 parts of the rosolic acid cetyl ester that mass concentration is 397mg/L is added later, Start stirring and found steam oil heater in tower reactor, set the temperature in the vertical tower reactor of stirring as 264.4 DEG C, PH is adjusted to 8.1, and pressure 1.31MPa, the reaction time is 0.9 hour；It is depressurized to normal pressure later, is cooled to 135.1 DEG C of dischargings Enter molding press to get to wind turbine water inlet pipe 3-9-1-12-3；

The grain size of the silver nano-particle is 148 μm.

Embodiment 3

Wind turbine water inlet pipe 3-9-1-12-3 of the present invention is prepared according to the following steps, and is counted in parts by weight：

1st step：In tower reactor is found in stirring, it is added and purifies 339.9 parts of lake water and N- methyl-1s, 1,2,2,3,3,4,4,5, 5,5- ten one 131.9 parts of fluoro -1- pentanes sulfonamide start stirring and found blender in tower reactor, and setting speed is 132rpm starts the steam oil heater in the vertical tower reactor of stirring, so that temperature is risen to 147.9 DEG C, 1- (methoxyl groups are added Methyl) 134.9 parts of -4- methylbenzenes stir evenly, and carry out reaction 124.9 minutes, and 130.9 parts of 4- (methyl mercapto) butyraldehyde is added, lead to The helium that inbound traffics are 123.9m3/min 124.9 minutes；133.9 parts of rutile is added in tower reactor is found in stirring later, The steam oil heater being again started up in the vertical tower reactor of stirring, makes temperature rise to 164.9 DEG C, keeps the temperature 124.9 minutes, add Enter 136.9 parts of the polymer of 4,4'- (1- methyl ethylidene) bis- [2- (2- acrylic)] phenol and (chloromethyl) ethylene oxide, adjusts The pH value that solution in tower reactor is found in whole stirring is 4.9, keeps the temperature 124.9 minutes；

2nd step：Separately take 138.9 parts of silver nano-particle, by silver nano-particle power be 6.649KW under ultrasonication 0.1309 After hour；Silver nano-particle is added to another stirring to stand in tower reactor, it is the poly- of 134.9mg/L that mass concentration, which is added, The 1,1,2,3,3,3 of oxidation is closed, 131.9 parts of dispersion silver nano-particles of-hexafluoro -1- propylene start stirring and stand in tower reactor Steam oil heater, make solution temperature at 45.9 DEG C, start stirring and found blender in tower reactor, and with 4.9 × 10²The speed of rpm stirs, and adjustment pH value is 4.9, insulated and stirred 130.9 minutes；Stop reaction later and stands 6.64 × 10 points Clock removes impurity；Suspension is added to 133.9 parts of the polymer of formaldehyde and dicyanodiamide and ethylenediamine sulfate, adjusts pH Value forms sediment purification lake water elution, solid content is obtained at 4.192 × 103rpm of rotating speed by centrifuge 1.9, 2.407×10²It is dry at a temperature of DEG C, 0.192 × 103 mesh sieve is crossed after grinding, it is spare；

3rd step：Another silver nano-particle after taking alkali formula aphthenic acids zinc salt 133.9 and the processing of the 2nd step, uses glancing incidence after mixing Low-angle gamma-rays diffusing reflection irradiates, and the energy of glancing incidence low-angle gamma-rays diffusing reflection irradiation is 121.9MeV, dosage is 169.9kGy, irradiation time are 133.9 minutes, obtain the alkali formula aphthenic acids zinc salt and silver nano-particle mixture of character change； Alkali formula aphthenic acids zinc salt and silver nano-particle mixture are placed in another stirring to stand in tower reactor, it is vertical tower anti-to start stirring The steam oil heater in device, 132.9 DEG C of set temperature is answered to start the blender in the vertical tower reactor of stirring, rotating speed is 124rpm, pH are adjusted to 4.9, are dehydrated 133.9 minutes, spare；

4th step：The alkali formula aphthenic acids zinc salt and silver nano-particle mixture that the character that 3rd step is obtained changes, it is dense to add to quality [- three base of tri- oxygen triazines -1,3,5 (2H, 4H, 6H) of 2,4,6-] three (cyclohexyl) that the methyl ethyl ketoxime that degree is 134.9mg/L blocks In 122.9 parts of isocyanates, the stirring that cocurrent adds to the 1st step is stood in tower reactor, flow acceleration 269.9mL/min；It opens Tower reactor blender, setting speed 138rpm are found in dynamic stirring；Stirring 4.9 minutes；Add 7- methyl octanals 121.9 Part, start the steam oil heater in the vertical tower reactor of stirring, is warming up to 168.9 DEG C, pH is adjusted to 4.9, is passed through helium Ventilatory capacity is 123.9m3/min, and heat preservation stands 158.9 minutes；It is again started up stirring and founds tower reactor blender, rotating speed is 130.9 parts of (2E)-formic acid -2- hexen-1-ols ester is added in 133rpm, and pH is made to be adjusted to 4.9, and heat preservation stands 157.9 points Clock；

5th step：Start the blender in the vertical tower reactor of stirring, setting speed 130rpm starts stirring and stands tower reaction Steam oil heater in device sets stirring and founds temperature in tower reactor as 1.287 × 10²DEG C, polyurethane is added 140.9 parts of polymer reacts 124.9 minutes；The rosolic acid cetyl ester 163.4 that mass concentration is 130mg/L is added later Part, start stirring and found steam oil heater in tower reactor, set temperature in the vertical tower reactor of stirring as 208.9 DEG C, pH is adjusted to 4.9, and pressure 1.3MPa, the reaction time is 0.41 hour；It is depressurized to normal pressure later, is cooled to 124.9 DEG C and goes out Expect into molding press to get to wind turbine water inlet pipe 3-9-1-12-3；

The grain size of the silver nano-particle is 138 μm.

