JP2007130620A5 - - Google Patents

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JP2007130620A5
JP2007130620A5 JP2005355384A JP2005355384A JP2007130620A5 JP 2007130620 A5 JP2007130620 A5 JP 2007130620A5 JP 2005355384 A JP2005355384 A JP 2005355384A JP 2005355384 A JP2005355384 A JP 2005355384A JP 2007130620 A5 JP2007130620 A5 JP 2007130620A5
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有機物処理機Organic matter processing machine

本発明は、地球規模の環境汚染防止に基づく国際条約批准によるわが国海洋汚染防止法対応の為、又地球環境保全の目的で海上、陸上を問わず有機廃棄物分解処理に係るもので、船舶搭載用、或は陸上施設用であって、排水の浄化と、有機物の水中分解消滅処理で分解水に変え、下水道への排水、有機液肥化への転用等のあらゆる処理に本発明で対応可能な幅広い用途で開発したものであり、地球環境全体から考慮して、省エネルギー、省スペース、無臭、消滅、メンテナンスフリーというあらゆる観点から環境に応じた用途選定ができ、環境保全の大局的観点から大きな役割を果たすものである。 The present invention relates to the decomposing treatment of organic waste on the sea and on land for the purpose of complying with the Japan Marine Pollution Control Act by ratification of international conventions based on the prevention of global environmental pollution, and for the purpose of protecting the global environment. It can be used for on-board or on-shore facilities, and it can be converted to decomposed water by purifying wastewater and decomposing and extinguishing organic matter in water, and can handle all treatments such as draining to sewers and diverting to organic liquid fertilization. It has been developed for a wide range of applications, and considering the global environment as a whole, it can be selected according to the environment from all aspects of energy saving, space saving, odorlessness, extinction, and maintenance-free. It plays a role.

種々の排水浄化と有機物発酵の原点は、酸化分解にあり、自然の河川や湖水も同様であるが、従来から排水浄化には空気散気方式或は空中散水による空気接触、有機物発酵は切り返し大気接触を主としているが、数億年の地球であれば気中酸素は30%近くあったものが、近代では十%少々しか酸素を持たない空気利用したのでは、酸化分解浄化には時間的に限界がある。
また、生ごみ等の有機物処理は、原形生ごみを処理槽に投入し生ごみ貯留槽、発酵槽、熟成貯留槽の堆肥目的とした方式が殆どであり、定期的発酵助成菌を添加して発酵を促進するが、数日単位での残渣排出、保管臭気、そのまま肥料に使用して不作現象となる為、やむを得ず焼却処分が殆どである。
The origin of various wastewater purification and organic matter fermentation is oxidative decomposition, and the same applies to natural rivers and lakes. Conventionally, wastewater purification has an air diffusion method , or air contact by air sprinkling, and organic matter fermentation is turned back. Although mainly have the air contact, if the Earth hundreds of millions of years ago, those aerial oxygen there was close to 30 percent, in than using the air only ten% a little does not have the oxygen is modern, the oxidative decomposition purification There is a limit in time.
Moreover, organic substance treatment of garbage, etc. was charged with original garbage treatment tank, garbage storage tank fermentor system for the purpose of compost maturation reservoir is most regularly fermentation Grant bacteria Fermentation is promoted by adding it, but residue discharge in units of several days, storage odor, as it is used as it is for fertilizer, and it becomes an unproductive phenomenon , so incineration is unavoidable.

また、近年、一槽式の発酵処理機と称する処理機で、分解媒体剤として木粉等の基材を装填し、発酵促進剤を処理槽に投入添加する生ごみの分解処理機が多いが、無機生ごみに近い卵の殻、魚の骨類は全く分解せず、その上残飯も含水炭素で分解不能であり、臭気が発生し、蛆虫の発生すらあり、同時に処理槽内発酵の条件である機械的攪拌方式から、水分保有率も大きい為に高温加熱ヒーター加温によるエネルギーのロスが膨大である。 Moreover, in recent years, there are many garbage decomposition processors that are loaded with a base material such as wood flour as a decomposition medium agent and are added to the treatment tank by adding a fermentation accelerator to the treatment tank, which is called a one-tank fermentation treatment machine. In addition, egg shells and fish bones that are close to inorganic food waste are not decomposed at all, and the remaining rice is indecomposable with hydrous carbon, odors are generated, and even worms are generated. from a certain mechanical stirring system, energy loss due to heating of the high temperature heater to moisture prevalence is large is enormous.

攪拌方式の欠点から、発酵による強烈な複合臭気が発生する為、消臭装置を設置しているが、複合臭的な生ごみ分解臭気は消臭不能に近く、臭気分子は発火ガスでもあり、場合によっては処理機内、或は処理機外部にガス漏洩、火災爆発の要因もはらんでおり、実際に火災・爆発事故の事実もある。   Due to the disadvantage of the stirring method, an intense deodorizing odor due to fermentation is generated, so a deodorizing device is installed, but the combined odor-like garbage decomposition odor is almost impossible to deodorize, and the odorous molecule is also an ignition gas. In some cases, there are gas leaks and fire explosions inside or outside the processor, and there are also facts of fire and explosion accidents.

処理能力の低さから分解媒体材の生ごみの分解に必装填量も極端に多く、当然ながら処理槽も大きくなり発酵促進剤の効果も低減する。 Required loadings to decomposition of garbage decomposition medium material from low processing capability extremely large, also reduces course treatment vessel also increases the effect of the fermentation promoter.

その上、日毎に臭気が増大し、分解度の低さから定期的に3か月前後で処理機内基材と残渣を取り出し、残渣処分迄の期間は保管を要し、又、その取り出し方法に於ても人力による袋詰め等の煩雑さを極め、大型になればなるほど機器の設置スペースを取り、その上攪拌機構に於ても処理槽内の過極条件を軽視して単なる有機物攪拌機的な感覚で製作し、機器の安全性、故障の発生率の大きさ、故障時の復旧修理の困難さから継続使用性がない。 Moreover, the odor increases every day, and the base material and residues in the processing machine are periodically taken out in about 3 months due to the low degree of decomposition, and storage is required until the residue disposal. Unusual complications of bagging due human power can have at the take installation space for the more devices if a large, underestimate over-poles conditions even in the processing tank have at its upper stirring mechanism, just Manufactured as if it were an organic agitator, and there is no continuous use due to the safety of the equipment, the rate of failure occurrence, and the difficulty of recovery and repair at the time of failure.

ましてや、近年、水分蒸散乾燥方式で、有形、又は粉末化して廃棄したり、処理機から撤去物有機肥料の原材料であっても有機肥料には値せず、固形化燃料での発電もエネルギーロスが大きく、又、自然発火の危険性はらんでいる。 Even more, in recent years, in water evaporation drying method, tangible or powdered or discarded, remove material from the processing machine without Ataise the organic fertilizer even raw organic fertilizers, also power generation in the solidified fuel energy Loss is large and there is a risk of spontaneous ignition.

さて、厨房排水の場合、米国の様にディスポーザーで破砕して下水に流すことは法条例違反であるが、現在の中小食品店舗で1日排水量50トン未満は、何の規制もなく濃厚厨房排水はそのまま下水道に放水しており、この浄化に対してはいずこの自治体も苦慮しており、従来の単なる上澄み水の曝気やそれに準じた浄化槽では、大勢を閉める中小企業では資金と場所と維持費において、改善されるきざしはまったくない上、露出された排水経路壁には有害物質の付着と共に、臭気発生の要因ともなっている。 Now, in the case of kitchen wastewater, it is a violation of the law to crush with a disposer and drain it into the sewage as in the United States. However, in current small and medium food stores, less than 50 tons of daily wastewater is concentrated without any restrictions. However, the local government is also struggling with this purification, and in the conventional simple aeration of supernatant water and septic tanks based on it, it is difficult for small and medium-sized enterprises to close the funds, place and maintenance costs. in, on signs is no ameliorated, with adhesion of harmful substances in the exposed drainage path walls, it has also become factors odor development.

特開2001−334238号公報JP 2001-334238 A

まず、有機物の水中分解消滅処理を行った場合は必然的に厨房排水の浄化も付随せずにはいられず、又有機物混入の排水浄化を行った場合は有機物の分解消滅処理は切っても切れない関係にあり、その両者を分離して処理することは片手落ちであり、両者併合処理をすべきであるが、世界的にも、有機物は沈殿撤去か、或は嫌気発酵処理で残渣を撤去するものしかなく、各地の集合住宅での集合処理上では、集合配管の高圧洗浄、集合処理槽殻の発臭問題で共益費用の増大を含めて問題が躍起しているのも、浄化槽知識しかない社が有機物消滅をも安易に想定した反動であろう。 First, the purification of the case of performing water decomposition annihilation process organic matter inevitably kitchen wastewater is also not not but accompanied also when performing the wastewater purification organic contamination off by turning off the decomposition disappearance process of the organic matter located irrelevant, is unfair be processed by separating the both, removal but should the merging process of the two, even globally, organic matter or precipitate removed, or a residue in anaerobic fermentation process In the collective treatment at collective housing in various places, the knowledge of septic tanks is also rising, including the high pressure cleaning of collective pipes and the problem of odor generation of collective treatment tank shells, including an increase in common service costs. would recoil only no company is also easily assumed the organic matter annihilation.

従来の有機性廃棄物発酵処理の場合、有機性廃棄物の処理過程で必然的に起きる加湿発酵分解臭気の発生の為、従来各社は大小各種の消臭装置が付設されているが、複合臭気の為に満足な消臭効果が得られない為、又臭気ガスは可燃性ガスでもあり、高温加熱水分蒸散装置でも高温触媒消臭装置を設置してるために、火災爆発事故まで起きており、ガス燃焼式、処理槽電気加温及び電気加温消臭装置無しで、安全な無臭分解消滅を継続させる事が重要である。 If the fermentation process of the conventional organic waste, for inevitably occurs humidified fermentation decomposition odor generated during processing of organic waste, although conventional companies large and small various deodorization apparatus is attached, combined for satisfactory deodorant effect for the odor can not be obtained, also odor gas is also a flammable gas, in order has established a high-temperature catalyst deodorizing device is also at a high temperature heating water evaporation apparatus, up until fire explosion accident Therefore, it is important to continue the safe odorless decomposition and elimination without the gas combustion type, the electric heating of the treatment tank and the electric heating and deodorizing device.

従来の有機性廃棄物発酵処理には大量の発酵湿度調整基材を要し、発酵による分解媒体剤の水分が多い為にそれを逃げようと処理機の大型化に走り、含水率が大である為の攪拌機トルクの増大による駆動装置の騒音と消費電力の増大という欠点ある。 The fermentation process of the conventional organic waste requires a large amount of fermented humidity control substrate, running in the size of the processing machine to escape it for moisture degradation media agent by fermentation is large, the water content is large Therefore, there is a drawback that the noise of the driving device and the power consumption increase due to the increase of the agitator torque.

従来の有機性廃棄物発酵処理は、適切微妙な水分と温度が必要となり、通常に於ても機械攪拌方式の機能低下の為、特に冬期は大きな加熱ヒーターの設置が条件的につきまとい電力の消費が多大となる物である。 Fermentation of a conventional organic waste is suitable delicate moisture and temperature are required, for hypofunction of mechanical stirring system can have at the normal, especially in winter power haunted installed conditionally large heater der consumption is a thing to be a great deal of Ru.

従来の有機性廃棄物発酵処理の場合、無機性廃棄物の魚の骨、蟹の甲羅、卵の殻等は分解不能と同時に、一般生ごみに於いてでさえも発酵日数を長く要し、処理機の大型化と共に、残渣の処理機からの取り出し保管、焼却処分が必須条件となっている。 In the case of the fermentation process of a conventional organic waste, at the same time fish bone of inorganic waste, crab shell, egg shells, etc. are non-degradable and, even takes a fermentation number of days longer than in the general garbage, along with the increase in the size of the processing machine, taken out of storage from the residue of the processing machine, incineration disposal that has become a prerequisite.

従来の有機性廃棄物発酵処理の場合、有機肥料製造機的感覚で、しかも、ここ7、8年来の環境問題から物真似的に発生したものであり、本発明の基本である海洋汚染防止国際条約批准の為に開発されたものでなく、環境保全の法律遵守的な感覚に乏しく、実地経験の不足から機構、強度に充分な検討がなされていない為、攪拌トルクの増大による攪拌装置等の故障が頻発し、処理機故障の場合は殆どの機構機械加工部品と溶接構造の為に一旦故障発生の場合は処理機本体を製造社工場に持ち帰って修理したり、現地で大工事になる。 If the fermentation process of a conventional organic waste, organic fertilizer production machine sensation, moreover, here 7, 8 years of environmental problems is obtained by mimicry to generation, marine pollution is the basis of the present invention It was not developed for ratification of international treaties, it lacks a sense of compliance with environmental laws, and due to lack of practical experience, the mechanism and strength have not been fully studied. In the case of a processing machine failure, due to most mechanical machined parts and welded structures, once the failure occurs, the processing machine body can be brought back to the manufacturer's factory for repair, or a large-scale construction on site. The

従来の有機性廃棄物発酵処理の場合、船舶に搭載したときに、海洋特有の気象条件と、船舶特有の航海条件により、ピッチング(前後の揺れ)、ローリング(左右の揺れ)、ウオーターハンマー(荒天航行時の船首での波による衝撃)、レシプロメインエンジン・レッドゾーン振動(主機関の常用回転到達迄の過大振動)等々による生ごみ処理機電気制御機器の異常発生、同時に可燃性ガスである臭気分子は、危険性の為に絶対的に船舶搭載は不可能である。 In the case of conventional organic waste fermentation treatment, when mounted on a ship, depending on the weather conditions peculiar to the ocean and the voyage conditions peculiar to the ship, pitching (back and forth shaking), rolling (left and right shaking), water hammer (stormy weather) It is a combustible gas at the same time as abnormalities in the electrical control equipment of the garbage disposal machine due to impacts caused by waves at the bow during navigation), reciprocating main engine, red zone vibration (excessive vibration until the main engine reaches normal rotation), etc. odor molecules, absolutely shipboard because of the risk Ru impossible der.

