[go: up one dir, main page]

WO2018135660A1 - Procédé et système de production de combustible solide, et combustible solide - Google Patents

Procédé et système de production de combustible solide, et combustible solide Download PDF

Info

Publication number
WO2018135660A1
WO2018135660A1 PCT/JP2018/001811 JP2018001811W WO2018135660A1 WO 2018135660 A1 WO2018135660 A1 WO 2018135660A1 JP 2018001811 W JP2018001811 W JP 2018001811W WO 2018135660 A1 WO2018135660 A1 WO 2018135660A1
Authority
WO
WIPO (PCT)
Prior art keywords
oil
solid
biomass
solid fuel
pieces
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Ceased
Application number
PCT/JP2018/001811
Other languages
English (en)
Japanese (ja)
Inventor
修蔵 福留
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Wind-Smile
WIND-SMILE Co Ltd
Original Assignee
Wind-Smile
WIND-SMILE Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Wind-Smile, WIND-SMILE Co Ltd filed Critical Wind-Smile
Priority to CN201880002309.0A priority Critical patent/CN109312243A/zh
Priority to JP2018548020A priority patent/JP6462971B2/ja
Publication of WO2018135660A1 publication Critical patent/WO2018135660A1/fr
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

Links

Images

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 OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • 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 disclosure relates to solid fuel production methods and systems, and solid fuels.
  • Biomass fuel is one of the renewable energy sources.
  • a biomass fuel a solid fuel produced by mixing a wood material and oil is known (see Patent Document 1).
  • a heated oil is sprayed onto a piece of solid biomass, and a spraying step of permeating the oil into the piece of solid biomass, and compression molding of the piece of solid biomass into which the oil has penetrated
  • a method of producing a solid fuel comprising the steps of: forming a solid fuel.
  • Solid fuel can be produced.
  • parameters such as spray amount / spray speed / spray time
  • the amount of oil penetration can be appropriately adjusted to produce a solid fuel. Therefore, according to the solid fuel manufacturing method according to one aspect of the present disclosure, it is possible to manufacture an appropriate solid fuel.
  • the method of producing a solid fuel may include the step of producing solid pieces of biomass by grinding solid biomass before the spraying step.
  • the method of producing a solid fuel may include the step of drying solid biomass before the spraying step.
  • drying helps to improve oil permeability and control oil penetration.
  • the solid biomass may be dried to a water content ratio corresponding to the target permeation amount of oil in the spraying step.
  • the drying step may include the step of lowering the target water content ratio as the target permeation amount increases, and drying the solid biomass until the target water content ratio is reached.
  • the spraying step may include moving the pieces of solid biomass to change the arrangement of pieces of solid biomass.
  • the spraying step may include spraying the heated oil on the moved solid biomass pieces to infiltrate the oil into the solid biomass pieces.
  • the spraying step may include a step of spraying the heated oil while agitating the solid biomass pieces to allow the oil to permeate the solid biomass pieces. According to the oil spray accompanied by stirring, the oil can be uniformly permeated into the pieces of solid biomass.
  • a method of producing a solid fuel may include the step of adding to the solid biomass a promoter that promotes the penetration of oil into the solid biomass.
  • promoters may include surfactants. The promoter helps to improve the permeability of the oil in the spraying process.
  • the method of producing a solid fuel may further include the step of adding a resin to the oil impregnated solid biomass pieces.
  • the forming step may include the step of producing a solid fuel by compression-molding a piece of solid biomass to which a resin is added.
  • the resin helps maintain the shape of the solid fuel after compression molding.
  • the resin may be a resin having a melting point that is solid without melting when stored and transported in solid fuel.
  • the spraying step may include the step of controlling the penetration of oil into solid biomass by controlling the spraying of oil.
  • the forming step may include the step of producing a solid fuel by compacting solid biomass in which the permeation amount of oil is controlled.
  • the spraying step may include the step of controlling the permeation amount of oil in the solid biomass so that the combustion temperature of the solid fuel falls within the range of 1000 ° C. to 1200 ° C.
  • Small scale biomass boilers assume combustion temperatures of about 1000 ° C to 1200 ° C. Therefore, according to the method for producing a solid fuel including the above-mentioned spraying step, a solid fuel usable in a small scale biomass boiler can be produced.
  • the above-mentioned solid biomass may be plant biomass.