Reference examples

Reference examples use the component same as the application wind turbine water inlet pipe 3-9-1-12-3 of certain commercially available brand, are tested for the property examination It tests.

Embodiment 4

The wind turbine water inlet pipe 3-9-1-12-3 and reference examples of the Examples 1 to 3 same component obtained are tested for the property examination It tests, to mechanical strength enhancing rate, compression strength enhancing rate, anti-yield strength enhancing rate, wear rate enhancing rate etc. after test Parameter is analyzed.Data analysis is as shown in table 1.

As seen from Table 1, wind turbine water inlet pipe 3-9-1-12-3 of the present invention, mechanical strength enhancing rate, compression strength Enhancing rate, anti-yield strength enhancing rate, wear rate enhancing rate are above the product of prior art production.

In addition, as shown in figure 12, wind turbine water inlet pipe 3-9-1-12-3 of the present invention is carried out with reference examples, with Usage time changes test data statistics.Find out in figure, Examples 1 to 3 is substantially better than existing in test data technical indicator There is the product that technology produces.

Claims (10)

1. a kind of cold air accelerator in sludge dewatering negative pressure High shear device, including：Shock-absorbing foot pad (1), fixed frame Frame (2), pushing mechanism (3), work piece holder (4), support platform (5), control system (6), rolling cutter (7)；It is characterized in that, The fixed frame (2) is stainless steel rectangular structure, and thickness is between 3cm~4cm；Shock-absorbing foot pad (1) quantity is four It is a, it is respectively and fixedly installed to fixed frame (2) bottom four corners；The support platform (5) is rectangle galvanized sheet, support platform (5) It is fixedly mounted on above fixed frame (2)；The pushing mechanism (3) is arranged in support platform (5) side；The work piece holder (4) it is arranged in support platform (5) other side；The control system (6) is fixedly mounted on fixed frame (2)；

The rolling cutter (7) is located on the left of pushing mechanism (3), the two connection；

The pushing mechanism (3), which is equipped with, pushes disk brake apparatus (3-9)；

Disk brake apparatus (3-9) is pushed to be equipped with brake cooling system (3-9-1)；

The top brake cooling system (3-9-1) is equipped with cold air accelerating chamber (3-9-1-12)；

The cold air accelerating chamber (3-9-1-12) includes：Cold air outlet (3-9-1-12-1), cold air accelerate room housing (3-9-1- 12-2), wind turbine water inlet pipe (3-9-1-12-3), two level acceleration wind turbine (3-9-1-12-4), wind turbine outlet pipe (3-9-1-12-5), Level-one accelerates wind turbine (3-9-1-12-6), cold air sucting inlet (3-9-1-12-7), electromagnetism ring (3-9-1-12-8), controls connecting rod (3-9-1-12-9), cold air import (3-9-1-12-10)；

Accelerate to be equipped with cold air import (3-9-1-12-10) at the top of room housing (3-9-1-12-2) in cold air, in cold air accelerating chamber shell The bottom body (3-9-1-12-2) is equipped with cold air outlet (3-9-1-12-1), cold air import (3-9-1-12-10) and cold air outlet (3- 9-1-12-1) up and down；It is equipped with electromagnetism ring (3-9-1-12-8), electromagnetism ring (3- in the lower part cold air import (3-9-1-12-10) 9-1-12-8) it is connect with control system (6) by conducting wire；It is equipped with cold air sucting inlet (3- in the lower part electromagnetism ring (3-9-1-12-8) 9-1-12-7), cold air sucting inlet (3-9-1-12-7) funnel-form, the upper end bore are more than lower end bore, cold air sucting inlet (3-9- 1-12-7) lower part is equipped with level-one acceleration wind turbine (3-9-1-12-6), and cold air sucting inlet (3-9-1-12-7) accelerates wind turbine with level-one Perforation connection that both (3-9-1-12-6) is seamless；Level-one accelerates the lower part wind turbine (3-9-1-12-6) to be equipped with two level and accelerates wind turbine (3- 9-1-12-4), level-one accelerates wind turbine (3-9-1-12-6) to accelerate the seamless perforation of both wind turbines (3-9-1-12-4) to connect with two level； Wind turbine (3-9-1-12-6) and two level is accelerated to accelerate to be equipped with cooling jacket, cooling jacket outside wind turbine (3-9-1-12-4) in level-one One end is connected to wind turbine outlet pipe (3-9-1-12-5), and the other end and the wind turbine water inlet pipe (3-9-1-12-3) of cooling jacket connect It is logical；Accelerate to be equipped with controls connecting rod (3-9-1-12-9), controls connecting rod (3-9-1- outside room housing (3-9-1-12-2) in cold air 12-9) airlock for accelerating wind turbine (3-9-1-12-6), two level to accelerate wind turbine (3-9-1-12-4) respectively at level-one controls connection； Cold air outlet (3-9-1-12-1) bell shape, thereon port and two level acceleration wind turbine (3-9-1-12-4) seamless perforation The bore of connection, lower port accelerates room housing (3-9-1-12-2) bore equal with cold air, and seamless welding；

