CN104446066B - With the equipment of boiling roaster mud, waste gypsum production belite-gypsum material - Google Patents
With the equipment of boiling roaster mud, waste gypsum production belite-gypsum material Download PDFInfo
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- CN104446066B CN104446066B CN201410626579.2A CN201410626579A CN104446066B CN 104446066 B CN104446066 B CN 104446066B CN 201410626579 A CN201410626579 A CN 201410626579A CN 104446066 B CN104446066 B CN 104446066B
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Abstract
With the equipment of boiling roaster mud, waste gypsum production belite-gypsum material, comprise feed preparing device, batching and homogeneous device, drying unit, calciner and grog fuel pulverizing plant; Feed preparing device comprises crusher, handling machinery I, pellet storehouse and bulk cargo filler bin; Batching and homogeneous device comprise meter material feeder I, meter material feeder II, Raymond mill I, handling machinery II, dry powder storehouse, roll over mixed clarifixator, forming machine and handling machinery III; Drying unit comprises dryer, handling machinery IV, flue I, flue II, fly-ash separator and blower fan; Calciner comprises fluidizing furnace, coal bunker, feeds coal device, feeds distributor, gas blower, removal device and handling machinery V; Grog fuel pulverizing plant comprises grog storehouse, extra material storehouse, meter material feeder III, Raymond mill II, handling machinery VI and ripe powder storehouse. Utilize the present invention, the mud that has a large capacity and a wide range of mass-producing, resource utilization, recovery energy, waste gypsum, barren rock slag the like waste can manufacture purposes belite-gypsum material widely.
Description
Technical field
The present invention relates to a kind of equipment producing belite-gypsum material, it is specifically related to the equipment of the production belite-gypsum materials such as a kind of boiling roaster mud, waste gypsum, barren rock slag.
Background technology
Currently, China's quantity of wastewater effluent is more than 5 �� 1010m3D, by every 10000m3The wet mud estimation of sewage 5 tons of water ratio 80%, if all sewage disposals, daily output sludge quantity, more than 2,500,000 tons, produces sludge quantity per year more than 900,000,000 tons. But, due to economy and technology, mud there is no stable and rational outlet, and total situation is still to fill, to stack, to topple over. At present, the main methods of mud have that ocean and culvert cloaca are toppled over, sanitary landfill, sludge composting, mud dry burning etc.
On the other hand, industrial waste gypsum (such as phosphogypsum) adds modified cement and is used as plastering and for except Sulphuric acid and by-product portland cement clinker be used as cement adjustable solidification agent or frying or roasting through modification except small part after, stored up in a large number or filled or be poured into cloaca culvert, serious mud groundwater resource.
Test proves, the mud having a large capacity and a wide range is easy to dehydration, air-dry through ridge grain seeding modification ridge, and modified sewage sludge slag and waste gypsum can production purposes belite-gypsum material widely, but there is no the equipment that investment is little and processing efficiency is high so far.
Obviously, to effectively, economical, solve the mud having a large capacity and a wide range and large waste residue such as industrial waste gypsum, barren rock slag with production purposes belite-gypsum novel material problem widely easily, urgent needs a kind of invest little, Charge Mixture Control and requires the equipment low, energy consumption is low, cost is low.
Summary of the invention
Technical problem to be solved by this invention is, it is provided that a kind of invest little, less energy-consumption, low cost with the equipment of boiling roaster mud, waste gypsum production belite-gypsum material. Utilize this equipment, the mud that has a large capacity and a wide range of mass-producing, resource utilization, recovery energy, waste gypsum, barren rock slag the like waste can manufacture purposes belite-gypsum material widely.
