CN201999910U - Biomass rod-shaped granule preparation system - Google Patents
Biomass rod-shaped granule preparation system Download PDFInfo
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- CN201999910U CN201999910U CN2011200464506U CN201120046450U CN201999910U CN 201999910 U CN201999910 U CN 201999910U CN 2011200464506 U CN2011200464506 U CN 2011200464506U CN 201120046450 U CN201120046450 U CN 201120046450U CN 201999910 U CN201999910 U CN 201999910U
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- biomass
- preparation system
- granules
- biomass material
- dust collector
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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
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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
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
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- Processing Of Solid Wastes (AREA)
- Solid Fuels And Fuel-Associated Substances (AREA)
Abstract
The utility model relates to a biomass rod-shaped granule preparation system. The system comprises a conveying device, a scalping machine, a drying system, a storage bin, a granulator, a cooling device and a vibration separation screen, wherein the conveying device is used for conveying biomass materials or fuels; the scalping machine is used for screening and removing larger biomass materials and impurities; the drying system is used for drying the biomass materials; the storage bin is used for storing the biomass materials, the fuels or molded granules; the granulator is used for compressing the biomass materials to form biomass granules; the cooling device is used for cooling the biomass granules; and the vibration separation screen is used for screening biomass molded granules according to sizes. In the preparation system, agriculture and forestry wastes (such as straws, bagasse, rice chaff, barks, branches and saw dust) are used as biomass raw materials, are subjected to processes such as grinding, extrusion, drying and the like and are prepared into granules or rod-shaped granules through special molding equipment; and the granules have the energy density which is about ten times that of unprocessed materials, are convenient to transport and store and have high combustion efficiency.
Description
Technical field
The utility model belongs to the shaped fuel preparation system, specifically relates to a kind of preparation biomass rodlike particulate system.
Background technology
Along with the continuous development of world economy, the energy and environmental problem become increasingly conspicuous.The human main energy sources of using at present has 3 kinds of oil, Sweet natural gas and coals.According to the International Energy Agency statistics, these 3 kinds of energy have only respectively about 35 years, 50 years and 240 years for the time limit of human exploitation on the earth.Fossil resources such as coal, oil exhaust the power supply constant tension day by day on the one hand; On the other hand, the excessive use of fossil resource has caused serious environmental problem day by day.Therefore, develop and seek new substitute energy and become the key subjects that human social must be solved in the new millennium.
Biomass energy is the sun power that is stored in by the photosynthesis of plant and sun power in the plant.According to estimates, the annual energy of storing of plant is equivalent to 10 times that world's main fuel consumes, and is less than 1% of its total amount as the utilization of the energy.Characteristics such as biomass material is because of having the volatility height, and carbon is active high, and N, S content are low, and ash content is low are a kind of fine fuel.By the biomass energy switch technology, can utilize this reproducible clean biomass energy efficiently, substitute fuel such as coal, oil and natural gas.
The preparation system of prior art, a kind of biomass fuel and preparation system and application as China's No. 200710063736.3 patent application disclosure, a kind of method of utilizing agricultural wastes to prepare shaped fuel that No. 200810054563.3 patent application of China discloses all is unfavorable for producing in enormous quantities a kind of shaped fuel of being convenient to preserve, transporting and using.
The utility model content
In order to solve the problem that prior art exists, the utility model provides a kind of shaped fuel preparation system of preserving, transport and using be convenient to.
In order to realize above purpose, the technical solution of the utility model is as follows: a kind of biomass rodlike particulate preparation system, and e Foerderanlage is used to carry biomass material or fuel; Receiving sieve is used for screening and rejects big part biomass material and impurity; Drying system, be used for biomass material is dried processing, it comprises pay-off, heating plant, drying unit and cyclonic separator, the outlet of described cyclonic separator connects pulse dust collector, the following outlet of pulse dust collector is provided with worm conveyor, pulse dust collector falls into worm conveyor with the biomass material of collecting when removing dust, be delivered to the equipment that next preparation section adopts by worm conveyor again; Feed bin is used to store biomass material, fuel or shaped granule; Nodulizer, the compacting biomass material becomes biological particles; Refrigerating unit cools off biological particles; Vibration separation screen carries out the size screening to biological substance shaped granule.
Further, described pulse dust collector is the two sack cleaners of secondary, comprises tornado dust collector and two cloth bag pulse dust collector.
Described heating plant is the hotblast stove of two hearth-type structures.
