JPS6090B2 - Human waste disposal method - Google Patents
Human waste disposal methodInfo
- Publication number
- JPS6090B2 JPS6090B2 JP56144171A JP14417181A JPS6090B2 JP S6090 B2 JPS6090 B2 JP S6090B2 JP 56144171 A JP56144171 A JP 56144171A JP 14417181 A JP14417181 A JP 14417181A JP S6090 B2 JPS6090 B2 JP S6090B2
- Authority
- JP
- Japan
- Prior art keywords
- human waste
- water
- incineration ash
- layer
- surplus sludge
- 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
Description
【発明の詳細な説明】
この発明は２０〜３０％の揮発物質を含有した顎粒状の
焼却灰を漣材とし、とくにし尿処理プロセスにおける２
次処理水あるいは凝集沈殿処理水中のＳＳ除去と同時に
、ＣＯＤＭｎおよび色度成分が効率よく除去できるし尿
処理方法に関する。DETAILED DESCRIPTION OF THE INVENTION This invention uses granular incineration ash containing 20 to 30% of volatile substances as a waste material, and is particularly suitable for use in the human waste treatment process.
The present invention relates to a human waste treatment method that can efficiently remove CODMn and chromaticity components at the same time as removing SS from subsequent treatment water or coagulation-sedimentation treatment water.
し尿処理プロセスにおける処理水中のＳＳを除去するた
めの櫨過装置としては、砂を櫨過材とするものが最も一
般的であるが、ＣＯＤＭｎや色度成分を除去することが
できないという点で満足すべきものとはいえない。The most common filtration device for removing SS from treated water in the human waste treatment process is one that uses sand as the filtration material, but it is unsatisfactory in that it cannot remove CODMn and chromaticity components. It cannot be said that it is something that should be done.
贋過材として活性炭を使用すればＣＯＤＭｎなどの除去
効果が格段に向上するが、活性炭のコストが着るしく高
いために、工業的な規模で使用することは経済的にも困
難である。この発明は、砂の猿過材では除去することの
できないＣＯＤＭｎなども効果的に除去することができ
る新規な漣過材を利用したし尿処理方法を提供すること
を目的としている。If activated carbon is used as a counterfeit material, the removal effect of CODMn etc. will be greatly improved, but the cost of activated carbon is prohibitively high, making it economically difficult to use it on an industrial scale. An object of the present invention is to provide a method for treating human waste using a novel filtration material that can effectively remove CODMn, which cannot be removed with sand filtration material.
この発明で使用される頬過材は、通常のし尿処理プロセ
スで発生した余剰汚泥を焼却処理することによって得ら
れた余剰汚泥焼却灰で、そのうちＶＭを２０〜３０％含
有している頚粒状のものである。ここで「ＶＭ」とは、
余剰汚泥焼却灰を７００ｑ０に加熱したときに揮発する
揮発成分の総量を指し、このＶＭが２０〜３０％になる
ような条件で得られた直径２〜３側程度の顎粒状の余剰
汚泥焼却灰が最も好適であることが実験によって判明し
た。つぎにこの発明の一実施例を図面にしたがって説明
する。The buccal filtration material used in this invention is surplus sludge incineration ash obtained by incinerating surplus sludge generated in the normal human waste treatment process. It is something. Here, "VM" means
Refers to the total amount of volatile components that evaporate when surplus sludge incineration ash is heated to 700q0, and surplus sludge incineration ash in the form of jaw granules with a diameter of 2 to 3 sides obtained under conditions such that this VM is 20 to 30%. It has been found through experiments that this is the most suitable. Next, one embodiment of the present invention will be described with reference to the drawings.
