CN106085544A - A kind of composite biomass fuel and processing technique thereof - Google Patents
A kind of composite biomass fuel and processing technique thereof Download PDFInfo
- Publication number
- CN106085544A CN106085544A CN201610594159.XA CN201610594159A CN106085544A CN 106085544 A CN106085544 A CN 106085544A CN 201610594159 A CN201610594159 A CN 201610594159A CN 106085544 A CN106085544 A CN 106085544A
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- China
- Prior art keywords
- biomass fuel
- parts
- processing technique
- composite biomass
- anthracite
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- 239000000446 fuel Substances 0.000 title claims abstract description 42
- 239000002028 Biomass Substances 0.000 title claims abstract description 36
- 238000000034 method Methods 0.000 title claims abstract description 29
- 239000002131 composite material Substances 0.000 title claims abstract description 25
- 238000012545 processing Methods 0.000 title claims abstract description 19
- 238000002485 combustion reaction Methods 0.000 claims abstract description 22
- RHZUVFJBSILHOK-UHFFFAOYSA-N anthracen-1-ylmethanolate Chemical compound C1=CC=C2C=C3C(C[O-])=CC=CC3=CC2=C1 RHZUVFJBSILHOK-UHFFFAOYSA-N 0.000 claims abstract description 18
- 239000003830 anthracite Substances 0.000 claims abstract description 18
- 238000010298 pulverizing process Methods 0.000 claims abstract description 16
- 239000002671 adjuvant Substances 0.000 claims abstract description 14
- 239000002994 raw material Substances 0.000 claims abstract description 12
- 239000010902 straw Substances 0.000 claims abstract description 11
- 238000007599 discharging Methods 0.000 claims abstract description 10
- 238000002156 mixing Methods 0.000 claims abstract description 10
- 235000013312 flour Nutrition 0.000 claims abstract description 9
- 239000003864 humus Substances 0.000 claims abstract description 9
- 230000008569 process Effects 0.000 claims abstract description 9
- 239000002689 soil Substances 0.000 claims abstract description 9
- 239000002023 wood Substances 0.000 claims abstract description 9
- 238000004519 manufacturing process Methods 0.000 claims abstract description 7
- 238000000465 moulding Methods 0.000 claims abstract description 4
- 239000000463 material Substances 0.000 claims description 26
- 239000002245 particle Substances 0.000 claims description 9
- AMWRITDGCCNYAT-UHFFFAOYSA-L hydroxy(oxo)manganese;manganese Chemical compound [Mn].O[Mn]=O.O[Mn]=O AMWRITDGCCNYAT-UHFFFAOYSA-L 0.000 claims description 6
- VWDWKYIASSYTQR-UHFFFAOYSA-N sodium nitrate Chemical compound [Na+].[O-][N+]([O-])=O VWDWKYIASSYTQR-UHFFFAOYSA-N 0.000 claims description 6
- 238000001035 drying Methods 0.000 claims description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 5
- 238000010438 heat treatment Methods 0.000 claims description 4
- 239000000203 mixture Substances 0.000 claims description 4
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 3
- 238000003556 assay Methods 0.000 claims description 3
- 229910052624 sepiolite Inorganic materials 0.000 claims description 3
- 235000019355 sepiolite Nutrition 0.000 claims description 3
- 235000010344 sodium nitrate Nutrition 0.000 claims description 3
- 239000004317 sodium nitrate Substances 0.000 claims description 3
- 238000012360 testing method Methods 0.000 claims description 3
- 239000003245 coal Substances 0.000 abstract description 3
- 239000002551 biofuel Substances 0.000 abstract description 2
- 238000005457 optimization Methods 0.000 abstract description 2
- 239000008188 pellet Substances 0.000 abstract description 2
- 239000008187 granular material Substances 0.000 abstract 1
- 238000005516 engineering process Methods 0.000 description 3
- 150000001875 compounds Chemical class 0.000 description 2
- 238000013461 design Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 240000007594 Oryza sativa Species 0.000 description 1
- 235000007164 Oryza sativa Nutrition 0.000 description 1
- 239000002154 agricultural waste Substances 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000010903 husk Substances 0.000 description 1
- 238000011031 large-scale manufacturing process Methods 0.000 description 1
- 239000003345 natural gas Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000001172 regenerating effect Effects 0.000 description 1
