CN108689574A - A kind of air inlet amount controller in dewatered sludge processing equipment - Google Patents
A kind of air inlet amount controller in dewatered sludge processing equipment Download PDFInfo
- Publication number
- CN108689574A CN108689574A CN201810493557.1A CN201810493557A CN108689574A CN 108689574 A CN108689574 A CN 108689574A CN 201810493557 A CN201810493557 A CN 201810493557A CN 108689574 A CN108689574 A CN 108689574A
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- China
- Prior art keywords
- air door
- fan
- stirring
- gear
- brake
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04D—NON-POSITIVE-DISPLACEMENT PUMPS
- F04D25/00—Pumping installations or systems
- F04D25/02—Units comprising pumps and their driving means
- F04D25/08—Units comprising pumps and their driving means the working fluid being air, e.g. for ventilation
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04D—NON-POSITIVE-DISPLACEMENT PUMPS
- F04D27/00—Control, e.g. regulation, of pumps, pumping installations or pumping systems specially adapted for elastic fluids
- F04D27/003—Control, e.g. regulation, of pumps, pumping installations or pumping systems specially adapted for elastic fluids by throttling
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Treatment Of Sludge (AREA)
Abstract
A kind of air inlet amount controller in dewatered sludge processing equipment of disclosure of the invention.Air door push rod positioned at bottom end is slided up and down with the air door pedestal positioned at its underpart to be connect;The air door cam is located at air door push rod lower part, and air door push rod engages connection with air door cam teeth;Cantilever and air door clamp are hinged on the outside of air door cam;Air door support arm is equipped in the middle part of air door clamp, one end of air door support arm is hinged with air door clamp, and the other end is hinged with air door push rod;It is equipped with air door plate in air door clamp end;Air door push rod positioned at bottom end moves up, and right side air door cam is driven to rotate clockwise, and right side air door clamp is driven to rotate clockwise;While air door push rod moves up, also drives air door support arm around its middle part fulcrum rotation, equally drive right side air door clamp to rotate clockwise, finally open air door plate;It is on the contrary then anti-.The device intelligence degree is high, and stability is good, is uniformly dispersed, small to whole equipment impact force.
Description
Technical field
The invention belongs to sludge drying treatment equipment fields, and in particular to it is a kind of in dewatered sludge processing equipment into
Blast volume controller.
Background technology
In sludge drying processing procedure, the local air output of cooling wind cycle has the thickness of sludge drying important shadow
It rings, the big position of air output, since sludge drying is quickly cooled down, in order to keep the uniformity of thickness, it is desirable that cooling vane
Air output want uniformity, but be extremely difficult to this requirement in many cases, intake controller architecture is unreasonable, air inlet
Amount controller deformation etc. can all cause the air quantity for reaching cooling vane inconsistent.It can be adjusted as needed big with the air quantity of variation
Small is those skilled in the art institute urgent need to solve the problem.
Invention content
In order to solve the above technical problem, the present invention provides a kind of intake controls in dewatered sludge processing equipment
Device, 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;It is described
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 speedup fan assembly 3-9-1-12;Vertical shift device 3-9-1-13 is located at butterfly plate 3-9-
The sides 1-1, vertical shift device 3-9-1-13 and butterfly plate 3-9-1-1 and butterfly ventilating hole plate 3-9-1-2 is hinged, vertical shift dress
Setting 3-9-1-13 drives butterfly plate 3-9-1-1 and butterfly ventilating hole plate 3-9-1-2 to move up and down.
Further, what this section was told about is heretofore described vertical shift device 3-9-1-13 structures.Positioned at vertical
Sliding bar 3-9-1-13-1 quantity outside mobile device 3-9-1-13 is 3, is equally spaced vertically, both ends are fixed on vertically
Mobile device 3-9-1-13 upper and lower ends;Sliding panel 3-9-1-13-8 is equipped on sliding bar 3-9-1-13-1, the two sliding connects
It connects;Sliding panel 3-9-1-13-8 is equipped with sliding block mobile motor 3-9-1-13-3, and the one end sliding block mobile motor 3-9-1-13-3 is set
There are sliding block mobile motor gear, sliding block mobile motor gear to engage connection with the surfaces sliding rail 3-9-1-13-4 rack;Sliding panel 3-
Sliding block moving handle 3-9-1-13-2, sliding block moving handle 3-9-1-13-2 one end gears and sliding rail 3- are additionally provided on 9-1-13-8
The rack engagement connection of the surfaces 9-1-13-4.
