CN106085543A - A kind of biomass synthetic fuel and processing technique thereof - Google Patents
A kind of biomass synthetic fuel and processing technique thereof Download PDFInfo
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- CN106085543A CN106085543A CN201610594085.XA CN201610594085A CN106085543A CN 106085543 A CN106085543 A CN 106085543A CN 201610594085 A CN201610594085 A CN 201610594085A CN 106085543 A CN106085543 A CN 106085543A
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- parts
- synthetic fuel
- biomass
- biomass synthetic
- fuel
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Classifications
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- 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
- C10L9/00—Treating solid fuels to improve their combustion
- C10L9/10—Treating solid fuels to improve their combustion by using additives
-
- 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
- C10L9/00—Treating solid fuels to improve their combustion
- C10L9/10—Treating solid fuels to improve their combustion by using additives
- C10L9/12—Oxidation means, e.g. oxygen-generating compounds
-
- 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
nullThe invention discloses a kind of biomass synthetic fuel，Relate to bio-fuel production technology field，The production raw material of described biomass synthetic fuel includes following component (by weight): straw 10 20 parts、Waste tire rubber 5 10 parts、Oxidant 25 parts、Waste oil 5 10 parts、Thermoplastic 15 20 parts、20 30 parts of anthracite、Combustion adjuvant 5 10 parts，The invention also discloses the production technology of a kind of biomass synthetic fuel，Including pulverization process、Dried、Hot melt processes、Mixing treatment、Compression molding and six technical processs of packed products，Fuel value of the present invention 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，And the waste material produced in commercial production and agricultural production can be made full use of，Well effect is played to improving environment，It is worthy to be popularized.
Description
Technical field
The present invention relates to bio-fuel production technology field, be specifically related to the production technology of a kind of biomass synthetic fuel.
Background technology
In order to well improve the problem of rural energy and environmental protection, factory and rural area are carried out existing biomass high-quality and turns
Changing utilizes imperative, and factory and agricultural production can produce substantial amounts of garbage, such as rice straw and industrial waste etc., and these
Material can burn in a large number or arbitrarily abandon habitually in the past, air the most not only can cause the biggest pollution, and be unfavorable for resource
Recycle.Biomass granule fuel is the major part of Biomass Industry, and current biomass fuel is in preparation process
The most nonflammable, and the heat produced in combustion process is inadequate, improves in combustion process to reduce the burning-point of biological particles
Energy heat may require that to add inside biomass granule fuel and ignite material, the most not only cost is high but also be unfavorable for environmental protection.
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 production technology is the most raw
Material synthetic fuel and processing technique thereof.
To achieve these goals, the technical scheme that the present invention takes is: a kind of biomass synthetic fuel, described biomass
The production raw material of synthetic fuel includes following component (by weight): straw 10-20 part, waste tire rubber 5-10 part,
Oxidant 2-5 part, waste oil 5-10 part, thermoplastic 15-20 part, anthracite 20-30 part, combustion adjuvant 5-10 part.
A kind of production technology of biomass synthetic fuel, described production technology follows the steps below:
(1) pulverization process: the straw in raw material, oxidant and anthracite are added in pulverizer and carries out pulverization process,
A length of 30min-40min during pulverizing, after pulverizing, particle diameter is 4mm-6mm；
(2) dried: the material that step (1) obtains is positioned over open field and air-dries, a length of 2h-when air-drying
3h；
(3) hot melt processes: waste tire rubber and thermoplastic are carried out high-temperature heating, and the material after melting is placed
Being stirred in agitator, and add waste oil and combustion adjuvant, heating-up temperature is 500 DEG C-700 DEG C；
(4) mixing treatment: material step (2) obtained carries out mix and blend in adding agitator, a length of 1h-during stirring
2h, whipping temp is 300 DEG C-500 DEG C；
(5) compression molding: being put into by the material that step (4) obtains and cool down in mould and pressurize, pressure is 15MPa-
30MPa；
(6) packed products: test the material obtained, packs warehouse-in after the assay was approved.
Preferably, in described raw material, combustion adjuvant is specifically made up of the material of following component (by weight): kieselguhr
10-15 part, meerschaum 20-25 part, manganese oxide 5-8 part.
Preferably, in described raw material, oxidant is specially potassium nitrate.
Preferably, after air-drying in described step (2), the water content of mixed material is 10%-15%.
