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JP2013111498A - Garbage treatment system - Google Patents

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Publication number
JP2013111498A
JP2013111498A JP2011257949A JP2011257949A JP2013111498A JP 2013111498 A JP2013111498 A JP 2013111498A JP 2011257949 A JP2011257949 A JP 2011257949A JP 2011257949 A JP2011257949 A JP 2011257949A JP 2013111498 A JP2013111498 A JP 2013111498A
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garbage
gasifier
dried
dryer
hot air
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Hirokazu Murata
博一 村田
Takashi Kurihara
栗原  隆
Katsutoshi Shibuya
勝利 渋谷
Kenji Nozaki
健次 野崎
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Shimizu Construction Co Ltd
Shimizu Corp
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Shimizu Corp
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    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/30Fuel from waste, e.g. synthetic alcohol or diesel

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Abstract

PROBLEM TO BE SOLVED: To provide a garbage treatment system capable of efficiently drying garbage and turning it into resources while suppressing generation of an odor.SOLUTION: The garbage treatment system includes a gasifier for gasifying biomass and a garbage drier for drying the garbage, waste heat of the gasifier is introduced to the garbage drier as hot air, the garbage housed inside the garbage drier is dried with the waste heat, and exhaust from the garbage drier is returned to a distribution route of the hot air distributed inside the gasifier. Also, the garbage dried in the garbage drier is supplied to the gasifier and utilized as the biomass.

Description

本発明は、生ごみの処理システムに関する。   The present invention relates to a garbage disposal system.

従来、生ごみを資源化処理する際には、大きく分けて、生ごみを微生物によって分解して減容化する微生物分解法と、生ごみを高温で乾燥させて減容化する高温乾燥法とが適用されている(例えば、特許文献1参照)。   Conventionally, when processing garbage into resources, it can be broadly divided into a microbial decomposition method that reduces the volume by decomposing the garbage with microorganisms, and a high-temperature drying method that reduces the volume by drying the garbage at a high temperature. Is applied (see, for example, Patent Document 1).

特開2004−167318号公報JP 2004-167318 A

一方、微生物分解法は、生ごみの含水率を30〜60%となるように維持するとともに60℃程度に加温し、微生物によって好気的に分解するものであるが、魚や肉などの分解時には不快な臭気が発生する。また、生ごみの含水率が70%以上であると、ただでさえ時間を要する微生物分解速度が急激に低下するとともに、嫌気状態になってメルカプタンなどが生成され、強烈な悪臭が発生する。   On the other hand, the microbial decomposition method maintains the moisture content of food waste at 30 to 60% and warms it to about 60 ° C. to decompose aerobically by microorganisms. Sometimes an unpleasant odor occurs. Further, if the moisture content of the garbage is 70% or more, the microbial decomposition rate, which requires time, is drastically reduced, and an anaerobic state is generated to generate mercaptans and a strong odor is generated.

また、高温乾燥法は、生ごみを加熱ヒーターによって例えば150℃以下に加熱して乾燥処理するものであり、含水率が80%を超える生ごみでも短時間で含水率を10%程度まで乾燥させることが可能であるが、100℃を超える温度域で処理すると、アルデヒド類などによる焦げ臭が発生する。   In addition, the high temperature drying method is a method in which raw garbage is heated to, for example, 150 ° C. or less with a heater and dried, and even when raw garbage exceeds 80%, the moisture content is dried to about 10% in a short time. However, if it is processed in a temperature range exceeding 100 ° C., a burning odor due to aldehydes or the like is generated.

このように、生ごみを減容化(資源化)処理する際に、微生物分解法では微生物分解臭、高温乾燥法では焦げ臭が発生するため、除臭装置や触媒を利用する臭気対策を講じる必要が生じ、これに伴い、生ごみの処理コストが高コストになるという問題があった。   In this way, when food waste is reduced in volume (recycling), microbial decomposition odors are generated by the microbial decomposition method, and burnt odors are generated by the high temperature drying method, so odor countermeasures using deodorizers and catalysts are taken. As a result, there is a problem that the cost of processing garbage becomes high.

