JPS6352000B2 - - Google Patents

Info

Publication number
JPS6352000B2
JPS6352000B2 JP56186119A JP18611981A JPS6352000B2 JP S6352000 B2 JPS6352000 B2 JP S6352000B2 JP 56186119 A JP56186119 A JP 56186119A JP 18611981 A JP18611981 A JP 18611981A JP S6352000 B2 JPS6352000 B2 JP S6352000B2
Authority
JP
Japan
Prior art keywords
livestock manure
tank
fermentation
anaerobic digestion
fermentation tank
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
JP56186119A
Other languages
Japanese (ja)
Other versions
JPS5888191A (en
Inventor
Tsuneji Hisanaga
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.)
HISANAGA KIKO KK
Original Assignee
HISANAGA KIKO KK
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 HISANAGA KIKO KK filed Critical HISANAGA KIKO KK
Priority to JP56186119A priority Critical patent/JPS5888191A/en
Publication of JPS5888191A publication Critical patent/JPS5888191A/en
Publication of JPS6352000B2 publication Critical patent/JPS6352000B2/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
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/30Fuel from waste, e.g. synthetic alcohol or diesel

Landscapes

  • Treatment Of Sludge (AREA)
  • Fertilizers (AREA)

Description

【発明の詳細な説明】 本発明は、家畜糞の堆肥化方法及びその装置に
関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method and apparatus for composting livestock manure.

尿や洗浄水が混入している湿潤家畜糞は、含水
率が約85%であつて、そのまゝでは堆肥化が困難
であるので、従来は湿潤家畜糞に等量の乾燥した
鋸屑や籾殻等を混合して含水率を66〜67%に下げ
てから堆肥化を行つていた。しかしながら生成さ
れた堆肥の肥効性が少なく、かつ最近では鋸屑や
籾殻等の入手が困難になつたために堆肥化に先立
つて湿潤家畜糞を脱水機にて醗酵し易い状態にま
で脱水調湿することが行われるようになつたけれ
ども、脱水調湿の際に分離された絞り水汚水の無
害化処理という問題が新たに提起されることにな
つた。
Wet livestock dung mixed with urine and washing water has a moisture content of approximately 85%, making it difficult to compost as it is. composting was carried out after lowering the moisture content to 66-67%. However, the fertilizer effect of the produced compost is low, and recently it has become difficult to obtain sawdust, rice husks, etc., so before composting, wet livestock manure is dehydrated and adjusted to a state where it is easy to ferment using a dehydrator. However, a new problem has arisen: how to detoxify the waste water from the squeeze water separated during dehydration and humidity control.

