CN101195234A - General wood substance grain processing technique and system - Google Patents
General wood substance grain processing technique and system Download PDFInfo
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- CN101195234A CN101195234A CNA2007100562649A CN200710056264A CN101195234A CN 101195234 A CN101195234 A CN 101195234A CN A2007100562649 A CNA2007100562649 A CN A2007100562649A CN 200710056264 A CN200710056264 A CN 200710056264A CN 101195234 A CN101195234 A CN 101195234A
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Abstract
The invention discloses a process of general-purpose wood particles, which employs remains of tending and cutting of forest and wood-curing waste as materials which are processed into wood chippings and crashed into wood particles. Crashed wood particles are screened, and wood particles with qualified size are passed to next process and wood particles with unqualified size are crashed again. Heat produced in forming process is used to vaporize contained water to soften the powder materials, and then the powder materials are compressed into particles under the effect of extrusion force. The formed particles which have high temperature and include a small amount of crushed aggregates must be cooled and screened. Screened crushed aggregates returns to the particle processing and forming process and the finished products of particles enters the final package process. Compared with prior art, the energetic consumption of specific yield of the invention can be remarkably reduced, and gross investment can be greatly decreased. The invention discloses a process for producing wood particles, which is on the premise that products quality is met, changes the order of processing technique, reduces gross investment of device, decreases energetic consumption of specific yield, and has low manufacture cost and simple process.
Description
Technical field:
The present invention discloses a kind of general wood substance grain processing technique, and the production system that adapts with it also is provided simultaneously, is applicable to that the wood substance grain moulding of unlike material in the biomass energy source domain is produced, and belongs to wood substance grain fuel forming processing technique field.
Background technology
At present, because the minimizing of fossil energy, China also more and more payes attention to the utilization of reproducible biomass energy, domestic some research unit carried out relevant research, some achievements have also been obtained, for example: " a kind of environmental protection wood substance grain fuel and production method thereof " (patent No.: ZL200410046987.7) described patented technology, its production technology is in proper order:
Section → drying → pulverizing → pelletizing forming → cooling, screening → packing
Because the common moisture of forestry waste is higher, adopt general hammer crusher to pulverize raw material, pulverizing process must be after drying process, otherwise the not enough granulation process demand of pulverizer output, and pulverizing process closely is connected with granulation process, require could satisfy the dedusting requirement in granulation workshop with expensive pulse dust removal system, so the energy consumption height of pulverizing process; Output descends, energy consumption increases severely if the granularity of section can make less than 10mm, need add the large slice granularity for just addressing this problem, drying process just can not be selected the pneumatic conveying drying system of low investment, low energy consumption for use like this, and must adopt expensive roller drying system, the investment of drying process and energy consumption increase much again, cause production cost still higher, cause it to apply and be under some influence.
Summary of the invention
The present invention discloses a kind of general wood substance grain processing technique, is common to multiple unlike material and contains the grain forming production and processing of the higher wood material of moisture.
The present invention also provides a kind of general purpose type wood substance grain production system, is applicable to above-mentioned production technology.
Wood material involved in the present invention is meant forest harvesting or fosters residue (as Mao Chai or brush wood) or wood-curing waste (as sawdust, wood shavings, slab etc.).
Technical solution of the present invention is as follows: at first, above-mentioned wood material cut into slices become wooden chipping, meeting granulates requires the wood chip of granularity through being crushed into, the material screening machine sieves the wood chip (perhaps sawdust) after pulverizing, the wood chip that granularity is qualified enters next procedure, the underproof sieve leakage of granularity is returned pulverizer and is pulverized, pneumatic drier carries out drying to the qualified wood chip of granularity, after being dried to certain moisture, carry out pelletizing forming, do not add any additives during moulding, utilize the heat that produces in the forming process that contained humidity is vaporized to soften powder, under the extruding force effect, make powder be compressed into particle again, particle temperature after the moulding is higher, contain a small amount of particle, must cool off and sieve, the particle that screening is come out returns the pelletizing forming operation, and finished particle then enters last packaging process.Product quality reaches wood substance grain standards such as Sweden, Germany.
