JP3579792B2 - Carbonization system - Google Patents
Carbonization system Download PDFInfo
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- JP3579792B2 JP3579792B2 JP2000327447A JP2000327447A JP3579792B2 JP 3579792 B2 JP3579792 B2 JP 3579792B2 JP 2000327447 A JP2000327447 A JP 2000327447A JP 2000327447 A JP2000327447 A JP 2000327447A JP 3579792 B2 JP3579792 B2 JP 3579792B2
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- Prior art keywords
- condenser
- carbonization system
- liquefied
- fuel
- cooled
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- Expired - Fee Related
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
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- Gasification And Melting Of Waste (AREA)
- Processing Of Solid Wastes (AREA)
- Coke Industry (AREA)
Description
【0001】
【発明の属する技術分野】
この発明は、対象物を加熱処理して有用物質を取り出し有害物を外部に出さず環境汚染を防ぐ炭化システムに関するものである。
【0002】
【従来の技術】
従来より、対象物を加熱処理して有用物質を取り出す炭化システムがある。
【0003】
この炭化システムでは、木質系廃材・廃棄物などの対象物を熱分解炉で加熱処理(熱分解)し、発生した木煙をコンデンサー(冷却器)で冷却液化する。この蒸留液化物は分留用ボイラーで分留し、低沸点留分、木酢液、高沸点留分残渣などに分ける。
【0004】
この炭化システムによると、前記木酢液留分からは精製木酢液を取り出すことができ、このように木炭や木酢液などの有用物質を得ることができる。
【0005】
ところで、対象物を加熱処理する際には燃料の燃焼時の煙などの二次汚染物が発生するが、外部環境に有害な物質や有害の可能性がある物質はできるだけ放出したくないという問題があった。
【0006】
【発明が解決しようとする課題】
そこでこの発明は、従来よりも外部環境に有害な物質を放出しない炭化システムを提供しようとするものである。
【0007】
【課題を解決するための手段】
前記課題を解決するためこの発明では次のような技術的手段を講じている。
▲1▼ この発明の炭化システムは、対象物を加熱処理し、発生したガス成分をコンデンサーで冷却液化するものであって、加熱処理の際に発生する燃料の燃焼時の二次汚染物もコンデンサーで冷却液化するようにしたことを特徴とする。
【0008】
この炭化システムでは、加熱処理の際に発生する燃料の燃焼時の二次汚染物もコンデンサーで冷却液化するようにしており、液化した状態で回収することができるので当該汚染物を大気中に排気しないで済む。
▲2▼ 付帯する生ゴミ処理プラントを加熱処理して発生したガス成分を前記コンデンサーにより冷却液化するようにしてもよい。
【0009】
このように構成すると、付帯する生ゴミ処理プラント(生ゴミ堆肥化プラントや生ゴミ炭化プラントなど)で発生したガス成分を冷却液化して有用成分を取り出すことができる。
▲3▼ 有用物質としての回収が不能な成分は高温で完全に焼却するようにしてもよい。このように、有用物質を取り出したうえで回収が最終的に不能な残渣を高温で完全に焼却すると、従来よりもさらに環境にやさしいものとなる。
▲4▼ 加熱処理の際の燃料の燃焼残渣は高温で完全に焼却するようにしてもよく、前記コンデンサーで残渣として残ったものは高温で完全に焼却するようにしてもよい。このように構成すると、従来よりもさらに環境にやさしいものとなる。
▲5▼ 焼却する際に排出されるガス成分は前記コンデンサーで冷却液化させるようにしてもよい。
【0010】
焼却炉の処理能力によって処理可能温度が低く完全に燃えて無害なものになりきれないなどは特に、これを繰り返すことよって二次汚染物を液化することができ外部に有害な物質を出さないようにすることができる。
【0011】
【発明の実施の形態】
以下、この発明の実施の形態を図面を参照して説明する。
【0012】
