JP2002219497A - A method for treating excrement and sludge, carbonized material produced thereby and common fertilizer using the same - Google Patents

A method for treating excrement and sludge, carbonized material produced thereby and common fertilizer using the same

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Publication number
JP2002219497A
JP2002219497A JP2001019303A JP2001019303A JP2002219497A JP 2002219497 A JP2002219497 A JP 2002219497A JP 2001019303 A JP2001019303 A JP 2001019303A JP 2001019303 A JP2001019303 A JP 2001019303A JP 2002219497 A JP2002219497 A JP 2002219497A
Authority
JP
Japan
Prior art keywords
sludge
oxide
carbonized
waste
treating
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP2001019303A
Other languages
Japanese (ja)
Inventor
Shuichi Takamura
修一 高村
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to JP2001019303A priority Critical patent/JP2002219497A/en
Publication of JP2002219497A publication Critical patent/JP2002219497A/en
Pending legal-status Critical Current

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Classifications

    • 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

Landscapes

  • Exhaust Gas Treatment By Means Of Catalyst (AREA)
  • Carbon And Carbon Compounds (AREA)
  • Catalysts (AREA)
  • Fertilizers (AREA)
  • Treatment Of Sludge (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a method for treating excrement and sludge being excellently energy-saving because a carbonizing furnace can be made smaller, for powdered or grained carbonized material is easily produced and the volume reduction ratio of the excrement and sludge is high, and meanwhile carbonized material which is superior in adsorptivity and usable for a base of a water treatment agent to prevent underground water contamination as well as offensive odor of cattle excrement, and also common fertilizer using the carbonized material. SOLUTION: The method for treating excrement and sludge comprises a stirring and mixing process wherein the excrement and sludge is mixed with a treatment agent containing quicklime and perlite, and further comprises a carbonizing process wherein carbonized material is produced by carbonizing the treated material of the excrement and sludge in the stirring and mixing process.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、汚物・汚泥の処理
方法及びその方法で得られた炭化処理物、並びに炭化処
理物を汚物・汚泥に混合して得られた普通肥料に関する
ものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for treating waste and sludge, a carbonized product obtained by the method, and an ordinary fertilizer obtained by mixing the carbonized product with the waste and sludge.

【0002】[0002]

【従来の技術】近年、汚水や雨水が下水処理場で処理さ
れる際に残る汚泥は、下水道の普及に伴って増加してお
り、大半の汚泥は焼却処分されるか産業廃棄物として埋
められているのが現状である。このような処理方法で
は、汚泥が有効に利用されないばかりか、その処理設備
負荷が大きくなるとともに省エネルギー性に欠けるとい
う問題点がある。また、牛や豚等の畜産施設の糞尿処理
施設や大規模な放牧場、運動場から発生する畜糞尿から
発生する悪臭を効率的に抑える技術がなく、その悪臭に
よる苦情が依然多く発生しているという問題点がある。
また、家畜糞尿を垂れ流すこと等が原因で、家畜糞尿に
多く含まれる硝酸性窒素による地下水汚染も問題となっ
ている。そのために家畜糞尿の垂れ流しを防止し硝酸性
窒素による地下水汚染を防止する技術が早急に必要とな
っている。
2. Description of the Related Art In recent years, the amount of sludge remaining when sewage and rainwater are treated at sewage treatment plants has increased with the spread of sewerage systems, and most of the sludge is incinerated or buried as industrial waste. That is the current situation. In such a treatment method, not only is the sludge not used effectively, but also there is a problem that the load on the treatment equipment is increased and energy saving is lacking. In addition, there is no technology to efficiently control the foul odor generated from livestock manure from livestock facilities such as cattle and pigs, large-scale pastures, and sports grounds, and complaints due to the bad odor still occur. There is a problem.
Also, groundwater pollution by nitrate nitrogen, which is contained in a large amount of livestock manure, has become a problem due to the dropping of livestock manure. For this reason, there is an urgent need for a technique for preventing the excretion of livestock manure and preventing groundwater contamination by nitrate nitrogen.

【0003】そこで、汚物・汚泥の処理方法や汚物・汚
泥の有効利用が種々検討されている。例えば、特開20
00−84599号公報(以下、イ号公報と呼ぶ)に
は、「汚物・汚泥に生石灰とパーライト、更には炭を混
合させ、汚物・汚泥を脱臭、脱水及び殺菌処理すること
による汚物・汚泥の処理方法、及びその処理方法で得ら
れた汚物・汚泥処理物を用いた土壌活性材」が開示され
ている。
[0003] Various methods for treating waste and sludge and effective use of waste and sludge have been studied. For example, JP
JP-A-00-84599 (hereinafter referred to as “A”) discloses that “soil and sludge are mixed with quicklime and perlite, and also charcoal, and deodorized, dehydrated, and sterilized to remove the sludge and sludge. A treatment method and a soil active material using the treated waste material or sludge obtained by the treatment method ”are disclosed.

【0004】[0004]

