JP2005289654A - Liquid manure generation method for livestock excreta - Google Patents

Liquid manure generation method for livestock excreta Download PDF

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JP2005289654A
JP2005289654A JP2004102576A JP2004102576A JP2005289654A JP 2005289654 A JP2005289654 A JP 2005289654A JP 2004102576 A JP2004102576 A JP 2004102576A JP 2004102576 A JP2004102576 A JP 2004102576A JP 2005289654 A JP2005289654 A JP 2005289654A
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aeration
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liquid manure
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Mikio Ichiyama
幹雄 市山
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CENTRALSUN KK
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    • 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
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A40/00Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
    • Y02A40/10Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
    • Y02A40/20Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses
    • 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
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a liquid manure generation method for livestock excreta which is great in treatment capability and therefore necessitates a small aeration tank, does not generate malodor and therefore does not require remedies against the malodor at all, unlike the conventional method. <P>SOLUTION: (1) The liquid manure generation method for the livestock excreta comprises spraying a deodorant/fermentation accelerator to a barn, guiding the livestock excreta of the barn to the aeration tank, and performing microair aeration. (2) The liquid manure generation method for the livestock excreta, as described in (1), wherein the aeration tank has an excreta digestion tank provided with a microorganism immobilizing reef and a liquid manure recovering tank and the bottoms of the respective tanks are provided with microair aeration sections. (3) The liquid manure generation method for the livestock excreta, as described in (1) or in (2), wherein the spraying of the deodorant/fermentation accelerator and the microair aeration are performed by automatic control. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

本発明は、畜産排泄物の液肥化方法に関する。   The present invention relates to a method for liquid fertilization of livestock excreta.

畜産排泄物を野積みしたり素掘池で腐熟処理したりすることが原因で、硝酸性窒素などにより地下水が汚染されたり、「クリプトスポリジウム」により水道の水源が汚染されたりして社会問題となっている。農業の分野では、家畜の糞尿や窒素肥料の過剰施肥により硝酸性窒素が発生し、それが植物に移行し、その植物を牛などが食べて硝酸塩中毒を起こすことがある。また、硝酸性窒素が地下に浸透すると地下水の汚染を引き起こし、その水を人が飲むと赤血球のヘモグロビンが破壊されて呼吸困難(チアノーゼ)となる。乳幼児の場合には死ぬこともある。一方「クリプトスポリジウム」は胞子虫類の原虫で、人間や動物の屎尿・糞尿を介して感染し、吐き気、腹痛、発熱、下痢などの症状を引き起こす。通常は10〜14日で治るが抵抗力の弱い人の場合には死ぬこともある。例えば1996年には埼玉県で8800人の集団感染が発生している。
このような状況に対処するため、1999年7月に畜産排泄物の管理の適正化や利用の促進を図る目的で、国により「畜産排泄物の管理と利用促進法」が制定された。
Due to the accumulation of livestock excrement and the ripening treatment in the underground pond, groundwater is contaminated by nitrate nitrogen, etc., and the water source of tap water is contaminated by “Cryptosporidium”. It has become. In the agricultural field, nitrate nitrogen is generated by excessive fertilization of livestock manure and nitrogen fertilizer, which can be transferred to plants, and cows can eat the plant and cause nitrate poisoning. In addition, when nitrate nitrogen penetrates into the ground, it causes groundwater contamination, and when people drink that water, hemoglobin in red blood cells is destroyed, making it difficult to breathe (cyanosis). Infants may die. Cryptosporidium is a spore protozoan that infects humans and animals through manure and manure, causing nausea, abdominal pain, fever, and diarrhea. Usually healed in 10-14 days, but in the case of a person with weak resistance, he may die. For example, in 1996, 8800 outbreaks occurred in Saitama Prefecture.
In order to deal with this situation, the “Law on the Management and Use of Livestock Excrements” was enacted by the government in July 1999 for the purpose of optimizing the management of livestock excretion and promoting its use.

畜産排泄物の多くは堆肥化して用いられているが、堆肥は施用に多くの労力を要するため、耕種農家は施用の楽な化成肥料を選ぶ傾向がある。
そこで、例えば畜産排泄物を何らかの手段で液肥化し動力噴霧装置で緑農地に施用できれば、労力を軽減でき、堆肥プラントに比べて施設の管理も容易で、設備投資も極めて少なくて済む画期的な畜産排泄物の有効利用システムとなるが、まだ実用可能なシステムは開発されていない。
また、汚水の処理法としては表1に示すような方法がある。活性汚泥法や生物膜法は設備コストが非常に高いが、肥料利用(処理後に肥料として利用する方法)の簡易曝気法は非常に安い費用で設置できる。但し、単純なエアレーションのみで処理するためには非常に大きな曝気槽を必要とし、且つ臭気対策が必要になるという問題がある。

