CN102731004B - Mixing regeneration aggregate milling production line and milling method thereof - Google Patents

Mixing regeneration aggregate milling production line and milling method thereof Download PDF

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Publication number
CN102731004B
CN102731004B CN201210147849.2A CN201210147849A CN102731004B CN 102731004 B CN102731004 B CN 102731004B CN 201210147849 A CN201210147849 A CN 201210147849A CN 102731004 B CN102731004 B CN 102731004B
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discharge pipe
production line
regeneration
mill
assembly
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CN102731004A (en
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徐东升
刘琼
王晓波
吕杰
钟宇东
陆沈磊
阮志伟
杨德志
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SHANGHAI DEBIN ENVIRONMENTAL PROTECTION TECHNOLOGY Co Ltd
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SHANGHAI DEBIN ENVIRONMENTAL PROTECTION TECHNOLOGY Co Ltd
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/91Use of waste materials as fillers for mortars or concrete

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Abstract

The present invention discloses a mixing regeneration aggregate milling production line and a milling method thereof, and relates to the technical field of building material processing. The mixing regeneration aggregate milling production line comprises a primary powder grinding assembly, a terminal powder grinding assembly and a grading material collecting assembly, wherein the output end of the primary powder grinding assembly is corresponding to the input end of the terminal powder grinding assembly, and the terminal powder grinding assembly and the grading material collecting assembly are connected. The mixing regeneration aggregate milling production line and the milling method thereof of the present invention provide significant energy saving effects, meet characteristic requirements of mixing regeneration aggregate milling, do not require the grinding media, and have characteristics of low energy consumption, large output, high grinding efficiency, capability of shaping, and investment saving.

Description

Mixed regeneration aggregate flour production line and its milling method
Technical field
The present invention relates to construction material processing technique field and in particular to a kind of mixed regeneration aggregate flour production line and its Milling method.
Background technology
Waste material of buildings builds waste and old construction material that is newly-built, reconstructing, remove and produce.China's current waste material of buildings resource Change the waste material of buildings recycling main task to be waste and old building demolition and producing.Because the building construction waste that China removes is dominated Composition is based on fired brick, supplemented by concrete, so pass through and crushing, sieve, going soil, roguing, the mixing dealing except ferrum etc. Regeneration aggregate, comprises a large amount of brickbats.This mixed regeneration aggregate is not suitable for using as concrete skeleton structural material.But this Plant the suitable deep processing of mixed regeneration aggregate containing a large amount of burnedc lay materials and become regenerative micro powder, blend as various cement based building materials Material uses.Burnedc lay material has pozzolanic activity, uses and can reduce cement consumption as admixture, greatly promotes waste and old sintering The recycle value of clay brick.
Because the mixed regeneration aggregate based on fired brick has the characteristic such as mixed, miscellaneous and wet, using building material industry tradition powder Grinding production line, all can not meet mixed regeneration aggregate powder needs, there is a problem of that high energy consumption, efficiency are low it is also difficult to realize dividing Class regenerates.The milling equipment of building material industry generally has high pressure roll press, vertical mill and three kinds of ball mill, adheres to squeezing mill separately, rolls Mill and three kinds of ball milling.Above-mentioned three kinds of conventional grinding machines require it is impossible to adapt to building waste powder completely.
High pressure roll press generally grinds not as terminal and uses, because the powder body that high pressure roll press grinds is mainly lamellar and pin Shape, so the powder body shape that high pressure roll press grinds is bad, also there is the powder fineness deficiency squeezing out in this high pressure roll press, The relatively low shortcoming of flour extraction.
Vertical mill is abstained to by metal object in grinding material, due to generally can not absolute guarantee enter vertical mill building give up Thing mixed regeneration aggregate does not contain the fine metal things such as iron nail, therefore the application of vertical mill is restricted.
Ball milling speculative investment is big and high energy consumption, thus relatively inefficient.
Vertical mill and ball mill are charging all to be worn into micropowder, due to the natural gravel in mixed regeneration aggregate and fluvial sand Belong to inert material, worn into micropowder, regenerative micro powder activity can be caused not high, and natural gravel and fluvial sand intensity are high, will The energy consumption that they are clayed into power is higher.
