JP2001010885A - Method and equipment for producing water-soluble organic fertilizer - Google Patents

Method and equipment for producing water-soluble organic fertilizer

Info

Publication number
JP2001010885A
JP2001010885A JP21572099A JP21572099A JP2001010885A JP 2001010885 A JP2001010885 A JP 2001010885A JP 21572099 A JP21572099 A JP 21572099A JP 21572099 A JP21572099 A JP 21572099A JP 2001010885 A JP2001010885 A JP 2001010885A
Authority
JP
Japan
Prior art keywords
bubbles
tank
air
water
filter
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
JP21572099A
Other languages
Japanese (ja)
Inventor
Yukihiro Taniguchi
幸弘 谷口
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP21572099A priority Critical patent/JP2001010885A/en
Publication of JP2001010885A publication Critical patent/JP2001010885A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C05FERTILISERS; MANUFACTURE THEREOF
    • C05FORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
    • C05F17/00Preparation of fertilisers characterised by biological or biochemical treatment steps, e.g. composting or fermentation
    • C05F17/40Treatment of liquids or slurries
    • CCHEMISTRY; METALLURGY
    • C05FERTILISERS; MANUFACTURE THEREOF
    • C05GMIXTURES OF FERTILISERS COVERED INDIVIDUALLY BY DIFFERENT SUBCLASSES OF CLASS C05; MIXTURES OF ONE OR MORE FERTILISERS WITH MATERIALS NOT HAVING A SPECIFIC FERTILISING ACTIVITY, e.g. PESTICIDES, SOIL-CONDITIONERS, WETTING AGENTS; FERTILISERS CHARACTERISED BY THEIR FORM
    • C05G5/00Fertilisers characterised by their form
    • C05G5/20Liquid fertilisers
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/141Feedstock
    • Y02P20/145Feedstock the feedstock being materials of biological origin
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/40Bio-organic fraction processing; Production of fertilisers from the organic fraction of waste or refuse

Abstract

PROBLEM TO BE SOLVED: To provide a method enabling cultures using organic fertilizer in view of the fact that much chemical fertilizer has been used in nutricultures, while there has been little organic fertilizer used in such nutricultures. SOLUTION: This method comprises the following practice: raw water is put into a tank 2, a bubbling nozzle 21 is set up at the bottom of the tank and mounted with an air feed tube 22 so as to extend to the outside above the tank, and air is then blown into the nozzle 21; thereby bubbles are filled throughout the tank; in this condition, a biodegradation is carried out by the aid of the bubbles; because bubbles break with time, they are replenished by blowing air into the nozzle for compensation; a filter 23 for breaking bubbles is set up as a device for air vent; when bubbles pass through the filter, they are separated into air and water, the air is vented upward through an exhaust tube 24, while the water falls down; wherein the filter 23 is e.g. a multilayered coarse cloth, being such as to make use of the principle that bubbles break when they pass gradually through meshes; thereby enabling shifting from a system that bubbles are replenished for compensating broken bubbles after bubbles are filled in a tank and part thereof breaks, to the new system as described above that a biodegradation reaction is promised while forcedly breaking bubbles in the tank and steadily converting raw water to bubbles, which are circulated by convection.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は水溶性有機肥料の製
造の方法,製造装置に関する。
The present invention relates to a method and an apparatus for producing a water-soluble organic fertilizer.

【0002】[0002]

【従来の技術】有機肥料においては堆肥,コンポスト,
ぼかし肥料(高級有機質発酵肥料),青草液肥,等の製
造技術があった。有機物を生物分解する方法としては汚
水処理の技術が有ったがこれは捨てる為の技術であり,
利用するための技術ではなかった。
2. Description of the Related Art In organic fertilizers, compost, compost,
There were manufacturing technologies such as blurred fertilizer (high-grade organic fermented fertilizer) and green grass liquid fertilizer. As a method of biodegrading organic matter, there was a technology of sewage treatment, but this is a technology for discarding,
It was not a technology to use.

【0003】[0003]

【発明が解決しようとする課題】養液栽培においては化
学肥料が多く有機肥料による栽培はほとんど無く,何ら
かの方法で有機肥料による栽培が必要であった。
In hydroponic culture, there are many chemical fertilizers and there is almost no cultivation using organic fertilizers, and cultivation using organic fertilizers by some method is required.