The technical solution adopted for the present invention to solve the technical problems is:
Technical scheme one: the equipment of a kind of boiling roaster mud, waste gypsum production belite-gypsum material, comprises feed preparing device, batching and homogeneous device, drying unit, calciner and grog fuel pulverizing plant;
Described feed preparing device comprises crusher, handling machinery I, pellet storehouse and bulk cargo filler bin, and described crusher is connected with handling machinery I, and described handling machinery I is connected with pellet storehouse, bulk cargo filler bin;
Described batching and homogeneous device comprise meter material feeder I, meter material feeder II, Raymond mill I, handling machinery II, dry powder storehouse, roll over mixed clarifixator, forming machine and handling machinery III, described meter material feeder I is connected with pellet storehouse, Raymond mill I, described Raymond mill I is connected with handling machinery II, described handling machinery II is connected with dry powder storehouse, described dry powder storehouse is connected with meter material feeder II, described meter material feeder II is connected with bulk cargo filler bin, the mixed clarifixator of rolling, forming machine, and described rolling mixes clarifixator, forming machine is connected with handling machinery III;
Described drying unit comprises dryer, handling machinery IV, flue I, flue II, fly-ash separator and blower fan, described calciner comprises fluidizing furnace, coal bunker, feeds coal device, feeds distributor, gas blower, removal device and handling machinery V, described dryer and handling machinery III, handling machinery IV is connected, distributor is connected described handling machinery IV with feeding, described distributor of feeding is connected with fluidizing furnace, coal device is connected described coal bunker with feeding, described coal device of feeding is connected with fluidizing furnace, described fluidizing furnace bottom is connected with removal device, described removal device discharge is connected with handling machinery V, the air port that goes out of described gas blower is connected by the blast inlet of airduct with fluidizing furnace bottom ebullated bed, the entrance end of described flue I is connected with the waste gas flue of fluidizing furnace, exit end is connected with the gas approach of dryer, the described entrance end of flue II is connected with the exhanst gas outlet of dryer, exit end is connected with the exhaust gas inlet end of fly-ash separator, the waste gas outlet end of described fly-ash separator is connected with the entrance end pipeline of blower fan,
Described grog fuel pulverizing plant comprises grog storehouse, extra material storehouse, meter material feeder III, Raymond mill II, handling machinery VI and ripe powder storehouse, described grog storehouse is connected with handling machinery V, described grog storehouse, extra material storehouse are connected with meter material feeder III, described meter material feeder III is connected with Raymond mill II, described Raymond mill II is connected with handling machinery VI, and described handling machinery VI is connected with ripe powder storehouse.
Further, being also provided with spiral ash-receiving device, described spiral ash-receiving device is connected with fly-ash separator, grog storehouse.
Technical scheme two: the equipment of a kind of boiling roaster mud, waste gypsum production belite-gypsum material, comprises feed preparing device, batching and homogeneous device, drying unit, calciner and grog fuel pulverizing plant;
Described feed preparing device comprises crusher, handling machinery I, pellet storehouse, and described crusher is connected with handling machinery I, and described handling machinery I is connected with pellet storehouse;
Described batching and homogeneous device comprise meter material feeder I, meter material feeder II, Raymond mill I, handling machinery II, dry powder storehouse, forming machine and handling machinery III, described meter material feeder I is connected with pellet storehouse, Raymond mill I, described Raymond mill I is connected with handling machinery II, described handling machinery II is connected with dry powder storehouse, described dry powder storehouse is connected with meter material feeder II, described meter material feeder II is connected with forming machine, and described forming machine is connected with handling machinery III;
Described drying unit comprises baker, handling machinery IV, flue II, fly-ash separator and blower fan, described calciner comprises fluidizing furnace, coal bunker, feeds coal device, gas blower, removal device and handling machinery V, described baker and handling machinery III, handling machinery IV is connected, described baker, handling machinery IV is positioned at the flue on fluidizing furnace top, the described entrance end of flue II is connected with the exhanst gas outlet of baker, exit end is connected with the exhaust gas inlet end of fly-ash separator, the waste gas outlet end of described fly-ash separator is connected with the entrance end pipeline of blower fan, coal device is connected described coal bunker with feeding, described coal device of feeding is connected with fluidizing furnace, described fluidizing furnace bottom is connected with removal device, described removal device discharge is connected with handling machinery V, the wind end of described gas blower is connected with the intake stack of fluidizing furnace bottom ebullated bed,
Described grog fuel pulverizing plant comprises grog storehouse, extra material storehouse, meter material feeder III, Raymond mill II, handling machinery VI and ripe powder storehouse, described grog storehouse is connected with handling machinery V, described grog storehouse, extra material storehouse are connected with meter material feeder III, described meter material feeder III is connected with Raymond mill II, described Raymond mill II is connected with handling machinery VI, and described handling machinery VI is connected with ripe powder storehouse.