How mixed regeneration aggregate to be ground required fineness, the micropowder being ground out is classified, produce the equipment of micropowder Energy consumption is low, yield is greatly the problem that those skilled in the art need to solve.
Content of the invention
The primary and foremost purpose of the present invention is that and overcomes the shortcomings of existing for existing milling equipment, thus providing a kind of mixing again Raw aggregate flour production line.
Second object of the present invention is to provide described mixed regeneration aggregate milling method.
The mixed regeneration aggregate flour production line of the present invention, receives including primary grinding assembly, terminal grinding assembly and classification Material assembly, the outfan of primary grinding assembly is correspondings with the input of terminal grinding assembly, terminal grinding assembly and be classified rewinding Assembly connects.
Described primary grinding assembly includes self-pressurization hopper and high pressure roll press, and self-pressurization hopper is with high pressure roll press even Connect, the outfan of high pressure roll press is corresponding with the input of terminal grinding assembly.
Described self-pressurization hopper is provided with feeding mouth.
Described high pressure roll press is the high pressure roll press to roller move toward one another, and the pressure limit of this high pressure roll press is 40- 200MPa.
Described terminal grinding assembly includes bucket elevator, impact mill, drying oven and airflow type drying box, and bucket type carries The input of the machine of liter is corresponding with the outfan of primary grinding assembly, the outfan of bucket elevator and the input of impact mill Correspond to, the discharging opening of impact mill and hot gas inlet are connected with airflow type drying box and drying oven respectively, airflow type drying box Outfan with classification rewinding assembly input corresponding.
The center of the grinding chamber of described impact mill is provided with one by motor-driven main shaft, and described main shaft is arranged with Multigroup mill, every group of mill is respectively equipped with one group of radially-arranged bistrique.
Described impact mill is high speed machine Type Impact Superfine Mill, the dynamic mill body spinner velocity model of described pulverizer Enclose for 700-1500r/min.
Described classification rewinding assembly includes inertia force classifier, whirlwind clarifier, air box impulse dust-precipitator, the first discharge nozzle Road, the second discharge pipe, the 3rd discharge pipe and aerator, the input of inertia force classifier is the input of classification rewinding assembly End, the ventilation end of inertia force classifier, transmission end and discharge end respectively with aerator, the input of whirlwind clarifier and the first discharging Pipeline connection, the transmission end of described whirlwind clarifier and discharge end input and the second discharging with air box impulse dust-precipitator respectively Pipeline connects, and the discharge end of air box impulse dust-precipitator is connected with the 3rd discharge pipe.
It is respectively equipped with out on first discharge pipe of described classification rewinding assembly, the second discharge pipe and the 3rd discharge pipe Material mouth, the first discharge pipe, the second discharge pipe and the 3rd discharge pipe discharging particle diameter are respectively 0.16-2.36mm, 0.08- 0.16mm、0-0.08mm.
The discharging opening of described first discharge pipe connects recycled fine aggregate warehouse.
The discharging opening of described second discharge pipe connects the first regenerative micro powder tank.
The discharging opening of described 3rd discharge pipe connects the second regenerative micro powder tank.
Described classification rewinding assembly, recycled fine aggregate warehouse, the first regenerative micro powder tank and the second regenerative micro powder tank are constituted to be received Collecting system.
The mixed regeneration aggregate milling method of the present invention, the method comprises the following steps:
The first step, building waste are stacked, crush, sieving, going soil, roguing, remove ferrum and separate lightweight combustible through classification, Prepare the mixed regeneration material that particle diameter is less than 50mm;
Second step, mixed regeneration material are conveyed into self-pressurization hopper, high pressure roll press carries out pre- grinding;
3rd step:, to impact mill, the outfan that regeneration feed passes through self-pressurization hopper is continuous for drying oven heat air delivery It is conveyed into impact mill;
4th step:Regeneration feed carries out whole grinding by impact mill;
5th step:Regeneration feed enters inertia force classifier, and inertia force classifier is classified to regeneration feed, 0.16- The regeneration feed of 2.36mm is passed through the first discharge pipe and is entered recycled fine aggregate warehouse, and the regeneration feed of 0-0.16mm enters next Level classifying equipoment, aerator provides wind-force for inertia force classifier;
6th step:Whirlwind clarifier is classified to regeneration feed again, isolates the regeneration that particle diameter is 0.08-0.16mm Material, and the first regenerative micro powder tank is transported to by the second discharge pipe;
7th step:To particle diameter, the regenerative micro powder for below 0.08mm is collected air box impulse dust-precipitator, and passes through the 3rd Discharge pipe is transported to the second regenerative micro powder tank.