従来の有機性廃棄物発酵処理のように、有機性廃棄物処理機を実際に使用する厨房担当員の知識経験不足は当然で、処理機内部の基材の過乾燥、過湿度等の判断が目視判断に頼られているため、未経験者による判断誤認による臭気発散、分解不能等々が発生する。 As the fermentation process of the conventional organic waste, lack of knowledge and experience kitchen personnel actually using the organic waste processing machine of course, over-drying of the processor inside the substrate, the determination of such peracetic humidity There because it is relying on visual judgment, odor divergence by determining mistaken by inexperienced person, non-degradable so that that occur.

従来の有機性廃棄物発酵処理の様に、有機性廃棄物の処理機は一定期間毎の定期的に残渣を処理機から排出する必要があり、船舶はもとより、陸上に設置した場合でも撤去残渣保管、処分等の問題が付随している。 Removal As the fermentation process of a conventional organic waste processing machine organic waste must be discharged from the processor periodically residue at regular intervals, even if the ship is the installed well, on land the remaining渣保tube, it is accompanied by a problem of disposal.

従来の有機性廃棄物発酵処理の様に、有機性廃棄物処理機は冬期の北海道のように連日マイナス20℃が続く場合は、電気ヒーター加温エネルギー的に使用不能であり、船舶の場合は特にその航路によっては赤道直下周辺の50℃以上の航路、或は北洋航路等のマイナス20℃極寒気象等々の、地球全域に航路を持つため、如何なる環境にも充分効果を発揮しなければならないが、従来の処理機は、わが国の冬期北海道の気候ですら対応可能な処理機はなく、本州中央の気候、特に春、秋を標準とした気候にしか対応出来ず、連続マイナス10℃の環境でも分解不能、連続プラス50℃での環境下で多大の臭気発生等の欠点がある。 As the fermentation process of a conventional organic waste, organic waste processing machine if the winter Hokkaido as every day minus 20 ° C. followed by a electric heater warming energetically unavailable, the ship in particular 50 ° C. or more routes of equatorial periphery depending on its route when, or Northern minus 20 ° C. coldest weather, etc. of such route, due to its route to earth throughout not exert sufficient effect to any environment shall, but conventional processing machine, rather than winter is the climate of Hokkaido al-enabled can be processing machine of Japan, Honshu center of the climate, especially in spring, not only it can respond to the climate that was standard the autumn, continuous negative 10 also non-degradable at ° C. environment, Ru disadvantage there of great odor such as in the environment of a continuous positive 50 ° C..

従来の有機性廃棄物発酵処理の様に、有機性廃棄物処理機は、攪拌翼が一定個所に装着されており、処理槽内の有機廃棄物の全量をまんべんなく攪拌することは困難であり、攪拌効率のアンバランス等からの臭気発散問題もある。 As the fermentation process of a conventional organic waste, organic waste processing machine, the stirring blade is mounted in a fixed location, it is difficult to agitate the total amount of organic waste in the treatment tank evenly , Ru mower odor divergence problem from the unbalance of stirring efficiency, and the like.

従来の有機性廃棄物の加水加温攪拌粉砕排水処理の場合、濃厚な未分解物質混入破砕水を処理機外に排出することから、排出濾過網の口径を大きくして、全て処理槽下部底に装着されており、破砕有機物流出のために、度々濾過網が目詰まりして処理槽内加水がオーバーフローする事故が頻繁に起きている。 For hydrolysis heated stirring pulverization treatment of waste water prior organic waste, since for discharging a thick undecomposed substances mixed crushed water treatment outside, by increasing the diameter of the exhaust filter screen, the bottom of all treatment tank bottom is mounted on, for outflow of crushed organic matter, an accident which often filtering network processing bath hydro clogged overflows are frequently occurring.

水分蒸散乾燥処理機の場合、只単に攪拌して加熱蒸散乾燥して容積縮小しているだけでそのままでは肥料にもならず、焼却処分しかなく、環境的見地の処理機からは程遠い物で、グローバルな環境対応処理機でない。 For water evaporation drying machine, only simply heated with stirring, evaporation, only dried and reduced in volume, is as it not to fertilizers, there is only incinerated, from processor environmental standpoint by far thing, not a global environment corresponding processing machine.

さて次は、従来の厨房排水を含めた有機物混入排水の浄化槽は、処理槽容積を大きくして可能な限り静と動の「静」のプロセスを採り、できるだけ有機物は沈殿させて上澄み水を処理するものであり、に曝気排水処理にしても上澄み水の散気方式あるが、空気の大半が窒素であり十数%の酸素混入空気で、1メートルから2メートルの深度から浮上する気中酸素の水中溶融は計算不可能なほど小さく、酸化分解、及び好気性菌類の活性にも限界がある。 Next, the conventional septic tank for mixed organic wastewater including kitchen wastewater uses a process of “static” that is as static and dynamic as possible by enlarging the volume of the treatment tank, and processing the supernatant water by precipitating the organic matter as much as possible. is intended to, even if the aeration wastewater treatment on the temporary there is a diffuser system of the supernatant water at ten percent of oxygen entrained air has most of the air is nitrogen, feel floats 2 meters depth from 1 m The melting of medium oxygen in water is so small that it cannot be calculated, and there are limits to oxidative degradation and activation of aerobic fungi.

発酵に使用する分解処理剤も、単なる理論で人体への影響も判明しない各種土壌菌類の発酵助剤を使用する危険性を排除すべきである。   The decomposition treatment agent used for fermentation should also eliminate the risk of using fermentation aids of various soil fungi whose effects on the human body are not revealed by mere theory.

投入される有機性廃棄物は、絶対的に発生量は一定するものではなく、これらの日毎変化する発生量と物質の変化に、機能的に対応すべきであり、そのためには、理論でなく、現場での高度なバイオ知識技術と、それを熟知した物理的流体力学迄必須であるが、厨房等の担当者にそれは絶対的に望めない。 The amount of organic waste to be input is not absolutely constant, and it should be functionally able to respond to these daily changes in production and material. , and bio knowledge technology advanced in the field is essential until physical hydrodynamics that familiar with it, it can not be expected absolutely the person responsible for kitchen or the like.

ディスポーザは破砕目的に開発された機器であるが為に、米国を除く各国の自治体によってはこれを単なる加水破砕して下水に流す目的に利用する事の懸念から、ディスポーザー設置を認めない国及び自治体もあるが、本発明は原形有機廃棄物を直接処理槽に投入すれば良く、排水も濾過網で分解水のみ放水するための発明でも有る。 For although the disposer over is a device that has been developed to crush purpose, because of concerns about possible to use it for the purpose of flow in sewage and mere hydrolysis crushed by local governments of the countries with the exception of the United States, do not allow the disposer installation country and some municipalities, but the present invention may be put original organic waste directly into the processing tank, waste water is also the inventions to discharge water only decompose water in the filtering net.

しかし、複数の厨房、それも遠く離れた厨房から発生する有機廃棄物を、厨房で投入すれば、遠隔地に設置の1基の処理装置に集めて処理するためには、厨房で発生した有機破砕物を、ディスポーザーで破砕して移送ポンプを使用して、処理槽に導入したいが、その目的でのディスポーザー使用も禁止している自治体が、現実にわが国にもある事も記憶すべきである However, if organic waste generated from a plurality of kitchens, which are distant from each other, is thrown into the kitchen, the organic waste generated in the kitchen can be collected and processed in a single processing device installed at a remote location. the crushed material, using crushed and transfer pump in the disposer, is to be introduced into the treatment tank, municipalities forbid the use of the disposer in that purpose, it is also to be stored, which actually also in Japan There is .

また、処理機本体に付属のディスポーザー容認されている自治体で使用するディスポーザーであっても、ディスポーザーで加水破砕されたものを一端タンクに貯留し、それを移送ポンプで目的地に運ぶ方式は、汚水ならいざ知らず、破砕有機物の比重の差から、破砕貯留タンクの水面に浮上したまま沈殿しないもの、或は貯留タンクの底に沈殿して流動しないもの、水中浮遊するものの3種が有り、特に浮上していて移送ポンプに吸われずに浮上堆積した場合には貯留タンクからの臭気発散が非常に大きく、厨房設置が出来ない事も有り、大きな課題で有る。 Also, even if the disposer used in the municipality where the disposer attached to the processing machine body is accepted, the one hydrolyzed by the disposer is stored in one tank and transported to the destination with a transfer pump, There are three types of sewage: one that does not settle while floating on the water surface of the crushing storage tank, the one that does not settle and float on the bottom of the storage tank, and the one that floats in water, When it floats and accumulates without being sucked by the transfer pump, the odor emission from the storage tank is very large, and it may be impossible to install a kitchen, which is a big problem.

これらの課題を解消するのが本発明であり、世界的にも例を視ない物である。 A These challenges solution for extinguishing the present invention, one in which unparalleled in the world.

前記課題を解決するため、本発明は、有機物処理機であって、汚水(5)又は有機廃棄物(6)が含まれるとともに、酸素供給剤又は酸素供給装置(3)によって酸素が供給される槽内処理水(4)が内部に充填される処理槽(2)を有する処理機本体(1)と、前記処理槽(2)の内部に設置された破砕循環水中ポンプ(7)と、を備え、前記破砕循環水中ポンプ(7)のポンプ吐出管(9)から前記槽内処理水(4)中への吐出によって、前記汚水(5)又は前記有機廃棄物(6)が攪拌流動するように構成されていることを特徴とする。In order to solve the above-mentioned problems, the present invention is an organic matter processing machine, which includes sewage (5) or organic waste (6) and is supplied with oxygen by an oxygen supply agent or an oxygen supply device (3). A treatment machine body (1) having a treatment tank (2) filled with treated water (4) in the tank, and a crushing circulating submersible pump (7) installed inside the treatment tank (2). The sewage (5) or the organic waste (6) is stirred and flowed by discharge from the pump discharge pipe (9) of the crushing circulation submersible pump (7) into the treated water (4) in the tank. It is comprised by these.

前記課題を解決するため、本発明の他の構成は、有機物処理機であって、汚水(5)又は有機廃棄物(6)が含まれるとともに、酸素供給剤又は酸素供給装置(3)によって酸素が供給される槽内処理水(4)が内部に充填される処理槽(2)を有する処理機本体(1)と、前記処理槽(2)の外部に設置された槽外破砕循環ポンプ(8)と、を備え、前記槽外破砕循環ポンプ(8)のポンプ吐出管(9)から前記槽内処理水(4)中への吐出によって、前記汚水(5)又は前記有機廃棄物(6)が攪拌流動するように構成されていることを特徴とする。In order to solve the above-mentioned problem, another configuration of the present invention is an organic matter processing machine, which includes sewage (5) or organic waste (6), and oxygen by an oxygen supply agent or an oxygen supply device (3) A processing machine main body (1) having a processing tank (2) filled with treated water (4) in the tank, and an outside tank crushing and circulating pump (4) installed outside the processing tank (2) 8), and the sewage (5) or the organic waste (6) by discharge from the pump discharge pipe (9) of the outside crushing circulation pump (8) into the treated water (4) in the tank. ) Is configured to flow with stirring.

前記した有機物処理機において、前記ポンプ吐出管(9)の先端の向きを変化させることにより、前記槽内処理水(4)の流動攪拌をコントロールするように構成することができる。In the organic substance processing machine described above, the flow stirring of the in-vessel treated water (4) can be controlled by changing the direction of the tip of the pump discharge pipe (9).

前記した有機物処理機において、攪拌時間の設定を、複数の種類に分割させることができる。In the organic substance processing machine described above, the setting of the stirring time can be divided into a plurality of types.

前記した有機物処理機において、前記破砕循環水中ポンプ(7)のモーター発熱部を前記槽内処理水(4)で冷却することで、前記槽内処理水(4)が水温上昇するように構成することができる。In the above organic substance processing machine, the motor heat generating part of the crushing circulation submersible pump (7) is cooled by the in-bath treated water (4), so that the in-bath treated water (4) rises in water temperature. be able to.

前記した有機物処理機において、前記処理槽(2)には、前記槽内処理水(4)に有酸素清水(11)を給水するための清水供給栓(13)が設けられているように構成することができる。In the organic matter processing machine described above, the treatment tank (2) is provided with a fresh water supply tap (13) for supplying aerobic fresh water (11) to the treated water (4) in the tank. can do.

前記した有機物処理機において、前記処理槽(2)内に設けられた槽内水中散気管(15)から、前記槽内処理水(4)にミクロン気泡を供給するように構成することができる。In the organic substance processing machine described above, micron bubbles can be supplied to the in-vessel treated water (4) from the in-vessel water diffusing pipe (15) provided in the treatment tank (2).

前記した有機物処理機において、前記処理槽(2)は、遠隔に配置された貯留槽を備え、前記貯留槽から前記汚水(5)又は前記有機廃棄物(6)が前記処理槽(2)内に投入されるように構成することができる。In the organic matter processing machine described above, the treatment tank (2) includes a storage tank disposed remotely, and the sewage (5) or the organic waste (6) is contained in the treatment tank (2) from the storage tank. It can be configured so that

前記した有機物処理機において、前記処理槽(2)は、厨房等の調理排水の汚水貯留槽であるように構成することができる。In the above-described organic matter processing machine, the processing tank (2) can be configured to be a sewage storage tank for cooking wastewater such as a kitchen.

前記した有機物処理機において、前記処理槽(2)は、産業用排水の汚水貯留槽であるように構成することができる。In the above-described organic matter processing machine, the processing tank (2) can be configured to be a wastewater storage tank for industrial wastewater.

前記した有機物処理機において、前記処理槽(2)内を、菌着床隔壁(43)で多段区切りして、前記槽内処理水(4)が前記菌着床隔壁(43)を通過することで浄化されるように構成することができる。In the organic matter treating machine, the inside of the treatment tank (2) is divided into multiple stages by the bacteria-implanted partition wall (43), and the treated water (4) in the tank passes through the bacteria-implanted partition wall (43). It can be configured to be purified.

