JP4557541B2 - Organic waste accumulation-free treatment system and treatment method thereof - Google Patents

Organic waste accumulation-free treatment system and treatment method thereof Download PDF

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JP4557541B2
JP4557541B2 JP2003425713A JP2003425713A JP4557541B2 JP 4557541 B2 JP4557541 B2 JP 4557541B2 JP 2003425713 A JP2003425713 A JP 2003425713A JP 2003425713 A JP2003425713 A JP 2003425713A JP 4557541 B2 JP4557541 B2 JP 4557541B2
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文 富 李
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葉山控股有限公司
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A40/00Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
    • Y02A40/10Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
    • Y02A40/20Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
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    • Y02W30/40Bio-organic fraction processing; Production of fertilisers from the organic fraction of waste or refuse

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Description

本発明は、一種の有機廃棄物堆積放置不要処理システム及びその処理方法に係わり、特に一種の処理効率を加速でき、作業スペースを縮減でき、悪臭と病気媒介生物の生成を避けられ、環境保護のコンセプトに該当すると共に、衛生品質を向上でき、有機廃棄物を堆積放置不要の有機肥料産物となるようにリサイクル転換して再度に利用に供することができる、有機廃棄物堆積放置不要処理システム及びその処理方法に関するものである。   The present invention relates to a kind of organic waste accumulation-free treatment system and a treatment method thereof, and in particular, can accelerate a kind of treatment efficiency, reduce a work space, avoid generation of malodor and disease-borne organisms, and protect the environment. An organic waste accumulation and disposal treatment system that is applicable to the concept, can improve sanitary quality, can be recycled and reused to become organic fertilizer products that do not require accumulation of organic waste, and its It relates to a processing method.

事業有機廃棄物(例えば、食品加工業やレストランや革製品工場などからの産物)や農業有機廃棄物(例えば、園芸や農場や牧場などからの産物)や民生有機廃棄物(例えば料理余剰物など)などの数量がかなり多く、且つ種類が雑多であり、世界各国の妥当に処理しなければならない環境保護事業の重点であり、そして、地球上の土壌資源がかなり有限的であるので、人口が密集する地区に対しては有機廃棄物の処理が加速しなければならない大切な事業となっている。   Business organic waste (for example, food processing industry, products from restaurants, leather factories, etc.), agricultural organic waste (for example, products from horticulture, farms, ranches, etc.) and consumer organic waste (for example, cooking surplus) The number of such items is quite large, and the types are miscellaneous, which is the focus of environmental protection projects that must be properly treated in various countries around the world. It is an important business that organic waste processing must accelerate for the districts that do.

従来の有機廃棄物処理方法は、例えば、埋め込み法や焼却法や堆肥法などが、処理スペースと工場建設コストがかかることと、堆積放置時間が長いことと、空気と水源が汚染される虞があるなどのそれぞれの課題を有している。   Conventional organic waste treatment methods include, for example, the embedding method, the incineration method, and the composting method, which requires processing space and factory construction cost, a long accumulation time, and air and water sources may be contaminated. Each has its own challenges.

料理余剰物を例としてあげると、それが有機廃棄物の中では占有する比率が最も多く、油成分含有量が高いので、処理し難く、ゴミとミックスすると、悪臭を放つと共に、汚水を生成し、それらより他のゴミ資源をリサイクルしがたくなることがある。なお且つ生活品質に悪影響を及ぼすこともあり、その沁み出す大量の水分の中では、よく大量の有機質を含有しており、容易に細菌と病気媒介を生成しやすく、不処理のまま直接排出すると、容易に川を汚染し、もし、埋め込み法によって処理すると、その処理が完璧でない場合、地下水を汚染する虞がある。料理余剰物が有機肥料資源であるので、任意に捨てると浪費になることがあり、もし、巧みに処理及び利用できれば、埋め込み場と焼却処理工場との使用寿命を延長できると共に、予算支出をも減少でき、ゴミ問題の引き起こす社会紛争を減少できる。その中、飼育動物の餌として利用する場合、収納容器の衛生の課題を有し、容易に酸化し悪臭を放ち、且つ病気を伝染するなどの課題を有する。家庭式の料理余剰物の収納容器を例として言う場合では、その配置場所には衛生の問題を有し、容易に酸化を生じ、悪臭を放ち、且つ汚水の溢れ出ることを招くことがあり、高速発酵装置によって処理する場合では、電気消費と腐り程度の課題を有し、そのため、先進国家では、大体高効率の料理余剰物堆肥の仕事を進め、料理余剰物を有機肥料になるように転換する。他に、化学肥料がその効き目が速く、且つ農産物の産量を増加できる明らかな効果を有するので、有機肥料の地位を取り換えたが、長期間且つ大量に使用されると、容易に土壌を貧乏化させ、且つ生態のバランスを破壊することもあり、環境保護の意識の台頭によって、有機肥料の利用がますます重要視を受けるようになってくる。   Taking cooking surplus as an example, it occupies the largest proportion of organic waste and has a high oil component content, so it is difficult to treat, and when mixed with garbage, it emits a foul odor and produces sewage. , It may be more difficult to recycle other garbage resources. In addition, it may have an adverse effect on quality of life, and in the large amount of water it contains, it often contains a large amount of organic matter, and easily produces bacteria and disease vectors. Easily pollute rivers, and if treated by embedding methods, can contaminate groundwater if the treatment is not perfect. Since cooking surplus is an organic fertilizer resource, it can be wasted if it is arbitrarily discarded.If skillfully processed and used, the service life of the embedding site and the incineration plant can be extended and budget expenditures can be increased. Can reduce social conflicts caused by garbage problems. Among them, when used as food for domestic animals, it has the problem of hygiene of the storage container, and easily oxidizes, gives off a bad odor, and transmits a disease. In the case of a home-style cooking surplus storage container as an example, there is a problem of hygiene in its place of placement, it easily oxidizes, gives off a bad odor, and may overflow sewage, In the case of processing with a high-speed fermenter, there is a problem of electricity consumption and rot, so in advanced countries, the work of cooking surplus compost with high efficiency is advanced, and the cooking surplus is converted to organic fertilizer. To do. In addition, the chemical fertilizer has a clear effect that the effect is fast and can increase the production of agricultural products, so the status of organic fertilizer was replaced, but when it is used for a long time and in large quantities, it easily depletes the soil The use of organic fertilizers will become increasingly important due to the rise of environmental protection awareness.

従来の料理余剰物の処理方法について、図1に示すように、大体料理余剰物90を砕け装置91に導入して砕け処理をし、また水92を加入して残滓93と油水混合物94となるように流し処理をし、それから、残滓93を直接的に投げ捨て94または堆肥発酵96を実行し、また、油水混合液94を直接的に排出97をし、または他の汚水処理98を実行する。   As shown in FIG. 1, the conventional cooking surplus treatment method introduces roughly cooking surplus 90 into a crushing device 91 for crushing treatment, and joins water 92 to form a residue 93 and an oil-water mixture 94. Then, the residue 93 is directly thrown away 94 or compost fermentation 96, the oil / water mixture 94 is directly discharged 97, or another sewage treatment 98 is performed.

