CN205313487U - Biomass solidified fuel production line - Google Patents
Biomass solidified fuel production line Download PDFInfo
- Publication number
- CN205313487U CN205313487U CN201520974363.5U CN201520974363U CN205313487U CN 205313487 U CN205313487 U CN 205313487U CN 201520974363 U CN201520974363 U CN 201520974363U CN 205313487 U CN205313487 U CN 205313487U
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- CN
- China
- Prior art keywords
- rotary kiln
- water
- communicated
- pipeline
- spray tower
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
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Classifications
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- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
- Y02A50/2351—Atmospheric particulate matter [PM], e.g. carbon smoke microparticles, smog, aerosol particles, dust
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- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
Abstract
The utility model provides a biomass solidified fuel production line, it includes rubbing crusher (1), material hoist (2), combustion chamber (3), air -blower (4), stoving rotary kiln (5), a set of fan cooler (6), conveyer (7), single lead screw ex truding briquetting machine (8), sieving mechanism (9), transfer chain (10), multitube cyclone dust collector (11), a draught fan (12), water spray tower (13), pond (14), water pump (15), spray header (16), shower nozzle (17), whirl board (18), catch water (19), B draught fan (20), active carbon absorption tower (21) and chimney (22). The utility model has the advantages that: this production line cools off raw materials fast drying, the raw materials after will drying through the cooling device of setting on the conveyer through the stoving rotary kiln to accord with the requirement of producing extrusion, the waste material of production can utilize again, has improved resource utilization rate, through setting up the tail -gas clean -up system, has purified the tail gas that produces in the production process, has reduced environmental pollution.
Description
Technical field
The utility model relates to biomass solidified fuel and produces and apparatus field, is specifically related to a kind of biomass solidified fuel production line.
Background technology
Biomass solidified fuel take forest and agricultural biomass as main raw material, through techniques such as section, pulverizing, mixing and extruding, finally make shaping environment-friendly fuel, calorific value height, sufficient combustion, it is the renewable energy source of a kind of clean low-carbon, as boiler oil, its combustion time is long, overheavy firing fire box temperature height, and economical and practical, environmentally safe simultaneously is the high-quality environment-friendly fuel substituting conventional fossil energy.
Existing biomass solidified fuel production line, structural principle is relatively simple, and production efficiency is low, and at the bottom of the product fuel value produced, the waste material produced in production process is not utilized effectively, and the tail gas produced in production process is not effectively addressed.
Practical novel content
In order to the problem that the biomass solidified fuel solved in above-mentioned background technology can produce in production, the utility model provides following technical scheme:
The utility model comprises pulverizer, material elevator, combustion chamber, gas blower, dry rotary kiln, one group of air cooling equipment, transfer roller, single-lead-screw extruding briquetting machine, screening device, transfer limes, multicyclone, A induced draft fan, Water spray tower, pond, water pump, spray header, shower nozzle, eddy flow plate, steam separator, B induced draft fan, activated carbon adsorber and chimney, described material elevator two ends lay respectively at the discharge port of pulverizer and dry the opening for feed place of rotary kiln, the entrance end of described gas blower and exit end are communicated with the exit end of combustion chamber and the blast inlet of oven dry rotary kiln respectively by pipeline, described transfer roller two ends lay respectively at the opening for feed place of discharge port and the single-lead-screw extruding briquetting machine drying rotary kiln, described one group of air cooling equipment is respectively by support installing on a conveyor, described screening device is arranged on the discharge outlet of single-lead-screw extruding briquetting machine, the waste outlet of described screening device is connected with the opening for feed of pulverizer with the fuel input port of combustion chamber by transfer limes, the entrance end of described multicyclone is communicated with the venting port drying rotary kiln by pipeline, the entrance end of described A induced draft fan and exit end are communicated with the exit end of tornado dust collector and the entrance end of Water spray tower by pipeline respectively, described pond is positioned at Water spray tower inner bottom part, described spray header, eddy flow plate and steam separator are arranged in Water spray tower respectively, and spray header and eddy flow plate lay respectively at the lower section of steam separator, described water pump is positioned at Water spray tower side, the water-in of described spray header is communicated with the water outlet of water pump by pipeline, described shower nozzle is arranged on spray header, the entrance end of described B induced draft fan and exit end are communicated with the exit end of Water spray tower and the entrance end of activated carbon adsorber by pipeline respectively, and the entrance end of described chimney is communicated with the exit end of activated carbon adsorber by pipeline.
