CN107442481A - Carbon tetrachloride karst deposits gluing roll maintenance unit and its operating method - Google Patents

Carbon tetrachloride karst deposits gluing roll maintenance unit and its operating method Download PDF

Info

Publication number
CN107442481A
CN107442481A CN201710591957.1A CN201710591957A CN107442481A CN 107442481 A CN107442481 A CN 107442481A CN 201710591957 A CN201710591957 A CN 201710591957A CN 107442481 A CN107442481 A CN 107442481A
Authority
CN
China
Prior art keywords
cleaning fluid
spray cleaning
central controller
parts
karst
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN201710591957.1A
Other languages
Chinese (zh)
Inventor
梁峙
张明胜
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Xuzhou University of Technology
Original Assignee
Xuzhou University of Technology
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Xuzhou University of Technology filed Critical Xuzhou University of Technology
Priority to CN201710591957.1A priority Critical patent/CN107442481A/en
Publication of CN107442481A publication Critical patent/CN107442481A/en
Pending legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B08CLEANING
    • B08BCLEANING IN GENERAL; PREVENTION OF FOULING IN GENERAL
    • B08B3/00Cleaning by methods involving the use or presence of liquid or steam
    • B08B3/02Cleaning by the force of jets or sprays
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B08CLEANING
    • B08BCLEANING IN GENERAL; PREVENTION OF FOULING IN GENERAL
    • B08B13/00Accessories or details of general applicability for machines or apparatus for cleaning

Landscapes

  • Cleaning By Liquid Or Steam (AREA)

Abstract

A kind of carbon tetrachloride karst deposits gluing roll maintenance unit and its operating method, automatic flushing device includes support base, it is arranged on the cleaning agent original fluid container and rotary middle spindle on support base top, the rotatable platform for being rotatably connected at rotary middle spindle upper end driven by rotation controlled motor, it is fixedly connected on lift telescopic post peripheral between rotatable platform and support platform, it is fixedly connected on the support post on support platform top, the pivot link that one end is hinged with support post upper end, the angle adjustment catch bar that both ends are hinged with support post and pivot link respectively, liquid device is cleaned with the be hinged spray of the other end of pivot link, the inlet of connection spray cleaning liquid device adds cleaning liquid device with cleaning agent original fluid container upper liquid outlet.Operating method, automatically control automatic spray cleaning fluid head that cleaning fluid is sprayed into dirt position by central controller.The apparatus structure is reasonable, and integrated level is high, and this method is favorably improved the operating efficiency for safeguarding gluing roll.

