JPS6341877B2 - - Google Patents

Info

Publication number
JPS6341877B2
JPS6341877B2 JP60213669A JP21366985A JPS6341877B2 JP S6341877 B2 JPS6341877 B2 JP S6341877B2 JP 60213669 A JP60213669 A JP 60213669A JP 21366985 A JP21366985 A JP 21366985A JP S6341877 B2 JPS6341877 B2 JP S6341877B2
Authority
JP
Japan
Prior art keywords
rotary kiln
composting
composted
cover casing
water vapor
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
Application number
JP60213669A
Other languages
Japanese (ja)
Other versions
JPS6278180A (en
Inventor
Masayuki Nanba
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 JP60213669A priority Critical patent/JPS6278180A/en
Publication of JPS6278180A publication Critical patent/JPS6278180A/en
Publication of JPS6341877B2 publication Critical patent/JPS6341877B2/ja
Granted legal-status Critical Current

Links

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

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は動物、植物、生物菌体、汚泥、厨芥等
の生物性物質を堆肥化するための堆肥化方法およ
び該堆肥化方法に使用する堆肥化装置に関するも
のである。
[Detailed Description of the Invention] (Industrial Application Field) The present invention relates to a composting method for composting biological materials such as animals, plants, biological bacteria, sludge, kitchen waste, etc., and uses for the composting method. This relates to composting equipment.

(従来の技術) 一般に、生物性物質の堆肥化は撹拌機を内蔵し
た竪型または横型の発酵槽内に被堆肥化物を投入
し、通気と撹拌とによつて行われる。そして、こ
の場合堆肥化反応を促進するために、堆肥化反応
の温度を60℃付近以上に上昇せしめて含有水分を
通気中に蒸発せしめて発酵槽外に排出する方法が
行われている。しかしこの方法では、含水率の高
い厨芥の如き被堆肥化物の場合は通気そのものが
困難となつて発酵速度が下がり、その結果堆肥化
温度および水分の蒸発除去速度が低下する。ま
た、製品堆肥の水分含有量も40%程度以下にする
ことも困難となり、貯蔵中に発臭、虫害を生じる
ような製品しか得られないし、かつ必然的に装置
は大型化して価格が高くなる。更に、内蔵した撹
拌機による必要撹拌動力も大きくなるという欠点
がある。更にまた、堆肥化温度の調節は通気量の
調節によつて行われているが、その調節の自由度
が小さくて、運転操作は厄介であるという難点が
ある。
(Prior Art) Generally, composting of biological materials is carried out by putting the material to be composted into a vertical or horizontal fermentation tank equipped with a stirrer, and by aeration and stirring. In this case, in order to promote the composting reaction, a method is used in which the temperature of the composting reaction is raised to around 60° C. or higher, and the water content is evaporated during aeration and discharged to the outside of the fermenter. However, in this method, when the material to be composted, such as kitchen waste, has a high moisture content, aeration itself becomes difficult and the fermentation rate decreases, resulting in a decrease in the composting temperature and the rate of evaporation of moisture. In addition, it is difficult to reduce the moisture content of finished compost to less than 40%, which results in products that emit odors and cause insect damage during storage, and the equipment inevitably becomes larger and more expensive. . Furthermore, there is a drawback that the required stirring power by the built-in stirrer becomes large. Furthermore, although the composting temperature is controlled by adjusting the aeration rate, there is a problem in that the degree of freedom in this adjustment is small and operation is cumbersome.

また、模型の回転キルン内に被堆肥化物を装填
し、通気と回転キルン方式による回転撹拌とによ
つて堆肥化を行う方法があるが、必要撹拌動力は
小さいけれでも、通気による水分の除去が困難で
あるという欠点がある。
Another method is to load the material to be composted into a model rotary kiln and compost it through aeration and rotational agitation using the rotary kiln method. The disadvantage is that it is difficult.

更に、撹拌機を内蔵した横型の堆肥化装置内に
被堆肥化物を装填し、通気と撹拌とによつて堆肥
化を行う際に被堆肥化物から蒸発する水蒸気を、
堆肥化装置内の上部空間に設けた冷却器にて凝縮
せしめ、凝縮水として集水パンに集水して堆肥化
装置外に排出せしめる方法もあるが、水分の除去
は良いけれども、必要撹拌動力が大きくなるとい
う欠点がある。
Furthermore, the material to be composted is loaded into a horizontal composting device with a built-in agitator, and the water vapor that evaporates from the material to be composted is removed when composting is performed by aeration and stirring.
There is also a method of condensing water in a cooler installed in the upper space of the composting equipment, collecting the condensed water in a water collection pan, and discharging it outside the composting equipment, but although it is good at removing water, the required stirring power is The disadvantage is that it becomes large.