Technological process is as follows:
Section → pulverizing → material screening → mixing → drying → pelletizing forming → cooling → screening → packing
Concrete production stage is as follows:
A, slicing process are wood material to be sent in the slicer shred, and the wooden granularity of chipping after its chopping is 15～20mm, and moisture is 40～50%, and after storing up air dry, moisture reduces to 25～35%;
B, pulverizing process are that be ground into major part (about 70%) granularity to chipping be that 3～5mm, moisture are 25～35% wood chip;
C, material screening operation are to utilize reciprocating gird or roller screen will pulverize that contained a small amount of super particle size material comes out through screening machine (sieve aperture Φ 5mm～Φ 6mm) screening in back wood chip (perhaps sawdust), granularity is that the qualified wood chip of 3～4mm enters next procedure, and the sieve of super particle size leaks and returns B (pulverizing process) by belt conveyor;
D, mixed processes are that various different types of raw materials are mixed, and make the quality balance unanimity of shaped granule, and fashionable of every batch mixing is 1～3 minute;
E, drying process are the wood chip behind the material screening to be sent into carry out drying in the pneumatic drier, it is 20～25m/s that pneumatic drier is responsible for wind speed, be no less than for 5 seconds drying time, the charging aperture hot blast temperature is regulated with charging moisture and charging rate difference, its baking temperature is 120 ℃～220 ℃, and making discharging moisture is 11%～18% to get final product;
F, pelletizing forming operation are dried wood chip to be sent in the wood substance grain make-up machine be pressed, and are pressed into the wood substance grain that diameter is 6mm or 8mm, and wood substance grain length is 1～5 times of diameter, and moisture is below 8%;
G, refrigerating work procedure are the wood substance grain behind the pelletizing forming to be sent into cool off 20～30 minutes in the cooler, and the particle cooling is not less than 60 ℃, and the particle rate is not more than 2%;
H, screening operation are cooled wood substance grain to be sent in the screening machine sieve, and screen rate is not less than 98%, and the particle after the screening returns F (pelletizing forming operation);
I, packaging process be with qualified wood substance grain send into carry out in the packing machine quantitative package wood substance grain fuel finished product.
In the existing actual production, produce 1.8～2.0 tons wood substance grain production line in the time of one, the power of the broken operation of fine powder of original technology is 13.5 ten thousand yuan of 70kW, costs, and the power of dry (roller drying) operation is 650,000 yuan of 90kW, costs; And adopt technology of the present invention, and with output wood substance grain production line, the broken operation cancellation of fine powder, coarse crushing operation in road increases by 10,000 yuan of power 15kW, costs before generation, and then pulverizing process reduces 12.5 ten thousand yuan of power 55kW, costs; Dry (pneumatic conveying drying) operation is 230,000 yuan of 55kW, costs, and then drying process reduces 420,000 yuan of power 35kW, costs; A whole set of production line general power reduces 90kW, specific yield energy consumption minimizing 45kWh/t, total cost reduces 54.5 ten thousand yuan.
Good effect of the present invention is: more original technology specific yield energy consumption obviously descends, and gross investment also has bigger reduction.Satisfying under the product quality premise, changing the simple and direct wood substance grain processing technique technology of low production cost, technology of production technology order, the gross investment of minimizing equipment, minimizing specific yield energy consumption.
Description of drawings:
Fig. 1 is a process flow diagram of the present invention;
Fig. 2 is general purpose type wood substance grain production system figure of the present invention.
1 mao of bavin; brush wood; raw materials such as slab are 2. chipped; shavings raw material, 3. sawdust raw material; 4. slicer, 5. pulverizer, 6. material screening machine; 7. discharging Sa Kelong 8. pulverizes the discharging Blowing stopper, and 9. sieve leaks; 10. sack cleaner, 11. mixers, 12. dry material loading flat-bottom bins; 13. hot-blast stove, 14. dry material loading Blowing stoppers, 15. pneumatic driers; 16. dry discharging Sa Kelong, 17. dry discharging Blowing stoppers, 18. dry discharging flat-bottom bins; 19. drag conveyor, 20. raw material elevators, 21. pipe magnetic separators; 22. the raw material conveying worm, 23. storehouses to be granulated, 24. granulators; 25. the particle drag conveyor, 26. hot particle elevators, 27. coolers; 28. screening machine, 29. particle conveying worms, 30. cooling and dedusting Sa Kelong; 31. cooling blower; 32. the finished particle elevator, 33. finished bin, 34. quantitative package machines.
→ filled arrows is represented grain flow
The specific embodiment
For the ease of understanding the present invention, especially exemplified by following examples.Its effect is understood that it is to explaination of the present invention but not to any type of restriction of the present invention.