Described heating plant is the hotblast stove of Automatic grate formula structure.
Also comprise the pulverizer that is used to pulverize agriculture and forestry organic waste material.
Comprise that also at least one pipe magnetic separator is used for the absorption iron contamination.
Described drying unit is a roller dryer, and the length of described roller dryer is at 10～16 meters, and rotating speed is at 9～13 rev/mins, and dryer charging place temperature is at 350～550 degree, and discharging place temperature 65～90 is spent.
The speed of the ring mould that described nodulizer adopts is at 3～9 meter per seconds, and the internal diameter of the external diameter of the pressure roller of employing and described ring mould is 0.3～0.48, and described ring mould percentage of open area is 25～35%.
Described e Foerderanlage comprises the conveying elephant trunk, and it is made up of U type groove, groove lid and sheet glass, and the inner bottom surface of described U type groove is laid one deck sheet glass.
The utility model biomass rodlike particulate preparation system; with agriculture and forestry organic waste material (as straw, bagasse, rice chaff, bark, branch, sawdust) as biomass material; through technologies such as pulverizing, extruding, oven dry; be suppressed into particle or bar-shaped through shaping equipment; its energy density is processed preceding about big ten times; be convenient to transportation and store the efficiency of combustion height.
Description of drawings
Fig. 1 is that the structure of the utility model rod-shpaed particle preparation system is formed synoptic diagram;
Fig. 2 is that the structure of drying system is formed synoptic diagram;
Fig. 3 is the structural representation of e Foerderanlage;
Fig. 4 is the cross section cut-away view of chute.
Embodiment
As shown in Figure 1, the utility model is a kind of biomass rodlike particulate preparation system, is made up of e Foerderanlage, receiving sieve, drying system, feed bin, refrigerating unit, vibration separation screen, pulverizer, pipe magnetic separator.
1, e Foerderanlage is used to carry biomass material or fuel, and scraper plate machine 2 or 5 or 8 or 11 are arranged, auger 4 or 15, chapelet 10, rotary conveyor 19, bucket type conveyor 14 etc.Between dog-house 1 and receiving sieve 3, arrange scraper plate machine 2; between receiving sieve 3 and drying system, arrange auger 4 and scraper plate machine 5; layout scraper plate machine 8 between dog-house 7 and pipe magnetic separator 9; between chapelet 10 and feed bin 12, arrange scraper plate machine 11; layout rotary conveyor 19 below nodulizer 13; at the arranged in front bucket type conveyor 14 of cooling tower 16, arrange rotary conveyor 18 and auger 15 in the back of vibration separation screen 17.
2, receiving sieve 3, are used for screening and reject big part biomass material and impurity;
3, drying system 6, as shown in Figure 2, are used for biomass material is dried processing, and it comprises pay-off, heating plant, drying unit and cyclonic separator.The outlet of cyclonic separator 23 connects pulse dust collector 20, and pulse dust collector is the two sack cleaners of two-stage, promptly is to be made of two cloth bag pulse dust collector series connection; Heating plant is the hotblast stove 22 of the Automatic grate formula structure of two hearth-types; Drying unit is a roller dryer 21,10～16 meters of its length, and rotating speed is at 9～13 rev/mins, and dryer charging place temperature is at 350～550 degree, and discharging place temperature 65～90 is spent.The following outlet of pulse dust collector is provided with worm conveyor 24.Pulse dust collector falls into worm conveyor with the biomass material of collecting when removing dust, be delivered to the equipment that next preparation section adopts by worm conveyor again.
4, feed bin is used to store biomass material, fuel or shaped granule, as the granulation feed bin 12 before the nodulizer.
5, nodulizer 13; the compacting biomass material becomes biological particles, has four and is arranged in parallel, and the speed of the ring mould that each nodulizer adopts is at 3～9 meter per seconds; the external diameter of the pressure roller that adopts and the internal diameter of described ring mould are 0.3～0.48, and described ring mould percentage of open area is 25～35%.The particle specification that nodulizer is made is: diameter 5～60mm, length is 2～6 times of diameter.
6, refrigerating unit cools off biological particles, generally is counterflow cooling tower 16;
7, vibration separation screen 17, and biological substance shaped granule is carried out the size screening.
8, pulverizer is used to pulverize agriculture and forestry organic waste material, can be arranged at the dog-house front.
9, pipe magnetic separator 9, are used for the absorption iron contamination, and it is positioned at the front of chapelet.
