JP3714674B1 - Modified material such as rice husk and method for producing modified material such as rice husk - Google Patents

Modified material such as rice husk and method for producing modified material such as rice husk Download PDF

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JP3714674B1
JP3714674B1 JP2004145483A JP2004145483A JP3714674B1 JP 3714674 B1 JP3714674 B1 JP 3714674B1 JP 2004145483 A JP2004145483 A JP 2004145483A JP 2004145483 A JP2004145483 A JP 2004145483A JP 3714674 B1 JP3714674 B1 JP 3714674B1
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rice husk
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rice
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calcium hydroxide
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浄二 高瀬
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株式会社西村組
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    • CCHEMISTRY; METALLURGY
    • C05FERTILISERS; MANUFACTURE THEREOF
    • C05DINORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C; FERTILISERS PRODUCING CARBON DIOXIDE
    • C05D3/00Calcareous fertilisers
    • C05D3/02Calcareous fertilisers from limestone, calcium carbonate, calcium hydrate, slaked lime, calcium oxide, waste calcium products
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B09DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
    • B09BDISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
    • B09B3/00Destroying solid waste or transforming solid waste into something useful or harmless
    • CCHEMISTRY; METALLURGY
    • C05FERTILISERS; MANUFACTURE THEREOF
    • C05GMIXTURES OF FERTILISERS COVERED INDIVIDUALLY BY DIFFERENT SUBCLASSES OF CLASS C05; MIXTURES OF ONE OR MORE FERTILISERS WITH MATERIALS NOT HAVING A SPECIFIC FERTILISING ACTIVITY, e.g. PESTICIDES, SOIL-CONDITIONERS, WETTING AGENTS; FERTILISERS CHARACTERISED BY THEIR FORM
    • C05G3/00Mixtures of one or more fertilisers with additives not having a specially fertilising activity
    • C05G3/80Soil conditioners
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K17/00Soil-conditioning materials or soil-stabilising materials
    • C09K17/40Soil-conditioning materials or soil-stabilising materials containing mixtures of inorganic and organic compounds
    • C09K17/48Organic compounds mixed with inorganic active ingredients, e.g. polymerisation catalysts
    • C09K17/50Organic compounds mixed with inorganic active ingredients, e.g. polymerisation catalysts the organic compound being of natural origin, e.g. cellulose derivatives
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K3/00Materials not provided for elsewhere
    • C09K3/18Materials not provided for elsewhere for application to surfaces to minimize adherence of ice, mist or water thereto; Thawing or antifreeze materials for application to surfaces
    • C09K3/185Thawing materials

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Materials Engineering (AREA)
  • Soil Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Pest Control & Pesticides (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Environmental & Geological Engineering (AREA)
  • Processing Of Solid Wastes (AREA)
  • Fertilizers (AREA)
  • Materials Applied To Surfaces To Minimize Adherence Of Mist Or Water (AREA)
  • Soil Conditioners And Soil-Stabilizing Materials (AREA)

Abstract

【課題】 従来、再利用が困難であった籾殻や藁等を付加価値の高い資材として様々に有効利用することが可能であるとともに、特に高品質の水分調整材や融雪材等として好適な籾殻等変性材料および籾殻等変性材料の製造方法を提供する。
【解決手段】 籾殻または藁に水酸化カルシウム源を混入し、前記籾殻または藁を燃焼させない所定の水蒸気圧力下で処理する。この場合、籾殻または藁を1.45MPa以上の水蒸気圧力下で処理するのが望ましい。
【選択図】 図1
PROBLEM TO BE SOLVED: To effectively use rice husks, rice husks and the like, which have been difficult to reuse, as various high-value-added materials, and particularly suitable as a high-quality moisture adjusting material, snow melting material, etc. Provided is a method for producing a modified material and a modified material such as rice husk.
The rice husk or cocoon is mixed with a calcium hydroxide source, and the husk or cocoon is treated under a predetermined water vapor pressure that does not cause the rice husk or cocoon to burn. In this case, it is desirable to treat rice husks or straws under a water vapor pressure of 1.45 MPa or more.
[Selection] Figure 1

Description

本発明は、籾殻や稲藁、麦藁等を再利用すべく性状を変化させた籾殻等変性材料およびその製造方法に関し、特に、水産系廃棄物や下水汚泥等の高湿潤廃棄物の含水率調整を行う水分調整材、あるいは融雪材、土壌改良材等として利用するのに好適な籾殻等変性材料およびその製造方法に関するものである。   The present invention relates to rice husks, rice straws, wheat straws and other modified materials whose properties have been changed to reuse them, and a method for producing the same, and in particular, to adjust the moisture content of high-humidity wastes such as marine waste and sewage sludge. The present invention relates to a modified material such as rice husk suitable for use as a moisture adjusting material, a snow melting material, a soil improving material or the like, and a method for producing the same.

従来より、生ゴミ、下水汚泥および家畜糞尿等のような含水率の高い高湿潤廃棄物を処理して堆肥等を製造する場合、おが屑等の水分調整材を使用して水分を減らし、含水率を調整するようになっている。例えば、特開平9−85220号公報には、生ゴミを堆肥化する際の水分調整材としておが屑を使用し、処理槽内の内容物の含水率を希望の値に保持しようとする発明が提案されている(特許文献1)。このように水分調整材としてはおが屑が最も一般的であるが、おが屑以外の水分調整材も提案されており、例えば、特開2001−294496号公報には、牛糞尿の水分調整材として石膏ボード廃材中の紙を使用する発明が提案されている(特許文献2)。   Conventionally, when producing high-humidity waste such as raw garbage, sewage sludge and livestock manure to produce compost etc., moisture content is reduced by using a moisture adjusting material such as sawdust, and the moisture content To be adjusted. For example, Japanese Patent Laid-Open No. 9-85220 proposes an invention in which sawdust is used as a moisture adjusting material when composting raw garbage and the moisture content of the contents in the treatment tank is maintained at a desired value. (Patent Document 1). As described above, sawdust is the most common moisture-adjusting material, but other moisture-adjusting materials have been proposed. For example, JP-A 2001-294498 discloses a gypsum board as a water-adjusting material for cow manure. An invention using paper in waste materials has been proposed (Patent Document 2).