(発明が解決しようとする問題点) 本発明は前述の難点や、欠点を解決するために
なされたものであつて、必要撹拌動力および通気
量が小さくて、被堆肥化物から水分を一方通行的
に順調かつ十分に除去できる堆肥化方法および該
堆肥化方法に使用する堆肥化装置の提供を目的と
するものである。
(Problems to be Solved by the Invention) The present invention has been made in order to solve the above-mentioned difficulties and disadvantages. The purpose of the present invention is to provide a composting method that can smoothly and sufficiently remove waste materials, and a composting device used in the composting method.

(問題点を解決するための手段) 本発明は必要撹拌動力を小さくするために回転
キルン方法となし、通気量は発酵を維持するため
に必要な量に留め、被堆肥化物から蒸発する水蒸
気は凝縮手段にて凝縮せしめることにより分離
し、更にこの分離を順調に行わせるために回転キ
ルンの円筒体を空気や水蒸気等のガスのみの透過
を許容する多数の細孔を有する疎水性材料製とな
したものである。すなわち、 本発明の堆肥化方法は、カバーケーシングの内
部に設置してあつて側面に空気や水蒸気等のガス
のみの透過を許容する多数の細孔を有する疎水性
材料製回転キルン内に被堆肥化物を装填し、該被
堆肥化物を酸素含有気体の通気と該回転キルンの
回転に伴う撹拌とによつて堆肥化せしめる反応過
程において前記被堆肥化物から蒸発する水蒸気
を、前記細孔を通して前記回転キルンを全面的に
または部分的に取り囲み、かつ堆肥化反応を阻害
しない程度に堆肥化反応温度よりも低い温度に維
持され、更にカバーケーシングと回転キルンの間
に配置された凝縮手段に移行させて凝縮せしめ、
凝縮水として前記カバーケーシング外に排出せし
めることを特徴とするものである。また、 本発明の堆肥化装置は、一方の端部には通気口
と被堆肥化物投入ホツパーとを設けるとともに他
方の端部には排気口と堆肥排出口と凝縮水排出口
とを設けてなる横型カバーケーシングの内部に、
空気や水蒸気等のガスのみの透過を許容する多数
の細孔を有する疎水性材料製円筒の内面に撹拌・
移送用邪魔板を装備し、かつ該円筒の一方の端部
には前記通気口に通じる導入口と前記被堆肥化物
投入ホツパーに通じる投入手段とを設けるととも
に他方の端部には前記堆肥排出口に通じる排出手
段とを設けてなる回転キルンを設置し、前記カバ
ーケーシングと回転キルンの間には回転キルンを
全面的にまたは部分的に取り囲む凝縮手段を設け
てなることを特徴とするものである。
(Means for Solving the Problems) The present invention adopts a rotary kiln method in order to reduce the required stirring power, the aeration amount is limited to the amount necessary to maintain fermentation, and the water vapor evaporated from the composted material is The cylindrical body of the rotary kiln is made of a hydrophobic material that has a large number of pores that allow only gases such as air and water vapor to pass through, in order to perform the separation smoothly. This is what was done. That is, in the composting method of the present invention, compost is placed inside a rotary kiln made of a hydrophobic material that is installed inside a cover casing and has a large number of pores on the side surface that allow only gases such as air and water vapor to pass through. In a reaction process in which a compound is loaded and the composted material is composted by aeration of an oxygen-containing gas and agitation accompanying the rotation of the rotary kiln, water vapor evaporated from the composted material is passed through the pores and composted by the rotation of the rotary kiln. It surrounds the kiln completely or partially and is maintained at a temperature below the composting reaction temperature to the extent that it does not inhibit the composting reaction, and is further transferred to a condensing means disposed between the cover casing and the rotating kiln. Condensed,
The present invention is characterized in that the condensed water is discharged outside the cover casing. Further, the composting device of the present invention is provided with a ventilation port and a compostable material input hopper at one end, and an exhaust port, a compost discharge port, and a condensed water discharge port at the other end. Inside the horizontal cover casing,
The inner surface of a cylinder made of hydrophobic material has numerous pores that allow only gases such as air and water vapor to pass through.
The cylinder is equipped with a transfer baffle plate, and one end of the cylinder is provided with an inlet communicating with the ventilation port and an input means communicating with the compostable material input hopper, and the other end is provided with the compost discharge port. A rotary kiln is provided with a discharge means leading to the rotary kiln, and a condensing means is provided between the cover casing and the rotary kiln, completely or partially surrounding the rotary kiln. .

