WO2009038241A1 - Method for preparing solid carbonizing fuels using wood biomass - Google Patents
Method for preparing solid carbonizing fuels using wood biomass Download PDFInfo
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- WO2009038241A1 WO2009038241A1 PCT/KR2007/004472 KR2007004472W WO2009038241A1 WO 2009038241 A1 WO2009038241 A1 WO 2009038241A1 KR 2007004472 W KR2007004472 W KR 2007004472W WO 2009038241 A1 WO2009038241 A1 WO 2009038241A1
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- WIPO (PCT)
- Prior art keywords
- fuel
- solid
- wood biomass
- solid carbonized
- carbonized fuel
- Prior art date
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- 239000000446 fuel Substances 0.000 title claims abstract description 101
- 239000007787 solid Substances 0.000 title claims abstract description 65
- 239000002023 wood Substances 0.000 title claims abstract description 50
- 239000002028 Biomass Substances 0.000 title claims abstract description 40
- 238000000034 method Methods 0.000 title claims abstract description 22
- 238000010000 carbonizing Methods 0.000 title claims description 12
- FGIUAXJPYTZDNR-UHFFFAOYSA-N potassium nitrate Chemical compound [K+].[O-][N+]([O-])=O FGIUAXJPYTZDNR-UHFFFAOYSA-N 0.000 claims abstract description 54
- 229920002472 Starch Polymers 0.000 claims abstract description 41
- 235000019698 starch Nutrition 0.000 claims abstract description 41
- 239000008107 starch Substances 0.000 claims abstract description 40
- 235000016735 Manihot esculenta subsp esculenta Nutrition 0.000 claims abstract description 39
- 238000010438 heat treatment Methods 0.000 claims abstract description 35
- 235000010333 potassium nitrate Nutrition 0.000 claims abstract description 25
- 239000004323 potassium nitrate Substances 0.000 claims abstract description 25
- 238000000465 moulding Methods 0.000 claims abstract description 10
- 238000002156 mixing Methods 0.000 claims abstract description 6
- 239000003610 charcoal Substances 0.000 claims description 61
- 239000000843 powder Substances 0.000 claims description 40
- 240000003183 Manihot esculenta Species 0.000 claims description 38
- 241000637252 Acacia harpophylla Species 0.000 claims description 17
- 235000017166 Bambusa arundinacea Nutrition 0.000 claims description 12
- 235000017491 Bambusa tulda Nutrition 0.000 claims description 12
- 235000015334 Phyllostachys viridis Nutrition 0.000 claims description 12
- 239000011425 bamboo Substances 0.000 claims description 12
- 238000000748 compression moulding Methods 0.000 claims description 7
- 238000001035 drying Methods 0.000 claims description 7
- 241000208140 Acer Species 0.000 claims description 2
- 241001133760 Acoelorraphe Species 0.000 claims description 2
- 244000060011 Cocos nucifera Species 0.000 claims description 2
- 235000013162 Cocos nucifera Nutrition 0.000 claims description 2
- 244000043261 Hevea brasiliensis Species 0.000 claims description 2
- 241000219492 Quercus Species 0.000 claims description 2
- 244000082204 Phyllostachys viridis Species 0.000 claims 1
- 238000002485 combustion reaction Methods 0.000 abstract description 28
- 239000000203 mixture Substances 0.000 abstract description 13
- 239000007800 oxidant agent Substances 0.000 abstract description 7
- 230000001590 oxidative effect Effects 0.000 abstract description 7
- 239000002994 raw material Substances 0.000 abstract description 5
- 230000005611 electricity Effects 0.000 abstract description 3
- 241000658379 Manihot esculenta subsp. esculenta Species 0.000 abstract 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 17
- 241001330002 Bambuseae Species 0.000 description 11
- 239000011230 binding agent Substances 0.000 description 10
- 230000000052 comparative effect Effects 0.000 description 10
- 239000000463 material Substances 0.000 description 10
- 238000002360 preparation method Methods 0.000 description 9
- 239000004449 solid propellant Substances 0.000 description 9
- 229920002261 Corn starch Polymers 0.000 description 8
- 239000008120 corn starch Substances 0.000 description 8
- 229940099112 cornstarch Drugs 0.000 description 8
- 229920000856 Amylose Polymers 0.000 description 5
- 239000000853 adhesive Substances 0.000 description 5
- 230000001070 adhesive effect Effects 0.000 description 5
- 238000004519 manufacturing process Methods 0.000 description 5
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 4
- 241000196324 Embryophyta Species 0.000 description 4
- 238000007254 oxidation reaction Methods 0.000 description 4
- 230000008569 process Effects 0.000 description 4
- 239000002699 waste material Substances 0.000 description 4
- 239000002916 wood waste Substances 0.000 description 4
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- 230000003247 decreasing effect Effects 0.000 description 3
- 230000001419 dependent effect Effects 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 3
- 230000003647 oxidation Effects 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 241000221017 Euphorbiaceae Species 0.000 description 2
- 241000233866 Fungi Species 0.000 description 2
- 229910002651 NO3 Inorganic materials 0.000 description 2
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 239000006227 byproduct Substances 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 238000010298 pulverizing process Methods 0.000 description 2
- 238000003892 spreading Methods 0.000 description 2
- 230000007480 spreading Effects 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- 238000006424 Flood reaction Methods 0.000 description 1
- 244000017020 Ipomoea batatas Species 0.000 description 1
- 235000002678 Ipomoea batatas Nutrition 0.000 description 1