Figure 2005289654
なお、表1中のBOD除去率とは、BODの対象となる有機物の除去率のことである。
一方、特許文献1には、本発明で言うマイクロエアーを発生させることができる「空気磁気処理器」に関する考案が開示されており、マイクロエアーが空気の脱臭能力を有し、居室内、冷蔵庫内、自動車の車内などの脱臭に有効であることも記載されている。また、特許文献2(本出願人の出願)には、植物由来の消臭剤兼発酵促進剤(サンインプレス)に関する発明が開示されている。しかしながら、本発明のようにマイクロエアーと消臭剤兼発酵促進剤を組み合わせて畜産排泄物の処理に応用し、従来技術の諸々の問題点を解決することについては何れの文献にも全く開示されていない。 Most of the livestock excrement is used after composting, but composting requires a lot of labor to apply, so cultivated farmers tend to choose chemical fertilizers that are easy to apply.
Therefore, for example, if livestock excrement can be liquefied by some means and applied to green farmland with a power spray device, labor can be reduced, facility management is easier compared with composting plant, and capital investment is extremely small. Although it is an effective use system for livestock excreta, no practical system has been developed yet.
Moreover, there exists a method as shown in Table 1 as a processing method of sewage. The activated sludge method and the biofilm method have very high equipment costs, but the simple aeration method using fertilizer (method to use as fertilizer after treatment) can be installed at a very low cost. However, in order to process only with simple aeration, there exists a problem that a very big aeration tank is needed and the countermeasure against an odor is needed.
Figure 2005289654
In addition, the BOD removal rate in Table 1 is the removal rate of organic substances that are the targets of BOD.
On the other hand, Patent Document 1 discloses a device relating to an “air magnetic processing device” capable of generating micro air as referred to in the present invention. Micro air has a deodorizing ability of air, and is used in a room or refrigerator. It is also described that it is effective for deodorizing the interior of a car. Patent Document 2 (filed by the present applicant) discloses an invention relating to a plant-derived deodorant and fermentation accelerator (Sun Impress). However, it is completely disclosed in any literature about solving various problems of the prior art by applying to the treatment of livestock excrement by combining micro air and deodorant / fermentation accelerator as in the present invention. Not.

実開平1−104147号公報Japanese Utility Model Publication No. 1-104147 特開2003−691号公報JP 2003-691 A

本発明は、処理能力が大きいので小さな曝気槽で済み、悪臭が発生しないので従来のような臭気対策が全く必要ない畜産排泄物の液肥化方法の提供を目的とする。   An object of the present invention is to provide a method for liquid fertilization of livestock excreta that does not require any conventional odor countermeasures because a processing capacity is large and a small aeration tank is sufficient and no bad odor is generated.

上記課題は、次の1)〜3)の発明によって解決される。
1) 畜舎に消臭剤兼発酵促進剤を散布すると共に、該畜舎の畜産排泄物を曝気槽に導き、マイクロエアー曝気を行うことを特徴とする畜産排泄物の液肥化方法。
2) 曝気槽が微生物固定礁を設けた糞尿消化槽と、液肥回収槽とを有し、各槽の底部にマイクロエアー曝気部が設けられていることを特徴とする1)記載の畜産排泄物の液肥化方法。
3) 消臭剤兼発酵促進剤の散布及びマイクロエアー曝気を自動制御で行うことを特徴とする1)又は2)記載の畜産排泄物の液肥化方法。
The above problems are solved by the following inventions 1) to 3).
1) A method for liquid fertilization of livestock excrement, characterized in that deodorant and fermentation accelerator are sprayed on a livestock barn, and livestock excrement in the barn is guided to an aeration tank and microair aeration is performed.
2) The livestock excrement according to 1), wherein the aeration tank has a manure digester tank provided with a microorganism-fixed reef and a liquid manure collection tank, and a micro-air aeration section is provided at the bottom of each tank Liquid fertilization method.
3) The method for liquid fertilization of livestock excreta according to 1) or 2), wherein the deodorant and fermentation accelerator are sprayed and micro air aeration is performed automatically.

