JPS5921855Y2 - Dehydration pretreatment equipment for fermentation treatment of food waste - Google Patents

Dehydration pretreatment equipment for fermentation treatment of food waste

Info

Publication number
JPS5921855Y2
JPS5921855Y2 JP1980073730U JP7373080U JPS5921855Y2 JP S5921855 Y2 JPS5921855 Y2 JP S5921855Y2 JP 1980073730 U JP1980073730 U JP 1980073730U JP 7373080 U JP7373080 U JP 7373080U JP S5921855 Y2 JPS5921855 Y2 JP S5921855Y2
Authority
JP
Japan
Prior art keywords
food waste
perforated plate
sewage
dehydration
fermentation treatment
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
JP1980073730U
Other languages
Japanese (ja)
Other versions
JPS56176014U (en
Inventor
樹弘 小田
Original Assignee
株式会社日本製鋼所
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 株式会社日本製鋼所 filed Critical 株式会社日本製鋼所
Priority to JP1980073730U priority Critical patent/JPS5921855Y2/en
Publication of JPS56176014U publication Critical patent/JPS56176014U/ja
Application granted granted Critical
Publication of JPS5921855Y2 publication Critical patent/JPS5921855Y2/en
Expired legal-status Critical Current

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  • Treatment Of Sludge (AREA)

Description

【考案の詳細な説明】 生活系高水分廃棄物、すなわち生ごみは、季節変化によ
ってもその含水率が増減するが、平均的にみても76〜
78%程度の高含水率をもっている。
[Detailed explanation of the idea] The moisture content of household high-moisture waste, that is, kitchen waste, increases and decreases depending on seasonal changes, but on average it is 76 to 76%.
It has a high moisture content of about 78%.

これを、発酵処理をなすには、68%以下の含水率にし
なければならないが、従来の脱水前処理装置では、せい
ぜい、71〜73%位までしか脱水を行うことができな
かった。
In order to carry out fermentation treatment, the water content must be reduced to 68% or less, but conventional dehydration pre-treatment equipment could only dehydrate to about 71-73% at most.

このためその発酵処理に当って、発酵槽内においても自
然脱水を行わなければならなかった。
Therefore, during the fermentation process, natural dehydration had to be performed within the fermenter.

また脱水処理後、これを粗篩分機にかけた後、発酵処理
がなされるが、脱水処理が前記のように不充分であると
、粗篩分機の穴明ドラムの目詰りが激しく、そのためそ
の掃除の頻度が多くなって処理能率が揚がらない上、こ
れが発酵処理全体としての連繋的な連続処理を阻害して
いた。
In addition, after dehydration, it is passed through a coarse sieve and then fermented, but if the dehydration is insufficient as described above, the perforated drum of the coarse sieve will become severely clogged, and the drum should be cleaned accordingly. This increased the frequency of the fermentation process, which hindered the improvement of processing efficiency, and also hindered the continuous continuous processing of the fermentation process as a whole.

本考案はこのよう□な欠点を解消し得るものである。The present invention can overcome these drawbacks.

これを図示のものについて説明する。This will be explained with reference to the diagram.

1は回転胴であって、生ごみの投入口10よりその排出
口11に向って下降傾斜を有するよう設置される。
Reference numeral 1 denotes a rotary cylinder, which is installed so as to have a downward slope from an inlet 10 for garbage to an outlet 11 thereof.

その内面には、彎曲した多孔板2をその一部に内張する
A part of its inner surface is lined with a curved perforated plate 2.

彎曲した多孔板2は、回転胴1の円周方向に90〜27
0°の範囲に亙って、これと適当な間・隙部9を有する
ように内張する。
The curved perforated plate 2 has a diameter of 90 to 27 mm in the circumferential direction of the rotating body 1.
It is lined so that it has an appropriate gap/gap 9 over the 0° range.

3′はそのサポート板である。3' is its support plate.

サポート板3′は多孔板2の補強を兼ねる。The support plate 3' also serves to reinforce the perforated plate 2.

4は、回転胴1内面の多孔板2の内張のない部分にその
軸方向に並設した掻き板であって、これは円周方向に沿
って設けた仕切板3で複数個に分断され回転胴1内の生
ごみがその回転操作中排出口11側へ自由に流れること
を制御する。
Reference numeral 4 denotes scraping plates arranged in parallel in the axial direction on the unlined part of the perforated plate 2 on the inner surface of the rotary drum 1, and this is divided into a plurality of pieces by a partition plate 3 provided along the circumferential direction. The garbage inside the rotary drum 1 is controlled to freely flow toward the discharge port 11 side during the rotation operation.

