JPS5839594B2 - Garbage processing method and equipment - Google Patents
Garbage processing method and equipmentInfo
- Publication number
- JPS5839594B2 JPS5839594B2 JP49031553A JP3155374A JPS5839594B2 JP S5839594 B2 JPS5839594 B2 JP S5839594B2 JP 49031553 A JP49031553 A JP 49031553A JP 3155374 A JP3155374 A JP 3155374A JP S5839594 B2 JPS5839594 B2 JP S5839594B2
- Authority
- JP
- Japan
- Prior art keywords
- tank
- water
- garbage
- sludge
- cylinder
- 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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
Landscapes
- Processing Of Solid Wastes (AREA)
- Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)
Description
【発明の詳細な説明】
本発明は一般家庭より放出される塵芥の処理に関するも
のであり、更に詳しくは一般家庭より放出される塵芥を
攪拌混合、分離、圧縮脱水、酸素曝気及び沈澱の諸工程
により処理する方法及び装置に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to the treatment of garbage discharged from ordinary households, and more specifically, the present invention relates to the treatment of garbage discharged from ordinary households, and more specifically, the various steps of stirring and mixing, separation, compression dehydration, oxygen aeration, and sedimentation of garbage discharged from ordinary households. The present invention relates to a method and apparatus for processing.
一般家庭より放出される塵芥はその大部分が食料品の残
滓であり、穀物、野菜、魚介類等がそれらの多くを占め
ている。Most of the garbage discharged from ordinary households is food residue, with grains, vegetables, seafood, etc. accounting for the majority.
これらの塵芥は各家庭から塵芥処理場に車で運ばれ、総
合炉において焼却されているのが現状である。Currently, this garbage is transported by car from each household to a garbage treatment plant, where it is incinerated in a general furnace.
しかしこれらの塵芥は重量比に於て80〜90%が水分
で占められているため、焼却に際して蒸発熱を奪い膨大
な熱量を必要とする。However, since these dusts are comprised of 80 to 90% water by weight, the heat of evaporation is taken away during incineration, requiring an enormous amount of heat.
そのため焼却用燃料を非常に多く必要とする。Therefore, a large amount of incineration fuel is required.
又水分が多いため、焼却の際の加熱により化学変化を起
し、悪臭を発するという欠陥がある。Also, since it contains a lot of water, it undergoes chemical changes when heated during incineration, resulting in a foul odor.
この2つの発明はこれらの欠陥を克服するために考えら
れたものである。These two inventions were devised to overcome these deficiencies.
以下2つの発明について図面に基いて説明する。The following two inventions will be explained based on the drawings.
第1図は2つの発明を説明する流れ図である。FIG. 1 is a flowchart illustrating two inventions.
一般家庭より集めて運ばれた塵芥は、まず混合ピット1
の中に投入される。The garbage collected and transported from ordinary households is first collected in the mixing pit 1.
is put into the.
塵芥はここで、2本のパイプより添加される水と攪拌翼
20作用により半流動状態となる。Here, the dust becomes semi-fluid due to the action of water added through the two pipes and the stirring blade 20.
添加水量は約70〜90%であり、この水の添加により
、粉塵の飛散防止上の効果を生ずる。The amount of water added is about 70 to 90%, and the addition of this water has the effect of preventing dust from scattering.
混合ピット中で半流動状態となった塵芥は、混合ピット
の下部に配置しである分離槽3に送られる0分離槽3に
は、マグネット板をエンドレス連6結したコンベア4が
垂直もしくは若干の傾斜を以て配置されており、ここで
塵芥中の鉄片が除去される。The waste in a semi-liquid state in the mixing pit is sent to a separation tank 3 located at the bottom of the mixing pit.In the separation tank 3, a conveyor 4 with endlessly connected magnetic plates 6 is installed vertically or slightly It is arranged at an angle, and iron pieces in the garbage are removed here.
除去された鉄片は金属片収容箱5に集められる。The removed iron pieces are collected in a metal piece storage box 5.
鉄片を除かれた塵芥は、塵芥樋6に流入する。The garbage from which the iron pieces have been removed flows into the garbage gutter 6.
塵芥樋6は、数個の直立する圧縮脱水機7に塵芥を供給
するようになっている。The waste trough 6 is adapted to supply waste to several upright compression dehydrators 7.