According among the figure shown in 1, A, slicing process are Mao Chai or brush wood etc. to be sent into as raw material shred in the slicer, and the wooden granularity of chipping after its chopping is 15～20mm, and moisture is 40～50%, and after storing up air dry, moisture reduces to 25～35%;
B, pulverizing process are that be ground into major part (about 70%) granularity to chipping be that 3～5mm, moisture are 25～35% wood chip;
C, material screening operation are to utilize reciprocating gird or roller screen will pulverize that contained a small amount of super particle size material comes out through screening machine (sieve aperture Φ 5mm～Φ 6mm) screening in back wood chip (perhaps sawdust), granularity is that the qualified wood chip of 3～4mm enters next procedure, and the sieve of super particle size leaks and returns B (pulverizing process) by belt conveyor;
D, mixed processes are that various different types of raw materials are mixed, and make the quality balance unanimity of shaped granule, and fashionable of every batch mixing is 1～3 minute;
E, drying process are the wood chip behind the material screening to be sent into carry out drying in the pneumatic drier, it is 20～25m/s that pneumatic drier is responsible for wind speed, be no less than for 5 seconds drying time, the charging aperture hot blast temperature is regulated with charging moisture and charging rate difference, its baking temperature is 120 ℃～220 ℃, and making discharging moisture is 11%～18% to get final product;
F, pelletizing forming operation are dried wood chip to be sent in the wood substance grain make-up machine be pressed, and are pressed into the wood substance grain that diameter is 6mm or 8mm, and wood substance grain length is 1～5 times of diameter, and moisture is below 8%;
G, refrigerating work procedure are the wood substance grain behind the pelletizing forming to be sent into cool off 20～30 minutes in the cooler, and the particle cooling is not less than 60 ℃, and the particle rate is not more than 2%;
H, screening operation are cooled wood substance grain to be sent in the screening machine sieve, and screen rate is not less than 98%, and the particle after the screening returns F (pelletizing forming operation);
I, packaging process are qualified wood substance grain to be sent into carry out quantitative package in the packing machine.
Referring to Fig. 2, slicer 4 of the present invention, pulverizer 5, discharging Sa Kelong 7, pulverize discharging Blowing stopper 8, material screening machine 6, mixer 11, dry material loading flat-bottom bin 12, hot-blast stove 13, dry material loading Blowing stopper 14, pneumatic drier 15, dry discharging Sa Kelong 16, dry discharging Blowing stopper 17, dry discharging flat-bottom bin 18, drag conveyor 19, raw material elevator 20, pipe magnetic separator 21, raw material conveying worm 22, the storehouse 23 of waiting to granulate, granulator 24, particle drag conveyor 25, hot particle elevator 26, cooler 27, screening machine 28, particle conveying worm 29, finished particle elevator 32, finished bin 33, quantitative package machine 34 is linked in sequence and constitutes the material work flow;
The big material screen in another road of material screening machine 6 leaks the 9 charging apertures formation aniseed that connect pulverizer 5 pulverizes the loop again;
The particle of screening machine 28 constitutes particle by particle conveying worm 29 with raw material elevator 20 and reclaims the loop;
Discharging Sa Kelong 7 air outlets are connected to sack cleaner 10;
Cooling blower 31 air inlets connect cooling and dedusting Sa Kelong 30 air outlets.
Operation operation method and parameter
In Fig. 2, according to three kinds of different wood materials: hair bavin, brush wood, slab raw material 1, chip, shavings raw material 2, sawdust raw material 3, send into from the difference inlet respectively: hair bavin, brush wood, slab raw material 1 are through slicer 4 sections, and the granularity of chipping after the section is controlled at 15～20mm; For chip, shavings raw material 2, send into pulverizer 5 and pulverize, pulverize back raw material granularity 70% and arrive 3～5mm; For sawdust raw material 3, directly send into material screening machine 6 and screen out the aniseed that granularity exceeds standard, the big material screen leakage 9 that screens out is out returned pulverizer 5 and is pulverized, screening once more, the aniseed that exceeds standard returns pulverizer 5 again and pulverizes once more, so repeatedly, till screening back raw material all is to meet the wood chip of granularity requirements.
Screening back wood chip is sent into mixer 11, and different types of wood chip is mixed, and fashionable of every batch mixing is 1～3 minute.