5は多孔板2の内張りのある側に位置して回転胴1に穿
設しi汚水排出孔であって、その外面に位置して、多孔
板2の外周に汚水受は管6を設ける。
A sewage discharge hole 5 is located on the side of the perforated plate 2 which is lined with the lining and is bored in the rotary drum 1, and a sewage receiving pipe 6 is provided on the outer surface of the perforated plate 2 on the outer periphery thereof.

汚水受は管6の汚水吐出口6′は汚水槽7に開口する。A sewage outlet 6' of a pipe 6 opens into a sewage tank 7.

8は生ごみを示す。なお回転胴1の大きさは、一般的に
3mφ×12mL程度であって、回転数は2r、p、m
位であり、また多孔板2はステンレス製の薄板2m、m
、程度のものがよい。
8 indicates food waste. The size of the rotary cylinder 1 is generally about 3 mφ x 12 mL, and the number of rotations is 2r, p, m.
The perforated plate 2 is a stainless steel thin plate of 2 m, m
, something of the order of magnitude is good.

これは回転胴と同じ厚板例えば16m、m、を使用して
小孔2〜8m6m、φを明けると、汚水の表面張力によ
り小孔内の汚水が流出し難いことと、汚水間の微細化物
が小孔に詰り易くなることによる。
This is because when a small hole of 2 to 8 m, φ is opened using the same thick plate as the rotary cylinder, for example, 16 m, the sewage inside the small hole is difficult to flow out due to the surface tension of the sewage, and the fine particles between the sewage are difficult to flow out. This is because the small holes become easily clogged.

その作用効果を述べる。I will describe its effects.

生ごみ8を投入口10より回転胴1内に投入すると、同
胴内の掻き板4でその底部より上方に掻き上げられ、そ
の頂部付近に運ばれて胴内の多孔板2上に落下し再び上
方に運ばれるという運動を繰返えし乍ら排出口11の方
に進んで行く。
When food waste 8 is thrown into the rotary cylinder 1 through the input port 10, it is scraped up from the bottom by the scraping plate 4 inside the cylinder, carried to the vicinity of the top, and falls onto the perforated plate 2 inside the cylinder. While repeating the movement of being carried upward again, it advances toward the discharge port 11.

そしてその進み方は仕切板3で制限されて前記掻き上げ
落下混線の作用を充分に行う。
The way it advances is restricted by the partition plate 3, so that the effect of the above-mentioned raking up and falling crosstalk is sufficiently performed.

前記多孔板2上に落下した生ごみ8の落下刃、あるいは
その混線によって生じる汚水は、回転胴1の回転による
遠心力による効果と自重により多孔板2を通過して間隙
部9に入り、回転胴1の汚水排出孔5より胴外に排出さ
れ、汚水受は管6を経て汚水槽7に流下する。
Sewage generated by the falling edge of the garbage 8 that has fallen onto the perforated plate 2 or its cross-conductor passes through the perforated plate 2 and enters the gap 9 due to the effect of the centrifugal force caused by the rotation of the rotary drum 1 and its own weight, and is rotated. The sewage is discharged to the outside of the sewage tank from the sewage discharge hole 5 of the sewage tank 1, and the sewage receiver flows down through the pipe 6 into the sewage tank 7.

なお、終業時などの回転胴1を停止する時には、多孔板
2を下側にして停止させると自然脱水がなされる。
In addition, when stopping the rotating drum 1 at the end of a working day, etc., natural dehydration can be achieved by stopping the rotary drum 1 with the perforated plate 2 facing downward.

本考案においては、生ごみは、回転胴内において掻き板
によって上方に掻き上げられこれが多孔板上に落下し、
そして多孔板と回転胴との間に間隙部があることと相俟
って、その落下刃と回転胴の回転による遠心力と自重に
より回転中よくその脱水が促進され、そしてこれが順次
下流側へと繰返えされるので脱水効果が極めてよい。
In the present invention, food waste is scraped upward by a scraping plate in the rotary drum, and falls onto a perforated plate.
Coupled with the presence of a gap between the perforated plate and the rotating barrel, the centrifugal force caused by the rotation of the falling blade and the rotating barrel and its own weight often promotes dewatering during rotation, and this water is gradually transferred to the downstream side. Since this process is repeated repeatedly, the dehydration effect is extremely good.

