CN101033042A - Glass waster material fluid transmission system - Google Patents
Glass waster material fluid transmission system Download PDFInfo
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- CN101033042A CN101033042A CN 200610058882 CN200610058882A CN101033042A CN 101033042 A CN101033042 A CN 101033042A CN 200610058882 CN200610058882 CN 200610058882 CN 200610058882 A CN200610058882 A CN 200610058882A CN 101033042 A CN101033042 A CN 101033042A
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- glass
- transmission system
- fluid transmission
- waster
- material fluid
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Abstract
This invention provides a fluid transmission system for glass wastes used in a dust-free chamber, in which, glass wastes are blown to a double-layer pipeline via a fan in low pressure and mid-speed and a pressure meter can be installed to monitor the pipeline, which is suitable for addition to current designs of workshops and is not limited by long distant pipelines or curvatures and the sealed transmission pipeline will not pollute environment.
Description
Technical field
The present invention relates to a kind of glass waste processing equipment, particularly relate to a kind of glass waster material fluid transmission system that is applied in the dust free room.
Background technology
Thin film transistor (TFT), Liquid Crystal Display (LCD) (LCD) opto-electronics circle are to satisfy the demand in face glass market now, therefore the production capacity of manufacturing line is alloted to maximum, but what produce is a large amount of residue rim charges after the cutting thereupon, the handling problem of this glass rim charge not only causes waste of manpower of panel factory and funds to go to handle, labor safety incident such as also cause that personnel hurt easily sometimes.
The processing mode of known glass waste material is the manpower carrying method, but this method is very consuming time, waste of manpower, and money, and does not meet economic benefit and cost, so the industrial community tendency adopts the automation load mode.
The type of transmission that existing opto-electronics circle nearly all adopts belt to carry method or spiral tube to carry method to handle as glass waste.Though these two kinds of type of transmission are comparatively saved the carrying manpower, but it is large volume and the complicated mechanism of design, makes the space availability ratio variation to be subject to its existing space easily; It is longer to set up difficulty and construction time, and its maintenance manpower is many; And be easy to dust and produced, may cause the reduction of the qualification rate and the quality of product.
Summary of the invention
In view of the foregoing, the object of the present invention is to provide a kind of glass waster material fluid delivery system, its volume simple in structure is little, and can not cause the pollution of working environment.
For achieving the above object, the invention provides a kind of glass waster material fluid transmission system, wherein this system comprises: an accumulator tank is connected in a transfer line, for placing powder glass waste material part; The single-revolution valve is the discharge control cock of this accumulator tank, is arranged on this transfer line; Double-deck delivery duct for carrying the pipeline of this powder glass waste material, wherein should comprise delivery pipe in an outer delivery pipe and by the bilayer delivery duct; The gas delivery engine installation is connected with this bilayer delivery duct, is used as the propulsion source that this powder glass waste material moves; And a feedback control unit, it is used to monitor the discharge of this rotovalve and the power size of described gas delivery engine installation.
In above-mentioned glass waster material fluid transmission system, delivery pipe is a seamless transfer line in this.
In above-mentioned glass waster material fluid transmission system, surface, inside of delivery pipe is coated with one deck abrasion resistant alloy metal material in this.
In above-mentioned glass waster material fluid transmission system, this abrasion resistant alloy metal material is chromium alloy, nickel alloy, titanium nitride alloy or titanium-tungsten.
In above-mentioned glass waster material fluid transmission system, the weighting material in the space between this outer delivery pipe of this bilayer delivery duct and this interior delivery pipe is the powder glass waste material.
In above-mentioned glass waster material fluid transmission system, this bilayer delivery duct is set up at least one manifold in an appropriate position, and described manifold links to each other with a blowing engine.
In above-mentioned glass waster material fluid transmission system, this bilayer delivery duct also installs several compression indicators additional.
In above-mentioned glass waster material fluid transmission system, this bilayer delivery duct tail end is provided with a storage bucket, and this storage bucket top connects a vaccum-pumping equipment.
In above-mentioned glass waster material fluid transmission system, this gas delivery engine installation is a blowing engine.
Glass waster material fluid delivery system of the present invention provides simple and the design of small size pipeline, sets up in the space of existing factory building with facility; The mode of movement of its low pressure middling speed make that the conveying of long distance is more easy, and the angle design of pipeline more has the space of performance; It can also by control rotovalve rotating speed (run perminute RPM), controls the operational throughput of fluid efficiently; Transfer line is the fully enclosed environment, the therefore pollution that can not produce dust, and institute is so that work and production environment are cleaner and tidier; Especially equipment is simple, makes maintaining simpler.
That is to say, the invention provides a kind of glass waster material fluid delivery system, this system comprises a blowing engine, single-revolution valve, two-layer at least above delivery tube, accumulator tank, reaches a feedback control unit.
