JPS59162193A - Composting method and composting fermentation cell - Google Patents
Composting method and composting fermentation cellInfo
- Publication number
- JPS59162193A JPS59162193A JP58035454A JP3545483A JPS59162193A JP S59162193 A JPS59162193 A JP S59162193A JP 58035454 A JP58035454 A JP 58035454A JP 3545483 A JP3545483 A JP 3545483A JP S59162193 A JPS59162193 A JP S59162193A
- Authority
- JP
- Japan
- Prior art keywords
- composting
- compost
- fermentation
- fermenter
- bag
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 238000009264 composting Methods 0.000 title claims description 34
- 238000000855 fermentation Methods 0.000 title claims description 26
- 230000004151 fermentation Effects 0.000 title claims description 26
- 238000000034 method Methods 0.000 title claims description 6
- 239000002361 compost Substances 0.000 claims description 40
- 239000002994 raw material Substances 0.000 claims description 29
- 238000005273 aeration Methods 0.000 claims 1
- 238000002474 experimental method Methods 0.000 description 13
- 238000010564 aerobic fermentation Methods 0.000 description 5
- 238000003756 stirring Methods 0.000 description 5
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- NJPPVKZQTLUDBO-UHFFFAOYSA-N novaluron Chemical compound C1=C(Cl)C(OC(F)(F)C(OC(F)(F)F)F)=CC=C1NC(=O)NC(=O)C1=C(F)C=CC=C1F NJPPVKZQTLUDBO-UHFFFAOYSA-N 0.000 description 4
- 229910052760 oxygen Inorganic materials 0.000 description 4
- 239000001301 oxygen Substances 0.000 description 4
- 239000010802 sludge Substances 0.000 description 4
- 241000196324 Embryophyta Species 0.000 description 3
- 238000007599 discharging Methods 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- 238000002156 mixing Methods 0.000 description 3
- 239000012209 synthetic fiber Substances 0.000 description 3
- 229920002994 synthetic fiber Polymers 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 241000218691 Cupressaceae Species 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 230000007797 corrosion Effects 0.000 description 2
- 238000005260 corrosion Methods 0.000 description 2
- 239000005416 organic matter Substances 0.000 description 2
- -1 polyethylene Polymers 0.000 description 2
- 230000001737 promoting effect Effects 0.000 description 2
- 238000009423 ventilation Methods 0.000 description 2
- 241000238631 Hexapoda Species 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- 239000004952 Polyamide Substances 0.000 description 1
- 239000004698 Polyethylene Substances 0.000 description 1
- 239000004743 Polypropylene Substances 0.000 description 1
- ISMSDURUTAMCEA-UHFFFAOYSA-N [N].OP(O)(O)=O Chemical compound [N].OP(O)(O)=O ISMSDURUTAMCEA-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 241001148470 aerobic bacillus Species 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- 230000002238 attenuated effect Effects 0.000 description 1
- 230000037429 base substitution Effects 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 239000004567 concrete Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 239000002440 industrial waste Substances 0.000 description 1
- 230000002401 inhibitory effect Effects 0.000 description 1
- 230000005764 inhibitory process Effects 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 230000007257 malfunction Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 239000010815 organic waste Substances 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 230000008635 plant growth Effects 0.000 description 1
- 239000002574 poison Substances 0.000 description 1
- 229920002647 polyamide Polymers 0.000 description 1
- 229920000728 polyester Polymers 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 230000002829 reductive effect Effects 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 229920003002 synthetic resin Polymers 0.000 description 1
- 239000000057 synthetic resin Substances 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05F—ORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
- C05F17/00—Preparation of fertilisers characterised by biological or biochemical treatment steps, e.g. composting or fermentation
- C05F17/90—Apparatus therefor
- C05F17/907—Small-scale devices without mechanical means for feeding or discharging material, e.g. garden compost bins
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/141—Feedstock
- Y02P20/145—Feedstock the feedstock being materials of biological origin
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/40—Bio-organic fraction processing; Production of fertilisers from the organic fraction of waste or refuse
Landscapes
- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Biochemistry (AREA)
- Biotechnology (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Microbiology (AREA)
- Molecular Biology (AREA)
- Organic Chemistry (AREA)
- 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】
この発明は有機物に空気を供給し発酵せしめ、堆肥化す
る方法および発酵槽、さらに詳くは製紙スラッジ等の産
業廃棄物や下水処理余剰汚泥のような有機質廃棄物を発
酵し堆肥化する方法および発酵槽に関する。DETAILED DESCRIPTION OF THE INVENTION This invention provides a method and a fermenter for fermenting and composting organic matter by supplying air with it, and more specifically, for composting organic waste such as industrial waste such as paper manufacturing sludge and surplus sludge from sewage treatment. The present invention relates to a fermentation and composting method and a fermenter.
