WO2006072999A1 - Process for producing liquid carbon fuel and apparatus therefor - Google Patents

Process for producing liquid carbon fuel and apparatus therefor Download PDF

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Publication number
WO2006072999A1
WO2006072999A1 PCT/JP2005/000325 JP2005000325W WO2006072999A1 WO 2006072999 A1 WO2006072999 A1 WO 2006072999A1 JP 2005000325 W JP2005000325 W JP 2005000325W WO 2006072999 A1 WO2006072999 A1 WO 2006072999A1
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Prior art keywords
carbon material
carbon
fuel
liquid carbon
oxygen
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PCT/JP2005/000325
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French (fr)
Japanese (ja)
Inventor
Megumi Yamada
Mamoru Itoh
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Megumi Yamada
Mamoru Itoh
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Priority to PCT/JP2005/000325 priority Critical patent/WO2006072999A1/en
Publication of WO2006072999A1 publication Critical patent/WO2006072999A1/en

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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
    • C10L1/00—Liquid carbonaceous fuels
    • C10L1/32—Liquid carbonaceous fuels consisting of coal-oil suspensions or aqueous emulsions or oil emulsions
    • C10L1/326—Coal-water suspensions

Definitions

  • the present invention relates to a method and apparatus for producing liquid carbon fuel that can be used in the same manner as a petrochemical liquid fuel using various organic substances including waste.
  • the invention of the method according to claim 1 comprises thermally decomposing organic matter by low-temperature indirect heating in an oxygen-free closed sealed atmosphere.
  • a liquid carbon fuel is produced by producing a carbon material, pulverizing the carbon material, and mixing a predetermined proportion of water with the powdered carbon material.
  • the method invention according to claim 2 is characterized in that the oxygen-free closed sealed atmosphere is produced by nitrogen substitution.
  • the invention of the apparatus according to claim 3 is a carbonization part that generates a carbon material by thermally decomposing organic matter by low-temperature indirect heating in an oxygen-free closed sealed atmosphere, and a pulverization process for treating the carbon material with powder. It is characterized by comprising a processing section and a mixing processing section for mixing a predetermined proportion of water with the powdered carbon material.
  • FIG. 1 shows an embodiment of the apparatus of the present invention, which is roughly composed of a carbonization part A, a powdering part B, and a mixing part C.
  • the carbonization part A is configured to generate the carbon material W by thermally decomposing the organic substance M by low-temperature indirect heating in an oxygen-free closed sealed atmosphere.
  • an oxygen-free closed sealed state is created by injecting nitrogen gas into a pyrolysis chamber equipped with a heat-resistant, heat-insulated closed-sealed structure and having an openable / closable shut-off door and exhausting the air inside the chamber to the outside
  • the far-infrared light is applied to the peripheral wall of the thermal decomposition chamber.
  • a heating element using electromagnetic waves is placed, the room is heated by the heating element, and the organic material is indirectly heated for a predetermined time, for example, at a low temperature of about 36.degree. It is configured as follows.
  • the pulverizing section B is configured to finely pulverize the carbon material with a pulverizing crusher, an ultrasonic stirrer, etc .. In this pulverization, it is better to make the carbon material as fine as possible. It can be said that the unit of is desirable. Since there is a risk of dust explosion at this pulverization stage, it is necessary to use a material that does not apply high pressure to the fine powder, or that has sufficient humidity, and that does not use fire. It is. Care must be taken not to mix foreign matter such as metal powder into this fine powder. If it is an inorganic substance that can be finely powdered, it can be mixed.