(作用) 本発明の堆肥化方法および装置によつて被堆肥
化物を堆肥化すると、堆肥化反応によつて被堆肥
化物から蒸発する水蒸気は温度の高い堆肥化物と
温度の低い凝縮手段の間に生成されている水蒸気
分圧の勾配によつて回転キルンの全周面の多数の
細孔を通つて速かに凝縮手段に移行せしめられ、
一方、被堆肥化物は回転キルン内に装填されてい
て凝縮手段に触れないので、前記水蒸気の凝縮は
順調に行われ、凝縮水は疎水性材料製の回転キル
ン内に入り込んで被堆肥化物をぬらすことがな
く、カバーケーシング外に排出されるとともに前
記水蒸気の一部だけが排気に伴われてカバーケー
シング外に排出され、堆肥化反応を終つた被堆肥
化物は堆肥となつてカバーケーシングの堆肥排出
口から排出されるのである。
(Function) When a material to be composted is composted by the composting method and apparatus of the present invention, water vapor evaporated from the material to be composted by the composting reaction is placed between the high-temperature composted material and the low-temperature condensing means. Due to the generated partial pressure gradient, water vapor is quickly transferred to the condensing means through a large number of pores on the entire circumference of the rotary kiln.
On the other hand, since the material to be composted is loaded in the rotary kiln and does not touch the condensing means, the water vapor is smoothly condensed, and the condensed water enters the rotary kiln made of hydrophobic material and wets the material to be composted. At the same time, only a part of the water vapor is discharged outside the cover casing along with the exhaust gas, and the composted material that has completed the composting reaction becomes compost and is discharged as compost from the cover casing. It is discharged from the exit.

