CN202016957U - Continuous gypsum powder production system of small gypsum boards for architectural decoration - Google Patents
Continuous gypsum powder production system of small gypsum boards for architectural decoration Download PDFInfo
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- CN202016957U CN202016957U CN2011201483063U CN201120148306U CN202016957U CN 202016957 U CN202016957 U CN 202016957U CN 2011201483063 U CN2011201483063 U CN 2011201483063U CN 201120148306 U CN201120148306 U CN 201120148306U CN 202016957 U CN202016957 U CN 202016957U
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Abstract
A continuous gypsum powder production system of small gypsum boards for architectural decoration comprises a crusher, hoisters, a boiling furnace, a dust settling chamber and a packaging machine. The two-stage crusher and the raw material hoister are arranged at an input end of a raw material bin; a disk feeder is arranged at the bottom of the raw material bin; the boiling furnace is arranged beside the disk feeder; a rotary drum for dewatering and drying is arranged in the boiling furnace; the dust settling chamber is arranged at the top of the boiling furnace; an air inlet pipe is arranged between one end of the rotary drum and the dust settling chamber; a spiral conveyor is arranged at the other end of the rotary drum; an air blower is arranged on an air inlet of the boiling furnace; the clinker hoister is arranged at an output end of the spiral conveyor and connected with an inlet of a clinker bin; a radiating pipe is arranged on the lower portion of the clinker bin and connected with an inlet of the crusher; an output end of the crusher is connected with a finished product bin; and the packaging machine is arranged at the bottom of the finished product bin. The system is capable of saving electric fee, fuel fee and labor for production enterprises, and improving production capacity without causing pollution to the ecological environment.
Description
Technical field
The utility model relates to a kind of production unit of gypsum for building powder, is the terra alba continous way production system of the little plasterboard of a kind of architectural decoration specifically.
Background technology
Existing terra alba old-fashioned production system, be a kind of production system of interval type, it is the marmite that utilizes rotation, adopts indirect heating that gypsum is dewatered, by hand-fed, behind the dehydration certain hour, the discharging of reversing again, the work that goes round and begins again.This production system power consumption, the consumption fuel, the consumption man-hour; And the production plant dust from flying, the Working environment extreme difference, to around several kilometers ecotope considerable influence is all arranged, have a strong impact on resident's healthy and activity in production.
Summary of the invention
For overcoming the above-mentioned defective of existing terra alba production system, the purpose of this utility model provides the terra alba continous way production system of the little plasterboard of a kind of architectural decoration
In order to realize continous way production, stabilized product quality improves the throughput of enterprise, reduces power consumption, coal consumption and artificial labour intensity.
For solving its technical problem, the technical solution adopted in the utility model is: the terra alba continous way production system of the little plasterboard of designing of architectural decoration, comprise hammer-crusher, lift, fluidizing furnace, dust-settling compartment, gas blower, induced draft fan, raw material silo, the grog storehouse, finished bin, pulverizer and wrapping machine, its feature is: 1. the input terminus at raw material silo is provided with two stage crusher and raw material lift, is provided with disk feeder in the bottom of raw material silo, at the other fluidizing furnace that is provided with of disk feeder, be provided with the barrel that is used for dewatered drying in the fluidizing furnace, be provided with dust-settling compartment, be provided with inlet pipe between an end of barrel and the dust-settling compartment at the top of fluidizing furnace, the other end at barrel is provided with worm conveyor, is provided with gas blower on the inlet mouth of fluidizing furnace; Be provided with the grog lift and link to each other at the output terminal of worm conveyor with grog storehouse inlet; Be provided with radiating pipe in the bottom in grog storehouse and link to each other with the inlet of pulverizer, the exit end of pulverizer links to each other with finished bin, is provided with wrapping machine in the bottom of finished bin.2. described fluidizing furnace is the kiln of being made by refractory materials, is provided with the rotary roller body in the kiln, and the outlet that the grate of kiln body has blast pipe and gas blower links to each other.3. described dust-settling compartment is located at the top of fluidizing furnace, be provided with the vapor pipe of band valve at the top of depositing dust reality, this vapor pipe links to each other with the waste-heated water-tank behind duplex fly-ash separator and tornado dust collector, bottom at this water tank is provided with thionizer, top at thionizer is provided with escape pipe, this escape pipe links to each other with the inlet of induced draft fan, and the outlet of induced draft fan links to each other with chimney through pipeline.
