CN205366987U - Automatic accomplish batching conveyor that glass gave birth to grog ratio - Google Patents
Automatic accomplish batching conveyor that glass gave birth to grog ratio Download PDFInfo
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- CN205366987U CN205366987U CN201620033061.2U CN201620033061U CN205366987U CN 205366987 U CN205366987 U CN 205366987U CN 201620033061 U CN201620033061 U CN 201620033061U CN 205366987 U CN205366987 U CN 205366987U
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Abstract
The utility model provides an automatic accomplish batching conveyor that glass gave birth to grog ratio, includes that the station is weighed to band conveyer, raw material, station, first batcher and second batcher are weighed to the grog, the station is weighed including first batching jar and first control ware to raw material, and first batching jar outer wall is equipped with a weighing module, is equipped with in the first batching jar to be used for measuring the ranging module who mixes perpendicular distance between third batcher discharge end that the machine below set up and the first batching jar interior material upper surface, and the real -time data that the first control ware transmitted according to a weighing module and ranging module controls the feed volume of third batcher, the grog is weighed the station and is equipped with the 2nd weighing module including second batching jar and the second controllor, a second batching jar outer wall, and the second controllor is according to the feed volume of the real -time data control second batcher of the 2nd weighing module transmission. The utility model discloses according to ripe ratio of setting for of life, expect that the garrulous glass of flow control arranges the material volume according to the row of mixture, make band conveyer go up and give birth to ripe ratio and meet the demands.
Description
Technical field
This utility model relates to preparing glass charge induction system, is specifically related to a kind of dispensing conveyer device being automatically performed the raw grog proportioning of glass.
Background technology
It is known that a large amount of cullet can be produced in the production of glass, processing and use procedure.According to investigations, existing hundreds of the glass production enterprises of China, often it is only the breakage of domestic glass just at about 2,000,000 tons.Developed countries attaches great importance to the recycling of cullet, the utilization rate such as Germany is 54%, Italy be 44%, Holland up to 66%, and China's cullet recovery utilization rate is only about 10%.Cullet are as the regenerated resources of sustainable use; its a large amount of losses not only waste the very limited amount of energy, raw material; also soil, subsoil water etc. are caused new harm, if making full use of economizing on resources, reduce cost and environmental conservation has immeasurable effect.Traditional cullet marker method, is directly pour in conveyer by disposable for whole cullet, namely completes operation, but the raw grog of discharge uneven, by the practice produced, the instability of the temperature schedule of melting furnaces and consuming excessively of fuel can be caused.
Utility model content
The purpose of this utility model is to provide a kind of dispensing conveyer device being automatically performed the raw grog proportioning of glass, it is ensured that compound raw material and two kinds of materials of cullet grog, can both be uniform according to setting percentage ratio in any position of belt conveyor.
The technical scheme that this utility model adopts for achieving the above object is: a kind of dispensing conveyer device being automatically performed the raw grog proportioning of glass, including belt conveyor, belt conveyor be arranged over raw material weighing station and grog weighing station, and the head end of raw material weighing station and belt conveyor is correspondingly arranged, raw material weighing station bottom is connected to for by the first batcher on raw material conveyor to belt conveyor, and grog weighing station bottom is connected to the second batcher for being discharged into by grog on belt conveyor；Described raw material weighing station includes the first material-compound tank and the first controller, first material-compound tank top is connected to mixer, the 3rd batcher it is additionally provided with between mixer and the first material-compound tank, the outer wall of the first material-compound tank is provided with the first Weighing module, being provided with for measuring in the 3rd batcher discharge end and the first material-compound tank the range finder module of vertical dimension between material upper surface in first material-compound tank, the first controller controls the feeding coal of the first batcher according to the real time data that the first Weighing module and range finder module transmit；Described grog weighing station includes the second material-compound tank and second controller, and the outer wall of the second material-compound tank is provided with the second Weighing module, and second controller controls the feeding coal of the 3rd batcher according to the real time data that the second Weighing module transmits.