- 241001465754 Metazoa Species 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 229910052788 barium Inorganic materials 0.000 description 1
- DSAJWYNOEDNPEQ-UHFFFAOYSA-N barium atom Chemical compound [Ba] DSAJWYNOEDNPEQ-UHFFFAOYSA-N 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 238000003763 carbonization Methods 0.000 description 1
- 231100000357 carcinogen Toxicity 0.000 description 1
- 239000003183 carcinogenic agent Substances 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 239000003721 gunpowder Substances 0.000 description 1
- 230000001771 impaired effect Effects 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 229920005610 lignin Polymers 0.000 description 1
- 230000005923 long-lasting effect Effects 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 230000002250 progressing effect Effects 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 235000011888 snacks Nutrition 0.000 description 1
- 230000004936 stimulating effect Effects 0.000 description 1
- 230000031068 symbiosis, encompassing mutualism through parasitism Effects 0.000 description 1
- 239000012855 volatile organic compound Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B53/00—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form
- C10B53/02—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form of cellulose-containing material
-
- 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
- C10L5/34—Other details of the shaped fuels, e.g. briquettes
- C10L5/36—Shape
- C10L5/363—Pellets or granulates
-
- 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
-
- 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
Definitions
- the present invention relates to a method for preparing a solid carbonized fuel using wood biomass, and more particularly, to a method for preparing an environmentally friendly, solid carbonized fuel by mixing wood biomass which is abundantly available in nature, cassava starch showing ignition, bonding and adhesion properties, and potassium nitrate as an oxidant, and then molding them.
- the plan 'the twenty-first century wood fire' which aims to utilize wood fuel as an alternative energy source, has been progressing at government level.
- the plan is to prepare a support system so that waste wood spontaneously generated from forest, or waste wood generated from households and industry, can be used as fuel for cogeneration process, and particularly, 'a plan for stimulating wood biomass supply' is suggested as one of plans for promoting renewable energy utilization.
- Biomass refers to living organisms, including plants receiving sunlight, plant- fungi symbiosis, and animals and plants feeding on the plant fungi.
- the fuel is prepared by adding volatile organic compounds such as benzene, and in this case, they produce carcinogens, harmful gases and thus cause environmental problems as well as are extremely harmful to the human body.
- the burning material is bamboo charcoal made from natural bamboo by a carbonization process
- the ignition material is prepared by molding a mixture of bamboo charcoal powder, activated charcoal, fine sugar, potassium nitrate, barium and starch in a mold, to cut into regular size of pieces, and the solid fuel is characterized in that the burning material combustion is performed by the heating power of ignition material.
- it has disadvantages in that a lot of raw materials are required to prepare the solid fuel, and fuel composition is complicated and production cost thereof is high, which cause limited supply of fuel, thus it is not suitable to be used as fuel for large boilers.
- the present invention provides a method for preparing a solid carbonized fuel using wood biomass, which comprises the steps of: (a) preparing charcoal powder by carbonizing wood biomass; (b) preparing a mold by mixing 8-17 parts by weight of cassava starch and 1-3 parts by weight of potassium nitrate to 100 parts by weight of the charcoal powder and molding them; and (c) drying the mold to obtain a solid carbonized fuel.
- the present invention also provides a solid carbonized fuel containing charcoal derived from wood biomass, cassava starch and potassium nitrate, which is prepared by the above method. [25] The above and other objects, features and embodiments of the present invention will be more clearly understood from the following detailed description and accompanying claims. [26]
- FIG. 1 is a flow chart showing the preparation process for the solid carbonized fuel using wood biomass according to the present invention.
- FIG. 2 shows a solid carbonized fuel using wood biomass, which is prepared according to the present invention.
- [31] [32] DETAILED DESCRIPTION OF THE INVENTION. AND PREF ERRED EM-
- the present invention relates to a method for preparing a solid carbonized fuel using wood biomass, which comprises the steps of: (a) preparing charcoal powder by carbonizing wood biomass; (b) preparing a mold by mixing 8-17 parts by weight of cassava starch and 1-3 parts by weight of potassium nitrate to 100 parts by weight of the charcoal powder and molding them; and (c) drying the mold to obtain a solid carbonized fuel (FIG.l).
- wood biomass means trees and herbaceous plants containing lignin and cellulose, and products, waste wood, paper etc. derived therefrom. Thus, it is different from wood which is not processed into products such as paper etc., and is limitlessly available in nature.
- the wood biomass is preferably selected from the group consisting of brigalow, oak, bamboo, rubber tree, maple, coconut tree, and palm tree.
- heating value of the charcoal powder in the step (a) is preferably 6,500-7,800 kcal/kg.
