WO2005093013A1 - 燃料製造方法および燃料製造装置 - Google Patents
燃料製造方法および燃料製造装置 Download PDFInfo
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- WO2005093013A1 WO2005093013A1 PCT/JP2005/005326 JP2005005326W WO2005093013A1 WO 2005093013 A1 WO2005093013 A1 WO 2005093013A1 JP 2005005326 W JP2005005326 W JP 2005005326W WO 2005093013 A1 WO2005093013 A1 WO 2005093013A1
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- Prior art keywords
- pressure
- steam
- temperature
- vessel
- fuel
- Prior art date
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Classifications
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- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05F—ORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
- C05F9/00—Fertilisers from household or town refuse
- C05F9/02—Apparatus for the manufacture
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
- C02F11/13—Treatment of sludge; Devices therefor by de-watering, drying or thickening by heating
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/18—Treatment of sludge; Devices therefor by thermal conditioning
-
- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05F—ORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
- C05F17/00—Preparation of fertilisers characterised by biological or biochemical treatment steps, e.g. composting or fermentation
- C05F17/90—Apparatus therefor
-
- 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
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L5/00—Solid fuels
- C10L5/40—Solid fuels essentially based on materials of non-mineral origin
- C10L5/44—Solid fuels essentially based on materials of non-mineral origin on vegetable substances
-
- 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
-
- 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
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A40/00—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
- Y02A40/10—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
- Y02A40/20—Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses
-
- 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
-
- 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
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/141—Feedstock
- Y02P20/145—Feedstock the feedstock being materials of biological origin
-
- 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
- Y02W30/00—Technologies for solid waste management
- Y02W30/40—Bio-organic fraction processing; Production of fertilisers from the organic fraction of waste or refuse
Definitions
- the present invention relates to an apparatus suitable for converting waste having a water rate of 1, 2, 3 or 4 into a form suitable for electric power.
- 2344749 discloses a method for processing food wood and paper materials into feed and food materials (). At this time, the food material is processed and charged, and this time is held in steam, the raw material is used, and steam is introduced with a predetermined force. Then, when the processing power reaches a predetermined value, steam is discharged, and when the raw material is used, it is hydrolyzed, pyrolyzed, dried, and processed into feed and raw materials.
- waste is pyrolyzed to generate electricity using the obtained gas as a heat source.
- gaseous substances consisting of oxygen and water vapor are supplied to the waste injected into the gas and heated.
- the waste used as fuel is a highly humid material such as raw sewage, the water content is as high as 8 so that it is very pyrolyzed and cannot generate enough gas.
- High-pressure steam is injected into the processing vessel and the fuel and the fuel according to the present invention, and the pressure inside the processing vessel is increased to 5 Pa and below 96 Pa and the temperature to 5 C above 5 C. The point is to produce a fine material by separating the connectors while holding them for 35 minutes below. Further, in order to obtain more efficient and practical properties, the conversion process is carried out by maintaining the force in the above-mentioned storage vessel at 82 82 Pa and under g Pa and the temperature at 28 C and ⁇ C for 335. Can be
- high-pressure steam is injected into the water supply charged into the processing container for the fuel and the device according to the present invention, and the pressure in the processing container is increased to 75 Pa and g Pa and the temperature to 6 C and C The point is to produce a fine material by separating the binder by holding it for 5655 below. Further, in order to obtain more efficient and practical properties, the pressure in the above-mentioned storage vessel is converted by maintaining the pressure in the above-8 Pa and below 85 Pa and the temperature in the range of 2 C to 25 C for 556. .
- high-pressure steam is injected into the processing container of the fuel and the device according to the present invention, and the pressure in the processing container is increased by 65 Pa to 85 Pa, and the temperature to 8 C and C below. In this way, a fine material can be produced by separating the binder while keeping it for 459 hours. Further, in order to obtain more efficient and practical properties, the pressure in the above-mentioned storage vessel is converted to a pressure of 75 Pa above 8 OPa, and a temperature of 2 C above 26 C for 556. Understand .
- high-pressure steam is injected into the livestock introduced into the processing container of the fuel and the device according to the present invention, and the pressure in the processing container is increased by 6 Pa to 96 Pa, and the temperature to 8 C by 5 C.