上記の目的を達するために、この発明は以下の手段を提供している。   In order to achieve the above object, the present invention provides the following means.

本発明の生ごみの処理システムは、バイオマスをガス化するガス化装置と、生ごみを乾燥処理するための生ごみ乾燥機とを備え、前記ガス化装置の排熱を熱風として前記生ごみ乾燥機に導入し、前記生ごみ乾燥機内に収容した生ごみを前記排熱によって乾燥処理するとともに、前記生ごみ乾燥機からの排気を前記ガス化装置内で流通する熱風の流通経路に返送するようにしたことを特徴とする。   The garbage processing system of the present invention includes a gasifier for gasifying biomass and a garbage dryer for drying the garbage, and the garbage drying using the exhaust heat of the gasifier as hot air. The garbage introduced into the machine and dried in the garbage dryer is dried by the exhaust heat, and the exhaust from the garbage dryer is returned to the circulation path of the hot air flowing in the gasifier. It is characterized by that.

本発明の生ごみの処理システムにおいては、前記生ごみ乾燥機で乾燥処理した生ごみを前記ガス化装置に投入し、前記バイオマスとして利用することが望ましい。   In the garbage processing system of the present invention, it is desirable that the garbage, which has been dried by the garbage dryer, is introduced into the gasifier and used as the biomass.

本発明の生ごみの処理システムにおいては、ガス化装置が、例えばバイオマスを供給してガス化するガス化反応炉と、ガス化反応に必要な熱を供給する外熱炉とを備えて構成され、このガス化装置の例えば200〜600℃の高温の排熱を熱風として生ごみ乾燥機に導入することで、生ごみを短時間で乾燥処理することが可能になる。すなわち、無駄な燃料や電気を使用することなく、特に都市域では利用が難しいガス化装置の排熱を利用して、効率的に生ごみを処理することが可能になる。   In the garbage processing system of the present invention, the gasification apparatus includes, for example, a gasification reaction furnace that supplies gas for gasification and an external heating furnace that supplies heat necessary for the gasification reaction. By introducing the exhaust heat at a high temperature of, for example, 200 to 600 ° C. of the gasifier as hot air into the garbage dryer, the garbage can be dried in a short time. In other words, it is possible to efficiently treat garbage without using wasteful fuel and electricity, using exhaust heat from a gasifier, which is difficult to use particularly in urban areas.

また、このように200〜600℃の高温で生ごみを乾燥することにより、さらに生ごみ乾燥機からの排気をガス化装置内の熱風の流通経路に返送することにより、従来の高温乾燥方式で生ごみを処理した際に問題となる悪臭の発生を確実に防止できる。すなわち、脱臭装置や触媒を利用することなく、臭気対策を施すことが可能になる。   In addition, by drying the garbage at a high temperature of 200 to 600 ° C. in this way, and further returning the exhaust from the garbage dryer to the hot air flow path in the gasifier, It is possible to reliably prevent the generation of bad odor that becomes a problem when garbage is treated. That is, odor countermeasures can be taken without using a deodorizing device or a catalyst.

また、生ごみ乾燥機で乾燥処理した後の生ごみをガス化装置に投入してガス化することにより、生ごみをバイオマスとして再資源化することが可能になる。   Moreover, by putting the garbage after being dried by the garbage dryer into a gasifier and gasifying it, the garbage can be recycled as biomass.

本発明の一実施形態に係る生ごみの処理システムを示す図である。It is a figure which shows the processing system of the garbage which concerns on one Embodiment of this invention.

以下、図1を参照し、本発明の一実施形態に係る生ごみの処理システムについて説明する。   Hereinafter, a garbage processing system according to an embodiment of the present invention will be described with reference to FIG.

本実施形態の生ごみの処理システムAは、図1に示すように、バイオマスをガス化するガス化装置1と、生ごみを乾燥処理するための生ごみ乾燥機2とを備えて構成されている。   As shown in FIG. 1, the garbage processing system A of the present embodiment includes a gasifier 1 for gasifying biomass and a garbage dryer 2 for drying the garbage. Yes.