- the charcoal powder prepared by carbonizing the wood biomass allows the solid fuel to emit heat corresponding to heating value of the charcoal powder by oxidation during combustion, and function as fuel.
- the charcoal powder is a main component of solid carbonized fuel prepared according to the present invention, and it emits heat corresponding to heating value of the charcoal powder, i.e., 6,500-7,800 kcal by oxidation during combustion, thus functioning as fuel.
- brigalow can be used as wood biomass.
- the brigalow is used for railroad ties, furniture, firewood, etc., and particularly, it emits little smoke and has superior heating power, thus it is highly useful as fuel.
- charcoal prepared using the brigalow contains more volatile components than that of charcoal prepared using other woods, and thus, has fast burning velocity and allows a long-lasting combustion.
- cassava starch functions as a natural binder available in nature, unlike the conventional chemical binders.
- Cassava is a South American dicotyledonous deciduous shrub belonging to the
- Spurge family Euphorbiaceae, which is characterized in that it is a tuberous root spreading widely. It is a tuberous root spreading widely, produces thick root tubers like sweet potato, and contains 20-25% starch. Starch extracted from cassava tubers is called tapioca, and has glutinous property, so that it can be used as an ingredient for snacks, alcohol, paste and foods.
- cassava starch is prepared by cutting cassava tubers into pieces, drying them, and grinding into a fine powder using a pulverizer, and the cassava starch is mixed with water, and then heated to prepare a cassava starch mixture, thus using the cassava starch mixture as a binder.
- cassava starch shows a function as an igniting agent for rapid ignition and a function as an adhesive capable of adhering to other materials to help attach them together. Therefore, the cassava starch used in the present invention has the effects of simplifying the constitution of the solid carbonized fuel according to the present invention, as well as enhancing the effectiveness thereof, compared to the conventional solid fuel in which a binder, an igniting agent, an adhesive etc. are separately added upon preparation of solid carbonized fuel.
- cassava starch has a high amylose concentration and low gelatinization temperature compared to natural starches such as cornstarch, thus reducing heating time in gelatinization process of cassava starch, so that it is possible to increase production due to reduced processing time, and less fuel is consumed for heating.
- the cassava starch is used in a ratio of less than 8 parts by weight, its viscosity weakens when mixed with charcoal powder, so that the resulting solid carbonized fuel is likely to be broken and its ignition velocity decreases, and if the cassava starch is used in a ratio of more than 17 parts by weight, the added amount of charcoal powder is relatively reduced, so that heating value of solid carbonized fuel is decreased and the solid carbonized fuel ignites suddenly to reduce its stability, resulting in low fuel effectiveness, thus the cassava starch is preferably used in a ratio of 8-17 parts by weight based on 100 parts by weight of charcoal powder.
- Niter is one of nitrate minerals containing KN03 that is used as an oxidant, and in the present invention, it functions as an oxidant upon combustion of solid carbonized fuel, so that it has the effect of allowing the solid carbonized fuel to be easily ignited, and to continuously burn.
- the potassium nitrate is one of gunpowder components that has a function of reducing combustion time since it produces oxygen upon combustion to rapidly react with carbon, resulting in an oxidation reaction, thus causing rapid combustion. That is, potassium nitrate improves the combustion efficiency of fuel to enable complete fuel combustion.
- the potassium nitrate is used in a ratio of less than 1 part by weight, its function as an oxidant is impaired, and if the potassium nitrate is used in a ratio of more than 3 parts by weight, its function as an oxidant remains the same, thus the potassium nitrate is preferably used in a ratio of 1-3 parts by weight based on 100 parts by weight of charcoal powder.
- water soluble nitrate in the form of a powder is preferably used such that it is uniformly mixed with the charcoal powder and the cassava starch.
- the molding in the step (b) is preferably compression molding.
- solid carbonized fuel having a regular shape and homogeneous composition can be prepared by the compression molding.
- the present invention relates to solid carbonized fuel containing charcoal derived from wood biomass, cassava starch and potassium nitrate, which is prepared by the above method (FIG.2).
- heating value of the solid carbonized fuel prepared by using the wood biomass is preferably 6,000 ⁇ 7,300 kcal/kg, and the solid carbonized fuel is preferably used as fuel for a large boiler.
- the solid carbonized fuel prepared according to the present invention has a regular shape and homogeneous composition to show a uniform heating value per unit weight, so that when they are used as fuel for a boiler which can produce electricity and steam, combustion control is easy and an output of the boiler is stabilized, which can reduce operator's burden during boiler operation and facility control efficiency can be improved.
- thermal NOx which is highly temperature dependent and thus is formed at the portion of flame close to the burner where high temperature oxidation of atmospheric nitrogen occurs by peak flame temperature, and also produced due to high levels of excess air upon combustion in a boiler facility, the thermal NOx formation increases when the excess air ratio increases upon combustion or local temperature increase occurs in a combustion chamber.
- a boiler can be operated under low air ratio upon fuel combustion due to constant heating value thereof as described above, and homogeneous temperature distribution can be achieved in a combustion chamber of a boiler, thus making it possible to reduce NOx formation, which is highly temperature dependent and excess-air-dependent.
