JPS6311317B2 - - Google Patents
Info
- Publication number
- JPS6311317B2 JPS6311317B2 JP56024083A JP2408381A JPS6311317B2 JP S6311317 B2 JPS6311317 B2 JP S6311317B2 JP 56024083 A JP56024083 A JP 56024083A JP 2408381 A JP2408381 A JP 2408381A JP S6311317 B2 JPS6311317 B2 JP S6311317B2
- Authority
- JP
- Japan
- Prior art keywords
- raw material
- path
- liquid
- processing chamber
- belt conveyor
- 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
- 239000002994 raw material Substances 0.000 claims description 24
- 239000007788 liquid Substances 0.000 claims description 21
- 239000002361 compost Substances 0.000 claims description 6
- 230000007246 mechanism Effects 0.000 claims description 5
- 238000011084 recovery Methods 0.000 claims description 5
- 238000004519 manufacturing process Methods 0.000 claims description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 4
- 229910052760 oxygen Inorganic materials 0.000 description 4
- 239000001301 oxygen Substances 0.000 description 4
- 238000003756 stirring Methods 0.000 description 4
- 239000006185 dispersion Substances 0.000 description 3
- 210000003608 fece Anatomy 0.000 description 3
- 239000010871 livestock manure Substances 0.000 description 3
- 239000010815 organic waste Substances 0.000 description 3
- 210000002700 urine Anatomy 0.000 description 3
- 238000009264 composting Methods 0.000 description 2
- 230000008020 evaporation Effects 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 238000000855 fermentation Methods 0.000 description 2
- 230000004151 fermentation Effects 0.000 description 2
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000003517 fume Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 230000007723 transport mechanism Effects 0.000 description 1
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
- Fertilizers (AREA)
Description
【発明の詳細な説明】
本発明は有機廃棄物、主として生糞等の畜糞を
原料とした堆肥製造装置に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an apparatus for producing compost using organic waste, mainly animal manure such as raw manure, as a raw material.
周知される様に、此種有機廃棄物を堆肥化する
には、水分調整が重要な課題であり、従来におい
てはこの調整にオガ屑を混入使用していた。 As is well known, moisture adjustment is an important issue in composting this type of organic waste, and in the past, sawdust was mixed in for this adjustment.
しかしながら、この様な手段においては、近年
にみられるオガ屑の入手難による処理原価の高騰
やオガ屑の発酵分解速度が糞尿に比して長い事に
起因する処理能率の低下が問題となる。 However, with such means, there are problems such as an increase in processing costs due to the recent difficulty in obtaining sawdust, and a decrease in processing efficiency due to the fact that the rate of fermentation and decomposition of sawdust is longer than that of manure.
本発明はこの様な問題を解決し得る堆肥製造装
置を提供せんとするものである。 The present invention aims to provide a compost manufacturing apparatus that can solve these problems.
以下に本発明装置を添付図面につき説明する。 The apparatus of the present invention will be explained below with reference to the accompanying drawings.
第1図において、1は水平方向に長い外装体
で、内部には搬送機構2と、液分回収手段として
の溝路3及び原料撹拌手段としての切返部4を内
蔵している。 In FIG. 1, reference numeral 1 denotes a horizontally long exterior body, which houses therein a transport mechanism 2, a groove 3 as a liquid collection means, and a cut section 4 as a raw material stirring means.
更に上記外装体1内には、所望により蒸発水分
回収樋5や有機廃液散布手段としての散布管系6
が設けられており、上記回収樋5は図示しない外
部排水路に連通し、又上記散布管系6は溝路3に
回収された液分を搬送原料に散布する様構成され
ている。 Furthermore, inside the exterior body 1, there may be provided an evaporated water recovery gutter 5 and a dispersion pipe system 6 as a means for dispersing organic waste liquid, if desired.
The collection gutter 5 communicates with an external drainage channel (not shown), and the dispersion pipe system 6 is configured to spray the liquid collected in the channel 3 onto the raw material to be transported.
