CN205032470U - Viscidity industry solid waste pretreatment systems - Google Patents
Viscidity industry solid waste pretreatment systems Download PDFInfo
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- CN205032470U CN205032470U CN201520773989.XU CN201520773989U CN205032470U CN 205032470 U CN205032470 U CN 205032470U CN 201520773989 U CN201520773989 U CN 201520773989U CN 205032470 U CN205032470 U CN 205032470U
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- solid waste
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- machine
- discharge valve
- waste pretreatment
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Abstract
The utility model relates to a viscidity industry solid waste pretreatment systems, including vertical drying -machine, hot -air pipes, hot -blast furnace, break up machine, feed inlet, selection powder machine, dust collector intake stack, cloth screen, flue gas pipeline and draught fan only, vertical drying -machine one end communicates with each other with the hot -blast furnace through hot -air pipes, and the other end communicates with each other with selection powder machine, vertical drying -machine one side is located the hot -air pipes top and communicates with each other with the feed inlet, the feed inlet upper end is equipped with the machine of breaing up, selection powder machine links to each other with the cloth screen through the dust collector intake stack, the cloth screen links to each other with the draught fan through clean flue gas pipeline, the utility model discloses a viscidity industry solid waste pretreatment systems, the simple and practical of its system has solved the material and easily glued the problem that wall, big cubic material can't dry by the fire, and drying efficiency is high, and equipment area is little, low in production cost, system's output is big, letting the chance that has obtained the reutilization useless admittedly, has higher practical value and spreading value.
Description
Technical field
The utility model relates to a kind of pretreatment system, particularly relates to a kind of viscosity Industrial Solid Waste pretreatment system.
Background technology
A large amount of industrial wastes can be inevitably produced in the industrial production of present stage, it is with toughness mostly, as desulfurated plaster, carbide slag, flyash etc., these waste materials easily cause secondary pollution and the wasting of resources, but these waste materials are in other industry, as cement industry etc. can obtain secondary application, turned waste into wealth, but its viscosity has had influence on again the normal use of desulfurated plaster, carbide slag, flyash etc., so be necessary to carry out fully utilizing again after its viscosity is eliminated in pretreatment to desulfurated plaster, carbide slag, flyash etc.
Utility model content
The utility model object provides a kind of structure simple to overcome the deficiencies in the prior art, and floor space is little, and system throughput is large, well can eliminate the viscosity Industrial Solid Waste pretreatment system of viscosity in industrial waste.
For achieving the above object, the technical solution adopted in the utility model is: a kind of viscosity Industrial Solid Waste pretreatment system, comprises tower drier, hot air duct, hot-blast stove, beater, charging aperture, powder concentrator, dust-precipitator intake stack, bagroom, neat stress pipeline and air-introduced machine; Described tower drier one end is communicated with hot-blast stove by hot air duct, and the other end communicates with powder concentrator; Described tower drier side is positioned at above hot air duct, communicates with charging aperture; Described charging aperture upper end is provided with beater; Described powder concentrator is connected with bagroom by dust-precipitator intake stack; Described bagroom is connected with air-introduced machine by neat stress pipeline.
Preferably, described tower drier is vertical suspending parallel flow dryer.
Preferably, described beater is the special beater of viscous material.
Preferably, described tower drier lower end is provided with lump material lock wind discharge valve, bulky grain lock wind discharge valve and bulky grain lock wind discharge valve successively.
Preferably, described powder concentrator lower end is provided with granule lock wind discharge valve; Described bagroom lower end is provided with granular material lock wind discharge valve.
Due to the utilization of technique scheme, the utility model compared with prior art has following advantages: the viscosity Industrial Solid Waste pretreatment system of the utility model scheme, after solid waste material is broken up by the special beater of viscous material, the surface area of solid waste material and hot air increases, thus accelerate the speed of moisture evaporation, improve drying efficiency, make material feed dryer simultaneously and become easy and smooth, solve material easily sticky wall, the problem that large-block material cannot dry, its system architecture is simple and practical, occupation area of equipment is little, production cost is low, system throughput is large, solid waste is allowed to obtain the chance of secondary utilization well, reduce cost of material, there is higher practical value and promotional value.
Accompanying drawing explanation
Below in conjunction with accompanying drawing, technical solutions of the utility model are described further.
Accompanying drawing 1 is the structural representation of the utility model viscosity Industrial Solid Waste pretreatment system.
Wherein: 1, tower drier; 2, hot air duct; 3, hot-blast stove; 4, beater; 5, charging aperture; 6, powder concentrator; 7, dust-precipitator intake stack; 8, bagroom; 9; Neat stress pipeline; 10, air-introduced machine; 11, lump material lock wind discharge valve; 12, bulky grain lock wind discharge valve; 13, granule lock wind discharge valve; 14, granular material lock wind discharge valve.
Detailed description of the invention
Below in conjunction with drawings and the specific embodiments, the utility model is described in further detail.
Described in the utility model a kind of viscosity Industrial Solid Waste pretreatment system as shown in Figure 1, comprises tower drier 1, hot air duct 2, hot-blast stove 3, beater 4, charging aperture 5, powder concentrator 6, dust-precipitator intake stack 7, bagroom 8, neat stress pipeline 9 and air-introduced machine 10; Described tower drier 1 one end is communicated with hot-blast stove 3 by hot air duct 2, and the other end communicates with powder concentrator 6; Described tower drier 1 side is positioned at above hot air duct 3 and communicates with charging aperture 5; Described charging aperture 5 upper end is provided with beater 4; Described powder concentrator 6 is connected with bagroom 8 by dust-precipitator intake stack 7; Described bagroom 8 is connected with air-introduced machine 10 by neat stress pipeline 9; Described tower drier 1 is vertical suspending parallel flow dryer; Described beater 4 is the special beater of viscous material; Described tower drier 1 lower end is provided with lump material lock wind discharge valve 11, bulky grain lock wind discharge valve 12 and bulky grain lock wind discharge valve 12 successively; Described powder concentrator 6 lower end is provided with granule lock wind discharge valve 13; Described bagroom 8 lower end is provided with granular material lock wind discharge valve 14.
