CN207646158U - Biomass fuel production system - Google Patents
Biomass fuel production system Download PDFInfo
- Publication number
- CN207646158U CN207646158U CN201721595399.8U CN201721595399U CN207646158U CN 207646158 U CN207646158 U CN 207646158U CN 201721595399 U CN201721595399 U CN 201721595399U CN 207646158 U CN207646158 U CN 207646158U
- Authority
- CN
- China
- Prior art keywords
- connect
- feed bin
- pulverizer
- drying oven
- biomass fuel
- 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
Links
- 239000002028 Biomass Substances 0.000 title claims abstract description 22
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 22
- 239000000446 fuel Substances 0.000 title claims abstract description 21
- 238000001035 drying Methods 0.000 claims abstract description 24
- 238000001816 cooling Methods 0.000 claims abstract description 20
- 229910052500 inorganic mineral Inorganic materials 0.000 claims abstract description 18
- 239000011707 mineral Substances 0.000 claims abstract description 18
- 239000006148 magnetic separator Substances 0.000 claims abstract description 11
- 238000001914 filtration Methods 0.000 claims abstract description 9
- 239000000428 dust Substances 0.000 claims abstract description 8
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 abstract description 16
- 229910052742 iron Inorganic materials 0.000 abstract description 8
- 239000002245 particle Substances 0.000 abstract description 6
- 238000004939 coking Methods 0.000 abstract description 4
- 238000002485 combustion reaction Methods 0.000 abstract description 4
- 238000010924 continuous production Methods 0.000 abstract description 4
- 239000000463 material Substances 0.000 description 9
- 238000005516 engineering process Methods 0.000 description 3
- 230000009286 beneficial effect Effects 0.000 description 2
- 239000003245 coal Substances 0.000 description 2
- 239000008187 granular material Substances 0.000 description 2
- 238000005453 pelletization Methods 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 239000004484 Briquette Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 238000000643 oven drying Methods 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000010977 unit operation Methods 0.000 description 1
- 238000004148 unit process Methods 0.000 description 1
Classifications
-
- 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
Biomass fuel production system, it is related to biomass fuel production facility technical field；Drum sieve feeding port is connect with cylinder screen device; cylinder screen device is connect with pulverizer, drying oven; cyclone dust collectors are connected on pulverizer; pulverizer is connect with drying oven; drying oven is connect by conveying auger with feed bin feeding port; the setting of feed bin feeding port is on temporary feed bin, and temporary feed bin is connect through pipe magnetic separator with granulator, and granulator is connect with cooling tower；The outer casing inner wall of the cylinder screen device is provided with magnet layer, is provided in shell except mineral grain net, except refined filtration net is provided with below mineral grain net, the upper end of shell is provided with clean-up port.Biomass fuel production system described in the utility model, can continuous production, production efficiency is high, and when pretreatment removes larger iron particle and mineral grain, and pulverizer is hardly damaged, and solves the problems such as fuel combustion ash content height, coking, slagging.
Description
Technical field
The utility model is related to biomass fuel production facility technical fields, and in particular to biomass fuel production system.
Background technology
Clean energy resource develops and Global climate change is the common focus of attention of international community, the whole world more than 200 years
Industrialization course in, only less than 1,000,000,000 populations developed country realize modernization, but global resources and ecology be this pair
Heavy cost is gone out, in this context, has all been increased one after another as many countries of representative using America and Europe and biomass energyization is utilized
Attention and input.
To promote the utilization of biomass, department of Chinese Government and scientific research institutions, and international machine by planning of science activities
Structure has successively carried out planning property and perspective research work to the development and utilization of Chinese biomass.And agricultural biomass is for I
The important energy resources in state rural area.Currently, in fuel in China's rural areas consumption structure, what is produced and live is respectively with energy ratio
44% and 56%, coal accounts for 50% or more in producting energy, and in life energy, biomass accounts for 52%, and coal accounts for 34%.China rural area
Energy-consuming is also faced with that commercial energy effective supply is insufficient, energy utilization rate is low, energy base other than there are unreasonable structure
Infrastructure builds the problems such as not perfect, and is based on above-mentioned background, and Biomass Briquette Technologies and industry development are a kind of
Long-term strategic selection.
Existing biomass fuel production system is all unit operation, and process is separated, low production efficiency, and pretreatment is not filled
Point, the problems such as larger iron particle and mineral grain are easily damaged pulverizer, manufactured fuel combustion ash content height, coking, slagging.
Utility model content
The purpose of this utility model is that in view of the drawbacks of the prior art and insufficient, providing one kind can continuous production, pre- place
Reason is abundant, is hardly damaged the biomass fuel production system of pulverizer.
