WO2011155667A1 - Dispositif de fabrication de combustible solide à l'aide d'un mélange de déchets marins et déchets combustibles comme matière première - Google Patents
Dispositif de fabrication de combustible solide à l'aide d'un mélange de déchets marins et déchets combustibles comme matière première Download PDFInfo
- Publication number
- WO2011155667A1 WO2011155667A1 PCT/KR2010/006166 KR2010006166W WO2011155667A1 WO 2011155667 A1 WO2011155667 A1 WO 2011155667A1 KR 2010006166 W KR2010006166 W KR 2010006166W WO 2011155667 A1 WO2011155667 A1 WO 2011155667A1
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- WIPO (PCT)
- Prior art keywords
- waste
- marine
- marine waste
- solid fuel
- combustible
- Prior art date
Links
- 239000002699 waste material Substances 0.000 title claims abstract description 138
- 239000004449 solid propellant Substances 0.000 title claims abstract description 35
- 239000010849 combustible waste Substances 0.000 title claims abstract description 31
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 29
- 239000000203 mixture Substances 0.000 title claims abstract description 14
- 239000002994 raw material Substances 0.000 title claims abstract description 13
- 238000002156 mixing Methods 0.000 claims abstract description 27
- 230000018044 dehydration Effects 0.000 claims description 50
- 238000006297 dehydration reaction Methods 0.000 claims description 50
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 40
- 238000010612 desalination reaction Methods 0.000 claims description 28
- 238000000034 method Methods 0.000 claims description 27
- 238000005406 washing Methods 0.000 claims description 21
- 238000005520 cutting process Methods 0.000 claims description 14
- 238000003825 pressing Methods 0.000 claims description 9
- 238000002788 crimping Methods 0.000 claims description 4
- 238000011033 desalting Methods 0.000 claims description 3
- 238000000227 grinding Methods 0.000 abstract description 7
- 238000000465 moulding Methods 0.000 abstract description 6
- 238000001125 extrusion Methods 0.000 abstract description 5
- 238000012545 processing Methods 0.000 abstract description 3
- 238000003860 storage Methods 0.000 abstract description 3
- 208000005156 Dehydration Diseases 0.000 description 44
- 150000003839 salts Chemical class 0.000 description 12
- 238000007906 compression Methods 0.000 description 11
- 230000006835 compression Effects 0.000 description 8
- 238000010586 diagram Methods 0.000 description 8
- 238000000746 purification Methods 0.000 description 8
- 239000010802 sludge Substances 0.000 description 7
- 238000010298 pulverizing process Methods 0.000 description 6
- 238000001035 drying Methods 0.000 description 5
- 229920003023 plastic Polymers 0.000 description 5
- 239000004033 plastic Substances 0.000 description 5
- 238000002485 combustion reaction Methods 0.000 description 4
- 239000000446 fuel Substances 0.000 description 4
- 238000010438 heat treatment Methods 0.000 description 4
- 238000002844 melting Methods 0.000 description 4
- 230000008018 melting Effects 0.000 description 4
- 238000004064 recycling Methods 0.000 description 4
- 239000000654 additive Substances 0.000 description 3
- 239000003795 chemical substances by application Substances 0.000 description 3
- 238000011161 development Methods 0.000 description 3
- 239000010794 food waste Substances 0.000 description 3
- 230000003472 neutralizing effect Effects 0.000 description 3
- 239000008188 pellet Substances 0.000 description 3
- 239000002893 slag Substances 0.000 description 3
- 238000012546 transfer Methods 0.000 description 3
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 2
- 235000011941 Tilia x europaea Nutrition 0.000 description 2
- 230000000996 additive effect Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 239000002440 industrial waste Substances 0.000 description 2
- 239000004571 lime Substances 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 238000011160 research Methods 0.000 description 2
- 239000013535 sea water Substances 0.000 description 2
- 239000010801 sewage sludge Substances 0.000 description 2
- 229920003002 synthetic resin Polymers 0.000 description 2
- 239000000057 synthetic resin Substances 0.000 description 2
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 description 2
- 229920002554 vinyl polymer Polymers 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- 241000258957 Asteroidea Species 0.000 description 1
- 241000237519 Bivalvia Species 0.000 description 1
- 241000238366 Cephalopoda Species 0.000 description 1
- 241000237502 Ostreidae Species 0.000 description 1
- 229920002472 Starch Polymers 0.000 description 1
- 238000009360 aquaculture Methods 0.000 description 1
- 244000144974 aquaculture Species 0.000 description 1
- 239000002956 ash Substances 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 239000012267 brine Substances 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 235000020639 clam Nutrition 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000000701 coagulant Substances 0.000 description 1