Further, being also provided with spiral ash-receiving device, described spiral ash-receiving device is connected with fly-ash separator, grog storehouse.
Technical scheme three: the equipment of a kind of boiling roaster mud, waste gypsum production belite-gypsum material, comprises feed preparing device, batching and homogeneous device, drying unit, calciner and grog fuel pulverizing plant;
Described feed preparing device comprises handling machinery I, bulk cargo filler bin, and described handling machinery I is connected with bulk cargo filler bin;
Described batching and homogeneous device comprise meter material feeder II, roll over mixed clarifixator and handling machinery III, and described meter material feeder II is connected with bulk cargo filler bin, the mixed clarifixator of rolling, and the mixed clarifixator of described rolling is connected with handling machinery III;
Described drying unit comprises drying crusher, handling machinery IV, flue I, flue II, fly-ash separator and blower fan; Described calciner comprises fluidizing furnace, coal bunker, feeds coal device, feeds distributor, gas blower, removal device and handling machinery V; Described drying crusher is connected with handling machinery III, handling machinery IV, distributor is connected described handling machinery IV with feeding, described distributor of feeding is connected with fluidizing furnace, the entrance end of described flue I is connected with the waste gas flue of fluidizing furnace, exit end is connected with the gas approach of drying crusher, the described entrance end of flue II is connected with the exhanst gas outlet of drying crusher, exit end is connected with the exhaust gas inlet end of fly-ash separator, and the waste gas outlet end of described fly-ash separator is connected with the entrance end pipeline of blower fan; Coal device is connected described coal bunker with feeding, and described coal device of feeding is connected with fluidizing furnace, and described fluidizing furnace bottom is connected with removal device, and described removal device discharge is connected with handling machinery V, and the wind end of described gas blower is connected with the intake stack of fluidizing furnace bottom ebullated bed;
Described grog fuel pulverizing plant comprises grog storehouse, extra material storehouse, meter material feeder III, Raymond mill II, handling machinery VI and ripe powder storehouse, described grog storehouse is connected with handling machinery V, described grog storehouse, extra material storehouse are connected with meter material feeder III, described meter material feeder III is connected with Raymond mill II, described Raymond mill II is connected with handling machinery VI, and described handling machinery VI is connected with ripe powder storehouse.
Further, described handling machinery I is the handling machinery of band hopper.
Further, being also provided with spiral ash-receiving device, described spiral ash-receiving device is connected with fly-ash separator, grog storehouse.
Aforesaid device for calcium sulfate raw material, taking barren rock slag etc. as calcareous raw material, is aided with high aluminium correction material taking ridge modified sewage sludge slag or solidification sludge as main siliceous raw material, industrial waste gypsum; The block particulate materials needing powder to grind is entered after a gradating material raymond grinding powder mill and makes powder, powder enters to roll over mixed clarifixator after B grade mixture material with the loose shape gypsum not needing powder to grind and wet state material again and carries out the mixed homogeneous of dry wet stock rolling, plasticity or half harsh mix after homogeneous send into drying unit, utilize from the whole waste gas residual heat dry packs in fluidizing furnace, and de-except major part SO in flue gas by this2; When all materials all need into mill or all can enter to grind, then all proportioning materials enter raymond grinding powder grind after through the shaping feeding drying unit of forming machine; When material is fine particle material or powder or wet state material and unnecessary powder grinds, then, after all materials are sent into after batching and rolled over mixed clarifixator homogeneous, send into drying unit; The compound going out dryer sends into fluidizing furnace, with the combustion heat energy roasting material of the combustiblematerials in mud and additional coal, produce the grog taking beta-dicalcium silicate-calcium sulphoaluminate-calcium sulfate as major ingredient, grog utilizes raymond grinding powder mill to make belite-gypsum material with addition of appropriate extra material, or the grog of roasting is directly taken out without powder mill.
