CN106622011A - A blending and controlling system for a paint curtaining segment of a silvering line and a control method thereof - Google Patents
A blending and controlling system for a paint curtaining segment of a silvering line and a control method thereof Download PDFInfo
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- CN106622011A CN106622011A CN201611027046.8A CN201611027046A CN106622011A CN 106622011 A CN106622011 A CN 106622011A CN 201611027046 A CN201611027046 A CN 201611027046A CN 106622011 A CN106622011 A CN 106622011A
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- 239000003973 paint Substances 0.000 title claims abstract description 71
- 238000000034 method Methods 0.000 title claims abstract description 21
- 238000002156 mixing Methods 0.000 title claims abstract description 13
- 239000007788 liquid Substances 0.000 claims abstract description 43
- 238000003756 stirring Methods 0.000 claims abstract description 16
- 230000007246 mechanism Effects 0.000 claims abstract description 11
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 10
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 claims description 37
- 239000000126 substance Substances 0.000 claims description 36
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 claims description 32
- 229910052709 silver Inorganic materials 0.000 claims description 31
- 239000004332 silver Substances 0.000 claims description 31
- 238000002386 leaching Methods 0.000 claims description 16
- 238000004364 calculation method Methods 0.000 claims description 7
- 238000004891 communication Methods 0.000 claims description 6
- 239000000463 material Substances 0.000 claims description 6
- 238000004458 analytical method Methods 0.000 claims description 4
- 230000006978 adaptation Effects 0.000 claims description 3
- 238000007654 immersion Methods 0.000 claims description 3
- 239000000203 mixture Substances 0.000 claims description 3
- 238000012544 monitoring process Methods 0.000 claims description 3
- 238000005086 pumping Methods 0.000 claims description 3
- 238000002560 therapeutic procedure Methods 0.000 claims description 3
- 238000012546 transfer Methods 0.000 claims description 3
- 230000008569 process Effects 0.000 abstract description 8
- 239000002699 waste material Substances 0.000 abstract description 4
- 239000013043 chemical agent Substances 0.000 abstract 3
- 230000001105 regulatory effect Effects 0.000 abstract 3
- 230000001276 controlling effect Effects 0.000 abstract 1
- 239000000243 solution Substances 0.000 description 49
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 6
- 239000000047 product Substances 0.000 description 6
- 238000010422 painting Methods 0.000 description 5
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- 208000027418 Wounds and injury Diseases 0.000 description 3
- 235000011114 ammonium hydroxide Nutrition 0.000 description 3
- 230000006378 damage Effects 0.000 description 3
- 239000011521 glass Substances 0.000 description 3
- 230000006872 improvement Effects 0.000 description 3
- 208000014674 injury Diseases 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 238000012986 modification Methods 0.000 description 3
- 230000004048 modification Effects 0.000 description 3
- 238000007789 sealing Methods 0.000 description 3
- 230000009286 beneficial effect Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 238000007689 inspection Methods 0.000 description 2
- 238000005259 measurement Methods 0.000 description 2
- 239000011259 mixed solution Substances 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 238000005070 sampling Methods 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- 230000008859 change Effects 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- XRRQZKOZJFDXON-UHFFFAOYSA-N nitric acid;silver Chemical compound [Ag].O[N+]([O-])=O XRRQZKOZJFDXON-UHFFFAOYSA-N 0.000 description 1
- 230000005693 optoelectronics Effects 0.000 description 1
- 238000007747 plating Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000012372 quality testing Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
- 230000009469 supplementation Effects 0.000 description 1
- 230000001988 toxicity Effects 0.000 description 1
- 231100000419 toxicity Toxicity 0.000 description 1
- 239000008096 xylene Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/20—Measuring; Control or regulation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/60—Pump mixers, i.e. mixing within a pump
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/20—Measuring; Control or regulation
- B01F35/22—Control or regulation
- B01F35/2201—Control or regulation characterised by the type of control technique used
- B01F35/2209—Controlling the mixing process as a whole, i.e. involving a complete monitoring and controlling of the mixing process during the whole mixing cycle
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/20—Measuring; Control or regulation
- B01F35/22—Control or regulation
- B01F35/221—Control or regulation of operational parameters, e.g. level of material in the mixer, temperature or pressure
- B01F35/2215—Temperature