【発明が解決しようとする課題】しかしながら上記従来
の汚物・汚泥の処理方法においては、以下のような課題
を有していた。 (1)イ号公報に記載の汚物・汚泥の処理方法は、汚物
や汚水等に混合されたパーライトや炭の吸着作用を利用
して汚物・汚泥の臭気を吸着し脱臭するものなので脱臭
効果が小さく、その方法で得られた汚物・汚泥処理物の
臭気を完全に抑えることができないという課題を有して
いた。 (2)イ号公報に記載の汚物・汚泥の処理方法で得られ
た汚物・汚泥処理物は、パーライトや炭の脱臭作用や吸
着作用を利用するものなので、脱臭作用や吸着作用が小
さく、畜産施設の糞尿処理施設や放牧場、運動場から発
生する強い糞尿臭気の脱臭のために汚物・汚泥処理物を
使用した場合には、悪臭を十分に吸着することができな
いという課題を有していた。また、吸着作用が小さいの
で、畜糞尿の垂れ流しを防止する糞尿の水分調整材とし
て汚物・汚泥処理物を使用した場合には、水分を十分吸
収することができず、畜糞尿に含まれる硝酸性窒素によ
る地下水汚染を防止することができないという課題を有
していた。 (3)混合攪拌される生石灰による発熱によって汚物・
汚泥に含有される水分が蒸発して減容・減量するだけな
ので、得られる汚物・汚泥処理物の嵩密度が大きく、汚
物・汚泥処理物を処理するための処理設備負荷を抑制す
ることができないという課題を有していた。 (4)汚物・汚泥処理物の機械的強度・磨耗強度が小さ
いため、粉塵化し易く取扱が困難であるという課題を有
していた。
However, the above-mentioned conventional methods for treating waste and sludge have the following problems. (1) The method of treating filth and sludge described in JP-A No. 1 uses the adsorbing action of perlite and charcoal mixed with filth and sewage to adsorb and deodorize the odor of filth and sludge. There was a problem that the odor of the sludge / sludge product obtained by the method was small and could not be completely suppressed. (2) Since the filth / sludge treated material obtained by the method for treating filth / sludge described in No. A utilizes the deodorizing or adsorbing action of perlite or charcoal, the deodorizing or adsorbing action is small, and When wastes and sludge treatment materials were used to deodorize strong manure odors generated from manure treatment facilities, pastures, and sports grounds of facilities, there was a problem that malodors could not be sufficiently absorbed. In addition, since the adsorption action is small, if waste materials or sludge treated materials are used as a moisture control material for manure to prevent runoff of manure, the water cannot be absorbed sufficiently and the nitric acid contained in manure There was a problem that groundwater contamination by nitrogen could not be prevented. (3) The waste generated by the heat generated by the mixed and stirred quicklime
Since the water contained in the sludge evaporates and only reduces the volume and weight, the bulk density of the resulting sludge and sludge treatment product is large, and the load on the processing equipment for treating the sludge and sludge treatment material cannot be suppressed. There was a problem that. (4) Since the mechanical strength and abrasion strength of the filth / sludge treated material are low, there is a problem that it is easily dusted and difficult to handle.

【0005】本発明は上記従来の課題を解決するもの
で、汚物・汚泥の減容率や減量率が高く、粒状の炭化処
理物が容易に得られ作業性に優れ、炭化炉を小型化でき
るため省エネルギー性に優れた汚物・汚泥の処理方法を
提供することを目的とする。また、本発明は、臭気が少
なく軽量で、機械的強度や磨耗強度が大きいため粉塵化
し難く取り扱いが容易で、さらに多孔質で吸着性に優れ
た、畜糞尿等の悪臭を防止する脱臭剤や水処理剤の基材
として、畜糞尿等による地下水汚染を防止する水分調整
剤や発酵促進剤として、また、微生物の保持や通気性を
高める土壌改質剤や法面の植生工で使用する法面剤の副
資材として、さらに、緊急用土嚢,防音材や断熱材とし
ても用いることができる炭化処理物を提供することを目
的とする。さらに、本発明は、重金属の溶出量が少なく
安全性に優れ、土壌を活性化するとともに施用用途の広
い汎用性に優れた普通肥料を提供することを目的とす
る。
SUMMARY OF THE INVENTION The present invention solves the above-mentioned conventional problems, and has a high volume reduction rate and a large volume reduction rate of filth and sludge. Therefore, it is an object of the present invention to provide a method for treating waste and sludge excellent in energy saving. In addition, the present invention has a low odor, is lightweight, has high mechanical strength and abrasion strength, is hard to be dusted, is easy to handle, and is porous and excellent in adsorptivity. As a base material for water treatment agents, as a water conditioner or fermentation accelerator to prevent groundwater contamination from animal waste, etc., and as a soil modifier to increase the retention and permeability of microorganisms and a method used in slope vegetation Another object of the present invention is to provide a carbonized product that can be used as an emergency sandbag, a soundproofing material, or a heat insulating material as a secondary material of the surface preparation. A further object of the present invention is to provide an ordinary fertilizer which has a small amount of heavy metal dissolved therein, is excellent in safety, activates soil, and is versatile and versatile.

【0006】[0006]

【課題を解決するための手段】上記従来の課題を解決す
るために本発明の汚物・汚泥の処理方法は、汚物・汚泥
の処理方法及びその方法で得られた炭化処理物、並びに
炭化処理物を用いた普通肥料は、以下の構成を有してい
る。
SUMMARY OF THE INVENTION In order to solve the above-mentioned conventional problems, a method for treating waste and sludge according to the present invention comprises a method for treating waste and sludge, a carbonized product obtained by the method, and a carbonized product. An ordinary fertilizer using the following has the following configuration.

【0007】請求項1に記載の汚物・汚泥の処理方法
は、汚物・汚泥に、生石灰とパーライトとを含有する処
理材を混合して攪拌する混合攪拌工程を有する汚物・汚
泥の処理方法であって、前記混合攪拌工程で得られた汚
物・汚泥処理物を炭化させて炭化処理物を得る炭化工程
を備えた構成を有している。この構成によって、以下の
ような作用が得られる。 (1)炭化工程によって、汚物・汚泥に含まれる有機物
が熱分解されるので、汚物や汚泥の嵩密度を小さくする
ことができる。 (2)炭化工程を備えているので、汚物・汚泥処理物に
含まれ悪臭の原因である有機物が熱分解され、臭気の少
ない炭化処理物が得られる。 (3)炭化工程によって汚物・汚泥が無定形炭素化し六
角炭素網平面の広がりと重なりが増加し表面積が増大す
るので、吸着性や脱臭性に優れる炭化処理物が得られ
る。 (4)炭化工程によって六角炭素網が構成されるので、
機械的強度や磨耗強度が増し、粉塵化し難く取扱が容易
で、かつ、軽量の炭化処理物が得られる。 (5)生石灰が汚物・汚泥の水分によって発熱し水分を
蒸発させる作用やパーライトの吸着作用により、汚物・
汚泥処理物の嵩密度を小さくするので、短時間の炭化で
炭化処理物が得られ、炭化炉内での滞留時間を短くでき
作業性に優れる。 (6)炭化炉内における滞留時間を短くできるので、炭
化炉を小型化でき、処理設備投資を小さくできるととも
に省エネルギー性に優れる。 (7)汚物・汚泥は、生石灰のカルシウムイオンを吸収
し凝集し、さらに生石灰と反応して安定な結晶鉱物とな
るので(以下、セメント固化反応という)、汚物・汚泥
に含有されるHg,Cd,As等の重金属を炭化処理物
内に固定化することができ、外部に溶出させず安全性に
優れる。 (8)生石灰が汚物・汚泥に含まれる水分と発熱反応を
起こし、汚物・汚泥を殺菌処理するとともに、生石灰が
水分と反応して生成されたアルカリ性を有する消石灰に
よっても汚物・汚泥が殺菌され衛生的である。
[0007] The method for treating waste and sludge according to claim 1 is a method for treating waste and sludge having a mixing and stirring step of mixing and agitating a treatment material containing quicklime and perlite with the waste and sludge. And a carbonization step of carbonizing the filth / sludge treatment product obtained in the mixing and stirring step to obtain a carbonization treatment product. With this configuration, the following operation is obtained. (1) The organic matter contained in the sludge / sludge is thermally decomposed by the carbonization step, so that the bulk density of the sludge / sludge can be reduced. (2) Since the carbonization step is provided, the organic matter contained in the sludge / sludge processed material and causing the bad smell is thermally decomposed, and a carbonized product with less odor is obtained. (3) The carbonization process turns the waste and sludge into amorphous carbon, which increases the area of the hexagonal carbon network plane and overlaps, thereby increasing the surface area, so that a carbonized product excellent in adsorptivity and deodorization can be obtained. (4) Since the carbonization process forms a hexagonal carbon network,
Mechanical strength and abrasion strength are increased, dusting is difficult, handling is easy, and a light carbonized product is obtained. (5) Quicklime generates heat by the moisture of the waste and sludge, and evaporates the moisture.
Since the bulk density of the sludge treatment material is reduced, a carbonized treatment material can be obtained by short-time carbonization, and the residence time in the carbonization furnace can be shortened, resulting in excellent workability. (6) Since the residence time in the carbonization furnace can be shortened, the size of the carbonization furnace can be reduced, the investment in processing equipment can be reduced, and energy saving is excellent. (7) Soil and sludge absorb calcium ions of quicklime and coagulate, and further react with quicklime to become a stable crystalline mineral (hereinafter referred to as cement solidification reaction), so that Hg and Cd contained in the waste and sludge are contained. Heavy metals such as As and As can be immobilized in the carbonized material, and are not eluted outside and have excellent safety. (8) Quicklime causes an exothermic reaction with the water contained in the waste and sludge to sterilize the waste and sludge, and the sludge and sludge are sterilized by the alkaline slaked lime generated by the reaction of the quicklime with the moisture and sanitation. It is a target.