Preferably, the quantity of spray header and eddy flow plate is at least two, and is interspersed respectively in Water spray tower.
Compared with prior art, the beneficial effects of the utility model are: this production line is by drying rotary kiln to raw material flash baking, by arranging refrigerating unit on a conveyor, the raw material after oven dry is cooled, extruded requirement is produced to meet, the waste material produced is re-used, it is to increase resource utilization, by arranging exhaust gas purification system, purify in production process the tail gas produced, decrease environmental pollution.
Accompanying drawing explanation
Fig. 1 is the utility model structural representation.
Embodiment
As shown in Figure 1, the utility model comprises pulverizer 1, material elevator 2, combustion chamber 3, gas blower 4, dry rotary kiln 5, one group of air cooling equipment 6, transfer roller 7, single-lead-screw extruding briquetting machine 8, screening device 9, transfer limes 10, multicyclone 11, A induced draft fan 12, Water spray tower 13, pond 14, water pump 15, spray header 16, shower nozzle 17, eddy flow plate 18, steam separator 19, B induced draft fan 20, activated carbon adsorber 21 and chimney 22, described material elevator 2 two ends lay respectively at the discharge port of pulverizer 1 and dry the opening for feed place of rotary kiln 5, the entrance end of described gas blower 3 and exit end are communicated with the exit end of combustion chamber 3 and the blast inlet of oven dry rotary kiln 5 respectively by pipeline, described transfer roller 7 two ends lay respectively at the opening for feed place of discharge port and the single-lead-screw extruding briquetting machine 8 drying rotary kiln 5, described one group of air cooling equipment 6 respectively by support installing on transfer roller 7, described screening device 9 is arranged on the discharge outlet of single-lead-screw extruding briquetting machine 8, the waste outlet of described screening device 9 is connected with the opening for feed of pulverizer 1 with the fuel input port of combustion chamber 3 by transfer limes 10, the entrance end of described multicyclone 11 is communicated with the venting port drying rotary kiln 5 by pipeline, the entrance end of described A induced draft fan 12 and exit end are communicated with the exit end of tornado dust collector 11 and the entrance end of Water spray tower 13 by pipeline respectively, described pond 14 is positioned at Water spray tower 13 inner bottom part, described spray header 16, eddy flow plate 18 and steam separator 19 are arranged in Water spray tower 13 respectively, and spray header 16 and eddy flow plate 18 lay respectively at the lower section of steam separator 19, described water pump 15 is positioned at Water spray tower 13 side, the water-in of described spray header 16 is communicated by the water outlet of pipeline with water pump 15, described shower nozzle 17 is arranged on spray header 16, the entrance end of described B induced draft fan 20 and exit end are communicated with the exit end of Water spray tower 13 and the entrance end of activated carbon adsorber 21 by pipeline respectively, and the entrance end of described chimney 22 is communicated by the exit end of pipeline with activated carbon adsorber 21.
Preferably, the quantity of spray header 16 and eddy flow plate 18 is at least two, and is interspersed respectively in Water spray tower 13.
Principle of work: during production, first raw material pulverizer 1 is pulverized, then being put into by material elevator 2 dries in rotary kiln 5, the hot gas that meanwhile combustion chamber 3 produces is sent into through gas blower 4 and is dried in rotary kiln 5, after raw material is dried in oven dry rotary kiln 5, it is discharged to transfer roller 7 from the discharge port drying rotary kiln 5, single-lead-screw extruding briquetting machine 8 is entered after air cooling equipment 6 cools, the solid fuel that single-lead-screw extruding briquetting machine 8 is produced is screened by screening device 9, the product meeting specification requirement directly packs, undesirable waste material drops on transfer limes 10 by screening the waste outlet of device 9, part waste material is transported in combustion chamber 3 through transfer limes 10, the thermal source drying rotary kiln 5 is provided after burning in combustion chamber 3, another part waste material is transported to after pulverizer 1 is pulverized and again puts into production, so circulation.
Tail gas clean-up process: first the tail gas drying rotary kiln 5 generation carry out rough dusting by multicyclone, then enter under the effect of A induced draft fan 12 in Water spray tower 13, cleaning water is transported in spray header 16 by pipeline by water pump 15, and spray from shower nozzle 17, the water smoke that the dust in tail gas in Water spray tower 13 and impurity spray with shower nozzle 17 is combined, drop downwards under gravity, the downward air-flow that eddy flow plate 18 produces, dropping of further accelerating impurity and dust, by arranging multiple spray header and eddy flow plate, dust removing effects can be strengthened, water, impurity and dust finally fall into pond 14, after tail gas after spray pouring processes upwards removes moisture by steam separator 19, activated carbon adsorber 21 is entered under the effect of B induced draft fan 20, it is drained in air by chimney 22 after fine particle in activated carbon adsorber 21 absorption tail gas.