以下、上記本発明について詳しく説明する。
本発明は、酸素供給能力の非常に高いマイクロエアーと消臭剤兼発酵促進剤を併用する点に特徴がある。
まずマイクロエアーについて説明する。
空気は、1500ガウス程度以上の強い磁力線の中を20〜30m/sec程度の高速度で通過させると、空気中の酸素分子と単分子の水(水蒸気)のポテンシャルエネルギーが高くなり、分子運動も加速される。このように強い磁力線でポテンシャルエネルギーを高めた空気をマイクロエアーと呼ぶことにする。磁力線強度は、磁性体の飽和磁束密度の制限から最大でも希土類のネオジム磁石で1万ガウス程度であり、空隙に通過させ得る最大磁束密度は、磁路を構成する磁気抵抗で減衰するため凡そ5000ガウス程度となる。マイクロエアー発生で好ましい磁力線強度は2000〜5000ガウスである。
マイクロエアーの発生機構を模式的に示すと図1のようになる。
このマイクロエアーを水中に曝気すると、運動性の高まった酸素分子と単分子の水が、離合集散を繰り返す水分子集団(クラスター)の中に高速度で浸透していき、クラスターを形成する会合分子数を小さくすると同時に水の中に閉じ込められている気体を押し出すので、酸素分子の溶存量(溶存酸素量)が著しく増加する。その結果、水は次の(a)〜(e)のような物性を示すようになる。
(a)クラスターが小さくなる。
(b)二酸化炭素・遊離塩素ガスが除去される。
(c)溶存酸素が増える。
(d)浸透性・濡れ性が高まる。
(e)粘性が下がる。
Hereinafter, the present invention will be described in detail.
The present invention is characterized in that micro air having a very high oxygen supply capacity and a deodorant / fermentation accelerator are used in combination.
First, micro air will be described.
When air passes through strong magnetic lines of about 1500 gauss or higher at a high speed of about 20 to 30 m / sec, the potential energy of oxygen molecules in the air and monomolecular water (water vapor) increases, and molecular motion also occurs. Accelerated. Air in which potential energy is increased by strong magnetic field lines is referred to as micro air. The magnetic field line strength is about 10,000 gauss at the maximum for rare earth neodymium magnets due to the limitation of the saturation magnetic flux density of the magnetic material, and the maximum magnetic flux density that can be passed through the air gap is attenuated by the magnetic resistance that constitutes the magnetic path. It becomes about Gaussian. A preferable magnetic field line strength for generating micro air is 2000 to 5000 gauss.
FIG. 1 schematically shows the micro air generation mechanism.
When this micro air is aerated into water, oxygen molecules with increased mobility and monomolecular water penetrate into the water molecule group (cluster) that repeats dissociation and scattering at high speed, and the associated molecules form clusters. Since the gas confined in the water is pushed out simultaneously with decreasing the number, the dissolved amount of oxygen molecules (dissolved oxygen amount) increases remarkably. As a result, water comes to exhibit the following physical properties (a) to (e).
(A) A cluster becomes small.
(B) Carbon dioxide and free chlorine gas are removed.
(C) Increase in dissolved oxygen.
(D) Improves permeability and wettability.
(E) The viscosity decreases.

図2に、磁路の長さ200mm、1500ガウスの強さの磁力線の中を20m/secの速度で通過させたマイクロエアーについて、曝気時間と溶存酸素濃度との関係を調べた結果を示す。曝気条件は、水量150リットル、水温26℃、曝気量40リットル/分とした。図2の結果について数値的に説明すると、次の(1)〜(3)の通りである。
(1)曝気開始後、DO(溶存酸素濃度)が3mg/l(リットル)に達するのに、マイクロエアーでは1.7分、普通の空気では4分かかった。
(2)曝気開始後、好気性環境として必要なDOである6mg/lに達するのに、マイクロエアーでは5.2分、普通の空気では10.2分かかった。
(3)到達飽和DOは、マイクロエアーが9.6mg/l、普通の空気が8mg/lであった(この点は図示せず)。
上記の結果から、マイクロエアーを水中に曝気した場合、普通の空気を水中に曝気した場合に比べて2倍以上の速さで酸素を供給できることが分る。
FIG. 2 shows the results of examining the relationship between the aeration time and the dissolved oxygen concentration for micro air that has been passed through magnetic lines having a magnetic path length of 200 mm and a strength of 1500 gauss at a speed of 20 m / sec. The aeration conditions were a water volume of 150 liters, a water temperature of 26 ° C., and an aeration volume of 40 liters / minute. The results of FIG. 2 are described numerically as follows (1) to (3).
(1) After starting aeration, it took 1.7 minutes for micro air and 4 minutes for ordinary air to reach DO (dissolved oxygen concentration) of 3 mg / l (liter).
(2) After starting aeration, it took 5.2 minutes for micro air and 10.2 minutes for ordinary air to reach 6 mg / l, which is the DO required for aerobic environment.
(3) The ultimate saturated DO was 9.6 mg / l for micro air and 8 mg / l for ordinary air (this point is not shown).
From the above results, it can be seen that when micro air is aerated in water, oxygen can be supplied at a rate twice or more faster than when ordinary air is aerated in water.