- the point is to produce a fine material by separating the binder while holding it for 35 45 under C.
- the pressure in the above-mentioned storage vessel was converted to a pressure of 35 Pa above and below 75 Pa and a temperature of 35 C above 35 C for 35 45 hours. Understand .
- high-pressure steam is injected into () of the fuel and the device according to the present invention, which has been introduced into the processing vessel, and the pressure in the processing vessel is increased by 6 Pa to 86 Pa, and the temperature by C
- a fine material is produced by holding the material under the upper temperature of 25 C for 565 and converting it into a form suitable for electric power and separating the connectors.
- it is necessary to increase the pressure inside the above-mentioned physical vessel. .
- high-pressure steam is injected into the midgut gland (scallop) of the scallop shell of the scallop of the fuel and the device according to the present invention, and the force in the physical container is increased by 75 P a to 88 P The point is to produce a fine material by separating the binder while maintaining the temperature between 72 C and 24 C for 5655.
- the high-humidity waste converted in this embodiment has a high water content in sewage, sewage, peat, livestock, scallop, and the midgut gland (scallop) of scallop, and is used as a gas power source. In addition, it targets waste.
- the treatment container 2 is formed of a first-class vessel provided with a container, and the portion treats highly wet waste.
- an inlet 2 for high-humidity waste is provided in the part of the processing container 2, and an outlet 22 is provided in the lower part.
- the inlet 2 and the outlet 22 have a structure in which a jack capable of withstanding high temperature and high pressure in the processing container 2 is used when processing highly wet waste.
- the inlet 2 and the outlet 22 are provided with a stem control that does not respond to opening and closing operations unless the pressure in the processing container 2 falls below 5 Pa.
- the processing container 2 is provided with an upper sensor 23a, a lower sensor 23b, and a power sensor 24, and detects the temperature and the force in the processing container 2.
- 3 is used to uniformly pressurize and remove the high-moisture waste.
- This 3 is horizontal 3 in the longitudinal direction in the processing vessel 2. It is constructed by attaching 32 inclined forward to the face of this flat country. Hirakuni 3 can do this
- No. 3 transfers the high-humidity waste that has been thrown into the tank, and extends from the inlet 2 to the outlet 22.
- the drive motor 33 is a motor whose rotation and direction of rotation are controlled by the intermediary, and the processing container 2 is used as necessary until the highly wet waste is converted into a form suitable for electric power. Reciprocate within.
- the steam inlet means 4 has a boiler 4 for generating high-pressure steam, and a trachea 42 for supplying the steam generated from the boiler 4 into the processing vessel 2.
- the steam generated in the boiler is maintained at a constant value, and the pressure in the processing vessel 2 and the pressure of the high-pressure steam are adjusted. Since the degree is determined in association with the pressure of the pressurized steam, the inside of the processing vessel 2 is maintained at a high temperature. Further, the air supply pipe 42 is connected to the processing container 2 in a horizontal direction at a position higher than the flat country 3.
- the pressure 5 is 5 which can be freely opened and closed by electric control.
- a cooling 8 is connected to the exhaust pipe 52 via a sensor 7, so that the steam from the processing vessel 2 is cooled and converted to be supplied to the wastewater 9.
- the signer 7 can be installed in the city area, etc., after the noise ordinance has been cleared.
- control means 6 is connected to 3, the steam input means 4 and 5 electricity, and controls them.
- the control means 6 controls the rotation direction and the rotation speed of the driving table 33 to control the feeding time of the highly wet waste in the processing container 2. Further, the control means 6 removes the high-moisture waste in the processing vessel 2.
- the steam input by the steam input means 4 is controlled so as to maintain a predetermined force for converting to a state suitable for an electric power for a certain period of time. If the temperature and the power in the processing vessel 2 decrease, the pressure of the steam from the steam inlet 4 is increased and the power is increased. Conversely, when the temperature or the power in the processing vessel 2 increases, the pressure 5 is released to exhaust the high-pressure water vapor and reduce the power.
- the control means 6 is connected to the sensors 23a and 23b and the power sensor 24 in the processing vessel 2 and controls the temperature and the power in the processing vessel 2 at predetermined values based on these results. I'm docked.
- high-humidity waste is charged into the processing container 2 from the charging port 2. At this time, come .