  • the mixing processing unit C is configured to mix and process a predetermined ratio of water to the powdered carbon material M.
  • the carbon material fine powder is in a volume ratio of water 2 to 4: fine powder 8 to 6
  • the ratio that is, the powdery carbon material M is mixed by adding 20 to 40% water, and this mixing ratio is determined according to the purpose to be used and the purpose of use.
  • various additives such as combustion accelerators and oxygen replenishers may be selected and added.
  • this mixed state is put into an emulsified state using an ultrasonic vibration stirrer, etc., and this vibration stirring causes water and fine powder to mix evenly and separation from water occurs. It becomes difficult to cause a combustion reaction between each component.
  • ultrasonic waves a liquid material in which water molecules and carbon particles of fine powder are evenly distributed is obtained, and this becomes a liquid carbon fuel.
  • carbides such as fixed carbon 82%, ash 2.7%, moisture 11%, and other 4.3% are obtained in oak and kunugi, and the concentration of fixed carbon is ⁇ in other organic substances as well. 3% difference but similar carbon content
  • This is a liquid carbon fuel that is pulverized and mixed with water to form an emulsified state by mixing water with a high concentration of fixed carbon.
  • a heated body or red soot that is reddish in can be continuously burned by continuing to spray on the flame. For example, combustion begins in the atmosphere at around 5400 ° C, and the combustion rate increases as the temperature rises. The smaller the powder, the better the combustion.
  • Various additives may be mixed to increase the calorie burn.
  • waste organic matter, etc. as raw materials for carbon materials, weeds grown on the roadside, waste leaves of vegetables and fruits, and raw garbage as raw materials for carbonization
  • waste organic matter, etc. as raw materials for carbon materials
  • weeds grown on the roadside waste leaves of vegetables and fruits
  • raw garbage as raw materials for carbonization
  • the liquid carbon fuel can be used to increase or decrease the amount of heat generated by adding additives for the purpose of use, and can be used from household air-conditioning equipment to fuel for power generation.
  • NO x and SO x are hardly generated unless nitrogen or chlorine groups are contained in the components of the product, and in storage and delivery, it is normal even if it is in a powdery carbon material or in an emulsion state In the air, there is no concern about combustion as it is, safety is high, and it can be used as energy without polluting the environment.
  • FIG. 1 is an explanatory configuration system diagram of an embodiment of the apparatus of the present invention.
  • various organic substances are thermally decomposed by low-temperature indirect heating in an oxygen-free closed sealed atmosphere.
  • a carbon material is produced, the carbon material is pulverized, and a liquid carbon fuel is produced by mixing a predetermined proportion of water with the powdered carbon material.
  • Indirect low temperature heating in an oxygen-free state This is a liquid carbon fuel that can be obtained by carbonization by pyrolysis of carbon, so that a carbon material with a high fixed carbon concentration can be obtained.
  • the carbon material with such a high fixed carbon concentration is pulverized and mixed with water to form an emulsion state. For this reason, a special nozzle is used! /
  • a heated body or layer that is red in the form of a mist can be continuously burned by continuing to mist in the flame, and can be used as a substitute for crude oil. be able to.
  • the oxygen-free closed sealed atmosphere can be easily obtained by producing the oxygen-free closed sealed atmosphere by nitrogen substitution. As described above, the intended purpose can be sufficiently achieved.

