JPS60155589A - Organic matter treatment and device - Google Patents

Organic matter treatment and device

Info

Publication number
JPS60155589A
JPS60155589A JP59007266A JP726684A JPS60155589A JP S60155589 A JPS60155589 A JP S60155589A JP 59007266 A JP59007266 A JP 59007266A JP 726684 A JP726684 A JP 726684A JP S60155589 A JPS60155589 A JP S60155589A
Authority
JP
Japan
Prior art keywords
organic matter
fermentation
stage
organic
partition plate
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.)
Granted
Application number
JP59007266A
Other languages
Japanese (ja)
Other versions
JPS6365637B2 (en
Inventor
恵谷 浩
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.)
Japan Steel Works Ltd
Original Assignee
Japan Steel Works 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 Japan Steel Works Ltd filed Critical Japan Steel Works Ltd
Priority to JP59007266A priority Critical patent/JPS60155589A/en
Publication of JPS60155589A publication Critical patent/JPS60155589A/en
Publication of JPS6365637B2 publication Critical patent/JPS6365637B2/ja
Granted legal-status Critical Current

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Classifications

    • 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
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A40/00Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
    • Y02A40/10Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
    • Y02A40/20Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses

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  • Fertilizers (AREA)

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 本発明は、都市ごみ、農村発棄物などの有機質物の処理
方法およびその装置に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method and apparatus for treating organic matter such as municipal waste and rural waste.

これらの有機質物の処理に際しては、埋立、焼却などの
方法がとられていたが、これらの方法では悪臭の発生、
地下水の汚染、有害ガスの発生などの二次公害を伴い、
環境面で社会問題となっている。このため、これらの有
機質物を発酵させて堆肥を得る処理方式が、近年になっ
て採用されている。堆肥を得る処理に際しては、従来は
屋外においてこれらの有機質物を野積に、適宜反覆切返
しを行って自然の熟成を待つ方式が採られてきたが、こ
の方法では、依然として悪臭の発生や地下水の汚染など
の二次公害が避けられない。このために、これらの有機
質物を人工的につくられた好気性条件下で発酵させて堆
肥化する処理方法が採られている。この処理方式には、
ロータリーキルン(回転ドラム)式、パドル式、オーガ
式、サイロ式などの発酵槽を用いた機械式方法がある。
Methods such as landfilling and incineration have been used to dispose of these organic materials, but these methods cause problems such as the generation of bad odors and
It is accompanied by secondary pollution such as groundwater contamination and the generation of harmful gases.
It has become an environmental and social problem. For this reason, in recent years, a treatment method has been adopted in which compost is obtained by fermenting these organic substances. Conventionally, the process of obtaining compost has been to pile up these organic materials outdoors and allow them to ripen naturally by turning over and over as needed. Secondary pollution such as these cannot be avoided. For this purpose, a treatment method has been adopted in which these organic substances are fermented under artificially created aerobic conditions and composted. This processing method includes
There are mechanical methods using fermenters such as rotary kiln (rotating drum) type, paddle type, auger type, and silo type.

