PLC dual controls lowering or hoisting gear and its control in a kind of high water-permeable brick production in sponge city
Method
Technical field
The invention belongs to building machinery application, and in particular to PLC dual controls in a kind of high water-permeable brick production in sponge city
Lowering or hoisting gear and its control method.
Background technology
With the propulsion of urbanization process, cell square quantity is continuously increased, and the living standard of people is improved constantly, with building
The corresponding auxiliary facility constantly improve in area, between block, the Condom such as road, square is also more and more.
Granite, Dali are mainly used in the ground in city square, commercial street, pavement, community activity ground, parking lot etc. at present
The fluid-tight material laying such as stone, glazed tile, cement and pitch, the harm in the face of urban environment is very big fluid-tightly.Under
During rain, waterproof ground prevent rainwater directly infiltrate through ground, completely ponding make one trip become very inconvenient;Precious
Expensive water resource has increased the burden of municipal drainage facility finally as drainage pipeline flows away;A large amount of losses of rainwater cause ground
Lower water level is difficult to, and directly influences the health of urban vegetation so that the ground flora in city is difficult to normal growth, increases
Municipal administration greening burden;A large amount of losses of rainwater further increase the arid in city, water shortage problem.
In city square, commercial street, pavement, community activity ground, water-permeable brick is laid, water-permeable brick has permeable spy
Property, but brick body fracture, unfilled corner and breakage is easily produced in the water-permeable brick production for using at present, transport, overall after laying
Cause property is not good enough, and brick body is easily dug so that road surface occurs where often having disappearance fragment of brick, and common water-permeable brick is being taken
Inconvenient when putting, in entrucking and when unloading, it is impossible to quickly loaded and unloaded.
As adopted ordinary red brick fork type elevator in production, its structure rises lifting platform using scissor-type frame for movement
There is higher stability after rising, but adjustable height is limited, and automaticity is relatively low.
As adopted floor tile Telescopic cylindrical lift, its structure uprightly to rise using multistage hydraulic cylinder in production, hydraulic cylinder is high-strength
The material of degree and good mechanical performance, but lack corresponding safety prevention measure, safety coefficient is relatively low.
Content of the invention
In order to solve above-mentioned technical problem, the present invention provides PLC dual controls lifting in a kind of high water-permeable brick production in sponge city
Device, including:Movable pulley 1, frame 2, operating platform 3, master control box 4, elevating mechanism 5;The movable pulley 1 is located at 2 bottom of frame,
Movable pulley 1 carries brake gear with 2 bottom Corner Strapped welding of frame, movable pulley 1;The frame 2 is stainless by high intensity rectangle
Steel pipe is fixed and is welded, and the stainless steel tube thickness is between 6cm~8cm;The operating platform 3 is arranged at 2 inframe of frame,
Operating platform 3 does lifting by elevating mechanism 5 in 2 inframe of frame and moves back and forth;The master control box 4 is arranged on is easy to staff
The ground location of operation.
Further, the operating platform 3 includes:Guard rail 3-1, dodge gate 3-2, safety lock 3-3, field control case 3-
4, storage tank 3-5, bearing platform 3-6, horizontal equilibrium detector 3-7;Wherein described bearing platform 3-6 be rectangle steel manganese plate, its thickness
Between 3cm~5cm;The guard rail 3-1 is arranged in bearing platform 3-6 length directions both sides and width side, guard rail
3-1 bottoms are welded and fixed with bearing platform 3-6 edges;The dodge gate 3-2 is located at bearing platform 3-6 width opposite sides, activity
With guard rail 3-1 by movable axis chain connection, dodge gate 3-2 opposite sides are by being fixed on guard rail 3-1 for door 3-2 sides
Safety lock 3-3 is fixedly connected with guard rail 3-1;The field control case 3-4 is weldingly fixed on guard rail 3-1 sides;The storage
Thing case 3-5 is fixedly connected with guard rail 3-1;The horizontal equilibrium detector 3-7 quantity is 2, is fixedly connected on bearing platform 3-6
Bottom;
The safety lock 3-3, horizontal equilibrium detector 3-7 are connected with field control case 3-4 controls by wire respectively.