- 238000000748 compression moulding Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000006837 decompression Effects 0.000 description 1
- 230000000593 degrading effect Effects 0.000 description 1
- 238000005115 demineralization Methods 0.000 description 1
- 230000002328 demineralizing effect Effects 0.000 description 1
- 239000010791 domestic waste Substances 0.000 description 1
- 238000005108 dry cleaning Methods 0.000 description 1
- 238000010981 drying operation Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 239000000295 fuel oil Substances 0.000 description 1
- 239000003673 groundwater Substances 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 230000001771 impaired effect Effects 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000006263 metalation reaction Methods 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 235000020636 oyster Nutrition 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000002203 pretreatment Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 235000015170 shellfish Nutrition 0.000 description 1
- 230000035939 shock Effects 0.000 description 1
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 235000019698 starch Nutrition 0.000 description 1
- 239000008107 starch Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
- 239000010920 waste tyre Substances 0.000 description 1
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, 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
- C10L5/46—Solid fuels essentially based on materials of non-mineral origin on sewage, house, or town refuse
-
- 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
- B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B30—PRESSES
- B30B—PRESSES IN GENERAL
- B30B11/00—Presses specially adapted for forming shaped articles from material in particulate or plastic state, e.g. briquetting presses, tabletting presses
- B30B11/22—Extrusion presses; Dies therefor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B30—PRESSES
- B30B—PRESSES IN GENERAL
- B30B15/00—Details of, or accessories for, presses; Auxiliary measures in connection with pressing
- B30B15/30—Feeding material to presses
- B30B15/302—Feeding material in particulate or plastic state to moulding presses
- B30B15/308—Feeding material in particulate or plastic state to moulding presses in a continuous manner, e.g. for roller presses, screw extrusion presses
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
- B09B2101/00—Type of solid waste
- B09B2101/02—Gases or liquids enclosed in discarded articles, e.g. aerosol cans or cooling systems of refrigerators
-
- 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
- C10L2290/00—Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
- C10L2290/08—Drying or removing water
-
- 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 solid fuel manufacturing apparatus using a mixture of marine waste and combustible waste as a raw material, and more specifically, marine waste for producing solid fuel by desalination, dehydration, and compression with combustible waste by pulverizing and mixing the marine waste.
- RDF solidified fuel
- Various manufacturing methods and manufacturing apparatuses are known.
- wastes such as various plastic wastes and stagnation fishing nets made of synthetic plastic fibers pollute the marine ecosystem, and in the past, these marine wastes were collected and incinerated or landfilled. Efforts and researches are being conducted to recycle these resources into resources.
- marine wastes contain salts by seawater. If this is not removed, moldability is impaired by polymer oxidation due to salts and cracks occur in solid fuels produced after extrusion. There is a problem such as desalination work for the removal of salt is required.
- Another method is to dissolve marine waste in the combustion melting chamber and recycle molten slag to recycled solids.
- This recycling method uses waste combustion furnaces as in Korean Patent Application Publication No. 10-2008-0030744. The molten slag that can be recycled by melting it at a high temperature with a burner can be obtained.
- a method of drying and incinerating sludge having high moisture content and condensing water vapor by condensing water vapor generated in the drying process is used to produce clean water vapor, which method is as in Korean Patent Laid-Open No. 10-2006-0129144.
- Fuel oil having a boiling point higher than water is mixed with sludge to incinerate the sludge for rapid and continuous heat transfer.
- the steam generated through this is recovered as condensate from the condenser and clean steam from the steam generator.
- the marine waste has a very high moisture content, unlike general waste treatment, which requires considerable time and cost in dehydration and drying operations in the combustion process, thereby degrading the economy and productivity of solid fuel.
- the waste with high water content is reduced by forced drying and dehydration using heating or dehydrator, or dehydration treatment of flocculated sludge using deaerator with dehydrator.
- heating, dehydration, and drying methods include heating and dehydration.