また、有機物であるかぎり、その形状にかかわらず、槽内処理水が充填された処理機本体に投入された有機物は全て、発生者最終処理観点から、100%有機液体肥料化に、又は排水を浄化槽で浄化するには、水中で有機廃棄物を分解消滅させるしか無い。 Moreover, as long as it is organic matter, regardless of its shape, all of the organic matter thrown into the main body of the processing machine filled with the treated water in the tank is converted into 100% organic liquid fertilizer or drained from the viewpoint of the final treatment of the generator. to clean the septic tank, there is only to decompose eliminate organic waste in water.

また、槽内処理水、常時攪拌には空気散気管から放出された空気上昇対流と、常時又は定期的及び有機廃棄物の投入時には、処理槽内の分解水を水流攪拌し、添加される有機物分解処理剤で有機性廃棄物の消滅を図るものである。 Further, intracisternal treated water, and air rising convection emitted from the air diffuser tubes in the stirring constantly, at the time of introduction of constantly or regularly and organic waste, the decomposition water in the treatment tank and water stirring, is added It is intended to eliminate organic waste with an organic substance decomposition treatment agent.

同時に、超シンプル化で処理槽内の水流攪拌を起こすには、水中ポンプを投入して吸引と吐出を槽内で行えば、吐出管の自由な向き設定で、円筒型処理槽から四角形型の箱型処理槽、多角形状、或は球体状迄、形状は自由に設定できる。 At the same time, the cause flow agitation in the treatment tank with ultra-simplified, by performing suction and discharge by introducing a submersible pump in the tank, in a free orientation setting of the discharge pipe, four prismatic type from a cylindrical treatment tank The shape can be freely set up to a box-shaped treatment tank, a polygonal shape, or a spherical shape.

つまり解り易く述べれば、従来の合併浄化槽等は有機廃棄物を処理槽の第1槽に流入沈殿させ、その上澄みを次の槽で曝気等によって残存した有機浮遊物を分解清浄化して排水するもので、一定期間毎に第1槽と第2槽等の沈殿物の撤去を要し、経費と労力を要するが、本発明はその第1槽に匹敵し、沈殿の静を逆に動に替え、機械的攪拌軸回転による攪拌翼での攪拌は一切せず、処理槽導入された有機物混入の槽内処理水の中で、水中ポンプの吸引吐出、及び空気酸素を放散して、その加圧空気上昇水流をも利用して常時攪拌と常時酸素供給、それに有機物分解剤の相互作用により残渣無しで、魚骨から卵殻にいたる迄、水中で無臭分解消滅させる物であり、学識者ですら不可能と称するものが、完全に実施例で実現している。 That Stated easy understanding, those conventional septic tanks or the like organic waste is allowed to flow precipitated first tank of the processing tank, draining and decomposed cleaning the organic suspended matter remaining the supernatant by aeration or the like in the next bath Therefore, it is necessary to remove the precipitates such as the first tank and the second tank at regular intervals, which requires cost and labor. However, the present invention is comparable to the first tank, and the movement of the precipitation is reversed. without stirring at the stirring blade by mechanical agitation shaft rotation at all, in the bath in the treated water introduced organic matter mixed into the treatment tank, suction and discharge of water pump, and to dissipate the air oxygen, its It is a scholar who is able to decompose and extinguish odorlessly in water from fish bones to eggshells without any residue by constantly stirring and constantly supplying oxygen using pressurized air rising water flow, and the interaction of organic substance decomposing agents. What is called impossible is fully realized in the embodiment.

例えば魚骨は当然カルシウム属であり現実にカルシウム元素は消滅不可能であるが、カルシウム自体には形成能力はなく、生態蛋白質を含む種々物性によって接着形成しているもので、その有機性の生態蛋白質を含む種々物性を分解することによって、魚骨も卵殻も姿を消すが、元素のカルシウムは目視不能で残存するものである。 For example, although fish bone is naturally Cal Siu beam genus reality Cal Siu arm element is not possible extinction, not forming ability to cull Siu arm itself, which are bonded formed by various properties including ecology protein in, by decomposing various physical properties including the organic ecological proteins, fish bone also eggshell also disappeared, but Cal Siu arm elements is that which remains impossible visually.

これによって、従来方式の全てが必要としている処理槽内充填の基材は全く不要で、槽内に添加する分解処理剤はハンドリングが容易な液体を使用する。   As a result, the base material for filling in the processing tank required by all the conventional methods is completely unnecessary, and the decomposition treatment agent added to the tank uses a liquid that is easy to handle.

また、処理槽内の投入物の100%消滅で残渣が無く、定期的残渣排出の経済的労力は解消される。 Further, 100% residues in disappearance of the input of the processing tank is not economical effort recurring residual渣排unloading is eliminated.

従来の浄化槽残渣のシルトが本発明の排水B.O.D.であり、有機物分解と排水浄化に関しては、浄化第1槽沈殿の未分解物はポンプによって処理槽本体に戻されて再分解し、浄化装置の最終槽からの放水値は、いかようにも可能である。 The silt of the conventional septic tank residue is the wastewater B. of the present invention. O. D. With regard to organic matter decomposition and wastewater purification, the undecomposed matter in the first purification tank is returned to the main body of the treatment tank by a pump and re-decomposed, and the water discharge value from the final tank of the purification device is possible in any way. It is.

また、機械加工がなく機器アッセンブリーのみで摺動部の摩耗交換も無く故障も装着機器故障以外には無く、装着機器部品は信頼性と実績あるメーカー機器を使用することが望ましい。 Further, there is no machining, there is no wear replacement of the sliding part only with the device assembly, and there is no failure other than the failure of the mounted device, and it is desirable that the mounted device parts use reliable and proven manufacturer equipment .

また、水中で分解する事と高濃度溶存酸素水による豊富な酸素供給で酸化分解が促進され、臭気も無い。 Moreover, the fact that degradation in water, oxidative decomposition rich oxygen supply by a high concentration of dissolved oxygen water is promoted, odor free.

また、芯だし等の複雑な機械調整部位は全く無く、超シンプルで、乾式発酵方式の様な攪拌トルクの大きな変化によって発生する機器破損摩耗も無く、何時も同じ槽内分解水のポンプ攪拌のみ行うもので有り、省エネルギーとなる。 In addition, there are no complicated mechanical adjustment parts such as centering, ultra-simple, no equipment damage and wear caused by large changes in stirring torque as in the dry fermentation method, and only pump stirring of the same cracked water in the tank at any time. It is a thing and energy saving.

また、省スペースで、超シンプル機構により、使用担当者の機器知識の必要は全くなく、異物投入を避けて分別のみを行えば良い。 In addition, in a space-saving, by the ultra-simple mechanism, without any need of equipment knowledge of the use person in charge, may be performed separation only to avoid the foreign matter is turned on.

また、破砕循環水中ポンプの場合には槽内処理水によるポンプモーターの冷却で、ヒーターを果たして水温が上昇し、分解促進にもなり、処理槽の槽壁を断熱層囲えば、極寒冷地でも、ヒーターによる加温の必要がなく、省エネルギーである。 Further, in the cooling of the pump motor by intracisternal treated water in the case of crushing the circulation water pump, the water temperature rises to play a role of the heater, becomes the decomposition accelerator, if Kakoe the bath wall of the processing tank with an insulating layer, even in very cold climates, there is no need for heating due to the heater, which is energy-saving.

また、処理槽内の槽内分解水攪拌は水流攪拌である為にポンプ吐出口の向きで如何なる形状の処理槽の使用も出来、設置場所に適した種々の形状が可能であり、又種々の既存容器の利用可能である。 In order stirred tank in degradation water in the processing bath is a water flow agitation, use of the processing tank of any shape in the direction of the pump discharge opening can also, but may be various shapes suitable for the installation site, and Various existing containers can also be used.

また、排水濾過網の網目も小さくすみ、槽壁の水面に装着されて槽内分解水攪拌対流摩擦清掃されて付着物もなく、排水詰まり現象も無く、万一には排水濾過網の処理槽壁外側、空気水中散気管によって定期的散気による水面造波で摩擦洗浄を行い、排水濾過網の目つまりはまったくない。 Further, only a small also mesh drainage filter screen, deposits the water surface are mounted at a stirring convection intracisternal decomposed water is friction cleaning tank wall without any drainage clogging phenomenon without the emergency drainage filtering net in a processing tank wall outside, the air-water diffusion pipe performs friction washed at regular by that water surface wave the diffuser, clogging of the drainage filter screen is no.

また、有機廃棄物の投入もディスポーザーを使用せずに原形投入を行い、ポンプ吸引口の外側で、又インペー軸とポンプ吸引口との吸引空間間隙に吸引口間隙破砕刃の単独或は併合装着で、大きな有機物による吸引口閉鎖を防止する。 Further, performs original introduced without a disposer also introduction of organic waste, outside of the pump suction port, and impeller La chromatography axis alone of the suction gap crushing blades in the gap of the suction space and the pump suction port Or it can be attached together to prevent the suction port from being closed by large organic substances.

また、分解発酵処理剤も食品発酵菌と酵素群で至極安全で、食品取扱上での最大な安全性を確保する。 In addition, the decomposition fermentation treatment agent is extremely safe with food fermenting bacteria and enzymes, ensuring maximum safety in food handling.

また、屋外設置の処理機本体に複数の場所が異なる遠隔の厨房で投入された有機廃棄物は、従来の加水破砕ポンプでの移送ディスポーザーでも良いが、ディスポーザーに変わって、破砕攪拌水中ポンプ、又は槽外破砕攪拌ポンプでの破砕自動移送可能にし、有機物貯留移送タンクに、破砕移送の為の水を注入すれば、遠隔の厨房から処理機本体までの破砕移送導入も出来、格安の移送機器も可能であり、ポンプでありながら有機物貯留移送タンク内の軽質浮上残留物も底面沈殿物も吸引し、タンク内の残存物を皆無にして、残留堆積発酵臭気を防止する。 Further, the processing machine body outdoor installation, organic waste plurality of locations have been introduced by different remote kitchen may be transported disposer of the conventional hydro fracturing pump, but changes the disposer, crushing stirred water pump, Or, automatic crushing with an outside tank crushing agitation pump is possible, and if water for crushing transfer is injected into the organic matter storage and transfer tank, crushing transfer can be introduced from a remote kitchen to the main body of the processor, and cheap transfer Equipment is also possible, and while it is a pump, it draws both light floating residue and bottom sediment in the organic matter storage and transfer tank, eliminating any residue in the tank and preventing residual sedimentary fermentation odor.

なお、従来の常識を破らなければ出来ない、わが国を含めて、世界の全メーカーにもない、次の問題点がある。 In addition, there are the following problems that cannot be done without breaking conventional common sense, which is not found in all manufacturers in the world including Japan.

1点目は、従来の水中ポンプは、処理槽の底部位で散気管によって気泡放出する中で、水中ポンプによって吸引すれば当然気泡を吸い込み、同時に水中ポンプの空気抜き孔は繊維素含有の大小形状の有機物によりすぐ閉鎖状態になり、通称エアーブロック現象、つまり水中ポンプのポンプインペラーに空気が溜まり吸引不能でポンプ機能は停止し、吐出ゼロとなり、処理槽内の水流攪拌は停止するのは当然であり、実際に体験した。 The first is the conventional water pumps, among which release bubbles by diffusing pipe at the bottom portion of the processing tank, naturally draws air bubbles if the suction by the water pump, at the same time air vent hole in the water pump of the cellulose-containing The organic substance of large and small shapes immediately closes, so-called air block phenomenon, that is, the air impinges on the pump impeller of the submersible pump, the pump function stops when the suction is impossible, the discharge becomes zero, and the water flow stirring in the treatment tank stops is a matter of course, was actually experienced.

この解決策は現在では世界中のポンプメーカーにも全く無く、特に下水貯留の水中ポンプ汲み上げの排水槽では、貯留水の汲み上げを一定水位で停止させ、残量を多くして、水中ポンプの吸引口からの空気吸い込みを未然に防止するしかなく臭気防止の為にも酸素供給散気管を設置したくても出来ないのが現状である。 This solution, at all without the pump manufacturer in the world at present, especially in the drainage tank of pumping water pump of the sewage reservoir, the pumping of the stored water is stopped at a constant level, by increasing the remaining amount, the water pump not only to prevent the intake air from the suction port in advance, can not I even want to set up the oxygen supply diffuser tubes also for odor prevention is the status quo.

そこで、従来の常識打破、清水用水中ポンプならいざ知らず、汚物水中ポンプの空気抜き孔は、有っても意味が無いばかりか、逆に災いの基でも有り、空気を吸わなくても必然的に空気抜き孔を汚物が通過する事によって繊維素が次第に詰まって、ポンプインペラーを圧迫し、最後には起動不能で停止した例の経験から、空気抜き孔を閉鎖する事によって空気抜き孔の通過水が無くなり、従って、空気抜き孔の詰まりによる種々の災い要因も当然無くなった。 So, to break the conventional wisdom, not knowing emergency if fresh water for the water pump, air vent hole of the waste water pump is, not only does not make sense to there, there is also a group of woe to the contrary, even without breathe air inevitable As a result of the example of the case where the filaments gradually clogged by passing dirt through the air vent hole, the pump impeller was compressed, and finally the pump could not be started and stopped, the air passing through the air vent hole was closed by closing the air vent hole. Therefore, various disaster factors due to clogging of the air vent holes are naturally eliminated.

しかし、汚物・汚水水中ポンプの設置方法を、従来常識の垂直の直立設置を止めて、仮に空気を吸っても吐出する様に、水中ポンプ吐出口を傾斜頂点側にして設置して、傾斜角度は約20度前後以上傾斜する事によって、ポンプ吸引口から吸い込まれた空気気泡は、ポンプインペラーの回転によってポンプ吐出口に排出され、空気吸い込みによる機能停止を防除する事に成功したものである。 However, the installation method of the sewage / sewage submersible pump is installed with the submersible pump discharge port at the top of the tilt so that it can be discharged even if air is sucked by stopping the conventional vertical installation, and the tilt angle it is by inclined approximately 20 degrees before and after the above, the bubbles of air sucked from the pump suction port is discharged to the pump discharge port by rotation of the pump impeller, in which succeeded in controlling outages by suction air .

