CN102277216A - Device for manufacturing solid fuel using a mixture of ocean waste and combustible waste as raw material - Google Patents
Device for manufacturing solid fuel using a mixture of ocean waste and combustible waste as raw material Download PDFInfo
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- CN102277216A CN102277216A CN2010102861882A CN201010286188A CN102277216A CN 102277216 A CN102277216 A CN 102277216A CN 2010102861882 A CN2010102861882 A CN 2010102861882A CN 201010286188 A CN201010286188 A CN 201010286188A CN 102277216 A CN102277216 A CN 102277216A
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- sea leave
- sea
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L5/00—Solid fuels
- C10L5/40—Solid fuels essentially based on materials of non-mineral origin
- C10L5/46—Solid fuels essentially based on materials of non-mineral origin on sewage, house, or town refuse
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L5/00—Solid fuels
- C10L5/40—Solid fuels essentially based on materials of non-mineral origin
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE
- B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
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- 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
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- 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
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE
- B09B2101/00—Type of solid waste
- B09B2101/02—Gases or liquids enclosed in discarded articles, e.g. aerosol cans or cooling systems of refrigerators
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L2290/00—Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
- C10L2290/08—Drying or removing water
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- 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
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- 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
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Mechanical Engineering (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Environmental & Geological Engineering (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
The present invention relates to a device for manufacturing solid fuel that uses a mixture of ocean waste and combustible waste as raw material and manufactures a solid fuel by desalinizing, dehydrating, and compressing ocean waste, and grinding and mixing the desalinized, dehydrated, and compressed ocean waste with the combustible waste. The solid fuel manufacturing device of the present invention includes a desalinizing device (1) for desalinizing and dehydrating ocean waste; a compressing device (3) for compressing the desalinized and dehydrated ocean waste; a grinding/mixing device (4) for grinding and mixing the compressed ocean waste with the combustible waste; and an extrusion molding device (5) for extruding and molding the mixture of the ocean waste and the combustible waste.
Description
Technical field
The solid fuel manufacturing installation that to the present invention relates to a kind of mixture with sea leave and combustible waste be raw material, specifically, the solid fuel manufacturing installation that the solid-fuelled mixture with sea leave and combustible waste of manufacturing is a raw material after exactly the combustible waste of the sea leave after desalination, dehydration, the compression after desalination, dehydration, compression being pulverized, being mixed.
Background technology
For utilize the solid shape fuel of various waste manufacturings (RDF: the fuel of the size by regulating moisture content, impurity and particle in the waste, the productions such as content of ash, generally all contain 5,700～17, the heat of 700J/g.) technology, existing multiple manufacture method and manufacturing installation.
In addition, along with industrial expansion, the various domestic refuses etc. of being located to flow into the various rubbish of ocean and being flowed into the ocean by the rivers and creeks by factory and city etc. are to having caused serious pollution in the ocean, especially culture the increase in fish farm along with bank, the sea leave of fishing gears such as fishnet and so on also becomes the major cause that increases the weight of pollution of the sea.People have done a large amount of research also paid many effort aspect the collection of these rubbish, processing.
That is to say that the stagnant fishnet the like waste of being made by various plastic refuses, plastics synthon pollutes over against Marine ecosystems.Past generally all is to burn or landfill disposal after these sea leaves are collected.But this method can cause 2 pollutions to environment in treating processes.To this, the scientific research personnel has just done a large amount of effort and research aspect resource reutilization.
But, sea leave is different with common waste, sea leave is subjected to seawater influence and contains salt, if be not removed, polymkeric substance (Polymer) oxygenizement will take place under the effect of salinity, make the forming process reduction, thereby problems such as division take place in the solid fuel that causes making after extrusion molding.Therefore, need to implement to remove the desalination operation of salinity.
In addition, owing to the sea leave of taking in the past to collect burns, the treatment process of landfill becomes the major cause that environment is caused 2 pollutions.Therefore, just adopt a kind of new method recently, be about to the sea leave fusion of burning, and in burning fused process, reclaim used heat or make slag.
Another kind method is carried out fusion with sea leave in burning melter exactly, then slag is utilized the generation solids again.As described in reference 1, this method is put into waste in the burning melter exactly, utilizes roasting kiln to make its fusion at high temperature, thus the slag that acquisition can utilize again.