- the weight and volume of charcoal powder prepared by carbonizing wood biomass are decreased compared to the wood biomass used for preparation thereof, and thus there is an advantage in that costs for transporting the solid carbonized fuel prepared using the charcoal powder can be greatly reduced.
- the weight percentage of carbonized charcoal powder weight is about 15-25% based on the weight of the wood biomass, and its volume percentage thereof is less than 40% based on the volume of the wood biomass.
- the water content of wood biomass is 40% before drying, and 20% after drying.
- fuel has a high water content
- the lower the water content of fuel is, the higher the thermal efficiency of fuel becomes and the higher heating value fuel has.
- heating value of the inventive solid carbonized fuel decreases through the steps of mixing charcoal powder prepared by carbonizing wood biomass having 6,500-7,800 kcal/kg of heating value, and cassava starch, then molding them. Thereafter, water content of the solid carbonized fuel is reduced by drying step to increase heating value thereof again, thus obtaining solid carbonized fuel having 6,000-7,300 kcal/kg of heating value.
- Example 1 Preparation of solid carbonized fuel using brigalow. cassava starch, and potassium nitrate [86]
- Brigalow was heated at 400 ⁇ 600°C for 22 hours in a carbonizing furnace with no air flow thereinto to eliminate water and volatile components, thus preparing carbonized brigalow charcoal, and then, the resulting charcoal was finely ground to prepare charcoal powder. At this time, heating value of the prepared charcoal was 6,800 kcal/ kg-
- bamboo was carbonized in a charcoal kiln to prepare bamboo charcoal, and then, the bamboo charcoal was finely pulverized to prepare bamboo charcoal powder.
- 100kg of the bamboo charcoal powder, 12kg of cassava starch obtained by adding water and heating the mixture, and 2kg of potassium nitrate were mixed and subjected to compression molding to prepare a mold. The resulting mold was dried at 12O 0 C for 3 hours to prepare cylindrical solid carbonized fuel.
- this result is due to difference between the levels of amylose present in the cassava starch and the cornstarch, that is, the cassava starch has high amylose content, so that its gelatinization temperature is low(66°C) and the cornstarch has low amylose content, so that its gelatinization temperature is high(76°C), thus, in a gelatinization process of the cassava starch, heating time is reduced, which results in overall reduction in the combustion time.
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- Life Sciences & Earth Sciences (AREA)
- Environmental & Geological Engineering (AREA)
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- Solid Fuels And Fuel-Associated Substances (AREA)
Abstract
The present invention relates to a method for preparing a solid carbonized fuel using wood biomass, and more particularly, to a method for preparing an environmentally friendly, solid carbonized fuel by mixing wood biomass which is abundantly available in nature, cassava starch showing ignition, bonding and adhesion properties, and potassium nitrate as an oxidant, and then molding them. According to the present invention, it is possible to prepare an environmentally friendly, solid carbonized fuel which is economical due to the use of wood biomass abundantly available in nature, can be easily prepared due to simple raw material compositions and has high combustion efficiency, as well as, high heating value per unit weight, and thus the solid carbonized fuel can be used as fuel for a large boiler which can produce electricity and steam.
Description
Description
METHOD FOR PREPARING SOLID CARBONIZING FUELS
USING WOOD BIOMASS
Technical Field
[1] The present invention relates to a method for preparing a solid carbonized fuel using wood biomass, and more particularly, to a method for preparing an environmentally friendly, solid carbonized fuel by mixing wood biomass which is abundantly available in nature, cassava starch showing ignition, bonding and adhesion properties, and potassium nitrate as an oxidant, and then molding them.
[2]
Background Art
[3] Recently, the plan 'the twenty-first century wood fire', which aims to utilize wood fuel as an alternative energy source, has been progressing at government level. Specifically, the plan is to prepare a support system so that waste wood spontaneously generated from forest, or waste wood generated from households and industry, can be used as fuel for cogeneration process, and particularly, 'a plan for stimulating wood biomass supply' is suggested as one of plans for promoting renewable energy utilization. Biomass refers to living organisms, including plants receiving sunlight, plant- fungi symbiosis, and animals and plants feeding on the plant fungi.
[4]
[5] Every year, 3,180,000 tons of wood, that can be used as fuel, are generated, which include wood waste generated from natural disaster, such as floods etc., woodland development, household furniture or industrial by-products, and it is estimated that, from which energy corresponding to 1,430,000 tons of petroleum can be obtained. However, at present, 90% of wood byproducts, and more than 60% of waste wood generated from household, construction industry and wood industry are discarded. Thus, there is an urgent need to develop a technique to utilize the discarded wood waste as an alternative energy source.
[6]
[7] At present, in an attempt to use wood biomass as an energy source, a study for bioethanol production using wood has been conducted, but it has not been commercialized yet, and, in other fields, the study results that can be used for practical application of wood biomass as an energy source, is insufficient.