Further, the elevating mechanism 5 includes:Variable-frequency motor 5-1, one-level driving wheel 5-2, two grades of driving wheel 5-3, limit
Fast device 5-4, support platform 5-5, special belt pulley 5-6, sliding bar 5-7, one-level driven pulley 5-8, two grades of driven pulley 5-9 test the speed
Inductor 5-10;Wherein described support platform 5-5 is fixedly connected at the top of frame 2;The one-level driving wheel 5-2 is fixedly connected on
Support platform 5-5 side, one-level driving wheel 5-2 one end and variable-frequency motor 5-1 drive connections, the one-level driving wheel 5-2 other ends are led to
Cross the axis of rolling and roll with two grades of driving wheel 5-3 and be connected;The limiter of speed 5-4 is fixedly connected one-level driving wheel 5-2 sides;Described one
Level driven pulley 5-8 is located at 2 bottom of frame, and one-level driven pulley 5-8 is slided by special belt pulley 5-6 and one-level driving wheel 5-2 and connected
Connect;Two grades of driven pulley 5-9 and one-level driven pulley 5-8 central axis coaxials, two grades of driven pulley 5-9 pass through special belt pulley 5-
6 are slidably connected with two grades of driving wheel 5-3;The inductor 5-10 that tests the speed is fixedly connected on one-level driven pulley 5-8 sides;The cunning
Lever 5-7 top is welded and fixed with support platform 5-5, and sliding bar 5-7 bottoms are fixedly connected with operating platform 3;
The variable-frequency motor 5-1, limiter of speed 5-4, the inductor 5-10 that tests the speed are connected by wire and field control case 3-4 controls respectively
Connect.
Further, warning device is provided with the field control case 3-4.
Further, the field control case 3-4 is connected with the control of master control box 4 by connection, and field control case 3-4 is controlled
The live electric elements of system connection are connected by the control of master control box 4 simultaneously.
Further, the special belt pulley 5-6 is molded by macromolecular material pressing mold, the composition of special belt pulley 5-6 into
Divide and manufacture process is as follows:
First, special belt pulley 5-6 constituents:
Count by weight, 26~62 parts of Alkylphenyl polyoxyethylene ether sufate salts, nonylphenol polyoxyethylene ether sulfate
(NPES) 78~136 parts, 100~150 parts of sodium octyphenol polyoxyethylene ether allyl sulfosuccinic diester, two-(2- ethyl hexyls
Base polyoxygenated alkene) 61~144 parts of sodium sulfosuccinic diester, ethoxylated dodecyl alcohol (n) hexyl butanedioic acid mixing dibasic acid esters
14~52 parts of sodium sulfonate, 83~162 parts of tridecanol polyoxyethylene (3) ether sulfosuccinic acid monoester disodium salt, concentration be 76ppm~
122~163 parts of the secondary alcohol polyoxyethylene ether sulfosuccinic acid disodium of 133ppm, sulfosuccinic acid AEO (3)
77~155 parts of base hexyl mixing diesteras, 128~176 parts of ethoxylation cottonseed oil alkane acid amides mono sulfosuccinates,
105~149 parts of crosslinking agent, 5- [(3- chlorphenyls) azo] -1,2- dihydro -6- hydroxyl -4- methyl -2- oxo -1- phenylamino -3- pyrroles
64~138 parts of pyridine nitrile, 1- butyl -5- [(the chloro- 2- nitre phenyl of 4-) azo] -1,2- dihydro -6- hydroxy-4-methyl -2- oxygen nicotine
152~207 parts of nitrile, 1,2- dihydro -6- hydroxy-4-methyl -5- [(4- aminomethyl phenyls) azo] -2- oxygen -3- pyridine nitriles 34~87
Part, 6- amino -5- (2- cyano group -4- nitrophenylazo groups) -2- [[3- (4- hydroxybutoxies) propyl group] amino] -4- methyl -
114~185 parts of 3- pyridine carbonitriles;
The crosslinking agent be N- (4- hydroxyl -2- anisyls) acetamide, N- (3- hydroxyl -2- naphthoyls) to ethoxybenzene
Any one in amine, 2- hydroxy-N-methvl antifebrins;
2nd, the manufacture process of special belt pulley 5-6, comprises the steps of:
1st step:Add 869~1460 parts of the ultra-pure water that electrical conductivity is 12.55 μ S/cm~18.46 μ S/cm in a kettle., open
Agitator in dynamic reactor, rotating speed are 83rpm~145rpm, start heat pump, make reactor temperature rise to 62 DEG C~94
℃;Sequentially add Alkylphenyl polyoxyethylene ether sufate salts, nonylphenol polyoxyethylene ether sulfate (NPES), octyl phenol polyoxy second
Alkene ether allyl succinic acid diester sodium sulfonate, stirs to being completely dissolved, and it is 3.8~8.4 to adjust pH value, and agitator speed is adjusted to
157rpm~220rpm, temperature are 135 DEG C~181 DEG C, esterification 5~13 hours;
2nd step:Take two-(2- ethylhexyl polyoxygenated alkene) sodium sulfosuccinic diesters, ethoxylated dodecyl alcohol (n) hexyl
Butanedioic acid mixing dibasic acid esters sodium sulfonate is crushed, and powder diameter is 2500~3700 mesh;Add tridecanol polyoxyethylene (3) ether sulphur
Base monomester succinate disodium salt is well mixed, and is laid in pallet, and tiling thickness is 16mm~28mm, adopts dosage for 19kGy