Described self-pressurization hopper, high pressure roll press are by squeezing mill, and squeezing mill carries out pre- grinding and thick to regeneration feed Mill, becomes particle diameter to be less than below 5mm regeneration feed regeneration feed crush and grind, and a part is easily ground to form the regeneration of powder body Micropowder is worn in material extruding.
The temperature of described hot blast is 400-600 degree.
Described impact mill is by whole grinding and fine grinding, and impact mill is by the active regeneration material in regeneration feed Further levigate to improve activity, and the inertia regeneration feed in regeneration feed is ground to form Spherical Sand.
The raw material of the present invention is mixed regeneration aggregate, and this aggregate comprises the materials such as clay brick, concrete, by this mixed regeneration Aggregate enters production line from self-pressurization hopper feeding mouth, and this mixed regeneration aggregate is delivered to high pressure roll-in from self-pressurization hopper afterwards Machine, high pressure roll press carries out pre- grinding to mixed regeneration aggregate.Because mixed regeneration aggregate is moist, high pressure roll press is extruded again Biological material journey pie, pie regeneration feed bucket elevator is promoted to next step crushing and grinding equipment impact mill.Punching The formula grinding machine of hitting is provided with feeding mouth, discharging opening, hot gas inlet, and hot gas inlet connects drying oven, provides 400-600 DEG C of hot-air.
The impact mill existing impact grinding effect of high-speed rotation, has Ball-stirring mill, squeezing mill, vibromill to grind special again Levy.To impact based on pulverizing, rear end is based on crush and grind for impact mill front end.Using concrete gravel and Behavior of Hardened Cement Paste, brick Head intensity difference and mixed regeneration aggregate process of lapping in produce selective molecular attraction phenomenon, brickbat, Behavior of Hardened Cement Paste crush be milled into micro- Powder, stone and sand are broken into fine sand, and its essence is exactly to have reached mixed regeneration aggregate to regenerate different regrown materiaves respectively And the purpose of recovery of classifying.Thinner due to entering the mixed regeneration aggregate size in impact mill, at 400-600 degree Celsius In mill chamber, moment is realized drying, and drying efficiency is high.
After impact mill, inertia force classifier is classified to regeneration feed.The regeneration feed of 0.16-2.36mm is entered Enter the first discharge pipe, the regeneration feed of 0-0.16mm enters next stage classifying equipoment.Aerator provides wind for inertia force classifier Power.
Whirlwind clarifier is classified to regeneration feed again, isolates the regeneration feed that particle diameter is 0.08-0.16mm, and It is transported to the first regenerative micro powder tank.
To particle diameter, the regenerative micro powder for below 0.08mm is collected air box impulse dust-precipitator, and it is micro- to be transported to the second regeneration Powder tank.
The invention has the beneficial effects as follows:
1)Energy-saving effect projects, the mixed regeneration aggregate flour production line of the present invention and its milling method, the comprehensive energy of powder processed Consume for 10-12kw h/t, and the tradition milling equipment flour production line comprehensive energy consumption 30-60kw h/t such as ball mill.High pressure roller Press is roughly ground equipment and high speed machine impacting superfine mill and is broadly fallen into China and advocate the high efficiency energy saving new grinding of development and sets Standby, it pulverizes effect rate between 70-80%, and ball mill is pulverized effect rate and only had 5%.
2)Meet mixed regeneration aggregate powder feature to require, this flour production line meets and gives full play to different building waste materials Property effect purpose, " grog " i.e. fired brick and Behavior of Hardened Cement Paste grind out regeneration micropowder, and " raw material " i.e. stone and sand grind out Regeneration sand.Avoid and treating construction waste, active material and inertia material are used for using traditional milling equipment and grinding process Material one broadly grinds to form powder body, the shortcoming reducing powder active.