ガス化装置1は、ガス化反応炉3と外熱炉4などからなり、ガス化反応炉3内にバイオマスを投入してガス化し、一酸化炭素や水素などを含むバイオマスガスを生成する。また、このとき、外熱炉4でガス化反応に必要な熱が供給される。ガス化反応炉3内でのガス化の反応温度は約700〜900℃とされているため、外熱炉温度は約1000℃以上に保たれている。さらに、ガス化装置1の排熱の一部は熱交換器5を通じて外熱炉4に返送される。   The gasification apparatus 1 includes a gasification reaction furnace 3 and an external heating furnace 4. The gasification apparatus 1 inputs biomass into the gasification reaction furnace 3 and gasifies it to generate biomass gas containing carbon monoxide, hydrogen, and the like. At this time, the heat required for the gasification reaction is supplied in the external heating furnace 4. Since the gasification reaction temperature in the gasification reactor 3 is about 700 to 900 ° C., the external heating furnace temperature is kept at about 1000 ° C. or more. Further, part of the exhaust heat from the gasifier 1 is returned to the external heating furnace 4 through the heat exchanger 5.

生ごみ乾燥機2としては、例えば熱風並流式で撹拌軸付のロータリーキルンなどが挙げられ、ガス化装置1の熱風が流通する流通経路Rと生ごみ乾燥機2の内部を熱風導入用の配管、排気返送用の配管で接続して配設されている。   Examples of the garbage dryer 2 include a hot air co-current type rotary kiln with a stirring shaft, and a distribution path R through which the hot air of the gasifier 1 circulates and the interior of the garbage dryer 2 for introducing hot air. The exhaust return pipes are connected and arranged.

そして、本実施形態の生ごみの処理システムAにおいては、内部に生ごみを収容した生ごみ乾燥機2にガス化装置1の高温排熱6を熱風として導入し、この排熱6を利用することで生ごみを乾燥処理する。このとき、ガス化装置1の排熱6を利用することによって、従来の高温乾燥法で利用する温度より数倍高い約200〜600℃で生ごみを乾燥処理する。これにより、例えば400℃で数分間〜6分間程度の短時間で生ごみが乾燥処理される。   And in the garbage processing system A of this embodiment, the high temperature exhaust heat 6 of the gasification apparatus 1 is introduce | transduced as a hot air into the garbage dryer 2 which accommodated the garbage inside, and this exhaust heat 6 is utilized. The garbage is dried. At this time, by using the exhaust heat 6 of the gasifier 1, the garbage is dried at about 200 to 600 ° C. several times higher than the temperature used in the conventional high-temperature drying method. Thus, for example, the garbage is dried at a temperature of 400 ° C. for a few minutes to 6 minutes.

また、生ごみ乾燥機2で生ごみを乾燥した後の排気7は、ガス化装置1の熱風の流通経路Rに再投入する。このとき、処理システムAの装置1内で循環させ、排気7を400℃以上の煙道に戻したり、臭気の要求レベルが高い場合には1000℃以上の外熱炉4に戻すことにより、400℃から条件によっては1000℃程度の高温で再加熱することができる。このため、通常の高温乾燥法で問題となる臭気成分を、例えば5秒以上の高温接触により、確実に分解することができる。   Further, the exhaust 7 after the garbage is dried by the garbage dryer 2 is reintroduced into the hot air flow path R of the gasifier 1. At this time, it is circulated in the apparatus 1 of the processing system A, and the exhaust 7 is returned to the flue having a temperature of 400 ° C. or higher, or is returned to the external heating furnace 4 having a temperature of 1000 ° C. or higher if the odor requirement level is high. Depending on the conditions, it can be reheated at a high temperature of about 1000 ° C. For this reason, the odor component which becomes a problem by the normal high temperature drying method can be reliably decomposed | disassembled by the high temperature contact for 5 seconds or more, for example.