本発明は、二次公害の原因となる汚水、汚泥等
を系外に排出することなく湿潤家畜糞を堆肥化処
理する方法及びその装置の提供を目的とするもの
であり、すなわちその方法は、処理すべき湿潤家
畜糞のほぼ半分量を醗酵し易い状態に脱水調湿し
て絞り水汚水と調湿家畜糞とに分離し、前記絞り
水汚水を嫌気性消化槽に導入し消化処理してメタ
ンガスを発生せしめるとともに同槽内にて消化汚
泥を生成し、前記発生したメタンガスを燃料とし
て得られた温風を前記調湿家畜糞に吹込みながら
一次醗酵を行わせ、該一次醗酵にて得られた乾燥
堆肥に前記した処理すべき湿潤家畜糞の残りほゞ
半分量を混合せしめることにより水分調整を行つ
て醗酵し易い状態に調湿して通気しながら二次醗
酵を行わせ、該二次醗酵にて得られた乾燥堆肥に
更に前記嫌気性消化槽内で生成した消化汚泥を系
外に排出させることなく混合吸収せしめることに
よつて水分調整された堆肥とすることであり、ま
たその方法を達成するための装置として、処理す
べき湿潤家畜糞のほぼ半分量を脱水調湿するスク
リユープレスと、該スクリユープレスにて分離し
た絞り水汚水を導入して消化処理する嫌気性消化
槽と、該嫌気性消化槽で発生したメタンガスを燃
料として温風を発生する温風発生装置と、該温風
発生装置にて発生した温風を吹込みながら前記ス
クリユープレスにて脱水調湿した調湿家畜糞を搬
入撹拌して一次醗酵せしめる一次醗酵槽と、該一
次醗酵にて得られた乾燥堆肥に前記処理すべき湿
潤家畜糞の残りほゞ半分量を混合せしめて醗酵し
易い状態に調湿する混合手段と、該混合手段によ
つて得られた調湿混合物を搬入して撹拌と通気と
によつて二次醗酵せしめる二次醗酵槽を備え、前
記嫌気性消化槽内に生成した消化汚泥を前記二次
醗酵槽内に導入するためのポンプ及び引抜管を設
けたものであり、これを図面に示す実施例につい
て説明する。
The object of the present invention is to provide a method and apparatus for composting wet livestock manure without discharging sewage, sludge, etc. that cause secondary pollution to the outside of the system. Approximately half of the wet livestock manure to be treated is dehydrated and moistened to a state that is easy to ferment, separated into squeezed wastewater and moistened livestock manure, and the squeezed wastewater is introduced into an anaerobic digestion tank for digestion treatment. Methane gas is generated and digested sludge is generated in the same tank, and primary fermentation is carried out while blowing hot air obtained by using the generated methane gas as fuel into the humidity-conditioned livestock manure, and the product obtained in the primary fermentation is The remaining half of the wet livestock manure to be treated as described above is mixed with the dried compost, and the moisture is adjusted to a state that facilitates fermentation. The purpose is to mix and absorb the digested sludge produced in the anaerobic digestion tank into the dry compost obtained by the next fermentation without discharging it outside the system, thereby producing compost with adjusted moisture content. The devices used to achieve this method include a screw press that dehydrates and moistens almost half of the wet livestock manure to be treated, and an anaerobic digestion system that introduces and digests the squeezing water sewage separated by the screw press. A tank, a hot air generator that generates hot air using the methane gas generated in the anaerobic digestion tank as fuel, and dehydration and humidity control using the screw press while blowing in the warm air generated by the hot air generator. A primary fermentation tank into which the humidified livestock manure is transported and agitated for primary fermentation, and a state in which approximately half of the remaining wet livestock manure to be treated is mixed with the dry compost obtained in the primary fermentation to facilitate fermentation. and a secondary fermentation tank into which the humidity-adjusted mixture obtained by the mixing means is brought in and subjected to secondary fermentation by stirring and aeration, A pump and a drawing pipe are provided for introducing the digested sludge into the secondary fermentation tank, and an embodiment shown in the drawings will be described.

処理すべき湿潤家畜糞Aのほぼ半分量をコンベ
ヤ71にてスクリユープレス1のホツパー11に
投入し、スクリユープレス1によつて醗酵し易い
状態に脱水調湿処理すると、湿潤家畜糞Aは脱水
処理され、絞り水汚水と調湿家畜糞A1とに分離
される。多孔壁12より分離された絞り水汚水は
受皿14、排水管15を経て貯槽16内に溜り、
次いで電動機付きポンプ17にて送水管18を経
て嫌気性消化槽2内に送り込まれる。他方、スク
リユープレス1の排出口13から排出される調湿
家畜糞A1はコンベヤ72にて一次醗酵槽4に搬
入されるようになつている。
Approximately half of the wet livestock manure A to be processed is put into the hopper 11 of the screw press 1 by the conveyor 71, and dehydrated and humidified by the screw press 1 to make it easy to ferment. It is dehydrated and separated into squeezed wastewater and humidified livestock manure A1 . The squeeze water wastewater separated from the porous wall 12 passes through the saucer 14 and the drain pipe 15 and accumulates in the storage tank 16.
Next, it is sent into the anaerobic digestion tank 2 via the water pipe 18 by a pump 17 with an electric motor. On the other hand, the humidity-controlled livestock manure A 1 discharged from the discharge port 13 of the screw press 1 is conveyed to the primary fermentation tank 4 by a conveyor 72 .