特開平9−85220号公報Japanese Patent Laid-Open No. 9-85220 特開2001−294496号公報JP 2001-294696 A

しかしながら、石膏ボード廃材から紙のみを分別するのは簡単ではなく、コスト的にも高くなり実用的ではない。一方、おが屑は使い易く、流通量も多いというメリットがあるが、水分調整材として利用されるだけでなく、牛舎や豚舎に敷かれたり、家畜飼料等としても利用される。このため、入手が困難になっており、価格も上昇しているという問題がある。また、おが屑の利用価値が高まることにより、おが屑を製造するために森林が破壊されることによる環境負荷の増大が心配される。   However, it is not easy to separate only paper from gypsum board waste, which is not practical because it is expensive. On the other hand, sawdust is advantageous in that it is easy to use and has a large amount of circulation, but it is not only used as a moisture adjusting material, but also laid in cowsheds and pig houses, and also used as livestock feed. For this reason, there are problems that it is difficult to obtain and the price is rising. In addition, since the utility value of sawdust increases, there is a concern about an increase in environmental load due to destruction of forests to produce sawdust.

一方、再利用が困難な廃棄物の1つとして籾殻や藁が知られている。これらの籾殻や藁は産業廃棄物であるため適正な処理が必要であるが、籾殻および藁はケイ酸成分を含有しているため硬度が高く再利用処理が困難であり、処理コストも高くなってしまうという問題がある。このため、野積みされたまま放置されたり、焼却処分による公害が問題視されている。   On the other hand, rice husks and straws are known as one of the wastes that are difficult to reuse. Since these rice husks and straws are industrial wastes, they need to be treated properly. However, the rice husks and straws contain a silicic acid component, so they are hard and difficult to reuse, and the processing costs also increase. There is a problem that it ends up. For this reason, it is left as it is, or pollution caused by incineration is regarded as a problem.

本発明は、このような問題点を解決するためになされたものであって、籾殻や藁等を付加価値の高い資材として様々に有効利用することが可能であるとともに、特に高品質の水分調整材として好適な籾殻等変性材料および籾殻等変性材料の製造方法を提供することを目的としている。   The present invention has been made to solve such problems, and can effectively use rice husks, straws and the like as high-value-added materials in various ways. It is an object of the present invention to provide a modified material such as rice husk suitable as a material and a method for producing a modified material such as rice husk.

本願発明者は、すでに特願2003−302971号において、籾殻または藁を高圧水蒸気処理することによりケイ酸含有粉末を製造する発明を特許出願しているところ、さらに鋭意研究した結果、籾殻または藁に消石灰やホタテ貝粉末等の水酸化カルシウム源を混入し、前記籾殻または藁を燃焼させない所定の水蒸気圧力下で処理することにより、籾殻や藁の性状を綿繊維のように柔らかく、吸水性の高い性状に変化させる技術を見出した。ここで、水酸化カルシウム源とは、籾殻または藁の変性処理過程において水酸化カルシウムとなり得る全ての物質をいうものとする。具体的には、水酸化カルシウム(いわゆる消石灰)はもとより、水と反応して水酸化カルシウムを発生させる酸化カルシウム(いわゆる生石灰)や、この酸化カルシウムを熱分解により発生させる炭酸カルシウム(貝殻の主成分)等もこれに該当する。   The inventor of the present application has already applied for a patent for an invention for producing a silicic acid-containing powder by subjecting rice husk or rice cake to high-pressure steam treatment in Japanese Patent Application No. 2003-302971. Mixing calcium hydroxide source such as slaked lime or scallop powder and processing under predetermined steam pressure that does not burn the rice husk or cocoon, so that the properties of rice husk and cocoon are soft like cotton fiber and have high water absorption I found a technology to change the properties. Here, the calcium hydroxide source refers to all substances that can become calcium hydroxide in the process of modifying rice husk or straw. Specifically, not only calcium hydroxide (so-called slaked lime) but also calcium oxide (so-called quicklime) that reacts with water to generate calcium hydroxide, and calcium carbonate (the main component of shells) that generates this calcium oxide by thermal decomposition. ) Etc. also fall under this category.

また、本発明において、籾殻または藁を1.45MPa以上の水蒸気圧力下で処理することが好ましい。   In the present invention, it is preferable to treat rice husks or straws under a water vapor pressure of 1.45 MPa or more.

また、本発明に係る籾殻等変性材料製造方法の特徴は、処理容器内で籾殻または藁と水酸化カルシウム源とを混合し、前記処理容器内に所定圧の水蒸気を注入して内圧および温度を上昇させ、前記籾殻または藁が燃焼しない水蒸気圧力下に保持して処理する点にある。   In addition, the method for producing a modified material such as rice husk according to the present invention is characterized by mixing rice husk or rice husk and a calcium hydroxide source in a processing container, and injecting water vapor at a predetermined pressure into the processing container to adjust the internal pressure and temperature. The process is to raise and hold the rice husk or soot under a steam pressure that does not burn.

