JPH0341431B2 - - Google Patents

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Publication number
JPH0341431B2
JPH0341431B2 JP61141385A JP14138586A JPH0341431B2 JP H0341431 B2 JPH0341431 B2 JP H0341431B2 JP 61141385 A JP61141385 A JP 61141385A JP 14138586 A JP14138586 A JP 14138586A JP H0341431 B2 JPH0341431 B2 JP H0341431B2
Authority
JP
Japan
Prior art keywords
fermentation
tank
air
exhaust gas
outside air
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
JP61141385A
Other languages
Japanese (ja)
Other versions
JPS632883A (en
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 filed Critical
Priority to JP61141385A priority Critical patent/JPS632883A/en
Publication of JPS632883A publication Critical patent/JPS632883A/en
Publication of JPH0341431B2 publication Critical patent/JPH0341431B2/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)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、鶏糞等の家蓄糞尿、水産加工廃棄物
等を原料とする堆肥の製造方法と、その実施に直
接使用する製造装置に関する。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a method for producing compost using household manure such as chicken manure, fish processing waste, etc. as raw materials, and a production apparatus directly used for carrying out the method.

〔従来の技術と問題点〕[Conventional technology and problems]

従来、この種の堆肥製造方法及び装置として
は、ハウス醗酵型すなわち築造醗酵槽によるも
の、機械醗酵型すなわちたとえば燃焼加熱式円筒
型醗酵機によるもの等が知られている。
Conventionally, as this type of compost manufacturing method and apparatus, a house fermentation type, that is, one using a built-up fermentation tank, and a mechanical fermentation type, that is, for example, one using a combustion heating cylindrical fermenter, are known.

ハウス醗酵は、完熱度の高い臭気の少ない製品
を得ることができ、ランニングコストも比較的安
いという特長がある反面、醗酵期間として30〜80
日という長期を要し、また特に低温地方あるいは
低温期(冬期)には醗酵作用が不充分であるとい
う欠点がある。
House fermentation can produce products with a high degree of completion and low odor, and has the advantage of relatively low running costs.
The drawback is that it takes a long time (days) and the fermentation effect is insufficient, especially in low temperature regions or low temperature periods (winter).

機械醗酵は、コンパクトな設備によつて迅速か
つ大量の原料を処理できるが、燃料代がかさみラ
ンニングコストが高いとか、悪臭を伴うとかいう
ような欠点がある。
Mechanical fermentation can quickly process large quantities of raw materials using compact equipment, but has disadvantages such as high fuel costs, high running costs, and unpleasant odors.

本発明は、上記それぞれ欠点を解消しその長所
だけを利用できるようにすることを目的に提案さ
れたものである。
The present invention has been proposed for the purpose of eliminating each of the above-mentioned drawbacks and making it possible to utilize only their advantages.

〔問題点を解決するための手段〕[Means for solving problems]

上記の目的を達成するために採用した本発明の
構成は次のとおりである。
The configuration of the present invention adopted to achieve the above object is as follows.

概括的には、ハウス醗酵と機械醗酵との組み合
わせてあり、かつその組み合わせは機械醗酵の排
熱ガスをハウス醗酵のエアレーシヨン用の外気の
加温に使用したことに特質がある。
Generally speaking, it is a combination of house fermentation and mechanical fermentation, and the unique feature of this combination is that the exhaust gas from the mechanical fermentation is used to heat the outside air for the aeration of the house fermentation.