前記嫌気性消化槽2は断熱カバー21とフロー
テイングカバー22とを備えていて、消化槽2内
に送り込まれた絞り水汚水の消化によつて同槽2
内に発生したメタンガスはフローテイングカバー
22内に貯溜され、該フローテイングカバー22
の自重による圧力にてガス引抜管23を経て温風
発生装置3のガスバーナ31に供給され、また、
消化槽2内に生成した消化汚泥は汚泥引抜管24
とポンプ25とによつて二次醗酵槽6の汚泥送入
口66を経て二次醗酵槽6内に導入されるように
なつている。必要に応じて前記ガス引抜管23に
脱硫器を挿入するようにする。
The anaerobic digestion tank 2 is equipped with a heat insulating cover 21 and a floating cover 22, and the anaerobic digestion tank 2 is equipped with a heat insulating cover 21 and a floating cover 22.
The methane gas generated inside is stored in the floating cover 22, and the floating cover 22
is supplied to the gas burner 31 of the hot air generator 3 through the gas extraction pipe 23 under pressure due to its own weight, and
The digested sludge generated in the digestion tank 2 is transferred to the sludge extraction pipe 24.
The sludge is introduced into the secondary fermentation tank 6 through the sludge inlet 66 of the secondary fermentation tank 6 by the pump 25 and the sludge inlet 66 of the secondary fermentation tank 6. A desulfurizer may be inserted into the gas extraction pipe 23 if necessary.

前記温風発生装置3はガスバーナ31と燃焼室
32と空気取入管33と送風機34とを備えてい
て、発生した温風は送風機34にて送風管35及
び一次醗酵槽4の温風導入管49を経て一次醗酵
槽4内に吹込まれるようになつている。
The hot air generator 3 includes a gas burner 31, a combustion chamber 32, an air intake pipe 33, and a blower 34, and the generated hot air is passed through the blower 34 to the blower pipe 35 and the hot air introduction pipe 49 of the primary fermentation tank 4. It is designed to be blown into the primary fermentation tank 4 through.

前記一次醗酵槽4は、第2図に示すように、モ
ータaとウオームbとウオームホイールcとによ
つて減速回転される縦軸44に取付けた撹拌器4
1と搬出器42と槽底に配置したノズル43とを
備えている。搬出器、例えばレーキ42は多数の
搬出板を備えていて一次醗酵された乾燥堆肥A2
を排出口45から排出するようになつている(第
2図参照)。ノズル43は、第3図に示すように、
内外二重に配置した環状ヘツダ46に取付けてあ
り、その上端部側面には、水平方向にノズル孔4
7を設けてある(第5図参照)。環状ヘツダ46
は分岐管48にて温風導入管49に接続し、温風
導入管49は前記温風発生装置3の送風管35に
接続してある。
As shown in FIG. 2, the primary fermentation tank 4 includes an agitator 4 attached to a vertical shaft 44 that is rotated at a reduced speed by a motor a, a worm b, and a worm wheel c.
1, an unloader 42, and a nozzle 43 arranged at the bottom of the tank. The transport device, for example the rake 42, is equipped with a large number of transport plates, and is used to collect dry compost A 2 that has undergone primary fermentation.
is discharged from the discharge port 45 (see Fig. 2). The nozzle 43, as shown in FIG.
It is attached to an annular header 46 arranged double-layered inside and outside, and a nozzle hole 4 is formed horizontally on the side surface of its upper end.
7 (see Figure 5). Annular header 46
is connected to a hot air introduction pipe 49 through a branch pipe 48, and the hot air introduction pipe 49 is connected to the blast pipe 35 of the hot air generator 3.

前記混合手段5は、一次醗酵槽4の排出口45
から排出される一次醗酵された乾燥堆肥A2とコ
ンベヤ73にて搬入されてくる前記処理すべき湿
潤家畜糞Aの残りほゞ半分とを混合して調湿する
もので、例えばホツパーであつて、混合された調
湿混合物A3はコンベヤ74にて二次醗酵槽6の
ホツパー65に投入するようになつている。
The mixing means 5 includes an outlet 45 of the primary fermentation tank 4.
The dry compost A 2 that has undergone primary fermentation and is discharged from the hopper is mixed with the remaining half of the wet livestock manure A to be treated that is carried in by the conveyor 73 to adjust the humidity. The mixed humidity control mixture A3 is fed into a hopper 65 of the secondary fermentation tank 6 via a conveyor 74.