- the amount of calories required for wastewater is higher than the amount of heat recovered from waste, which is not only economical but also takes much time when using flocculant.
- Korean Patent Publication No. 10-2005-0112931 discloses a pretreatment process for treating sewage sludge and waste plastic, and mixing and melting the waste sewage sludge and waste plastic after the pretreatment process to pellet the pellets.
- a process for treating impurities such as steam and dust generated in a mixed mixer process to be formed, a cooling process of granulated pellets, a pretreatment process, and a mixed mixer process is disclosed.
- Republic of Korea Patent Publication No. 10-0595026 is equipped with a complex treatment system consisting of a pre-treatment system, a resource system, such as a system suitable for the limited size of the vessel and stable management in the future so that marine waste can be directly processed in the vessel to transport marine waste
- a resource system such as a system suitable for the limited size of the vessel and stable management in the future so that marine waste can be directly processed in the vessel to transport marine waste
- an automation system that can handle all processes such as resource, resource management, and land transportation.
- Korean Laid-Open Patent Publication No. 10-2003-0075045 discloses groundwater of soft soil by mixing marine fishery wastes such as aquaculture wastes, shellfish (cocktails, oysters, clams, etc.), industrial wastes such as by-products of thermal power plants, and lime.
- a technique for manufacturing an improved solidified fire is disclosed, and
- Korean Laid-Open Patent Publication No. 10-2003-0050529 uses waste sludge, starfish and aquatic waste sludge generated from aquatic product processing plants such as squid thaw to remove heavy metals from coastal regions. The technique to remove is published.
- Korean Patent Publication No. 10-2005-0109055 discloses a cutting machine for pre-cutting waste fishing nets to a predetermined size, a washing apparatus for washing the cut waste fishing nets to remove foreign substances from salt, and cutting the cut waste fishing nets in a centrifuge to make them smaller.
- a waste fishing net recycling device consisting of a centrifuge for removing both salt and water, an extruder for heating and extruding the waste fishing net through the centrifuge to a high temperature, a cutter for cutting the extruded rod-shaped material to a certain size
- the device requires a lot of energy to remove the salt by using a cleaning device consisting of dry cleaning to remove the salt, there is a problem such that the washing process and dehydration process is carried out separately, which takes a lot of time and manpower in the treatment process .
- combustible waste refers to combustible regardless of the general waste and industrial waste among the waste generated by various activities of human being, the following briefly look at the production of solid fuel using the combustible waste.
- Korean Patent Laid-Open Publication No. 10-1998-67783 discloses that food waste is cooked by separating food waste into starch raw materials and other raw materials. Discuss how to make solid fuel.
- Korean Unexamined Patent Publication No. 10-2000-015759 discloses a method for producing a solid fuel in which food waste is mixed with wastewater sludge cake and combustible waste (waste tire, waste vinyl) powder and put into a molding machine.
- Korean Patent Laid-Open Publication No. 10-2003-25985 discloses a method for producing solid fuel by pulverizing flammable waste, adding calcined lime and extruding and molding in a molding machine, and in Korean Patent Publication No. 10-2002-059074 Disclosed is a method of drying waste and compressing it at high temperature to fuel it, and Publication No. 10-2002-075763 discloses adding a coagulant to a pulverized chip, pulverizing the waste, and then extruding and molding. The method for producing a solid fuel is disclosed.
- salts having high salinity and moisture content due to brine are efficiently desalted and dehydrated and compressed, and the desalted, dehydrated and compressed marine waste is mixed with combustible wastes such as waste vinyl and waste plastic to produce solid fuel.
- combustible wastes such as waste vinyl and waste plastic
- the present invention In the construction of a solid fuel production apparatus using a mixture of marine waste and combustible waste as a raw material, Desalination dehydration apparatus for desalination, dehydration of marine waste; A crimping device for crimping the desalted and dehydrated marine waste; A grinding / mixing device for grinding and mixing the compressed marine waste with flammable waste; It consists of an extruder for extruding a mixture of marine waste and combustible waste.
- the present invention can reduce the processing cost of marine waste transportation, storage, etc. by desalting, dehydrating, compressing and reducing the volume of marine waste containing a large amount of salt by stagnation in sea water for a long time through a series of processes.