(実施例) 以下、本発明の実施例を図面によつて詳細に説
明する。本発明の堆肥化方法に使用する堆肥化装
置を示す図において、10は横型カバーケーシン
グであり、該カバーケーシング10は横型円筒体
の両端にそれぞれ通気口18ならびに軸受孔11
を有する端板13と排気口19ならびに軸受孔1
2を有する端板14を設けてなるカバーケーシン
グ本体の一方の端部には前記通気口18を経て軸
受孔11にて支持される後記中空回転軸22内に
臨む被堆肥化物投入ホツパー15を設けるととも
に他方の端部の下部には堆肥排出口16ならびに
凝縮水排出口17を設けてなるものである。20
は横型カバーケーシング10の内部に設置した回
転キルンであり、該回転キルン20は空気や水蒸
気等のガスのみの透過を許容する多数の細孔2
1,……を有しているテフロン、ポリエチレン、
ポリプロピレン等の疎水性材料製円筒体の両端に
それぞれ前記軸受孔11にて支持される中空回転
軸22を有する端板24と前記軸受孔12にて支
持される回転軸23を有する端板25を設け、か
つ該円筒体の内面に撹拌・移送用邪魔板26,…
…を装備し、更に該円筒体の一方の端部には前記
被堆肥化物投入ホツパー15に通じる投入手段、
例えば投入螺旋27を設けるとともに他方の端部
には前記堆肥排出口16に通じる排出手段、例え
ば排出口28を設けてなるものである。前記中空
回転軸22の中空孔は前記通気口18から回転キ
ルン20内へ空気を導入する導入口40になつて
いる。前記排気口19と回転キルン20の内部と
は細孔21,……によつて通じている。31は前
記カバーケーシング10の外側に施した断熱材で
あり、該断熱材31とカバーケーシング10とに
よつて前記回転キルン20を全面的に取り囲む凝
縮手段30が形成されている。図示を省略してあ
るけれども、カバーケーシング10の外側に断熱
材31を施して凝縮手段を形成するのに替えて、
カバーケーシング10と回転キルン20の間の空
間部に回転キルンを部分的に取り囲むように冷却
器を配置して凝縮手段となすことがある。なお、
回転キルン20は図示のように水平に支持するの
に替えて排出口28側が若干低くなるように傾斜
せしめて支持してもよい。また、回転キルン20
の円筒体を図示の構造に替えて、補強用孔明き円
筒体の内外側を疎水性材料製布で被覆してもよ
い。更に、通気口18、排気口19、導入口40
等をそれぞれ図示以外の部分に形成してもよい。
(Example) Hereinafter, an example of the present invention will be described in detail with reference to the drawings. In the diagram showing the composting apparatus used in the composting method of the present invention, 10 is a horizontal cover casing, and the cover casing 10 has a ventilation hole 18 and a bearing hole 11 at both ends of the horizontal cylinder.
An end plate 13 having an exhaust port 19 and a bearing hole 1
A compostable material input hopper 15 is provided at one end of the cover casing main body, which is provided with an end plate 14 having an end plate 14 having a casing 2, and faces into a hollow rotating shaft 22 (described later) supported by a bearing hole 11 through the ventilation hole 18. At the same time, a compost outlet 16 and a condensed water outlet 17 are provided at the lower part of the other end. 20
is a rotary kiln installed inside a horizontal cover casing 10, and the rotary kiln 20 has a large number of pores 2 that allow only gases such as air and water vapor to pass through.
1, Teflon, polyethylene, having...
An end plate 24 having a hollow rotating shaft 22 supported in the bearing hole 11 at both ends of a cylindrical body made of a hydrophobic material such as polypropylene, and an end plate 25 having a rotating shaft 23 supported in the bearing hole 12. A stirring/transfer baffle plate 26,... is provided on the inner surface of the cylindrical body.
..., and further, at one end of the cylindrical body, a charging means communicating with the compostable material charging hopper 15,
For example, an input spiral 27 is provided, and the other end is provided with a discharge means, such as a discharge port 28, which communicates with the compost discharge port 16. The hollow hole of the hollow rotary shaft 22 serves as an inlet 40 for introducing air into the rotary kiln 20 from the vent 18. The exhaust port 19 and the inside of the rotary kiln 20 communicate with each other through pores 21, . Reference numeral 31 denotes a heat insulating material applied to the outside of the cover casing 10, and the heat insulating material 31 and the cover casing 10 form a condensing means 30 that completely surrounds the rotary kiln 20. Although not shown, instead of providing a heat insulating material 31 on the outside of the cover casing 10 to form a condensing means,
A cooler may be disposed in a space between the cover casing 10 and the rotary kiln 20 so as to partially surround the rotary kiln to serve as a condensing means. In addition,
Instead of supporting the rotary kiln 20 horizontally as shown, the rotary kiln 20 may be supported at an angle so that the discharge port 28 side is slightly lower. In addition, rotary kiln 20
The cylindrical body may be replaced with the structure shown in the drawings, and the inside and outside of the reinforcing perforated cylindrical body may be covered with cloth made of a hydrophobic material. Furthermore, a ventilation port 18, an exhaust port 19, an inlet port 40
etc. may be formed in portions other than those shown.