Further, the end of belt conveyor is provided with dump skip, and dump skip top is provided with cleaner unit, and dump skip bottom is accepted and is provided with kiln hood storehouse.
In this utility model, the first described material-compound tank outer wall is provided with three bearings along its circumference uniform intervals, and each bearing is correspondingly provided with first Weighing module.
In this utility model, the second described material-compound tank outer wall is provided with three bearings along its circumference uniform intervals, and each bearing is correspondingly provided with second Weighing module.
In this utility model, described the first batcher, the second batcher and the 3rd batcher are electro-vibrating feeder.
nullBeneficial effect: this device is in use，Start the first batcher in advance and carry out discharge raw material，When raw material arrive grog weighing station，Second controller controls the emission flow of the second batcher addition cullet according to setting percentage ratio，According to the raw ripe ratio of the ratio requirement of the compound set and cullet，Withdrawal rate according to compound，Control cullet discharge flow，On any point made on the batch of conveying on belt conveyor，The proportioning of compound and cullet is satisfied by the requirement of raw ripe ratio，Ensure that compound and cullet two kinds of materials set-mounted percentage ratio on belt conveyor are uniform，Guarantee that the ratio of compound and cullet is steady state value on belt conveyor，Be equivalent to compound and cullet are once remixed fully，Stable raw grog premix is conducive to the temperature of melting furnaces to control，Guarantee stablizing of vitreous humour fusion process.
Accompanying drawing explanation
Fig. 1 is schematic diagram of the present utility model；
Fig. 2 is the schematic diagram of the first material-compound tank；
Fig. 3 is the schematic diagram of the second material-compound tank；
Fig. 4 is compound and cullet discharge curve chart.
Accompanying drawing labelling: 1, belt conveyor, 2, raw material weighing station, the 20, first material-compound tank, 21, the first controller, the 22, first Weighing module, 23, range finder module, 3, grog weighing station, the 30, second material-compound tank, 31, second controller, 32, the second Weighing module, the 4, first batcher, the 5, second batcher, 6, mixer, the 7, the 3rd batcher, 8, dump skip, 9, cleaner unit, 10, kiln hood storehouse, 11, bearing.
Detailed description of the invention
Below in conjunction with specific embodiment, the dispensing conveyer device being automatically performed the raw grog proportioning of glass of the present utility model is described further, so that those skilled in the art can be better understood from this utility model and can be practiced, but illustrated embodiment is not as to restriction of the present utility model.
A kind of dispensing conveyer device being automatically performed the raw grog proportioning of glass, as shown in Figure 1, including belt conveyor 1, belt conveyor 1 be arranged over raw material weighing station 2 and grog weighing station 3, and the head end of raw material weighing station 2 and belt conveyor 1 is correspondingly arranged, the end of belt conveyor 1 is provided with dump skip 8, and dump skip 8 top is provided with cleaner unit 9, and dump skip 8 bottom is accepted and is provided with kiln hood storehouse 10.Raw material weighing station 2 bottom is connected to for by the first batcher 4 on raw material conveyor to belt conveyor 1, and grog weighing station 3 bottom is connected to the second batcher 5 for being discharged into by grog on belt conveyor 1.Wherein, first batcher the 4, second batcher 5 and the 3rd batcher 7 are electro-vibrating feeder.
