JPS5912629B2 - How to purify municipal waste compost - Google Patents
How to purify municipal waste compostInfo
- Publication number
- JPS5912629B2 JPS5912629B2 JP55160364A JP16036480A JPS5912629B2 JP S5912629 B2 JPS5912629 B2 JP S5912629B2 JP 55160364 A JP55160364 A JP 55160364A JP 16036480 A JP16036480 A JP 16036480A JP S5912629 B2 JPS5912629 B2 JP S5912629B2
- Authority
- JP
- Japan
- Prior art keywords
- compost
- materials
- composted
- moisture content
- brittle
- 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
Links
Classifications
-
- 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
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A40/00—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
- Y02A40/10—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
- Y02A40/20—Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses
Landscapes
- Processing Of Solid Wastes (AREA)
- Electrostatic Separation (AREA)
- Fertilizers (AREA)
Description
【発明の詳細な説明】
本発明は、都市こみより堆肥を製造する場合の精製方法
に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a purification method for producing compost from municipal waste.
都市どみを好気性発酵せしめて堆肥化する場合、都市こ
み中に含まれる軟質プラスチック類、金属、布などの非
堆肥化物は部分別や磁力選別、風力分別などによっであ
る程度分別し得るが、ガラス・陶磁器・硬質プラスチッ
クなどの脆性な非堆肥化物は一般に粒径が小さく、特に
前処理として破砕を行う場合にはその過程で細粒化され
て堆肥化物との分別が困難である。When municipal waste is composted through aerobic fermentation, non-compostable materials such as soft plastics, metals, and cloth contained in the municipal waste can be separated to some extent by sorting, magnetic sorting, wind sorting, etc. Brittle non-compostable materials such as glass, ceramics, and hard plastics generally have small particle sizes, and especially when they are crushed as a pretreatment, they become finer in the process and are difficult to separate from compostable materials.
従来これらの脆性な非堆肥化物を除去するために、堆肥
化物と異物との弾性の差を利用した反発式分別法や、比
重差を利用した風力分別法などが種々試みられていたが
、これら異物の粒径が大きい場合には比較的よい結果が
得られても、粒径が小さい場合には実質的に分別、f)
3不可能であった。In the past, various attempts have been made to remove these brittle non-composted materials, such as a repulsion type separation method that takes advantage of the difference in elasticity between composted materials and foreign materials, and an air separation method that uses the difference in specific gravity. Even if relatively good results are obtained when the particle size of the foreign material is large, when the particle size is small, it is substantially separated, f)
3 It was impossible.
而して、これ等の異物即ちガラス・陶磁器・硬質プラス
チックなどの脆性な非堆肥化物は、自然分解しないので
土壌に蓄積するのみならす、農耕作業上危険であるので
実質的な完全除去が必要であり、換言すれはこれ等の異
物除去は都市こみ堆肥を実用に供し得る為の必須条件と
して極めて重要である。However, these foreign substances, such as brittle non-compostable materials such as glass, ceramics, and hard plastics, do not decompose naturally, so they only accumulate in the soil, and are dangerous to agricultural operations, so they must be virtually completely removed. In other words, the removal of these foreign substances is extremely important as an essential condition for putting urban compost into practical use.
上記に鑑み、本発明は、静電分別を行なうことにより、
在来困難であった比較的粒径の小さいガラス・陶磁器・
硬質プラスチックなどの脆性非堆肥化物をも精度よく分
別し得て精製を容易、確実となし、都市どみの堆肥化を
実用可能ならしめることを目的とするものである。In view of the above, the present invention provides, by performing electrostatic separation,
Glass, ceramics, and ceramics with relatively small particle sizes, which were previously difficult to manufacture.
The purpose is to make it possible to accurately separate brittle non-compostable materials such as hard plastics, to easily and reliably purify them, and to make composting in urban areas practical.