In addition, also have a kind of method, exactly that water ratio is higher sludge carries out drying, burning, makes the water vapor condensation that produces in drying process, and water of condensation is reclaimed generation clean water steam.As described in reference 2, aforesaid method is exactly oil fuel and the sludge mixed firing that boiling point is higher than water, make rapid, the lasting generation of sludge heat passage, the water vapor that produces is generated water of condensation by condenser reclaim, and then reclaim by vapour generator generation clean water steam.
But the processing of above-mentioned sea leave is different with common waste, because its water ratio is very high, dewaters in processes such as burning, drying operation needs considerable time and high expense, thereby reduces solid-fuelled economy and productivity.
Therefore, just with the waste of high-moisture percentage by heating or utilize water trap to carry out forced drying, dehydration is compressed, and perhaps will utilize the mud of flocculation agent agglomeration separation to carry out processed by water trap.This heating, dehydration, drying means required input heat in heating, dehydration is far longer than the heat that can reclaim from waste, so not only uneconomical, and when using flocculation agent, can lower efficiency and productivity because of a large amount of time of needs.Therefore, be difficult to sea leave as the Energy resources utilization.
Therefore, as making solid-fuelled prepared using, exploitation can be with the desalination of sea leave, the key that dewatering operation carries out more economically and have more the productivity treatment technology beyond doubt for water ratio is the high and sea leave that is rich in salinity.
Below, the Collecting and dealing of the sea leave relevant with sea leave and original technology of utilizing again etc. are described.
About to swimming in the sea or sinking to the technology that waste is in the sea collected, Korea S's publication 10-2005-0006094 number, same communique 10-2004-0041924 number, same communique 10-2004-0041925 number, same communique 10-2004-0041927 number, same communique 10-2004-0041928 number, same communique 10-2004-004279 number, same communique 10-2005-0006094 number, same communique 10-2006-0129144 number, Korean registered patent gazette 10-0694020 number, Korean registered utility model communique 20-0333613 number, same communique 20-0374608 grade is all on the books.
In addition, about the processing of sea leave with utilize again, put down in writing following a few procedure in Korea S's publication communique 10-2005-0112931 number: the pretreatment procedure that sewage sludge (sludge) and plastic waste are handled, will mix through sewage sludge and the plastic waste that above-mentioned pretreatment procedure is handled, mixing agitating procedure that fusion forms pellet, the granulate cooling operation after the particlized processing, operation that impurities such as the steam that produces in pretreatment procedure and the mixing agitating procedure and dust are handled.
Following two systems have been put down in writing in Korean registered patent gazette 10-0595026 number: the preprocessing system that sea leave directly can be handled on boats and ships; Be equipped with by resource utilization system etc. and be suitable for the Combined Processing system that the system of limited boats and ships size and stable management from now on constitutes, the automation system that all can handle handover, resource utilization and the processed compressed of sea leave, road transit etc.
In addition, put down in writing in Korea S's publication communique 10-2003-0075045 number and will culture waste, shellfish marine fishery wastes such as (mud blood clam, oyster, clams) mix the foundation improvement type solid material of making moisture weak soil with trade wastes such as by product, the lime of heat power station technology, put down in writing the technology that utilize inkfish to thaw etc. the useless sludge of useless sludge, starfish and aquatic products that processing of aquatic products factory produces is removed the geographic heavy metal of seashore in Korea S's publication communique 10-2003-0050529 number.
Particularly, put down in writing the useless fishnet re-use device that is made of following components in publication communique 10-2005-0109055 number: the fishnet that will give up prepares the cutting machine of cutting according to a certain size; Useless fishnet after the cutting is cleaned washing device except that foreign matters such as freshens; Useless fishnet after the cutting is put into centrifuge separator and rotated, with it further chopping the time, the centrifuge separator that salinity and moisture are all removed; With the above-mentioned extrusion machine that under hot conditions, heats and push through the useless fishnet of centrifuge separator processing; The cutting machine that cuts according to certain size of excellent section bar material with extruding.But, above-mentioned useless fishnet re-use device uses the washing device with dry-cleaning function for salinity being removed, it needs to consume a large amount of energy in removing the process of freshen, and washing procedure separates with dehydration procedure and carries out, therefore, in its treating processes, to consume a large amount of time and manpower exactly.