[8]
[9] Meanwhile, in prior art, in a process for preparing carbonized fuel, as an adhesive for molding carbonized charcoal powder, kneaded grain starch was added or chemical
adhesives such as silicon was added. However, the grain starch dough has a problem in that it is impossible to mass-produce it and thus it is not economical for the production of carbonized fuel, and the chemical adhesives have a problem in that they generate harmful gases upon combustion of the carbonized fuel.
[10]
[11] In addition, in order to improve combustion efficiency of the carbonized fuel, the fuel is prepared by adding volatile organic compounds such as benzene, and in this case, they produce carcinogens, harmful gases and thus cause environmental problems as well as are extremely harmful to the human body.
[12]
[13] Recently, solid fuel prepared by pulverizing wood biomass and compressing it at
180~230°C, was developed, but its strength is weak and its heating value is merely 4800~5500kcal, so that its effectiveness as fuel is limited (WO 06/077652A1). In addition, solid fuel prepared by pulverizing wood waste to adjust the water content of wood waste, and then compressing it at 50~200°C under a pressure of 100~1000kgf/cm without using a binder, was recently developed, but since binders are not used, relatively high-intensity pressure is required in the compression process, the prepared fuel has a disadvantage in that it is apt to be broken (JP 2006-31531A2).
[14]
[15] As a representative example of solid fuel preparation technologies using carbonized wood charcoal, a solid fuel unit having a unit packaged burning material and a unit packaged ignition material was disclosed (Korean Patent Registration 10-0478876). In the solid fuel unit, the burning material is bamboo charcoal made from natural bamboo by a carbonization process, and the ignition material is prepared by molding a mixture of bamboo charcoal powder, activated charcoal, fine sugar, potassium nitrate, barium and starch in a mold, to cut into regular size of pieces, and the solid fuel is characterized in that the burning material combustion is performed by the heating power of ignition material. However, it has disadvantages in that a lot of raw materials are required to prepare the solid fuel, and fuel composition is complicated and production cost thereof is high, which cause limited supply of fuel, thus it is not suitable to be used as fuel for large boilers.
[16]
[17] Accordingly, the present inventors have made extensive efforts to solve the above- described problems occurring in the prior art, and, as a result, prepared a solid carbonized fuel, only using carbonized charcoal powder derived from brigalow biomass, cassava starch, and potassium nitrate as raw materials, and confirmed that the solid carbonized fuel prepared with simple raw material composition shows a high combustion efficiency without producing harmful gases, thereby completing the
present invention. [18] [19] SUMMARY OF THE INVENTION
[20] It is a main object of the present invention to provide a solid carbonized fuel using wood biomass, and a method for preparing the same. [21] [22] It is another object of the present invention to provide a solid carbonized fuel containing charcoal derived from wood biomass, cassava starch and potassium nitrate. [23] To achieve the above object, the present invention provides a method for preparing a solid carbonized fuel using wood biomass, which comprises the steps of: (a) preparing charcoal powder by carbonizing wood biomass; (b) preparing a mold by mixing 8-17 parts by weight of cassava starch and 1-3 parts by weight of potassium nitrate to 100 parts by weight of the charcoal powder and molding them; and (c) drying the mold to obtain a solid carbonized fuel. [24] The present invention also provides a solid carbonized fuel containing charcoal derived from wood biomass, cassava starch and potassium nitrate, which is prepared by the above method. [25] The above and other objects, features and embodiments of the present invention will be more clearly understood from the following detailed description and accompanying claims. [26]
[27] BRIEF DESCRIPTION OF THE DRAWINGS
[28] FIG. 1 is a flow chart showing the preparation process for the solid carbonized fuel using wood biomass according to the present invention. [29] [30] FIG. 2 shows a solid carbonized fuel using wood biomass, which is prepared according to the present invention. [31] [32] DETAILED DESCRIPTION OF THE INVENTION. AND PREF ERRED EM-
BODIMENTS [33] In one aspect, the present invention relates to a method for preparing a solid carbonized fuel using wood biomass, which comprises the steps of: (a) preparing charcoal powder by carbonizing wood biomass; (b) preparing a mold by mixing 8-17 parts by weight of cassava starch and 1-3 parts by weight of potassium nitrate to 100 parts by weight of the charcoal powder and molding them; and (c) drying the mold to obtain a solid carbonized fuel (FIG.l). [34] [35] In the present invention, wood biomass means trees and herbaceous plants containing
lignin and cellulose, and products, waste wood, paper etc. derived therefrom. Thus, it is different from wood which is not processed into products such as paper etc., and is limitlessly available in nature.
[36]
[37] In the present invention, the wood biomass is preferably selected from the group consisting of brigalow, oak, bamboo, rubber tree, maple, coconut tree, and palm tree. In the present invention, heating value of the charcoal powder in the step (a) is preferably 6,500-7,800 kcal/kg.
[38]
[39] Specifically, when wood biomass is carbonized by heating in a carbonizing furnace with no air flow thereinto, water and some volatile components are eliminated and the amount of fixed carbon is increased, so that it is possible to obtain charcoal whose heating value is increased by more than two folds per unit weight, and the thus obtained charcoal is pulverized to prepare charcoal powder, thus using the charcoal powder for the preparation of the inventive solid carbonized fuel.