  • Plant-based biomass includes at least one of wood-based biomass and non-wood-based biomass.
  • woody biomass include forest residues and lumber scraps.
  • non-woody biomass include rice husk and coconut husk.
  • the oil may be, for example, a vegetable oil such as palm oil or coconut oil.
  • the spraying step may include the step of controlling the penetration amount of the vegetable oil to the vegetable biomass so that the content of the vegetable oil in the vegetable biomass falls within the range of 5% by weight to 35% by weight.
  • the spraying step may include a step of controlling the penetration amount of the vegetable oil to the vegetable biomass so that the weight ratio of the vegetable oil to the vegetable biomass is 30% or less.
  • oil in the spraying step, oil may be sprayed onto the pieces of solid biomass so that the spray amount increases as the moisture content ratio of the solid biomass decreases.
  • a heated apparatus is sprayed on a solid biomass segment to spray the oil into the solid biomass segment, and compression molding is performed on the oil-impregnated solid biomass segment.
  • a solid fuel production system comprising: a forming device for producing solid fuel.
  • the solid fuel production system may be configured to produce solid fuel by any of the production methods described above.
  • a solid fuel comprising a piece of solid biomass and an oil infiltrated into the piece of solid biomass.
  • the solid fuel may be a compression-molded body of oil impregnated solid biomass pieces.
  • the permeation amount of oil in solid biomass may be such that the combustion temperature of solid fuel falls within the range of 1000 ° C. to 1200 ° C.
  • a solid fuel comprising a segment of plant-based biomass containing at least one of woody and non-wood-based and a vegetable oil infiltrated into the segment of plant-based biomass .
  • the solid fuel may be a compression-molded body of plant biomass fragments into which vegetable oil has penetrated.
  • the vegetable oil content in the vegetable biomass may be in the range of 5% by weight to 35% by weight.
  • a solid fuel having a weight ratio of vegetable oil to vegetable biomass of 30% or less may be provided.
  • FIG. 1 is a block diagram showing the configuration of a solid fuel production system.
  • FIG. 2 is a flow chart showing a solid fuel production process.
  • FIG. 3 is a diagram illustrating an oil spray configuration for solid biomass.
  • FIG. 4 is an explanatory view of intermittent spraying.
  • 5A and 5B are graphs showing the relationship between weight ratio and calorific value.
  • 6A and 6B are graphs showing the calorific value per unit amount when it is assumed that the combustion body is only oil.
  • FIG. 7 is a view for explaining a modification in which oil is sprayed onto the transport belt.
  • SYMBOLS 1 Solid fuel manufacturing system, 10 ... Drying machine, 20 ... Pulverizer, 30 ... 1st processing apparatus, 31 ... Tank, 32 ... Stirrer, 33 ... Spraying apparatus, 33A, 33B ... Spraying mechanism, 34 ... Heating apparatus , 35: Discharge device, 39: Controller, 40: Second processing device, 50: Pelletizer, 61: Transport belt, 63: Spraying device, 65: Mechanical device.
  • the solid fuel production system 1 includes a dryer 10, a crusher 20, a first processing device 30, a second processing device 40, and a pelletizer 50.
  • This system 1 is configured to produce a solid fuel M3 according to the production process shown in FIG.
  • the dryer 10 is configured to dry the solid biomass M1 input as a fuel source. Drying may be performed, for example, using warm air.
  • the solid biomass M1 is dried by the dryer 10 to a target water content ratio, for example, a water content ratio of 5%.
  • the solid biomass M1 input to the dryer 10 is a plant-based biomass including at least one of a wood-based biomass and a non-wood-based biomass.
  • woody biomass include forest residues and lumber scraps
  • non-woody biomass include coconut husk and rice husk.
  • the solid biomass M1 may be an aggregate of roughly crushed wood, an aggregate of raw, semi-dried or completely dried vegetables, or rice husk It may be an aggregate of grains such as coconut shell and the like.
  • the solid biomass M1 dried by the dryer 10 is introduced into the grinder 20.
  • the solid biomass M1 which has already been dried to the target water content ratio before being introduced into the dryer 10 can be introduced into the pulverizer 20 without the intervention of the dryer 10.
  • the grinder 20 is configured to grind the input solid biomass M1 to generate pieces of the solid biomass M1.
  • Each of the fragments referred to here may be a part, a piece or a grain of physically, mechanically or chemically degraded solid biomass M1.
  • Generating the pieces of solid biomass M1 may be to generate powder of solid biomass M1.
  • the solid biomass M1 is pulverized using the pulverizer 20.
  • the solid biomass M1 is crushed, fragmented, or pulverized into pieces of about 5 mm or less in order to uniformly permeate the oil M2 into the pieces of the crushed solid biomass M1. Is preferred.