Cold air enters cold air accelerating chamber (3-9-1-12) from cold air import (3-9-1-12-10), by way of electromagnetism ring (3-9-1-12- 8) it is magnetized, in the case where level-one accelerates wind turbine (3-9-1-12-6), two level to accelerate the acceleration of wind turbine (3-9-1-12-4), from cold Gas exports (3-9-1-12-1) and sprays；Meanwhile cooling water enters cooling jacket from wind turbine water inlet pipe (3-9-1-12-3), is level-one Accelerate wind turbine (3-9-1-12-6), two level that wind turbine (3-9-1-12-4) is accelerated to cool down, and from wind turbine outlet pipe (3-9-1- 12-5) flow out.

2. a kind of cold air accelerator in sludge dewatering negative pressure High shear device according to claim 1, special Sign is that the pushing mechanism (3) includes：Slideway fixed block (3-1), slideway (3-2), sliding block (3-3), speed regulating motor (3-4), Fuel tank (3-5), hydraulic cylinder (3-6) push disk (3-7), slide motor (3-8) to push disk brake apparatus (3-9), speed regulating motor Transmission shaft (3-10)；Wherein, the slideway (3-2) is fixedly connected by slideway fixed block (3-1) with support platform (5)；It is described The cross section slideway (3-2) is in " Ω " shape, and slideway (3-2) quantity is 2；The sliding block (3-3) connects with slideway (3-2) sliding It connects, the end sliding block (3-3) is provided with slide motor (3-8), and slide motor (3-8) drives sliding block (3-3) sliding on slideway (3-2) It is dynamic；The speed regulating motor (3-4) is variable-frequency motor, and speed regulating motor (3-4) pedestal is welded and fixed with sliding block (3-3)；The speed governing Motor transmission shaft one end (3-10) is connect with speed regulating motor (3-4), and the other end passes through fuel tank (3-5), pushes disk brake apparatus (3- 9), hydraulic cylinder (3-6) is fixedly connected with disk (3-7) is pushed, and speed regulating motor (3-4), which drives, pushes disk (3-7) to rotate；The fuel tank (3-5) is connected to the one end hydraulic cylinder (3-6) conduit；Hydraulic cylinder (3-6) other end pushes disk (3-7) to connect with detachable； The promotion disk brake apparatus (3-9), which is located at, pushes disk (3-7) and hydraulic cylinder (3-6) between the two；Speed regulating motor (the 3- 4), hydraulic cylinder (3-6), promotion disk (3-7) central axis in the same horizontal line, push disk (3-7) to connect with rolling cutter (7) It connects, pushes disk (3-7) that rolling cutter (7) is driven to rotate；

The speed regulating motor (3-4), hydraulic cylinder (3-6) are connected by conducting wire and control system (6) control respectively；

The slide motor (3-8) is connected by conducting wire and control system (6) control.

3. a kind of cold air accelerator in sludge dewatering negative pressure High shear device according to claim 2, special Sign is that the rolling cutter (7) includes：Driven wheel (7-1), transformer (7-2), cutting edge (7-3), back-up roller bearing (7- 4), heating tube (7-5), cutting edge nozzle (7-6), water inlet pipe (7-7) are intake port (7-8), transmission shaft (7-9)；Positioned at one end Driven wheel (7-1), connect with external cutter motor, meanwhile, driven wheel (7-1) is fixedly connected with transmission shaft (7-9)； Back-up roller bearing (7-4) is equipped on the inside of driven wheel (7-1), back-up roller bearing (7-4) quantity is 2, is located at transmission The both ends of axis (7-9)；Transmission shaft (7-9) hollow structure, is internally provided with transformer (7-2), heating tube (7-5), water inlet pipe (7-7)；Water inlet pipe (7-7) is parallel to transmission shaft (7-9), and the quantity of water inlet pipe (7-7) is 3, water inlet pipe (7-7) and water inlet end Mouth (7-8) connection, water inlet port (7-8) are connected to external pump；Water inlet pipe (7-7) periphery is equipped with heating tube (7-5), heating tube (7-5) helical structure, heating tube one end (7-5) are connected to by conducting wire with transformer (7-2), and the other end of transformer (7-2) is logical It crosses conducting wire to be electrically connected with external city, heating tube (7-5) is implemented to heat to water inlet pipe (7-7), and transformer (7-2) is to heating temperature reality Apply adjusting；Cutting edge (7-3) is equipped with outside transmission shaft (7-9), cutting edge (7-3) quantity is 4,4 cutting edges (7-3) etc. Angle, mode substantially symmetrical about its central axis are fixed on transmission shaft (7-9)；It is equipped with cutting edge nozzle (7-6) in the root cutting edge (7-3), Cutting edge nozzle (7-6) open at one end designs and is directed toward cutting edge (7-3) knife face, cutting edge nozzle (7-6) other end and water inlet Manage (7-7) connection；

Driven wheel (7-1) drives cutting edge (7-3) to rotate by transmission shaft (7-9), and cutting edge (7-3) equidistantly cuts material implementation It cuts；Meanwhile cutting edge nozzle (7-6) is implemented to clean to cutting edge (7-3) knife face.