The useful effect of the present invention:
1) structure is simple, invests little, and the treatment capacity such as mud and industrial waste gypsum is big.
2) with the raymond grinding powder of Low investment grind, the production purposes belite-gypsum material widely such as boiling roaster mud, waste gypsum, its material cost is low, grinding pow consumption is low, it is low to burn till energy consumption, and speed firing technique production capacity height, also can save desulfurization and denitration cost, it is easily owner's acceptance, for the recycling of the mud that has a large capacity and a wide range and waste gypsum, barren rock slag etc. provides the outlet of practicable.
3) both mass-producing can dissolve mud and waste gypsum, barren rock slag etc., and without other secondary pollution, also can save a large amount of energy consumption, alleviate environmental pollution, be beneficial to environmental protection, there is significant Social benefit and economic benefit.
Accompanying drawing explanation
Fig. 1 is the device structure schematic diagram of the boiling roaster production belite-gypsum material of embodiment of the present invention 1-two-stage batching homogeneous;
Fig. 2 is the device structure schematic diagram of the boiling roaster production belite-gypsum material of embodiment of the present invention 2-mono-gradating material powder mill homogeneous;
Fig. 3 is the device structure schematic diagram that embodiment of the present invention 3-one-level proportioning wheel rolles over the boiling roaster production belite-gypsum material of homogeneous;
In figure: 101-crusher, 102-handling machinery I, 103-pellet storehouse, 104-bulk cargo filler bin, 201-counts material feeder I, 202-counts material feeder II, 203-Raymond mill I, 204-handling machinery II, 205-dry powder storehouse, 206-rolles over mixed clarifixator, 207-forming machine, 208-handling machinery III, 301-dryer, 301a-baker, 301b-drying crusher, 302-handling machinery IV, 303-flue I, 304-flue II, 305-fly-ash separator, 305a-spiral ash-receiving device, 306-blower fan, 401-fluidizing furnace, 402-coal bunker, 402a-feeds coal device, 403-feeds distributor, 404-gas blower, 404a-airduct, 405-removal device, 406-handling machinery V, 501-grog storehouse, 502-extra material storehouse, 503-counts material feeder III, 504-Raymond mill II, 505-handling machinery VI, the ripe powder storehouse of 506-.
Embodiment
Below in conjunction with drawings and Examples, the invention will be further described.
Embodiment 1
With reference to Fig. 1, the present embodiment comprises feed preparing device, batching and homogeneous device, drying unit, calciner and grog fuel pulverizing plant;
Described feed preparing device comprises crusher 101, handling machinery I 102, pellet storehouse 103 and bulk cargo filler bin 104, and described crusher 101 is connected with handling machinery I 102, and described handling machinery I 102 is connected with pellet storehouse 103, bulk cargo filler bin 104;
Described batching and homogeneous device comprise meter material feeder I 201, meter material feeder II 202, Raymond mill I 203, handling machinery II 204, dry powder storehouse 205, roll over mixed clarifixator 206, forming machine 207 and handling machinery III 208, described meter material feeder I 201 and pellet storehouse 103, Raymond mill I 203 is connected, described Raymond mill I 203 is connected with handling machinery II 204, described handling machinery II 204 is connected with dry powder storehouse 205, described dry powder storehouse 205 is connected with meter material feeder II 202, described meter material feeder II 202 and bulk cargo filler bin 104, roll over mixed clarifixator 206, forming machine 207 is connected, described rolling mixes clarifixator 206, forming machine 207 is connected with handling machinery III 208,
Described drying unit comprises dryer 301, handling machinery IV 302, flue I 303, flue II 304, fly-ash separator 305 and blower fan 306, described calciner comprises fluidizing furnace 401, coal bunker 402, feeds coal device 402a, feeds distributor 403, gas blower 404, removal device 405 and handling machinery V 406, described dryer 301 and handling machinery III 208, handling machinery IV 302 is connected, distributor 403 is connected described handling machinery IV 302 with feeding, described distributor 403 of feeding is connected with fluidizing furnace 401, coal device 402a's described coal bunker 402 is connected with feeding, the described coal device 402a that feeds is connected with fluidizing furnace 401, described fluidizing furnace 401 bottom is connected with removal device 405, described removal device 405 discharge is connected with handling machinery V 406, the air port that goes out of described gas blower 404 is connected by the blast inlet of airduct 404a with fluidizing furnace 401 bottom ebullated bed, the entrance end of described flue I 303 is connected with the waste gas flue of fluidizing furnace 401, exit end is connected with the gas approach of dryer 301, the entrance end of described flue II 304 is connected with the exhanst gas outlet of dryer 301, exit end is connected with the exhaust gas inlet end of fly-ash separator 305, the waste gas outlet end of described fly-ash separator 305 is connected with the entrance end pipeline of blower fan 306,
Described grog fuel pulverizing plant comprises grog storehouse 501, extra material storehouse 502, meter material feeder III 503, Raymond mill II 504, handling machinery VI 505 and ripe powder storehouse 506, described grog storehouse 501 is connected with handling machinery V 406, described grog storehouse 501, extra material storehouse 502 are connected with meter material feeder III 503, described meter material feeder III 503 is connected with Raymond mill II 504, described Raymond mill II 504 is connected with handling machinery VI 505, and described handling machinery VI 505 is connected with ripe powder storehouse 506.