【0004】[0004]

【解決するための手段】有機物を泡の状態で生物分解を
させ肥料水を作る。
The organic matter is biodegraded in the form of foam to produce fertilizer water.

【0005】[0005]

【発明の実施形態】以下発明の実施の形態について説明
するが,本発明は平成11年5月25日特許申請人出願
の受付番号29909700192に関連する。基本事
項としては肥料を作るために必要な有機成分を含む原料
水または原料を水に混ぜたものを生物分解により肥料水
を作る。有機物を水に入れるに当たっては,充分に細か
くした物であり,量にあっては通常の流体として取り扱
える範囲内である量とした条件とする。生物分解とは微
生物(菌,菌が出す消化酵素,原生動物等)が有機物を
分解し元素に戻ることを,生物分解と定義する。用語等
は汚水処理分野の技術用語を使用し,用語等の説明は省
略する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The embodiments of the present invention will be described below, but the present invention relates to Japanese Patent Application No. 29909700192 filed on May 25, 1999. As a basic matter, fertilizer water is produced by biodegrading raw water or a mixture of raw water containing organic components necessary for producing fertilizer. When the organic matter is put into water, it must be sufficiently fine and the amount must be within the range that can be handled as a normal fluid. Biodegradation is defined as biodegradation in which microorganisms (fungi, digestive enzymes produced by fungi, protozoa, etc.) decompose organic matter and return to elements. The terms and the like use technical terms in the field of sewage treatment, and descriptions of the terms and the like are omitted.

【0006】 製造の方法の説明...(分解の基礎理論) 有機成分を含む原料水をBOD高濃度のまま生物分解を
させる方法で図3に示す槽に空気を下から吹き込む生物
分解の方法が一般的であるが,この方法では分解に時間
がかかるので分解の速度を上げるためには下記の様な方
法がある。 1 空気を限り無く大量にすれば良い...散水濾床に
移行する 2 槽を細くし高くすれば良い...深槽曝気に移行す
る 3 槽を限り無く細くし傾斜させる...多重曝気に移
行する 1の散水濾床よりもっと多く空気に接触させるには泡に
より濾床を形成すると粒の細かさによる空気との接触面
積は膨大になり,よって分解能力が増大する。有機物に
は通常泡の発つ成分が存在するが不確定要素を含むので
空気を吹き込んで,泡の出来具合をセンサーによりチェ
クし不足であれば泡たて剤を投入するものとする。(カ
ゼイン,ケラチン等50PPM程度になるように) 好気性菌にあっては酸素の量に比例することが考えら
れ,曝気式においては,水中溶存酸素による訳では有る
が取り込める体積で比較すると泡の千分の1以下であ
り,言い換えれば泡で分解する場合は,同じ能力であれ
ば千分の1の空気を送り込めば良いと理論的には成り立
つ。(実質でも百分の1程度) このことは送り込むポンプの小型化,消費する電気量の
大幅な削減で大きく特徴があり,界面活性剤の分解の方
法でもある。(曝気槽でのBOD濃度は200PPM程
度で分解するので,それ以下になるように原水流入量を
常時制御する必要が高濃度有機物の処理ではでてくる) 汚水処理においては過剰曝気(空気を入れ過ぎると逆に
BOD濃度が上がる)があるが,これは有機物が細かく
なった現象で水を捨てる時には重要で全体を分解するに
は当然必要空気が大量にあるほうが良く,水を捨てるた
めには有機物と水を分離する方法を採用しているので,
残された有機物は汚泥と言う名称で別処理されている。
肥料水を作る目的では汚泥と言うものは存在せず,未分
解有機物と言う名称に表現されるべきである。投入され
る有機物により又はその内部組成により遅いものと早い
ものがでる,遅いものは再度原水等に戻して分解を繰り
返す。散水濾床とどこが違うかと言えばろ材があるか無
いかではあるが,ろ材をどんどん小さくした場合は,近
い効果が得られる筈ではあるが小さくすると目づまりを
するので余り小さくは出来ないので,泡式には,かなわ
ない。(通常のろ材は50ミリ程度でありその体積分は
使われ無い部分であり,残りの部分を水が流れる時に,
空気と触れ生物分解をさせる,従って使われる体積を使
わない体積が上回るので余り採用されていない)
Description of the manufacturing method. . . (Basic Theory of Decomposition) A method of biodegrading raw water containing organic components at a high BOD concentration by blowing air from below into the tank shown in Fig. 3 is a general method. Therefore, the following methods are available to increase the decomposition speed. 1 It is sufficient to make the air infinitely large. . . The two tanks that move to the trickling filter bed should be made thinner and higher. . . Shift to deep tank aeration. 3 Make the tank as thin as possible and tilt it. . . Transitioning to Multiple Aerations In order to contact more air than a single trickling filter bed, forming a filter bed with foam increases the contact area with air due to the fineness of the grains and thus increases the decomposition capacity. The organic matter usually contains a component that emits bubbles, but contains uncertainties, so that air is blown in, the quality of the bubbles is checked by a sensor, and if insufficient, a foaming agent is added. (To be about 50 PPM for casein, keratin, etc.) In aerobic bacteria, it is considered that it is proportional to the amount of oxygen. It is less than one-thousandth. In other words, in the case of decomposing with foam, it is theoretically possible to supply one-thousandth of air with the same capacity. This is characterized by the downsizing of the pump to be fed and the drastic reduction in the amount of electricity consumed, and it is also a method for decomposing surfactants. (Because the BOD concentration in the aeration tank decomposes at about 200 PPM, it is necessary to constantly control the inflow of raw water so as to keep it below that in the treatment of high-concentration organic substances.) In the treatment of sewage, excessive aeration (add air) However, this is important when discarding water due to the phenomenon that organic matter has become finer. It is naturally better to have a large amount of air to decompose the whole, and to discard water Since the method of separating organic matter and water is adopted,
The remaining organic matter is treated separately under the name of sludge.
There is no sludge for the purpose of producing fertilizer water, and it should be described as undegraded organic matter. Depending on the organic substance charged or the internal composition, some are late and some are late. If it is late, it is returned to raw water or the like again and decomposition is repeated. The difference from the trickling filter is whether there is a filter medium or not. If the filter medium is made smaller, a similar effect should be obtained, but if the filter medium is made smaller, it will not be too small. I can't match the expression. (Normal filter media is about 50 mm and its volume is not used. When water flows through the rest,
Not used because air is used for biodegradation, so the used volume is greater than the unused volume)