- it is possible to supply high quality solid fuel by producing solid fuel more efficiently by mixing desalted, dehydrated and compressed marine waste with combustible waste.
- FIG. 1 is an overall configuration diagram of a solid fuel production apparatus according to the present invention.
- FIG. 2 is a block diagram of the desalination apparatus in the present invention.
- FIG. 3 is a block diagram of a dehydration tank in the present invention.
- FIG. 4 is a block diagram of a compactor in the present invention.
- FIG. 1 is an overall configuration diagram of a solid fuel production apparatus according to the present invention
- Figure 2 is a configuration diagram of the dehydration apparatus in the present invention
- Figure 3 is a configuration diagram of the dehydration tank in the present invention
- Figure 4 is a configuration diagram of the compactor in the present invention .
- the present invention consists of a desalination dehydration apparatus (1), a pressing apparatus (3), a crushing and mixing apparatus (4), an extrusion molding machine (5), and a cutting machine (6) according to the solid fuel manufacturing step.
- the desalination dehydration device 1 will be intensively mentioned.
- the demineralization dehydration apparatus 1 opens the upper part of the dehydration tank 11 in which the washing water is filled to form an inlet 12 for injecting marine waste, and rotates the marine waste at the bottom to contact the washing water and The waste is rubbed together to form an impeller 13 to perform desalination and dehydration.
- Impeller 13 has a rotary blade 14 is formed on the rotary shaft to wash the marine waste with contact water and shock waves and at the same time rub off the marine waste to each other to wash the salt contained in the marine waste to be desalted.
- a drain port 16 is formed below the dehydration tank 11 in which the impeller 13 is installed, and a valve 16a is installed at the drain port 16 to connect with the water purification tank 7.
- the water purification tank 7 is connected to the inlet 72 formed above the dehydration tank 11 as a pump 71 to purify the washing water used in the dehydration tank 11 to be recycled back into the washing water.
- the centrifugal separator (73) is installed in the water purification tank (7) to separate the residues of marine waste mixed in the washing water drained from the dehydration tank (11), and the separated residues are sent to the compactor (3) for desalination. It can be crimped together with the finished marine waste, and the washing water can be recycled through the water purification process in the water purification tank (7).
- the marine waste introduced from the inlet 12 does not fall directly to the dehydration tank 11, but is cut and shredded in the moving process so that the shredder 2, so as to flow into the impeller 13, 2 ').
- the shredders 2 and 2 alternatively form the guide plates 15 and 15' which are inclined downward, and install several cutting cutters 21 and 21 'on the guide plates 15 and 15' to incline the guide plates. Marine waste moving along (15, 15 ') is cut and crushed by the cutting cutters (21, 21').
- the cutting cutters 21 and 21 ' may be installed to rotate a plurality of rotary blades on the rotating shaft to cut and shred marine waste moving along the guide plates 15 and 15'.
- a discharge path 17 is formed at one side of the bottom of the dehydration tank 11 in which the impeller 13 is installed, and an opening and closing plate 18 is formed at the discharge path 17 to drain the washing water in the dehydration tank 11 and then dewater again. Rotating the impeller 13 in the tank 11 to dewater marine waste, and then open and close the opening and closing plate 18 to rotate the impeller 13 to discharge the dehydrated marine waste out of the dehydration tank (11).
- a discharge guide 19 is formed in the discharge path 17 in which the opening and closing plate 18 is formed to guide the discharged marine waste to the conveyor.
- Compressor (3) is a pair of pressing rollers (31, 31 ') (32, 32') arranged up and down to face each other to be rotationally driven and the vertical pressing rollers (31, 31 ') (32, 32') ) So that marine waste can be compressed.
- Marine wastes compressed by the compression rollers 31, 31 ′, 32, 32 ′ are dehydrated in the remaining water in the compression process and are reduced in volume by compression.
- the marine waste that has undergone the compression process is again transferred to the grinding and mixing apparatus 4 using a conveyor, and then pulverized and mixed with the combustible waste.
- the crushing and mixing apparatus 4 is a crushing and mixing operation of the desalted and dehydrated marine waste and combustible waste together, and the neutralizing agent and the additive may be mixed in the mixing process.
- the marine waste and combustible wastes pulverized and mixed in the crushing and mixing device 4 are put into the compression molding machine 5 to be extruded and cut into a predetermined size (length) by the cutting machine 6 to produce solid fuel.