4. a kind of cold air accelerator in sludge dewatering negative pressure High shear device according to claim 3, special Sign is that slideway (3-2) is equipped with cooling device, and cooling device includes：By coolant liquid entrance (3-2-1), heat-exchange tube (3-2- 2), heat-exchanging chamber (3-2-3), partition board (3-2-4), buffered room (3-2-5), refrigerant inlet (3-2-6) are exported by coolant liquid (3-2-7), medicament mixing device (3-2-8), refrigerant exit (3-2-9)；

It is connected to heat-exchanging chamber (3-2-3) by coolant liquid entrance (3-2-1) positioned at side, and by coolant liquid entrance (3-2-1) Positioned at the lower part heat-exchanging chamber (3-2-3), low level；It is described by coolant liquid outlet (3-2-7) be located at the top heat-exchanging chamber (3-2-3), A high position, and be connected to heat-exchanging chamber (3-2-3) by coolant liquid outlet (3-2-7)；The heat-exchange tube (3-2-2) is located at heat exchange In the middle part of room (3-2-3), the quantity of heat-exchange tube (3-2-2) hollow structure, heat-exchange tube (3-2-2) is 20, more heat exchanges Manage (3-2-2) vertical equidistant arrangement；The both ends heat-exchange tube (3-2-2) are respectively equipped with buffered room (3-2-5), heat-exchange tube The both ends (3-2-2) are connected to the buffered room (3-2-5) for being located at its upper and lower ends respectively；The heat-exchanging chamber (3-2-3) is logical It crosses partition board (3-2-4) and the buffered room (3-2-5) of upper and lower ends separates；Superposed buffered room (3-2-5), Top is equipped with refrigerant inlet (3-2-6), and the buffered room (3-2-5) on top is connected to refrigerant inlet (3-2-6), is located at lower part Its bottom buffered room (3-2-5) be equipped with refrigerant exit (3-2-9), the buffered room (3-2-5) of lower part and bottom Refrigerant exit (3-2-9) is connected to；The medicament mixing device (3-2-8) is connected to heat-exchanging chamber (3-2-3).

5. a kind of cold air accelerator in sludge dewatering negative pressure High shear device according to claim 4, special Sign is that the medicament mixing device (3-2-8) is L-type pipe structure, both ends perforation, and medicament mixing device (3-2-8) includes：Medicine Agent import (3-2-8-1), diffusant jet pipe (3-2-8-2), diffusant enter pipe (3-2-8-3), buffer subsystem (3-2-8-4), agitation Ball (3-2-8-5) stablizes net (3-2-8-6), and diffusion horn mouth (3-2-8-7), decentralized network (3-2-8-8), diluent enters pipe (3-2-8-9), agent outlet (3-2-8-10)；

Medicament inlet (3-2-8-1) positioned at one end, medicament inlet (3-2-8-1) right side enter pipe (3-2-8- equipped with diluent 9), diluent enters pipe one end (3-2-8-9) and is connected to external diluent bottle, and diluent enters pipe (3-2-8-9) other end To be open, and it is internal to be inserted into diffusion horn mouth (3-2-8-7)；Decentralized network (3- is equipped in the middle part of diffusion horn mouth (3-2-8-7) 2-8-8), it is holey, vertical display；It is flared structure to spread horn mouth (3-2-8-7), and heavy caliber end direction is right Side, the diameter ratio for spreading horn mouth (3-2-8-7) heavy caliber end and small-caliber end is 3:1；The diffusant jet pipe (3-2-8-2) It is hollow ring pipe structure on the right side of diffusion horn mouth (3-2-8-7), the ring pipe of diffusant jet pipe (3-2-8-2) is right Side surface is equipped with a large amount of through-holes, and diffusant jet pipe one end (3-2-8-2) enters pipe (3-2-8-3) with diffusant and is connected to；The buffering Net (3-2-8-4) is located at diffusant and enters on the right side of pipe (3-2-8-3), and buffer subsystem (3-2-8-4) is holey, vertical display；Institute Agitation ball (3-2-8-5) to be stated to be located on the right side of buffer subsystem (3-2-8-4), agitation ball (3-2-8-5) is macromolecule thin-walled hollow structure, The density that ball (3-2-8-5) material density is less than water is stirred, agitation ball (3-2-8-5) quantity is 50~100, single to stir Ball (3-2-8-5) quality is less than 10 grams, and multiple agitation balls (3-2-8-5) are limited at buffer subsystem (3-2-8-4) and stablize net (3- Between 2-8-6), the agitation ball (3-2-8-5) is scattered distribution, and the mutual gap of agitation ball (3-2-8-5) is more than 5cm；For the stable net (3-2-8-6) on the right side of agitation ball (3-2-8-5), stable net (3-2-8-6) is holey, vertically It puts；

Medicament enters from medicament inlet (3-2-8-1), and the diluent that pipe (3-2-8-9) ejection is entered with diluent meets, and is dividing Under the action of dissipating net (3-2-8-8), diffusion horn mouth (3-2-8-7), diluent is further disperseed and is mixed with medicament；

Diffusant enters pipe (3-2-8-3) by diffusant and is sprayed from diffusant jet pipe (3-2-8-2), and buffer subsystem (3-2-8-4) is right The diffusant of ejection implements buffering, and enters together with medicament, diluent and be located at buffer subsystem (3-2-8-4) and stablize net (3-2- Agitation ball (3-2-8-5) action space between 8-6), in the case where stirring ball (3-2-8-5) agitaion, diffusant, diluent, Medicament is sufficiently mixed, and mixture is discharged from agent outlet (3-2-8-10).