The alpha ray irradiation 111~164 minutes of~34kGy, energy for 28MeV~42MeV, and the β x ray irradiation xs 77 of Isodose~
122 minutes;
3rd step:It is dissolved in secondary alcohol polyoxyethylene ether sulfosuccinic acid disodium through the mixed-powder of the 2nd step process, adds reactor,
Agitator speed be 108rpm~159rpm, temperature be 93 DEG C~147 DEG C, start vavuum pump make the vacuum of reactor reach-
0.18MPa~1.42MPa, keeps this state response 18~26 hours;Pressure release is simultaneously passed through radon gas, makes the reacting kettle inner pressure be
0.59MPa~1.67MPa, insulation stand 7~16 hours;Agitator speed is promoted to 182rpm~247rpm, simultaneous reactions kettle
Pressure release is to 0MPa;Sequentially add sulfosuccinic acid AEO (3) base hexyl mixing diesteras, ethoxylation cottonseed
After oily alkane acid amides mono sulfosuccinates are completely dissolved, crosslinking agent stirring mixing is added so that the parent of reactor solution
Hydrophile-lipophile balance value is 4.1~9.5, and insulation stands 19~27 hours;
4th step:Agitator speed be 283rpm~342rpm when, sequentially add 5- [(3- chlorphenyls) azo] -1,2- dihydros -
6- hydroxyl -4- methyl -2- oxo -1- phenylamino -3- pyridine nitriles, 1- butyl -5- [(the chloro- 2- nitre phenyl of 4-) azo] -1,2- dihydros -
6- hydroxy-4-methyl -2- oxygen nicotine nitriles, 1,2- dihydro -6- hydroxy-4-methyl -5- [(4- aminomethyl phenyls) azo] -2- oxygen -3-
Pyridine nitrile and 6- amino -5- (2- cyano group -4- nitrophenylazo groups) -2- [[3- (4- hydroxybutoxies) propyl group] amino] -4-
Methyl -3- pyridine carbonitriles, lift reactor pressure so as to reach 2.9MPa~4.7MPa, and temperature is 175 DEG C~217 DEG C, polymerization
Reaction 16~24 hours;Reacting kettle inner pressure is down to 0MPa after the completion of reaction, 31 DEG C~43 DEG C are cooled to, is discharged, is entered pressing mold
Machine can be prepared by special belt pulley 5-6.
Further, the invention also discloses in a kind of production of the high water-permeable brick in sponge city PLC dual control lowering or hoisting gears control
Method processed, the method include following step:
1st step:Operating personnel moves the device into and treats operating area, and fixes the brake gear on movable pulley 1;
2nd step:Operating personnel connects 4 power supply of master control box, by another staff in 4 each data mode of ground monitoring master control box;
Operating personnel is entered on operating platform 3, is connected field control case 3-4 power supplys on guard rail 3-1, and is locked safety lock 3-3,
Dodge gate 3-2 is made to be fixed on guard rail 3-1;Safety lock 3-3 is sent to locking information after field control case 3-4, operation people
Member presses the start button on field control case 3-4, starts the variable-frequency motor 5-1 being located at the top of frame 2;
3rd step:One-level driving wheel 5-2 is done with one-level driven pulley 5-8 by special belt pulley 5-6 under variable-frequency motor 5-1 drivings
Rolling movement, meanwhile, two grades of driving wheel 5-3 under the drive of one-level driving wheel 5-2, by special belt pulley 5-6 and two grades from
Driving wheel 5-9 does rolling movement, and operating platform 3 does ascending motion along sliding bar 5-7 under special belt pulley 5-6 drives;When reaching
During operation height, operating personnel presses the stop button on field control case 3-4, and field control case 3-4 stops variable-frequency motor 5-1
4th step:In special belt pulley 5-6 sliding processes, the inductor 5-10 that tests the speed on one-level driven pulley 5-8 is to Special belt
The speed real-time monitoring of wheel 5-6;When the speed that the inductor 5-10 that tests the speed detects special belt pulley 5-6 is higher than 3.5m/s, survey
Feedback signal is sent to field control case 3-4 by fast inductor 5-10, and field control case 3-4 control variable-frequency motor 5-1 are adjusted and turned
Speed, so that reduce speed;
5th step:The limiter of speed 5-4 on one-level driving wheel 5-2 is located to special belt pulley 5-6 instantaneous acceleration real-time monitorings;When
When limiter of speed 5-4 detects special belt pulley 5-6 instantaneous acceleration moments and increases, the warning device on field control case 3-4 is sent out
Go out alarm signal, the staff positioned at ground presses rapidly the scram button in master control box 4, jerk variable-frequency motor 5-1;
6th step:The horizontal equilibrium detector 3-7 of bearing platform 3-6 bottoms is located to bearing platform 3-6 level angle real-time monitorings;When
When horizontal equilibrium detector 3-7 detects bearing platform 3-6 level angles more than 30 °, horizontal equilibrium detector 3-7 is by feedback signal
Field control case 3-4 is sent to, the warning device on field control case 3-4 sends alarm signal, positioned at the staff on ground
Scram button master control box 4 in, jerk variable-frequency motor 5-1 are pressed rapidly.