図において符号１で示す猿過槽内には、その底面から所
定の高さだけ上昇した位置に、通水性を有する支持体２
が設けられ、この支持体２上に、レキなどの支持材層３
および櫨材層４が支持されている。この櫨材層４は、Ｖ
Ｍが２０〜３０％になるように焼却された余剰汚泥焼却
灰の顎粒からなっている。また櫨材層４の上方には原水
流入用トラフ５が設けられている。一方、支持体２の下
方には、渡液を受入れるための室６が形成され、この室
６内に流入した櫨液は、バルブ７を有するパイプ８を経
て外部に排出されるようになっている。一般の櫨過装置
のような逆洗設備はつけず、飽和になったら再度焼却す
る。櫨材層４は、２０〜３０％のＶＭを含有する直径２
〜３肌の顎粒状の余剰汚泥焼却灰からなり、トラフ５か
ら流下した原水がこの櫨材層４を通過する間に、ＳＳの
捕捉を主とする猿過が行われる。A water-permeable support 2 is provided in the sieve tank designated by reference numeral 1 in the figure at a predetermined height above the bottom of the tank.
is provided, and on this support 2, a support material layer 3 such as reki is provided.
and the oak layer 4 are supported. This oak layer 4 is made of V
It consists of granules of surplus sludge incineration ash that have been incinerated so that M is 20 to 30%. Further, above the oak layer 4, a trough 5 for raw water inflow is provided. On the other hand, a chamber 6 for receiving liquid is formed below the support 2, and the liquid that has flowed into the chamber 6 is discharged to the outside through a pipe 8 having a valve 7. There is. There is no backwashing equipment like a regular filtration system, and once it becomes saturated, it is incinerated again. The oak layer 4 has a diameter of 2 containing 20-30% VM.
This layer consists of surplus sludge incineration ash in the form of granules of 1 to 3 skins, and while the raw water flowing down from the trough 5 passes through this oak layer 4, filtration is performed mainly to capture SS.
この櫨週は一般に１２仇ｈ／日程度の速度でなされる。
櫨材層４の濠過効果を確認するためにつぎの実験が行わ
れた。This period is generally done at a speed of about 12 h/day.
The following experiment was conducted to confirm the moat effect of the oak layer 4.
実験 １
直径７仇松のカラムに、余剰汚泥焼却灰の額粒（平均粒
蓬約３柳、ＶＭ含有量２４％）を層高が１００側になる
ように充填して濠過層を形成した。Experiment 1 A moated layer was formed by filling a column with a diameter of 7 mm with grains of surplus sludge incineration ash (average grain size: 3 mm, VM content: 24%) so that the bed height was on the 100 mm side. .
カラム内の額粒の重量は１５鷺（乾燥重量）であった。
通水実験水として、し尿の３倍希釈処理水を用意し、上
記のカラムを通して通水実験水を１２皿／日の線速度で
流し、櫨液のＳＳ値、ＣＯＤＭｎ値、色度を測定した。The weight of the grains in the column was 15 sagi (dry weight).
Three-fold diluted human waste treated water was prepared as the water flow test water, and the water flow test water was flowed through the above column at a linear rate of 12 plates/day to measure the SS value, CODMn value, and chromaticity of the turmeric solution. .
測定結果は第１表のとおりであった。第１表
実験 ２
実験１で用いられたものと同じ余剰汚泥焼却灰を水洗し
て微粒炭を除去し、３個のビーカ中に乾燥重量で１ｇ、
１雌、１０咳の余剰汚泥焼却灰をそれぞれ入れ、さらに
各ビーカにし尿の３倍希釈処理水１〆を力ｏえた。The measurement results are shown in Table 1. Table 1 Experiment 2 The same surplus sludge incineration ash used in Experiment 1 was washed with water to remove granulated coal, and 1 g of dry weight was placed in three beakers.
Surplus sludge incineration ash from 1 female and 10 coughs was added to each beaker, and 1 volume of treated water diluted 3 times with human urine was poured into each beaker.
各ピーカの収容物をジャーテスタで１時間嬢拝し、上燈
液を分析に供した。分析結果を第２表に示す。第２表
以上の実験から明らかなように、この発明が適用される
櫨過装置に使用される余剰汚泥焼却灰からなる猿過材は
、ＳＳを捕捉すると同時に、原水中に含まれているＣＯ
ＤＭｎおよび色度成分を効率よく除去する効果を有して
いる。The content of each peaker was tested in a jar tester for 1 hour, and the top liquid was analyzed. The analysis results are shown in Table 2. As is clear from the experiments shown in Table 2 and above, the filtration material made of surplus sludge incineration ash used in the filtration equipment to which this invention is applied can capture SS and at the same time remove CO contained in raw water.