3)Mill must be equipped be situated between, mixed regeneration aggregate mutually collides autogenous grinding from realizing pulverizing, and decreases mill dielectric loss consumption.
4)Energy consumption is low, yield is big, crush efficiency is high.
5)There is shaping feature, product shape spherical in shape.
6)Multi-functional, integrate pulverizing, grind, dry and be classified.
7)Investment-saving, reduces investment 50% about through comparing than traditional milling equipment.
Brief description
Fig. 1 is the structural representation of the mixed regeneration aggregate flour production line of the present invention.
Fig. 2 is that the structure of the mixed regeneration aggregate flour production line of the present invention connects block diagram.
Fig. 3 is the process chart of the mixed regeneration aggregate milling method of the present invention.
Specific embodiment
Below in conjunction with specific embodiment, the invention will be further described.It should be understood that following examples are merely to illustrate this Invention is not for restriction the scope of the present invention.
Embodiment 1
As shown in figure 1, the mixed regeneration aggregate flour production line of the present invention, including primary grinding assembly 1, terminal grinding group Part 2 and classification rewinding assembly 3, the outfan of primary grinding assembly 1 is corresponding with the input of terminal grinding assembly 2, terminal grinding Assembly 2 is connected with classification rewinding assembly 3.
Described primary grinding assembly 1 includes self-pressurization hopper 11 and high pressure roll press 12, self-pressurization hopper 11 and high pressure roller Press 12 connects, and the outfan of high pressure roll press 12 is corresponding with the input of terminal grinding assembly 2.
Described self-pressurization hopper 11 is provided with feeding mouth.
Described high pressure roll press 12 is the high pressure roll press 12 to roller move toward one another, the pressure limit of this high pressure roll press 12 For 40-200MPa.
Described terminal grinding assembly 2 includes bucket elevator 21, impact mill 22, drying oven 23 and airflow type drying box 24, the input of bucket elevator 21 is corresponding with the outfan of primary grinding assembly 1, the outfan of bucket elevator 21 and impact The input of formula grinding machine 22 corresponds to, the discharging opening of impact mill 22 and hot gas inlet respectively with airflow type drying box 24 and drying Stove 23 connects, and the outfan of airflow type drying box 24 is corresponding with the input of classification rewinding assembly 3.
The center of the grinding chamber of described impact mill 22 is provided with one by motor-driven main shaft 221, described main shaft 221 On be arranged with multigroup mill 222, every group of mill 222 is respectively equipped with one group of radially-arranged bistrique 2221.
Described impact mill 22 is high speed machine Type Impact Superfine Mill, the dynamic mill body spinner velocity of described pulverizer Scope is 700-1500r/min.
Described classification rewinding assembly 3 includes inertia force classifier 31, whirlwind clarifier 32, air box impulse dust-precipitator 33, first Discharge pipe 34, the second discharge pipe 35, the 3rd discharge pipe 36 and aerator 37, the input of inertia force classifier 31 is classification The input of rewinding assembly 3, the ventilation end of inertia force classifier 31, transmission end and discharge end respectively with aerator 37, cyclone classified The input of machine 32 and the first discharge pipe 34 connect, the transmission end of described whirlwind clarifier 32 and discharge end respectively with gas tank arteries and veins Rush the input of dust-precipitator 33 and the second discharge pipe 35 connects, the discharge end of air box impulse dust-precipitator 33 and the 3rd discharge pipe 36 connections.
Divide on first discharge pipe 34 of described classification rewinding assembly 3, the second discharge pipe 35 and the 3rd discharge pipe 36 It is not provided with discharging opening, the first discharge pipe 34, the second discharge pipe 35 and the 3rd discharge pipe 36 discharging particle diameter are respectively 0.16- 2.36mm、0.08-0.16mm、0-0.08mm.
The discharging opening of described first discharge pipe 34 connects recycled fine aggregate warehouse 41.
The discharging opening of described second discharge pipe 35 connects the first regenerative micro powder tank 42.
The discharging opening of described 3rd discharge pipe 36 connects the second regenerative micro powder tank 43.
