CN101688140B - Apparatus for the utilization of wet waste material - Google Patents
Apparatus for the utilization of wet waste material Download PDFInfo
- Publication number
- CN101688140B CN101688140B CN200880015177.1A CN200880015177A CN101688140B CN 101688140 B CN101688140 B CN 101688140B CN 200880015177 A CN200880015177 A CN 200880015177A CN 101688140 B CN101688140 B CN 101688140B
- Authority
- CN
- China
- Prior art keywords
- waste material
- dry
- heat
- air
- moisture eliminator
- 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.)
- Expired - Fee Related
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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
- C10L5/48—Solid fuels essentially based on materials of non-mineral origin on industrial residues and waste materials
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L5/00—Solid fuels
- C10L5/02—Solid fuels such as briquettes consisting mainly of carbonaceous materials of mineral or non-mineral origin
- C10L5/34—Other details of the shaped fuels, e.g. briquettes
- C10L5/36—Shape
- C10L5/363—Pellets or granulates
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B21/00—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B23/00—Heating arrangements
- F26B23/001—Heating arrangements using waste heat
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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
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/10—Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working
-
- 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
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/30—Wastewater or sewage treatment systems using renewable energies
- Y02W10/37—Wastewater or sewage treatment systems using renewable energies using solar energy
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- Geochemistry & Mineralogy (AREA)
- Geology (AREA)
- Sustainable Development (AREA)
- Processing Of Solid Wastes (AREA)
- Drying Of Solid Materials (AREA)
- Paper (AREA)
- Treatment Of Sludge (AREA)
- Solid Fuels And Fuel-Associated Substances (AREA)
Abstract
Apparatus for the utilization of wet waste material, which apparatus comprises at least a dryer arrangement for drying of wet waste material and a press arrangement (3) for pelletizing dried wet waste material. The apparatus is meant particularly for the utilization of the deinked mass (x), such as waste material comprising flour or like, in pelletized form by combustion, wherein the dryer arrangement comprises one or several dryers (1) in order to dry the deinked mass by an air flow (w) to be led therethrough, and/or one or several mixers (2) in order to dry the deinked mass by adding a drier ingredient (m) among the same.
Description
Technical field
The present invention relates to for utilizing the equipment of wet waste material, this equipment comprises that at least one moisture eliminator for wet waste material is dried is arranged and the squeezing machine layout for the waste material being dried is granulated.
Background technology
Especially, in making sheet industry and paper industry, produce every year a large amount of deinked mass (deinked mass) (for example) as so-called zero fibre or powdered solid fuel, it is from the isolated flour of a process (flour) block.This waste material also comprises a small amount of kaolin and the latex as coated material conventionally.And, particularly, in pulp factories, for example the sewage lagoon from wastewater facilities finds corresponding deinked mass as deinking solid material, and it discloses conventionally waddy shorter, that be usually less than 5mm length, flour block and how much have a bit other material, such as sand, clay etc.Now, this waste material only can mainly be used in paper pulp boiler (pulp boiler), and wherein mentioned waste material can marginally burn together with other combustible matl.In not thering is the factory of paper pulp boiler, there is not the possibility that this burning occurs, wherein, for example, the required process steam of factory is normally produced with Sweet natural gas.Therefore the deinked mass, generating will not be exploited completely.Due to the high humidity of deinked mass, thereby can not make it successfully burn, Here it is, and why current unique replacement scheme is to utilize deinked mass (for example) for the reason of soil improvement object.But due to its high heating value, this deinked mass is suitable for energy object especially, its high heating value is because decomposition reduces, for example the situation of mud coal.
Deinked mass is transported to beyond factory area and causes and except transportation cost, also have additional cost, for example, significant dumping area expense, in addition, mentioned material also causes smell harm at composting plant, and this is considered to environmental hazard now.At present, can not like this deinked mass be successfully pressed into particle, for example, because () has 40% to 80% humidity conventionally from the isolated flour material of a process.