Further, what this section was told about is heretofore described dispersal device 3-9-1-5 structures.The dispersion main shaft 3-
9-1-5-3 cylinder steel constructions, the one end dispersion main shaft 3-9-1-5-3 are equipped with dispersion driving wheel 3-9-1-5-2, dispersion main shaft 3-9-1-
The 5-3 other ends are equipped with dispensing support wheel 3-9-1-5-4;The dispersion driving wheel 3-9-1-5-2 central shafts and dispersion main shaft 3-9-
1-5-3 is fixedly connected, and dispersion driving wheel 3-9-1-5-2 outer rims are connect with outer scattered motor gear teeth meshing, dispensing support wheel 3-
9-1-5-4 central shafts are rotatablely connected with dispersion main shaft 3-9-1-5-3, and dispensing support wheel 3-9-1-5-4 outer rims are fixed with holder.
Further, what this section was told about is heretofore described speedup fan assembly 3-9-1-12 structures.Positioned at top
Fan room air inlet 3-9-1-12-4 with positioned at bottom fan room gas outlet 3-9-1-12-1 penetrate through;Fan room's wind speed
Sensing instrument 3-9-1-12-5 is located at the lower parts fan room air inlet 3-9-1-12-4, fan room wind speed sensing instrument 3-9-1-12-5 and control
System 6 processed connects, the fan shaft 3-9-1-12-6 connections of fan room wind speed sensing instrument 3-9-1-12-5 and its underpart;Fan shaft 3-
9-1-12-6 is located at speedup fan assembly 3-9-1-12 inside centers, longitudinally disposed, cylindrical hollow structure, be internally provided with including
The rotor of armature core and armature winding;It is equipped with fan shaft cooling channel 3-9-1-12-2 in fan shaft 3-9-1-12-6 waists,
The two is fixedly connected, fan shaft cooling channel 3-9-1-12-2 horizontal circle fan shaft 3-9-1-12-6, fan shaft cooling channel
3-9-1-12-2 hollow structures, outer surface are set there are four fan shaft side air inlet 3-9-1-12-7, and fan shaft cools down channel 3-
9-1-12-2 is mutually communicated with fan shaft side air inlet 3-9-1-12-7.
Further, what this section was told about is heretofore described air inlet amount controller 3-9-1-12-10 structures.The bottom of positioned at
The air door push rod 3-9-1-12-10-1 at end is slided up and down with the air door pedestal 3-9-1-12-10-6 positioned at its underpart and is connect;It is described
Air door cam 3-9-1-12-10-2 is located at the lower parts air door push rod 3-9-1-12-10-1, air door push rod 3-9-1-12-10-1 and wind
Door cam 3-9-1-12-10-2 teeth engagement connection;Cantilever and air door clamp 3-9-1- on the outside of air door cam 3-9-1-12-10-2
12-10-4 is hinged;Air door support arm 3-9-1-12-10-3, air door support arm 3-9- are equipped in the middle part of air door clamp 3-9-1-12-10-4
One end of 1-12-10-3 is hinged with air door clamp 3-9-1-12-10-4, and the other end is cut with scissors with air door push rod 3-9-1-12-10-1
It connects.
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 air door plate 3-9-1-12-10-5 is molded by high molecular material pressing mold, air door plate 3-9-1-12-
The constituent and manufacturing process of 10-5 is as follows:
One, air door plate 3-9-1-12-10-5 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 air door plate 3-9-1-12-10-5, 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 ] 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 air door plate 3-9-1-12-10-5;Institute
The grain size for stating silver nano-particle is 138 μm~148 μm.
Further, a kind of working method for the air inlet amount controller in dewatered sludge processing equipment, this method packet
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 air inlet amount controller in dewatered sludge processing equipment of the present invention, the device intelligence degree
Height, time intelligence is controllable, and mobile energy is substantially improved, and stability is high, and the speed of service is fast, small to other equipment impact force, work
Make efficient.
Description of the drawings
Fig. 1 is a kind of heretofore described air inlet amount controller schematic diagram in dewatered sludge processing equipment.
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 vertical shift device 3-9-1-13 structural schematic diagrams.
Fig. 9 is heretofore described dispersal device 3-9-1-5 structural schematic diagrams.
Figure 10 is heretofore described speedup fan assembly 3-9-1-12 structural schematic diagrams.
Figure 11 is heretofore described air inlet amount controller 3-9-1-12-10 structural schematic diagrams.
Figure 12 is heretofore described 4 structural schematic diagram of work piece holder.
Figure 13 is heretofore described lap count 4-7 structural schematic diagrams.
Figure 14 is heretofore described workpiece handgrip 4-3 structural schematic diagrams.
Figure 15 is heretofore described air door plate 3-9-1-12-10-5 material wear-resistant rates with usage time variation diagram.
Specific implementation mode
With reference to the accompanying drawings and examples to a kind of intake in dewatered sludge processing equipment provided by the invention
Controller is further described.
