JP2012096219A - Technique and equipment for substance circulation in organism waste - Google Patents

Technique and equipment for substance circulation in organism waste Download PDF

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JP2012096219A
JP2012096219A JP2011103915A JP2011103915A JP2012096219A JP 2012096219 A JP2012096219 A JP 2012096219A JP 2011103915 A JP2011103915 A JP 2011103915A JP 2011103915 A JP2011103915 A JP 2011103915A JP 2012096219 A JP2012096219 A JP 2012096219A
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waste
carbon
biological
soil
nitrogen
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JP5625201B2 (en
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Jiao Xuezhen
学真 矯
Jiao Xuecheng
学成 矯
Sho Ikeda
捷 池田
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Gakushin Kyo
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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
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00Combustion technologies with mitigation potential
    • Y02E20/12Heat utilisation in combustion or incineration of waste
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/10Process efficiency
    • Y02P20/129Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines
    • 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
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/30Wastewater or sewage treatment systems using renewable energies
    • Y02W10/37Wastewater or sewage treatment systems using renewable energies using solar energy
    • 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
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/40Valorisation of by-products of wastewater, sewage or sludge processing
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/20Waste processing or separation

Abstract

PROBLEM TO BE SOLVED: To provide a method for storing carbon, nitrogen, minerals and the like of organism waste in order to circulate into soil, instead of embedding, composting or burning.SOLUTION: Waste is treated by "a low oxygen circulation system with sealed hot air" composed of a combination of a drying kiln, a condenser and a hot blast stove and by a process of "scenting-condensation-carbonization". Waste is feed to a drying kiln for scenting drying, sterilization deodorizing, solid separation and mineralization, and then vaporized liquid in a discharged gas of the kiln is collected by condensation by a condensation device to obtain vinegar liquid of organisms. The scented dried products produced from the kiln are classified into organisms and artificial products, and the former ones are scented organisms storing carbon and nitrogen and can be refined into scented organism fertilizer or carbon nitrogen agent. The latter ones are carbonized in the hot blast furnace. Hot air generated is once again sucked into the drying kiln, and successively transportation of heat and substances is performed. Zero emission of dioxin and gas by green house effect is achieved. Since nutritional elements in organism waste can be returned 100% to soil, substances can be circulated and soil can be enriched, and further the amount of organic carbon in soil can be increased.

Description

本発明は「生物体(バイオマス)廃棄物」における栄養元素貯留循環技術及び設備について触れる。ここで触れる生物体廃棄物とは、生ごみと食品加工や農林牧漁業廃棄物等中の生物体廃棄物及び家畜家禽糞又は下水汚泥等(以下「ごみ」又は「生物体廃棄物」と称す) のことを指す。即ちこれも生ごみや下水汚泥等の廃棄物処理の新しい方式である。本発明では、生態学や生物学、環境学、土壌学、植物栄養肥料学、化学、熱学、廃棄物処理、バイオマスエネルギー等の技術分野に触れる。   The present invention touches on nutrient element storage and circulation technology and equipment in “organism (biomass) waste”. The biological waste mentioned here refers to biological waste in food waste, food processing, agriculture, forestry, and fishery waste, livestock poultry manure, sewage sludge, etc. (hereinafter referred to as `` garbage '' or `` biological waste ''). ). That is, this is also a new method for waste disposal such as garbage and sewage sludge. The present invention touches on technical fields such as ecology, biology, environmental science, soil science, plant nutrition fertilizer science, chemistry, thermology, waste treatment, and biomass energy.

生物体廃棄物処理の1例として生ごみ処理の現状を見てみよう。今採用されている生ごみ処理は主に埋め立てや堆肥化、焼却(発電)という3つの方式がある。ごみ埋め立ての場合、大量の土地を占用するほか、悪臭を生じ、ろ液の浸出、メタンガスCH4と二酸化炭素CO2等の温室効果ガスが発生する。堆肥の場合はメタンや亜酸化窒素N2O等の温室効果ガスも生成し、また良質な肥料を製造するのは難しく、炭素・窒素等の揮発損失は大きい。焼却処理は本来土壌に還すべき生物体中の炭素・窒素も人為的に「短絡」揮発され、大量に焼却した結果、二酸化炭素・窒素酸化物等の排出汚染や資源損失が発生し、また発がん性物質であるダイオキシンも生じ易い。これは人類の重大な「過ち」であるかもしれない。さらにこの処理には非常に高いコストがかかる割に、エネルギーへの還元率は低い。この従来式生ごみ焼却処理プロセスは、ダイオキシン生成の条件を備えることから排ガス中のダイオキシン包含量は比較的高く、大気中のダイオキシンの90%はごみ焼却による。このごみ焼却をいち早く進めてきた国又は地域ではすでにダイオキシン被害が深刻である。このことから埋め立てや堆肥化、焼却(発電)の各方式はそれぞれ致命的弊害を抱え、いずれも無害処理を達成することができなく、理想的な処理方法とは言えない。   Let's look at the current state of garbage disposal as an example of biological waste disposal. Currently, there are three main types of garbage disposal: landfill, composting, and incineration (power generation). In the case of landfill, in addition to occupying a large amount of land, it produces a foul odor, leaching the filtrate, and generating greenhouse gases such as methane gas CH4 and carbon dioxide CO2. In the case of compost, greenhouse gases such as methane and nitrous oxide N2O are also generated, and it is difficult to produce high-quality fertilizers, and the volatilization loss of carbon and nitrogen is large. The incineration process artificially causes carbon and nitrogen in organisms that should be returned to the soil to be “short-circuited” and volatilized. As a result of large-scale incineration, emission pollution such as carbon dioxide and nitrogen oxides and resource loss occur, and carcinogenesis occurs. Dioxin, which is a chemical substance, is also likely to occur. This may be a serious “error” of humanity. Furthermore, although this process requires a very high cost, the reduction rate to energy is low. Since this conventional garbage incineration process has conditions for generating dioxins, the amount of dioxins contained in the exhaust gas is relatively high, and 90% of the dioxins in the atmosphere are from incineration. Dioxin damage is already serious in the country or region where waste incineration has been promoted. For this reason, landfilling, composting, and incineration (power generation) methods each have fatal harmful effects, and none of them can achieve harmless treatment, and are not ideal treatment methods.

先進国が埋め立て処理から焼却処理を主として転向して以来、ダイオキシン等の致命的な危害の発現により、ごみ焼却技術の「先進性」に対し懐疑的である。一方発展途上国では、依然として埋め立て処理が主流であったが、年々焼却処理が増加傾向にあり、この処理の「メリット」について物議を醸す中「焼却」事業が発展しつつある。疑う余地なく、従来式のごみ焼却が発展し続け、結果としてダイオキシンが倍増し、地球の生態環境と我々の生存環境を著しく破壊しようとしている。これはまさに人類社会の発展による最大の危機、-生態の災難-である。   Ever since advanced countries turned from incineration to incineration, they are skeptical about the “advancement” of waste incineration technology due to the emergence of fatal hazards such as dioxins. On the other hand, landfilling is still the mainstream in developing countries, but incineration is increasing year by year, and the “incineration” business is developing while controversial over the “merits” of this treatment. Undoubtedly, traditional incineration continues to develop, and as a result, dioxins are doubling, trying to significantly destroy the ecological environment of our planet and our living environment. This is exactly the greatest crisis caused by the development of human society, the ecological disaster.