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/80—Forming a predetermined ratio of the substances to be mixed
- B01F35/88—Forming a predetermined ratio of the substances to be mixed by feeding the materials batchwise
-
- G—PHYSICS
- G05—CONTROLLING; REGULATING
- G05D—SYSTEMS FOR CONTROLLING OR REGULATING NON-ELECTRIC VARIABLES
- G05D27/00—Simultaneous control of variables covered by two or more of main groups G05D1/00 - G05D25/00
- G05D27/02—Simultaneous control of variables covered by two or more of main groups G05D1/00 - G05D25/00 characterised by the use of electric means
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F2101/00—Mixing characterised by the nature of the mixed materials or by the application field
- B01F2101/30—Mixing paints or paint ingredients, e.g. pigments, dyes, colours, lacquers or enamel
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Physics & Mathematics (AREA)
- General Physics & Mathematics (AREA)
- Engineering & Computer Science (AREA)
- Automation & Control Theory (AREA)
- Coating Apparatus (AREA)
Abstract
A blending and controlling system for a paint curtaining segment of a silvering line is disclosed. The system includes a stirring tank, a solution using tank, an adding mechanism, a regulating motor and a PLC, wherein the top of the stirring tank is provided with an electrically controlled exhaust valve, the inside of the stirring tank is provided with a gravitometer and a pH meter, the solution using tank is communicated with the stirring tank through a metering pump and a pipeline, a liquid level sensor is disposed in the solution using tank, the adding mechanism is used for adding components into the solution using tank in a metering manner, the regulating motor is disposed at one side of a water curtain plate and can drive the water curtain plate to rotate so as to adjust the size of a paint curtain, and the PLC is in controllable connection with the liquid level sensor, the gravitometer, the pH meter, the electrically controlled exhaust valve, the regulating motor and the adding mechanism. Addition of chemical agents is adjusted in real time according to feedback information of a blended solution in a blending process, thus ensuring stability and accuracy of a chemical agent blending ratio, and reducing or radically eliminating the risk of waste products caused by an unstable chemical agent solution ratio.
Description
Technical field
The present invention relates to silver mirror processing technique field, more particularly to a kind of silver jacketed wire leaching paint section dispensing and control system and
Its control method.
Background technology
Being currently used for the paint of the silver jacketed wire leaching paint section of production speculum silver mirror needs artificial allotment, and by inspection oil is observed
The artificial judgement consumption of the paint liquid level of case is painted, paint pours by hand deployed paint and xylene solution into when not enough.
And silver jacketed wire chemicals allotment addition scheme is, manually by chemicals by metering, to enter according to certain ratio in FX
Row configuration, then stirs.Need to make an inspection tour solution service condition in silver jacketed wire chemical solutions case according to approximate time in production, when
When solution lacks in silver jacketed wire chemical solutions case, workman is supplemented.Artificial allotment chemical solutions are according to predetermined rule
Then allocating, workman accurately cannot in real time understand matched somebody with somebody solution and accurately configure proportion and ratio ratio, need quality testing department not
The precision of the sampling observation checking allotment solution of timing.
This chemicals dispensing mode, needs tank solution to allocate workman, greatly improves human cost, and solution
The precision of allotment fully relies on the feedback of sampling observation person, if solution goes wrong in debugging process, it is impossible to timely find, will
Substantial amounts of waste product is caused to occur.Also accurately cannot be improved by changing chemical solutions proportioning or verify that new technique is needed
Ask.Simultaneously during allotment chemical solutions, workman can touch these by way of air or directly contact unavoidably
Chemicals, although silver jacketed wire chemicals is without strong toxicity or corrosivity, long-time contact also can be caused sternly to body
The injury of weight.
And the control of paint paint curtain uses completely workman's experience to be adjusted, it is impossible to carry out accurately adjustment paint
The size of curtain, also cannot accurately record paint consumption in real time.It is unfavorable for controlling the stability of quality, quality is easily subject to people
For the impact of factor.Also it is unfavorable for improving production technology and reduces cost simultaneously.
The content of the invention
The purpose of the present invention is to be directed to technological deficiency present in prior art, and provides a kind of silver jacketed wire leaching paint section dispensing
And control system.