【0007】原料水及び投入する有機物についての説明 どの材料をどの程度の比率で混合するとどのような肥料
が得られるか,肥料としての不足成分はどの材料を入れ
て補うかは植物を栽培する人に委ねる。同じ理由で単独
素材に近い肥料水をどの比率で混合し,どの様に,どの
時期に,どれだけ植物にあたえるのが最良であるかは植
物を栽培する人に委ねる。当然の事ながら栽培をする所
で肥料水を作ることを原則とする。しかしながら肥料を
作る場所が有機物を出す所と言う場合もある,例えば畜
産農家,汚水処理場,食品加工場であったりする。これ
らの場合は高濃度で有機肥料を作るほうが運送するのに
便利である事,又肥料水を加熱殺菌する場合も便利であ
る。勿論堆肥,コンポスト,ぼかし肥料を水に溶きこの
装置に入れて液肥を作ることも可能である。この場合は
分解の確実性,養分の抽出を重視する。このほかに肥料
用の草を栽培しそれを肥料とする方法もある,例えばク
ロバー,レンゲ,等の柔らかいものは有望である。多種
多様の成分の組み合わせが考えられるが装置と方法の提
供迄にとどめる。
Description of raw water and organic matter to be charged [0007] The type of fertilizer that can be obtained by mixing which materials and in what proportion, and which material is used to make up for the insufficiency of fertilizer is determined by the person who grows the plant. Entrust it to For the same reason, it is up to the person who grows the plant to determine what proportion of fertilizer water, which is close to a single material, is best mixed, how, when and how much it is best to feed the plant. As a matter of course, it is necessary to make fertilizer water in the place where it is grown. However, the place where the fertilizer is made may be said to be a place where organic matter is produced, for example, a livestock farm, a sewage treatment plant, or a food processing plant. In these cases, it is more convenient to transport organic fertilizer at a high concentration, and it is also convenient to heat sterilize fertilizer water. Of course, it is also possible to make liquid fertilizer by dissolving compost, compost, and blurred fertilizer in water and putting into this device. In this case, emphasis is placed on the certainty of decomposition and the extraction of nutrients. In addition, there is a method of cultivating fertilizer grass and using it as a fertilizer. For example, soft ones such as clover and vetch are promising. A wide variety of component combinations are conceivable, but only until the provision of equipment and methods.