As shown in Figure 1, being that a kind of heretofore described air inlet amount controller in dewatered sludge processing equipment shows
It is intended to.The fixed frame 2 is stainless steel rectangular structure, and thickness is between 3cm~4cm;1 quantity of the shock-absorbing foot pad is four
It is a, it is respectively and fixedly installed to 2 bottom four corners of fixed frame;The support platform 5 is rectangle galvanized sheet, and support platform 5 fixes peace
Above fixed frame 2;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 dispersal device 3-9-1-5, and the one end dispersal device 3-9-1-5 is connect with external refrigeration room stirring motor,
Its other end is fixedly connected with cool room paddle 3-9-1-3;It is equipped with oscillating deck 3-9- in the lower parts cool room paddle 3-9-1-3
1-8, the oscillating deck 3-9-1-8 thin-slab structures, single oscillating deck 3-9-1-8 is horizontal positioned, and oscillating deck 3-9-1-8 quantity is 20
A, it is two groups that 20 oscillating deck 3-9-1-8, which are divided to, is vertically arranged, and with oscillating deck 3-9-1-8 is organized, distance is 10cm between each other, together
Soft rope chain concatenation between group oscillating deck 3-9-1-8, and it is fixed with the tops brake cooling system 3-9-1, it is same to organize oscillating deck 3-9-1-8
Vacantly at the central axes brake cooling system 3-9-1, oscillating deck 3-9-1-8 swings with air-flow;It is right in oscillating deck 3-9-1-8
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 horizontal positioned, 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 vertical shift device 3-9-1-13 structural schematic diagrams.The external fixation
Seat 3-9-1-13-5 is fixedly connected with sliding panel 3-9-1-13-8, in outer connection fixed seat 3-9-1-13-5 and sliding panel 3-9-1-
It is slided by brake block equipped with brake plate 3-9-1-13-6, brake plate 3-9-1-13-6 and sliding bar 3-9-1-13-1 between 13-8
Connection;The brake governor 3-9-1-13-7 is located on brake plate 3-9-1-13-6, brake governor 3-9-1-13-7 and brake
Vehicle piece connects;Sliding block mobile motor 3-9-1-13-3 drivings sliding panel 3-9-1-13-8 is moved down along sliding bar 3-9-1-13-1
It is dynamic, and drive outer connection fixed seat 3-9-1-13-5 movements;Meanwhile sliding panel 3-9-1-13-8 passes through sliding block moving handle 3-9-1-
13-2 manual rotation's handle drives sliding panels 3-9-1-13-8 is moved up and down;Brake governor 3-9-1-13-7 is hindered by brake block
On-slip movable plate 3-9-1-13-8 falls.
As shown in figure 9, being heretofore described dispersal device 3-9-1-5 structural schematic diagrams.In dispersion main shaft 3-9-1-
The surfaces 5-3 are equipped with dispersion tooth 3-9-1-5-1, and dispersion tooth 3-9-1-5-1 quantity is 12, and 12 3-9-1-5-1 points of dispersion teeth are
Four groups, every group of dispersion tooth 3-9-1-5-1 is to disperse main shaft 3-9-1-5-3 as axle center angularly axial alignment;The dispersion tooth 3-
9-1-5-1 includes dispersion tooth fourth 3-9-1-5-1-1 and dispersion tooth post 3-9-1-5-1-2, disperses tooth fourth 3-9-1-5-1-1U type knots
Structure;Dispersion tooth fourth 3-9-1-5-1-1 in the middle part of be equipped with dispersion tooth post 3-9-1-5-1-2, dispersion the one end tooth post 3-9-1-5-1-2 with
Dispersion tooth fourth 3-9-1-5-1-1 is fixed, and the other end is fixed with dispersion main shaft 3-9-1-5-3;Outer scattered motor passes through dispersion
Driving wheel 3-9-1-5-2 drives the 3-9-1-5-3 rotations of dispersion main shaft, and then drives four groups of dispersion tooth 3-9-1-5-1 rotations, realizes
Dispersion to material.
As shown in Figure 10, it is heretofore described speedup fan assembly 3-9-1-12 structural schematic diagrams.In fan shaft 3-
The both ends 9-1-12-6 are respectively equipped with fan blade 3-9-1-12-9;Fan room is equipped on speedup fan assembly 3-9-1-12 inner walls
Stator 3-9-1-12-3, fan room stator 3-9-1-12-3 are internally provided with stator core and stator winding, fan room stator 3-9-
1-12-3 is connect with external power supply;Energization rear fan room stator 3-9-1-12-3 generates rotating excitation field, pushes fan shaft 3-9-1-
12-6 is rotated, and then drives fan blade 3-9-1-12-9 rotations, and air-flow is promoted to enter from fan room air inlet 3-9-1-12-4,
And it is sprayed from fan room gas outlet 3-9-1-12-1 high speeds;At the same time, part cold wind is from fan shaft side air inlet 3-9-1-12-
7 enter, and are fan shaft 3-9-1-12-6 coolings, and air outlet 3-9-1-12-8 is discharged under fan shaft.