Thus, for example, in bulletin US2006/0108459, proposed dry (for example) different types of organic waste materials and made them can be used as the scheme of fuel, its main points are to develop cow dung and pig manure especially by this.In mentioned bulletin, a kind of waste material that the proposal paper pulp that also use particularly generates in papermaking or paper mill sludge are used as being applicable to mentioned scheme on the other hand.In this scheme, waste sludge is dumped in mixing chamber, in mixing chamber, is subject to the impact of mechanical rotor, solid material impact cavity locular wall in waste sludge with and during interior flow plate, generate extremely many kinetic energy so that the temperature of waste sludge raises and its moisture evaporation.Solid material is partly dried by air flowing, and solid material further betransported for entering in swirler (cyclone) and carries out last being dried, and the result of this process is thus, has realized combustible matl, and its humidity is about 15%.In this scheme, also propose for example before drying process, muck to be mixed mutually with sawdust, wood chip, straw or hay.But do not propose the waste material of drying to granulate in this bulletin.
At bulletin US5, the scheme proposing in 431,702 relates to especially with waste sludge and municipal wastes manufactures fuel pellet, proposes especially thus to add waste paper, ickings or stone last (chalice) in mentioned waste material.As the tackiness agent in mixture, propose to utilize the black liquor obtaining from paper industry.This be there is (for example) 50% to 75% water why waste sludge before it is pressed into particle without dry reason.But in this scheme, must use than the more coal of waste material itself.
And, at bulletin US4, in 363,636, propose especially in the continuous stage, bagasse to be dried, the humidity from 48% humidity to 30% to 40% first, and afterwards to 8% to 18% the humidity that is suitable for granulation.The hot blast of sugar plant self is employed in dry.
And, according to the scheme proposing in DE361 3398 at bulletin, likely from paper or some other organic waste materials (such as from paper mill sludge), produce particularly fuel brick.This scheme of proposing is thus based on using oxygen and ultrasonic, obviously particularly has the bacterium of elimination and to the object being oxidized such as the such odoriferous substance of sulphur component.
From a technical standpoint, bulletin US2006/0108459 has disclosed a kind of separator structure of complexity, and due to mechanical rotor and swirler and to preheating of air (it is for dry), the power requirement of described separator structure is very high.The decisive minimizing that therefore can't bring cost for the use of this mentioned scheme of above-mentioned purpose, at present, cost is in particular because the disposal to flour causes.
And for example, at patent announcement US5, the scheme proposing in 431,702 and US4,363,636 is disadvantageous, because their process or technical process based in source mill, these processes or technical process can not utilize in each case.Thereby the scheme proposing in bulletin DE361 3398 can not brought any help to current situation.
Document US2003/186052 has described a kind of execution and with wet waste material, has formed the system of cellulose fiber pellets process, and wet waste material is such as the wood powder existing in the waste streams in paper mill.This process comprises the following steps of following order: receiving step, drying step, grinding steps and granulation step.Can use the multiple dehumidification system that can buy on market, dryer system comprises heated air source.And, also can be dried this waste material with fluidized-bed, wherein air is directed through material.Particle can be used as the fuel of generating.
From the known a kind of system of EP0 348 238, wherein container is connected to dryer system.This moisture eliminator comprises container, and container can be by vehicle mobile.This container has base plate, the second base plate of upstanding wall and perforation.Between the first base plate and the second base plate, have cavity, and dryer unit can be connected to cavity via the opening in wall.Dryer unit is transportable or independently.Can by this dryer unit in addition dry Several Typical Load be cereal crop.
Summary of the invention
The object of utilizing the equipment of wet waste material according to the present invention is to realize the decisive improvement to problem mentioned above, and thereby improves in itself the level of prior art.In order to achieve this end, according to the principal character of equipment of the present invention, be that movably air dryer comprises the interchangeable platform that is applicable to transportation, the upper surface of the central bottom in this platform possesses perforation plate, on perforation version top, is moisture eliminator line.