従来、堆肥を製造するには、堆肥原料を直接発酵槽内に
投入し、空気を送り込み好気性発酵、を起さしめ、原゛
料の腐朽化を図っていた。このため従来の発酵槽には給
気装置のほか、攪拌装置、および堆肥搬出装置を設ける
必要があった。Conventionally, in order to produce compost, compost raw materials were directly put into a fermentation tank and air was pumped in to cause aerobic fermentation, thereby decomposing the raw materials. For this reason, conventional fermenters needed to be equipped with an agitation device and a compost transport device in addition to an air supply device.
しかし攪拌装置および搬出装置の作動は、堆肥あるいは
原料を団塊または板状に団結せしめ通気性を低下させ、
堆肥化を阻害する原因となる事例が多かった。また、従
来の方法では、製造した堆肥は搬出装置を介し槽外に取
出し、別途包装したり、あるいはバラ積の形で運搬する
必要があり、作業に人手と時間を委し、コストアップの
原因となっている。発酵槽に付帯した攪拌装置、搬出装
置は堆肥原料の発酵腐朽化とともに腐蝕され易く、故障
、損耗が多発し、装置寿命が短い欠点があった。However, the operation of the stirring device and the discharging device causes the compost or raw materials to aggregate into lumps or plates, reducing air permeability.
There were many cases where this was the cause of inhibiting composting. In addition, in conventional methods, the produced compost must be taken out of the tank via a transport device, packaged separately, or transported in bulk, which requires manpower and time, leading to increased costs. It becomes. The stirring device and the discharging device attached to the fermenter are easily corroded as the compost raw material ferments and rots, resulting in frequent breakdowns and wear and tear, and the drawbacks are that the device has a short lifespan.
この発明は上記事情に鑑みなされたものであり、その要
旨は、発酵堆肥化条件に適合する堆肥原料を通気性袋体
で包み、堆肥化発酵槽に入れ、通気を行なって堆肥化を
進めることを特徴とする堆肥化方法である。他の一つの
発明の要旨は、底部に給気装置半毒ジ毒妻、上部に排気
口を有する発酵槽に、堆肥原料が通気性袋体で包み入れ
であることを特徴とする堆肥化発酵槽である。This invention was made in view of the above circumstances, and its gist is to wrap compost raw materials that meet the fermentation and composting conditions in a breathable bag, place them in a composting fermenter, and proceed with composting by aerating the materials. This is a composting method characterized by: Another gist of the invention is a composting fermentation system characterized in that compost raw materials are wrapped in a breathable bag in a fermenter having an air supply device semi-poison at the bottom and an exhaust port at the top. It's a tank.
この方法、および装置では、堆肥原料を適度の大きさの
通気性袋体に包み発酵槽に入れることにより、撹拌する
ことなく好気性発酵が進行し、短期間に堆肥化が完了す
る。攪拌装置や搬出装置の作動による団塊等の発生がな
く通気の障害は起らない。製造された堆肥は袋の才ま発
酵槽外に取出し、堆肥施用現場韮で車積みして運送でき
るため、労力、作業時間の節減になり堆肥コストの低減
化が達成できる。また発酵槽には攪拌装置や搬出装置を
取付ける必要がなく、設備費が節減でき、故障が少ない
ので哲理、経費の負担も低減し、装置寿命が延びる。In this method and device, the compost raw material is wrapped in an appropriately sized air-permeable bag and placed in a fermentation tank, whereby aerobic fermentation proceeds without stirring and composting is completed in a short period of time. No lumps or the like are generated due to the operation of the stirring device or the discharging device, so there is no problem with ventilation. Manufactured compost can be taken out of the fermentation tank in a bag and loaded onto vehicles at the compost application site for transport, saving labor and working time and reducing compost costs. In addition, there is no need to attach a stirring device or a transport device to the fermenter, which reduces equipment costs, reduces malfunctions, reduces costs, and extends the life of the device.