In the present embodiment, being also provided with spiral ash-receiving device 305a, described spiral ash-receiving device 305a is connected with fly-ash separator 305, grog storehouse 501.
Embodiment 2
With reference to Fig. 2, the present embodiment comprises feed preparing device, batching and homogeneous device, drying unit, calciner and grog fuel pulverizing plant;
Described feed preparing device comprises crusher 101, handling machinery I 102, pellet storehouse 103, and described crusher 101 is connected with handling machinery I 102, and described handling machinery I 102 is connected with pellet storehouse 103;
Described batching and homogeneous device comprise meter material feeder I 201, meter material feeder II 202, Raymond mill I 203, handling machinery II 204, dry powder storehouse 205, forming machine 207 and handling machinery III 208, described meter material feeder I 201 is connected with pellet storehouse 103, Raymond mill I 203, described Raymond mill I 203 is connected with handling machinery II 204, described handling machinery II 204 is connected with dry powder storehouse 205, described dry powder storehouse 205 is connected with meter material feeder II 202, described meter material feeder II 202 is connected with forming machine 207, and described forming machine 207 is connected with handling machinery III 208;
Described drying unit comprises baker 301a, handling machinery IV 302, flue II 304, fly-ash separator 305 and blower fan 306, described calciner comprises fluidizing furnace 401, coal bunker 402, feeds coal device 402a, gas blower 404, removal device 405 and handling machinery V 406, described baker 301a and handling machinery III 208, handling machinery IV 302 is connected, described baker 301a, handling machinery IV 302 is positioned at the flue on fluidizing furnace 401 top, the entrance end of described flue II 304 is connected with the exhanst gas outlet of baker 301, exit end is connected with the exhaust gas inlet end of fly-ash separator 305, the waste gas outlet end of described fly-ash separator 305 is connected with the entrance end pipeline of blower fan 306, coal device 402a's described coal bunker 402 is connected with feeding, the described coal device 402a that feeds is connected with fluidizing furnace 401, described fluidizing furnace 401 bottom is connected with removal device 405, described removal device 405 discharge is connected with handling machinery V 406, the wind end of described gas blower 404 is connected with the intake stack of fluidizing furnace 401 bottom ebullated bed,
Described grog fuel pulverizing plant comprises grog storehouse 501, extra material storehouse 502, meter material feeder III 503, Raymond mill II 504, handling machinery VI 505 and ripe powder storehouse 506, described grog storehouse 501 is connected with handling machinery V 406, described grog storehouse 501, extra material storehouse 502 are connected with meter material feeder III 503, described meter material feeder III 503 is connected with Raymond mill II 504, described Raymond mill II 504 is connected with handling machinery VI 505, and described handling machinery VI 505 is connected with ripe powder storehouse 506.
In the present embodiment, being also provided with spiral ash-receiving device 305a, described spiral ash-receiving device 305a is connected with fly-ash separator 305, grog storehouse 501.