本発明は、都市どみを発酵させて堆肥化する都市こみ堆
肥の精製方法において、堆肥化発酵工程の前若しくは後
の少なくとも一刀の時点において、少なくとも軟質プラ
スチック類・金属・布などの非脆性堆肥化物を除去して
堆肥化物とガラス・陶磁器・硬質プラスチックなどの脆
性非堆肥化物との混合物を得、該混合物の含水率が50
係以下5%以上の範囲において、15wl1以下5M以
上の網目のスクリーンによって篩分し、その後静電分別
工程によって堆肥化物と脆性非堆肥化物とに分別し堆肥
化物のみを堆肥としてとり出すことを特徴とする都市こ
み堆肥の精製方法である。The present invention provides a method for refining municipal waste compost in which urban waste is fermented and composted, in which at least non-brittle compost such as soft plastics, metals, cloth, etc. The compound is removed to obtain a mixture of composted material and brittle non-composted material such as glass, ceramics, hard plastic, etc., and the moisture content of the mixture is 50.
In the range of 5% or more, the compost is sieved through a screen with a mesh size of 15 wl1 or less and 5 M or more, and then separated into compostable materials and brittle non-compostable materials by an electrostatic separation process, and only the composted materials are taken out as compost. This is a method for refining municipal waste compost.
本発明は、発明者等の行なった研究・実験に基づいて得
られた下記の諸知見に着目して為されたものである。The present invention was made by focusing on the following findings obtained based on research and experiments conducted by the inventors.
(1)都市こみ堆肥の平均含水率は一般に約40%〜5
0%程度であるが、このうち堆肥化物は含水率が高く、
−カガラス・陶磁器・硬質プラスチックなどの脆性異物
は吸湿しない為に両者の間に著しい電気抵抗の差がある
。(1) The average moisture content of municipal waste compost is generally about 40% to 5.
The moisture content is around 0%, but composted material has a high moisture content.
-Brittle foreign materials such as glass, ceramics, and hard plastics do not absorb moisture, so there is a significant difference in electrical resistance between them.
発明者等の測定によれば、第1図に示すように少なく共
平均含水率50%以下数係以上の範囲に於ては、ガラス
・陶磁器・硬質プラスチックなどの脆性異物の電気抵抗
値の下限は、堆肥化物の電気抵抗値の上限よりも高いこ
とが判明した。According to the inventors' measurements, as shown in Figure 1, in the range where the co-average water content is less than 50% or more, the lower limit of the electrical resistance value of brittle foreign materials such as glass, ceramics, hard plastics, etc. was found to be higher than the upper limit of the electrical resistance value of the composted material.
その結果、電気抵抗の異なる二種類の物質を帯電せしめ
て高圧静電界の作用により両者を分別する公知の静電分
別法が、多種の物質からなる堆肥に対しても堆肥化物と
脆性異物群との分別に於て高い精度で可能となることが
予見された。As a result, the well-known electrostatic separation method, in which two types of substances with different electrical resistances are charged and separated by the action of a high-voltage electrostatic field, has been found to be able to separate composted materials and brittle foreign matter even for compost made of a variety of materials. It was predicted that this would be possible with high precision in the separation of
(2)都市こみを予め破砕篩分して軟質プラスチック類
・金属・布・木などの非堆肥化物を除去し、厩芥と紙な
どの堆肥化にガラス・陶磁器・硬質プラスチックなどの
脆性異物の混入した原料を好気性発酵により堆肥化した
後、更に5wl1網目の篩にかけた篩下群に含水率を種
々調整し乍ら、第2図に示す静電分別装置によって試験
を行った。(2) Municipal waste is crushed and sieved in advance to remove non-compostable materials such as soft plastics, metals, cloth, and wood, and brittle foreign materials such as glass, ceramics, and hard plastics are composted from garbage and paper. After the mixed raw materials were composted by aerobic fermentation, they were further sieved through a 5 wl 1 mesh sieve, and the moisture content was variously adjusted, and a test was conducted using the electrostatic separator shown in FIG. 2.
図中8は原料、9は振動板、10は高電圧極、11は接
地極、12は仕切り、13は堆肥化物、14は脆性異物
である非堆肥化物である。In the figure, 8 is a raw material, 9 is a diaphragm, 10 is a high voltage electrode, 11 is a ground electrode, 12 is a partition, 13 is a composted material, and 14 is a non-composted material that is a brittle foreign material.