As shown in figure 11, it is heretofore described air inlet amount controller 3-9-1-12-10 structural schematic diagrams.It is clamped in air door
It presss from both sides the ends 3-9-1-12-10-4 and is equipped with air door plate 3-9-1-12-10-5;Positioned at bottom end air door push rod 3-9-1-12-10-1 to
Upper movement drives right side air door cam 3-9-1-12-10-2 to rotate clockwise, and drives right side air door clamp 3-9-1-12-10-
4 rotate clockwise;While air door push rod 3-9-1-12-10-1 is moved up, also air door support arm 3-9-1-12-10-3 is driven to enclose
It is same that right side air door clamp 3-9-1-12-10-4 is driven to rotate clockwise around its middle part fulcrum rotation, finally by air door plate 3-9-
1-12-10-5 is opened;It is on the contrary then anti-.
As shown in figure 12, it is heretofore described 4 structural schematic diagram of 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.
As shown in figure 13, 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 14, 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 air door plate 3-9-1-12-10-5, it is of the invention
Significant components increase the service life of integral device due to its presence, it sends out for the safety of integral device, even running
Wave key effect.For this purpose, by it is following be embodiment, further verify air door plate 3-9-1-12-10-5 of the present invention,
The physical characteristic higher than other related patents shown.
Embodiment 1
Air door plate 3-9-1-12-10-5 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 ] 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 air door plate 3-9-1-12-10-5;The grain size of the silver nano-particle is 138 μm.
Embodiment 2
Air door plate 3-9-1-12-10-5 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 ] 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 air door plate 3-9-1-12-10-5;The grain size of the silver nano-particle is 148 μm.
Embodiment 3
Air door plate 3-9-1-12-10-5 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 ] 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 air door plate 3-9-1-12-10-5;The grain size of the silver nano-particle is 138 μm.
Reference examples
Reference examples use the component same as the application air door plate 3-9-1-12-10-5 of certain commercially available brand, are tested for the property examination
It tests.
Embodiment 4
The air door plate 3-9-1-12-10-5 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, air door plate 3-9-1-12-10-5 of the present invention, mechanical strength enhancing rate, compression strength carry
The rate of liter, anti-yield strength enhancing rate, wear rate enhancing rate are above the product of prior art production.
In addition, as shown in figure 15, air door plate 3-9-1-12-10-5 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 air inlet amount controller in dewatered sludge processing equipment, including:Shock-absorbing foot pad (1), fixed frame (2),
Pushing mechanism (3), work piece holder (4), support platform (5), control system (6), rolling cutter (7);It is characterized in that, described solid
It is stainless steel rectangular structure to determine frame (2), and thickness is between 3cm~4cm;Shock-absorbing foot pad (1) quantity is four, respectively
It is fixedly mounted on fixed frame (2) bottom four corners;The support platform (5) is rectangle galvanized sheet, and support platform (5) is fixedly mounted
Above fixed frame (2);The pushing mechanism (3) is arranged in support platform (5) side;The work piece holder (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);
Disk brake apparatus (3-9) is pushed to be equipped with brake cooling system (3-9-1);
Brake cooling system (3-9-1) is equipped with dispersal device (3-9-1-5), speedup fan assembly (3-9-1-12), vertical shift
Device (3-9-1-13);
Speedup fan assembly (3-9-1-12) is equipped with air inlet amount controller (3-9-1-12-10);
The air inlet amount controller (3-9-1-12-10) includes:Air door push rod (3-9-1-12-10-1), air door cam (3-9-1-