To realize that the technical scheme that the purpose of the present invention is adopted is：
A kind of silver jacketed wire leaching paint section dispensing and control system, including,
Agitator tank, its top is provided with electric control exhaust valve, and densimeter and pH meter are provided with it；
Case is used by the solution of measuring pump and pipeline communication with described agitator tank, in it liquid level sensor is provided with；
To the addition mechanism that addO-on therapy is measured to described agitator tank,
Being arranged on the side of water curtain plate can drive its upset to adjust the regulation motor of paint curtain size,
And it is controllable with described liquid level sensor, densimeter, pH meter, electric control exhaust valve, regulation motor and addition mechanism
The PLC of connection.
Also include the environment temperature sensor being connected with described PLC communications.
Described addition mechanism is measuring pump or screw fixed-weight feeder.
The bottom that its solution uses case is set using the port of the pipeline of case feed liquor to described solution.
The bottom of correspondence casing is arranged on to the entrance point for extracting the pipeline of solution and be provided with entrance leaching
Enter formula flowmeter.
The control method of a kind of described silver jacketed wire leaching paint section dispensing and control system, it is characterised in that including following step
Suddenly,
One) paint deployment step
11) PLC monitoring paint uses the liquid level of case with solution, while according to the operation opaquing fluid of the measuring pump for pumping out liquid
Position；
12) when paint is less than predetermined value with solution using the liquid level of case, PLC reads the numerical value of environment thermometer, according to two
The temperature of toluene goes out the proportioning of dimethylbenzene and paint with volatility curve and preset value calculation；
13) PLC control open paint agitator tank electronic vent valve, and according to step 12) in proportioning to paint use
The paint and dimethylbenzene of scheduled volume are pumped into agitator tank and is stirred while starting mixing pump；
14) charging finishes the electronic vent valve of closing and stirs the scheduled time；
15) open electronic vent valve and the paint after allotment is pumped into paint solution using measuring pump and use case；
Two) chemicals adaptation step
21) PLC calculates liquid level by chemicals with flow pump；
22) when chemicals with solution using case liquid level be less than predetermined value, PLC is according to step 21) in result of calculation open
Dynamic measuring pump or screw fixed-weight feeder add the component of respective preset blending ratio amount in chemicals agitator tank and stir；
23) proportion for being measured by densimeter and pH meter and pH value analysis composition are up to standard to judge whether, as up to standard, stop
Addition, such as below standard criterion is added again according to result；If still below standard alert after allotment set point number；
Three) curtain set-up procedure is painted
PLC calculates coated weight and drives regulation motor to adjust water curtain plate to predetermined angle according to the transfer rate and size of base material
Degree.
Compared with prior art, the invention has the beneficial effects as follows：
Allocation process adjusts in real time the addition of chemicals according to the feedback information of allotment solution, so as to ensure that chemistry
The stability and accuracy of product allotment proportioning, reduces or prevents the waste product hidden danger caused because liquid proportion is unstable.Carry out
Silver jacketed wire technological requirement and the test of chemicals proportioning and checking, when improving existing process, can be greatly enhanced the accurate of result
Property and stability.
Description of the drawings
Fig. 1 show the silver jacketed wire leaching paint section dispensing of the present invention and the structural representation of control system.
Specific embodiment
The present invention is described in further detail below in conjunction with the drawings and specific embodiments.It should be appreciated that described herein
Specific embodiment only to explain the present invention, be not intended to limit the present invention.
As shown in figure 1, the silver jacketed wire leaching paint section dispensing and control system of the present invention include,
Agitator tank, its top is provided with electric control exhaust valve, and densimeter and pH meter are provided with it；
Case is used by the solution of measuring pump and pipeline communication with described agitator tank, in it liquid level sensor is provided with；
To the addition mechanism to described agitator tank addO-on therapy and measurable addition, such as measuring pump or spiral quantitative
Batcher；The bottom of correspondence casing is arranged on to the entrance point for extracting the pipeline of solution and be provided with entrance immersion
Formula flowmeter, it is therefore an objective to which solution in bucket is drained into net guarantee accurate measurement simultaneously.
Being arranged on the side of water curtain plate can drive its upset to adjust the regulation motor of paint curtain size, such as stepper motor；
And it is controllable with described liquid level sensor, densimeter, pH meter, electric control exhaust valve, regulation motor and addition mechanism
The PLC of connection.