二次醗酵槽6は、第4図に示すように、撹拌器
61とノズル62とを備えていて、撹拌器61は
減速モータdにて回転する水平軸63に取付けて
あり、ノズル62は槽底に配置した送気管64に
取付けてあり、前記第1醗酵槽4の槽底に配置し
たノズル43と同様に上端部側面にノズル孔を設
けてある。65は前記したように調湿混合物A3
を投入するホツパーであり、66は嫌気性消化槽
4で生成された消化汚泥をポンプ25及び汚泥引
抜管24を経て送入せしめる汚泥送入口であり、
67は二次醗酵によつて得られた乾燥堆肥に前記
消化汚泥を混合吸収せしめて所望の水分調整堆肥
とした使用可能の堆肥を排出する堆肥排出口であ
り、該排出口67から送り出された水分調整堆肥
A4はコンベヤ75によつて装置外に搬出される
ようになつている。
The secondary fermentation tank 6, as shown in FIG. It is attached to an air supply pipe 64 placed at the bottom, and, like the nozzle 43 placed at the bottom of the first fermentation tank 4, a nozzle hole is provided on the side surface of the upper end. 65 is the humidity control mixture A 3 as described above.
66 is a sludge inlet port through which the digested sludge generated in the anaerobic digestion tank 4 is sent through the pump 25 and the sludge extraction pipe 24;
Reference numeral 67 is a compost discharge port for discharging usable compost by mixing and absorbing the digested sludge into the dry compost obtained by secondary fermentation to obtain the desired moisture-adjusted compost. Moisture-adjusted compost
A 4 is conveyed out of the apparatus by a conveyor 75.

本発明における嫌気性消化槽2、一次醗酵槽4
及び二次醗酵槽6のそれぞれの容量は次のように
するのが好適である。すなわち、嫌気性消化槽2
の容量は1日に送り込まれる絞り水汚水の約20日
分を貯溜できる大きさに、一次醗酵槽4の容量は
1日に投入される調湿家畜糞A1の約15日分を貯
溜できる大きさに、二次醗酵槽6の容量は1日に
投入される調湿混合物A3の約15日分を貯溜でき
る大きさに設計すれば好適な家畜糞の堆肥化装置
となる。
Anaerobic digestion tank 2 and primary fermentation tank 4 in the present invention
It is preferable that the respective capacities of the secondary fermenter 6 and the secondary fermenter 6 are as follows. That is, anaerobic digestion tank 2
The capacity of the primary fermentation tank 4 is large enough to store approximately 20 days' worth of squeeze water wastewater that is sent in each day, and the capacity of the primary fermentation tank 4 can store approximately 15 days' worth of humidity-controlled livestock manure A1 that is inputted each day. In terms of size, if the capacity of the secondary fermentation tank 6 is designed to be large enough to store about 15 days' worth of humidity control mixture A3 input in one day, it will become a suitable livestock manure composting device.

以上のように構成される本発明の家畜糞の堆肥
化方法及びその装置の作用を説明すると、例え
ば、家畜舎から尿や洗浄水が混入していて含水率
85%程度の湿潤家畜糞を猫車等にて搬出し、1日
に発生する量の半分の湿潤家畜糞Aをコンベヤ7
1にてスクリユープレス1のホツパー11に投入
し、スクリユープレス1を稼動して家畜糞Aを醗
酵し易い状態、例えば含水率58―60%程度になる
ように圧搾脱水して調湿すると、そのとき多孔壁
12から出る絞り水汚水と、排出口13から出る
調湿家畜糞A1とに分離される。この一方の絞り
水汚水は受皿14、排水管15を経て貯槽16内
に溜まり、次いで、電動機付きポンプ17にて送
水管18を経て嫌気性消化槽2内に送り込まれる
とともに、他方の調湿家畜糞A1はコンベヤ72
にて一次醗酵槽4内に搬入される。
To explain the operation of the livestock manure composting method and apparatus of the present invention constructed as described above, for example, urine and washing water from the livestock house are mixed in and the moisture content is reduced.
Approximately 85% of the wet livestock manure is carried out using a cat cart, etc., and the wet livestock manure A, which is half of the amount generated in a day, is transferred to conveyor 7.
1, put it into the hopper 11 of the screw press 1, operate the screw press 1, and compress and dehydrate the livestock manure A so that it can be easily fermented, for example, to have a moisture content of about 58-60%. At that time, it is separated into squeezing water wastewater coming out of the porous wall 12 and humidity-controlled livestock manure A1 coming out of the discharge port 13. The waste water from one of the squeezed water passes through the saucer 14 and the drain pipe 15, accumulates in the storage tank 16, and is then sent into the anaerobic digestion tank 2 via the water supply pipe 18 by the motorized pump 17, and is sent to the other humidity-controlled livestock tank. Feces A 1 is on conveyor 72
It is carried into the primary fermentation tank 4.

