JPS61161200A - Treatment of night soil - Google Patents

Treatment of night soil

Info

Publication number
JPS61161200A
JPS61161200A JP60001822A JP182285A JPS61161200A JP S61161200 A JPS61161200 A JP S61161200A JP 60001822 A JP60001822 A JP 60001822A JP 182285 A JP182285 A JP 182285A JP S61161200 A JPS61161200 A JP S61161200A
Authority
JP
Japan
Prior art keywords
separated
humic acid
night soil
acid
sedimentation
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.)
Pending
Application number
JP60001822A
Other languages
Japanese (ja)
Inventor
Masahito Fujita
雅人 藤田
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Takuma Co Ltd
Original Assignee
Takuma Co Ltd
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 Takuma Co Ltd filed Critical Takuma Co Ltd
Priority to JP60001822A priority Critical patent/JPS61161200A/en
Publication of JPS61161200A publication Critical patent/JPS61161200A/en
Pending legal-status Critical Current

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  • Treatment Of Sludge (AREA)

Abstract

PURPOSE:To remove the contaminants contained in concd. night soil by adding humic acid to the concd. night soil freed of deposits, agitating at specified pH, and separating the night soil by sedimentation into a separated liq. and separated sludge. CONSTITUTION:To concd. night soil freed of deposits, 0.1-10wt% humic acid is added, and agitated and mixed at 3-5pH. The mixture is separated by sedimentation into a separated liq. and separated sludge. Namely, a chemical agent for decreasing the COD in the night soil is not used in this case, and the use of an expensive oxidizing agent can be dispensed with by adopting colloidal sedimentation. Consequently, the COD substances are economically removed with the inexpensive humic acid. Moreover, the deposited and separated contaminants can be used as excellent fertilizer and soil improving agent.

Description

【発明の詳細な説明】 産業上の利用分野: 本発明はし尿の処理法、さらに詳しくいうと、フミン酸
を用いた濃厚し尿の処理方法に関する。
DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application: The present invention relates to a method for treating human waste, and more particularly to a method for treating concentrated human waste using humic acid.

従来技術: 濃厚し尿の処理は、従来、繊維質、紙片等のし鉄系凝集
剤などを使用して、有機物質を減らした後に生物学的浄
化する方法により行われていた。
Conventional technology: Conventionally, concentrated human waste has been treated by biological purification after reducing organic substances using iron-based flocculants such as fibers and paper pieces.

発EJIKより解決される問題点 前者(生物学的方法)によると、多鰍の希釈水が必要で
あるばかりでなく、処理槽の容歓が1日当り投入量の3
0倍以上必要で、1m!投費、運@黄、敷地面積が大き
くなる欠点があった。
Problems solved by Hatsu EJIK According to the former (biological method), not only is it necessary to use water for diluting many fish, but the capacity of the treatment tank is 3 times the amount of input per day.
0 times more required, 1m! There were disadvantages of investment, luck @ yellow, and large site area.

一方後者(化学処理+生物学的処理)の場合、所要薬品
類を処理し尿に対し、約1〜3%使用しなければならず
、その効果はCOD除去率で約30〜70%に過ぎず、
経済的とは言えなかった。
On the other hand, in the case of the latter (chemical treatment + biological treatment), the required chemicals must be used at approximately 1 to 3% of the treated urine, and the effectiveness is only approximately 30 to 70% in terms of COD removal rate. ,
It wasn't economical.

問題点を解決するための手段: 本発明では濃厚し尿にフミン酸またはアミン酸のアルカ
リ塩を加えて浄化を行う。この際、無機凝集剤例、tば
塩化第二鉄、硫酸アルミニウムを併用するとさらに浄化
時間が短縮できる。
Means for solving the problem: In the present invention, concentrated human urine is purified by adding an alkali salt of humic acid or amino acid. At this time, if an inorganic flocculant such as ferric chloride or aluminum sulfate is used in combination, the purification time can be further shortened.

フミン酸の使用量fi−厚し尿の約0.1〜10%が適
当で、0.1%以下では効果が充分でなく、10%以上
使用しても、その幼果はほとんど変らず、経済的でない
。また、フミン酸を加えた混合物のpHは約3〜5の弱
酸性に呆つことか好ましい。また、混合物を約0.5時
間〜4時間撹拌して混合すると反応が充分進行する。
The appropriate amount of humic acid to use fi - about 0.1 to 10% of human urine. If it is less than 0.1%, the effect is not sufficient, and even if it is used more than 10%, the young fruit will hardly change, making it economical. Not on point. Further, it is preferable that the pH of the mixture to which humic acid is added is a weak acidity of about 3 to 5. Further, if the mixture is stirred for about 0.5 to 4 hours, the reaction will proceed sufficiently.