【0008】ここで、汚物・汚泥としては、牛,馬,
羊,豚等の畜類の畜糞尿、し尿系汚泥、食品加工工場の
残渣・廃液,焼酎製造工場の廃液等の工場廃水処理から
排出される汚泥、下水汚泥及び農林水産廃棄物等が用い
られる。
Here, the filth and sludge include cows, horses,
Sludge, sewage sludge, agriculture, forestry and fisheries waste, etc. discharged from factory wastewater treatment, such as animal excreta from livestock such as sheep and pigs, human waste sludge, residues and effluents from food processing plants, and effluents from shochu manufacturing plants are used.

【0009】また、炭化工程で得られた炭化処理物は、
機械的強度が高く硬度が高いので、所定の粒径に分級す
ることができる。これにより、略均一な粒径を有する炭
化処理物を得ることができる。炭化処理物は、用途にも
よるが、ふるい目開き3〜15mm、好ましくは5〜1
0mmの粒子径に分級することができる。炭化処理物の
粒子径が5mmよりも小さくなるにつれ、炭化処理物を
土壌改質材や軽量緑化材として使用した場合に土壌の通
気性が低下する傾向がみられ、10mmよりも大きくな
るにつれ、炭化処理物を水浄化材として使用した場合に
水浄化材に接触せずにショートパスを起こす水が多量に
発生する傾向がみられるため、好ましくない。特に、3
mmよりも小さくなるか15mmよりも大きくなると、
これらの傾向が著しくなるため、いずれも好ましくな
い。また、用途によっては、混合攪拌工程や、混合攪拌
工程後炭化工程前に、汚物・汚泥処理物にタール,ピッ
チ,リグニン,糖蜜等の粘結剤を加え、一定粒度に成形
したり、略球状,略角柱状,略円柱状,略角錐状等に成
形したりすることもできる。これにより、形状が均一で
表面が滑らかな炭化処理物が得られるので、炭化処理物
の流動性を高め摩擦損失を小さくすることができる。
The carbonized product obtained in the carbonizing step is
Since it has high mechanical strength and high hardness, it can be classified into a predetermined particle size. Thus, a carbonized product having a substantially uniform particle size can be obtained. Depending on the application, the carbonized product has a sieve opening of 3 to 15 mm, preferably 5 to 1 mm.
It can be classified to a particle size of 0 mm. As the particle size of the carbonized product becomes smaller than 5 mm, the permeability of the soil tends to decrease when the carbonized product is used as a soil modifying material or a lightweight greening material, and as the particle size becomes larger than 10 mm, When the carbonized material is used as a water purifying material, a large amount of water that causes a short path without contacting the water purifying material tends to be generated, which is not preferable. In particular, 3
mm or larger than 15 mm,
These tendencies become remarkable, so none of them is preferable. In addition, depending on the application, a binder such as tar, pitch, lignin, molasses, etc. may be added to the filth / sludge treatment product before the mixing and stirring process, or after the mixing and stirring process and before the carbonization process, to form into a uniform particle size, , A substantially prismatic shape, a substantially cylindrical shape, a substantially pyramid shape, or the like. As a result, a carbonized product having a uniform shape and a smooth surface can be obtained, so that the fluidity of the carbonized product can be increased and the friction loss can be reduced.

【0010】本発明の請求項2に記載の発明は、請求項
1に記載の汚物・汚泥の処理方法であって、前記汚物・
汚泥40〜90重量部、好ましくは50〜80重量部
に、前記生石灰0.1〜35重量部、好ましくは0.5
〜25重量部、及び、前記パーライト0.1〜30重量
部、好ましくは0.5〜20重量部を混合する構成を有
している。この構成によって、請求項1で得られる作用
に加え、以下のような作用が得られる。 (1)最適な量の生石灰が汚物・汚泥に含有される水分
を発熱反応によって蒸発させ、パーライトの細孔が水分
を保持して汚物・汚泥の水分調整材として作用するの
で、汚物・汚泥が混合攪拌工程で粒状化され、成形工程
を用いなくても粒状の炭化処理物が容易に得られ作業性
に優れる。
[0010] The invention according to claim 2 of the present invention is the method for treating filth and sludge according to claim 1, wherein the filth and sludge are treated.
40 to 90 parts by weight of sludge, preferably 50 to 80 parts by weight, 0.1 to 35 parts by weight of the quicklime, preferably 0.5 to 0.5 parts by weight
-25 parts by weight, and 0.1-30 parts by weight of the perlite, preferably 0.5-20 parts by weight. With this configuration, the following operation is obtained in addition to the operation obtained in the first aspect. (1) Since the optimal amount of quicklime evaporates the water contained in the dirt and sludge by the exothermic reaction, and the pores of the pearlite retain the water and act as a moisture adjusting material for the dirt and sludge, the dirt and sludge are removed. It is granulated in the mixing and stirring step, and a granular carbonized product can be easily obtained without using a molding step, and the workability is excellent.