その結果、完全乾燥(含水率0)の条件では堆肥化物と
脆性異物群との分別は不可能であったが、少なく共平均
含水率50係以下数係以上の範囲に於ては、はぼ100
%純度の堆肥化物を分別することが可能なことが判明し
た。As a result, although it was impossible to separate the composted material from the brittle foreign matter group under conditions of complete dryness (moisture content 0), it was not possible to separate the composted material from the brittle foreign material group under conditions of complete dryness (moisture content 0). 100
It has been found that it is possible to separate the composted material with % purity.
印力ρ電圧3に■の場合の、平均含水率と堆肥化物(は
ぼ100%純度)の収率との関係を第3図に示す。FIG. 3 shows the relationship between the average moisture content and the yield of composted material (100% purity) when the applied ρ voltage is 3 and ■.
平均含水率が50%を越すと、異物に堆肥化物が付着し
易くなる為と、堆肥化物の見掛比重が増大する為などの
理由で、仕切り位置を適宜修正しても堆肥化物の収率は
著しく低下する。When the average moisture content exceeds 50%, the composted material tends to adhere to foreign matter and the apparent specific gravity of the composted material increases, so even if the partition position is adjusted appropriately, the yield of the composted material will decrease. decreases significantly.
静電分別に最適な平均含水率は概ね35係から5%の範
囲であるが、含水率を10%未満に調整することは工業
的に困難な場合も多いので、実施に当っては35%以下
10%以上に調整することが好ましい。The optimal average moisture content for electrostatic separation is generally in the range of 35% to 5%, but it is often industrially difficult to adjust the moisture content to less than 10%, so in practice it is recommended to use 35%. It is preferable to adjust the amount below to 10% or more.
而して、堆肥の取扱い性・輸送・商品価値などの点で含
水率は一般に40係以下が好ましく、この条件は不法の
実施に轟って望まれる含水率の条件とも一致する。In terms of handling, transportation, commercial value, etc. of compost, it is generally preferable that the moisture content is 40 or less, and this condition also coincides with the moisture content that is highly desired in illegal practices.
尚、平均含水率が高い場合(50係付近)の堆肥化物の
収率は、印加電圧を上げること及び粒径を小さくするこ
とによって、第3図に示す結果よりも改善される傾向と
なる。Note that the yield of composted material when the average moisture content is high (around 50 parts) tends to be improved more than the results shown in FIG. 3 by increasing the applied voltage and decreasing the particle size.
(3)説明を単純化する為、一様な水平静電界(電圧E
)中で、空気抵抗を無視し堆肥化物(導電性物質)の挙
動を考察するに、堆肥化物の比重をγとし、粒径dなる
球体とすると、水平力向の電気力J1はf1’oc d
2・Ee垂垂直南向重力f2はf2d3■・rである
から、第4図に示すような合力Fが垂直力向に対して為
す角θはθ■1E2
t、an −となる。(3) To simplify the explanation, a uniform horizontal electrostatic field (voltage E
), ignoring air resistance and considering the behavior of the composted material (conductive material).If the specific gravity of the composted material is γ and the particle size is d, then the electric force J1 in the horizontal force direction is f1'oc d
2.Ee Since the vertical southward gravity f2 is f2d3.multidot.r, the angle .theta. that the resultant force F makes with respect to the vertical force direction as shown in FIG.
分別精度を上げる為には可dγ
友釣にθを大きくすること、即ち電圧Eを太きくし粒径
dと比重γを小さくすることが好ましいが、電圧は実用
上一般に40〜50KV以下に限定され、比重γは含水
率によって規定される。In order to improve the separation accuracy, it is preferable to increase θ to a greater extent than dγ, that is, to increase the voltage E and decrease the particle diameter d and specific gravity γ, but for practical purposes, the voltage is generally limited to 40 to 50 KV or less. The specific gravity γ is defined by the water content.
従って粒径を可及的に小さくすることが寧ろ好ましいの
であって、この点が細2粒化され易い脆性異物の分別を
目的とする不法が、従来の反発式や風力式に比して甚だ
有利となる理由の−っでもある。Therefore, it is preferable to reduce the particle size as much as possible, and in this respect, illegal activities aimed at separating brittle foreign substances that are easily divided into fine particles are much more difficult than with conventional repulsion methods or wind power methods. There are also reasons why it is advantageous.
