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JPS5924874B2 - How to purify raw human urine - Google Patents
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JPS5924874B2 - How to purify raw human urine - Google Patents

How to purify raw human urine

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Publication number
JPS5924874B2
JPS5924874B2 JP16169680A JP16169680A JPS5924874B2 JP S5924874 B2 JPS5924874 B2 JP S5924874B2 JP 16169680 A JP16169680 A JP 16169680A JP 16169680 A JP16169680 A JP 16169680A JP S5924874 B2 JPS5924874 B2 JP S5924874B2
Authority
JP
Japan
Prior art keywords
slaked lime
human urine
foam
separated
raw
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
JP16169680A
Other languages
Japanese (ja)
Other versions
JPS5678676A (en
Inventor
忠幸 吉田
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.)
Asahi Kasei Corp
Original Assignee
Asahi Kasei Corp
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 Asahi Kasei Corp filed Critical Asahi Kasei Corp
Priority to JP16169680A priority Critical patent/JPS5924874B2/en
Publication of JPS5678676A publication Critical patent/JPS5678676A/en
Publication of JPS5924874B2 publication Critical patent/JPS5924874B2/en
Expired legal-status Critical Current

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  • Physical Water Treatments (AREA)

Description

【発明の詳細な説明】 本発明は、生し尿の浄化処理に関する。[Detailed description of the invention] TECHNICAL FIELD The present invention relates to a purification process for human waste.

従来、生し尿の浄化処理法としては、処理槽に溜めた生
し尿中に消石灰を投入し、これと生し尿中の溶解成分と
を析出沈殿せしめて液分と沈殿物とに分離する方法が採
られている。
Conventionally, as a method for purifying raw human waste, slaked lime is added to the raw human urine collected in a treatment tank, and this and the dissolved components in the raw human urine are precipitated and separated into liquid and precipitate. It is taken.

このような浄化処理においては、できるだけ短時間に十
分な反応を達成するため、過剰の消石灰を投入するのが
通例である。
In such purification treatments, it is customary to add an excess of slaked lime to achieve a sufficient reaction in as short a time as possible.

しかしながら、未反応消石灰は、沈殿物さ共に廃棄され
るこさになって無駄であるばかりか、この沈殿物は、肥
料原料やその他の原料として利用し得るものであるにも
拘らず多量の未反応消石灰が含まれていてはその有効利
用を図りにくくなるため、一般には、生し尿中の溶解成
分をカルシウム塩や付加物として析出させるのに必要な
化学量論量の1.5〜2倍程度の消石灰を投入している
に過ぎず、必ずしも上記短時間での十分な反応が満足さ
れているとはいい難い。
However, unreacted slaked lime is not only wasted as it is discarded together with the precipitate, but also this precipitate contains a large amount of unreacted lime even though it can be used as a raw material for fertilizers and other raw materials. If slaked lime is included, it will be difficult to utilize it effectively, so in general, the amount is about 1.5 to 2 times the stoichiometric amount required to precipitate dissolved components in raw human urine as calcium salts and adducts. However, it is difficult to say that sufficient reaction in the short time mentioned above is necessarily achieved.

また、沈殿物を得るには、生し尿さ消石灰との混合物を
4〜5時間静置しなければならないため、処理に長時間
を要するばかりか、設置の敷地面積が大きくなる等の欠
点がある。
In addition, in order to obtain the precipitate, the mixture of raw human waste and slaked lime must be allowed to stand for 4 to 5 hours, which not only takes a long time to process, but also has drawbacks such as increasing the installation area. .

上述のような処理方法の他には、本発明者等が先に特公
昭33−685号さして提供した方法が知られている。
In addition to the above-mentioned treatment method, a method previously provided by the present inventors in Japanese Patent Publication No. 33-685 is known.

即ち、生し尿中に金属塩類、石灰乳及び起泡剤を加えて
空気を流入させつつ撹拌混合して気泡を発生させ、この
気泡に固形分を付着浮揚させるこ々によって生し尿を液
さ泡沫さに分離し、泡沫は乾燥して肥料とし、液は稀釈
して下水へ放出する方法である。
That is, metal salts, milk of lime, and a foaming agent are added to raw human urine, stirred and mixed while air is introduced, and air bubbles are generated.The solid content is attached to the air bubbles and floated, thereby turning the raw human urine into a liquid foam. The foam is dried and used as fertilizer, and the liquid is diluted and discharged into the sewage system.

