CN108178500A - A kind of basalt fibre waste silk recycling system - Google Patents
A kind of basalt fibre waste silk recycling system Download PDFInfo
- Publication number
- CN108178500A CN108178500A CN201711496109.9A CN201711496109A CN108178500A CN 108178500 A CN108178500 A CN 108178500A CN 201711496109 A CN201711496109 A CN 201711496109A CN 108178500 A CN108178500 A CN 108178500A
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- CN
- China
- Prior art keywords
- basalt fibre
- waste silk
- feeding device
- conveying trough
- basalt
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- 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.)
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Classifications
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- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B37/00—Manufacture or treatment of flakes, fibres, or filaments from softened glass, minerals, or slags
- C03B37/01—Manufacture of glass fibres or filaments
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geochemistry & Mineralogy (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Preliminary Treatment Of Fibers (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
The present invention discloses a kind of basalt fibre waste silk recycling system, wire-drawing frame including producing basalt fibre, conveyer belt for transmitting basalt waste silk is set below the wire-drawing frame, conveyer belt tail end is equipped with incinerator, ball mill is equipped with behind incinerator, the feeding device I for adding in the waste silk recycled is equipped with behind ball mill, feeding device I connects kiln, the feeding device II for adding in basalt stone is additionally provided on kiln.Relative to the prior art, by treated, basalt fibre waste silk is added to as a kind of new raw material in basalt fibre batch the recycling system of the present invention according to a certain percentage, after mixing, basalt fibre wire-drawing operation production is carried out according to normal basalt fibre technological process input kiln, realizes recycling for basalt fibre waste silk.
Description
Technical field
The present invention relates to basalt technical fields, and in particular to a kind of basalt fibre waste silk recycling system.
Background technology
Basalt fibre is using broken basalt rock as material, in 1450~1500 DEG C of gas burning kiln or electric heating
After middle thawing, then the continuous fiber cutting formed is drawn by platinum-rhodium alloy bushing and is formed.Basalt fibre not only has height
Intensity, high-modulus, also with the excellent characteristics such as acid and alkali-resistance, high temperature resistant, ageing-resistant, low humidity, renewable.
Basalt fibre waste silk is the industrial tailing generated in basalt fibre production, is a kind of solid waste.It is this
Solid waste has to look for a suitable utilization ways, is a greatly burden for manufacturing enterprise, to society otherwise
Very big waste but will be caused for meeting.Therefore, this field urgent need is a kind of can realize what basalt fibre waste silk recycled
Device.
Invention content
To solve the above problems, the present invention provides a kind of basalt fibre waste silk recycling system.
The purpose of the present invention is what is realized in the following manner：
A kind of basalt fibre waste silk recycling system, the wire-drawing frame including producing basalt fibre, the wire-drawing frame
For transmitting the conveyer belt of basalt waste silk, conveyer belt tail end is equipped with incinerator, ball mill is equipped with behind incinerator for lower section setting,
The feeding device I for adding in the waste silk recycled is equipped with behind ball mill, feeding device I connects kiln, use is additionally provided on kiln
In the feeding device II for adding in basalt stone.
Screening plant is equipped between the ball mill and feeding device I.
The feeding device I and feeding device II be can quantitative, automatic, continuous feed arrangement, and feeding device II
Charging rate is five times of the charging rate of feeding device I.
The feeding device I is identical with the structure of feeding device II, including storage bin 1, storing bin bracket and control system
System, the storage bin 1 are furnished with metering device, and the lower section of storage bin 1 is equipped with feed supplement conveying trough 2, one end edge storage of feed supplement conveying trough 2
Feed bin 1 protrudes horizontally up, and is provided with cylinder charger 3 below one end that feed supplement conveying trough 2 stretches out, 3 bottom of cylinder charger is equipped with
Flowmeter and propeller, the one side edge of the top of cylinder charger 3 are equipped with charging conveying trough 4, feed one end of conveying trough 4 along circle
Cylinder charger 3 protrudes horizontally up, and is equipped with feeding cylinder 5 below one end that charging conveying trough 4 stretches out, feeding cylinder 5 is connect with kiln 6；Institute
It states 3 inner wall of cylinder charger to accept equipped with helicla flute, helicla flute top and one end of charging conveying trough 4, cylinder charger 3 can
Quantitative continuous feed, material are transferred to by the helicla flute of 3 inner wall of cylinder charger on charging conveying trough 4.