−力、堆肥化速度を速める為には一般に堆肥化物の粒径
は小さい方が好ましく且つ又、極度に小さい粒径では篩
の目づまりや動力消費の点及びエアレーションの点など
で不利トなる。- In order to increase the power and composting speed, it is generally preferable for the particle size of the compost to be small, and extremely small particle sizes are disadvantageous in terms of sieve clogging, power consumption, aeration, etc.
以上の静電分別精度および堆肥化条件の両条件を勘案す
ると篩の網目は15M以下5顛以上とすることが望まし
い。Considering both the electrostatic separation accuracy and composting conditions described above, it is desirable that the mesh size of the sieve is 15M or less and 5 or more meshes.
以上述べたところによって、本発明の方法が在来困難で
あった堆肥中の脆性異物を精度高く分別し得るのみなら
ず、不法を適用するに当っての含水率や粒径の最適調整
条件が堆肥化の操作条件や商品価値を高める条件ともよ
くマツチすることが基本的に明らかにされた。As described above, the method of the present invention not only enables highly accurate separation of brittle foreign substances in compost, which was previously difficult, but also provides optimal adjustment conditions for moisture content and particle size when applying illegal methods. It has basically been clarified that the conditions match well with the operating conditions for composting and the conditions for increasing commercial value.
本発明を、実施例につき図面を用いて説明すれば、都市
こみは先づ一次破砕・篩分機1によって、軟質プラスチ
ック類・金属・布・木などの非堆肥化物A群と、厩芥、
紙などの堆肥化物Bとガラス・陶磁器・硬質プラスチッ
クなどの異物(脆性非堆肥化物)C群との混合物(B+
C)群とに分別する。To explain the present invention with reference to the drawings in accordance with an embodiment, municipal waste is first crushed and sieved into non-compostable materials A group such as soft plastics, metals, cloth, wood, etc., as well as stable waste,
A mixture of compostable materials B such as paper and foreign materials (brittle non-compostable materials) group C such as glass, ceramics, and hard plastics (B+
C) Separate into groups.
此の際篩分の網目は30M前後が望ましい。尚必要があ
れば紙は相当部分をA群に移行せしめることもできる。In this case, the mesh size of the sieve is preferably around 30M. If necessary, a considerable portion of the paper can be transferred to Group A.
次いで(B+C)群を発酵槽2によって好気性発酵せし
め平均含水率を50%以下(好ましくは35%以下)に
調整した後、15原以下5朧以上の網目を有する二次破
砕・篩分機3によって残存する非堆肥化物A′群を除去
すると共に(B+C)群の粒径を整える。Next, the (B+C) group is subjected to aerobic fermentation in a fermenter 2 to adjust the average moisture content to 50% or less (preferably 35% or less), and then subjected to a secondary crushing/sieving machine 3 having a mesh size of 15 pores or less and 5 haze or more. The remaining non-composted materials A' group are removed by this process, and the particle size of the (B+C) group is adjusted.
一次破砕・篩分機1及び二次破砕・篩分機3の破砕・篩
分機としては破砕機と篩分機とを直結することによって
機能し得るが、第7図に示すよ−うな公知の選択破砕分
別機を用いるとよい。Although the crushing and sieving machines of the primary crushing and sieving machine 1 and the secondary crushing and sieving machine 3 can function by directly connecting the crushing machine and the sieving machine, known selective crushing and sorting as shown in FIG. It is better to use a machine.
これは駆動装置17によって回転する円筒スクリーン1
5とこの中で駆動装置18によって円筒と異なる速度で
回転する掻板16とを備え、原料を軸方向に送って破砕
と篩分とを繰り返して一体的に行う方式であって、本機
により(B+C)群とA群とは容易に粗選される。This is a cylindrical screen 1 rotated by a drive device 17.
