JP2001213683A - Method for manufacturing compost-like material and its manufacturing apparatus - Google Patents
Method for manufacturing compost-like material and its manufacturing apparatusInfo
- Publication number
- JP2001213683A JP2001213683A JP2000017391A JP2000017391A JP2001213683A JP 2001213683 A JP2001213683 A JP 2001213683A JP 2000017391 A JP2000017391 A JP 2000017391A JP 2000017391 A JP2000017391 A JP 2000017391A JP 2001213683 A JP2001213683 A JP 2001213683A
- Authority
- JP
- Japan
- Prior art keywords
- heating
- compost
- exhaust gas
- time
- heat treatment
- 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.)
- Pending
Links
Classifications
-
- 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
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A40/00—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
- Y02A40/10—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
- Y02A40/20—Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
- Y02P20/129—Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines
-
- 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
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/40—Bio-organic fraction processing; Production of fertilisers from the organic fraction of waste or refuse
Landscapes
- Fertilizers (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明はコンポスト様物の製
造方法及び製造装置に係り、特に、有機性廃棄物を処理
してコンポストに類似した悪臭の無い製品を製造して資
源化するための方法及び装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method and apparatus for producing compost-like material, and more particularly, to a method for producing organic waste and producing a product having no odor similar to compost and recycling it. And an apparatus.
【0002】[0002]
【従来の技術及び先行技術】従来、生物処理汚泥や生ご
み、畜糞等の有機性廃棄物の再資源化処理方法として
は、主にコンポスト化処理法が実施されている。コンポ
スト化処理方法は、有機性廃棄物を醗酵させる方法であ
り、得られた熟成コンポストは、悪臭成分が分解されて
いるが有機物は十分残留しているため、取り扱い性に優
れた肥料となる。2. Description of the Related Art Conventionally, a composting method is mainly used as a method of recycling organic waste such as biologically treated sludge, garbage, and livestock dung. The composting method is a method of fermenting an organic waste, and the obtained aged compost is a fertilizer excellent in handleability because the offensive odor component is decomposed, but the organic matter remains sufficiently.
【0003】しかしながら、このようなコンポスト化処
理法は、処理に数週間以上の長期間を要するなどの問題
があることから、近年、短時間でコンポスト様の製品が
製造できる技術の開発が試みられ、特願平11−235
745号(以下「先願」という。)には、有機性廃棄物
を乾燥処理後、更に100〜200℃で加熱して、臭気
成分を除去することにより、悪臭の殆どないコンポスト
様物を製造する方法が提案されている。この方法によれ
ば、加熱乾燥後も更に100〜200℃での加熱を継続
することにより、10〜20時間程度の短時間の処理
で、悪臭がなく、しかも、有機肥料分も十分に残留して
いる上に塩分もさほど高くなく、有機肥料として有効な
熟成コンポスト類似の取り扱い性に優れた製品を得るこ
とができる。[0003] However, such a composting method has a problem that it takes a long time of several weeks or more for processing, and in recent years, there has been an attempt to develop a technique for manufacturing a compost-like product in a short time. , Japanese Patent Application No. 11-235
No. 745 (hereinafter referred to as “prior application”) is a method of producing a compost-like material having almost no bad odor by removing the odor component by drying the organic waste and further heating at 100 to 200 ° C. A way to do that has been proposed. According to this method, by continuing the heating at 100 to 200 ° C. even after the heating and drying, there is no odor and the organic fertilizer remains sufficiently in a short treatment of about 10 to 20 hours. In addition, the salt content is not so high, and it is possible to obtain a product which is effective as an organic fertilizer and has excellent handling properties similar to aged compost.
【0004】上記先願に示される処理方法では、乾燥処
理後更に100〜200℃で加熱処理するに際して、適
当な加熱時間の設定のために事前に予備試験を十分に行
って予め設定した時間で運転したり、或いは処理途中で
原料の処理状況を作業員が観察、分析して適当な処理時
間の終了を判断する必要があった。In the processing method disclosed in the above-mentioned prior application, when further heating at 100 to 200 ° C. after the drying treatment, a preliminary test is sufficiently performed in advance in order to set an appropriate heating time, and a predetermined time is set. It is necessary for the operator to observe and analyze the processing status of the raw material during operation or during the processing, and to determine the end of an appropriate processing time.