特開2010−1169号公報JP 2010-1169 A 特開2008−20093号公報JP 2008-20093 A

George Tchobanoglous,Hilary Theisen,Samuel Vigil 「INTEGRATED SOLID WASTER MANAGEMENT」Engineering Principles and Management Issues 1993 by McGraw-Hill,Inc. 田中勝監訳代表 「廃棄物処理総論」廃棄物工学の原理と廃棄物処理の問題 エヌ・ティー・エス 1998年George Tchobanoglous, Hilary Theisen, Samuel Vigil “INTEGRATED SOLID WASTER MANAGEMENT” Engineering Principles and Management Issues 1993 by McGraw-Hill, Inc. TS 1998 福本勤著 産業・都市・放射性「廃棄物処理技術」 新増補:ダイオキシン類ゼロ化技術(増訂2版) 共立出版株式会社 1998年Fukumoto Tsutomu Industry / city / radioactive “waste treatment technology” New supplement: Dioxin zeroization technology (2nd edition) Kyoritsu Publishing Co., Ltd. 1998 下平利和著 自然と共生する循環型社会形成のための 生態系に学ぶ「廃棄物処理技術」 ほおずき書籍 2011年Toshikazu Shimohira “Waste disposal technology” learned from the ecosystem for the creation of a recycling-oriented society in harmony with nature Hozuki Book 2011 NPO法人生ごみリサイクル全国ネットーワーク著 ガイドブックNo.2「生ごみのふしぎ!」 日報出版株式会社 2010年NPO Life Garbage Recycling Nationwide Network Guidebook No.2 “Mystery of Garbage!” Nikkan Publishing Co., Ltd. 2010 久馬一剛編 「最新土壌学」 朝倉書店 1997年Kazuyoshi Hisuma “Latest Soil Science” Asakura Shoten 1997 山崎耕宇等著 「植物栄養・肥料学」 朝倉書店 1993年Kosuke Yamazaki "Plant nutrition and fertilizers" Asakura Shoten 1993 西尾道徳著 「農業と環境汚染」日本と世界の土壌環境政策と技術 農文協 2005年Michinori Nishio “Agriculture and Environmental Pollution” Japan and the World Soil Environmental Policy and Technology 惣田いく(上に日下に立という漢字)夫等著 「物質と生命科学」 現代図書 2011年Iku Hamada (Kanji above Kusakabe) “Matter and Life Sciences” Modern Books 2011 松原聡著 「環境生物科学」(改訂版) 裳華房 2006年Akira Matsubara “Environmental Biological Sciences” (revised edition) Hanakabo 2006

ごみ焼却処理の技術的問題点では、我々は考えている2つの望ましくないことがある。   In the technical problem of waste incineration, there are two undesirable things we consider.

その1、燃やすことは望ましくない。生物体(バイオマス)廃棄物を「焼却」するもったいないだけではなく、温室効果ガスや有害排ガスも発生する。焼却する場合に生物体廃棄物中の炭素や窒素等の栄養元素は土に戻られず温室効果ガスや有害排ガス、水蒸気等に転換して大気中に排出しまい、貴重な土壌の有機栄養資源の「短絡」損失が生ずる。焼却を続ければ、生態系における物質循環の悪化や土壌有機炭素貯留量の減少、土壌肥沃度の低下、地球温暖化等の問題を解決することは難しくなるだろう。   First, it is not desirable to burn. Not only is it wasteful to “incinerate” biological (biomass) waste, but it also generates greenhouse gases and harmful exhaust gases. When incinerated, nutrient elements such as carbon and nitrogen in biological waste are not returned to the soil, but are converted into greenhouse gases, harmful exhaust gases, water vapor, etc., and discharged into the atmosphere. A “short circuit” loss occurs. If incineration continues, it will be difficult to solve problems such as deterioration of material circulation in ecosystems, reduction of soil organic carbon storage, reduction of soil fertility, and global warming.

その2、湿式焼却することは望ましくない。ごみの湿式焼却はダイオキシンが生じやすい。従来のごみ焼却方法は湿式焼却で、乾燥と燃焼プロセスは同一の焼却炉で行っている。生ごみに水分を多く含んでるため、乾燥及び燃焼初期における焼却炉内温度を低下させることにつながり、800℃以下(特に250〜600℃の間)で焼却すると、水蒸気と塩化物との不完全燃焼でダイオキシンの発生しやすくなる。   Second, wet incineration is undesirable. Dioxins are likely to occur during the wet incineration of garbage. The conventional waste incineration method is wet incineration, and the drying and combustion processes are performed in the same incinerator. Since the garbage contains a lot of water, it leads to a decrease in the temperature in the incinerator at the beginning of drying and combustion, and incineration at 800 ° C or less (especially between 250 and 600 ° C) causes incomplete steam and chloride. Dioxins are easily generated by combustion.

本発明では、生ごみや汚水汚泥等の生物体廃棄物の焼却とダイオキシンや温室効果ガス、有害物質の大気中への排出を避け、埋め立てや堆肥化、焼却する代わりに生物体中の炭素や窒素、ミネラル等のエネルギーと栄養元素等を100%程に貯留し、炭素を緩効・惰効化、栄養元素を可給態化又は無機化して土壌へ循環させ、肥沃な土壌を育め、土壌有機炭素貯留量を増やせる方法を提供する。 In the present invention, incineration of biological wastes such as garbage and sewage sludge and dioxins, greenhouse gases, and emission of harmful substances into the atmosphere are avoided, and instead of landfilling, composting, or incineration, Energy and nutrient elements, such as nitrogen and minerals, are stored to about 100%, carbon is released slowly and fertilized, nutrient elements are made available or mineralized and circulated through the soil to cultivate fertile soil, Provide a way to increase soil organic carbon storage.

本発明の生物体(バイオマス)廃棄物におけるエネルギーと栄養元素(炭素や窒素、ミネラル等)を貯留して土壌へ循環させる技術(「炭素・窒素貯留技術」又は「物質循環技術」と称す)は、乾燥窯や凝縮器(又は凝縮槽)、熱風炉等を組み合わせた「低酸素熱風密閉式循環システム」及び「薫留(薫煙蒸留)‐凝縮‐乾留」工程に基づいてごみ(生ごみと食品加工や農林牧漁業廃棄物及び家畜家禽糞又は下水汚泥等)を薫留乾燥や殺菌消臭、固液分離してからその蒸発液は凝縮回収し、その薫留乾物は「生物体」や「人工物」等に分類し(うち生物体に炭素や窒素、ミネラル等のエネルギーと栄養元素が貯留されており、且つ炭素が惰効化、栄養元素が可給態化又は無機化され)、それぞれ「生物酢液」や「生物薫肥」又は「炭素窒素剤」(土壌全元素剤-生物複合肥料)等を精製して生物ごみの栄養元素を100%貯留して植物の全元素肥料として土壌に還すことでその物質循環が生かせ、肥沃な土壌を育め、土壌有機炭素貯留量を増やせ、またダイオキシンや温室効果ガス、有害物質のゼロエミッションを実現する生態系における「物質循環技術」である。 Technology for storing energy and nutrient elements (carbon, nitrogen, minerals, etc.) in the biological waste (biomass) of the present invention and circulating it to the soil (referred to as `` carbon / nitrogen storage technology '' or `` material circulation technology '') , Based on the `` low oxygen hot air closed circulation system '' and `` Shiodome (smoke distillation) -condensation-dry distillation '' process combined with a drying kiln, condenser (or condensing tank), hot air furnace, etc. Food processing, agriculture, forestry, and fishery waste, livestock poultry manure or sewage sludge, etc.) are subjected to destillation drying, sterilization and deodorization, solid-liquid separation, and then the evaporated liquid is condensed and recovered. Classified as `` artificial '' etc. (of which energy and nutrient elements such as carbon, nitrogen, mineral etc. are stored in the organism, and carbon is effective, nutrient elements are made available or mineralized) “Biological vinegar”, “Biological manure” or “Carbon nitrogen agent” By refining (composite fertilizer) etc. and storing 100% of the nutrient elements of biological waste and returning it to the soil as all-element fertilizer of the plant, it is possible to make use of its material cycle, nurture fertile soil, and increase soil organic carbon storage In addition, it is a “material recycling technology” in ecosystems that realizes zero emissions of dioxins, greenhouse gases, and harmful substances.

本発明の技術的特徴は、下記プロセスの複合により実現する。   The technical features of the present invention are realized by a combination of the following processes.