PLC dual control lowering or hoisting gears in a kind of high water-permeable brick production in sponge city disclosed by the invention, have an advantage in that:
(1) device is controlled using PLC, and high degree of automation is easy to operate;
(2) device is provided with two kinds of control modes of field control and ground master control, when there are emergency situations, ground master control
System can be fixed a breakdown in time, and safety coefficient is high;
(3) device arranges speed limiter and speed measuring device, to elevating mechanism running state real-time monitoring, it is ensured that operating personnel pacifies
Work is effectively completed entirely.
PLC dual control lowering or hoisting gears in a kind of high water-permeable brick production in sponge city of the present invention, the plant automation journey
Degree is high, realizes scene and ground dual control, arranges speed limiter and speed measuring device, real-time monitoring elevating mechanism running status, safety
Coefficient is high.
Description of the drawings
Fig. 1 is PLC dual control lowering or hoisting gear schematic diagrames in a kind of high water-permeable brick production in heretofore described sponge city.
Fig. 2 is heretofore described operating platform structural representation.
Fig. 3 is heretofore described elevating mechanism structural representation.
Fig. 4 is heretofore described special belt pulley material corrosion resistant erosion degree with use time variation diagram.
In figure 1 above~Fig. 3, movable pulley 1, frame 2, operating platform 3, guard rail 3-1, dodge gate 3-2, safety lock 3-3,
Field control case 3-4, storage tank 3-5, bearing platform 3-6, horizontal equilibrium detector 3-7, master control box 4, elevating mechanism 5, variable-frequency electric
Machine 5-1, one-level driving wheel 5-2, two grades of driving wheel 5-3, limiter of speed 5-4, support platform 5-5, special belt pulley 5-6, sliding bar
5-7, one-level driven pulley 5-8, two grades of driven pulley 5-9, test the speed inductor 5-10.
Specific embodiment
With reference to the accompanying drawings and examples to PLC dual control liters in a kind of high water-permeable brick production in the sponge city for providing of the invention
Falling unit is further described.
As shown in figure 1, being that PLC dual control lowering or hoisting gears show in a kind of high water-permeable brick production in heretofore described sponge city
It is intended to.It is seen in fig. 1, that including:Movable pulley 1, frame 2, operating platform 3, master control box 4, elevating mechanism 5;The movable pulley 1
In 2 bottom of frame, movable pulley 1 carries brake gear with 2 bottom Corner Strapped welding of frame, movable pulley 1;The frame 2 is by height
Intensity rectangle stainless steel tube is fixed and is welded, and the stainless steel tube thickness is between 6cm~8cm;The operating platform 3 is arranged
In 2 inframe of frame, operating platform 3 does lifting by elevating mechanism 5 in 2 inframe of frame and moves back and forth;The master control box 4 is arranged on
It is easy to the ground location of operated by personnel.
