CN108706842A - A kind of movable type river and lake is desilted and dredged the cooling device in sludge sample processing device - Google Patents

Abstract

A kind of mobile river and lake of disclosure of the invention is desilted and dredged the cooling device in sludge sample processing device.Barrier board is equipped on the left of oscillating deck, barrier board is placed vertically, and barrier board is internally provided with a large amount of horizontal grates, and barrier board or so is penetrating；Lower open mouth wing plate is equipped on the left of barrier board, between the two away from for 10cm, lower open mouth wing plate is vertically arranged；Lower open mouth wing plate is set there are two facing side wing directly, and two are faced directly side wing central symmetry, and two are faced directly open design between side wing, two face side wing directly between hard cable wire be fixedly connected；It is equipped with oily atomizer in brake cooling system side；It is equipped with oil collection box in cool room gas outlet lower part, is equipped with certain distance between the two；The cold air that the deep fat sprayed from oily atomizer generates in brake cooling system with cool room cold air import carries out heat exchange, and oil after cooling converges in oil collection box.The device intelligence degree is high, and stability is high, high yield rate small to whole equipment impact force.

Description

A kind of movable type river and lake is desilted and dredged the cooling device in sludge sample processing device

Technical field

It desilts and dredges sludge sample processing device field the invention belongs to river and lake, and in particular to a kind of movable type river and lake dredging Cooling device in Dredged Sludge sample processing device.

Background technology

The dehumidifying of currently known cooling device, cooling function are single, and synchronization has been only capable of using surface cooling means Independently made at while for dehumidifying or cooling target single homework, can not achieve for cooling target with dehumidifying target Industry.The whole air-flows for flowing through conditioner are down to dew-point temperature when executing except wet construction, can generally be less than system and need Wind pushing temperature, need again by heating apparatus improve air themperature, increase the internal loss of conditioner.

Invention content

It desilts and dredges sludge sample processing device in order to solve the above technical problem, the present invention provides a kind of mobile river and lake In cooling device, the fixed frame 2 be stainless steel rectangular structure, thickness is between 3cm~4cm；The shock-absorbing foot pad 1 Quantity 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 are fixedly mounted on 2 top of fixed frame.

Further, what this section was told about is 3 structure of heretofore described pushing mechanism.The slideway 3-2 is solid by slideway Determine block 3-1 to be fixedly connected with support platform 5；The cross sections the slideway 3-2 are in " Ω " shape, and slideway 3-2 quantity is 2；It is described Sliding block 3-3 is slidably connected with slideway 3-2, and the ends sliding block 3-3 are provided with slide motor 3-8, slide motor 3-8 driving sliding blocks 3-3 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；Institute It states speed regulating motor one end transmission shaft 3-10 to connect with speed regulating motor 3-4, 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 rotations.

Further, what this section was told about is 7 structure of heretofore described rolling cutter.Driven wheel 7-1 positioned at one end, It is connect with external cutter motor, meanwhile, driven wheel 7-1 is fixedly connected with transmission shaft 7-9；Branch is equipped on the inside of driven wheel 7-1 Support 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；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 The quantity of pipe 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.

Further, what this section was told about is heretofore described slideway 3-2 refrigerating device inside structures.Quilt positioned at side Coolant inlet 3-2-1 is connected to heat-exchanging chamber 3-2-3, and by coolant liquid entrance 3-2-1 be located at the lower parts heat-exchanging chamber 3-2-3, Low level；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 by coolant liquid outlet 3-2-7 and heat Switch room 3-2-3 is connected to；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, The quantity of heat-exchange tube 3-2-2 is 20, the more vertical equidistant arrangements of heat-exchange tube 3-2-2；Distinguish at the both ends heat-exchange tube 3-2-2 Equipped with buffered room 3-2-5, the both ends heat-exchange tube 3-2-2 connect with the buffered room 3-2-5 for being located at its upper and lower ends respectively It is logical；The heat-exchanging chamber 3-2-3 is separated by the partition board 3-2-4 and buffered room 3-2-5 of upper and lower ends.