Description

Carbon tetrachloride karst deposits gluing roll maintenance unit and its operating method
Technical field
The present invention relates to field of environment protection equipment, specifically a kind of carbon tetrachloride karst deposits gluing roll maintenance unit and Its operating method, belong to building structure technology field.
Background technology
Carbon tetrachloride (CCl4) it is a kind of organic chlorohydrocarbon of artificial synthesized low boiling (proportion 1.591g/cm3, boiling point 77 DEG C), it is slightly soluble in water.Foreign study shows:Carbon tetrachloride belongs to typical hepatotoxic agent, is influence maincenter first during high concentration Nervous system, then influence liver, kidney.It has persistence, extended residual and bioconcentration in the environment, therefore certainly " pollutant of priority acccess control in underground water containing carbon tetrachloride " was included in by U.S. EPA in 1979, has also been included in 68 kinds by China " pollutant of priority acccess control in water " list.
Eighties of last century the seventies cause some regional underground water by carbon tetrachloride due to a large amount of manufactures and using agricultural chemicals Pollution, as the water-bearing layer near the Michigan water-bearing layer in the U.S. and Canadian Ottawa by the polluting of carbon tetrachloride ( It exists with nonaqueous phase (NAPL) more in water-bearing layer).
CCl in the municipal water supply for causing Marina is polluted before the U.S. caused by FortordArmy military bases4It is exceeded, In August, 2000 measures CCl4Concentration is up to 15 μ g/L.The groundwater monitoring in U.S. Livermore areas finds poisonous and harmful rubbish Stacking causes CCl4The generation of pollutant, CCl in noxious material percolate4At concentrations up to 500 μ g/L.In April, 2000, Underground water CCl4 concentration is up to 6.3 μ g/L in MW-10 wells near Hafner&Sons refuse landfills.
Existing Treatment process:Carbon tetrachloride is that organic pollutants are common are in soil and groundwater, easily with rainwater or filling Irrigate water by eluviation to enter in soil and groundwater, cause the pollution of soil and groundwater body.At present in relevant underground water The conventional method that Carbon Tetrachloride Contamination is administered has following several:
1. active carbon adsorption
With the carbon tetrachloride in charcoal absorption water source, without adding any chemical reagents, technical requirements are not high, low concentration Advantages of good adsorption effect, some materials for being difficult to degrade can be directly adsorbed on activated carbon.By having investigated activated carbon dosage, having inhaled Influence of the factors such as attached time, temperature to removal effect.
This method technical maturity, effect simple to operate is reliable, but adsorption efficiency is unstable, and carbon tetrachloride is in low concentration timeliness Fruit is good, handles during high concentration unstable, effectively adsorbs short life, and carrier needs to carry out secondary desorption that circulating use could be carried out, And by the solution after solvent desorption, the mixture containing carbon tetrachloride is formed again, how to be isolated again, it is necessary to further grind Study carefully.
2. aeration process repairing method
Compressed air is injected underground water saturated zone by aeration process reparation, causes volatility dirty in the upward motion process of gas Dye thing enters gas phase from the soil body and underground water so that the air containing pollutant rises to unsaturation band, then is extracted by gas phase and be System processing removes the purpose of pollutant so as to reach.Repair the original position of this processing underground water saturated zone volatile organic contaminant Recovering technology, due to can the advantage of construction in situ it is used widely, it is be applied to that molecular weight is smaller, is easily changed into from liquid phase more The pollutant of gas phase.
But aeration process repairing method is easily changed by gas flow shape, number of bubbles, bubble size, gas channel density Influenceed etc. factor, while disposal ability is reduced because handling process is different.Aeration process repairing method in force, if contaminated area In the presence of local hypotonicity soil layer, air is difficult to fully contact with pollutant, if underground water saturated zone occur structural crack or Fracture belt, the air of injection then easily form preferential stream, cause aeration short circuit, greatly influence process range and treatment effect, dirty Dye area hardly results in effective reparation.Aeration process repairing method is also by soil response type, place homogenieity, underground water simultaneously Position and flowing, the water-soluble of pollutant directly affect with volatile so that remediation efficiency declines, cost increase.
3. in situ chemical oxidation method
Oxidant permanganate, Fenton reagent, hydrogen peroxide and persulfate that in-situ chemical recovery technique uses etc..
Oxidant is injected into underground pollution area, soil and water-bearing layer are in itself containing substantial amounts of natural iron mineral, in iron ore Oxidation reaction can the effective organic pollution of rehabilitating soil and underground water in the presence of thing catalysis.Research shows that in-situ chemical is repaiied Recovering technology easily makes reparation area soil produce mineralising, makes reparation area soil hardening, bad hydraulic permeability, changes and repairs area's soil knot Structure.
4. biological restoration
Using bio-inert and organic clay adsorbed bioactive bacterium, by the metabolism of biology, underground environment is reduced In poisonous and harmful compound engineering techniques, biology in situ repairing method can handle large-scale pollutant, and can be complete Full decomposing pollutant.
Biology in situ repairing method is an emerging technology for processing underground water Organic Pollution source at present, biological prosthetic Key factor be suitable electron acceptor, and the oxygen acceptor that has been best electricity, due to lacking oxygen this electricity in underground environment Sub- acceptor, while the supply deficiency of microbial nutrition material, also cause the biodegradation of microorganism from lasting.
5. permeable reactive wall repairing method
Using the dependent response area filled with Active reaction medium material, when contaminated underground water by when, it is therein Polluter occurs the effect such as physics, chemistry and biology with reaction medium and is degraded, adsorbs, precipitates or removes, so that dirty Water is purified.
But permeable coefficient tensor, in the presence of being easily blocked, its native environmental conditions such as oxidation-reduction potential of underground water are subject to brokenly It is bad, it is higher plus bimetallic systems, nanometer technology cost the shortcomings of reaction wall engineering measure and relative complex operation maintenance, this A little factors hinder the further development of permeable coefficient tensor and widelyd popularize.
6. original position aeration repairing method
Aeration process in situ is a kind of based technique for in-situ remediation of emerging underground water volatile organic matter, is injected air into Below Polluted area, volatile organic compounds are resolved to from underground water to air stream and lead to the in-situ immobilization skill handled on ground Art, while enough oxygen can be provided for the aerobic microbiological in underground water to deep well injection air, promote the drop of indigenous microorganism Solution acts on.The technology can handle more Polluted Groundwater in acceptable cost-range, system easily installation and Transfer, easily used with other technical combinations.
But because geologic structure is complicated, when injection air runs into complete rock stratum band, loosening crushed zone or flexural deformation band When, the injection air for carrying volatile organic matter is difficult to penetrate above-mentioned geologic structure, while injects air and run into above-mentioned geology During structure, air drag is big, will cause the device to consumption and greatly improves.Biodegradable pollutant is not easy to being neither easy volatilization Treatment effect is more bad.
With growing, the raising of living standards of the people of industry, the yield of various industrial carbon tetrachloride waste water is also anxious Increase severely plus, this not only make in processing it is increasingly difficult, and if karst deposits contained in carbon tetrachloride waste water without appropriate place Reason is arbitrarily toppled over will more cause secondary destruction to environment.Typically in the processing procedure of carbon tetrachloride waste water karst deposits, Carrying, burning or the landfill of karst deposits are carried out in order to high efficiency and economically, should try one's best and remove institute in karst deposits The moisture contained, to reach the purpose of minimizing and curable type.Therefore, dewatering and filtering is most in karst deposits processing system Important karst deposits minimizing means.
Current most common karst deposits dehydration equipment is filter-press type karst deposits dewaterer (Filter PressMachine).Filter-press type karst deposits dewaterer has karst deposits moisture content height, the rate of filtration is fast, is applied to The advantages that chemical karst water product substance treating method.It is existing to carry out karst deposits using filter-press type karst deposits dewaterer The method of dewater treatment is:Filter plate is compressed by oil gear first, the mistake that may filter that karst deposits is formed between filter plate Filter chamber;Then, high pressure karst deposits pump is recycled to pump karst deposits to filter chamber from karst deposits accumulator tank In, until filter chamber fills karst deposits;Then, the pressure differential formed using the filter cloth on filter plate in filter chamber will Moisture extruding discharge in karst deposits, after the moisture discharge of karst deposits, karst water product will be formed in filter chamber Thing cake;And then separate filter plate using oil gear, karst deposits cake is come off from filter chamber, to reach karst water The purpose of product thing dehydration.