堆肥製造方法 築造醗酵槽aに投入した家蓄糞尿等の原料に槽
底の送気パイプ1を通じエアレーシヨン用の給気
をするとともに、その原料を、槽上面を走行する
撹拌機bにより適宜撹拌、切り返ししながら行う
予備醗酵と、この予備醗酵原料を、燃焼加熱式円
筒型醗酵機cに投入し、その投入口2側から取出
口3側へ撹拌しつつ移送する間に行う本醗酵とを
並行して行う。かつ、上記燃焼加熱式円筒型醗酵
機cの排熱ガスとの熱交換で外気を加温し、その
加温外気を、築造醗酵槽aの上記送気パイプ1に
送つて上記エアレーシヨン用の給気を行う。
Compost production method Air is supplied for aeration through the air supply pipe 1 at the bottom of the tank to the raw material such as household manure put into the built fermentation tank a, and the raw material is appropriately stirred by the stirrer b running on the top of the tank. The pre-fermentation is carried out while turning the fermentation material back and forth, and the main fermentation is carried out in parallel while the pre-fermented raw material is charged into the combustion heating cylindrical fermenter c and transferred from the input port 2 side to the output port 3 side while stirring. and do it. In addition, the outside air is heated by heat exchange with the exhaust gas of the combustion heating type cylindrical fermenter c, and the heated outside air is sent to the air supply pipe 1 of the construction fermentation tank a to supply the air for the aeration. Take care.

堆肥製造装置 築造醗酵aが、開放した槽上面に撹拌機bを走
行自在に乗載するとともに槽底にエアレーシヨン
用の送気パイプ1を敷設している。燃焼加熱式円
筒型醗酵機cが、原料を投入口2側から取出口3
側へ撹拌しつつ移送することができかつ上記取出
口3側には機内に熱風を送入するバーナ4を装備
している。この醗酵機cの排熱ガスを取り入れ送
出する排熱ガス通路5と、外気を取り入れ送出す
る外気通路6とを各別に備え、これら排熱ガスと
外気との間で熱交換させる熱交換器dの排熱ガス
通路5の取入口5′を上記醗酵機cの排熱ガス送
出口7に、また外気通路6の送出口6″を上記醗
酵槽aの送気パイプ1の取入口1′にそれぞれ接
続している。
Compost production equipment Build fermentation a has an agitator b movably mounted on the top of an open tank, and an air supply pipe 1 for aeration is installed at the bottom of the tank. The combustion heating type cylindrical fermenter c transfers raw materials from the input port 2 side to the output port 3.
A burner 4 is installed on the outlet 3 side to send hot air into the machine. A heat exchanger d is provided with a separate exhaust gas passage 5 that takes in and sends out the exhaust gas of the fermenter c, and an outside air passage 6 that takes in and sends outside air, and exchanges heat between these exhaust gas and outside air. The intake port 5' of the exhaust gas passage 5 is connected to the exhaust gas outlet 7 of the fermenter c, and the outlet 6'' of the outside air passage 6 is connected to the intake port 1' of the air supply pipe 1 of the fermentation tank a. They are connected to each other.

〔作用〕[Effect]

本発明は、原料を築造醗酵槽aにより予備醗酵
させ、これを燃焼加熱式円筒型醗酵機cにより本
醗酵させるとともに、醗酵機cの排熱ガスとの熱
交換で外気を加温し、その加温外気を、上記予備
醗酵時のエアレーシヨン用給気として使用するの
で、従来の築造醗酵槽だけによる場合のような長
期の醗酵期間を要せずに、また、燃焼加熱式円筒
型醗酵機だけによる場合のような高いランニング
コストをかけないで、効率的、経済的に完熟製品
を得ることができる。しかもそれは、低温地方あ
るいは低温期においても特に影響を受けない。
In the present invention, raw materials are prefermented in a built-up fermentation tank a, and then main fermentation is carried out in a combustion heating type cylindrical fermenter c, and the outside air is heated by heat exchange with the exhaust gas of the fermenter c. Since warmed outside air is used as the air supply for aeration during the pre-fermentation, there is no need for a long fermentation period like in the case of conventional built-up fermentation tanks, and there is no need for a combustion heating cylindrical fermenter. It is possible to efficiently and economically obtain ripe products without incurring high running costs as in the case of conventional methods. Moreover, it is not particularly affected even in low-temperature regions or low-temperature periods.