- 235000009566 rice Nutrition 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L5/00—Solid fuels
- C10L5/40—Solid fuels essentially based on materials of non-mineral origin
- C10L5/44—Solid fuels essentially based on materials of non-mineral origin on vegetable substances
- C10L5/445—Agricultural waste, e.g. corn crops, grass clippings, nut shells or oil pressing residues
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L5/00—Solid fuels
- C10L5/02—Solid fuels such as briquettes consisting mainly of carbonaceous materials of mineral or non-mineral origin
- C10L5/04—Raw material of mineral origin to be used; Pretreatment thereof
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L5/00—Solid fuels
- C10L5/02—Solid fuels such as briquettes consisting mainly of carbonaceous materials of mineral or non-mineral origin
- C10L5/06—Methods of shaping, e.g. pelletizing or briquetting
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L5/00—Solid fuels
- C10L5/40—Solid fuels essentially based on materials of non-mineral origin
- C10L5/44—Solid fuels essentially based on materials of non-mineral origin on vegetable substances
- C10L5/442—Wood or forestry waste
-
- 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
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Environmental & Geological Engineering (AREA)
- Geology (AREA)
- Geochemistry & Mineralogy (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Biodiversity & Conservation Biology (AREA)
- Wood Science & Technology (AREA)
- Forests & Forestry (AREA)
- Ecology (AREA)
- Engineering & Computer Science (AREA)
- Agronomy & Crop Science (AREA)
- Solid Fuels And Fuel-Associated Substances (AREA)
Abstract
nullThe invention discloses a kind of composite biomass fuel，Relate to bio-fuel processing technique field，The production raw material of described composite biomass fuel includes following component (by weight): straw 10 20 parts、Caulis et Folium Oryzae 20 30 parts、Wood flour 20 30 parts、25 parts of humus layer soil，10 20 parts of branch，20 30 parts of anthracite，Combustion adjuvant 5 10 parts，The invention also discloses the processing technique of a kind of composite biomass fuel，Including pulverization process、Anthracite is pulverized、Mixing treatment、Dried、Discharging molding and six technical processs of packed products，Granule moisture content of the present invention is low，Fuel value is high，Compared with conventional biomass fuel pellet，The present invention passes through modulation and the optimization of formula，Pass through coal、Combustion adjuvant and the collaborative combustion of biomass，Efficiency of combustion can be greatly improved，Reduce ignition temperature，And burning time is long、Burning is fully，Can fully substitute non-renewable energy resources，It is worthy to be popularized.
Description
Technical field
The present invention relates to bio-fuel processing technique field, be specifically related to a kind of composite biomass fuel and one is compound raw
The processing technique of biomass fuel.
Background technology
In Agricultural Activities, can produce substantial amounts of garbage, such as straw, Caulis et Folium Oryzae, rice husk etc., these materials are normal
Often abandoned by random, or directly burn in field, but so not only air can be caused the biggest pollution, and
Also recycling of resource it is unfavorable for.In recent years, along with development and the birth of biomass energy, the need that people are urgent of science and technology
Want the production method that can carry out agricultural wastes recycling.Biomass fuel is a kind of regenerative resource, be a kind of novel,
Environmental protection, energy-conservation clean energy resource, be widely used in the use of Industrial Boiler and domestic stove, replaceable coal, liquefied gas, natural gas
Deng.But the volume of fuel that tradition is made is relatively large, the time lighted is long, burns insufficient, and the moisture content in fuel is difficult to wave
Send out, and automatically feed combustion apparatus can not be used, can only use on the combustion apparatus of manual charging.
Summary of the invention
Problem to be solved by this invention is to provide one, and performance is more excellent, fuel value is higher and processing technique is the most compound
Biomass fuel and processing technique thereof.