【0005】[0005]
【発明が解決しようとする課題】しかしながら、予備試
験結果に基づいた運転では、処理すべき原料の量や、原
料の含水率などの性状の変化に応じた適正な運転を行う
ことは困難であり、処理時間が短かった場合には処理が
不十分で製品から悪臭が発生し、処理時間を必要以上に
長くした場合には製品からの悪臭の発生はないものの、
燃料を浪費し、また生産性が低下するといった不具合を
生じていた。また、作業員が処理状況を観察、分析して
処理時間の終了を判断する方法では、多大な人手や時間
を要し、工業的に不利である。However, in the operation based on the results of the preliminary test, it is difficult to perform an appropriate operation in accordance with the amount of the raw material to be treated and a change in properties such as the water content of the raw material. If the treatment time is short, the treatment is insufficient and the product produces a bad smell.If the treatment time is made longer than necessary, there is no foul odor from the product.
Problems such as wasting fuel and reducing productivity have occurred. Further, the method in which the worker observes and analyzes the processing status to determine the end of the processing time requires a lot of manpower and time, and is industrially disadvantageous.
【0006】本発明は、上記先願の問題点を解決し、原
料の量や性状が異なっても、加熱処理の終了時間を自動
的に判断して装置の運転を終了させることにより、適正
な処理時間で原料を処理することができ、目標とする悪
臭のない高品質の製品を、燃料や時間、人手を浪費する
ことなく効率的に製造することができる方法及び装置を
提供することを目的とする。[0006] The present invention solves the above-mentioned problems of the prior application, and automatically terminates the operation of the apparatus by automatically judging the end time of the heat treatment even if the amount and properties of the raw materials are different. It is an object of the present invention to provide a method and an apparatus capable of processing raw materials in a processing time and efficiently producing a target high-quality product without a bad odor without wasting fuel, time and manpower. And
【0007】[0007]
【課題を解決するための手段】本発明のコンポスト様物
の製造方法は、有機性廃棄物を加熱乾燥した後、100
〜200℃で加熱処理する工程を経てコンポスト様物を
製造する方法において、該加熱処理工程から排出される
排ガスに含まれる所定成分を検知して該加熱処理時間を
設定することを特徴とする。The method for producing compost-like material according to the present invention comprises heating and drying organic waste,
A method for producing a compost-like product through a step of performing heat treatment at a temperature of up to 200 ° C., wherein a predetermined component contained in exhaust gas discharged from the heat treatment step is detected to set the heat treatment time.
【0008】本発明のコンポスト様物の製造装置は、有
機性廃棄物を100〜200℃に加熱する加熱装置と、
該加熱装置から排出される排ガスの所定成分を検知する
検知手段と、該検知手段の検知信号に基づき、前記加熱
装置の加熱処理時間を制御する制御手段とを具備するこ
とを特徴とする。[0008] The apparatus for producing compost-like products of the present invention comprises: a heating device for heating organic waste to 100 to 200 ° C;
It is characterized by comprising a detecting means for detecting a predetermined component of the exhaust gas discharged from the heating device, and a control means for controlling a heating processing time of the heating device based on a detection signal of the detecting means.
【0009】加熱乾燥した有機性廃棄物を100〜20
0℃で加熱処理する工程では、加熱に伴って原料中の水
分や、原料に含まれている臭気成分、或いは加熱によっ
て原料の有機性廃棄物が分解されて新たに発生した各種
の臭気成分等が、原料から除去され、排ガスとして排出
される。本発明では、このように加熱処理に伴って発生
する排ガス中の水蒸気や、アンモニア、メチルメルカプ
タン、硫化水素、硫化メチル等の各種臭気成分の濃度が
処理に伴って増減するとの知見に基き、これらの成分を
検知し、この結果に基いて加熱処理時間を設定する。[0009] The heat-dried organic waste is 100 to 20
In the step of heating at 0 ° C., the moisture in the raw material and the odor component contained in the raw material due to the heating, or various odor components newly generated by decomposing the organic waste of the raw material by heating, etc. Is removed from the raw material and discharged as exhaust gas. In the present invention, based on the knowledge that the concentration of various odor components such as water vapor and ammonia, methyl mercaptan, hydrogen sulfide, methyl sulfide and the like in the exhaust gas generated by the heat treatment increases or decreases with the treatment, Is detected, and the heat treatment time is set based on this result.