しかしながら、この処理方法における石灰乳は、生し尿
中の溶解成分をカルシウム塩または付加物さして析出さ
せるきいう積極的意味で使用されているのではなく、そ
のアルカリ性による発泡の促進及び生成される炭酸カル
シぐ7ムによる気泡への付着性の向上きいういわば補助
的な意味で用いられているため、投入量も極めて微量で
ある。
However, milk of lime in this treatment method is not used in a positive sense to precipitate dissolved components in human urine as calcium salts or adducts, but rather to promote foaming due to its alkalinity and to produce carbon dioxide. Calcium is used in an auxiliary manner to improve adhesion to air bubbles, so the amount of calcium added is extremely small.

従って、前述の処理力法のように、未反応消石灰の無駄
を生することがない反面、生し尿中の溶存成分の除去が
必ずしも十分なものではなかった。
Therefore, unlike the above-mentioned processing power method, there is no waste of unreacted slaked lime, but on the other hand, the removal of dissolved components in raw human urine is not always sufficient.

本発明者は、このような従来の欠点に鑑みて鋭意研究の
結果、消石灰は親水性が良好であるために気泡に付着し
にくいことを見出し、上記特公昭33−685号の発明
を応用して未反応消石灰の循環利用を可能ならしめ、も
って消石灰の大量投入による生し尿中の溶存成分との短
時間での確実な反応ができるようにすると共に、その連
続処理を可能にしたものである。
In view of these conventional drawbacks, the inventor of the present invention conducted extensive research and discovered that slaked lime has good hydrophilicity and therefore does not easily adhere to air bubbles. This makes it possible to recycle unreacted slaked lime, thereby making it possible to reliably react with the dissolved components in raw human urine in a short time by adding a large amount of slaked lime, and also to enable continuous processing. .

特に本発明による生し尿の連続処理は、消石灰の大量投
入による溶存成分との短時間での確実な反応が成される
ことによって始めて実効あるものとなるのであり、この
消石灰の大量投入は、未反応消石灰の循環利用ができる
からこそ成し得るのである。
In particular, the continuous treatment of raw human waste according to the present invention becomes effective only when a large amount of slaked lime is added to ensure a reliable reaction with dissolved components in a short period of time. This is possible because the reactive slaked lime can be recycled.

即ち本発明は、粗大異物を予め除去した生し尿に、生し
尿中の溶解成分をカルシウム塩または付加物として析出
分離するに必要な化学量論量の3倍以上の消石灰を投入
し、空気を導入しつつ撹拌することによって上記混合物
をエマルジョン化して泡立てた後、これを浮選法により
泡沫部分と液体部分とに分離し、更に分離された液体部
分に含まれる未反応消石灰を沈殿分離し、これを生し尿
と消石灰上の反応系に循環利用する生し尿の浄化処理方
法を提供するものである。
That is, in the present invention, slaked lime in an amount more than three times the stoichiometric amount required to precipitate and separate dissolved components in the human urine as calcium salts or adducts is added to raw human waste from which coarse foreign substances have been removed in advance, and air is removed. After the mixture is emulsified and foamed by stirring while introducing the mixture, the mixture is separated into a foam portion and a liquid portion by a flotation method, and unreacted slaked lime contained in the separated liquid portion is separated by precipitation, The object of the present invention is to provide a method for purifying human waste in which the human waste is recycled and used in a reaction system on human waste and slaked lime.

本発明において、生し尿中の溶解成分をカルシウム塩ま
たは付加物として析出分離するに必要な化学量論量の3
倍以上もの大量の消石灰を投入するのは、生し尿中の溶
解成分と短時間に確実に反応させるためである。
In the present invention, the stoichiometric amount of
The reason why more than double the amount of slaked lime is added is to ensure that it reacts with dissolved components in raw human urine in a short period of time.

このような大量の消石灰が投入された生し尿を空気を導
入しつつ撹拌することにより、生し尿中の脂肪酸蛋白質
、炭酸ガス等の溶解成分は、短時間のうちにほさんど消
石灰と反応してカルシウム塩または付加物きして析出し
、他の固形分と共に微粒子状となって分散し、エマルジ
ョン化され、これが泡立てられて分散微細粒子は泡沫に
付着される。
By stirring the raw human waste into which a large amount of slaked lime has been added while introducing air, most of the dissolved components in the raw human urine, such as fatty acid proteins and carbon dioxide gas, react with the slaked lime in a short period of time. Calcium salts or adducts are precipitated and dispersed together with other solids in the form of fine particles to form an emulsion, which is then foamed and the dispersed fine particles are attached to the foam.