【0008】分解の装置の説明 ここでは分解に必要な部分のみの装置を図に基づいて説
明する。図1では基本思想を表すもので,槽(2)の中
に原料水を入れ,槽の底の位置に発泡ノズル(21)を
配置し,発泡ノズルに気送管(22)を取り付け,管を
槽の外まで配管し,その管に空気を吹き込むことを表現
し,それにより泡が槽全体に充満した様子を表現した,
この状態で泡の部分で生物分解を行う。泡は時間と共に
潰れるのでその分を空気を吹き込みながら泡を補充す
る。上記方法に空気を抜く装置として泡潰し用のフィル
ター(23)を設け,そこを通ると空気と水に分離さ
れ,空気は排気管(24)を通り上に抜け,水は下に落
ちる。このフィルターは目の荒い布等を多層に配列した
物等で特筆すべき物ではないが,目の間を泡がゆっくり
通ると潰れる原理を利用したものである。これにより泡
を充満した後,泡が潰れる分を補充する方式から,強制
的に潰し原料水をどんどん泡にして対流させながら,分
解反応を待つ方式に移行できる。これにより分解反応時
間の短縮が出来,界面活性剤の分解装置でもある。 発泡ノズルに付いて 発泡ノズルはこの発明の根幹を構成するものなので詳細
に記載する。泡を作る方法の原則は空気と水を混ぜ合わ
せる事ではあるが,どの様にして混ぜ合わせることが,
より確実に,消費電力が少なく,故障が無く,簡易に,
より小さな粒の泡が出来るかが問われる。小さい粒の泡
がこの装置の特徴を発揮するための条件となる,粒が大
きいと,空気との接触面積が少なくなるので,生物分解
性能が落ちる。水中で小さな穴より空気を吹き込む方法
が上記条件を満たす。(かくはん方式も可能ではある
が,消費電力,簡易性において劣る。) このとき所定の泡量を確保する為に小さな穴を多数,寄
せ集めたものが必要で,これを発泡ノズル(21)と仮
称した。小さい穴を多数設ける訳ではあるが穴と穴との
間隔(0.5ミリ程度)も必要で,ただ単に小さい穴で
あれば良いと,言う訳ではない。(水を巻き込む空間) 現実的な素材としては多孔質セラミック、焼結金属,多
孔質ゴム,等があり,金属板等に小さな穴をあけても良
いがどの程度小さく出来るかが問題である。図2では泡
を一旦上に揚げてその泡を槽全体に対流することを表現
した,原料水が泡となり槽の中で対流する装置とし,槽
内全体での分解の均一化をはかる。筒(25),発泡ノ
ズル,気送菅でひとつのポンプとしての機能を構成し,
新しい形のポンプではある。上記項目は別に特許出願済
み,であるので簡単に説明すると,汚水処理で言うとこ
ろのエアーリフトポンプの変形でノズルから先が,泡の
状態になる事により押し揚げ能力が比重比(水対泡)の
割合で,揚程が高くなる原理である。
Explanation of the device for disassembly Here, the device for only the parts necessary for disassembly will be described with reference to the drawings. FIG. 1 shows the basic concept, in which raw water is put in a tank (2), a foaming nozzle (21) is arranged at the bottom of the tank, and a pneumatic pipe (22) is attached to the foaming nozzle. To the outside of the tank and express the blowing of air into the pipe, thereby expressing the foam filled the entire tank.
In this state, biodegradation is performed at the foam. The foam collapses over time, so refill the foam while blowing air. In the above method, a filter (23) for crushing air is provided as a device for bleeding air, through which air and water are separated, the air passes through an exhaust pipe (24) and goes up, and the water falls down. Although this filter is not remarkable because it is a multi-layered array of coarse cloths, it is based on the principle of crushing when bubbles slowly pass between the eyes. In this way, it is possible to shift from a system in which the foam is filled and then supplementing the amount in which the foam is crushed to a system in which the raw material water is forcibly crushed and the convection is made, and the decomposition reaction is waited. As a result, the decomposition reaction time can be shortened, and the device is also a device for decomposing a surfactant. Regarding the foaming nozzle The foaming nozzle forms the basis of the present invention and will be described in detail. The principle of the method of making bubbles is to mix air and water, but how to mix
More reliably, less power consumption, no failures, easier
The question is whether smaller bubbles can be formed. Small-grained foam is a condition for exhibiting the features of this device. Larger-grained foam reduces the biodegradability because the area of contact with air is reduced. A method of blowing air from a small hole in water satisfies the above condition. (The stirring method is also possible, but the power consumption and simplicity are inferior.) In this case, a large number of small holes are required to secure a predetermined amount of foam, and this is required to be combined with the foaming nozzle (21). I tentatively named it. Although a large number of small holes are provided, a space between the holes (about 0.5 mm) is also required, and it is not to say that a small hole is sufficient. (Space for Involving Water) Practical materials include porous ceramic, sintered metal, porous rubber, and the like. A small hole may be made in a metal plate or the like, but the problem is how small the hole can be made. In FIG. 2, a device is described in which the foam is once lifted up and the convection of the foam is performed in the entire tank. The apparatus is configured such that the raw material water becomes a foam and is convected in the tank, so as to uniformize the decomposition in the entire tank. The cylinder (25), foaming nozzle, and pneumatic tube constitute a single pump function,
It is a new shape pump. Since the above items have been patented separately, it will be briefly described that the lift from the nozzle becomes a bubble state due to the deformation of the air lift pump in the case of sewage treatment. It is the principle that the head is increased by the ratio of ()).