- the husk is processed using the scallop of this embodiment. Specifically, the scallop with slaked lime is mixed with the scallop. ⁇ 45 Pa ⁇ 96 MPa, more preferably ⁇ 65 Pa ⁇ 85 P Processed with 5 a held.
- the shell thus treated is as soft as cotton. By mixing the shell material, it is possible to safely adjust the water content even though it is expensive but not used.
- the internal pressure of the treatment for each high-humidity waste to be introduced, the internal pressure of the treatment, the time for maintaining the constant pressure, and the internal pressure corresponding to the fixed force are set in the control means 6.
- it is the force required to convert various wet wastes in the set vessel into a form suitable for electric power.
- it is preferable to set the pressure holding time to a time at which the high-moisture waste starts hydrolysis, and a time sufficient for the high-moisture waste to be converted into a state suitable for electric power. .
- it is set in the container each time it is accompanied by the power of steam.
- the high-moisture waste put into the processing container 2 is transferred to the outlet 22 while being enlarged by 32.
- the processing may not be completed in only one direction, but in this case, the driving Then, it was transferred to the inlet 2 and reciprocated. Thereby, a sufficient time can be obtained even in the processing vessel 2.
- control means 6 keeps the temperature and the power inside the processing vessel 2 at the predetermined temperature and the power based on the results of the sensors 23 a 23 b and the calorimeter 24. Thus, the steam inlet means 4 and 5 are controlled.
- the control means 6 controls the steam input means 4 to stop the introduction of steam, and controls the pressure 5 to release 5.
- the high-pressure steam in the processing vessel 2 is exhausted to the exhaust pipe 52, and the pressure in the processing vessel 2 is reduced.
- the control means 6 controls the steam input means 4 to stop the introduction of steam, and controls the pressure 5 to release 5.
- the high-pressure steam in the processing vessel 2 is exhausted to the exhaust pipe 52, and the pressure in the processing vessel 2 is reduced.
- the control means 6 controls the steam input means 4 to stop the introduction of steam, and controls the pressure 5 to release 5.
- the high pressure of the processing vessel 2 is 96 Pa, it cannot be performed at a pressure higher than that.However, if the temperature and pressure are excessively high or the processing is performed for a long time, the calorific value decreases. Note that
- the physical conditions for reducing the water content without changing the water content and converting the fuel into a state suitable for fuel, especially for electricity are as follows. It is preferable to maintain a pressure of 5 Pa above 96 Pa below the temperature and a temperature of 35 C above 5 C below 35 C, and more preferable to keep the pressure above 82 Pa above g Pa below 2 It is a condition to hold for 3 335 times above 8 C and below C. ⁇ The meaning of holding for a certain time is to add a condition for decomposing. The timing is such that the solution as soon as possible starts slowly, and then the decomposition proceeds along the mosquito. At this time, the water and steam contained in the water are cooled, and the water thus generated is converted into a substance having an appropriate water content with a change in pressure.
- the mud was treated as shown in 5. Prior to this, the water content was 8 and the possession was 55. On the other hand, the pressure and the interval in the processing container 2 were changed for the processing. The sludge water has melted in, so the time is longer than in other places. As a result of the test, when the pressure in the processing vessel 2 was maintained at -45 Pa / 75 Pa and the temperature at 4 CC for 556, However, the water content was 69, which was too impractical because of too much water content for electricity. However, like the implementation, Water is apt to be generated due to the dissociation and dissociation of the nucleosides, and the water content drops to about half if left overnight.
- the pressure in the processing vessel 2 was maintained at 75 Pa and 8 Pa, and the temperature was maintained at 6 C 2 C, and 556 processing was performed. As a result, the water rate in the treatment is 39 little, and
- the processing in the processing vessel 2 was maintained at 8 Pa and 85 Pa, and the temperature was maintained at 2 C 25 C and 55 6 processing was performed.
- the water rate of the treatment is almost 23, which is almost equal to that of 38.