次に、前述の堆肥化装置によつて堆肥化を行う
には、被堆肥化物100を被堆肥化物投入ホツパ
ー15と投入螺旋27にて回転キルン20内に装
填し、次いで、排気口19から吸引排気せしめる
ことによつて通気口18および導入口40から被
堆肥化物100に酸素含有気体、例えば空気を通
気せしめながら、該回転キルン20を徐々に、例
えば4分間に1回の速さで回転せしめると、被堆
肥化物100は撹拌・移送用邪魔板26,……に
よつて撹拌され、通気と撹拌とによつて被堆肥化
物100の堆肥化反応が行われ、堆肥化反応によ
り生じる発酵熱によつて被堆肥化物の温度は60℃
〜70℃になり、被堆肥化物の含有水分は蒸発す
る。そして、前記回転キルン20の円筒体が空気
または水蒸気等のガスのみの透過を許容する多数
の細孔21,……を有する疎水性材料製であるの
で、被堆肥化物100は回転キルン20の内面に
付着して細孔21,……を塞ぐことがなく、かつ
被堆肥化物100は回転キルン20を全面的にま
たは部分的に取り囲んだ凝縮手段30に触れるこ
とがなく、更に該凝縮手段30の温度を堆肥化反
応を阻害しない程度に堆肥化反応温度よりも若干
低い温度、例えば45℃に維持しておくことによつ
て、回転キルン20と凝縮手段30の間には水蒸
気分圧の勾配が生成されるので、前記被堆肥化物
100から蒸発する水蒸気は回転中の回転キルン
20の全周面の多数の細孔21,……を通つて凝
縮手段30、例えば断熱材31を施した横型カバ
ーケーシング10の内面に移行せしめられ、該凝
縮手段30によつて凝縮せしめられて45℃の凝縮
水となり、該凝縮水は疎水性材料製の回転キルン
の円筒体内に入り込むことなく、凝縮水排出口1
7を経てカバーケーシング10外へ排出されると
ともに、被堆肥化物から蒸発した水蒸気の一部だ
けが排気に伴われてカバーケーシング10外に排
出され、堆肥化反応を終つた被堆肥化物は堆肥と
なつて撹拌・移送用邪魔板26,……によつてカ
バーケーシング10の堆肥排出口16から排出さ
れるのである。
Next, in order to perform composting using the above-mentioned composting apparatus, the material to be composted 100 is loaded into the rotary kiln 20 using the material to be composted input hopper 15 and the input spiral 27, and then suctioned from the exhaust port 19. The rotary kiln 20 is gradually rotated at a speed of, for example, once every 4 minutes, while an oxygen-containing gas, such as air, is vented to the composted material 100 through the vent 18 and the inlet 40 by evacuation. Then, the material to be composted 100 is stirred by the stirring/transfer baffle plate 26, . Therefore, the temperature of the composted material is 60℃.
The temperature reaches ~70℃, and the moisture contained in the composted material evaporates. Since the cylindrical body of the rotary kiln 20 is made of a hydrophobic material having a large number of pores 21 that allow only gas such as air or water vapor to pass through, the material to be composted 100 is The material to be composted 100 does not adhere to the rotary kiln 20 and block the pores 21, . By maintaining the temperature at a temperature slightly lower than the composting reaction temperature, for example, 45°C, to the extent that the composting reaction is not inhibited, a water vapor partial pressure gradient is created between the rotary kiln 20 and the condensing means 30. The water vapor evaporated from the composted material 100 passes through a large number of pores 21, . The condensed water is transferred to the inner surface of the casing 10 and condensed by the condensing means 30 to become condensed water at a temperature of 45° C., and the condensed water does not enter the cylindrical body of the rotary kiln made of hydrophobic material, but instead flows through the condensed water outlet. 1
7 and is discharged to the outside of the cover casing 10, and only a part of the water vapor evaporated from the composted material is discharged outside the cover casing 10 along with the exhaust, and the composted material that has completed the composting reaction becomes compost. The compost is then discharged from the compost discharge port 16 of the cover casing 10 by the stirring/transfer baffle plates 26, .

そして、以上のように堆肥化反応の過程におい
て発酵熱等によつて被堆肥化物100から蒸発す
る水蒸気のほとんどがカバーケーシング10内に
おいて凝縮手段30にて凝縮せしめられ、一方、
通気量は発酵に必要な量に制限されているため
に、カバーケーシング10外に水蒸気として捨て
られる熱量が少くてすむので、被堆肥化物の水分
除去に必要な熱量を節減できる。
As described above, most of the water vapor that evaporates from the material to be composted 100 due to fermentation heat etc. in the process of the composting reaction is condensed in the cover casing 10 by the condensing means 30, and on the other hand,
Since the amount of ventilation is limited to the amount necessary for fermentation, the amount of heat that is discarded as steam outside the cover casing 10 is small, so the amount of heat required for removing moisture from the composted material can be reduced.

更に、堆肥化反応を促進するために、被堆肥化
物に発酵堆肥を混合して、回転キルンに装填して
もよい。
Furthermore, in order to promote the composting reaction, fermented compost may be mixed with the material to be composted and the mixture may be loaded into the rotary kiln.