Further, what this section was told about is heretofore described medicament mixing device 3-2-8 structures.Medicament positioned at one end Enter pipe 3-2-8-9 equipped with diluent on the right side of import 3-2-8-1, medicament inlet 3-2-8-1, diluent enters pipe 3-2-8-9 mono- It holds and is connected to external diluent bottle, it is open that diluent, which enters the pipe 3-2-8-9 other ends, and is inserted into diffusion horn mouth 3-2- Inside 8-7；It is equipped with decentralized network 3-2-8-8 in the middle part of diffusion horn mouth 3-2-8-7, is holey, vertical display；Spread loudspeaker Mouth 3-2-8-7 is flared structure, heavy caliber end towards right side, diffusion horn mouth 3-2-8-7 heavy calibers end with it is small-bore The diameter ratio at 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 The ring pipe right lateral surface of structure, diffusant jet pipe 3-2-8-2 is equipped with a large amount of through-holes, diffusant one end jet pipe 3-2-8-2 and expansion Powder enters pipe 3-2-8-3 connections.

Further, what this section was told about is heretofore described promotion disk brake apparatus 3-9 structures.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.

Further, what this section was told about is heretofore described brake cooling system 3-9-1 structures.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.

Further, what this section was told about is 4 structure of heretofore described work piece holder.The gear wheel 4-4 is arranged in inspection It repaiies 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 It is outer toothing that central gear 4-5 and handgrip gear 4-6, central gear 4-5, handgrip gear 4-6 are equipped in 4-4；The center Gear 4-5 is located at the central axes gear wheel 4-4, and handgrip gear 4-6, gear wheel 4-4, center are surrounded by central gear 4-5 Gear 4-5, handgrip gear 4-6 three engage connection；The handgrip gear 4-6 quantity is three, around central gear 4-5 in circle Week is symmetrical.

Further, what this section was told about is heretofore described lap count 4-7 structures.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.

Further, what this section was told about is heretofore described workpiece handgrip 4-3 structures.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.

Further, the butterfly ventilating hole plate 3-9-1-2 is molded by high molecular material pressing mold, butterfly ventilating hole plate 3-9-1-2 Constituent and manufacturing process it is as follows：

One, butterfly ventilating hole plate 3-9-1-2 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, 4,4'(1- methyl ethylidene) Shuan [2- (2- acrylic)s ]Phenol 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;Tri- oxygen triazine -1 2,4,6-, 3,5 (2H, 4H, 6H)-three Ji ]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 butterfly ventilating hole plate 3-9-1-2, 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, Heat preservation 124.4~135.4 minutes is added 4,4'(1- methyl ethylidene) Shuan [2- (2- acrylic)s ]Phenol and (chloromethyl) ring 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 The methyl ethyl ketoxime that degree is 134mg/L~364mg/L blocks [- three Ji &#93 of tri- oxygen triazines -1,3,5 (2H, 4H, 6H) of 2,4,6-;Three 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 butterfly ventilating hole plate 3-9-1-2；It is described The grain size of silver nano-particle is 138 μm~148 μm.

Further, a kind of mobile river and lake is desilted and dredged the work side of the cooling device in sludge sample processing device Method, this method include 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 mobile river and lake of the present invention is desilted and dredged the cooling device in sludge sample processing device, the device Intelligence degree is high, and time intelligence is controllable, and stability is high, and the speed of service is fast, small to other equipment impact force, and work efficiency is high.

Description of the drawings

Fig. 1 is the cooling device that a kind of heretofore described mobile river and lake is desilted and dredged in sludge sample processing device Schematic diagram.

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 4 structural schematic diagram of work piece holder.

Fig. 9 is heretofore described lap count 4-7 structural schematic diagrams.

Figure 10 is heretofore described workpiece handgrip 4-3 structural schematic diagrams.