【0010】例えば、水分については、排ガス中の水蒸
気が検出されなくなった時点を始点として更に一定時間
加熱することで処理を終了させることができる。また、
アンモニア等の各種の臭気成分については、加熱に伴っ
て排ガス中の濃度が一旦増大した後減少するが、排ガス
中のアンモニア濃度のピークを検出後、所定のアンモニ
ア濃度に低下する時点まで加熱処理時間を設定する、好
ましくは排ガス中にアンモニアがほぼ検出されなくなっ
た時点を処理終了とすることができる。For example, with respect to moisture, the processing can be terminated by heating for a certain period of time starting from the point when water vapor in the exhaust gas is no longer detected. Also,
With respect to various odor components such as ammonia, the concentration in the exhaust gas increases once with heating and then decreases, but after the peak of the ammonia concentration in the exhaust gas is detected, the heat treatment time is reduced until the ammonia concentration decreases to a predetermined ammonia concentration. , Preferably when the ammonia is almost not detected in the exhaust gas.
【0011】[0011]
【発明の実施の形態】以下に図面を参照して本発明の実
施の形態を詳細に説明する。Embodiments of the present invention will be described below in detail with reference to the drawings.
【0012】図1は本発明の実施の形態を示す系統図、
図2は本発明に好適な間接加熱装置を示す断面図であ
る。FIG. 1 is a system diagram showing an embodiment of the present invention.
FIG. 2 is a sectional view showing an indirect heating device suitable for the present invention.
【0013】本発明においては、有機性廃棄物、例え
ば、下水処理汚泥や余剰汚泥、消化汚泥等、廃水や廃棄
物の生物処理工程で生じる生物処理汚泥、生ごみ、畜糞
等を加熱乾燥し、この乾燥処理により有機性廃棄物中の
水分が徐々に蒸発し、含水率が1%未満となって乾燥が
完了した後も、更に100〜200℃で加熱を継続する
に当たり、加熱処理工程から排出される排ガスに含まれ
る所定成分を検知し、この結果に基いて加熱処理時間を
設定する。In the present invention, organic wastes such as sewage sludge, surplus sludge, digested sludge, and the like, biologically treated sludge, garbage, livestock dung, etc. generated in the biological treatment of wastewater and waste are heated and dried. Even after the moisture in the organic waste is gradually evaporated by this drying treatment and the moisture content becomes less than 1% and the drying is completed, the heating is continued at 100 to 200 ° C., and the wastewater is discharged from the heating treatment step. A predetermined component contained in the exhaust gas to be detected is detected, and a heat treatment time is set based on the result.
【0014】有機性廃棄物の加熱乾燥で水分が蒸発する
過程において、水分が残留している間は、被処理物であ
る有機性廃棄物の温度は100℃未満であるが、水分が
完全に蒸発除去された後も加熱を継続すると、被処理物
の温度は100℃以上に上昇する。この状態で加熱を所
定時間継続すると臭気の殆どない熟成コンポスト様物を
得ることができる。なお、この乾燥が完了した後の加熱
温度は100〜200℃、好ましくは150〜200℃
とする。この温度範囲であれば、水分は完全に蒸発除去
され、臭気成分も揮散、分解される一方で、良好な熟成
コンポスト様物を得ることができる。In the process of evaporating water by heating and drying the organic waste, while the water remains, the temperature of the organic waste to be treated is lower than 100 ° C., but the water is completely removed. If heating is continued even after the removal by evaporation, the temperature of the object to be processed rises to 100 ° C. or higher. When heating is continued for a predetermined time in this state, an aged compost-like product having almost no odor can be obtained. The heating temperature after completion of the drying is 100 to 200 ° C, preferably 150 to 200 ° C.
And Within this temperature range, moisture is completely evaporated and removed, and odor components are also volatilized and decomposed, while a good aged compost-like product can be obtained.