(1)、乾燥窯や凝縮器(コンデンサーとサイクロン分離器又は凝縮槽等)、生物酢液貯留装置、熱風炉、太陽光発電システム、二段ヒートポンプとヒートパイプ余熱回収システム(以下「余熱回収システム」と称す)等を組み合わせた「低酸素熱風密閉式循環システム」(以下「密閉式システム」と称す)を設置する。この「密閉式システム」でごみを「薫留‐凝縮‐乾留」の処理工程を行う。   (1) Drying kiln, condenser (condenser and cyclone separator or condenser tank, etc.), biological vinegar storage device, hot stove, solar power generation system, two-stage heat pump and heat pipe residual heat recovery system (hereinafter referred to as `` remaining heat recovery system '') "Low oxygen hot air closed circulation system" (hereinafter referred to as "closed system"). This “closed system” is used to process the waste “condensation-condensation-dry distillation”.

(2)、まず湿ごみを熱風乾燥窯へ送り込み、薫留乾燥・固液分離・炭素や窒素などの元素が分解させると同時に殺菌消臭する。熱風乾燥窯に吸い込まれた熱風は前工程の熱風炉で調製した熱風である。   (2) First, wet waste is sent to a hot-air drying kiln, and it is sterilized and deodorized at the same time that it is decomposed by distillation, solid-liquid separation, carbon, nitrogen and other elements. The hot air sucked into the hot air drying kiln is hot air prepared in the hot air furnace of the previous process.

(3)、薫留乾燥プロセスの熱風温度は110〜150℃(最高200℃以下)である。この温度域は、ごみの薫留乾燥や水分蒸発、固液分離をさせると同時に殺菌消毒除臭し、また燃焼反応も発生せず、代わりに生物体中の炭素や窒素、ミネラル等のエネルギーと栄養元素を分解し-惰効化・可給態化又は無機化させて貯留する。またごみ湿式焼却と違い、ダイオキシンの産生を徹底的に抑えられる。   (3) The hot air temperature of the Shiodome drying process is 110-150 ° C (maximum 200 ° C or less). This temperature range does not cause sterilization, sterilization and deodorization at the same time as waste drying, evaporation of water and solid-liquid separation, and combustion reaction does not occur. Instead, energy such as carbon, nitrogen and minerals in the organism is used. Decompose nutrients-make them effective, make available or mineralize and store. Also, unlike the waste incineration, dioxin production can be suppressed thoroughly.

(4)、「密閉式システム」で、排ガスとごみ蒸発液は大気へ排出しない。乾燥と燃焼のプロセス間にサイクロンや凝縮器等の凝縮分離装置を設置し、乾燥窯出口から出る排ガスを冷却し、排ガス中の薫留水蒸気(蒸発液)を凝縮分離回収し、静置・ろ過・再蒸留等の工程を経て、自然資源として生態的な「生物酢液」を精製する。この生物酢液は抗菌消臭防虫の多機能に優れ、優良な「抗菌消臭剤」又は「生物液肥」である。   (4) The “closed system” does not discharge exhaust gas and waste vapor to the atmosphere. A condensation / separation device such as a cyclone or a condenser is installed between the drying and combustion processes, the exhaust gas exiting the drying kiln is cooled, the condensed water vapor (evaporated liquid) in the exhaust gas is condensed, separated, and left standing and filtered. -Purify ecological "biological vinegar" as a natural resource through processes such as redistillation. This biological vinegar is excellent in antibacterial, deodorant and insecticide, and is an excellent “antibacterial deodorant” or “biological liquid fertilizer”.

(5)、二段ヒートポンプとヒートパイプ余熱回収システムを構築し、生物体の蒸発液の凝縮回収に用いられる凝縮器の冷却水の温度を下げて循環使用する上に、冷却水が排ガスから奪った熱量は余熱回収システムの低温側で放出させ、ヒートパイプの役でその高温側に通過流れの循環ガスに伝え、その循環ガスの温度は150℃以上に達して再び乾燥窯に送り込まれ、湿ごみを繰り返し循環乾燥する。   (5) Construct a two-stage heat pump and heat pipe residual heat recovery system, reduce the temperature of the condenser cooling water used for condensation recovery of the organism's evaporating liquid, circulate and use the cooling water from the exhaust gas The amount of heat generated is released at the low temperature side of the residual heat recovery system and is transferred to the circulating gas in the passing flow to the high temperature side as a heat pipe. The temperature of the circulating gas reaches 150 ° C or higher and is sent to the drying kiln again. Recycle the garbage repeatedly.

(6)、乾燥窯から出た薫留乾燥物は無菌無臭無水の環境で自動制御で行う「風力選別機」、「鉄・アルミ磁力選別機」、「粉砕機」また「高密度複合選別機」等の工程を経て、「再利用類」(金属やプラスチック等)、「生物体」(厨芥類生ごみや剪定枝、草、落葉、紙ごみ又は農林牧漁業廃棄物等の自然物)、「人工物」(プラスチックごみ、ゴム、布ごみ等の容器包装類や工業製品に由来するごみ)と「不可燃物」(無機物)の4種類に分類し回収処理する。そのうちの「生物体」はそれらの炭素や窒素、ミネラル等のエネルギーと栄養元素が貯留されている薫留生物体乾物で、原料として粉砕、篩い分け、成分添加等の工程を経て生態的な「生物薫肥」又は「炭素窒素剤」(土壌全元素剤-生物複合肥料) 等を精製する。「人工物」(容器包装類ごみ) は乾燥した可燃物で、本システムの太陽光発電における高温熱風炉に投入、高温低酸素燃焼(乾留)され、循環ガスが高温まで加熱される。熱風炉より発生した高温熱風は熱風炉出口で熱風炉をバイパスした循環ガスと混合させて温度を調整した後再び乾燥窯に吸込まれ、湿ごみを薫留乾燥し続ける。このように湿ごみの薫留乾燥には太陽エネルギーを利用し、人工物ごみを燃焼し、「密閉式システム」の中で循環ガスは繰り返し熱・物質移動を行う。   (6) The “Toshiba”, “Iron / Aluminum Magnetic Sorter”, “Pulverizer” and “High Density Combined Sorter” are used to automatically control the dried product from the drying kiln in a sterile, odorless and anhydrous environment. `` Reusables '' (metal, plastic, etc.), `` organisms '' (natural products such as moss, garbage, pruned branches, grass, fallen leaves, paper waste or agriculture, forestry, and fishery waste), It is classified into four types: “artificials” (containers and packaging such as plastic waste, rubber, cloth waste, and industrial products) and “incombustibles” (inorganic). Among them, the “organisms” are dry matter of the living organisms in which energy and nutrient elements such as carbon, nitrogen, minerals, etc. are stored. Purify "biological manure" or "carbon nitrogen agent" (soil all-elements-biological compound fertilizer). The “artificial” (container and packaging waste) is a dry combustible material that is put into the high-temperature hot-air stove in the solar power generation system of this system, burned at high temperature and low oxygen (dry distillation), and the circulating gas is heated to a high temperature. The hot hot air generated from the hot stove is mixed with the circulating gas bypassing the hot stove at the exit of the hot stove to adjust the temperature, and then sucked into the drying kiln again to continue drying the wet waste. As described above, solar energy is used to dry and dry wet waste, and artificial waste is burned, and the circulating gas repeatedly performs heat and mass transfer in the “closed system”.

(7)、凝縮器を通過流れの脱水された循環ガスはアフターサイクロン分離器でさらに脱水し、「生物酢液」を再分離回収する。サイクロン分離器出口の脱水した循環ガスはパイプラインにより電熱高温熱風炉に戻り、(6)に述べたように熱風又は循環ガスとして、繰り返し熱・物質移動を行う。   (7) The dehydrated circulating gas passing through the condenser is further dehydrated by an after cyclone separator, and the “biological vinegar” is separated and recovered again. The dehydrated circulating gas at the outlet of the cyclone separator is returned to the electric hot blast furnace by the pipeline, and heat / mass transfer is repeated as hot air or circulating gas as described in (6).