第1,2図は発酵槽の実施態様例を示すものである。発
酵槽は円筒形の本体部1と円錐形のカバー2とからなり
、底部には給気用バイブ3、架台4が配設しである。廿
テ沿≠パ昧ミミづ奥4ミミ本体部1上部周縁には排気
およびドレイン−を導くベルト6が取付けてあり、力六
−2の下周縁にはベルト6に連通ずる排気ロアが開口し
ている。架台4は第4図のごとく、円形の上面に網状多
孔板8を配し通気性を付与してあり、給気用バイブ3の
下面には給気口が穿設しである。Figures 1 and 2 show examples of embodiments of the fermenter. The fermenter consists of a cylindrical main body 1 and a conical cover 2, and an air supply vibe 3 and a pedestal 4 are arranged at the bottom. A belt 6 that guides exhaust and drain is attached to the upper periphery of the main body 1, and an exhaust lower that communicates with the belt 6 is opened at the lower periphery of the power 6-2. ing. As shown in FIG. 4, the pedestal 4 has a circular perforated plate 8 arranged on its upper surface to provide ventilation, and the lower surface of the air supply vibe 3 is provided with an air supply port.
この発酵槽を用い堆肥化を行なうには、堆肥原料9全通
気性の袋体10で包み、発酵槽内の架台4の上に例えば
3つの袋体1oを3層に重ね収納し、給気バイブ5がら
空気を送り込み、好気性発酵を起さしめて堆−胞化を進
める。To perform composting using this fermenter, the compost raw material 9 is wrapped in a completely breathable bag 10, and for example, three bags 1o are stacked and stored in three layers on a pedestal 4 in the fermenter, and air is supplied. Air is sent through the vibrator 5 to cause aerobic fermentation and promote composting.
袋体は、堆肥原料が脱落せす、しかも誦い通気性が保た
れる密度の布帛からなり、発酵槽内で下方から上方に向
い流れる空気がよく通過し、堆肥原料とを気との接触を
妨げないbまた、袋体10はオ・6図のごとく堆肥原料
9を入れた状態で、“例えはフック11で引掛けて懸吊
して搬入、搬出したり、袋体の上端あるいは下端を紐で
締め、上端を開いて原料を投入し、堆肥化後は袋体のま
ま取出し貯蔵所あるいは運搬先で袋体下端の紐を開いて
内部の堆肥を落下させるようにできる。これら条件を満
足する袋体は、・ポリアマイド、ポリエステル、ポリエ
チレン、ポリプロピレン等の合成−繊維を用いたものが
好適であシ、腐蝕して強度低下を起さず長期間の使用に
耐える。The bag body is made of a fabric with a density that allows the compost raw materials to fall out and maintains breathability.The bag body allows the air flowing from the bottom to the top in the fermenter to pass through easily, allowing the compost raw materials to come into contact with air. In addition, when the bag 10 is filled with compost raw material 9 as shown in Fig. It is possible to tighten the bag with a string, open the top end and put the raw materials in, and after composting, take the bag out as it is and open the string at the bottom end of the bag at the storage or transportation destination to allow the compost inside to fall out. Satisfactory bags are preferably made of synthetic fibers such as polyamide, polyester, polyethylene, polypropylene, etc., and can withstand long-term use without corrosion or loss of strength.
なお、堆肥原料9を発酵槽1に搬入する際に、第3図に
示すごとく、袋体10の底部に結び付けたロープ5を頂
部に引出しておく。こうすると原料9を投入した後に、
ローブ5を引いて袋体10内の堆肥原料を容易に平Vこ
ならすことができ発酵時の空気の流通の円滑化が図り得
る。Incidentally, when carrying the compost raw material 9 into the fermentation tank 1, as shown in FIG. 3, the rope 5 tied to the bottom of the bag body 10 is pulled out to the top. In this way, after adding raw material 9,
By pulling the lobes 5, the compost material in the bag 10 can be easily flattened, thereby facilitating air circulation during fermentation.
発酵槽は材料として金属、合成樹脂、コンクリート等か
ら選択できる。しかし、断熱性能全高め、発酵熱を蓄積
して昇温せしめ、短時間に良好な堆肥化を図ることが肝
要であり同時に耐腐蝕性とすることが好−ましい。The material for the fermenter can be selected from metal, synthetic resin, concrete, etc. However, it is important to fully enhance the insulation performance, accumulate fermentation heat and raise the temperature, and achieve good composting in a short time, and at the same time, it is preferable to have corrosion resistance.