【0009】[0009]

【実施例1】基本原理は前記の通り,ではあるが、周り
との関連,が記載されていないのでバケツで入れて,バ
ケツでくみ出せば,出来ない訳ではないが,連続処理の
例を記載する,にあたり製造能力,精度,有機原料の種
類,等により多種多様の装置が考えられ,全部を記載す
ることは出来ないが,代表的なものと,連続式にする為
に必要なものと特殊装置を記載する。(機能上の附加は
色々有る) 図5は分解のフローシート(工程説明図)で,図6の系
統図と併せて装置の説明図とし,記号番号等は連動して
いる。(特に必要の有るもの,のみを記載) この中で粉砕は原料によりいるものといらない物がある
ので二手に分けた。原料を分解するのに泡ポンプ,搬送
するのにも泡ポンプを使い,但し沈殿より以降はエアー
リフトポンプとする。原料槽に空気を送り込んでいるの
は,有機物が余り長い時間,空気無しでおくと,嫌気性
菌が多過ぎて良くないことが多い。(物にもよるが)
(通常8時間) この所は浄化槽,汚水処理とは違う考え方になる。搬送
又は分解の都度泡の検出が必要で気送後所定の時間内に
泡が検出されないと,起泡剤の弁を開けて所定量の起泡
剤を注入する。通常は有機原料に泡の出る成分が,ある
場合が多いが,全てと言う訳でもないのでこの様に記載
した。(起泡剤50PPM程度になるように) 図5図6中nと有るのは色々有ってその最後の番号まで
とする表示とする。図6で通気管を原料槽,泡分解槽を
接続し最後に排気管で大気に放流するが,泡潰し用にフ
ィルターを設けるところに特徴がある。このフィルター
を通る事により泡が潰れる他に悪臭の除去にも役立つ,
菌が悪臭の成分を分解する。(菌による脱臭フィルタ
ー) 泡分解処理槽を段階ごとに増やすこと,分解時間を長く
すること,により分解度は高くなり,どの有機原料を使
うかにより設計する。(ここでは原理のみ) 量との関係も記載しないが設計の範囲と考え省略する。
[Embodiment 1] Although the basic principle is as described above, the relationship with the surroundings is not described, so if a bucket is inserted and extracted with a bucket, it is not impossible to do so. In describing, a wide variety of devices can be considered depending on production capacity, precision, type of organic raw material, etc., and it is not possible to describe all of them. Describe special equipment. (There are various functional additions.) FIG. 5 is an exploded flow sheet (process explanatory diagram), which is an explanatory diagram of the apparatus together with the system diagram of FIG. 6, and the symbol numbers and the like are linked. (Only those that are particularly necessary are described.) Among them, some of the pulverization depends on the raw material, and some are not. A foam pump is used to decompose the raw materials, and a foam pump is used to transport the raw materials. When air is sent into the raw material tank, anaerobic bacteria are often too large if organic matter is left without air for a very long time. (Depending on things)
(Usually 8 hours) This place is different from septic tank and sewage treatment. When foam is required to be detected each time the material is transported or disassembled, and the foam is not detected within a predetermined time after the air supply, the foaming agent valve is opened and a predetermined amount of the foaming agent is injected. Normally, there are many components that produce bubbles in the organic raw material, but this is not always the case. (In order to make the foaming agent about 50 PPM) In FIG. 5 and FIG. 6, “n” is used to indicate that there are various types up to the last number. In FIG. 6, a ventilation pipe is connected to a raw material tank and a foam decomposition tank, and finally discharged to the atmosphere by an exhaust pipe. The feature is that a filter is provided for crushing bubbles. By passing through this filter, the foam will be crushed and it will also help remove bad smells.
Bacteria break down odorous components. (Bacterial deodorizing filter) The degree of decomposition is increased by increasing the number of foam decomposition tanks for each stage and by prolonging the decomposition time, and it is designed according to which organic raw material is used. (Here, only the principle) Although the relationship with the quantity is not described, it is considered as the design range and is omitted.