嫌気性消化槽2に送り込まれた絞り水汚水は
BOD15000〜20000PPM、固形物濃度6〜8%を
含有しており、嫌気性消化槽2において、前記絞
り水汚水は消化処理されてメタンガスを発生する
とともにBOD3000〜4000PPM程度の消化汚泥が
生成される。前記の発生したメタンガスはフロー
テイングカバー22内に貯溜され、フローテイン
グカバー22の自重による圧力にてガス引抜管2
3を経て温風発生装置3のガスバーナー31に供
給されるとともに、消化汚泥は、毎月、電動機付
きポンプ17にて嫌気性消化槽2に送入した絞り
水汚水の量に相当する分量だけポンプ25にて汚
泥引抜管24を経て引抜かれ、二次醗酵槽6の汚
泥送入口66より二次醗酵槽6内に送り込まれ
る。
The squeezed water wastewater sent to the anaerobic digestion tank 2 is
It contains a BOD of 15,000 to 20,000 PPM and a solids concentration of 6 to 8%. In the anaerobic digestion tank 2, the squeezed water wastewater is digested to generate methane gas and digested sludge with a BOD of about 3,000 to 4,000 PPM. The generated methane gas is stored in the floating cover 22, and the gas extraction pipe 2 is pumped under pressure due to the weight of the floating cover 22.
3 to the gas burner 31 of the hot air generator 3, and the digested sludge is pumped in an amount equivalent to the amount of squeezed water sewage sent to the anaerobic digestion tank 2 every month using the motorized pump 17. At 25, the sludge is drawn out through the sludge drawing pipe 24, and sent into the secondary fermentation tank 6 through the sludge inlet 66 of the secondary fermentation tank 6.

温風発生装置3においては、ガスバーナ31に
て供給されたメタンガスは燃焼室32内において
燃焼して高温ガスとなり、これに空気取入管33
から取入れた空気を混合して約60℃の温風とな
し、温風は送風機34にて加圧のうえ、送風管3
5を経て一次醗酵槽4の温風導入管49より一次
醗酵槽4内に導入される。
In the hot air generator 3, methane gas supplied by the gas burner 31 burns in the combustion chamber 32 to become high-temperature gas, which is then passed through the air intake pipe 33.
The air taken in from the air is mixed to produce warm air at approximately 60°C, and the hot air is pressurized by the blower 34 and sent to the air pipe 3.
5 and is introduced into the primary fermentation tank 4 from the hot air introduction pipe 49 of the primary fermentation tank 4.

一次醗酵槽4においては、コンベヤ72にて搬
入された調湿家畜糞A1は、モータa、ウオーム
b、ウオームホイルc及び縦軸44によつて緩速
回転される撹拌器41にて撹拌され、次第に槽底
に向つて沈降し堆積する。前記したように温風発
生装置3から温風導入管49に導入された温風は
分岐管48、環状ヘツダ46を経て一次醗酵槽4
の槽底に配置したノズル43から前記堆積家畜糞
中に吹込まれる。撹拌器41の撹拌によつて調湿
家畜糞A1は好気的に保持され醗酵し、さらに前
記した状態で吹込まれる温風によつて醗酵が促進
され、醗酵が進行するにしたがつて槽内は醗酵熱
によつて約70℃になり、家畜糞中の水分を蒸発さ
せながら堆肥化が行われる。醗酵が終了して槽4
の底部に沈降堆積した乾燥堆肥A2は含水率が約
15%であつて、前記の縦軸44の下端部に取付け
てある搬出器42によつて排出口45から混合手
段、例えばホツパー5に排出される。
In the primary fermentation tank 4, the humidity-controlled livestock manure A1 carried in by the conveyor 72 is stirred by an agitator 41 that is slowly rotated by a motor a, a worm b, a worm wheel c, and a vertical shaft 44. , gradually settles and accumulates toward the bottom of the tank. As described above, the hot air introduced from the hot air generator 3 into the hot air introduction pipe 49 passes through the branch pipe 48 and the annular header 46 to the primary fermentation tank 4.
It is blown into the accumulated livestock manure from a nozzle 43 arranged at the bottom of the tank. The humidified livestock manure A1 is aerobically maintained and fermented by stirring by the stirrer 41, and the fermentation is further promoted by the warm air blown in the above-mentioned state, and as the fermentation progresses. The temperature inside the tank reaches approximately 70 degrees Celsius due to fermentation heat, and composting takes place while the water in the livestock dung evaporates. Fermentation is completed and tank 4
The dry compost A 2 that has settled and accumulated at the bottom has a moisture content of approximately
15%, which is discharged from a discharge port 45 to a mixing means, for example, a hopper 5, by a discharge device 42 attached to the lower end of the vertical shaft 44.