〔実施例〕〔Example〕

以下には本発明の実施例についてさらにくわし
く説明する。
Examples of the present invention will be described in more detail below.

a,aは並設した2基の築造醗酵槽で、これら
は、複数本の送気パイプ1を槽底に平行に列設し
た凹溝8の各々に敷設している。
A and a are two built-up fermentation tanks installed in parallel, each of which has a plurality of air supply pipes 1 laid in grooves 8 arranged in parallel on the bottom of the tank.

bは上記醗酵槽a,aの上面を自動的に走行で
きるように架設した撹拌機で、側壁9上に敷設し
たレール10に乗載されている。10′は一方の
醗酵槽aのレール10から他方の醗酵槽aのレー
ル10に撹拌機bを移乗させるための移乗用レー
ルである。
Reference numeral b denotes an agitator installed so that it can automatically run on the upper surface of the fermentation tanks a, a, and is mounted on a rail 10 laid on the side wall 9. 10' is a transfer rail for transferring the stirrer b from the rail 10 of one fermentation tank a to the rail 10 of the other fermentation tank a.

c,cは並設した2基の燃焼加熱式円筒型醗酵
機で、これらは、機台11上の支承体12に回転
自在に支承した円筒体13の両側の投入口2側端
と取出口3側端を、機台11上に設置した原料投
入口体14と取出口体15に嵌合している。16
はこれら口体14,15間に円筒体13内を貫通
させて横架した固定横杆で、これに、その軸線に
直交する方向に延びる固定翼片16′を多数設け
ている。16″は円筒体13の内周面に配設した
撹拌送り片、4は上記口体15に設けたバーナで
ある。
c and c are two combustion heating type cylindrical fermenters installed in parallel, and these are connected to the input port 2 side end and the output port on both sides of a cylindrical body 13 rotatably supported on a support 12 on a machine stand 11. The third side end is fitted into a raw material inlet body 14 and an outlet body 15 installed on the machine stand 11. 16
1 is a fixed transverse rod that extends horizontally through the cylindrical body 13 between the mouth bodies 14 and 15, and is provided with a large number of fixed wing pieces 16' extending in a direction perpendicular to its axis. Reference numeral 16'' represents a stirring and feeding piece disposed on the inner peripheral surface of the cylindrical body 13, and reference numeral 4 represents a burner provided on the mouth body 15.

d,dは醗酵槽a,aと醗酵機c,c間に設置
した熱交換器で、一側から取り入れた外気を、醗
酵槽a,aにエアレーシヨン用として加温送給す
るために、醗酵機c,cの排熱ガスとの間で熱交
換させるためのものである。
d and d are heat exchangers installed between fermentation tanks a and a and fermenters c and c. This is for exchanging heat with the exhaust gas from machines c and c.

この熱交換器dは、ハウジングd′の上下多孔板
17,17′間にパイプを蛇行架設して外気通路
6とし、上下多孔板17,17′間に充填した脱
臭剤層18中に上記パイプを埋設しているととも
に、下多孔板17′の下方空処の一側の取入口
5′から脱臭剤層18を経て上多孔板17の上方
空処の一側の排出口5″に達する排熱ガス通路5
を形成してなる。
This heat exchanger d has a pipe meanderingly installed between upper and lower perforated plates 17, 17' of a housing d' to form an outside air passage 6, and the pipe is placed in a deodorizing agent layer 18 filled between the upper and lower perforated plates 17, 17'. is buried, and the exhaust gas reaches the outlet 5'' on one side of the upper cavity of the upper perforated plate 17 from the intake port 5' on one side of the lower cavity of the lower perforated plate 17' through the deodorizing agent layer 18. Hot gas passage 5
It forms.

6′,6″は外気通路6の取入口、送出口であ
る。
Reference numerals 6' and 6'' are an intake port and a discharge port of the outside air passage 6.

排熱ガス通路5の取入口5′は、醗酵機cの原
料投入口体14に設けた排熱ガス送出口7にガス
パイプ19により接続され、排出口5″は吸引フ
アン20を介し大気に開放されるか、あるいは土
壌脱臭層(図示していない)に接続されている。
The intake port 5' of the exhaust gas passage 5 is connected to the exhaust gas outlet 7 provided in the raw material inlet body 14 of the fermenter c by a gas pipe 19, and the exhaust port 5'' is opened to the atmosphere via a suction fan 20. or connected to a soil deodorization layer (not shown).