【0015】具体的には、図1に示す如く、加熱装置1
1、排ガス検出手段12、排ガス処理装置13及び制御
装置14を備える装置を用い、有機性廃棄物を加熱装置
11に投入して加熱処理し、この加熱装置11で発生す
る排ガスを図示しないブロワで強制換気し、排ガス中の
所定成分を排ガス検出手段12で検出する。この検出結
果は、制御装置14に入力され、制御装置14では、こ
の検出結果に基いて加熱の継続又は終了を判断し、加熱
を終了する場合には、加熱装置11の停止信号を出力す
る。なお、排ガス検出手段12を通過した排ガスは排ガ
ス処理装置13で処理される。[0015] Specifically, as shown in FIG.
1. Using an apparatus provided with an exhaust gas detecting means 12, an exhaust gas treatment device 13 and a control device 14, an organic waste is put into a heating device 11 for heat treatment, and the exhaust gas generated in the heating device 11 is blown by a blower (not shown). Forced ventilation is performed, and a predetermined component in the exhaust gas is detected by the exhaust gas detecting means 12. The detection result is input to the control device 14, and the control device 14 determines continuation or termination of the heating based on the detection result, and outputs a stop signal of the heating device 11 when the heating is terminated. The exhaust gas that has passed through the exhaust gas detecting means 12 is processed by the exhaust gas processing device 13.
【0016】本発明において、加熱処理時間の設定のた
めに検出する排ガス中の成分としては、前述の如く、加
熱処理により排ガス中に含まれて排出され、被処理物の
状況に応じて排ガス中の濃度が増減する水蒸気や各種の
臭気成分であり、このうち臭気成分としては、各種臭気
成分のうちで最も濃度が高いアンモニアを検出するのが
好ましい。In the present invention, as described above, the components in the exhaust gas detected for setting the heat treatment time are contained in the exhaust gas by the heat treatment and are discharged, and depending on the condition of the object to be treated, And various odor components whose concentration increases or decreases. Among them, it is preferable to detect ammonia having the highest concentration among various odor components.
【0017】本発明において、排ガス中の水蒸気を検出
して加熱処理時間を設定する場合には、排ガス中の水蒸
気が検出されなくなった時点から、更に所定時間加熱を
継続した後加熱を終了するようにするのが好ましく、こ
れにより、殆ど臭気のない良好なコンポスト様物を得る
ことができる。In the present invention, when the heat treatment time is set by detecting the water vapor in the exhaust gas, the heating is continued for a further predetermined time after the water vapor in the exhaust gas is no longer detected, and then the heating is terminated. It is preferable to obtain a good compost-like substance having almost no odor.
【0018】この場合、上記所定時間は、処理する有機
性廃棄物の量や性状等によっても異なるが、通常の場
合、3〜5時間程度で十分である。In this case, the predetermined time varies depending on the amount and properties of the organic waste to be treated, but usually, about 3 to 5 hours is sufficient.
【0019】一方、排ガス中の臭気成分、例えばアンモ
ニアを検出して加熱時間を設定する場合には、処理を継
続することにより、排ガス中のアンモニア濃度が次第に
上昇し、ピーク濃度となった後、所定のアンモニア濃度
にまで低下するまで加熱を継続し、この時点で加熱を終
了するのが好ましい。この場合、加熱を終了するアンモ
ニア濃度は、処理する有機性廃棄物の量や性状等によっ
ても異なるが、通常の場合アンモニア濃度が100pp
m以下、特に50ppm以下となった時点で加熱を終了
することにより、殆ど臭気のないコンポスト様物を得る
ことができる。On the other hand, when the heating time is set by detecting an odor component in the exhaust gas, for example, ammonia, by continuing the treatment, the ammonia concentration in the exhaust gas gradually increases and reaches a peak concentration. It is preferable to continue heating until the ammonia concentration decreases to a predetermined value, and to end the heating at this point. In this case, the ammonia concentration at which the heating is completed varies depending on the amount and properties of the organic waste to be treated, but usually the ammonia concentration is 100 pp.
By stopping the heating when the temperature becomes m or less, particularly 50 ppm or less, a compost-like substance having almost no odor can be obtained.
【0020】本発明において、排ガス中の水蒸気や臭気
成分を検出する手段としては水蒸気やアンモニアを直接
検出するセンサや、臭気成分の場合には、この成分を一
旦液中に溶解させた後、液中の濃度を検出する手段など
を採用することができる。In the present invention, the means for detecting water vapor and odor components in the exhaust gas include a sensor for directly detecting water vapor and ammonia, and in the case of odor components, this component is once dissolved in a liquid and then dissolved in the liquid. Means for detecting the concentration in the medium can be employed.