前記の従来の料理余剰物の処理装置と処理方法による場合、料理余剰物からなるゴミの体積を1/3〜1/6になるまで減少できるが、その残滓を投げ捨てるための場所と埋め込みを実行する場所では大きい範囲の土地を利用する必要があり、また、高速発酵処理装置によって処理を実行する場合、48〜72時間の乾燥化を実行後に、さらに15日間以上堆積放置する必要があり、そうする場合こそ、有機物の要求される半分成熟程度に達することが出来、かなり時間と手数がかかり、且つその発酵過程中に容易に有毒ガス(例えば、腐りガスやアンモニアや酸化炭素など)を生じ、環境汚染を招く場合があり、且つ長時間の処理過程において生成する化学物質が機械設備を腐らせることもあり、機械の寿命を短縮する課題を有し、且つ運営コストを向上する課題もあり、また、油水混合液には大量の有機物質を含有しているので、容易に細菌の大量繁殖の課題を招くことがあり、不処理のまま直接的に河川に排水されると、容易に河川に酸化させ、環境を二度目に汚染する虞がある。   In the case of the conventional cooking surplus processing apparatus and processing method described above, the volume of garbage made from cooking surplus can be reduced to 1/3 to 1/6. It is necessary to use a large area of land at the place to be used, and when processing is performed by a high-speed fermentation processing device, it is necessary to leave it for another 15 days or more after performing drying for 48 to 72 hours. If you do, you can reach the required half-maturity of organic matter, take a lot of time and effort, and easily produce toxic gases (such as rotting gas, ammonia and carbon oxide) during the fermentation process, It may cause environmental pollution, and chemical substances generated in the long-term treatment process may rot the machinery and equipment. There is also a problem of improving costs, and the oil / water mixture contains a large amount of organic substances, which can easily lead to the problem of mass reproduction of bacteria. Doing so can easily oxidize the river and pollute the environment a second time.

そのため、前記の説明から分かるように、前記の従来の料理余剰物処理方法は実際的に処理する場合では、明らかに不便さと欠陥を有し、至極改善される必要がある。   Therefore, as can be seen from the above description, the above-described conventional cooking surplus processing method clearly has inconveniences and defects when it is actually processed, and needs to be improved extremely.

本発明は、有機廃棄物の処理時間を短縮化でき、作業スペースを減少でき、且つ悪臭と病気媒介物を生成することがなく、環境保護と衛生品質を確保でき、有機廃棄物を堆積放置不要の有機肥料産物になるようにリサイクル転換可能な、有機廃棄物堆積放置不要処理システム及びその処理方法を提供することをその主要な解決しようとする課題とする。   The present invention can shorten the processing time of organic waste, can reduce the work space, does not generate malodor and disease mediators, can ensure environmental protection and sanitary quality, and does not need to deposit organic waste It is a main problem to be solved to provide an organic waste accumulation and disposal treatment system that can be recycled and converted into an organic fertilizer product and a treatment method thereof.

前記の目的を図るために、本発明は、一種の有機廃棄物堆積放置不要処理システム及びその処理方法を提供し、その中、その処理システムにおいては、熱源装置と、有機廃棄物を導入してジャムになるように処理する前処理装置と、前記前処理装置の下流に配置され、前記ジャムに微生物酵素と所定の反応添加物を添加して混合物を生成する、分解装置と、を備えており、その中、前記熱源装置が前記混合物を加熱し、前記分解装置が前記混合物を分解すると共に、滅菌を実行することによって堆積放置不要の有機肥料産物を製造する。   In order to achieve the above-mentioned object, the present invention provides a kind of organic waste accumulation unneeded treatment system and a treatment method thereof, in which a heat source device and organic waste are introduced in the treatment system. A pre-processing device for processing to become a jam, and a decomposition device that is arranged downstream of the pre-processing device and generates a mixture by adding a microbial enzyme and a predetermined reaction additive to the jam. Among them, the heat source device heats the mixture, and the decomposition device decomposes the mixture and performs sterilization to produce an organic fertilizer product that does not need to be deposited.

また、本発明による処理方法は、下記のようなステップを有しており、つまり、
有機廃棄物を砕けてジャム状に形成させるステップ(一)と、
微生物酵素と反応添加物を前記ジャム状物に添加して混合物を生成させるステップ(二)と、
前記混合物を分解させると共に、滅菌を実行することによって堆積放置不要の有機肥料産物を作るステップ(三)とを有する。
Further, the processing method according to the present invention includes the following steps:
Crushing organic waste into jams (1),
Adding a microbial enzyme and a reaction additive to the jam to form a mixture (2);
A step (3) of decomposing the mixture and performing sterilization to produce an organic fertilizer product that does not require deposition.

本発明の達成しようとする予定目的とその採用する技術手段とその効果性を詳しく説明するために、以下に添付図面を参照しながら、本発明の実施可能な実施の形態を挙げて詳細的で具体的に説明するが、それらの説明による具体的な構造は本発明のある実施可能な実施例に過ぎず、本発明の権利主張範囲を狭義的に定義するものではないことは言うまでもない。   DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS In order to explain in detail the intended purpose of the present invention, the technical means adopted by it, and the effectiveness thereof, the present invention will be described in detail with reference to the accompanying drawings. Although specifically described, the specific structures according to these descriptions are merely possible embodiments of the present invention, and needless to say, the scope of claim of the present invention is not narrowly defined.

図2と図3に示すように、本発明による有機廃棄物堆積放置不要処理システム及びその処理方法において、そのシステムには、熱源装置34と、前処理装置30と、分解装置32とを含んでおり、その中、熱源装置34として密閉循環式ホット灯油加熱システムまたは密閉循環式蒸気加熱システムを採用することができ、ボイラー加熱または電源加熱の方式を選択的に採用できる。   As shown in FIG. 2 and FIG. 3, in the organic waste deposition unneeded treatment system and treatment method according to the present invention, the system includes a heat source device 34, a pretreatment device 30, and a decomposition device 32. Among them, a closed circulation hot kerosene heating system or a closed circulation steam heating system can be adopted as the heat source device 34, and a boiler heating method or a power source heating method can be selectively adopted.

また、前処理装置30には、有機廃棄物10が導入され、且つそれらをジャム状物11になるように処理が実行される。   In addition, the organic waste 10 is introduced into the pretreatment device 30, and processing is performed so that they become the jammed material 11.

また、分解装置32が前処理装置30の下流位置に位置し、ジャム状物11に対し微生物酵素と反応添加物12を添加して混合物13を形成させる。   In addition, the decomposition device 32 is positioned downstream of the pretreatment device 30, and the microbial enzyme and the reaction additive 12 are added to the jammed material 11 to form the mixture 13.

また、熱源装置34によって混合物13を加熱し、且つ分解装置32によって混合物13を分解させると共に、滅菌処理を実行することによって堆積放置処理不要の有機肥料産物25を生成する。   Further, the mixture 13 is heated by the heat source device 34, and the mixture 13 is decomposed by the decomposition device 32, and the sterilization process is performed, thereby generating the organic fertilizer product 25 that does not require the sedimentation treatment.