Mix the back wood chip and enter dry material loading flat-bottom bin 12; drying material loading Blowing stopper 14 adds pneumatic drier 15 and carries out drying, delivers to granulator 24 by dry discharging Sa Kelong 16, dry discharging Blowing stopper 17, dry discharging flat-bottom bin 18, drag conveyor 19, raw material elevator 20, pipe magnetic separator 21, raw material conveying worm 22, the storehouse 23 of waiting to granulate.It is 20～25m/s that pneumatic drier 15 is responsible for wind speed, is no less than for 5 seconds drying time.Pneumatic drier 15 charging aperture hot blast temperatures are regulated with wood chip moisture and charging rate difference, hot-blast stove 13 outlet temperatures are 150 ℃～260 ℃, pneumatic drier 15 inlet temperatures are that 120 ℃～220 ℃, outlet temperature are 50 ℃～130 ℃, and making discharging wood chip moisture is 11%～18% to get final product.
Particle behind the pelletizing forming needs cooling and shaping, send into cooler 27 by particle drag conveyor 25, hot particle elevator 26, cooling air is provided through cooling and dedusting Sa Kelong 30 by cooling blower 31, and for the granulation system of output 1.8～2t/h, cooling air quantity is not less than 6500m
3/ h, the outlet caliber is not less than 500mm, negative blast is not less than 2600Pa, particle bed of material in cooling procedure requires to keep smooth, thickness of feed layer is controlled by level detector, the bed of material is kept between the bound, and general thickness of feed layer is 0.5～0.6m, to guarantee cooling effect, usually cooling is 20～30 minutes, and the particle cooling is not less than 60 ℃.
Enter screening machine 28 after the particle cooling, a small amount of bull screen in the cooled wood substance grain is removed, screen rate is not less than 98%, and the particle after the screening returns raw material elevator 20 through particle conveying worm 29 and reclaims, and mixes in the wood chip and granulates once more.The qualified particle in screening back is sent into finished bin 33 through finished particle elevator 32.Finished bin 33 lower ends connect quantitative package machine 34 inlets, and qualified particle is by quantitative package machine 34 packing back warehouse-ins.
Claims (2)
1. a general wood substance grain processing technique mainly comprises the steps:
A, slicing process: wood material sent in the slicer shred, the wooden granularity of chipping after its chopping is 15～20mm, and moisture is 40～50%, and after storing up air dry, moisture reduces to 25～35%;
B, pulverizing process: being ground into granularity to chipping is that 3～5mm, moisture are 25～35% wood chip;
C, material screening operation: to pulverizing super particle size material screen branch in back wood chip or the sawdust, granularity is that the qualified wood chip of 3～4mm enters next procedure, and the sieve of super particle size leaks and returns step B;
D, mixed processes: various different types of raw materials are mixed, make the quality balance unanimity of shaped granule, fashionable of every batch mixing is 1～3 minute;
E, drying process: the wood chip behind the material screening sent into carry out drying in the pneumatic drier, it is 20～25m/s that pneumatic drier is responsible for wind speed, be no less than for 5 seconds drying time, the charging aperture hot blast temperature is regulated with charging moisture and charging rate difference, its baking temperature is 120 ℃～220 ℃, and making discharging moisture is 11%～18% to get final product;
F, pelletizing forming operation: dried wood chip sent in the wood substance grain make-up machine be pressed, be pressed into the wood substance grain that diameter is 6mm～8mm, wood substance grain length is 1～5 times of diameter, and moisture is below 8%;
G, refrigerating work procedure: the wood substance grain behind the pelletizing forming sent into cool off 20～30 minutes in the cooler, the particle cooling is not less than 60 ℃, and the particle rate is not more than 2%;
H, screening operation: cooled wood substance grain sent in the screening machine sieve, screen rate is not less than 98%, and the particle after the screening returns step F;
I, packaging process: with qualified wood substance grain send into carry out in the packing machine quantitative package wood substance grain fuel finished product.