  • the pieces of solid biomass M1 generated through drying and grinding are introduced into the first processing device 30.
  • solid biomass M1 may be ground in the first step (S1) of the manufacturing process and then dried in the second step (S2).
  • the first processing apparatus 30 is configured to spray the heated oil M2 on the segment of the input solid biomass M1 to permeate the oil M2 into the segment of the solid biomass M1.
  • the first treatment device 30 performs a process of spraying the heated oil M2 onto the pieces of solid biomass M1 and permeating the oil M2 into the pieces of solid biomass M1 .
  • the third step (S3) includes a process of spraying oil M2 while stirring a piece of solid biomass M1 and a process of controlling the permeation amount of oil M2 in solid biomass M1. Agitation of the pieces of solid biomass M1 corresponds to moving so that the arrangement of pieces of solid biomass M1 changes, and contributes to the permeation of the equivalent oil M2 into the pieces of solid biomass M1.
  • the first processing device 30 includes a tank 31, a stirrer 32, a spraying device 33, a heating device 34, a discharging device 35, and a controller 39.
  • the pieces of the solid biomass M ⁇ b> 1 input to the first treatment device 30 are accommodated in the tank 31.
  • the agitator 32 is configured to agitate the fragments of the solid biomass M ⁇ b> 1 stored in the tank 31 in the tank 31.
  • the misty oil M2 is sprayed from the spraying device 33 to the solid biomass M1.
  • the oil M2 to be sprayed is a vegetable oil. Examples of vegetable oils include palm oil, coconut oil and vegetable oils.
  • the oil M2 may be a combination of multiple types of vegetable oils.
  • the spraying device 33 is configured to spray the oil M2 heated by the heating device 34 onto the fragments of the solid biomass M1 stirred in the tank 31, as shown in FIG.
  • the heating device 34 is configured to provide the spray device 33 with the oil M2 heated to the set temperature.
  • the set temperature is not limited, but is, for example, a temperature of 65 ° C. to 200 ° C.
  • the spray amount of oil M2 may be adjusted according to the amount of solid biomass M1 receiving oil M2.
  • the spraying amount may be further adjusted according to the water content ratio of the solid biomass M1.
  • the oil M2 may be sprayed continuously or intermittently to the stirred solid biomass M1.
  • the oil M2 may be sprayed periodically, for example, at intervals of 3 to 5 seconds.
  • the spraying device 33 is controlled so that the operation of injecting the oil M2 and the operation of temporarily stopping the injection are alternately performed.
  • the pieces of the solid biomass M1 in which the oil M2 has penetrated in the tank 31 by spraying are discharged from the tank 31 by the discharge device 35 and are introduced into the second processing device 40.
  • the controller 39 of the first processing device 30 is configured to control the agitator 32, the spray device 33, the heating device 34, and the discharge device 35. Specifically, the controller 39 controls the agitator 32, the spray device 33, the heating device 34, and the discharge device 35 so that the combustion temperature at the time of power generation of the solid fuel M3 (pellet) manufactured becomes the target temperature range. Control. This control includes control of the spraying time and the spraying amount per unit time of the oil M2, and the stirring time and speed.
  • the amount of oil M2 in the solid biomass M1 may be controlled.
  • the controller 39 controls the spraying time and the spraying amount per unit time of the oil M2 and the stirring time and speed so that the permeation amount of the oil M2 in the solid biomass M1 corresponds to the target temperature range. Can.
  • the heat-resistant temperature of the furnace which a small scale biomass boiler has is less than 2000 ° C. Therefore, the combustion temperature of the solid fuel M3 is preferably in the range of 1000 ° C. to 1200 ° C. Therefore, in the third step (S3), the permeation amount of the oil M2 in the solid biomass M1 can be controlled, for example, so that the combustion temperature of the solid fuel M3 falls within the range of 1000 ° C to 1200 ° C.
  • the first treatment device 30 controls the spraying of the oil M2 to penetrate the solid biomass M1 into pieces of the solid biomass M1 when the amount of the oil M2 corresponding to the target temperature range permeates into the pieces of the solid biomass M1.
  • the pieces are discharged, and the pieces of the solid biomass M1 after oil penetration are introduced into the second processing device 40.
  • the second processing apparatus 40 is configured to add and discharge a resin to the piece of solid biomass M1 input from the first processing apparatus 30.
  • the second processing device 40 performs a process of adding a resin to the segment of the solid biomass M1 in which the oil M2 has permeated.
  • the resin added to the solid biomass M1 piece functions as a shape-retaining agent and an adhesive when pelletizing the solid biomass M1 piece.