- the pressure in the processing vessel 2 was kept at 85 P a ⁇ g Pa and the temperature was kept at 2 C C to carry out 55 65 treatment. As a result, almost complete water was recognized, and although the water content in the treatment decreased to 225, the holding amount decreased to 7 of the pre-treatment amount, and the heat of 99
- the physical conditions for reducing the water content without losing the amount of sewage, converting the fuel into a state suitable for fuel, particularly gas power generation are as follows. It is preferable to maintain the pressure in container 2 at 75 Pa above g Pa below 55 ° C and 6 C above C below 55 65, more preferably at 8 OP a above 85 Pa below This is a condition where the temperature is maintained at 2 C above 25 C for 556.
- FIG. 8 is a view showing a state after the processing.
- the amount of water it is not preferable to increase the power or the space any more. 040
- the amount of water is not lost, the water rate is reduced, and fuel, especially gas
- the physical conditions for converting to a state suitable for the material used are: the pressure in the processing vessel 2 is 65 Pa above 85 Pa below, and the temperature is 8 C It is preferable to maintain the pressure for 459 under C, and more preferable to maintain the pressure at 75 Pa to 8 Pa under temperature and the temperature at 2 oC to 26 C for 556.
- the water content of the treatment was 25%.
- the physical conditions for converting the peat into a form suitable for fuel, especially for electric power, without reducing the water content without losing the amount of peat It is preferable to maintain the pressure in the processing vessel 2 at 5 Pa over g Pa under, and the temperature at C over C for 26 for more preferably ⁇ It is the condition that the temperature is maintained for 25 3 above 7 Pa, 8 Pa below, and 24 C below C.
- the processing pressure in the processing container 2 is set to 7 Pa, 75 Pa, and the temperature to 25 C 2
- Example 5 the physical conditions for reducing the water content without losing the amount of livestock, and converting it to a form suitable for fuel, especially for electricity, are as follows: Pressure inside 2 ⁇ 6 Pa above 96 Pa below, temperature 8 C It is preferable to maintain the pressure at 35 ° C under 35 C for 35 45 hours, and more preferable to maintain the pressure at 7 Pa to 75 Pa under temperature and the temperature at 25 ° C. under C for 35 45 hours.
- the water content of the treated squid grew to 32.28, which was almost appropriate, and was held at 7.2.
- the size of the squid was small, but under the above conditions, the water volume could be reduced to about 32 by keeping the pretreatment volume at 5 degrees. This is a practical area for gas power generation.
- the pressure inside the processing vessel 2 was kept at 7 gPa and gPa, and the temperature was kept at CC, and 6595 treatment was performed. As a result, the water content of the treated organs was reduced to 29553, but it was reduced to 4.99, making it inefficient as a gas power source.
- Example 6 according to the physical conditions for reducing the water content without losing the amount of squid offal and converting it into a property that can be used as a fuel, particularly as a material for electricity, It is preferable to maintain the pressure in the processing vessel 2 at 6 Pa above 86 Pa below, and to maintain the temperature between C above 25 C below 565 for 655, and more preferably to maintain the pressure above 7 Pa above Under the conditions of 86 Pa, the temperature is maintained at 65 ° C. above 72 C for 565.
- scallop intestinal glands were treated as shown in 5 as high wet waste.
- the water content before this scallop intestinal gland was 85 and was retained at 79.
- the scallop intestinal gland was subjected to 456 treatment while maintaining the pressure in the processing container 2 at 66 Pa and 77 Pa and the temperature at CC.
- the water content of the intestinal glands of the treated scallop was 725, which was not reduced and decreased to 6.9. This is necessary because the water content is too high, and it is not practical for electricity.
- the processing pressure in processing vessel 2 was 75 Pa 88 Pa and the temperature was 72. C2.
- the amount of the midgut gland of the scallop is reduced, the water content is reduced, and the scallop is converted into a form that can be used as a fuel, particularly as a material for electricity.
- the processing conditions are as follows: the pressure inside the processing vessel 2
- FIG. 52 shows a microscopic photograph of the waste of the treatment. 7 is before sewage The later microscope is true, 8 is a commentary on 7. 9 is a microscopic image of other waste.
- the water is dehydrated before the treatment, but water is limited because bacteria form a cake and store moisture inside.
- the bacteria were destroyed and dispersed by the treatment.
- those of fibers are supplied as moisture.
- the treatment is fine, the water contained therein is easy to escape, and a fruit that keeps the dehydration can be obtained.