大きな面積の出し昆布の生ゴミの様に、ポンプ吸引口を塞ぐ大きな有機物への対応は、水中ポンプのインペラー軸をポンプ吸引口の外部迄延長し、その先端には種々形状のポンプ吸引口破砕刃を装着し、軽質のキャベツの葉っぱの様な浮上物は、ポンプ吸引口を水面に向けて倒立設置によって、つまり逆立ち状態で、水面とポンプ吸引口との距離は水中ポンプ能力によって代わるが、1馬力の0.75kw/hの水中ポンプの場合は約250mm前後が適当であり、ポンプ吸引で浮上有機物は順次ポンプに引き込まれ、逆に沈殿有機物はポンプ吐出管を処理槽底に向けて吐出する事によって強制的に水流で処理槽内を上昇遊泳して攪拌が有効に行え分解速度が上昇する。 Corresponding to large organic matter that closes the pump suction port, such as raw garbage from a large area of kelp, extends the impeller shaft of the submersible pump to the outside of the pump suction port, and crushes the pump suction port of various shapes at the tip Floating objects such as light cabbage leaves attached with blades are placed upside down with the pump suction port facing the water surface, that is, in the inverted state, the distance between the water surface and the pump suction port varies depending on the submersible pump capacity, In the case of a 0.75 kw / h submersible pump with 1 horsepower, approximately 250 mm is appropriate, and the floating organic matter is sequentially drawn into the pump by pump suction, and conversely, the precipitated organic matter is discharged toward the bottom of the treatment tank. By doing so, the water can be forcibly swallowed up in the treatment tank and agitation can be effectively performed, and the decomposition speed can be increased.

しかし、沈殿有機物の大きさ比重質量から、ポンプ吐出管を処理槽底に向けて吐出しても、浮上遊泳しない有機物がある場合は、別途水中ポンプのポンプ吸引口の外迄延長したインペラー軸の先端にポンプ吸引口破砕刃付きの水中ポンプを前述の様に約20度前後傾斜させてポンプ吐出口を処理槽形状に合わせて向ければ、如何なる有機物が混入しても、完全な攪拌可能で問題はまったくない。 However, if there is organic matter that does not float and float even if the pump discharge pipe is discharged toward the bottom of the treatment tank due to the size specific gravity of the precipitated organic matter, the impeller shaft extended to the outside of the pump suction port of the submersible pump separately. If a submersible pump with a crushing blade at the tip of the pump is tilted about 20 degrees as described above and the pump discharge port is oriented to the shape of the treatment tank, complete mixing is possible regardless of any organic matter mixed in. There is no problem.

本発明は、処理槽内はバイオ添加の水のみで、従来の発酵処理の様に、大量の基材装填の必要がない。 This onset Ming, the processing tank water only bio addition, as in the conventional fermentation process, there is no need of a large amount of substrate loaded.

本発明は、投入する有機廃棄物の水切り等の制約は全くない。 This onset Ming, no restriction of the draining of the organic waste to be introduced.

本発明は、ポンプ吐出圧力による水流攪拌で、如何なる機械的攪拌の必要も無い為に、故障要因が全くなくなり、特に省エネルギー小型ポンプで良い。 This onset Ming, a water-jet agitation due to the pressure of the pump discharge, for there is no need of any mechanical agitation, completely eliminates the failure factors, in particular may be a small pump of energy saving.

本発明は、非常に効率が良いことから小型化が可能であり、50kg/日の処理能力機種は縦形円筒形で直径1m弱,高さ1m熟の処理槽で十分な大きさで、小型化、省スペースである。 This onset Ming are capable of very compact since efficient processing capacity models 1m diameter slightly less than vertical cylindrical 50 kg / day, large enough in the processing tank height 1m ripe, small And space-saving.

本発明は、冬期寒冷地設置の場合は、電気的加温の必要が無く、極寒地の場合でも、水冷の水中ポンプモーターの発熱エネルギーで槽内の処理水温度は十分に上昇し、電力ヒーター設置する必要は全く無い。 This onset Ming, in the case of installation in winter in cold areas, electrical warming without the need for, even if the cold land, the temperature of the treated water in the tank at heating energy of water cooled submersible pump motor is sufficiently There is no need to install a power heater.

本発明は、攪拌方式が槽内空気放出による分解水上昇対流攪拌とポンプ吐出による加圧水流の為、槽内吐出し管の方向性だけで、如何なる形状の処理槽形状でも水流攪拌は瞬時に可能であり、機械的攪拌翼による軸受け、シール、ベアリング等々の摺動部品が無く、機器寿命も永く、故障個所も無い。 This onset bright, because stirring system is pressurized water flow by increasing the convective stirring and pump discharge decomposition water by intracisternal air discharge, only the direction of the discharge tank pipe, the water flow stirred at processing tank form of any shape instantaneous There are no sliding parts such as bearings, seals, bearings, etc. with mechanical stirring blades.

本発明では、処理槽内の排水濾過網が上部水面近くにあり、処理水の攪拌流動によって、遊泳する流動摩擦で清浄されて排水濾過網の目詰まりは皆無である。 In this onset bright, wastewater filtering net in the treatment tank is located near the top surface of the water, by stirring the flow of the treated water, the clogging of the drainage filter screen is cleaned by the flow friction swimming is none.

また、排水濾過網は、0.7mmから2mm穴で米粒一つ排出することなく、実地試験では複数の処理機継続使用したが一度も目詰まりしていない。 In addition, the drainage filter net does not discharge one rice grain through a hole of 0.7 mm to 2 mm , and a plurality of processing machines are continuously used in the field test, but it is never clogged.

また、生ごみの中には魚の骨、卵の殻等も必然的に発生するが、魚の骨はカルシウムと生体蛋白質等の結合によって形成されており、その蛋白質の分解で、骨、殻は崩壊し、微細化されて目視不能となり、排水濾過網の網目以下になれば濾過網の目を通過して排水されるので、その無機系廃棄物を極力排出させない為に、排水沈殿槽を排水濾過網の外部に設け、微細未分解物が排出されれば比重で自然沈殿する事を利用して、無機系投入物が多い場合には、場合によっては槽内戻し管により、再び処理槽内に落下注入し、微細未分解物の再分解消滅を行う実施例もあり、有効であった。 Moreover, garbage fishbone Some, but occur egg shells such even necessarily, fish bone is formed by bonds such as Cal Siu arm and biological proteins, the decomposition of the protein, bone, shell collapsed, is miniaturized becomes impossible visually because through the eye drainage filtering net filtering net if the mesh following is drained, to the inorganic wastes not minimize emissions, waste water settling tank If there is a large amount of inorganic inputs, if the fine undegraded material is discharged, it will be treated again by a return pipe in the tank. There was an example in which a drop was injected into the tank and the fine undecomposed material was re-decomposed and disappeared, which was effective.

また、処理槽内の有機物分解菌着床材は、遊泳する着床材の使用も可能であるが、処理槽の槽壁の内側に固定する事によって、完全な水流攪拌で目的を果たす。 In addition, the organic material-degrading bacteria flooring material in the treatment tank can use a swimming flooring material, but by fixing it to the inside of the tank wall of the treatment tank, the purpose can be achieved with complete agitation.

また、分解処理剤に食品発酵菌、又は純粋分解酵素群を、単種、或は複合で使用し、特に必要な場合には油脂分解酵素、或はセルローズ分解酵素、蛋白質分解酵素等々の、各種発酵菌と各種酵素の配合割合を増やし、この上ない短時間分解消滅効果を揚げており、特に食品を扱う場所に設置することが多い事から、衛生面からは十分な考慮がなされた。 In addition, fermentative bacteria for food or pure degrading enzymes are used as a decomposition treatment agent, either alone or in combination, and various oil-degrading enzymes, cellulose-degrading enzymes, proteolytic enzymes, etc. if necessary. The ratio of fermenting bacteria and various enzymes was increased, and the effect of decomposing and extinguishing was raised in an exceptionally short time. In particular, it was often installed in a place where food is handled, so sufficient consideration was given from the hygiene aspect.

また、有機物の発酵分解には、分解菌類が加担する事は周知の事実であるが、自然的有機物付着菌類は無数にあり、その中で発酵に加担する菌類に欠かせない栄養素があり、その中での重要な物質を混合して栄養素として添加する事により、分解促進につながった。 Further, the fermentation decomposition of organic matter, but that the degradation fungi is complicity is a well-known fact, there are numerous natural organic matter deposited fungi, there are nutrients indispensable to fungi complicit in fermentation therein, Mixing important substances in the mixture and adding them as nutrients led to accelerated decomposition.

また、有機性廃棄物の発生する所は、その発生場所が学校や企業の給食調理、レストラン、ホテル等の調理場、食品産業製造工場に至るまで、毎日の発生量が一定するところは絶対になく、絶えず増減変化する中で、設置された機種の能力に余裕がある場合はさておいて、少なくとも1機種で余裕を持って処理するためには処理機の攪拌稼働時間とバイオ添加量の差が必要であるが、従来の機種では知識的欠如で、これを解消した物は皆無であり、本発明は、投入ゼロから、瞬間的には投入規定量の倍の量の投入も可能とした。 In addition, where organic waste is generated, it is absolutely where the amount of daily generation is constant, from school and company meals, restaurants, hotels, etc. to food industry manufacturing factories. However, if there is a margin in the capacity of the installed model, while there is a constant increase / decrease, the difference between the agitation operating time of the processing machine and the amount of bio-added in order to process with a margin in at least one model. it is necessary, in the conventional model knowledge specific lack a none thing that solves this invention, from the input zero, the instantaneous between manner and can also be turned twice the amount of input specified amount did.

また、水中分解消滅処理は、投入される有機性廃棄物の種類や量が日毎に変化するものであり、分解排水基準値に問題が起き得ると想定される場合で既設の浄化槽もない時には、分解水排水管を別途設置の排水浄化タンクに結属して環境汚染を防止している。 Also, underwater decomposition and extinction treatment is when the type and amount of organic waste that is input changes every day, and it is assumed that there may be a problem with the standard value of decomposition wastewater , and there is no existing septic tank The decomposition water drain pipe is attached to a separate waste water purification tank to prevent environmental pollution.

また、有機廃棄物の分解に費やした処理水中の溶存酸素の補充で、空気供給による酸素供給も行うが、有酸素水の供給が適切であるために水道水を使用した場合には下水道料金も同額に近く支払う事でもあり、環境的には水道水にもエネルギーが費やされており、これを極力避ける為には、井戸水、工業用水、雨水、既存の浄化槽の末端処理槽の浄化された水を有酸素水として使用するのも有効な効果であった。 In addition, oxygen supply by air supply is performed by replenishing dissolved oxygen in the treated water spent for decomposing organic waste, but when tap water is used because oxygen water is adequately supplied, sewerage charges are also charged. In order to avoid this as much as possible, energy is also spent on tap water in the environment, and in order to avoid this as much as possible, well water, industrial water, rainwater, and end treatment tanks of existing septic tanks were purified. It was also effective to use water as aerobic water.

また、機廃棄物発生場所と処理槽の設置場所が遠く離れているような場合、或は、処理槽設置場所が1か所で、有機廃棄物発生場所が複数あるような場合は、処理槽内の破砕循環水中ポンプ、又は槽外破砕循環ポンプによる自己破砕機能を持っているが、有機廃棄物発生場所からの移送目的で、有機廃棄物移送タンクを設置して、そのタンク内に有機物と移送目的の清水を供給し、タンク内に破砕循環ポンプを装着してポンプ吸引口に吸引可能な大きさに自己破砕するポンプ吐出管を処理機本体に結合するか、又はディスポーザーを設置して加水破砕し移送ポンプの稼働で移送管経由、自動移送投入するかの2方法が有り、省労力にも貢献する。 Further, if organic, such as the installation location of the place of occurrence and treatment tank waste are separated rather far, or, at the installation site is one place in the processing tank, the occurrence location of the organic waste plurality If there is the case, crushing the circulating water pump in the processing tank, or Sogai have self crushing function by crushing the circulating pump, but in the transport object of the place of occurrence of organic waste, organic waste transport set up a tank, the fresh water of the organic substance and the transport object is supplied to the tank, processing machine pump discharge pipe for self crushing wearing the crushing circulation pump in the tank attractable size to the pump suction port There are two methods of connecting to the main body, or installing a disposer to hydrolyse and crush it, and then use the transfer pump to automatically transfer through the transfer pipe, contributing to labor saving.

また、水中分解処理の場合、投入物の100%リサイクルで有機液体肥料になるが、肥料不要の場合には、分解排水は浄化機能を持った既存の浄化槽、或は別途排水処理タンクを設置、それを経由して放水する事とした。 In the case of underwater decomposition treatment, 100% recycling of the input material becomes organic liquid fertilizer, but if no fertilizer is required, the existing wastewater treatment tank with a purification function or a separate wastewater treatment tank is installed for the decomposition wastewater. It was decided to discharge water via it.

また、省エネルギーの観点から、処理槽の槽壁断熱材付きにした理由は、破砕循環水中ポンプのモーター冷却は槽内処理水による水冷方式であり、電気的なヒーター加熱を必要としない温水状態の槽内処理水の熱放出を防止するためである。 In addition, from the viewpoint of energy conservation, the reason why the tank wall of the treatment tank is equipped with a heat insulating material is that the motor cooling of the crushing circulating submersible pump is a water cooling system using treated water in the tank, and a hot water state that does not require electrical heater heating This is to prevent heat release from the treated water in the tank.

また、分解処理剤は安全な食品発酵菌類と各種分解酵素の混合であるが、外国によってはわが国の食品発酵酵素菌であっても問題視される事があるので、有機物に既に付着している各種菌類の有効利用から、分解菌添加をせずに、炭素軽物質や窒素物質、及び空気供給を含めた酸素発生剤による酸素追加で、分解処理する事も行った。 In addition, the decomposition treatment agent is a mixture of safe food fermenting fungi and various degrading enzymes, but in some foreign countries, even food fermenting enzyme bacteria in Japan may be regarded as a problem, so they are already attached to organic matter. the effective utilization of various fungi, without degrading bacteria added, carbon light substances and nitrogen-based material, and the oxygen added by the oxygen generating agent, including an air supply, it was also to decompose.