  • a resin having a melting point of 60 ° C. or higher can be used so that the resin does not melt during storage and transportation.
  • vegetable resin especially vegetable resin containing cellulose can be used as resin added to the piece of solid biomass M1.
  • the second processing apparatus 40 can add the resin so as to cover the surface of the solid biomass M1 piece into which the oil M2 has penetrated by stirring the melted resin and the solid biomass M1 piece.
  • the second processing apparatus 40 is configured to supply the pellet of the solid biomass M1 to which the resin is added to the pelletizer 50.
  • the pelletizer 50 is configured to pelletize the pieces of the solid biomass M1 to which the above-described resin supplied from the second processing apparatus 40 is added by compression molding, specifically by extrusion.
  • the pieces of the solid biomass M1 to which the oil M2 penetrates and the resin is applied are pelletized by compression molding to produce a solid fuel M3.
  • the pellet which is a compression molded body of the piece of solid biomass M1 generated by the pelletizer 50 is discharged as solid fuel M3 and stored in a storage bag or box.
  • the solid fuel M3 produced by the solid fuel production system 1 is a compression molded body of a solid biomass M1 piece to which the oil M2 penetrates and the resin is applied.
  • the solid fuel M3 is configured as a compact of plant-based biomass into which a vegetable oil has penetrated.
  • the solid fuel M3 composed of plant biomass and plant oil is effective as a renewable energy source because the whole is biomass.
  • the energy generated by the fuel of this solid fuel M3 is used, for example, for power generation.
  • the solid fuel M3 combustible within the temperature range in which the existing small-scale biomass boiler has resistance is controlled by controlling the penetration amount of the oil M2, and the calorific value per weight is high. It is possible to produce a solid fuel M3 that can realize efficient power generation.
  • the electric energy generated by the power generation can be sold in Japan using a fixed price purchase system of renewable energy. Therefore, according to the present embodiment, it is possible to provide a solid fuel production system 1 and a solid fuel M3 that help to spread renewable energy.
  • the solid fuel M3 is preferably produced so that the vegetable oil content as the oil M2 is in the range of 5% by weight to 35% by weight.
  • Such solid fuel M3 can be used for small-scale biomass boilers because the combustion temperature is in the range of 1000 ° C. to 1200 ° C.
  • solid fuel M3 is such that the weight ratio of oil M2 to solid biomass M1 is 30% or less within the range that satisfies the required heat value. It is preferable to be manufactured.
  • 5A and 5B graphically show the relationship between the weight ratio k of the oil M2 to the solid biomass M1 in the solid fuel M3 and the calorific value Y per unit amount of the solid fuel M3.
  • the calorific value Y is expressed by the following equation.
  • ⁇ is a multiplication symbol and “/” is a division symbol.
  • Q1 is the calorific value per unit weight of the solid biomass M1
  • Q2 is the calorific value per unit weight of the oil M2.
  • W1 is the weight of solid biomass M1 contained in solid fuel M3
  • W2 is the weight of oil M2 contained in solid fuel M3.
  • a digital calorimeter specifically, Ogawa Sampling Corporation O. S. K 200 was used.
  • FIG. 6A and FIG. 6B show the calorific value Z when assuming that the above-mentioned sample consists only of oil M2, on a graph having a horizontal axis of weight ratio k.
  • the calorific value Z is expressed by the following equation.
  • the calorific value Z of the time is shown.
  • the circular points shown in FIG. 6A indicate the calorific value Z when the calorific value Y corresponding to the circular point shown in FIG. 5A is converted according to the above conversion formula.
  • the circular points shown in FIG. 6B indicate the calorific value Z when the calorific value Y corresponding to the circular point shown in FIG. 5B is converted according to the above conversion formula.
  • the above graph shows an example where the oil M2 is coconut oil and vegetable oil.
  • palm oil or other vegetable oil may be used as the oil M2, and in this case also, for the same reason, the solid fuel M3 has a weight ratio of the oil M2 to the solid biomass M1 of 30% or less. Preferably it is manufactured.
  • a high calorific value is required for the solid fuel M3, it is particularly advantageous to use at least one of palm oil and coconut oil having a high calorific value as the oil M2.
  • solid fuel production system 1 and production method of the present embodiment and the solid fuel M3 using biomass have been described above, but the present disclosure is not limited to the above embodiment, and various aspects may be taken. it can.