第2図は任意の1個の圧縮脱水機7と塵芥樋6の拡大図
で、シリンダー8と塵芥樋6は第1図のA −A’の切
断面を示す。FIG. 2 is an enlarged view of one arbitrary compression dehydrator 7 and the garbage gutter 6, and the cylinder 8 and the garbage gutter 6 are shown along the line A-A' in FIG.
第2図において、半流動塵芥流は、底を油圧によって下
方から押し上げられたステンレス板9によって閉ざされ
たシリンダー8の中に流入する。In FIG. 2, the semi-liquid waste stream flows into a cylinder 8 whose bottom is closed by a stainless steel plate 9 which is pushed up from below by hydraulic pressure.
次にピストン10が油圧により上方から押し上げ、まず
塵芥樋の流入口11を閉ざし、次いでシリンダー中の塵
芥を圧縮する。Next, the piston 10 is pushed up from above by hydraulic pressure, first closing the inlet 11 of the garbage trough, and then compressing the garbage in the cylinder.
ステンレス板9には垂直に多数の孔が設けであるので、
塵芥中の水分はその孔からシリンダー外へ流出する。Since the stainless steel plate 9 has many holes vertically,
Moisture in the dust flows out of the cylinder through the holes.
シリンダー8中でピストン10が塵芥を圧縮するときの
圧力は、1ton/crti程度で塵芥の含水率を約1
6%まで低下させることができる。The pressure when the piston 10 compresses the garbage in the cylinder 8 is about 1 ton/crti, which lowers the moisture content of the garbage by about 1.
It can be reduced to 6%.
−回にシリンダー8に供給する塵芥流の量は、塵芥の流
動度と、ピストン10が塵芥樋6の流入口11とを開い
ている時間を任意に変更することにより、適正に保つこ
とができる。- The amount of garbage flow supplied to the cylinder 8 at each time can be maintained at an appropriate level by arbitrarily changing the flow rate of the garbage and the time during which the piston 10 opens the inlet 11 of the garbage gutter 6. .
」隻圧縮が終ったら、再びピストン10を上昇せしめ、
塵芥流をシリンダー8に適当量大れて、また圧縮をくり
返す。” When the compression is finished, raise the piston 10 again,
A suitable amount of the dust flow is introduced into the cylinder 8, and the compression is repeated again.
この工程を数回くり返すことにより、シリンダー8の下
部には含水率約16%の円盤状の圧縮された塵芥ができ
る。By repeating this process several times, a disk-shaped compressed garbage with a moisture content of about 16% is formed at the bottom of the cylinder 8.
最後の圧縮が終ったら、ピストン10を上昇せしめず、
下側ステンレス板9を下げてピストン10を更に押し上
げることにより、シリンダーより固形化した塵芥が外に
出る。After the final compression is completed, the piston 10 is not raised;
By lowering the lower stainless steel plate 9 and further pushing up the piston 10, solidified dust is discharged from the cylinder.
この固形塵芥はコンベアーにより集積する。This solid waste is collected by a conveyor.
圧縮脱水機により塵芥と区別された汚水は、シリンダー
8の下部のステンレス板9の孔からパイプに導びかれる
ようになっており、これは集められて反応槽12中に落
下する。Sewage separated from dust by the compression dehydrator is led to a pipe through a hole in a stainless steel plate 9 at the bottom of the cylinder 8, where it is collected and falls into a reaction tank 12.
反応槽12中では、活性汚泥法による酸素曝気の処理が
行なわれる。In the reaction tank 12, oxygen aeration is performed using an activated sludge method.
すなわち、第1図においてエアーポンプ13により反応
槽中に圧縮空気が送られ、一方薬品タンク14より、陽
酸アンモニアあるいは尿素等を添加することにより酸化
処理を行う。That is, in FIG. 1, compressed air is sent into the reaction tank by an air pump 13, and oxidation treatment is performed by adding ammonia or urea or the like from a chemical tank 14.
この処理は、攪拌翼150作用により一層効果を上げる
ことができる。This treatment can be made more effective by the action of the stirring blade 150.
酸化処理された尿水は、次に沈澱槽16に送られる。The oxidized urine water is then sent to the sedimentation tank 16.
沈澱槽においては、凝固した物質の浮上を防止する交互
に配した数個の傾斜板17と薬品タンク18より送られ
るノニオン系凝集剤の作用により、清浄な水とスラッジ
とに分離される。In the sedimentation tank, clean water and sludge are separated by the action of several inclined plates 17 arranged alternately to prevent the coagulated substances from floating and a nonionic flocculant sent from the chemical tank 18.