【0010】[0010]

【実施例2】図7に基づき説明する。この方式は汚水処
理施設等の沈殿槽より直接,有機分(汚泥)を取り出す
方式で泡分解による,肥料を作る事と,汚泥量を極端に
減量する事の,両方を兼ね備える,理想の方式であり,
汚泥処理装置でもある。従来は汚泥を脱水し焼却処分し
ていたが,泡方式の分解技術により,焼却する量を膨大
に削減し,肥料として利用し,地球環境に優しく,理想
的である。汚泥を処理施設に運搬するコスト程度で肥料
が出来るので理想的であり,処理施設の基本構造を変え
ないで設置可能なところに特徴がある。
[Embodiment 2] A description will be given based on FIG. This method is an ideal method that combines the production of fertilizer by foam decomposition with the method of extracting organic components (sludge) directly from the sedimentation tank of a sewage treatment facility, and the extremely reduction of the amount of sludge. Yes,
It is also a sludge treatment device. In the past, sludge was dewatered and incinerated, but the decomposition method of the foam system greatly reduces the amount of incineration and is used as fertilizer, which is environmentally friendly and ideal. It is ideal because fertilizer can be produced at the cost of transporting sludge to the treatment facility, and it can be installed without changing the basic structure of the treatment facility.

【0011】[0011]

【発明の効果】泡状に有機水を形成する事により高濃度
で分解することが出来る。堆肥コンポストの他に短時間
での有機肥料の製造方法が出来た。排水処理施設と組み
合わせる事により汚泥処理装置と有機肥料製造装置の両
方の機能を,ひとつの装置で兼ね備える究極の装置とな
る。当然のことながら畜産排水処理施設,その他の排水
にも同様である。この装置は界面活性剤の分解装置にも
使用できる。
According to the present invention, the organic water can be decomposed at a high concentration by forming the organic water into a foam. In addition to compost compost, a method for producing organic fertilizer in a short time was achieved. By combining with a wastewater treatment facility, it becomes the ultimate device that combines the functions of both a sludge treatment device and an organic fertilizer production device with one device. Naturally, the same applies to livestock wastewater treatment facilities and other wastewater. This device can also be used as a surfactant decomposition device.

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

【図1】本発明の断面図FIG. 1 is a sectional view of the present invention.

【図2】本発明の断面図FIG. 2 is a sectional view of the present invention.

【図3】従来の曝気槽の断面図FIG. 3 is a cross-sectional view of a conventional aeration tank.

【図4】従来の散水ろ床の断面図FIG. 4 is a cross-sectional view of a conventional sprinkling filter bed.

【図5】本発明の分解工程図FIG. 5 is an exploded view of the present invention.

【図6】本発明の系統図FIG. 6 is a system diagram of the present invention.

【図7】本発明の装置と既存汚水処理技術装置との接続
の系統図
FIG. 7 is a system diagram of connection between the apparatus of the present invention and an existing sewage treatment technology apparatus.