(8)、本発明の高温熱風を発生する熱風炉の燃焼性状は高温低酸素燃焼になる。太陽光発電システムを設置し、「電熱乾燥可燃物高温熱風炉」の「高温空気加熱器」に給電する。一定量の空気と循環ガスが900℃以上加熱し、熱風炉内に噴入し、高温低酸素燃焼性状を維持すると同時に「人工物」の乾燥可燃ごみを高温気流中に送り込んで乾留を行う。発生した高温熱風とパイパス管路の循環ガスと混合、調温してから再び乾燥窯へ送り込まれ、繰り返し湿ごみを薫留乾燥する。太陽エネルギーと人工物乾燥ごみの燃焼はともに熱源となり、化石燃料を節約する。   (8) The combustion property of the hot air furnace for generating the high temperature hot air of the present invention is high temperature low oxygen combustion. A solar power generation system will be installed and power will be supplied to the “hot air heater” of the “electrically-heated combustible high-temperature hot stove”. A certain amount of air and circulating gas are heated to 900 ° C or higher and injected into a hot stove to maintain high-temperature, low-oxygen combustion properties. At the same time, dry artificial combustible waste is sent into a high-temperature air stream for dry distillation. The generated hot air and the circulating gas in the pipe line are mixed and temperature-controlled, and then sent to the drying kiln again to repeatedly damp and dry wet waste. Both solar energy and the combustion of man-made dry waste become heat sources, saving fossil fuels.

本発明の上記の生物体廃棄物の処理技術は「炭素・窒素貯留技術」又は「物質循環技術」と称し、「薫留-凝縮法」とも称する。   The biological waste treatment technology of the present invention is referred to as “carbon / nitrogen storage technology” or “material circulation technology”, and is also referred to as “shiodome-condensation method”.

以上に述べたように、従来のごみ焼却に存在している問題は、生物体ごみの焼却と湿式焼却することで炭素・窒素等の「短絡」揮発損失やダイオキシン、温室効果ガス、有害排ガス等の発生する-であるが、本発明ではこれらの問題はすべて解決した。本発明「炭素・窒素貯留技術」では、生物体(バイオマス)廃棄物を発酵・焼却する代わりに、「密閉式システム」で「薫留-凝縮-乾留」等の処理工程を行い、薫留したごみの乾燥物質を「生物体」と「人工物」等に分類処理することで、炭素や窒素、ミネラル等が分離・貯留され、且つ炭素は緩効・惰効性炭素(プール)となり、窒素とミネラル等は100℃以上の煙薫留乾燥でそれらの栄養元素を全量全元素貯留・可給態化又は無機化され、全元素肥料とすると植物が直接吸収できる。だから、最終的には「生物酢液」や「生物薫肥」又は「炭素窒素剤」等の生態系素材を得る。生物体廃棄物の「炭素・窒素貯留技術」により、ダイオキシン発生を抑えることができ、炭素・窒素酸化物、メタンガスを発生させることなく、温室効果ガス(CO2,CH4,N2O等)や有害物質ゼロエミッションを実現した。故に本発明は、生物体廃棄物の栄養元素を惰効性炭素や可給態又は無機態窒素、ミネラルの形で土壌に還すことでそれらの物質循環が生かせ、肥沃な土壌を育め、土壌有機炭素貯留量を増やせる生態系における「物質循環技術」である。   As mentioned above, the problems that exist in conventional waste incineration are the “short-circuit” volatilization loss of carbon and nitrogen, dioxins, greenhouse gases, harmful exhaust gases, etc. by incineration of biological waste and wet incineration. However, the present invention has solved all of these problems. In the “carbon / nitrogen storage technology” of the present invention, instead of fermenting and incinerating biological (biomass) waste, the “sealed system” was used to carry out treatment processes such as “stain-condensation-dry distillation” and so on. By classifying the dry matter of garbage into `` organisms '' and `` artifacts '', carbon, nitrogen, minerals, etc. are separated and stored, and carbon becomes slow and effective carbon (pool), nitrogen And minerals, etc., can be directly absorbed by plants when all elements are stored, made available, or mineralized by drying the smoke at 100 ° C or higher. Therefore, ultimately, ecosystem materials such as “biological vinegar”, “biological manure” or “carbon nitrogen agent” are obtained. Biological waste “carbon / nitrogen storage technology” can reduce the generation of dioxins, and does not generate carbon / nitrogen oxides or methane gas, and does not emit greenhouse gases (CO2, CH4, N2O, etc.) and hazardous substances. Realized. Therefore, the present invention allows the recycling of the nutrient elements of biological waste to the soil in the form of effective carbon, available or inorganic nitrogen, and minerals, thereby cultivating fertile soil. “Material recycling technology” in ecosystems that can increase organic carbon storage.

また、燥窯の熱源方式は以下の4つからなる。1)乾燥な「人工物」(非生物体)可燃ごみを燃料とする太陽光発電システムで給電する電熱乾燥可燃物高温熱風炉(本炉内に高温空気加熱器を設置する)。2) 乾燥可燃ごみと石炭(或は重油やガス等)を燃料とする熱風炉。3)太陽光発電システムにより給電する電熱熱風炉。4) 乾燥窯内はその他工業生産のプロセスで出る高温排ガスと本系統の乾燥可燃物熱風炉。 Moreover, the heat source system of a drying kiln consists of the following four. 1) Electrothermal dry combustible high-temperature hot-air oven (powered by a high-temperature air heater in the main furnace) powered by a photovoltaic power generation system that uses dry “artificial” (non-living) combustible waste as fuel. 2) A hot stove powered by dry combustible waste and coal (or heavy oil, gas, etc.). 3) An electric hot stove powered by a solar power generation system. 4) Inside the drying kiln is a high-temperature exhaust gas from other industrial production processes and a dry combustible material hot air oven of this system.

「物質循環技術」におけるごみ処理プロセスフロー図1である。図1では、乾燥窯内は可燃人工物乾燥ごみを燃料とし、太陽光発電システムで給電する電熱式可燃乾燥ごみ複合熱風炉で調製した高温熱風を使ってごみを薫留乾燥するのである。FIG. 1 is a waste treatment process flow diagram 1 in “Material Circulation Technology”. In FIG. 1, combustible artificial dry waste is used as fuel in the drying kiln, and waste is dried by using hot hot air prepared in an electrothermal combustible dry waste combined hot air furnace fed by a solar power generation system. 「物質循環技術」におけるごみ処理プロセスフロー図2である。図2では、乾燥窯内は可燃乾燥人工物ごみと石炭や重油等を燃料とする混合熱風炉で調製した高温熱風を使ってごみを薫留乾燥するのである。FIG. 2 is a waste treatment process flow diagram 2 in the “material circulation technology”. In FIG. 2, the inside of the drying kiln is dry-dried using high-temperature hot air prepared in a mixed hot air furnace using combustible dry artificial waste and coal or heavy oil as fuel. 「物質循環技術」におけるごみ処理プロセスフロー図3である。図3では、乾燥窯内は太陽光発電システムで給電する電熱炉で調製した高温ガスを使ってごみを薫留乾燥するのである。FIG. 3 is a waste treatment process flow chart 3 in “Material recycling technology”. In FIG. 3, the inside of the drying kiln is detained and dried using high-temperature gas prepared in an electric furnace fed with a solar power generation system. 「物質循環技術」におけるごみ処理プロセスフロー図4である。図4では、乾燥窯内はその他工業生産のプロセスで出る高温排ガスと本系統の乾燥ごみ熱風炉で調製した高温熱風を使ってごみを薫留乾燥するのである。FIG. 4 is a waste treatment process flow diagram 4 in the “material circulation technology”. In FIG. 4, the inside of the drying kiln is dried by using the high-temperature exhaust gas produced in other industrial production processes and the high-temperature hot air prepared in the dry waste hot-air furnace of this system. 「物質循環技術」におけるごみ処理プロセスの系統図である。図5は図1に示す技術的系統図であり、本発明の「物質循環技術」におけるごみ処理技術の系統図の一つである(図2〜4の技術的系統図はここでは省略するが、図5を参照できる)。It is a systematic diagram of the waste disposal process in "Material circulation technology". FIG. 5 is a technical system diagram shown in FIG. 1 and is one of the system diagrams of the waste treatment technology in the “material circulation technology” of the present invention (although the technical system diagrams of FIGS. 2 to 4 are omitted here). FIG. 5 can be referred to).