作   用: フミン酸は低石炭化度の草炭・亜炭、土壊海底土などに
含まれるアルカリに可溶、酸く不溶のカッ色ないし黒色
の無定形酸性有機物質の総称である。酸性を示すのはカ
ルボキシル基、フェノール基の存在によるもので、酸あ
たりの化学当量は300〜400の場合が多く炭素50
−65%、水素4−6%、残部は大部分酸素であるが成
因により窒素、イオタを含むこともある。本発明でいう
フミン酸は成因に拘らずすべてのものを含む。
Function: Humic acid is a general term for amorphous acidic organic substances that are alkali-soluble, acid-insoluble, brownish or black, and are contained in grass charcoal and lignite with a low degree of coalification, broken seabed soil, etc. The acidity is due to the presence of carboxyl groups and phenol groups, and the chemical equivalent per acid is often 300 to 400 carbon 50.
-65%, hydrogen 4-6%, and the remainder is mostly oxygen, but may also contain nitrogen or iota depending on the source. The humic acid referred to in the present invention includes all humic acids regardless of their origin.

次に除法後のし尿100重量部に対し0.1〜10重量
部のフミン酸を加えた場合(0,1〜10%と表示する
。)第11に示したとおり、フミン酸を0.1%添加す
ると、すでにCODが降下すること、1#添加まではC
ODの降下が続く。10%以上フミン酸を使用すること
は、増分に対する効果が少なく、経済的理由からも好ま
しくない。なお、フミン酸のCOυ降下作用は凝集剤(
第1fcの実線では塩化第二鉄を使用しているが、その
ほか、硫酸アルミニウムなど)の併用により増加する。
Next, when 0.1 to 10 parts by weight of humic acid is added to 100 parts by weight of excreted human waste (expressed as 0.1 to 10%), as shown in No. 11, 0.1 to 10 parts by weight of humic acid is added. % addition, the COD already decreases, and up to the addition of 1#, C
OD continues to decline. Using humic acid in an amount of 10% or more is not preferable for economical reasons since it has little effect on increase. Furthermore, the COυ-lowering effect of humic acid is due to the flocculant (
In the solid line of 1st fc, ferric chloride is used, but it increases when used in combination with other materials (aluminum sulfate, etc.).

混合懸濁液のpnFi、3〜5に保てばCODの降下に
ついて実質的が差異がないが5以上ではCODの降下が
少ないため好ましくない。またpH以下の酸性にすると
、酸に基づく腐食などのトラブルが殖える。
If the pnFi of the mixed suspension is kept between 3 and 5, there will be virtually no difference in the drop in COD, but if it is 5 or more, the drop in COD will be small, which is not preferable. Furthermore, if the pH is lower than the acidity, problems such as acid-based corrosion will increase.

フミン酸は、既述の化学構造から、アニオン凝集剤、ま
たはカチオン交換樹脂と考えられ、し尿中のアミノ基そ
の他のカチオン性官能基と結合して大粒子を形成し沈殿
するものと考えられ、またput−3−5に呆りことは
、例えばタンパク質をその等電点より小さ%1oHIC
してそのアミ7基をカチオン化するのと同様に、し尿の
アミノ基をカチオン化するための条件と推定される。な
お、無機凝集剤はフミン酸の作用と対象的に、懸濁液中
の負の′Tjt#を待った粒子を中和沈降させる効果を
持つ。もち論フミン酸と第二鉄カチオン、アルミニクム
カチオンとの中和反応によって両者の凝縮も起こり、コ
ロイドレベルでのこれらの複雑な中和反応により、結果
的に沈殿が促進される。
Based on the chemical structure described above, humic acid is considered to be an anion flocculant or a cation exchange resin, and is thought to combine with amino groups and other cationic functional groups in human urine to form large particles and precipitate. Also, what is disappointing about put-3-5 is that, for example, if a protein has a %1oHIC smaller than its isoelectric point,
This is presumed to be a condition for cationizing the amino group of human waste in the same way as cationizing the amino group of human waste. In contrast to the action of humic acid, the inorganic flocculant has the effect of neutralizing and settling particles that have reached a negative 'Tjt# in the suspension. Naturally, the neutralization reaction between humic acid and ferric cations and aluminum cations also causes condensation of both, and these complex neutralization reactions at the colloidal level eventually promote precipitation.