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  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Processing Of Solid Wastes (AREA)
  • Carbon And Carbon Compounds (AREA)

Abstract

A carbon material having a high fixed-carbon concentration can be obtained. This carbon material, which has a high fixed-carbon concentration, is powdered and mixed with water to form a liquid carbon fuel in an emulsified state. By atomizing this fuel with a special nozzle and continuously spraying it over a heating element being red-heated at a high temperature or over a flame, continuous combustion can be attained. The fuel is hence utilizable as a petroleum-substitute energy. An organic substance (K) is thermally decomposed in an oxygen-free closed atmosphere by low-temperature indirect heating to yield a carbon material (M). This carbon material is powdered. A given proportion of water is mixed with the powdered carbon material to produce a liquid carbon fuel (W).

Description

明細書 液状炭素燃料の製造方法及ぴその装置 技術分野  TECHNICAL FIELD The manufacturing method and apparatus of liquid carbon fuel
本発明は廃棄物を含む各種有機物により石化液体燃料と同様な方法で使 用し得る液状炭素燃料の製造方法及びその装置に関するものである。 背景技術  The present invention relates to a method and apparatus for producing liquid carbon fuel that can be used in the same manner as a petrochemical liquid fuel using various organic substances including waste. Background art
従来からエネルギー源として石化液体燃料が主として使用されているが、 現在の埋蔵量ではあと数十年で枯渴してしまうと指摘され、 これに代わる 代替エネルギーの出現は必至であり、 現在、 産業廃棄物を含む不用有機物 の再利用について種々検討されているが、 その大部分は相変わらず、 焼却 処理又は埋立処理によって処分されている。  Conventionally, petrochemical liquid fuel has been mainly used as an energy source, but it has been pointed out that the current reserves will be depleted in the next few decades, and the emergence of alternative energy is inevitable. Various studies have been conducted on the reuse of waste organic matter including waste, but most of it is still disposed of by incineration or landfill.
しかしながら、 これら焼却処理又は埋立処理において、 近年は合成樹脂 と他の有機物又は無機物とが混合しているものが大量に排出されるように なり、 これに伴いそれらの分別作業も必要になり、 分別作業後において、 焼却処理又は埋立処理をしなければならず、 それだけ処理作業が困難とな り、 さらに焼却処理場の増設ゃ埋立処理地の確保も困難となっており、 社 会的にも大きな問題となっている。 発明の開示  However, in these incineration or landfill treatments, in recent years, a large amount of synthetic resin mixed with other organic or inorganic substances has been discharged, and as a result, separation work has become necessary. After work, incineration or landfill processing must be performed, which makes it difficult to handle, and it is difficult to increase the number of incineration plants and secure a landfill site. It is a problem. Disclosure of the invention
本発明はこのような不都合を解決することを目的とするもので、 本発明 のうち、 請求項 1記載の方法の発明は、 有機物を無酸素閉鎖密閉雰囲気下 において低温間接加熱により熱分解させて炭素素材を生成し、 該炭素素材 を粉化処理し、 該粉状の炭素素材に所定割合の水を混合させることにより 液状炭素燃料を製造することを特徴とするものである。  The present invention aims to solve such inconveniences. Among the present inventions, the invention of the method according to claim 1 comprises thermally decomposing organic matter by low-temperature indirect heating in an oxygen-free closed sealed atmosphere. A liquid carbon fuel is produced by producing a carbon material, pulverizing the carbon material, and mixing a predetermined proportion of water with the powdered carbon material.
請求項 2記載の方法の発明は、 上記無酸素閉鎖密閉雰囲気を窒素置換に より作製することを特徴とするものである。  The method invention according to claim 2 is characterized in that the oxygen-free closed sealed atmosphere is produced by nitrogen substitution.
請求項 3記載の装置の発明は、 有機物を無酸素閉鎖密閉雰囲気下におい て低温間接加熱により熱分解させて炭素素材を生成する炭素化部と、 該炭 素素材を粉ィ匕処理する粉化処理部と、 該粉状の炭素素材に所定割合の水を 混合させる混合処理部とを備えてなることを特徴とするものである。  The invention of the apparatus according to claim 3 is a carbonization part that generates a carbon material by thermally decomposing organic matter by low-temperature indirect heating in an oxygen-free closed sealed atmosphere, and a pulverization process for treating the carbon material with powder. It is characterized by comprising a processing section and a mixing processing section for mixing a predetermined proportion of water with the powdered carbon material.