上記外装体1は、例へば所定長さのトンネル状
外装ユニツト11を順次連結する等して地上に長
く形設されており、その屋根部分12は全部又は
1部が透光面13に形成されている。 The exterior body 1 is formed long above the ground by, for example, sequentially connecting tunnel-shaped exterior units 11 of a predetermined length, and its roof portion 12 is formed in whole or in part as a transparent surface 13. There is.
上記屋根部分12は実施例の如く凸曲面である
事が望ましく、かくすれば、第2図に示す如く、
蒸発水分回収樋5を屋根部分12の内面両側部に
設けて、屋根部分12の内面で結露した水滴を屋
根部分の内面に沿つて回収樋5内に滴下せしめる
事が出来る。 It is desirable that the roof portion 12 has a convex curved surface as in the embodiment, and if so, as shown in FIG.
The evaporated water recovery gutter 5 is provided on both sides of the inner surface of the roof part 12, and water droplets condensed on the inner surface of the roof part 12 can be made to drip into the recovery gutter 5 along the inner surface of the roof part.
上記透光面13は内部の原料7を太陽熱によつ
て加熱し、これにより原料7の水分を蒸発せしめ
るため設けられる。 The transparent surface 13 is provided to heat the raw material 7 inside by solar heat and thereby evaporate the moisture in the raw material 7.
従つて、夏期と冬期では、原料7の含水率に相
当な開きが生じる事を避けられないから、例へば
透光面13に図示しない遮光蓋を設けて、透光面
13の面積を増減し得る様に構成する事が望まし
い。 Therefore, it is unavoidable that the moisture content of the raw material 7 varies considerably between summer and winter, so for example, a light-shielding lid (not shown) may be provided on the light-transmitting surface 13 to increase or decrease the area of the light-transmitting surface 13. It is desirable to configure it in the same way.
特に外装体1の長さが10mを超える様な大型装
置の場合には、原料搬送速度との関係もあるが、
外装体1の屋根部分12に部分的な非透光面を設
ける事が望ましい。 Particularly in the case of large equipment where the length of the exterior body 1 exceeds 10 m, there is also a relationship with the raw material conveyance speed.
It is desirable to provide the roof portion 12 of the exterior body 1 with a partial non-light-transmitting surface.
上記外装体1の内部には細長いトンネル状処理
室14が形成されており、この処理室14の1端
に原料の投入部15が設けられると共に他端には
排出部16が設けられている。 An elongated tunnel-shaped processing chamber 14 is formed inside the exterior body 1, and a raw material input section 15 is provided at one end of the processing chamber 14, and a discharge section 16 is provided at the other end.
上記処理室14内には投入部15から投入され
た原料7を排出部16迄搬送する搬送機構2が内
設されており、この搬送機構2の全部又は1部は
脱液路21に構成されている。 A conveyance mechanism 2 for conveying the raw material 7 inputted from the input section 15 to the discharge section 16 is installed inside the processing chamber 14, and all or a part of this conveyance mechanism 2 is configured as a deliquification path 21. ing.
上記脱液路21は1対のベルトコンベヤ22,
23を搬送方向に沿つて平行状に装架すると共に
此等ベルトコンベヤ22,23の接近側を他方側
より低くして、両コンベヤ22,23が断面V状
の路面を形成する様構成してある。 The liquid removal path 21 includes a pair of belt conveyors 22,
23 are mounted in parallel along the conveyance direction, and the approach side of the belt conveyors 22 and 23 is lower than the other side, so that both conveyors 22 and 23 form a road surface with a V-shaped cross section. be.
この脱液路21は、通常透光面13と上下対向
する様形設されるが、必ずしもこの様に限定する
必要はない。 The liquid removal path 21 is usually formed to vertically face the light-transmitting surface 13, but it is not necessarily limited to this.
このV状脱液路21の底部には液分回収手段と
しての溝路3が脱液路21に沿つて設けてあり、
この溝路3に脱液路21上の原料から浸出した液
分が回収されると共にドレイン31によつて所定
箇処に貯溜される。 At the bottom of this V-shaped liquid removal path 21, a groove path 3 as a liquid collection means is provided along the liquid removal path 21,
The liquid leached from the raw material on the draining path 21 is collected in the channel 3 and is stored at a predetermined location by the drain 31.
