CN104930816A - Clay drying system - Google Patents
Clay drying system Download PDFInfo
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- CN104930816A CN104930816A CN201510376765.XA CN201510376765A CN104930816A CN 104930816 A CN104930816 A CN 104930816A CN 201510376765 A CN201510376765 A CN 201510376765A CN 104930816 A CN104930816 A CN 104930816A
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- disc type
- dust collector
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- tower drier
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Abstract
A clay drying system comprising a disc type vertical type dryer, and a heat supply unit and a screening unit which are connected with the disc type vertical type dryer; a feed inlet of the disc type vertical type dryer is provided with a spiral feeder; the heat supply unit comprises a raw coal bunker, a crusher, a crushed coal bunker and a fluidized bed roaster; and the screening unit comprises a powder concentrator, a gas tank type pulse bag dust collector, a pneumatic fluidizing conveyor, an electric vibrating screen and a first adhesive tape conveyer. Compared with the prior art, raw coal is screened and crushed with multiple levels by the heat supply unit, crushed coal is enabled to be combusted fully and stably, and a good base is provided for the drying process; and in the screening unit, clay fine powder and coarse powder are fully separated by the powder concentrator and the gas tank type pulse bag dust collector, control is convenient, separating effect is good, and production efficiency and production benefit are improved.
Description
Technical field
The present invention relates to pottery mud production field, be specifically applied to the one pottery mud drying system in ceramic mud comprehensive utilization process flow process.
Background technology
In ceramic mud comprehensive utilization process flow process, traditional pottery mud drying system, thorough not with being separated of fine powder for meal, cause the program that the later stage also needs to carry out sieving powder, separation again, such waste is not said man-hour, just causes the very large wasting of resources in oven dry link; And in oven dry link, the hot blast controlled quentity controlled variable that baking needed is wanted and supply stability have a great impact dries quantity, and traditional heat source supply mode is stable not, efficiency is low, these cause production efficiency low, the situation that the output value is not high, are unfavorable for the raising of productivity effect.
Summary of the invention
The object of the present invention is to provide a kind of pottery mud drying system of efficient, stable, good separating effect, to solve the problem proposed in above-mentioned background technology.
For achieving the above object, the invention provides following technical scheme:
A kind of pottery mud drying system, the heating unit comprising disc type tower drier and be connected with disc type tower drier and sieve unit, be provided with screw(-type) feeder at the charging aperture place of disc type tower drier, described heating unit includes run coal bin, disintegrating machine, broken coal storehouse and fluidized bed furnace, the outer bulkhead of described run coal bin is provided with hopper wall vibrator, the lower end of run coal bin is provided with rod gate, the second rubber conveyer is provided with between run coal bin and disintegrating machine, second rubber conveyer is provided with permanent magnetism self-unloading type deferrization device, the discharging opening of described disintegrating machine is connected by the charging aperture of bucket elevator with broken coal storehouse, the outer bulkhead in broken coal storehouse is fixed with hopper wall vibrator, the lower end of the discharging opening in broken coal storehouse is provided with dise feeder, dise feeder is connected with the charging aperture of fluidized bed furnace, the lower end of fluidized bed furnace is connected with air blast, the hot-blast outlet of fluidized bed furnace and described disc type vertical drying motor spindle hot wind inlet pipeline be connected, described sieve unit includes powder concentrator, air box type pulse bag dust collector, air conveyer flume, electric vibrating screen and the first rubber conveyer, described powder concentrator is arranged on the upper end of disc type tower drier, powder concentrator is connected with air box type pulse bag dust collector by pipeline, skewed slot centrifugal fan is provided with in air box type pulse bag dust collector lower end discharge outlet, the discharging opening of air box type pulse bag dust collector is stored with the pottery mud in next production link by air conveyer flume and is connected between bulk vehicle, the exhaust ports of air box type pulse bag dust collector is provided with centrifugal fan, the escape pipe of centrifugal fan is divided into two-way, one tunnel is connected with outside exhaust chimney, pipeline of separately leading up to is connected with the inlet end of disc type tower drier, below described air box type pulse bag dust collector disc type tower drier sidewall on be provided with weight flap valve, electric vibrating screen is provided with in the lower end of weight flap valve, the first rubber conveyer is had at electric vibrating screen.
Further, the first sampler be connected with electric vibrating screen is provided with in the first rubber conveyer upper end.
Further, air conveyer flume is provided with the second sampler.
Further, the hot blast intake line of disc type tower drier is provided with electric louver valve.