As shown in Figure 3, e Foerderanlage between chapelet 10 of the present utility model and the granulation feed bin 12 can adopt elephant trunk 25, and chapelet is higher than feed bin, produces difference of altitude, biomass fuel under self-gravity action, is transported to feed bin from chapelet along elephant trunk.As shown in Figure 4, elephant trunk 25 is made up of U type groove 27, groove lid 26 and sheet glass 28.Sheet glass is layed in the inner bottom surface of U type groove, available screw fixings.Groove is placed on the U type groove.
Claims (9)
1. biomass rodlike particulate preparation system is characterized in that comprising:
E Foerderanlage is used to carry biomass material or fuel;
Receiving sieve is used for screening and rejects big part biomass material and impurity;
Drying system, be used for biomass material is dried processing, it comprises pay-off, heating plant, drying unit and cyclonic separator, the outlet of described cyclonic separator connects pulse dust collector, the following outlet of pulse dust collector is provided with worm conveyor, pulse dust collector falls into worm conveyor with the biomass material of collecting when removing dust, be delivered to the equipment that next preparation section adopts by worm conveyor again;
Feed bin is used to store biomass material, fuel or shaped granule;
Nodulizer, the compacting biomass material becomes biological particles;
Refrigerating unit cools off biological particles;
Vibration separation screen carries out the size screening to biological substance shaped granule.
2. preparation system according to claim 1 is characterized in that, described fly-ash separator is the two sack cleaners of secondary, comprises tornado dust collector and two cloth bag pulse dust collector.
3. preparation system according to claim 1 is characterized in that, described heating plant is the hotblast stove of two hearth-type structures.
4. preparation system according to claim 1 is characterized in that, described heating plant is the hotblast stove of Automatic grate formula structure.
5. preparation system according to claim 1 is characterized in that, also comprises the pulverizer that is used to pulverize agriculture and forestry organic waste material.
6. preparation system according to claim 1 is characterized in that, comprises that also at least one pipe magnetic separator is used for the absorption iron contamination.
7. preparation system according to claim 1 is characterized in that, described drying unit is a roller dryer, the length of described roller dryer is at 10～16 meters, rotating speed is at 9～13 rev/mins, and dryer charging place temperature is at 350～550 degree, and discharging place temperature 65～90 is spent.
8. preparation system according to claim 1 is characterized in that, the speed of the ring mould that described nodulizer adopts is at 3～9 meter per seconds, and the internal diameter of the external diameter of the pressure roller of employing and described ring mould is 0.3～0.48, and described ring mould percentage of open area is 25～35%.
9. preparation system according to claim 1 is characterized in that described e Foerderanlage comprises the conveying elephant trunk, and it is made up of U type groove, groove lid and sheet glass, and the inner bottom surface of described U type groove is laid one deck sheet glass.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011200464506U CN201999910U (en) | 2011-02-22 | 2011-02-22 | Biomass rod-shaped granule preparation system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011200464506U CN201999910U (en) | 2011-02-22 | 2011-02-22 | Biomass rod-shaped granule preparation system |
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| Publication Number | Publication Date |
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| CN201999910U true CN201999910U (en) | 2011-10-05 |
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| CN2011200464506U Expired - Fee Related CN201999910U (en) | 2011-02-22 | 2011-02-22 | Biomass rod-shaped granule preparation system |
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Cited By (15)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102146308A (en) * | 2011-02-22 | 2011-08-10 | 苏州迪森生物能源有限公司 | System for preparing biomass rod-shaped particles |