ホツパー5内においては、一次醗酵槽4から排
出されてきた乾燥堆肥A2にコンベヤ73にて搬
入する1日に発生した量の半分の湿潤家畜糞Aを
混合して含水率65%程度に調湿された調湿混合物
A3とし、該調湿混合物A3はコンベヤ74にて二
次醗酵槽6のホツパー65に投入される。
In the hopper 5, the dry compost A2 discharged from the primary fermentation tank 4 is mixed with wet livestock manure A, which is half the amount generated in a day and carried in by the conveyor 73, to adjust the moisture content to about 65%. moistened humidity control mixture
A3 , and the humidity-adjusted mixture A3 is fed into the hopper 65 of the secondary fermentation tank 6 via the conveyor 74.

二次醗酵槽6においては、ホツパー65から投
入された調湿混合物A3は減速モーターd及び水
平軸63によつて緩速回転する撹拌器61にて撹
拌される際に乾燥堆肥中に含まれている多量の醗
酵菌が湿潤家畜糞に種付けされるとともに、送風
管64のノズル62から送入される空気によつて
醗酵が促進されて堆肥化が行われ、堆肥化が終了
したのちに、生成された乾燥堆肥に、前記した嫌
気性消化槽2で生成された消化汚泥をポンプ25
により汚泥引抜管24にて引き抜き二次醗酵槽6
の汚泥送入口66より二次醗酵槽6内に送入し、
前記の乾燥堆肥と混合し、乾燥堆肥に吸収され水
分調整堆肥A4とされ、排出口67より排出され、
コンベヤ75にて装置外に搬出されるのである。
In the secondary fermentation tank 6, the humidity-controlled mixture A3 fed from the hopper 65 is mixed in the dry compost by the agitator 61 which rotates slowly by the deceleration motor d and the horizontal shaft 63. A large amount of fermenting bacteria are inoculated into the wet livestock manure, and fermentation is promoted by air introduced from the nozzle 62 of the blower pipe 64 to perform composting. After the composting is completed, A pump 25 pumps the digested sludge generated in the anaerobic digestion tank 2 into the generated dry compost.
The sludge is drawn out through the sludge drawing pipe 24 and transferred to the secondary fermentation tank 6.
The sludge is fed into the secondary fermentation tank 6 from the sludge inlet 66,
It is mixed with the dry compost mentioned above, absorbed into the dry compost to become moisture-adjusted compost A4 , and discharged from the discharge port 67.
It is carried out of the apparatus by a conveyor 75.