また、前記のそれぞれの熱源装置34と前処理装置30と分解装置32とがすべてある電気回路コントロール・ユニット(図示省略)に電気的に接続され、その電気回路コントロール・ユニットによってそれぞれの装置の所要する仕事条件、例えば温度や時間や速度などを設定する。   The heat source device 34, the pretreatment device 30 and the decomposition device 32 are all electrically connected to an electric circuit control unit (not shown), and the electric circuit control unit requires each device. Set work conditions such as temperature, time and speed.

本発明による処理方法には次のようなステップを有する。つまり、
有機廃棄物10をジャム状物11になるように砕ける60ステップ(一)と、
微生物酵素と反応添加物12をジャム状物11に添加して混合物13を形成させるステップ(二)と、
混合物13を分解する61と共に、滅菌62を実行することによって堆積放置処理不要の有機肥料産物25を生成するステップ(三)とを有する。
The processing method according to the present invention includes the following steps. That means
60 steps (one) of crushing organic waste 10 to jam 11;
Adding a microbial enzyme and reaction additive 12 to the jam 11 to form a mixture 13 (2);
The step (3) of generating the organic fertilizer product 25 that does not require the sedimentation treatment by performing the sterilization 62 is performed together with the decomposition 61 of the mixture 13.

また、図4と図5に示すように、本発明における前処理装置30とその前処理のステップは、次のとおりであり、つまり、前処理装置30には、収納槽33と、砕け装置31と、油水分離装置35とを備えており、収納槽33が砕け装置31の下流に位置し、油水分離装置35が収納槽33の下流に位置し、砕け装置31には有機廃棄物10が導入され、砕け装置31が有機廃棄物10を砕けて油含有のジャム状物26を生成し、それを収納槽33に導入する。熱源装置34が灯油または蒸気を輸送して逆止弁と安全弁と圧力メータを経過して前処理装置30の収納槽33の挟み層に進入させ、熱源装置34が収納槽33内の油含有ジャム状物26を加熱してジャム状物11と表面油水混合液15とを分離させ、表面油水混合液15が油水分離装置35に導入されて有機廃棄物10の油液16と回収水17とを分離し出し、油水分離装置35にはそれぞれ油液16を回収するための油収集管路36と、回収水17を回収するための水収集管路37が設けられ、油液16を回収すると、洗浄用のソープの材料とすることができ、また、水収集管路37が収納槽33の上流に連接され、その回収水17を収納槽33へ回収して再度に処理に利用する。本発明の前処理装置30とその前処理ステップが後記のようにしてもよく、つまり、その前処理装置30には、収納槽33と、砕け装置31と、油水分離装置35と、を有し、収納槽33が砕け装置31と油水分離装置35の上流位置に位置し、収納槽33には有機廃棄物10が導入され、熱源装置34が前処理装置30の収納槽33内の有機廃棄物10を摂氏80度まで加熱し、水液と、残滓と、表面油水混合液15とに分離し出させ、その中、収納槽33内には攪拌装置39が設けられ、それによって収納槽33内の有機廃棄物10を充分に攪拌し、且つ熱源装置34を合せて使用し、有機廃棄物10を均一的に仕事温度まで達させ、前記水液と前記残滓とが砕け装置31に伝送されてジャム状物11となるように砕け加工される。前処理装置30の収納槽33と砕け装置31との間には隔膜式のポンプと螺旋輸送装置が配置され、前記隔膜式ポンプによって水液を砕け装置31に輸送し、前記螺旋輸送装置が前記残滓を砕け装置31へ強引に輸送し、前処理装置30の収納槽33の上流では、粗末砕け装置を配置してもよく、それによって体積が大きいほうの有機廃棄物10を粗末にカットして細かい塊状物に形成させる。   As shown in FIGS. 4 and 5, the pretreatment device 30 and the pretreatment steps in the present invention are as follows. That is, the pretreatment device 30 includes a storage tank 33 and a crushing device 31. The storage tank 33 is located downstream of the crushing apparatus 31, the oil / water separation apparatus 35 is located downstream of the storage tank 33, and the organic waste 10 is introduced into the crushing apparatus 31. Then, the crushing device 31 crushes the organic waste 10 to produce an oil-containing jam 26 and introduces it into the storage tank 33. The heat source device 34 transports kerosene or steam, passes through the check valve, the safety valve, and the pressure meter and enters the sandwiched layer of the storage tank 33 of the pretreatment device 30, and the heat source device 34 contains the oil-containing jam in the storage tank 33. The product 26 is heated to separate the jam 11 and the surface oil / water mixture 15, the surface oil / water mixture 15 is introduced into the oil / water separator 35, and the oil 16 and the recovered water 17 of the organic waste 10 are separated. The oil / water separation device 35 is provided with an oil collection line 36 for collecting the oil liquid 16 and a water collection line 37 for collecting the recovered water 17. When the oil liquid 16 is collected, The soap can be used as a cleaning soap material, and a water collecting pipe 37 is connected upstream of the storage tank 33, and the recovered water 17 is recovered into the storage tank 33 and used again for processing. The pretreatment device 30 and the pretreatment step of the present invention may be as described later, that is, the pretreatment device 30 includes a storage tank 33, a crushing device 31, and an oil-water separation device 35. The storage tank 33 is positioned upstream of the crushing device 31 and the oil / water separator 35, the organic waste 10 is introduced into the storage tank 33, and the heat source device 34 is the organic waste in the storage tank 33 of the pretreatment device 30. 10 is heated to 80 degrees Celsius and separated into a water liquid, a residue, and a surface oil / water mixture 15, in which a stirring device 39 is provided in the storage tank 33, thereby The organic waste 10 is sufficiently stirred, and the heat source device 34 is used together to uniformly reach the organic waste 10 to the working temperature, and the aqueous liquid and the residue are transmitted to the crushing device 31. It is crushed so as to be a jam 11. A diaphragm-type pump and a spiral transport device are disposed between the storage tank 33 and the crushing device 31 of the pretreatment device 30, and the diaphragm-type pump transports water to the crushing device 31. The residue is forcibly transported to the crushing device 31, and a coarse powder crushing device may be arranged upstream of the storage tank 33 of the pretreatment device 30, thereby cutting the organic waste 10 having a larger volume into the coarse powder. A fine lump is formed.