次に、図示の堆肥化装置における回転キルンの
内容積を7m3となし、該回転キルンに含水率67%
の粉砕厨芥230Kgを装填し、カバーケーシングの
内面温度を45℃に保ち、かつ通気量を発酵を維持
するために必要な量に制限して、7日間堆肥化処
理を行つたところ、発酵温度は63℃付近に達し、
蒸発した水蒸気はきわめて順調に凝縮せしめられ
て、80Kgの凝縮水となり、一方、排気に伴われて
除去された水蒸気は45Kgとなり、含水率30%の堆
肥90Kgが得られたが、このものは安定して貯蔵す
ることができた。更に、堆肥化工程中には厳密な
通気量の調節を必要としなかつた。という実験結
果が得られた。
Next, the inner volume of the rotary kiln in the illustrated composting apparatus is set to 7 m 3 , and the rotary kiln has a water content of 67%.
Composting was carried out for 7 days by loading 230 kg of crushed kitchen waste, keeping the inner temperature of the cover casing at 45°C, and limiting the amount of ventilation to the amount necessary to maintain fermentation. It reached around 63℃,
The evaporated water vapor condensed very smoothly and became 80 kg of condensed water, while the water vapor removed during exhaust was 45 kg, yielding 90 kg of compost with a moisture content of 30%, which was stable. and could be stored. Furthermore, strict regulation of the aeration rate was not required during the composting process. The experimental result was obtained.

(発明の効果) 本発明は、回転キルンを用いるものであるの
で、撹拌動力は小さくてすみ、発酵熱等を有効に
利用して被堆肥化物から蒸発する水蒸気をカバー
ケーシングの内面または内側において凝縮手段に
て凝縮水となし、多数の細孔を有する疎水性材料
によつて被堆肥化物への還流を防止することによ
り、被堆肥化物の水分除去に必要な熱量を節減で
き堆肥化が十分に可能となるのである。また、被
堆肥化物から蒸発する水蒸気は多数の細孔を有す
る疎水性材料製回転キルンを全面的にまたは部分
的に取り囲む凝縮手段にて凝縮せしめるものであ
るので、凝縮が順調に行われるとともに、凝縮水
が回転キルン内に入り込むことがなくカバーケー
シング外へ排出され、蒸発水蒸気の一部だけが排
気に伴われてカバーケーシング外へ排出されるた
めに、被堆肥化物から多量の水分を効果的に除去
することが可能となるのである。
(Effects of the Invention) Since the present invention uses a rotary kiln, the stirring power is small, and fermentation heat is effectively used to condense water vapor that evaporates from the material to be composted on the inside or inside of the cover casing. By converting the water into condensed water and preventing it from flowing back into the composted material using a hydrophobic material with a large number of pores, the amount of heat required to remove water from the composted material can be reduced and composting can be achieved sufficiently. It becomes possible. In addition, since the water vapor evaporated from the composted material is condensed by the condensing means that completely or partially surrounds the rotary kiln made of hydrophobic material having many pores, the condensation is carried out smoothly and Since condensed water does not enter the rotary kiln and is discharged outside the cover casing, and only a portion of the evaporated water vapor is discharged outside the cover casing along with the exhaust, a large amount of moisture can be effectively removed from the composted material. Therefore, it becomes possible to remove it.

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

図面は本発明の堆肥化方法に使用する堆肥化装
置の実施例を示すものであつて、第1図は一部を
切欠した縦断正面図、第2図は第1図の―線
に沿う縦断側面図である。 10:カバーケーシング、11,12:軸受
孔、13,14:端板、15:被堆肥化物投入ホ
ツパー、16:堆肥排出口、17:凝縮水排出
口、18:通気口、19:排気口、20:回転キ
ルン、21:細孔、22:中空回転軸、23:回
転軸、24,25:端板、26:撹拌・移送用邪
魔板、27:投入螺旋、28:排出口、30:凝
縮手段、31:断熱材、40:導入口、100:
被堆肥化物。
The drawings show an embodiment of the composting apparatus used in the composting method of the present invention, in which Fig. 1 is a longitudinal sectional front view with a part cut away, and Fig. 2 is a longitudinal sectional view taken along the line - in Fig. 1. FIG. 10: Cover casing, 11, 12: Bearing hole, 13, 14: End plate, 15: Composted material input hopper, 16: Compost discharge port, 17: Condensed water discharge port, 18: Ventilation port, 19: Exhaust port, 20: Rotating kiln, 21: Pore, 22: Hollow rotating shaft, 23: Rotating shaft, 24, 25: End plate, 26: Stirring/transfer baffle plate, 27: Input spiral, 28: Discharge port, 30: Condensation Means, 31: Heat insulating material, 40: Inlet, 100:
Compostable material.