As shown in Fig. 2 being heretofore described operating platform structural representation.Find out from Fig. 2 or Fig. 1, operation is flat
Platform 3 includes:Guard rail 3-1, dodge gate 3-2, safety lock 3-3, field control case 3-4, storage tank 3-5, bearing platform 3-6, level
Balanced detector 3-7;Wherein described bearing platform 3-6 is rectangle steel manganese plate, and its thickness is between 3cm~5cm;The guard rail 3-
1 is arranged in bearing platform 3-6 length directions both sides and width side, and guard rail 3-1 bottoms are solid with the welding of bearing platform 3-6 edges
Fixed;The dodge gate 3-2 is located at bearing platform 3-6 width opposite sides, and dodge gate 3-2 sides are with guard rail 3-1 by activity
Pivot hinge connects, and dodge gate 3-2 opposite sides are fixed by the safety lock 3-3 and guard rail 3-1 being fixed on guard rail 3-1 and connected
Connect;The field control case 3-4 is weldingly fixed on guard rail 3-1 sides;The storage tank 3-5 is fixedly connected with guard rail 3-1;
The horizontal equilibrium detector 3-7 quantity is 2, is fixedly connected on bearing platform 3-6 bottoms;
The safety lock 3-3, horizontal equilibrium detector 3-7 are connected with field control case 3-4 controls by wire respectively.
Warning device is provided with the field control case 3-4.
The field control case 3-4 is connected with the control of master control box 4 by connection, field control case 3-4 control connections
Live electric elements are connected by the control of master control box 4 simultaneously.
As shown in figure 3, being heretofore described elevating mechanism structural representation.Find out from Fig. 3 or Fig. 2 or Fig. 1, rise
Descending mechanism 5 includes:Variable-frequency motor 5-1, one-level driving wheel 5-2, two grades of driving wheel 5-3, limiter of speed 5-4, support platform 5-5, specially
Belt pulley 5-6, sliding bar 5-7, one-level driven pulley 5-8, two grades of driven pulley 5-9 are used, test the speed inductor 5-10;Wherein described support
Platform 5-5 is fixedly connected at the top of frame 2;The one-level driving wheel 5-2 is fixedly connected on support platform 5-5 side, one-level master
Driving wheel 5-2 one end and variable-frequency motor 5-1 drive connections, the one-level driving wheel 5-2 other ends are by the axis of rolling and two grades of driving wheel 5-3
Roll connection;The limiter of speed 5-4 is fixedly connected one-level driving wheel 5-2 sides;The one-level driven pulley 5-8 is located at 2 bottom of frame
Portion, one-level driven pulley 5-8 are slidably connected with one-level driving wheel 5-2 by special belt pulley 5-6;Two grades of driven pulley 5-9 with
One-level driven pulley 5-8 central axis coaxials, two grades of driven pulley 5-9 are slided and are connected by special belt pulley 5-6 and two grades of driving wheel 5-3
Connect;The inductor 5-10 that tests the speed is fixedly connected on one-level driven pulley 5-8 sides;The sliding bar 5-7 tops and support platform
5-5 is welded and fixed, and sliding bar 5-7 bottoms are fixedly connected with operating platform 3;
The variable-frequency motor 5-1, limiter of speed 5-4, the inductor 5-10 that tests the speed are connected by wire and field control case 3-4 controls respectively
Connect.
In a kind of high water-permeable brick production in sponge city of the present invention, the course of work of PLC dual control lowering or hoisting gears is:
1st step:Operating personnel moves the device into and treats operating area, and fixes the brake gear on movable pulley 1;
2nd step:Operating personnel connects 4 power supply of master control box, by another staff in 4 each data mode of ground monitoring master control box;
Operating personnel is entered on operating platform 3, is connected field control case 3-4 power supplys on guard rail 3-1, and is locked safety lock 3-3,
Dodge gate 3-2 is made to be fixed on guard rail 3-1;Safety lock 3-3 is sent to locking information after field control case 3-4, operation people
Member presses the start button on field control case 3-4, starts the variable-frequency motor 5-1 being located at the top of frame 2;
3rd step:One-level driving wheel 5-2 is done with one-level driven pulley 5-8 by special belt pulley 5-6 under variable-frequency motor 5-1 drivings
Rolling movement, meanwhile, two grades of driving wheel 5-3 under the drive of one-level driving wheel 5-2, by special belt pulley 5-6 and two grades from
Driving wheel 5-9 does rolling movement, and operating platform 3 does ascending motion along sliding bar 5-7 under special belt pulley 5-6 drives;When reaching
During operation height, operating personnel presses the stop button on field control case 3-4, and field control case 3-4 stops variable-frequency motor 5-1
4th step:In special belt pulley 5-6 sliding processes, the inductor 5-10 that tests the speed on one-level driven pulley 5-8 is to Special belt
The speed real-time monitoring of wheel 5-6;When the speed that the inductor 5-10 that tests the speed detects special belt pulley 5-6 is higher than 3.5m/s, survey
Feedback signal is sent to field control case 3-4 by fast inductor 5-10, and field control case 3-4 control variable-frequency motor 5-1 are adjusted and turned
Speed, so that reduce speed;
5th step:The limiter of speed 5-4 on one-level driving wheel 5-2 is located to special belt pulley 5-6 instantaneous acceleration real-time monitorings;When
When limiter of speed 5-4 detects special belt pulley 5-6 instantaneous acceleration moments and increases, the warning device on field control case 3-4 is sent out
Go out alarm signal, the staff positioned at ground presses rapidly the scram button in master control box 4, jerk variable-frequency motor 5-1;
6th step:The horizontal equilibrium detector 3-7 of bearing platform 3-6 bottoms is located to bearing platform 3-6 level angle real-time monitorings;When
When horizontal equilibrium detector 3-7 detects bearing platform 3-6 level angles more than 30 °, horizontal equilibrium detector 3-7 is by feedback signal
Field control case 3-4 is sent to, the warning device on field control case 3-4 sends alarm signal, positioned at the staff on ground
Scram button master control box 4 in, jerk variable-frequency motor 5-1 are pressed rapidly.