Compared with prior art, the heating unit in the present invention to the multi-level screening of raw coal and pulverizing, guarantee broken coal can fully, smooth combustion, provide good basis for drying link; In sieve unit, pottery mud fine powder is fully separated with meal with air box type pulse bag dust collector by powder concentrator by the present invention, and it is convenient to control, and good separating effect, improves production efficiency and productivity effect.
Accompanying drawing explanation
Fig. 1 is the structural representation of a kind of mud drying system of making pottery of the present invention.
In figure: 1-first rubber conveyer, 2-makes pottery between mud storage and bulk vehicle, 3-first sampler, 4-centrifugal fan, 5-air conveyer flume, 6-air box type pulse bag dust collector, 7-skewed slot centrifugal fan, 8-powder concentrator, 9-disc type tower drier, 10-screw(-type) feeder, 11-weight flap valve, 12-electric vibrating screen, 13-second sampler, 14-run coal bin, 15-permanent magnetism self-unloading type deferrization device, 16-broken coal storehouse, 17-dise feeder, 18-fluidized bed furnace, 19-air blast, 20-bucket elevator, 21-disintegrating machine, 22-second rubber conveyer.
Detailed description of the invention
Below in conjunction with the accompanying drawing in the embodiment of the present invention, be clearly and completely described the technical scheme in the embodiment of the present invention, obviously, described embodiment is only the present invention's part embodiment, instead of whole embodiments.Based on the embodiment in the present invention, those of ordinary skill in the art, not making the every other embodiment obtained under creative work prerequisite, belong to the scope of protection of the invention.
Refer to Fig. 1, a kind of pottery mud drying system, the heating unit comprising disc type tower drier 9 and be connected with disc type tower drier 9 and sieve unit, screw(-type) feeder is provided with at the charging aperture place of disc type tower drier 9, realize even, stable material supply, described heating unit includes run coal bin 14, disintegrating machine 21, broken coal storehouse 16 and fluidized bed furnace 18, the outer bulkhead of described run coal bin 14 is provided with hopper wall vibrator, the lower end of run coal bin 14 is provided with rod gate, prevent coal bunker from exporting the phenomenon occurring blocking caking, the second rubber conveyer 22 is provided with between run coal bin 14 and disintegrating machine 21, coal fuel area density in run coal bin 14 is entered broken coal storehouse 16 and carries out pulverization process by the second rubber conveyer 22, second rubber conveyer 22 is provided with permanent magnetism self-unloading type deferrization device 15, in order to the bulky grain iron tramp in coal fuel is removed, in order to avoid affect next step pulverizing link, the discharging opening of described disintegrating machine 21 is connected with the charging aperture in broken coal storehouse 16 by bucket elevator 20, coal fuel is after the pulverization process through disintegrating machine 21, be transported to broken coal storehouse 16 temporarily to store, the outer bulkhead in broken coal storehouse 16 is fixed with hopper wall vibrator, prevent discharging opening from occurring the phenomenon of blocking caking, the lower end of the discharging opening in broken coal storehouse 16 is provided with dise feeder 17, dise feeder 17 is connected with the charging aperture of fluidized bed furnace 18, the lower end of fluidized bed furnace 18 is connected with air blast 19, the hot-blast outlet of fluidized bed furnace 19 with bottom described disc type tower drier 9 hot wind inlet pipeline be connected, described sieve unit includes powder concentrator 8, air box type pulse bag dust collector 6, air conveyer flume 5, electric vibrating screen 12 and the first rubber conveyer 1, described powder concentrator 8 is arranged on the upper end of disc type tower drier 9, powder concentrator 9 is connected with air box type pulse bag dust collector 6 by pipeline, skewed slot centrifugal fan 7 is provided with in air box type pulse bag dust collector 6 lower end discharge outlet, the discharging opening of air box type pulse bag dust collector 6 is stored with the pottery mud in next production link by air conveyer flume 5 and 2 to be connected between bulk vehicle, the exhaust ports of air box type pulse bag dust collector 6 is provided with centrifugal fan 4, the escape pipe of centrifugal fan 4 is divided into two-way, one tunnel is connected with outside exhaust chimney, pipeline of separately leading up to is connected with the inlet end of disc type tower drier 9, below described air box type pulse bag dust collector 6 disc type tower drier 9 sidewall on be provided with weight flap valve 11, electric vibrating screen 12 is provided with in the lower end of weight flap valve 11, the first rubber conveyer 1 is had at electric vibrating screen 12.