To achieve these goals, the technical scheme that the present invention takes is: a kind of composite biomass fuel, its feature exists
Following component (by weight) is included: straw 10-20 part, Caulis et Folium Oryzae 20-in: the production raw material of described composite biomass fuel
30 parts, wood flour 20-30 part, humus layer soil 2-5 part, branch 10-20 part, anthracite 20-30 part, combustion adjuvant 5-10 part.
A kind of processing technique of composite biomass fuel, described processing technique follows the steps below:
(1) pulverization process: the straw in raw material, Caulis et Folium Oryzae, wood flour, humus layer soil and branch are added in pulverizer
Carrying out pulverization process, a length of 30min-40min during pulverizing, after pulverizing, particle diameter is 4mm-6mm；
(2) anthracite is pulverized: is put in pulverizer by the anthracite in raw material and pulverizes, a length of 20min-during pulverizing
30min；
(3) mixing treatment: the material that step (1) and step (2) obtain is put into and carries out in Horizontal type mixer heating batch mixing,
And add combustion adjuvant, a length of 30min-40min during batch mixing；
(4) dried: be dried in the material that step (3) obtains is positioned over baking oven, baking temperature is 70 DEG C-80
DEG C, a length of 2h-3h when being dried；
(5) discharging molding: dried material is carried out discharging by granule-forming machine, a diameter of 3mm-4mm of discharging, go out
Material temperature degree is 60 DEG C-80 DEG C；
(6) packed products: test the material obtained, packs warehouse-in after the assay was approved.
Preferably, described combustion adjuvant is specifically made up of the material of following component (by weight): kieselguhr 10-12 part,
Sodium nitrate 10-15 part, meerschaum 25-30 part, manganese oxide 3-5 part.
Preferably, in described step (2), anthracite particle diameter after crushed is 5mm-8mm.
Preferably, in described step (3), mixture temperature is 60 DEG C-70 DEG C.
Preferably, in described step (4), material moisture after drying is 10%-15%.
Preferably, the biomass fuel finished product water content obtained in described step (5) is 8%-12%.
Using technical scheme, the composite biomass fuel particle moisture content that the present invention produces is low, fuel value
Height, compared with conventional biomass fuel pellet, the present invention passes through modulation and the optimization of formula, by coal, combustion adjuvant with biological
The collaborative combustion of matter, it is possible to be greatly improved efficiency of combustion, reduces ignition temperature, and length burning time, burning is fully, for
National economy produces the high temperature energy providing a kind of low cost, it is possible to meet most industry heating and the temperature of furnace fuel
Requirement so that biomass fuel can be widely used in industrial energy field, is worthy to be popularized.
Accompanying drawing explanation
Fig. 1 is the flow chart of the processing technique of a kind of composite biomass fuel of the present invention.
Detailed description of the invention
For the technological means making the present invention realize, creation characteristic, reach purpose and be easy to understand with effect, below in conjunction with
Detailed description of the invention, is expanded on further the present invention.
Embodiment 1:
As it is shown in figure 1, a kind of composite biomass fuel of the present embodiment, the production raw material of described composite biomass fuel
Including following component (by weight): straw 10 parts, Caulis et Folium Oryzae 20 parts, wood flour 30 parts, 2 parts of humus layer soil, 10 parts of branch,
30 parts of anthracite, combustion adjuvant 5 parts, wherein combustion adjuvant is specifically made up of the material of following component (by weight): kieselguhr 10
Part, sodium nitrate 10 parts, meerschaum 30 parts, manganese oxide 4 parts.