In addition, no matter common waste or trade waste in the waste that combustible waste is the comings and goings by the mankind to be produced all have combustibility.Below, will carry out simple declaration to utilizing combustible waste to make solid-fuelled situation.
Put down in writing the solid-fuelled method of a kind of manufacturing in Korea S's publication communique 10-1998-67783 number, exactly in food refuse being separated into the process that starchy material and other raw material cook, ignition dope mixes, extrusion molding with adding in the combustible wastes such as plastic waste after the separation of the incombustible in the food refuse, thereby makes solid fuel.
Put down in writing the solid-fuelled method of a kind of manufacturing in Korea S's publication communique 10-2000-015759 number, adding wastewater sludge cake, combustible waste (damaged tire, plastic waste) powder mix in food refuse exactly, put into the shaper extrusion molding then, thereby make solid fuel.
Having put down in writing the solid-fuelled method of a kind of manufacturing in Korea S's publication communique 10-2003-25985 number, is exactly combustible waste to be pulverized the back add white lime, then, again by shaper extruding, moulding, thereby makes solid fuel.Put down in writing the solid-fuelled method of a kind of manufacturing in same communique 10-2002-059074 number, thus exactly with after the combustible waste drying under hot conditions extrusion molding make solid fuel.Put down in writing the solid-fuelled method of a kind of manufacturing in same communique 10-2002-075763 number, added ignition dope in the chip after combustible waste is pulverized exactly and mix, after heating, compression, extruding, moulding again, thus make solid fuel.
The prior art document
(patent documentation 0001) reference 1: Korea S's publication communique 10-2008-0030744 number
(patent documentation 0002) reference 2: Korea S's publication communique 10-2006-0129144 number
Summary of the invention
Invent technical task to be solved
As mentioned above, though the research staff is utilizing sea leave manufacturing, exploitation to carry out many research aspect the solid fuel, but, sea leave is different with common waste, contain higher salinity and water ratio owing to influenced by marine brinish, this has brought many difficulties for desalination, dewatering operation, and as solid-fuelled raw material, its economy and efficiency are all very low with it.
Therefore, the objective of the invention is to, provide a kind of sea leave that more effectively and economically utilizes to make solid-fuelled method, to be subjected to salt solution to influence all higher sea leave of its salinity and water ratio effectively after compressing again after desalination, the dehydration, mix with combustible wastes such as plastic waste, plastic waste, thereby just can make solid fuel.
Technical scheme
In order to solve above-mentioned problem, among the present invention
First invention is, is the solid fuel manufacturing installation of raw material for the mixture with sea leave and combustible waste, and it is made of following several sections: the desalting dewatering device that sea leave is carried out desalination, processed; The compression set that will compress through the sea leave after desalination, the processed; With after compression sea leave with combustible waste pulverize, blended is pulverized, mixing device; Single-lead-screw extruding briquetting machine with the mixture extrusion molding of sea leave and combustible waste.
Be that in the solid fuel manufacturing installation of record, above-mentioned desalting dewatering device is made of following several sections in first invention in second invention: washing water are housed, can be from the dewatering tank of top throw-in part with the sea leave input; Make sea leave carry out the impeller of desalination, processed to sea leave in the inner rotation of above-mentioned dewatering tank; Be arranged on downward-sloping directing plate top between the top throw-in part of above-mentioned dewatering tank and the bottom impeller, the pulverizer that the sea leave that will move with directing plate cut, pulverize with the cutting knife of rotation; The exhaust channel of sea leave being discharged by the switching that is arranged on above-mentioned dewatering tank bottom one side opening-closing plate.
The 3rd invention is, in first invention in the solid fuel manufacturing installation of record, above-mentioned compression set is along a pair of extrusion roll that is oppositely arranged rotatable driving up and down, sea leave put into above-mentionedly just can be compressed it between the extrusion roll up and down.