  • the solid biomass M1 in the drying step (S1) of the solid biomass M1, can be dried to a water content ratio according to the target permeation amount of the oil M2 with respect to the solid biomass M1. That is, in the first step (S1), as the target permeation amount of the oil M2 increases, the target water content ratio can be lowered to dry the solid biomass M1 until the target water content ratio is reached. According to the drying step (S1), as the target permeation amount increases, the solid biomass M1 is dried well, and the oil permeability in the solid biomass M1 is increased. Therefore, the processing efficiency in the first processing apparatus 30 is enhanced.
  • the amount of spraying of oil M2 in a spraying process may be adjusted according to the quantity of solid biomass M1 of spraying object, and the moisture content of solid biomass M1.
  • the spray amount may be adjusted to a larger amount as the water content ratio is smaller (the solid biomass M1 is more dry). In other words, the spray amount can be adjusted to a smaller amount as the water content ratio is larger.
  • Information on the water content ratio may be input to the controller 39 of the first processing apparatus 30 by the operation of the worker, or may be input to the controller 39 from a sensor capable of detecting the water content ratio of the solid biomass M1.
  • a sensor may be provided, for example, in the dryer 10 and / or the first processing device 30.
  • the water content ratio may be estimated from the weight per volume of solid biomass M1.
  • the first treatment device 30 may be configured to add an accelerator that promotes the penetration of the oil M2 to the solid biomass M1 simultaneously with the spraying of the oil M2 and / or before and after the spraying of the oil M2.
  • the spray device 33 may be configured to include the spray mechanism 33A of the oil M2 and the spray mechanism 33B of the promoter.
  • promoters include surfactants.
  • the addition of the promoter increases the permeability (penetration rate) of the oil, and the solid biomass M1 can be efficiently permeated with the oil M2 to the target permeation amount.
  • the oil M2 penetrated by the solid biomass M1 may be a non-vegetable oil.
  • the solid biomass M1 may be impregnated at least in part with an oil that does not correspond to a renewable energy source.
  • the control of the penetration amount of oil M2 is not limited to the control for realizing the above-mentioned fuel temperature or the content of oil M2.
  • the pieces of solid biomass M1 generated by grinding may be disposed on the conveyance belt 61 shown in FIG. 7, and the elements of the solid biomass M1 on the conveyance belt 61 may be disposed between the start point and the end point of the conveyance belt 61.
  • a plurality of spraying devices 63 that spray oil M2 from above onto the piece may be provided along the transport belt 61.
  • the spraying device 63 can receive the supply of the heated oil M2 from the heating device 34.
  • a plurality of mechanical devices 65 alternately arranged with the spraying device 63 change the arrangement of the pieces of solid biomass M1 and spray oil M2 uniformly on the pieces of solid biomass M1. It may be provided to
  • the mechanical device 65 applies mechanical action to the pieces of the solid biomass M1 so that the orientation and position of each front and back of the pieces on the transport belt 61 change at random, similarly to the stirrer 32. it can.
  • the mechanical device 65 may be a device that applies vibration to the transport belt 61 so that the pieces on the transport belt 61 are turned over, or may be configured to incline the transport belt 61.
  • the transport belt 61 may be configured to have a height difference. In this case, the piece of the solid biomass M1 transported by the transport belt 61 may change in position due to the height difference.
  • the transport belt 61, the spray device 63 and the mechanical device 65 may be provided in the first processing device 30 instead of the tank 31, the spray device 33 and the stirrer 32.
  • the transport belt 61, the spray device 63 and the mechanical device 65 may be provided instead of the discharge device 35.
  • the transport belt 61 may be configured to transport the pieces of the solid biomass M1 to the second processing device 40.
  • spraying of the solid biomass M1 into the oil M2 may be performed under a low pressure environment in order to promote the penetration of the oil M2 into the solid biomass M1.
  • the pressure acting on the infiltrated solid biomass M1 of the oil M2 is increased by eliminating the low pressure environment, and it is conceivable that the oil M2 penetrates further into the solid biomass M1.
  • the oil M2 may be encapsulated with a resin or the like so that the oil M2 is not sticky on the surface of the solid biomass M1.
  • the functions of one component in the above embodiment may be distributed to a plurality of components.
  • the functions of multiple components may be integrated into one component.
  • a part of the configuration of the above embodiment may be omitted.
  • At least a part of the configuration of the above embodiment may be added to or replaced with the configuration of the other above embodiments.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Solid Fuels And Fuel-Associated Substances (AREA)