【0011】ここで、汚物・汚泥の量は、40〜90重
量部、好ましくは50〜80重量部とされる。汚物・汚
泥が50重量部より少なくなるにつれ、水分の量が少な
くなり汚物・汚水処理物が固まり難くなる傾向がみられ
るため好ましくない。80重量部より多くなるにつれ、
水分の量が多くなり混合される生石灰やパーライトでは
水分の蒸発や吸収が困難で汚物・汚水処理物がべたつい
て粒状化し難くなる傾向がみられるため好ましくない。
特に、汚物・汚泥の量が40重量部より少なくなるか9
0重量部より多くなると、これらの傾向が著しくなるた
めいずれも好ましくない。なお、汚物・汚泥としては、
含水率が60〜90wt%のものが用いられる。また、
生石灰の混合量は、汚物・汚泥40〜90重量部、好ま
しくは50〜80重量部に対して0.1〜35重量部、
好ましくは0.5〜25重量部とされる。これによっ
て、汚物・汚泥のpHを調整することができる。汚泥処
理場によっては、汚泥処理を行う際に脱水性の改善を図
る目的で工業用石灰等を汚泥に添加する調質処理を行う
場合があるからである。なお、生石灰の混合量が0.5
重量部より少なくなるにつれ、汚物・汚泥処理物のpH
を上げ難くなりアルカリ性による殺菌作用や得られた炭
化処理物による土壌の活性作用が得られ難くなる傾向が
みられ、25重量部より多くなるにつれpHが上がりす
ぎ得られた炭化処理物の施肥性が低くなる傾向がみられ
るため好ましくない。特に、生石灰の混合量が0.1重
量部より少なくなるか35重量部より多くなると、これ
らの傾向が著しくなるためいずれも好ましくない。さら
に、パーライトの混合量は、汚物・汚泥40〜90重量
部、好ましくは50〜80重量部に対して0.1〜30
重量部、好ましくは0.5〜20重量部とされる。パー
ライトの混合量が0.5重量部より少なくなるにつれ、
パーライトの水分調整作用が低下し汚物・汚泥が粒状化
され難くなる傾向がみられ、20重量部より多くなるに
つれ、混合したパーライトによって汚物・汚泥処理物の
嵩が増量し汚物・汚泥の減容率が低下し難くなる傾向が
みられるため好ましくない。特に、パーライトの混合量
が0.1重量部より少なくなるか30重量部より多くな
ると、これらの傾向が著しくなるため、いずれも好まし
くない。
Here, the amount of waste / sludge is 40 to 90 parts by weight, preferably 50 to 80 parts by weight. As the amount of filth / sludge becomes less than 50 parts by weight, the amount of water decreases and the filth / sewage treated material tends to harden, which is not preferable. As more than 80 parts by weight,
It is not preferable for quick lime or perlite mixed with a large amount of water because evaporation and absorption of the water are difficult and the filth / sewage treated material tends to become sticky and hard to granulate.
In particular, if the amount of waste / sludge is less than 40 parts by weight
When the amount is more than 0 parts by weight, these tendencies become remarkable, and neither is preferable. In addition, as waste and sludge,
Those having a water content of 60 to 90% by weight are used. Also,
The mixing amount of quicklime is 0.1 to 35 parts by weight per 40 to 90 parts by weight of sewage and sludge, preferably 50 to 80 parts by weight,
Preferably it is 0.5 to 25 parts by weight. Thereby, the pH of the filth / sludge can be adjusted. This is because, depending on the sludge treatment plant, there may be a case where a refining treatment in which industrial lime or the like is added to the sludge is performed for the purpose of improving the dewatering property when performing the sludge treatment. In addition, the mixing amount of quicklime is 0.5
As the weight becomes lower, the pH of the waste and sludge
And it is difficult to obtain the sterilizing action due to alkalinity and the soil activation action by the obtained carbonized material, and as the amount becomes more than 25 parts by weight, the pH becomes too high. Is unfavorable because of the tendency to decrease. In particular, if the mixing amount of quicklime is less than 0.1 part by weight or more than 35 parts by weight, these tendencies become remarkable, and neither is preferable. Further, the mixing amount of pearlite is 0.1 to 30 parts by weight per 40 to 90 parts by weight of filth / sludge, preferably 50 to 80 parts by weight.
Parts by weight, preferably 0.5 to 20 parts by weight. As the mixing amount of perlite becomes less than 0.5 parts by weight,
The moisture control effect of perlite tends to decrease, and it tends to be difficult to granulate waste and sludge. As the amount exceeds 20 parts by weight, the volume of waste and sludge treated material increases due to the mixed perlite, and the volume of waste and sludge decreases. This is not preferable because the rate tends to be less likely to decrease. In particular, if the mixing amount of pearlite is less than 0.1 part by weight or more than 30 parts by weight, these tendencies become remarkable, and neither is preferable.

【0012】本発明の請求項3に記載の発明は、請求項
1又は2に記載の汚物・汚泥の処理方法であって、前記
炭化工程で得られる前記炭化処理物の溶出液が、pH8
〜10である構成を有している。この構成によって、請
求項1又は2で得られる作用に加え、以下のような作用
が得られる。 (1)得られる炭化処理物の溶出液のpHが8〜10の
アルカリ性で石灰分を有しているので、土壌の活性化作
用に優れる。 (2)得られたアルカリ性の炭化処理物を酸性の牛や豚
等の畜糞尿と混合すると、畜糞尿を中和し略中性の普通
肥料が得られるので、酸性や中性の土壌を好む水田,
畑,樹園地等にも施肥することができ汎用性に優れる。
According to a third aspect of the present invention, there is provided the method for treating waste and sludge according to the first or second aspect, wherein the eluate of the carbonized product obtained in the carbonizing step has a pH of 8 or more.
-10. With this configuration, the following operation is obtained in addition to the operation obtained in claim 1 or 2. (1) Since the pH of the resulting eluate of the carbonized product is 8 to 10 and alkaline and has lime, it is excellent in soil activation. (2) When the obtained alkaline carbonized product is mixed with acidic manure of cattle and pigs, it neutralizes animal manure and obtains a nearly neutral ordinary fertilizer, and thus prefers acidic or neutral soil. Paddy field,
It can be fertilized in fields, orchards, etc., and has excellent versatility.