Preferably, described solution arranges its bottom using the inner port of the pipeline in case, and bottom is provided with immersion
Flowmeter.Can so prevent from causing liquid level to form ripple during charging, affect the precision of liquid level gauge.
Meanwhile, because dimethylbenzene at different temperatures degree of volatility is different, present invention additionally comprises connecting with described PLC communications
The environment temperature sensor for connecing, by monitors environment temperature, according to temperature and volatility curve and the preset value calculation of dimethylbenzene
Go out the proportioning of dimethylbenzene and paint, improve finish paint coating quality, and using addition automatically, reduce human contact, it is to avoid right
The injury of human body.
The control method of silver jacketed wire leaching paint section dispensing of the present invention and control system, comprises the following steps,
One) paint deployment step
11) PLC monitoring paint uses the liquid level of case with solution, while according to the operation opaquing fluid of the measuring pump for pumping out liquid
Position；
12) when paint is less than predetermined value with solution using the liquid level of case, PLC reads the numerical value of environment thermometer, according to two
The temperature of toluene goes out the proportioning of dimethylbenzene and paint with volatility curve and preset value calculation；
13) PLC control open paint agitator tank electronic vent valve, and according to step 12) in proportioning to paint use
The paint and dimethylbenzene of scheduled volume are pumped into agitator tank and is stirred while starting mixing pump；
14) charging finishes the electronic vent valve of closing and stirs the scheduled time；The electronic vent valve of agitator tank medium realizes sealing
Or close sealing state, when running into some cases, when needing shutdown or other actions, paint need not be added for a long time
Solution, and agitated in agitator tank complete etc. to be fed.At this moment agitator tank sealing can prevent dimethylbenzene volatilization from avoiding impact from matching somebody with somebody
Than.
15) open electronic vent valve and the paint after allotment is pumped into paint solution using measuring pump and use case；
Two) chemicals adaptation step
21) PLC calculates liquid level by chemicals with flow pump；
22) when chemicals with solution using case liquid level be less than predetermined value, PLC is according to step 21) in result of calculation open
Dynamic measuring pump or screw fixed-weight feeder add the component of respective preset blending ratio amount；
23) proportion for being measured by densimeter and pH meter and pH value analysis composition are up to standard to judge whether, as up to standard, stop
Addition, such as below standard criterion are added again until meeting standard according to result；
Three) curtain set-up procedure is painted
PLC calculates coated weight and drives regulation motor to adjust water curtain plate to predetermined angle according to the transfer rate and size of base material
Degree.
Concrete manipulation is as follows：
1) PLC reads paint solution and uses case liquid level by liquid level gauge, deposits to enter to reading data with time interval t
Row caching, PLC records the opening/closing time and data on flows of two measuring pumps simultaneously, is sent to server.
2) server calculates the real-time usage information of paint according to liquid level data according to corresponding algorithm, while according to
Real-time usage information is corrected according to measuring pump information.
3) when silver jacketed wire liquid level reaches some liquid level higher limit, PLC reads the numerical value of environment thermometer, according to diformazan
The temperature of benzene goes out the proportioning of dimethylbenzene and paint with volatility curve and allowable error range computation.
4) PLC opens electronic ventilative threshold switch；
5) according to dimethylbenzene and the proportioning of paint, the flow-rate ratio of PLC setting dimethylbenzene measuring pumps and paint measuring pump starts
Flow pump adds dimethylbenzene and paint in agitator tank, while start mixing pump being stirred.
6) when the paint and dimethylbenzene that add reach the 80% of agitator tank, stop measuring pump, close electronic vent valve, according to
Continue to stir according to the mixing time of technological requirement, it is static afterwards.
7) when silver jacketed wire paint and dimethylbenzene mixed solution liquid level reach charging lower limit, electronic vent valve is opened, PLC beats
Motor switch is driven, mixed solution is added into silver jacketed wire paint solution and is used in case.
8) PLC calculates the stream of paint curtain according to paint solution consumption and the piece number ratio and craft precision scope of silvered glass
Amount, is adjusted by adjusting the number of steps of stepper motor to painting curtain flow.