PLC dual control lowering or hoisting gears in a kind of high water-permeable brick production in sponge city of the present invention, the plant automation journey
Degree is high, realizes scene and ground dual control, arranges speed limiter and speed measuring device, real-time monitoring elevating mechanism running status, safety
Coefficient is high.
The embodiment of the manufacture process of special belt pulley 5-6 of the present invention is the following is, embodiment is in order to furtherly
Bright present disclosure, but should not be construed as limiting the invention.Without departing from the spirit and substance of the case in the present invention, right
Modification and replacement that the inventive method, step or condition are made, belong to the scope of the present invention.
If not specializing, the conventional meanses that technological means used is well known to those skilled in the art in embodiment.
Embodiment 1
Special belt pulley 5-6 of the present invention is manufactured according to following steps, and is counted by weight:
1st step:Add 869 parts of the ultra-pure water that electrical conductivity is 12.55 μ S/cm in a kettle., start agitator in reactor, turn
Speed is 83rpm, starts heat pump, makes reactor temperature rise to 62 DEG C;Sequentially add polyoxyethylene alkylphenol ether sulfuric acid
26 parts of sodium, 78 parts of nonylphenol polyoxyethylene ether sulfate (NPES), OPEO allyl succinic acid diester sulfonic acid
100 parts of sodium, stirs to being completely dissolved, and it is 3.8 to adjust pH value, and agitator speed is adjusted to 157rpm, and temperature is 135 DEG C, esterification
Reaction 5 hours;
2nd step:Take two-(2- ethylhexyl polyoxygenated alkene) 61 parts of sodium sulfosuccinic diesters, ethoxylated dodecyl alcohol (n)
14 parts of hexyl butanedioic acid mixing dibasic acid esters sodium sulfonate is crushed, and powder diameter is 2500 mesh;Add tridecanol polyoxyethylene (3) ether
83 parts of mono sulfosuccinates are well mixed, and are laid in pallet, tiling thickness be 16mm, adopt dosage for 19kGy,
Alpha ray irradiation 111 minute of the energy for 28MeV, and β x ray irradiation xs of Isodose 77 minutes;
3rd step:The secondary alcohol polyoxyethylene ether sulfosuccinic acid disodium that concentration is 76ppm is dissolved in through the mixed-powder of the 2nd step process
In 122 parts, reactor is added, agitator speed is 108rpm, and temperature is 93 DEG C, and starting vavuum pump reaches the vacuum of reactor
To -0.18MPa, this state response is kept 18 hours;Pressure release is simultaneously passed through radon gas, makes reacting kettle inner pressure for 0.59MPa, is incubated quiet
Put 7 hours;Agitator speed is promoted to 182rpm, simultaneous reactions kettle pressure release to 0MPa;Sequentially add sulfosuccinic acid fatty alcohol
77 parts of APEO (3) base hexyl mixing diesteras, ethoxylation cottonseed oil alkane acid amides mono sulfosuccinates 128
After part is completely dissolved, 105 parts of stirring mixing of crosslinking agent are added so that the hydrophilic lipophilic balance of reactor solution is 4.1, insulation
Stand 19 hours;
4th step:When agitator speed is 283rpm, 5- [(3- chlorphenyls) azo] -1,2- dihydro -6- hydroxyl -4- are sequentially added
64 parts of methyl -2- oxo -1- phenylamino -3- pyridine nitriles, 1- butyl -5- [(the chloro- 2- nitre phenyl of 4-) azo] -1,2- dihydro -6-
152 parts of hydroxy-4-methyl -2- oxygen nicotine nitrile, 1,2- dihydro -6- hydroxy-4-methyl -5- [(4- aminomethyl phenyls) azo] -2- oxygen -
34 parts of 3- pyridine nitriles, 6- amino -5- (2- cyano group -4- nitrophenylazo groups) -2- [[3- (4- hydroxybutoxies) propyl group] ammonia
Base] 114 parts of -4- methyl -3- pyridine carbonitriles, lift reactor pressure so as to reach 2.9MPa, temperature is 175 DEG C, polymerisation
16 hours;Reacting kettle inner pressure is down to 0MPa after the completion of reaction, 31 DEG C are cooled to, discharge, enter molding press can be prepared by special
Belt pulley 5-6;
The crosslinking agent is N- (4- hydroxyl -2- anisyls) acetamide.