【0013】ここで、炭化処理物の溶出液としては、容
器に入れた炭化処理物が全て浸漬されるまで純水を加え
振とうした後、炭化処理物と分離された液が用いられ
る。なお、炭化処理物の溶出液のpHが8より小さくな
ると、セメント固化反応が起こり難く重金属の固定化が
乏しいため好ましくない。また、pHが10より大きく
なると、酸性の牛や豚等の畜糞尿と混合しても中性にな
らずアルカリ性の石灰肥料となるため好ましくない。
Here, as the eluate of the carbonized product, a liquid separated from the carbonized product is used after adding pure water and shaking until all the carbonized products placed in the container are immersed. If the pH of the eluate of the carbonized product is lower than 8, it is not preferable because the cement hardening reaction hardly occurs and the fixation of heavy metals is poor. On the other hand, if the pH is higher than 10, it is not preferable because it becomes an alkaline lime fertilizer without becoming neutral even when mixed with animal manure of an acidic cow or pig.

【0014】本発明の請求項4に記載の発明は、請求項
1乃至3の内いずれか1に記載の汚物・汚泥の処理方法
であって、前記処理材が、前記生石灰の一部又は全部に
代えて、消石灰を含有する構成を有している。この構成
によって、請求項1乃至3の内いずれか1で得られる作
用に加え、以下のような作用が得られる。 (1)消石灰は、生石灰と比較して安定で保管が容易で
あり、作業性や取扱性に優れる。 (2)消石灰は炭化炉内で加熱されると580℃で生石
灰となり、セメント固化反応により汚物・汚泥と反応し
て安定な結晶鉱物を生成するので、汚物・汚泥に含有さ
れるHg,Cd,As等の重金属を炭化処理物内に固定
化することができ外部への溶出量が小さく安全性に優れ
る。
According to a fourth aspect of the present invention, there is provided the method for treating filth and sludge according to any one of the first to third aspects, wherein the treatment material is a part or all of the quicklime. Instead of slaked lime. With this configuration, the following operation is obtained in addition to the operation obtained in any one of the first to third aspects. (1) Slaked lime is stable and easy to store compared to quick lime, and is excellent in workability and handling. (2) Slaked lime becomes quicklime at 580 ° C. when heated in a carbonization furnace, and reacts with the dirt and sludge by the cement solidification reaction to produce stable crystalline minerals. Therefore, Hg, Cd, Heavy metals such as As can be immobilized in the carbonized material, and the amount of elution to the outside is small and the safety is excellent.

【0015】本発明の請求項5に記載の発明は、請求項
1乃至4の内いずれか1に記載の汚物・汚泥の処理方法
であって、前記炭化工程が、温度400〜900℃、好
ましくは500〜800℃で処理された構成を有してい
る。この構成によって、請求項1乃至4の内いずれか1
で得られる作用に加え、以下のような作用が得られる。 (1)六角炭素網の広がりと重なりがより大きくなり、
吸着性に優れる炭化処理物が得られる。
According to a fifth aspect of the present invention, there is provided the method for treating waste or sludge according to any one of the first to fourth aspects, wherein the carbonization step is performed at a temperature of 400 to 900 ° C., preferably. Has a configuration processed at 500 to 800 ° C. According to this configuration, any one of claims 1 to 4 is provided.
In addition to the effect obtained by the above, the following effect is obtained. (1) The spread and overlap of the hexagonal carbon network become larger,
A carbonized product having excellent adsorptivity is obtained.

【0016】ここで、炭化工程で用いられる炭化装置と
しては、平炉法や掘込み堆積法,ビーハイブ炉,鉄製移
動窯,減圧炉等のバッチ式の炭化炉、横型スクリュー移
動法等の炭化炉や流動層型,攪拌流動層型,流動輸送層
型,ロータリーキルン,多段炉等の連続式の炭化炉が用
いられるが、大量の汚物・汚泥処理物を連続的に処理で
き、炉内で汚物・汚泥処理物が転動されることで均一に
炭化されるロータリーキルンが好ましく用いられる。
The carbonization apparatus used in the carbonization step includes a batch type carbonization furnace such as a flat furnace method, a digging and deposition method, a beehive furnace, an iron moving kiln, a vacuum furnace, and a carbonization furnace such as a horizontal screw moving method. A continuous type carbonization furnace such as a fluidized bed type, a stirred fluidized bed type, a fluidized bed type, a rotary kiln, a multi-stage furnace, etc. is used. A rotary kiln in which the processed material is uniformly carbonized by being rolled is preferably used.

【0017】なお、炭化炉の処理温度(炉内の雰囲気温
度)は、炭化炉の長さや滞留時間にもよるが、400〜
900℃、好ましくは500〜800℃とされる。炭化
工程の処理温度が500℃より低くなるにつれ、生成さ
れた六角炭素網同士の融合が起こり難く、高い吸着性能
を有する大きな六角炭素網が生成され難い傾向がみら
れ、また、畜糞尿を処理した場合には臭気が残る傾向が
みられ、800℃より高くなるにつれ、緻密化が進み得
られる炭化処理物の吸着性能が低下する傾向がみられる
ため好ましくない。特に、400℃よりも低くなるか9
00℃よりも高くなると、これらの傾向が著しくなるた
め、いずれも好ましくない。なお、処理温度が高い場合
は滞留時間を短くし、処理温度が低い場合は滞留時間を
長くして炭化率を調節することができる。
The processing temperature of the carbonization furnace (atmosphere temperature in the furnace) depends on the length of the carbonization furnace and the residence time.
The temperature is set to 900 ° C, preferably 500 to 800 ° C. As the treatment temperature of the carbonization step becomes lower than 500 ° C., the generated hexagonal carbon networks are less likely to fuse with each other, and a large hexagonal carbon network having high adsorption performance tends to be less likely to be generated. In this case, an odor tends to remain, and as the temperature rises above 800 ° C., the densification proceeds, and the adsorption performance of the obtained carbonized product tends to decrease, which is not preferable. In particular, will it be lower than 400 ° C or 9
If the temperature is higher than 00 ° C., these tendencies become remarkable, and neither is preferable. When the processing temperature is high, the residence time can be shortened, and when the processing temperature is low, the residence time can be extended to adjust the carbonization rate.