6. a kind of cold air accelerator in sludge dewatering negative pressure High shear device according to claim 5, special Sign is that the promotion disk brake apparatus (3-9) includes：Brake cooling system (3-9-1), haulage gear (3-9-2), braking is led Straw line (3-9-3), brake caliper (3-9-4), radiator fan (3-9-5), friction plate (3-9-6)；

Speed regulating motor transmission shaft (3-10) on central axes is surrounded by friction plate (3-9-6), friction plate (3-9-6) Quantity is 4, and 4 friction plates (3-9-6) wrap up speed regulating motor transmission shaft (3-10) wherein, outside friction plate (3-9-6) It encloses and is equipped with brake caliper (3-9-4), brake caliper (3-9-4) is cyclic annular, is divided into pintongs, and friction plate (3-9-6) is fixed on braking clamp The inside of disk (3-9-4)；Radiator fan (3-9-5) is equipped on the left of brake caliper (3-9-4), radiator fan (3-9-5) is braking Chuck (3-9-4) cools down；Brake caliper (3-9-4) periphery is equipped with braking hauling rope (3-9-3), brakes hauling rope (3-9-3) ring Around brake caliper (3-9-4) surrounding, and the two is hinged；The other end and haulage gear (3-9-2) for braking hauling rope (3-9-3) connect It connects；It is equipped with brake cooling system (3-9-1) on the top brake caliper (3-9-4), the two is connected by conduit；

Haulage gear (3-9-2) is tightened brake caliper (3-9-4) by braking hauling rope (3-9-3), promotes friction plate (3-9- 6) generation friction brake force is closely encircled to speed regulating motor transmission shaft (3-10), the heat that friction generates passes through radiator fan (3-9-5), brake cooling system (3-9-1) take away heat.

7. a kind of cold air accelerator in sludge dewatering negative pressure High shear device according to claim 6, special Sign is that the brake cooling system (3-9-1) includes：Butterfly plate (3-9-1-1), butterfly ventilating hole plate (3-9-1-2), cool room Paddle (3-9-1-3), cool room cold air import (3-9-1-4), cool room agitating shaft (3-9-1-5), lower open mouth wing plate (3-9- 1-6), barrier board (3-9-1-7), oscillating deck (3-9-1-8), cool room gas outlet (3-9-1-9), oily atomizer (3-9-1- 10), oil collection box (3-9-1-11), cold air accelerating chamber (3-9-1-12)；

Cool room cold air import (3-9-1-4) positioned at top is passed through up and down with the cool room gas outlet (3-9-1-9) positioned at bottom It is logical；It is equipped with cool room agitating shaft (3-9-1-5), cool room agitating shaft (3- at cool room cold air import (3-9-1-4) vertical pivot center 9-1-5) one end is connect with external refrigeration room stirring motor, and the other end is fixedly connected with cool room paddle (3-9-1-3)； The lower part cool room paddle (3-9-1-3) be equipped with oscillating deck (3-9-1-8), oscillating deck (3-9-1-8) thin-slab structure, individually Oscillating deck (3-9-1-8) is placed vertically, and oscillating deck (3-9-1-8) quantity is 20, and 20 oscillating decks (3-9-1-8) are divided into two Group is vertically arranged, and with group oscillating deck (3-9-1-8), distance is 10cm between each other, with soft rope between group oscillating deck (3-9-1-8) Chain concatenates, and is fixed at the top of brake cooling system (3-9-1), with group oscillating deck (3-9-1-8) vacantly in brake cooling system At the central axes (3-9-1), oscillating deck (3-9-1-8) swings with air-flow；Butterfly plate is equipped on the right side of oscillating deck (3-9-1-8) (3-9-1-1), butterfly plate (3-9-1-1) thin-slab structure, single butterfly plate (3-9-1-1) are placed vertically, butterfly plate (3-9-1-1) Quantity is 20, and 20 butterfly plates (3-9-1-1) are vertically arranged；Butterfly plate (3-9-1-1) is set there are two arc side wing, two Arc side wing central symmetry, two arc side wings are connected by butterfly ventilating hole plate (3-9-1-2), butterfly ventilating hole plate (3-9- 1-2) air-flow is promoted to form turbulent flow in its both sides；Barrier board (3-9-1-7), barrier board are equipped on the left of oscillating deck (3-9-1-8) (3-9-1-7) is placed vertically, and barrier board (3-9-1-7) is internally provided with a large amount of horizontal grates, and barrier board (3-9-1-7) left and right is logical Thoroughly；Lower open mouth wing plate (3-9-1-6) is equipped on the left of the barrier board (3-9-1-7), between the two away from for 10cm, lower open mouth wing plate (3- 9-1-6) it is vertically arranged；

Lower open mouth wing plate (3-9-1-6) is set there are two side wing is faced directly, and two are faced directly side wing central symmetry, and two are faced directly flank Open design between plate, two face side wing directly between hard cable wire be fixedly connected；

It is equipped with oily atomizer (3-9-1-10) in the side brake cooling system (3-9-1)；At cool room gas outlet (3-9-1-9) Lower part is equipped with oil collection box (3-9-1-11), is equipped with certain distance between the two；

It is equipped with cold air accelerating chamber (3-9-1-12) on the top the import of cool room cold air (3-9-1-4)；

Cold air enters from cool room cold air import (3-9-1-4), and oscillating deck (3-9-1-8) is driven to swing, meanwhile, it is sprayed from mist of oilization Head (3-9-1-10) spray deep fat, butterfly plate (3-9-1-1), butterfly ventilating hole plate (3-9-1-2), barrier board (3-9-1-7), Oscillating deck (3-9-1-8) forms oil film, and heat exchange is carried out with the cold air that cool room cold air import (3-9-1-4) generates, cooling Oil afterwards converges in oil collection box (3-9-1-11).