To maintain karst deposits to be dehydrated the performance of gluing roll and reducing moisture content and the reduction of karst deposits cake Karst deposits clears processing cost, after the above step, is generally also taken off using high pressure washing water cleaning karst deposits Water gluing roll, to complete the complete cycle operation of filter-press type karst deposits dewaterer.
But deposited in the program using filter-press type karst deposits dewaterer progress karst deposits dewater treatment In some problems.For example, when the karst deposits of filter-press type karst deposits dewaterer is dehydrated gluing roll through multiple karst water After product thing dehydration procedure, hole on karst deposits dehydration gluing roll will be by karst deposits particle Severe blockage, even The moisture in karst deposits can be caused not filter out, and filter-press type dewatering machine is not worked.It is if clear using high pressure washing water , then must great Fei when karst deposits dehydration gluing roll can not be cleaned up by washing karst deposits dehydration gluing roll Karst deposits dehydration gluing roll is disassembled from filter-press type karst deposits dewaterer with being scared, then carried out again Karst deposits is dehydrated gluing roll etching procedures, so that karst deposits is dehydrated gluing roll recycling.In this process In, existing karst deposits dehydration gluing roll etching procedures are:Need karst deposits dehydration gluing roll dismounting first Get off;Clear water is reused tentatively to clean the dirt of karst deposits dehydration gluing roller surface;Then karst water is accumulated Thing dehydration gluing roll is dipped into 5% or so hydrochloric acid solution at normal temperatures, to utilize the good dissolving power of hydrochloric acid by karst Water product thing is dehydrated the obturator dissolution in gluing roll hole, and the time soaked at least takes 3 days;Afterwards by karst deposits Dehydration gluing roll is cleaned with clear water;Filter-press type rock is reinstalled after its natural air drying, then by karst deposits dehydration gluing roll On molten water product thing dewaterer.
The content of the invention
In view of the above-mentioned problems of the prior art, the present invention provides a kind of carbon tetrachloride karst deposits gluing roll dimension Device and its operating method are repaiied, the maintenance unit lift adjustment is easy, and its flexibility is more preferable, and its is compact-sized, integrated level is high; The operating method can easily realize maintenance process, can effectively reduce the work load of maintenance personal, can help to improve maintenance Efficiency.
To achieve these goals, the present invention provides a kind of carbon tetrachloride karst deposits gluing roll maintenance unit, bag Automatic flushing device and central controller are included, the automatic flushing device includes support base, is arranged on support base bottom Wheel, the cleaning agent original fluid container for being arranged on support base top, the rotary middle spindle for being fixedly arranged at support base top, Be rotatably connected at the rotatable platform of rotary middle spindle upper end, be fixedly connected on rotatable platform top rotation controlled motor, Support platform above rotatable platform, it is fixedly connected on multiple liftings peripheral between rotatable platform and support platform and stretches The be hinged rotation in contracting post, the support post for being fixedly connected on support platform central upper portion region, one end and support post upper end connects Bar, both ends respectively the angle adjustment catch bar be hinged with the middle part of support post and the middle part of pivot link, with pivot link The other end be hinged spray cleaning liquid device, inlet and the high-pressure pump on cleaning agent original fluid container of connection spray cleaning liquid device go out Between liquid mouth plus cleaning liquid device;
The output shaft for rotating controlled motor is equipped with drive gear, the rotation after penetrating rotatably rotatable platform Driven gear is equipped with central shaft, the drive gear engages with driven gear;
The spray cleaning liquid device includes spray cleaning fluid encirclement bar, two-way automatic push-pull bar and leveling hydraulic cylinder, the spray The quantity of cleaning fluid encirclement bar is two, and it is cavity structure that it is internal, and spray cleaning fluid encirclement bar one end is half ring type structure, spray The cleaning fluid encirclement bar other end is staight shank structure, and two spray cleaning fluid encirclement bars are oppositely disposed, and are cut with scissors by rotary positioning pin Connect;Between the two-way automatic push-pull bar is on the inside of two spray cleaning fluid encirclement bar straight handle ends, the two of two-way automatic push-pull bar End is hinged with spray cleaning fluid encirclement bar staight shank one end respectively;It is uniformly arranged on the inside of described half ring-like one end of spray cleaning fluid encirclement bar There are multiple automatic spray cleaning fluid heads with its connects with the internal cavities;The end of the spray cleaning fluid encirclement bar staight shank one end of one of them End is hinged with the one end of pivot link away from support post, middle part and the leveling of the spray cleaning fluid encirclement bar staight shank one end One end of hydraulic cylinder is hinged, and the other end of the leveling hydraulic cylinder and the middle part of pivot link are hinged;
The high-pressure pump, rotate controlled motor, lift telescopic post, angle adjustment catch bar, two-way automatic push-pull bar with Central controller connects.
The apparatus structure compact and reasonable, integrated level are high, and automaticity is high, convenient and swift using process, and karst water is accumulated Thing removal efficiency is high, can be suitably used for different types gluing work roll cooling, meanwhile, it can help to the high efficiency to gluing roll Safeguard, can effectively make a price reduction the work load of attendant.Freely adjusting for height can be carried out by lift telescopic post in the device Whole, flexibility is preferable.The setting of central controller, it can automatically control high-pressure pump, rotate controlled motor, lift telescopic The action of post, angle adjustment catch bar and two-way automatic push-pull bar, maintenance efficiency can be improved, meanwhile, also can be conveniently and efficiently right Gluing roll is safeguarded.
In order to further improve the overall automaticity of device, in addition to adjustable height survey meter, inclination sensor With dirt position inductance gauge, the adjustable height survey meter is located at support platform upper surface, and inclination sensor is arranged on spray cleaning The surface of liquid device, dirt position inductance gauge are arranged at the inner side of half ring-like one end of spray cleaning fluid encirclement bar;Adjustable height detects Instrument, inclination sensor and dirt position inductance gauge are connected with central controller.
Further, the moving process of the device is controlled for convenience, and can be carried out position in time when needed and be fixed, it is described Wheel is automatically controlled steering brake wheel, and wheel is four, is respectively arranged at the corner of support base bottom, four wheels are with Centre controller passes through wireless connection.
Further, manual curved handle has been bolted to connection it for the ease of hand push, described support base one end;Hand push is curved Angle between handle and horizontal plane is between 30 °~75 °;The support base is a rectangular steel plates structure, support base thickness Not less than 10mm;The support platform is a rectangular steel plates structure, and support platform thickness is not less than 5mm;The lift telescopic Post is four groups, and the stroke range value of the lift telescopic post is between 0m~5m;The cleaning agent stoste tank volume 5L~ Between 15L.
Further, for convenience control injection process, it is described plus cleaning liquid device on set respectively loading pump, flowmeter and Electrically-controlled valve, loading pump, flowmeter and the electrically-controlled valve are connected with central controller respectively.
Further, in order that the service life of spray cleaning fluid head is longer automatically, meanwhile, also for more effectively ensureing decoction Effective supply, the automatic spray cleaning fluid head is matched in parts by weight by following components to be formed:The fluoro- 2- chlorine of 1,1,1,2- tetra- 64~144 parts of ethane, 84~144 parts of tetrachlorodifluoroethane, 1,1- 144~454 parts of Difluoroethane, trimethylol melamine 84~194 parts of resin, 74~154 parts of magnetic melamine formaldehyde resin, 2- [[(2'- cyanobiphenyl -4- bases) methyl] ammonia Base] 144~444 parts of -3- ethyl nitrobenzoates, concentration is 54ppm~94ppm 2- [(3- chloro-2-methyls phenyl) amino] 84~144 parts of benzoic acid, ureaformaldehyde -74~144 parts of melamino-formaldehyde compound resin, 3- ketobutyric acids 2- (methyl (phenyl first Base) amino) 74~184 parts of ethyl ester, 94~164 parts of crosslinking agent, the chloro- 2- of 4- [(6- methoxyl group -3- pyridine radicals) amino] benzoic acid 54~144 parts, 94~174 parts of the chloro- 6- methylphenols of 3- amino -2-, the chloro- 3- methylphenols hydrochloride 44 of 6- amino -2,4- bis- ~84 parts, the chloro- N- of 2- (3- methoxyl group -2- thiophene phenyls) -2 ', 54~144 parts of 6 '-dimethylacetamide aniline.
Further, in order to improve the performance of automatic spray cleaning fluid head, the crosslinking agent is 1- Chloro-O-Phenyl -1- phenyl -3- Dimethylamino propanol hydrochloride, 7- amino -3- chlorine cephalosporanic acid benzhydryl esters hydrochloride, 6- (3,5- diaminourea benzene carbon amides Base) any one in n-caproic acid hydrochloride.
Further, in order to improve the performance of automatic spray cleaning fluid head, the manufacturing process of the automatic spray cleaning fluid head is as follows:
Step 1:544~1404 parts of the ultra-pure water that electrical conductivity is the μ S/cm of 0.44 μ S/cm~0.74 is added in a kettle, Start reactor in agitator, rotating speed be 94rpm~444rpm, startup heat pump, make reactor temperature rise to 64 DEG C~ 84℃;Sequentially add 1,1,1,2- tetra- fluoro- 2- chloroethanes, tetrachlorodifluoroethane, 1,1- Difluoroethanes, stirring to being completely dissolved, It is 4.4~7.4 to adjust pH value, agitator speed is adjusted into 144rpm~454rpm, temperature is 94 DEG C~164 DEG C, esterification 44~54 hours;
Step 2:Trimethylol melamine resin, magnetic melamine formaldehyde resin is taken to be crushed, powder diameter For 414~544 mesh;Add 2- [[(2'- cyanobiphenyl -4- bases) methyl] amino] -3- ethyl nitrobenzoates to be well mixed, put down It is laid in pallet, tiling thickness is 44mm~54mm, and it for 4.4kGy~8.4kGy, energy is 4.4MeV~14MeV to use dosage Alpha ray irradiate 54~144 minutes, and β x ray irradiation xs 74~164 minutes of Isodose;
Step 3:The mixed-powder handled through step 2 is dissolved in 2- [(3- chloro-2-methyls phenyl) amino] benzoic acid, is added Enter the reactor in step 1, agitator speed is 84rpm~184rpm, and temperature is 94 DEG C~144 DEG C, and starting vavuum pump makes The vacuum pressure of reactor reaches -0.44MPa~-0.84MPa, keeps this state response 44~54 hours;Pressure release is simultaneously passed through nitrogen Gas, it is 0.44MPa~0.74MPa to make reacting kettle inner pressure, and insulation stands 44~54 hours;Agitator speed is promoted to 114 Rpm~454rpm, simultaneous reactions kettle pressure release to 0MPa;Sequentially add ureaformaldehyde-melamino-formaldehyde compound resin, 3- oxo fourths After sour 2- (methyl (phenyl methyl) amino) ethyl ester is completely dissolved, adds crosslinking agent and be stirred so that the parent of reactor solution Hydrophile-lipophile balance value is 4.4~7.4, and insulation stands 44~54 hours;
Step 4:When agitator speed is 144rpm~464rpm, the chloro- 2- of 4- [(6- methoxyl group -3- pyrroles are sequentially added Piperidinyl) amino] benzoic acid, the chloro- 6- methylphenols of 3- amino -2-, the chloro- 3- methylphenols hydrochlorides of 6- amino -2,4- two, 2- Chloro- N- (3- methoxyl group -2- thiophene phenyls) -2 ', 6 '-dimethylacetamide aniline, reactor pressure is lifted, reaches 0.84MPa ~1.64MPa, temperature are 144 DEG C~474 DEG C, polymerisation 14~24 hours;Reacting kettle inner pressure is down to after the completion of reaction 0MPa, 24 DEG C~34 DEG C are cooled to, discharging, enters molding press and can be prepared by spraying cleaning fluid head automatically.
A kind of operating method of carbon tetrachloride karst deposits gluing roll maintenance unit, comprises the following steps:
Step 1:Automatic flushing device is pushed near gluing roll, is started by central controller and rotates controlled motor Cleaning liquid device will be sprayed to turn to close to the position of gluing roll side;
Step 2:Top is outwards done by the knock-pin of central controller controls angle adjustment catch bar and stretches motion, drives spray Cleaning liquid device moves upwards, and after predetermined altitude is reached, the piston rod by central controller controls leveling hydraulic cylinder is outside Stretch out, to clean liquid device leveling to spray, when inclination sensor detects that spray cleaning liquid device is horizontal, tilt Sensor sends an electric signal, central controller controls angle adjustment catch bar stop motion to central controller;
Step 3:Two-way automatic push-pull bar, two knock-pins point of two-way automatic push-pull bar are started by central controller Top is not done to both ends and stretch motion, drive spray cleaning fluid encirclement bar to be circled by the center of circle of rotary positioning pin, cleaning fluid to be painted The opening of half ring-like one end of encirclement bar be available for gluing roll by when, by central controller controls wheel to close to gluing Roll direction is moved, and when half ring-like one end of cleaning fluid encirclement bar is enclosed in the outside of gluing roll, passes through central controller control Wheel brake processed is fixed with carrying out position, and controls two-way automatic push-pull bar stop motion;
Step 4:Multiple lift telescopic posts are started by central controller and synchronize action, make the top of lift telescopic post Rod does top and stretches motion upwards, and adjustable height survey meter monitors adjustable height and will measure value in real time feeds back to central controller, Then central controller can automatically control the running situation of lift telescopic post when inputting setting height;
Step 5:In lifting process, dirt position inductance gauge detects the dirt position on gluing roll in real time, works as dirt When position inductance gauge detects dirt position, electric signal is fed back to central controller, central controller by dirt position inductance gauge Control plus the loading pump startup cleaned in liquid device, control electrically-controlled valve are opened, while control the high-pressure pump on cleaning agent original fluid container Start, cleaning fluid is pumped in spray cleaning liquid device, and cleaning fluid is sprayed to dirt portion by spraying cleaning fluid head automatically Position, so as to reach scavenging effect.
The operating process can make attendant easily complete the cleaning to gluing roll, can effectively reduce maintenance people The work load of member, meanwhile, it can help to the significantly lifting of maintenance efficiency.
Brief description of the drawings
Fig. 1 is the structural representation of the present invention;
Fig. 2 is the structural representation of automatic flushing device in the present invention;
Fig. 3 is spray cleaning fluid apparatus structure schematic diagram in the present invention;
Fig. 4 is to spray cleaning fluid head material and decontamination enhancing rate graph of a relation in the present invention automatically.
In figure:1st, gluing roll, 2, automatic flushing device, 2-1, support base, 2-2, wheel, 2-3, hand push curved handle, 2- 4th, cleaning agent original fluid container, 2-5, rotatable platform, 2-6, rotary middle spindle, 2-7, rotation controlled motor, 2-8, lift telescopic post, 2-9, support platform, 2-10, support post, 2-11, pivot link, 2-12, angle adjustment catch bar, 2-13, spray cleaning fluid dress Put, 2-13-1, spray cleaning fluid encirclement bar, 2-13-2, rotary positioning pin, 2-13-3, two-way automatic push-pull bar, it is 2-13-4, automatic Cleaning fluid head is sprayed, 2-13-5, dirt position inductance gauge, 2-14, adds and cleans liquid device, 2-15, adjustable height survey meter, 2-16, Leveling hydraulic cylinder, 3, central controller.
Embodiment
The invention will be further described below.
As depicted in figs. 1 and 2, a kind of carbon tetrachloride karst deposits gluing roll maintenance unit, including automatic cleaning dress 2 and central controller 3 are put, the automatic flushing device 2 includes support base 2-1, is arranged on the car of support base 2-1 bottoms Wheel 2-2, it is arranged on the cleaning agent original fluid container 2-4 on support base 2-1 tops, is fixedly arranged at turning for support base 2-1 tops Dynamic central shaft 2-6, it is rotatably connected at the rotatable platform 2-5 of rotary middle spindle 2-6 upper ends, is fixedly connected on rotatable platform The rotation controlled motor 2-7 on 2-5 tops, the support platform 2-9 above rotatable platform 2-5, it is fixedly connected on rotatable platform Peripheral multiple lift telescopic post 2-8 between 2-5 and support platform 2-9, it is fixedly connected on support platform 2-9 central upper portions area The be hinged pivot link 2-11 in the support post 2-10 in domain, one end and support post 2-10 upper ends, both ends respectively with support post It is the be hinged angle adjustment catch bar 2-12 in 2-10 middle part and pivot link 2-11 middle part, another with pivot link 2-11 The be hinged spray cleaning liquid device 2-13 in end, connect high pressure on spray cleaning liquid device 2-13 inlet and cleaning agent original fluid container 2-4 Between the liquid outlet of pump plus cleaning liquid device 2-14;Rotatable platform 2-5 is a disc structure, itself and rotary middle spindle (2-6) Center overlapping of axles.Angle adjustment catch bar 2-12, lift telescopic post 2-8 can be Linear motor-driven push rod or oil cylinder or electric cylinders In one kind.Two-way automatic push-pull bar 2-13-3 is double piston-rod two-way cylinder.
The output shaft for rotating controlled motor 2-7 is equipped with drive gear after penetrating rotatably rotatable platform 2-5, institute State and driven gear is equipped with rotary middle spindle 2-6, the drive gear engages with driven gear;
As shown in figure 3, the spray cleaning liquid device 2-13 includes spray cleaning fluid encirclement bar 2-13-1, two-way automatic push-pull bar 2-13-3 and leveling hydraulic cylinder 2-16, the quantity of the spray cleaning fluid encirclement bar 2-13-1 is two, and it is cavity knot that it is internal Structure, spray cleaning fluid encirclement bar 2-13-1 one end is half ring type structure, and the spray cleaning fluid encirclement bar 2-13-1 other ends are staight shank knot Structure, two spray cleaning fluid encirclement bar 2-13-1 are oppositely disposed, and are hinged by rotary positioning pin 2-13-2;It is described it is two-way from Between dynamic pull bar 2-13-3 is on the inside of two spray cleaning fluid encirclement bar 2-13-1 straight handle ends, two-way automatic push-pull bar 2-13- 3 both ends are hinged with spray cleaning fluid encirclement bar 2-13-1 staight shanks one end respectively;The spray cleaning fluid encirclement bar 2-13-1 half is ring-like Multiple automatic spray cleaning fluid head 2-13-4 with its connects with the internal cavities are evenly arranged with the inside of one end;The spray of one of them is clear The end of washing lotion encirclement bar 2-13-1 staight shanks one end is hinged with the one end of pivot link 2-11 away from support post 2-10, the spray The middle part and one end of the leveling hydraulic cylinder 2-16 of cleaning fluid encirclement bar 2-13-1 staight shanks one end are hinged, the leveling hydraulic cylinder The middle part of the 2-16 other end and pivot link 2-11 is hinged;Automatic spray cleaning fluid head 2-13-4 quantity is preferably not less than 10 Group;The inlet of the spray cleaning liquid device 2-13 is two, respectively positioned at two spray cleaning fluid encirclement bar 2-13-1 staight shanks one On end.Pipeline on connection spray cleaning liquid device 2-13 inlet and cleaning agent original fluid container 2-4 between the liquid outlet of high-pressure pump Preferably flexible pipe.