- the washing water for the desalination of marine waste is filled, and the marine waste is introduced from the inlet 12 of the upper part of the dehydration tank 11 in which the washing water is filled.
- the marine waste is to remove the deposits, such as metal and to separate only the synthetic resin.
- the drain port 16 is opened to drain the washing water in the dehydration tank 11 to the water purification tank 7, and when the washing water is drained, the impeller 13 is turned at high speed.
- the marine waste is dewatered by rotation, and the dewatered water is sent to the water purification tank 7 through the drain 16.
- the drain port 16 may be provided with a screen to filter the residue or foreign matter of the marine waste mixed in the drained wash water.
- the drain port 16 is closed and the opening and closing plate 18 of the discharge path 17 is opened to rotate the impeller 13 to discharge marine waste inside the dewatering tank 11.
- the opening and closing plate 18 is configured to open and close the drain hole 16 by linearly moving the opening and closing plate 18 with a driving cylinder.
- the marine waste discharged from the above is moved to the conveyor along the discharge guide 19 and transferred to the compactor (3).
- the dehydration tank 11 in which the dewatering operation is finished is closed by closing the opening and closing plate 18 and supplying the washing water from the water purification tank 7 to fill in the marine waste, and desalination operation is performed by introducing marine waste as described above.
- the dewatered marine waste passes between a pair of compression rollers 31, 31 ′ (32, 32 ′) and is left in marine waste by compression by the compression rollers 31, 31 ′ (32, 32 ′).
- the dehydrated water and the dewatered and compressed marine waste are transferred to a pulverization and mixing device 4 to be pulverized and mixed with flammable waste.
- neutralizing agents In the grinding and mixing process, neutralizing agents, additives and the like may be mixed.
- the marine waste and combustible wastes of the crushing and mixing work are transferred to an extruder 5 to be extruded and cut at the cutting machine 6.
- the present invention is to provide a manufacturing apparatus for producing a solid fuel with a mixed raw material desalted, dehydrated and compressed by desalination, dehydration, compressed marine waste mixed with combustible waste.
- the present invention provides benefits for transportation, storage, etc. of marine waste by reducing the volume by desalination, dehydration, compression treatment of the collected marine waste through a series of processes, by extrusion molding with combustible waste more efficient and It is to manufacture solid fuel economically.
- Solid fuel production according to the present invention is to remove the debris, such as metal and desalination, dehydration of the marine waste classified into synthetic resins only, the desalting, dehydration and compression step, and the compressed marine waste with the combustible waste Mixing and pulverizing, mixing a neutralizing agent, an additive, and the like in the pulverizing process, and extruding and molding a mixture of the pulverized marine waste and combustible waste,
- Solid fuel manufacturing apparatus is a desalination dehydration apparatus for desalination, dehydration of marine waste, a decompression apparatus for compressing desalination and dehydrated marine waste, and a crushing and mixing apparatus for crushing and mixing the compressed marine waste with flammable waste And an extruder for extruding the mixture of marine waste and combustible waste.
- the desalination dehydration device is an impeller formed inside the dehydration tank into which the washing water is input, and the desalination is performed by washing the marine waste in the water by the impeller. After desalination, the washing water is drained from the dehydration tank. Transfer to.
- the pressing device is provided with a pair of pressing rollers facing each other arranged up and down to decompress the marine waste desalted, dehydrated in the dehydration tank to dehydrate the residual moisture and to reduce the volume by the pressing operation to transfer to the grinder, crushing and It is mixed with combustible waste in a mixing apparatus and extruded in an extruder.
- the present invention can contribute to related industries such as fisheries by treating various marine wastes that cause marine pollution, and can produce various fuels by mixing with flammable wastes and supply them to various industrial fields to expect various economic benefits.