Embodiment 3
With reference to Fig. 3, the present embodiment comprises feed preparing device, batching and homogeneous device, drying unit, calciner and grog fuel pulverizing plant;
Described feed preparing device comprises handling machinery I 102, bulk cargo filler bin 104, and described handling machinery I 102 is connected with bulk cargo filler bin 104; Described handling machinery I 102 is the handling machinery of band hopper;
Described batching and homogeneous device comprise meter material feeder II 202, roll over mixed clarifixator 206 and handling machinery III 208, and described meter material feeder II 202 is connected with bulk cargo filler bin 104, the mixed clarifixator 206 of rolling, and the mixed clarifixator 206 of described rolling is connected with handling machinery III 208;
Described drying unit comprises drying crusher 301b, handling machinery IV 302, flue I 303, flue II 304, fly-ash separator 305 and blower fan 306, described calciner comprises fluidizing furnace 401, coal bunker 402, feeds coal device 402a, feeds distributor 403, gas blower 404, removal device 405 and handling machinery V 406, described drying crusher 301b and handling machinery III 208, handling machinery IV 302 is connected, distributor 403 is connected described handling machinery IV 302 with feeding, described distributor 403 of feeding is connected with fluidizing furnace 401, the entrance end of described flue I 303 is connected with the waste gas flue of fluidizing furnace 401, exit end is connected with the gas approach of drying crusher 301b, the entrance end of described flue II 304 is connected with the exhanst gas outlet of drying crusher 301b, exit end is connected with the exhaust gas inlet end of fly-ash separator 305, the waste gas outlet end of described fly-ash separator 305 is connected with the entrance end pipeline of blower fan 306, coal device 402a's described coal bunker 402 is connected with feeding, the described coal device 402a that feeds is connected with fluidizing furnace 401, described fluidizing furnace 401 bottom is connected with removal device 405, described removal device 405 discharge is connected with handling machinery V 406, and the wind end of described gas blower 404 is connected with the intake stack of fluidizing furnace 401 bottom ebullated bed,
Described grog fuel pulverizing plant comprises grog storehouse 501, extra material storehouse 502, meter material feeder III 503, Raymond mill II 504, handling machinery VI 505 and ripe powder storehouse 506, described grog storehouse 501 is connected with handling machinery V 406, described grog storehouse 501, extra material storehouse 502 are connected with meter material feeder III 503, described meter material feeder III 503 is connected with Raymond mill II 504, described Raymond mill II 504 is connected with handling machinery VI 505, and described handling machinery VI 505 is connected with ripe powder storehouse 506.
In the present embodiment, being also provided with spiral ash-receiving device 305a, described spiral ash-receiving device 305a is connected with fly-ash separator 305, grog storehouse 501.
Aforesaid device for calcium sulfate raw material, taking barren rock slag etc. as calcareous raw material, is aided with high aluminium correction material taking ridge modified sewage sludge slag or solidification sludge as main siliceous raw material, industrial waste gypsum; The block particulate materials needing powder to grind is entered after a gradating material raymond grinding powder mill and makes powder, powder enters to roll over mixed clarifixator after B grade mixture material with the loose shape gypsum not needing powder to grind and wet state material again and carries out the mixed homogeneous of dry wet stock rolling, plasticity or half harsh mix after homogeneous send into drying unit, utilize from the whole waste gas residual heat dry packs in fluidizing furnace, and de-except major part SO in flue gas by this2; When all materials all need into mill or all can enter to grind, then all proportioning materials enter raymond grinding powder grind after through the shaping feeding drying unit of forming machine; When material is fine particle material or powder or wet state material and unnecessary powder grinds, then, after all materials are sent into after batching and rolled over mixed clarifixator homogeneous, send into drying unit; The compound going out dryer sends into fluidizing furnace, with the combustion heat energy roasting material of the combustiblematerials in mud and additional coal, produce the grog taking beta-dicalcium silicate-calcium sulphoaluminate-calcium sulfate as major ingredient, grog utilizes raymond grinding powder mill to make belite-gypsum material with addition of appropriate extra material, or the grog of roasting is directly taken out without powder mill.