8. a kind of cold air accelerator in sludge dewatering negative pressure High shear device according to claim 7, special Sign is that the work piece holder (4) includes：Electric rotating machine (4-1), service chamber (4-2), workpiece handgrip (4-3), gear wheel (4- 4), central gear (4-5), handgrip gear (4-6), lap count (4-7)；Wherein, the gear wheel (4-4) is arranged in maintenance Case (4-2) is internal, and gear wheel (4-4) is interior tooth type hollow structure, and interior teeth are located in gear wheel (4-4) internal circumference, greatly Central gear (4-5) and handgrip gear (4-6) are equipped in gear (4-4), central gear (4-5), handgrip gear (4-6) are external tooth Structure；The central gear (4-5) is located at the central axes gear wheel (4-4), and handgrip gear is surrounded by central gear (4-5) (4-6), gear wheel (4-4), central gear (4-5), handgrip gear (4-6) three engage connection；Handgrip gear (4-6) number Amount is three, circumferentially symmetrical around central gear (4-5)；The electric rotating machine (4-1) is fixedly mounted on service chamber (4- 2) side, electric rotating machine (4-1) are drivingly connected with central gear (4-5)；The workpiece handgrip (4-3) is arranged in service chamber (4- 2) other side, workpiece handgrip one end (4-3) are fixedly connected with handgrip gear (4-6)；The lap count (4-7) is fixedly connected On electric rotating machine (4-1) turntable；

The electric rotating machine (4-1), lap count (4-7) are connected by conducting wire and control system (6) control respectively；

Electric rotating machine (4-1) drives central gear (4-5) to rotate, and then drives three, periphery handgrip gear (4-6) along canine tooth Wheel (4-4) interior tooth does revolution motion, while three handgrip gears (4-6) also do rotation movement, and handgrip gear (4-6) passes through workpiece Handgrip (4-3) drives workpiece revolution and rotation.

9. a kind of cold air accelerator in sludge dewatering negative pressure High shear device according to claim 8, special Sign is that the lap count (4-7) includes：Laser Measuring circle is popped one's head in (4-7-1), conversion head (4-7-2), deboost axle (4-7- 3), temperature sensor (4-7-4), gearbox (4-7-5), velocity sensor (4-7-6), rotary shaft (4-7-7), secondary light source (4-7-8), Laser emission receiver (4-7-9), electric rotating machine (4-7-10), spare Laser Measuring circle pop one's head in (4-7-11)；It is located at The Laser Measuring circle probe (4-7-1) of bottom, surface further includes secondary light source (4-7-8) and Laser emission receiver (4-7-9), The Laser emission receiver (4-7-9) is located at Laser Measuring circle probe (4-7-1) bottom centre, direction is aimed downwardly, laser hair It penetrates receiver (4-7-9) and is surrounded by secondary light source (4-7-8), secondary light source (4-7-8) is 12, secondary light source (4-7-8) For LE light sources；The conversion head (4-7-2) is located at the top of Laser Measuring circle probe (4-7-1), conversion head (4-7-2) and top Rotary shaft (4-7-7) is rotatablely connected, meanwhile, Laser Measuring circle probe (4-7-1) is fixedly connected with the rotary shaft (4-7-7) on top； Spare Laser Measuring circle is equipped in conversion head (4-7-2) horizontal direction to pop one's head in (4-7-11), quantity is 4, spare Laser Measuring circle Popping one's head in, (4-7-11) is identical as Laser Measuring circle probe (4-7-1) structure, and Laser Measuring circle is popped one's head in (4-7-1) and spare Laser Measuring circle is visited Head (4-7-11) is Demountable；Rotary shaft (4-7-7) top is equipped with gearbox (4-7-5), gearbox (4-7-5) It is internally provided with deboost axle (4-7-3), deboost axle (4-7-3) engages connection with rotary shaft (4-7-7) gear；Gearbox (4-7-5) Top is equipped with electric rotating machine (4-7-10), and electric rotating machine (4-7-10) engages connection with deboost axle (4-7-3) gear；Gearbox The bottom (4-7-5) is equipped with temperature sensor (4-7-4), velocity sensor (4-7-6)；

Electric rotating machine (4-7-10) drives Laser Measuring circle probe (4-7-1) to turn by deboost axle (4-7-3), rotary shaft (4-7-7) It is dynamic, to exchange the operating angle of Laser Measuring circle probe (4-7-1)；At the same time, the temperature for being located at the bottom gearbox (4-7-5) passes Sensor (4-7-4), velocity sensor (4-7-6) are in real time monitored the object state on workbench (4).