図6と図7に示すのは、本発明の生成する液状肥料化の堆積放置処理不要の有機肥料産物23を示す説明図であり、その前処理装置30の収納槽33と分解装置32との間には研磨装置41が配置され、研磨装置41と分解装置32との間には開放式予備槽42が配置され、研磨装置41がジャム状物11を研磨して細い分子のジャム状物19を生成し、且つ予備槽42に輸送する。前記微生物酵素と反応添加物12が予備槽42内に添加されて、細い分子ジャム状物19と混合して混合物13を生成し、前記反応添加物が細い分子ジャム状物19の反応物と炭素/窒素の比を調整することに利用されるものであり、それによって所定の酸性を保持し、微生物酵素の分解に利するように使用されるものであり、その反応添加物の成分比例を変更させることによってそれぞれ異なるタイプの堆積放置処理不要の有機肥料産物25を取得できる。予備槽42には隔膜式ポンプ45が設けられ、それによって混合物13を分解装置32の分解槽へ輸送し、分解装置32には材料輸送バルブと呼吸バルブが配置され、隔膜式ポンプ45が運転時に分解槽内において正圧力を生成して空気を対流させることを生じることを避けるために設けたものであり、熱源装置34が灯油または蒸気を逆止弁と安全弁と圧力メータを経過して分解装置32の分解槽の挟み層に進入させるように輸送をし、熱源装置34が摂氏100度以上の温度によって分解装置32の分解槽内の混合物13を加熱する。その中、前記分解槽内には攪拌装置44が配置され、その攪拌装置44が15rpmぐらいの回転速度で分解槽内の混合物13を充分に攪拌し、混合物13の受熱を均一的にならせると共に、仕事温度に達させ、混合物13が分解する反応に利するように処置する。前記分解槽として密閉高圧反応槽を使用し、混合物13がその分解槽内で分解と吸着と毒性分解と中和などの分解61の反応を受け、且つ滅菌62を受け、その混合物13に分解反応後に液状肥料化の堆積放置処理不要の有機肥料産物23を形成する。分解装置32の下流にはさらに順次的に包装装置とパッケージング装置が配置され、それらによって前記液状肥料化体積放置処理不要の有機肥料産物23をパッケージングする。   FIG. 6 and FIG. 7 are explanatory views showing the organic fertilizer product 23 that is not required to be left as a liquid fertilizer produced by the present invention, and shows the storage tank 33 and the decomposition device 32 of the pretreatment device 30. A polishing device 41 is disposed between them, and an open-type preliminary tank 42 is disposed between the polishing device 41 and the disassembling device 32, and the polishing device 41 polishes the jam-like material 11 to jam the thin molecule jam-like material 19. And transported to the reserve tank 42. The microbial enzyme and the reaction additive 12 are added into the preparatory tank 42 and mixed with the fine molecular jam 19 to form a mixture 13, and the reaction additive is the fine molecular jam 19 reactant and carbon. It is used to adjust the ratio of nitrogen / nitrogen, thereby maintaining a predetermined acidity and being used to help break down microbial enzymes, changing the proportion of components of the reaction additive By doing so, it is possible to obtain different types of organic fertilizer products 25 that do not require sedimentation treatment. The preliminary tank 42 is provided with a diaphragm pump 45, which transports the mixture 13 to the decomposition tank of the decomposition device 32. The decomposition device 32 is provided with a material transport valve and a breathing valve, and the diaphragm pump 45 is in operation. It is provided in order to avoid generating a positive pressure in the decomposition tank and causing convection of air, and the heat source device 34 passes kerosene or steam through a check valve, a safety valve, and a pressure meter, and the decomposition device. The heat source device 34 heats the mixture 13 in the decomposition tank of the decomposition device 32 at a temperature of 100 degrees Celsius or more. Among them, a stirring device 44 is disposed in the decomposition tank, and the stirring device 44 sufficiently stirs the mixture 13 in the decomposition tank at a rotational speed of about 15 rpm, and makes the heat reception of the mixture 13 uniform. The working temperature is reached and the mixture 13 is treated to benefit the decomposition reaction. A closed high-pressure reaction tank is used as the decomposition tank, and the mixture 13 undergoes a reaction of decomposition 61 such as decomposition, adsorption, toxic decomposition, and neutralization in the decomposition tank, and also receives sterilization 62, and the mixture 13 undergoes a decomposition reaction. Later, an organic fertilizer product 23 is formed which does not require the deposition of the liquid fertilizer. A packaging device and a packaging device are sequentially arranged downstream of the decomposition device 32, and the organic fertilizer product 23 that does not require the liquid fertilizer volume leaving treatment is packaged by them.