| CN102517112A (en) * | 2011-11-30 | 2012-06-27 | 杜金宇 | Automatic molding system for biomass flat-die particle |
| CN102643702A (en) * | 2012-05-04 | 2012-08-22 | 陆海燕 | Cold-state compact forming device of biomass particle fuel |
| CN102660345A (en) * | 2012-05-04 | 2012-09-12 | 陆海燕 | Process for preparing biomass compact solidified fuel |
| CN103305305A (en) * | 2013-06-29 | 2013-09-18 | 许成荫 | Fuel forming method |
| CN103480637A (en) * | 2012-06-12 | 2014-01-01 | 安徽厚源正位环保科技有限公司 | Technical method for processing domestic waste |
| CN103710067A (en) * | 2012-09-28 | 2014-04-09 | 北京奥科瑞丰新能源股份有限公司 | Automatic biomass fuel briquette production technology |
| CN103710068A (en) * | 2012-09-28 | 2014-04-09 | 北京奥科瑞丰新能源股份有限公司 | Automatic biomass fuel briquette production line |
| CN104312653A (en) * | 2014-08-22 | 2015-01-28 | 苏州熙瑞新能源科技有限公司 | Biomass pellet fuel production equipment |
| CN104629781A (en) * | 2013-11-07 | 2015-05-20 | 永胜县益农新能源开发有限公司 | Machine-made charcoal rod-making production system |
| CN105542895A (en) * | 2016-01-28 | 2016-05-04 | 无锡南理工科技发展有限公司 | Biomass fuel processing system |
| CN104312653B (en) * | 2014-08-22 | 2017-01-04 | 苏州熙瑞新能源科技有限公司 | A kind of biomass granule fuel produces equipment |
| CN107878789A (en) * | 2017-09-28 | 2018-04-06 | 江苏福亿自动化设备有限公司 | A kind of screw extruding powder granulating system and prilling |
| CN108085088A (en) * | 2017-12-27 | 2018-05-29 | 郑州紫竹林健康管理有限公司 | A kind of electrolytic aluminium waste Slag treatment compound additive, preparation method and applications |
| CN108211991A (en) * | 2018-03-21 | 2018-06-29 | 庞中化 | A kind of straw biomass particle manufacture assembly line |
-
2011
- 2011-02-22 CN CN2011200464506U patent/CN201999910U/en not_active Expired - Fee Related
Cited By (18)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102146308A (en) * | 2011-02-22 | 2011-08-10 | 苏州迪森生物能源有限公司 | System for preparing biomass rod-shaped particles |
| CN102517112A (en) * | 2011-11-30 | 2012-06-27 | 杜金宇 | Automatic molding system for biomass flat-die particle |
| CN102643702A (en) * | 2012-05-04 | 2012-08-22 | 陆海燕 | Cold-state compact forming device of biomass particle fuel |
| CN102660345A (en) * | 2012-05-04 | 2012-09-12 | 陆海燕 | Process for preparing biomass compact solidified fuel |
| CN103480637B (en) * | 2012-06-12 | 2016-03-02 | 安徽厚源正位环保科技有限公司 | A kind of process processing house refuse |
| CN103480637A (en) * | 2012-06-12 | 2014-01-01 | 安徽厚源正位环保科技有限公司 | Technical method for processing domestic waste |
| CN103710067A (en) * | 2012-09-28 | 2014-04-09 | 北京奥科瑞丰新能源股份有限公司 | Automatic biomass fuel briquette production technology |
| CN103710068A (en) * | 2012-09-28 | 2014-04-09 | 北京奥科瑞丰新能源股份有限公司 | Automatic biomass fuel briquette production line |
| CN103710068B (en) * | 2012-09-28 | 2015-11-11 | 北京奥科瑞丰新能源股份有限公司 | The compact formed automatic production line of biomass fuel |
| CN103305305A (en) * | 2013-06-29 | 2013-09-18 | 许成荫 | Fuel forming method |
| CN104629781A (en) * | 2013-11-07 | 2015-05-20 | 永胜县益农新能源开发有限公司 | Machine-made charcoal rod-making production system |
| CN104312653A (en) * | 2014-08-22 | 2015-01-28 | 苏州熙瑞新能源科技有限公司 | Biomass pellet fuel production equipment |
| CN104312653B (en) * | 2014-08-22 | 2017-01-04 | 苏州熙瑞新能源科技有限公司 | A kind of biomass granule fuel produces equipment |
| CN105542895A (en) * | 2016-01-28 | 2016-05-04 | 无锡南理工科技发展有限公司 | Biomass fuel processing system |
| CN107878789A (en) * | 2017-09-28 | 2018-04-06 | 江苏福亿自动化设备有限公司 | A kind of screw extruding powder granulating system and prilling |
| CN107878789B (en) * | 2017-09-28 | 2019-07-12 | 江苏福亿自动化设备有限公司 | A kind of screw extruding powder granulating system and prilling |
| CN108085088A (en) * | 2017-12-27 | 2018-05-29 | 郑州紫竹林健康管理有限公司 | A kind of electrolytic aluminium waste Slag treatment compound additive, preparation method and applications |
| CN108211991A (en) * | 2018-03-21 | 2018-06-29 | 庞中化 | A kind of straw biomass particle manufacture assembly line |
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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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20111005 Termination date: 20180222 |