A kind of processing technique of composite biomass fuel, described processing technique follows the steps below:
(1) pulverization process: the straw in raw material, Caulis et Folium Oryzae, wood flour, humus layer soil and branch are added in pulverizer
Carrying out pulverization process, a length of 30min during pulverizing, after pulverizing, particle diameter is 6mm；
(2) anthracite is pulverized: is put in pulverizer by the anthracite in raw material and pulverizes, a length of 20min during pulverizing,
Wherein anthracite particle diameter after crushed is 8mm；
(3) mixing treatment: the material that step (1) and step (2) obtain is put into and carries out in Horizontal type mixer heating batch mixing,
And adding combustion adjuvant, a length of 30min during batch mixing, wherein mixture temperature is 60 DEG C；
(4) dried: be dried in the material that step (3) obtains is positioned over baking oven, baking temperature is 70 DEG C, dry
A length of 2h time dry, material moisture the most after drying is 15%；
(5) discharging molding: dried material is carried out discharging by granule-forming machine, a diameter of 3mm of discharging, go out material temperature
Degree is 60 DEG C, and the biomass fuel finished product water content wherein obtained is 12%；
(6) packed products: test the material obtained, packs warehouse-in after the assay was approved.
Embodiment 2: remaining is same as in Example 1, difference is the production raw material of described composite biomass fuel
Including following component (by weight): straw 15 parts, Caulis et Folium Oryzae 25 parts, wood flour 25 parts, 3 parts of humus layer soil, 15 parts of branch,
25 parts of anthracite, combustion adjuvant 8 parts, in described step (2), anthracite particle diameter after crushed is 6mm, mixed in described step (3)
Material temperature degree is 70 DEG C, and in described step (4), material moisture after drying is 13%, the biology obtained in described step (5)
Matter fuel finished product water content is 10%.
Embodiment 3: remaining is same as in Example 1, difference is the production raw material of described composite biomass fuel
Including following component (by weight): straw 20 parts, Caulis et Folium Oryzae 20 parts, wood flour 30 parts, 5 parts of humus layer soil, 20 parts of branch,
20 parts of anthracite, combustion adjuvant 5 parts, in described step (2), anthracite particle diameter after crushed is 5mm, mixed in described step (3)
Material temperature degree is 70 DEG C, and in described step (4), material moisture after drying is 10%, the biology obtained in described step (5)
Matter fuel finished product water content is 8%.
After process above step, take out composite biomass fuel sample, obtain data below:
From data above, the product burning-point acquired by the present invention is relatively low, units of heat is big and the unit combustion time relatively
Long, it is possible to be greatly improved efficiency of combustion, reduce ignition temperature, and length burning time, burning are fully, it is possible to reduce crop straw burning
Deng the movable pollution to air, preparation technology is simple, easily realizes large-scale production, is worthy to be popularized.
Obviously the present invention implements and is not subject to the restrictions described above, as long as have employed method design and the skill of the present invention
The improvement of the various unsubstantialities that art scheme is carried out, or the most improved design by the present invention and technical scheme directly apply to it
Its occasion, all within protection scope of the present invention.
Claims (7)
1. a composite biomass fuel, it is characterised in that: the production raw material of described composite biomass fuel includes following group
Part (by weight): straw 10-20 part, Caulis et Folium Oryzae 20-30 part, wood flour 20-30 part, humus layer soil 2-5 part, branch 10-
20 parts, anthracite 20-30 part, combustion adjuvant 5-10 part.
2. the processing technique of a composite biomass fuel according to claim 1, it is characterised in that: described processing technique is pressed
Carry out according to following steps:
(1) pulverization process: the straw in raw material, Caulis et Folium Oryzae, wood flour, humus layer soil and branch are added in pulverizer and carries out
Pulverization process, a length of 30min-40min during pulverizing, after pulverizing, particle diameter is 4mm-6mm；
(2) anthracite is pulverized: is put in pulverizer by the anthracite in raw material and pulverizes, a length of 20min-during pulverizing
30min；
(3) mixing treatment: the material that step (1) and step (2) obtain is put into and carries out in Horizontal type mixer heating batch mixing, and add
Enter combustion adjuvant, a length of 30min-40min during batch mixing；
(4) dried: be dried in the material that step (3) obtains is positioned over baking oven, baking temperature is 70 DEG C-80 DEG C,
A length of 2h-3h when being dried；
(5) discharging molding: dried material is carried out discharging by granule-forming machine, a diameter of 3mm-4mm of discharging, go out material temperature
Degree is 60 DEG C-80 DEG C；
(6) packed products: test the material obtained, packs warehouse-in after the assay was approved.