フミン酸添加と同時に、凝集剤、特に県濃厚し尿に対し
0.3〜0.5重量%の無機凝集剤例えば塩化第二鉄、
硫酸アルミニクムを加えることに汚濁物質の沈降分離が
容易になる(第1表)。さらに多蝦の使用は一般的に経
済的でない〇 なお除渣したし尿を水で希釈すると、撹拌が容易になり
また配管中を輸送し易いなどのメリットがあるが、浄化
効率すなわち、分離水に移行する全し尿量が増加する。
At the same time as adding humic acid, add a flocculant, especially an inorganic flocculant such as ferric chloride, 0.3 to 0.5% by weight based on the prefecture's concentrated human waste.
Addition of aluminum sulfate facilitates sedimentation and separation of pollutants (Table 1). Furthermore, the use of multiple shrimp is generally not economical.Also, diluting the removed human waste with water has the advantage of making it easier to stir and transport through pipes, but the purification efficiency, that is, the separated water The amount of total human urine transferred increases.

このことから希釈倍率を5倍以上にすることは好ましく
ない。なお、市販フミン酸には酸形のものと、ナトリウ
ム塩形のものがあるが、使用pHが3〜5であることか
ら酸形のものが好ましいことは言うまでもない。
For this reason, it is not preferable to increase the dilution ratio to 5 times or more. It should be noted that commercially available humic acids include those in acid form and those in sodium salt form, but it goes without saying that acid form is preferable since the pH used is 3 to 5.

第      1      表 注(1)  株式会社チルナイト製CH−011に使用
した。
Table 1 Note (1) Used in CH-011 manufactured by Chill Night Co., Ltd.

(2)  マンガン法(JIS KO102Φ17)K
よった。
(2) Manganese method (JIS KO102Φ17)K
Yes.

実施例: @1図において、障渣された濃厚し尿はAから、フミン
酸はフミン酸供袷槽1から、希硫酸は酸貯槽3から、さ
らに必要に応じて凝集剤水溶液が凝集剤貯槽4から、そ
れぞれ所望の混合比になるよう〈流献調節されて、撹拌
機付混合槽2に供給される。2を出た懸濁液はII+離
器5に至り、分離液Bと分離汚泥Cとに分離される。
Example: @1 In Figure 1, blocked concentrated human waste is taken from A, humic acid is taken from humic acid supply tank 1, dilute sulfuric acid is taken from acid storage tank 3, and if necessary, flocculant aqueous solution is taken from flocculant storage tank 4. From there, the flow is adjusted to a desired mixing ratio and supplied to the mixing tank 2 with an agitator. The suspension coming out of 2 reaches II+ separator 5, where it is separated into separated liquid B and separated sludge C.

次に第2図では、混合槽2で原濃厚し尿とフミン酸のみ
を酸貯槽3からの酸によりpH調節して撹拌混合し、分
1lII湿5で上澄液と汚濁物質とに分離し、汚濁物質
の一部を混合槽2に返送し、他部を外部に収出し、上面
分離液全撹拌機付凝集槽7に送入し、7内に必要な場合
さらにpH調節用の酸を酸貯槽3から、必要な場合′#
集剤を凝集剤貯槽4から流域調節して送入して凝集を促
進し、第2分離4ζおいて上澄分離水B2と分離汚泥C
2とに分離する。この第2図の方法は装置がいく分複雑
になるが、分離2!7半が高く・する。
Next, in FIG. 2, in the mixing tank 2, only the raw concentrated human urine and humic acid are mixed by stirring with the pH adjusted with the acid from the acid storage tank 3, and separated into a supernatant liquid and pollutants in a minute 1lII humidity 5, A part of the pollutant is returned to the mixing tank 2, the other part is collected outside, and the upper surface separated liquid is sent to the aggregation tank 7 with a stirrer. From storage tank 3, if necessary'#
A collection agent is fed from the flocculant storage tank 4 while adjusting the flow area to promote flocculation, and in the second separation 4ζ, supernatant separated water B2 and separated sludge C are
Separate into 2. The method of FIG. 2 requires a somewhat more complicated apparatus, but the separation is 2.7 and 1/2 times higher.

