JPH0351966B2 - - Google Patents

Info

Publication number
JPH0351966B2
JPH0351966B2 JP59027175A JP2717584A JPH0351966B2 JP H0351966 B2 JPH0351966 B2 JP H0351966B2 JP 59027175 A JP59027175 A JP 59027175A JP 2717584 A JP2717584 A JP 2717584A JP H0351966 B2 JPH0351966 B2 JP H0351966B2
Authority
JP
Japan
Prior art keywords
carbonization
incinerator
combustion
food waste
complete combustion
Prior art date
Legal status (The legal status 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 status listed.)
Expired - Lifetime
Application number
JP59027175A
Other languages
Japanese (ja)
Other versions
JPS60174417A (en
Inventor
Atsushi Nogami
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Sanki Engineering Co Ltd
Original Assignee
Sanki Engineering Co Ltd
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 Sanki Engineering Co Ltd filed Critical Sanki Engineering Co Ltd
Priority to JP59027175A priority Critical patent/JPS60174417A/en
Publication of JPS60174417A publication Critical patent/JPS60174417A/en
Publication of JPH0351966B2 publication Critical patent/JPH0351966B2/ja
Granted legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/006General arrangement of incineration plant, e.g. flow sheets
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/02Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
    • F23G5/027Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment pyrolising or gasifying stage
    • 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
    • Y02E20/00Combustion technologies with mitigation potential
    • Y02E20/34Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Incineration Of Waste (AREA)
  • Gasification And Melting Of Waste (AREA)

Description

【発明の詳細な説明】 本発明は、小規模団地等で用いられ、ごみの発
生場所近傍で簡易に生ごみを焼却処理するのに好
適な生ごみ焼却方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for incinerating food waste, which is used in small-scale housing complexes and the like, and is suitable for easily incinerating food waste near the place where the waste is generated.

家庭等から排出される都市ごみの処理は、通常
大規模な焼却場に運搬され、大型の焼却装置を使
用して焼却されるが、近年ごみの収集や輸送に多
大の費用や人手を必要とし、また焼却場の立地条
件の悪化等の要因から、ごみの発生場所近傍で小
型の焼却炉により焼却処理することが望まれてい
る。ところで、都市ごみのうち生ごみは含水量が
多いため、発熱量が低く、不完全燃焼を生じ易く
なり、従来型の小型焼却炉では有害な排ガスや煤
煙等が多量に発生して環境を汚染し、また燃焼残
渣物も大量に発生するためにその処理が面倒であ
る等の不都合がある。そこで、生ごみを予め乾留
し、この乾留によつて生成される水素、一酸化炭
素等の燃焼性ガス及び炭化物を主成分とする乾留
残渣物を完全燃焼させるようにした焼却方法も知
られているが、かかる焼却方法では、前述の燃焼
性ガスを完全燃焼させる関係上、燃焼装置が大型
化し、その構造や制御が複雑となり、しかも完全
燃焼のために多量の空気を必要として燃焼効率が
良好でない欠点があつた。
Municipal waste generated from households, etc. is normally transported to large-scale incinerators and incinerated using large incinerators, but in recent years the collection and transportation of waste has increased in cost and manpower. In addition, due to factors such as deteriorating location conditions for incinerators, it is desired to incinerate waste in small incinerators near the place where the waste is generated. By the way, among municipal waste, food waste has a high water content, so it has a low calorific value and is prone to incomplete combustion.In conventional small incinerators, large amounts of harmful exhaust gas and soot are generated, polluting the environment. However, since a large amount of combustion residue is generated, it is troublesome to dispose of it. Therefore, an incineration method is also known in which food waste is carbonized in advance and the carbonized residue, which is mainly composed of hydrogen, carbon monoxide, and other combustible gases produced by this carbonization, is completely combusted. However, in this incineration method, since the combustible gas mentioned above is completely combusted, the combustion equipment becomes large and its structure and control are complicated, and a large amount of air is required for complete combustion, making it difficult to achieve good combustion efficiency. There was a drawback that it wasn't.