図1に示すように、この実施形態の炭化システムは、木質系廃材・廃棄物などの対象物を木質系熱分解炉で加熱処理(熱分解)し、発生した木煙などのガス成分をコンデンサー(冷却器)で冷却液化している。コンデンサーの数は、1つでも2つ以上に設定してもよい。
【0013】
前記コンデンサーでの蒸留液化物は分留用ボイラーで加熱して分留し、低沸点留分、木酢液、高沸点留分残渣などに分ける。前記木酢液留分からは精製木酢液を取り出し、このように木炭や木酢液などの有用物質を得ることができる。
【0014】
また、木質系熱分解炉における加熱処理の際に発生する燃料の燃焼時の二次汚染物(重油を燃やしたバーナーの煙など)もコンデンサーで冷却液化するようにしている(図示▲1▼Aの燃料燃焼時の煙)。分留用ボイラーにおける加熱処理の際に発生する燃料の燃焼時の二次汚染物もコンデンサーで冷却液化するようにしている(図示▲1▼Bの燃料燃焼時の煙)。
【0015】
さらに、付帯する生ゴミ処理プラント(生ゴミ堆肥化プラントや生ゴミ炭化プラントなど)で生ゴミを加熱処理して発生した不要なガス成分も、前記コンデンサーにより冷却液化するようにしている(図示▲1▼Cの燃料燃焼時の煙)。
【0016】
一方、木質系熱分解炉における加熱処理の際の燃料の燃焼残渣(図示▲2▼Aの燃料の燃焼残渣)や、前記生ゴミ処理プラントにおける加熱処理の際の燃料の燃焼残渣(図示▲2▼Bの燃料の燃焼残渣)、分留用ボイラー(図示▲2▼Cの燃料の燃焼残渣)やコンデンサー(図示▲3▼の液化時の固形残渣)で残渣として残ったものは、焼却炉に入れて高温で完全に焼却するようにしている。
【0017】
また有用物質としての回収が不能な成分も、前記焼却炉により高温で完全に焼却するようにしている。ここで、これらを焼却炉にて焼却する際に排出されるガス成分は前記コンデンサーに導いて冷却液化させるようにしている(図示▲4▼の燃焼時に生成する気体など)。
【0018】
次に、この実施形態の炭化システムの使用状態を説明する。
【0019】
この炭化システムでは、加熱処理の際に発生する燃料の燃焼時の二次汚染物(図示▲1▼Aの燃料燃焼時の煙)もコンデンサーで冷却液化するようにしており、液化した状態で回収することができるので当該汚染物を大気中に排気しないで済む。すなわち、二次汚染物も液化して回収し大気中に排気しないで済むので、従来よりも外部環境に有害な物質や有害の可能性がある物質を放出しないという利点がある。
【0020】
また分留用ボイラーにおける加熱処理の際に発生する燃料の燃焼時の二次汚染物(図示▲1▼Bの燃料燃焼時の煙)や、付帯する生ゴミ処理プラントを加熱処理して発生したガス成分(図示▲1▼Cの燃料燃焼時の煙)も前記コンデンサーにより冷却液化するようにしたので、従来よりも外部環境に有害な物質や有害の可能性がある物質を放出しないと共に生ゴミ処理プラントで発生したガス成分等を冷却液化して有用成分を取り出すことができるという利点がある。
【0021】
さらに、加熱処理の際の燃料の燃焼残渣(図示▲2▼Aの燃料の燃焼残渣)や、生ゴミ処理プラントにおける加熱処理の際の燃料の燃焼残渣(図示▲2▼Bの燃料の燃焼残渣)、分留用ボイラー(図示▲2▼Cの燃料の燃焼残渣)やコンデンサーで残渣として残ったもの(図示▲3▼の液化時の固形残渣)は焼却炉において高温で完全に焼却するようにしているので、従来よりもさらに環境にやさしいという利点がある。
【0022】
有用物質としての回収が不能な成分は高温で完全に焼却するようにしたので、有用物質を取り出したうえで回収が最終的に不能な残渣を高温で完全に焼却すると、従来よりもさらに環境にやさしいものとなるという利点がある。
【0023】
そのうえ、前記焼却炉で焼却する際に排出されるガス成分もコンデンサーで冷却液化させるようにしており(図示▲4▼の燃焼時に生成する気体など)、焼却炉の処理能力によって処理可能温度が低く完全に燃えて無害なものになりきれないなどは特に、これらの工程を繰り返すことによって二次汚染物を液化することができ外部に有害な物質を出さないようにすることができるという利点がある。
【0024】
このように、この炭化システムは全システムにおいて閉鎖システムをとっており、外部に有害な物質や有害の可能性がある物質は放出されないという非常に優れた利点がある。
【0025】
【発明の効果】
この発明は上述のような構成であり、次の効果を有する。
【0026】
二次汚染物も液化して回収し大気中に排気しないで済むので、従来よりも外部環境に有害な物質を放出しない炭化システムを提供することができる。
【図面の簡単な説明】
【図1】この発明の炭化システムの実施形態を説明する図。[0001]
TECHNICAL FIELD OF THE INVENTION
The present invention relates to a carbonization system that heats an object, extracts useful substances, and does not emit harmful substances to the outside to prevent environmental pollution.