Figure 11 is heretofore described butterfly ventilating hole plate 3-9-1-2 material wear-resistant rates with usage time variation diagram.

Specific implementation mode

It desilts and dredges sludge sample process to a kind of mobile river and lake provided by the invention with reference to the accompanying drawings and examples Cooling device in equipment is further described.

As shown in Figure 1, being that a kind of heretofore described mobile river and lake is desilted and dredged in sludge sample processing device Cooling device schematic diagram.The pushing mechanism 3 is arranged in 5 side of support platform；The work piece holder 4 is arranged in support platform 5 The other side；The control system 6 is fixedly mounted on fixed frame 2；The rolling cutter 7 is located at 3 left side of pushing mechanism, the two Connection.

As shown in Fig. 2, being heretofore described 3 structural schematic diagram of pushing mechanism.The fuel tank 3-5 and hydraulic cylinder 3-6 One end conduit connection；The hydraulic cylinder 3-6 other ends push disk 3-7 to connect with detachable；Promotion disk brake apparatus 3-9 Between the two in promotion disk 3-7 and hydraulic cylinder 3-6；The speed regulating motor 3-4, hydraulic cylinder 3-6, disk 3-7 central axis is pushed to exist In same horizontal line, disk 3-7 is pushed 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 are connected by conducting wire and the control of control system 6 respectively；The slide motor 3-8 passes through conducting wire and control system 6 control connection of system.

As shown in figure 3, being 7 structural schematic diagram of heretofore described rolling cutter.The peripheries water inlet pipe 7-7 are equipped with heating tube 7- 5, heating tube 7-5 helical structures, one end heating tube 7-5 is 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 implements heating to water inlet pipe 7-7, and transformer 7-2 implements to adjust to heating temperature Section；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, central shaft Symmetric mode is fixed on transmission shaft 7-9；It is equipped with cutting edge nozzle 7-6, the one end cutting edge nozzle 7-6 in the roots cutting edge 7-3 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 passes through Transmission shaft 7-9 drives cutting edge 7-3 rotations, cutting edge 7-3 to implement equidistant cutting to material；Meanwhile cutting edge nozzle 7-6 is to cutting Blade 7-3 knife faces implement cleaning.

As shown in figure 4, being the cooling device structural schematic diagram being arranged for slideway 3-2 in the present invention.Superposed buffering Process chamber 3-2-5, top are equipped with refrigerant inlet 3-2-6, and the buffered room 3-2-5 on top is connected to refrigerant inlet 3-2-6, Buffered room its bottom 3-2-5 positioned at lower part is equipped with refrigerant exit 3-2-9, the buffered room 3-2-5 of lower part and bottom Refrigerant exit 3-2-9 connection；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, will be hot caused by heat-exchange tube 3-2-2 Amount absorbs, and is 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, it will Heat transfer gives heat-exchange tube 3-2-2, and from by coolant liquid outlet 3-2-7 outflows；Meanwhile external agent is mixed by medicament and is filled It sets 3-2-8 to be controllably added to inside heat-exchanging chamber 3-2-3, be reacted with by coolant liquid.

As shown in figure 5, being heretofore described medicament mixing device 3-2-8 structural schematic diagrams.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；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 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.

As shown in fig. 6, being heretofore described promotion disk brake apparatus 3-9 structural schematic diagrams.Outside brake caliper 3-9-4 It encloses equipped with braking hauling rope 3-9-3, braking hauling rope 3-9-3 is around brake caliper 3-9-4 surroundings, and the two is hinged；Braking is led The other end of straw line 3-9-3 is connect with haulage gear 3-9-2；It is equipped with brake cooling system 3-9- on the tops brake caliper 3-9-4 1, the two is connected by conduit；Haulage gear 3-9-2 rotations, tightening braking hauling rope 3-9-3, and then pass through brake caliper 3-9- 4 are tightly attached to 4 friction plate 3-9-6 on speed regulating motor transmission shaft 3-10, and speed regulating motor transmission shaft 3-10 is made to stop operating；With this Meanwhile the heat that friction plate 3-9-6 is generated by friction, pass through the brake cooling system 3-9-1 bands being connect with brake caliper 3-9-4 It walks.