図 1は本発明装置の実施の形態例を示し、 大別すると、 炭素化部 Aと、 粉化処理部 Bと、 混合処理部 Cとから構成される。  FIG. 1 shows an embodiment of the apparatus of the present invention, which is roughly composed of a carbonization part A, a powdering part B, and a mixing part C.
この場合、 炭素化部 Aは有機物 Mを無酸素閉鎖密閉雰囲気下において低 温間接加熱により熱分解させて炭素素材 Wを生成するように構成されてい る。 具体的には、 耐熱、 断熱閉鎖密閉構造にして開閉自在な遮断扉を備え る加熱分解室内に窒素ガスを注入すると共にその室内の空気を室外に排出 して、 無酸素閉鎖密閉状態を作製し、 この加熱分解室の周壁に遠赤外線ヒ ータゃ電磁波を利用した加熱体を配置し、 加熱体により室内を加熱し、 有 機物を例えば 3 6 0 ° (：〜 4 5 0 °C程度の低温度条件で所定時間間接加熱す るように構成されている。 In this case, the carbonization part A is configured to generate the carbon material W by thermally decomposing the organic substance M by low-temperature indirect heating in an oxygen-free closed sealed atmosphere. Specifically, an oxygen-free closed sealed state is created by injecting nitrogen gas into a pyrolysis chamber equipped with a heat-resistant, heat-insulated closed-sealed structure and having an openable / closable shut-off door and exhausting the air inside the chamber to the outside The far-infrared light is applied to the peripheral wall of the thermal decomposition chamber. A heating element using electromagnetic waves is placed, the room is heated by the heating element, and the organic material is indirectly heated for a predetermined time, for example, at a low temperature of about 36.degree. It is configured as follows.
粉化処理部 Bは、 粉状化破砕機、 超音波撹拌機等により炭素素材を微粉 末化するように構成され、 この粉化に際しては、 炭素素材をできるだけ微 粉末とした方がよく、 ミクロンの単位が望ましいといえる。 この微粉化の 段階では粉塵爆発の危険性が有るため微粉末に高圧が掛からないようなェ 夫や十分な湿度を持たせてり、 火元となるようなものを使わな ヽことが必 要である。 この微粉末に金属粉等異物が混合しないような注意も必要であ る。無機物で微粉末ィ匕できるものであれば混合していても差し支えがない。 混合処理部 Cは、 この粉状の炭素素材 Mに所定割合の水を混合処理する ように構成され、 例えば、 炭素素材の微粉末を容積比率で、 水 2〜4 ：微 粉末 8〜 6の割合、 即ち粉状の炭素素材 Mに水 2 0〜 4 0 %を加えて混合 することになり、 この混合比率はその利用すべき目的に応じて決定するこ とになり、 又その使用目的に応じて各種添加剤、 例えば燃焼促進剤や酸素 補給剤等を選定し添加することもある。 具体的には、 この混合状態のもの を超音波振動撹拌器等を使つてェマルジョン状態とすることになり、 この 振動撹拌によって水と微粉末は均等に混合し合 、、 水との分離が起きにく くなり、 各構成成分間の燃焼反応が起きやすい状態になる。 この場合超音 波を利用するために水の分子と微粉末の炭素の分子が均等分布した液体状 のものが得られ、 これが液状炭素燃料となる。  The pulverizing section B is configured to finely pulverize the carbon material with a pulverizing crusher, an ultrasonic stirrer, etc .. In this pulverization, it is better to make the carbon material as fine as possible. It can be said that the unit of is desirable. Since there is a risk of dust explosion at this pulverization stage, it is necessary to use a material that does not apply high pressure to the fine powder, or that has sufficient humidity, and that does not use fire. It is. Care must be taken not to mix foreign matter such as metal powder into this fine powder. If it is an inorganic substance that can be finely powdered, it can be mixed. The mixing processing unit C is configured to mix and process a predetermined ratio of water to the powdered carbon material M. For example, the carbon material fine powder is in a volume ratio of water 2 to 4: fine powder 8 to 6 The ratio, that is, the powdery carbon material M is mixed by adding 20 to 40% water, and this mixing ratio is determined according to the purpose to be used and the purpose of use. Depending on the case, various additives such as combustion accelerators and oxygen replenishers may be selected and added. Specifically, this mixed state is put into an emulsified state using an ultrasonic vibration stirrer, etc., and this vibration stirring causes water and fine powder to mix evenly and separation from water occurs. It becomes difficult to cause a combustion reaction between each component. In this case, in order to use ultrasonic waves, a liquid material in which water molecules and carbon particles of fine powder are evenly distributed is obtained, and this becomes a liquid carbon fuel.