[0002]
[Prior art]
BACKGROUND ART Conventionally, there is a carbonization system in which an object is subjected to a heat treatment to extract a useful substance.
[0003]
In this carbonization system, objects such as wood-based waste materials and wastes are subjected to heat treatment (pyrolysis) in a pyrolysis furnace, and the generated smoke is cooled and liquefied by a condenser (cooler). This distilled liquefied product is fractionated by a fractionation boiler and divided into a low boiling fraction, a wood vinegar solution, a high boiling fraction residue, and the like.
[0004]
According to this carbonization system, a purified wood vinegar liquid can be taken out from the wood vinegar liquid fraction, and thus useful substances such as charcoal and wood vinegar liquid can be obtained.
[0005]
By the way, when the object is heated, secondary contaminants such as smoke generated when burning the fuel are generated. However, there is a problem that substances that are harmful or possibly harmful to the external environment are not released as much as possible. was there.
[0006]
[Problems to be solved by the invention]
Therefore, the present invention is to provide a carbonization system that does not emit any harmful substances to the external environment than before.
[0007]
[Means for Solving the Problems]
In order to solve the above problems, the present invention employs the following technical means.
{Circle around (1)} The carbonization system of the present invention heat-treats an object and cools and liquefies the gas components generated by the condenser. Secondary pollutants generated during fuel combustion during the heat treatment are also removed from the condenser. Liquefied by cooling.
[0008]
In this carbonization system, secondary contaminants generated during combustion of fuel generated during the heat treatment are also cooled and liquefied by the condenser, and can be recovered in a liquefied state, so that the contaminants are exhausted to the atmosphere. Don't do it.
{Circle around (2)} The gas component generated by heating the accompanying garbage processing plant may be cooled and liquefied by the condenser.
[0009]
With this configuration, it is possible to cool and liquefy a gas component generated in an accompanying garbage disposal plant (a garbage composting plant, a garbage carbonization plant, or the like) to extract a useful component.
{Circle around (3)} Components that cannot be recovered as useful substances may be completely incinerated at high temperatures. As described above, when the useful substance is taken out and the residue that cannot be finally recovered is completely incinerated at a high temperature, it becomes more environmentally friendly than before.
{Circle around (4)} The combustion residue of the fuel during the heat treatment may be completely incinerated at a high temperature, and the residue remaining in the condenser may be completely incinerated at a high temperature. With this configuration, it is more environmentally friendly than before.
(5) The gas component discharged during incineration may be cooled and liquefied by the condenser.
[0010]
Especially if the processing temperature is low due to the processing capacity of the incinerator and it cannot be burned completely to be harmless, especially by repeating this, secondary contaminants can be liquefied and no harmful substances are emitted to the outside Can be
[0011]
BEST MODE FOR CARRYING OUT THE INVENTION
Hereinafter, embodiments of the present invention will be described with reference to the drawings.
[0012]
As shown in FIG. 1, the carbonization system of this embodiment heats (pyrolyzes) an object such as wood-based waste material and waste in a wood-based pyrolysis furnace, and converts a gas component such as generated wood smoke into a condenser. (Cooler) is liquefied. The number of capacitors may be set to one or two or more.
[0013]
The liquefied product in the condenser is heated and fractionated by a fractionating boiler and fractionated into low-boiling fractions, wood vinegar, and high-boiling fraction residues. A purified wood vinegar liquid is taken out from the wood vinegar liquid fraction, and thus useful substances such as charcoal and wood vinegar liquid can be obtained.
[0014]
Also, secondary contaminants (such as smoke from a burner burning heavy oil) generated during the combustion of fuel generated during the heat treatment in the wood-based pyrolysis furnace are cooled and liquefied by the condenser (1A in the figure). Smoke from burning fuel). Secondary contaminants generated during the combustion of the fuel during the heat treatment in the fractionation boiler are also cooled and liquefied by the condenser (see (1) in FIG. 1B).
[0015]
Unnecessary gas components generated by heating garbage in the accompanying garbage disposal plant (garbage composting plant, garbage carbonization plant, etc.) are also cooled and liquefied by the condenser (see FIG. 1). (1) Smoke during combustion of C fuel).