Described in the utility model a kind of viscosity Industrial Solid Waste pretreatment system as shown in Figure 1, its nucleus equipment is beater and tower drier, during practical operation, first by air-heater, powder concentrator and bagroom unlatching work, then sticky lumpy material is dropped in beater, sticky lumpy material is broken up after blade cuts becomes particle by the viscous material of high-speed rotation is special, flow in vertical suspending parallel flow dryer by charging aperture, granule materials contacts with thermal current from bottom to top in the process fallen, granule materials is suspended in dryer pipeline, realize heat exchange along thermal current direction and thermal current to be dried, bulky grain in granule materials after oven dry falls into two bulky grains lock wind discharge valves of tower drier lower end in the effect of impact and gravity, then granule materials enters into powder concentrator, part small particles material falls under gravity in small particles material lock wind discharge valve, then a small amount of powdered granule enters into bagroom by dust-precipitator intake stack, finally falls into particulate dust lock wind discharge valve, there is a small amount of lump material in the material that wherein beater is broken up and carry out circular treatment via reentering beater after the discharge of lump material lock wind discharge valve.
Viscosity Industrial Solid Waste pretreatment system of the present utility model, drying hot blast is provided by hot-blast stove, and powder concentrator is used for filtering out small particles material, and bagroom carries out work, for collecting granular material by air-introduced machine and neat stress pipeline.
Further, tower drier dries duct bottom and is provided with a lump material lock wind discharge valve and two large granular materials lock wind discharge valves, when the lump material collected and large granular materials overweight after lump material lock wind discharge valve and large granular materials lock wind discharge valve automatically open respectively, then material is sent in mutually deserved feed bin.
Further, small particles material lock wind discharge valve and granular material lock wind discharge valve is provided with respectively bottom powder concentrator and bagroom, when collect small particles material and particulate dust overweight after, small particles material lock wind discharge valve and granular material lock wind discharge valve are opened automatically, and then material is sent in corresponding feed bin.
Viscosity Industrial Solid Waste pretreatment system of the present utility model, solid waste material is glued after beater breaks up, the surface area of solid waste material and hot air increases, thus accelerate the speed of moisture evaporation, improve drying efficiency, make material feed dryer simultaneously and become easy and smooth, solve material easily sticky wall, the problem that large-block material cannot dry, its system architecture is simple and practical, occupation area of equipment is little, production cost is low, system throughput is large, solid waste is allowed to obtain the chance of secondary utilization very well, reduce cost of material, there is higher practical value and promotional value.
Below be only embody rule example of the present utility model, protection domain of the present utility model is not constituted any limitation.The technical scheme that all employing equivalents or equivalence are replaced and formed, all drops within the utility model rights protection scope.
Claims (5)
1. a viscosity Industrial Solid Waste pretreatment system, is characterized in that: comprise tower drier, hot air duct, hot-blast stove, beater, charging aperture, powder concentrator, dust-precipitator intake stack, bagroom, neat stress pipeline and air-introduced machine; Described tower drier one end is communicated with hot-blast stove by hot air duct, and the other end communicates with powder concentrator; Described tower drier side is positioned at above hot air duct, communicates with charging aperture; Described charging aperture upper end is provided with beater; Described powder concentrator is connected with bagroom by dust-precipitator intake stack; Described bagroom is connected with air-introduced machine by neat stress pipeline.
2. viscosity Industrial Solid Waste pretreatment system according to claim 1, is characterized in that: described tower drier is vertical suspending parallel flow dryer.
3. viscosity Industrial Solid Waste pretreatment system according to claim 1, is characterized in that: described beater is the special beater of viscous material.
4. the viscosity Industrial Solid Waste pretreatment system according to Claims 2 or 3, is characterized in that: described tower drier lower end is provided with lump material lock wind discharge valve, bulky grain lock wind discharge valve and bulky grain lock wind discharge valve successively.
5. viscosity Industrial Solid Waste pretreatment system according to claim 4, is characterized in that: described powder concentrator lower end is provided with granule lock wind discharge valve; Described bagroom lower end is provided with granular material lock wind discharge valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520773989.XU CN205032470U (en) | 2015-10-08 | 2015-10-08 | Viscidity industry solid waste pretreatment systems |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520773989.XU CN205032470U (en) | 2015-10-08 | 2015-10-08 | Viscidity industry solid waste pretreatment systems |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205032470U true CN205032470U (en) | 2016-02-17 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520773989.XU Expired - Fee Related CN205032470U (en) | 2015-10-08 | 2015-10-08 | Viscidity industry solid waste pretreatment systems |
Country Status (1)
| Country | Link |
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| CN (1) | CN205032470U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105149324A (en) * | 2015-10-08 | 2015-12-16 | 盐城市富仕环保科技有限公司 | Viscous industrial solid waste pre-treatment system |
-
2015
- 2015-10-08 CN CN201520773989.XU patent/CN205032470U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105149324A (en) * | 2015-10-08 | 2015-12-16 | 盐城市富仕环保科技有限公司 | Viscous industrial solid waste pre-treatment system |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160217 Termination date: 20171008 |
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| CF01 | Termination of patent right due to non-payment of annual fee |