[40]
[41] The charcoal powder prepared by carbonizing the wood biomass allows the solid fuel to emit heat corresponding to heating value of the charcoal powder by oxidation during combustion, and function as fuel. The charcoal powder is a main component of solid carbonized fuel prepared according to the present invention, and it emits heat corresponding to heating value of the charcoal powder, i.e., 6,500-7,800 kcal by oxidation during combustion, thus functioning as fuel.
[42]
[43] According to an embodiment of the present invention, as wood biomass, brigalow can be used. The brigalow is used for railroad ties, furniture, firewood, etc., and particularly, it emits little smoke and has superior heating power, thus it is highly useful as fuel. Moreover, charcoal prepared using the brigalow contains more volatile components than that of charcoal prepared using other woods, and thus, has fast burning velocity and allows a long-lasting combustion.
[44]
[45] In the present invention, cassava starch functions as a natural binder available in nature, unlike the conventional chemical binders.
[46]
[47] Cassava is a South American dicotyledonous deciduous shrub belonging to the
Spurge family, Euphorbiaceae, which is characterized in that it is a tuberous root spreading widely. It is a tuberous root spreading widely, produces thick root tubers like sweet potato, and contains 20-25% starch. Starch extracted from cassava tubers is called tapioca, and has glutinous property, so that it can be used as an ingredient for
snacks, alcohol, paste and foods.
[48]
[49] In the present invention, cassava starch is prepared by cutting cassava tubers into pieces, drying them, and grinding into a fine powder using a pulverizer, and the cassava starch is mixed with water, and then heated to prepare a cassava starch mixture, thus using the cassava starch mixture as a binder.
[50]
[51] As described above, in addition to the function as a binder allowing a material to congeal by providing viscosity, cassava starch shows a function as an igniting agent for rapid ignition and a function as an adhesive capable of adhering to other materials to help attach them together. Therefore, the cassava starch used in the present invention has the effects of simplifying the constitution of the solid carbonized fuel according to the present invention, as well as enhancing the effectiveness thereof, compared to the conventional solid fuel in which a binder, an igniting agent, an adhesive etc. are separately added upon preparation of solid carbonized fuel.
[52]
[53] Meanwhile, the ignition property of cassava starch is due to high amylose level. The cassava starch has a high amylose concentration and low gelatinization temperature compared to natural starches such as cornstarch, thus reducing heating time in gelatinization process of cassava starch, so that it is possible to increase production due to reduced processing time, and less fuel is consumed for heating.
[54]
[55] In the present invention, if the cassava starch is used in a ratio of less than 8 parts by weight, its viscosity weakens when mixed with charcoal powder, so that the resulting solid carbonized fuel is likely to be broken and its ignition velocity decreases, and if the cassava starch is used in a ratio of more than 17 parts by weight, the added amount of charcoal powder is relatively reduced, so that heating value of solid carbonized fuel is decreased and the solid carbonized fuel ignites suddenly to reduce its stability, resulting in low fuel effectiveness, thus the cassava starch is preferably used in a ratio of 8-17 parts by weight based on 100 parts by weight of charcoal powder.
[56]
[57] Niter is one of nitrate minerals containing KN03 that is used as an oxidant, and in the present invention, it functions as an oxidant upon combustion of solid carbonized fuel, so that it has the effect of allowing the solid carbonized fuel to be easily ignited, and to continuously burn.
[58]
[59] Specifically, the potassium nitrate is one of gunpowder components that has a function of reducing combustion time since it produces oxygen upon combustion to
rapidly react with carbon, resulting in an oxidation reaction, thus causing rapid combustion. That is, potassium nitrate improves the combustion efficiency of fuel to enable complete fuel combustion.
[60]
[61] In the present invention, if the potassium nitrate is used in a ratio of less than 1 part by weight, its function as an oxidant is impaired, and if the potassium nitrate is used in a ratio of more than 3 parts by weight, its function as an oxidant remains the same, thus the potassium nitrate is preferably used in a ratio of 1-3 parts by weight based on 100 parts by weight of charcoal powder.
[62]
[63] Meanwhile, in the present invention, water soluble nitrate in the form of a powder is preferably used such that it is uniformly mixed with the charcoal powder and the cassava starch.
[64]
[65] In the present invention, the molding in the step (b) is preferably compression molding. In the present invention, solid carbonized fuel having a regular shape and homogeneous composition can be prepared by the compression molding.
[66]
[67] In another aspect, the present invention relates to solid carbonized fuel containing charcoal derived from wood biomass, cassava starch and potassium nitrate, which is prepared by the above method (FIG.2).
[68]
[69] In the present invention, heating value of the solid carbonized fuel prepared by using the wood biomass is preferably 6,000~7,300 kcal/kg, and the solid carbonized fuel is preferably used as fuel for a large boiler.
[70]
[71] The solid carbonized fuel prepared according to the present invention has a regular shape and homogeneous composition to show a uniform heating value per unit weight, so that when they are used as fuel for a boiler which can produce electricity and steam, combustion control is easy and an output of the boiler is stabilized, which can reduce operator's burden during boiler operation and facility control efficiency can be improved.