次に、消臭剤兼発酵促進剤について説明する。
本発明では消臭剤兼発酵促進剤を効果的に用いて無臭にする。環境汚染に対する影響も考慮すると、消臭剤兼発酵促進剤としては化成品よりも天然物由来のものの方が好ましく、その具体例としては、前述した特許文献2に開示されたホウセンカから抽出されたもの(商品名「サンインプレス」)が挙げられる。なお、ここで言う発酵促進剤とは、好気性微生物の活性を高める作用を有する物質のことである。
サンインプレスには、消臭効果を有するケンフェノール、クエルセチン(何れもフラボノイド)、微生物活性効果を有するフェルラ酸、植物成長促進効果を有するスコポレチン、抗酸化作用を有するナフトキノン、抗菌作用を有するパラヒドロキシンなどが含まれており、飲酒の口臭、ニンニク臭、体臭、タバコ臭、生ゴミ臭、畜舎臭などの消臭作用の他に微生物活性化作用、即ち発酵促進作用も有するので、本発明に最適である。
即ち、サンインプレスを1日2回程度畜舎の空間に散布すると、畜舎内の臭気が除去されるだけでなく、床に落ちた散布液は床洗いの時に洗い水と一緒に曝気槽に流入し曝気槽内で活躍する好気性微生物の活性を高めるので、臭気のない液肥の製造に有効である。
通常の場合、主要な悪臭成分はアンモニア、硫化水素、揮発性脂肪酸などであるが、嫌気状態(酸欠状態)になると嫌気性微生物が活躍し、これらの悪臭成分が増加する。これに対し、好気状態で処理すれば好気性微生物が活躍し悪臭成分は速やかに分解される。
好気性微生物は、活性が高まるにつれて益々大量の酸素を消費するようになるが、この酸素をマイクロエアー曝気により迅速かつ大量に供給すれば更に好気性微生物の活性を高めることが可能となる。
上記のように、マイクロエアーには空気の脱臭能力があり、サンインプレスには消臭作用や発酵促進作用があるが、以降に説明するように畜産排泄物に由来する畜産汚水は負荷が非常に大きいため、マイクロエアーのみ又はサンインプレスのみで効率よく液肥化することは難かしく、両者を併用して始めて実用可能な液肥化方法となる。
Next, the deodorant and fermentation accelerator will be described.
In the present invention, a deodorant and fermentation accelerator is effectively used to make it odorless. Considering the influence on environmental pollution, the deodorant and fermentation accelerator is preferably a natural product-derived one rather than a chemical product, and a specific example thereof is extracted from the spinach disclosed in Patent Document 2 mentioned above. Products (trade name “Sun Impress”). In addition, the fermentation promoter said here is a substance which has the effect | action which raises the activity of an aerobic microorganism.
Sun Impress includes kenphenol with odor eliminating effect, quercetin (both flavonoids), ferulic acid with microbial activity, scopoletin with plant growth promoting effect, naphthoquinone with antioxidant effect, parahydroxylone with antibacterial effect In addition to the deodorizing action such as bad breath of drinking, garlic odor, body odor, tobacco odor, garbage odor, livestock odor, etc. It is.
That is, when Sun Impress is sprayed twice a day in the barn space, not only the odor in the barn is removed, but also the sprayed liquid that has fallen on the floor flows into the aeration tank together with the washing water when washing the floor. Since the activity of aerobic microorganisms active in the aeration tank is increased, it is effective for producing liquid fertilizer without odor.
Usually, the main malodorous components are ammonia, hydrogen sulfide, volatile fatty acids and the like. However, when anaerobic conditions (oxygen deficient state) are reached, anaerobic microorganisms play an active role, and these malodorous components increase. In contrast, when treated in an aerobic state, aerobic microorganisms are active and malodorous components are rapidly decomposed.
The aerobic microorganisms consume more and more oxygen as the activity increases, and if this oxygen is supplied rapidly and in large quantities by microair aeration, the activity of the aerobic microorganisms can be further increased.
As mentioned above, micro air has the ability to deodorize air, and Sun Impress has a deodorizing action and a fermentation promoting action, but as described later, livestock sewage derived from livestock excrement has a very heavy load. Since it is large, it is difficult to efficiently liquid fertilize only with micro air or only Sun Impress, and it becomes a practical liquid fertilization method only when both are used together.