Preferably, the top of the feeding cylinder 5 is equipped with feeding cylinder head 51, and feeding cylinder head 51 is hollow cube, into
Every one side edge of 51 upper end of barrel head is connected with baffle 52, and baffle 52 is respectively positioned on feeding cylinder head 51 during normal work
There are the gaps of charging on internal and central axis.
Preferably, the charging conveying trough 4 is U-lag, and the bottom of U-lag is arc.
Beneficial effects of the present invention：Relative to the prior art, recycling system of the invention will treated basalt
Fiber waste silk is added to as a kind of new raw material in basalt fibre batch according to a certain percentage, after mixing, according to
Normal basalt fibre technological process input kiln carries out basalt fibre wire-drawing operation production, realizes basalt fibre and gives up
Silk recycles.
Description of the drawings
Fig. 1 is the flow chart of the present invention.
Fig. 2 is the structure diagram of the feeding device of the present invention.
Wherein, 1 is storage bin；2 be feed supplement conveying trough；3 be cylinder charger；4 be charging conveying trough；5 be feeding cylinder；6
It is kiln；51 be feeding cylinder head；52 be baffle.
Specific embodiment
1, Fig. 2 and specific embodiment are described in further detail the present invention below in conjunction with the accompanying drawings, it should be understood that herein
Described specific embodiment is only used to explain the present invention, is not intended to limit the present invention.
As shown in Figure 1 and Figure 2, a kind of basalt fibre waste silk recycling system, the wire drawing including producing basalt fibre
Device, for transmitting the conveyer belt of basalt waste silk, conveyer belt tail end is equipped with incinerator, burns for wire-drawing frame lower section setting
Ball mill is equipped with behind stove, the feeding device I for adding in the waste silk recycled is equipped with behind ball mill, feeding device I connects kiln
Stove is additionally provided with the feeding device II for adding in basalt stone on kiln.Wherein, wire-drawing frame is Chinese patent
The wire-drawing frame of the production continuous basalt fiber of CN206069703U.
Due to having used a large amount of organic matter size in basalt fibre production process, in basalt fibre waste silk
Surface, although being rinsed with water during crushing, can also also have big there are a large amount of organic matter size
Part is attached on basalt fibre waste silk, if these organic matters are brought directly to melt in kiln, can influence the oxygen in kiln
Change reducing atmosphere, incinerator needs thoroughly to incinerate these organic matter sizes, only retains inorganic glass waste silk, in this way
Just ensure that the waste silk raw material recycled is clean as possible, meet requirement.
Preferably, screening plant is equipped between the ball mill and feeding device I.Screening is in basalt fibre waste silk
Impurity carried out primary removing again, the impurity content being reduced as far as in basalt fibre waste silk.
The feeding device I and feeding device II be can quantitative, automatic, continuous feed arrangement, and feeding device II
Charging rate is five times of the charging rate of feeding device I, that is to say, that the cylinder charging motor spindle turntable of two feeding devices
Rotating speed be it is different, due to rotating speed difference, so charging speed it is also different, ensure that eventually enter into kiln in this way
Basalt raw material, waste silk ratio only account for 1/5th, so as to ensure final product quality.
The feeding device I is identical with the structure of feeding device II, including storage bin 1, storing bin bracket and control system
System, the storage bin 1 are furnished with metering device, and the lower section of storage bin 1 is equipped with feed supplement conveying trough 2, one end edge storage of feed supplement conveying trough 2
Feed bin 1 protrudes horizontally up, and is provided with cylinder charger 3 below one end that feed supplement conveying trough 2 stretches out, 3 bottom of cylinder charger is equipped with
Flowmeter and propeller, the one side edge of the top of cylinder charger 3 are equipped with charging conveying trough 4, feed one end of conveying trough 4 along circle
Cylinder charger 3 protrudes horizontally up, and is equipped with feeding cylinder 5 below one end that charging conveying trough 4 stretches out, feeding cylinder 5 is connect with kiln 6；Institute
It states 3 inner wall of cylinder charger to accept equipped with helicla flute, helicla flute top and one end of charging conveying trough 4, cylinder charger 3 can
Quantitative continuous feed, material are transferred to by the helicla flute of 3 inner wall of cylinder charger on charging conveying trough 4.