To achieve the above object, the technical solution adopted in the utility model is：It includes drum sieve feeding port, drum sieve dress
It sets, pulverizer, cyclone dust collectors, drying oven, conveying auger, keep in feed bin, feed bin feeding port, pipe magnetic separator, granulator, cooling
Tower；The drum sieve feeding port is connect with cylinder screen device, and cylinder screen device is connect with pulverizer, drying oven, on pulverizer
Cyclone dust collectors are connected with, pulverizer is connect with drying oven, and drying oven is connect by conveying auger with feed bin feeding port, and feed bin is thrown
Material mouth setting is on temporary feed bin, and temporary feed bin is connect through pipe magnetic separator with granulator, and granulator is connect with cooling tower；The circle
The outer casing inner wall of shaft screen device is provided with magnet layer, is provided in shell except mineral grain net, except being set below mineral grain net
It is equipped with refined filtration net, the upper end of shell is provided with clean-up port.
Preferably, the cooling tower is connect with finished product bin.
Preferably, the finished product bin is connect with baling press.
Preferably, being connected with air blower on the drying oven, air blower is connect with conveying auger.
Preferably, being connected with cooling blower on the cooling tower.
When the utility model operates, raw material enter cylinder screen device through drum sieve feeding port, and drum sieve is driven by motor
Rotation, the iron particle for being easily damaged pulverizer are adsorbed by magnet layer, are easily damaged the mineral grain of pulverizer by except mineral grain
Net filtration, rest materials enter refined filtration side on the net, and drying oven is entered after being crushed by pulverizer and is dried, crushing while is removed
Dirt, thinner material enters refined filtration side off the net in cylinder screen device, is directly entered drying oven drying, is delivered to by conveying auger temporary
Feed bin, then remove the iron tramp in dry powder-shaped material and granule materials, then pelletizing forming, cooling through pipe magnetic separator.
With the above structure, what the utility model generated has the beneficial effect that：Biomass fuel described in the utility model
Production system, can continuous production, production efficiency is high, and when pretreatment removes larger iron particle and mineral grain, and pulverizer is not easy
Damage, and solves the problems such as fuel combustion ash content height, coking, slagging, the utility model have simple in structure, setting is reasonable,
The advantages that low manufacture cost.
Description of the drawings
Fig. 1 is the structure chart of the utility model；
Fig. 2 is the structure chart of the utility model cylinder screen device.
Reference sign：
Drum sieve feeding port 1, pulverizer 3, cyclone dust collectors 4, drying oven 5, conveying auger 6, is kept at cylinder screen device 2
Feed bin 7, pipe magnetic separator 9, granulator 10, cooling tower 11, shell 12, magnet layer 13, removes mineral grain net 14, essence at feed bin feeding port 8
Strainer 15, clean-up port 16, finished product bin 17, baling press 18, air blower 19, cooling blower 20, mineral grain 21.
Specific implementation mode
In order to illustrate the embodiment of the utility model or the technical proposal in the existing technology more clearly, below will be to embodiment
Or attached drawing needed to be used in the description of the prior art is briefly described, it should be apparent that, the accompanying drawings in the following description is only
It is some embodiments of the utility model, for those of ordinary skill in the art, before not making the creative labor property
It puts, other drawings may also be obtained based on these drawings.
Referring to such as Fig. 1 --- shown in Fig. 2, present embodiment adopts the following technical scheme that：It feeds intake comprising drum sieve
Mouthful 1, cylinder screen device 2, pulverizer 3, cyclone dust collectors 4, drying oven 5, conveying auger 6, temporary feed bin 7, feed bin feeding port 8,
Pipe magnetic separator 9, granulator 10, cooling tower 11；The drum sieve feeding port 1 is connect with cylinder screen device 2, cylinder screen device 2 with
Pulverizer 3, drying oven 5 connect, and cyclone dust collectors 4 are connected on pulverizer 3, and pulverizer 3 is connect with drying oven 5, and drying oven 5 is logical
It crosses conveying auger 6 to connect with feed bin feeding port 8, feed bin feeding port 8 is arranged on temporary feed bin 7, keeps in feed bin 7 through pipe magnetic separator 9
It is connect with granulator 10, granulator 10 is connect with cooling tower 11；12 inner wall of shell of the cylinder screen device 2 is provided with magnet
Layer 13 is provided with except mineral grain net 14 in shell 12, except the lower section of mineral grain net 14 is provided with refined filtration net 15, shell 12
Upper end is provided with clean-up port 16.
Preferably, the cooling tower 11 is connect with finished product bin 17.
Preferably, the finished product bin 17 is connect with baling press 18.
Preferably, being connected with air blower 19 on the drying oven 5, air blower 19 is connect with conveying auger 6.
Preferably, being connected with cooling blower 20 on the cooling tower 11.