As shown in Figure 2, raw material weighing station 2 includes the first material-compound tank 20 and the first controller 21, first material-compound tank 20 top is connected to mixer 6, it is additionally provided with the 3rd batcher 7 between mixer 6 and the first material-compound tank 20, the centrage to the first material-compound tank 20 is rectified in the discharging of the 3rd batcher 7, the outer wall of the first material-compound tank 20 is provided with the first Weighing module 22, and the first material-compound tank outer wall 20 is provided with three bearings along its circumference uniform intervals, and each bearing is correspondingly provided with first Weighing module 22.Being provided with for measuring in the 3rd batcher 7 discharge end and the first material-compound tank 20 range finder module 23 of vertical dimension between material upper surface in first material-compound tank 20, the first controller 21 controls the feeding coal of the 3rd batcher 7 according to the real time data that the first Weighing module 22 and range finder module 23 transmit.nullThe first Weighing module 22 and range finder module 23 is adopted to match，Vertical dimension between material upper surface in the 3rd batcher 7 discharge end that first controller 21 is measured according to range finder module 23 and the first material-compound tank 20，Calculate the blanking time，According to blanking speed and blanking time，Calculate suspension amount weight，When the first Weighing module 22 detect in the first material-compound tank 20 the weighing value of material deduct suspension amount gravimetric value equal to formula value or within range of error when，First controller 21 sends halt instruction，Stop the 3rd batcher 7 immediately to feed in raw material，That is give the weight turned off in advance automatically，Owing to flow accurately calculates，Enable the system to obtain real-time suspension amount weight data accurately，Suspended material can be carried out quantification treatment accurately，To ensure that suspended material will accurately and strictly by weighed amount control within range of error after falling into，Reach the purpose of non differential regulation.
As shown in Figure 3, grog weighing station 3 includes the second material-compound tank 30 and second controller 31, the outer wall of the second material-compound tank 30 is provided with the second Weighing module 32, and the second material-compound tank 30 outer wall is provided with three bearings along its circumference uniform intervals, and each bearing is correspondingly provided with second Weighing module 32.Second controller 31 controls the feeding coal of the second batcher 5 according to the real time data that the second Weighing module 32 transmits.
The control process of this device: only need to set the addition percentage 20% of cullet for user, the first controller 21 and second controller 31 are PLC.Mixer 6 discharge enters raw material weighing station 2, first controller 21 controls the 3rd batcher 7 and stops material and the first batcher 4 discharge, now, first controller 21 records compound emission flow curve on belt conveyor 1, when compound arrives grog weighing station 3, in grog weighing station 3 by the flow curve according to compound, the emission flow controlling the second batcher 5 according to setting percentage ratio adds cullet, ensure that compound and two kinds of materials of cullet are strictly uniform by setting percentage ratio in any position of belt conveyor 1, ratio at belt conveyor any position compound Yu cullet is all steady state value 1:0.2.Wherein, the discharge curve chart of compound and cullet is as shown in Figure 4.
This utility model enters flow and the flow curve of belt conveyor 1 by detecting compound, according to the raw ripe ratio of the ratio requirement of the compound set and cullet, withdrawal rate according to compound, control cullet discharge flow, the proportioning making the cullet on any point on the batch of belt conveyor 1 conveying and compound is satisfied by the requirement of raw ripe ratio, the discharge of cullet whole process is realized servo-actuated according to setting ratio tracking discharge, ensure that the ratio at belt conveyor any position compound Yu cullet is all steady state value, stable raw grog premix is conducive to the temperature of melting furnaces to control, guarantee stablizing of vitreous humour fusion process.
This utility model guarantees compound and cullet according to the strict ripe ratio requirement of predetermined life, evenly laid out on belt conveyor 1, is transported to kiln hood storehouse 9.By the practice produced, in various preparing glass charge systems, use this device, stable and fuel the consumption of the temperature schedule of melting furnaces can all be had some improvement.Wherein, this device can provide as integral device, and cullet discharge controls the electro-vibrating feeder controllable silicon controller of employing standard, and this controller is also by complete offer.