また、有機廃棄物排出する企業の殆どが、一定量の排出は殆どなく、少ない時も、或は急激に増大する事もあるが、特に投入量が増大した時は処理不能になる事も想定され、電気制御盤のコントロールで、破砕循環水中ポンプ、或は槽外破砕循環ポンプの、稼動時間を切り替えて、投入される有機物が多い場合には稼動時間を長く、少ない時は省エネルギー観点から稼動時間を短くする事によって、処理能力の変化対応もでき、超極寒冷地の冬期には、ポンプ稼働時間の延長だけで水温上昇させることもでき、船舶の南極航路でも使用が可能である。 Also, most companies for discharging organic waste, one quantification of discharge little, when less or rapidly also possible to increase, but it becomes impossible process particularly when input amount is increased It is assumed that the operation time of the crushing / circulating submersible pump or the crushing / circulating pump outside the tank is switched under the control of the electric control panel. By shortening the operation time, it is possible to cope with changes in processing capacity, and in winter in extremely cold regions, the water temperature can be raised only by extending the pump operation time, and it can also be used on the Antarctic route of ships.

また、処理機本体の処理槽から排水される水は、有機液肥でも使用できるが、有機液肥不要の場合は、既存の浄化槽に導入して浄化後の放水とする事もあり、既存浄化槽を持たない施設での使用は、処理槽併設された排水浄化タンク、或は別途設置の排水浄化タンクに導入して、浄化後放水を行う。 In addition, water drained from the treatment tank of the main body of the processor can be used in organic liquid fertilizer, but when organic liquid fertilizer is unnecessary, it may be introduced into an existing septic tank and discharged after purification. use in free facility, hotel has been drained purification tank to the processing tank, or by introducing the waste water purification tank installed separately, perform water discharge after purification.

また、処理槽内では空気放散して酸素供給すると同時に酸素発生剤装填で有酸素水の使用が最もベターである事から、水道水でも良いが、省エネルギー観点から、工業用水、地下水、或は浄化槽設置ある場合は、その末端槽の浄化済み清水を循環して使用する事が望ましい。 Further, in the processing tank, and at the same time by air stripping oxygen supply, from that used for aerobic water at the loading of the oxygen generator is most better, it may be tap water, but the energy saving point of view, industrial water, ground water, or if there is the installation of a septic tank, it is desirable to use circulating purification already Shimizu of its ends bath.

また、有酸素水の維持のためには、空気供給した水中散気管から気泡放散するが、この気泡をミクロン気泡の水中放散を行う事もより有効である。 Further, in order to maintain aerobic water, although bubbles dissipate from diffusing water was supplied air pipe, it is also more effective to perform water dissipation of the bubbles micron bubbles.

また、厨房排水のグリストラップでは、有機物流入を防止するための網籠の目詰まりでオーバーフローして流れ込んだ原形有機物によって、リストラップ自体の機能低下や清掃に労力を費やしているが、グリストラップの第一槽内に本発明の空気抜き不要の破砕循環水中ポンプを槽内に設置して、油脂分解の酵素配合分解剤を含む各種の分解発酵菌、酵素類を添加して水流攪拌し、流入有機物も消滅させる事も有益である。 Further, in the grease trap for kitchen wastewater, the original organic matter flowed overflows in clogging of the net cage to prevent the inflow of organic matter, but spends effort hypofunction and cleaning of grayed list wrap itself, grayed In the first tank of the wrist wrap, the pulverized circulating submersible pump of the present invention is installed in the tank, and various degrading fermentative bacteria and enzymes containing an oil-degrading enzyme-containing decomposing agent are added, and the water is stirred. It is also beneficial to eliminate the inflowing organic matter.

同時に、下水管ラインで、下水貯留槽にも原形有機物が流れ込み、装填の水中ポンプのポンプ吸引口を塞いだり、或は下水貯留槽内の貯留水を排出する時に、有機物によって空気抜き穴閉塞状態となり槽内貯留水排出されたときに空気をかみ込み、ポンプ機能停止が頻発するが、空気抜き穴不要の破砕循環水中ポンプの装填で問題点が解消された。 At the same time, the original organic matter also flows into the sewage storage tank in the sewage pipe line, and when the pump suction port of the loaded submersible pump is blocked or the stored water in the sewage storage tank is discharged, the air vent hole is blocked by the organic substance. Then, when the stored water in the tank was discharged , air was trapped and the pump function stopped frequently . However, the problem was solved by loading a crushing circulating submersible pump that did not require an air vent hole.

また、一つの処理機で、汚水から有機廃棄物の処理をして、なおかつ廃水の浄化を行って放水する処理機が理想的であり、そのためには、処理機本体の処理槽内を、菌着床隔壁で複数室に区切り、特に第一槽で、可能な限り酸素供給剤や槽内水中散気管で酸素供給向上を図り、分解促進の上、次の隔壁室にて分解水の浄化促進で、放水水質の向上を図ることも有益である。 Moreover, in one processor, and the processing of organic waste from sewage is yet processor is ideally water discharge performing purification of waste water, To this end, in the processing tank of the processing machine body, fungus Separate multiple chamber implantation septum, especially in the first tank, aims to improve the oxygen supply at the oxygen supply agent or intracisternal water diffuser tube as possible, on the accelerated degradation, purification of the decomposition water in the next partition wall chamber It is also beneficial to improve the quality of the discharged water through promotion.

前述の様に、従来には無い種々のメリットがあり、以下簡単に列挙する。 As described above, the conventional has no various benefits, easier listed below.

1、厨房で有機物移送槽に投入すれば処理機本体迄ポンプで加水破砕して移送が可能。
2、処理槽に原形有機物を投入しても破砕循環水中ポンプにより槽内循環攪拌可能。
3、基材は一切不要で槽内処理水のみ、基材交換廃棄等は必要ない。
4、破砕循環水中ポンプは空気抜き孔不要でエアー咬み込み機能停止はない。
5、破砕循環水中ポンプが処理槽内で槽内処理水を吸引と吐出で対流攪拌。
6、処理槽排水は、処理排水濾過網で、米粒一つ槽外への排出は無い。
7、処理排水濾過網の処理槽内側は槽内処理水の強制対流で常に摩擦清浄維持。
8、処理排水濾過網の処理槽外側は、濾過網洗浄噴射管で定期的に洗浄。
9、投入有機物の100%が有機液肥に変換され、100%リサイクル。
10、有機液肥不要な場合は、浄化装置で浄化放出。
11、処理槽は樹脂断熱構造で外気遮断で極寒極暑地でも使用可能。
12、処理機本体は機械加工構造は一品もなく機器部品装着構造の超シンプル。
13、処理機能力は水流攪拌トルク一定の為、小型から大型迄格安製造可能。
14、攪拌は、層内処理水の水流攪拌と水中散気のみで、動力電気代は微小。
15、破砕循環水中ポンプ放熱で槽内処理水が受熱され、ヒーター不要の経済性。
16、従来の排水浄化グリストラップの油脂分離機能性は低く、グリストラップ通過水を処理槽に導入すれば、油脂分解添加バイオで浄化可能。
17、下水貯留槽での沈殿物定期的撤去、或は大面積有機物による貯留槽内設置されたグラインダーポンプ吸引口封鎖による機能停止が皆無で懸案解消。
1. If it is put into the organic substance transfer tank in the kitchen, it can be transferred to the main body of the processing machine by hydrolyzing it.
2, be charged intact organic matter in the processing tank can be circulated stirred in a bath by breaking the circulation water pump.
3. No base material is required, only the treated water in the tank is used , and replacement of the base material is not required.
4. The crushing circulating submersible pump does not require an air vent and does not stop the air biting function.
5. Crushing circulation submersible pump convection and agitation by suction and discharge of treated water in the treatment tank.
6, the processing tank wastewater, in wastewater filtering mesh, is not discharged to the rice grains even one Sogai.
7, the processing tank inside of the processing waste water filtering mesh is always friction cleaning is maintained in forced convection of the bath in the treated water.
8. The outside of the treatment tank of the treated wastewater filtration net is periodically cleaned with a filter net cleaning jet pipe.
9. 100% of the input organic matter is converted to organic liquid fertilizer and 100% recycled.
10. When organic liquid fertilizer is unnecessary, it is purified and released with a purification device.
11. The treatment tank has a resin insulation structure and can be used even in extremely cold and extremely hot areas.
12. The main body of the processing machine has no machined structure and is very simple with equipment parts mounting structure.
13. The processing capability is constant because the water agitation torque is constant.
14. Stirring is only by stirring the water in the in-layer treated water and aeration of the water, and the power cost is very small.
15, Tank treated water is received by the heat radiation of the crushing circulating water pump and heating unnecessary economy.
16. The oil and fat separation functionality of the conventional drainage purification grease trap is low, and if the grease trap water is introduced into the treatment tank, it can be purified with oil and fat decomposition added bio.
17, periodic removal, or outage none a pending eliminated by the suction port blockade of the installed grinder pump in the storage tank due to organic substances having a large area of the precipitate in sewage reservoir.

実施形態に使用した水中汚物・汚水水中ポンプは、汚物による空気抜き孔のまりにより、排水貯留水槽全量排水した場合に最後に空気を吸い込んで停止、次の槽内増水で水中ポンプが稼動しても空気溜まりで水能力が無く機能停止事故が頻発しているにもかかわらず、世界中の汚物・汚水水中ポンプメーカーには該当品が存在しない。 Water waste-sewage water pumps used in the present embodiment, by In other words the air vent hole due to dirt, in the case where the wastewater reservoir water tank and the total amount drained, finally stopping draws in air, underwater pump in the following intracisternal swollen be up and running without the fried water capacity in the reservoir air, in spite of the outage accidents are frequent, there is no corresponding article in filth, sewage submersible pump manufacturers around the world.

ましてや本実施形態の破砕循環水中ポンプ(5)は、処理槽(2)内では水中散気管(12)から水中放散する空気も、ポンプ吸引口から当然吸い込むので、該当品が市販品には無い為、「図2」「図3」「図4」のように、空気抜き穴不要の汚物・汚水水中ポンプを開発し、同時に、ポンプ吸引口破砕刃(8)を装着し破砕循環水中ポンプ(5)として、抜群の機能を発揮した。 Furthermore, in the crushing circulation submersible pump (5) of the present embodiment, the air diffused from the submerged aeration pipe (12) is naturally sucked from the pump suction port in the treatment tank (2), so there is no corresponding product in the commercial product. Therefore, as shown in "Fig. 2,""Fig.3," and "Fig. 4," a filth and sewage submersible pump that does not require air vent holes has been developed, and at the same time a crushing circulating submersible pump equipped with a pump suction crushing blade (8) ( As 5), it exhibited outstanding functions.

また、槽外破砕循環ポンプ(6)は、構成的に空気抜き孔不要、及び、ポンプ吸引口破砕刃(8)が装着されているものは市販品には全く無いので、新規に「図2」「図3」「図4」の様に、ポンプインペラー軸を延長して陸上設置汚物・汚水ポンプに、ポンプ吸引口破砕刃(8)を装着し、槽外破砕循環ポンプ(6)として使用し、これも抜群の効果を発揮した。 In addition, the external crushing circulation pump (6) does not require a vent hole in terms of structure, and there is no commercially available product equipped with a pump suction crushing blade (8). As shown in “Fig. 3” and “Fig. 4”, the pump impeller shaft is extended to install the pump suction blade crushing blade (8) on the land-installed filth / sewage pump and used as the crushing circulation pump (6) outside the tank. This also showed a remarkable effect.

破砕機能を持った水中ポンプには、下水管有機物貯留槽設置する目的グラインダー水中ポンプと言う機種が市販品にあるが、これはポンプ吸引口が、固定刃と回転刃のディスポーザーと全く同様機構で、10mm前後の有機物は吸い込み破砕はするが、ポンプ吸引口口径よりも大きなものはポンプ吸引口を塞いだまま吸引され、吸いついたまま破砕せず、逆に吸引停止したままで、ポンプメカニカルシールの破損まで引き起こすので、「図4」の様に、これも回転軸を延長してその先端に破砕刃を付け、ポンプ吸引口以下に破砕して、本来のグラインダーポンプの機能を発揮させた。この理由は、有機廃棄物、特に生ごみの場合には、大きな面積のだし昆布や、キャベツの半割そのまま、大根、薩摩いも等の大きな形状が、そのままの廃棄投入されるためである。 The submersible pump having a crushing function, although models say grinder water pump for the purpose of installing a reservoir of organic matter in sewage in commercial products, which pump suction port, and disposer of the fixed blade and the rotary blade by exactly the same mechanism, but the organic material of about 10mm suction crushing is, larger than the diameter of the pump suction port is sucked remains closes the pump suction port, not crushed still attached sucking, opposite the suction is stopped As shown in Fig. 4, this also extends the rotating shaft, attaches a crushing blade to the tip, crushes it below the pump suction port, and the original grinder pump The function was demonstrated . The reason for this is that the organic waste, especially in the case of garbage, and soup stock kelp large area, as it is half percent of the cabbage, radish, is a large shape such as Satsuma potatoes, is because the raw waste is turned on.

最後に、究極の汚水や生ごみの浄化処理は、一つの処理機で有機物の消滅から排水の浄化までを行うのがベターである事は言うまでもない。   Finally, it goes without saying that the ultimate purification process for sewage and garbage is performed from the disappearance of organic matter to the purification of wastewater with a single processor.

そこで、図10」の様に、処理機本体の処理槽を効率よく仕切るために、菌着床隔壁で複数団の分解室を作り、第一槽には原形生ごみでも処理可能破砕循環水中ポンプで水流攪拌対流を作り、酸素供給剤で水中溶存酸素を増大させ、内水中散気管からの微細気泡、汚水流入、或は投入有機廃棄物の種々の物性に合わせた分解処理剤を添加して、可能な限りコンパクトで、機能性に富んだ機構とした。 Therefore, as shown in Fig. 10”, in order to efficiently partition the treatment tank of the main body of the treatment machine, a group of decomposition chambers are created with the fungus-implanted partition walls, and the first tank is capable of crushing and circulating even with raw garbage. make water flow stirred convection in water pump, to increase the water dissolved oxygen an oxygen supply agent, fine bubbles from tank water diffusion pipe, sewage inflow, or a decomposition treatment agent tailored to various physical properties of the charged organic waste The mechanism was as compact as possible and rich in functionality.