It has the effect of efficiently removing DMn and chromaticity components.
以上のようにこの発明によれば、猿適材としてＶＭを２
０〜３０％含有する余剰汚泥焼却灰粒子を使用したので
、原水中のＳＳとともに、砂の猿材層では除去すること
のできないＣＯＤＭｎおよび色度成分をも効果的に除去
することができるし、逆洗をしなくてすむ。As described above, according to this invention, two VMs are suitable for monkeys.
Since surplus sludge incineration ash particles containing 0 to 30% were used, it is possible to effectively remove CODMn and chromaticity components that cannot be removed with the sand layer, along with SS in the raw water. Eliminates the need for backwashing.
したがって櫨過水の水質が向上し、また後段の処理工程
の負荷が軽くなるという効果が得られる。特に、し尿処
理に当っては一般的な生物処理では、一定以上の色度Ｃ
ＯＤの除去は困難で、希釈水を減少した場合、これらの
除去が切望されていた。Therefore, it is possible to improve the quality of the Hashipurashi water and to reduce the burden on subsequent treatment steps. In particular, in general biological treatment for human waste treatment, chromaticity C above a certain level is required.
Removal of OD is difficult and their removal is highly desired when dilution water is reduced.
この発明は、これらし尿の低希釈あるいは無希釈処理に
最適である。また、効果が減退した場合、もう一度焼却
すれば再生できる。This invention is most suitable for low dilution or no dilution treatment of human waste. Also, if the effect diminishes, it can be regenerated by incinerating it again.
図はこの発明の一実施例が適用される櫨過装置の概略的
縦断面図である。
１・・・櫨過層、２・・・支持体、３・・・支持材層、
４・・・猿材層、５・・・トラフ、６・・・室、７・・
・バルブ、８・・・パイプ。The figure is a schematic vertical sectional view of a scrubbing device to which an embodiment of the present invention is applied. DESCRIPTION OF SYMBOLS 1... Hashimoto layer, 2... Support body, 3... Support material layer,
4...Saruwood layer, 5...trough, 6...chamber, 7...
・Valve, 8...pipe.
Claims (1)
処理水を濾過装置で濾過する処理方法であって、その処
理過程で発生する余剰汚泥を焼却処理した後水洗し、２
０〜３０％の揮発物質を含有した顆粒状の焼却灰を得、
これを上記濾過装置の濾材とするし尿処理方法。1. A treatment method in which human waste is treated in a normal human waste treatment process and the resulting treated water is filtered with a filtration device, in which excess sludge generated in the treatment process is incinerated and then washed with water.
Obtaining granular incineration ash containing 0 to 30% volatile matter,
A human waste treatment method using this as a filter medium of the above-mentioned filter device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP56144171A JPS6090B2 (en) | 1981-09-11 | 1981-09-11 | Human waste disposal method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP56144171A JPS6090B2 (en) | 1981-09-11 | 1981-09-11 | Human waste disposal method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5845707A JPS5845707A (en) | 1983-03-17 |
| JPS6090B2 true JPS6090B2 (en) | 1985-01-05 |
Family
ID=15355850
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP56144171A Expired JPS6090B2 (en) | 1981-09-11 | 1981-09-11 | Human waste disposal method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6090B2 (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH06214417A (en) * | 1993-01-14 | 1994-08-05 | Fuji Electric Co Ltd | Electrophotographic organic sensitive body |
| US5863687A (en) | 1995-11-02 | 1999-01-26 | Konica Corporation | Electrophotographic photoreceptor |
| WO2013191209A1 (en) | 2012-06-20 | 2013-12-27 | 三菱化学株式会社 | Electrophotographic photoreceptor, electrophotographic photoreceptor cartridge, and image-forming device |
-
1981
- 1981-09-11 JP JP56144171A patent/JPS6090B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5845707A (en) | 1983-03-17 |
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