本発明における具体的実施方法は4つあり、当該『説明書』(プロセス(2))と図面説明及び図1〜4に述べた通りである。この4つ方式ではごみ乾燥窯でごみの薫留乾燥に使う熱源に違いがある。次に、図1と図5の具体的な実施例を紹介する。   There are four specific implementation methods in the present invention, as described in the “instructions” (process (2)), the drawings, and FIGS. In these four systems, there are differences in the heat sources used to dry waste in a garbage drying kiln. Next, specific examples of FIGS. 1 and 5 will be introduced.

図5は本発明の「物質循環技術」におけるごみ処理プロセスの系統図である。この処理プロセスに使う燃料は乾燥した可燃人工物ごみで、また太陽光発電システムにより高温熱風炉(高温空気燃焼炉)に給電する。   FIG. 5 is a system diagram of the waste treatment process in the “material circulation technology” of the present invention. The fuel used in this treatment process is dry combustible man-made waste, and power is supplied to a high-temperature hot-air furnace (high-temperature air-fired furnace) by a photovoltaic power generation system.

図5に示す通り、本発明の「物質循環技術」におけるごみ処理技術では以下の手順を含める。(1)乾燥窯1、蒸発液冷却分離回収装置(サイクロン分離器21、23と凝縮器3)、生物酢液貯蔵タンク41,42、熱風炉5、太陽光発電システム6、二段余熱回収システム10等を組み合わせたごみ「薫留-凝縮-乾留」処理工程の「密閉式システム」を設置する。(2)湿ごみをごみホッパ86へ投入し、ホッパ下部の給塵機87により乾燥窯1に送り込み、薫留乾燥・固液分離・炭素惰効化・窒素とミネラル可給態化又は無機化する同時に殺菌消臭する。(3)乾燥窯1の熱風温度は110〜150℃である。(4)乾燥窯内での蒸発した排ガス中の水蒸気(蒸発液)はサイクロン分離器21と水冷凝縮器3で遠心及び凝縮分離・回収を行い、トラップ25と34とろ過器26と35を別々に通り生物酢液貯蔵タンク41と42へと貯蔵される。(5)凝縮器3の冷却水にて奪った熱量は余熱回収システム10で回収され、ヒートパイプの高温側から放出熱量は循環ガス復管103のガスへ伝え、加熱し、加熱された熱風管104のガスは乾燥窯内の循環ガスの一部となり、高温熱風炉5出口の循環回路1の高温熱風管15と混合させて乾燥窯1に送り込み、乾燥窯内の湿ごみを薫留乾燥を行う。(6)凝縮器3を通って脱水後の排ガスはサイクロン分離器23に入りさらに脱水され、トラップ27とろ過器28等の装置でさらに生物酢液を回収し貯蔵タンク42へゆく。サイクロン分離器23出口ですでに脱水した循環ガスはパイプラインを通り一部は高温熱風炉5(循環ガス回路1)へ戻り、他の一部は余熱回収システム10(循環ガス回路2)に戻って別々に加熱された後バイパス管18の循環ガスと混合させて温度調節し、再度乾燥窯に送り込まれ次の熱・物質移動を行う。(7)薫留乾燥後のごみは乾燥窯1の乾燥ごみ出口から出た後、無菌無臭無水の状況の下で自動「風力選別機」111、「磁力選別機」112、「粉砕機」113と「高密度複合選別機」114を経て、再利用115及び116、包装類(人工物)117、生物体(自然物)118、また無機物119等の無害無臭の資源物質に分別されそれぞれ処理を加え利用する。そのうちの生物体(自然物)118は炭素と窒素が分離貯留された薫留生物体で、「生物薫肥」又は「炭素窒素剤」を精製する。人工物可燃乾燥ごみ117は本システムの電熱乾燥可燃物高温熱風炉5で乾留し、循環ガスを加熱し、高温熱風炉5出口の発生した高温熱風(循環ガス回路1)と余熱回収システム10で加熱した熱風(循環ガス回路2)と混合した後、再び乾燥窯1に吸込まれ、繰り返しごみの薫留乾燥-熱・物質移動を行う。このように循環ガスは2つの回路を通り絶え間なく循環利用される。(8)太陽光発電システム6を設置し、電熱可燃乾燥ごみ高温熱風炉5内の高温空気加熱器51へ供電し、一定量の空気と循環ガスを900℃以上にまで予熱して熱風炉へ噴入し、高温空気燃焼を維持させる。循環回路1の循環ガスは加熱後乾燥窯1に送り込まれ湿ごみを乾燥させる。バイパス管18の作用はバイパス内の循環ガスの比率により乾燥窯の熱風温度を調整する。以上の工程を実施することにより生物体廃棄物中の炭素や窒素、ミネラル等のエネルギーと栄養元素が分解され、それぞれ惰効性炭素(プール)と可給態又は無機態窒素とミネラル等の形で貯留されたので、それぞれ「生物酢液」と「生物薫肥」又は「炭素窒素剤」等を精製する。   As shown in FIG. 5, the following procedure is included in the waste treatment technology in the “material circulation technology” of the present invention. (1) Drying kiln 1, Evaporated liquid cooling / recovery device (cyclone separators 21, 23 and condenser 3), biological vinegar storage tanks 41, 42, hot stove 5, solar power generation system 6, two-stage residual heat recovery system Installed a “closed system” for the “Shiodome-Condensation-Drying” process that combines 10 etc. (2) Dust is put into the waste hopper 86 and sent to the drying kiln 1 by the dust feeder 87 at the bottom of the hopper, and it is dried by distillation, solid-liquid separation, carbon effect, nitrogen and mineral availability, or mineralization At the same time sterilize and deodorize. (3) The hot air temperature of the drying kiln 1 is 110 to 150 ° C. (4) The water vapor (evaporated liquid) in the exhaust gas evaporated in the drying kiln is centrifuged, condensed, separated and recovered by the cyclone separator 21 and the water-cooled condenser 3, and the traps 25 and 34 and the filters 26 and 35 are separated. And stored in the bio-vinegar storage tanks 41 and 42. (5) The amount of heat taken by the cooling water of the condenser 3 is recovered by the residual heat recovery system 10, and the amount of heat released from the high temperature side of the heat pipe is transferred to the gas in the circulating gas return pipe 103, heated, and heated hot air pipe 104 gas becomes a part of the circulating gas in the drying kiln, mixed with the hot hot air pipe 15 in the circulation circuit 1 at the outlet of the high temperature hot stove 5 and sent to the drying kiln 1 to dry the debris in the drying kiln. Do. (6) The exhaust gas after dehydration passes through the condenser 3 enters the cyclone separator 23 and is further dehydrated, and further collects the biological vinegar liquid with a device such as a trap 27 and a filter 28, and goes to the storage tank 42. The circulating gas already dehydrated at the outlet of the cyclone separator 23 passes through the pipeline, partly returns to the high-temperature hot stove 5 (circulating gas circuit 1), and the other part returns to the residual heat recovery system 10 (circulating gas circuit 2). After being heated separately, the temperature is adjusted by mixing with the circulating gas in the bypass pipe 18 and sent again to the drying kiln for the next heat and mass transfer. (7) Garbage after drying in Shiodome goes out from the dry waste outlet of the drying kiln 1, and then automatically “wind sorter” 111, “magnetic sorter” 112, “pulverizer” 113 under sterile and odorless conditions And “High-Density Combined Sorter” 114, recycle 115 and 116, packaging (artificial) 117, biological (natural) 118, and non-toxic and odorless resource materials such as inorganic 119 and add treatments respectively. Use. Among them, the organism (natural product) 118 is a tethered organism in which carbon and nitrogen are separated and stored, and purifies “biological manure” or “carbon nitrogen agent”. Artificial combustible dry waste 117 is carbonized in the electrothermal dry combustible high-temperature hot stove 5 of this system, the circulating gas is heated, and the high-temperature hot air (circulation gas circuit 1) generated at the outlet of the high-temperature hot stove 5 and the residual heat recovery system 10 are used. After mixing with the heated hot air (circulation gas circuit 2), it is again sucked into the drying kiln 1 and repeatedly performs the detained drying-heat / mass transfer of the waste. In this way, the circulating gas is continuously circulated through the two circuits. (8) Install the solar power generation system 6 and supply electricity to the high-temperature air heater 51 in the electrothermal combustible dry waste high-temperature hot stove 5 to preheat a certain amount of air and circulating gas to 900 ° C or higher to the hot stove Inject and maintain hot air combustion. The circulating gas in the circulation circuit 1 is heated and sent to the drying kiln 1 to dry the wet waste. The operation of the bypass pipe 18 adjusts the hot air temperature of the drying kiln according to the ratio of the circulating gas in the bypass. By carrying out the above processes, energy and nutrient elements such as carbon, nitrogen and minerals in biological waste are decomposed, and the form of effective carbon (pool) and available or inorganic nitrogen and mineral, etc., respectively. In this case, “biological vinegar” and “biological manure” or “carbon nitrogen agent” are purified.