Claims (1)

【特許請求の範囲】 1 カバーケーシングの内部に設置してあつて側
面に空気や水蒸気等のガスのみの透過を許容する
多数の細孔を有する疎水性材料製回転キルン内に
被堆肥化物を装填し、該被堆肥化物を酸素含有気
体の通気と該回転キルンの回転に伴う撹拌とによ
つて堆肥化せしめる反応過程において前記被堆肥
化物から蒸発する水蒸気を、前記細孔を通して前
記回転キルンを全面的にまたは部分的に取り囲
み、かつ堆肥化反応を阻害しない程度に堆肥化反
応温度よりも低い温度に維持され、更にカバーケ
ーシングと回転キルンの間に配置された凝縮手段
に移行させて凝縮せしめ、凝縮水として前記カバ
ーケーシング外に排出せしめることを特徴とする
堆肥化方法。 2 一方の端部には通気口と被堆肥化物投入ホツ
パーとを設けるとともに他方の端部には排気口と
堆肥排出口と凝縮水排出口とを設けてなる横型カ
バーケーシングの内部に、空気や水蒸気等のガス
のみの透過を許容する多数の細孔を有する疎水性
材料製円筒の内面に撹拌・移送用邪魔板を装備
し、かつ該円筒の一方の端部には前記通気口に通
じる導入口と前記被堆肥化物投入ホツパーに通じ
る投入手段とを設けるとともに他方の端部には前
記堆肥排出口に通じる排出手段とを設けてなる回
転キルンを設置し、前記カバーケーシングと回転
キルンの間には回転キルンを全面的にまたは部分
的に取り囲む凝縮手段を設けてなることを特徴と
する堆肥化装置。 3 前記凝縮手段はカバーケーシングの外側に断
熱材を施してなることを特徴とする特許請求の範
囲第2項記載の堆肥化装置。 4 前記凝縮手段はカバーケーシングと回転キル
ンとの間の空間部に冷却器を施してなることを特
徴とする特許請求の範囲第2項記載の堆肥化装
置。
[Claims] 1. A rotary kiln made of a hydrophobic material that is installed inside a cover casing and has a large number of pores on the side surface that allow only gases such as air and water vapor to pass through, and the material to be composted is loaded into the rotary kiln. In the reaction process in which the composted material is composted by aeration of oxygen-containing gas and agitation accompanying the rotation of the rotary kiln, water vapor evaporated from the composted material is passed through the pores to the entire surface of the rotary kiln. completely or partially surrounded and maintained at a temperature lower than the composting reaction temperature to the extent that the composting reaction is not inhibited, and further transferred to a condensing means disposed between the cover casing and the rotary kiln for condensation; A composting method characterized by discharging condensed water outside the cover casing. 2 A horizontal cover casing is provided with a ventilation port and a compostable material input hopper at one end, and an exhaust port, a compost discharge port, and a condensed water discharge port at the other end. A cylinder made of a hydrophobic material having a large number of pores that allows only gases such as water vapor to permeate is equipped with a baffle plate for stirring and transfer on the inner surface, and one end of the cylinder is equipped with an inlet that leads to the ventilation hole. A rotary kiln is installed, the rotary kiln having a mouth and an input means communicating with the compostable material input hopper, and a discharge means communicating with the compost discharge port at the other end, and between the cover casing and the rotary kiln. A composting device characterized in that it is provided with condensing means that completely or partially surrounds a rotary kiln. 3. The composting apparatus according to claim 2, wherein the condensing means is provided with a heat insulating material on the outside of the cover casing. 4. The composting apparatus according to claim 2, wherein the condensing means includes a cooler provided in a space between the cover casing and the rotary kiln.
JP60213669A 1985-09-28 1985-09-28 Composting method and apparatus Granted JPS6278180A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60213669A JPS6278180A (en) 1985-09-28 1985-09-28 Composting method and apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60213669A JPS6278180A (en) 1985-09-28 1985-09-28 Composting method and apparatus

Publications (2)

Publication Number Publication Date
JPS6278180A JPS6278180A (en) 1987-04-10
JPS6341877B2 true JPS6341877B2 (en) 1988-08-19

Family

ID=16642998

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60213669A Granted JPS6278180A (en) 1985-09-28 1985-09-28 Composting method and apparatus

Country Status (1)

Country Link
JP (1) JPS6278180A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4642197B2 (en) * 1999-10-29 2011-03-02 太平洋セメント株式会社 Fermentation processing equipment, raw fuel production equipment for cement production, and cement production plant
JP4642196B2 (en) * 1999-11-02 2011-03-02 太平洋セメント株式会社 Fermentation processing method and cement manufacturing method

Also Published As

Publication number Publication date
JPS6278180A (en) 1987-04-10

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