この実施の形態例は上記構成であるから、 各種の有機物 Kを無酸素閉鎖 密閉雰囲気下において低温間接加熱により熱分解させて炭素素材 Mを生成 し、 該炭素素材を粉化処理し、 該粉状の炭素素材に所定割合の水を混合さ せることにより液状炭素燃料 Wを製造することになり、 無酸素状態の中で の低温間接加熱による熱分解により炭素化された炭素素材には酸化物が存 在発生せず、 固定炭素濃度の高い炭素素材を得ることができる、 例えば、 固定炭素濃度が 8 0 %以上のものも得ることができる、 更に具体的には 4 5 0 °Cにて炭素化を行なった場合は、 ナラ、 クヌギでは固定炭素 8 2 %、 灰分 2 . 7 %、 水分 1 1 %、 その他 4.3 %という炭化物が得られ、 その他 の有機物においても、 固定炭素の濃度は ± 3 %程度の違いは有るが同程度 の炭素素材が得られる、 し力 し、 このような固定炭素濃度の高い炭素素材 を粉化処理し、 水を混合してェマルジョン状態とした液状炭素燃料である から、 特殊ノズルを用 、霧状にして高温で赤化している加熱体或!/ヽは炎に 噴霧し続けることによって連続的な燃焼を得ることができる。 例えば、 5 4 0 °C前後から大気中で燃焼を始め、 温度が上がるにしたがって燃焼速度 は速くなり、 この粉体の大きさは小さいほどよく燃焼する。  Since this embodiment has the above-described configuration, various organic substances K are pyrolyzed by low-temperature indirect heating in an oxygen-free closed and sealed atmosphere to produce carbon material M, and the carbon material is pulverized. The liquid carbon fuel W is produced by mixing a predetermined proportion of water with the carbon material in the form of carbon, and the carbon material carbonized by thermal decomposition by low-temperature indirect heating in an oxygen-free state is an oxide. Can be obtained, and a carbon material with a high fixed carbon concentration can be obtained.For example, a carbon material having a fixed carbon concentration of 80% or more can be obtained, more specifically at 45 ° C. When carbonization is performed, carbides such as fixed carbon 82%, ash 2.7%, moisture 11%, and other 4.3% are obtained in oak and kunugi, and the concentration of fixed carbon is ±± in other organic substances as well. 3% difference but similar carbon content This is a liquid carbon fuel that is pulverized and mixed with water to form an emulsified state by mixing water with a high concentration of fixed carbon. A heated body or red soot that is reddish in can be continuously burned by continuing to spray on the flame. For example, combustion begins in the atmosphere at around 5400 ° C, and the combustion rate increases as the temperature rises. The smaller the powder, the better the combustion.
尚、 燃焼カロリーを高めるために各種添加剤を混合してもよい。 Various additives may be mixed to increase the calorie burn.
従って、 不用になった有機物等を炭素素材の原料として考えるならば、 道端に生えている雑草、 野菜果物の不用枝葉、 生ゴミを炭化の原料として 考えるならば、 原油の埋蔵量力、枯渴する時期を相当期間伸ばすことが出来 る、 又は産業廃棄物を原料として使用することによつて資源の再利用を図 ることができて焼却場の新設や埋立地施設の確保の問題も解消され、 有害 排ガスの発生がないため、 環境保護にも役立つと共に産業廃棄物の処理費 用の節減もでき、 又この液状炭素燃料をボイラー等で燃焼させた場合には 重油、 石油、 石炭などを燃焼させた場合に発生する窒素酸化物などの発生 はほとんど無く、 なぜならばこの炭素素材の構成成分は固定炭素が最も多 く、 残りは水分と灰分であるためであり、 空気 (酸素)と反応しても、 二酸 化炭素と水のみが発生するだけである。 この液状炭素燃料は、 その利用目 的のために添加剤等を加えることによつて燃焼発熱量の増減ができ、 家庭 用冷暖房機器から発電の燃料まで利用でき、 燃焼の際の排ガスもその炭化 物の成分中に窒素、塩素基などが含有しない限り NOx、 S Oxの発生は殆 どなく、 保管や配送においては、 粉状の炭素素材のまま、 或いはェマルジ ョン状態であっても通常の空気中においてはそのままでの燃焼の心配は無 く、 安全†生は高く、 環境を汚染することなくエネルギーとして利用するこ とができる。 Therefore, if we consider waste organic matter, etc. as raw materials for carbon materials, weeds grown on the roadside, waste leaves of vegetables and fruits, and raw garbage as raw materials for carbonization Considering that, it is possible to extend the reserve capacity of crude oil, the time to dry up for a considerable period of time, or to reuse resources by using industrial waste as a raw material. The problem of securing landfill facilities and landfill facilities has also been eliminated, and no harmful exhaust gas is generated, which helps protect the environment and saves on the cost of processing industrial waste. In some cases, there is almost no generation of nitrogen oxides when burning heavy oil, oil, coal, etc., because the constituents of this carbon material are the most fixed carbon, the rest are moisture and ash Therefore, even if it reacts with air (oxygen), only carbon dioxide and water are generated. The liquid carbon fuel can be used to increase or decrease the amount of heat generated by adding additives for the purpose of use, and can be used from household air-conditioning equipment to fuel for power generation. NO x and SO x are hardly generated unless nitrogen or chlorine groups are contained in the components of the product, and in storage and delivery, it is normal even if it is in a powdery carbon material or in an emulsion state In the air, there is no concern about combustion as it is, safety is high, and it can be used as energy without polluting the environment.