図8と図9に示すのは、本発明の生成する固形肥料化の堆積放置処理不要の有機肥料産物24を示す説明図である。その中、前処理装置30の収納槽33と分解装置32との間には開放式予備槽42が設けられ、収納槽33よりジャム状物11を予備槽42へ輸送し、前記微生物酵素と反応添加物12が予備槽42に添加されてジャム状物11と混合して混合物13を生成し、前記反応添加物はジャム状物11の反応物とその炭素/窒素レシオを調整することに利用されるものであり、それによって所定の酸性を保持し、微生物酵素の分解に利するように使用するものであり、その反応添加物の成分比例を変更することによってそれぞれ異なるタイプの堆積放置不要の有機肥料産物25を取得できる。予備槽42内には隔膜式ポンプ45が設けられ、それによって混合物13を分解装置32の分解槽に輸送し、分解装置32にはさらに材料輸送バルブと呼吸バルブが設けられ、それらによって隔膜式ポンプ45の運転時に分解槽内において正圧力を生じて空気を対流させることを避けるために設けたものであり、混合物13の輸送も圧縮真空自己吸引法を使用でき、即ち、まず分解装置32を真空になるようにエアを抽出し、それから予備槽42を密封し、それから分解装置32を打開して自然に混合物13を分解装置32内へ吸い込ませる。熱源装置34が灯油または蒸気を逆止弁と安全弁と圧力メータを経由して分解装置32の分解槽の挟み層に輸送し、また、熱源装置34が摂氏100度以上の加熱温度によって分解装置32の分解槽内の混合物13を仕事温度まで加熱し、その中、前記分解槽内に攪拌装置44が配置され、攪拌装置44が15rpmぐらいの回転速度で分解槽内の混合物13を充分に攪拌し、その混合物13の受熱状況を均一的にならせると共に、仕事温度まで到達させ、混合物13に分解反応を進行させることに利するようにし、また、前記分解槽が真空槽であり、混合物13が分解槽内で分解と吸着と毒性解除と中和などの分解(61)反応と滅菌(62)を進行し、分解装置32には前記分解槽に接続される圧縮排気装置46が設けられ、前記分解装置32の熱源装置34が混合物13の含有する水分を摂氏150度ぐらいまで昇温し、それによって水分の分離を加速し、前記圧縮排気装置46が加熱によって生成する水蒸気20を抽出して乾燥処理を実行し、圧縮排気装置46の下流に順次的に熱交換器47と貯水装置49とろ過装置48とが設けられ、前記熱交換器47が水蒸気20を液体水21になるように熱交換冷却をし、かつその水分を前記貯水装置49に導入し、ろ過装置48がその液体水21をろ過して飲用水22を形成し、混合物13が分解されて固形化堆積放置処理不要有機肥料産物24になるように乾燥加工される。本発明の生成する固形肥料化堆積放置処理不要有機肥料産物24も、分解槽として一般の槽を使用し、且つ分解装置32にブロワー50を前記分解槽に連通するように配置するような方式によって処理でき、そうする場合では、材料輸送バルブと呼吸バルブを不要にすることが出来、前記ブロワー50によって直接的に加熱によって生成する水蒸気20を抽出し、乾燥加工を実行することが出来、混合物13が分解且つ乾燥されて固形肥料化堆積放置処理不要の有機肥料産物24を生成する。   FIG. 8 and FIG. 9 are explanatory diagrams showing the organic fertilizer product 24 that is not required to be deposited and left as solid fertilizer produced by the present invention. Among them, an open type preparatory tank 42 is provided between the storage tank 33 and the decomposition apparatus 32 of the pretreatment device 30, and the jammed material 11 is transported from the storage tank 33 to the preparatory tank 42 and reacted with the microbial enzyme. The additive 12 is added to the preliminary tank 42 and mixed with the jam 11 to form a mixture 13, which is used to adjust the reactant of the jam 11 and its carbon / nitrogen ratio. It is used to maintain a predetermined acidity and thereby be useful for the degradation of microbial enzymes. By changing the proportion of the components of the reaction additive, different types of organic materials that do not need to be deposited are left. The fertilizer product 25 can be acquired. A diaphragm pump 45 is provided in the preparatory tank 42, thereby transporting the mixture 13 to the decomposition tank of the decomposition apparatus 32, and the decomposition apparatus 32 is further provided with a material transport valve and a breathing valve, and thereby the diaphragm pump. It is provided in order to avoid generating positive pressure in the decomposition tank during the operation of 45 and causing convection of air, and the transport of the mixture 13 can also use the compression vacuum self-suction method, that is, the decomposition apparatus 32 is first evacuated. The air is then extracted, and then the preliminary tank 42 is sealed, and then the cracking device 32 is opened so that the mixture 13 is naturally sucked into the cracking device 32. The heat source device 34 transports kerosene or steam to the sandwiching layer of the decomposition tank of the decomposition device 32 via the check valve, the safety valve, and the pressure meter, and the heat source device 34 generates the decomposition device 32 at a heating temperature of 100 degrees Celsius or more. The mixture 13 in the decomposition tank is heated to the work temperature, and a stirring device 44 is disposed in the decomposition tank, and the stirring device 44 sufficiently stirs the mixture 13 in the decomposition tank at a rotation speed of about 15 rpm. The heat receiving condition of the mixture 13 is made uniform, reaches the work temperature, and is useful for allowing the mixture 13 to proceed with a decomposition reaction. The decomposition tank is a vacuum tank, and the mixture 13 is Decomposition (61) reaction and sterilization (62) such as decomposition, adsorption, toxicity release, and neutralization proceed in the decomposition tank, and the decomposition apparatus 32 is provided with a compression exhaust device 46 connected to the decomposition tank, Disassembly 32 heat source devices 34 raise the water content of the mixture 13 to about 150 degrees Celsius, thereby accelerating the separation of the water, and the compression exhaust device 46 extracts the water vapor 20 generated by the heating and performs a drying process. The heat exchanger 47, the water storage device 49, and the filtration device 48 are sequentially provided downstream of the compression / exhaust device 46, and the heat exchanger 47 performs heat exchange cooling so that the water vapor 20 becomes the liquid water 21. In addition, the water is introduced into the water storage device 49, and the filtration device 48 filters the liquid water 21 to form drinking water 22, and the mixture 13 is decomposed into an organic fertilizer product 24 that is not required to be solidified and deposited. It is dried so as to be. The organic fertilizer product 24 that is produced by the present invention and does not need to be left as it is is also used as a decomposition tank, and the blower 50 is arranged in the decomposition apparatus 32 so as to communicate with the decomposition tank. In this case, the material transport valve and the breathing valve can be dispensed with, the water vapor 20 produced by heating can be directly extracted by the blower 50, and the drying process can be carried out. Is decomposed and dried to produce an organic fertilizer product 24 which does not require solid fertilization and deposition treatment.

そのため、本発明の有機廃棄物堆積放置不要処理システム及びその処理方法による場合、少なくとも次のような産業上利用性と優れた点を有する。
(一)その前処理装置が有機廃棄物をジャム状物と表面油水混合液になるよう分離し、有機廃棄物を処理しやすくすることが出来、その前処理装置の油水分離装置が表面油水混合液を分離してリサイクル利用できる。
(二)前記前処理装置の砕け装置が有機廃棄物をジャム状物となるように砕け加工でき、有機廃棄物を微細化させることが出来、反応作用の表面面積を増加でき、3ないし24時間の速成処理効果を実現できる。
(三)前記ジャム状物に添加される微生物酵素と反応添加物と、前記分解装置とを合せて利用する場合、分解作業と滅菌作業とを実施でき、且つ堆積放置処理不要の有機肥料産物を生成してリサイクル利用できる。
(四)前記有機廃棄物堆積放置処理不要の処理システムが、同時に分解と吸着と毒性解除と中和と養分調整と熱分解とを実行できるので、その処理効率がかなり高く、人力を減少でき、且つ設備の使用するスペースが少なく、油、水、残滓がそれぞれリサイクルされて再利用され、排水がなく、悪臭や病気媒介生物を生成するなどの二次的汚染の課題も有しない。
(五)前記有機廃棄物にそれぞれ異なる反応添加物が添加されると、それぞれ異なるタイプの堆積放置処理不要の有機肥料産物、例えば、土壌改良剤や動物用餌や飼料添加剤や堆積放置処理不要有機肥料や堆積処理用肥料の菌類培養材料などを取得できるので、資源をフルに再利用でき、土壌の劣化されることを避けることが出来、且つ土壌の性質を改善でき、無効の養分を有効的な材料に転化させることが出来、農作物の成長性を向上できる。
For this reason, the organic waste deposition unneeded treatment system and the treatment method of the present invention have at least the following industrial applicability and excellent points.
(1) The pre-treatment device can separate the organic waste into jam-like material and surface oil / water mixture, making it easy to treat organic waste. The liquid can be separated and recycled.
(2) The crushing device of the pretreatment device can crush the organic waste so as to be jammed, the organic waste can be refined, the surface area of the reaction can be increased, and 3 to 24 hours It is possible to realize the rapid process effect.
(3) When the microbial enzyme and reaction additive added to the jam-like material are used in combination with the decomposition device, the decomposition and sterilization operations can be performed, and the organic fertilizer product that does not need to be deposited is not used. It can be generated and recycled.
(4) The above-mentioned treatment system that does not require organic waste accumulation treatment can simultaneously perform decomposition, adsorption, release of toxicity, neutralization, nutrient adjustment, and thermal decomposition, so that the treatment efficiency is considerably high and human power can be reduced. In addition, the space used by the facility is small, oil, water and residue are recycled and reused, there is no drainage, and there is no problem of secondary pollution such as generation of malodors and disease vectors.
(5) When different reaction additives are added to the organic waste, different types of organic fertilizer products that do not require sedimentation treatment, such as soil conditioners, animal feed, feed additives, and sedimentation treatment, are not required. Since it is possible to acquire fungal culture materials for organic fertilizers and sedimentation fertilizers, resources can be fully reused, soil deterioration can be avoided, soil properties can be improved, and invalid nutrients can be used effectively It can be converted into a new material and the growth of crops can be improved.