【符号の説明】[Explanation of symbols]

1 原料貯蔵槽 11 泡ポンプ 2 分解槽 21 発泡ノズル 22 気送管 23 フィルター 24 排気管 25 筒 26 分解用泡ポンプ 27 放出口 2n 分解槽 3 沈殿分離槽 31 返送ポンプ(エアーリフトポンプ) 4 肥料水貯蔵槽 5 起泡剤槽 51 起泡剤用ポンプ 52 起泡剤用管 53 電磁弁 54 泡感知センサー 60 圧縮機 7 従来水処理施設 DESCRIPTION OF SYMBOLS 1 Raw material storage tank 11 Bubble pump 2 Decomposition tank 21 Foaming nozzle 22 Pneumatic pipe 23 Filter 24 Exhaust pipe 25 Tube 26 Decomposition foam pump 27 Outlet 2n Decomposition tank 3 Precipitation separation tank 31 Return pump (air lift pump) 4 Fertilizer water Storage tank 5 Foaming agent tank 51 Foaming agent pump 52 Foaming agent tube 53 Solenoid valve 54 Foam sensing sensor 60 Compressor 7 Conventional water treatment facility

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 高濃度の有機成分を持つ原料水を気泡化
させ,泡の状態を1定時間維持させることによる,生物
分解反応をさせること,を特徴とする水溶性有機肥料の
製造方法。
1. A method for producing a water-soluble organic fertilizer, comprising subjecting raw water having a high concentration of an organic component to foaming and maintaining a foam state for one fixed time to cause a biodegradation reaction.
【請求項2】 分解槽(2)の中の底面付近に発泡ノズ
ル(21)を取り付け,ノズルには送気管(22)を取
り付けたこと,槽の上部に排気管(24)を取り付け,
管にはフィルター(23)を取り付ける事,を特徴とす
る,水溶性有機肥料の製造装置。
2. A foaming nozzle (21) is attached to the decomposition tank (2) near the bottom thereof, an air supply pipe (22) is attached to the nozzle, and an exhaust pipe (24) is attached to the upper part of the tank.
An apparatus for producing a water-soluble organic fertilizer, wherein a filter (23) is attached to a pipe.
【請求項3】 分解槽(2)の中に筒(25)を底面よ
り少し離して,上方向に取り付け,水面より上まで配置
し,筒の中の下の方に発泡ノズル(21)を取り付け,
ノズルには送気管(22)を取り付けること,槽の上部
に排気管(24)を取り付け,管にはフィルター(2
3)を取り付ける事,を特徴とする,水溶性有機肥料の
製造装置。
3. A tube (25) is mounted in the decomposition tank (2) slightly upward from the bottom surface, slightly apart from the bottom surface, is disposed above the water surface, and a foaming nozzle (21) is provided at the bottom of the tube. attachment,
An air supply pipe (22) is attached to the nozzle, an exhaust pipe (24) is attached to the upper part of the tank, and a filter (2) is attached to the pipe.
3. An apparatus for producing a water-soluble organic fertilizer, comprising:
JP21572099A 1999-06-24 1999-06-24 Method and equipment for producing water-soluble organic fertilizer Pending JP2001010885A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP21572099A JP2001010885A (en) 1999-06-24 1999-06-24 Method and equipment for producing water-soluble organic fertilizer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP21572099A JP2001010885A (en) 1999-06-24 1999-06-24 Method and equipment for producing water-soluble organic fertilizer

Publications (1)

Publication Number Publication Date
JP2001010885A true JP2001010885A (en) 2001-01-16

Family

ID=16677073

Family Applications (1)

Application Number Title Priority Date Filing Date
JP21572099A Pending JP2001010885A (en) 1999-06-24 1999-06-24 Method and equipment for producing water-soluble organic fertilizer

Country Status (1)

Country Link
JP (1) JP2001010885A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102010256A (en) * 2010-06-09 2011-04-13 徐维康 Ferment biological organic liquid fertilizer for aquaculture and preparation method thereof
CN102267839A (en) * 2011-05-19 2011-12-07 浙江天凌农业科技有限公司 Plant organic nutrient solution containing saccharicterpenin and preparation method thereof
US8327581B2 (en) 2006-12-04 2012-12-11 Makoto Shinohara Method for producing biomineral-containing substance and organic hydroponics method

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8327581B2 (en) 2006-12-04 2012-12-11 Makoto Shinohara Method for producing biomineral-containing substance and organic hydroponics method
CN102010256A (en) * 2010-06-09 2011-04-13 徐维康 Ferment biological organic liquid fertilizer for aquaculture and preparation method thereof
CN102267839A (en) * 2011-05-19 2011-12-07 浙江天凌农业科技有限公司 Plant organic nutrient solution containing saccharicterpenin and preparation method thereof

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