WO2006072999A1 - Procédé de fabrication de combustible carboné liquide et appareil correspondant - Google Patents

Procédé de fabrication de combustible carboné liquide et appareil correspondant Download PDF

Info

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
Authority
WO
WIPO (PCT)
Prior art keywords
carbon material
carbon
fuel
liquid carbon
oxygen
Prior art date
Application number
PCT/JP2005/000325
Other languages
English (en)
Japanese (ja)
Inventor
Megumi Yamada
Mamoru Itoh
Original Assignee
Megumi Yamada
Mamoru Itoh
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Megumi Yamada, Mamoru Itoh filed Critical Megumi Yamada
Priority to PCT/JP2005/000325 priority Critical patent/WO2006072999A1/fr
Publication of WO2006072999A1 publication Critical patent/WO2006072999A1/fr

Links

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
    • 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.

Landscapes

  • 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

L’invention permet d’obtenir un matériau carboné de forte concentration en carbone fixe. Ce matériau carboné, de forte concentration en carbone fixe, est réduit en poudre et mélangé à de l’eau pour constituer un combustible carboné liquide en état émulsifié. L’atomisation de ce combustible avec une buse spéciale et la pulvérisation en continu de ce combustible sur un élément de chauffage étant chauffé pour atteindre une température élevée ou sur une flamme permettent d’obtenir une combustion continue. Le combustible est alors utilisable comme énergie de substitution au pétrole. Une substance organique (K) est décomposée thermiquement dans une atmosphère fermée exempte d’oxygène par chauffage indirect à basse température pour donner un matériau carboné (M). Ce matériau carboné est réduit en poudre. On mélange une proportion d’eau donnée avec le matériau carboné en poudre pour produire un combustible carboné liquide (W).
PCT/JP2005/000325 2005-01-06 2005-01-06 Procédé de fabrication de combustible carboné liquide et appareil correspondant WO2006072999A1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
PCT/JP2005/000325 WO2006072999A1 (fr) 2005-01-06 2005-01-06 Procédé de fabrication de combustible carboné liquide et appareil correspondant

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
PCT/JP2005/000325 WO2006072999A1 (fr) 2005-01-06 2005-01-06 Procédé de fabrication de combustible carboné liquide et appareil correspondant

Publications (1)

Publication Number Publication Date
WO2006072999A1 true WO2006072999A1 (fr) 2006-07-13

Family

ID=36647487

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/JP2005/000325 WO2006072999A1 (fr) 2005-01-06 2005-01-06 Procédé de fabrication de combustible carboné liquide et appareil correspondant

Country Status (1)

Country Link
WO (1) WO2006072999A1 (fr)

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61225287A (ja) * 1985-03-29 1986-10-07 Tsuneo Masuda 炭化物水スラリ−およびその製造方法ならびに製造装置
JP2000008054A (ja) * 1998-06-18 2000-01-11 Mn Engineering Kk 液状化燃料
JP2002003855A (ja) * 2000-06-23 2002-01-09 Ngk Insulators Ltd 炭化物の製造方法
JP2002020758A (ja) * 2000-07-05 2002-01-23 Yusuke Tanaka 熱処理の方法
JP2003213271A (ja) * 2002-01-20 2003-07-30 Kenji Yamane 有機性汚泥の炭化方法およびその炭化装置
JP2004163075A (ja) * 2002-11-13 2004-06-10 Tokyo Electric Power Co Inc:The 燃料貯蔵装置、燃料供給装置及び発電システム

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61225287A (ja) * 1985-03-29 1986-10-07 Tsuneo Masuda 炭化物水スラリ−およびその製造方法ならびに製造装置
JP2000008054A (ja) * 1998-06-18 2000-01-11 Mn Engineering Kk 液状化燃料
JP2002003855A (ja) * 2000-06-23 2002-01-09 Ngk Insulators Ltd 炭化物の製造方法
JP2002020758A (ja) * 2000-07-05 2002-01-23 Yusuke Tanaka 熱処理の方法
JP2003213271A (ja) * 2002-01-20 2003-07-30 Kenji Yamane 有機性汚泥の炭化方法およびその炭化装置
JP2004163075A (ja) * 2002-11-13 2004-06-10 Tokyo Electric Power Co Inc:The 燃料貯蔵装置、燃料供給装置及び発電システム

Similar Documents

Publication Publication Date Title
CA2559875C (fr) Procede et appareil de traitement de dechets
WO2001010978A1 (fr) Procede de traitement de dechets combustibles
WO2017158649A1 (fr) Appareil de production de biomasse végétale semi-carbonisée
WO2014069234A1 (fr) Système de traitement et dispositif de traitement
JP2010106133A (ja) 廃棄物の燃料化方法および装置
CN101264479B (zh) 碳化装置
WO2015172265A1 (fr) Dispositif de régénération de source d'énergie perdue
CN106594756A (zh) 一种垃圾焚烧炉
WO2006072999A1 (fr) Procédé de fabrication de combustible carboné liquide et appareil correspondant
JP2008106209A (ja) 分散型発電機能付き小型炭化炉
JPH10130663A (ja) 液状炭素燃料の製造方法及びその装置
CN212673222U (zh) 一种废弃物的处理设备
JP2023117258A (ja) 熱分解処理装置
Sahu et al. CO2 pyrolysis and gasification of COVID‐19 based wastes (overall gown) with Indian high ash coal
JP2022521270A (ja) 都市固形廃棄物の高度な熱化学変換処理のための方法及び反応器
CN115515728A (zh) 含废塑料的一般废弃物的再生资源化系统和方法、及用于其的远红外线催化剂还原处理装置
CN104998541A (zh) 低温热解-催化降解处理焚烧飞灰中挥发性有机物的装置
KR20010110384A (ko) 탄화연료용 폐기물 재활용 방법
JP2024004322A (ja) 熱分解装置
JP6925081B1 (ja) 廃棄物減容処理方法および廃棄物減容処理システム
JPH1199373A (ja) ダイオキシン等の有害ガスを発生させない廃棄物の処理方法とその装置
TW201542978A (zh) 廢棄物能源再生裝置
JP2007077717A (ja) 建築用ボード及びその製造方法
MD3193B2 (en) Process for thermochemical gasification of carboniferous raw material
TW202206196A (zh) 廢棄物的再生資源處理裝置及其方法

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application
NENP Non-entry into the national phase

Ref country code: DE

32PN Ep: public notification in the ep bulletin as address of the adressee cannot be established

Free format text: NOTING OF LOSS PURSUANT TO RULE 69(1) EPC (EPO FORM 1205A DATED 10-10-2007 )

122 Ep: pct application non-entry in european phase

Ref document number: 05703564

Country of ref document: EP

Kind code of ref document: A1

WWW Wipo information: withdrawn in national office

Ref document number: 5703564

Country of ref document: EP

NENP Non-entry into the national phase

Ref country code: JP