Embodiment 2
Special belt pulley 5-6 of the present invention is manufactured according to following steps, and is counted by weight:
1st step:Add 1460 parts of the ultra-pure water that electrical conductivity is 18.46 μ S/cm in a kettle., start agitator in reactor,
Rotating speed is 145rpm, starts heat pump, makes reactor temperature rise to 94 DEG C;Sequentially add polyoxyethylene alkylphenol ether sulphur
62 parts of sour sodium, 136 parts of nonylphenol polyoxyethylene ether sulfate (NPES), OPEO allyl succinic acid diester sulphur
150 parts of sour sodium, stirs to being completely dissolved, and it is 8.4 to adjust pH value, and agitator speed is adjusted to 220rpm, and temperature is 181 DEG C, ester
Change reaction 13 hours;
2nd step:Take two-(2- ethylhexyl polyoxygenated alkene) 144 parts of sodium sulfosuccinic diesters, ethoxylated dodecyl alcohol
N 52 parts of () hexyl butanedioic acid mixing dibasic acid esters sodium sulfonate is crushed, powder diameter is 3700 mesh;Add tridecanol polyoxyethylene
(3) 162 parts of ether sulfosuccinic acid monoester disodium salt is well mixed, and is laid in pallet, tiling thickness be 28mm, adopt dosage for
The alpha ray irradiation 164 minutes of 34kGy, energy for 42MeV, and β x ray irradiation xs of Isodose 122 minutes;
3rd step:The secondary alcohol polyoxyethylene ether sulfosuccinic acid disodium that concentration is 133ppm is dissolved in through the mixed-powder of the 2nd step process
In 163 parts, reactor is added, agitator speed is 159rpm, and temperature is 147 DEG C, and starting vavuum pump makes the vacuum of reactor
1.42MPa is reached, this state response is kept 26 hours;Pressure release is simultaneously passed through radon gas, makes reacting kettle inner pressure for 1.67MPa, insulation
Stand 16 hours;Agitator speed is promoted to 247rpm, simultaneous reactions kettle pressure release to 0MPa;Sequentially add sulfosuccinic acid fat
155 parts of alcohol APEO (3) base hexyl mixing diesteras, ethoxylation cottonseed oil alkane acid amides mono sulfosuccinates
After 176 parts are completely dissolved, 149 parts of stirring mixing of crosslinking agent are added so that the hydrophilic lipophilic balance of reactor solution is 9.5,
Insulation stands 27 hours;
4th step:When agitator speed is 342rpm, 5- [(3- chlorphenyls) azo] -1,2- dihydro -6- hydroxyl -4- are sequentially added
138 parts of methyl -2- oxo -1- phenylamino -3- pyridine nitriles, 1- butyl -5- [(the chloro- 2- nitre phenyl of 4-) azo] -1,2- dihydro -6-
207 parts of hydroxy-4-methyl -2- oxygen nicotine nitrile, 1,2- dihydro -6- hydroxy-4-methyl -5- [(4- aminomethyl phenyls) azo] -2- oxygen -
87 parts of 3- pyridine nitriles, 6- amino -5- (2- cyano group -4- nitrophenylazo groups) -2- [[3- (4- hydroxybutoxies) propyl group] ammonia
Base] 185 parts of -4- methyl -3- pyridine carbonitriles, lift reactor pressure so as to reach 4.7MPa, temperature is 217 DEG C, polymerisation
24 hours;Reacting kettle inner pressure is down to 0MPa after the completion of reaction, 43 DEG C are cooled to, discharge, enter molding press can be prepared by special
Belt pulley 5-6;
The crosslinking agent is 2- hydroxy-N-methvl antifebrins.