12-10-2), air door support arm (3-9-1-12-10-3), air door clamp (3-9-1-12-10-4), air door plate (3-9-1-12-10-
5), air door pedestal (3-9-1-12-10-6);
On air door push rod (3-9-1-12-10-1) positioned at bottom end and the air door pedestal (3-9-1-12-10-6) positioned at its underpart
Lower slider connects;The air door cam (3-9-1-12-10-2) is located at the lower part air door push rod (3-9-1-12-10-1), and air door pushes away
Bar (3-9-1-12-10-1) engages connection with air door cam (3-9-1-12-10-2) teeth;Air door cam (3-9-1-12-10-
2) outside cantilever and air door clamp (3-9-1-12-10-4) are hinged;Air door is equipped in the middle part of air door clamp (3-9-1-12-10-4)
Support arm (3-9-1-12-10-3), one end and the air door clamp (3-9-1-12-10-4) of air door support arm (3-9-1-12-10-3) are cut with scissors
It connects, the other end is hinged with air door push rod (3-9-1-12-10-1);It is equipped with wind in the end air door clamp (3-9-1-12-10-4)
Door-plate (3-9-1-12-10-5);
Air door push rod (3-9-1-12-10-1) positioned at bottom end moves up, and drives right side air door cam (3-9-1-12-10-2)
It rotates clockwise, and right side air door clamp (3-9-1-12-10-4) is driven to rotate clockwise;Air door push rod (3-9-1-12-10-
1) while moving up, also drive air door support arm (3-9-1-12-10-3) around its middle part fulcrum rotation, it is same to drive right side
Air door clamp (3-9-1-12-10-4) rotates clockwise, and finally opens air door plate (3-9-1-12-10-5);It is on the contrary then anti-;
The vertical shift device (3-9-1-13) includes:Sliding bar (3-9-1-13-1), sliding block moving handle (3-9-1-13-
2), sliding block mobile motor (3-9-1-13-3), sliding rail (3-9-1-13-4), outer connection fixed seat (3-9-1-13-5), brake plate (3-
9-1-13-6), brake governor (3-9-1-13-7), sliding panel (3-9-1-13-8);
Sliding bar (3-9-1-13-1) quantity external positioned at vertical shift device (3-9-1-13) is 3, is equally spaced vertically,
Its both ends is fixed on vertical shift device (3-9-1-13) upper and lower ends;Sliding panel is equipped on sliding bar (3-9-1-13-1)
(3-9-1-13-8), the two is slidably connected;Sliding panel (3-9-1-13-8) is equipped with sliding block mobile motor (3-9-1-13-3), sliding
The one end block mobile motor (3-9-1-13-3) is equipped with sliding block mobile motor gear, sliding block mobile motor gear and sliding rail (3-9-1-
13-4) surface rack engagement connection;Sliding block moving handle (3-9-1-13-2), sliding block are additionally provided on sliding panel (3-9-1-13-8)
Moving handle (3-9-1-13-2) one end gear engages connection with the surface sliding rail (3-9-1-13-4) rack;The outer connection fixed seat
(3-9-1-13-5) is fixedly connected with sliding panel (3-9-1-13-8), in outer connection fixed seat (3-9-1-13-5) and sliding panel (3-
Brake plate (3-9-1-13-6) is equipped between 9-1-13-8), brake plate (3-9-1-13-6) is logical with sliding bar (3-9-1-13-1)
Brake block is crossed to be slidably connected;The brake governor (3-9-1-13-7) is located on brake plate (3-9-1-13-6), and braking is adjusted
Device (3-9-1-13-7) is connect with brake block;
Sliding block mobile motor (3-9-1-13-3) driving sliding panel (3-9-1-13-8) moves down along sliding bar (3-9-1-13-1)
It is dynamic, and drive outer connection fixed seat (3-9-1-13-5) mobile;Meanwhile sliding panel (3-9-1-13-8) passes through sliding block moving handle
(3-9-1-13-2) manual rotation's handle drives sliding panel (3-9-1-13-8) moves up and down;Brake governor (3-9-1-13-7)
Sliding panel (3-9-1-13-8) is prevented to fall by brake block;
The speedup fan assembly (3-9-1-12) includes:Fan room gas outlet (3-9-1-12-1), fan shaft cooling channel (3-
9-1-12-2), fan room's stator (3-9-1-12-3), fan room's air inlet (3-9-1-12-4), fan room wind speed sensing instrument (3-
9-1-12-5), fan shaft (3-9-1-12-6), fan shaft side air inlet (3-9-1-12-7), air outlet (3-9-1- under fan shaft
12-8), fan blade (3-9-1-12-9), air inlet amount controller (3-9-1-12-10);
Superposed fan room's air inlet (3-9-1-12-4) is passed through with the fan room gas outlet (3-9-1-12-1) positioned at bottom