Claims (2)
1. a biomass solidified fuel production line, it is characterized in that it comprises pulverizer (1), material elevator (2), combustion chamber (3), gas blower (4), dry rotary kiln (5), one group of air cooling equipment (6), transfer roller (7), single-lead-screw extruding briquetting machine (8), screening device (9), transfer limes (10), multicyclone (11), A induced draft fan (12), Water spray tower (13), pond (14), water pump (15), spray header (16), shower nozzle (17), eddy flow plate (18), steam separator (19), B induced draft fan (20), activated carbon adsorber (21) and chimney (22), described material elevator (2) two ends lay respectively at the discharge port of pulverizer (1) and dry the opening for feed place of rotary kiln (5), the entrance end of described gas blower (3) and exit end are communicated with the exit end of combustion chamber (3) and the blast inlet of oven dry rotary kiln (5) respectively by pipeline, described transfer roller (7) two ends lay respectively at the opening for feed place of discharge port and the single-lead-screw extruding briquetting machine (8) drying rotary kiln (5), described one group of air cooling equipment (6) respectively by support installing on transfer roller (7), described screening device (9) is arranged on the discharge outlet of single-lead-screw extruding briquetting machine (8), the waste outlet of described screening device (9) is connected with the opening for feed of pulverizer (1) with the fuel input port of combustion chamber (3) by transfer limes (10), the entrance end of described multicyclone (11) is communicated with the venting port drying rotary kiln (5) by pipeline, the entrance end of described A induced draft fan (12) and exit end are communicated with the exit end of tornado dust collector (11) and the entrance end of Water spray tower (13) by pipeline respectively, described pond (14) is positioned at Water spray tower (13) inner bottom part, described spray header (16), eddy flow plate (18) and steam separator (19) are arranged in Water spray tower (13) respectively, and spray header (16) and eddy flow plate (18) lay respectively at the lower section of steam separator (19), described water pump (15) is positioned at Water spray tower (13) side, the water-in of described spray header (16) is communicated by the water outlet of pipeline with water pump (15), described shower nozzle (17) is arranged on spray header (16), the entrance end of described B induced draft fan (20) and exit end are communicated with the exit end of Water spray tower (13) and the entrance end of activated carbon adsorber (21) by pipeline respectively, the entrance end of described chimney (22) is communicated by the exit end of pipeline with activated carbon adsorber (21).
2. a kind of biomass solidified fuel production line as claimed in claim 1, it is characterised in that, the quantity of described spray header (16) and eddy flow plate (18) is at least two, and is interspersed respectively in Water spray tower (13).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201520974363.5U CN205313487U (en) | 2015-12-01 | 2015-12-01 | Biomass solidified fuel production line |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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CN201520974363.5U CN205313487U (en) | 2015-12-01 | 2015-12-01 | Biomass solidified fuel production line |
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CN205313487U true CN205313487U (en) | 2016-06-15 |
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Family Applications (1)
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CN201520974363.5U Expired - Fee Related CN205313487U (en) | 2015-12-01 | 2015-12-01 | Biomass solidified fuel production line |
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CN (1) | CN205313487U (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109028086A (en) * | 2018-07-18 | 2018-12-18 | 宣城恒通机械设备有限公司 | Crush the second level environmental protection incinerator of agricultural solid residue |
CN110184104A (en) * | 2019-05-12 | 2019-08-30 | 哈尔滨迎春科技有限公司 | A kind of biomass ring touches cuber comprehensive utilization process |
-
2015
- 2015-12-01 CN CN201520974363.5U patent/CN205313487U/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109028086A (en) * | 2018-07-18 | 2018-12-18 | 宣城恒通机械设备有限公司 | Crush the second level environmental protection incinerator of agricultural solid residue |
CN110184104A (en) * | 2019-05-12 | 2019-08-30 | 哈尔滨迎春科技有限公司 | A kind of biomass ring touches cuber comprehensive utilization process |
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Legal Events
Date | Code | Title | Description |
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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: 20160615 Termination date: 20181201 |
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CF01 | Termination of patent right due to non-payment of annual fee |