本発明は叙上の点に鑑みてなされたもので、小
型で簡単な装置を使用して清潔かつ安全で、しか
も効率的に生ごみを焼却処理し得る生ごみ焼却方
法を提供することを目的とするものである。
The present invention has been made in view of the above points, and an object of the present invention is to provide a method for incinerating food waste in a clean, safe, and efficient manner using a small and simple device. That is.

前述の目的を達成するために、本発明は2基設
置した焼却炉のうち一方の焼却炉に生ごみを投入
して乾留する乾留工程と、他方の焼却炉に生ごみ
を投入して乾留を行ない、この乾留時に発生する
燃焼性ガスを前記一方の焼却炉に導入することに
より当該一方の焼却炉内で乾留残渣物と共に完全
燃焼させる第1の乾留・完全燃焼工程と、前記一
方の焼却炉に生ごみを投入して乾留を行ない、こ
の乾留時に発生する燃焼性ガスを前記他方の焼却
炉に導入することにより当該他方の焼却炉内で乾
留残渣物と共に完全燃焼させる第2の乾留・完全
燃焼工程とからなり、前記乾留工程完了後、当該
第1、第2の乾留・完全燃焼工程を順次繰り返す
ようにしたことをその特徴とするものである。
In order to achieve the above-mentioned object, the present invention includes a carbonization process in which food waste is charged into one of two incinerators and carbonized, and a carbonization process in which food waste is charged into the other incinerator and carbonized. a first carbonization/complete combustion step in which the combustible gas generated during carbonization is introduced into the one incinerator to completely burn it together with the carbonization residue in the one incinerator; In the second carbonization and complete carbonization process, food waste is put into the furnace and carbonized, and the combustible gas generated during carbonization is introduced into the other incinerator to completely burn it together with the carbonization residue in the other incinerator. The method is characterized in that after the carbonization step is completed, the first and second carbonization/complete combustion steps are repeated in sequence.

以下、本発明の実施例を図面に基づき詳細に説
明するに、まず第1図に本発明に係る方法に使用
される装置の具体例を示す。同図中、1a,1b
はそれぞれ生ごみを回分式で乾留して燃焼させる
ことにより焼却を行なう焼却炉を示し、該各焼却
炉1a,1bはバーナ等の焼却装置を備えた同一
構造のもので、それらには燃焼用の空気を供給す
る空気供給配管2a,2bがそれぞれ接続されて
いる。該各空気供給配管2a,2bの他端は燃焼
用の空気を乾留用の小流量供給状態と完全燃焼用
の大流量供給状態との間に切換えて焼却炉1a,
1bに分配する分配装置3を介して燃焼用空気供
給源4に接続されている。燃焼用空気供給源4は
ブロワ等からなる空気源5と、該空気源5から供
給される空気を酸素富化する酸素富化器6とから
なり、酸素富化器6は例えば、供給された空気の
うち酸素のみを通過させる酸素富化膜や供給空気
中の酸素を吸着除去する粒状のゼオライト等が用
いられ、これにより酸素含有率が80%〜90%とな
るように酸素富化した空気を焼却炉1a,1bに
供給し得るようになつている。また、焼却炉1
a,1b間には燃焼性ガスを流通させるガス流通
路7が接続され、いずれか一方の焼却炉の乾留中
に発生する水素、一酸化炭素等を含む燃焼性ガス
を他方の焼却炉に導入させることができるように
なつている。
Hereinafter, embodiments of the present invention will be described in detail with reference to the drawings. First, FIG. 1 shows a specific example of an apparatus used in the method according to the present invention. In the same figure, 1a, 1b
1 and 2 respectively indicate incinerators that perform incineration by carbonizing and burning raw garbage in batches, and each incinerator 1a and 1b has the same structure equipped with incineration equipment such as a burner, and they are equipped with a combustion Air supply pipes 2a and 2b that supply air are connected to each other. The other ends of the air supply pipes 2a and 2b are connected to the incinerators 1a and 2b by switching combustion air between a small flow rate supply state for carbonization and a large flow rate supply state for complete combustion.
It is connected to a combustion air supply source 4 via a distribution device 3 which distributes it to 1b. The combustion air supply source 4 includes an air source 5 such as a blower, and an oxygen enricher 6 that enriches the air supplied from the air source 5 with oxygen. Oxygen-enriched membranes that allow only oxygen to pass through the air and granular zeolites that adsorb and remove oxygen from the supplied air are used to create oxygen-enriched air with an oxygen content of 80% to 90%. can be supplied to the incinerators 1a and 1b. In addition, incinerator 1
A gas flow passage 7 for circulating combustible gas is connected between a and 1b, and combustible gas containing hydrogen, carbon monoxide, etc. generated during carbonization in one of the incinerators is introduced into the other incinerator. I am now able to do this.