以上が本発明の具体的実施例の1つである。次に主な設備の特徴を紹介する。   The above is one specific embodiment of the present invention. Next, the features of the main equipment are introduced.

(1)乾燥窯:本システムの乾燥窯1の特徴は横置円筒回転式、直火式熱風乾燥窯である(或は円筒は回転せず、円筒内部にミキサー式撹拌機を設置して湿ごみを撹拌する)。直火式とは直接燃焼式、即ち、熱風炉で発生した熱風が材料と直接接触させ利用することである。乾燥窯円筒の直径及び長さはごみ処理量をもとに確定される。乾燥窯には湿ごみ入口11、乾燥物出口12、熱風入口13と排ガス出口14を設置し、回転式乾燥窯下部にはローラーと駆動システムを備え、回転数は1回転/分以下である。ごみ乾燥窯円筒内の内壁には防腐塗装を施す。内壁に一定数の放射状リフタ板を設置し、ドラム内でのごみがリフタにより持ち上げられたり自由落下したりすることで材料の分散、熱風の偏流を防止する。よく撹拌し、薫留乾燥の効率を高める。ドラム外壁は断熱材で保温する。熱風とごみの流動は同じ方向(順流式)にも反対方向(逆流式)にもできる。圧力、温度、湿度等の自動感知や防燃防爆装置そしてモニター監視システムも設置する。同窯内のガス温度は110〜150℃で、ごみの薫留乾燥を行うだけで燃焼はしない。   (1) Drying kiln: The feature of the drying kiln 1 of this system is the horizontal cylinder rotary type, direct fire type hot air drying kiln (or the cylinder does not rotate, and a mixer type stirrer is installed inside the cylinder to make it wet. Stir the garbage). The direct fire type is a direct combustion type, that is, hot air generated in a hot stove is used in direct contact with a material. The diameter and length of the drying kiln cylinder are determined based on the amount of waste. The drying kiln is provided with a wet waste inlet 11, a dry matter outlet 12, a hot air inlet 13 and an exhaust gas outlet 14. The lower part of the rotary drying kiln is provided with a roller and a drive system, and the rotation speed is 1 revolution / min or less. Antiseptic coating is applied to the inner wall of the garbage drying kiln cylinder. A certain number of radial lifter plates are installed on the inner wall, and the dust in the drum is lifted by the lifter or falls freely to prevent material dispersion and hot air drift. Stir well to increase the efficiency of the tidal drying. The drum outer wall is kept warm with a heat insulating material. Hot air and waste can flow in the same direction (forward flow) or in the opposite direction (reverse flow). Automatic sensing of pressure, temperature, humidity, etc., fire and explosion proof devices and monitor monitoring system will also be installed. The gas temperature in the kiln is 110 to 150 ° C.

(2)サイクロン分離器:サイクロン分離器21と23の特徴は開孔内筒式低圧損、高捕集効率のサイクロン(この前の発明)で、除塵と除液の機能を備える。サイクロン分離器の排塵と排液は自動制御で行う。排液はトラップ25,27とろ過器26,28を別々に通った後生物酢液貯蔵タンク41,42に入る。   (2) Cyclone Separator: Cyclone separators 21 and 23 are open-cylinder, low pressure loss, high collection efficiency cyclones (previous invention) and have functions of dust removal and liquid removal. The dust and drainage of the cyclone separator are automatically controlled. The drainage passes through the traps 25 and 27 and the filters 26 and 28 separately, and then enters the bio-vinegar storage tanks 41 and 42.

(3)凝縮器(又は凝縮槽):凝縮器3は排ガス循環回路のサイクロン分離器21と23の間につながっている。その特徴はステンレス製フィン付き凝縮器で、外側は循環ガス、パイプ内は冷却水が通る。冷却器機能はパイプラインを循環する冷却水が凝縮器内のフィン表面温度を低温維持し、外側を流れの排ガスの水蒸気は露点温度まで冷えたフィン表面に接触して結露する。こうして循環ガス中の水蒸気を凝結させて水となり析出される。最後にトラップ34とろ過器35等を通り生物酢液貯蔵タンク42に集められる。貯蔵タンクの生物酢液は静置、ろ過、再蒸留等の工程を経て生物酢液製品を精製する。化学検査の結果により、生物酢液とは有機酸、アルコール類、ケトン類、フェノール類を主成分とする多機能に優れた有機資源液体で除臭剤又は生物液肥になる。   (3) Condenser (or condensing tank): The condenser 3 is connected between the cyclone separators 21 and 23 in the exhaust gas circulation circuit. The feature is a condenser with a fin made of stainless steel. Circulating gas passes outside and cooling water passes inside the pipe. In the cooler function, the cooling water circulating in the pipeline maintains the fin surface temperature in the condenser at a low temperature, and the water vapor of the exhaust gas flowing outside contacts with the fin surface cooled to the dew point temperature to condense. In this way, the water vapor in the circulating gas is condensed to form water. Finally, it is collected in a biological vinegar storage tank 42 through a trap 34, a filter 35 and the like. The biological vinegar liquid in the storage tank is purified through a process such as standing, filtration, and re-distillation. According to the result of the chemical test, the biological vinegar is a multi-functional organic resource liquid mainly composed of organic acids, alcohols, ketones and phenols, which becomes a deodorant or biological liquid fertilizer.

(4) 熱風発生炉(熱風炉):熱風炉はごみ乾燥に必要な熱源を供給するための装置である。本発明の熱源装置の特徴は以下の4つからなる。1).可燃乾燥ごみを燃料とし、太陽光発電システムの給電による電熱式可燃乾燥ごみ複合熱風炉で、炉内は電熱ガス予熱装置(図1と図5)を設置する。2).可燃乾燥ごみと石炭や重油、ガス等を燃料とする複合熱風炉(図2)。3).太陽光発電システムの給電による電熱炉(図3)。4).その他工場生産工程の温度150℃以上の排ガス(セメントキルンプロセスからの排ガス、発電所のタービンからの排気、様々なボイラーや炉窯等からの排気等)が乾燥ごみ熱風炉に加わる(図4)。本発明における各熱風炉の技術的特徴は炉内に電熱ガス予熱装置を設置し、高温低酸素燃焼を維持できる。湿ごみを焼却せず乾燥窯で乾燥を経た後の乾燥ごみを燃焼する(乾留)。また「密閉式システム」で、送風機52はごみピットから悪臭空気を吸い込み、負圧を維持すると同時に臭気は熱風炉内に送り込まれ燃焼し、送風量は燃料の無炎燃焼性状を維持するだけに限る。熱風炉内に入る風量の多くは循環ガスとなり、加熱後再び乾燥窯に入り湿ごみを薫留乾燥し、循環し続ける。本システムではいかなる気体も大気中に排出させない。   (4) Hot air generating furnace (hot air furnace): A hot air furnace is a device for supplying a heat source necessary for drying garbage. The heat source device of the present invention has the following four features. 1). An electrothermal combustible dry waste combined hot air furnace using combustible dry waste as a fuel and powered by a photovoltaic power generation system. An electric heating gas preheating device (Figures 1 and 5) is installed in the furnace. 2) Combined hot stove with combustible dry waste and coal, heavy oil, gas, etc. as fuel (Fig. 2). 3) Electric furnace with power supply from solar power generation system (Fig. 3). 4) Other exhaust gas at a temperature of 150 ° C or higher in the factory production process (exhaust gas from cement kiln process, exhaust gas from power plant turbine, exhaust gas from various boilers, furnace kilns, etc.) is added to the dry waste hot stove ( (Fig. 4). The technical feature of each hot stove in the present invention is that an electric heating gas preheating device is installed in the furnace to maintain high temperature and low oxygen combustion. Burning dry waste after drying in a drying kiln without incinerating wet waste (dry distillation). Also, in the “closed system”, the blower 52 sucks malodorous air from the garbage pit and maintains negative pressure. At the same time, the odor is sent into the hot stove and burns, and the amount of blown air only maintains the flameless combustion characteristics of the fuel. Limited. Most of the amount of air entering the hot stove becomes circulating gas, and after heating, it enters the drying kiln again, damps and dries the waste and continues to circulate. This system does not discharge any gas into the atmosphere.