Preferably, a length of 30min-50min when stirring in described step (4).
Preferably, in described step (5), material is cooled to room temperature, a length of 15min-20min during pressurization.
Using technical scheme, the biomass synthetic fuel fuel value that the present invention provides is high, with conventional biology
Matter fuel particle is compared, and the present invention passes through modulation and the optimization of formula, is made by the collaborative burning of coal, combustion adjuvant and biomass
With, it is possible to it is greatly improved efficiency of combustion, and the waste material produced in commercial production and agricultural production can be made full use of, to improving ring
Well effect is played in border, the utilization of waste oil also plays the effect of twice laid, produces for national economy and provide one
Plant the high temperature energy of low cost 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 production technology of a kind of biomass synthetic 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 biomass synthetic fuel of the present embodiment and production technology thereof, described biomass synthetic fuel
Production raw material include following component (by weight): straw 10 parts, waste tire rubber 5 parts, oxidant 2 parts, trench
Oil 5 parts, thermoplastic 15 parts, 20 parts of anthracite, combustion adjuvant 5 parts, wherein combustion adjuvant is specifically by following component (by weight
Meter) material composition: 10 parts of kieselguhr, meerschaum 20 parts, manganese oxide 5 parts, wherein oxidant is specially potassium nitrate.
A kind of production technology of biomass synthetic fuel, described production technology follows the steps below:
(1) pulverization process: the straw in raw material, oxidant and anthracite are added in pulverizer and carries out pulverization process,
A length of 30mi during pulverizing, after pulverizing, particle diameter is 4mm；
(2) dried: the material that step (1) obtains is positioned over open field and air-dries, a length of 2h when air-drying, its
In air-dry after the water content of mixed material be 10%；
(3) hot melt processes: waste tire rubber and thermoplastic are carried out high-temperature heating, and the material after melting is placed
Being stirred in agitator, and add waste oil and combustion adjuvant, heating-up temperature is 500 DEG C；
(4) mixing treatment: material step (2) obtained carries out mix and blend in adding agitator, a length of 1h during stirring,
Whipping temp is 300, wherein a length of 30min during stirring；
(5) compression molding: being put into by the material that step (4) obtains and cool down in mould and pressurize, pressure is 15MPa, wherein
Material is cooled to room temperature, a length of 15min during pressurization；
(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 biomass synthetic fuel
Including following component (by weight): straw 15 parts, waste tire rubber 8 parts, oxidant 3 parts, waste oil 8 parts, thermoplasticity
15 parts of plastics, 25 parts of anthracite, combustion adjuvant 8 parts, wherein combustion adjuvant is specifically made up of the material of following component (by weight):
12 parts of kieselguhr, meerschaum 25 parts, manganese oxide 5 parts, after air-drying in described step (2), the water content of mixed material is 12%, institute
A length of 40min when stating stirring in step (4), in described step (5), material is cooled to room temperature, a length of 18min during pressurization.
Embodiment 3: remaining is same as in Example 1, difference is the production raw material of described biomass synthetic fuel
Including following component (by weight): straw 20 parts, waste tire rubber 10 parts, oxidant 5 parts, waste oil 10 parts, thermoplastic
Property 20 parts of plastics, 30 parts of anthracite, combustion adjuvant 10 parts, wherein combustion adjuvant is specifically by the material group of following component (by weight)
Becoming: 15 parts of kieselguhr, meerschaum 25 parts, manganese oxide 8 parts, after air-drying in described step (2), the water content of mixed material is 15%,
A length of 50min during stirring in described step (4), in described step (5), material is cooled to room temperature, a length of 20min during pressurization.
After process above step, take out biomass synthetic fuel sample, obtain data below:
From data above, the product burning-point acquired by the present invention is moderate, 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, the residual after terminating of burning
Thing is less, it is possible to reduce the movable pollution to air such as crop straw burning, not only can reduce pollution, and energy producing fuel stage
Enough minimizing residues after burning terminates, production procedure 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 biomass synthetic fuel, it is characterised in that: the production raw material of described biomass synthetic fuel includes following group
Part (by weight): straw 10-20 part, waste tire rubber 5-10 part, oxidant 2-5 part, waste oil 5-10 part, thermoplasticity
Plastics 15-20 part, anthracite 20-30 part, combustion adjuvant 5-10 part.