そして脱水した液は回転胴の回転による遠心力で、常に
、多孔板の外側の回転胴壁面に沿って流れ排水される。
The dehydrated liquid always flows along the wall surface of the rotating barrel outside the perforated plate due to the centrifugal force caused by the rotation of the rotating barrel and is drained.

また生ごみは回転胴の下降傾斜により投入口より排出口
の方に順次進み、しかもその進み方は掻き板の仕切板で
制限されるので、生ごみに対し掻き上げ落下混線の作用
とともにその脱水の作用を充分に行うことができる。
In addition, food waste sequentially advances from the input port to the discharge port due to the downward slope of the rotary cylinder, and the way it advances is restricted by the partition plate of the raking board. This function can be fully performed.

したがって76〜78%の高水分の生ごみであっても、
その発酵処理に必要な含水率68%以下に、1回の操作
で充分に脱水させることができるので、発酵処理期間を
大巾に短縮することができ、またその脱水が充分なされ
ているので、脱水処理後の工程である粗篩分機の目詰り
がなくなり、これを排除するために装置を停止するとい
う必要もなくなり、発酵処理装置全体の連繋的連続運転
を効率よくすることができ均一な製品と量産が可能とな
る。
Therefore, even if food waste has a high moisture content of 76-78%,
Since it is possible to sufficiently dehydrate in one operation to reduce the moisture content to 68% or less required for fermentation processing, the fermentation processing period can be greatly shortened, and since the dehydration is sufficient, There is no clogging of the rough sieve machine, which is a process after dehydration treatment, and there is no need to stop the equipment to eliminate this, and the continuous continuous operation of the entire fermentation processing equipment can be made more efficient, resulting in a uniform product. and mass production becomes possible.

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

第1図は本装置の縦断側面図、第2図は第1図のA−A
線横断側面図である。 1・・・・・・回転胴、2・・・・・・多孔板、3・・
・・・・仕切板、4・・・・・・掻き板、5・・・・・
・汚水排出孔、9・・・・・・間隙部。
Figure 1 is a longitudinal cross-sectional side view of this device, and Figure 2 is A-A in Figure 1.
It is a line cross-sectional side view. 1... Rotating cylinder, 2... Perforated plate, 3...
...Partition board, 4...Scraping board, 5...
- Sewage discharge hole, 9... Gap.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 投入口10より排出口11に向って下降傾斜するように
設けた回転胴1内面に、これと少許の間隙部9を存して
彎曲した多孔板2をその一部に内張し、多孔板2の内張
のない胴内面に掻き板4を軸方向に並設し、かつこれを
円周方向に沿って設けた仕切板3で複数個に分断し、そ
して間脳には、多孔板2の内張りのある側において汚水
気出孔5を穿設した生ごみの発酵処理のための脱水前処
理装置。
A perforated plate 2 curved with a small gap 9 is lined in a part of the inner surface of the rotary drum 1, which is provided so as to be inclined downward from the input port 10 toward the discharge port 11. Scraping plates 4 are arranged in parallel in the axial direction on the inner surface of the trunk without lining of 2, and this is divided into a plurality of pieces by a partition plate 3 provided along the circumferential direction. A dehydration pretreatment device for fermentation processing of food waste, which has a sewage vent hole 5 on the side with the lining.
JP1980073730U 1980-05-27 1980-05-27 Dehydration pretreatment equipment for fermentation treatment of food waste Expired JPS5921855Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1980073730U JPS5921855Y2 (en) 1980-05-27 1980-05-27 Dehydration pretreatment equipment for fermentation treatment of food waste

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1980073730U JPS5921855Y2 (en) 1980-05-27 1980-05-27 Dehydration pretreatment equipment for fermentation treatment of food waste

Publications (2)

Publication Number Publication Date
JPS56176014U JPS56176014U (en) 1981-12-25
JPS5921855Y2 true JPS5921855Y2 (en) 1984-06-29

Family

ID=29436496

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1980073730U Expired JPS5921855Y2 (en) 1980-05-27 1980-05-27 Dehydration pretreatment equipment for fermentation treatment of food waste

Country Status (1)

Country Link
JP (1) JPS5921855Y2 (en)

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5344138U (en) * 1976-09-16 1978-04-15

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5344138U (en) * 1976-09-16 1978-04-15

Also Published As

Publication number Publication date
JPS56176014U (en) 1981-12-25

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