Preferably, the top of the feeding cylinder 5 is equipped with feeding cylinder head 51, and feeding cylinder head 51 is hollow cube, into
Every one side edge of 51 upper end of barrel head is connected with baffle 52, and baffle 52 is respectively positioned on feeding cylinder head 51 during normal work
There are the gaps of charging on internal and central axis.This design can not only realize lasting, a small amount of charging, but also can prevent
The hot gas and cigarette of kiln are emerged do harm to huamn body.
Preferably, the charging conveying trough 4 is U-lag, and the bottom of U-lag is arc.Basalt stone can be made few in this way
Amount continues into feeding cylinder 5, avoids causing to feed due to basalt stone flocks together more.
The course of work of the feeding device of the present invention is as follows：Under the action of control system, storage bin 1 is quantitative by the Black Warrior
Rock reaches cylinder charger 3 by feed supplement conveying trough 2, and the bottom of cylinder charger 3 is turntable, on 3 inner wall of cylinder charger
Equipped with helicla flute, helicla flute is communicated with charging conveying trough 4, under the action of 3 bottom turntable of cylinder charger, basalt stone
It is transported on the helicla flute of 3 inner wall of cylinder charger by quantitative, is then sent to kiln 6 through charging conveying trough 4, feeding cylinder 5,
The speed of discharging can be controlled by controlling rotary speed, persistently fed so as to fulfill a small amount of basalt stone.
The course of work of the present invention is as follows：
Outflow that basalt stone melt is stablized from wire-drawing frame is simultaneously drawn lower into silk, if tow is qualified, is wound on winder, if silk
Unqualified beam is waste silk, then it is at will coiled into one and is placed on the conveyer belt of lower section, and the communicated band of waste silk enters incinerator, gives up
Silk enters the feeder of incinerator, later by high temperature incineration, completely removes and is attached to having for basalt fibre waste silk surface
Machine matter size, then automatic discharging.Waste silk after burning enters a transition feed bin, then uniformly steady according to sets requirement
Surely it is added in ceramic ball mill and is ground, the large or fine granule after grinding all enters vibrating screening machine by elevator, sieve
Be waste silk recycling finished product down, waste silk recycles finished product subsequently into feeding device I, feeding device I and feeding device II simultaneously to
Kiln 6 is fed, since feeding device I is different with the charging rate of feeding device II, so basalt stone and basalt fibre give up
Silk simultaneously into kiln 6, realizes the recycling of basalt fibre waste silk by a certain percentage.
What has been described above is only a preferred embodiment of the present invention, it is noted that for those skilled in the art,
Under the premise of general idea of the present invention is not departed from, several changes and improvements can also be made, these should also be considered as the present invention's
Protection domain, these all do not interfere with the effect and practical applicability that the present invention is implemented.
Claims (6)
1. a kind of basalt fibre waste silk recycling system, the wire-drawing frame including producing basalt fibre, it is characterised in that：
Setting is for transmitting the conveyer belt of basalt waste silk below the wire-drawing frame, and conveyer belt tail end is equipped with incinerator, after incinerator
Face is equipped with ball mill, and the feeding device I for adding in the waste silk recycled is equipped with behind ball mill, and feeding device I connects kiln, kiln
The feeding device II for adding in basalt stone is additionally provided on stove.
2. basalt fibre waste silk recycling system as described in claim 1, it is characterised in that：The ball mill and charging
Screening plant is equipped between device I.
3. basalt fibre waste silk recycling system as described in claim 1, it is characterised in that：I He of feeding device
Feeding device II is quantitative, automatic, the continuous feed arrangement of energy, and the charging rate of feeding device II is adding for feeding device I
Expect speed five times.