As shown in fig. 7, being heretofore described brake cooling system 3-9-1 structural schematic diagrams.In oscillating deck 3-9-1-8 Right side is equipped with butterfly plate 3-9-1-1, and butterfly plate 3-9-1-1 thin-slab structures, single butterfly plate 3-9-1-1 are placed vertically, butterfly plate 3-9-1-1 quantity is 20, and 20 butterfly plate 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 symmetries, two arc side wings pass through the 3-9-1-2 connections of butterfly ventilating hole plate, butterfly ventilating hole plate 3-9- 1-2 promotes air-flow to form turbulent flow in its both sides；Barrier board 3-9-1-7, barrier board 3-9-1- are equipped on the left of oscillating deck 3-9-1-8 7 vertical placements, barrier board 3-9-1-7 are internally provided with a large amount of horizontal grates, and barrier board 3-9-1-7 or so is penetrating；In barrier board 3- Lower open mouth wing plate 3-9-1-6 is equipped on the left of 9-1-7, between the two away from being vertically arranged for 10cm, lower open mouth wing plate 3-9-1-6；It is lower spacious 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 opening between side wing Design, two face side wing directly between hard cable wire be fixedly connected；It is equipped with oily atomizer in the sides brake cooling system 3-9-1 3-9-1-10；It is equipped with oil collection box 3-9-1-11 in the cool room gas outlet lower parts 3-9-1-9, is equipped with certain distance between the two；From The deep fat that oily atomizer 3-9-1-10 sprays generates in brake cooling system 3-9-1 with cool room cold air import 3-9-1-4 Cold air carry out heat exchange, oil after cooling converges in oil collection box 3-9-1-11.

As shown in figure 8, being heretofore described 4 structural schematic diagram of work piece holder.The electric rotating machine 4-1 is fixedly mounted In 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 service chamber The other sides 4-2, workpiece one end handgrip 4-3 are fixedly connected with handgrip gear 4-6；The lap count 4-7 is fixedly connected on rotation On rotating motor 4-1 turntables；The electric rotating machine 4-1, lap count 4-7 are connected by conducting wire and the control of control system 6 respectively； Electric rotating machine 4-1 driving central gear 4-5 rotations, and then three, periphery handgrip gear 4-6 is driven to be done along gear wheel 4-4 interior tooths Revolution motion, while three handgrip gear 4-6 are also done rotation movement, handgrip gear 4-6 drives workpiece public by workpiece handgrip 4-3 Turn and rotation.

As shown in figure 9, being heretofore described lap count 4-7 structural schematic diagrams.In the level sides conversion head 4-7-2 To equipped with spare Laser Measuring circle probe 4-7-11, quantity is 4, and spare Laser Measuring circle probe 4-7-11 pops one's head in Laser Measuring circle 4-7-1 structures are identical, and Laser Measuring circle probe 4-7-1 and spare Laser Measuring circle probe 4-7-11 are Demountable；The rotation The tops shaft 4-7-7 are equipped with gearbox 4-7-5, and gearbox 4-7-5 is internally provided with deboost axle 4-7-3, deboost axle 4-7-3 and rotation The engagement connection of axis 4-7-7 gears；The tops gearbox 4-7-5 are equipped with electric rotating machine 4-7-10, electric rotating machine 4-7-10 and deboost axle The engagement connection of 4-7-3 gears；The bottoms gearbox 4-7-5 are equipped with temperature sensor 4-7-4, velocity sensor 4-7-6；Electric rotating machine 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 probe The operating angle of 4-7-1；At the same time, it is located at temperature sensor 4-7-4, the velocity sensor 4-7-6 of the bottoms gearbox 4-7-5 The object state on workbench 4 is monitored in real time.