As according to the most important advantage of device of the present invention, can mention the simplicity of its principle of operation and efficiency and included apparatus wherein, thus, as deinked mass, first likely utilize to be and using the flour of particle form even as fuel that can business development utilization, flour in most of the cases can only cause cost at present.In the device in accordance with the invention, first likely by means of the directed air flowing through deinked mass, be dried deinked mass, therefore, moisture wherein will be evaporated in dry air.And can improve drying efficiency by recovery of heat, likely from the dry air for example being blowed, through () flour waste material, reclaim heat thus, dry air is conventionally still warm after utilizing the process of heat exchanger, heat can for example for example, for example, further be shifted by means of being arranged on () second heat exchanger in () dry air passage thus, for example, for dry air is carried out to preheating.When employing is of the present invention, also advantageously, by independent instrument air dryer is placed in to dry air passage in the place ahead of blower fan, also can further improve the dry efficiency that affects that air blows.As supplementing or substitute above-mentioned, in the device in accordance with the invention, thereby also likely by mixing therein comparatively dry material, reduce the dry deinked mass of its moisture, afterwards, formed block is mixed into the uniform fiber block that is suitable for granulation.Thus, as blendable raw material, can use sorted scrap such as sawdust, cereal, Semen Brassicae campestris core, reed canary grass, millet straw, waste paper, cutting machine chip etc.The deinked mass that utilization equipment according to the present invention produces, such as flour particle and the material mixing with it mentioned above, is all the material based on biological, this mentioned particle and without discharge permit of making to burn.
Due to the present invention, the form that can make processed deinked mass become can business development to utilize, for energy object, utilizes it likely to replace for example by the oily gentle energy generation operating.By means of equipment according to the present invention, also likely promote to cause at present environmental problem factory employment and improve their image.
In relative dependent claims, show according to the present invention for utilizing other advantageous embodiment of the equipment of wet waste material.
Accompanying drawing explanation
In the following description, referring to accompanying drawing, understand in detail the present invention, in the accompanying drawings:
The particularly general operation principle based on air dried a kind of equipment shown in Figure 1,
Shown in Figure 2 when utilizing the moisture eliminator of implementing based on so-called interchangeable platform principle, according to the advantageous embodiment of equipment of the present invention,
Shown in Figure 3 according to another advantageous embodiment of equipment of the present invention, it is based on by making deinked mass mix and be dried deinked mass with comparatively dry material; And
Shown in Figure 4 according to the embodiment of favourable complementary recovery of heat of the present invention.
Embodiment
The present invention relates to for utilizing the equipment of wet waste material.This equipment comprises that at least one moisture eliminator is arranged and a squeezing machine arranges 3, this at least one moisture eliminator is arranged for being dried such as the such wet waste material x of deinked mass that comprises flour etc. through the air flowing of wet waste material by guiding, this squeezing machine arranges that 3 for the waste material through super-dry is granulated, and this equipment is for utilizing the waste material of drying of a granular form by burning.This moisture eliminator is arranged and is comprised at least one movably air dryer 1, it possesses linkage arrangement and the air flowing for air flowing w below the central bottom v of moisture eliminator movably and arranges 1b, with guide air flowing w from below via the blow openings this main body through wet waste material.Movably air dryer 1 comprises the interchangeable platform that is applicable to transportation, and the upper surface of the central bottom v in this platform possesses perforation plate, at the top of perforation plate, is moisture eliminator line.
Especially referring to Fig. 1, as advantageous embodiment, dry air w is for example directed through deinked mass from below, wherein, as advantageous embodiment, dry air w utilizes overvoltage to deliver to and belong to the instrument air dryer 1 that moisture eliminator is arranged from one or more blower fan 1a, and deinked mass is transmitted through two continuous moisture eliminators on transfer roller k.Thus, as favourable, substitute, also likely by instrument air dryer is connected in, in the suction side of one or more blower fans, instrument air dryer is arranged to can be in under-voltage lower operation.
As another advantageous embodiment, the principle based on shown in Fig. 1 and Fig. 2 for example, about belonging to the instrument air dryer 1 that moisture eliminator arranges, be also furnished with assembly 1c, such as for collecting the overhead extraction hood (overhead extractor) of the directed dry air through deinked mass.As advantageous embodiment, this equipment also comprises assembly 1d, its for by means of the first heat exchanger from the directed air flowing through deinked mass, and/or carry out recovery of heat from the particle of manufacturing, and for transmitting reclaimed heat especially for being further dried by means of the second heat exchanger or preheating and drying air w.