5 and a scraping plate 16 which is rotated by a drive device 18 at a speed different from that of the cylinder, and the raw material is sent in the axial direction to repeat crushing and sieving in an integrated manner. The (B+C) group and the A group are easily selected.
尚、一次破砕・篩分機と発酵槽2の工程の間で、(B+
C)群中に若干混入してくる金属(導電性非堆肥化物)
の小片は、磁力選別機及び反発式分別機など(倒れも図
示せず)によって除去すると良い。In addition, between the process of primary crushing/sieving machine and fermenter 2, (B+
C) Some metals mixed into the group (conductive non-composted material)
The small pieces may be removed using a magnetic separator, a repulsion type separator, etc. (falling is also not shown).
二次破砕・篩分機3を通過した(B+C)群は含水率及
び粒径共に静電分別が可能な範囲に調整されているので
、静電分別機4によってほぼ完全に脆性非堆肥化物C群
を除去して、純度の極めて高い堆肥化物Bを分別するこ
とができる。The moisture content and particle size of the (B+C) group that has passed through the secondary crushing/sieving machine 3 have been adjusted to a range that allows electrostatic separation, so the electrostatic separator 4 almost completely removes the brittle non-compostable C group. can be removed to separate compost B with extremely high purity.
尚、静電分別機4は第8図に示すようにコロナ電界と静
電界とを併有する公知の複合型円筒式を用いてよい。As shown in FIG. 8, the electrostatic separator 4 may be a known composite cylindrical type having both a corona electric field and an electrostatic field.
即ち、コンベア19を経て接地回転円筒20に落下した
( B+C)群はコロナ電界を通過したのち、さらに静
電界を通って、導電性の堆肥化物Bと絶縁性の脆性非堆
肥化物C群とに図のように夫々分別される。That is, the (B+C) group that has fallen into the grounded rotating cylinder 20 via the conveyor 19 passes through a corona electric field and then further passes through an electrostatic field to become conductive composted material B and insulating brittle non-composted material C group. They are separated as shown in the figure.
21はブラシ、22はコロナ放電極、23は堆肥化物ホ
ッパ、24は異物ホッパである。21 is a brush, 22 is a corona discharge electrode, 23 is a compost hopper, and 24 is a foreign matter hopper.
静電分別機4としては上記の複合型円筒式のほか、純静
電型円筒式、コロナ放電型円筒式、水平電界中を落下せ
しめる方式、摩擦帯電式など、公知の方式を用いること
ができる。As the electrostatic separator 4, in addition to the above-mentioned composite cylindrical type, known methods such as a pure electrostatic cylindrical type, a corona discharge type cylindrical type, a method of dropping in a horizontal electric field, a frictional charging type, etc. can be used. .
第6図は本発明の他の実施例を示すもので、此の例では
堆肥化物Bの収率を高めることが意図されている。FIG. 6 shows another embodiment of the invention, in which it is intended to increase the yield of compost B.
第3図に示すように、実験結果によると静電分別に於け
る抽肥化物の収率は、平均含水率が10%〜15係程度
に於て最高となる。As shown in FIG. 3, according to the experimental results, the yield of extracted material in electrostatic separation is highest when the average moisture content is about 10% to 15%.
一方段市どみ原料の含水率にも依るが、一次発酵槽を出
た堆肥の平均含水率は一般に40%〜50係程度であり
、其の後屋内で10日間位養生堆積しても含水率は30
%〜35%位にしか低下しない。On the other hand, although it depends on the moisture content of the raw materials left for fermentation, the average moisture content of the compost leaving the primary fermentation tank is generally around 40% to 50%, and even if it is left to cure indoors for about 10 days, it still retains moisture. The rate is 30
It only decreases to around 35%.
従ってこれを工業的に10%〜15%迄に引き下げよう
とすると加熱乾燥が必要となる。Therefore, if this is to be reduced industrially to 10% to 15%, heat drying is required.
本実施例は、このために加熱乾燥を行ない、収率を高め
ると同時に、この熱により混入スラッジの脱水にも有効
利用をはからんとするものである。In this embodiment, heat drying is carried out for this purpose to increase the yield, and at the same time, the heat is effectively used to dehydrate the mixed sludge.
