CN104446066A - Equipment of producing belite-gypsum material by roasting sludge and waste gypsum by virtue of fluidized-bed furnace - Google Patents
Equipment of producing belite-gypsum material by roasting sludge and waste gypsum by virtue of fluidized-bed furnace Download PDFInfo
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- CN104446066A CN104446066A CN201410626579.2A CN201410626579A CN104446066A CN 104446066 A CN104446066 A CN 104446066A CN 201410626579 A CN201410626579 A CN 201410626579A CN 104446066 A CN104446066 A CN 104446066A
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Abstract
The invention discloses equipment of producing a belite-gypsum material by roasting sludge and waste gypsum by virtue of a fluidized-bed furnace. The equipment comprises a material preparing device, a material batching and homogenizing device, a drying device, a roasting device and a clinker pulverizing device, wherein the material preparing device comprises a crusher, a conveyor I, an aggregate bin and a bulk powder bin; the material batching and homogenizing device comprises a metering feeder I, a metering feeder II, a Raymond mill I, a conveyor II, a dry powder bin, a rolling and mixing homogenizer, a molder and a conveyor III; the drying device comprises a dryer, a conveyor IV, a flue gas pipeline I, a flue gas pipeline II, a dust collector and an air blower; the roasting device comprises a fluidized-bed furnace, a fuel coal bin, a coal feeder, a feeding material distributor, a fan, a material discharger and a conveyor V; and the clinker pulverizing device comprises a clinker bin, an admixture bin, a metering feeder III, a Raymond mill II and a clinker bin. The equipment disclosed by the invention can be used for realizing large-scale, recycling and energy-regeneration utilization of a good deal and a wide range of waste such as sludge, waste gypsum and waste rock ballasts so as to manufacture the belite-gypsum material with extensive use.
Description
Technical field
The present invention relates to a kind of equipment producing belite-gypsum material, be 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
Current, China's quantity of wastewater effluent is more than 5 × 10
10m
3∕ d, by every 10000m
3the 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, total situation still based on landfill, stack, topple over.At present, the main methods of mud has that ocean and culvert underdrain are toppled over, sanitary landfill, sludge composting, mud dries and burn.
On the other hand, industrial waste gypsum (as phosphogypsum) is used as plastering and for except Sulphuric acid and by-product portland cement clinker except small part is used as to add after cement adjustable solidification agent or frying or roasting modified cement through modification, stored up in a large number or landfill or be poured into cloaca culvert, serious mud groundwater resource.
Test proves, the mud had 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 produce broad-spectrum belite-gypsum material, but there is no the little and equipment that processing efficiency is high of investment so far.
Obviously, to effectively, economical, solve the mud that has a large capacity and a wide range and large waste residue such as industrial waste gypsum, barren rock slag to produce broad-spectrum belite-gypsum novel material problem easily, invest little, Charge Mixture Control require the equipment low, energy consumption is low, cost is low in the urgent need to a kind of.
Summary of the invention
Technical problem to be solved by this invention is, provides a kind of equipment with boiling roaster mud, waste gypsum production belite-gypsum material of investing little, less energy-consumption, low cost.Utilize this equipment, mass-producing, resource utilization, the recovery energy mud, waste gypsum, the barren rock slag the like waste that have a large capacity and a wide range can manufacture broad-spectrum belite-gypsum material.
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 to be counted material feeder I, counts 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 and bulk cargo filler bin, roll over mixed clarifixator, forming machine is connected, 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, described handling machinery IV is connected with hello distributor, described distributor of feeding is connected with fluidizing furnace, described coal bunker is connected with hello coal device, 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 outlet 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, be 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 count material feeder I, count 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, described coal bunker is connected with hello coal device, 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 outlet air 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, be 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 to be counted material feeder II, rolles over mixed clarifixator and handling machinery III, described meter material feeder II and bulk cargo filler bin, rolles over and mixes clarifixator and be connected, and described rolling mixes clarifixator and 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, described handling machinery IV is connected with hello distributor, 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; Described coal bunker is connected with hello coal device, 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 outlet air 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, be also provided with spiral ash-receiving device, described spiral ash-receiving device is connected with fly-ash separator, grog storehouse.
Aforesaid device with ridge modified sewage sludge slag or solidification sludge be main siliceous raw material, industrial waste gypsum for calcium sulfate raw material, with barren rock slag etc. for calcareous raw material, be aided with high alumina and correct material; After a gradating material, enter raymond grinding powder by needing the block particulate materials of grinding and grind into powder, powder again with do not need the loose shape gypsum of grinding and hygrometric state material after B grade mixture material, enter to roll over mixed clarifixator to carry out dry wet stock and roll over the matter that is mixed, plasticity after homogeneous or half harsh mix send into drying unit, utilize from the whole waste gas residual heat dry packs in fluidizing furnace, and remove most of SO in flue gas by this
2; When all materials all need into mill or all can enter to grind, then all proportioning materials enter after Raymond mill grinding through the shaping feeding drying unit of forming machine; When material be fine particle material or powder or hygrometric state material and unnecessary grinding time, then after all materials are sent into and rolled over mixed clarifixator homogeneous after batching, send into drying unit; The compound going out dryer sends into fluidizing furnace, with the combustiblematerials in mud and additional burning of coal heat energy roasting material, produce the grog being major ingredient with beta-dicalcium silicate-calcium sulphoaluminate-calcium sulfate, grog utilizes raymond grinding powder to grind into belite-gypsum material with addition of appropriate extra material, or the grog of roasting is directly taken out without grinding.
Beneficial effect of the present invention:
1) structure is simple, and invest little, the treatment capacity such as mud and industrial waste gypsum is large.