しかし、 この液状炭素燃料を燃焼可能な温度下において、 火元となるも のを設置し、 この液状炭素燃料を霧状にし、 適量な空気と共に火元に向か ぃ嘖霧し続けることにより、 自らの液体が含有している元素 H、 0、 じが 燃焼反応を起こし発熱燃焼することになり、 この際に微粉末が純粋な炭素 素材であれば燃焼後の排ガスには二酸化炭素と水蒸気のみが排出され、 無 害の排ガスの空中放出がなされ、 又この液状炭素燃料はその液状炭素燃料 の噴出ノズルの交換と残存灰分の取り除き部分を取り付けることによって —般に市販されているボイラーなどの燃焼機器でも使用することができる。 この液状炭素燃料の原料としての有機物は、 自然に発生してくる雑草な どのような草木でもよく、 枯れてしまったものや、 落ち葉でもよく、 産業 廃棄物でもよく、 家庭、 レストランの生ゴミでもよいため、 その原料の確 保のため山林の伐採などしなくても大量に供給でき、 その量は無尽蔵にあ るといえる。  However, by installing a source of fire at a temperature at which this liquid carbon fuel can be combusted, making this liquid carbon fuel into a mist, and continuing to mist toward the fire with an appropriate amount of air, The elements H, 0, and J contained in their liquid cause a combustion reaction and exothermic combustion.If the fine powder is a pure carbon material, only carbon dioxide and water vapor are included in the exhaust gas after combustion. The liquid carbon fuel is released into the air, and the liquid carbon fuel is burned by replacing the liquid carbon fuel injection nozzle and removing the residual ash. It can also be used in equipment. The organic matter used as the raw material for this liquid carbon fuel may be any kind of naturally occurring weed, such as withered, fallen leaves, industrial waste, household waste, restaurant garbage. For this reason, it is possible to supply a large amount without logging the forest to secure the raw materials, and the amount is inexhaustible.
尚、 本発明は上記実施の形態例に限られるものではなく、 炭素化部 A、 粉 化処理部 B、 混合処理部 Cの構造や大きさ等は適宜変更して設計される。 図面の簡単な説明  Note that the present invention is not limited to the above embodiment, and the structure and size of the carbonization part A, the pulverization part B, and the mixing part C are appropriately changed and designed. Brief Description of Drawings
図 1は本発明装置実施の形態例の説明構成系統図である。  FIG. 1 is an explanatory configuration system diagram of an embodiment of the apparatus of the present invention.
符号の説明： A炭素化部、 B粉化処理部、 C混合処理部、 K有機物、 M炭 素素材、 W液状炭素燃料。 産業上の利用可能性  Explanation of symbols: A carbonization section, B pulverization processing section, C mixing processing section, K organic matter, M carbon material, W liquid carbon fuel. Industrial applicability
本発明は上述の如く、 請求項 1又は 3記載の発明にあっては各種の有機 物を無酸素閉鎖密閉雰囲気下において低温間接加熱により熱分解させて 炭素素材を生成し、 該炭素素材を粉化処理し、 粉状の炭素素材に所定割合 の水を混合させることにより液状炭素燃料を製造することになり、 無酸素 状態の中での低温間接加熱による熱分解により炭素化されるので固定炭素 濃度の高い炭素素材を得ることができる、 このような固定炭素濃度の高い 炭素素材を粉化処理し水を混合してェマルジヨン状態とした液状炭素燃料 であるから特殊ノズルを用!/、霧状にして高温で赤化している加熱体或レヽは 炎に嘖霧し続けることによって連続的な燃焼を得ることができ、 原油の代 替エネルギーとして利用することができる。 As described above, according to the present invention, various organic substances are thermally decomposed by low-temperature indirect heating in an oxygen-free closed sealed atmosphere. A carbon material is produced, the carbon material is pulverized, and a liquid carbon fuel is produced by mixing a predetermined proportion of water with the powdered carbon material. Indirect low temperature heating in an oxygen-free state This is a liquid carbon fuel that can be obtained by carbonization by pyrolysis of carbon, so that a carbon material with a high fixed carbon concentration can be obtained. The carbon material with such a high fixed carbon concentration is pulverized and mixed with water to form an emulsion state. For this reason, a special nozzle is used! / A heated body or layer that is red in the form of a mist can be continuously burned by continuing to mist in the flame, and can be used as a substitute for crude oil. be able to.
請求項 2記載の発明にあっては、 無酸素閉鎖密閉雰囲気を窒素置換によ り作製することにより、容易に無酸素閉鎖密閉雰囲気を得ることができる。 以上所期の目的を充分達成することができる。  In the invention according to claim 2, the oxygen-free closed sealed atmosphere can be easily obtained by producing the oxygen-free closed sealed atmosphere by nitrogen substitution. As described above, the intended purpose can be sufficiently achieved.