袋体は上下方向の寸法が過大となると空気の流ノ出が不
良となって良好な堆肥化が阻害される1、通常上下方向
が21nhJ内であれば発酵堆肥化全促進する上で支障
とはならない。大型発酵槽とする場合には、故体表複数
個横方向に並べて、上下方向に2m以下にするのが好ま
しい。If the vertical dimension of the bag body is too large, air flow will be poor and good composting will be inhibited1. Normally, if the vertical dimension is within 21nhJ, it will be a hindrance to fully promoting fermentation and composting. Must not be. When using a large fermenter, it is preferable that a plurality of dead body surfaces are arranged horizontally and the length is 2 m or less in the vertical direction.
堆肥化原料は炭素のほか、適当量の燐、窒素を含有し、
好気性細菌、および水分が存在する有機質物質である。In addition to carbon, composting raw materials contain appropriate amounts of phosphorus and nitrogen.
Aerobic bacteria and organic matter in which water is present.
これら原料を短期間に充分に熟成された堆肥とするため
には、発酵槽内の最高温度が60°〜80℃に保たれる
よう、空気供給#を調整し発酵させる必要がある。給気
量が多すぎると発酵時の発熱を余剰空気が槽外に持出し
、給気蓋が少なすぎると発酵反応が抑制されて発酵熱の
発生が減少し、檜内温反の降下をもたらし堆肥化の遅延
音もたらす。従って、堆肥化に際しては、発酵槽の排気
ガス中の酸素。In order to turn these raw materials into compost that has matured sufficiently in a short period of time, it is necessary to ferment by adjusting the air supply # so that the maximum temperature in the fermenter is maintained at 60° to 80°C. If the amount of air supply is too large, excess air will carry out the heat generated during fermentation outside the tank, and if the air supply lid is too small, the fermentation reaction will be suppressed and the generation of fermentation heat will be reduced, leading to a drop in the temperature inside the cypress and composting. Delay of sound brings about. Therefore, during composting, oxygen in the exhaust gas of the fermenter.
炭酸ガス量を測定し、極力過剰の酸素を減じ、必要にし
て充分な讃の空気を供給し、檜内金編温に維持するのが
好ましい。このように槽内全高温に保ち、堆肥原料を通
気性袋体に入れて発酵堆肥化を進めるならば、作業能率
が極めて高く、短い発酵期間で充分に熟成した堆肥を製
造することが可+1ヒとなる。It is preferable to measure the amount of carbon dioxide gas, reduce excess oxygen as much as possible, supply sufficient air as necessary, and maintain the temperature at the inside of the cypress. If the entire tank is kept at a high temperature in this way and the compost raw materials are placed in a breathable bag to proceed with fermentation, the work efficiency is extremely high and it is possible to produce fully matured compost in a short fermentation period. It becomes Hi.
実験1(対照例〕
堆肥原料は炭素源と(7てパルプスラッジ、窒素燐酸諒
として水産加工業余剰汚泥、微生物源として返送堆肥を
用い、配合比率はO/N比18、C7P比67を目標と
してlt′i算蓋の原料を秤取混合した。この堆肥原料
11.2図に示した構造の堆肥化発酵lri!(同番(
★100t)中に仕込み、5t/minの流速で通気し
、7日間発酵を継続した。Experiment 1 (Comparative example) The compost raw materials were carbon source (pulp sludge, nitrogen phosphoric acid, surplus sludge from fisheries processing industry, and microbial source was recycled compost. The target blending ratio was O/N ratio 18 and C7P ratio 67. The raw materials for the composting lid were weighed out and mixed.This composting raw material 11.2 Composting and fermenting lri! (same number (
*100t), aerated at a flow rate of 5t/min, and fermentation was continued for 7 days.
発酵期間中、槽内品温ならびに排気ガス酸素製置全自動
分析装置により′lK時記録し、発酵経過を追跡した。During the fermentation period, the temperature of the product in the tank and the temperature of the exhaust gas were recorded using a fully automatic analyzer to monitor the progress of the fermentation.