When present embodiment operates, raw material enter cylinder screen device 2 through drum sieve feeding port 1, and drum sieve is by electricity
Machine driving rotation, the iron particle for being easily damaged pulverizer 3 are adsorbed by magnet layer 13, are easily damaged the mineral grain 21 of pulverizer 3
It is filtered except mineral grain net 14, rest materials enter 15 top of refined filtration net, and entering drying oven 5 after being crushed by pulverizer 3 dries
Dry, crushing while, is dusted, and thinner material enters 15 lower section of refined filtration net in cylinder screen device 2, is directly entered the baking of drying oven 5
It is dry, temporary feed bin 7 is delivered to by conveying auger 6, then the iron tramp in dry powder-shaped material and granule materials is removed through pipe magnetic separator 9,
Then pelletizing forming, cooling.
Pulverizer 3, cyclone dust collectors 4, drying oven 5, conveying auger 6 described in present embodiment, temporary feed bin 7,
Feed bin feeding port 8, pipe magnetic separator 9, granulator 10, cooling tower 11 and baling press 18 are all the existing equipments that can be bought in the market,
Therefore, it is not specifically described in this application.
With the above structure, what present embodiment generated has the beneficial effect that：Life described in present embodiment
Biomass fuel production system, can continuous production, production efficiency is high, and when pretreatment removes larger iron particle and mineral grain, powder
Broken machine is hardly damaged, and solves the problems such as fuel combustion ash content height, coking, slagging, and present embodiment has structure letter
Single, setting rationally, low manufacture cost the advantages that.
The advantages of basic principles and main features and the utility model of the utility model have been shown and described above.This
The technical staff of industry is retouched in above embodiments and description it should be appreciated that the present utility model is not limited to the above embodiments
That states only illustrates the principles of the present invention, on the premise of not departing from the spirit and scope of the utility model, the utility model
It will also have various changes and improvements, these various changes and improvements fall within the scope of the claimed invention.This practicality is new
Type is claimed range and is defined by the appending claims and its equivalent thereof.
Claims (5)
1. biomass fuel production system, it is characterised in that：It includes drum sieve feeding port, cylinder screen device, pulverizer, whirlwind
Deduster, drying oven, conveying auger, temporary feed bin, feed bin feeding port, pipe magnetic separator, granulator, cooling tower；The drum sieve
Feeding port is connect with cylinder screen device, and cylinder screen device is connect with pulverizer, drying oven, and cyclone dust removal is connected on pulverizer
Device, pulverizer are connect with drying oven, and drying oven is connect by conveying auger with feed bin feeding port, and the setting of feed bin feeding port is temporary
On feed bin, temporary feed bin is connect through pipe magnetic separator with granulator, and granulator is connect with cooling tower；The shell of the cylinder screen device
Inner wall is provided with magnet layer, is provided in shell except mineral grain net, except being provided with refined filtration net, shell below mineral grain net
Upper end be provided with clean-up port.
2. biomass fuel production system according to claim 1, it is characterised in that：The cooling tower and finished product bin
Connection.
3. biomass fuel production system according to claim 2, it is characterised in that：The finished product bin and baling press
Connection.
4. biomass fuel production system according to claim 1, it is characterised in that：It is connected with drum on the drying oven
Wind turbine, air blower are connect with conveying auger.
5. biomass fuel production system according to claim 1, it is characterised in that：It is connected on the cooling tower cold
But wind turbine.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721595399.8U CN207646158U (en) | 2017-11-25 | 2017-11-25 | Biomass fuel production system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721595399.8U CN207646158U (en) | 2017-11-25 | 2017-11-25 | Biomass fuel production system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207646158U true CN207646158U (en) | 2018-07-24 |
Family
ID=62881037
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721595399.8U Expired - Fee Related CN207646158U (en) | 2017-11-25 | 2017-11-25 | Biomass fuel production system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207646158U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109158200A (en) * | 2018-10-31 | 2019-01-08 | 上海成界制药设备有限公司 | A kind of modified form discharging device |
-
2017
- 2017-11-25 CN CN201721595399.8U patent/CN207646158U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109158200A (en) * | 2018-10-31 | 2019-01-08 | 上海成界制药设备有限公司 | A kind of modified form discharging device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20191217 Address after: 511100 No.1, Xinma Avenue, Matou Industrial Park, Matou Town, Xinfeng County, Shaoguan City, Guangdong Province Patentee after: Shaoneng group xinfengxuneng Biomass Power Generation Co.,Ltd. Address before: 529200 H 3, Jiangdong Industrial Zone, Dajiang Town, Taishan City, Jiangmen, Guangdong. Patentee before: TAISHAN BRANCH COMPANY, GUANGDONG COME PROFIT GREEN ENERGY Co.,Ltd. |
|
| 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: 20180724 |