2. a general purpose type wood substance grain production system is characterized in that: slicer, pulverizer, discharging Sa Kelong, pulverize the discharging Blowing stopper, the material screening machine, mixer, dry material loading flat-bottom bin, hot-blast stove, dry material loading Blowing stopper, pneumatic drier, dry discharging Sa Kelong, dry discharging Blowing stopper, dry discharging flat-bottom bin, drag conveyor, the raw material elevator, pipe magnetic separator, the raw material conveying worm, storehouse to be granulated, granulator, the particle drag conveyor, hot particle elevator, cooler, screening machine, the particle conveying worm, the finished particle elevator, finished bin, quantitative package machine is linked in sequence and constitutes the material work flow;
The big material screen in another road of material screening machine is missed the charging aperture formation aniseed of pulverizer and is pulverized the loop again;
The particle of screening machine constitutes particle by particle conveying worm and raw material elevator and reclaims the loop;
The air outlet of discharging Sa Kelong is connected to sack cleaner;
The air outlet of cooler connects the air inlet of cooling and dedusting Sa Kelong;
The air inlet of cooling blower connects the air outlet of cooling and dedusting Sa Kelong.
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| CN102228198A (en) * | 2011-07-02 | 2011-11-02 | 广东一家人食品有限公司 | Rice noodle production system and method |
| CN102839030A (en) * | 2012-09-17 | 2012-12-26 | 江西省高安市东盛环保生物科技发展有限公司 | Novel bio-particle fuel and preparation method |
| CN104232200A (en) * | 2013-06-18 | 2014-12-24 | 海南福佳能源开发有限公司 | Method for continuously producing wood granular fuel |
| CN104293405A (en) * | 2014-06-24 | 2015-01-21 | 连云港恒昌环境资源开发有限公司 | Device dispersion production method of biomass particles |
| CN105413836A (en) * | 2015-11-24 | 2016-03-23 | 洛阳开拓新能源开发有限公司 | Biomass fuel production system |
| CN106912678A (en) * | 2017-03-07 | 2017-07-04 | 山东金格瑞机械有限公司 | A kind of intelligent feed granulating production technology |
| CN107267248A (en) * | 2017-08-15 | 2017-10-20 | 建水县千原木业有限公司 | A kind of biomass molding fuel tinuous production |
| CN107745430A (en) * | 2016-12-28 | 2018-03-02 | 福建省沙县鸿源安生物科技有限公司 | A kind of mao bamboon raw material prepares the production line of bamboo powder |
| CN111113608A (en) * | 2020-01-01 | 2020-05-08 | 白国动 | Forestry cleans thing processing apparatus |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN102228198A (en) * | 2011-07-02 | 2011-11-02 | 广东一家人食品有限公司 | Rice noodle production system and method |
| CN102228198B (en) * | 2011-07-02 | 2013-07-24 | 广东一家人食品有限公司 | Rice noodle production system and method |
| CN102839030A (en) * | 2012-09-17 | 2012-12-26 | 江西省高安市东盛环保生物科技发展有限公司 | Novel bio-particle fuel and preparation method |
| CN104232200A (en) * | 2013-06-18 | 2014-12-24 | 海南福佳能源开发有限公司 | Method for continuously producing wood granular fuel |
| CN104293405B (en) * | 2014-06-24 | 2017-03-01 | 连云港恒昌环境资源开发有限公司 | The equipment decentralized manufacture method of biological particles |
| CN104293405A (en) * | 2014-06-24 | 2015-01-21 | 连云港恒昌环境资源开发有限公司 | Device dispersion production method of biomass particles |
| CN105413836A (en) * | 2015-11-24 | 2016-03-23 | 洛阳开拓新能源开发有限公司 | Biomass fuel production system |
| CN105413836B (en) * | 2015-11-24 | 2018-09-28 | 广东粤电湛江生物质发电有限公司 | Biomass fuel production system |
| CN107745430A (en) * | 2016-12-28 | 2018-03-02 | 福建省沙县鸿源安生物科技有限公司 | A kind of mao bamboon raw material prepares the production line of bamboo powder |
| CN106912678A (en) * | 2017-03-07 | 2017-07-04 | 山东金格瑞机械有限公司 | A kind of intelligent feed granulating production technology |
| CN107267248A (en) * | 2017-08-15 | 2017-10-20 | 建水县千原木业有限公司 | A kind of biomass molding fuel tinuous production |
| CN107267248B (en) * | 2017-08-15 | 2023-05-16 | 建水县千原木业有限公司 | Biomass briquette fuel continuous production line |
| CN111113608A (en) * | 2020-01-01 | 2020-05-08 | 白国动 | Forestry cleans thing processing apparatus |
| CN112254503A (en) * | 2020-10-16 | 2021-01-22 | 安徽沃园生物科技有限公司 | Rapid cooling device used after organic fertilizer granulation by breeding waste |
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