本発明にかゝる家畜糞の堆肥化方法及びその装
置は、処理すべき湿潤家畜糞のほぼ半分量を脱水
調湿するものであるので、家畜糞の全量を一時に
脱水調湿する場合に比して絞り水汚水の量がほゞ
半分となり、汚水に含まれる固形物も少ないの
で、消化処理が迅速に行われ、かつ、消化処理に
よつて生成された消化汚泥の量も少なくなるの
で、この生成された消化汚泥を二次醗酵後の乾燥
堆肥に混合吸収せしめて堆肥化処理することがで
きる効果があり、さらに処理すべき量の残りほゞ
半分量を一次醗酵により得られた乾燥堆肥に混合
せしめて水分調整を行い醗酵しやすい状態として
二次醗酵を行わせるものであり、従来のように、
湿潤家畜糞を調湿するために入手困難な鋸屑や籾
殻等を混入する必要はなく、また鋸屑や籾殻等の
混合物による堆肥の肥効性の低減を来たす恐れは
全くなく、更に、本発明においては、前記したよ
うに絞り水汚水の消化処理によつて生成された汚
泥を系外に排出することなく、ポンプ、汚泥引抜
管を用いて二次醗酵槽に送入せしめて堆肥化処理
するもので、従来のように、消化槽にて消化処理
して排出された汚水、汚泥をさらに無害化するた
めに必要とした汚水の生物学的等の処理設備や汚
泥の乾燥設備がともに不要となる効果を有するも
のである。
The method and apparatus for composting livestock manure according to the present invention dehydrates and moisturizes approximately half of the wet livestock manure to be treated, so it is difficult to dehydrate and moisturize the entire amount of livestock manure at once. Comparatively, the amount of wastewater from the squeeze water is about half, and the solids contained in the wastewater are also small, so the digestion process is carried out quickly, and the amount of digested sludge produced by the digestion process is also reduced. , this generated digested sludge can be mixed and absorbed into the dry compost after secondary fermentation for composting treatment, and the remaining half of the amount to be treated can be added to the dry compost obtained from the primary fermentation. It is mixed with compost to adjust the moisture content and perform secondary fermentation to make it easier to ferment.
There is no need to mix sawdust, rice husks, etc., which are difficult to obtain, in order to adjust the humidity of wet livestock manure, and there is no fear that the mixture of sawdust, rice husk, etc. will reduce the fertilizing efficiency of the compost. As mentioned above, the sludge generated through the digestion treatment of squeeze water sewage is composted by being sent to a secondary fermentation tank using a pump and sludge extraction pipe without discharging it outside the system. This eliminates the need for biological treatment equipment for sewage and sludge drying equipment, which were required in the past to further detoxify the sewage and sludge discharged through digestion in a digestion tank. It is effective.

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

第1図は、本発明の工程図を示す概略図、第2
図は一次醗酵槽の縦断面立面図、第3図は第2図
の―線に沿う横断平面図、第4図は二次醗酵
槽の一部切欠側面図、第5図はノズルの拡大断面
図である。 1:脱水機、2:嫌気性消化槽、3:温風発生
装置、4:一次醗酵槽、5:混合手段、6:二次
醗酵槽、A:湿潤家畜糞、A1:調湿家畜糞、
A2:乾燥堆肥、A3:調湿混合物、A4:水分調整
堆肥。
FIG. 1 is a schematic diagram showing the process diagram of the present invention, and FIG.
The figure is a vertical cross-sectional elevation view of the primary fermentation tank, Figure 3 is a cross-sectional plan view taken along the - line in Figure 2, Figure 4 is a partially cutaway side view of the secondary fermentation tank, and Figure 5 is an enlarged view of the nozzle. FIG. 1: Dehydrator, 2: Anaerobic digestion tank, 3: Hot air generator, 4: Primary fermentation tank, 5: Mixing means, 6: Secondary fermentation tank, A: Moist livestock manure, A 1 : Humidified livestock manure ,
A 2 : Dry compost, A 3 : Moisture-adjusted mixture, A 4 : Moisture-adjusted compost.

Claims (1)