発明の効果 上記のとおり、本発明は濃厚し尿のCODを下げる。た
めに、化学的酸化剤を使用することなく、コロイド沈殿
(コロイド中和)を採用することにより高価な酸化剤使
用の必要をなくシ、安価なフミン酸(実際には酸不溶物
である7ムス物質を含んでいても使用可能)で、 CO
D物質を沈殿除去する点に径済面から見た特徴があり、
さらに、塩化鉄、硫酸アルミニウムなどの凝集剤を併用
することにより、その幼果を増すことができる。さらに
沈殿分離した汚濁物・質は、蓬れた肥料、土壊改良剤と
なるので、その経済的7h果は一石二鳥である。
Effects of the Invention As mentioned above, the present invention lowers the COD of concentrated human urine. Therefore, by employing colloidal precipitation (colloidal neutralization) without using chemical oxidizing agents, the need for expensive oxidizing agents is eliminated, and inexpensive humic acids (actually acid-insoluble 7 (can be used even if it contains mus substances), CO
From a cost perspective, it is characterized by the fact that it precipitates and removes substance D.
Furthermore, the number of young fruits can be increased by using a flocculant such as iron chloride or aluminum sulfate. Furthermore, the precipitated and separated pollutants can be used as fertilizer and soil damage improver, so the economical 7-hour effect is to kill two birds with one stone.

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

第1図、第2図ばそれぞれ本発明の実施例の、装置の概
要を併示した流れ図である。 1・・・フミン酸供袷槽、2・・・混合槽ζ 3・・・
酸貯槽、4・・・凝集剤貯槽、5・・・分離器、6・・
・pHメーター、7・・・凝集槽、8・・・第2分離器
。 出願人  抹式会社 り り i’ ”−1代理人  
 中 村 義 −、l・、−5−=、烙1      
 −が
FIGS. 1 and 2 are flowcharts showing an outline of the apparatus according to the embodiment of the present invention. 1... Humic acid supply tank, 2... Mixing tank ζ 3...
Acid storage tank, 4... Coagulant storage tank, 5... Separator, 6...
- pH meter, 7... agglomeration tank, 8... second separator. Applicant: Riri I’”-1 Agent
Yoshi Nakamura -, l・, -5-=, Kaori 1
− is

Claims (1)

【特許請求の範囲】 1 除渣後の濃厚し尿に、フミン酸をその0.1〜10
重量%加え、pHを3〜5の状態で撹拌混合した後、沈
降分離して、分離液と分離汚泥とする濃厚し尿中に含ま
れる汚濁物質を除去する方法。 2 フミン酸とともに凝集剤を添加する特許請求の範囲
第1項記載の方法。 3 凝集剤が、塩化第二鉄および硫酸アルミニウムから
選んだ1以上の物質で、その使用量が濃厚し尿の0.3
〜0.5重量%である特許請求の範囲第2項記載の方法
[Claims] 1. Adding 0.1 to 10% of humic acid to concentrated human urine after sediment removal.
A method for removing pollutants contained in concentrated night soil by adding % by weight and stirring and mixing at a pH of 3 to 5, followed by sedimentation separation to produce a separated liquid and separated sludge. 2. The method according to claim 1, wherein a flocculant is added together with humic acid. 3 The flocculant is one or more substances selected from ferric chloride and aluminum sulfate, and the amount used is 0.3 of the amount of concentrated human urine.
3. The method of claim 2, wherein the amount is 0.5% by weight.
JP60001822A 1985-01-08 1985-01-08 Treatment of night soil Pending JPS61161200A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60001822A JPS61161200A (en) 1985-01-08 1985-01-08 Treatment of night soil

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60001822A JPS61161200A (en) 1985-01-08 1985-01-08 Treatment of night soil

Publications (1)

Publication Number Publication Date
JPS61161200A true JPS61161200A (en) 1986-07-21

Family

ID=11512251

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60001822A Pending JPS61161200A (en) 1985-01-08 1985-01-08 Treatment of night soil

Country Status (1)

Country Link
JP (1) JPS61161200A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0478500A (en) * 1990-07-20 1992-03-12 Nippon Health Kogyo Kk Deodorization method for preventing generation of odorous material from sludge and dehydrated cake after dehydration stage
CN112811761A (en) * 2020-12-23 2021-05-18 山西晋联环境科技有限公司 Method and system for recovering macromolecular substances in sludge

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0478500A (en) * 1990-07-20 1992-03-12 Nippon Health Kogyo Kk Deodorization method for preventing generation of odorous material from sludge and dehydrated cake after dehydration stage
CN112811761A (en) * 2020-12-23 2021-05-18 山西晋联环境科技有限公司 Method and system for recovering macromolecular substances in sludge

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