Embodiment 3
Special belt pulley 5-6 of the present invention is manufactured according to following steps, and is counted by weight:
1st step:Add 1120 parts of the ultra-pure water that electrical conductivity is 15.44 μ S/cm in a kettle., start agitator in reactor,
Rotating speed is 113rpm, starts heat pump, makes reactor temperature rise to 76 DEG C;Sequentially add polyoxyethylene alkylphenol ether sulphur
46 parts of sour sodium, 108 parts of nonylphenol polyoxyethylene ether sulfate (NPES), OPEO allyl succinic acid diester sulphur
125 parts of sour sodium, stirs to being completely dissolved, and it is 5.3 to adjust pH value, and agitator speed is adjusted to 192rpm, and temperature is 160 DEG C, ester
Change reaction 9 hours;
2nd step:Take two-(2- ethylhexyl polyoxygenated alkene) 101 parts of sodium sulfosuccinic diesters, ethoxylated dodecyl alcohol
N 34 parts of () hexyl butanedioic acid mixing dibasic acid esters sodium sulfonate is crushed, powder diameter is 3100 mesh;Add tridecanol polyoxyethylene
(3) 123 parts of ether sulfosuccinic acid monoester disodium salt is well mixed, and is laid in pallet, tiling thickness be 22mm, adopt dosage for
The alpha ray irradiation 136 minutes of 26kGy, energy for 35MeV, and β x ray irradiation xs of Isodose 102 minutes;
3rd step:The secondary alcohol polyoxyethylene ether sulfosuccinic acid disodium that concentration is 106ppm is dissolved in through the mixed-powder of the 2nd step process
In 142 parts, reactor is added, agitator speed is 133rpm, and temperature is 118 DEG C, and starting vavuum pump makes the vacuum of reactor
0.92MPa is reached, this state response is kept 22 hours;Pressure release is simultaneously passed through radon gas, makes reacting kettle inner pressure for 1.22MPa, insulation
Stand 11 hours;Agitator speed is promoted to 212rpm, simultaneous reactions kettle pressure release to 0MPa;Sequentially add sulfosuccinic acid fat
117 parts of alcohol APEO (3) base hexyl mixing diesteras, ethoxylation cottonseed oil alkane acid amides mono sulfosuccinates
After 153 parts are completely dissolved, 125 parts of stirring mixing of crosslinking agent are added so that the hydrophilic lipophilic balance of reactor solution is 6.8,
Insulation stands 23 hours;
4th step:When agitator speed is 313rpm, 5- [(3- chlorphenyls) azo] -1,2- dihydro -6- hydroxyl -4- are sequentially added
98 parts of methyl -2- oxo -1- phenylamino -3- pyridine nitriles, 1- butyl -5- [(the chloro- 2- nitre phenyl of 4-) azo] -1,2- dihydro -6-
177 parts of hydroxy-4-methyl -2- oxygen nicotine nitrile, 1,2- dihydro -6- hydroxy-4-methyl -5- [(4- aminomethyl phenyls) azo] -2- oxygen -
59 parts of 3- pyridine nitriles, 6- amino -5- (2- cyano group -4- nitrophenylazo groups) -2- [[3- (4- hydroxybutoxies) propyl group] ammonia
Base] 149 parts of -4- methyl -3- pyridine carbonitriles, lift reactor pressure so as to reach 3.5MPa, temperature is 195 DEG C, polymerisation
20 hours;Reacting kettle inner pressure is down to 0MPa after the completion of reaction, 37 DEG C are cooled to, discharge, enter molding press can be prepared by special
Belt pulley 5-6;
The crosslinking agent is N- (3- hydroxyl -2- naphthoyls) p-ethoxyaniline.
Reference examples
Reference examples are the special belt pulley of certain brand commercially available.
Embodiment 4
Special belt pulley described in the special belt pulley 5-6 that embodiment 1~3 is prepared and reference examples carries out using effect pair
Than.
The two power coefficient, wear-resistant rate, anti-slip degree, deformation ratio are counted, as a result as shown in table 1.
As seen from Table 1, special belt pulley 5-6 of the present invention, its power coefficient, wear-resistant rate, anti-slip degree, deformation
The indexs such as rate are superior to the product of prior art production.
Additionally, as shown in figure 4, being that special belt pulley 5-6 materials corrosion resistant erosion degree of the present invention changes with use time
Statistics.Find out in figure, special belt pulley 5-6 used by embodiment 1~3, its material corrosion resistant erosion degree is with use time intensity of variation
Significantly it is better than existing product.