次に畜産排泄物に由来する畜産汚水の特徴と本発明の関係について説明する。
処理対象となる汚水が生物的処理に適しているかどうかはCOD(化学的酸素要求量)やTOC(全有機炭素量)に対するBOD(生化学的酸素要求量)の比率で判断する。
一般にBOD/COD>1かつBOD/TOC>1ならば、活性汚泥処理などの生物的処理に向いていると言われる。畜産汚水の場合、CODやTOCに対するBODの比率が高いので、生物的処理に適した汚水と言える。
また、一般に浄水処理に適した汚水は、BODを100とした濃度比で、BOD:N:P=100:5:1とされている。下水などはこの濃度比に近いが、畜産汚水は窒素濃度が高く、BOD:N=100:20〜40程度である。BOD:N=100:15程度までならば浄化処理が可能であるが、これよりも窒素の割合が高くなると浄化処理が困難になると言われている。
1日に家畜から排泄される汚濁物質の量の目安は表2に示す通りである。体重60kgの成人の場合、排泄量は1.5(kg/日)、BODの対象となる(BODに影響を与える)有機物量は13(g/日)なので、これに比べると家畜から排泄される汚濁物質の量はかなり多いことが分る。
このように畜産排水は有機物濃度が高い上に含有される有機物の総量も多いので、好気性微生物が充分な活動をするためには大量の酸素が必要であり酸欠状態になり易い。しかしマイクロエアー曝気を行うと前述したように通常の空気の2倍以上の速度で酸素を供給できるので酸欠を起さないで済む。
Next, the relationship between the characteristics of livestock wastewater derived from livestock excrement and the present invention will be described.
Whether the sewage to be treated is suitable for biological treatment is determined by the ratio of BOD (biochemical oxygen demand) to COD (chemical oxygen demand) or TOC (total organic carbon quantity).
In general, if BOD / COD> 1 and BOD / TOC> 1, it is said to be suitable for biological treatment such as activated sludge treatment. In the case of livestock wastewater, the ratio of BOD to COD and TOC is high, so it can be said that the wastewater is suitable for biological treatment.
Moreover, generally the sewage suitable for a water purification process is BOD: N: P = 100: 5: 1 by the density | concentration ratio which made BOD 100. Sewage and the like are close to this concentration ratio, but livestock wastewater has a high nitrogen concentration and is about BOD: N = 100: 20-40. The purification treatment is possible up to about BOD: N = 100: 15, but it is said that the purification treatment becomes difficult when the ratio of nitrogen becomes higher than this.
The standard of the amount of pollutant excreted from livestock in a day is as shown in Table 2. In the case of an adult with a body weight of 60 kg, the amount of excretion is 1.5 (kg / day), and the amount of organic matter subject to BOD (which affects BOD) is 13 (g / day). It can be seen that the amount of pollutants is quite large.
As described above, livestock wastewater has a high organic matter concentration and a large total amount of organic matter contained therein. Therefore, a large amount of oxygen is required for the aerobic microorganisms to perform sufficient activities, and it tends to be deficient in oxygen. However, when micro air aeration is performed, as described above, oxygen can be supplied at a rate twice or more that of normal air, so that no oxygen deficiency occurs.

また、豚のBODの対象となる有機物量をみると、糞114(g/日)、尿18(g/日)であり、糞が88%を占める。同様に豚のSS(水中に浮遊している有機性物質や泥粒などの総称)量をみると、糞418(g/日)、尿16(g/日)であり、糞が97%を占める。このように汚濁物質は圧倒的に糞中に多い。従って、予め家畜排泄物から糞を除去しておけば汚濁物質を大幅に減らすことができ、汚水処理を比較的容易に行うことができるが、このような処理には労力と経費がかかる上に、除去した糞を何らかの手段で処理する必要があるから根本的な解決にはならない。
しかし、本発明ではこのような糞の除去を行う必要は全くない。
また、一般の下水では、BODの対象となる有機物濃度は200mg/l(リットル)前後であるが、家畜糞尿に由来する汚水は数千〜数万mg/lと非常に高い。
豚を例にとると、糞尿混合物中のBODの対象となる有機物濃度は1頭当り24000mg/lである。予め糞の70%を除去したとしても13000mg/lであり、これに1頭当り10〜20リットルの管理水を混合しても2600〜5200mg/l程度にしかならない。従って、通常の活性汚泥法では希釈水を加えて更にBODの対象となる有機物濃度を低減する必要がある。
これに対し、本発明では希釈水は全く不要である。

Figure 2005289654
In addition, when the amount of organic matter that is a target of BOD of pigs is found to be feces 114 (g / day) and urine 18 (g / day), feces account for 88%. Similarly, the swine SS (generic name for organic substances and mud particles floating in water) is feces 418 (g / day), urine 16 (g / day) and feces 97% Occupy. In this way, pollutants are overwhelmingly present in feces. Therefore, if feces are removed from the livestock excrement in advance, pollutants can be greatly reduced, and sewage treatment can be performed relatively easily. However, such treatment requires labor and cost. It is not a fundamental solution because the removed feces must be treated by some means.
However, in the present invention, it is not necessary to remove such feces.
In general sewage, the concentration of organic matter targeted for BOD is around 200 mg / l (liter), but the amount of sewage derived from livestock manure is as high as several thousand to several tens of thousands mg / l.
Taking pigs as an example, the concentration of organic matter targeted for BOD in the manure mixture is 24,000 mg / l. Even if 70% of feces is removed in advance, it is 13000 mg / l, and even if 10-20 liters of control water per head is mixed with this, it becomes only about 2600-5200 mg / l. Therefore, in the normal activated sludge method, it is necessary to add dilution water to further reduce the organic matter concentration that is the target of BOD.
In contrast, in the present invention, no dilution water is required.
Figure 2005289654