【0018】また、汚物・汚泥処理物が炭化炉内で燃焼
してしまうのを防止するために、炭化炉内に水蒸気を加
え、汚物・汚泥に吹き付けることができる。加熱された
高温の水蒸気を吹き付けて汚物・汚泥の周囲に充満させ
ることにより、汚物・汚泥が燃焼しない低酸素濃度の雰
囲気に曝された状態にすることができるとともに短時間
で炭化処理を行うことができ、さらに汚物・汚泥からC
OやCO2が発生するのを抑制するので炭化処理物の表
面にタールが残存するのを防止することができ、炭化処
理物の比表面積を増大させ吸着性能を高めるため好まし
い。この場合は、加熱された高温の水蒸気の温度が、炉
内の雰囲気温度である。また、この場合、炉内で高温の
水蒸気に曝される滞留時間は10〜60分、好ましくは
20〜50分とされる。20分よりも短くなるにつれ、
炭化がすすまず得られた炭化処理物の硬度が小さく粉化
し易くなる傾向がみられ、50分よりも長くなるにつ
れ、緻密化がすすみ炭化処理物の吸着性能が低下する傾
向がみられるため好ましくない。特に、10分よりも短
くなるか60分よりも長くなると、これらの傾向が著し
くなるため、いずれも好ましくない。なお、処理温度が
高い場合は滞留時間を短くし、処理温度が低い場合は滞
留時間を長くして炭化率を調節することができる。
Further, in order to prevent the waste material / sludge treated material from burning in the carbonization furnace, steam can be added to the carbonization furnace and sprayed on the waste material / sludge. By spraying heated high-temperature steam to fill the area around dirt and sludge, it can be exposed to an atmosphere of low oxygen concentration where the dirt and sludge do not burn and perform carbonization in a short time. Is produced, and C is further reduced from waste and sludge.
Since generation of O and CO 2 is suppressed, tar can be prevented from remaining on the surface of the carbonized product, and the specific surface area of the carbonized product is increased, which is preferable because the adsorption performance is enhanced. In this case, the temperature of the heated high-temperature steam is the ambient temperature in the furnace. In this case, the residence time of exposure to high-temperature steam in the furnace is 10 to 60 minutes, preferably 20 to 50 minutes. As it gets shorter than 20 minutes,
The hardness of the carbonized product obtained without carbonization tends to be small and the powder tends to be easily pulverized. As the carbonized product becomes longer than 50 minutes, the adsorption performance of the carbonized product tends to decrease and the carbonized product is likely to be deteriorated. Absent. In particular, if the time is shorter than 10 minutes or longer than 60 minutes, these tendencies become remarkable, and neither is preferable. When the processing temperature is high, the residence time can be shortened, and when the processing temperature is low, the residence time can be extended to adjust the carbonization rate.

【0019】本発明の請求項6に記載の発明は、請求項
1乃至5の内いずれか1に記載の汚物・汚泥の処理方法
であって、前記炭化工程で得られた前記炭化処理物を賦
活するガス賦活工程を備えていることを特徴とする。こ
の構成によって、請求項1乃至5の内いずれか1で得ら
れる作用に加え、以下のような作用が得られる。 (1)炭化処理物の表面がガス化されて微細孔をつく
り、比表面積が増大し吸着性能が高まる。 (2)炭化処理物の表面に付着している異物質や組織の
壊れた無定形炭素等が除去されるので、比表面積が増大
し吸着性能が高まる。 (3)賦活工程におけるガス化反応の活性化エネルギー
が、混合攪拌工程で混合される生石灰や消石灰に含まれ
るCaによって低下されるので、ガス賦活工程に要する
エネルギーを抑制でき省エネルギー性に優れるととも
に、炭化処理物の表面が容易にガス化して微細孔をつく
り、比表面積が増大し易く吸着性能が高まる。 (4)ガス賦活法を用いているので、薬品賦活法の場合
に発生する酸性ガス、特に塩素ガスによる金属材料の腐
食や環境汚染の問題が少ない。 (5)また、賦活処理に薬品賦活剤を使用していないの
で、薬品賦活剤による炭化処理物への重金属イオンの残
存がなく、得られた炭化処理物を土壌改質剤としても安
全に使用することができ、土壌改質剤の他、水分調整
剤、水浄化剤、脱臭剤、建設資材等の多様な用途で用い
ることができる炭化処理物が得られる。 (6)さらに、ガス吸着性に適した微細孔が生成されガ
ス吸着性に優れ脱臭作用に優れる炭化処理物が得られ
る。
According to a sixth aspect of the present invention, there is provided the method for treating filth and sludge according to any one of the first to fifth aspects, wherein the carbonized material obtained in the carbonizing step is used. It is characterized by comprising a gas activating step for activating. With this configuration, the following operation is obtained in addition to the operation obtained in any one of the first to fifth aspects. (1) The surface of the carbonized product is gasified to form micropores, the specific surface area increases, and the adsorption performance increases. (2) Since foreign substances and amorphous carbon having a broken structure are removed from the surface of the carbonized product, the specific surface area is increased and the adsorption performance is enhanced. (3) Since the activation energy of the gasification reaction in the activation step is reduced by Ca contained in quicklime and slaked lime mixed in the mixing and stirring step, the energy required for the gas activation step can be suppressed, and energy saving is excellent. The surface of the carbonized material is easily gasified to form micropores, the specific surface area is easily increased, and the adsorption performance is enhanced. (4) Since the gas activation method is used, there are few problems of corrosion of metal materials and environmental pollution caused by an acid gas, particularly chlorine gas, generated in the case of the chemical activation method. (5) In addition, since no chemical activator is used in the activation treatment, there is no heavy metal ion remaining in the carbonized material by the chemical activator, and the obtained carbonized material can be safely used as a soil modifier. Thus, a carbonized product that can be used in various applications such as a soil conditioner, a water conditioner, a water purifier, a deodorant, a construction material, and the like can be obtained. (6) Further, fine pores suitable for gas adsorbability are generated, and a carbonized product excellent in gas adsorbability and excellent in deodorizing action can be obtained.