[72]
[73] In addition, an environment-polluting material, nitrogen oxides emitted are mostly thermal NOx, which is highly temperature dependent and thus is formed at the portion of flame close to the burner where high temperature oxidation of atmospheric nitrogen occurs by peak flame temperature, and also produced due to high levels of excess air upon combustion in a boiler facility, the thermal NOx formation increases when the
excess air ratio increases upon combustion or local temperature increase occurs in a combustion chamber. When the solid carbonized fuel according to the present invention is used, a boiler can be operated under low air ratio upon fuel combustion due to constant heating value thereof as described above, and homogeneous temperature distribution can be achieved in a combustion chamber of a boiler, thus making it possible to reduce NOx formation, which is highly temperature dependent and excess-air-dependent.
[74]
[75] Meanwhile, the weight and volume of charcoal powder prepared by carbonizing wood biomass are decreased compared to the wood biomass used for preparation thereof, and thus there is an advantage in that costs for transporting the solid carbonized fuel prepared using the charcoal powder can be greatly reduced. Specifically, the weight percentage of carbonized charcoal powder weight is about 15-25% based on the weight of the wood biomass, and its volume percentage thereof is less than 40% based on the volume of the wood biomass.
[76]
[77] Generally, the water content of wood biomass is 40% before drying, and 20% after drying. When fuel has a high water content, there is a disadvantage in that its weight is increased to incur high transport costs, as well as, thermal efficiency is reduced since 600 kcal per unit weight (kg) of water for evaporating water, are released. In other words, the lower the water content of fuel is, the higher the thermal efficiency of fuel becomes and the higher heating value fuel has.
[78]
[79] In the present invention, heating value of the inventive solid carbonized fuel decreases through the steps of mixing charcoal powder prepared by carbonizing wood biomass having 6,500-7,800 kcal/kg of heating value, and cassava starch, then molding them. Thereafter, water content of the solid carbonized fuel is reduced by drying step to increase heating value thereof again, thus obtaining solid carbonized fuel having 6,000-7,300 kcal/kg of heating value.
[80]
[81] Examples
[82] The present invention will hereinafter be described in further detail by examples.
However, it is to be understood that these examples can be modified into other various forms, and the scope of the present invention is not intended to be limited to such examples.
[83]
[84] Example 1: Preparation of solid carbonized fuel using brigalow. cassava starch, and potassium nitrate
[86] Brigalow was heated at 400~600°C for 22 hours in a carbonizing furnace with no air flow thereinto to eliminate water and volatile components, thus preparing carbonized brigalow charcoal, and then, the resulting charcoal was finely ground to prepare charcoal powder. At this time, heating value of the prepared charcoal was 6,800 kcal/ kg-
[87]
[88] 100kg of the charcoal powder, 12kg of cassava starch obtained by adding water and heating the mixture, and 2kg of potassium nitrate were mixed and then subjected to compression molding to prepare a mold. The mold was dried at 12O0C for 3 hours to prepare cylindrical solid carbonized fuel.
[89]
[90] Comparative Example 1 : Preparation of solid carbonized fuel using brigalow. cornstarch, and potassium nitrate
[91]
[92] Brigalow was heated at 400~600°C for 22 hours in a carbonizing furnace with no air flow thereinto to eliminate water and volatile components, thus preparing carbonized brigalow charcoal, and then, the resulting charcoal was finely ground to prepare charcoal powder. At this time, heating value of the prepared charcoal was 6,800 kcal/ kg-
[93]
[94] 100kg of the charcoal powder, 12kg of cornstarch obtained by adding water and heating the mixture, and 2kg of potassium nitrate were mixed and then subjected to compression molding to prepare a mold. The molded material was dried at 12O0C for 3 hours to prepare cylindrical solid carbonized fuel.
[95]
[96] Comparative Example 2: Preparation of solid carbonized fuel using brigalow and potassium nitrate
[97]
[98] Brigalow was heated at 400~600°C for 22 hours in a carbonizing furnace with no air flow thereinto to eliminate water and volatile components, thus preparing carbonized brigalow charcoal, and then, the resulting charcoal was finely ground to prepare charcoal powder. At this time, heating value of the prepared charcoal was 6,800 kcal/ kg-
[99]
[100] 101kg of the charcoal powder and 13kg of cornstarch obtained by adding water and heating the mixture were mixed and then subjected to compression molding to prepare a mold. The mold was dried at 12O0C for 3 hours to prepare cylindrical solid
carbonized fuel.
[101]
[102] Comparative Example 3: Preparation of solid carbonized fuel using bamboo charcoal, cassava starch and potassium nitrate
[103]
[104] Bamboo was carbonized in a charcoal kiln to prepare bamboo charcoal, and then, the bamboo charcoal was finely pulverized to prepare bamboo charcoal powder. 100kg of the bamboo charcoal powder, 12kg of cassava starch obtained by adding water and heating the mixture, and 2kg of potassium nitrate were mixed and subjected to compression molding to prepare a mold. The resulting mold was dried at 12O0C for 3 hours to prepare cylindrical solid carbonized fuel.