Beneficial effect
The present invention compresses the long-time stagnant sea leave that contains higher salinity in seawater after desalination, processed to dwindle its volume by a series of operation again, so just can save required processing costss such as sea leave transport, takes care of.Simultaneously, will mix with combustible waste, and can make solid fuel more effectively, thereby just can provide high-quality and the high solid fuel of economy through desalination, dehydration and sea leave after compression.
Description of drawings
Fig. 1 represents the whole pie graph of solid fuel manufacturing installation of the present invention;
Fig. 2 represents the pie graph of desalting dewatering device among the present invention;
Fig. 3 represents the pie graph of dewatering tank among the present invention;
Fig. 4 represents the pie graph of compressor among the present invention.
Detailed description of main elements
1: desalting dewatering device 11: dewatering tank
12: throw-in part 13: impeller
14: the rotation wing 15,15 ': directing plate
16: water port 17: exhaust channel
18: opening-closing plate 19: discharge conduit
2,2 ': pulverizer 21,21 ': cutting knife
3: compressor 31,31 ', 32,32 ': extrusion roll
4: pulverize mixing device 5: single-lead-screw extruding briquetting machine
6: cutting machine 7: clean water tank
71: pump 72: influx
Embodiment
The objective of the invention is to, provide a kind of utilization that the sea leave of collecting also will be mixed the mixing raw material that forms through desalination, processed and compressed sea leave after compression again through desalination, processed with combustible waste and make solid-fuelled manufacturing installation.
Particularly, the objective of the invention is to, the sea leave collected is carried out desalination, dewaters and carry out processed compressed dwindling its volume by a series of operation, thereby save required processing costss such as sea leave transport, takes care of.Simultaneously, with itself and combustible waste be mixed together, extrusion molding so that more effectively and economically make solid fuel.
Comprise following several steps according to solid-fuelled manufacturing of the present invention: after removing dirt settling such as metal, will only carry out the step of desalination, processed by the sea leave of synthetic resin classification; Through the step of compressing behind above-mentioned desalination, the dehydration procedure; The step of pulverizing after compressed sea leave and combustible waste be mixed together; In above-mentioned crushing process, add neutralizing agent, additive etc. and carry out the blended step; With the mixture of the sea leave pulverized and combustible waste push, the step of moulding.
Constitute by following several sections according to solid fuel manufacturing installation of the present invention: the desalting dewatering device that sea leave is carried out desalination, processed; The compression set that will compress through the sea leave after desalination, the processed; With after compression sea leave with combustible waste pulverize, blended pulverizes mixing device; Single-lead-screw extruding briquetting machine with the mixture extrusion molding of sea leave and combustible waste.
Above-mentioned desalting dewatering device is provided with impeller in the dewatering tank inside that washing water are housed, by impeller with sea leave after desalting treatment is carried out in water washing, washing water are discharged by dewatering tank, then, by impeller sea leave is carried out processed again, then, transfer to compression set again.
The edge is relatively set with a pair of extrusion roll up and down in the above-mentioned compression set, to in dewatering tank, carry out sea leave after desalination, the processed compress residual moisture taken off in, transfer to pulverizer again after its volume is dwindled in operation by compressing, then, in pulverizing mixing device, be mixed together with combustible waste, then, again by the single-lead-screw extruding briquetting machine extrusion molding.
Below, with reference to the accompanying drawings concrete implementation content of the present invention is elaborated.
Fig. 1 represents the whole pie graph according to solid fuel manufacturing installation of the present invention, and Fig. 2 represents the pie graph of dewatering unit among the present invention, and Fig. 3 represents the pie graph of dewatering tank among the present invention, and Fig. 4 represents the pie graph of compressor among the present invention.
The present invention is according to the solid fuel manufacturing step, constitute by desalting dewatering device 1, compression set 3, pulverizing mixing device 4, single-lead-screw extruding briquetting machine 5, cutting machine 6, below, introduce the desalting dewatering device 1 that is used for sea leave is carried out desalination, processed.
Desalting dewatering device 1 is provided with throw-in part 12, and dewatering tank 11 tops that washing water are housed are opened to guarantee the input of sea leave.Be provided with impeller 13 in the bottom, when the sea leave rotation is contacted with washing water sea leave stirred mutually and carry out desalination, dewatering operation.Impeller 13 turning axles are provided with the rotation wing 14, sea leave is contacted with washing water and when washing by shockwave, sea leave is stirred mutually, and the salinity that contains in the sea leave is washed to carry out desalination.