4. basalt fibre waste silk recycling system as described in claim 1, it is characterised in that：I He of feeding device
The structure of feeding device II is identical, including storage bin（1）, storing bin bracket and control system, the storage bin（1）Equipped with meter
Measure device, storage bin（1）Lower section be equipped with feed supplement conveying trough（2）, feed supplement conveying trough（2）One end along storage bin（1）Level is stretched
Go out, feed supplement conveying trough（2）Cylinder charger is provided with below one end of stretching（3）, cylinder charger（3）Bottom is equipped with flowmeter
And propeller, cylinder charger（3）The one side edge of top is equipped with charging conveying trough（4）, feed conveying trough（4）One end along circle
Cylinder charger（3）It protrudes horizontally up, feeds conveying trough（4）Feeding cylinder is equipped with below one end of stretching（5）, feeding cylinder（5）With kiln
（6）Connection；The cylinder charger（3）Inner wall is equipped with helicla flute, helicla flute top and charging conveying trough（4）One end hold
It connects, cylinder charger（3）Continuous feed can be quantified, material passes through cylinder charger（3）The helicla flute of inner wall is transferred to charging
Conveying trough（4）On.
5. basalt fibre waste silk recycling system as claimed in claim 4, it is characterised in that：The feeding cylinder（5）'s
Top is equipped with feeding cylinder head（51）, feeding cylinder head（51）For hollow cube, feeding cylinder head（51）Every one side of upper end
Edge is connected with baffle（52）, baffle during normal work（52）It is respectively positioned on feeding cylinder head（51）Inside and central axis on
There are the gaps of charging.
6. basalt fibre waste silk recycling system as claimed in claim 4, it is characterised in that：The charging conveying trough
（4）For U-lag, the bottom of U-lag is arc.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711496109.9A CN108178500B (en) | 2017-12-31 | 2017-12-31 | Basalt fiber waste silk recycling system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711496109.9A CN108178500B (en) | 2017-12-31 | 2017-12-31 | Basalt fiber waste silk recycling system |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN108178500A true CN108178500A (en) | 2018-06-19 |
| CN108178500B CN108178500B (en) | 2021-05-11 |
Family
ID=62549558
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201711496109.9A Active CN108178500B (en) | 2017-12-31 | 2017-12-31 | Basalt fiber waste silk recycling system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN108178500B (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109775959A (en) * | 2019-02-18 | 2019-05-21 | 姚树飞 | A kind of dedicated charging system of basalt fibre production |
| CN114368525A (en) * | 2020-10-14 | 2022-04-19 | 张家港百盛新材料有限公司 | Dosing device for electronic component packaging |
| CN115504663A (en) * | 2022-08-29 | 2022-12-23 | 炬石玄纤科技(安阳)有限公司 | Be used for basalt all-electric melting kiln feeding system device |
-
2017
- 2017-12-31 CN CN201711496109.9A patent/CN108178500B/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109775959A (en) * | 2019-02-18 | 2019-05-21 | 姚树飞 | A kind of dedicated charging system of basalt fibre production |
| CN114368525A (en) * | 2020-10-14 | 2022-04-19 | 张家港百盛新材料有限公司 | Dosing device for electronic component packaging |
| CN115504663A (en) * | 2022-08-29 | 2022-12-23 | 炬石玄纤科技(安阳)有限公司 | Be used for basalt all-electric melting kiln feeding system device |
Also Published As
| Publication number | Publication date |
|---|---|
| CN108178500B (en) | 2021-05-11 |
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| 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 | ||
| CB02 | Change of applicant information | ||
| CB02 | Change of applicant information |
Address after: 452477 Yangcheng Industrial Zone, Dengfeng City, Zhengzhou City, Henan Province Applicant after: Zhengzhou electric Basalt Fiber Co. Ltd Address before: 452483 Sanlizhuang High-tech Park, Dengfeng City, Zhengzhou City, Henan Province Applicant before: Zhengzhou electric Basalt Fiber Co. Ltd |
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| GR01 | Patent grant | ||
| GR01 | Patent grant |