The high-pressure pump, rotate controlled motor 2-7, be lift telescopic post 2-8, angle adjustment catch bar 2-12, two-way automatic Pull bar 2-13-3 is connected with central controller 3.Central controller 3 can be arranged on support base 2-1 tops.
The apparatus structure compact and reasonable, integrated level are high, and automaticity is high, convenient and swift using process, and karst water is accumulated Thing removal efficiency is high, can be suitably used for different types gluing work roll cooling, meanwhile, it can help to the high efficiency to gluing roll Safeguard, can effectively make a price reduction the work load of attendant.Freely adjusting for height can be carried out by lift telescopic post in the device Whole, flexibility is preferable.
In order to further improve the overall automaticity of device, in addition to adjustable height survey meter 2-15, inclination are passed Sensor and dirt position inductance gauge 2-13-5, the adjustable height survey meter 2-15 are located at support platform 2-9 upper surfaces, tilt Sensor is arranged on spray cleaning liquid device 2-13 surface, and dirt position inductance gauge 2-13-5 is arranged at spray cleaning fluid encirclement bar The inner side of half ring-like one end of 2-13-1;Adjustable height survey meter 2-15, inclination sensor and dirt position inductance gauge 2-13-5 are equal It is connected with central controller 3.Adjustable height survey meter 2-15 model TRIS-972;Inclination sensor is that YHQ type two dimensions are inclined Angled sensors;Dirt position inductance gauge 2-13-5 is OMD-D-L type foreign-body locators;
In order to facilitate the moving process of the control device, and position can be carried out in time when needed and fixed, the wheel 2-2 For automatically controlled steering brake wheel, wheel 2-2 is four, is respectively arranged at the corner of support base 2-1 bottoms, four wheel 2-2 are equal Pass through wireless connection with central controller 3.
For the ease of hand push, described support base 2-1 one end has been bolted to connection manual curved handle 2-3;Hand push is curved Angle between handle 2-3 and horizontal plane is between 30 °~75 °;The support base 2-1 is a rectangular steel plates structure, supports bottom Seat 2-1 thickness is not less than 10mm;The support platform 2-9 is a rectangular steel plates structure, and support platform 2-9 thickness is not less than 5mm;The lift telescopic post 2-8 is four groups, and the stroke range value of the lift telescopic post 2-8 is between 0m~5m;It is described clear Lotion original fluid container 2-4 volumes are between 5L~15L.
In order to facilitate control injection process, loading pump, flowmeter and electricity are set respectively on described plus cleaning liquid device 2-14 Valve is controlled, loading pump, flowmeter and the electrically-controlled valve are connected with central controller 3 respectively.
In order that the service life of spray cleaning fluid head is longer automatically, meanwhile, also for the effective of more effectively guarantee decoction Supply, the automatic spray cleaning fluid head 2-13-4 is matched in parts by weight by following components to be formed:The fluoro- 2- chlorine of 1,1,1,2- tetra- 64~144 parts of ethane, 84~144 parts of tetrachlorodifluoroethane, 1,1- 144~454 parts of Difluoroethane, trimethylol melamine 84~194 parts of resin, 74~154 parts of magnetic melamine formaldehyde resin, 2- [[(2'- cyanobiphenyl -4- bases) methyl] ammonia Base] 144~444 parts of -3- ethyl nitrobenzoates, concentration is 54ppm~94ppm 2- [(3- chloro-2-methyls phenyl) amino] 84~144 parts of benzoic acid, ureaformaldehyde -74~144 parts of melamino-formaldehyde compound resin, 3- ketobutyric acids 2- (methyl (phenyl first Base) amino) 74~184 parts of ethyl ester, 94~164 parts of crosslinking agent, the chloro- 2- of 4- [(6- methoxyl group -3- pyridine radicals) amino] benzoic acid 54~144 parts, 94~174 parts of the chloro- 6- methylphenols of 3- amino -2-, the chloro- 3- methylphenols hydrochloride 44 of 6- amino -2,4- bis- ~84 parts, the chloro- N- of 2- (3- methoxyl group -2- thiophene phenyls) -2 ', 54~144 parts of 6 '-dimethylacetamide aniline.The crosslinking agent is 1- Chloro-O-Phenyl -1- phenyl -3- dimethylaminos propanol hydrochloride, 7- amino -3- chlorine cephalosporanic acid benzhydryl esters hydrochloride, 6- Any one in (3,5- diaminobenzenes formamido group) n-caproic acid hydrochloride.
In order to improve the performance of automatic spray cleaning fluid head, the manufacturing process of the automatic spray cleaning fluid head 2-13-4 is as follows:
Step 1:544~1404 parts of the ultra-pure water that electrical conductivity is the μ S/cm of 0.44 μ S/cm~0.74 is added in a kettle, Start reactor in agitator, rotating speed be 94rpm~444rpm, startup heat pump, make reactor temperature rise to 64 DEG C~ 84℃;Sequentially add 1,1,1,2- tetra- fluoro- 2- chloroethanes, tetrachlorodifluoroethane, 1,1- Difluoroethanes, stirring to being completely dissolved, It is 4.4~7.4 to adjust pH value, agitator speed is adjusted into 144rpm~454rpm, temperature is 94 DEG C~164 DEG C, esterification 44~54 hours;
Step 2:Trimethylol melamine resin, magnetic melamine formaldehyde resin is taken to be crushed, powder diameter For 414~544 mesh;Add 2- [[(2'- cyanobiphenyl -4- bases) methyl] amino] -3- ethyl nitrobenzoates to be well mixed, put down It is laid in pallet, tiling thickness is 44mm~54mm, and it for 4.4kGy~8.4kGy, energy is 4.4MeV~14MeV to use dosage Alpha ray irradiate 54~144 minutes, and β x ray irradiation xs 74~164 minutes of Isodose;
Step 3:The mixed-powder handled through step 2 is dissolved in 2- [(3- chloro-2-methyls phenyl) amino] benzoic acid, is added Enter the reactor in step 1, agitator speed is 84rpm~184rpm, and temperature is 94 DEG C~144 DEG C, and starting vavuum pump makes The vacuum pressure of reactor reaches -0.44MPa~-0.84MPa, keeps this state response 44~54 hours;Pressure release is simultaneously passed through nitrogen Gas, it is 0.44MPa~0.74MPa to make reacting kettle inner pressure, and insulation stands 44~54 hours;Agitator speed is promoted to 114 Rpm~454rpm, simultaneous reactions kettle pressure release to 0MPa;Sequentially add ureaformaldehyde-melamino-formaldehyde compound resin, 3- oxo fourths After sour 2- (methyl (phenyl methyl) amino) ethyl ester is completely dissolved, adds crosslinking agent and be stirred so that the parent of reactor solution Hydrophile-lipophile balance value is 4.4~7.4, and insulation stands 44~54 hours;
Step 4:When agitator speed is 144rpm~464rpm, the chloro- 2- of 4- [(6- methoxyl group -3- pyrroles are sequentially added Piperidinyl) amino] benzoic acid, the chloro- 6- methylphenols of 3- amino -2-, the chloro- 3- methylphenols hydrochlorides of 6- amino -2,4- two, 2- Chloro- N- (3- methoxyl group -2- thiophene phenyls) -2 ', 6 '-dimethylacetamide aniline, reactor pressure is lifted, reaches 0.84MPa ~1.64MPa, temperature are 144 DEG C~474 DEG C, polymerisation 14~24 hours;Reacting kettle inner pressure is down to after the completion of reaction 0MPa, 24 DEG C~34 DEG C are cooled to, discharging, enters molding press and can be prepared by spraying cleaning fluid head 2-13-4 automatically.
Embodiment 1:
According to following steps manufacture spray cleaning fluid head 2-13-4, and fraction meter by weight automatically of the present invention:
1st step:544 parts of the ultra-pure water that electrical conductivity is 0.44 μ S/cm is added in a kettle, is started in reactor and is stirred Device, rotating speed 94rpm, start heat pump, reactor temperature is risen to 64 DEG C;Sequentially add the fluoro- 2- chlorine of 1,1,1,2- tetra- 64 parts of ethane, 84 parts of tetrachlorodifluoroethane, 144 parts of 1,1- Difluoroethanes, to being completely dissolved, regulation pH values are 4.4 for stirring, will Agitator speed is adjusted to 144rpm, and temperature is 94 DEG C, esterification 44 hours;
2nd step:84 parts of trimethylol melamine resin, 74 parts of magnetic melamine formaldehyde resin is taken to be crushed, powder Last particle diameter is 414 mesh;Add the 144 parts of mixing of 2- [[(2'- cyanobiphenyl -4- bases) methyl] amino] -3- ethyl nitrobenzoates equal It is even, it is laid in pallet, tiling thickness is 44mm, and the alpha ray for using dosage to be 4.4MeV for 4.4kGy, energy irradiates 54 points Clock, and the β x ray irradiation xs 74 minutes of Isodose;
3rd step:The mixed-powder handled through step 2 is dissolved in 2- [(3- chloro-2-methyls phenyl) ammonia that concentration is 54ppm Base] in 84 parts of benzoic acid, reactor, agitator speed 84rpm are added, temperature is 94 DEG C, and starting vavuum pump makes reactor Vacuum pressure reach -0.44MPa, keep this state response 44 hours;Pressure release is simultaneously passed through nitrogen, makes the reacting kettle inner pressure be 0.44MPa, insulation stand 44 hours;Agitator speed is promoted to 114rpm, simultaneous reactions kettle pressure release to 0MPa;Sequentially add Ureaformaldehyde -74 parts of melamino-formaldehyde compound resin, 74 parts of 3- ketobutyric acids 2- (methyl (phenyl methyl) amino) ethyl ester are completely molten Xie Hou, add 94 parts of crosslinking agent and be stirred so that the hydrophilic lipophilic balance of reactor solution is 4.4, and it is small that insulation stands 44 When;
4th step:When agitator speed is 144rpm, the chloro- 2- of 4- [(6- methoxyl group -3- pyridine radicals) amino] are sequentially added Chloro- 44 parts of the 3- methylphenols hydrochloride of 94 parts of the chloro- 6- methylphenols of 54 parts of benzoic acid, 3- amino -2-, 6- amino -2,4- two, The chloro- N- of 2- (3- methoxyl group -2- thiophene phenyls) -2 ', 54 parts of 6 '-dimethylacetamide aniline, reactor pressure is lifted, is reached 0.84MPa, temperature are 144 DEG C, polymerisation 14 hours;Reacting kettle inner pressure is down to 0MPa after the completion of reaction, is cooled to 24 DEG C, discharging, enter molding press and can be prepared by spraying cleaning fluid head 2-13-4 automatically;
The crosslinking agent is 1- Chloro-O-Phenyl -1- phenyl -3- dimethylamino propanol hydrochlorides.
Embodiment 2:
According to following steps manufacture spray cleaning fluid head 2-13-4, and fraction meter by weight automatically of the present invention:
1st step:1404 parts of the ultra-pure water that electrical conductivity is 0.74 μ S/cm is added in a kettle, is started in reactor and is stirred Device, rotating speed 444rpm, start heat pump, reactor temperature is risen to 84 DEG C;Sequentially add tetra- fluoro- 2- of 1,1,1,2- 144 parts of chloroethanes, 44 parts of tetrachlorodifluoroethane, 454 parts of 1,1- Difluoroethanes, to being completely dissolved, regulation pH values are 7.4 for stirring, Agitator speed is adjusted to 454rpm, temperature is 164 DEG C, esterification 54 hours;
2nd step:194 parts of trimethylol melamine resin, 154 parts of magnetic melamine formaldehyde resin is taken to be crushed, Powder diameter is 544 mesh;Add the 444 parts of mixing of 2- [[(2'- cyanobiphenyl -4- bases) methyl] amino] -3- ethyl nitrobenzoates Uniformly, it is laid in pallet, tiling thickness is 54mm, uses the alpha ray irradiation 144 that dosage is 14MeV for 8.4kGy, energy Minute, and the β x ray irradiation xs 164 minutes of Isodose;
3rd step:The mixed-powder handled through step 2 is dissolved in 2- [(3- chloro-2-methyls phenyl) ammonia that concentration is 94ppm Base] in 144 parts of benzoic acid, reactor, agitator speed 184rpm are added, temperature is 144 DEG C, and starting vavuum pump makes reaction The vacuum pressure of kettle reaches -0.84MPa, keeps this state response 54 hours;Pressure release is simultaneously passed through nitrogen, makes reacting kettle inner pressure For 0.74MPa, insulation stands 54 hours;Agitator speed is promoted to 454rpm, simultaneous reactions kettle pressure release to 0MPa;Successively plus It is complete to enter ureaformaldehyde -144 parts of melamino-formaldehyde compound resin, 3- ketobutyric acids 2- (methyl (phenyl methyl) amino) 184 parts of ethyl ester After fully dissolved, add 164 parts of crosslinking agent and be stirred so that the hydrophilic lipophilic balance of reactor solution is 7.4, and insulation is quiet Put 44~54 hours;
4th step:When agitator speed is 464rpm, the chloro- 2- of 4- [(6- methoxyl group -3- pyridine radicals) amino] are sequentially added The chloro- 3- methylphenols hydrochloride 84 of 174 parts of the chloro- 6- methylphenols of 144 parts of benzoic acid, 3- amino -2-, 6- amino -2,4- two Part, the chloro- N- of 2- (3- methoxyl group -2- thiophene phenyls) -2 ', 144 parts of 6 '-dimethylacetamide aniline, reactor pressure is lifted, makes it Reach 1.64MPa, temperature is 474 DEG C, polymerisation 24 hours;Reacting kettle inner pressure is down to 0 MPa after the completion of reaction, cooled To 34 DEG C, discharging, enter molding press and can be prepared by spraying cleaning fluid head 2-13-4 automatically;
The crosslinking agent is 6- (3,5- diaminobenzenes formamido group) n-caproic acid hydrochloride.
Embodiment 3:
According to following steps manufacture spray cleaning fluid head 2-13-4, and fraction meter by weight automatically of the present invention:
1st step:1104 parts of the ultra-pure water that electrical conductivity is 0.54 μ S/cm is added in a kettle, is started in reactor and is stirred Device, rotating speed 244rpm, start heat pump, reactor temperature is risen to 74 DEG C;Sequentially add tetra- fluoro- 2- of 1,1,1,2- 124 parts of chloroethanes, 114 parts of tetrachlorodifluoroethane, 354 parts of 1,1- Difluoroethanes, to being completely dissolved, adjusting pH values is for stirring 6.4, agitator speed is adjusted to 254rpm, temperature is 134 DEG C, esterification 48 hours;
2nd step:124 parts of trimethylol melamine resin, 134 parts of magnetic melamine formaldehyde resin is taken to be crushed, Powder diameter is 464 mesh;Add the 344 parts of mixing of 2- [[(2'- cyanobiphenyl -4- bases) methyl] amino] -3- ethyl nitrobenzoates Uniformly, it is laid in pallet, tiling thickness is 48mm, uses the alpha ray irradiation 84 that dosage is 10.5MeV for 6.4kGy, energy Minute, and the β x ray irradiation xs 124 minutes of Isodose;
3rd step:The mixed-powder handled through step 2 is dissolved in 2- [(3- chloro-2-methyls phenyl) ammonia that concentration is 84ppm Base] in 104 parts of benzoic acid, reactor, agitator speed 154rpm are added, temperature is 104 DEG C, and starting vavuum pump makes reaction The vacuum pressure of kettle reaches -0.64MPa, keeps this state response 48 hours;Pressure release is simultaneously passed through nitrogen, makes reacting kettle inner pressure For 0.64MPa, insulation stands 48 hours;Agitator speed is promoted to 354rpm, simultaneous reactions kettle pressure release to 0MPa;Successively plus It is complete to enter ureaformaldehyde -104 parts of melamino-formaldehyde compound resin, 3- ketobutyric acids 2- (methyl (phenyl methyl) amino) 164 parts of ethyl ester After fully dissolved, add 134 parts of crosslinking agent and be stirred so that the hydrophilic lipophilic balance of reactor solution is 6.4, and insulation is quiet Put 48 hours;
4th step:When agitator speed is 364rpm, the chloro- 2- of 4- [(6- methoxyl group -3- pyridine radicals) amino] are sequentially added The chloro- 3- methylphenols hydrochloride 64 of 114 parts of the chloro- 6- methylphenols of 104 parts of benzoic acid, 3- amino -2-, 6- amino -2,4- two Part, the chloro- N- of 2- (3- methoxyl group -2- thiophene phenyls) -2 ', 104 parts of 6 '-dimethylacetamide aniline, reactor pressure is lifted, makes it Reach 1.34MPa, temperature is 374 DEG C, polymerisation 18 hours;Reacting kettle inner pressure is down to 0 MPa after the completion of reaction, cooled To 28 DEG C, discharging, enter molding press and can be prepared by spraying cleaning fluid head 2-13-4 automatically;
The crosslinking agent is 7- amino -3- chlorine cephalosporanic acid benzhydryl ester hydrochlorides.
Reference examples:
Reference examples are used for the service condition of gluing roll decontamination for the automatic spray cleaning fluid head of certain commercially available brand.
The automatic spray cleaning fluid described in automatic spray cleaning fluid head 2-13-4 and reference examples that embodiment 1~3 is prepared The service condition that head is used for the decontamination of gluing roll is contrasted, and is carried with hardness enhancing rate, anti-solarization degree enhancing rate, corrosion resistant erosion degree The rate of liter, Degree of Ageing enhancing rate are that technical indicator is counted, as a result as shown in table 1:
Table 1 is used for the service condition of gluing roll decontamination for the automatic spray cleaning fluid head described in embodiment 1~3 and reference examples Parameters comparing result, as seen from Table 1, automatic spray cleaning fluid head 2-13-4 of the present invention, the lifting of its hardness Rate, anti-solarization degree enhancing rate, corrosion resistant erosion degree enhancing rate, Degree of Ageing enhancing rate are above the product of prior art production.
In addition, as shown in figure 4, it is automatic spray cleaning fluid head 2-13-4 materials of the present invention and decontamination enhancing rate relation Figure.Find out in figure, spray cleaning fluid head 2-13-4 materials are evenly distributed automatically used in embodiment 1~3, and effect of spraying pesticide is good;Show in figure Show automatic spray cleaning fluid head 2-13-4 of the present invention, it decontaminates enhancing rate and is significantly better than existing product.
A kind of operating method of carbon tetrachloride karst deposits gluing roll maintenance unit, comprises the following steps:
Step 1:Automatic flushing device 2 is pushed near gluing roll 1, is started by central controller 3 and rotates control electricity Machine 2-7 will spray cleaning liquid device 2-13 and turn to close to the position of the side of gluing roll 1;
Step 2:Control angle adjustment catch bar 2-12 knock-pin outwards to do top by central controller 3 and stretch motion, band Dynamic spray cleaning liquid device 2-13 is moved upwards, and after predetermined altitude is reached, leveling hydraulic cylinder 2- is controlled by central controller 3 16 piston rod is protruding, to clean liquid device 2-13 leveling to spray, when inclination sensor detects spray cleaning liquid device 2- 13 when being horizontal, and inclination sensor sends an electric signal to central controller 3, and central controller 3 controls angle to adjust Whole catch bar 2-12 stop motions;
Step 3:Two-way automatic push-pull bar 2-13-3 is started by central controller 3, two-way automatic push-pull bar 2-13-3's Two knock-pins do top to both ends respectively and stretch motion, drive spray cleaning fluid encirclement bar 2-13-1 using rotary positioning pin 2-13-2 as The center of circle circles, the opening of cleaning fluid encirclement bar 2-13-1 to be painted half ring-like one end be available for gluing roll 1 by when, Wheel 2-2 is controlled to be moved to close to the direction of gluing roll 1 by central controller 3, when cleaning fluid encirclement bar 2-13-1 semi-ring Type one end is enclosed in the outside of gluing roll 1, controls wheel 2-2 brakes to be fixed to carry out position by central controller 3, and Control two-way automatic push-pull bar 2-13-3 stop motions;
Step 4:Multiple lift telescopic post 2-8 are started by central controller 3 and synchronize action, make lift telescopic post 2-8 knock-pin does top and stretches motion upwards, and adjustable height survey meter 2-15 monitors adjustable height and will measure value and feeds back in real time Central controller 3, then central controller 3 lift telescopic post 2-8 operation feelings can be automatically controlled when inputting setting height Condition;
Step 5:In lifting process, dirt position inductance gauge 2-13-5 detects the dirt portion on gluing roll 1 in real time Position, when when dirt position, inductance gauge 2-13-5 detects dirt position, dirt position inductance gauge 2-13-5 feeds back to electric signal Central controller 3, the control of central controller 3 plus the loading pump startup cleaned in liquid device 2-14, control electrically-controlled valve are opened, together When control high pressure pump startup on cleaning agent original fluid container 2-4, cleaning fluid is pumped in spray cleaning liquid device 2-13, and by Cleaning fluid is sprayed to dirt position by automatic spray cleaning fluid head 2-13-4, so as to reach scavenging effect.
The operating process can make attendant easily complete the cleaning to gluing roll, can effectively reduce maintenance people The work load of member, meanwhile, it can help to the significantly lifting of maintenance efficiency.