また、前記に具体的に説明したものは、単に本発明の実施可能な実施例に過ぎず、いずれの当該分野における技術者が本発明の明細書の記載と図面に開示した構造などの要旨に相同効果の修飾や変更などを実施できるが、それらも本発明の権利保護範囲内に納入されるべきことは言うまでもない。   Moreover, what has been specifically described above is merely an example in which the present invention can be implemented, and any technical person in the field concerned can describe the structure and the like disclosed in the description and drawings of the present invention. Although modifications and changes of the homologous effect can be implemented, it goes without saying that they should also be delivered within the scope of protection of the rights of the present invention.

従来の料理用状物の処理方法を示すフローチャートである。It is a flowchart which shows the processing method of the conventional culinary goods. 本発明の構成を示す説明図である。It is explanatory drawing which shows the structure of this invention. 本発明の処理フローを示す説明図である。It is explanatory drawing which shows the processing flow of this invention. 本発明の前処理装置の構造を示す説明図である。It is explanatory drawing which shows the structure of the pre-processing apparatus of this invention. 本発明の前処理過程を示す説明図である。It is explanatory drawing which shows the pre-processing process of this invention. 本発明の液状肥料化堆積放置処理不要有機肥料産物を生成する場合の構成を示す説明図である。It is explanatory drawing which shows the structure in the case of producing | generating the organic fertilizer product which does not need the liquid fertilizer accumulation deposition process of this invention. 本発明の液状肥料化堆積放置処理不要有機肥料産物を生成する場合のフローを示す説明図である。It is explanatory drawing which shows the flow in the case of producing | generating the organic fertilizer product which does not need the liquid fertilizer accumulation deposition process of this invention. 本発明の固形肥料化堆積放置処理不要有機肥料産物を生成する場合の構成を示す説明図である。It is explanatory drawing which shows the structure in the case of producing | generating the organic fertilizer product which does not require solid fertilizer accumulation deposition processing of this invention. 本発明の固形肥料化堆積放置処理不要有機肥料産物を生成する場合のフローを示す説明図である。It is explanatory drawing which shows the flow in the case of producing | generating the organic fertilizer product which does not require solid fertilizer accumulation deposition processing of this invention.

符号の説明Explanation of symbols

10 有機廃棄物
11 ジャム状物
12 微生物酵素と反応添加物
13 混合物
15 表面油水混合液
16 油液
17 回収水
19 細い分子ジャム状物
20 水蒸気
21 液体水
22 飲用水
23 液状肥料化堆積放置処理不要有機肥料産物
24 固形肥料化堆積放置処理不要有機肥料産物
25 堆積放置処理不要有機肥料産物
26 油含有ジャム状物
30 前処理装置
31 砕け装置
32 分解装置
33 収納槽
34 熱源装置
35 油水分離装置
36 油収集管路
37 水収集管路
39、44 攪拌装置
41 研磨装置
42 予備槽
45 隔膜式ポンプ
46 圧縮排気装置
47 熱交換器
48 ろ過装置
49 貯水装置
50 ブロワー
60 砕け加工
61 分解加工
62 滅菌加工
DESCRIPTION OF SYMBOLS 10 Organic waste 11 Jam-like substance 12 Microbial enzyme and reaction additive 13 Mixture 15 Surface oil water mixed liquid 16 Oil liquid 17 Collected water 19 Fine molecular jam-like substance 20 Water vapor 21 Liquid water 22 Drinking water 23 Organic fertilizer product 24 Solid fertilizer deposition accumulation treatment unnecessary organic fertilizer product 25 Organic sedimentation treatment unnecessary organic fertilizer product 26 Oil-containing jam-like material 30 Pretreatment device 31 Crushing device 32 Decomposition device 33 Storage tank 34 Heat source device 35 Oil water separator 36 Oil Collection line 37 Water collection line 39, 44 Stirring device 41 Polishing device 42 Preliminary tank 45 Diaphragm pump 46 Compression exhaust device 47 Heat exchanger 48 Filtration device 49 Water storage device 50 Blower 60 Crushing process 61 Decomposition process 62 Sterilization process

Claims (8)