また、本発明において、前記水酸化カルシウム源は、アルカリ度が65〜80%の場合、籾殻または藁に対して6重量%以上の割合で投入されることが好ましい。ここで、アルカリ度とは、水中に含まれるアルカリ成分(炭酸:HCO,炭酸イオン:CO 2−,炭酸水素イオン:HCO ,水酸化物イオン:OH等)を炭酸カルシウム(CaCO)に換算した値である。 Moreover, in this invention, when the alkalinity is 65-80%, it is preferable that the said calcium hydroxide source is thrown in in the ratio of 6 weight% or more with respect to rice husk or straw. Here, the alkalinity refers to an alkali component (carbonic acid: H 2 CO 3 , carbonate ion: CO 3 2− , hydrogen carbonate ion: HCO 3 , hydroxide ion: OH −, etc.) contained in water as calcium carbonate. It is the value converted into (CaCO 3 ).

さらに、本発明において、前記水酸化カルシウム源として、アルカリ度が約65%の消石灰を籾殻または藁に対して約10重量%の割合で投入することが望ましい。   Furthermore, in the present invention, it is desirable to add slaked lime having an alkalinity of about 65% as the calcium hydroxide source at a ratio of about 10% by weight with respect to rice husk or straw.

また、本発明において、前記処理容器内の圧力を1.45MPa以上に保持することが好ましい。   Moreover, in this invention, it is preferable to hold | maintain the pressure in the said processing container to 1.45 Mpa or more.

本発明によれば、籾殻または藁から有害物質を発生させずに、短時間、かつ低コストで籾殻または藁を性状変換処理し、従来、再利用が困難であった籾殻または藁を水分調整材や融雪材等の有用な資材として利用することができる。   According to the present invention, the rice husk or cocoon is subjected to property conversion treatment in a short time and at a low cost without generating harmful substances from the husk or cocoon, and the rice husk or cocoon that has been difficult to reuse is conventionally used as a moisture adjusting material. It can be used as a useful material such as snow melting material.

以下、本発明に係る籾殻等変性材料および籾殻等変性材料の製造方法の好適な一実施形態について図面を用いて説明する。   DESCRIPTION OF EMBODIMENTS Hereinafter, a preferred embodiment of a modified material for rice husks and the like and a method for producing a modified material for rice husks according to the present invention will be described with reference to the drawings.

本実施形態の籾殻等変性材料は、籾殻または藁を対象とし、この籾殻または藁に水酸化カルシウム源を混入して所定の高圧水蒸気によって処理することにより製造される。水酸化カルシウム源としては、水酸化カルシウムである消石灰を混入してもよいし、ホタテの貝殻の粉砕物を混入してもよい。水酸化カルシウム源の必要混入量はアルカリ度に応じて上下するが、アルカリ度が約65〜80%のものであれば、籾殻または藁に対して約6〜10重量%程度混入すればよい。また、高圧水蒸気による処理条件は、籾殻または藁が燃焼しないで綿のように柔らかい性状に変化させ得る圧力に保持する必要があり、約1.45MPa以上に保持すれば充分であるが、1.65MPa以上に保持すれば約5分〜30分程度で処理が可能である。   The modified material such as rice husk of the present embodiment is produced by treating rice husk or rice husk with a calcium hydroxide source mixed in the rice husk or rice husk and treating with a predetermined high-pressure steam. As the calcium hydroxide source, slaked lime which is calcium hydroxide may be mixed, or scallop shell pulverized material may be mixed. The required mixing amount of the calcium hydroxide source varies depending on the alkalinity, but if the alkalinity is about 65 to 80%, about 6 to 10% by weight may be mixed with the rice husk or straw. The treatment conditions with high-pressure steam need to be maintained at a pressure that can be changed to a soft property such as cotton without burning rice husks or soot, and it is sufficient to maintain the pressure at about 1.45 MPa or more. If the pressure is maintained at 65 MPa or more, the treatment can be performed in about 5 to 30 minutes.

つぎに、本実施形態の籾殻等変性材料を製造するシステム1について、図1に示す模式図によって説明する。この籾殻等変性材料製造システム1は、籾殻または藁を収容して処理するための処理容器2と、この処理容器2に投入された籾殻または藁および水酸化カルシウム源を攪拌するための攪拌手段3と、処理容器2内の籾殻または藁および水酸化カルシウム源の混合物に対して高圧の水蒸気を注入するための水蒸気注入手段4と、処理容器2内の圧力を調節するための圧力調節手段5と、前記攪拌手段3、前記水蒸気注入手段4および前記圧力調節手段5を制御するための制御手段6とから構成されている。   Next, a system 1 for producing a modified material such as rice husk of the present embodiment will be described with reference to a schematic diagram shown in FIG. This modified material production system 1 for rice husks and the like includes a processing vessel 2 for containing and processing rice husks or straws, and a stirring means 3 for stirring the rice husks or straws and the calcium hydroxide source charged in the processing vessel 2. A steam injection means 4 for injecting high-pressure steam into a mixture of rice husk or straw and a calcium hydroxide source in the processing container 2, and a pressure adjusting means 5 for adjusting the pressure in the processing container 2. The control means 6 controls the stirring means 3, the water vapor injection means 4 and the pressure adjusting means 5.