It is logical;Fan room's wind speed sensing instrument (3-9-1-12-5) is located at the lower part fan room's air inlet (3-9-1-12-4), fan room's wind
Speed sensing instrument (3-9-1-12-5) is connect with control system (6), fan room's wind speed sensing instrument (3-9-1-12-5) and its underpart
Fan shaft (3-9-1-12-6) connects;Fan shaft (3-9-1-12-6) is located at speedup fan assembly (3-9-1-12) inside center,
Longitudinally disposed, cylindrical hollow structure is internally provided with the rotor including armature core and armature winding;In fan shaft (3-9-1-
12-6) waist is equipped with fan shaft and cools down channel (3-9-1-12-2), and the two is fixedly connected, fan shaft cooling channel (3-9-1-12-
2) horizontal circle fan shaft (3-9-1-12-6), fan shaft cooling channel (3-9-1-12-2) hollow structure, outer surface is equipped with
Four fan shaft side air inlets (3-9-1-12-7), fan shaft cooling channel (3-9-1-12-2) and fan shaft side air inlet (3-
9-1-12-7) it is mutually communicated;It is respectively equipped with fan blade (3-9-1-12-9) at the both ends fan shaft (3-9-1-12-6);In speedup
Fan assembly (3-9-1-12) inner wall is equipped with fan room's stator (3-9-1-12-3), and fan room's stator (3-9-1-12-3) is internal
Equipped with stator core and stator winding, fan room's stator (3-9-1-12-3) is connect with external power supply;
Energization rear fan room stator (3-9-1-12-3) generates rotating excitation field, pushes fan shaft (3-9-1-12-6) to rotate, in turn
It drives fan blade (3-9-1-12-9) to rotate, promotes air-flow to enter from fan room's air inlet (3-9-1-12-4), and from fan
Room gas outlet (3-9-1-12-1) high speed sprays;At the same time, part cold wind from fan shaft side air inlet (3-9-1-12-7) into
Enter, cool down for fan shaft (3-9-1-12-6), and air outlet (3-9-1-12-8) is discharged under fan shaft;
The top fan room's air inlet (3-9-1-12-4) is equipped with air inlet amount controller (3-9-1-12-10), air inlet amount controller (3-
9-1-12-10) control speedup fan assembly (3-9-1-12) intake;
The dispersal device (3-9-1-5) includes:Disperse tooth (3-9-1-5-1), dispersion tooth fourth (3-9-1-5-1-1) disperses tooth
Column (3-9-1-5-1-2), dispersion driving wheel (3-9-1-5-2), dispersion main shaft (3-9-1-5-3), dispensing support wheel (3-9-1-5-
4);Dispersion main shaft (3-9-1-5-3) the cylinder steel construction, dispersion one end main shaft (3-9-1-5-3) are equipped with dispersion driving wheel (3-
9-1-5-2), dispersion main shaft (3-9-1-5-3) other end is equipped with dispensing support wheel (3-9-1-5-4);Dispersion driving wheel (the 3-
9-1-5-2) central shaft is fixedly connected with dispersion main shaft (3-9-1-5-3), disperses driving wheel (3-9-1-5-2) outer rim and outer portion
Motor gear teeth meshing connection is dissipated, dispensing support wheel (3-9-1-5-4) central shaft is rotatablely connected with dispersion main shaft (3-9-1-5-3),
Dispensing support wheel (3-9-1-5-4) outer rim is fixed with holder;It is equipped with dispersion tooth (3-9- on dispersion surface main shaft (3-9-1-5-3)
1-5-1), dispersion tooth (3-9-1-5-1) quantity is 12, and 12 dispersion teeth (3-9-1-5-1) are divided into four groups, every group of dispersion tooth
(3-9-1-5-1) is axle center angularly axial alignment to disperse main shaft (3-9-1-5-3);Dispersion tooth (3-9-1-5-1) packet
Dispersion tooth fourth (3-9-1-5-1-1) and dispersion tooth post (3-9-1-5-1-2) are included, tooth fourth (3-9-1-5-1-1) U-shaped structure is disperseed;
Dispersion tooth post (3-9-1-5-1-2), dispersion tooth post (3-9-1-5-1-2) one are equipped in the middle part of dispersion tooth fourth (3-9-1-5-1-1)
End is fixed with dispersion tooth fourth (3-9-1-5-1-1), and the other end is fixed with dispersion main shaft (3-9-1-5-3);
Outer scattered motor drives dispersion main shaft (3-9-1-5-3) to rotate by disperseing driving wheel (3-9-1-5-2), and then drives
Four groups of dispersion tooth (3-9-1-5-1) rotations, realize the dispersion to material.