外気通路6の送出口6″は、リングブロワー2
1を介し醗酵槽aの前記送気パイプ1の取入口
1′に接続されている。
The outlet 6″ of the outside air passage 6 is connected to the ring blower 2.
1 to the intake port 1' of the air supply pipe 1 of the fermentation tank a.

以上は本発明装置の実施例の構成であるが、次
にこの装置による本発明方法、鶏糞を原料とする
場合について説明する。
The above is the configuration of an embodiment of the apparatus of the present invention. Next, the method of the present invention using this apparatus and the case where chicken manure is used as a raw material will be explained.

水分約70〜85%の鶏糞を後記製品戻し操作等に
より水分約65%に調整した原料を築造醗酵槽a,
aに投入し、各送気パイプ1から後記加温外気を
供給してエアレーシヨするとともに、撹拌機bを
適宜走行させて、粉砕、撹拌及び切り返しを行い
ながら、予備醗酵させ、10〜15日で水分約60%の
予備醗酵原料を得る。
Chicken manure with a moisture content of approximately 70 to 85% is adjusted to approximately 65% moisture by the product return operation described later, and the raw material is then put into a fermentation tank a.
a, supply warmed outside air from each air pipe 1 for aeration, and run the stirrer b as appropriate to carry out pulverization, stirring, and turning, and pre-ferment it for 10 to 15 days. Obtain a pre-fermented raw material with a moisture content of approximately 60%.

この予備醗酵原料を、醗酵機c,cに原料投入
口体14を通じ投入するとともに、円筒体13を
回転して撹拌しつつ取出口体15側へ移送する間
に、バーナ4により熱風をその円筒体13に送入
して本醗酵させ、約3日で水分約30%の本醗酵原
料を得る。
This pre-fermented raw material is introduced into the fermenters c, c through the raw material inlet body 14, and while the cylindrical body 13 is rotated to be stirred and transferred to the outlet body 15 side, the burner 4 blows hot air into the cylinder. The raw material for main fermentation is delivered to the body 13 for main fermentation, and the main fermentation raw material with a moisture content of about 30% is obtained in about 3 days.

本醗酵原料をさらに3〜6日自然冷却すること
により水分約25%の製品とする。
This fermented raw material is further naturally cooled for 3 to 6 days to produce a product with a moisture content of approximately 25%.

上記の予備醗酵、本醗酵及び自然冷却は連続的
にしかも並行して行う。
The above-mentioned preliminary fermentation, main fermentation, and natural cooling are performed continuously and in parallel.

その間、自然冷却後の製品の一部を予備醗酵前
の水分調整に戻し、前記したように、原料の鶏糞
の水分を約70〜85%から65%に下げ、醗酵槽a内
で醗酵しやすい状態にする。
During that time, a part of the product after natural cooling is returned to the water adjustment level before pre-fermentation, and as mentioned above, the water content of the raw chicken manure is reduced from about 70-85% to 65%, making it easier to ferment in fermenter a. state.

また、醗酵機cの排熱ガスを熱交換器dに供給
するとともに外気通路6に外気を取り入れること
により、外気と排熱ガスとの間で熱交換を行わ
せ、その加温された外気をリングブロワー21を
介し送気パイプ1へ供給し、前記エアレーシヨン
作用を行わせる。
In addition, by supplying the exhaust gas from the fermenter c to the heat exchanger d and introducing outside air into the outside air passage 6, heat exchange is performed between the outside air and the exhaust gas, and the heated outside air is Air is supplied to the air supply pipe 1 through the ring blower 21 to perform the aeration effect.