前記籾殻等変性材料の製造システム1の各構成部についてより詳細に説明すると、処理容器2は、耐圧性を備えた第一種圧力容器により構成されており、その上部には籾殻または藁の投入口21が設けられ、下部には排出口22が設けられている。投入口21および排出口22は、安全性を考慮して、処理容器2内の圧力が0.015MPa以下に達しない限り、開閉操作が反応しないシステム制御を備えている。また、処理容器2には、上部温度センサ23a、下部温度センサ23bおよび圧力センサ24が配備されており、処理容器2内の温度および圧力が検出される。   The constituent parts of the rice husk and other modified material manufacturing system 1 will be described in more detail. The processing vessel 2 is constituted by a first-type pressure vessel having pressure resistance, and the upper portion is filled with rice husk or straw. A port 21 is provided, and a discharge port 22 is provided in the lower part. In consideration of safety, the input port 21 and the discharge port 22 are provided with system control in which the opening / closing operation does not react unless the pressure in the processing container 2 reaches 0.015 MPa or less. Further, the processing container 2 is provided with an upper temperature sensor 23a, a lower temperature sensor 23b, and a pressure sensor 24, and the temperature and pressure in the processing container 2 are detected.

攪拌手段3は、処理容器2内で水平に支持された水平回動軸31と、この水平回動軸31に前方側へ傾斜されて取り付けられている撹拌羽根32とから構成されている。水平回動軸31には、正逆回動させる駆動モータ33が連結されている。撹拌羽根32は籾殻または藁および水酸化カルシウム源を混合・撹拌すると共に移送するため、前記水平回転軸31の全体にわたって配置されている。また、前記駆動モータ33はインバータ制御によって回転数および回転方向が制御可能であり、必要に応じて籾殻または藁および水酸化カルシウム源の混合物を処理容器2内で往復動させられる。   The stirring means 3 includes a horizontal rotation shaft 31 that is horizontally supported in the processing container 2 and a stirring blade 32 that is attached to the horizontal rotation shaft 31 so as to be inclined forward. A drive motor 33 that rotates forward and backward is connected to the horizontal rotation shaft 31. The stirring blade 32 is arranged over the entire horizontal rotating shaft 31 for mixing, stirring and transferring the rice husk or straw and the calcium hydroxide source. Further, the drive motor 33 can control the rotation speed and rotation direction by inverter control, and can reciprocate the rice husk or the mixture of rice husk and calcium hydroxide source in the processing vessel 2 as necessary.

つぎに、水蒸気注入手段4は、高圧の水蒸気を発生させるボイラー41と、このボイラー41から発生した水蒸気を処理容器2内に供給するための送気管42とを有している。ボイラーで発生する水蒸気の圧力は一定値に保持されており、処理容器2内の圧力は、高圧水蒸気の注入量で調節するようになっている。この高圧水蒸気の圧力に付随して温度が定まるので処理容器2内は高温に保持される。また、送気管42は、処理容器2に対して水平回動軸31よりも上方位置であって略水平方向に連結されている。これは、処理容器2内の籾殻または藁および水酸化カルシウム源の混合物が撹拌されて中空に浮いているときに高圧水蒸気を当てるためであり、堆積される籾殻または藁に処理ムラが生じるのを防止するものである。これにより高い処理効率が得られる。   Next, the water vapor injection means 4 has a boiler 41 that generates high-pressure water vapor, and an air supply pipe 42 for supplying the water vapor generated from the boiler 41 into the processing vessel 2. The pressure of water vapor generated in the boiler is maintained at a constant value, and the pressure in the processing vessel 2 is adjusted by the injection amount of high-pressure water vapor. Since the temperature is determined in association with the pressure of the high-pressure steam, the inside of the processing container 2 is kept at a high temperature. The air supply pipe 42 is connected to the processing container 2 in a substantially horizontal direction at a position above the horizontal rotation shaft 31. This is to apply high-pressure steam when the mixture of rice husk or cocoon and the calcium hydroxide source in the processing vessel 2 is stirred and floated in the air, and processing unevenness occurs in the deposited rice husk or cocoon. It is to prevent. Thereby, high processing efficiency is obtained.

つぎに、圧力調節手段5は、電気制御により開閉が自在の圧力調整バルブ51と、この圧力調整バルブ51を介して処理容器2内の水蒸気を排気するための排気管52から構成されている。そして、処理容器2内の圧力が所定値を越えると圧力調整バルブ51を開放し、処理容器2内の圧力を抜いて所定の圧力に保持するようになっている。また、排気管52にはサイレンサー7を経由して冷却装置8が連結されており、処理容器2からの水蒸気を冷却して液化し、排水処理設備9に供給するようになっている。さらに、サイレンサー7により、騒音防止条例の規制値をクリアして市街地などに設置できるよう設計されている。   Next, the pressure adjusting means 5 includes a pressure adjusting valve 51 that can be freely opened and closed by electrical control, and an exhaust pipe 52 for exhausting water vapor in the processing container 2 through the pressure adjusting valve 51. When the pressure in the processing container 2 exceeds a predetermined value, the pressure adjusting valve 51 is opened, and the pressure in the processing container 2 is released and held at a predetermined pressure. In addition, a cooling device 8 is connected to the exhaust pipe 52 via the silencer 7, and the water vapor from the processing container 2 is cooled and liquefied and supplied to the wastewater treatment facility 9. Furthermore, the silencer 7 is designed so that the regulation value of the noise prevention regulations can be cleared and installed in an urban area or the like.