[105]
[106] Experimental example 1 : Comparison between solid carbonized fuels according to the kind of binder
[107]
[108] As a result of comparing efficiencies of solid carbonized fuels prepared in Example 1 and Comparative Example 1, as shown in Table 1, the results showed that heating values of both fuels were similar, but the combustion time of solid carbonized fuel prepared in Example 1 was shorter than that of solid carbonized fuel prepared in Comparative Example 1. The above result was due to the difference between cassava starch and cornstarch which were used as a binder in Example 1 and Comparative Example 1, respectively, suggesting that although both of the cassava starch and the cornstarch are natural binders, in the case of preparing fuel using cassava starch, combustion time is decreased. Specifically, this result is due to difference between the levels of amylose present in the cassava starch and the cornstarch, that is, the cassava starch has high amylose content, so that its gelatinization temperature is low(66°C) and the cornstarch has low amylose content, so that its gelatinization temperature is high(76°C), thus, in a gelatinization process of the cassava starch, heating time is reduced, which results in overall reduction in the combustion time.
[109]
[110] Table 1
[Table 1] [Table ]
[111] [112] Experimental example 2: Comparison between solid carbonized fuels according to whether potassium nitrate is used
[113] As a result of comparing efficiencies of solid carbonized fuels prepared in Example 1 and Comparative Example 2, as shown in Table 1, the results showed that heating values of both fuels were similar, but the combustion time of the solid carbonized fuel prepared in Example 1 was shorter than that of the solid carbonized fuel prepared in Comparative Example 1. This result is due to the absence and presence of potassium nitrate, which suggests that the potassium nitrate functions as an oxidant upon combustion to induce rapid combustion.
[114] [115] Experimental example 3: Comparison between solid carbonized fuels according to the kind of charcoal powder
[116] As a result of comparing efficiencies of solid carbonized fuels prepared in Example 1 and Comparative Example 3, as shown in Table 1, it was observed that they showed similar combustion time, but heating value of solid carbonized fuel prepared in Example 1 was higher than that of solid carbonized fuel prepared in Comparative Example 3. This result is due to difference between the brigalow charcoal powder and bamboo charcoal powder, suggesting that fuel prepared using brigalow charcoal powder has high heating value and thus has high fuel efficiency, and it has high levels of volatile components, and thus has possibility of being used as fuel for equipment like large boiler.
[117]
Industrial Applicability
[118] As described above in detail, according to the present invention, it is possible to prepare an environmentally friendly, solid carbonized fuel which is economical due to the use of wood biomass abundantly available in nature, can be easily prepared due to simple raw material compositions and has high combustion efficiency, as well as, high
heating value per unit weight, and thus the solid carbonized fuel can be used as fuel for a large boiler which can produce electricity and steam.
[119]
[120] While the present invention has been described with reference to the particular illustrative embodiment, it is not to be restricted by the embodiment but only by the appended claims. It is to be appreciated that those skilled in the art can change or modify the embodiment without departing from the scope and spirit of the present invention.
[121]
Claims
[1] A method for preparing a solid carbonized fuel using wood biomass, the method comprises the steps of:
(a) preparing charcoal powder by carbonizing wood biomass;
(b) preparing a mold by mixing 8-17 parts by weight of cassava starch and 1-3 parts by weight of potassium nitrate to 100 parts by weight of the charcoal powder and molding them; and
(c) drying the mold to obtain a solid carbonized fuel.
[2] The method according to claim 1, wherein the wood biomass in the step (a) is selected from the group consisting of brigalow, oak, bamboo, rubber tree, maple, coconut tree, and palm tree. [3] The method according to claim 1, wherein heating value of the charcoal powder in the step (a) is 6,500-7,800 kcal/kg. [4] The method according to claim 1, wherein the molding in the step (b) is compression molding. [5] A solid carbonized fuel containing charcoal derived from wood biomass, cassava starch and potassium nitrate, which is prepared by the method of any one claim among claims 1 to 4. [6] The solid carbonized fuel according to claim 5, wherein heating value thereof is
6,000-7,300 kcal/kg. [7] The solid carbonized fuel according to claim 5, which is fuel for a large boiler.
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CN102796549A (en) * | 2011-05-21 | 2012-11-28 | 邵阳佰龙竹木有限责任公司 | Method for extracting oil and producing environmentally-friendly charcoal by utilizing from fir, camphor and cypress chips |
CN108277055A (en) * | 2018-03-05 | 2018-07-13 | 农业部规划设计研究院 | A kind of biomass charcoal powder densification briquetting fuel preparation method |
CN109111971A (en) * | 2017-06-23 | 2019-01-01 | 江苏元方缘新能源有限公司 | A kind of coke-removing agent and preparation method thereof being used to prepare biomass granule fuel |
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CN108277055A (en) * | 2018-03-05 | 2018-07-13 | 农业部规划设计研究院 | A kind of biomass charcoal powder densification briquetting fuel preparation method |
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