【0021】なお、本発明において、有機性廃棄物の加
熱を、直接加熱方式で行うと発火の恐れがあることか
ら、図2に示すような間接加熱装置を用いて、間接加熱
を行うのが好ましい。In the present invention, if the organic waste is heated by the direct heating method, there is a risk of ignition. Therefore, it is preferable to perform the indirect heating using an indirect heating device as shown in FIG. preferable.
【0022】図1の間接加熱装置は、加熱媒体が循環す
るように、2重壁構造とされた加熱容器1の循環路に媒
体油2を循環させて、内部の被処理物10を間接加熱す
るものである。この媒体油2は熱交換器3で加熱されて
加熱容器1の循環路を循環する。有機性廃棄物は加熱容
器1の上部投入口(図示せず)から投入され、回転軸4
の回転により攪拌羽根5で攪拌されると共に、媒体油2
で加熱され、製品のコンポスト様物は加熱容器1の底部
出口(図示せず)から取り出される。6は回転軸4の駆
動用モーターである。The indirect heating apparatus shown in FIG. 1 circulates a medium oil 2 in a circulation path of a heating vessel 1 having a double wall structure so that a heating medium circulates, and indirectly heats an object 10 to be treated inside. Is what you do. The medium oil 2 is heated by the heat exchanger 3 and circulates in the circulation path of the heating vessel 1. Organic waste is introduced from an upper inlet (not shown) of the heating vessel 1 and the rotating shaft 4
Of the medium oil 2
And the compost-like product of the product is taken out from the bottom outlet (not shown) of the heating vessel 1. Reference numeral 6 denotes a drive motor for driving the rotating shaft 4.
【0023】このような間接加熱装置で有機性廃棄物を
加熱する場合、媒体油2の温度を150〜200℃に維
持すると、後述の実施例の結果からも明らかなように、
乾燥終了前は100℃未満の被処理物10が乾燥完了後
は100〜200℃に維持され、良好な加熱が行われ
る。When heating the organic waste with such an indirect heating device, if the temperature of the medium oil 2 is maintained at 150 to 200 ° C., as will be apparent from the results of the examples described later,
Before the drying is completed, the object to be processed 10 having a temperature of less than 100 ° C. is maintained at 100 to 200 ° C. after the completion of the drying, and good heating is performed.
【0024】[0024]
【実施例】以下に実施例を挙げて本発明をより具体的に
説明する。The present invention will be described more specifically with reference to the following examples.
【0025】実施例1 し尿処理施設から発生した余剰汚泥の脱水汚泥(含水率
83%)1tonを間接加熱装置により目標処理温度2
00℃で加熱し、加熱装置から発生する排ガスをブロワ
で強制換気して(ブロワ量1m3/min)、排ガス中
のアンモニアをアンモニアセンサーにより検出し、この
結果に基いて制御装置で加熱時間を制御した。この制御
装置では排ガス中のアンモニア濃度が一旦400ppm
以上となり、その後50ppm以下となったときに、加
熱装置を停止するように設定して自動制御で処理を行っ
たところ、コンポスト様物の製造に要する所要時間約1
2時間で悪臭のない良好な性状のコンポスト様物を製造
することができた。Example 1 1 ton of dehydrated sludge (water content: 83%) of excess sludge generated from a night soil treatment facility was processed at a target treatment temperature of 2 tons using an indirect heating device.
Heated at 00 ° C., the exhaust gas generated from the heating device was forcibly ventilated by a blower (blower amount 1 m 3 / min), ammonia in the exhaust gas was detected by an ammonia sensor, and based on the result, the heating time was controlled by a control device. Controlled. In this control device, the ammonia concentration in the exhaust gas is once 400 ppm
After that, when it became 50 ppm or less, the heating device was set to be stopped and the processing was performed by automatic control.
In 2 hours, a compost-like product having good properties without odor could be produced.