仕込み後2日目に堆肥品温は60℃を超え、3日目に最
高品温71℃に到達、以降徐々に品温降下を示した。全
期間中、堆肥品温が65℃以上を維持した期間は68時
間であった。酸素吸収量は6日目に最高品温到達よりや
や早くピークに達した後、次オに減少し、6日目以降は
軽度の酸素吸収に変じ、主要の好気発酵反応が減衰した
ことを示した。The compost product temperature exceeded 60°C on the second day after preparation, reached a maximum product temperature of 71°C on the third day, and thereafter showed a gradual decline in material temperature. During the entire period, the period during which the compost product temperature was maintained at 65° C. or higher was 68 hours. The amount of oxygen absorbed reached its peak on the 6th day, a little earlier than the maximum product temperature, and then decreased, and from the 6th day onward, the oxygen absorption changed to a mild level, indicating that the main aerobic fermentation reaction was attenuated. Indicated.
7日目、発酵槽から堆肥を掘り出す際、品温は43℃で
あったが、室温放置後3時間で常温近くまで降温した。On the 7th day, when the compost was dug out from the fermenter, the product temperature was 43°C, but after 3 hours of being left at room temperature, the temperature dropped to near room temperature.
取出した堆肥は全量にカヒが繁殖し、灰黒色を呈する。Kahi grows in all of the compost that is taken out, giving it a grayish-black color.
原料の魚臭は全く消失し、かすか7こ土の臭を帯びる。The fishy odor of the raw material completely disappears, and a faint earthy odor takes over.
虫の発生は全く認められない。堆肥のpHは弱アルカI
J (00の中性を示し、原料混合物の弱酸性と比較し
て明らかに好気発酵に伴う化学変化の跡がうかがえた。No insects were observed at all. The pH of compost is weakly alkaline I.
It showed neutrality of J (00), and compared with the weak acidity of the raw material mixture, traces of chemical changes accompanying aerobic fermentation were clearly seen.
取出し直後の堆肥の塩基置換容量は56m−e・、室温
放w、1ケ月後は93m・0・に到達した。The base substitution capacity of the compost immediately after removal was 56 m·e·, and reached 93 m·0· after one month of being left at room temperature.
この堆肥を用いた植物栽培試験の結果は、明瞭な植物生
育促進効果を示し、堆肥人世施用(土/堆肥= 1/1
(容量比))においても全く障害は認められなかった
。The results of a plant cultivation test using this compost showed a clear plant growth promoting effect, and the compost was applied to humans (soil/compost = 1/1).
(capacity ratio)), no failure was observed at all.
実験2(本発明の実施例)
実験1と同じ、配合比率の原料を用い、これを1個の合
成繊維製の通気性袋体に入れ、前記実験1と同様に、発
酵槽に収め、発酵堆肥化を行なった。゛
発酵経過は第5図に示すように実験1とほとんど同じで
あった。7日目、袋体のまま発酵槽から取出した。袋体
内の堆肥は実験1のものと殆んど同じであシ、無美、無
虫、植物栽培の結果も実験1のものと有意差を示さす、
良質であった。Experiment 2 (Example of the present invention) Using raw materials with the same mixing ratio as in Experiment 1, this was placed in a breathable synthetic fiber bag, placed in a fermenter in the same manner as in Experiment 1, and fermented. Composting was done. ``The fermentation process was almost the same as in Experiment 1, as shown in Figure 5. On the 7th day, the bag was taken out from the fermenter. The compost inside the bag was almost the same as that in Experiment 1, and the results of plant cultivation were also significantly different from those in Experiment 1.
It was of good quality.
実験3(本発明の実施例)
実験1と同じ原料、配合比率の堆肥原料を2個の合成繊
維製の通気性袋体に分納し、発酵槽内に2つの袋体を績
み垂ね収め、実験1,2と同様にして堆肥化を行った。Experiment 3 (Example of the present invention) Compost raw materials with the same raw materials and mixing ratio as in Experiment 1 were divided into two breathable synthetic fiber bags, and the two bags were folded and stored in a fermenter. , Composting was performed in the same manner as in Experiments 1 and 2.
第2図に示す通り、発酵経過は実験1,2と殆んど同じ
であった。発酵終了後、袋体ごと発酵槽から取り出し、
内部の堆肥を評価した四性状、植物栽培の結果は実験1
の結果と同様であった。As shown in Figure 2, the fermentation process was almost the same as in Experiments 1 and 2. After fermentation is complete, remove the bag from the fermenter,
Experiment 1 shows the four properties evaluated for internal compost and the results of plant cultivation.