しかし、これらの既知の方法によるときには、いずれも
有機質物の含水率が、微生物発酵に適した50〜65%
の場合でなければ良好な好気性発酵をビない。そのため
に、有機質物を発酵槽に投入するときに、あらかじめも
みがら、公りずあるいはすでに堆肥化した最終製品の一
部を還元して使用するなどの水分調整材を有機質物中に
混入して含水率を50〜65q6に調整して、槽内で好
気性発酵をさせているのが実状である。含水率65チ以
上の有機質物の場合には、嫌気性発酵が行われて、酢酸
、プロピオン酸、酪酸、吉草酸などの低級脂肪酸や、硫
化水素、硫化メチル、メチルメルカプタンなどの硫化物
が生成され、強度の刺激臭と悪臭を発生して二次公害を
発生させるとともに、上記生成物は、まだ有機質の十分
な微生物分解が進行していない。従って、生成物の腐敗
熟成度は農業に施用するのに充分でない二堆肥化を完r
するためには、さらに長期間にわたって、堆積場で堆積
して、適宜切返し熟成させる必要があり、広い堆積面積
と長時間を要するなどの欠点がある。
However, when using these known methods, the moisture content of the organic matter is 50 to 65%, which is suitable for microbial fermentation.
Otherwise, good aerobic fermentation will not occur. To this end, when adding organic matter to the fermentation tank, a moisture regulating agent such as rice husks, rice husks, or reduced part of the final product that has already been composted is mixed into the organic matter in advance. The actual situation is that the water content is adjusted to 50 to 65q6 and aerobic fermentation is carried out in the tank. In the case of organic substances with a moisture content of 65 cm or more, anaerobic fermentation is performed to produce lower fatty acids such as acetic acid, propionic acid, butyric acid, and valeric acid, and sulfides such as hydrogen sulfide, methyl sulfide, and methyl mercaptan. This causes strong pungent and offensive odors, causing secondary pollution, and the organic matter in the products has not yet undergone sufficient microbial decomposition. Therefore, the spoilage maturity of the product is not sufficient for agricultural application, and the composting is not complete.
In order to do this, it is necessary to deposit it in a deposition site for a longer period of time, and then turn it over and ripen it as appropriate, which has disadvantages such as requiring a large deposition area and a long time.

本発明は、上記欠点を解消し、含水率が65%以上の高
水分の有機質物を、もみがら、のこくずあるいはすでに
堆肥化した最終製品の一部を還元して使用するなどの水
分調整材を使用せずに、早期に脱水し、好気性状況の下
で発酵させて、臭気を発止せずに堆肥が得られる有機質
物の処理方法およびその装置を提供する。
The present invention solves the above-mentioned drawbacks, and the present invention solves the above-mentioned drawbacks by adjusting the moisture content by using high-moisture organic matter with a moisture content of 65% or more by reducing rice husks, sawdust, or a part of the final product that has already been composted. To provide a method for processing organic matter and an apparatus thereof, capable of obtaining compost without emitting odor by early dehydration and fermentation under aerobic conditions without using wood.

本発明に係る有機質物の処理方法および処理装置を、図
面に示す実施例に基づいて説明する。図において、所要
の内容量を有する縦形発酵槽1は、その内部が仕切板2
によって、上下方向に2以上に、段階状に分割されて多
段式の複数の発酵室A。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS A method and apparatus for treating organic substances according to the present invention will be explained based on embodiments shown in the drawings. In the figure, a vertical fermenter 1 having the required internal capacity has a partition plate 2 inside.
A plurality of multistage fermentation chambers A are divided into two or more stages in the vertical direction.

B 、 ム虻揃成する。仕切板2は、その上に積載さφ れた都市ごみ、農村発棄物などの有機質物3を支持し、
かつ所定時間経過後にはこれらの有機質物3を落下させ
るために、連動制御される任意適切な仕切板動作装置1
0により、それぞれ開閉あるいは滑動などの適宜な手段
を用いて開口部■1を形成するように構成される。仕切
板2は、堆積された有機質物8の通気性を向上するため
に、鋼製多孔板などを用いて形成する。
B. The flies are all together. The partition plate 2 supports the organic matter 3 such as municipal waste and rural waste loaded on it,
In order to drop these organic substances 3 after a predetermined period of time has elapsed, an arbitrary appropriate partition plate operating device 1 that is controlled in conjunction with the organic substance 3 is provided.
0, the opening part 1 is formed using appropriate means such as opening/closing or sliding. The partition plate 2 is formed using a perforated steel plate or the like in order to improve the permeability of the deposited organic matter 8.