消石灰の大量投入により大量の未反応消石灰が生ずるが
、消石灰は親水性が良好であるためにほとんど泡沫に付
着されないことから、上記泡立てられた生し尿と消石灰
の混合物を浮選法により泡沫部分き液体部分とに分離す
るさ、未反応消石灰は、液体部分に残存するとキキなり
、泡沫に付着された他の固形分とは分離される。
A large amount of unreacted slaked lime is produced by adding a large amount of slaked lime, but slaked lime has good hydrophilic properties and hardly sticks to the foam. During separation into the liquid part, unreacted slaked lime remains in the liquid part and is separated from other solids attached to the foam.

従って、液体部分をある程度静置しておくことにより未
反応消石灰を容易に沈殿分離させることができ、これを
生じ床上消石灰の反応系に循環利用するので、前記消石
灰の大量投入にも拘らず未反応消石灰を無駄にすること
がない。
Therefore, by allowing the liquid portion to stand still to some extent, unreacted slaked lime can be easily precipitated and separated, and this is recycled to the on-bed slaked lime reaction system. There is no waste of reactive slaked lime.

浮選法により分離された泡沫部分は、乾燥して生し尿中
の種々の有機成分を含む固形分を取出すこ七により、肥
料原料やその他の原料として有効利用することができる
The foam portion separated by the flotation method can be dried to extract the solid content containing various organic components from the raw human waste, and can be effectively used as raw materials for fertilizers and other raw materials.

この場合、前述したように未反応消石灰は、はとんど泡
沫に付着されないので、取得された固形分に多量の未反
応消石灰が含まれるこ七によって、その有効利用が妨げ
られるようなことがない。
In this case, as mentioned above, unreacted slaked lime is rarely attached to the foam, so the fact that the obtained solid content contains a large amount of unreacted slaked lime may impede its effective utilization. do not have.

また、本発明において、消臭効果を得るために消石灰と
共に塩化鉄などの鉄化合物を投入することもできる。
Further, in the present invention, an iron compound such as iron chloride may be added together with slaked lime in order to obtain a deodorizing effect.

更に、大量の消石灰の投入のみでも良好な発泡状態が得
られるが、より発泡を促進するためにパインオイル、オ
レイン酸ソーダ、サポニン等の起泡剤を添加するこきも
効果的である。
Further, although a good foaming state can be obtained by simply adding a large amount of slaked lime, it is also effective to add a foaming agent such as pine oil, sodium oleate, or saponin to further promote foaming.

以下、本発明を図面を参照しつつ詳細に説明する。Hereinafter, the present invention will be explained in detail with reference to the drawings.

第1図は、本発明の説明図で、図中1は撹拌機、2は浮
選器、3は泡沫乾燥機、4はサイクロンである。
FIG. 1 is an explanatory diagram of the present invention, in which 1 is an agitator, 2 is a flotation device, 3 is a foam dryer, and 4 is a cyclone.

子す、浄化rべき生し尿は、前述の如き大量の消石灰と
共に撹拌機1に投入される。
The raw human waste to be purified is fed into the stirrer 1 together with a large amount of slaked lime as described above.

この撹拌機1は、モーター5によって回動する翼6及び
空気を強制的に導入するためのポンプ7を有するもので
、投入された生し深さ消石灰を空気を導入しつつ混合し
、これをエマルジョン化する々ともに泡立てるものであ
る。
This stirrer 1 has blades 6 rotated by a motor 5 and a pump 7 for forcibly introducing air.The stirrer 1 mixes the charged slaked lime while introducing air. It emulsifies and foams at the same time.

かくして、生し尿中の脂肪酸、蛋白質、炭酸ガス等の溶
解成分は、消石灰と反応してカルシウム塩または付加物
として析出し、撹拌により他の固形分と共に微細粒子き
なって分散し、エマルジョン化される。
In this way, dissolved components such as fatty acids, proteins, and carbon dioxide gas in raw human urine react with slaked lime and precipitate as calcium salts or adducts, and are dispersed into fine particles along with other solids by stirring, forming an emulsion. Ru.