In addition, be provided with water port 16, on water port 16, also be provided with valve 16a, be connected with clean water tank 7 in dewatering tank 11 bottoms that are provided with impeller 13.Above-mentioned clean water tank 7 is connected with the influx 72 that is arranged on dewatering tank 11 tops by pump 71, carries out being re-used as the washing water use after the purifying treatment with the washing water that will use in the dewatering tank 11.
Above-mentioned clean water tank 7 is provided with centrifuge separator 73, the residue that it will sneak into the sea leave in the washing water of being discharged by dewatering tank 11 separates, and isolated residue carried to compressor 3, compress operation with the sea leave through the desalting and dewatering operation, washing water can utilize through after the purifying treatment in clean water tank 7 again.
In addition, above-mentioned dewatering tank 11 be provided with pulverizer 2,2 ', it can guarantee can directly not drop to dewatering tank 11 bottoms from the sea leave that throw-in part 12 drops into, but in moving process it is cut, pulverizes, and then to impeller 13 1 side inflows.
Above-mentioned pulverizer 2,2 ', a plurality of cutting knifes 21,21 ' are set on directing plate 15,15 ' top with downward-sloping directing plate 15,15 ' be crisscross arranged, thus will cut, pulverize with the directing plate 15, the 15 ' sea leave that moves that tilt.
Above-mentioned cutting knife 21,21 ' goes up that a plurality of rotation blades are rotatable to be arranged on the turning axle drivingly, with to cutting, pulverize with directing plate 15, the 15 ' sea leave that moves.
In addition, be provided with exhaust channel 17 in dewatering tank 11 bottoms one side that is provided with impeller 13, exhaust channel 17 is provided with opening-closing plate 18, after discharging the washing water of dewatering tank 11 inside, it makes impeller 13 rotations of dewatering tank 11 inside again, sea leave is carried out after the processed, again opening-closing plate 18 is opened, impeller 13 is rotated, thereby will outside dewatering tank 11, discharge through the sea leave after the dehydration.
The exhaust channel 17 that is provided with above-mentioned opening-closing plate 18 is provided with the discharge conduit 19 that the sea leave of discharging can be guided by transport unit.
To transfer to compressor 3 by the sea leave that above-mentioned dewatering tank 11 is discharged, and dewater by compression and can dwindle its volume.Below, will be elaborated to compressor 3.Compressor 3, is put into sea leave between the above-mentioned extrusion roll up and down 31,31 ', 32,32 ' and just can be compressed it along being oppositely arranged formation up and down by the extrusion roll 31,31 ', 32 of a pair of rotatable driving, 32 '.
Sea leave through above-mentioned extrusion roll 31,31 ', 32,32 ' compression can be taken off residual moisture in compression process once more, to reduce its volume by compression.
To utilize transport unit to transfer through the sea leave after above-mentioned compression section is handled again, and pulverize, mix with combustible waste to pulverizing mixing device 4.Above-mentioned pulverizing mixing device 4 will be pulverized with combustible waste and mix through the sea leave that desalting and dewatering is handled.In above-mentioned mixing process, can add neutralizing agent, additive.
In addition, will pulverize through above-mentioned pulverizing mixing device 4, the blended sea leave cuts according to certain specification length by cutting machine 6, thereby makes solid fuel after combustible waste drops into single-lead-screw extruding briquetting machine 5 extrusion moldings.
Below, will be to describing according to solid fuel manufacturing processed of the present invention.
In dewatering tank 11, pack into and be used for sea leave is carried out the washing water of desalting treatment, then, the throw-in part 12 of sea leave from dewatering tank 11 tops that washing water are housed dropped into.After dirt settlings such as metal in the above-mentioned sea leave are removed, only the synthetic resin separating substances is come out.
The sea leave that drops into from above-mentioned throw-in part 12 moves to the bottom with the pulverizer that is crisscross arranged 2,2 ' directing plate 15,15 ' the process that the impeller 13 by the bottom moves, and the cutting knife 21,21 ' cutting, the pulverizing that are rotated, then, be put to again in the impeller 13.