As shown in Figure 10, it is heretofore described workpiece handgrip 4-3 structural schematic diagrams.Banjo traction splint 4-3-3 drivings Motor, workpiece clamp tightness inductor 4-3-4 are connected by conducting wire and the control of control system 6 respectively.Setting in the control system 6 There are timer, the timer to be connect with speed regulating motor 3-4 actuating coil polygon control surveys.

The content that following embodiment further illustrates the present invention, as butterfly ventilating hole plate 3-9-1-2, it is the weight of the present invention Component is wanted, due to its presence, increases the service life of integral device, it is played for the safety of integral device, even running Key effect.For this purpose, by it is following be embodiment, further verify butterfly ventilating hole plate 3-9-1-2 of the present invention, institute's table The physical characteristic higher than other related patents revealed.

Embodiment 1

Butterfly ventilating hole plate 3-9-1-2 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 4,4'(1- methyl ethylidene) Shuan [2- (2- acrylic)s ]136.9 parts of the polymer of phenol and (chloromethyl) ethylene oxide is adjusted 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 The methyl ethyl ketoxime that degree is 134mg/L blocks [- three Ji &#93 of tri- oxygen triazines -1,3,5 (2H, 4H, 6H) of 2,4,6-;Three (cyclohexyl) 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 butterfly ventilating hole plate 3-9-1-2；

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

Embodiment 2

Butterfly ventilating hole plate 3-9-1-2 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 4,4'(1- methyl ethylidene) Shuan [2- (2- acrylic)s ]197.5 parts of the polymer of phenol and (chloromethyl) ethylene oxide is adjusted 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 The methyl ethyl ketoxime that degree is 364mg/L blocks [- three Ji &#93 of tri- oxygen triazines -1,3,5 (2H, 4H, 6H) of 2,4,6-;Three (cyclohexyl) 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 butterfly ventilating hole plate 3-9-1-2；

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

Embodiment 3

Butterfly ventilating hole plate 3-9-1-2 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 4,4'(1- methyl ethylidene) Shuan [2- (2- acrylic)s ]136.9 parts of the polymer of phenol and (chloromethyl) ethylene oxide is adjusted 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 The methyl ethyl ketoxime that degree is 134.9mg/L blocks [- three Ji &#93 of tri- oxygen triazines -1,3,5 (2H, 4H, 6H) of 2,4,6-;Three (cyclohexyl) 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 butterfly ventilating hole plate 3-9-1-2；

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

Reference examples

Reference examples use the component same as the application butterfly ventilating hole plate 3-9-1-2 of certain commercially available brand, are tested for the property experiment.

Embodiment 4

The butterfly ventilating hole plate 3-9-1-2 and reference examples of the Examples 1 to 3 same component obtained are tested for the property experiment, To parameters such as mechanical strength enhancing rate, compression strength enhancing rate, anti-yield strength enhancing rate, wear rate enhancing rates after test It is analyzed.Data analysis is as shown in table 1.

As seen from Table 1, butterfly ventilating hole plate 3-9-1-2 of the present invention, mechanical strength enhancing rate, compression strength are promoted Rate, anti-yield strength enhancing rate, wear rate enhancing rate are above the product of prior art production.

In addition, as shown in figure 11, butterfly ventilating hole plate 3-9-1-2 of the present invention is carried out with reference examples, with making It is counted with time change test data.Find out in figure, Examples 1 to 3 is substantially better than existing in test data technical indicator The product of technology production.