Abstract

Selon un mode de réalisation, la présente invention concerne un procédé de production d'un combustible solide comprenant : une étape de pulvérisation où une huile chauffée est pulvérisée sur des fragments de biomasse solide de façon à imprégner d'huile lesdits fragments de biomasse solides ; et une étape de moulage où les fragments de biomasse solides imprégnés d'huile sont soumis à un moulage par compactage pour obtenir un combustible solide.
PCT/JP2018/001811 2017-01-23 2018-01-22 Procédé et système de production de combustible solide, et combustible solide Ceased WO2018135660A1 (fr)

Priority Applications (2)

Application Number Priority Date Filing Date Title
CN201880002309.0A CN109312243A (zh) 2017-01-23 2018-01-22 固体燃料的制造方法、固体燃料制造系统和固体燃料
JP2018548020A JP6462971B2 (ja) 2017-01-23 2018-01-22 固形燃料の製造方法、固形燃料製造システム、及び、固形燃料

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP2017-009573 2017-01-23
JP2017009573 2017-01-23

Publications (1)

Publication Number Publication Date
WO2018135660A1 true WO2018135660A1 (fr) 2018-07-26

Family

ID=62908225

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/JP2018/001811 Ceased WO2018135660A1 (fr) 2017-01-23 2018-01-22 Procédé et système de production de combustible solide, et combustible solide

Country Status (3)

Country Link
JP (1) JP6462971B2 (fr)
CN (1) CN109312243A (fr)
WO (1) WO2018135660A1 (fr)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2025082568A (ja) * 2023-11-17 2025-05-29 有限会社丸源油脂 有機廃棄物燃料の製造方法

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5918794A (ja) * 1982-07-23 1984-01-31 Norihiro Mitsunaga 燃料
JPS59168096A (ja) * 1983-03-15 1984-09-21 Nippon Plant Kiyouriyoku Kk 木質燃料ペレツトおよびその生産方法
JP2002020771A (ja) * 2000-07-05 2002-01-23 Nkk Corp 廃木材の処理方法
JP2007000707A (ja) * 2005-06-21 2007-01-11 Mitsubishi Chemicals Corp 含油固形物およびその製造方法
JP2010121047A (ja) * 2008-11-20 2010-06-03 Assess Corp ペレット燃料の製造方法、およびペレット燃料
JP2013023513A (ja) * 2011-07-15 2013-02-04 Taniguchi Yuhan:Kk バイオマス固形燃料及びその製造方法

Family Cites Families (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2131449C1 (ru) * 1998-06-15 1999-06-10 Лурий Валерий Григорьевич Формованное топливо и способ его получения
KR101386731B1 (ko) * 2006-03-02 2014-04-17 다이헤이요 세멘토 가부시키가이샤 가연성 가스가 휘발하는 물질의 취급 방법
JP4593657B2 (ja) * 2008-07-11 2010-12-08 株式会社クリエイティブ 固体燃料
KR101131270B1 (ko) * 2011-03-30 2012-03-30 전영철 합성수지-펄프제 폐기물을 주재료로 하는 고체연료 제조방법
CN103450961B (zh) * 2013-09-13 2014-12-03 蓬溪县天桥木业有限公司 纯柏木生物质颗粒燃料的制备工艺
CN104946338B (zh) * 2015-06-24 2018-05-29 广州明颂生物质成型燃料有限公司 一种生物燃料及其制备方法
CN105969453A (zh) * 2016-02-17 2016-09-28 蚌埠华东石膏有限公司 一种低氯值生物质成型燃料及其制作方法
CN105885988A (zh) * 2016-05-12 2016-08-24 安徽省珍云生物能源有限公司 一种具有防霉效果的燃料棒及其制作工艺