As shown in figures 1 and 3, described classification rewinding assembly 3, recycled fine aggregate warehouse 41, the first regenerative micro powder tank 42 and Second regenerative micro powder tank 43 constitutes collection system.
As shown in Figures 2 and 3, the mixed regeneration aggregate milling method of the present invention, step is:
The first step, building waste are stacked, crush, sieving, going soil, roguing, remove ferrum and separate lightweight combustible through classification, Prepare the mixed regeneration material that particle diameter is less than 50mm;
Second step, mixed regeneration material are conveyed into self-pressurization hopper 11, high pressure roll press 12 carries out pre- grinding;
3rd step:Drying oven 23 heat air delivery passes through the output of self-pressurization hopper 11 to impact mill 22, regeneration feed End continuous conveying enters impact mill 22;
4th step:Regeneration feed carries out whole grinding by impact mill 22;
5th step:Regeneration feed enters inertia force classifier 31, and inertia force classifier 31 is classified to regeneration feed, 0.16- The regeneration feed of 2.36mm enters recycled fine aggregate warehouse 41 by the first discharge pipe 34, and the regeneration feed of 0-0.16mm enters Next stage classifying equipoment, aerator 37 provides wind-force for inertia force classifier 31;
6th step:Whirlwind clarifier 32 is classified to regeneration feed again, isolates particle diameter for 0.08-0.16mm again Biological material, and the first regenerative micro powder tank 42 is transported to by the second discharge pipe 35;
7th step:To particle diameter, the regenerative micro powder for below 0.08mm is collected air box impulse dust-precipitator 33, and by the Three discharge pipes 36 are transported to the second regenerative micro powder tank 43.
Described self-pressurization hopper 11, high pressure roll press 12 are by squeezing mill, and squeezing mill carries out pre- grinding to regeneration feed And corase grind, become particle diameter to be less than below 5mm regeneration feed regeneration feed crush and grind, and a part is easily ground to form powder body Micropowder is worn in regeneration feed extruding.
The temperature of described hot blast is 400-600 degree.
Described impact mill 22 by the active regeneration material in regeneration feed further levigate to improve activity, and will again Inertia regeneration feed in biological material grinds to form Spherical Sand.
Described first step breaking method includes:Slightly break and two-stage nitration breaks.
Described slightly break be broken using jaw, counterattack is broken, roller breaks and hammer is broken etc. has and slightly break the equipment of function and realize building waste Coarse crushing is less than 100mm regeneration feed to particle diameter.
It is to break and hammer into shape the equipment such as broken using counterattack that described two-stage nitration breaks, broken in realization, is broken into particle diameter and is less than below 50mm regeneration Material.
Described go soil to be because the native intensity in waste material of buildings is relatively low, in broken equipment, by hitting, beating, grind and rub with the hands Technique, quickly becomes powder.
Described screening is the regeneration feed that recovery particle diameter is less than 50mm, and particle diameter is more than to break in the return of 50mm regeneration feed and adds Work.
The regeneration feed that described particle diameter is less than 50mm includes broken brick aggregate and Waste concrete aggregate, the as building of the present invention Garbage regeneration raw material.
The raw material of the present invention is mixed regeneration aggregate, and this aggregate comprises the materials such as clay brick, concrete, by this mixed regeneration Aggregate enters production line from self-pressurization hopper 11 feeding mouth, and this mixed regeneration aggregate is delivered to high pressure from self-pressurization hopper 11 afterwards Roll squeezer 12, high pressure roll press 12 carries out pre- grinding to mixed regeneration aggregate.Because mixed regeneration aggregate is moist, high pressure roll press The regeneration feed journey pie of 12 extrusions, pie regeneration feed bucket elevator 21 is promoted to the punching of next step crushing and grinding equipment Hit formula grinding machine 22.Impact mill 22 is provided with feeding mouth, discharging opening, hot gas inlet, and hot gas inlet connects drying oven 23, provides 400-600 DEG C of hot-air.