清浄な水は隣り合って配置する貯水タンク19に入る。Clean water enters water storage tanks 19 arranged next to each other.
一方スラッジは沈澱槽の低部に沈澱しこれは圧送ポンプ
20によって再びピット1中に送り込まれ、新たに加え
られた塵芥と一層に混り合って、攪拌混合、分離、圧縮
脱水、酸化、沈澱の諸工程を繰返すことになる。On the other hand, the sludge settles in the lower part of the settling tank, and is sent into the pit 1 again by the pressure pump 20, where it is further mixed with the newly added dust, and undergoes agitation mixing, separation, compression dehydration, oxidation, and precipitation. The steps will be repeated.
貯水タンクに貯えられた水は、その内一部又は全部を再
び混合ピットに加えることにより、新たな塵芥の半流動
化に役立つことになる。Some or all of the water stored in the water storage tank can be added back to the mixing pit to help semi-fluidize the new waste.
これら2つの発明による塵芥処理は、まず固形圧縮化さ
れた塵芥を生ずるか、これは水分が約16%でかつ容積
が小さいので、運搬及び燃焼が容易であり、焼却炉を本
発明に示す装置と別の場所に設置することに対しても抵
抗が少なく、又焼却燃料を著しく節約できる。The waste treatment according to these two inventions first produces solid compressed waste, which has a moisture content of about 16% and a small volume, so it is easy to transport and burn, and an incinerator is used as the apparatus shown in the present invention. There is little resistance to installing it in a different location, and incineration fuel can be significantly saved.
更に無為に焼却するにとどめず、若干の自然乾燥又は人
工乾燥を加えることにより、固形燃料としても使用しう
る。Furthermore, rather than simply incinerating it, it can also be used as a solid fuel by subjecting it to some natural or artificial drying.
更に固形圧縮化された塵芥は、燃焼に際して水蒸気を発
生しにくいので、悪臭も従来に比べて著しく少なくなる
。Furthermore, since solid compressed dust is less likely to generate water vapor when burned, it produces significantly less bad odor than before.
本塵芥処理により最終的に生ずる没澱槽低部のスラッジ
は、再び混合ピットに投入されるため二次公害を発生し
ない。The sludge at the bottom of the sedimentation tank, which is ultimately produced by this waste treatment, is thrown into the mixing pit again, so it does not cause secondary pollution.
この処理においては、その主要部である圧縮脱水7はそ
のシリンダー8の直径及び個数を任意に組合せることに
より、処理能力を任意に変更することが可能である。In this process, the processing capacity of the compression dehydrator 7, which is the main part, can be changed arbitrarily by arbitrarily combining the diameter and number of cylinders 8.
以上のように特定発明による塵芥処理方法は、焼却に際
して焼却燃料を節約し、悪臭を発生しない固形圧縮塵芥
を生産する効果を有し、他の発明によるその製造装置は
二次公害を発生せず、処理能力を容易に変更しうる効果
を有する。As described above, the garbage processing method according to the specified invention has the effect of saving incineration fuel during incineration and producing solid compacted garbage that does not generate bad odor, and the manufacturing apparatus according to other inventions does not generate secondary pollution. , which has the effect of easily changing processing capacity.
第1図は2つの発明を説明するための流れ図であり、第
2図は圧縮脱水機の原理を説明するための要部を示した
ものであり、切断面は第1図におけるA−A’線に沿っ
た断面を示す。
各部の名称は次のとおりである。
1・−・・−混合ピント、2・−・−・−攪拌翼、3・
・−・・−分離槽、4・・−・・・マグネット・コンベ
ア、5・・−・・金属片収容箱、6・・・・・・塵芥樋
、7・・−・−・圧縮脱水機、8・−・°°シリンダー
、9・・・・・°低部ステンレス板、10・−・−゛ピ
ストン、11・・−・−流入口、12反応槽、13・・
−・・−エアーポンプ、14・−・−薬品タンク、15
・・−・−・・・攪拌翼、16・−・・・−沈澱槽、1
7−・・・−傾斜板、18・−・−薬品タンク、19・
・−・・・貯水タンク、2゜・・−・・・圧送ポンプ。Fig. 1 is a flowchart for explaining the two inventions, and Fig. 2 shows the main parts for explaining the principle of the compression dehydrator. A cross section along the line is shown. The names of each part are as follows. 1.--.-mixing focus, 2.--.--stirring blade, 3.