10. a kind of cold air accelerator in sludge dewatering negative pressure High shear device according to claim 9, special Sign is that the workpiece handgrip (4-3) includes：Arm (4-3-1), workpiece slot (4-3-2), banjo traction splint (4-3-3), workpiece Clamping degree inductor (4-3-4)；Wherein, the workpiece slot (4-3-2) is arranged in the top arm (4-3-1), workpiece slot (4-3-2) For circular groove, diameter is 8cm~12cm；Banjo traction splint (4-3-3) quantity is three, and circumference is equally spaced Around workpiece slot (4-3-2), the end banjo traction splint (4-3-3) is equipped with antiskid protection pad and workpiece clamp tightness inductor (4-3-4)；

Banjo traction splint (4-3-3) driving motor, workpiece clamp tightness inductor (4-3-4) pass through conducting wire and control system respectively (6) control connection；

Timer is provided in the control system (6), the timer connects with speed regulating motor (3-4) actuating coil polygon control survey It connects；The wind turbine water inlet pipe (3-9-1-12-3) is molded by high molecular material pressing mold, the group of wind turbine water inlet pipe (3-9-1-12-3) It is as follows at ingredient：

339.2~564.8 parts of lake water of meter purification in parts by weight, N- methyl-1s, 1,2,2,3,3,4,4,5,5,5- ten one fluoro- 131.5~173.6 parts of 1- pentanes sulfonamide, 134.2~243.1 parts of 1- (methoxy) -4- methylbenzenes, 4- (methyl mercapto) fourth 130.4~147.4 parts of aldehyde, 133.1~190.3 parts of rutile, bis- [2- (2- the acrylic)] phenol of 4,4'- (1- methyl ethylidene) With 136.9~197.5 parts of the polymer of (chloromethyl) ethylene oxide, 138.7~193.3 parts of silver nano-particle, polymerization oxidation 1,1,2,3,3,3,131.1~173.6 parts of-hexafluoro -1- propylene, the polymer of formaldehyde and dicyanodiamide and ethylenediamine sulfate 133.6~173.5 parts, 133.9~156.6 parts of alkali formula aphthenic acids zinc salt, methyl ethyl ketoxime sealing end [2,4,6- tri- oxygen triazine -1, 3,5 (2H, 4H, 6H)-three base] three 122.5~158.8 parts of (cyclohexyl) isocyanates, 121.2~164.8 parts of 7- methyl octanals, 130.8~175.4 parts of (2E)-formic acid -2- hexen-1-ols ester, 140.3~184.3 parts of the polymer of polyurethane, mass concentration are 163.4~217.8 parts of the rosolic acid cetyl ester of 130mg/L~397mg/L；

The manufacturing process of wind turbine water inlet pipe (3-9-1-12-3), comprises the steps of：

1st step：In tower reactor is found in stirring, it is added and purifies lake water and N- methyl-1s, 1,2,2,3,3,4,4,5,5,5- ten One fluoro -1- pentane sulfonamide starts the blender in the vertical tower reactor of stirring, and setting speed is 132rpm~178rpm, Start the steam oil heater in the vertical tower reactor of stirring, so that temperature is risen to 147.2 DEG C~148.8 DEG C, 1- (methoxies are added Ylmethyl) -4- methylbenzenes stir evenly, and carry out reaction 124.5~135.6 minutes, and 4- (methyl mercapto) butyraldehyde is added, is passed through flow For 123.5m³/ min~164.4m³The helium of/min 124.5~135.6 minutes；It is added in tower reactor is found in stirring later Rutile, the steam oil heater being again started up in the vertical tower reactor of stirring, makes temperature rise to 164.2 DEG C~197.1 DEG C, 4,4'- (1- methyl ethylidene) bis- [2- (2- acrylic)] phenol and (chloromethyl) ring is added in heat preservation 124.4~135.4 minutes The polymer of oxidative ethane, the pH value that solution in tower reactor is found in adjustment stirring are 4.1~8.3, keep the temperature 124.1~364.1 points Clock；

2nd step：Separately take silver nano-particle, by silver nano-particle power be 6.64KW~12.08KW under ultrasonication 0.130 After~1.197 hours；Silver nano-particle is added to another stirring to stand in tower reactor, addition mass concentration is 134mg/ The 1 of the polymerization oxidation of L~364mg/L, 1,2,3,3,3,-hexafluoro -1- propylene disperses silver nano-particle, and it is vertical tower anti-to start stirring The steam oil heater in device is answered, makes solution temperature between 45 DEG C~89 DEG C, starts stirring and stands stirring in tower reactor Machine is mixed, and with 4 × 10²Rpm~8 × 10²The speed of rpm stirs, and adjusts pH value between 4.5~8.8, and insulated and stirred 130~ 197 minutes；Stop reaction later and stand 6.64 × 10~12.08 × 10 minutes, removes impurity；Formaldehyde and two is added in suspension The polymer of cyano diamides and ethylenediamine sulfate, adjustment pH value form sediment and are washed with purification lake water between 1.5~2.8 It is de-, by centrifuge in rotating speed 4.192 × 10³Rpm~9.643 × 10³Solid content is obtained under rpm, 2.407 × 10²DEG C~ 3.642×10²It is dry at a temperature of DEG C, 0.192 × 10 is crossed after grinding³~1.643 × 10³Mesh sieves, spare；