【0026】なお、この処理においては、加熱開始から
約9時間後に被処理物の温度が100℃以上に上昇し、
この時点で乾燥が終了したものと推定された。その後の
被処理物の温度は150〜200℃の範囲であった。ま
た、加熱開始からの経過時間と排ガス中のアンモニア濃
度との関係は図3に示す通りであり、アンモニア濃度が
,,の時点で加熱を終了して取り出したコンポス
ト様物に水を添加して臭気を確認したところ、のアン
モニア濃度がピークとなる時点以前では強い汚泥臭があ
り、のアンモニア濃度のピーク時点でもやや汚泥臭が
あった。しかし、その後、アンモニア濃度が50ppm
以下となったの時点では臭気の殆どない製品を得るこ
とができた。In this treatment, the temperature of the object to be treated rises to 100 ° C. or more after about 9 hours from the start of heating.
At this point, it was presumed that the drying was completed. Thereafter, the temperature of the object was in the range of 150 to 200 ° C. The relationship between the elapsed time from the start of the heating and the ammonia concentration in the exhaust gas is as shown in FIG. 3. When the ammonia concentration is, the heating is terminated and water is added to the compost-like material taken out. When the odor was confirmed, there was a strong sludge odor before the ammonia concentration peaked, and there was a slight sludge odor even at the ammonia concentration peak. However, after that, the ammonia concentration became 50 ppm
At the time of the following, a product with almost no odor could be obtained.
【0027】この結果から、排ガス中のアンモニアが殆
ど検出されなくなるまで、100〜200℃で加熱処理
することにより、臭気のない製品を得ることができるこ
とがわかる。From this result, it can be seen that a product having no odor can be obtained by performing the heat treatment at 100 to 200 ° C. until almost no ammonia in the exhaust gas is detected.
【0028】実施例2 実施例1において、アンモニアセンサの代りに湿度検出
器を設け、排ガス中の水蒸気を検出し、制御装置にて、
排ガス中の水蒸気が検出されなくなってから3時間加熱
を継続したら、加熱装置を停止するように設定して自動
制御で処理を行ったところ、同様に、コンポスト様物の
製造に要する所要時間約12時間で悪臭のない良好な性
状のコンポスト様物を製造することができた。Embodiment 2 In Embodiment 1, a humidity detector is provided in place of the ammonia sensor to detect the water vapor in the exhaust gas.
When heating was continued for 3 hours after the water vapor in the exhaust gas was no longer detected, the heating device was set to stop and the processing was performed by automatic control. Similarly, the time required for the production of compost-like material was about 12 hours. A compost-like product having good properties without odor could be produced in a short time.
【0029】この処理において、排ガス中の水蒸気が検
出されなくなってからの経過時間とその時点で加熱を終
了して取り出したコンポスト様物について、実施例1と
同様にして調べた臭気との関係は下記表1の通りであ
り、排ガス中に水蒸気を検出しなくなってから、3時間
加熱を継続した後処理を終了することにより、臭気のな
い製品を得ることができることがわかる。In this treatment, the relationship between the time elapsed since the detection of water vapor in the exhaust gas was stopped and the compost-like material taken out after heating was stopped at that time was examined in the same manner as in Example 1. As shown in Table 1 below, it can be seen that a product without odor can be obtained by ending the treatment after continuing heating for 3 hours after the detection of water vapor in the exhaust gas is stopped.
【0030】[0030]
【表1】 [Table 1]
【0031】上記実施例1及び実施例2の制御方法で含
水率等の性状の異なる他の様々な有機性廃棄物について
処理を行ったところ、同様に殆ど臭気のないコンポスト
様物を製造することができた。When various other organic wastes having different properties such as moisture content were treated by the control methods of the above-mentioned Examples 1 and 2, it was found that a compost-like material having almost no odor was produced. Was completed.
【0032】[0032]
【発明の効果】以上詳述した通り、本発明のコンポスト
様物の製造方法及びコンポスト様物の製造装置によれ
ば、原料の量や性状が異なっても、100〜200℃で
加熱処理で発生する排ガス中の成分濃度を検知し、この
結果に基いて加熱処理の終了時期を自動的に判断して装
置の運転を終了させることにより、適正な処理時間で原
料を処理することができ、目標とする悪臭のない高品質
のコンポスト様物を燃料や時間、人手を浪費することな
く自動運転で効率的に製造することができる。As described above in detail, according to the method for producing a compost-like material and the apparatus for producing a compost-like material of the present invention, even if the amounts and properties of the raw materials are different, they are generated by heat treatment at 100 to 200 ° C. By detecting the concentration of the components in the exhaust gas, and automatically determining the end time of the heat treatment based on the result and terminating the operation of the apparatus, the raw material can be processed in an appropriate processing time, and the target It is possible to efficiently produce a high-quality compost-like product without odor by automatic operation without wasting fuel, time, or manpower.