And, advantageously, embodiment as a supplement, particularly about the embodiment shown in Fig. 2, in the device in accordance with the invention, the principle based on shown in Fig. 4 for example, also likely utilize auxiliary heat reclaim assembly 1d1 transmit the heat that externally reclaims, especially for dry or preheating and drying air w and/or for corresponding object.As another advantageous embodiment, auxiliary heat reclaims assembly 1d1 and comprises: one or more solar cells, heat pump etc., and for " and/or the energy collection unit 1d1 ' that reclaims hot transport sector 1d1.
Naturally likely utilize auxiliary heat shown in Fig. 4 to reclaim assembly 1d1, thereby reclaim assembly without the basal heat of type as shown in Figure 2.Auxiliary heat as shown in Figure 4 reclaims assembly 1d1 can be advantageously for example usings the air heat pump that circulating liquid (such as water) operates and realizes as heat reclamation device by using, and the heat that reclaimed thus for example can be stored in boiler 1d1 ' to for example " reclaimed heat is transferred to dry air w from boiler 1d1 ' by means of the second heat exchanger ld by adjustable mixing tank valve 1d1.
In example scheme as shown in Figure 2, use the interchangeable platform moisture eliminator 1 of buckle, it has five sections, as shown in the cross section of portion in the drawings, nozzle and flow module 1b are inducted into dry air in these five sections, and nozzle and flow module 1b are present in the below of the central bottom v of moisture eliminator platform.The upper surface of central bottom is advantageously perforation plate, is equipped with for example moisture eliminator line on the top of perforation plate.And, according to the embodiment shown in Fig. 4, also likely utilize moisture eliminator line-perforation plate embodiment of type mentioned above as the upper wall of moisture eliminator platform, it during drying prevents that dust from propagating into environment or similar discharge and noise effectively.
The central bottom v of interchangeable platform also tilts towards blow openings, during transportation interchangeable platform, described opening has for example connector, during the described interchangeable platform of transportation, due to connector, from the water of deinked mass drift to be dried, will can not be leaked to road from platform.Under dry situation, the blowpipe being connected with centrifugal blower is for example connected in blow openings by cam lock-fastening piece.
When dry-matter content is for for example 70% to 85% time, dry be interrupted and interchangeable platform is emptied in the mixing tank of granulation device, mixing tank is mixed into even quality for granulating by this block.And in this case, as advantageous embodiment, also likely by recovery of heat mentioned above, be more effectively dried, thus, by the first heat exchanger, from the heat of exhaust gas recovery, by means of the second heat exchanger, transfer to dry air.In this way, the air of preheating makes dry acceleration.And as advantageous embodiment, especially, so-called moulding press (matrix press) is used as pressing assembly 3, when compacting moisture is for for example 25% to 30% time, by means of 3 of this pressing assemblies, likely produce particle.It likely produces such compressed granulate from having the mixture of 50% flour waste material and 50% reed canary grass.
Example equipment as shown in Figure 1 comprises moisture eliminator le and the storage silo A for dry air extraly, moisture eliminator le is also advantageously placed in the place ahead of blower fan la, and eliminate the moisture in introducing air by means of moisture eliminator le, for example, by electric condensation, this equipment is advantageously placed in the factory area that (for example) produces waste material.In the case, waste material transportation does not cause any cost, thus, only needs the subsidiary material that may need in this process to take to from outside granulation facility.
The ashes that produce due to deinked mass particle burning also can be used as soil improvement material, so it has reduced the needs that soil is limited.
Obviously, shown in the present invention is not limited to above or described embodiment, but alternatively can in design of the present invention, in the possible mode of the best, make a change at any given time.Therefore, first will be clear that and can utilize in the layout of under-voltage lower operation and/or flow and be dried interchangeable platform by the dry air occurring to bottom from top.Except above-mentioned, also likely particle is directly produced on dry platform, they are cooling on dry platform, and in the case, after cooling, whole particle platform will be transported to combustion plant.