Native system is compared with existing interval type production system, following progress is arranged: 1, water vapour and incidental dust and sulfurous gas because of producing in the native system dehydration, handle and reclaim dust through the dust-settling compartment at fluidizing furnace top, making the tail gas of fluidizing furnace enter thionizer again behind the 3-stage dust-removal device arranges at last to atmosphere, therefore, not only the production plant dust pollution is little, particularly ecotope is not all around polluted, can be enterprise and reduce a large sum of environmental pollution expense, help preserving the ecological environment; 2. can reduce production costs, reduce energy consumption, drop to 9 yuan of/ton powder, power saving 167% by 24-26 yuan/tons of powder of original electricity consumption through one ton of terra alba of production on probation; Fuel cost drops to 18 yuan of/ton powder by original 45-50 unit/ton powder, and fuel economy takes 150%; 3. can raise labour productivity, existing interval type production system every workday is produced about 3 tons, can produce 8-10 ton/work day with the every workday behind the native system, saves artificial 160%; Factory's throughput of same scale is brought up to 40,000 tons/year by original 1.8 ten thousand tons/year, improves throughput 220%.
Description of drawings
Below in conjunction with the drawings and specific embodiments the utility model is further specified:
Fig. 1 is an one-piece construction synoptic diagram of the present utility model;
Fig. 2 is fluidizing furnace of the present utility model and dust-settling compartment structural representation.
Among the figure: 1, jaw crusher, 2, hammer mill, 3, the raw material lift, 4, raw material silo, 5, disk feeder, 6, the barrel of dehydration dryer, 7, fluidizing furnace, 8, dust-settling compartment 9, worm conveyor, 10, gas blower, 11, the grog lift, 12, the grog storehouse, 13, radiating pipe, 14, pulverizer, 15, finished bin, 16, wrapping machine, 17, inlet pipe, 18, the dust-settling compartment vapor pipe, 19, valve, 20, the depositing dust bucket, 21, secondary doubly-linked fly-ash separator, 22, three grades of tornado dust collector, 23, relay1 valve, 24, the waste-heated water-tank, 25, thionizer, 26, induced draft fan, 27, chimney.
Embodiment
With reference to accompanying drawing: be provided with at the input terminus of raw material silo 4 and be used for just broken jaw crusher 1 and thin broken hammer mill 2 two stage crushers, output terminal at hammer mill is connected with raw material lift 3, the output terminal of this lift with join at its top feed mouth of raw material silo 4, raw material silo 4 bottoms are provided with disk feeder 5, at the other fluidizing furnace 7 that is provided with of this disk feeder, be provided with the barrel 6 of dehydration dryer in the fluidizing furnace, be provided with dust-settling compartment 8 at the top of fluidizing furnace, be provided with inlet pipe 17 between one end of barrel 6 and the dust-settling compartment 8, the other end at barrel 6 is provided with worm conveyor 9, is provided with gas blower 10 on the inlet mouth of fluidizing furnace; Be provided with grog lift 11 and link to each other at the output terminal of worm conveyor with the inlet in grog storehouse 12; Be provided with radiating pipe 13 in the bottom in grog storehouse and link to each other with the inlet of pulverizer 14, the exit end of this pulverizer links to each other with finished bin 15, is provided with wrapping machine 16 in the bottom of finished bin.Wherein said fluidizing furnace is the kiln of being made by refractory materials, is provided with the rotary roller body in the kiln, and the outlet that the grate of kiln body has blast pipe and gas blower 10 links to each other.Be located at the top of fluidizing furnace at described dust-settling compartment, be provided with the vapor pipe 18 of band valve 19 at the top of depositing dust reality, the lower end of this vapor pipe is connected with the depositing dust bucket 20 that is used to recycle flue dust, be connected with the vapor pipe 18 of another root band valve 19 that is used for supplied flue gases on this depositing dust bucket, link to each other with waste-heated water-tank 24 behind the secondary doubly-linked fly-ash separator 21 of the output terminal of this vapor pipe through being installed in parallel and the three grades of tornado dust collector 22, wherein the bottom of secondary doubly-linked fly-ash separator 21 and three grades of tornado dust collector 22 is provided with the relay1 valve 23 that is used for dust discharge; Be provided with thionizer 25 in this waste-heated water-tank's bottom, be provided with escape pipe on the top of thionizer, this escape pipe links to each other with the inlet of induced draft fan 26, and the outlet of induced draft fan links to each other with chimney 27 through pipeline.
During work, selected gypsum raw ore carefully breaks through the broken machine 1 first broken hammer mill 2 that enters again in Hubei Province, make pellet below 8 ㎜, entering lift 3 more quantitatively sends into the raw material disk feeder 5 of packing in the raw material silo 4 in the holder water dryer 6 with raw material, through fluidizing furnace 7 heating, 850 ℃-950 ℃ of furnace temperature, 120 ℃-170 ℃ of dehydration temperaturres, dehydration about 75%, generate semi-hydrated gypsum, drop temperature is controlled within 140 ℃-150 ℃, and grog is sent into ageing in the grog storehouse 12 by lift 11, enter pulverizer 14 after 24 hours by radiating pipe 13 radiating and coolings and pulverize, after finished bin 15, enter wrapping machine 16 within discharging-material size 80-150 orders again and pack warehouse-in.