つぎに、制御手段6は、攪拌手段3、水蒸気注入手段4および圧力調節手段5と電気的に接続されており、これらを制御するようになっている。この制御手段6は、駆動モータ33の回転方向や回転速度を制御して、処理容器2内における籾殻または藁の撹拌移送時間を制御する。また、籾殻または藁を処理するために、後述する実施例の実験結果に基づいて処理容器2内の圧力を1.45MPa〜1.96MPaに保持するようになっている。もし、処理容器2内の温度や圧力が低下した場合には、水蒸気注入手段4からの高圧水蒸気の注入量を増加させて温度および圧力を上昇させる。逆に、処理容器2内の温度や圧力が上昇した場合には、圧力調節手段5の圧力調整バルブ51を開放して高圧水蒸気を排気し温度および圧力を低下させる。なお、制御手段6は、処理容器2内の各温度センサ23a,23bおよび圧力センサ24と電気的に接続されており、これらの検出結果に基づいて処理容器2内の温度および圧力を所定の値で保持するようにフィードバック制御している。   Next, the control means 6 is electrically connected to the stirring means 3, the water vapor injection means 4, and the pressure adjusting means 5, and controls them. The control means 6 controls the rotation direction and the rotation speed of the drive motor 33 to control the time for stirring and transferring the rice husk or straw in the processing container 2. Moreover, in order to process rice husks or cocoons, the pressure in the processing container 2 is maintained at 1.45 MPa to 1.96 MPa based on experimental results of examples described later. If the temperature or pressure in the processing container 2 decreases, the amount of high-pressure steam injected from the steam injection means 4 is increased to increase the temperature and pressure. On the contrary, when the temperature or pressure in the processing container 2 rises, the pressure regulating valve 51 of the pressure regulating means 5 is opened to exhaust the high-pressure steam to lower the temperature and pressure. The control means 6 is electrically connected to the temperature sensors 23a and 23b and the pressure sensor 24 in the processing container 2, and the temperature and pressure in the processing container 2 are set to predetermined values based on the detection results. Feedback control is performed so that

つぎに、籾殻等変性材料製造システム1を使った本実施形態における籾殻等変性材料の製造方法について説明する。   Next, a method for producing a modified material such as rice husks in this embodiment using the modified material production system 1 such as rice husk will be described.

まず、籾殻または藁と水酸化カルシウム源とを投入口21から処理容器2内に投入する。このとき、水酸化カルシウム源のアルカリ度が65〜80%であれば、投入する籾殻または藁に対して水酸化カルシウム源を6〜10重量%の割合で混合する。これは、アルカリ度が65%よりも低かったり、混入量が6重量%よりも少ないと、処理後の籾殻等変性材料が酸性を示すことがあり、肥料として使用する場合には、pH値を調整する必要が生じるためである。   First, rice husks or straws and a calcium hydroxide source are charged into the processing container 2 from the charging port 21. At this time, if the alkalinity of the calcium hydroxide source is 65 to 80%, the calcium hydroxide source is mixed at a ratio of 6 to 10% by weight with respect to the rice husk or straw to be added. This means that if the alkalinity is lower than 65% or the mixing amount is less than 6% by weight, the modified material such as rice husk after the treatment may show acidity. This is because it is necessary to adjust.

一方、アルカリ度が高ければ混入量を低減することができるため、たとえば水酸化カルシウム源の量は10重量%でも充分である。水酸化カルシウム源をあまりに過剰に混入させると処理装置の故障の原因となるし、コスト的にも無駄になる。   On the other hand, if the alkalinity is high, the amount of mixing can be reduced, so that for example, 10% by weight of the calcium hydroxide source is sufficient. If the calcium hydroxide source is mixed excessively, it causes a failure of the processing apparatus and is wasteful in terms of cost.

また、籾殻または藁が保管されていた場所の湿度にも影響され、たとえば屋内で保管されていた場合には、比較的に乾燥しており、野外で保管されていたものと比べて含水率が小さいため、より少量(約6重量%)の水酸化カルシウム源によって所望の性状を示す。したがって、混入させる水酸化カルシウム源の量およびアルカリ度は、処理対象の籾殻または藁の量と含水率等により適宜調整するのが好ましい。   It is also affected by the humidity where the rice husks or straws were stored. For example, when stored indoors, it is relatively dry and has a moisture content compared to that stored outdoors. Because of its small size, it exhibits the desired properties with a smaller amount (about 6% by weight) of calcium hydroxide source. Therefore, it is preferable to appropriately adjust the amount and alkalinity of the calcium hydroxide source to be mixed according to the amount of rice husk or straw to be treated and the moisture content.

また、予め制御手段6に対して処理容器2内の圧力が1.45MPa以上となるよう設定するとともに、この設定圧力を保持する時間、撹拌時間および設定した圧力に対応する容器内温度をそれぞれ設定しておく。この場合、圧力保持時間は、籾殻または藁が加水分解を開始する時間に設定することが好ましく、攪拌時間は籾殻または藁の性状が好適に変化し得る時間に設定することが好ましい。また、容器内温度は、水蒸気の理論圧力に付随する温度に設定される。   In addition, the control unit 6 is set in advance so that the pressure in the processing container 2 is 1.45 MPa or more, and the time for holding the set pressure, the stirring time, and the temperature in the container corresponding to the set pressure are set. Keep it. In this case, the pressure holding time is preferably set to a time when the rice husk or cocoon starts hydrolysis, and the stirring time is preferably set to a time at which the properties of the rice husk or cocoon can be suitably changed. Further, the temperature in the container is set to a temperature associated with the theoretical pressure of water vapor.

処理容器2内に投入された籾殻または藁と水酸化カルシウム源は、撹拌羽根32によって大きく攪拌されながら徐々に排出口22方向側へ移送される。処理量によっては一方向の移送だけでは処理が完了しない場合があるが、この場合には、駆動モータ33を逆方向に反転させて投入口21側へと移送し、往復移送を行う。これにより小さい処理容器2であっても充分な撹拌時間が得られる。   The rice husk or straw and the calcium hydroxide source charged into the processing container 2 are gradually transferred toward the outlet 22 while being largely stirred by the stirring blade 32. Depending on the amount of processing, the processing may not be completed by only transferring in one direction. In this case, the drive motor 33 is reversed in the reverse direction and transferred to the input port 21 side to perform reciprocal transfer. Even if the processing container 2 is smaller than this, sufficient stirring time can be obtained.

