CN103292588A - Automatic drying system for ceramic balls - Google Patents
Automatic drying system for ceramic balls Download PDFInfo
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- CN103292588A CN103292588A CN201310218433XA CN201310218433A CN103292588A CN 103292588 A CN103292588 A CN 103292588A CN 201310218433X A CN201310218433X A CN 201310218433XA CN 201310218433 A CN201310218433 A CN 201310218433A CN 103292588 A CN103292588 A CN 103292588A
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- ceramic balls
- dryer
- hopper
- drying system
- elevator
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Abstract
An automatic drying system for ceramic balls comprises a heating device, a drying machine and a cooling device. The heating device comprises a tunnel kiln, a draught pipe and a draught fan, wherein the tunnel kiln is connected with the drying machine through the draught pipe and the draught fan is disposed on the draught pipe. The drying machine comprises a pipe shell provided with a feed bin on the top of one end of the shell. The feed bin is conical. A screen plate is disposed at the bottom end of the feed bin. A screw conveyer shaft is disposed in the shell and is connected with a speed-regulating motor. The bottom of the other end of the shell is provided with a discharge hole. The cooling device comprises a transfer tank connected with the discharge hole, an elevator connected with the transfer tank, a hopper connected with the elevator, and a chute connected with the hopper. The automatic drying system for ceramic balls is high in drying efficiency, compact in structure and small in floor area.
Description
Technical field
The present invention relates to ceramic drying plant, relate in particular to a kind of wet feed Ceramic Balls drying plant.
Background technology
Polishing is one important procedure in the Production of Ceramics, and is moisture through the ceramic product surface after the polishing, needs just can be for further processing after the drying.At present, most of producers all adopt the measure that is layered on ground airing, wind, this method exist automaticity low, be subjected to that such environmental effects is big, drying efficiency is low, floor space is big, problems such as temperature control difference, and easily cause the pollution of product.Simultaneously, the waste heat supply temperature that the tunnel cave of production ceramic product produces is about 400 ℃, and this waste heat does not well utilize, and has caused the waste of the energy.
Summary of the invention
The present invention is for solving the problems of the technologies described above, and improved a kind of drying efficiency height, compact conformation, drying system that floor space is little.
Key problem in technology of the present invention is by set up sieve plate in the charging aperture of dryer, make large granular impurity in its effective ceramic for filtration ball, and change dryer inside into the helical feed mode, make the material heat exchange of in transportation, overturning, improve heat exchange efficiency, and be promoted to behind the hopper from chute by elevator, slowly disperse landing, make its acceleration air-dry, concentrate the pack transportation at last, its concrete technical scheme is: a kind of Ceramic Balls automatic drying system is characterized in that comprising heating plant, dryer and heat abstractor, described heating plant is by tunnel cave, the air-introduced machine that connects the air inducing pipeline of tunnel cave and dryer and be arranged on the air inducing pipeline is formed; Described dryer comprises tubular shell, and housing one end top is provided with feeding warehouse, and described feeding warehouse is the taper warehouse, the warehouse bottom is provided with sieve plate, be provided with screw conveyor shaft in the housing, screw conveyor shaft connects buncher, and housing other end bottom is provided with discharging opening; Described heat abstractor comprises the transfer pond that is connected with discharging opening, the elevator that is connected with the transfer pond, the hopper that is connected with elevator and the chute that is connected with hopper.
As preferably, have additional temperature sensor on the described air inducing pipeline.
Beneficial effect of the present invention: compact conformation, the automaticity height, floor space is little.Take full advantage of the waste heat in the tunnel cave, by regulating the air quantity of air-introduced machine, can effectively utilize hot blast, when having reduced energy waste, also improved drying efficiency.The rotating speed of dryer is adjustable, can effectively guarantee drying effect, and product is fully dried; The adjustable-speed of elevator, the tilt adjustable of square chute can guarantee that product fully dispels the heat, and do not handle and can not influence next step pack.
Description of drawings
Fig. 1 is structural representation of the present invention.
The specific embodiment
A kind of Ceramic Balls automatic drying system comprises heating plant, dryer 5 and heat abstractor, and described heating plant is made up of tunnel cave 1, connection tunnel cave 1 and the air inducing pipeline 3 of dryer 5 and the air-introduced machine 2 that is arranged on the air inducing pipeline 3; Described dryer 5 comprises tubular shell, and housing one end top is provided with feeding warehouse 4, and described feeding warehouse 4 is the taper warehouse, the warehouse bottom is provided with sieve plate 12, be provided with screw conveyor shaft 13 in the housing, screw conveyor shaft 13 connects buncher 11, and housing other end bottom is provided with discharging opening 14; Described heat abstractor comprises the transfer pond 6 that is connected with discharging opening 14, the elevator 7 that is connected with transfer pond 6, the hopper 8 that is connected with elevator 7 and the chute 10 that is connected with hopper 8.Have additional temperature sensor 9 on the described air inducing pipeline 3.