Then, sloughed, then, finish the desalination operation in the washing water thereby be dissolved in by the salinity that above-mentioned pulverizer 2,2 ' cutting, the sea leave pulverized contacts with washing water under the rotation wing 14 effects of rotary blade 13 and mutual stirring will be adhered to.After finishing above-mentioned demineralising process by impeller 13, water port 16 is opened, made the washing water in the dewatering tank 11 be discharged to clean water tank 7, after washing water are discharged, high speed rotating impeller 13 rotates sea leave to dewater together, and the water that will deviate from is discharged in the clean water tank 7 by water port 16 again.
On above-mentioned water port 16, filter screen can be set, filter out so that will sneak into the residue of discharging the sea leave in the washing water or foreign matter etc.
Finish after the above-mentioned dewatering operation, close water port 16, the opening-closing plate 18 of exhaust channel 17 is opened, rotary blade 13 is discharged the sea leave in the dewatering tank 11.Above-mentioned opening-closing plate 18 makes opening-closing plate 18 do translational motion by driving cylinder etc., thereby water port 16 is opened or closed.
The sea leave of above-mentioned discharge moves to transport unit along discharging conduit 19, then, is transplanted on compressor 3.
Then, opening-closing plate 18 is closed, finish the dewatering tank 11 of above-mentioned dewatering operation and supply with washing water, as mentioned above, the sea leave input is carried out the desalting and dewatering operation by clean water tank 7.
Make above-mentioned sea leave pass through a pair of extrusion roll 31,31 ' through processed, 32, between 32 ', by extrusion roll 31,31 ', 32,32 ' the compression moisture that will remain in the sea leave is taken off, then, above-mentioned sea leave through dehydration, processed compressed is transferred to pulverizing mixing device 4, pulverized, mix with combustible waste.
In above-mentioned pulverizing, mixture operation process, can add neutralizing agent, additive.
Above-mentioned sea leave and the combustible waste of finishing pulverizing, mixture operation transferred after extrusion molding to single-lead-screw extruding briquetting machine 5, cut through cutting machine 6 again.
Claims (3)
1. solid fuel manufacturing installation that the mixture with sea leave and combustible waste is a raw material is characterized in that it is made of following several sections:
Sea leave is carried out the desalting dewatering device (1) of desalination, processed; The compression set (3) that will compress through the sea leave after desalination, the processed; With after compression sea leave with combustible waste pulverize, blended pulverizes mixing device (4); Single-lead-screw extruding briquetting machine (5) with the mixture extrusion molding of sea leave and combustible waste.
2. the mixture with sea leave and combustible waste according to claim 1 is the solid fuel manufacturing installation of raw material, it is characterized in that, above-mentioned desalting dewatering device (1) is made of following several sections:
Washing water are housed, can be from the dewatering tank (11) of top throw-in part (12) with the sea leave input; Make sea leave carry out the impeller (13) of desalination, processed to sea leave in the inner rotation of above-mentioned dewatering tank (11); Be arranged on downward-sloping directing plate (15,15 ') top between the top throw-in part (12) of above-mentioned dewatering tank (11) and the bottom impeller (13), the pulverizer (2,2 ') that will cut, pulverize with cutting knife (21,21 ') with the sea leave that directing plate (15,15 ') moves; By being arranged on the exhaust channel (17) of switching so that sea leave is discharged of above-mentioned dewatering tank (11) bottom one side opening-closing plate (18).