2) broad-spectrum belite-gypsum material is produced with the Raymond mill grinding, boiling roaster mud, waste gypsum etc. of Low investment, the cost of material is low for it, grinding pow consumption is low, it is low to burn till energy consumption, and fast firing technique production capacity is high, also can save desulfurization and denitration cost, be easily owner's acceptance, the recycling for 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 to 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 grinding 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 counts 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, described handling machinery IV 302 is connected with hello distributor 403, described distributor 403 of feeding is connected with fluidizing furnace 401, described coal bunker 402 is connected with hello coal device 402a, 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 outlet of described gas blower 404 is connected with the blast inlet of fluidizing furnace 401 bottom ebullated bed by airduct 404a, 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, be 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 count material feeder I 201, count 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, described coal bunker 402 is connected with hello coal device 402a, 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 outlet air 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, be 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 to be counted material feeder II 202, rolles over mixed clarifixator 206 and handling machinery III 208, described meter material feeder II 202 and bulk cargo filler bin 104, rolles over and mixes clarifixator 206 and be connected, and described rolling mixes clarifixator 206 and 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, described handling machinery IV 302 is connected with hello distributor 403, 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, described coal bunker 402 is connected with hello coal device 402a, 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 outlet air 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, be 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 with ridge modified sewage sludge slag or solidification sludge be main siliceous raw material, industrial waste gypsum for calcium sulfate raw material, with barren rock slag etc. for calcareous raw material, be aided with high alumina and correct material; After a gradating material, enter raymond grinding powder by needing the block particulate materials of grinding and grind into powder, powder again with do not need the loose shape gypsum of grinding and hygrometric state material after B grade mixture material, enter to roll over mixed clarifixator to carry out dry wet stock and roll over the matter that is mixed, plasticity after homogeneous or half harsh mix send into drying unit, utilize from the whole waste gas residual heat dry packs in fluidizing furnace, and remove most of SO in flue gas by this
2; When all materials all need into mill or all can enter to grind, then all proportioning materials enter after Raymond mill grinding through the shaping feeding drying unit of forming machine; When material be fine particle material or powder or hygrometric state material and unnecessary grinding time, then after all materials are sent into and rolled over mixed clarifixator homogeneous after batching, send into drying unit; The compound going out dryer sends into fluidizing furnace, with the combustiblematerials in mud and additional burning of coal heat energy roasting material, produce the grog being major ingredient with beta-dicalcium silicate-calcium sulphoaluminate-calcium sulfate, grog utilizes raymond grinding powder to grind into belite-gypsum material with addition of appropriate extra material, or the grog of roasting is directly taken out without grinding.
Claims (7)
1. with an equipment for boiling roaster mud, waste gypsum production belite-gypsum material, it is characterized 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 to be counted material feeder I, counts 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 and bulk cargo filler bin, roll over mixed clarifixator, forming machine is connected, 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, described handling machinery IV is connected with hello distributor, described distributor of feeding is connected with fluidizing furnace, described coal bunker is connected with hello coal device, 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 outlet 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, is characterized in that: be also provided with spiral ash-receiving device, and described spiral ash-receiving device is connected with fly-ash separator, grog storehouse.
3. with an equipment for boiling roaster mud, waste gypsum production belite-gypsum material, it is characterized 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 count material feeder I, count 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, described coal bunker is connected with hello coal device, 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 outlet air 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, is characterized in that: be also provided with spiral ash-receiving device, and described spiral ash-receiving device is connected with fly-ash separator, grog storehouse.
5. with an equipment for boiling roaster mud, waste gypsum production belite-gypsum material, it is characterized 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 to be counted material feeder II, rolles over mixed clarifixator and handling machinery III, described meter material feeder II and bulk cargo filler bin, rolles over and mixes clarifixator and be connected, and described rolling mixes clarifixator and 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, described handling machinery IV is connected with hello distributor, 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; Described coal bunker is connected with hello coal device, 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 outlet air 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, is characterized in that: described handling machinery I is the handling machinery of band hopper.
7. the equipment with boiling roaster mud, waste gypsum production belite-gypsum material according to claim 5 or 6, it is characterized in that: be also provided with spiral ash-receiving device, described spiral ash-receiving device is connected with fly-ash separator, grog storehouse.
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105352334A (en) * | 2015-12-09 | 2016-02-24 | 故城北新建材有限公司 | Hot smoke recycling system |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20090071374A1 (en) * | 2006-03-29 | 2009-03-19 | Zeobond Research Pty Ltd | Dry Mix Cement Composition, Methods and Systems Involving Same |
| CN202016957U (en) * | 2011-05-11 | 2011-10-26 | 澧县金辉石膏制品有限责任公司 | Continuous gypsum powder production system of small gypsum boards for architectural decoration |
| CN204162606U (en) * | 2014-11-10 | 2015-02-18 | 尹小林 | With the equipment of boiling roaster mud, waste gypsum production belite-gypsum material |
-
2014
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Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20090071374A1 (en) * | 2006-03-29 | 2009-03-19 | Zeobond Research Pty Ltd | Dry Mix Cement Composition, Methods and Systems Involving Same |
| CN202016957U (en) * | 2011-05-11 | 2011-10-26 | 澧县金辉石膏制品有限责任公司 | Continuous gypsum powder production system of small gypsum boards for architectural decoration |
| CN204162606U (en) * | 2014-11-10 | 2015-02-18 | 尹小林 | With the equipment of boiling roaster mud, waste gypsum production belite-gypsum material |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105352334A (en) * | 2015-12-09 | 2016-02-24 | 故城北新建材有限公司 | Hot smoke recycling system |
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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 |