【0020】ここで、ガス賦活工程で用いられるガス賦
活剤としては、水蒸気,二酸化炭素,空気及びこれらの
気体の混合されたもの,塩素ガス,いおう蒸気,亜硫酸
ガス,アンモニア等が用いられるが、金属材料の腐食や
環境汚染の問題の少ない水蒸気,二酸化炭素,空気及び
これらの気体の混合されたものが、好ましく用いられ
る。
Here, as the gas activator used in the gas activation step, steam, carbon dioxide, air and a mixture of these gases, chlorine gas, sulfur vapor, sulfurous acid gas, ammonia and the like are used. Water vapor, carbon dioxide, air and a mixture of these gases, which are less likely to cause corrosion of metal materials and environmental pollution, are preferably used.

【0021】ガス賦活工程で用いられるガス賦活装置と
しては、特に限定されるものではなく、固定層方式、ロ
ータリーキルン,多段床炉等の移動層方式、流動層方式
等の装置が用いられる。
The gas activating device used in the gas activating step is not particularly limited, and an apparatus of a fixed bed type, a moving bed type such as a rotary kiln, a multistage floor furnace, or a fluidized bed type is used.

【0022】本発明の請求項7に記載の発明は、請求項
1乃至6の内いずれか1に記載の汚物・汚泥の処理方法
であって、前記炭化工程前の前記混合攪拌工程におい
て、前記汚物・汚泥に光触媒機能を有する酸化チタン,
酸化亜鉛,酸化スズ,酸化鉄,酸化ジルコニウム,酸化
タングステン,酸化クロム,酸化モリブデン,酸化ルテ
ニウム,酸化ゲルマニウム,酸化鉛,酸化カドミウム,
酸化銅,酸化バナジウム,酸化ニオブ,酸化タンタル,
酸化マンガン,酸化コバルト,酸化ロジウム,酸化レニ
ウム,酸化ビスマス,チタン酸ストロンチウムからなる
群より選ばれる少なくとも1種の酸化物が混合された構
成を有している。この構成によって、請求項1乃至6の
内いずれか1で得られる作用に加え、以下のような作用
が得られる。 (1)炭化処理物の表面に固定された酸化チタン等の酸
化物が光触媒として作用するので、これに紫外線をあて
ると表面の水分子からヒドロキシラジカルが生成され
る。ヒドロキシラジカルは種々の有機物を分解するの
で、炭化処理物による物理的な吸着による脱臭作用に加
え、ヒドロキシラジカルによる空気中の環境汚染物質の
除去作用、水の浄化作用、殺菌・抗菌作用、脱臭・防臭
作用等に優れる炭化処理物が得られる。
According to a seventh aspect of the present invention, there is provided the method for treating filth and sludge according to any one of the first to sixth aspects, wherein the mixing and stirring step before the carbonizing step includes the step of: Titanium oxide with photocatalytic function for waste and sludge,
Zinc oxide, tin oxide, iron oxide, zirconium oxide, tungsten oxide, chromium oxide, molybdenum oxide, ruthenium oxide, germanium oxide, lead oxide, cadmium oxide,
Copper oxide, vanadium oxide, niobium oxide, tantalum oxide,
It has a configuration in which at least one oxide selected from the group consisting of manganese oxide, cobalt oxide, rhodium oxide, rhenium oxide, bismuth oxide, and strontium titanate is mixed. With this configuration, the following operation is obtained in addition to the operation obtained in any one of the first to sixth aspects. (1) An oxide such as titanium oxide fixed on the surface of the carbonized product acts as a photocatalyst, and when exposed to ultraviolet light, hydroxyl radicals are generated from water molecules on the surface. Hydroxy radicals decompose various organic substances, so in addition to the deodorizing effect of physical adsorption by carbonized products, the removal of environmental pollutants in the air by hydroxy radicals, the purification of water, the sterilization / antibacterial effect, the deodorization / A carbonized product excellent in deodorant action and the like can be obtained.

【0023】ここで、酸化チタン等の光触媒機能を有す
る酸化物は、水又は溶剤に分散させた形態で、又は粉末
状で汚物・汚泥に混合することができる。なお、酸化チ
タン等の1種又は2種以上の酸化物の混合率は、汚物・
汚泥の種類にもよるが、汚物・汚泥が炭化されて得られ
る炭化処理物に対して0.01〜5wt%とされる。混
合率が0.01wt%よりも小さくなると光触媒として
の作用が著しく低下し、5wt%よりも大きくなると物
理的な吸着による脱臭作用を示す炭化処理物の微細孔が
閉塞され物理的吸着作用が低下するため好ましくない。
Here, an oxide having a photocatalytic function, such as titanium oxide, can be mixed with water or a solvent in the form of being dispersed in water or a solvent, or in the form of powder. The mixing ratio of one or more oxides such as titanium oxide is determined by
Although it depends on the type of sludge, the content is 0.01 to 5% by weight based on the carbonized material obtained by carbonizing the sludge / sludge. When the mixing ratio is less than 0.01 wt%, the action as a photocatalyst is remarkably reduced, and when the mixing ratio is more than 5 wt%, the fine pores of the carbonized material exhibiting a deodorizing action by physical adsorption are blocked and the physical adsorption action is reduced. Is not preferred.

【0024】本発明の請求項8に記載の発明は、請求項
1乃至7の内いずれか1に記載の汚物・汚泥の処理方法
であって、前記炭化工程で得られた前記炭化処理物の嵩
比重が、0.5〜0.9である構成を有している。この
構成によって、請求項1乃至7の内いずれか1で得られ
る作用に加え、以下のような作用が得られる。 (1)軽量なので、屋根等に負担をかけず、ビルの屋上
等の緑化材として土と混合して用いることができる炭化
処理物を得ることができる。 (2)汚物や汚泥に含有されている有機物が分解されて
除去されるので、臭気が少なく快適性に優れる炭化処理
物を得ることができる。
[0024] The invention according to claim 8 of the present invention is the method for treating filth and sludge according to any one of claims 1 to 7, wherein the carbonized product obtained in the carbonization step is treated. The bulk specific gravity is 0.5 to 0.9. With this configuration, the following operation is obtained in addition to the operation obtained in any one of the first to seventh aspects. (1) Since it is lightweight, it is possible to obtain a carbonized product that can be used as a greening material for building rooftops or the like by mixing with soil without placing a burden on a roof or the like. (2) Since organic substances contained in dirt and sludge are decomposed and removed, it is possible to obtain a carbonized product having low odor and excellent comfort.