Claims (9)

1. a kind of carbon tetrachloride karst deposits gluing roll maintenance unit, including automatic flushing device (2) and central controller (3), it is characterised in that the automatic flushing device (2) includes support base (2-1), is arranged on support base (2-1) bottom Wheel (2-2), the cleaning agent original fluid container (2-4) for being arranged on support base (2-1) top, it is fixedly arranged at support base (2- 1) rotary middle spindle (2-6) on top, the rotatable platform (2-5) for being rotatably connected at rotary middle spindle (2-6) upper end, fixation It is connected to the rotation controlled motor (2-7) on rotatable platform (2-5) top, the support platform (2- above rotatable platform (2-5) 9) multiple lift telescopic posts (2-8) peripheral between rotatable platform (2-5) and support platform (2-9), fixed company, are fixedly connected on Support post (2-10), one end and support post (2-10) upper end for being connected on support platform (2-9) central upper portion region are be hinged The angle that pivot link (2-11), both ends are hinged with the middle part of support post (2-10) and the middle part of pivot link (2-11) respectively Adjustment catch bar (2-12), the spray cleaning liquid device (2-13) be hinged with the other end of pivot link (2-11), it is connected spray cleaning Add cleaning liquid device (2- between the liquid outlet of high-pressure pump on the inlet and cleaning agent original fluid container (2-4) of liquid device (2-13) 14);
The output shaft for rotating controlled motor (2-7) is equipped with drive gear after penetrating rotatably rotatable platform (2-5), institute State and driven gear is equipped with rotary middle spindle (2-6), the drive gear engages with driven gear;
It is described spray cleaning liquid device (2-13) include spray cleaning fluid encirclement bar (2-13-1), two-way automatic push-pull bar (2-13-3) and Leveling hydraulic cylinder (2-16), the quantity of the spray cleaning fluid encirclement bar (2-13-1) is two, and it is cavity structure that it is internal, and spray is clear Washing lotion encirclement bar (2-13-1) one end is half ring type structure, and spray cleaning fluid encirclement bar (2-13-1) other end is staight shank structure, two Individual spray cleaning fluid encirclement bar (2-13-1) is oppositely disposed, and be hinged by rotary positioning pin (2-13-2);It is described two-way automatic Between pull bar (2-13-3) is on the inside of two spray cleaning fluid encirclement bar (2-13-1) straight handle ends, two-way automatic push-pull bar (2- Both ends 13-3) are hinged with spray cleaning fluid encirclement bar (2-13-1) staight shank one end respectively;The spray cleaning fluid encirclement bar (2-13- 1) multiple automatic spray cleaning fluid heads (2-13-4) with its connects with the internal cavities are evenly arranged with the inside of half ring-like one end;Wherein one The end of individual spray cleaning fluid encirclement bar (2-13-1) staight shank one end and the remote support post (2-10) of pivot link (2-11) One end is hinged, and the middle part of spray cleaning fluid encirclement bar (2-13-1) the staight shank one end is cut with scissors with one end of the leveling hydraulic cylinder (2-16) Connect, the middle part of the other end and pivot link (2-11) of the leveling hydraulic cylinder (2-16) is hinged;
The high-pressure pump, rotate controlled motor (2-7), lift telescopic post (2-8), angle adjustment catch bar (2-12), it is two-way from Dynamic pull bar (2-13-3) is connected with central controller (3).
2. a kind of carbon tetrachloride karst deposits gluing roll maintenance unit according to claim 1, it is characterised in that also Including adjustable height survey meter (2-15), inclination sensor and dirt position inductance gauge (2-13-5), the adjustable height detection Instrument (2-15) is located at support platform (2-9) upper surface, and inclination sensor is arranged on the surface of spray cleaning liquid device (2-13), dirt Position inductance gauge (2-13-5) is arranged at the inner side of spray cleaning fluid encirclement bar (2-13-1) half ring-like one end;Adjustable height survey meter (2-15), inclination sensor and dirt position inductance gauge (2-13-5) are connected with central controller (3).
3. a kind of carbon tetrachloride karst deposits gluing roll maintenance unit according to claim 1 or 2, its feature exist In the wheel (2-2) is automatically controlled steering brake wheel, and wheel (2-2) is four, is respectively arranged at support base (2-1) bottom At corner, four wheels (2-2) pass through wireless connection with central controller (3).
A kind of 4. carbon tetrachloride karst deposits gluing roll maintenance unit according to claim 3, it is characterised in that institute State support base (2-1) one end and be bolted to connection manual curved handle (2-3);Hand push curved handle (2-3) is between horizontal plane Angle between 30 °~75 °;The support base (2-1) is a rectangular steel plates structure, and support base (2-1) thickness is not low In 10mm;The support platform (2-9) is a rectangular steel plates structure, and support platform (2-9) thickness is not less than 5mm;The lifting Telescopic mast (2-8) is four groups, and the stroke range value of the lift telescopic post (2-8) is between 0m~5m;The cleaning agent stoste Tank (2-4) volume is between 5L~15L.
A kind of 5. carbon tetrachloride karst deposits gluing roll maintenance unit according to claim 4, it is characterised in that institute State plus clean on liquid device (2-14) and loading pump, flowmeter and electrically-controlled valve, loading pump, flowmeter and the electrically-controlled valve are set respectively It is connected respectively with central controller (3).
A kind of 6. carbon tetrachloride karst deposits gluing roll maintenance unit according to claim 5, it is characterised in that institute State automatic spray cleaning fluid head (2-13-4) and matched in parts by weight by following components and formed:The fluoro- 2- chloroethanes 64 of 1,1,1,2- tetra- ~144 parts, 84~144 parts of tetrachlorodifluoroethane, 1,1- 144~454 parts of Difluoroethane, trimethylol melamine resin 84~ 194 parts, 74~154 parts of magnetic melamine formaldehyde resin, 2- [[(2'- cyanobiphenyl -4- bases) methyl] amino] -3- nitros 144~444 parts of ethyl benzoate, 2- [(3- chloro-2-methyls phenyl) amino] benzoic acid 84 that concentration is 54ppm~94ppm~ 144 parts, ureaformaldehyde -74~144 parts of melamino-formaldehyde compound resin, 3- ketobutyric acids 2- (methyl (phenyl methyl) amino) ethyl ester 74~184 parts, 94~164 parts of crosslinking agent, the chloro- 2- of 4- [(6- methoxyl group -3- pyridine radicals) amino] 54~144 parts of benzoic acid, 3- 94~174 parts of the chloro- 6- methylphenols of amino -2-, 44~84 parts of the chloro- 3- methylphenols hydrochloride of 6- amino -2,4- bis-, 2- is chloro- N- (3- methoxyl group -2- thiophene phenyls) -2 ', 54~144 parts of 6 '-dimethylacetamide aniline.
A kind of 7. carbon tetrachloride karst deposits gluing roll maintenance unit according to claim 6, it is characterised in that institute Crosslinking agent is stated as 1- Chloro-O-Phenyl -1- phenyl -3- dimethylaminos propanol hydrochloride, 7- amino -3- chlorine cephalosporanic acid benzhydryl esters Any one in hydrochloride, 6- (3,5- diaminobenzenes formamido group) n-caproic acid hydrochloride.
A kind of 8. carbon tetrachloride karst deposits gluing roll maintenance unit according to claim 7, it is characterised in that institute The manufacturing process for stating automatic spray cleaning fluid head (2-13-4) is as follows:
Step 1:544~1404 parts of the ultra-pure water that electrical conductivity is the μ S/cm of 0.44 μ S/cm~0.74 is added in a kettle, is started Agitator in reactor, rotating speed are 94rpm~444rpm, start heat pump, reactor temperature is risen to 64 DEG C~84 DEG C; 1,1,1,2- tetra- fluoro- 2- chloroethanes, tetrachlorodifluoroethane, 1,1- Difluoroethanes are sequentially added, stirring adjusts pH to being completely dissolved It is worth for 4.4~7.4, agitator speed is adjusted to 144rpm~454rpm, temperature is 94 DEG C~164 DEG C, esterification 44~54 Hour;
Step 2:Trimethylol melamine resin, magnetic melamine formaldehyde resin is taken to be crushed, powder diameter 414 ~544 mesh;Add 2- [[(2'- cyanobiphenyl -4- bases) methyl] amino] -3- ethyl nitrobenzoates to be well mixed, be laid in support In disk, tiling thickness is 44mm~54mm, uses the alpha ray that dosage is 4.4MeV~14MeV for 4.4kGy~8.4kGy, energy Irradiation 54~144 minutes, and the β x ray irradiation xs 74~164 minutes of Isodose;
Step 3:The mixed-powder handled through step 2 is dissolved in 2- [(3- chloro-2-methyls phenyl) amino] benzoic acid, adds step Reactor in rapid one, agitator speed are 84rpm~184rpm, and temperature is 94 DEG C~144 DEG C, and starting vavuum pump makes reactor Vacuum pressure reach -0.44MPa~-0.84MPa, keep this state response 44~54 hours;Pressure release is simultaneously passed through nitrogen, makes anti- It is 0.44MPa~0.74MPa to answer pressure in kettle, and insulation stands 44~54 hours;Agitator speed be promoted to 114rpm~ 454rpm, simultaneous reactions kettle pressure release to 0MPa;Sequentially add ureaformaldehyde-melamino-formaldehyde compound resin, 3- ketobutyric acid 2- (first Base (phenyl methyl) amino) after ethyl ester is completely dissolved, adds crosslinking agent and be stirred so that the hydrophilic and oleophilic of reactor solution is put down Weighing apparatus value is 4.4~7.4, and insulation stands 44~54 hours;
Step 4:When agitator speed is 144rpm~464rpm, the chloro- 2- of 4- [(6- methoxyl group -3- pyridine radicals) are sequentially added Amino] benzoic acid, the chloro- 6- methylphenols of 3- amino -2-, the chloro- 3- methylphenols hydrochlorides of 6- amino -2,4- two, the chloro- N- of 2- (3- methoxyl group -2- thiophene phenyls) -2 ', 6 '-dimethylacetamide aniline, lifted reactor pressure, reach 0.84MPa~ 1.64MPa, temperature are 144 DEG C~474 DEG C, polymerisation 14~24 hours;Reacting kettle inner pressure is down to after the completion of reaction 0MPa, 24 DEG C~34 DEG C are cooled to, discharging, enters molding press and can be prepared by spraying cleaning fluid head (2-13-4) automatically.
9. a kind of operating method of carbon tetrachloride karst deposits gluing roll maintenance unit, it is characterised in that including following step Suddenly:
Step 1:Automatic flushing device (2) is pushed near gluing roll (1), is started by central controller (3) and rotates control Motor (2-7) is turned to cleaning liquid device (2-13) is sprayed close to the position of gluing roll (1) side;
Step 2:Control the knock-pin of angle adjustment catch bar (2-12) outwards to do top by central controller (3) and stretch motion, band Dynamic spray cleaning liquid device (2-13) is moved upwards, and after predetermined altitude is reached, leveling hydraulic cylinder is controlled by central controller (3) The piston rod of (2-16) is protruding, to clean liquid device (2-13) leveling to spray, when inclination sensor detects spray cleaning fluid When device (2-13) is horizontal, inclination sensor sends an electric signal, central controller to central controller (3) (3) angle adjustment catch bar (2-12) stop motion is controlled;
Step 3:Two-way automatic push-pull bar (2-13-3), two-way automatic push-pull bar (2-13-3) are started by central controller (3) Two knock-pins do top to both ends respectively and stretch motion, drive spray cleaning fluid encirclement bar (2-13-1) with rotary positioning pin (2-13- 2) circled for the center of circle, the opening of half ring-like one end of cleaning fluid encirclement bar (2-13-1) to be painted is available for gluing roll (1) By when, by central controller (3) control wheel (2-2) to close to gluing roll (1) direction move, when cleaning fluid encirclement bar The half ring-like one end of (2-13-1) is enclosed in the outside of gluing roll (1), controls wheel (2-2) to stop by central controller (3) Car is fixed with carrying out position, and controls two-way automatic push-pull bar (2-13-3) stop motion;
Step 4:Multiple lift telescopic posts (2-8) are started by central controller (3) and synchronize action, make lift telescopic post The knock-pin of (2-8) does top and stretches motion upwards, and adjustable height survey meter (2-15) monitors adjustable height and will measure value instead in real time Central controller (3) is fed to, then central controller (3) can automatically control lift telescopic post (2-8) when inputting setting height Running situation;
Step 5:In lifting process, dirt position inductance gauge (2-13-5) detects the dirt portion on gluing roll (1) in real time Position, when dirt position inductance gauge (2-13-5) detects dirt position, dirt position inductance gauge (2-13-5) is anti-by electric signal Central controller (3) is fed to, central controller (3) control adds the loading pump startup cleaned in liquid device (2-14), control automatically controlled Valve is opened, while controls the high pressure pump startup on cleaning agent original fluid container (2-4), and cleaning fluid is pumped into spray cleaning liquid device In (2-13), and cleaning fluid is sprayed to dirt position by spraying cleaning fluid head (2-13-4) automatically, so as to reach scavenging effect.
CN201710591957.1A 2017-07-19 2017-07-19 Carbon tetrachloride karst deposits gluing roll maintenance unit and its operating method Pending CN107442481A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201710591957.1A CN107442481A (en) 2017-07-19 2017-07-19 Carbon tetrachloride karst deposits gluing roll maintenance unit and its operating method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201710591957.1A CN107442481A (en) 2017-07-19 2017-07-19 Carbon tetrachloride karst deposits gluing roll maintenance unit and its operating method