即ち本実施例に於ては、畜産廃棄物(電蓄ふん尿)や下
水スラッジなどの含水率の高い有機スラッジを堆肥化し
ようとする場合、70係以上の含水率では好気性発酵が
困難であり前処理として若干の脱水を要すること、及び
これ等の有機スラッジには問題となる異物が含まれてお
らず分別の必要がないことに着目し、前記加熱乾燥後精
製された堆肥化物Bとこの有機スラッジとを混合して含
水率を調整[2て再発酵せしめるものである。That is, in this example, when attempting to compost organic sludge with a high moisture content such as livestock waste (electrified manure) or sewage sludge, aerobic fermentation is difficult at a moisture content of 70 parts or more. Focusing on the fact that some dehydration is required as a pretreatment and that these organic sludges do not contain problematic foreign substances and do not need to be separated, the composted material B purified after heating and drying and this The moisture content is adjusted by mixing with organic sludge [2] and re-fermented.
此のような方法を採用することによって、都市こみ堆肥
化物Bの収率を高める為の、加熱乾燥に用いたエネルギ
は、高含水率の有機スラッジの脱水に有効に利用される
ことになり合理的となる。By adopting such a method, the energy used for heating and drying to increase the yield of composted municipal waste B can be effectively used for dewatering organic sludge with a high moisture content, which is rational. become a target.
第6図によって説明すると、第5図の実施例と同様に都
市こみは一次破砕・篩分機1、発酵槽2、二次破砕・篩
分機3を経て(B+C)群を選別した後、水分調整槽5
によって含水率を低下せしめてから静電分別機4にかけ
る。To explain with reference to Fig. 6, as in the embodiment shown in Fig. 5, municipal solid waste passes through a primary crusher/sieve machine 1, a fermenter 2, a secondary crusher/sieve machine 3, and is sorted into groups (B+C), and then water content is adjusted. Tank 5
After lowering the moisture content, it is applied to the electrostatic separator 4.
水分調整槽5は長期間の屋内養生堆積法若しくは加熱乾
燥法倒れでもよく、設備費、運転費、堆肥化物Bの収率
などを勘案して定める。The moisture adjustment tank 5 may be formed by a long-term indoor curing deposition method or a heat drying method, and is determined by taking into consideration equipment costs, operating costs, yield of compost B, etc.
静電分別機4によって精製された堆肥化物Bは更に混合
槽6に於て前記高含水率の有機スラッジ(異物を含まな
い)と混合して含水率を70係以下に調整し、再発酵槽
Iに於て再発酵せしめて良質の堆肥を得る。The compost B purified by the electrostatic separator 4 is further mixed with the high water content organic sludge (contains no foreign matter) in a mixing tank 6 to adjust the water content to 70% or less, and then transferred to a re-fermenter. Ferment it again in I to obtain high quality compost.
本発明により、従来は極めて困難とされていた、ガラス
、・陶磁器、硬質プラスチックなどの脆性非堆肥化物を
堆肥化物から除く分別を、たとえ脆性非堆肥化物が粒径
が小なる場合であっても可能となし、精度よく分別して
精製を容易にかつ確実となし、都市こみ堆肥を実用可能
とする都市こみ堆肥の精製方法を提供することができ、
実用上廃棄物処理及びその有効利用上、公害防止上極め
て犬なる効果を有するものである。The present invention makes it possible to remove brittle non-compostable materials such as glass, ceramics, and hard plastics from compost, which has been considered extremely difficult in the past, even when the particle size of the brittle non-compostable materials is small. It is possible to provide a method for refining municipal waste compost that makes it possible, accurately separates it, and purifies it easily and reliably, making it practical.
In terms of practical waste treatment, its effective use, and pollution prevention, it has extremely effective effects.