「実施形態1」では、処理槽(1)の形状は縦形円筒形、円錐形状、四角矩形筒型、及び横形円筒形の各種類の形状を実施したが、「図1」によって説明すれば、縦形円筒形状の処理槽で、既存容器を利用し、機能性は一切損なわずに可能な限り装置簡潔を計ったものである。 In “Embodiment 1”, the shape of the treatment tank (1) is a vertical cylindrical shape, a conical shape, a rectangular rectangular cylindrical shape, and a horizontal cylindrical shape, but if described with reference to FIG. a processing tank of a vertical cylindrical shape, utilizing the existing container, functionality is that measure the brief of the device as possible without compromising at all.

本実施形態では処理槽(2)内には槽内処理水(4)が一定量充填されているが、処理槽(2)の内部には、破砕循環水中ポンプ(7)が単数装着された。 In this embodiment , the treatment tank (2) is filled with a certain amount of treated water (4) in the tank, but a single crushing circulating water pump (7) is mounted inside the treatment tank (2). .

ポンプの吐出口(37)は、槽内循環攪拌対流に最も適した方向に向けられるが、槽内底部に沈殿した有機物は槽内処理水(4)対流によって浮遊させ、上部位浮遊した有機物も槽内処理水の吸引吐出で攪拌対流、ポンプ吐出口(37)を傾斜上部向きで、20度傾斜させて設置し、ポンプの空気抜き孔(40)空気抜き孔閉鎖材(41)で潰し、吐出口(37)を円周方向にも向けて、沈殿物の対流遊泳攪拌と、円周回転する方向性で、槽内浮上分解着床材(18)による処理排水濾過網(17)の接触摩擦洗浄の相乗作用を図った。 Pump discharge port (37) is directed to the most appropriate direction for the circulation stirring convection tank, organic matter precipitated in the tank bottom are suspended by convection of intracisternal treated water (4), it was suspended in the upper position organic matter stirred convection absorption引吐and out of the bath in the treated water, the pump discharge opening (37) in the inclined upper direction and is inclined 20 degrees to installed, the pump air purge opening (40) at the air vent hole closing member (41) crushed, the discharge port (37) and directed in the circumferential direction, and convection swimming stirred precipitate in direction of circumference rotating, wastewater filtering net by intracisternal floating decomposing bacteria Chakuyukazai (18) (17 ) Of contact friction cleaning.

また、新鮮有酸素清水(11)を処理槽(2)内に供給するために、日本水道協会の規定により、13mm口径の清水供給栓(13)から25mm空間設置で、上水道水をジョウゴ受水してから処理槽(2)に落下給水し、公衆衛生法条例を順守した。 In addition, in order to supply fresh aerobic fresh water (11) into the treatment tank (2), according to the provisions of the Japan Water Works Association, water supply is received from the 13mm caliber water supply tap (13) in a 25mm space. After that, water was dropped into the treatment tank (2) and the public health law regulations were observed.

空気圧縮機(14)の稼動によって、槽底に設置した槽内水中散気管(15)からの空気放出上昇で、槽内処理水(4)への酸素供給と、処理槽(2)内に装填した酸素供給剤(3)による溶存酸素上昇をる為、常時空気上昇による対流攪拌によって可能にした。 By the operation of the air compressor (14), the release of air from the in-tank aeration pipe (15) installed at the bottom of the tank causes the oxygen supply to the in-tank treated water (4) and the treatment tank (2). for Ru FIG dissolved oxygen increased by loading the oxygen-supplying agents (3), it was possible by the convection stirring by continuously air rises.

槽内処理水(4)の水位付近の槽壁(16)を開口して装着した処理排水濾過網(17)の処理槽(2)内側はポンプ水流攪拌で摩擦洗浄されるが、処理排水濾過網(17)の処理槽(2)外側の汚物付着洗浄は、濾過網外面洗浄水中散気管(20)による水中散気によ造波流動接触させて洗浄するもので有る。 Treatment tank (2) inside the tank in the treated water (4) raw wastewater filtering net of a tank wall (16) was opened and attached near water level (17), which is friction washed with pump water flow stirring, treated treatment tank (2) outside of the waste deposited washing wastewater filtering mesh (17) is a one washing the wave-making that by the water diffuser to flow contact by filtration halftone outer surface wash water diffusing tube (20).

処理排水濾過網(9)の網目が2.0mmの網目、1.7mmの目、1.5mmの網目の3種類を実施したが、卵殻等の無機系有機廃棄物が分解されて微細粉になっても槽付きU字型排水管(19)からの放水に混入しない方が良いために、脱着可能な漏出微細物沈殿槽又は袋(24)を設けて比重落下で沈殿させ、一定期間ごとに撤去する。 Mesh mesh is 2.0mm in wastewater filtering net (9), the halftone th 1.7 mm, was carried out three 1.5mm mesh, fine powder is decomposed inorganic organic wastes such as eggshell Since it is better not to mix with the water discharged from the U-shaped drain pipe (19) with a tank, a detachable leakage fine substance settling tank or bag (24) is provided and settled by dropping with a specific gravity for a certain period It removed by withdrawal every time.

汚水(5)の導入、有機廃棄物(4)の分解消滅浄化目的で、分解処理剤タンク(28)から一定量の分解処理剤(27)を処理槽(2)内に添加する為、分解処理材ポンプ(29)によって処理槽(2)に定期的に電気制御で添加され、添加量の制御が簡単な液体の分解処理剤(27)を使用した。 In order to add a certain amount of decomposition treatment agent (27) from the decomposition treatment agent tank (28) into the treatment tank (2) for the purpose of introducing sewage (5) and decomposing and extinguishing the organic waste (4), A liquid decomposition treatment agent (27) which is periodically added to the treatment tank (2) by the decomposition treatment material pump (29) by electric control and whose addition amount can be easily controlled is used.

処理槽(2)上部には、有機廃棄物投入口(25)を装着し、本発明は投入口蓋開放でも接触稼働機器は無いが、それでも安全の為に、有機性廃棄物投入口(25)蓋の開閉で処理機稼働の自動発停センサーを装着し、「開」で稼働停止、「閉」で自動復帰の安全センサーを装着した。 An organic waste input port (25) is mounted on the upper part of the treatment tank (2), and the present invention has no contact operating device even when the input port cover is opened. However, for safety, the organic waste input port (25 ) An automatic start / stop sensor for processing machine operation was installed by opening / closing the lid, operation was stopped by "open", and safety sensor for automatic return was installed by "closed".

処理機本体(1)の処理槽(2)底部の側壁(16)には、点検口(26)を装着し、機械的攪拌機構は無いが、破砕循環水中ポンプ(5)及び槽内空気散気管(12)、その他点検と機器交換の為に設置した他の実施例では、機器交換は有機廃棄物投入口(25)を使用したがまったく問題はなかった。 An inspection port (26) is attached to the side wall (16) of the processing tank (2) bottom of the processor main body (1), and there is no mechanical stirring mechanism, but the crushing circulation submersible pump (5) and air dispersion in the tank The trachea (12) was installed for other inspections and equipment replacement . In another example, the equipment replacement used the organic waste inlet (25), but there was no problem at all.

また、処理槽(2)内への新鮮有酸素清水(11)の供給量、空気圧縮機(14)の稼働と停止時間、破砕循環水中ポンプ(7)、又は処理槽外に設置の槽外循環ポンプ(8)の稼働と休止時間、分解処理剤タンク(28)の分解処理材ポンプ(29)の処理槽(2)内添加量等々の電気制御も電気制御盤(22)によって制御した。 Moreover, the supply amount of fresh aerobic fresh water (11) into the treatment tank (2), the operation and stop time of the air compressor (14), the crushing circulation submersible pump (7), or the outside of the treatment tank The electrical control panel (22) also controlled the electrical control such as the operation and downtime of the circulation pump (8) and the amount added in the treatment tank (2) of the decomposition treatment material pump (29) of the decomposition treatment agent tank (28).

図2「図3「図4」の様に、ポンプ吸引口(34)のフラットバー折り曲げ間隙破砕刃(36)の目的は、ポンプ吸引によって、くさび型形状の有機物が、ポンプ吸引口(34)と延長したインペラー軸(32)との間隙にはさまり、ポンプ吸引口間隙が狭隘化又は閉鎖されることを事前予防する目的ある。 As in "Figure 2" "Figure 3" "Figure 4", the purpose of the flat bar bent gap crushing blades (36) of the pump suction port (34), the pump suction, organic matter wedge shaped, pump suction port The purpose is to prevent in advance that the pump suction port gap is narrowed or closed by being caught in the gap between (34) and the extended impeller shaft (32).

インペラー軸(32)を、ポンプ吸引口(34)を貫通してインペラーハウジング(33)外に伸ばして先端にフラットバー折り曲げ破砕翼(35)を装着する理由は、原形投入による大きな有機物がポンプ吸引口(34)に覆いかぶさって閉塞状態になる事防止するためである。 The reason why the impeller shaft (32) extends through the pump suction port (34) to the outside of the impeller housing (33) and the flat bar bent crushing blade (35) is attached to the tip is that large organic matter due to the introduction of the original shape is pump suction This is to prevent the mouth (34) from covering the mouth (34).

処理槽(2)内での破砕循環水中ポンプ(7)の通常の設置姿勢は、最低約20度前後以上の傾斜設置で、ポンプ吐出し口は傾斜上部に位置して設置しているが、仮に空気を吸っても自動的にポンプ吐出口(37)から排出させるためで、ポンプ吐出口(37)の端末は処理槽(2)内の水流攪拌方向に向ける。 Normal installation posture of crushing circulating water pump in the treatment vessel (2) (7), in the installation at least about 20 degrees before and after more inclined, but the pump outlet is you are placed in position on the inclined top Even if air is sucked, the pump discharge port (37) is automatically discharged from the pump discharge port (37), and the terminal of the pump discharge port (37) is directed in the direction of the water flow stirring in the treatment tank (2).

また、浮上して沈殿しない有機物の場合は、ポンプ吸引口(34)を水面に向けた逆立ち方向で倒立させて設置し、ポンプ吐出口は処理槽(2)底部に向けて、沈殿有機物野水流攪拌で水中遊泳させと同時に、処理槽(2)の側壁に添って回転水流で、沈殿物の水流遊泳にするが、設置姿勢が逆立ちで倒立させて設置した場合にでも「図2」「図3」「図4」の様に、空気抜き孔(40)を空気抜き孔閉鎖材(41)で閉鎖しなければ、常時通水による繊維状有機物でインペラハウジング(33)内での閉塞物が次第に肥大化し最後にはポンプインペラ(31)を圧迫して停止させる事故がある。 Also, in the case of organic matter that floats and does not settle, the pump suction port (34) is installed upside down in the upside-down direction toward the water surface, and the pump discharge port faces the bottom of the treatment tank (2), and the precipitated organic matter field water flow simultaneously that is water swimming in stirring, a rotating water flow along the side wall of the processing tank (2), although the water swimming precipitate even if the installation position is established by inverted in headstand "Figure 2"" Figure 3 "as in" Figure 4 ", unless closed air vent hole (40) in the air vent hole closing member (41), the obstruction within the impeller over the housing (33) in the fibrous organic material by continuously passing water it is unable to stop by pressing the pump impeller chromatography (31) at the end gradually enlarged.

キャベツの葉が多い残飯処理の様な場合は浮上物が多く、同時にご飯つぶや大きな形状の生ごみが多い場合、破砕攪拌水中ポンプ(7)の吸引口を上に向けた姿勢と、処理(2)底に、20度前後傾斜させた通常の立脚姿勢との両方の破砕攪拌水中ポンプ(7)を装着する事によって、大きな形状の有機廃棄物の破砕によって表面積を増やして、バイオ分解速度を速めた。 If there is a lot of cabbage leaves, such as leftover processing, if there is a lot of floating material , and if there is a lot of crushed rice or large-sized garbage at the same time, the posture with the suction port of the crushing stirring submersible pump (7) facing upward The surface of the tank (2) is increased by crushing large-sized organic waste by attaching both crushing and stirring water pumps (7) with a normal standing posture inclined about 20 degrees to the bottom of the tank (2). Increased decomposition speed.

実施形態に使用した「図1」の破砕循環水中ポンプ(7)の他に、「図3」の様に市販のグラインダー水中ポンプ(38)をも改善して使用したが、市販品そのまま使用は出来ない理由は、グラインダー水中ポンプ(38)は、ポンプ吸引口(34)にキャベツの半割平面が吸引で吸いつき、塞がれ場合、ポンプグラインダーポンプ回転刃(39)が平面状態で有るために吸いつき、それを排除する形状でないためで、その改善する機構として、グラインダー水中ポンプ(38)の回転刃軸を伸ばしてフラットバー折り曲げ破砕翼(35)を装着し、大きな形状の有機物でもポンプ吸引口が塞がれる事はなくなった。 Other crushing circulating water pump used in this embodiment, "1" (7) "3" was used to improve also the commercial grinder submersible pump (38) as in the commercially available products thereof reason can not use or or angel, grinder submersible pump (38) is cabbage half plane to the pump suction port (34) is attached sucking suction, when closed, the pump grinder pump rotary blade (39) Because it is in a flat state, it sucks and is not in a shape that eliminates it, and as a mechanism to improve it, the rotating blade shaft of the grinder submersible pump (38) is extended and the flat bar bending crushing blade (35) is attached, The pump suction port is no longer clogged even with large organic substances.

実施形態の処理機本体(1)の槽壁(16)を断熱構造にした理由は、破砕攪拌水中ポンプ(7)の稼動によるポンプモーターの冷却は当然ながら処理槽(2)内の槽内処理水(4)によって冷却されるもので、そのエネルギーを有効に利用し、加熱ヒーターの必要が無い事も大きな特徴である。 The reason why the tank wall (16) of the processing machine main body (1) of this embodiment has a heat insulating structure is that the pump motor is cooled by the operation of the crushing and stirring submersible pump (7), of course, in the tank in the processing tank (2). It is cooled by the treated water (4), and its energy is effectively used, and there is no need for a heater.