上記熱交換器dによれば、醗酵器cの排熱ガス
は脱臭剤層18中を通過する間に外気を加温する
と同時に脱臭されるから、そのまま大気に排出す
ることが可能であり、また必要に応じ土壌脱臭層
へ誘導することよつて、より効果的に脱臭でき
る。さらに、上記エアレーシヨンには排熱ガスで
はなく新鮮な外気を使用することになるので、醗
酵の促進に必要な醗酵を充分に供給することがで
きる。
According to the heat exchanger d, the exhaust gas from the fermenter c is deodorized while warming the outside air while passing through the deodorizing agent layer 18, so it can be discharged to the atmosphere as is, and By guiding the soil to the soil deodorizing layer as necessary, more effective deodorization can be achieved. Furthermore, since the aeration uses fresh outside air instead of exhaust heat gas, it is possible to sufficiently supply the fermentation necessary to promote fermentation.

〔発明の効果〕〔Effect of the invention〕

叙上のように、本発明によれば、原料を築造醗
酵槽aにより予備醗酵させ、これを燃焼加熱式円
筒型醗酵機cにより本醗酵させるとともに、醗酵
機cの排熱ガスとの熱交換で新鮮な外気を加温
し、その加温外気を、上記予備醗酵時のエアレー
シヨン用給気として使用することによつて、従来
の築造醗酵槽だけによる場合のような長期の醗酵
期間を要せずに、また、燃焼加熱式円筒型醗酵機
だけによる場合のような高いランニングコストを
かけないで、効率的、経済的に完熟製品を得るこ
とができ、しかもそれは、低温地方あるいは低温
期においても特に影響を受けない、という諸々の
効果を奏する。
As mentioned above, according to the present invention, the raw material is pre-fermented in the built-up fermentation tank a, and then main fermentation is carried out in the combustion heating type cylindrical fermenter c, and heat exchange with the exhaust heat gas of the fermenter c is carried out. By heating fresh outside air and using the warmed outside air as air supply for aeration during the pre-fermentation process, the long fermentation period required using only conventional fermentation tanks can be avoided. It is possible to efficiently and economically obtain a fully ripened product without incurring the high running costs of a combustion-heated cylindrical fermenter alone, and even in low-temperature regions or periods. It has various effects such as not being particularly affected.

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

図面は本発明の実施例を説明するためのもの
で、第1図は装置全体の概略平面図、第2図は築
造醗酵層の要部断面図、第3図は燃焼加熱式円筒
型醗酵機の1例の一部省略断面図、第4,5図は
熱交換器の断面図である。 a……築造醗酵槽、1……送気パイプ、b……
撹拌機、c……燃焼加熱式円筒型醗酵機、2……
投入口、3……取出口、4……バーナ、5……排
熱ガス通路、6……外気通路、d……熱交換器、
5′……取入口、7……送出口、6″……送出口、
1′……取入口。
The drawings are for explaining embodiments of the present invention, and Fig. 1 is a schematic plan view of the entire apparatus, Fig. 2 is a cross-sectional view of the main part of the built fermentation layer, and Fig. 3 is a combustion heating cylindrical fermenter. FIGS. 4 and 5 are cross-sectional views of a heat exchanger, with a partially omitted cross-sectional view of one example. a... Built fermentation tank, 1... Air supply pipe, b...
Stirrer, c... Combustion heating cylindrical fermenter, 2...
Inlet, 3... Outlet, 4... Burner, 5... Exhaust gas passage, 6... Outside air passage, d... Heat exchanger,
5'...Intake port, 7...Outlet port, 6''...Outlet port,
1'...Intake port.

Claims (1)