Pottery mud raw material is dried in disc type tower drier 9, in disc type tower drier 9, gas is entrained with pottery mud powder and enters powder concentrator 8 and carry out sorting, and pottery mud meal to store and between bulk vehicle 2 by delivering to follow-up pottery mud through the first rubber conveyer 1 after the weight flap valve 11 of disc type tower drier 9 side; Pottery mud fine powder then enters air box type pulse bag dust collector 6 with gas, after collection through air conveyer flume 5 also deliver to follow-up pottery mud store and bulk vehicle between 2, the rear gas of purification then returns disc type tower drier 9 by centrifugal fan 4 part and circulates, remaining, enters air.
In addition, be provided with the first sampler 3 be connected with electric vibrating screen 12 in the first rubber conveyer 1 upper end, in order to detect the sampling of pottery mud fine powder; Air conveyer flume 5 is provided with the second sampler 13, in order to detect the sampling of crude pottery mud powder.
In addition, the hot blast intake line of disc type tower drier 9 is provided with electric louver valve, in order to control into mill hot blast rate.
Pottery mud fine powder fineness realizes mainly through regulating throughput in powder concentrator 8 rotating speed and mill.
Thermal source for drying pottery mud raw material moisture content carrys out spontaneous combustion coal fluidized bed furnace 18, raw coal is through rod gate, second rubber conveyer 22, disintegrating machine 21, bucket elevator 20 and rotary disc feeder 17 enter fluidized bed furnace 18 and enter fluidized bed furnace 18 coal amount by rotary disc feeder 17 variable frequency regulating speed control, regulate electric louver valve 2 to control into mill hot blast rate and to enter to grind wind-warm syndrome according to going out the make pottery temperature of the moisture of mud fine powder finished product and system off gas, pressure condition of disc type tower drier 9.
To those skilled in the art, obviously the invention is not restricted to the details of above-mentioned one exemplary embodiment, and when not deviating from spirit of the present invention or essential characteristic, the present invention can be realized in other specific forms.Therefore, no matter from which point, all should embodiment be regarded as exemplary, and be nonrestrictive, scope of the present invention is limited by claims instead of above-mentioned explanation, and all changes be therefore intended in the implication of the equivalency by dropping on claim and scope are included in the present invention.Any Reference numeral in claim should be considered as the claim involved by limiting.
In addition, be to be understood that, although this description is described according to embodiment, but not each embodiment only comprises an independently technical scheme, this narrating mode of description is only for clarity sake, those skilled in the art should by description integrally, and the technical scheme in each embodiment also through appropriately combined, can form other embodiments that it will be appreciated by those skilled in the art that.
Claims (4)
1. a pottery mud drying system, it is characterized in that: comprise disc type tower drier (9) and the heating unit that is connected with disc type tower drier (9) and sieve unit, be provided with screw(-type) feeder at the charging aperture place of disc type tower drier (9), described heating unit includes run coal bin (14), disintegrating machine (21), broken coal storehouse (16) and fluidized bed furnace (18), the outer bulkhead of described run coal bin (14) is provided with hopper wall vibrator, the lower end of run coal bin (14) is provided with rod gate, the second rubber conveyer (22) is provided with between run coal bin (14) and disintegrating machine (21), second rubber conveyer (22) is provided with permanent magnetism self-unloading type deferrization device (15), the discharging opening of described disintegrating machine (21) is connected with the charging aperture of broken coal storehouse (16) by bucket elevator (20), the outer bulkhead in broken coal storehouse (16) is fixed with hopper wall vibrator, the lower end of the discharging opening in broken coal storehouse (16) is provided with dise feeder (17), dise feeder (17) is connected with the charging aperture of fluidized bed furnace (18), the lower end of fluidized bed furnace (18) is connected with air blast (19), the hot-blast outlet of fluidized bed furnace (19) and described disc type tower drier (9) bottom hot wind inlet pipeline be connected, described sieve unit includes powder concentrator (8), air box type pulse bag dust collector (6), air conveyer flume (5), electric vibrating screen (12) and the first rubber conveyer (1), described powder concentrator (8) is arranged on the upper end of disc type tower drier (9), powder concentrator (9) is connected with air box type pulse bag dust collector (6) by pipeline, skewed slot centrifugal fan (7) is provided with in air box type pulse bag dust collector (6) lower end discharge outlet, the discharging opening of air box type pulse bag dust collector (6) is stored with the pottery mud in next production link by air conveyer flume (5) and between bulk vehicle, (2) are connected, the exhaust ports of air box type pulse bag dust collector (6) is provided with centrifugal fan (4), the escape pipe of centrifugal fan (4) is divided into two-way, one tunnel is connected with outside exhaust chimney, pipeline of separately leading up to is connected with the inlet end of disc type tower drier (9), the sidewall of described air box type pulse bag dust collector (6) below disc type tower drier (9) is provided with weight flap valve (11), electric vibrating screen (12) is provided with in the lower end of weight flap valve (11), the first rubber conveyer (1) is had at electric vibrating screen (12).