[0016]
On the other hand, fuel combustion residues during the heat treatment in the wood-based pyrolysis furnace (the fuel residue of A in FIG. 2) and fuel combustion residues during the heat treatment in the garbage treatment plant (FIG. 2) ▼ Fuel residue of B), fractionation boiler (fuel residue of C in Fig. 2) and condenser (solid residue during liquefaction in Fig. 3) are left in the incinerator. To incinerate completely at high temperatures.
[0017]
Also, components that cannot be recovered as useful substances are completely incinerated at a high temperature by the incinerator. Here, the gas components discharged when these are incinerated in an incinerator are guided to the condenser to be cooled and liquefied (such as the gas generated during combustion as shown in FIG. 4).
[0018]
Next, the use state of the carbonization system of this embodiment will be described.
[0019]
In this carbonization system, secondary contaminants generated during the heat treatment during the combustion of the fuel (smoke generated during the combustion of the fuel in FIG. 1A) are also cooled and liquefied by the condenser, and collected in a liquefied state. So that the pollutants do not have to be exhausted to the atmosphere. In other words, the secondary contaminants do not have to be liquefied and collected, and do not need to be exhausted to the atmosphere. Therefore, there is an advantage that substances that are harmful or possibly harmful to the external environment are not released as compared with the related art.
[0020]
In addition, secondary contaminants generated during the combustion of the fuel during the heat treatment in the fractionation boiler (smoke generated during the combustion of the fuel shown in (1) B) and gas generated by heating the accompanying garbage treatment plant The components (smoke generated during fuel combustion of C in FIG. 1) are also cooled and liquefied by the condenser, so that substances that are harmful or potentially harmful to the external environment are not released and garbage disposal is performed. There is an advantage that useful components can be taken out by cooling and liquefying gas components and the like generated in the plant.
[0021]
Further, the fuel combustion residue at the time of the heat treatment (the fuel combustion residue of A in FIG. 2) and the fuel combustion residue at the time of the heat treatment in the garbage processing plant (the fuel combustion residue of the B in FIG. 2) ), The residue remaining in the boiler for fractionation boiler (combustion residue of fuel in Fig. 2C) and the condenser (solid residue in liquefaction in Fig. 3) is completely incinerated at high temperature in an incinerator. Therefore, there is an advantage that it is more environmentally friendly than before.
[0022]
The components that cannot be recovered as useful substances are completely incinerated at high temperatures.Therefore, if the useful substances are removed and the finally unrecoverable residues are completely incinerated at high temperatures, the environment will be more environmentally friendly than before. It has the advantage of being easy.
[0023]
In addition, the gas components discharged during incineration in the incinerator are also cooled and liquefied by a condenser (such as the gas generated during combustion in FIG. 4), and the processable temperature is low due to the processing capacity of the incinerator. In particular, there is an advantage that by repeating these steps, secondary contaminants can be liquefied and harmful substances can not be emitted to the outside, especially when they can not completely burn and become harmless .
[0024]
In this way, the carbonization system has a closed system in the whole system, and has an excellent advantage that no harmful substances or potentially harmful substances are released to the outside.
[0025]
【The invention's effect】
The present invention is configured as described above and has the following effects.
[0026]
Since the secondary contaminants do not need to be liquefied and collected and exhausted to the atmosphere, it is possible to provide a carbonization system that does not emit harmful substances to the external environment as compared with the related art.
[Brief description of the drawings]
FIG. 1 is a diagram illustrating an embodiment of a carbonization system according to the present invention.
Claims (6)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2000327447A JP3579792B2 (en) | 2000-10-26 | 2000-10-26 | Carbonization system |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2000327447A JP3579792B2 (en) | 2000-10-26 | 2000-10-26 | Carbonization system |
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| Publication Number | Publication Date |
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| JP2002129166A JP2002129166A (en) | 2002-05-09 |
| JP3579792B2 true JP3579792B2 (en) | 2004-10-20 |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| JP2005179450A (en) * | 2003-12-18 | 2005-07-07 | Japan Science & Technology Agency | Method for extracting pyroligneous acid and apparatus therefor |
| KR102633277B1 (en) * | 2023-06-21 | 2024-02-07 | 주식회사 센티넬이노베이션 | A biochar pellet production system that utilizes livestock manure without the discharge of concentrated wastewater |
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