【特許請求の範囲】 1 処理すべき湿潤家畜糞のほぼ半分量を醗酵し
易い状態に脱水調湿して絞り水汚水と調湿家畜糞
とに分離し、前記絞り水汚水を嫌気性消化槽に導
入し消化処理してメタンガスを発生せしめるとと
もに、同槽内にて消化汚泥を生成し、前記発生し
たメタンガスを燃料として得られた温風を前記調
湿家畜糞に吹込みながら一次醗酵を行わせ、該一
次醗酵にて得られた乾燥堆肥に前記した処理すべ
き湿潤家畜糞の残りほゞ半分量を混合せしめるこ
とにより水分調整を行つて醗酵し易い状態に調湿
して通気しながら二次醗酵を行わせ、該二次醗酵
にて得られた乾燥堆肥に、更に前記嫌気性消化槽
内で生成した消化汚泥を系外に排出させることな
く混合吸収せしめることによつて水分調整堆肥と
することを特徴とする家畜糞の堆肥化方法。 2 処理すべき湿潤家畜糞のほぼ半分量を脱水調
湿するスクリユープレスと、該スクリユープレス
にて分離した絞り水汚水を導入して消化処理する
嫌気性消化槽と、該嫌気性消化槽で発生したメタ
ンガスを燃料として温風を発生する温風発生装置
と、該温風発生装置にて発生した温風を吹込みな
がら前記スクリユープレスにて脱水調湿した調湿
家畜糞を搬入撹拌して一次醗酵せしめる一次醗酵
槽と、該一次醗酵槽にて得られた乾燥堆肥に前記
処理すべき湿潤家畜糞の残りほゞ半分量を混合せ
しめて醗酵し易い状態に調湿する混合手段と、該
混合手段によつて得られた調湿混合物を搬入して
撹拌と通気とによつて二次醗酵せしめる二次醗酵
槽を備え、前記嫌気性消化槽内に生成した消化汚
泥を前記二次醗酵槽内に導入するためのポンプ及
び引抜管を設けたことを特徴とする家畜糞の堆肥
化装置。
[Scope of Claims] 1 Approximately half of the wet livestock manure to be treated is dehydrated and moistened to a state where it can be easily fermented, separated into squeezed wastewater and moistened livestock manure, and the squeezed wastewater is passed through an anaerobic digestion tank. At the same time, digested sludge is generated in the same tank, and primary fermentation is carried out while blowing the warm air obtained using the generated methane gas as fuel into the humidified livestock manure. Then, the remaining half of the wet livestock manure to be treated is mixed with the dry compost obtained in the first fermentation to adjust the moisture content to a state that facilitates fermentation, and the mixture is heated while aerating. By carrying out a second fermentation and mixing and absorbing the digested sludge produced in the anaerobic digestion tank into the dry compost obtained by the second fermentation without discharging it outside the system, it is possible to create moisture-adjusted compost. A method for composting livestock manure, characterized by: 2. A screw press that dehydrates and moistens approximately half of the wet livestock manure to be treated, an anaerobic digestion tank that introduces and digests squeezed water sewage separated by the screw press, and the anaerobic digestion tank. A hot air generator that generates warm air using the methane gas generated by the hot air generator as fuel, and the humidified livestock manure that has been dehydrated and humidified using the screw press while blowing in the warm air generated by the hot air generator and is agitated. a primary fermentation tank for carrying out primary fermentation, and a mixing means for mixing approximately half of the remaining wet livestock manure to be treated with the dry compost obtained in the primary fermentation tank to adjust the humidity to a state that facilitates fermentation. , a secondary fermentation tank is provided in which the humidity-controlled mixture obtained by the mixing means is carried in and subjected to secondary fermentation by stirring and aeration, and the digested sludge produced in the anaerobic digestion tank is fermented in the secondary fermentation tank. A composting device for livestock manure, characterized in that it is equipped with a pump and a pull-out pipe for introduction into a fermentation tank.
JP56186119A 1981-11-21 1981-11-21 Livestock excrement treatment and equipments Granted JPS5888191A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56186119A JPS5888191A (en) 1981-11-21 1981-11-21 Livestock excrement treatment and equipments

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56186119A JPS5888191A (en) 1981-11-21 1981-11-21 Livestock excrement treatment and equipments

Publications (2)

Publication Number Publication Date
JPS5888191A JPS5888191A (en) 1983-05-26
JPS6352000B2 true JPS6352000B2 (en) 1988-10-17

Family

ID=16182688

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56186119A Granted JPS5888191A (en) 1981-11-21 1981-11-21 Livestock excrement treatment and equipments

Country Status (1)

Country Link
JP (1) JPS5888191A (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20020081996A (en) * 2001-04-23 2002-10-30 김종세 Compost Manufacturing Method Utilize Waste Material and Appratus Thereof
KR102072456B1 (en) * 2019-04-05 2020-02-04 정문성 Composition manufacturing apparatus and composition manufacturing method using strain particles
CN110396009B (en) * 2019-08-02 2021-11-30 济南中合环保科技有限公司 Method for producing organic fertilizer by using municipal sludge

Also Published As

Publication number Publication date
JPS5888191A (en) 1983-05-26

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