・・・・Separation tank, 4・・・・Magnetic conveyor, 5・・・・Metal piece storage box, 6・・・・Garbage gutter, 7・・・・・・・Compression dehydrator , 8...°Cylinder, 9...°Lower stainless steel plate, 10...- Piston, 11...-Inlet, 12 Reaction tank, 13...
--- Air pump, 14 --- Chemical tank, 15
...------ Stirring blade, 16...- Sedimentation tank, 1
7-...- inclined plate, 18...- chemical tank, 19...
・−・・Water tank, 2゜・・・・Pressure pump.
Claims (1)
流動状態となし、分離槽に送り、マグネットコンベアに
より鉄片を除去し、塵芥樋を経て圧縮脱水機に供給し、
シリンダー中にて油圧により加圧されたピストンにより
圧縮脱水し、固形圧縮塵芥と汚水とに分け、汚水を反応
槽中で酸素曝気し、沈澱槽にて凝集剤を添加して、スラ
ッジと清浄な水に分け、スラッジを再び混合ピットに送
ることを特徴とする塵芥処理方法。 2 水の添加パイプ及び攪拌翼を備えた混合槽を置き、
その下部にマグネットコンベアを備えた分離槽を設け、
分離槽より出た半流動物質を圧縮脱水機に供給する塵芥
樋を連結し、これに下部を油圧により上下に作動する多
孔のステンレス板で閉じ上部より油圧によりシリンダー
中のものを圧縮するピストンを配した1個又は数個の圧
縮脱水機を配し、脱線脱水された水を反応槽に導くパイ
プを設け、エアーポンプ及び攪拌翼を備えた反応槽を置
き、この下部に多数の傾斜板を有する沈澱槽を設け、沈
澱槽の上澄液を入れる貯水タンクをその側方に設け、更
に沈澱槽下部のスラッジを再び混合ピットに送る圧送ポ
ンプ及びパイプを設けることを特徴とする塵芥処理装置
。[Claims] 1. Dust is put into a mixing pit, water is added and stirred to make it semi-fluid, sent to a separation tank, iron pieces are removed by a magnetic conveyor, and fed to a compression dehydrator via a trash gutter. death,
The water is compressed and dehydrated using a piston pressurized by hydraulic pressure in a cylinder, separated into solid compacted waste and sewage, the sewage is aerated with oxygen in a reaction tank, and a flocculant is added in a settling tank to separate sludge and clean water. A waste treatment method characterized by separating the sludge into water and sending the sludge back to the mixing pit. 2 Place a mixing tank equipped with a water addition pipe and stirring blades,
A separation tank equipped with a magnetic conveyor is installed at the bottom.
A garbage gutter is connected to feed the semi-liquid material from the separation tank to the compression dehydrator, and the lower part is closed with a porous stainless steel plate that moves up and down using hydraulic pressure, and the upper part is equipped with a piston that compresses the material in the cylinder using hydraulic pressure. One or several compression dehydrators are installed, a pipe is installed to lead the dehydrated water to a reaction tank, a reaction tank is installed with an air pump and stirring blades, and a number of inclined plates are installed at the bottom of the reaction tank. What is claimed is: 1. A garbage processing device comprising: a sedimentation tank having a sedimentation tank, a water storage tank for storing supernatant liquid from the sedimentation tank on the side thereof, and a pressure pump and a pipe for feeding sludge at the bottom of the sedimentation tank to a mixing pit again.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP49031553A JPS5839594B2 (en) | 1974-03-22 | 1974-03-22 | Garbage processing method and equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP49031553A JPS5839594B2 (en) | 1974-03-22 | 1974-03-22 | Garbage processing method and equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS50125567A JPS50125567A (en) | 1975-10-02 |
| JPS5839594B2 true JPS5839594B2 (en) | 1983-08-31 |
Family
ID=12334364
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP49031553A Expired JPS5839594B2 (en) | 1974-03-22 | 1974-03-22 | Garbage processing method and equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5839594B2 (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5369475A (en) * | 1976-12-01 | 1978-06-20 | Hitachi Metals Ltd | Scrubbing dehydrator |
| JPS6027589Y2 (en) * | 1977-08-26 | 1985-08-20 | 日立機電工業株式会社 | Effluent treatment equipment during screen residue cleaning and dewatering |
-
1974
- 1974-03-22 JP JP49031553A patent/JPS5839594B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS50125567A (en) | 1975-10-02 |
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