【特許請求の範囲】 1 築造醗酵槽に投入した家蓄糞尿等の原料に槽
底の送気パイプを通じ給気するとともに、その原
料を、槽上面を走行する撹拌機により適宜撹拌、
切り返ししながら行う予備醗酵と、この予備醗酵
原料を、燃焼加熱式円筒型醗酵機に投入し、その
投入口側から取出口側へ撹拌しつつ移送する間に
行う本醗酵とを並行して行い、かつ、上記燃焼加
熱式円筒型醗酵機の排熱ガスとの熱交換で外気を
加温し、その加温外気を、築造醗酵槽の上記送気
パイプに送つて上記の給気を行うことを特徴とす
る堆肥製造方法。 2 開放した槽上面に撹拌機を走行自在に乗載す
るとともに槽底に送気パイプを敷設した築造醗酵
槽と、原料を投入口側から取出口側へ撹拌しつつ
移送することができかつ上記取出口側には機内に
熱風を送入するバーナを装備した燃焼加熱式円筒
型醗酵機と、この醗酵機の排熱ガスを取り入れ送
出する排熱ガス通路と、外気を取り入れ送出する
外気通路とを各別に備え、これら排熱ガスと外気
との間で熱交換させる熱交換器とからなり、熱交
換器の排熱ガス通路の取入口を上記醗酵機の排熱
ガス送出口に、また外気通路の送出口を上記醗酵
槽の送気パイプの取入口にそれぞれ接続したこと
を特徴とする堆肥製造装置。
[Scope of Claims] 1. Air is supplied to raw materials such as household excrement and urine put into a built-up fermentation tank through an air supply pipe at the bottom of the tank, and the raw materials are appropriately stirred by a stirrer running on the top of the tank.
The pre-fermentation is carried out while turning the fermentation process back and forth, and the main fermentation is carried out in parallel while the pre-fermentation raw materials are fed into a combustion heating type cylindrical fermenter and transferred from the inlet side to the outlet side while stirring. , and heating the outside air by heat exchange with the exhaust gas of the combustion heating type cylindrical fermenter, and supplying the air by sending the heated outside air to the air supply pipe of the built-up fermentation tank. A compost production method characterized by: 2. A constructed fermentation tank in which an agitator is movably mounted on the open top of the tank and an air pipe is installed at the bottom of the tank, and the raw materials can be transferred from the input port side to the output port side while stirring, and the above-mentioned fermentation tank is constructed. On the outlet side, there is a combustion heating type cylindrical fermenter equipped with a burner that sends hot air into the machine, an exhaust gas passage that takes in and sends out the exhaust gas of this fermenter, and an outside air passage that takes in and sends out outside air. and a heat exchanger for exchanging heat between these exhaust gases and outside air, and the intake of the exhaust gas passage of the heat exchanger is connected to the exhaust gas outlet of the fermenter, and A compost manufacturing apparatus characterized in that the outlet of the passage is connected to the intake of the air supply pipe of the fermentation tank.
JP61141385A 1986-06-19 1986-06-19 Compost manufacturing method and equipment Granted JPS632883A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61141385A JPS632883A (en) 1986-06-19 1986-06-19 Compost manufacturing method and equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61141385A JPS632883A (en) 1986-06-19 1986-06-19 Compost manufacturing method and equipment

Publications (2)

Publication Number Publication Date
JPS632883A JPS632883A (en) 1988-01-07
JPH0341431B2 true JPH0341431B2 (en) 1991-06-24

Family

ID=15290765

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61141385A Granted JPS632883A (en) 1986-06-19 1986-06-19 Compost manufacturing method and equipment

Country Status (1)

Country Link
JP (1) JPS632883A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AT395180B (en) * 1989-08-16 1992-10-12 Andritz Ag Maschf METHOD FOR CRUSHING MATERIALS AND SYSTEM FOR IMPLEMENTING IT
US6126781A (en) 1991-08-01 2000-10-03 Union Camp Patent Holding, Inc. Process for conditioning ozone gas recycle stream in ozone pulp bleaching

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS54146767A (en) * 1978-05-08 1979-11-16 Kaneko Agricult Machinery Method and apparatus for producing compost by utilizing solar energy
JPS6014736U (en) * 1983-07-08 1985-01-31 渡内 俊弘 folding legs of low table

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS54146767A (en) * 1978-05-08 1979-11-16 Kaneko Agricult Machinery Method and apparatus for producing compost by utilizing solar energy
JPS6014736U (en) * 1983-07-08 1985-01-31 渡内 俊弘 folding legs of low table

Also Published As

Publication number Publication date
JPS632883A (en) 1988-01-07

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