Claims (10)

1. A kind of cooling device 1. movable type river and lake is desilted and dredged in sludge sample processing device, including：Shock-absorbing foot pad (1), Gu Determine frame (2), pushing mechanism (3), work piece holder (4), support platform (5), control system (6), rolling cutter (7)；Its feature It is, the fixed frame (2) is stainless steel rectangular structure, and thickness is between 3cm~4cm；Shock-absorbing foot pad (1) quantity It is four, 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 workpiece clamp Tool (4) 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)；

   The promotion disk brake apparatus (3-9) is equipped with brake cooling system (3-9-1)；

   The brake cooling system (3-9-1) includes：Butterfly plate (3-9-1-1), butterfly ventilating hole plate (3-9-1-2), cool room stirs Mix leaf (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)；

   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；

   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).
2. Cooling device 2. a kind of mobile river and lake according to claim 1 is desilted and dredged in sludge sample processing device, It is characterized in 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), adjust Speed motor transmission shaft (3-10)；Wherein, the slideway (3-2) connects by the way that slideway fixed block (3-1) and support platform (5) are fixed It connects；Slideway (3-2) cross section is in " Ω " shape, and slideway (3-2) quantity is 2；The sliding block (3-3) and slideway (3-2) It is slidably connected, the end sliding block (3-3) is provided with slide motor (3-8), and slide motor (3-8) drives sliding block (3-3) in slideway (3- 2) it is slided on；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)；Institute It states speed regulating motor transmission shaft one end (3-10) to connect with speed regulating motor (3-4), the other end passes through fuel tank (3-5), pushes disk braking Device (3-9), hydraulic cylinder (3-6) are 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- with detachable 7) it connects；The promotion disk brake apparatus (3-9), which is located at, pushes disk (3-7) and hydraulic cylinder (3-6) between the two；The speed governing electricity Machine (3-4), pushes disk (3-7) central axis in the same horizontal line at hydraulic cylinder (3-6), pushes disk (3-7) and 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. Cooling device 3. a kind of mobile river and lake according to claim 2 is desilted and dredged in sludge sample processing device, It is characterized in 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)；It is located at The driven wheel (7-1) of one end is connect with external cutter motor, meanwhile, driven wheel (7-1) and the fixed company of transmission shaft (7-9) It connects；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 The both ends of transmission shaft (7-9)；Transmission shaft (7-9) hollow structure, be internally provided with transformer (7-2), heating tube (7-5), into Water 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) with into Water end (W.E.) mouth (7-8) is connected to, and water inlet port (7-8) is connected to external pump；Water inlet pipe (7-7) periphery is equipped with heating tube (7-5), adds Heat pipe (7-5) helical structure, heating tube one end (7-5) are connected to by conducting wire with transformer (7-2), transformer (7-2) it is another End is electrically connected by conducting wire with external city, and heating tube (7-5) is implemented to heat to water inlet pipe (7-7), and transformer (7-2) is to heating temperature Degree is implemented to adjust；Cutting edge (7-3) is equipped with outside transmission shaft (7-9), cutting edge (7-3) quantity is 4,4 cutting edge (7- 3) angularly, mode substantially symmetrical about its central axis is fixed on transmission shaft (7-9)；It is equipped with cutting edge nozzle (7- in the root cutting edge (7-3) 6), 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 with into Water pipe (7-7) is connected to；