【図1】本発明のコンポスト様物の製造方法及びコンポ
スト様物の製造装置の実施の形態を示す系統図である。FIG. 1 is a system diagram showing an embodiment of a method for producing a compost-like material and an apparatus for producing a compost-like material according to the present invention.
【図2】本発明における加熱処理に好適な間接加熱装置
を示す断面図である。FIG. 2 is a cross-sectional view showing an indirect heating device suitable for a heat treatment in the present invention.
【図3】実施例1における排ガス中のアンモニア濃度の
推移を示すグラフである。FIG. 3 is a graph showing changes in the concentration of ammonia in exhaust gas in Example 1.
1 加熱容器 2 媒体油 3 熱交換器 4 回転軸 5 攪拌羽根 6 モーター 10 被処理物 11 加熱装置 12 排ガス検出手段 13 排ガス処理装置 14 制御装置 DESCRIPTION OF SYMBOLS 1 Heating container 2 Medium oil 3 Heat exchanger 4 Rotating shaft 5 Stirring blade 6 Motor 10 Workpiece 11 Heating device 12 Exhaust gas detection means 13 Exhaust gas treatment device 14 Control device
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) C05F 9/04 C05F 17/02 17/02 B09B 3/00 ZABA ──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 7 Identification symbol FI Theme coat ゛ (Reference) C05F 9/04 C05F 17/02 17/02 B09B 3/00 ZABA
Claims (4)
〜200℃で加熱処理する工程を経てコンポスト様物を
製造する方法において、 該加熱処理工程から排出される排ガスに含まれる所定成
分を検知して該加熱処理時間を設定することを特徴とす
るコンポスト様物の製造方法。1. After drying organic waste by heating, 100
A method for producing a compost-like product through a heat treatment step at a temperature of 200 to 200 ° C., wherein a predetermined component contained in exhaust gas discharged from the heat treatment step is detected to set the heat treatment time. Manufacturing method of similar products.
を実質的に検出しなくなった時点から所定の加熱処理時
間を設定することを特徴とするコンポスト様物の製造方
法。2. The method for producing a compost-like product according to claim 1, wherein a predetermined heat treatment time is set from a point in time when water vapor in said exhaust gas is substantially no longer detected.
ニア濃度のピークを検出後、所定のアンモニア濃度に低
下する時点まで加熱処理時間を設定することを特徴とす
るコンポスト様物の製造方法。3. The method for producing a compost-like product according to claim 1, wherein after detecting the peak of the ammonia concentration in the exhaust gas, the heat treatment time is set until a point at which the ammonia concentration falls to a predetermined ammonia concentration.
する加熱装置と、該加熱装置から排出される排ガスの所
定成分を検知する検知手段と、該検知手段の検知信号に
基づき、前記加熱装置の加熱処理時間を制御する制御手
段とを具備することを特徴とするコンポスト様物の製造
装置。4. A heating device for heating organic waste to 100 to 200 ° C., a detecting device for detecting a predetermined component of exhaust gas discharged from the heating device, and the heating device based on a detection signal of the detecting device. An apparatus for manufacturing a compost-like product, comprising: control means for controlling a heat treatment time of the apparatus.
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Application Number | Priority Date | Filing Date | Title |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2010083742A (en) * | 2008-10-03 | 2010-04-15 | K Con Kk | Manufacturing method of fertilizer |
CN103496530A (en) * | 2013-09-29 | 2014-01-08 | 邱泽国 | Full-automatic carbonization rubbish can |
-
2000
- 2000-01-26 JP JP2000017391A patent/JP2001213683A/en active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2010083742A (en) * | 2008-10-03 | 2010-04-15 | K Con Kk | Manufacturing method of fertilizer |
CN103496530A (en) * | 2013-09-29 | 2014-01-08 | 邱泽国 | Full-automatic carbonization rubbish can |
CN103496530B (en) * | 2013-09-29 | 2016-08-17 | 邱泽国 | Full-automatic carbonization refuse receptacle |
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