この攪拌の際、処理容器2内では、水平回動軸31よりも上方に取り付けられた送気管42から高圧の水蒸気が注入される。このため、籾殻または藁と水酸化カルシウム源は撹拌手段3の攪拌によって水平回動軸31の上方にばらばらに飛散されたときに、高圧の水蒸気が効果的に吹き付けられる。したがって、水蒸気圧力に付随する加熱および水蒸気の加水分解が効果的に進められる。   During this agitation, high-pressure steam is injected into the processing container 2 from the air supply pipe 42 attached above the horizontal rotation shaft 31. For this reason, when the rice husk or straw and the calcium hydroxide source are scattered apart above the horizontal rotation shaft 31 by the stirring of the stirring means 3, high-pressure steam is effectively sprayed. Therefore, the heating accompanying the water vapor pressure and the hydrolysis of the water vapor proceed effectively.

また、籾殻または藁と水酸化カルシウム源が攪拌されている間、制御手段6は、各温度センサ23a,23bおよび圧力センサ24の検出結果に基づき、処理容器2内の温度が設定温度を保持するとともに、圧力が1.45MPa以上を保持するように水蒸気注入手段4および圧力調整手段5を制御している。   Further, while the rice husk or straw and the calcium hydroxide source are being stirred, the control means 6 maintains the set temperature of the temperature in the processing container 2 based on the detection results of the temperature sensors 23a and 23b and the pressure sensor 24. At the same time, the water vapor injection means 4 and the pressure adjustment means 5 are controlled so that the pressure is maintained at 1.45 MPa or more.

設定した圧力保持時間が経過すると、制御手段6は水蒸気注入手段4を制御して水蒸気の注入を停止するとともに、圧力調節手段5を制御して圧力調整バルブ51を開放し、高圧水蒸気を排気管52に排気して処理容器2内を減圧する。   When the set pressure holding time has elapsed, the control means 6 controls the water vapor injection means 4 to stop the water vapor injection, and also controls the pressure adjustment means 5 to open the pressure adjustment valve 51 so that the high pressure water vapor is exhausted from the exhaust pipe. The inside of the processing container 2 is depressurized by exhausting to 52.

以上の処理により、籾殻または藁は結合分子の分離と分解が起こり、さらに水酸化カルシウム源の作用によって綿のように柔らかく繊維状に変化した材料を得ることができる。また、籾殻または藁に含有されている有害物質や臭気がほとんど消滅し、吸水性も向上する。   By the above treatment, the rice husk or cocoon is separated and decomposed by the binding molecules, and further, a material that is soft and changed into a fiber like cotton can be obtained by the action of the calcium hydroxide source. In addition, harmful substances and odors contained in rice husk or straw are almost eliminated and water absorption is improved.

つぎに、本実施形態の具体的な実施例について説明する。本実施例では、籾殻250kgに対し、アルカリ度が65%の消石灰を25kg(10重量%)混入させて処理を行った。処理容器2は、容積が3000リットルのものを使用し、処理容器2内の圧力は、上述した本願発明者の特許出願(特願2003−302971号)によって適当とされる1.45MPa〜1.96MPa、特に処理時間とコストを考慮すれば1.65〜1.85MPaが好適であるため、本実施例では1.85MPaに保持して処理を行った。なお、本実施例では、最高圧力を1.96MPaに設定したが、それ以上の圧力値であっても同様の効果を得ることができ、より処理速度を短くできる。   Next, specific examples of the present embodiment will be described. In this example, slaked lime having an alkalinity of 65% was mixed with 25 kg (10% by weight) of 250 kg of rice husk. The processing vessel 2 has a capacity of 3000 liters, and the pressure in the processing vessel 2 is 1.45 MPa to 1. .5 which is appropriate according to the above-mentioned patent application of the present inventor (Japanese Patent Application No. 2003-302971). 96 MPa, particularly 1.65 to 1.85 MPa is preferable in consideration of processing time and cost. Therefore, in this example, the processing was performed at 1.85 MPa. In the present embodiment, the maximum pressure is set to 1.96 MPa, but the same effect can be obtained even with a pressure value higher than that and the processing speed can be further shortened.

また、容器内温度は、水蒸気の理論圧力に付随する温度である200℃前後に保持するとともに、籾殻と消石灰を充填率が65%〜95%となるよう充填した。また、攪拌速度は、籾殻と消石灰とを均一に攪拌するため、下部温度センサ23bの値が上部温度センサ23aの値と一致するまでは2〜18rpmとし、一致した時点から0.15MPaまで減圧するまでは、5〜15rpmとした。一方、本実施例に対する比較例として、消石灰を混入させず、籾殻だけで同様の条件により処理を行った。これら実施例および比較例の処理結果を図2に示す。また、籾殻の処理前の形状を撮影したデジタル写真画像を図3に示し、本実施例による処理後の籾殻状態を図4に示し、比較例による処理後の籾殻状態を図5に示す。   Further, the container temperature was maintained around 200 ° C., which is a temperature associated with the theoretical pressure of water vapor, and rice husk and slaked lime were filled so that the filling rate was 65% to 95%. Further, in order to stir the rice husk and slaked lime uniformly, the stirring speed is set to 2 to 18 rpm until the value of the lower temperature sensor 23b matches the value of the upper temperature sensor 23a, and the pressure is reduced to 0.15 MPa from the time of matching. Up to 5-15 rpm. On the other hand, as a comparative example with respect to the present example, the slaked lime was not mixed, and the treatment was performed under the same conditions using only rice husk. The processing results of these examples and comparative examples are shown in FIG. Moreover, the digital photograph image which image | photographed the shape before the process of a chaff was shown in FIG. 3, the chaff state after the process by a present Example is shown in FIG. 4, and the chaff state after the process by a comparative example is shown in FIG.