このように、臭気の発生を抑え、短時間で生ごみが乾燥処理される。また、本実施形態では、処理後の乾燥生ごみ8をガス化装置1に供給してガス化し、バイオマスガスの生成に利用する。これにより、生ごみの再資源化が図れる。   In this way, the generation of odor is suppressed and the garbage is dried in a short time. Moreover, in this embodiment, the dry garbage 8 after a process is supplied to the gasifier 1, gasified, and it utilizes for the production | generation of biomass gas. Thereby, the recycling of garbage can be achieved.

したがって、本実施形態の生ごみの処理システムAにおいては、ガス化装置1が、バイオマスを供給してガス化するガス化反応炉3と、ガス化反応に必要な熱を供給する外熱炉4とを備えて構成され、このガス化装置1の例えば200〜600℃の高温の排熱6を熱風として生ごみ乾燥機2に導入することで、生ごみを短時間で乾燥処理することが可能になる。すなわち、無駄な燃料や電気を使用することなく、特に都市域では利用が難しいガス化装置の排熱を利用して、効率的に生ごみを処理することが可能になる。   Therefore, in the garbage processing system A of this embodiment, the gasification apparatus 1 supplies biomass and gasifies the gasification reaction furnace 3, and the external heating furnace 4 supplies the heat required for the gasification reaction. It is possible to dry the garbage in a short time by introducing the high-temperature exhaust heat 6 of, for example, 200 to 600 ° C. of the gasifier 1 into the garbage dryer 2 as hot air. become. In other words, it is possible to efficiently treat garbage without using wasteful fuel and electricity, using exhaust heat from a gasifier, which is difficult to use particularly in urban areas.

また、このように200〜600℃の高温で生ごみを乾燥することにより、さらに生ごみ乾燥機2からの排気7をガス化装置1内の熱風の流通経路Rに返送することにより、従来の高温乾燥方式で生ごみを処理した際に問題となる悪臭の発生を確実に防止できる。すなわち、脱臭装置や触媒を利用することなく、臭気対策を施すことが可能になる。   In addition, by drying the garbage at a high temperature of 200 to 600 ° C. in this way, the exhaust 7 from the garbage dryer 2 is further returned to the hot air flow path R in the gasifier 1, so that Occurrence of bad odor that becomes a problem when garbage is treated by high temperature drying method can be surely prevented. That is, odor countermeasures can be taken without using a deodorizing device or a catalyst.

また、生ごみ乾燥機2で乾燥処理した後の生ごみ8をガス化装置1のガス化反応炉3に投入してガス化することにより、生ごみ8をバイオマスとして再資源化することが可能になる。   Moreover, by putting the garbage 8 after being dried by the garbage dryer 2 into the gasification reactor 3 of the gasifier 1 and gasifying it, the garbage 8 can be recycled as biomass. become.

よって、従来の微生物分解法や高温乾燥法と比較し、短時間で生ごみの乾燥が可能になるとともに、除臭装置や触媒などを用いることなく、臭気の発生を抑制することができ、生ごみを処理(減容化、資源化)するコストを大幅に低減することが可能になる。   Therefore, compared to conventional microbial decomposition methods and high-temperature drying methods, garbage can be dried in a short time, and the generation of odor can be suppressed without using a deodorizing device or catalyst. It is possible to greatly reduce the cost of processing (reducing volume and recycling) waste.

以上、本発明に係る生ごみの処理システムの一実施形態について説明したが、本発明は上記の一実施形態に限定されるものではなく、その趣旨を逸脱しない範囲で適宜変更可能である。   As mentioned above, although one Embodiment of the garbage processing system which concerns on this invention was described, this invention is not limited to said one Embodiment, In the range which does not deviate from the meaning, it can change suitably.