2. a kind of air inlet amount controller in dewatered sludge processing equipment according to claim 1, which 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) pushes 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);Slideway (the 3-
2) cross section is in " Ω " shape, and slideway (3-2) quantity is 2;The sliding block (3-3) is slidably connected with slideway (3-2), sliding block
The end (3-3) is provided with slide motor (3-8), and slide motor (3-8) driving sliding block (3-3) slides on slideway (3-2);It is described
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 regulating motor transmission
Axis 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 pressure
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) with
The one end hydraulic cylinder (3-6) conduit connection;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;The speed regulating motor (3-4), hydraulic cylinder
(3-6), it pushes disk (3-7) central axis in the same horizontal line, disk (3-7) is pushed to be connect with rolling cutter (7), push disk
(3-7) drives rolling cutter (7) 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 air inlet amount controller in dewatered sludge processing equipment according to claim 2, which 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
It manages (7-5), cutting edge nozzle (7-6), water inlet pipe (7-7), intakes port (7-8), transmission shaft (7-9);Positioned at the driven of one end
It takes turns (7-1), is connect with external cutter motor, meanwhile, driven wheel (7-1) is fixedly connected with transmission shaft (7-9);In driven wheel
Back-up roller bearing (7-4) is equipped on the inside of (7-1), back-up roller bearing (7-4) quantity is 2, is located at transmission shaft (7-9)
Both ends;Transmission shaft (7-9) hollow structure, is internally provided with transformer (7-2), heating tube (7-5), water inlet pipe (7-7);Into
Water 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 port (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) spiral shell
Revolve structure, heating tube one end (7-5) is connected to by conducting wire with transformer (7-2), the other end of transformer (7-2) by conducting wire and
External city's electrical connection, heating tube (7-5) are implemented to heat to water inlet pipe (7-7), and transformer (7-2) is implemented to adjust to heating temperature;
Cutting edge (7-3) is equipped with outside the transmission shaft (7-9), cutting edge (7-3) quantity is 4,4 cutting edges (7-3) angularly, in
Mandrel symmetric mode is fixed on transmission shaft (7-9);It is equipped with cutting edge nozzle (7-6), cutting edge spray in the root cutting edge (7-3)
Head (7-6) open at one end designs and is directed toward cutting edge (7-3) knife face, and cutting edge nozzle (7-6) other end connects with water inlet pipe (7-7)
It is logical;
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 air inlet amount controller in dewatered sludge processing equipment according to claim 3, which is characterized in 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 exchange
Room (3-2-3), partition board (3-2-4), buffered room (3-2-5), refrigerant inlet (3-2-6) export (3-2-7) by coolant liquid,
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 air inlet amount controller in dewatered sludge processing equipment according to claim 4, which is characterized in that
The medicament mixing device (3-2-8) is L-type pipe structure, both ends perforation, and medicament mixing device (3-2-8) 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), agitation ball (3-2-
8-5), stablize net (3-2-8-6), spread 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 air inlet amount controller in dewatered sludge processing equipment according to claim 5, which is characterized in that
The promotion disk brake apparatus (3-9) includes:Brake cooling system (3-9-1), haulage gear (3-9-2), braking 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. a kind of air inlet amount controller in dewatered sludge processing equipment according to claim 6, which is characterized in 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), dispersal device (3-9-1-5), lower open mouth wing plate (3-9-1-6), fence
Plate (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), speedup fan assembly (3-9-1-12), vertical shift device (3-9-1-13);
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 dispersal device (3-9-1-5), dispersal device (3-9-1-5) one at cool room cold air import (3-9-1-4) vertical pivot center
End is connect with external refrigeration room stirring motor, and the other end is fixedly connected with cool room paddle (3-9-1-3);It is stirred in cool room
It mixes the lower part leaf (3-9-1-3) and is equipped with oscillating deck (3-9-1-8), oscillating deck (3-9-1-8) thin-slab structure, single oscillating deck
(3-9-1-8) is horizontal positioned, and oscillating deck (3-9-1-8) quantity is 20,20 oscillating decks (3-9-1-8) be divided into two groups, it is vertical
Arrangement is 10cm with the mutual distance of oscillating deck (3-9-1-8) is organized, and is concatenated with soft rope chain between organizing oscillating deck (3-9-1-8),
And fixed at the top of brake cooling system (3-9-1), with group oscillating deck (3-9-1-8) vacantly at brake cooling system (3-9-1)
At central axes, oscillating deck (3-9-1-8) swings with air-flow;Butterfly plate (3-9-1- is equipped on the right side of oscillating deck (3-9-1-8)
1), butterfly plate (3-9-1-1) thin-slab structure, single butterfly plate (3-9-1-1) are horizontal positioned, and butterfly plate (3-9-1-1) quantity is
20,20 butterfly plates (3-9-1-1) are vertically arranged;Butterfly plate (3-9-1-1) is set there are two arc side wing, two curved sides
Wing plate central symmetry, two arc side wings are connected by butterfly ventilating hole plate (3-9-1-2), and butterfly ventilating hole plate (3-9-1-2) promotees
Inlet air flow forms 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 to place, barrier board (3-9-1-7) is internally provided with a large amount of horizontal grates, and the left and right barrier board (3-9-1-7) is penetrating;In fence
Lower open mouth wing plate (3-9-1-6) is equipped on the left of plate (3-9-1-7), between the two away from for 10cm, lower open mouth wing plate (3-9-1-6) is vertical
Arrangement;
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;
From oily atomizer (3-9-1-10) spray deep fat in brake cooling system (3-9-1) with cool room cold air import
The cold air that (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 equipped with speedup fan assembly (3-9-1-12) on the top the import of cool room cold air (3-9-1-4);
Vertical shift device (3-9-1-13) is located at the side butterfly plate (3-9-1-1), vertical shift device (3-9-1-13) and butterfly
Butterfly plate (3-9-1-1) and butterfly ventilating hole plate (3-9-1-2) are hinged, and vertical shift device (3-9-1-13) drives butterfly plate (3-9-
1-1) moved up and down with butterfly ventilating hole plate (3-9-1-2).