上記ベルトコンベヤ22,23はネツトベルト
等の多孔性ベルトを用いて構成するのが望まし
く、かくすればベルトの孔からも液分が浸出する
から脱液処理が良好になる。 It is desirable that the belt conveyors 22 and 23 be constructed using porous belts such as net belts, and in this way, the liquid content will also seep out from the holes in the belts, so that the liquid removal process will be improved.
この場合には、第2図に示す如く、ベルトコン
ベヤ22,23の下方に受板25を傾斜状に展張
して、浸出液分を溝路3へ案内する様構成する事
が要望される。 In this case, as shown in FIG. 2, it is desirable to extend the receiving plate 25 in an inclined manner below the belt conveyors 22, 23 to guide the leachate to the channel 3.
上記の如く、ベルトコンベヤ22,23を多孔
性ベルトで構成した場合には、ベルトコンベヤの
内側から圧縮空気を吹上げて、原料7に酸素を供
給する事が出来る。 As described above, when the belt conveyors 22 and 23 are made of porous belts, compressed air can be blown up from inside the belt conveyors to supply oxygen to the raw material 7.
即ち処理室14内の原料7には室内において酸
素を供給する必要があるが、この場合において、
第4図に示す如く、ベルトコンベヤ22(及び2
3)内に酸素供給手段としての噴気部8を設けて
おけば、原料7に対する酸素の供給を良好ならし
める事が出来る。 That is, it is necessary to supply oxygen to the raw material 7 in the processing chamber 14, but in this case,
As shown in FIG.
3) If a fume section 8 is provided as an oxygen supply means inside the reactor, the supply of oxygen to the raw material 7 can be improved.
更に上記処理室14内には、通常原料7を撹拌
して空気との接触面積を増大せしめる撹拌手段が
設けられており、この撹拌手段としては切返部4
が用いられる。 Further, in the processing chamber 14, a stirring means for stirring the raw material 7 to increase the contact area with air is provided.
is used.
上記切返部4は原料7を上下方向に混合すれば
良く、例へば第5図の如く、ベルトコンベヤ2
2,24間に回転送り部材41を設けたり、或は
又第6図の如く、ベルトコンベヤ22,24間に
落差42を設けたりして構成すれば良い。 The above-mentioned cutting section 4 may mix the raw materials 7 in the vertical direction, for example, as shown in FIG. 5, the belt conveyor 2
A rotary feed member 41 may be provided between the belt conveyors 2 and 24, or a head 42 may be provided between the belt conveyors 22 and 24 as shown in FIG.
上記散布管系6は原料7から得た尿液成分を原
料7に散布するもので、この散布は原料7の含液
量が過小になつた場合に、これを補充調整するた
めに行なわれる。 The above-mentioned dispersion pipe system 6 is for dispersing the urine component obtained from the raw material 7 onto the raw material 7, and this spraying is performed to replenish and adjust the liquid content of the raw material 7 when it becomes too small.
従つて、原料7からの水分蒸発を多くして、原
料7に尿液を多量に追加する様設計すれば堆肥の
品質向上と尿液処理との双方が同時に可能とな
る。本発明装置は、この様に太陽熱による水分蒸
発と脱液路21による液分回収とによつて原料7
の含液量を調整するものであるから、従来の堆肥
化処理における前述問題を解決出来ると共に、発
酵に要する処理室内部の温度も太陽熱で得られる
から別途エネルギーの省除もなし得ると云う効果
がある。 Therefore, if the design is designed to increase water evaporation from the raw material 7 and add a large amount of urine to the raw material 7, it is possible to improve the quality of the compost and treat the urine at the same time. In this way, the apparatus of the present invention utilizes water evaporation due to solar heat and liquid recovery through the dewatering path 21 to remove the raw material 7.
Since it adjusts the liquid content of the compost, it is possible to solve the problems mentioned above in conventional composting processing, and the temperature inside the processing chamber required for fermentation can be obtained from solar heat, which also has the effect of saving energy. There is.