Publications (1)

Publication Number Publication Date
CN107442481A true CN107442481A (en) 2017-12-08

Family

ID=60487400

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201710591957.1A Pending CN107442481A (en) 2017-07-19 2017-07-19 Carbon tetrachloride karst deposits gluing roll maintenance unit and its operating method

Country Status (1)

Country Link
CN (1) CN107442481A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108825941A (en) * 2018-05-03 2018-11-16 长春工业大学 A kind of Airborne Camera ground motion test device of multiaxis cooperative motion
CN110404905A (en) * 2019-08-26 2019-11-05 信壮壮 A kind of livestock-raising watering trough cleaner for inner wall
CN111183884A (en) * 2020-03-03 2020-05-22 江西理工大学应用科学学院 Navel orange is planted with all-round device that waters
CN111648563A (en) * 2020-06-14 2020-09-11 哈尔滨市三棵中药材市场太清参茸行 Building body spraying equipment for building
CN113977935A (en) * 2021-11-15 2022-01-28 温州大学 Hot rolling device suitable for FDM type 3D prints

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105918291A (en) * 2016-05-04 2016-09-07 徐州工程学院 Vehicle-mounted diagnosis and treatment equipment for endangered plant Cercidiphyllum japonicum and working method of vehicle-mounted diagnosis and treatment equipment
CN106002572A (en) * 2016-05-30 2016-10-12 徐州工程学院 Engineering equipment for removing rust on surface of construction steel structure and working method of engineering equipment

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105918291A (en) * 2016-05-04 2016-09-07 徐州工程学院 Vehicle-mounted diagnosis and treatment equipment for endangered plant Cercidiphyllum japonicum and working method of vehicle-mounted diagnosis and treatment equipment
CN106002572A (en) * 2016-05-30 2016-10-12 徐州工程学院 Engineering equipment for removing rust on surface of construction steel structure and working method of engineering equipment

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108825941A (en) * 2018-05-03 2018-11-16 长春工业大学 A kind of Airborne Camera ground motion test device of multiaxis cooperative motion
CN110404905A (en) * 2019-08-26 2019-11-05 信壮壮 A kind of livestock-raising watering trough cleaner for inner wall
CN111183884A (en) * 2020-03-03 2020-05-22 江西理工大学应用科学学院 Navel orange is planted with all-round device that waters
CN111648563A (en) * 2020-06-14 2020-09-11 哈尔滨市三棵中药材市场太清参茸行 Building body spraying equipment for building
CN113977935A (en) * 2021-11-15 2022-01-28 温州大学 Hot rolling device suitable for FDM type 3D prints

Similar Documents

Publication Publication Date Title
CN107442481A (en) Carbon tetrachloride karst deposits gluing roll maintenance unit and its operating method
CN107470344A (en) The method of nanometer humic acid joint ferrous ion activation persulfate renovation of organic pollution soil
CN105347519B (en) A kind of nano-bubble generator and its application
CN205701843U (en) A kind of reparation integration apparatus of polycyclic aromatic hydrocarbon pollution
CN104147908B (en) Biofilm reactor-biological deodorizing tower system locking device and the method processing foul smell
CN206731796U (en) A kind of circulation well for removably descending water pollutant
CN104743667B (en) Device for in-situ remediation of underground water pollution of agricultural irrigator well and method for remediation of underground water by using device
CN208684701U (en) A kind of indegradable industrial effluent biochemical treatment system
CN205628904U (en) Be used for polluting prosthetic device of soil normal position
KR20030087915A (en) Method for purifying a layer of contaminated soil and apparatus
CN105417769A (en) Laboratory carbon tetrachloride separation treatment system and treatment process thereof
CN105692919B (en) A kind of TiO2Carbon tetrachloride device and its method of work in photocatalytic degradation underground water
CN213613318U (en) Horizontal extraction gas injection well for biological ventilation
CN206624752U (en) A kind of plant stand builds special sewage treatment equipment
CN111250537A (en) Bioremediation system for organic pollution site
CN106006908B (en) A kind of vehicular underground water carbon tetrachloride processing equipment and its process for purifying water
CN105800766B (en) Carbon tetrachloride device and its method of work in a kind of high temperature aeration removal underground water
CN105819609B (en) A kind of production method for the towers units and its critical component decomposing ethlyene dichloride
CN205856037U (en) A kind of atomising device in continuous processing subsoil water in volatile organic matter complete set of equipments
CN105776714B (en) Carbon tetrachloride device and its method of work in one kind heating membrane by accelerant process processing underground water
CN210711060U (en) Process system for jointly treating water and soil in polluted site
CN105776516B (en) A kind of biological contact oxidation process removes the device and its working method of carbon tetrachloride in underground water
CN208182656U (en) A kind of industrial pollution area building substrate contamination object separation purifying system
CN108455477A (en) A kind of carbon tetrachloride UV photooxidations catalytic treatment equipment elevator
CN108439285B (en) Carbon tetrachloride reation kettle linkage platform

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
RJ01 Rejection of invention patent application after publication

Application publication date: 20171208

RJ01 Rejection of invention patent application after publication