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Environmental & Geological Engineering (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
L'invention concerne un dispositif permettant de fabriquer un combustible solide qui utilise un mélange de déchets marins et de déchets combustibles comme matière première, et de fabriquer un combustible solide par dessalement, déshydratation, et compression des déchets marins, et par broyage et mélange de déchets marins et de déchets combustibles dessalés, déshydratés et comprimés. Le dispositif de fabrication de combustible solide selon l'invention comporte un dispositif de dessalement (1) permettant de dessaler et déshydrater les déchets marins; un dispositif de compression (3) permettant de comprimer les déchets marins dessalés et déshydratés; un dispositif de broyage/mélange (4) permettant de broyer et de mélanger les déchets marins comprimés avec les déchets combustibles; et un dispositif de moulage par extrusion (5) conçu pour extruder et mouler le mélange de déchets marins et de déchets combustibles. Le dispositif selon l'invention permet de réduire les coûts de traitement tels que les coûts de transport et de stockage des déchets marins, et de mélanger les déchets marins aux déchets combustibles pour produire un combustible solide économique et de haute qualité.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
KR10-2010-0055222 | 2010-06-11 | ||
KR1020100055222A KR101004462B1 (ko) | 2010-06-11 | 2010-06-11 | 해양폐기물과 가연성폐기물의 혼합물을 원료로 하는 고형연료 제조장치 |
Publications (1)
Publication Number | Publication Date |
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WO2011155667A1 true WO2011155667A1 (fr) | 2011-12-15 |
Family
ID=43513479
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/KR2010/006166 WO2011155667A1 (fr) | 2010-06-11 | 2010-09-10 | Dispositif de fabrication de combustible solide à l'aide d'un mélange de déchets marins et déchets combustibles comme matière première |
Country Status (3)
Country | Link |
---|---|
KR (1) | KR101004462B1 (fr) |
CN (1) | CN102277216A (fr) |
WO (1) | WO2011155667A1 (fr) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
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US11273580B2 (en) | 2018-05-30 | 2022-03-15 | Philip John Milanovich | Waste management system |
US11325280B2 (en) | 2018-05-30 | 2022-05-10 | Philip John Milanovich | Waste management system |
US11491493B2 (en) | 2018-05-30 | 2022-11-08 | Philip John Milanovich | Waste management system |
US11708135B2 (en) | 2018-05-30 | 2023-07-25 | Philip John Milanovich | Waste management system |
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CN103223416A (zh) * | 2012-01-29 | 2013-07-31 | 王自新 | 一种可燃性燃料的制作方法 |
KR101473961B1 (ko) | 2013-01-31 | 2014-12-17 | 성안이엔티주식회사 | 매립쓰레기에서 선별된 가연성의 고순도 연료화 제조장치 |
CN104028532B (zh) * | 2014-05-20 | 2016-03-16 | 牧原食品股份有限公司 | 病死禽畜骨肉、油脂无害化分离系统 |
CN107900067A (zh) * | 2017-10-19 | 2018-04-13 | 荆门市格林美新材料有限公司 | 一种工业旧料清洗烘干破碎回收装置 |
KR102153478B1 (ko) * | 2019-10-25 | 2020-09-10 | 강복길 | 해양폐기물의 선상 처리 시스템 |
JP6695540B1 (ja) * | 2019-12-16 | 2020-05-20 | 株式会社手工仁久 | 海洋浮遊プラスチックごみを利用した合成樹脂成形品の製造方法 |
KR102428058B1 (ko) * | 2021-01-11 | 2022-08-02 | 김형주 | 해양 폐플라스틱 수거 및 고형연료제조용 선박 |
KR102357116B1 (ko) * | 2021-06-22 | 2022-02-08 | 윤문중 | 해상 폐기물의 기체 연료화를 위한 선박 시스템 |
KR102561922B1 (ko) * | 2021-10-05 | 2023-08-02 | 이우호 | 폐그물을 이용한 고형연료 제조장치 |
KR20240030758A (ko) | 2022-08-31 | 2024-03-07 | 주식회사 포어시스 | 이동형 해양폐기물 자원화 시스템 |
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Publication number | Priority date | Publication date | Assignee | Title |
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US11273580B2 (en) | 2018-05-30 | 2022-03-15 | Philip John Milanovich | Waste management system |
US11325280B2 (en) | 2018-05-30 | 2022-05-10 | Philip John Milanovich | Waste management system |
US11491493B2 (en) | 2018-05-30 | 2022-11-08 | Philip John Milanovich | Waste management system |
US11708135B2 (en) | 2018-05-30 | 2023-07-25 | Philip John Milanovich | Waste management system |
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KR101004462B1 (ko) | 2010-12-31 |
CN102277216A (zh) | 2011-12-14 |
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