The water vapour that produces during gypsum dehydration can be carried all gases such as grit and sulfur-bearing secretly after dust-settling compartment inlet pipe 17 enters dust-settling compartment 8 depositing dust dryings, is discharged by worm conveyor 9 and recycles.Dust-settling compartment tail gas enters depositing dust bucket 20 by valve 19 dominant discharge through vapor pipe 18.Fluidizing furnace dust-laden tail gas enters chimney after enter thionizer 25 induced draft fans 26 after waste-heated water-tank's 24 coolings with tail gas through entering secondary doubly-linked fly-ash separator 21 behind the depositing dust bucket and entering 3-stage dust-removal device 22 again.
Claims (3)
1. the terra alba continous way production system of the little plasterboard of architectural decoration, comprise hammer-crusher, lift, fluidizing furnace, dust-settling compartment, gas blower, induced draft fan, raw material silo, the grog storehouse, finished bin, pulverizer and wrapping machine, it is characterized in that: the input terminus at raw material silo is provided with two stage crusher and raw material lift, bottom at raw material silo is provided with disk feeder, is provided with fluidizing furnace on the disk feeder side, is provided with the barrel that is used for dewatered drying in the fluidizing furnace, top at fluidizing furnace is provided with dust-settling compartment, be provided with inlet pipe between one end of barrel and the dust-settling compartment, be provided with worm conveyor, on the inlet mouth of fluidizing furnace, be provided with gas blower at the other end of barrel; Be provided with the grog lift and link to each other at the output terminal of worm conveyor with grog storehouse inlet; Be provided with radiating pipe in the bottom in grog storehouse and link to each other with the inlet of pulverizer, the exit end of pulverizer links to each other with finished bin, is provided with wrapping machine in the bottom of finished bin.
2. the terra alba continous way production system of the little plasterboard of a kind of architectural decoration according to claim 1, it is characterized in that: described fluidizing furnace is the kiln of being made by refractory materials, be provided with the rotary roller body in the kiln, the outlet that the grate of kiln body has blast pipe and gas blower links to each other.
3. the terra alba continous way production system of the little plasterboard of a kind of architectural decoration according to claim 1 and 2, it is characterized in that: described dust-settling compartment is located at the top of fluidizing furnace, be provided with the vapor pipe of band valve at the top of depositing dust reality, this vapor pipe links to each other with the waste-heated water-tank behind duplex fly-ash separator and tornado dust collector, bottom at this water tank is provided with thionizer, top at thionizer is provided with escape pipe, and this escape pipe links to each other with the inlet of induced draft fan, and the outlet of induced draft fan links to each other with chimney through pipeline.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011201483063U CN202016957U (en) | 2011-05-11 | 2011-05-11 | Continuous gypsum powder production system of small gypsum boards for architectural decoration |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011201483063U CN202016957U (en) | 2011-05-11 | 2011-05-11 | Continuous gypsum powder production system of small gypsum boards for architectural decoration |
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| Publication Number | Publication Date |
|---|---|
| CN202016957U true CN202016957U (en) | 2011-10-26 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN2011201483063U Expired - Fee Related CN202016957U (en) | 2011-05-11 | 2011-05-11 | Continuous gypsum powder production system of small gypsum boards for architectural decoration |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102765614A (en) * | 2012-07-30 | 2012-11-07 | 山东博丰利众化工有限公司 | Dust-fall treatment system for fluorine gypsum truck loading |
| CN104446066A (en) * | 2014-11-10 | 2015-03-25 | 尹小林 | Equipment of producing belite-gypsum material by roasting sludge and waste gypsum by virtue of fluidized-bed furnace |
| CN105731843A (en) * | 2016-01-23 | 2016-07-06 | 澧县方石坪镇杨朴矿山机械厂 | Dustless production method of building gypsum powder |
-
2011
- 2011-05-11 CN CN2011201483063U patent/CN202016957U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102765614A (en) * | 2012-07-30 | 2012-11-07 | 山东博丰利众化工有限公司 | Dust-fall treatment system for fluorine gypsum truck loading |
| CN102765614B (en) * | 2012-07-30 | 2015-05-13 | 山东博丰利众化工有限公司 | Dust-fall treatment system for fluorine gypsum truck loading |
| CN104446066A (en) * | 2014-11-10 | 2015-03-25 | 尹小林 | Equipment of producing belite-gypsum material by roasting sludge and waste gypsum by virtue of fluidized-bed furnace |
| CN105731843A (en) * | 2016-01-23 | 2016-07-06 | 澧县方石坪镇杨朴矿山机械厂 | Dustless production method of building gypsum powder |
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| Date | Code | Title | Description |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20111026 Termination date: 20130511 |