3. the mixture with sea leave and combustible waste according to claim 1 is the solid fuel manufacturing installation of raw material, it is characterized in that:
Above-mentioned compression set (3) is along a pair of extrusion roll (31,31 ') (32,32 ') that is oppositely arranged rotatable driving up and down, with sea leave put into above-mentioned up and down between the extrusion roll (31,31 ') (32,32 ') so that it compresses to sea leave.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| KR10-2010-0055222 | 2010-06-11 | ||
| KR1020100055222A KR101004462B1 (en) | 2010-06-11 | 2010-06-11 | The rdf manufacture apparatus from mixture of marine waste and combustibility waste |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN102277216A true CN102277216A (en) | 2011-12-14 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010102861882A Pending CN102277216A (en) | 2010-06-11 | 2010-09-19 | Device for manufacturing solid fuel using a mixture of ocean waste and combustible waste as raw material |
Country Status (3)
| Country | Link |
|---|---|
| KR (1) | KR101004462B1 (en) |
| CN (1) | CN102277216A (en) |
| WO (1) | WO2011155667A1 (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104028532A (en) * | 2014-05-20 | 2014-09-10 | 牧原食品股份有限公司 | Harmless separation system for bone, meat and grease of livestock dying of diseases |
| CN107900067A (en) * | 2017-10-19 | 2018-04-13 | 荆门市格林美新材料有限公司 | A kind of industry old material cleaning, drying crushes retracting device |
| WO2021125009A1 (en) * | 2019-12-16 | 2021-06-24 | 株式会社手工仁久 | Method for producing synthetic resin molded article in which marine floating plastic waste is used |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103223416A (en) * | 2012-01-29 | 2013-07-31 | 王自新 | Method for producing combustible fuel |
| KR101473961B1 (en) | 2013-01-31 | 2014-12-17 | 성안이엔티주식회사 | Selected from the landfill of combustible fuel manufacturing high-purity method and device |
| US11708135B2 (en) | 2018-05-30 | 2023-07-25 | Philip John Milanovich | Waste management system |
| 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 |
| KR102153478B1 (en) * | 2019-10-25 | 2020-09-10 | 강복길 | System for onboard treatment of ocean waste |
| KR102428058B1 (en) * | 2021-01-11 | 2022-08-02 | 김형주 | Marine waste cleaning and solid fuel manufacturing system ship |
| KR102357116B1 (en) * | 2021-06-22 | 2022-02-08 | 윤문중 | Movable Incineration Ship for Maritime Waste using microwave |
| KR102561922B1 (en) * | 2021-10-05 | 2023-08-02 | 이우호 | Apparatus for manufacturing of solid fuel using waste net |
| KR20240030758A (en) | 2022-08-31 | 2024-03-07 | 주식회사 포어시스 | Mobile marine waster resource circulation system |
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- 2010-06-11 KR KR1020100055222A patent/KR101004462B1/en active IP Right Grant
- 2010-09-10 WO PCT/KR2010/006166 patent/WO2011155667A1/en active Application Filing
- 2010-09-19 CN CN2010102861882A patent/CN102277216A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN1490094A (en) * | 2002-10-18 | 2004-04-21 | 伊诺太科有限公司 | Food refuse treater |
| KR100527041B1 (en) * | 2003-03-31 | 2005-11-09 | 한국에너지기술연구원 | Method and device for producing fuel from food wastes |
| KR20050112929A (en) * | 2004-05-28 | 2005-12-01 | 동명산업 주식회사 | Method to manufacture solid fuel of waste plastic |
| CN101121905A (en) * | 2006-08-10 | 2008-02-13 | 株式会社韩国能量 | A solid fuel manufacturing method and its device use of the food waste and the plastic waste |
| WO2009093639A1 (en) * | 2008-01-23 | 2009-07-30 | Kouichi Shin-Ya | Garbage disposer |
| CN101362977A (en) * | 2008-09-12 | 2009-02-11 | 周泽宇 | Technique for preparing consumer waste regenerated coal |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104028532A (en) * | 2014-05-20 | 2014-09-10 | 牧原食品股份有限公司 | Harmless separation system for bone, meat and grease of livestock dying of diseases |
| CN104028532B (en) * | 2014-05-20 | 2016-03-16 | 牧原食品股份有限公司 | Poultry of dying of illness kindred, the innoxious piece-rate system of grease |
| CN107900067A (en) * | 2017-10-19 | 2018-04-13 | 荆门市格林美新材料有限公司 | A kind of industry old material cleaning, drying crushes retracting device |
| WO2021125009A1 (en) * | 2019-12-16 | 2021-06-24 | 株式会社手工仁久 | Method for producing synthetic resin molded article in which marine floating plastic waste is used |
Also Published As
| Publication number | Publication date |
|---|---|
| KR101004462B1 (en) | 2010-12-31 |
| WO2011155667A1 (en) | 2011-12-15 |
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