Claims (7)
1. one kind with the equipment of boiling roaster mud, waste gypsum production belite-gypsum material, it is characterised in that: comprise feed preparing device, batching and homogeneous device, drying unit, calciner and grog fuel pulverizing plant;
Described feed preparing device comprises crusher, handling machinery I, pellet storehouse and bulk cargo filler bin, and described crusher is connected with handling machinery I, and described handling machinery I is connected with pellet storehouse, bulk cargo filler bin;
Described batching and homogeneous device comprise meter material feeder I, meter material feeder II, Raymond mill I, handling machinery II, dry powder storehouse, roll over mixed clarifixator, forming machine and handling machinery III, described meter material feeder I is connected with pellet storehouse, Raymond mill I, described Raymond mill I is connected with handling machinery II, described handling machinery II is connected with dry powder storehouse, described dry powder storehouse is connected with meter material feeder II, described meter material feeder II is connected with bulk cargo filler bin, the mixed clarifixator of rolling, forming machine, and described rolling mixes clarifixator, forming machine is connected with handling machinery III;
Described drying unit comprises dryer, handling machinery IV, flue I, flue II, fly-ash separator and blower fan, described calciner comprises fluidizing furnace, coal bunker, feeds coal device, feeds distributor, gas blower, removal device and handling machinery V, described dryer and handling machinery III, handling machinery IV is connected, distributor is connected described handling machinery IV with feeding, described distributor of feeding is connected with fluidizing furnace, coal device is connected described coal bunker with feeding, described coal device of feeding is connected with fluidizing furnace, described fluidizing furnace bottom is connected with removal device, described removal device discharge is connected with handling machinery V, the air port that goes out of described gas blower is connected by the blast inlet of airduct with fluidizing furnace bottom ebullated bed, the entrance end of described flue I is connected with the waste gas flue of fluidizing furnace, exit end is connected with the gas approach of dryer, the described entrance end of flue II is connected with the exhanst gas outlet of dryer, exit end is connected with the exhaust gas inlet end of fly-ash separator, the waste gas outlet end of described fly-ash separator is connected with the entrance end pipeline of blower fan,
Described grog fuel pulverizing plant comprises grog storehouse, extra material storehouse, meter material feeder III, Raymond mill II, handling machinery VI and ripe powder storehouse, described grog storehouse is connected with handling machinery V, described grog storehouse, extra material storehouse are connected with meter material feeder III, described meter material feeder III is connected with Raymond mill II, described Raymond mill II is connected with handling machinery VI, and described handling machinery VI is connected with ripe powder storehouse.
2. the equipment of boiling roaster mud according to claim 1, waste gypsum production belite-gypsum material, it is characterised in that: being also provided with spiral ash-receiving device, described spiral ash-receiving device is connected with fly-ash separator, grog storehouse.
3. one kind with the equipment of boiling roaster mud, waste gypsum production belite-gypsum material, it is characterised in that: comprise feed preparing device, batching and homogeneous device, drying unit, calciner and grog fuel pulverizing plant;
Described feed preparing device comprises crusher, handling machinery I, pellet storehouse, and described crusher is connected with handling machinery I, and described handling machinery I is connected with pellet storehouse;
Described batching and homogeneous device comprise meter material feeder I, meter material feeder II, Raymond mill I, handling machinery II, dry powder storehouse, forming machine and handling machinery III, described meter material feeder I is connected with pellet storehouse, Raymond mill I, described Raymond mill I is connected with handling machinery II, described handling machinery II is connected with dry powder storehouse, described dry powder storehouse is connected with meter material feeder II, described meter material feeder II is connected with forming machine, and described forming machine is connected with handling machinery III;
Described drying unit comprises baker, handling machinery IV, flue II, fly-ash separator and blower fan, described calciner comprises fluidizing furnace, coal bunker, feeds coal device, gas blower, removal device and handling machinery V, described baker and handling machinery III, handling machinery IV is connected, described baker, handling machinery IV is positioned at the flue on fluidizing furnace top, the described entrance end of flue II is connected with the exhanst gas outlet of baker, exit end is connected with the exhaust gas inlet end of fly-ash separator, the waste gas outlet end of described fly-ash separator is connected with the entrance end pipeline of blower fan, coal device is connected described coal bunker with feeding, described coal device of feeding is connected with fluidizing furnace, described fluidizing furnace bottom is connected with removal device, described removal device discharge is connected with handling machinery V, the wind end of described gas blower is connected with the intake stack of fluidizing furnace bottom ebullated bed,
Described grog fuel pulverizing plant comprises grog storehouse, extra material storehouse, meter material feeder III, Raymond mill II, handling machinery VI and ripe powder storehouse, described grog storehouse is connected with handling machinery V, described grog storehouse, extra material storehouse are connected with meter material feeder III, described meter material feeder III is connected with Raymond mill II, described Raymond mill II is connected with handling machinery VI, and described handling machinery VI is connected with ripe powder storehouse.