The impact mill 22 existing impact grinding effect of high-speed rotation, has Ball-stirring mill, squeezing mill, vibromill to grind special again Levy.To impact based on pulverizing, rear end is based on crush and grind for impact mill 22 front end.Using concrete gravel and Behavior of Hardened Cement Paste, The selective molecular attraction phenomenon producing in brick intensity difference and mixed regeneration aggregate process of lapping, brickbat, Behavior of Hardened Cement Paste crush and are milled into Micropowder, stone and sand are broken into fine sand, and its essence is exactly to have reached mixed regeneration aggregate to regenerate different regenerated materials respectively Expect and classify the purpose of recovery.Thinner due to entering the mixed regeneration aggregate size in impact mill 22, Celsius in 400-600 In the mill chamber of degree, moment is realized drying, and drying efficiency is high.
After impact mill 22, inertia force classifier 31 is classified to regeneration feed.The regrowth of 0.16-2.36mm Material enters the first discharge pipe 34, and the regeneration feed of 0-0.16mm enters next stage classifying equipoment.Aerator 37 is inertial classification Machine 31 provides wind-force.
Whirlwind clarifier 32 is classified to regeneration feed again, isolates the regeneration feed that particle diameter is 0.08-0.16mm, And it is transported to the first regenerative micro powder tank 42.
To particle diameter, the regenerative micro powder for below 0.08mm is collected air box impulse dust-precipitator 33, and is transported to the second regeneration Micropowder tank 43.

Claims (9)

1. a kind of mixed regeneration aggregate flour production line is it is characterised in that including primary grinding assembly, terminal grinding assembly and dividing Level rewinding assembly, the outfan of primary grinding assembly is corresponding with the input of terminal grinding assembly, terminal grinding assembly and classification Rewinding assembly connects, and described terminal grinding assembly includes bucket elevator, impact mill, drying oven and airflow type drying box, The input of bucket elevator is correspondings with the outfan of primary grinding assembly, the outfan of bucket elevator and impact mill Input corresponds to, and the discharging opening of impact mill and hot gas inlet are connected with airflow type drying box and drying oven respectively, air-flowing type The outfan of drying baker is corresponding with the input of classification rewinding assembly.
2. mixed regeneration aggregate flour production line as claimed in claim 1 is it is characterised in that described primary grinding assembly includes Self-pressurization hopper and high pressure roll press, self-pressurization hopper is connected with high pressure roll press, the outfan of high pressure roll press and terminal powder The input of mill assembly corresponds to.
3. mixed regeneration aggregate flour production line as claimed in claim 2 it is characterised in that described self-pressurization hopper be provided with into Material mouth.
4. mixed regeneration aggregate flour production line as claimed in claim 2 is it is characterised in that described high pressure roll press is to roller The high pressure roll press of move toward one another, the pressure limit of this high pressure roll press is 40-200MPa.
5. mixed regeneration aggregate flour production line as claimed in claim 1 is it is characterised in that the grinding of described impact mill The center of room is provided with one by motor-driven main shaft, described main shaft is arranged with multigroup mill, every group of mill is respectively equipped with One group of radially-arranged bistrique.
6. mixed regeneration aggregate flour production line as claimed in claim 1 is it is characterised in that described impact mill is at a high speed Mechanical shock formula ultrafine crusher, the dynamic mill body spinner velocity scope of described pulverizer is 700-1500r/min.
7. mixed regeneration aggregate flour production line as claimed in claim 1 is it is characterised in that described classification rewinding assembly includes Inertia force classifier, whirlwind clarifier, air box impulse dust-precipitator, the first discharge pipe, the second discharge pipe, the 3rd discharge pipe and Aerator, the input of inertia force classifier is the input of classification rewinding assembly, the ventilation end of inertia force classifier, transmission end and go out Material end is connected with aerator, the input of whirlwind clarifier and the first discharge pipe respectively, the transmission end of described whirlwind clarifier It is connected with the input of air box impulse dust-precipitator and the second discharge pipe respectively with discharge end, the discharge end of air box impulse dust-precipitator It is connected with the 3rd discharge pipe.