9) two meterings are stopped when material liquid level is less than the lower limit of throw-in type liquid level in dimethylbenzene bucket or paint kettle
Pump, and send charging and report to the police, afterwards more than not feeding in setting time, then its leading body at a higher level of SMS notification.
The addition control of chemical solutions：
1) when silver jacketed wire chemical solutions case solution level reaches lower limit (obtaining by the liquid inventory meter of silver jacketed wire)
When, PLC opens measuring pump and adds ammoniacal liquor and water in agitator tank according to special ratios, and addition is the 80% of its total amount.
2) after the completion of ammoniacal liquor and water add, PLC opens compact spiral constant feeder, by controlling stepper motor/servo
The rotation revolution control solid nitric acid silver feeding coal of motor, addition is the 80% of total amount.
3) charging is completed, and PLC starts stirring motor, the time that stirring technique is required.
4) by PH meters and densimeter measurement solution pH value now and rate of specific gravity, it is to accord with to calculate according to two values to PLC
Close and require.
If 5) as a result meet technological requirement, silver jacketed wire chemical solutions case solution addition signal is waited.
If 6) as a result do not meet technological requirement, PLC provides second charging proportioning according to value of feedback, circulate successively until
Meet the requirements, if do not met the requirements yet after allotment set point number, alert.
7) PLC starts charging motor and measuring pump addition chemicals raw material, and scheduled volume is added again, and such as addition is total amount
5%, by several times uneven addition, is effectively ensured mixed effect and mixing velocity.
8) PLC starts stirring motor, stirs setting time, measures analog value.
9) operate above successively, after reaching requirement, wait silver jacketed wire chemical solutions case solution addition signal as passed through plating
The liquid inventory meter of silver wire is obtained.
10) chemical solutions are required supplementation with, then open motor switch and supplement chemical solutions.
11) if solution reaches called putting-into-type liquid level meter lower limit in ammoniacal liquor or bucket in chemical solutions allocation process
Hereinafter, stop feed, and send the not enough warning of chemicals raw material
If 12) the optoelectronic switch conducting in batcher funnel, equally sends and lacks material warning.
13) the liquid level change that PLC measures high precision liquid level gauge is sent to server, and server calculates liquid consumption and glass
Ratio of the glass piece number in special time is simultaneously stored, used as the reference data of process modification.
In sum, beneficial effects of the present invention are：
Allocation process adjusts in real time the addition of chemicals according to the feedback information of allotment solution, so as to ensure that chemistry
The stability and accuracy of product allotment proportioning, reduces or prevents the waste product hidden danger caused because liquid proportion is unstable.Carry out
Silver jacketed wire technological requirement and the test of chemicals proportioning and checking, when improving existing process, can be greatly enhanced the accurate of result
Property and stability.
By the accurate recording to painting consumption, accurately the consumption of material accurately not only can be controlled, together
When improvement also for technique provide important data.By the accurate adjust automatically to painting curtain size, it is ensured that paint the steady of curtain
It is qualitative, and accurately painting thickness can be controlled in the range of technological requirement by painting the calculating analysis of real-time usage,
Ensure reduces cost on the premise of quality.
Reduce or substituted chemistry product allotment workman and silver jacketed wire chemical solutions consumption tour personnel, reduce manpower into
This, at the same also prevent workers with long time carry out allocate chemical solutions cause to healthy injury.
The above is only the preferred embodiment of the present invention, it is noted that for the common skill of the art
For art personnel, under the premise without departing from the principles of the invention, some improvements and modifications can also be made, these improvements and modifications
Also should be regarded as protection scope of the present invention.
Claims (6)
1. a kind of silver jacketed wire leaching paint section dispensing and control system, it is characterised in that include,
Agitator tank, its top is provided with electric control exhaust valve, and densimeter and pH meter are provided with it；
Case is used by the solution of measuring pump and pipeline communication with described agitator tank, in it liquid level sensor is provided with；
To the addition mechanism that addO-on therapy is measured to described agitator tank,
Being arranged on the side of water curtain plate can drive its upset to adjust the regulation motor of paint curtain size,
And with described liquid level sensor, densimeter, pH meter, electric control exhaust valve, the controllable connection of regulation motor and addition mechanism
PLC.