1 ガス化装置
2 生ごみ乾燥機
3 ガス化反応炉
4 外熱炉
5 熱交換器
6 排熱
7 排気
8 乾燥処理した生ごみ
A 生ごみの処理システム
R 流通経路
1 Gasifier 2 Garbage Dryer 3 Gasification Reactor 4 Outer Heat Furnace 5 Heat Exchanger 6 Exhaust Heat 7 Exhaust 8 Dried Garbage A Garbage Processing System R Distribution Channel

Claims (2)

バイオマスをガス化するガス化装置と、生ごみを乾燥処理するための生ごみ乾燥機とを備え、
前記ガス化装置の排熱を熱風として前記生ごみ乾燥機に導入し、前記生ごみ乾燥機内に収容した生ごみを前記排熱によって乾燥処理するとともに、前記生ごみ乾燥機からの排気を前記ガス化装置内で流通する熱風の流通経路に返送するようにしたことを特徴とする生ごみの処理システム。
A gasifier for gasifying biomass and a garbage dryer for drying garbage;
The exhaust heat of the gasifier is introduced into the garbage dryer as hot air, the garbage stored in the garbage dryer is dried by the exhaust heat, and the exhaust from the garbage dryer is exhausted from the gas A garbage disposal system characterized in that it is returned to the distribution channel of hot air circulating in the gasification device.
請求項1記載の生ごみの処理システムにおいて、
前記生ごみ乾燥機で乾燥処理した生ごみを前記ガス化装置に投入し、前記バイオマスとして利用するようにしたことを特徴とする生ごみの処理システム。
In the garbage processing system according to claim 1,
The garbage processing system, wherein the garbage dried by the garbage dryer is put into the gasifier and used as the biomass.
JP2011257949A 2011-11-25 2011-11-25 Garbage treatment system Pending JP2013111498A (en)

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Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003002755A (en) * 2001-06-22 2003-01-08 Meidensha Corp Castable material stock, method for producing castable material, refractory heat resistant body and refractory heat resistant structure
JP2003181496A (en) * 2001-09-20 2003-07-02 Nippon Zoki Pharmaceut Co Ltd Carbonization method of organic waste and apparatus therefor
JP2003183665A (en) * 2001-12-14 2003-07-03 Mitsui Eng & Shipbuild Co Ltd Livestock manure processing equipment and char collection system
JP2005319373A (en) * 2004-05-07 2005-11-17 Tokyo Electric Power Co Inc:The Method and apparatus for converting sludge into fuel
JP2006075693A (en) * 2004-09-08 2006-03-23 Babcock Hitachi Kk Combustible gas production method and apparatus
JP2007032950A (en) * 2005-07-28 2007-02-08 Nohmi Bosai Ltd Offensive odor alarm system for refuse disposal apparatus
JP2007119641A (en) * 2005-10-28 2007-05-17 Electric Power Dev Co Ltd Solid fuel derived from organic sludge
JP2011167649A (en) * 2010-02-19 2011-09-01 Daido Steel Co Ltd Carbonization treatment facility of sludge

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003002755A (en) * 2001-06-22 2003-01-08 Meidensha Corp Castable material stock, method for producing castable material, refractory heat resistant body and refractory heat resistant structure
JP2003181496A (en) * 2001-09-20 2003-07-02 Nippon Zoki Pharmaceut Co Ltd Carbonization method of organic waste and apparatus therefor
JP2003183665A (en) * 2001-12-14 2003-07-03 Mitsui Eng & Shipbuild Co Ltd Livestock manure processing equipment and char collection system
JP2005319373A (en) * 2004-05-07 2005-11-17 Tokyo Electric Power Co Inc:The Method and apparatus for converting sludge into fuel
JP2006075693A (en) * 2004-09-08 2006-03-23 Babcock Hitachi Kk Combustible gas production method and apparatus
JP2007032950A (en) * 2005-07-28 2007-02-08 Nohmi Bosai Ltd Offensive odor alarm system for refuse disposal apparatus
JP2007119641A (en) * 2005-10-28 2007-05-17 Electric Power Dev Co Ltd Solid fuel derived from organic sludge
JP2011167649A (en) * 2010-02-19 2011-09-01 Daido Steel Co Ltd Carbonization treatment facility of sludge

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