本発明の1態様によれば、仕切板2は、図のごとく水平
面に対して所定角度をもって傾斜して設置される。仕切
板2の傾斜下方端縁、本実施例では発酵槽lの側壁への
隣接縁\は該側壁に沿って縦方向に設けられた汚水排出
路4と連通し、汚水排出路4は、各発酵室を形成する各
階仕切板2の下方端縁とそれぞれ連通しつつ下端におい
て、外部への排出手段を具備する汚水り留5に接続する
ように構成される。
According to one aspect of the present invention, the partition plate 2 is installed to be inclined at a predetermined angle with respect to a horizontal plane as shown in the figure. The inclined lower edge of the partition plate 2, in this embodiment the edge adjacent to the side wall of the fermenter l, communicates with a sewage discharge passage 4 provided longitudinally along the side wall. It is configured to communicate with the lower edge of each floor partition plate 2 forming the fermentation chamber, and to be connected at the lower end to a sewage reservoir 5 provided with a means for discharging to the outside.

仕切板2の傾斜角度αは、上記の構成のごとく、積載さ
れた有機質物中から自然に浸出する水分、および後述す
るごとく、発酵処理中に各仕切板の下面に生ずる結露水
を、汚水排出路4に傾斜を利用して排出させるだめのも
のであり、有機質物の性状、それが形成する安息角、有
機質物から出る水分の量、仕切板の材質などから定まる
ものであって、一般に25’ −45’の範囲が適当で
ある。もし傾斜角度が25’よりも小さくなると、有機
質物の性状、有機質物からの浸出〜水分、仕切板の形状
、仕切板の材質などが通常に考えられるいかなるもので
あっても、この水分は流動摩擦、表面張力などの影響に
より、仕切板に沿って流れずに滞留し、仕切板下方の発
酵室内に所在する有機質物の表面に落下してしまう。一
方、傾斜角度が45″以上に大きい場合には、水分は有
機質物3中を重力によって垂下、にじみ出るが、有機質
物8の堆積厚さは通常はぼ800〜600mであり、仕
切板2の傾斜角度が大きい程、傾斜角度の逆余弦である
水分の流れる垂直距離が長くなるから、必然的に水1分
が流れにじみ出にくくなる。通常の含水率が65係以上
の都市ごみなどの有機質の場合には、仕切板に沿って有
効に排水可能な角度αは45゛が上限となる。
As with the above configuration, the inclination angle α of the partition plate 2 is set such that water that naturally leaches from the loaded organic matter and dew water that forms on the bottom surface of each partition plate during the fermentation process, as described later, are used to drain waste water. It is a device that is used to drain the passageway 4 using a slope, and is determined based on the properties of the organic material, the angle of repose it forms, the amount of moisture released from the organic material, the material of the partition plate, etc., and is generally 25. A range of '-45' is appropriate. If the angle of inclination is smaller than 25', this water will flow, regardless of the nature of the organic material, the leaching of water from the organic material, the shape of the partition plate, the material of the partition plate, etc. Due to the effects of friction, surface tension, etc., it does not flow along the partition plate, but remains, and falls onto the surface of organic matter located in the fermentation chamber below the partition plate. On the other hand, if the inclination angle is greater than 45'', water will sag and ooze out in the organic matter 3 due to gravity, but the accumulated thickness of the organic matter 8 is usually about 800 to 600 m, and the inclination of the partition plate 2 The larger the angle, the longer the vertical distance through which water flows, which is the inverse cosine of the inclination angle, so naturally it becomes difficult for each minute of water to seep out.In the case of organic matter such as municipal waste whose normal moisture content is 65 coefficients or higher. In this case, the upper limit of the angle α at which water can be effectively drained along the partition plate is 45°.

さらに、送風装置6、送風ライン、排風ラインおよび排
風装置7をもって構成した通気装置を設け、ここにおい
てこの送風系と排風系は図の矢印で示すごとく、各段の
発酵室について交互段に1対として設けるものであり、
これにより通気は1対となった上段階の発酵室内の有機
物質から仕切板2を経由して下段の有機質物を通って排
気されて、発酵に必要な空気が供給される。空気の供給
量は、投入有機物質の量、性状などに応じて発酵にr適
した量に定める。
Furthermore, an aeration system consisting of an air blower 6, an air line, an air exhaust line, and an air exhaust apparatus 7 is provided, and the air blowing system and the air exhaust system are arranged in alternating stages for each stage of the fermentation chamber, as shown by the arrows in the figure. It is provided as a pair in
Thereby, ventilation is exhausted from the organic matter in the pair of upper stage fermentation chambers via the partition plate 2 and through the lower stage organic matter, thereby supplying air necessary for fermentation. The amount of air supplied is determined to be suitable for fermentation depending on the amount and properties of the input organic substances.