また、処理槽(2)が樹脂構造によって、軽量化と共に、沖縄を含む紫外光線が強い地域をも考慮して紫外線劣化防止剤混入で15年以上の耐用で、万一の運搬車両との接触破損等も補修は容易に可能である。 In addition, the treatment tank (2) has a resin structure, is lightweight, and has a durability of more than 15 years due to the inclusion of UV deterioration inhibitors in consideration of regions with strong UV rays including Okinawa. Repairs such as contact damage can be easily done.

実施形態2」は、分解処理剤タンク(28)内に充填している分解処理剤(27)処理槽(2)内に定期的に一定量加するものであるが、人類健康安全確保の為に、種々の食品発酵菌を、又分解酵素の単種類から複合種類迄種々行って効果を得たが、特に有機物分解酵素の種類は、繊維素分解の酸性又は中性の分解酵素、澱粉分解の植物性又は動物性の各種分解酵素、蛋白質の各種分解酵素、油脂分解の各種酵素、これらの単独又は必要に応じた複合種類、これらを液体にそれぞれが干渉し合わない様に水中遊泳させる苦労はあったが、完全な分解処理が完成した事により、卵の殻も、魚の骨も、破砕機能が無くても、人体に何等危険を及ぼす事もなく、排水後安全性も確認されて消滅する事実が判明した。 "Embodiment 2" is regularly constant weight degradation treatment agent tank (28) decomposing agent is filled into the (27) to the treatment tank (2) in a to shall added pressure, mankind for health safety of the various food fermenting bacteria, also various performed to obtain a effect, but in particular the type of organic matter degrading enzyme until the composite type from a single type of decomposition enzymes, the fibrinolysis acidic or medium Degrading enzymes, starch-degrading plant- or animal-degrading enzymes, protein-degrading enzymes, oil-degrading enzymes, these alone or in combination as needed, and these interfere with the liquid. Although there was a hard time to swim underwater, the complete decomposition treatment agent was completed, so even if there was no crushing function for egg shells, fish bones, etc., there was no danger to the human body, drainage Later , the fact that the safety was confirmed and disappeared was found.

実施形態3」は、分解処理剤の種別が異なり、汚水導入、或は投入された有機廃棄物(6)に既に付着している各種菌類のなかで、有機物分解に有効な、有機廃棄物に既に付着している菌類の繁殖を促して分解消滅を行うもので、その為の菌類に必要な栄養素のエッセンスを液体化したもので、世界的な販路で、国によっては外国の土壌菌類の分解菌類を使用できない為の画期的な物で、これまた目を見張る分解消滅機能を発揮した。 Embodiment 3” is an organic waste that is effective in decomposing organic matter among various fungi already attached to the organic waste (6) introduced into sewage or introduced into the organic waste (6). It promotes the growth of fungi already adhering to the soil, and disintegrates and extinguishes it. It is a liquefied essence of nutrients necessary for the fungi for that purpose. the revolutionary thing for you can not use the decomposition fungi, exerted a which is also eye-popping decomposition annihilation function.

実施形態4」は、破砕循環水中ポンプ(7)又は槽外循環ポンプ(8)の稼働時間を、「短」、「中」、「長」の3種類に分割させて、「短」は短時間の回転で攪拌休止時間を長く、「中」は攪拌時間と停止時間を標準時間に設定し、「長」は攪拌時間を長くして休止時間を短くし、同一処理機の期間別投入量の過小や増大にも対応させる様に、電気制御盤(22)のセレクトスイッチでコントロールさせたことにより、使用過程でのやむを得ない投入量の増大、縮小をも1機種で対応する事が出来た。 In “ Embodiment 4”, the operation time of the crushing circulation submersible pump (7) or the outside circulation pump (8) is divided into three types of “short”, “medium”, and “long”. A short period of time makes the agitation pause longer, "medium" sets the agitation time and stop time to the standard time, and "long" lengthens the agitation time to shorten the pause time. By controlling with the select switch of the electric control panel (22) so as to cope with the amount of increase or decrease, one model can cope with the inevitably increase or decrease of the input amount in the process of use. It was.

同時に、冬期の極寒冷地で、処理槽(2)内の水温が上昇しない場合、セレクトスイッチで、稼働時間をくして温度上昇を図り、汚水や有機廃棄物の分解処理、浄化効率を上げた。 At the same time, in winter extremely cold place, if the water temperature in the processing tank (2) does not rise, by the select switch, achieving a temperature increase uptime Te long comb, decomposition treatment of wastewater and organic waste, increase the purification efficiency It was.

実施形態5」は、本実施形態の処理後の排水が、設置場所で既存の浄化槽にも導入出来ず、或は既存の浄化槽の機能が低下している様な場合、排水基準をクリアーして排水させるために、「図5」「図6」の様に、処理機本体(1)付設、又は別途設置の別置き浄化タンク(42)に本実施形態の槽付きU字型排水管(19)を接続して浄化後放水するもので、その効果も十分に検証した。 Embodiment 5” clears the drainage standard when the treated wastewater of this embodiment can not be introduced into the existing septic tank at the installation location, or the function of the existing septic tank is degraded. As shown in FIG. 5 and FIG. 6, a U-shaped drain pipe with a tank according to the present embodiment is attached to a separate purification tank (42) attached to the processor main body (1) or separately installed ( 19) was connected and discharged after purification, and the effect was also fully verified.

実施形態6」は、新鮮有酸素水(9)の供給源として使用する水道水の他、既存の井戸水、雨水、既存浄化槽最終槽水を利用して省エネルギーと省ランニングコストの削減を図った。 In “ Embodiment 6,” in addition to tap water used as a source of fresh aerobic water (9), existing well water, rain water, and existing final septic tank water are used to save energy and reduce running costs. .

実施形態7」は、処理槽(2)内に散気する圧縮空気を、より細かいミクロンエアーで水中散気して、分解を速めるものである。 In “ Embodiment 7”, compressed air diffused into the treatment tank (2) is diffused in water with finer micron air to accelerate decomposition.

実施形態8」は、本実施形態の処理機本体(1)設置した場所から離れた所で有機性廃棄物が発生、又は厨房等が複数あってその集合廃棄物を1基の本発明の処理機本体(1)で処理する場合に、破砕循環水中ポンプ(7)、又は槽外循環ポンプ(8)によって加水破砕された有機物を、そのままポンプ吐出口(37)から有機物移送管経由で破砕水と共に処理槽(2)投入されることによって、省労力と高価なディスポーザーの必要もなく有効であった。 "Embodiment 8" is present in 1 group organic waste is generated, or kitchen etc. The collective waste a plurality away from the processing machine body (1) the installation location of the embodiment when processed in the processing machine body of the invention (1), shredding the circulation water pump (7), or by Sogai circulating pump (8) to hydrolytic crushed organic matter, organic matter transfer pipe as it is from the pump discharge port (37) by being treatment tank (2) charged with crushed water through was saving labor and expensive necessary rather than valid disposer.

実施形態9」は、業務用厨房排水に必需設備のグリストラップの濾過膜が清掃不良で機能を果たしていないものがほとんどであり、グリストラップの第一槽に、破砕循環水中ポンプ(7)を装填し、同時に、油脂分解、でんぷん、蛋白質、繊維素の各分解処理材(27)を添加し、グリストラップの機能回復を図ったものである。 In “ Embodiment 9”, most of the filtration membranes of grease traps that are essential for commercial kitchen drainage do not perform their functions due to poor cleaning , and the crushing circulation submersible pump (7) is installed in the first tank of grease traps. At the same time, oil decomposition, starch, protein, and fiber decomposition materials (27) were added to restore the function of the grease wrap.

実施形態10」は、家庭、或は自治体における下水位貯留槽に、破砕循環水中ポンプ(7)を設置し、有機物の流入も、空気吸い込みによる機能停止もなく、従来の欠点を完全に解消した。 "Embodiment 10", the family, or the sewage level reservoir in municipalities, established the granulated circulation water pump (7) fracture, the inflow of organic matter, no outage by suction air, complete the deficiencies of the prior art It was solved.

実施形態11」は、1機の処理槽(2)で、汚水(5)から有機廃棄物(6)までを処理するものである。 " Embodiment 11" treats sewage (5) to organic waste (6) in one processing tank (2).

そのためには、処理槽(2)を複数室に分離するが、単なる壁でなく、菌着床隔壁(43)で区切り、投入物で、特にキャベツ葉類の様に浮上して水中遊泳も沈殿もしない場合は、破砕循環水中ポンプの1機吸引口を水面にむけて設置し、時にはもう1機の破砕循環水中ポンプを正常姿で設置するが、当然、本発明の破砕循環水中ポンプはすべて空気抜き孔不要で、吐出口を傾斜上部にして約20度の傾斜設置である。 For this purpose, the treatment tank (2) is separated into a plurality of chambers, but is not separated from a mere wall but separated by a fungus-implanted partition wall (43), and floats with the input, particularly like cabbage leaves, to settle underwater swimming. If not, install the crushing circulating submersible pump with the suction port facing the water surface, and sometimes install the other crushing circulating submersible pump in a normal state. No air vent is required, and the outlet is inclined at an upper part with an inclination of about 20 degrees.

内水中散気管(15)によって微細気泡の散気を行うが、より効率を上げるため、酸素供給剤(3)を装填し、数か月ごとの交換とした。 It performs air diffusion of micro-bubbles by intracisternal water diffusion pipe (15), but to increase the more efficient, charged oxygen supply agent (3), was replaced every few months.

当然ながら、分解処理剤(27)は、汚水の質、有機廃棄物の種類によって、油脂混入度も含めて、種々配合添加して、分解水の排水を含めて、厨房排水量が1日50t未満の無規制の無秩序な排水を、少しでも浄化して排水することの重要さを感じての発明である。 Naturally, the decomposition treatment agent (27) is added in various amounts including the fat and oil mixing degree depending on the quality of the sewage and the type of organic waste, and the amount of kitchen wastewater including the drainage of the decomposition water is less than 50t per day. the chaotic drainage of unregulated, is the inventions of feel the importance of drainage to purify even a little.

グローバルな世界環境保全の意識高揚のもと、家庭用の小型機種も簡単に設置、業務では全国のファミリーレストラン、食堂、コンビニエンスストアー、食品スーパー、ハバーガーショップ、病院給食、学校給食、工場給食、アパート・マンションに至る各施設には欠かせない有機廃棄物の処理に貢献する為、如何なる環境にもフィットする機構、部品点数を極限迄削減し、機械加工部品は皆無で、それでいて、有機廃棄物処理機能力は従来処理機の数倍の機能性を持っている。 Under the awareness of the global world environment conservation, small model is also easy to install for the home, in commercial nationwide family restaurant, cafeteria, convenience store, supermarket, ha down burger shop, hospital meals, school meals, factory In order to contribute to the disposal of organic waste, which is indispensable for facilities such as school lunches, apartments and condominiums, the mechanism that fits any environment, the number of parts is reduced to the limit, there are no machined parts, yet organic processing function force waste has several times the functionality of a conventional processor.

処理機価格は如何に廉価で販売が可能かの極限の開発、如何にランニングコストを低廉にするかのメンテナンスフリー、しかも有機廃棄物50kg/日の消滅で直径1m以下の処理槽の省スペース、それでいて従来の機能を遥かに上回る能力、このためには高価な機械加工部品数をゼロで量産可能機構とし、組み立ても特殊技能を必要とせず、人件費も削減可能とし、環境社会に普及貢献可能な生ごみ等の有機廃棄物の水中分解消滅機の完成をみた。 The ultimate development of how low the price of a processing machine is, the maintenance is free of how to reduce the running cost, and the waste of organic waste is reduced to 50 kg / day and the processing tank with a diameter of 1 m or less is saved. Space, yet far superior to conventional functions, and for this purpose, it is a mechanism that can mass-produce expensive machined parts with zero, assembly does not require special skills, labor costs can be reduced, and environmental society We saw the completion of an underwater decomposition and extinguishing machine for organic waste such as garbage that can contribute to popularization.

発酵処理方式が従来から最も多く生産されているが、今後の農業問題でも有機液体肥料として100%リサイクルが可能本発明の使用法に切り替えれば、処理機自体の格安購入、メンテナンスフリー、無臭分解消滅、本発明は、この社会的環境の全面にフィットする処理機として、世界唯一の物である Fermentation treatment method has been produced most abundantly, but if you switch to the usage method of the present invention that can be 100% recycled as organic liquid fertilizer even in the future agricultural problems, cheap purchase of the processing machine itself, maintenance-free, odorless decomposition Disappearance, the present invention is the only one in the world as a processing machine that fits the entire surface of this social environment .

その利点を列挙すれば、従来の様な機械加工による高価な攪拌軸、攪拌翼、同様に高トルク対応の頑丈な攪拌翼と高kwの駆動機にかわって、本発明はトルク変化が殆ど無いポンプ吐出し圧力による水流攪拌と、槽内空気吐出し空気の上昇対流攪拌で攪拌効率は機械的攪拌よりもはるかに効果がある。   To list its advantages, the present invention has little torque change, instead of expensive stirring shafts and stirring blades by conventional machining, as well as sturdy stirring blades and high kW drive units capable of handling high torque. The stirring efficiency is much more effective than mechanical stirring by water flow stirring by pump discharge pressure and rising convection stirring of air discharged from the tank.

有機廃棄物が原形投入であっても、自己破砕能力が有り、汚水導入でも処理機で分解処理材共に酸素供給剤の効果も有りいかなる導入対応が可能である。 Organic waste is a original turned also, there is a self-breaking capability, it is possible to both effects there any introduction corresponding oxygen supply agent decomposition treatment material with even processor sewage introduced.