Claims

請求の範囲 有機物を無酸素閉鎖密閉雰囲気下において低温間接加熱により熱分解 させて炭素素材を生成し、 該炭素素材を粉化処理し、 該粉状の炭素素 材に所定割合の水を混合させることにより液状炭素燃料を製造するこ とを特徴とする液状炭素燃料の製造方法。 Claims Organic materials are pyrolyzed by low-temperature indirect heating in an oxygen-free, closed and sealed atmosphere to produce a carbon material, the carbon material is pulverized, and a predetermined proportion of water is mixed with the powdered carbon material. A liquid carbon fuel production method, characterized in that liquid carbon fuel is produced.
上記無酸素閉鎖密閉雰囲気を窒素置換により作製することを特徴とす る請求項 1記載の液状炭素燃料の製造方法。 2. The method for producing a liquid carbon fuel according to claim 1, wherein the oxygen-free closed sealed atmosphere is produced by nitrogen substitution.
有機物を無酸素閉鎖密閉雰囲気下において低温間接加熱により熱分解 させて炭素素材を生成する炭素化部と、 該炭素素材を粉化処理する粉 化処理部と、 該粉状の炭素素材に所定割合の水を混合させる混合処理 部とを備えてなる液状炭素燃料の製造装置。 A carbonization part that thermally decomposes organic matter by low-temperature indirect heating in an oxygen-free closed sealed atmosphere to generate a carbon material, a pulverization part that pulverizes the carbon material, and a predetermined ratio to the powdery carbon material An apparatus for producing a liquid carbon fuel comprising a mixing processing unit for mixing water.
PCT/JP2005/000325 2005-01-06 2005-01-06 Process for producing liquid carbon fuel and apparatus therefor WO2006072999A1 (en)

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Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61225287A (en) * 1985-03-29 1986-10-07 Tsuneo Masuda Carbide-water slurry, process and apparatus for production thereof
JP2000008054A (en) * 1998-06-18 2000-01-11 Mn Engineering Kk Liquefied fuel
JP2002003855A (en) * 2000-06-23 2002-01-09 Ngk Insulators Ltd Manufacturing method of carbide
JP2002020758A (en) * 2000-07-05 2002-01-23 Yusuke Tanaka Method for heat treatment
JP2003213271A (en) * 2002-01-20 2003-07-30 Kenji Yamane Method for carbonizing organic sludge and carbonization installation therefor
JP2004163075A (en) * 2002-11-13 2004-06-10 Tokyo Electric Power Co Inc:The Fuel storage device, fuel feeder, and power generation system

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61225287A (en) * 1985-03-29 1986-10-07 Tsuneo Masuda Carbide-water slurry, process and apparatus for production thereof
JP2000008054A (en) * 1998-06-18 2000-01-11 Mn Engineering Kk Liquefied fuel
JP2002003855A (en) * 2000-06-23 2002-01-09 Ngk Insulators Ltd Manufacturing method of carbide
JP2002020758A (en) * 2000-07-05 2002-01-23 Yusuke Tanaka Method for heat treatment
JP2003213271A (en) * 2002-01-20 2003-07-30 Kenji Yamane Method for carbonizing organic sludge and carbonization installation therefor
JP2004163075A (en) * 2002-11-13 2004-06-10 Tokyo Electric Power Co Inc:The Fuel storage device, fuel feeder, and power generation system

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