次に、前述の装置を使用して行なう生ごみの焼
却方法は乾留工程と、第1及び第2の乾留・完全
燃焼工程とから構成される。
Next, the method of incinerating food waste using the above-mentioned apparatus consists of a carbonization step, and first and second carbonization/complete combustion steps.

まず、乾留工程は、一方の焼却炉(例えば焼却
炉1a)に生ごみを投入し、酸素富化器6によつ
て酸素富化された燃焼用空気を分配装置3を介し
て小流量で空気供給管2aから当該焼却炉1aに
供給し、低温状態で生ごみの乾留を行なう工程で
ある。
First, in the carbonization process, food waste is put into one incinerator (for example, incinerator 1a), and combustion air enriched with oxygen is sent to the oxygen enricher 6 at a small flow rate through the distribution device 3. In this step, garbage is supplied from the supply pipe 2a to the incinerator 1a and carbonized at a low temperature.

次に、第1の乾留・完全燃焼工程は、第2図に
示した如く、他方の焼却炉(ここでは焼却炉1
b)に生ごみを投入し、分配装置3を焼却炉1b
には小流量で、また焼却炉1aには大流量で燃焼
用空気を供給する状態に切換える。そして、焼却
炉1bでは前述と同様にして生ごみの乾留を行な
い、また焼却炉1aでは既に乾留が完了している
から、この乾留残渣物を大流量の燃焼用空気を利
用して高温で完全燃焼させる。而して、焼却炉1
aにおいて完全燃焼を行なつている間に焼却炉1
bにおいて行つている乾留により一酸化炭素や水
素等を含む燃焼性ガスが発生するが、この燃焼性
ガスは外部に排出されることなく、ガス流通路7
を介して焼却炉1a内に導入され、当該焼却炉1
a内で前記燃焼性ガスは炭化物を主成分とする乾
留残渣物と共に完全燃焼される。
Next, the first carbonization/complete combustion step is performed in the other incinerator (in this case, incinerator 1), as shown in FIG.
b) Put food waste into the incinerator 1b and transfer the distribution device 3 to the incinerator 1b.
The combustion air is supplied to the incinerator 1a at a small flow rate, and the combustion air is supplied to the incinerator 1a at a large flow rate. Then, in the incinerator 1b, the garbage is carbonized in the same manner as described above, and since the carbonization has already been completed in the incinerator 1a, the carbonized residue is completely removed at high temperature using a large flow of combustion air. Burn it. Therefore, incinerator 1
While complete combustion is being carried out in a, the incinerator 1
Although combustible gas containing carbon monoxide, hydrogen, etc. is generated by the carbonization carried out in step b, this combustible gas is not discharged to the outside and flows through the gas flow passage 7.
is introduced into the incinerator 1a through the incinerator 1a.
In the chamber a, the combustible gas is completely combusted together with the carbonization residue mainly composed of carbide.

さらに、第2の乾留・完全燃焼工程は、第3図
に示した如く、分配装置3を切換えて焼却炉1a
には小流量で、焼却炉1bには大流量で燃焼用空
気を供給し、完全燃焼を終えた焼却炉1aには新
たな生ごみを投入して乾留を行ない、また焼却炉
1bでは乾留が完了しているから、乾留残渣物の
完全燃焼が行なわれる。このとき、焼却炉1aで
発生する燃焼性ガスは焼却炉1bに導入されて、
そこで乾留残渣物と共に完全燃焼される。
Furthermore, the second carbonization/complete combustion step is performed by switching the distribution device 3 to the incinerator 1a as shown in FIG.
Combustion air is supplied at a small flow rate to the incinerator 1b, and at a large flow rate to the incinerator 1b. After complete combustion, fresh garbage is introduced into the incinerator 1a and carbonized. Complete combustion of the carbonization residue takes place. At this time, the combustible gas generated in the incinerator 1a is introduced into the incinerator 1b,
There, it is completely combusted together with the carbonization residue.