8. mixed regeneration aggregate flour production line as claimed in claim 7 it is characterised in that described classification rewinding assembly It is respectively equipped with discharging opening, the first discharge pipe, the second discharge nozzle on one discharge pipe, the second discharge pipe and the 3rd discharge pipe Road and the 3rd discharge pipe discharging particle diameter are respectively 0.16-2.36mm, 0.08-0.16mm, 0-0.08mm;
The discharging opening of described first discharge pipe connects recycled fine aggregate warehouse;
The discharging opening of described second discharge pipe connects the first regenerative micro powder tank;
The discharging opening of described 3rd discharge pipe connects the second regenerative micro powder tank.
9. a kind of mixed regeneration aggregate system based on the mixed regeneration aggregate flour production line any one of claim 1-8 Powder method is it is characterised in that the method comprises the following steps:
The first step, building waste are stacked, crush, sieving, going soil, roguing, remove ferrum and separate lightweight combustible through classification, preparation Go out the mixed regeneration material that particle diameter is less than 50mm;
Second step, mixed regeneration material are conveyed into self-pressurization hopper, high pressure roll press carries out pre- grinding;
3rd step:Drying oven heat air delivery passes through the outfan continuous conveying of self-pressurization hopper to impact mill, regeneration feed Enter impact mill;
4th step:Regeneration feed carries out whole grinding by impact mill;
5th step:Regeneration feed enters inertia force classifier, and inertia force classifier is classified to regeneration feed, 0.16-2.36mm's Regeneration feed is passed through the first discharge pipe and is entered recycled fine aggregate warehouse, and the regeneration feed of 0-0.16mm enters next stage classification and sets Standby, aerator provides wind-force for inertia force classifier;
6th step:Whirlwind clarifier is classified to regeneration feed again, isolates the regrowth that particle diameter is 0.08-0.16mm Material, and the first regenerative micro powder tank is transported to by the second discharge pipe;
7th step:To particle diameter, the regenerative micro powder for below 0.08mm is collected air box impulse dust-precipitator, and passes through the 3rd discharging Pipeline is to the second regenerative micro powder tank.
CN201210147849.2A 2012-05-11 2012-05-11 Mixing regeneration aggregate milling production line and milling method thereof Expired - Fee Related CN102731004B (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104844041A (en) * 2015-05-21 2015-08-19 南通天蓝环保能源成套设备有限公司 Building rubbish recycling reclaimed sand powder efficient production system
CN106111665A (en) * 2016-06-28 2016-11-16 杭州市环境集团有限公司 A kind of building waste processing method
CN115594430A (en) * 2022-10-03 2023-01-13 天津朝阳环保科技集团有限公司(Cn) Production method of aggregate
CN115972378B (en) * 2023-02-20 2024-01-30 沭阳县晟一建筑垃圾处理有限公司 Environment-friendly regenerated brick intelligent production line

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1353019A (en) * 2000-11-08 2002-06-12 人善企业株式会社 Production equipment of regenerated aggregate using building waste material as raw material and regenerated aggregate
CN201381285Y (en) * 2009-04-24 2010-01-13 西安墙体材料研究设计院 Manufacturing equipment for building rubbish recycled aggregate
JP4676245B2 (en) * 2005-05-18 2011-04-27 Eacle有限会社 Method for producing recycled fine aggregate, and recycled fine aggregate
CN102115313A (en) * 2009-12-31 2011-07-06 上海德滨环保科技有限公司 Method for producing reclaimed machine-made sand with building rubbish
CN102211889A (en) * 2011-04-19 2011-10-12 上海德滨环保科技有限公司 Method for resource recovery of construction wastes

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1353019A (en) * 2000-11-08 2002-06-12 人善企业株式会社 Production equipment of regenerated aggregate using building waste material as raw material and regenerated aggregate
JP4676245B2 (en) * 2005-05-18 2011-04-27 Eacle有限会社 Method for producing recycled fine aggregate, and recycled fine aggregate
CN201381285Y (en) * 2009-04-24 2010-01-13 西安墙体材料研究设计院 Manufacturing equipment for building rubbish recycled aggregate
CN102115313A (en) * 2009-12-31 2011-07-06 上海德滨环保科技有限公司 Method for producing reclaimed machine-made sand with building rubbish
CN102211889A (en) * 2011-04-19 2011-10-12 上海德滨环保科技有限公司 Method for resource recovery of construction wastes

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