2. silver jacketed wire leaching paint section dispensing as claimed in claim 1 and control system, it is characterised in that also include with it is described
The environment temperature sensor of PLC communication connections.
3. silver jacketed wire leaching paint section dispensing as claimed in claim 1 and control system, it is characterised in that described addition mechanism is
Measuring pump or screw fixed-weight feeder.
4. silver jacketed wire leaching paint section dispensing as claimed in claim 1 and control system, it is characterised in that use to described solution
The port of the pipeline of case feed liquor arranges the bottom that its solution uses case.
5. silver jacketed wire leaching paint section dispensing as claimed in claim 1 and control system, it is characterised in that to the pipe for extracting solution
The entrance point on road is arranged on the bottom of correspondence casing and immersion flowmeter is provided with entrance.
6. a kind of control method of silver jacketed wire leaching paint section dispensing as claimed in claim 1 and control system, it is characterised in that bag
Include following steps,
One) paint deployment step
11) PLC monitoring paint uses the liquid level of case with solution, while according to the operation amendment liquid level of the measuring pump for pumping out liquid；
12) when paint is less than predetermined value with solution using the liquid level of case, PLC reads the numerical value of environment thermometer, according to dimethylbenzene
Temperature and volatility curve and preset value calculation go out dimethylbenzene and the proportioning painted；
13) PLC control open paint agitator tank electronic vent valve, and according to step 12) in proportioning to paint stirring
The paint and dimethylbenzene of scheduled volume are pumped into case and is stirred while starting mixing pump；
14) charging finishes the electronic vent valve of closing and stirs the scheduled time；
15) open electronic vent valve and the paint after allotment is pumped into paint solution using measuring pump and use case；
Two) chemicals adaptation step
21) PLC calculates liquid level by chemicals with flow pump；
22) when chemicals with solution using case liquid level be less than predetermined value, PLC is according to step 21) in result of calculation start meter
Amount pump or screw fixed-weight feeder add the component of respective preset blending ratio amount in chemicals agitator tank and stir；
23) proportion for being measured by densimeter and pH meter and pH value analysis composition are up to standard to judge whether, addition is stopped if up to standard,
As below standard criterion is added again according to result；If still below standard alert after allotment set point number；
Three) curtain set-up procedure is painted
PLC calculates coated weight and drives regulation motor to adjust water curtain plate to predetermined angular according to the transfer rate and size of base material.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611027046.8A CN106622011A (en) | 2016-11-17 | 2016-11-17 | A blending and controlling system for a paint curtaining segment of a silvering line and a control method thereof |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611027046.8A CN106622011A (en) | 2016-11-17 | 2016-11-17 | A blending and controlling system for a paint curtaining segment of a silvering line and a control method thereof |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106622011A true CN106622011A (en) | 2017-05-10 |
Family
ID=58808595
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201611027046.8A Pending CN106622011A (en) | 2016-11-17 | 2016-11-17 | A blending and controlling system for a paint curtaining segment of a silvering line and a control method thereof |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106622011A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111437770A (en) * | 2020-04-07 | 2020-07-24 | 广东博智林机器人有限公司 | Proportioning system and method |
| CN112878099A (en) * | 2021-02-05 | 2021-06-01 | 互联智慧信息科技(北京)有限公司 | Card paper information element measurement feeding system |
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| WO2003082452A1 (en) * | 2002-03-28 | 2003-10-09 | Cps Color Equipment S.P.A. | Equipment for the metered dispensing of a fluid product, in particular a colouring agent for paints |
| CN101362061A (en) * | 2007-08-07 | 2009-02-11 | 莫雷托股份公司 | Process and device for processing granular material mixtures |
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| CN206276344U (en) * | 2016-11-17 | 2017-06-27 | 天津滨海光热反射技术有限公司 | Silver jacketed wire leaching paint section dispensing and control system |
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| CN111437770A (en) * | 2020-04-07 | 2020-07-24 | 广东博智林机器人有限公司 | Proportioning system and method |
| CN112878099A (en) * | 2021-02-05 | 2021-06-01 | 互联智慧信息科技(北京)有限公司 | Card paper information element measurement feeding system |
| CN112878099B (en) * | 2021-02-05 | 2023-12-01 | 互联智慧信息科技(北京)有限公司 | Card paper information element metering and feeding system |
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