2. the production technology of a biomass synthetic fuel according to claim 1, it is characterised in that: described production technology is pressed
Carry out according to following steps:
(1) pulverization process: the straw in raw material, oxidant and anthracite are added in pulverizer and carries out pulverization process, pulverize
Shi Changwei 30min-40min, after pulverizing, particle diameter is 4mm-6mm；
(2) dried: the material that step (1) obtains is positioned over open field and air-dries, a length of 2h-3h when air-drying；
(3) hot melt processes: waste tire rubber and thermoplastic are carried out high-temperature heating, and the material after melting is positioned over and stirs
Being stirred in mixing bucket, and add waste oil and combustion adjuvant, heating-up temperature is 500 DEG C-700 DEG C；
(4) mixing treatment: material step (2) obtained carries out mix and blend in adding agitator, a length of 1h-2h during stirring,
Whipping temp is 300 DEG C-500 DEG C；
(5) compression molding: being put into by the material that step (4) obtains and cool down in mould and pressurize, pressure is 15MPa-30MPa；
(6) packed products: test the material obtained, packs warehouse-in after the assay was approved.
A kind of biomass synthetic fuel the most according to claim 1, it is characterised in that: in described raw material, combustion adjuvant is concrete
It is made up of the material of following component (by weight): kieselguhr 10-15 part, meerschaum 20-25 part, manganese oxide 5-8 part.
A kind of biomass synthetic fuel the most according to claim 1, it is characterised in that: in described raw material, oxidant is concrete
For potassium nitrate.
The production technology of a kind of biomass synthetic fuel the most according to claim 1, it is characterised in that: described step (2)
In air-dry after the water content of mixed material be 10%-15%.
The production technology of a kind of biomass synthetic fuel the most according to claim 1, it is characterised in that: described step (4)
A length of 30min-50min during middle stirring.
The production technology of a kind of biomass synthetic fuel the most according to claim 1, it is characterised in that: described step (5)
Middle material is cooled to room temperature, a length of 15min-20min during pressurization.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610594085.XA CN106085543A (en) | 2016-07-26 | 2016-07-26 | A kind of biomass synthetic fuel and processing technique thereof |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201610594085.XA CN106085543A (en) | 2016-07-26 | 2016-07-26 | A kind of biomass synthetic fuel and processing technique thereof |
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| CN106085543A true CN106085543A (en) | 2016-11-09 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201610594085.XA Pending CN106085543A (en) | 2016-07-26 | 2016-07-26 | A kind of biomass synthetic fuel and processing technique thereof |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108998138A (en) * | 2018-08-01 | 2018-12-14 | 赖子丹 | A kind of biomass synthetic fuel |
| CN111808647A (en) * | 2020-07-17 | 2020-10-23 | 东北林业大学 | Wood-plastic-based fuel and preparation method thereof |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103805303A (en) * | 2014-02-10 | 2014-05-21 | 王立才 | Bio-fuel coal briquettes |
| CN105018168A (en) * | 2014-04-24 | 2015-11-04 | 南京博海水产有限公司 | Method for manufacturing straw-blended coal briquettes |
| 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 |
| CN105296048A (en) * | 2015-11-21 | 2016-02-03 | 陆仲权 | Biomass granular fuel and production technology thereof |
| CN105400556A (en) * | 2015-10-17 | 2016-03-16 | 安徽昌信生物质能源有限公司 | Biomass fuel based on combustion-supporting meerschaum and preparation method thereof |
-
2016
- 2016-07-26 CN CN201610594085.XA patent/CN106085543A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103805303A (en) * | 2014-02-10 | 2014-05-21 | 王立才 | Bio-fuel coal briquettes |
| CN105018168A (en) * | 2014-04-24 | 2015-11-04 | 南京博海水产有限公司 | Method for manufacturing straw-blended coal briquettes |
| 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 |
| CN105400556A (en) * | 2015-10-17 | 2016-03-16 | 安徽昌信生物质能源有限公司 | Biomass fuel based on combustion-supporting meerschaum and preparation method thereof |
| CN105296048A (en) * | 2015-11-21 | 2016-02-03 | 陆仲权 | Biomass granular fuel and production technology thereof |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108998138A (en) * | 2018-08-01 | 2018-12-14 | 赖子丹 | A kind of biomass synthetic fuel |
| CN111808647A (en) * | 2020-07-17 | 2020-10-23 | 东北林业大学 | Wood-plastic-based fuel and preparation method thereof |
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Application publication date: 20161109 |