牛の糞尿の場合、BODの対象となる有機物量は1頭で800g/日であり、100頭の飼育舎では80kg/日の処理が必要になる。活性汚泥法の処理能力は、BODの対象となる有機物量で、通常0.2kg/m程度であるから、有効面積400mの曝気槽が必要となる。これに対し、本発明は処理能力が少なくとも0.4kg/m程度であり、全く問題なく処理できるので、曝気槽の有効面積は活性汚泥法の半分の200m程度以下で済む。また、マイクロエアーは非常に効率よく水に溶解するので、普通の空気を用いる場合に比べて、少ない曝気風量で充分な好気性環境を維持できる。
本発明の実施の態様の一例について図3〜図6を参照しつつ説明する。図中の数字は寸法(単位mm)である。
図3は、牛舎に本発明を適用した例であり、糞尿の中継ピット及び回収管を介して本発明の曝気システムを付設した状態を示している。(a)は正面からみた断面図、(b)は平面図である。回収管に接続する曝気槽は上部に(好気性)微生物固定礁を設けた糞尿消化槽と液肥回収槽からなり、それらの底部にはマイクロエアー散気管を設け、マイクロエア発生器から送気配管を経由してマイクロエアーを供給する(図では嵩上台の上に散気管を設けた例を示した)。送気配管と散気管の接続部には必要に応じて流量調整バルブを設けてもよい。糞尿消化槽に微生物固定礁を設けることにより好気性微生物の能力がより確実に発揮され、糞尿の無臭分解処理に資することになる。
図4は曝気槽の一例を示す。(a)は正面図、(b)は平面図、(c)は右側面図である。通常、曝気槽は内側を耐水モルタル仕上げした鉄筋コンクリート製とし、ビニール波板などで簡単な上屋を建てる。
図5、図6はサンインプレスの散布ノズルとその配管系統を示しており、図5は概要を示す鳥瞰図、図6は平面図である。自動希釈システム(図示せず)により所定の濃度に希釈したサンインプレスを貯蔵タンクから供給し、動噴(動力噴霧装置、例えば散布用高圧ポンプ)と制御盤で代表される制御機構により自動散布する。
In the case of cattle manure, the amount of organic matter targeted for BOD is 800 g / day for one head, and 80 kg / day of treatment is required for 100 breeding houses. The treatment capacity of the activated sludge method is the amount of organic matter that is the target of BOD and is usually about 0.2 kg / m 3 , so an aeration tank with an effective area of 400 m 3 is required. In contrast, the present invention has a processing capacity of at least about 0.4 kg / m 3 and can be processed without any problem, so that the effective area of the aeration tank is about 200 m 3 or less, which is half of the activated sludge method. In addition, since micro air dissolves in water very efficiently, a sufficient aerobic environment can be maintained with a small aeration volume compared to the case of using normal air.
An example of an embodiment of the present invention will be described with reference to FIGS. The numbers in the figure are dimensions (unit: mm).
FIG. 3 is an example in which the present invention is applied to a barn, and shows a state in which the aeration system of the present invention is attached via a urine relay pit and a collection pipe. (A) is sectional drawing seen from the front, (b) is a top view. The aeration tank connected to the recovery pipe consists of a manure digester tank and a liquid fertilizer recovery tank with an aerobic microorganism fixed reef at the top, and a micro air diffuser pipe at the bottom of the aeration tank and an air supply pipe from the micro air generator (The figure shows an example in which a diffuser tube is provided on the bulkhead). If necessary, a flow rate adjusting valve may be provided at the connection between the air supply pipe and the air diffusion pipe. By providing a microorganism-fixed reef in the manure digester, the ability of aerobic microorganisms is more reliably exhibited, which contributes to the odorless decomposition treatment of manure.
FIG. 4 shows an example of an aeration tank. (A) is a front view, (b) is a plan view, and (c) is a right side view. Normally, the aeration tank is made of reinforced concrete with water-resistant mortar inside, and a simple roof is built with vinyl corrugated sheet.
FIG. 5 and FIG. 6 show a spray nozzle of Sun Impress and its piping system, FIG. 5 is a bird's eye view showing an outline, and FIG. 6 is a plan view. A sun-impress diluted to a predetermined concentration by an automatic dilution system (not shown) is supplied from a storage tank, and is automatically sprayed by a control mechanism represented by a dynamic spray (power spraying device, for example, a high-pressure pump for spraying) and a control panel. .

本発明によれば、マイクロエアーと消臭剤兼発酵促進剤を併用することにより、畜産排泄物の処理能力が非常に大きくなるので従来に比べて小さな曝気槽で済み、悪臭が発生しないので従来のような臭気対策が全く必要ない畜産排泄物の液肥化方法を提供できる。   According to the present invention, the combined use of micro air and a deodorant / fermentation accelerator increases the processing capacity of livestock excrement, so a smaller aeration tank is required compared to the conventional case, and no bad odor is generated. It is possible to provide a method for liquid fertilization of livestock excreta that does not require any odor countermeasures.