本実施例の結果、実施例および比較例のいずれも処理時間は5〜10分間程度の短時間で完了した。一方、性状を比較すると、比較例において消石灰を混入せずに処理した籾殻は微粉末状であって砂のように硬いものとなったが、本実施例により消石灰を混入して処理した籾殻は綿のように柔らかいものとなり、全く異なる性状に変化した。   As a result of this example, both the example and the comparative example were completed in a short time of about 5 to 10 minutes. On the other hand, when comparing the properties, the rice husk treated without mixing slaked lime in the comparative example was a fine powder and hard like sand, but the rice husk treated by mixing slaked lime according to this example was It became soft like cotton and changed to completely different properties.

吸水性については比較例による処理の場合、吸水性が少ないものとなったが、本実施例による処理の場合は吸水率が相当高く、水分調整材に好適な性状が認められた。また、pH値については、比較例による処理の場合、pH4.3の酸性を示して酢酸系の臭気が生じているのに対し、本実施例による処理の場合、pH値は7.02の中性を示して臭気はほとんどなく、水分調整材や堆肥としても極めて扱いやすいものである。   In the case of the treatment according to the comparative example, the water absorption was low in the case of the treatment according to the comparative example. However, in the case of the treatment according to the present example, the water absorption rate was considerably high, and properties suitable for the moisture adjusting material were recognized. As for the pH value, in the case of the treatment according to the comparative example, acidity of pH 4.3 was shown and an acetic acid-based odor was generated, whereas in the case of the treatment according to this example, the pH value was 7.02. It shows the nature and has almost no odor, and it is extremely easy to handle as a moisture adjusting material or compost.

さらに処理前の籾殻の含水率は19%、保有熱量は11.24kJであったが、本実施例による処理後24時間経過したときの籾殻の含水率は11%、保有熱量は12.15kJであった。通常、時間経過によって空気中の水分を吸水して含水率が高まってしまうが、本実施例による処理後の籾殻は24時間経過後も低含水率を保持しており、この点からも水分調整材として実用性が高いといえる。また、高い保有熱量を維持していることから燃料化資源としての利用も可能である。   Furthermore, the moisture content of the rice husk before the treatment was 19% and the retained heat amount was 11.24 kJ, but the moisture content of the rice husk after the treatment according to this example was 11% and the retained heat amount was 12.15 kJ. there were. Normally, the moisture content in the air increases due to the passage of time, and the moisture content increases. However, the rice husk after the treatment according to this example retains a low moisture content even after the lapse of 24 hours. It can be said that it is highly practical as a material. In addition, since it retains a high amount of heat it can be used as a fuel resource.

上記実施例を参考にして、消石灰の混入量を変えて実験したところ、室内保管等の保管条件によって籾殻が乾燥していれば、籾殻250kgに対して消石灰の量は15kg程度であっても本実施例に近い結果が得られる。また、消石灰のアルカリ度が高ければ、例えばアルカリ度が80%程度であれば、籾殻250kgに対して消石灰18kgであっても本実施例に近い結果が得られる。   The experiment was conducted by changing the amount of slaked lime with reference to the above example. As long as the rice husk was dried according to storage conditions such as indoor storage, the amount of slaked lime was about 15 kg with respect to 250 kg of rice husk. Results close to those of the examples are obtained. Moreover, if the alkalinity of slaked lime is high, for example, if the alkalinity is about 80%, a result close to the present example can be obtained even with 18 kg of slaked lime with respect to 250 kg of rice husk.

以上より、籾殻を水分調整材として有用な性状に変換するための処理条件は、アルカリ度が65〜80%の消石灰を、籾殻に対して6重量%以上、好ましくは6〜10重量%の割合で投入することがよく、より好ましくは、アルカリ度が約65%の消石灰を籾殻に対して約10重量%の割合で投入することである。また、処理容器2内の圧力は、1.45MPa以上で5分〜90分間保持することが好ましく、より好ましくは1.65〜1.85MPaで5〜30分保持することが好ましい。高温・高圧で一定時間保持する意味は、籾殻を分解させるための余裕条件を付加させるためである。できるだけ籾殻の分解が緩やかに始まるタイミングとし、その後の減圧開始と同時にカーブに沿って分解が進行する。このとき、籾殻に含まれる水分と水蒸気が冷却され、凝縮された水分は有圧から無圧への状態変化に伴って容器外へ放散されて適度な含水率に調整され、綿状の繊維のように性状が変換される。   As mentioned above, the processing conditions for converting rice husk into a useful property as a moisture adjusting material are slaked lime having an alkalinity of 65 to 80%, a ratio of 6% by weight or more, preferably 6 to 10% by weight with respect to rice husk. More preferably, slaked lime having an alkalinity of about 65% is added at a ratio of about 10% by weight to the rice husk. Moreover, it is preferable to hold | maintain the pressure in the processing container 2 at 1.45 MPa or more for 5 minutes-90 minutes, More preferably, it is preferable to hold | maintain at 1.65-1.85 MPa for 5 to 30 minutes. The purpose of holding at high temperature and high pressure for a certain period of time is to add a margin condition for decomposing the rice husk. The timing for the decomposition of rice husk begins as slowly as possible, and the decomposition proceeds along the curve simultaneously with the start of the subsequent decompression. At this time, the moisture and water vapor contained in the rice husk are cooled, and the condensed moisture is diffused out of the container with a change in state from pressure to no pressure, adjusted to an appropriate moisture content, The properties are converted as follows.