4. the equipment of boiling roaster mud according to claim 3, waste gypsum production belite-gypsum material, it is characterised in that: being also provided with spiral ash-receiving device, described spiral ash-receiving device is connected with fly-ash separator, grog storehouse.
5. one kind with the equipment of boiling roaster mud, waste gypsum production belite-gypsum material, it is characterised in that: comprise feed preparing device, batching and homogeneous device, drying unit, calciner and grog fuel pulverizing plant;
Described feed preparing device comprises handling machinery I, bulk cargo filler bin, and described handling machinery I is connected with bulk cargo filler bin;
Described batching and homogeneous device comprise meter material feeder II, roll over mixed clarifixator and handling machinery III, and described meter material feeder II is connected with bulk cargo filler bin, the mixed clarifixator of rolling, and the mixed clarifixator of described rolling is connected with handling machinery III;
Described drying unit comprises drying crusher, handling machinery IV, flue I, flue II, fly-ash separator and blower fan; Described calciner comprises fluidizing furnace, coal bunker, feeds coal device, feeds distributor, gas blower, removal device and handling machinery V; Described drying crusher is connected with handling machinery III, handling machinery IV, distributor is connected described handling machinery IV with feeding, described distributor of feeding is connected with fluidizing furnace, the entrance end of described flue I is connected with the waste gas flue of fluidizing furnace, exit end is connected with the gas approach of drying crusher, the described entrance end of flue II is connected with the exhanst gas outlet of drying crusher, exit end is connected with the exhaust gas inlet end of fly-ash separator, and the waste gas outlet end of described fly-ash separator is connected with the entrance end pipeline of blower fan; Coal device is connected described coal bunker with feeding, and described coal device of feeding is connected with fluidizing furnace, and described fluidizing furnace bottom is connected with removal device, and described removal device discharge is connected with handling machinery V, and the wind end of described gas blower is connected with the intake stack of fluidizing furnace bottom ebullated bed;
Described grog fuel pulverizing plant comprises grog storehouse, extra material storehouse, meter material feeder III, Raymond mill II, handling machinery VI and ripe powder storehouse, described grog storehouse is connected with handling machinery V, described grog storehouse, extra material storehouse are connected with meter material feeder III, described meter material feeder III is connected with Raymond mill II, described Raymond mill II is connected with handling machinery VI, and described handling machinery VI is connected with ripe powder storehouse.
6. the equipment of boiling roaster mud according to claim 5, waste gypsum production belite-gypsum material, it is characterised in that: described handling machinery I is the handling machinery of band hopper.
7. according to claim 5 or 6 with the equipment of boiling roaster mud, waste gypsum production belite-gypsum material, it is characterised in that: being also provided with spiral ash-receiving device, described spiral ash-receiving device is connected with fly-ash separator, grog storehouse.
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Effective date of registration: 20161130 Address after: 410205 Hunan province high tech Development Zone Changsha Wenxuan Road No. 27 Lu Valley Yuyuan D3-101 building two floor Patentee after: CHANGSHA ZICHEN TECHNOLOGY DEVELOPMENT CO., LTD. Address before: 410013 Hunan province high tech Development Zone C2 group Binjiang fortune Silicon Valley building, room 5, building 510, room Patentee before: Yin Xiaolin |