熱源装置と、
有機廃棄物を導入してジャム状物になるように処理する前処理装置と、
前記前処理装置の下流に配置され、前記ジャム状物に微生物酵素と所定の添加物を添加することにより生成された混合物を分解する分解装置と、
を含み、
前記熱源装置が前記混合物を加熱し、前記分解装置が前記混合物を分解すると共に、滅菌を実行することによって堆積放置不要の有機肥料産物を製造し、
前記前処理装置には、収納槽と、砕け装置と、油水分離装置とが含まれ、前記収納槽が前記砕け装置の下流に位置し、前記油水分離装置が前記収納槽の下流に位置し、前記砕け装置には有機廃棄物が導入され、前記砕け装置が前記有機廃棄物を砕けて油含有ジャム状物を生成し、該油含有ジャム状物を前記収納槽に導入し、前記熱源装置が前記収納槽内の該油含有ジャム状物を加熱して前記ジャム状物と表面油水混合液とを分離させ、前記油水分離装置にはそれぞれ油収集管路と水収集管路が設けられ、前記水収集管路が前記収納槽の上流まで接続され
前記前処理装置の前記収納槽と前記分解装置との間には研磨装置が配置され、当該研磨装置と前記分解装置との間には開放式予備槽が配置され、前記研磨装置が前記ジャム状物を研磨して細い分子のジャム状物を生成し、且つ前記予備槽に輸送し、前記微生物酵素と前記添加物が前記予備槽内に添加されて、前記細い分子のジャム状物と混合して前記混合物を生成し、前記予備槽には隔膜式ポンプが設けられ、該隔膜式ポンプによって前記混合物を前記分解装置の分解槽へ輸送し、前記分解槽内には攪拌装置が配置され、また、前記分解装置には材料輸送バルブと呼吸バルブが配置され、前記熱源装置が前記分解槽内の混合物を加熱し、前記分解槽として密閉高圧反応槽を使用し、前記混合物に液状肥料化堆積放置処理不要の有機肥料産物を形成させるように分解加工を実行する、
ことを特徴とする有機廃棄物堆積放置不要処理システム。
A heat source device;
A pre-treatment device that introduces organic waste and processes it into jam-like materials;
A decomposing apparatus that is disposed downstream of the pretreatment apparatus and decomposes a mixture produced by adding a microbial enzyme and a predetermined additive to the jam-like material;
Including
The heat source device heats the mixture, the decomposition device decomposes the mixture, and performs sterilization to produce an unfertilized organic fertilizer product,
The pretreatment device includes a storage tank, a crushing device, and an oil / water separation device, the storage tank is located downstream of the crushing device, and the oil / water separation device is located downstream of the storage tank, Organic waste is introduced into the crushing device, the crushing device crushes the organic waste to produce an oil-containing jam, introduces the oil-containing jam into the storage tank, and the heat source device The oil-containing jam in the storage tank is heated to separate the jam and the surface oil / water mixture, and the oil / water separator is provided with an oil collection line and a water collection line, respectively. A water collection line is connected to the upstream of the storage tank ,
A polishing apparatus is disposed between the storage tank and the decomposition apparatus of the pretreatment apparatus, an open-type preliminary tank is disposed between the polishing apparatus and the decomposition apparatus, and the polishing apparatus has a jam shape. The product is polished to produce a fine molecule jam and transported to the preparatory tank, where the microbial enzyme and the additive are added to the preparatory tank and mixed with the thin molecular jam. The mixture is produced, and the preliminary tank is provided with a diaphragm pump, and the diaphragm pump transports the mixture to the decomposition tank of the decomposition apparatus, and a stirring apparatus is disposed in the decomposition tank. The decomposition apparatus is provided with a material transport valve and a breathing valve, the heat source device heats the mixture in the decomposition tank, uses a sealed high-pressure reaction tank as the decomposition tank, and the liquid fertilizer deposition deposits in the mixture Organic fertilizer products that do not require treatment Performing a decomposition process so as to made,
An organic waste accumulation-free treatment system characterized by that.
前記前処理装置の前記収納槽と前記分解装置との間には開放式予備槽が配置され、前記収納槽が前記ジャム状物を前記予備槽に輸送し、前記微生物酵素と前記添加物が前記予備槽内に添加されて、前記ジャム状物と混合して混合物を生成し、前記予備槽には隔膜式ポンプが設けられ、該隔膜式ポンプによって前記混合物を前記分解装置の分解槽へ輸送し、前記分解槽内には攪拌装置が配置され、また、前記分解装置には材料輸送バルブと呼吸バルブが配置され、前記熱源装置が前記分解槽内の前記混合物を加熱し、前記分解槽として真空槽を使用し、前記分解装置には前記分解槽に接続される圧縮排気装置が設けられ、前記圧縮排気装置が加熱によって生成する水蒸気を抽出して乾燥処理を実行し、圧縮排気装置の下流に順次的に熱交換器と貯水装置とろ過装置とが設けられ、前記熱交換器が前記水蒸気を液体水になるように熱交換冷却をし、かつその水分を前記貯水装置に導入し、前記ろ過装置がその液体水をろ過して飲用水を形成し、前記混合物が分解されて固形化堆積放置処理不要有機肥料産物になるように乾燥加工される、
ことを特徴とする請求項1に記載の有機廃棄物堆積放置不要処理システム。
An open-type preliminary tank is disposed between the storage tank and the decomposition apparatus of the pretreatment device, the storage tank transports the jam-like material to the preliminary tank, and the microbial enzyme and the additive are the It is added to a preliminary tank and mixed with the jam to produce a mixture. The preliminary tank is provided with a diaphragm pump, and the diaphragm pump is used to transport the mixture to the decomposition tank of the decomposition apparatus. A stirring device is disposed in the decomposition tank, a material transport valve and a breathing valve are disposed in the decomposition apparatus, the heat source device heats the mixture in the decomposition tank, and the vacuum is used as the decomposition tank. The decomposition apparatus is provided with a compression exhaust device connected to the decomposition tank, the steam generated by heating is extracted from the compression exhaust apparatus, a drying process is performed, and the downstream of the compression exhaust apparatus Sequentially with heat exchanger A water device and a filtration device are provided, the heat exchanger cools the water vapor so that it becomes liquid water, and introduces the moisture into the water storage device, and the filtration device filters the liquid water. To form potable water, and the mixture is decomposed and dried so that it becomes an organic fertilizer product that does not require solidification and deposition,
The organic waste accumulation-needed treatment system according to claim 1.
前記前処理装置の前記収納槽と前記分解装置との間には開放式予備槽が配置され、前記収納槽が前記ジャム状物を前記予備槽に輸送し、前記微生物酵素と前記添加物が前記予備槽内に添加されて、前記ジャム状物と混合して混合物を生成し、前記予備槽には隔膜式ポンプが設けられ、該隔膜式ポンプによって前記混合物を前記分解装置の分解槽へ輸送し、前記分解槽内に攪拌装置が配置され、前記熱源装置が前記分解槽内の前記混合物を加熱し、前記分解装置にはブロワーが前記分解槽に連通するように配置され、前記ブロワーによって直接的に加熱によって生成する水蒸気を抽出し、前記混合物が分解且つ乾燥されて固形肥料化堆積放置処理不要の有機肥料産物を生成する、
ことを特徴とする請求項1に記載の有機廃棄物堆積放置不要処理システム。
An open-type preliminary tank is disposed between the storage tank and the decomposition apparatus of the pretreatment device, the storage tank transports the jam-like material to the preliminary tank, and the microbial enzyme and the additive are the It is added to a preliminary tank and mixed with the jam to produce a mixture. The preliminary tank is provided with a diaphragm pump, and the diaphragm pump is used to transport the mixture to the decomposition tank of the decomposition apparatus. A stirring device is disposed in the cracking tank, the heat source device heats the mixture in the cracking tank, and a blower is disposed in the cracking device so as to communicate with the cracking tank. The steam generated by heating is extracted, and the mixture is decomposed and dried to produce an organic fertilizer product that does not require solid fertilization and sedimentation treatment,
The organic waste accumulation-needed treatment system according to claim 1.
前記熱源装置として密閉循環式ホット灯油加熱システムまたは密閉循環式蒸気加熱システムを採用し、ボイラー加熱または電源加熱の方式を選択的に採用する、
ことを特徴とする請求項1に記載の有機廃棄物堆積放置不要処理システム。
Adopting a closed circulation hot kerosene heating system or a closed circulation steam heating system as the heat source device, selectively adopting a boiler heating or power supply heating method,
The organic waste accumulation-needed treatment system according to claim 1.
前記熱源装置と前記前処理装置と前記分解装置とが所定の電気回路コントロール・ユニットに電気的に接続される、
ことを特徴とする請求項1に記載の有機廃棄物堆積放置不要処理システム。