At first with this glass waste through behind viteous fracture, make it become size and be the graininess of 50mm-10mm, utilize disintegrating mechanism that this granular glass waste is smashed Powdered to 1mm * 1mm again, be positioned in the accumulator tank at last.
The present invention utilizes blowing engine to blow the interior Powdered glass waste of accumulator tank; Double layer pipeline via particular design is carried; its outside installs the pressure that compression indicator is monitored this transfer line at any time additional; so when compression indicator feedback mal or broken pipe; can be by feedback control unit acquired information, and can take treatment step immediately.And the design of carrying of this Double layer pipeline, can not produce any dust fully to dust free room, and then the situation of the product that causes having problems.
The size of this Double layer pipeline is littler than traditional large scale delivery pipe, therefore can be installed in easily on existing other pipeline frame, and as electric wire, water pipe, breather pipe or the like, and this double tube design is not subjected to the restriction of fed distance or angle.Because blowing engine adopts the mode that blows of low pressure middling speed, as long as design suitable airshed, the loss of pressure that transportation volume and pipeline are connected or turn and caused just can drive Powdered glass waste to very long distance, and the delivery duct by any angle easily.When the length of this double-deck delivery duct, surpass the conveying strength of a blowing engine, and Powdered glass waste can't be sent to the time, can install manifold outward additional and be connected in another blowing engine as the power of strengthening blowing.
For cooperating the different of each tame factory building position and distance, can install many blowing engines additional and make in the pipeline end and carry strength bigger to cooperatively interact or to install vacuum-pumping equipment additional, the length that is suitable for large-sized workshop is apart from transfer line.The propulsion source that also can use vacuum-pumping equipment to do delivery air in the pipeline end merely weares and teares to reduce pipeline, thereby increases duration of service.The mode that can carry from the bottom up in addition, for example factory building is positioned at the position of subterranean room, needs waste material to carry from lower to upper, so this mode of movement from lower to upper can reach its purpose easily.
So the present invention can reach easily and simplify manpower, saving trucking expenses, so the cost-cutting expense; Simplify the internal structure of an organization and transfer process, make maintenance of equipment and maintenance simpler and easy; With the direct recycling of this glass waste, and then meet the advanced idea of modern environmental protection.
Cooperate detailed description and the claim of following diagram, embodiment at this, will on address other objects and advantages of the present invention and be specified in after.
Description of drawings
The step that Fig. 1 handles for glass waste;
Fig. 2 is the scheme drawing of fluid delivery system of the present invention;
Fig. 3 is the second embodiment of the present invention;
Fig. 4 is the third embodiment of the present invention;
Fig. 5 is the fourth embodiment of the present invention.
Wherein, description of reference numerals is as follows:
11 viteous fracturees, 12 pulverization process
13 fluid delivery systems 14 store and filing collector
15 recycle
21 accumulator tanks, 22 pulverous glass wastes
23 rotovalves, 24 feedback control units
25 blowing engines, 26 double-deck delivery ducts
Delivery pipe in the 261 outer delivery pipes 262
263 adaptor unions, 28 compression indicators
30 pressure spaces, 31 smalls weighting materials
41 blowing engines
51 vaccum-pumping equipments, 52 storage buckets
53 connection pipes
The specific embodiment
The step that Fig. 1 handles for glass waste.At first, behind the glass waste process viteous fracture 11 with the generation of photoelectricity factory, become the particle of 50mm-10mm size, utilize pulverization process 12 again, make this particle be milled to the Powdered glass waste of 1mm * 1mm, by fluid delivery system 13 this Powdered glass waste is concentrated on storage and filing collector 14, utilize truck to carry at last as specific recycling 15.
Fig. 2 is the scheme drawing of fluid delivery system of the present invention.This system comprises accumulator tank 21, Powdered glass waste 22, single-revolution valve 23, a feedback control unit 24, a gas delivery engine installation and double-deck delivery duct 26.This gas delivery engine installation can be blowing engine 25 or vaccum-pumping equipment.Wherein the gas delivery engine installation is connected with double-deck delivery duct 26, is used as the propulsion source that this powder glass waste material moves.
This double-deck delivery duct 26 also comprises outer delivery pipe 261, one an interior delivery pipe 262, reaches several adaptor unions 263.Should can be a seamless transfer line by interior delivery pipe.
Rotovalve 23 is the size of these Powdered glass waste 22 flows of adjustment, and is connected with feedback control unit 24.This feedback control unit 24 is monitored the output strength of rotovalve 22 blowing engines 25 simultaneously, and can receive the situation of the integral pressure feedback of several compression indicators 28 that add.