Claims (10)
1. an equipment that utilizes wet waste material, described equipment comprises that at least one moisture eliminator is arranged and a squeezing machine is arranged, this at least one moisture eliminator is arranged for carrying out dry wet waste material (x) by guiding through the air flowing (w) of wet waste material, described squeezing machine arranges that (3) are for granulating to the waste material through super-dry, described equipment is for utilizing the waste material being dried of a granular form by burning, described moisture eliminator is arranged and is comprised at least one movably air dryer (1), described air dryer (1) possesses is movably arranging that for linkage arrangement and the air flowing of air flowing (w) (1b) is to guide air flowing through wet waste material from below via the blow openings of this main body below the central bottom of moisture eliminator (v), it is characterized in that, described movably air dryer (1) comprises the interchangeable platform that is applicable to transportation, the upper surface of wherein said central bottom (v) possesses perforation plate, on described perforation plate top, it is moisture eliminator line.
2. equipment according to claim 1, it is characterized in that, the described central bottom (v) of described interchangeable platform tilts towards described blow openings, described blow openings is equipped with connector and cam lock firmware, described connector is used in the closed described blow openings of described interchangeable platform In transit, and under dry situation, described cam lock firmware is used for making described blow openings to connect with blowpipe.
3. equipment according to claim 1 and 2, is characterized in that, the moisture eliminator line that the upper wall of described interchangeable platform is included on perforation plate top is during drying propagated to prevent dust.
4. according to the equipment described in aforementioned claim 1 or 2, it is characterized in that, about described interchangeable platform, be furnished with the high extraction hood of frame (1c) for collecting the dry air of the described wet waste material of directed process, be also furnished with thus assembly (1d) for utilize the first heat exchanger carry out recovery of heat with transmit the heat of described recovery be further used for by the second heat exchanger be dried or preheating described in dry air.
5. equipment according to claim 1 and 2, is characterized in that, the dry air passage connecting with the blower fan of described dry air possesses the second heat exchanger and/or independent instrument air dryer to improve the drying efficiency of described air flowing (w).
6. equipment according to claim 4, it is characterized in that, about the particle of manufacturing, be furnished with assembly (1d) and carry out recovery of heat for transmitting the heat of described recovery and be further used for described in dry or preheating dry air and/or for corresponding object for the particle from described manufacture.
7. equipment according to claim 4, wherein, about described instrument air dryer (1), be furnished with supplemental heat and reclaim assembly (1d1), it is characterized in that described supplemental heat reclaims assembly (1d1) and comprises that (1d ") is so that transmission is reclaimed energy that assembly produces for dry air described in dry or preheating and/or for corresponding object by described supplemental heat for energy storage units (1d ') and/or transport sector.
8. equipment according to claim 1, it is characterized in that, belonging to that described instrument air dryer (1) that described moisture eliminator arranges is arranged to can be by described moisture eliminator being arranged in the suction side that is connected to one or more blower fans (1a) and with under-voltage operation.
9. equipment according to claim 1, wherein, described wet waste material (x) is the deinked mass that comprises flour.
10. equipment according to claim 7, wherein, described supplemental heat reclaims assembly (1d1) and comprises one or more solar cells and/or heat pump.