発酵槽1の最上段の発酵室Aの上方に有機質物3を供給
する供給コンベア8を設け、最下段の発酵室下方に、発
酵処理された生成堆肥を発酵槽外へ排出する排出コンベ
ア9を設ける。
A supply conveyor 8 for supplying organic matter 3 is provided above the fermentation chamber A at the top of the fermentation tank 1, and a discharge conveyor 9 for discharging the fermented compost out of the fermentation tank is provided below the fermentation chamber at the bottom. establish.

上述のごとく構成された処理装置を用いて、含水率が6
5%以上の高水分の都市とみ、農村廃棄物などの有機質
物を発酵させて堆肥化処理する方法は、あらかじめ好気
性発酵に適した粒度に破砕した有機質物を、供給コンベ
ア8によって、多段の発酵槽1の最上段の発酵室Aに供
給し、所要の厚さに堆積する。この状態において、堆積
された有機質物8中の水分は、時間の経過とともに漸次
、傾斜した仕切板2に沿って流れ出るから、有機質物3
の含水率は、堆肥化に有効な、好気性の細菌、放線菌の
増殖と活性化に適した65チ程度まで低下する。有機質
物は上段室から下段室に落下される都度自動的に混合さ
れ、微生物の栄養源の均一分散化が行なわれる。この間
の所要日数は、有機質物の性状によって相違するが、通
常1〜3日前後である。含水率がほぼ65チに低下した
状態において、発酵室内の有機質物8は良好な好気性発
酵を行い、その温度は55〜65℃となって、活溌に水
分を蒸発し、これにより仕切板2の下側の表面、すなわ
ち下方室の天井に結露水が発生する。
Using the treatment equipment configured as described above, the moisture content is 6.
The method of fermenting and composting organic materials such as rural waste in cities with a high moisture content of 5% or more is to first crush organic materials to a particle size suitable for aerobic fermentation in a multi-stage manner using a supply conveyor 8. It is supplied to the fermentation chamber A at the top of the fermenter 1 and deposited to the required thickness. In this state, the moisture in the deposited organic matter 8 gradually flows out along the inclined partition plate 2 over time, so that the organic matter 8
The moisture content of the compost decreases to about 65%, which is suitable for the growth and activation of aerobic bacteria and actinomycetes, which are effective for composting. Organic substances are automatically mixed each time they are dropped from the upper chamber to the lower chamber, thereby uniformly dispersing nutrients for microorganisms. The number of days required during this period varies depending on the properties of the organic material, but is usually around 1 to 3 days. In a state where the moisture content has decreased to approximately 65 degrees Celsius, the organic matter 8 in the fermentation chamber undergoes good aerobic fermentation, and the temperature reaches 55 to 65 degrees Celsius, actively evaporating moisture, and as a result, the partition plate 2 Condensation water forms on the lower surface of the room, i.e. on the ceiling of the lower room.

収集されて槽外に排出処理される。従って、その際、下
段の発酵室内に存在する有機質物中に結露水が落下して
該有機物の水分低下を妨げる現象は避けられる。その結
果、このような好適な発酵処理が各段の発酵室を逐次経
過しつつ実施され、当初投入された含水率が65チ以上
の高水分の有機質物は、約5〜7日間経過することによ
り、充分な発酵処理が終って堆肥化され、そのC/N値
が低下し、還元糖態炭素割合が低下し、PH値がほぼ8
〜9となって、最下段の発酵室内に堆積された堆肥製品
を、排出コンベア9により所定区域に送出する。
It is collected and disposed of outside the tank. Therefore, in this case, it is possible to avoid a phenomenon in which condensed water falls into the organic matter existing in the lower fermentation chamber and prevents the moisture content of the organic matter from decreasing. As a result, such a suitable fermentation process is carried out while sequentially passing through each stage of the fermentation chamber, and the initially charged high-moisture organic material with a moisture content of 65 cm or more is processed for about 5 to 7 days. After sufficient fermentation treatment is completed, the compost is composted, its C/N value decreases, the reduced sugar carbon ratio decreases, and the pH value reaches approximately 8.
9, the compost product deposited in the bottom fermentation chamber is delivered to a predetermined area by the discharge conveyor 9.