A kind of composite biomass fuel the most according to claim 1, it is characterised in that: described combustion adjuvant is specifically by following group
The material composition of part (by weight): kieselguhr 10-12 part, sodium nitrate 10-15 part, meerschaum 25-30 part, manganese oxide 3-5
Part.
The processing technique of a kind of composite biomass fuel the most according to claim 2, it is characterised in that: described step (2)
Middle anthracite particle diameter after crushed is 5mm-8mm.
The processing technique of a kind of composite biomass fuel the most according to claim 1, it is characterised in that: described step (3)
Middle mixture temperature is 60 DEG C-70 DEG C.
The processing technique of a kind of composite biomass fuel the most according to claim 1, it is characterised in that: described step (4)
In material moisture after drying be 10%-15%.
The processing technique of a kind of composite biomass fuel the most according to claim 1, it is characterised in that: described step (5)
In the biomass fuel finished product water content that obtains be 8%-12%.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
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| CN201610594159.XA CN106085544A (en) | 2016-07-26 | 2016-07-26 | A kind of composite biomass fuel and processing technique thereof |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610594159.XA CN106085544A (en) | 2016-07-26 | 2016-07-26 | A kind of composite biomass fuel and processing technique thereof |
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| CN106085544A true CN106085544A (en) | 2016-11-09 |
Family
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Family Applications (1)
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| CN201610594159.XA Pending CN106085544A (en) | 2016-07-26 | 2016-07-26 | A kind of composite biomass fuel and processing technique thereof |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106622024A (en) * | 2017-01-05 | 2017-05-10 | 安徽润发生物能源科技有限公司 | Biomass fuel granulation process |
| CN106867616A (en) * | 2017-03-22 | 2017-06-20 | 合肥浦尔菲电线科技有限公司 | A kind of Novel environment-friendlymaterial material and preparation method thereof |
| CN109022086A (en) * | 2018-08-06 | 2018-12-18 | 安徽上元新型家居材料有限公司 | A kind of straw fuel rod and its preparation process |
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| CN101985575A (en) * | 2010-11-05 | 2011-03-16 | 华南理工大学 | Biomass moulded coal and preparation method thereof |
| CN105219471A (en) * | 2015-10-17 | 2016-01-06 | 明光市龙腾矿物有限公司 | A kind of containing sepiolite composite biomass fuel and preparation method thereof |
| CN105238481A (en) * | 2015-10-17 | 2016-01-13 | 明光市龙腾矿物有限公司 | Composite biomass fuel and preparation method thereof |
| CN105779066A (en) * | 2016-04-06 | 2016-07-20 | 南通市元方缘家具制造有限公司 | Manufacturing process of biological grain fuel |
-
2016
- 2016-07-26 CN CN201610594159.XA patent/CN106085544A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101985575A (en) * | 2010-11-05 | 2011-03-16 | 华南理工大学 | Biomass moulded coal and preparation method thereof |
| CN105219471A (en) * | 2015-10-17 | 2016-01-06 | 明光市龙腾矿物有限公司 | A kind of containing sepiolite composite biomass fuel and preparation method thereof |
| CN105238481A (en) * | 2015-10-17 | 2016-01-13 | 明光市龙腾矿物有限公司 | Composite biomass fuel and preparation method thereof |
| CN105779066A (en) * | 2016-04-06 | 2016-07-20 | 南通市元方缘家具制造有限公司 | Manufacturing process of biological grain fuel |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106622024A (en) * | 2017-01-05 | 2017-05-10 | 安徽润发生物能源科技有限公司 | Biomass fuel granulation process |
| CN106867616A (en) * | 2017-03-22 | 2017-06-20 | 合肥浦尔菲电线科技有限公司 | A kind of Novel environment-friendlymaterial material and preparation method thereof |
| CN109022086A (en) * | 2018-08-06 | 2018-12-18 | 安徽上元新型家居材料有限公司 | A kind of straw fuel rod and its preparation process |
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Application publication date: 20161109 |