   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. Cooling device 4. a kind of mobile river and lake according to claim 3 is desilted and dredged in sludge sample processing device, It is characterized in that, slideway (3-2) is equipped with cooling device, 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 gone out by coolant liquid Mouth (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. Cooling device 5. a kind of mobile river and lake according to claim 4 is desilted and dredged in sludge sample processing device, It is characterized in that, the medicament mixing device (3-2-8) is L-type pipe structure, both ends perforation, medicament mixing device (3-2-8) packet It includes：Medicament inlet (3-2-8-1), diffusant jet pipe (3-2-8-2), diffusant enter pipe (3-2-8-3), buffer subsystem (3-2-8-4), Stir ball (3-2-8-5), stablize net (3-2-8-6), diffusion horn mouth (3-2-8-7), decentralized network (3-2-8-8), diluent into Enter 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. Cooling device 6. a kind of mobile river and lake according to claim 5 is desilted and dredged in sludge sample processing device, It is characterized in that, the promotion disk brake apparatus (3-9) includes：Brake cooling system (3-9-1), haulage gear (3-9-2), system Dynamic hauling rope (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. Cooling device 7. a kind of mobile river and lake according to claim 6 is desilted and dredged in sludge sample processing device, It is characterized in 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 Service chamber (4-2) is internal, and gear wheel (4-4) is interior tooth type hollow structure, and interior teeth are located at gear wheel (4-4) internal circumference On, central gear (4-5) and handgrip gear (4-6), central gear (4-5), handgrip gear (4-6) are equipped in gear wheel (4-4) For outer toothing；The central gear (4-5) is located at the central axes gear wheel (4-4), is surrounded by and grabs in central gear (4-5) Hand gear (4-6), gear wheel (4-4), central gear (4-5), handgrip gear (4-6) three engage connection；The handgrip gear (4-6) quantity is three, circumferentially symmetrical around central gear (4-5)；The electric rotating machine (4-1) is fixedly mounted on inspection The side case (4-2) is repaiied, electric rotating machine (4-1) is drivingly connected with central gear (4-5)；The workpiece handgrip (4-3) is arranged in inspection The other side case (4-2) is repaiied, workpiece handgrip one end (4-3) is fixedly connected with handgrip gear (4-6)；The lap count (4-7) It 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.
8. Cooling device 8. a kind of mobile river and lake according to claim 7 is desilted and dredged in sludge sample processing device, It is characterized in 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), auxiliary 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)； Laser Measuring circle positioned at bottom is popped 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 swashs Light emitting receiver (4-7-9) is surrounded by secondary light source (4-7-8), and secondary light source (4-7-8) is 12, secondary light source (4- 7-8) it is LE light sources；The conversion head (4-7-2) be located at Laser Measuring circle probe (4-7-1) top, conversion head (4-7-2) with it is upper The rotary shaft (4-7-7) in portion is rotatablely connected, meanwhile, Laser Measuring circle is popped one's head in (4-7-1) and the rotary shaft (4-7-7) on top is fixed and connected It connects；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 probe (4-7-11) is identical as Laser Measuring circle probe (4-7-1) structure, Laser Measuring circle probe (4-7-1) and spare Laser Measuring circle (4-7-11) is popped one's head in as 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).
9. Cooling device 9. a kind of mobile river and lake according to claim 8 is desilted and dredged in sludge sample processing device, It is characterized in that, the workpiece handgrip (4-3) includes：Arm (4-3-1), workpiece slot (4-3-2), banjo traction splint (4-3-3), Workpiece clamp tightness 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) it is circular groove, diameter is 8cm~12cm；Banjo traction splint (4-3-3) quantity is three, and circumference is equidistant It is distributed in around workpiece slot (4-3-2), the end banjo traction splint (4-3-3) is equipped with antiskid protection pad and the induction of workpiece clamp tightness Device (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.
10. Cooling device 10. a kind of mobile river and lake according to claim 9 is desilted and dredged in sludge sample processing device, It is characterized in that, the butterfly ventilating hole plate (3-9-1-2) is molded by high molecular material pressing mold, butterfly ventilating hole plate (3-9-1-2) Constituent is as follows：

    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, 4,4'(1- methyl ethylidene) Shuan [2- (2- acrylic)s ]Phenol 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;Tri- oxygen triazine -1 2,4,6-, 3,5 (2H, 4H, 6H)-three Ji ]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 butterfly ventilating hole plate (3-9-1-2), 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, Heat preservation 124.4~135.4 minutes is added 4,4'(1- methyl ethylidene) Shuan [2- (2- acrylic)s ]Phenol and (chloromethyl) ring 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 The methyl ethyl ketoxime that degree is 134mg/L~364mg/L blocks [- three Ji &#93 of tri- oxygen triazines -1,3,5 (2H, 4H, 6H) of 2,4,6-;Three 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 butterfly ventilating hole plate (3-9-1-2)；

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

    A kind of movable type river and lake is desilted and dredged the working method of the cooling device in sludge sample processing device, this method include with Under several 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) 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.