なお、発酵槽内の好気性条件を最適に保つためには、発
酵槽lの供給口部と排出口部は、送風装置と排風装置の
効果を十分に発揮するために、密封性を高めた構造とす
ることが望ましい。
In addition, in order to maintain optimal aerobic conditions within the fermenter, the supply and discharge ports of the fermenter must be sealed tightly in order to fully utilize the effects of the blower and exhaust device. It is desirable to have a structure that allows for

本発明により、縦形多段式発酵槽の最上段に投入した含
水率が65%以上の高水分の有機質物の堅期脱水と、好
気性細菌類の微生物に増殖と活性化の環境を与えて有機
質物の発酵を促進させるとともに、発酵段階において有
機質物からの蒸発水分に起因する仕切板への結露を仕切
板の傾斜特性により、発酵槽外に排除させることにより
発酵中の有機質物への落下に伴なう有機質物の含水率の
低下を防出でき、有機質物の効率の高い堆肥化処理が遂
行できる。
According to the present invention, organic matter with a high moisture content of 65% or more is dehydrated in the uppermost stage of a vertical multi-stage fermenter, and an environment for the growth and activation of aerobic bacteria is provided. In addition to promoting the fermentation of materials, the sloping characteristics of the partition plates allow condensation on the partition plates caused by evaporated water from the organic materials to be removed from the fermentation tank during the fermentation stage, thereby preventing condensation from falling onto the organic materials during fermentation. The accompanying decrease in the moisture content of the organic matter can be prevented, and highly efficient composting of the organic matter can be carried out.

さらに、本発明により、従来の機械式の方法によるごと
き嫌気性発酵に伴なう強度の悪臭発生、その他地下水汚
染のごとき環境公害や、極めて長い堆肥化所要期間が軽
減され、有機質物の堆肥化処理に極めて顕著な効果を奏
する。
Additionally, the present invention reduces the strong odor and other environmental pollution associated with anaerobic fermentation, such as groundwater contamination, as well as the extremely long composting times associated with conventional mechanical methods. It has a very noticeable effect on processing.