第1図は本発明装置の斜視図、第2図は同上装
置の縦断正面図、第3図は同上装置の側面図、第
4図は同上装置に使用するベルトコンベヤの実施
例を示す縦断側面図、第5図、第6図は夫々本発
明装置に使用する切返部の実施例を示す略解側面
図である。
図中1は外装体、12は屋根部分、13は透光
面、14は処理室、15は投入部、16は排出
部、2は搬送機構、21は脱液路、22,23は
夫々脱液路のベルトコンベヤ、3は液分回収手段
としての溝路、4は撹拌手段としての切返部を示
す。
Fig. 1 is a perspective view of the device of the present invention, Fig. 2 is a longitudinal sectional front view of the same device, Fig. 3 is a side view of the same device, and Fig. 4 is a longitudinal sectional side view showing an embodiment of the belt conveyor used in the above device. Figures 5 and 6 are schematic side views showing embodiments of the cut section used in the device of the present invention. In the figure, 1 is the exterior body, 12 is the roof part, 13 is the transparent surface, 14 is the processing chamber, 15 is the input section, 16 is the discharge section, 2 is the conveyance mechanism, 21 is the draining path, and 22 and 23 are the draining sections, respectively. A belt conveyor as a liquid path, 3 a groove path as a liquid collection means, and 4 a cut section as a stirring means.
Claims (1)
成したトンネル状処理室と、この処理室の屋根部
分に形成した透光面とを備えた外装体を作り、上
記処理室内には上記投入部から排出部に向けて原
料を搬送する搬送機構を設けると共にこの搬送機
構には脱液路を形設し、上記脱液路は1対のベル
トコンベヤを搬送方向に沿つて平行状に装架する
と共に此等ベルトコンベヤの接近側を他方側より
低くして断面V状の路面が形成される様構成し、
上記脱液路の下方には脱液路上の原料から滲出す
る液体を回収するべく液分回収手段を設けた事を
特徴とした堆肥製造装置。 2 上記脱液路のベルトコンベヤが多孔性のベル
トで構成されている事を特徴とした特許請求の範
囲第1項記載の堆肥製造装置。[Scope of Claims] 1. An exterior body is made that includes a tunnel-shaped processing chamber with a raw material input section at one end and a discharge section at the other end, and a transparent surface formed on the roof of the processing chamber. A conveying mechanism for conveying the raw material from the input section to the discharge section is provided in the processing chamber, and a deliquing path is formed in this conveying mechanism, and the deliquing path connects a pair of belt conveyors in the conveying direction. The belt conveyor is mounted in parallel along the belt conveyor, and the approach side of the belt conveyor is lower than the other side, so that a road surface with a V-shaped cross section is formed.
A compost manufacturing apparatus characterized in that a liquid recovery means is provided below the liquid removal path to collect liquid exuding from the raw material on the liquid removal path. 2. The compost manufacturing apparatus according to claim 1, wherein the belt conveyor of the liquid removal path is composed of a porous belt.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP56024083A JPS57140393A (en) | 1981-02-19 | 1981-02-19 | Compost manufacturing apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP56024083A JPS57140393A (en) | 1981-02-19 | 1981-02-19 | Compost manufacturing apparatus |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS57140393A JPS57140393A (en) | 1982-08-30 |
| JPS6311317B2 true JPS6311317B2 (en) | 1988-03-14 |
Family
ID=12128506
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP56024083A Granted JPS57140393A (en) | 1981-02-19 | 1981-02-19 | Compost manufacturing apparatus |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS57140393A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0435518U (en) * | 1990-07-24 | 1992-03-25 |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP5295514B2 (en) * | 2007-03-30 | 2013-09-18 | 株式会社奥村組 | Ceiling structure of composting facility |
-
1981
- 1981-02-19 JP JP56024083A patent/JPS57140393A/en active Granted
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0435518U (en) * | 1990-07-24 | 1992-03-25 |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS57140393A (en) | 1982-08-30 |
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