(5)太陽光発電システムと余熱回収システム:太陽光発電システム6と2段ヒートポンプとヒートパイプ熱回収システム10は本発明のごみ栄養元素貯留技術における新エネルギー利用と省エネの特徴である。前者は燃料炉5内の高温空気加熱器51及びすべての工程に給電し、この装置の設置により複合熱風炉での高温低酸素燃焼を助ける。後者は凝縮器3のパイプライン側の冷却水の循環利用を保証する上で、余熱回収システムの低温側を通った凝縮器の冷却水復管33から奪った熱量はヒートパイプで同システムの高温側を流れの循環ガスに伝える。その循環ガスの温度は150℃以上まで加熱されて再び乾燥窯に送り込まれ、湿ごみを繰り返し乾燥する。太陽光発電と余熱回収システムの応用により本発明の固液分離と栄養元素貯留の全工程において石炭や重油等の鉱物燃料を使う必要はない。   (5) Photovoltaic power generation system and residual heat recovery system: The solar power generation system 6, the two-stage heat pump, and the heat pipe heat recovery system 10 are features of new energy utilization and energy saving in the waste nutrient element storage technology of the present invention. The former supplies power to the high-temperature air heater 51 and all processes in the fuel furnace 5, and the installation of this apparatus helps high-temperature low-oxygen combustion in the combined hot-air furnace. The latter guarantees the circulation and use of the cooling water on the pipeline side of the condenser 3, and the amount of heat taken from the condenser cooling water return pipe 33 that passes through the low temperature side of the residual heat recovery system is the high temperature of the system by the heat pipe. Tell the side to the circulating gas in the flow. The temperature of the circulating gas is heated to 150 ° C or higher and sent again to the drying kiln, where the wet waste is repeatedly dried. It is not necessary to use mineral fuels such as coal and heavy oil in the whole process of solid-liquid separation and nutrient element storage according to the present invention by applying solar power generation and residual heat recovery system.

本発明では、産業上の利用では問題はない。建設コストと運営コストでは、ともに焼却式より大幅に低減し、また生物体廃棄物が無駄ゼロ、100%資源に地球生態系の物質循環することを実現できる。ごみ埋め立てや堆肥化、焼却する際に炭素と窒素は気化する(CO2,CH4,N2O等が大気中に排出される)代わりに「生物酢液」と「生物薫肥」又は「炭素窒素剤」として地球への「炭素や窒素、ミネラル等の補充」となり、炭素や窒素、ミネラルの土への循環を強化し、土壌有機炭素貯留量と栄養元素を増加し、肥沃な土壌つくりとグリーンな農業の発展と生態系のバランスを促す。そして未来のバイオエネルギー作物の開発・生産を助け、地球温暖化を防止し、社会の持続可能な発展を促進する。   In the present invention, there is no problem in industrial use. Both construction costs and operational costs are significantly lower than incineration, and biological waste is zero waste and 100% resources can be recycled into the global ecosystem. Carbon and nitrogen vaporize when landfilling, composting and incineration (CO2, CH4, N2O, etc. are discharged into the atmosphere) instead of `` biological vinegar '' and `` biological manure '' or `` carbon nitrogen agent '' As a “replenishment of carbon, nitrogen, minerals, etc.” to the earth, strengthening the circulation of carbon, nitrogen, minerals to the soil, increasing soil organic carbon storage and nutrient elements, creating fertile soil and green agriculture Promote the balance between development and ecosystem. It will help develop and produce future bioenergy crops, prevent global warming and promote sustainable development of society.

本発明の生物体資源を活かして土壌に「充炭素、充窒素等」により、さらに深い意味がある「バイオエネ循環法則」という未来のバイオ燃料の時代はもう遠くない。本発明に基づいて推論した「バイオエネ循環法則」は次の通りである。   By utilizing the biological resources of the present invention, the future of biofuels called the “Bio-Energy Circulation Law”, which has a deeper meaning due to “carbon filling, nitrogen filling, etc.” in the soil, is not far away. The “bioenergy circulation law” inferred based on the present invention is as follows.

「-本発明の「炭素・窒素貯留技術」により生物体廃棄物から炭素・窒素剤(土壌全元素剤)をつくり、生物体中の有機炭素や窒素等を大地に還す-土壌有機炭素貯留量と栄養元素を増加-肥沃な土壌(山地や砂漠を含む)を育む-バイオエネルギー作物を大規模に開発・植え-バイオ燃料を大規模に生産-一方生物体(バイオエネ作物を含む)廃棄物で炭素窒素剤をつくり生物体中の有機炭素や窒素等を大地に還す-」。これは未来のバイオエネ時代のエネルギー再生法則である。   ``-Using the `` carbon / nitrogen storage technology '' of the present invention to produce carbon / nitrogen agents (soil all elemental agents) from biological waste and return organic carbon and nitrogen in the organism to the ground-Soil organic carbon storage volume -Increase fertile soil (including mountains and deserts)-Develop and plant bioenergy crops on a large scale-Produce biofuels on a large scale-On the other hand, with biological waste (including bioenergy crops) Create a carbon-nitrogen agent to return organic carbon and nitrogen in living organisms to the ground. This is the energy regeneration law of the future bioenergy era.

生態系における物質循環と生態系のバランスも「持続可能な形」や「可変な形」になる。「バイオエネ循環法則」によりバイオ燃料は完全に化石燃料の代替物となれ、地球温暖化を防止できるだろう。資源、環境と持続可能な発展等の問題は解決できる。「持続可能な発展」の3 本柱(経済性、生態系のバランス、社会的責任)を「炭素・窒素貯留技術」(物質循環技術)の梁で繋ぐことができる。   The balance between the material cycle and the ecosystem in the ecosystem is also “sustainable” and “variable”. The “Bio-Energy Circulation Law” will make biofuels a perfect alternative to fossil fuels and prevent global warming. Problems such as resources, environment and sustainable development can be solved. The three pillars of “sustainable development” (economic efficiency, ecological balance, social responsibility) can be connected by the “carbon / nitrogen storage technology” (material recycling technology) beam.