Claims (5)
1. the dispensing conveyer device being automatically performed the raw grog proportioning of glass, including belt conveyor (1), it is characterized in that: belt conveyor (1) be arranged over raw material weighing station (2) and grog weighing station (3), and the head end of raw material weighing station (2) and belt conveyor (1) is correspondingly arranged, raw material weighing station (2) bottom is connected to for by the first batcher (4) on raw material conveyor to belt conveyor (1), and grog weighing station (3) bottom is connected to the second batcher (5) for being discharged into by grog on belt conveyor (1)；
Described raw material weighing station (2) includes the first material-compound tank (20) and the first controller (21), first material-compound tank (20) top is connected to mixer (6), the 3rd batcher (7) it is additionally provided with between mixer (6) and the first material-compound tank (20), the outer wall of the first material-compound tank (20) is provided with the first Weighing module (22), it is provided with for measuring the range finder module (23) of vertical dimension between the 3rd batcher (7) discharge end and the interior material upper surface of the first material-compound tank (20) in first material-compound tank (20), first controller (21) controls the feeding coal of the 3rd batcher (7) according to the real time data that the first Weighing module (22) and range finder module (23) transmit；Described grog weighing station (3) includes the second material-compound tank (30) and second controller (31), the outer wall of the second material-compound tank (30) is provided with the second Weighing module (32), and second controller (31) controls the feeding coal of the second batcher (5) according to the real time data that the second Weighing module (32) transmits.
2. a kind of dispensing conveyer device being automatically performed the raw grog proportioning of glass according to claim 1, it is characterized in that: the end of belt conveyor (1) is provided with dump skip (8), dump skip (8) top is provided with cleaner unit (9), and dump skip (8) bottom is accepted and is provided with kiln hood storehouse (10).
3. a kind of dispensing conveyer device being automatically performed the raw grog proportioning of glass according to claim 1, it is characterized in that: the first described material-compound tank outer wall (20) is provided with three bearings along its circumference uniform intervals, and each bearing is correspondingly provided with first Weighing module (22).
4. a kind of dispensing conveyer device being automatically performed the raw grog proportioning of glass according to claim 1, it is characterized in that: described the second material-compound tank (30) outer wall is provided with three bearings along its circumference uniform intervals, and each bearing is correspondingly provided with second Weighing module (32).
5. a kind of dispensing conveyer device being automatically performed the raw grog proportioning of glass according to claim 1, it is characterised in that: described the first batcher (4), the second batcher (5) and the 3rd batcher (7) are electro-vibrating feeder.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620033061.2U CN205366987U (en) | 2016-01-14 | 2016-01-14 | Automatic accomplish batching conveyor that glass gave birth to grog ratio |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201620033061.2U CN205366987U (en) | 2016-01-14 | 2016-01-14 | Automatic accomplish batching conveyor that glass gave birth to grog ratio |
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| CN205366987U true CN205366987U (en) | 2016-07-06 |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112358166A (en) * | 2020-12-11 | 2021-02-12 | 重庆鑫景特种玻璃有限公司 | Automatic control system for regulating and controlling discharge capacity of glass kiln |
| CN111427314B (en) * | 2020-03-16 | 2021-09-21 | 浙江大华技术股份有限公司 | Batching system and batching method |
| CN114408459A (en) * | 2021-12-30 | 2022-04-29 | 中国建材国际工程集团有限公司 | Glass mill's garrulous glass conveying system of batch |
-
2016
- 2016-01-14 CN CN201620033061.2U patent/CN205366987U/en active Active
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111427314B (en) * | 2020-03-16 | 2021-09-21 | 浙江大华技术股份有限公司 | Batching system and batching method |
| CN112358166A (en) * | 2020-12-11 | 2021-02-12 | 重庆鑫景特种玻璃有限公司 | Automatic control system for regulating and controlling discharge capacity of glass kiln |
| CN112358166B (en) * | 2020-12-11 | 2023-11-21 | 重庆鑫景特种玻璃有限公司 | Automatic control system for regulating and controlling unloading amount of glass kiln |
| CN114408459A (en) * | 2021-12-30 | 2022-04-29 | 中国建材国际工程集团有限公司 | Glass mill's garrulous glass conveying system of batch |
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