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| FI20070191U FI7754U1 (en) | 2007-05-09 | 2007-05-09 | Equipment for the recovery of wet waste |
| FIU20070191 | 2007-05-09 | ||
| PCT/FI2008/050248 WO2008139026A1 (en) | 2007-05-09 | 2008-05-07 | Apparatus for the utilization of wet waste material |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN101688140A CN101688140A (en) | 2010-03-31 |
| CN101688140B true CN101688140B (en) | 2014-08-20 |
Family
ID=38069579
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN200880015177.1A Expired - Fee Related CN101688140B (en) | 2007-05-09 | 2008-05-07 | Apparatus for the utilization of wet waste material |
Country Status (5)
| Country | Link |
|---|---|
| EP (1) | EP2147086A4 (en) |
| CN (1) | CN101688140B (en) |
| FI (1) | FI7754U1 (en) |
| RU (1) | RU2478447C2 (en) |
| WO (1) | WO2008139026A1 (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103185450A (en) * | 2011-12-31 | 2013-07-03 | 中粮集团有限公司 | Method of cassava wet grain drying |
| CN102585867B (en) * | 2012-03-08 | 2014-08-13 | 无锡亿恩科技股份有限公司 | System for conditioning through coking charge coal humidity difference |
| JP2016532544A (en) * | 2013-07-25 | 2016-10-20 | コテュク エナジー アクチエンゲゼルシャフトＫＯＴＹＫ ｅｎｅｒｇｙ ＡＧ | Biomass processing apparatus and biomass processing method |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1741882A (en) * | 2002-03-29 | 2006-03-01 | 纤维技术聚合物有限公司 | Fiber pellets and processes for forming fiber pellets |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE2001595A1 (en) * | 1970-01-15 | 1971-07-22 | Ohrtmann Hans Otto | Container |
| SU1048015A1 (en) * | 1982-02-02 | 1983-10-15 | Ордена Трудового Красного Знамени Производственное Объединение "Запорожтрансформатор" Им.В.И.Ленина | Method and apparatus for making articles from fibrous mass |
| DE3616947A1 (en) * | 1986-05-20 | 1987-11-26 | Organ Faser Technology Co | METHOD FOR PRODUCING PRESSURES FROM DAMP WASTE AND DEVICE FOR CARRYING OUT THE METHOD |
| NO892576L (en) * | 1988-06-23 | 1989-12-27 | Rangemore Systems Ltd | TOERKEINNRETNING. |
| SU1716256A1 (en) * | 1989-03-20 | 1992-02-28 | Ереванский государственный университет | Movable domestic waste reprocessing apparatus |
| RU2076272C1 (en) * | 1995-07-07 | 1997-03-27 | Григорий Исакович Двоскин | Device for reworking solid wastes |
| DE19734319A1 (en) * | 1997-08-08 | 1999-02-11 | Krc Umwelttechnik Gmbh | Process conditioning wet residues by drying, composting and loosening-up |
| DE10027728A1 (en) * | 2000-06-03 | 2001-12-13 | Landkreis Calw Abfallwirtschaf | Method to treat waste, e.g. household garbage, bulky refuse or wood chips; involves transporting crushed material to drying unit and drying material using heated air, which is then condensed |
| DE102004002285A1 (en) * | 2004-01-16 | 2005-08-04 | Tobias Ellermann | Container for storing organic waste, has walls made up of layers of sheet metal e.g. Corten steel joggling sheet, damming material and metal such as steel, where strutting units are arranged at walls and container base |
| US7024796B2 (en) * | 2004-07-19 | 2006-04-11 | Earthrenew, Inc. | Process and apparatus for manufacture of fertilizer products from manure and sewage |
| DE102004051975B3 (en) * | 2004-10-25 | 2006-04-13 | Volkmar Schäfer | Drying clarified sludge, useful for prepartion of fuel, using a drier supplied with a low temperature heat stream from an organic Rankine cycle |
-
2007
- 2007-05-09 FI FI20070191U patent/FI7754U1/en not_active IP Right Cessation
-
2008
- 2008-05-07 CN CN200880015177.1A patent/CN101688140B/en not_active Expired - Fee Related
- 2008-05-07 RU RU2009143634/13A patent/RU2478447C2/en not_active IP Right Cessation
- 2008-05-07 EP EP08761644.7A patent/EP2147086A4/en not_active Withdrawn
- 2008-05-07 WO PCT/FI2008/050248 patent/WO2008139026A1/en active Application Filing
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1741882A (en) * | 2002-03-29 | 2006-03-01 | 纤维技术聚合物有限公司 | Fiber pellets and processes for forming fiber pellets |
Also Published As
| Publication number | Publication date |
|---|---|
| EP2147086A1 (en) | 2010-01-27 |
| FIU20070191U0 (en) | 2007-05-09 |
| RU2478447C2 (en) | 2013-04-10 |
| CN101688140A (en) | 2010-03-31 |
| FI7754U1 (en) | 2008-01-30 |
| RU2009143634A (en) | 2011-06-20 |
| EP2147086A4 (en) | 2016-06-08 |
| WO2008139026A1 (en) | 2008-11-20 |
| WO2008139026A9 (en) | 2009-02-19 |
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