処理槽の素材は、ステンレス鋼板でも良いが、ステンレスとは言え、欠点であるキャビーション部分腐食によるピンポイント穴あきが、本発明の処理槽内がバイオ水であるために問題であることから、FRPを含めて樹脂製は如何なる樹脂製でも十分に強度を保ちうるのであれば、SUS製よりも耐用年数が長く、断熱性も加算され、世界中の如何なる地域でも使用が可能である。 The material of the treatment tank may be a stainless steel plate, but although it is stainless steel, pinpoint holes due to corrosion of the cavitation portion , which is a disadvantage, is a problem because the inside of the treatment tank of the present invention is bio water. As long as any resin, including FRP, can maintain sufficient strength, the service life is longer than that of SUS, heat insulation is added, and it can be used in any region of the world.

従来の攪拌軸の必要が無く、空気供給とポンプで十分な攪拌効果が得られ、機械的メンテナンス不要と、機械加工による製造部位皆無で、コストダウンに大きく貢献し、価格的には格安に加えて機能性では抜群の製品が販売可能である。 There is no need for a conventional agitation shaft, sufficient agitation effect can be obtained with air supply and pump, no mechanical maintenance is required, there are no manufacturing parts by machining, which greatly contributes to cost reduction and is inexpensive In addition, excellent products can be sold in terms of functionality.

従来の攪拌伝達方式のチェーン・スプロケットの必要がなく、チェーン伸び交換、スプロケット摩耗交換の欠点がなく、機械的メンテナンス・ランニングコストは皆無になり、強いて言えば、年単位のポンプのメカニカル軸シールの交換のみである。   There is no need for conventional agitation transmission type chains and sprockets, there are no disadvantages of chain extension exchange and sprocket wear exchange, and there is no mechanical maintenance and running cost. It is only exchange.

部品点数の極限的削減で、原価価格構成も低く、その上、ある段階までの機種では同一部品であるため、発注数量も予定発注が可能となり、生産コスト削減に大きなメリットを生んだ。 In extreme reduction in the number of parts, the configuration of the cost price is also low, on it, because in the model up to a certain stage is the same parts, order quantity also makes it possible to schedule orders, gave birth to great advantage in production cost savings.

同一型式で少々の処理能力増大処理も可能であるため、又小型化も可能になり生産コストの大幅削減が可能となった。 Since the same model can be processed with a slight increase in processing capacity , it is also possible to reduce the size and production cost.

なによりも、密閉処理機で無臭連続使用であるため、消臭装置の必要がなく、その上、只投入するだけで、分解水に変化するために、半永久的にメンテナンスフリーであるが、せめて、2年に1回位は、異物撤去でのメンテナンスを行えば良い。 Above all, since it is a odorless continuous use in a closed processing machine, there is no need for a deodorizing device. About once every two years, maintenance by removing foreign objects may be performed.

部品点数が5本の指で数えられる程、極端に少なく、電気機器も水中対流攪拌の為にトルクが微小で故障率も皆無に近い。   As the number of parts is counted with 5 fingers, the number of parts is extremely small, and the electric equipment has a small torque due to underwater convection agitation and almost no failure rate.

同時に機械的知識不要の全自動であり、投入口蓋を開けて有機廃棄物を投入した後投入口蓋を閉めるだけである。 Is a fully automatic mechanical knowledge is not required at the same time, it is only close the input palate after turning the organic waste to open the input palate.

既存容器を使用した、汚水浄化と生ゴミの有機物処理機で破砕循環水中ポンプを設置した処理機本体の、断面図である。It is sectional drawing of the processing machine main body which installed the crushing circulation submersible pump by the organic matter processing machine of sewage purification and garbage which used the existing container. 本発明に使用する、空気抜き孔を閉鎖し破砕循環水中ポンプの断面図である。It is sectional drawing of the crushing circulation submersible pump which closed the air vent hole used for this invention. 本発明に使用する、槽外破砕循環ポンプの断面図である。It is sectional drawing of the crushing circulation pump outside a tank used for this invention. 本発明に使用する、グラインダー水中ポンプの断面図である。It is sectional drawing of the grinder submersible pump used for this invention. 汚水浄化と生ゴミの有機物処理機で破砕循環水中ポンプを設置した処理機本体とそれに結続した別置き浄化タンクの透視図、一部断面図。A perspective view and a partial cross-sectional view of a main body of a sewage purification and garbage organic matter processing machine installed with a crushing circulation submersible pump and a separate purification tank connected thereto. 汚水処理専用で、酸素供給剤と水中散気と分解バイオによる攪拌処理浄化の、透視図、一部断面図。A perspective view and a partial cross-sectional view of an agitation treatment purification by oxygen supply agent, underwater aeration and decomposed bio, dedicated to wastewater treatment. グリストラップ浄化の斜視図、一部側面図。The perspective view and partial side view of grease strap purification. 下水道汚水貯留槽の、断面図、一部透視図である。It is sectional drawing and a partial perspective view of a sewer sewage storage tank. 遠隔厨房、或は複数厨房からの排出物を、1機の処理機本体で処理する系統斜視で有る。It is a system perspective view which processes the discharge from a remote kitchen or a plurality of kitchens with one processor main part. 処理機本体に汚水浄化隔壁を持って、汚水浄化と生ゴミの水中分解消滅機を1機で消化する機構の破砕循環水中ポンプを設置した処理機本体の斜視図、一部断面図である。With dirty water partition wall to the processing machine body, perspective view of the processing machine body set up crushing circulation water pump digestion to mechanism dirty water and garbage in water degradation annihilation machine 1 machine, is a partial sectional view .

符号の説明Explanation of symbols

1 処理機本体
2 処理槽
3 酸素供給剤又は酸素供給装置
4 槽内処理水
5 汚水
6 有機廃棄物
7 破砕循環水中ポンプ
8 槽外破砕循環ポンプ
9 ポンプ吐出管
10 ポンプ吸引口破砕刃
11 新鮮有酸素清水
12 電磁弁或は電動弁
13 清水供給栓
14 空気圧縮機
15 槽内水中散気管
16 槽壁
17 処理排水濾過網
18 槽内浮上分解菌着床材
19 槽付きU字型排水管
20 濾過網外面洗浄水中散気管
21 排水管内浮上分解菌着床材
22 電気制御盤
23 空気逃がし管
24 漏出微細物沈殿槽又は袋
25 有機廃棄物投入口
26 点検口
27 分解処理剤
28 分解処理剤タンク
29 分解処理剤ポンプ
30 分解処理剤添加管
31 ポンプインペラー
32 ポンプインペラー軸
33 インペラーハウジング
34 ポンプ吸引口
35 フラットバー折り曲げ破砕翼
36 フラットバー折り曲げ間隙破砕刃
37 ポンプ吐出口
38 グラインダー水中ポンプ
39 グラインダー水中ポンプ回転刃
40 空気抜き孔
41 空気抜き孔閉鎖剤
42 別置き浄化タンク
43 菌着床隔壁
44 グリストラップ
45 下水道汚水貯留槽
46 槽内排水導管
47 槽内排水導管水中散気管
DESCRIPTION OF SYMBOLS 1 Processing machine body 2 Processing tank 3 Oxygen supply agent or oxygen supply device 4 In-tank treated water 5 Sewage 6 Organic waste 7 Crush circulation water pump 8 Crush circulation pump 9 Pump discharge pipe 10 Pump suction crushing blade 11 Fresh existence Oxygen fresh water 12 Solenoid valve or motorized valve 13 Fresh water supply plug 14 Air compressor 15 Underwater diffuser pipe 16 Tank wall 17 Treated wastewater filtration network 18 Floating decomposition bacteria bed material 19 Tank U-shaped drainpipe 20 with tank Washing air diffuser pipe 21 for outer surface of the net Floating decomposition bacteria flooring material 22 in the drain pipe Electric control panel 23 Air escape pipe 24 Leakage fine substance sedimentation tank or bag 25 Organic waste inlet 26 Inspection port 27 Decomposition agent 28 Decomposition agent tank 29 Decomposition treatment agent pump 30 Decomposition treatment agent addition pipe 31 Pump impeller 32 Pump impeller shaft 33 Impeller housing 34 Pump suction port 35 Flat bar bent crushing blade 36 Rat bar bending gap crushing blade 37 Pump discharge port 38 Grinder submersible pump 39 Grinder submersible pump rotary blade 40 Air vent hole 41 Air vent hole closing agent 42 Separate purification tank 43 Bacteria implantation partition wall 44 Grease strap 45 Sewer sewage storage tank 46 Tank drainage conduit 47 Drainage pipe in the tank

Claims (11)

汚水(5)又は有機廃棄物(6)が含まれるとともに、酸素供給剤又は酸素供給装置(3)によって酸素が供給される槽内処理水(4)が内部に充填される処理槽(2)を有する処理機本体(1)と、Treatment tank (2) containing sewage (5) or organic waste (6) and filled with treated water (4) in the tank supplied with oxygen by an oxygen supply agent or oxygen supply device (3) A processor body (1) having
前記処理槽(2)の内部に設置された破砕循環水中ポンプ(7)と、を備え、A crushing circulating submersible pump (7) installed inside the treatment tank (2),
前記破砕循環水中ポンプ(7)のポンプ吐出管(9)から前記槽内処理水(4)中への吐出によって、前記汚水(5)又は前記有機廃棄物(6)が攪拌流動するように構成されていることを特徴とする有機物処理機。The waste water (5) or the organic waste (6) is stirred and flowed by discharge from the pump discharge pipe (9) of the crushing circulation submersible pump (7) into the treated water (4) in the tank. Organic matter processing machine characterized by being made.
汚水(5)又は有機廃棄物(6)が含まれるとともに、酸素供給剤又は酸素供給装置(3)によって酸素が供給される槽内処理水(4)が内部に充填される処理槽(2)を有する処理機本体(1)と、Treatment tank (2) containing sewage (5) or organic waste (6) and filled with treated water (4) in the tank supplied with oxygen by an oxygen supply agent or oxygen supply device (3) A processor body (1) having
前記処理槽(2)の外部に設置された槽外破砕循環ポンプ(8)と、を備え、An outside tank crushing circulation pump (8) installed outside the processing tank (2),
前記槽外破砕循環ポンプ(8)のポンプ吐出管(9)から前記槽内処理水(4)中への吐出によって、前記汚水(5)又は前記有機廃棄物(6)が攪拌流動するように構成されていることを特徴とする有機物処理機。The sewage (5) or the organic waste (6) is stirred and flowed by discharge from the pump discharge pipe (9) of the external crushing circulation pump (8) into the treated water (4) in the tank. Organic matter processing machine characterized by being comprised.
前記ポンプ吐出管(9)の先端の向きを変化させることにより、前記槽内処理水(4)の流動攪拌をコントロールするように構成されていることを特徴とする請求項1又は請求項2に記載の有機物処理機。 The structure according to claim 1 or 2 , wherein the flow agitation of the treated water (4) in the tank is controlled by changing the direction of the tip of the pump discharge pipe (9). The organic matter processing machine described . 攪拌時間の設定を、複数の類に分割させたことを特徴とする請求項1から請求項3のいずれか一項に記載の有機物処理機。 Setting of the stirring time, organic substance treatment machine according to any one of claims 1 to 3, characterized in that is divided into a plurality of types. 破砕循環水中ポンプ(7)のモーター発熱部を前記槽内処理水(4)で冷却することで、前記槽内処理水(4)が水温上昇するように構成されていることを特徴とする請求項1記載の有機物処理機。 The motor heat generation part of the crushing circulation submersible pump (7) is cooled by the treated water (4) in the tank, so that the treated water (4) in the tank rises in water temperature. Item 2. The organic substance processing machine according to Item 1 . 前記処理槽(2)には、前記槽内処理水(4)に有酸素清水(11)を給水するための清水供給栓(13)が設けられていることを特徴とする請求項1から請求項のいずれか一項に記載の有機物処理機。 Wherein the treatment tank (2), wherein the preceding claims, wherein the vessel treated water (4) to the fresh water faucet to water aerobic Shimizu (11) (13) is provided Item 6. The organic substance processing machine according to any one of Items 5 . 前記処理槽(2)内に設けられた槽内水中散気管(15)から、前記槽内処理水(4)にミクロン気泡を供給するように構成されていることを特徴とする請求項1から請求項のいずれか一項に記載の有機物処理機。 From said processing bath (2) intracisternal water diffuser tubes provided in the (15), claim 1, characterized in that it is configured for supplying a micron bubbles in the tank processing water (4) The organic substance processing machine as described in any one of Claims 6 . 前記処理槽(2)は、遠隔に配置された貯留槽を備え、前記貯留槽から前記汚水(5)又は前記有機廃棄物(6)が前記処理槽(2)内に投入されることを特徴とする請求項1から請求項のいずれか一項に記載の有機物処理機。 The said processing tank (2) is equipped with the storage tank arrange | positioned remotely, The said waste water (5) or the said organic waste (6) is thrown in into the said processing tank (2) from the said storage tank. organic matter treatment machine according to any one of claims 1 to 7 to. 前記処理槽(2)は、厨房等の調理排水の汚水貯留槽であることを特徴とする請求項1から請求項のいずれか一項に記載の有機物処理機。 The organic processing machine according to any one of claims 1 to 8 , wherein the processing tank (2) is a sewage storage tank for cooking wastewater such as a kitchen . 前記処理槽(2)は、産業用排水の汚水貯留槽であることを特徴とする請求項1から請求項8のいずれか一項に記載の有機物処理機。 The said treatment tank (2) is a wastewater storage tank of industrial wastewater, The organic substance processing machine as described in any one of Claims 1-8 characterized by the above-mentioned . 前記処理槽(2)内を、菌着床隔壁(43)で多段区切りして、前記槽内処理水(4)が前記菌着床隔壁(43)を通過することで浄化されるように構成されていることを特徴とする請求項1から請求項10のいずれか一項に記載の有機物処理機。 The treatment vessel (2) within, as in the interest multistage separated by fungal implantation partition wall (43), said tank treated water (4) is purified by passing through the bacteria landing partition wall (43) It is comprised , The organic substance processing machine as described in any one of Claims 1-10 characterized by the above-mentioned .
JP2005355384A 2005-11-10 2005-11-10 Organic matter processing machine Expired - Fee Related JP4638337B2 (en)

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