3rd step：Another silver nano-particle after taking alkali formula aphthenic acids zinc salt and the processing of the 2nd step, uses the small angle of glancing incidence after mixing Gamma-rays diffusing reflection irradiation is spent, the energy of glancing incidence low-angle gamma-rays diffusing reflection irradiation is 121.2MeV~149.8MeV, agent Amount is 169.2kGy~209.8kGy, irradiation time is 133.2~158.8 minutes, obtains the alkali formula zinc naphthenate of character change Salt and silver nano-particle mixture；Alkali formula aphthenic acids zinc salt and silver nano-particle mixture are placed in another stirring and stand tower reaction In device, start the steam oil heater in the vertical tower reactor of stirring, 132.8 DEG C~178.4 DEG C of set temperature starts stirring Blender in vertical tower reactor, rotating speed are 124rpm~519rpm, and pH is adjusted between 4.3~8.3, dehydration 133.3~ 147.3 minute, spare；

4th step：The alkali formula aphthenic acids zinc salt and silver nano-particle mixture that the character that 3rd step is obtained changes, it is dense to add to quality [- three base of tri- oxygen triazines -1,3,5 (2H, 4H, 6H) of 2,4,6-] three that the methyl ethyl ketoxime that degree is 134mg/L~364mg/L blocks In (cyclohexyl) isocyanates, cocurrent add to the 1st step stirring stand tower reactor in, flow acceleration be 269mL/min~ 997mL/min；Start stirring and found tower reactor blender, setting speed is 138rpm~178rpm；Stirring 4~8 minutes；Again 7- methyl octanals are added, starts the steam oil heater in the vertical tower reactor of stirring, is warming up to 168.4 DEG C~205.8 DEG C, PH is adjusted between 4.4~8.8, and it is 123.118m to be passed through helium ventilatory capacity³/ min~164.273m³/ min, heat preservation are stood 158.2~188.8 minutes；It is again started up stirring and founds tower reactor blender, rotating speed is 133rpm~178rpm, is added (2E)-formic acid -2- hexen-1-ol esters, and pH is adjusted between 4.4~8.8, heat preservation stands 157.5~197.6 minutes；

5th step：Start the blender in the vertical tower reactor of stirring, setting speed is 130rpm~197rpm, and it is vertical to start stirring Steam oil heater in tower reactor sets stirring and founds temperature in tower reactor as 1.287 × 10²DEG C~2.32 ×10²DEG C, the polymer of polyurethane is added, reacts 124.2~135.1 minutes；Rosolic acid cetyl ester is added later, starts The steam oil heater in tower reactor is found in stirring, set temperature in the vertical tower reactor of stirring as 208.4 DEG C~ 264.4 DEG C, pH is adjusted between 4.1~8.1, and pressure is 1.3MPa~1.31MPa, and the reaction time is 0.4~0.9 hour；It After be depressurized to normal pressure, be cooled to 124.2 DEG C~135.1 DEG C and discharge into molding press to get to wind turbine water inlet pipe (3-9-1-12-3)；

The grain size of the silver nano-particle is 138 μm~148 μm；

A kind of working method for the cold air accelerator in sludge dewatering negative pressure High shear device, this method includes following several A step：

1st step：Object to be cut is encased in the workpiece slot (4-3-2) on workpiece handgrip (4-3) by treatment process, control system (6) control banjo traction splint (4-3-3) of uniting works, and process object is clamped；Workpiece clamp tightness inductor (4-3-4) monitors in real time Clamping degree is dealt with objects, when workpiece clamp tightness inductor (4-3-4) detects that process object clamping degree reaches default value M When, feedback signal is sent to control system (6) by workpiece clamp tightness inductor (4-3-4), and control system (6) controls finger traction Folder (4-3-3) is stopped；

2nd step：At the same time, control system (6) starts the slide motor (3-8) of the end sliding block (3-3), in slide motor (3- 8) under driving, sliding block (3-3) does sliding motion along slideway (3-2), pushes disk (3-7) to being fixed on workpiece handgrip to drive The workpiece of the end (4-3) is close；When pushing disk (3-7) apart from workpiece 3cm~5cm, control system (6) stops slide motor (3-8) works, while controlling hydraulic cylinder (3-6) work；Under hydraulic cylinder (3-6) driving, disk (3-7) is pushed slowly to be leaned on to workpiece Closely, until disk (3-7) front end blade is pushed to be in contact with process object end face；

3rd step：Control system (6) while starting the rotation in speed regulating motor (3-4) and work piece holder (4) in pushing mechanism (3) Rotating motor (4-1)；Under speed regulating motor (3-4) driving, disk (3-7) is pushed to do circular motion clockwise；At electric rotating machine (4-1) Under motor driving, workpiece handgrip (4-3) does counterclockwise circular motion by handgrip gear (4-6)；

4th step：In electric rotating machine (4-1) rotary course, lap count (4-7) monitors electric rotating machine (4-1) rotation in real time The number of turns；When lap count (4-7) detects that electric rotating machine (4-1) rotating cycle reaches default value R, lap count Feedback signal is sent to control system (6) by (4-7), and control system (6) control electric rotating machine (4-1) is stopped；

5th step：In speed regulating motor (3-4) course of work, it is located at the timer in control system (6) to speed regulating motor (3-4) Working time carries out timing；When timer, which adds up timing time, reaches default value T, control system (6) stops speed governing electricity Machine (3-4)；

6th step：Control system (6) controls banjo traction splint (4-3-3) and unclamps, and the workpiece handled well enters subsequent processing.