図面は本発明の実施例に関するものであり、第1図は実
験結果を示すグラフ、第2図は実験装置の説明図、第3
図は実験結果を示すグラフ、第4図は作動説明図、第5
図、第6図は異なる実施例のフローシート、第7図は破
砕・篩分機の説明図、第8図は静電分別機の説明図であ
る。
1・・・・・・一次破砕・篩分機、2・・・・・・発酵
槽、3・・・・・・二次破砕・篩分機、4・・・・・・
静電分別機、5・・・・・・水分調整槽、6・・・・・
・混合槽、7・・・・・・再発酵槽、8・・・・・・原
料、9・・・・・・振動板、10・・・・・・高電圧極
、11・・・・・・接地極、12・・・・・・仕切り、
13・・・・・・堆肥化物、14・・・・・・非准肥化
物、15・・・・・・円筒スクリーン、16・−・・・
・掻板、17.18・・・・・・駆動装置、19・・・
・・・コンベア、20・・・・・・接地回転円筒、21
・・・・・・ブラシ、22・・・・・・コロナ放電極、
23・・・・・・堆肥化物ホッパ、24・・・・・・異
物ホッパ。
145−The drawings relate to embodiments of the present invention, and Fig. 1 is a graph showing experimental results, Fig. 2 is an explanatory diagram of the experimental apparatus, and Fig. 3 is a graph showing experimental results.
The figure is a graph showing the experimental results, Figure 4 is an explanation diagram of the operation, and Figure 5 is a graph showing the experimental results.
6 is a flow sheet of a different embodiment, FIG. 7 is an explanatory diagram of a crushing/sieving machine, and FIG. 8 is an explanatory diagram of an electrostatic separator. 1...Primary crushing/sieving machine, 2...Fermentation tank, 3...Secondary crushing/sieving machine, 4...
Electrostatic separator, 5...Moisture adjustment tank, 6...
・Mixing tank, 7... Re-fermenting tank, 8... Raw material, 9... Vibration plate, 10... High voltage pole, 11... ...Grounding electrode, 12...Partition,
13... Composted material, 14... Non-composted material, 15... Cylindrical screen, 16...
- Scraping board, 17.18... Drive device, 19...
... Conveyor, 20 ... Ground rotating cylinder, 21
...Brush, 22...Corona discharge electrode,
23... Composted material hopper, 24... Foreign material hopper. 145-
Claims (1)
製方法において、堆肥化発酵工程の前若しくは後の少な
くとも磁力の時点において、少なくとも軟質プラスチッ
ク類・金属・布などの非脆性非堆肥化物を除去して堆肥
化物とガラス・陶磁器硬質プラスチックなどの脆性非堆
肥化物との混合物を得、該混合物の含水率が50係以下
5係以上の範囲において、15履以下58以上の網目の
スクリーンによって篩分し、その後静電分別工程によっ
て堆肥化物と脆性非堆肥化物とに分別し堆肥化物のみを
堆肥としてとり出すことを特徴とする都市こみ堆肥の精
製方法。1. In a method for refining urban waste compost by fermenting and composting urban waste, at least at the time of magnetic application before or after the composting fermentation process, at least non-brittle non-compostable materials such as soft plastics, metals and cloth are removed. A mixture of composted materials and brittle non-composted materials such as glass and ceramic hard plastics is obtained, and when the moisture content of the mixture is in the range of 50 parts or less and 5 parts or more, the mixture is sieved through a screen with a mesh size of 15 parts to 58 parts. A method for refining municipal waste compost, which comprises separating the compost into compostable materials and brittle non-compostable materials using an electrostatic separation process, and extracting only the compostable materials as compost.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP55160364A JPS5912629B2 (en) | 1980-11-14 | 1980-11-14 | How to purify municipal waste compost |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP55160364A JPS5912629B2 (en) | 1980-11-14 | 1980-11-14 | How to purify municipal waste compost |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5696795A JPS5696795A (en) | 1981-08-05 |
| JPS5912629B2 true JPS5912629B2 (en) | 1984-03-24 |
Family
ID=15713370
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP55160364A Expired JPS5912629B2 (en) | 1980-11-14 | 1980-11-14 | How to purify municipal waste compost |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5912629B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0395230U (en) * | 1990-01-22 | 1991-09-27 |
-
1980
- 1980-11-14 JP JP55160364A patent/JPS5912629B2/en not_active Expired
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0395230U (en) * | 1990-01-22 | 1991-09-27 |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5696795A (en) | 1981-08-05 |
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