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5918794A (ja) * 1982-07-23 1984-01-31 Norihiro Mitsunaga 燃料
JPS59168096A (ja) * 1983-03-15 1984-09-21 Nippon Plant Kiyouriyoku Kk 木質燃料ペレツトおよびその生産方法
JP2002020771A (ja) * 2000-07-05 2002-01-23 Nkk Corp 廃木材の処理方法
JP2007000707A (ja) * 2005-06-21 2007-01-11 Mitsubishi Chemicals Corp 含油固形物およびその製造方法
JP2010121047A (ja) * 2008-11-20 2010-06-03 Assess Corp ペレット燃料の製造方法、およびペレット燃料
JP2013023513A (ja) * 2011-07-15 2013-02-04 Taniguchi Yuhan:Kk バイオマス固形燃料及びその製造方法

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2025082568A (ja) * 2023-11-17 2025-05-29 有限会社丸源油脂 有機廃棄物燃料の製造方法

Also Published As

Publication number Publication date
JP6462971B2 (ja) 2019-01-30
JPWO2018135660A1 (ja) 2019-01-24
CN109312243A (zh) 2019-02-05

Similar Documents

Publication Publication Date Title
JP7134127B2 (ja) バイオマス燃料化システム及びバイオマス由来燃料ペレットの製造方法
CA2890687C (fr) Procede et processus de fabrication d'une forme de biomasse torrefiee mecaniquement stable resistant a l'eau
US9557105B2 (en) Method and arrangement for torrefaction with controlled addition of cooling liquid to the torrefied material
JP6302193B2 (ja) 木質ペレット製造用生木の乾燥方法及びこの乾燥方法を適用した乾燥工程を備える木質ペレット製造装置
KR101281672B1 (ko) 하수 슬러지를 이용한 고형 연료의 제조 방법
WO2018135660A1 (fr) Procédé et système de production de combustible solide, et combustible solide
KR101455028B1 (ko) 이동식 축분 펠릿 제조시스템
JP5537614B2 (ja) 廃棄物処理システム
KR101931159B1 (ko) 식물성 오일 부산물을 이용한 화력발전소 및 제철소용 고발열량 바이오매스 성형연료 및 이의 제조방법
JP2004137144A (ja) 多孔性炭素材、それを使った多孔性炭素材粉末、およびそれらの製造方法、ならびにそれら多孔性炭素材粉末を使った多孔性炭素材製品の製造方法
KR20160112129A (ko) 목재부산물을 이용한 연료용 복합펠릿의 제조방법
US10844343B2 (en) Device for the electrical disintegration of cell structures, and installation and use of the device for producing feed intermediates and feed products
JP2014062155A (ja) 乾燥可燃物質の製造方法及び乾燥可燃物質
KR20100109005A (ko) 식물성 부산물을 이용한 친환경 고체연료와 그의 제조방법
JP2018053101A (ja) バイオマス燃料製造方法及びバイオマス燃料製造装置
KR101574653B1 (ko) 향기를 품은 판상의 우드펠릿을 제조하는 방법
KR20080090832A (ko) 연료화 장치 및 연료의 제조 방법
KR101629741B1 (ko) 펠렛 제조장치
JP2019172766A (ja) 燃料ペレットの製造方法
EP2405998A2 (fr) Agrégats frittés de poids léger
JP6283724B2 (ja) 混合燃料の製造方法
Hamid et al. Research Article An Experimental Study of Briquetting Process of Torrefied Rubber Seed Kernel and Palm Oil Shell
JP5595552B2 (ja) 貯蔵乾燥ヤード及びオガ粉又は木質チップの乾燥方法
RU129501U1 (ru) Автономный торфоперерабатывающий комплекс
JP2010270279A (ja) 燃料用ペレット

Legal Events

Date Code Title Description
ENP Entry into the national phase

Ref document number: 2018548020

Country of ref document: JP

Kind code of ref document: A

121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 18741483

Country of ref document: EP

Kind code of ref document: A1

NENP Non-entry into the national phase

Ref country code: DE

122 Ep: pct application non-entry in european phase

Ref document number: 18741483

Country of ref document: EP

Kind code of ref document: A1