以下、実施例及び参考例により本発明を更に具体的に説明するが、本発明は実施例により限定されるものではない。   EXAMPLES Hereinafter, although an Example and a reference example demonstrate this invention further more concretely, this invention is not limited by an Example.

実施例1
飼育数30頭の乳牛の牛舎に対し、図3〜図6に概要を示す曝気システムを構築した。
牛舎の天井にサンインプレス散布用ノズルを設けた。配管の概要は図5、図6に示した通りであり、動噴に接続する塩ビ管(25A)に、1.8m間隔で枝管(15A)を接続させ、この枝管にノズルを設けた。
別に、動噴、即ちサンインプレス散布用高圧ポンプ(1.5kW:40リットル/min at 2Mpa)、サンインプレスの原液自動希釈システム(希釈倍率300倍、原液消費量:8リットル/月)、自動散布制御装置(散布時間:1日2回1分ずつ)、マイクロエアー発生器(3.7kW:3m/min at 0.05Mpa)を設けた。
曝気槽は、内面を耐水モルタル仕上げにした鉄筋コンクリート製で、縦8m、横2m、深さ(有効深さ)2mとし、曝気槽の上屋はビニール波板囲いの木造建屋とした。
床の洗い水と糞尿の総量は3m/日であり、BODは8000ppmであった。
上記曝気システムを稼動して得られた液肥と、処理前の液肥の原料(牛の糞尿)を、容量2リットルのプラスチック容器にそれぞれ1リットル入れ、約1時間後にヘッドスペースガスを測定した。結果を表3に示す。
なお、表中の「においセンサー値」の測定には、ポータブル型においセンサーXP−329(新コスモス電機社製)を用いた。「においセンサー値」はベース値(測定室内空気)の50を減じた値である。「快・不快度」は、表4に示す「9段階式快・不快度表示法」による値である。「ガス濃度」は検知管(ガステック社製)を用いた。NDは不検出(変色なし)を示す。「臭気濃度」は3点比較式臭袋法による値である。3点比較式臭袋法とは、袋を三つ用意し、一つに採取してきた空気、残りの二つに無臭の空気を入れ、6人のパネラーにどれが採取してきた空気かを当ててもらう方法であり、採取してきた空気の濃度を徐々に薄めながら、区別がつかなくなるまで繰り返す方法である。なお、臭気強度と臭気濃度の間には、表5に示すような関係がある。
表3から分るように、本発明の方法で処理して得られた液肥は、各項目について極めて良好な結果を示しており、「臭質」の項に示したように、液肥のにおいは非常に薄く、殆どにおいを感じない程度(かすかにアンモニア臭を感じるが他のにおいは感じない状態)であった。
Example 1
An aeration system as outlined in FIGS. 3 to 6 was constructed for a cowshed with 30 dairy cows.
A nozzle for spraying Sun Impress was installed on the ceiling of the barn. The outline of the piping is as shown in FIGS. 5 and 6. Branch pipes (15A) are connected to the polyvinyl chloride pipe (25A) connected to the moving jet at intervals of 1.8 m, and nozzles are provided on the branch pipes. .
Separately, dynamic injection, that is, a high pressure pump for spraying Sun Impress (1.5 kW: 40 liters / min at 2 Mpa), an automatic dilution system for Sun Impress's undiluted solution (dilution rate 300 times, undiluted solution consumption: 8 liters / month), automatic spraying A control device (spraying time: twice a day for 1 minute each) and a micro air generator (3.7 kW: 3 m 3 / min at 0.05 Mpa) were provided.
The aeration tank was made of reinforced concrete with water-resistant mortar finish on the inner surface. The aeration tank was 8m long, 2m wide and 2m deep (effective depth), and the roof of the aeration tank was a wooden building with vinyl corrugated board enclosure.
The total amount of floor washing water and manure was 3 m 3 / day, and the BOD was 8000 ppm.
One liter of liquid fertilizer obtained by operating the aeration system and the raw material of the liquid fertilizer (cow manure) before treatment were placed in a plastic container having a capacity of 2 liters, and the headspace gas was measured after about 1 hour. The results are shown in Table 3.
For the measurement of the “odor sensor value” in the table, a portable odor sensor XP-329 (manufactured by New Cosmos Electric Co., Ltd.) was used. The “odor sensor value” is a value obtained by subtracting 50 of the base value (measurement room air). “Pleasure / discomfort” is a value according to the “9-step pleasure / discomfort display method” shown in Table 4. For the “gas concentration”, a detector tube (manufactured by Gastec) was used. ND indicates no detection (no discoloration). “Odor concentration” is a value obtained by the three-point comparative odor bag method. The three-point comparative odor bag method prepares three bags, puts air collected in one, odorless air in the other two, and puts the collected air in six panelists. It is a method that repeats until the concentration of collected air is gradually diminished while it becomes indistinguishable. There is a relationship shown in Table 5 between the odor intensity and the odor concentration.
As can be seen from Table 3, the liquid fertilizer obtained by the treatment of the method of the present invention showed very good results for each item, and as shown in the section of “odor quality”, the smell of liquid fertilizer It was very thin and almost no smell (a slight ammonia odor but no other smells).