ここで、分配装置3による燃焼用空気の小流量
供給状態における供給量と大流量状態におけるそ
れとの比率を3:7程度に設定しておけば、乾留
は例えば400℃〜600℃程度の比較的低温な状態で
行なえ、また完全燃焼は1000℃〜1200℃程度の高
温状態で行ない得るため、極めて好都合である。
Here, if the ratio of the amount of combustion air supplied by the distribution device 3 in a small flow rate state and that in a large flow rate state is set to about 3:7, carbonization can be carried out at a relatively low temperature of, for example, 400°C to 600°C. It is extremely convenient because it can be carried out at a low temperature and complete combustion can be carried out at a high temperature of about 1000°C to 1200°C.

而して、前述の乾留工程を終えた後は第1、第
2の乾留・完全燃焼工程を順次繰返すことによつ
て、生ごみを迅速かつ効率的に焼却処理すること
ができる。しかも、この第1、第2の乾留・完全
燃焼工程を繰返している間は、乾留時に発生する
燃焼性ガスはそのままでは外部に排出されること
なく完全燃焼されるから、煤煙や悪臭の発生が防
止され、また従来の燃焼法に比較してガス量が極
めて少ないためにガスの清浄化も容易である。さ
らに、このように燃焼性ガスを乾留残渣物と共に
完全燃焼させ、また燃焼用空気を酸素富化器6で
酸素富化させていること、および2段に分けて燃
焼することによる燃焼効率の向上から両焼却炉1
a,1b併せての酸素使用量は理論酸素量の約
1.1倍程度となり、通常の焼却法の場合は一般に
理論酸素量の1.5倍程度必要であることから、空
気の使用量が少なくてよく、このために熱量の損
失が少なく、高温化が容易で燃焼効率が向上す
る。さらにまた、完全燃焼後、焼却炉中の燃焼灰
分は焼結化して粒状物となるから、例えば道路材
等として再利用することができる。
After the above-mentioned carbonization step is completed, the first and second carbonization/complete combustion steps are sequentially repeated, thereby making it possible to quickly and efficiently incinerate the garbage. Moreover, while the first and second carbonization and complete combustion steps are repeated, the combustible gas generated during carbonization is completely combusted without being discharged to the outside, so soot and bad odors are not generated. Furthermore, since the amount of gas is extremely small compared to conventional combustion methods, the gas is easy to clean. Furthermore, combustion efficiency is improved by completely combusting the combustible gas together with the carbonization residue, enriching the combustion air with oxygen in the oxygen enricher 6, and combusting in two stages. From both incinerators 1
The combined amount of oxygen used in a and 1b is approximately the theoretical amount of oxygen.
The amount of oxygen is approximately 1.1 times that of the theoretical amount, and in the case of normal incineration methods, the amount of oxygen is generally required to be approximately 1.5 times the theoretical amount, so the amount of air used is small, so there is little loss of heat, and it is easy to raise the temperature and combust. Increased efficiency. Furthermore, after complete combustion, the combustion ash in the incinerator is sintered into granules, which can be reused, for example, as road materials.