8. a kind of air inlet amount controller in dewatered sludge processing equipment according to claim 7, which 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), center
Gear (4-5), handgrip gear (4-6), lap count (4-7);Wherein, the gear wheel (4-4) is arranged in service chamber (4-2)
Inside, gear wheel (4-4) are interior tooth type hollow structure, and interior teeth are located in gear wheel (4-4) internal circumference, gear wheel (4-
4) central gear (4-5) and handgrip gear (4-6) are equipped in, central gear (4-5), handgrip gear (4-6) are outer toothing;Institute
It states central gear (4-5) to be located at the central axes gear wheel (4-4), handgrip gear (4-6) is surrounded by central gear (4-5),
Gear wheel (4-4), central gear (4-5), handgrip gear (4-6) three engage connection;Handgrip gear (4-6) quantity is three
It is a, it is circumferentially symmetrical around central gear (4-5);The electric rotating machine (4-1) is fixedly mounted on service chamber (4-2) one
Side, electric rotating machine (4-1) are drivingly connected with central gear (4-5);It is another that the workpiece handgrip (4-3) is arranged in service chamber (4-2)
Side, workpiece handgrip one end (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) 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 air inlet amount controller in dewatered sludge processing equipment according to claim 8, which 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), 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);Positioned at swashing for bottom
Flash ranging circle 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
Transceiver (4-7-9) is located at Laser Measuring circle probe (4-7-1) bottom centre, direction is aimed downwardly, Laser emission receiver
(4-7-9) is surrounded by secondary light source (4-7-8), and secondary light source (4-7-8) is 12, and secondary light source (4-7-8) is LE light sources;
The conversion head (4-7-2) is located at the top of Laser Measuring circle probe (4-7-1), the rotary shaft (4- of conversion head (4-7-2) and top
7-7) it is rotatablely connected, meanwhile, Laser Measuring circle probe (4-7-1) is fixedly connected with the rotary shaft (4-7-7) on top;In conversion head
(4-7-2) horizontal direction is equipped with spare Laser Measuring circle and pops one's head in (4-7-11), and quantity is 4, spare Laser Measuring circle probe (4-7-
11) identical as Laser Measuring circle probe (4-7-1) structure, Laser Measuring circle is popped one's head in (4-7-1) and spare Laser Measuring circle probe (4-7-
11) it is Demountable;Rotary shaft (4-7-7) top is equipped with gearbox (4-7-5), is set inside gearbox (4-7-5)
There are deboost axle (4-7-3), deboost axle (4-7-3) to engage connection with rotary shaft (4-7-7) gear;The top gearbox (4-7-5) is set
There are electric rotating machine (4-7-10), electric rotating machine (4-7-10) to engage connection with deboost axle (4-7-3) gear;Gearbox (4-7-5)
Bottom 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 air inlet amount controller in dewatered sludge processing equipment according to claim 9, feature exist
In the workpiece handgrip (4-3) includes:Arm (4-3-1), workpiece slot (4-3-2), banjo traction splint (4-3-3), Workpiece clamping
Spend inductor (4-3-4);Wherein, the workpiece slot (4-3-2) is arranged in the top arm (4-3-1), and workpiece slot (4-3-2) is circle
Connected in star, diameter are 8cm~12cm;Banjo traction splint (4-3-3) quantity is three, and circumference is equally distributed on work
Around part 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 air door plate (3-9-1-12-10-5) is molded by high molecular material pressing mold, the composition of air door plate (3-9-1-12-10-5)
Ingredient 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 air door plate (3-9-1-12-10-5), 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 ] 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 air door plate (3-9-1-12-10-5);
The grain size of the silver nano-particle is 138 μm~148 μm;
A kind of working method for the air inlet amount controller in dewatered sludge processing equipment, this method includes following step
Suddenly:
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.
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CN112086376A (en) * | 2019-06-12 | 2020-12-15 | 北京北方华创微电子装备有限公司 | Cooling device and vertical furnace system |
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CN112086376A (en) * | 2019-06-12 | 2020-12-15 | 北京北方华创微电子装备有限公司 | Cooling device and vertical furnace system |
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