このようにしてエマルジョン化された生し尿と消石灰の
混合物が泡立てられるこ々により、分散微細粒子は、泡
沫に付着されるっこのようにしてエマルジョン化され泡
立てられた生し尿は、導管8を通じて浮選器2へ送られ
る。
As the mixture of human waste and slaked lime emulsified in this way is foamed, the dispersed fine particles are attached to the foam. Sent to selector 2.

浮選器2は、エマルジョン化され泡立てられた生し尿を
、泡沫部分と液体部分とに分離するためのもので、撹拌
機1から送られてくるエマルジョン化され泡立てられた
生し尿を塔状体11に導入することにより、その液体部
分を受容々器9内に落下収納し、泡沫部分を水面上に浮
揚堆積せしめて塔状体11上部の溢出口10より取り出
すものである。
The flotation device 2 is for separating the emulsified and foamed human waste into a foam portion and a liquid portion. 11, the liquid part falls and is stored in the receiver 9, and the foam part is floated and deposited on the water surface and taken out from the overflow port 10 at the upper part of the tower-like body 11.

受容々器11中の液状部分の上澄液は、排水口12から
排出される。
The supernatant of the liquid portion in the receptor 11 is discharged from the drain port 12.

泡沫部分き分離された液体部分は、生し尿中の溶解成分
及び固形分が十分除去されており、未反応消石灰は親水
性がよいため泡沫に付着されずにこれに混在し、受容々
器9内に沈殿する。
In the liquid part separated from the foam part, the dissolved components and solid content in the human urine have been sufficiently removed, and unreacted slaked lime is not attached to the foam but mixes with it due to its good hydrophilicity, and is transferred to the receptor 9. precipitate within.

沈殿した未反応消石灰は、すり林状の底部によって中央
部に集積され、循環パイプ13を介して再び撹拌機1へ
送られて再利用される。
The precipitated unreacted slaked lime is accumulated in the center by the forest-like bottom, and is sent to the agitator 1 again via the circulation pipe 13 for reuse.

溢出口10には、泡沫乾燥機3が接続されており、ここ
で固形分が付着した泡沫を破泡乾燥した後サイクロン4
によって前記固形分を取得することができる。
A foam dryer 3 is connected to the overflow port 10, where the foam with solid content is broken and dried, and then passed through a cyclone 4.
The solid content can be obtained by:

このように本発明によれば、未反応消石灰を無駄に投棄
したり、これが多量に含まれることによる取得固形分の
有効利用が妨げられることがないばかりか、消石灰の大
量投入及び未反応消石灰の循環利用による効率的な連続
処理が可能きなるものである。
As described above, according to the present invention, not only is it possible to avoid wasteful disposal of unreacted slaked lime or to prevent the effective use of acquired solids due to the presence of a large amount of unreacted slaked lime, but also it is possible to avoid wasteful disposal of unreacted slaked lime and prevent the effective use of acquired solid content due to large amounts of unreacted slaked lime being included. This makes efficient continuous processing possible through cyclical use.

また、浄化作用に優れており、受容々器の排出口より流
出する浄化水のBODは、3500〜4000ppmあ
るから、そのまま下水へ放流するこさができ、シックナ
ーや濾過機が不要さなって設備を大幅に簡略化できる。
In addition, it has an excellent purification effect, and the BOD of purified water flowing out from the outlet of the receptor is 3,500 to 4,000 ppm, so it can be directly discharged into the sewer, eliminating the need for thickeners or filters and reducing equipment. It can be greatly simplified.

実施例 第1図に示される如き装置の受容々器に予め水を充満し
たのち、生し尿100部、消石灰5部、オレイン酸ソー
ダ0.0001部の混合物を80Orpmで回転してい
る撹拌機に導入し、同時に空気を導入した。
Example After filling the receiver of the apparatus shown in FIG. 1 with water in advance, a mixture of 100 parts of human urine, 5 parts of slaked lime, and 0.0001 part of sodium oleate was placed in a stirrer rotating at 80 rpm. air was introduced at the same time.

充分エマルジョン化して泡立てたのち、塔状体下部に導
入した。
After sufficient emulsification and foaming, the mixture was introduced into the lower part of the tower.

エマルジョン中の泡沫は、塔状体内に堆積し、頂部の溢
出口より流出した。
Foam in the emulsion was deposited inside the tower and flowed out through the overflow port at the top.