The results were similar to those of .
上記三個の実験データは第1表の通シであシ、袋体の使
用によシ、発酵堆肥化の阻害は全く認められなかった。The above three experimental data were consistent with those shown in Table 1, and no inhibition of fermentation and composting was observed due to the use of bags.
/ /″ 第1表/ /″ Table 1
第1図、第2図は堆肥化発酵槽の斜視図および縦断面図
、第6図は堆肥原料を入れた袋体を懸吊搬送する状態の
図面、第4図は架台の斜視図、第5図は実験1,2.3
の発酵堆肥化時の経過時間と品温との相関クラ7である
。
1・・発酵槽本体部、2・・カバー、3・・給気用パイ
プ、4・・架台、5・・ロープ、6・・ベルト、7・・
排気口、8・・網状多孔板、9・・堆肥原料、10・・
袋体、11・・フック〇
第1図
第2図
第 3 図 第 41第5図
6−Figures 1 and 2 are a perspective view and a vertical cross-sectional view of the composting fermenter, Figure 6 is a diagram showing a state in which a bag containing compost raw materials is suspended and conveyed, Figure 4 is a perspective view of the pedestal, and Figure 4 is a perspective view of the mount. Figure 5 shows Experiments 1 and 2.3.
This is the correlation between the elapsed time during fermentation and composting and the product temperature. 1. Main body of fermenter, 2. Cover, 3. Air supply pipe, 4. Frame, 5. Rope, 6. Belt, 7.
Exhaust port, 8... Reticular porous plate, 9... Compost raw material, 10...
Bag, 11...Hook〇Figure 1 Figure 2 Figure 3 Figure 41 Figure 5 6-
Claims (2)
袋体で包み堆肥化発酵槽に入れ、通気を行なって堆肥化
を進めることを特徴とする堆肥化方法。(1) A composting method characterized by wrapping compost raw materials that meet fermentation and composting conditions in a breathable bag, placing them in a composting fermentation tank, and proceeding with composting by aeration.
有する発酵槽に、堆肥原料が通気性袋体で包み入れであ
るこ逅を特徴とする堆肥化発酵槽。(2) A composting fermenter characterized by having an air supply device at the bottom and an exhaust port at the top, in which compost raw materials are wrapped in a breathable bag.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58035454A JPS59162193A (en) | 1983-03-04 | 1983-03-04 | Composting method and composting fermentation cell |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58035454A JPS59162193A (en) | 1983-03-04 | 1983-03-04 | Composting method and composting fermentation cell |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPS59162193A true JPS59162193A (en) | 1984-09-13 |
Family
ID=12442246
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP58035454A Pending JPS59162193A (en) | 1983-03-04 | 1983-03-04 | Composting method and composting fermentation cell |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS59162193A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH05727U (en) * | 1991-06-27 | 1993-01-08 | 功 田中 | Composting container structure |
| JPH0569128U (en) * | 1991-05-08 | 1993-09-17 | 明治製菓株式会社 | Breathable compost maker |
| JP2007152383A (en) * | 2005-12-02 | 2007-06-21 | Ishikawa Seiki:Kk | Hand press machine |
| WO2014141804A1 (en) * | 2013-03-14 | 2014-09-18 | 株式会社北誠商事 | Fermentation heat utilization system |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS57123883A (en) * | 1981-01-23 | 1982-08-02 | Cubic Eng Kk | Composting method |
-
1983
- 1983-03-04 JP JP58035454A patent/JPS59162193A/en active Pending
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS57123883A (en) * | 1981-01-23 | 1982-08-02 | Cubic Eng Kk | Composting method |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0569128U (en) * | 1991-05-08 | 1993-09-17 | 明治製菓株式会社 | Breathable compost maker |
| JPH05727U (en) * | 1991-06-27 | 1993-01-08 | 功 田中 | Composting container structure |
| JP2007152383A (en) * | 2005-12-02 | 2007-06-21 | Ishikawa Seiki:Kk | Hand press machine |
| WO2014141804A1 (en) * | 2013-03-14 | 2014-09-18 | 株式会社北誠商事 | Fermentation heat utilization system |
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