Fig. 3 is the second embodiment of the present invention.Present embodiment will not assemble any compression indicator 263, but with smalls weighting material 31 fill up in interior delivery pipe 262 with outside the intermediate gaps of delivery pipe 261.It is the filling material of the best that this powder weighting material 31 is worked as with powder glass waste material 22, when outer delivery pipe 261 has when breaking or wearing and tearing, can fill up its breakage on the contrary and flow in addition the powder glass waste material 22 of delivery pipe 261, delivery pipe 261 is still kept completely beyond the institute, does not have the situation that powder glass waste material 22 leaks outside and takes place.
Fluid delivery system of the present invention also can increase blowing engine as embodiment, with reference to figure 4.Be displaced in the delivery pipe of longer distance in order to make the powder glass waste material can have steady speed, therefore present embodiment is set up at least one manifold 42 in the appropriate location, this manifold 42 directly communicates in interior delivery pipe 262, and passes outer delivery pipe 261, is connected with blowing engine 41 again.This design is applicable to long transmission apart from delivery pipe, and is applicable to the pipeline (with reference to figure 3) of manometric pipeline of device (with reference to figure 2) or powder weighting material, and the effect of highly significant can both be arranged.
Fig. 5 is the fourth embodiment of the present invention.Present embodiment adds pair of lamina pipeline 53 in the upper position of storage bucket 52, and is connected in a vaccum-pumping equipment 51.This principle of design is for when powder glass waste material 22 blows to storage bucket 52 via blowing engine 25, and the transfer line of this section can produce the effect of a malleation; And the vaccum-pumping equipment 51 that is connected in storage bucket 52 tops draws mode with suction, and these storage bucket 52 inner airs are discharged, and can produce the effect of a negative pressure this moment.Therefore, the present invention utilizes this malleation, negative pressure principle, makes the delivery speed of fluid, stability more significantly reach more efficient.
But the above only for the most preferred embodiment of invention, can not limit scope of the invention process according to this.Be all equivalent variations and modifications of in claim scope of the present invention, being done, all should still belong in the scope that the present invention contains.
Claims (12)
1. glass waster material fluid transmission system, wherein this system comprises:
One accumulator tank is connected in a transfer line, for placing powder glass waste material part;
The single-revolution valve is the discharge control cock of this accumulator tank, is arranged on this transfer line;
Double-deck delivery duct for carrying the pipeline of this powder glass waste material, wherein should comprise delivery pipe in an outer delivery pipe and by the bilayer delivery duct;
The gas delivery engine installation is connected with this bilayer delivery duct, is used as the propulsion source that this powder glass waste material moves; And
One feedback control unit, it is used to monitor the discharge of this rotovalve and the power size of described gas delivery engine installation.
2. glass waster material fluid transmission system as claimed in claim 1 should interior delivery pipe be a seamless transfer line wherein.
3. glass waster material fluid transmission system as claimed in claim 1, the surface, inside of delivery pipe is coated with one deck abrasion resistant alloy metal material in wherein being somebody's turn to do.
4. glass waster material fluid transmission system as claimed in claim 3, wherein this abrasion resistant alloy metal material is a chromium alloy.
5. glass waster material fluid transmission system as claimed in claim 3, wherein this abrasion resistant alloy metal material is a nickel alloy.
6. glass waster material fluid transmission system as claimed in claim 3, wherein this abrasion resistant alloy metal material is the titanium nitride alloy.
7. glass waster material fluid transmission system as claimed in claim 3, wherein this abrasion resistant alloy metal material is a titanium-tungsten.
8. glass waster material fluid transmission system as claimed in claim 1, wherein should the bilayer delivery duct should outer delivery pipe with this interior delivery pipe between the weighting material in space be the powder glass waste material.
9. glass waster material fluid transmission system as claimed in claim 1 wherein should set up at least one manifold in an appropriate position by the bilayer delivery duct, and described manifold links to each other with blowing engine.
10. glass waster material fluid transmission system as claimed in claim 1 wherein should also install several compression indicators additional by the bilayer delivery duct.
11. glass waster material fluid transmission system as claimed in claim 1 wherein should be provided with a storage bucket by bilayer delivery duct tail end, and this storage bucket top connects a vaccum-pumping equipment.