これを泡沫乾燥機のダクトに導き熱風で乾燥した後サイ
クロンを通して乾燥粉体5部を得た。
This was introduced into the duct of a foam dryer and dried with hot air, and then passed through a cyclone to obtain 5 parts of dry powder.

−力、受容々器内には、未反応の消石灰3.5部が沈殿
した。
- 3.5 parts of unreacted slaked lime precipitated in the receptor.

12時間運転後、(予め受容々型中に充満されいた水が
完全に排出された後)受容々器から排出された浄化水の
BODは約3600ppmであった。
After 12 hours of operation, the BOD of the purified water discharged from the receiver (after the water previously filled in the receiver mold was completely drained) was about 3600 ppm.

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

第1図は、本発明に係る生し尿の浄化処理方法の説明図
である。 1・・・・・・撹拌機、2・・・・・・浮選機、3・・
・・・・泡沫乾燥機−’ 4・・・・・・サイクロン、
5・・・・・・モーター、6・・・・・・翼、・7・・
・・・・ポンプ、8・・・・・・導管、9・・・・・・
受容々器、10・・・・・・溢出口、11・・・・・・
塔状体、12・・・・・・排出口、13・・・・・・循
環パイプ。
FIG. 1 is an explanatory diagram of the human waste purification method according to the present invention. 1... Stirrer, 2... Flotation machine, 3...
...foam dryer-' 4...cyclone,
5...Motor, 6...Wing, 7...
... Pump, 8 ... Conduit, 9 ...
Receptor, 10... Outflow port, 11...
Tower-shaped body, 12...Discharge port, 13...Circulation pipe.

Claims (1)

【特許請求の範囲】 1 粗大異物を予め除去した生し尿に、生し尿中の溶解
成分をカルシウム塩または付加物さして析出分離するに
必要な化学量論量の3倍以上の消石灰を投入し、空気を
導入しつつ撹拌するこさによって上記混合物をエマルジ
ョン化して泡立てた後、これを浮選法により泡沫部分き
液体部分きに分離し、更に分離された液体部分に含まれ
る未反応消石灰を沈殿分離し、これを生し尿さ消石灰と
の反応系に循環利用するこさを特徴とする生し尿の浄化
処理方法。 2 消石灰と共に鉄塩を添加することを特徴とする特許
請求の範囲第1項記載の生し尿の浄化処理方法。 3 消石灰と共に起泡剤を添加することを特徴とする特
許請求の範囲第1項記載の生し尿の浄化処理方法。
[Scope of Claims] 1. Adding at least three times the stoichiometric amount of slaked lime to the human urine from which coarse foreign substances have been removed in advance to precipitate and separate dissolved components in the human urine using calcium salts or adducts, After the above mixture is emulsified and foamed by vigorous stirring while introducing air, this is separated into a foam part and a liquid part by a flotation method, and unreacted slaked lime contained in the separated liquid part is separated by precipitation. A method for purifying raw human waste characterized by recycling and reusing the raw human urine in a reaction system with slaked lime. 2. The method for purifying human waste according to claim 1, characterized in that iron salt is added together with slaked lime. 3. The method for purifying human waste according to claim 1, characterized in that a foaming agent is added together with slaked lime.
JP16169680A 1980-11-17 1980-11-17 How to purify raw human urine Expired JPS5924874B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16169680A JPS5924874B2 (en) 1980-11-17 1980-11-17 How to purify raw human urine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16169680A JPS5924874B2 (en) 1980-11-17 1980-11-17 How to purify raw human urine

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
JP15815977A Division JPS5493852A (en) 1977-12-30 1977-12-30 Method of and device for purifying crude nighttsoil

Publications (2)

Publication Number Publication Date
JPS5678676A JPS5678676A (en) 1981-06-27
JPS5924874B2 true JPS5924874B2 (en) 1984-06-12

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JP16169680A Expired JPS5924874B2 (en) 1980-11-17 1980-11-17 How to purify raw human urine

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103723783A (en) * 2013-11-28 2014-04-16 瓮福(集团)有限责任公司 Method for recovering flotation reagents from phosphorite mineral processing wastewater

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20000018028A (en) * 2000-01-04 2000-04-06 박종순 Waste-water tretment system of foaming generater
CN104148197B (en) * 2014-09-05 2016-06-08 吉首大学 Cyclone type mineral floating disappears foam device

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103723783A (en) * 2013-11-28 2014-04-16 瓮福(集团)有限责任公司 Method for recovering flotation reagents from phosphorite mineral processing wastewater

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