The heat source device, the pretreatment device, and the decomposition device are electrically connected to a predetermined electric circuit control unit.
The organic waste accumulation-needed treatment system according to claim 1.
有機廃棄物を砕けてジャム状物に形成させるステップ(一)と、
微生物酵素と添加物を前記ジャム状物に添加して混合物を生成させるステップ(二)と、
前記混合物を分解させると共に、滅菌を実行することによって堆積放置不要の有機肥料産物を作るステップ(三)と、
を含み、
前記ステップ(一)では、前記有機廃棄物を前処理装置に導入して砕けさせながら、熱源装置によって加熱して前記ジャム状物を生成し、且つ前記ステップ(三)では、前記混合物を分解装置に導入すると共に、前記熱源装置によって前記混合物を加熱し、
前記ステップ(一)において、
前記前処理装置には、収納槽と、砕け装置と、油水分離装置とが含まれ、前記収納槽が前記砕け装置の下流に位置し、前記油水分離装置が前記収納槽の下流に位置し、前記砕け装置には前記有機廃棄物が導入され、前記砕け装置が前記有機廃棄物を砕けて油含有ジャム状物を生成し、該油含有ジャム状物を前記収納槽に導入し、前記熱源装置が前記収納槽内の油含有ジャム状物を加熱して前記ジャム状物と表面油水混合液とを分離させ、前記油水分離装置にはそれぞれ油収集管路と水収集管路が設けられ、前記水収集管路が前記収納層の上流まで接続され
前記ステップ(三)において、
前記前処理装置の前記収納槽と前記分解装置との間には研磨装置が配置され、当該研磨装置と前記分解装置との間には開放式予備槽が配置され、前記研磨装置が前記ジャム状物を研磨して細い分子のジャム状物を生成し、且つ前記予備槽に輸送し、前記微生物酵素と前記添加物が前記予備槽内に添加されて、前記細い分子のジャム状物と混合して前記混合物を生成し、前記予備槽には隔膜式ポンプが設けられ、該隔膜式ポンプによって前記混合物を前記分解装置の分解槽へ輸送し、前記分解槽内には攪拌装置が配置され、また、前記分解装置には材料輸送バルブと呼吸バルブが配置され、前記熱源装置が前記分解槽内の前記混合物を加熱し、前記分解槽として密閉高圧反応槽を使用し、前記混合物に液状肥料化堆積放置処理不要の有機肥料産物を形成させるように分解加工を実行する、
ことを特徴とする有機廃棄物堆積放置不要処理方法。
Crushing organic waste to form jams (1);
Adding a microbial enzyme and an additive to the jam to form a mixture (2);
Decomposing the mixture and performing sterilization to produce an unfertilized organic fertilizer product (3);
Including
In the step (1), the organic waste is introduced into a pretreatment device to be crushed and heated by a heat source device to produce the jam-like material. In the step (3), the mixture is decomposed. And heating the mixture by the heat source device,
In the step (1),
The pretreatment device includes a storage tank, a crushing device, and an oil / water separation device, the storage tank is located downstream of the crushing device, and the oil / water separation device is located downstream of the storage tank, The organic waste is introduced into the crushing device, the crushing device crushes the organic waste to produce an oil-containing jam, the oil-containing jam is introduced into the storage tank, and the heat source device The oil-containing jam in the storage tank is heated to separate the jam from the surface oil / water mixture, and the oil / water separator is provided with an oil collecting line and a water collecting line, respectively. A water collection line is connected to the upstream of the storage layer ,
In the step (3),
A polishing apparatus is disposed between the storage tank and the decomposition apparatus of the pretreatment apparatus, an open-type preliminary tank is disposed between the polishing apparatus and the decomposition apparatus, and the polishing apparatus has a jam shape. The product is polished to produce a fine molecule jam and transported to the preparatory tank, where the microbial enzyme and the additive are added to the preparatory tank and mixed with the thin molecular jam. The mixture is produced, and the preliminary tank is provided with a diaphragm pump, and the diaphragm pump transports the mixture to the decomposition tank of the decomposition apparatus, and a stirring apparatus is disposed in the decomposition tank. The decomposition apparatus includes a material transport valve and a breathing valve, the heat source apparatus heats the mixture in the decomposition tank, uses a sealed high-pressure reaction tank as the decomposition tank, and deposits liquid fertilizer on the mixture Organic fertilizer production without leaving treatment Performing a decomposition process so as to form a,
An organic waste accumulation-free treatment method characterized by that.
前記ステップ(三)において、
前記前処理装置の前記収納槽と前記分解装置との間には開放式予備槽が配置され、前記収納槽が前記ジャム状物を前記予備槽に輸送し、前記微生物酵素と前記添加物が前記予備槽内に添加されて、前記ジャム状物と混合して前記混合物を生成し、前記予備槽には隔膜式ポンプが設けられ、該隔膜式ポンプによって前記混合物を前記分解装置の分解槽へ輸送し、前記分解槽内には攪拌装置が配置され、また、前記分解装置には材料輸送バルブと呼吸バルブが配置され、前記熱源装置が前記分解槽内の前記混合物を加熱し、前記分解槽として真空槽を使用し、前記分解装置には前記分解槽に接続される圧縮排気装置が設けられ、前記圧縮排気装置が加熱によって生成する水蒸気を抽出して乾燥処理を実行し、圧縮排気装置の下流に順次的に熱交換器と貯水装置とろ過装置とが設けられ、前記熱交換器が前記水蒸気を液体水になるように熱交換冷却をし、かつその水分を前記貯水装置に導入し、前記ろ過装置がその液体水をろ過して飲用水を形成し、前記混合物が分解されて固形化堆積放置処理不要有機肥料産物になるように乾燥加工される、
ことを特徴とする請求項6に記載の有機廃棄物堆積放置不要処理方法。
In the step (3),
An open-type preliminary tank is disposed between the storage tank and the decomposition apparatus of the pretreatment device, the storage tank transports the jam-like material to the preliminary tank, and the microbial enzyme and the additive are the It is added into a preliminary tank and mixed with the jam to produce the mixture. The preliminary tank is provided with a diaphragm pump, and the diaphragm pump transports the mixture to the decomposition tank of the decomposition apparatus. A stirring device is disposed in the decomposition tank, a material transport valve and a breathing valve are disposed in the decomposition apparatus, and the heat source device heats the mixture in the decomposition tank, and serves as the decomposition tank. A vacuum tank is used, and the decomposition apparatus is provided with a compression exhaust apparatus connected to the decomposition tank. The compression exhaust apparatus extracts a water vapor generated by heating to perform a drying process, and the downstream of the compression exhaust apparatus. Sequentially heat exchange And a water storage device and a filtration device, the heat exchanger cools the water vapor so that it becomes liquid water, and introduces the water into the water storage device, and the filtration device removes the liquid water. Filtered to form potable water, and the mixture is decomposed and dried to become an organic fertilizer product that does not need to be solidified and deposited,
7. The organic waste accumulation-needed treatment method according to claim 6 ,
前記ステップ(三)において、
前記前処理装置の前記収納槽と前記分解装置との間には開放式予備槽が配置され、前記収納槽が前記ジャム状物を前記予備槽に輸送し、前記微生物酵素と前記添加物が前記予備槽内に添加されて、前記ジャム状物と混合して前記混合物を生成し、前記予備槽には隔膜式ポンプが設けられ、該隔膜式ポンプによって前記混合物を前記分解装置の分解槽へ輸送し、前記分解槽内には攪拌装置が配置され、前記熱源装置が前記分解槽内の混合物を加熱し、前記分解装置にはブロワーが前記分解槽に連通するように配置され、前記ブロワーによって直接的に加熱によって生成する水蒸気を抽出し、前記混合物が分解且つ乾燥されて固形肥料化堆積放置処理不要の有機肥料産物を生成する、
ことを特徴とする請求項6に記載の有機廃棄物堆積放置不要処理方法。
In the step (3),
An open-type preliminary tank is disposed between the storage tank and the decomposition apparatus of the pretreatment device, the storage tank transports the jam-like material to the preliminary tank, and the microbial enzyme and the additive are the It is added into a preliminary tank and mixed with the jam to produce the mixture. The preliminary tank is provided with a diaphragm pump, and the diaphragm pump transports the mixture to the decomposition tank of the decomposition apparatus. In addition, a stirring device is disposed in the decomposition tank, the heat source device heats the mixture in the decomposition tank, and a blower is disposed in the decomposition device so as to communicate with the decomposition tank. Water vapor produced by heating is extracted, and the mixture is decomposed and dried to produce an organic fertilizer product that does not require solid fertilization and sedimentation treatment.
7. The organic waste accumulation-needed treatment method according to claim 6 ,
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