Operation principle of the present invention is: using air-introduced machine 2 is that the hot blast of tunnel cave 1 waste heat about 400 ℃ is incorporated in the dryer 5 by air inducing pipeline 3 with temperature, and can regulate air quantity by air-introduced machine 2.Ceramic Balls after the polishing is added by feeding warehouse 4, fall a part of water and granule impurity by sieve plate 12 preliminary drops, sieve plate 12 can freely be adjusted with the angle of dryer 5.After Ceramic Balls entered dryer 5, dryer 5 began rotation, and Ceramic Balls is then driven by screw conveyor shaft 13 advances.The rotating speed of dryer 5 can be adjusted according to specification and the water content of different product.Ceramic Balls is carried out exchange heat with hot blast in dryer 5, the Ceramic Balls temperature after the oven dry is about 60 ℃, enters into transfer pond 6, is risen in the hopper 8 by band elevator 7 afterwards, and hopper 8 is arranged on the platform, and this process can dissipate a part of heat.Ceramic Balls in the hopper 8 is slided by square chute 10, and this process can further be dispelled the heat, and is convenient to pack.
Claims (2)
1. a Ceramic Balls automatic drying system is characterized in that comprising heating plant, dryer and heat abstractor, and described heating plant is made up of tunnel cave, connection tunnel cave and the air inducing pipeline of dryer and the air-introduced machine that is arranged on the air inducing pipeline; Described dryer comprises tubular shell, and housing one end top is provided with feeding warehouse, and described feeding warehouse is the taper warehouse, the warehouse bottom is provided with sieve plate, be provided with screw conveyor shaft in the housing, screw conveyor shaft connects buncher, and housing other end bottom is provided with discharging opening; Described heat abstractor comprises the transfer pond that is connected with discharging opening, the elevator that is connected with the transfer pond, the hopper that is connected with elevator and the chute that is connected with hopper.
2. a kind of Ceramic Balls automatic drying system according to claim 1 is characterized in that having additional temperature sensor on the described air inducing pipeline.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310218433XA CN103292588A (en) | 2013-06-04 | 2013-06-04 | Automatic drying system for ceramic balls |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310218433XA CN103292588A (en) | 2013-06-04 | 2013-06-04 | Automatic drying system for ceramic balls |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN103292588A true CN103292588A (en) | 2013-09-11 |
Family
ID=49093862
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201310218433XA Pending CN103292588A (en) | 2013-06-04 | 2013-06-04 | Automatic drying system for ceramic balls |
Country Status (1)
| Country | Link |
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| CN (1) | CN103292588A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114136091A (en) * | 2021-12-03 | 2022-03-04 | 萍乡市环宇电瓷厂 | High-temperature furnace calcining device for ceramic insulator processing |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2771197Y (en) * | 2005-02-17 | 2006-04-12 | 董玉库 | Plate storehouse type gas active limestone kiln |
| JP2006191909A (en) * | 2005-01-11 | 2006-07-27 | Ricetech:Kk | Heat-treating device for granule |
| CN201138126Y (en) * | 2007-12-13 | 2008-10-22 | 吕江强 | Closed cycle hinge cage conveying dryer |
| CN202032859U (en) * | 2011-04-25 | 2011-11-09 | 攀枝花学院 | Dry kiln |
| CN202048768U (en) * | 2011-01-07 | 2011-11-23 | 东莞宜安科技股份有限公司 | Afterheat recycling and drying device |
| WO2012104509A1 (en) * | 2011-02-04 | 2012-08-09 | Aqualter | Process and plant for sludge hygienization treatment |
| CN203349624U (en) * | 2013-06-04 | 2013-12-18 | 江苏锡阳研磨科技有限公司 | Automatic drying system for ceramic ball |
-
2013
- 2013-06-04 CN CN201310218433XA patent/CN103292588A/en active Pending
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2006191909A (en) * | 2005-01-11 | 2006-07-27 | Ricetech:Kk | Heat-treating device for granule |
| CN2771197Y (en) * | 2005-02-17 | 2006-04-12 | 董玉库 | Plate storehouse type gas active limestone kiln |
| CN201138126Y (en) * | 2007-12-13 | 2008-10-22 | 吕江强 | Closed cycle hinge cage conveying dryer |
| CN202048768U (en) * | 2011-01-07 | 2011-11-23 | 东莞宜安科技股份有限公司 | Afterheat recycling and drying device |
| WO2012104509A1 (en) * | 2011-02-04 | 2012-08-09 | Aqualter | Process and plant for sludge hygienization treatment |
| CN202032859U (en) * | 2011-04-25 | 2011-11-09 | 攀枝花学院 | Dry kiln |
| CN203349624U (en) * | 2013-06-04 | 2013-12-18 | 江苏锡阳研磨科技有限公司 | Automatic drying system for ceramic ball |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114136091A (en) * | 2021-12-03 | 2022-03-04 | 萍乡市环宇电瓷厂 | High-temperature furnace calcining device for ceramic insulator processing |
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| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C05 | Deemed withdrawal (patent law before 1993) | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20130911 |