12. glass waster material fluid transmission system as claimed in claim 1, wherein this gas delivery engine installation is a blowing engine.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200610058882 CN101033042A (en) | 2006-03-08 | 2006-03-08 | Glass waster material fluid transmission system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200610058882 CN101033042A (en) | 2006-03-08 | 2006-03-08 | Glass waster material fluid transmission system |
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| CN101033042A true CN101033042A (en) | 2007-09-12 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 200610058882 Pending CN101033042A (en) | 2006-03-08 | 2006-03-08 | Glass waster material fluid transmission system |
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| CN (1) | CN101033042A (en) |
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102530525A (en) * | 2012-02-20 | 2012-07-04 | 北京佳时代包装制品有限责任公司 | Feeder with radial air grid plates |
| CN102900911A (en) * | 2012-09-21 | 2013-01-30 | 三一重工股份有限公司 | Double-layer connecting bent pipe, double material pipe and connecting method of double material pipe |
| CN103466326A (en) * | 2013-08-26 | 2013-12-25 | 张家港保税区万盛机械工业有限公司 | Dilute-phase positive-pressure conveying device |
| CN103569676A (en) * | 2012-07-27 | 2014-02-12 | 李宁 | Mobile high-efficiency grain conveying vehicle |
| CN104640683A (en) * | 2012-09-04 | 2015-05-20 | 温德默勒&霍乐沙两合公司 | Device for suctioning off waste products from a production machine, comprising a suction element |
| CN105715895A (en) * | 2016-04-06 | 2016-06-29 | 南京普能新材料科技有限公司 | Slurry insulating, defoaming and delivering pipe of perfluorinated ionomer membrane for tape casting |
| CN106276260A (en) * | 2016-09-20 | 2017-01-04 | 河南工业大学 | The air conveying spiral of Dual-Phrase Distribution of Gas olid distance strengthens system |
| CN107498031A (en) * | 2017-08-19 | 2017-12-22 | 合肥智贤智能化科技有限公司 | A kind of pouring ladle sand-removal device |
| CN109987416A (en) * | 2019-03-18 | 2019-07-09 | 吴元修 | A kind of electric automatization gas pushes away feed device |
| CN111013372A (en) * | 2019-12-26 | 2020-04-17 | 龚明瀚 | Fluidization groove for flue gas treatment process |
| CN112425369A (en) * | 2020-12-02 | 2021-03-02 | 云南农业大学 | Coffee fresh fruit harvesting device |
-
2006
- 2006-03-08 CN CN 200610058882 patent/CN101033042A/en active Pending
Cited By (17)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102530525B (en) * | 2012-02-20 | 2015-04-22 | 北京佳时代包装制品有限责任公司 | Feeder with radial air grid plates |
| CN102530525A (en) * | 2012-02-20 | 2012-07-04 | 北京佳时代包装制品有限责任公司 | Feeder with radial air grid plates |
| CN103569676A (en) * | 2012-07-27 | 2014-02-12 | 李宁 | Mobile high-efficiency grain conveying vehicle |
| US9764896B2 (en) | 2012-09-04 | 2017-09-19 | Windmöller & Hölscher Kg | Device for suctioning off waste products from a production machine, comprising a suction element |
| CN104640683A (en) * | 2012-09-04 | 2015-05-20 | 温德默勒&霍乐沙两合公司 | Device for suctioning off waste products from a production machine, comprising a suction element |
| CN102900911A (en) * | 2012-09-21 | 2013-01-30 | 三一重工股份有限公司 | Double-layer connecting bent pipe, double material pipe and connecting method of double material pipe |
| CN102900911B (en) * | 2012-09-21 | 2016-03-23 | 三一重工股份有限公司 | The connecting means of extra quality pipe and extra quality pipe |
| CN103466326A (en) * | 2013-08-26 | 2013-12-25 | 张家港保税区万盛机械工业有限公司 | Dilute-phase positive-pressure conveying device |
| CN103466326B (en) * | 2013-08-26 | 2016-04-13 | 张家港保税区万盛机械工业有限公司 | Dilute phase positive-pressure conveying device |
| CN105715895A (en) * | 2016-04-06 | 2016-06-29 | 南京普能新材料科技有限公司 | Slurry insulating, defoaming and delivering pipe of perfluorinated ionomer membrane for tape casting |
| CN106276260A (en) * | 2016-09-20 | 2017-01-04 | 河南工业大学 | The air conveying spiral of Dual-Phrase Distribution of Gas olid distance strengthens system |
| CN106276260B (en) * | 2016-09-20 | 2018-06-22 | 河南工业大学 | Gas-solid phase long range Geldart-D particle spiral enhances system |
| CN107498031A (en) * | 2017-08-19 | 2017-12-22 | 合肥智贤智能化科技有限公司 | A kind of pouring ladle sand-removal device |
| CN109987416A (en) * | 2019-03-18 | 2019-07-09 | 吴元修 | A kind of electric automatization gas pushes away feed device |
| CN111013372A (en) * | 2019-12-26 | 2020-04-17 | 龚明瀚 | Fluidization groove for flue gas treatment process |
| CN111013372B (en) * | 2019-12-26 | 2022-05-13 | 广东建绿环保工程有限公司 | Fluidization groove for flue gas treatment process |
| CN112425369A (en) * | 2020-12-02 | 2021-03-02 | 云南农业大学 | Coffee fresh fruit harvesting device |
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Open date: 20070912 |