次は用語の説明である。
「生物体廃棄物」―生ごみと食品加工や農林牧漁業廃棄物等中の生物体(バイオマス)廃棄物及び家畜家禽糞又は下水汚泥等である。また「生物体」は「自然物」ともいい、その対義語は「人工物」である。「生物体」(自然物)の例は生ごみや雑草、植木剪定枝、落葉、わら、紙くず等であり、「人工物」の例はプラスチックごみやゴム、合成繊維ごみ等である。
「薫留」―100℃以上の煙ガスで薫煙・蒸留し、水分を蒸発させ、燃焼の反応を生じさせず固液分離をすることである。
「炭素・窒素貯留技術」―即ち「物質循環技術」である。本発明の「低酸素熱風密閉式循環システム」と「薫留‐凝縮‐乾留」工程に基づく生物体廃棄物処理技術で、「薫留-凝縮法」とも称する。この処理法で、生物体廃棄物中の炭素や窒素、ミネラル等のエネルギーと栄養元素等が分解され、それぞれ惰効性炭素(プール)と水溶性窒素・ミネラル等の形で貯留され、「生物酢液」と「生物薫肥」又は「炭素窒素剤」(土壌全元素剤)等として土壌に還し、生態系の物質循環が起こるから、「物質循環技術」とも称する。
「バイオエネ循環法則」―本発明の「炭素・窒素貯留技術」により生物体廃棄物から炭素窒素剤(土壌全元素剤)をつくり、生物体中の有機炭素や窒素等を大地に還すことにより土壌有機炭素貯留量と栄養元素を増加し、肥沃な土壌を育んで、山地や砂漠を改造し、バイオエネルギー作物を大規模に開発と植え、バイオ燃料を大規模に生産し、また再び生物体廃棄物より炭素窒素剤をつくり、生物体中の有機炭素や窒素等を大地に還すというバイオ時代のバイオエネルギー再生法則である。
The following is an explanation of terms.
"Biological waste"-biological waste (biomass) in food waste and food processing, agriculture, forestry, and fishery waste, and livestock poultry manure or sewage sludge. The “organism” is also called “natural object”, and its synonym is “artifact”. Examples of “organisms” (natural objects) are raw garbage, weeds, pruned branches, fallen leaves, straw, waste paper, etc., and examples of “artificial objects” are plastic garbage, rubber, synthetic fiber garbage, and the like.
“Shiodome” —To smoke and distill with smoke gas at 100 ° C or higher, evaporate water, and to separate solid and liquid without causing a combustion reaction.
“Carbon / nitrogen storage technology” – “Material recycling technology”. This is a biological waste treatment technology based on the “low oxygen hot air sealed circulation system” and the “shiodome-condensation-dry distillation” process of the present invention, and is also referred to as “shiodome-condensation method”. By this treatment method, energy and nutrient elements such as carbon, nitrogen and minerals in biological waste are decomposed and stored in the form of effective carbon (pool) and water-soluble nitrogen and minerals, respectively. It is also referred to as “material circulation technology” because it is returned to the soil as “vinegar liquor” and “biological manure” or “carbon nitrogen agent” (soil all-elements agent) and so on, causing material circulation in the ecosystem.
“Bio-Energy Circulation Law”-Carbon / nitrogen storage technology of the present invention creates carbon nitrogen agent (soil all-element agent) from biological waste, and returns organic carbon, nitrogen, etc. in the organism to the ground Increase organic carbon storage and nutrient elements, nurture fertile soil, remodel mountains and deserts, develop and plant bioenergy crops on a large scale, produce biofuels on a large scale, and again destroy organisms It is a bioenergy regeneration law in the bio-era that creates carbon-nitrogen agents from materials and returns organic carbon, nitrogen, etc. in living organisms to the earth.

Claims (3)

本発明の生物体(バイオマス)廃棄物におけるエネルギーと栄養元素(炭素や窒素、ミネラル等)を貯留して土壌へ循環させる技術(「炭素・窒素貯留技術」又は「物質循環技術」)は、生ごみや生物体廃棄物の埋め立てや堆肥化、焼却を避け、乾燥窯や凝縮器(又は凝縮槽)、熱風炉等を組み合わせた「低酸素熱風密閉式循環システム」及び「薫留‐凝縮‐乾留」工程に基づいてごみ(生ごみと食品加工や農林牧漁業廃棄物及び家畜家禽糞又は下水汚泥等)を薫留乾燥や殺菌消臭、固液分離してからその蒸発液は凝縮回収し、その薫留乾物は「生物体」や「人工物」等に分類し(うち生物体に炭素や窒素、ミネラル等のエネルギーと栄養元素が貯留されており、且つ炭素が惰効化、栄養元素が可給態化又は無機化され)、それぞれ「生物酢液」や「生物薫肥」又は「炭素窒素剤」(土壌全元素剤-生物複合肥料)等を精製して生物ごみの栄養元素を100%貯留して植物の全元素肥料として土壌に還すことでその物質循環が生かせ、肥沃な土壌を育め、土壌有機炭素貯留量を増やせ、またダイオキシンや温室効果ガス、有害物質のゼロエミッションを実現する生態系における「物質循環技術」である。   The technology for storing energy and nutrient elements (carbon, nitrogen, minerals, etc.) in the biological waste (biomass) of the present invention and circulating it to the soil (“carbon / nitrogen storage technology” or “material circulation technology”) Avoiding landfills, composting and incineration of garbage and biological waste, “low oxygen hot air closed circulation system” combined with drying kiln, condenser (or condensing tank), hot air furnace, etc. and “Shiodome-condensation-dry distillation” Based on the process, garbage (food waste, food processing, agricultural / forestry / fishery waste and livestock poultry manure or sewage sludge, etc.) is detained, sterilized and deodorized, separated into solid and liquid, and the evaporated liquid is condensed and recovered. The Shiodome dry matter is classified into `` organisms '' and `` artifacts '' (of which energy and nutrient elements such as carbon, nitrogen and minerals are stored in the organism, and carbon is effective and nutrient elements are (Available or mineralized), `` biological vinegar '' and `` biological manure, respectively Or, by refining `` carbon nitrogen agent '' (soil all-element agent-biological complex fertilizer), etc., 100% of the nutrient elements of biological waste are stored and returned to the soil as all-element fertilizer of plants, so that the material circulation can be utilized and fertile It is a “material recycling technology” in ecosystems that nurtures healthy soil, increases soil organic carbon storage, and realizes zero emissions of dioxins, greenhouse gases, and harmful substances. 本発明の生物体廃棄物処理システムに二段ヒートポンプとヒートパイプ余熱回収システムを構築し、生物体の蒸発液の凝縮回収に用いられる凝縮器の冷却水の温度を下げて循環使用する上に、冷却水が排ガスから奪った熱量は余熱回収システムの低温側で放出させ、ヒートパイプの役でその高温側に通過流れの循環ガスに伝え、その循環ガスの温度は150℃以上に達して再び乾燥窯に送り込まれ、湿ごみを繰り返し循環乾燥し、熱効率は80%以上になる。 In constructing a two-stage heat pump and heat pipe residual heat recovery system in the biological waste treatment system of the present invention, and lowering the temperature of the condenser cooling water used for condensation recovery of the biological vapor, The amount of heat taken by the cooling water from the exhaust gas is released at the low temperature side of the residual heat recovery system, and is transferred to the circulating gas through the high temperature side as a heat pipe, and the temperature of the circulating gas reaches 150 ° C or higher and is dried again. It is sent to the kiln and the waste is repeatedly circulated and dried, resulting in a thermal efficiency of over 80%. 本発明の生物体廃棄物処理システムに太陽光発電システムを設置し、「電熱乾燥可燃物高温熱風炉」の「高温空気加熱器」に給電し、一定量の空気と循環ガスが900℃以上加熱し、熱風炉内に噴入し、高温低酸素燃焼性状を維持すると同時に「人工物」の乾燥可燃ごみを高温気流中に送り込んで乾留を行い、発生した高温熱風とパイパス管路の循環ガスと混合、調温してから再び乾燥窯へ送込まれ、繰り返し湿ごみを薫留乾燥する。太陽エネルギーと人工物乾燥ごみの燃焼はともに熱源となり、化石燃料を節約する。 A photovoltaic power generation system is installed in the biological waste treatment system of the present invention, and power is supplied to the “high-temperature air heater” of the “electrothermal drying combustible high-temperature hot stove”, and a certain amount of air and circulating gas are heated to 900 ° C. or more. It is injected into the hot air furnace to maintain high temperature and low oxygen combustion properties, and at the same time, dry combustible waste of `` artificial products '' is sent to the high temperature air stream to perform dry distillation, and the generated high temperature hot air and the circulation gas in the pipeline are After mixing and adjusting the temperature, it is sent again to the drying kiln, and the wet waste is repeatedly dried by distillation. Both solar energy and the combustion of man-made dry waste become heat sources, saving fossil fuels.
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