以上詳述した如く、本発明に係る生ごみ焼却方
法は2基の焼却炉を使用して一方の焼却炉で乾留
を行なつている間は他方の焼却炉では完全燃焼を
行ない、また一方の焼却炉の完全燃焼中は他方の
焼却炉では乾留を行なうようにしたから、小型で
制御の容易な焼却装置を使用して簡便かつ迅速に
生ごみの焼却処理を行なうことができ、また乾留
時に生成する燃焼性ガスを完全燃焼が行なわれて
いる焼却炉に導入して乾留残渣物と共に完全燃焼
させるようにしているから、燃焼効率が良好で、
排ガス量が少なく灰分の飛散を生じるおそれがな
く、さらに燃焼後の灰分は焼結するから、処理を
容易に行なうことができる等の諸効果を奏する。
As detailed above, the food waste incineration method according to the present invention uses two incinerators, and while carbonization is being carried out in one incinerator, complete combustion is carried out in the other incinerator, and Since carbonization is performed in the other incinerator while one incinerator is completely burning, it is possible to incinerate food waste easily and quickly using a small and easily controlled incinerator. Since the generated combustible gas is introduced into an incinerator where complete combustion is being carried out and completely combusted together with the carbonization residue, combustion efficiency is good.
The amount of exhaust gas is small, there is no risk of ash scattering, and since the ash after combustion is sintered, it can be easily disposed of.

【図面の簡単な説明】[Brief explanation of drawings]

第1図は本発明に係る生ゴミ焼却方法を実施す
るための装置構成図、第2図及び第3図はそれぞ
れ異なる作動状態を示す作動説明図である。 1a,1b:焼却炉、2a,2b:空気供給配
管、3:分配装置、4:燃焼用空気供給源、5:
空気源、6:酸素富化器、7:ガス流通路。
FIG. 1 is a configuration diagram of an apparatus for implementing the garbage incineration method according to the present invention, and FIGS. 2 and 3 are operation explanatory diagrams showing different operating states. 1a, 1b: Incinerator, 2a, 2b: Air supply piping, 3: Distribution device, 4: Combustion air supply source, 5:
Air source, 6: Oxygen enricher, 7: Gas flow path.

Claims (1)

【特許請求の範囲】[Claims] 1 2基設置した焼却炉のうち一方の焼却炉に生
ごみを投入して乾留する乾留工程と、他方の焼却
炉に生ごみを投入して乾留を行ない、この乾留時
に発生する燃焼性ガスを前記一方の焼却炉に導入
することにより当該一方の焼却炉内で乾留残渣物
と共に完全燃焼させる第1の乾留・完全燃焼工程
と、前記一方の焼却炉に生ごみを投入して乾留を
行ない、この乾留時に発生する燃焼性ガスを前記
他方の焼却炉に導入することにより当該他方の焼
却炉内で乾留残渣物と共に完全燃焼させる第2の
乾留・完全燃焼工程とからなり、前記乾留工程完
了後、当該第1、第2の乾留・完全燃焼工程を順
次繰り返すようにしたことを特徴とする生ごみ焼
却方法。
1 A carbonization process in which food waste is put into one of the two incinerators and carbonized, and a carbonization process in which food waste is put into the other incinerator and carbonized, and the combustible gas generated during carbonization is removed. A first carbonization/complete combustion step of completely burning the waste together with the carbonization residue in the one incinerator by introducing it into the one incinerator, and carbonizing the food waste by putting it into the one incinerator, It consists of a second carbonization/complete combustion step in which the combustible gas generated during carbonization is introduced into the other incinerator and completely combusted together with the carbonization residue in the other incinerator, and after the carbonization step is completed, A method of incinerating raw garbage, characterized in that the first and second carbonization and complete combustion steps are repeated in sequence.
JP59027175A 1984-02-17 1984-02-17 Incinerating method of garbage Granted JPS60174417A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59027175A JPS60174417A (en) 1984-02-17 1984-02-17 Incinerating method of garbage

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59027175A JPS60174417A (en) 1984-02-17 1984-02-17 Incinerating method of garbage

Publications (2)

Publication Number Publication Date
JPS60174417A JPS60174417A (en) 1985-09-07
JPH0351966B2 true JPH0351966B2 (en) 1991-08-08

Family

ID=12213727

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59027175A Granted JPS60174417A (en) 1984-02-17 1984-02-17 Incinerating method of garbage

Country Status (1)

Country Link
JP (1) JPS60174417A (en)

Also Published As

Publication number Publication date
JPS60174417A (en) 1985-09-07

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