なお、本実施形態の各構成は前述したものに限るものではなく、適宜変更することができる。   In addition, each structure of this embodiment is not restricted to what was mentioned above, It can change suitably.

例えば、上述した実施例では、水分調整材として有用な性状に変換処理させていたが、処理後の籾殻等変性材料は、融雪材、土壌改良材および肥料等にも好適な性状を備えている。   For example, in the above-described embodiment, the material is converted into a property useful as a moisture adjusting material, but the modified material such as rice husk after the processing has properties suitable for a snow melting material, a soil improvement material, a fertilizer, and the like. .

本発明に係る籾殻等変性材料を製造するシステムの一実施形態を示す模式図である。It is a mimetic diagram showing one embodiment of a system which manufactures modification materials, such as a rice husk concerning the present invention. 本実施形態における実施例および比較例の処理結果を示す表である。It is a table | surface which shows the process result of the Example in this embodiment, and a comparative example. 本実施例で処理する前の籾殻を示すデジタル写真画像である。It is a digital photograph image which shows the chaff before processing in a present Example. 本実施例で処理した後の籾殻を示すデジタル写真画像である。It is a digital photograph image which shows the chaff after processing by a present Example. 比較例によって処理した後の籾殻を示すデジタル写真画像である。It is a digital photograph image which shows the chaff after processing by a comparative example.

符号の説明Explanation of symbols

1 籾殻等変性材料製造システム
2 処理容器
3 攪拌手段
4 水蒸気注入手段
5 圧力調節手段
6 制御手段
7 サイレンサー
8 冷却装置
9 排水処理設備
21 投入口
22 排出口
23a 上部温度センサ
23b 下部温度センサ
24 圧力センサ
31 水平回動軸
32 攪拌羽根
33 駆動モータ
41 ボイラー
42 送気管
51 圧力調整バルブ
52 排気管
DESCRIPTION OF SYMBOLS 1 Modified material production system, such as rice husk 2 Processing container 3 Stirring means 4 Steam injection means 5 Pressure adjusting means 6 Control means 7 Silencer 8 Cooling device 9 Waste water treatment equipment 21 Input port 22 Outlet port 23a Upper temperature sensor 23b Lower temperature sensor 24 Pressure sensor 31 Horizontal rotation shaft 32 Stirrer blade 33 Drive motor 41 Boiler 42 Air supply pipe 51 Pressure adjustment valve 52 Exhaust pipe

Claims (6)

籾殻または藁に水酸化カルシウム源を混入し、前記籾殻または藁を燃焼させない所定の水蒸気圧力下で処理したことを特徴とする籾殻等変性材料。   A modified material for rice husks or the like, wherein the rice husk or cocoon is mixed with a calcium hydroxide source and treated under a predetermined water vapor pressure that does not burn the rice husk or cocoon. 請求項1において、籾殻または藁を1.45MPa以上の水蒸気圧力下で処理したことを特徴とする籾殻等変性材料。   The modified material for rice husks or the like according to claim 1, wherein the rice husks or cocoons are treated under a water vapor pressure of 1.45 MPa or more. 処理容器内で籾殻または藁と水酸化カルシウム源とを混合し、前記処理容器内に所定圧の水蒸気を注入して内圧および温度を上昇させ、前記籾殻または藁が燃焼しない水蒸気圧力下に保持して処理することを特徴とする籾殻等変性材料の製造方法。   A rice husk or cocoon and a calcium hydroxide source are mixed in the processing container, and a predetermined pressure of water vapor is injected into the processing container to increase the internal pressure and temperature, and the husk or cocoon is maintained at a water vapor pressure at which the rice husk or cocoon does not burn. And a method for producing a modified material such as rice husk. 請求項3において、前記水酸化カルシウム源は、アルカリ度が65〜80%の場合、籾殻または藁に対して6重量%以上の割合で投入されることを特徴とする籾殻等変性材料の製造方法。   4. The method for producing a modified material for rice husks or the like according to claim 3, wherein the calcium hydroxide source is added at a ratio of 6% by weight or more with respect to rice husk or rice husk when the alkalinity is 65 to 80%. . 請求項4において、前記水酸化カルシウム源として、アルカリ度が約65%の消石灰を籾殻または藁に対して約10重量%の割合で投入することを特徴とする籾殻等変性材料の製造方法。   5. The method for producing a modified material such as rice husk according to claim 4, wherein slaked lime having an alkalinity of about 65% is added as the calcium hydroxide source at a ratio of about 10% by weight to rice husk or rice husk. 請求項3から請求項5のいずれかにおいて、前記処理容器内の圧力を1.45MPa以上に保持することを特徴とする籾殻等変性材料の製造方法。
6. The method for producing a modified material such as rice husk according to claim 3, wherein the pressure in the processing container is maintained at 1.45 MPa or more.
JP2004145483A 2004-05-14 2004-05-14 Modified material such as rice husk and method for producing modified material such as rice husk Expired - Fee Related JP3714674B1 (en)

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TW094115073A TWI250901B (en) 2004-05-14 2005-05-10 Material comprising modified chaff or other modified substances and method for manufacturing the same
PCT/JP2005/008605 WO2005110633A1 (en) 2004-05-14 2005-05-11 Pulverized husk material and method of manufacturing the same

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