- it since it is extremely fine and extremely fluid, it can be directly irradiated as a fuel, or can be directly mixed with the body and shot.
- the material can be formed by freely adjusting the degree, hardness, shape, particle size and the like. Therefore, when it is used as a material for gas electricity, one heat can be given to the fuel body, so that there is a result that the fuel gasification can be efficiently performed.
- the present embodiment even for highly burned and wet waste, the loss of heat is suppressed and the water content is reduced, making it suitable not only for general use but also for electricity for conditions. It can be converted to other properties. Therefore, it can be used as a gas power equipment management facility.
- a condition for converting highly wet waste into a form suitable for electric power was determined.
- the property is suitable as well as a general one.
- it usually takes more than 36 hours since June to reach the point where natural creatures use natural organisms to decompose high-humidity waste. Do this According to the state system, the fuel can be produced in about 6 minutes to 9 hours including the time, and it can be safely processed under aseptic conditions. Note that the present invention is not limited to the above-described embodiment, but can be modified.
- the drainage 9 is not provided, but as shown in 2, a spare may be provided separately.
- the pressure of the water discharged from the outlet 22 of the sensor 7 is adjusted so that the discharged water is cured.
- 006 shows the state of fuel production according to the present invention.
- FIG. 9 is a table showing the physical conditions and results of the first embodiment to the seventh embodiment.
- 3 is a digital image showing the raw image before processing.
- 62 is a digital image showing mud after being processed under appropriate processing conditions.
- 83 is a digital image showing fish after being processed under appropriate processing conditions.
- 146 is a digital image showing the organ after processing under appropriate processing conditions.
- 167 is a digital image showing the midgut gland of scallop after processing under suitable processing conditions.
- 17 is a microscopic photograph comparing before and after conditions according to the light, () is a microscopic photograph before sewage mud treatment, and () is a microscopic photograph of the treatment.
- FIG 20 shows another embodiment of the fuel device according to the present invention.
Abstract
Description
Claims
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
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AU2005226345A AU2005226345B2 (en) | 2004-03-26 | 2005-03-24 | Process for fuel production and fuel production apparatus |
BRPI0506172 BRPI0506172A (pt) | 2004-03-26 | 2005-03-24 | processo para produção de combustìvel e aparelho para produção de combustìvel |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
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JP2004-092463 | 2004-03-26 | ||
JP2004092463A JP3613567B1 (ja) | 2004-03-26 | 2004-03-26 | 燃料製造装置および燃料製造方法 |
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WO2005093013A1 true WO2005093013A1 (ja) | 2005-10-06 |
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PCT/JP2005/005326 WO2005093013A1 (ja) | 2004-03-26 | 2005-03-24 | 燃料製造方法および燃料製造装置 |
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JP (1) | JP3613567B1 (ja) |
CN (1) | CN1771315A (ja) |
AU (1) | AU2005226345B2 (ja) |
BR (1) | BRPI0506172A (ja) |
TW (1) | TW200531932A (ja) |
WO (1) | WO2005093013A1 (ja) |
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JP3613567B1 (ja) * | 2004-03-26 | 2005-01-26 | 株式会社西村組 | 燃料製造装置および燃料製造方法 |
CN101290121B (zh) * | 2007-04-18 | 2011-02-09 | 深圳市环源科技发展有限公司 | 湿污泥干化焚烧处理系统与工艺 |
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WO2009072454A1 (ja) * | 2007-12-03 | 2009-06-11 | Cdm Consulting Co., Ltd | バイオマスの処理方法 |
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CN101758059B (zh) * | 2009-12-24 | 2012-05-30 | 华南农业大学 | 垃圾与污泥的高压热解处理方法与系统及其应用 |
CN102319718A (zh) * | 2011-07-06 | 2012-01-18 | 加拿大国原企业有限公司 | 一种垃圾处理方法 |
Also Published As
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CN1771315A (zh) | 2006-05-10 |
AU2005226345B2 (en) | 2008-05-01 |
AU2005226345A1 (en) | 2005-10-06 |
JP2007075659A (ja) | 2007-03-29 |
JP3613567B1 (ja) | 2005-01-26 |
BRPI0506172A (pt) | 2006-10-31 |
TW200531932A (en) | 2005-10-01 |
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