2. pottery mud drying system according to claim 1, is characterized in that, is provided with the first sampler (3) be connected with electric vibrating screen (12) in the first rubber conveyer (1) upper end.
3. pottery mud drying system according to claim 1, is characterized in that, air conveyer flume (5) is provided with the second sampler (13).
4. pottery mud drying system according to claim 1, is characterized in that, the hot blast intake line of disc type tower drier (9) is provided with electric louver valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510376765.XA CN104930816A (en) | 2015-06-29 | 2015-06-29 | Clay drying system |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510376765.XA CN104930816A (en) | 2015-06-29 | 2015-06-29 | Clay drying system |
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| CN104930816A true CN104930816A (en) | 2015-09-23 |
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| CN201510376765.XA Pending CN104930816A (en) | 2015-06-29 | 2015-06-29 | Clay drying system |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105403019A (en) * | 2015-11-03 | 2016-03-16 | 郭庆叶 | Coal dryer |
| CN111854335A (en) * | 2020-07-30 | 2020-10-30 | 李国安 | Floated powder drying-machine |
| CN111854404A (en) * | 2020-07-30 | 2020-10-30 | 李国安 | Gravity type particle dryer |
Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1482090A (en) * | 2002-09-09 | 2004-03-17 | 上海宝田新型建材有限公司 | Instantly grinding scoria micro powder and process for manufacturing the same |
| CN101152636A (en) * | 2006-09-28 | 2008-04-02 | 上海宝田新型建材有限公司 | Production control logical system for blast-furnace cinder grinder |
| CN201999951U (en) * | 2011-03-16 | 2011-10-05 | 济南鲍安环保技术开发有限公司 | Production device for three-dimensional steel slag micropowder |
| CN102500455A (en) * | 2011-12-21 | 2012-06-20 | 湖北工业大学 | Tailing efficient recovery treatment method |
| CN102531418A (en) * | 2011-12-30 | 2012-07-04 | 中信重工机械股份有限公司 | Steel slag grinding production technology and system |
| CN202921398U (en) * | 2012-11-21 | 2013-05-08 | 秀山县嘉源矿业有限责任公司 | Energy-saving and environment-friendly vertical mill crushing system |
| CN203571779U (en) * | 2013-11-27 | 2014-04-30 | 江苏沃尔夫机械有限公司 | Automatic coal loading device for drier |
| CN103949322A (en) * | 2014-05-14 | 2014-07-30 | 中材（天津）粉体技术装备有限公司 | Nickel slag grinding system and production process thereof |
-
2015
- 2015-06-29 CN CN201510376765.XA patent/CN104930816A/en active Pending
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1482090A (en) * | 2002-09-09 | 2004-03-17 | 上海宝田新型建材有限公司 | Instantly grinding scoria micro powder and process for manufacturing the same |
| CN101152636A (en) * | 2006-09-28 | 2008-04-02 | 上海宝田新型建材有限公司 | Production control logical system for blast-furnace cinder grinder |
| CN201999951U (en) * | 2011-03-16 | 2011-10-05 | 济南鲍安环保技术开发有限公司 | Production device for three-dimensional steel slag micropowder |
| CN102500455A (en) * | 2011-12-21 | 2012-06-20 | 湖北工业大学 | Tailing efficient recovery treatment method |
| CN102531418A (en) * | 2011-12-30 | 2012-07-04 | 中信重工机械股份有限公司 | Steel slag grinding production technology and system |
| CN202921398U (en) * | 2012-11-21 | 2013-05-08 | 秀山县嘉源矿业有限责任公司 | Energy-saving and environment-friendly vertical mill crushing system |
| CN203571779U (en) * | 2013-11-27 | 2014-04-30 | 江苏沃尔夫机械有限公司 | Automatic coal loading device for drier |
| CN103949322A (en) * | 2014-05-14 | 2014-07-30 | 中材（天津）粉体技术装备有限公司 | Nickel slag grinding system and production process thereof |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105403019A (en) * | 2015-11-03 | 2016-03-16 | 郭庆叶 | Coal dryer |
| CN111854335A (en) * | 2020-07-30 | 2020-10-30 | 李国安 | Floated powder drying-machine |
| CN111854404A (en) * | 2020-07-30 | 2020-10-30 | 李国安 | Gravity type particle dryer |
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Application publication date: 20150923 |