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

図面は本発明の一実施例を示す有機質物の処理方法およ
びその装置を示す概略説明図である。 l・・・・・・発酵槽、 2・・・・・・仕切板。 8・・・・・・有機質物、4・・・・・・汚水排出路。 5・・・・・・汚水溜、 6・・・・・・送風装置。 7・・・・・・排風装置、8・・・・・・供給コンベア
。 9・・・・・・排出コンベア、IO・・・・・・開閉動
作装置。 手 続 補 正 書 (自発) 昭和59年 3月 9日 特許庁長官 殿 1、事件の表示 昭和59年 特許願 第 7266号
2、発明の名称 41機質物の処理方法及びその装置 3、補正をする者 事件との関係 特許出願人 (421)株式会社日木製鋼所 4、代 理 人 住所 東京都港区赤坂1丁目9#20号第16興和ビル
8階 氏名 弁理士(7021) 若 林 忠′電話(585
)1882 5、補正の対象 明細書の「発明の詳細な説明」の欄および図面。 6、補正の内容 (1)明細書第6頁第17行目、第20行目の「有機物
質」を「有機買物」に補正する。 (2)明細書第8頁第3〜4行目の「活溌」を「活発」
に補正する。 (3)明細書第8頁第10行目の「該有機物」を「該有
機質物」に補正する。 (4)図面を別紙の通り補正する。
The drawings are schematic explanatory diagrams showing a method for treating organic matter and an apparatus therefor, which represent an embodiment of the present invention. 1...Fermentation tank, 2...Partition plate. 8...Organic matter, 4...Sewage discharge channel. 5... Sewage sump, 6... Air blower. 7... Air exhaust device, 8... Supply conveyor. 9...Discharge conveyor, IO...Opening/closing operation device. Procedural amendment (spontaneous) March 9, 1980 Commissioner of the Patent Office 1. Indication of case 1988 Patent Application No. 7266 2. Title of invention 41. Method and apparatus for processing organic matter 3. Amendment Patent applicant (421) Nikki Steel Works Co., Ltd. 4, Agent Address 8F, Kowa Building 16, 1-9 #20 Akasaka, Minato-ku, Tokyo Name Patent attorney (7021) Tadashi Wakabayashi 'Telephone (585
) 1882 5, "Detailed Description of the Invention" column and drawings of the specification subject to amendment. 6. Contents of the amendment (1) "Organic substance" on page 6, line 17 and line 20 of the specification is amended to "organic purchase." (2) "Active" in lines 3-4 on page 8 of the specification is "active"
Correct to. (3) "The organic substance" on page 8, line 10 of the specification is amended to "the organic substance." (4) Correct the drawing as shown in the attached sheet.

Claims (1)

【特許請求の範囲】 1、含水率が65%以上の高水分の公共廃棄物などの有
機質物を、水分調整を行わずに、これを多段式発酵槽の
最上段に供給し、該有機質物の含水率を低下させつつ、
順次下段に落下させて発酵させ、最下段において堆肥を
得ることを特徴とする有機質物の処理方法。 2、有機質物を最上段の発酵室に定量ずつ供給する搬入
手段と、最下段の発酵室に生成された堆肥を排出する搬
出手段を設け、かつ各段に通気性を付与する通気手段を
有する多段式発酵槽において、各段の発酵室の仕切板を
水平に対して角度25°〜45°の範囲に傾斜させ、か
つ各段の発酵室の仕切板を開閉自在に構成して成る有機
質物の処理装置。
[Claims] 1. Organic matter such as high-moisture public waste with a moisture content of 65% or more is supplied to the top stage of a multi-stage fermenter without moisture adjustment, and the organic matter is While reducing the moisture content of
A method for processing organic matter, which is characterized in that organic matter is allowed to fall in sequence to the lower stage for fermentation, and compost is obtained at the lowest stage. 2. It has a carrying means for supplying organic matter in fixed amounts to the fermentation chamber at the top level, a carrying means for discharging the generated compost to the fermentation chamber at the bottom level, and a ventilation means for imparting ventilation to each stage. An organic material comprising a multi-stage fermenter, in which the partition plates of the fermentation chambers of each stage are inclined at an angle of 25° to 45° with respect to the horizontal, and the partition plates of the fermentation chambers of each stage are configured to be openable and closable. processing equipment.
JP59007266A 1984-01-20 1984-01-20 Organic matter treatment and device Granted JPS60155589A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59007266A JPS60155589A (en) 1984-01-20 1984-01-20 Organic matter treatment and device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59007266A JPS60155589A (en) 1984-01-20 1984-01-20 Organic matter treatment and device

Publications (2)

Publication Number Publication Date
JPS60155589A true JPS60155589A (en) 1985-08-15
JPS6365637B2 JPS6365637B2 (en) 1988-12-16

Family

ID=11661223

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59007266A Granted JPS60155589A (en) 1984-01-20 1984-01-20 Organic matter treatment and device

Country Status (1)

Country Link
JP (1) JPS60155589A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6467168A (en) * 1987-09-07 1989-03-13 Toshiko Osuga Fermentation treatment of fish

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6467168A (en) * 1987-09-07 1989-03-13 Toshiko Osuga Fermentation treatment of fish

Also Published As

Publication number Publication date
JPS6365637B2 (en) 1988-12-16

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