Figure 2005289654
Figure 2005289654
Figure 2005289654
Figure 2005289654
Figure 2005289654
Figure 2005289654

参考例
実施例1の対象となった牛舎に対し、サンインプレスのみを1日2回1分ずつ散布した場合と散布しなかった場合について、牛舎中央の床上200mmの所の空気をにおいセンサー(実施例1で用いたのと同じ)で測定した。結果を表6に示す。

Figure 2005289654
Reference Example For the barn that was the target of Example 1, the sun impress was sprayed twice a day for 1 minute and when it was not sprayed, and the air at 200 mm above the floor in the center of the barn was smelled (implemented) The same as in Example 1). The results are shown in Table 6.
Figure 2005289654

マイクロエアーの発生機構を模式的に示す図。The figure which shows typically the generation | occurrence | production mechanism of micro air. マイクロエアー曝気時間と溶存酸素量との関係を調べた結果を示す図。The figure which shows the result of having investigated the relationship between micro air aeration time and the amount of dissolved oxygen. 牛舎に、糞尿回収溝を介して本発明の曝気システムを付設した例を示す図。(a)は正面からみた断面図、(b)は平面図。The figure which shows the example which attached the aeration system of this invention to the cowshed through the manure collection groove | channel. (A) is sectional drawing seen from the front, (b) is a top view. 曝気槽を示す図。(a)は正面図、(b)は平面図、(c)は右側面図。The figure which shows an aeration tank. (A) is a front view, (b) is a plan view, and (c) is a right side view. サンインプレスの散布ノズルとその配管系統の概要を示す鳥瞰図。The bird's-eye view which shows the outline | summary of the spray nozzle of Sun Impress, and its piping system. サンインプレスの散布ノズルとその配管系統を示す平面図。The top view which shows the spray nozzle of Sun Impress, and its piping system.

Claims (3)

畜舎に消臭剤兼発酵促進剤を散布すると共に、該畜舎の畜産排泄物を曝気槽に導き、マイクロエアー曝気を行うことを特徴とする畜産排泄物の液肥化方法。   A method for liquid fertilization of livestock excreta, characterized in that a deodorant and fermentation accelerator is sprayed on a livestock barn, and livestock excrement in the barn is guided to an aeration tank and microair aeration is performed. 曝気槽が微生物固定礁を設けた糞尿消化槽と、液肥回収槽とを有し、各槽の底部にマイクロエアー曝気部が設けられていることを特徴とする請求項1記載の畜産排泄物の液肥化方法。   The livestock excrement according to claim 1, wherein the aeration tank has a manure digestion tank provided with a microorganism-fixed reef and a liquid manure collection tank, and a micro air aeration section is provided at the bottom of each tank. Liquid fertilization method. 消臭剤兼発酵促進剤の散布及びマイクロエアー曝気を自動制御で行うことを特徴とする請求項1又は2記載の畜産排泄物の液肥化方法。
The method for liquid fertilization of livestock excrement according to claim 1 or 2, wherein the deodorant and fermentation accelerator is sprayed and micro air aeration is automatically controlled.
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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008174438A (en) * 2007-01-17 2008-07-31 Fujio Goto Sales system including installation of deodorant and liquid fertilizer-producing apparatus, buying out and recovery of degraded and treated liquid, and recycling of the liquid as liquid fertilizer
JP2008179523A (en) * 2007-01-23 2008-08-07 Fujio Goto Apparatus for producing liquid deodorant and liquefied manure using organic sewage such as livestock feces and foodstuff drain as raw material
KR102053381B1 (en) * 2019-04-15 2019-12-09 농업회사법인 인워터솔루션 주식회사 Smart farm interlocking livestock wastewater treatment facility using a micro bubble generator alternately

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008174438A (en) * 2007-01-17 2008-07-31 Fujio Goto Sales system including installation of deodorant and liquid fertilizer-producing apparatus, buying out and recovery of degraded and treated liquid, and recycling of the liquid as liquid fertilizer
JP2008179523A (en) * 2007-01-23 2008-08-07 Fujio Goto Apparatus for producing liquid deodorant and liquefied manure using organic sewage such as livestock feces and foodstuff drain as raw material
KR102053381B1 (en) * 2019-04-15 2019-12-09 농업회사법인 인워터솔루션 주식회사 Smart farm interlocking livestock wastewater treatment facility using a micro bubble generator alternately

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