【0025】ここで、炭化処理物の嵩比重が、0.5よ
りも小さくなると炭化処理物が灰化し脱臭作用や吸着作
用が得られなくなり、0.9よりも大きくなると汚物や
汚泥に含有されている有機物の分解が不十分で臭気が残
るため好ましくない。
Here, if the bulk specific gravity of the carbonized product is smaller than 0.5, the carbonized product is ashed and no deodorizing action or adsorption action can be obtained, and if it is larger than 0.9, the carbonized product is contained in filth and sludge. It is not preferable because the decomposition of the organic substance is insufficient and an odor remains.

【0026】本発明の請求項9に記載の炭化処理物は、
請求項1乃至8の内いずれか1に記載の汚物・汚泥の処
理方法で得られた構成を有している。この構成によっ
て、以下のような作用が得られる。 (1)悪臭の原因である汚物・汚泥に含有される有機物
が熱分解されているので、臭気が少なく快適性に優れ
る。 (2)炭化工程によって構成された六角炭素網を有して
いるので、機械的強度や磨耗強度が大きく、粉塵化し難
く取扱が容易で、かつ、軽量である。 (3)表面積が大きく吸着性に優れているので、牛,
馬,羊,豚等の畜類の畜糞尿の水分を吸収させる水分調
整剤として使用すると、畜糞尿の垂れ流しを防止できる
ので、畜糞尿に多く含まれる硝酸性窒素による地下水汚
染を防止できる。また、畜糞尿の悪臭を吸収し、畜産施
設から発生する強い糞尿臭気を発生源で効率的に抑える
ことができる。 (4)また、生石灰と汚水とが反応して生成された、又
は、予め混合された消石灰がアルカリ性を有するので、
酸性の畜糞尿の中和剤として作用し、畜産施設の放牧
場、運動場の土壌の酸性化を防止する。また、多孔質で
あり微生物の着床が促進されるので発酵促進材として作
用し、短期間で畜糞尿を普通肥料化できる。 (5)表面積が大きく吸着性に優れ、さらに機械的強さ
や磨耗強さが大きいので、BOD,COD,SS等の低
減に適した水処理剤の基材として用いることができる。 (6)セメント固化反応によって、汚物・汚泥に含有さ
れるHg,Cd,As等の重金属が固定化されているの
で、重金属の溶出量が少なく、かつ、石灰分を有するの
で、安全な土壌改質剤として用いることができる。 (7)表面積が大きく多孔状なので、土壌改質材として
用いた場合は、微生物の着床を促進するとともに、土壌
の通気性・保水性・保肥性を高め植物育成に必要なリン
酸やカリ等の流出を防止する。 (8)酸化チタン等の光触媒機能を有する酸化物が固定
されている場合は、紫外線があたることにより種々の有
機物を分解するので、空気の浄化による環境汚染物質の
除去、水の浄化、殺菌・抗菌、脱臭・防臭等に優れる。 (9)軽量・多孔質なので、ビル等の屋上に敷設できる
軽量緑化材として、また、法面を防護する植生工に用い
られる法面剤の副資材として、さらには、緊急用土嚢,
高速道路等の防音材・遮音材,壁材や床材等の断熱材と
しても用いることができる。
The carbonized product according to claim 9 of the present invention is
It has a configuration obtained by the method for treating waste and sludge according to any one of claims 1 to 8. With this configuration, the following operation is obtained. (1) Since the organic matter contained in the sewage and sludge that causes the offensive odor is thermally decomposed, the odor is small and the comfort is excellent. (2) Since it has a hexagonal carbon net formed by the carbonization step, it has high mechanical strength and abrasion strength, is hard to be dusted, is easy to handle, and is lightweight. (3) Being a cow,
When used as a water regulator to absorb the moisture of animal manure of livestock such as horses, sheep, pigs, etc., it is possible to prevent runoff of animal manure and to prevent groundwater contamination by nitrate nitrogen contained in animal manure. Further, the odor of animal manure can be absorbed, and the strong manure odor generated from animal husbandry facilities can be efficiently suppressed at the source. (4) In addition, since slaked lime produced by the reaction of quicklime and sewage or mixed in advance has alkalinity,
It acts as a neutralizer for acidic animal manure and prevents acidification of the soil in pastures and playgrounds in livestock facilities. In addition, since it is porous and promotes implantation of microorganisms, it acts as a fermentation promoting material, and can convert animal manure into ordinary fertilizer in a short period of time. (5) Since it has a large surface area and excellent adsorbability, and also has high mechanical strength and abrasion strength, it can be used as a base material for a water treatment agent suitable for reducing BOD, COD, SS and the like. (6) Since heavy metals such as Hg, Cd, and As contained in the sewage and sludge are fixed by the cement solidification reaction, the amount of elution of heavy metals is small, and lime is contained. It can be used as a filler. (7) Since it has a large surface area and is porous, when it is used as a soil modifier, it promotes the implantation of microorganisms and enhances the permeability, water retention, and fertilization of the soil. Prevent outflow of potash etc. (8) When an oxide having a photocatalytic function, such as titanium oxide, is fixed, various organic substances are decomposed by exposure to ultraviolet rays. Therefore, removal of environmental pollutants by air purification, water purification, sterilization, Excellent antibacterial, deodorant, deodorant, etc. (9) As it is lightweight and porous, it can be used as a lightweight greening material that can be laid on the roof of a building or the like, as a secondary material of a slope material used for vegetation work to protect the slope, and furthermore, an emergency sandbag,
It can also be used as a soundproofing material and soundproofing material for highways and the like, and a heat insulating material such as wall materials and flooring materials.

【0027】本発明の請求項10に記載の普通肥料は、
請求項9に記載の炭化処理物が、汚物・汚泥に混合され
た構成を有している。この構成によって、以下のような
作用が得られる。 (1)炭化処理物に肥料有効成分に富む汚物等が混合さ
れ、肥料有効成分が炭化処理物の微細孔に吸着されてい
るので、肥料有効成分がゆっくり土壌に放出され長期に
渡り施肥効果を得ることができる。 (2)石灰分を含有しているので、土壌を活性化する土
壌活性材として用いることができる。 (3)普通肥料として規制がされている重金属の溶出量
が少ないので、安全性に優れる。 (4)生石灰と汚水とが反応して生成された、又は、予
め混合された消石灰がアルカリ性を有するので、汚物・
汚泥として畜糞尿を用いた場合には、酸性の畜糞尿が中
和され中性の普通肥料が得られる。そのため、農業用の
水田,畑,果樹園,茶畑等の営業用農地や家庭用の庭,
園芸用鉢等の様々な用途に使用することができるので施
用用途が広く、汎用性に優れる。 (5)普通肥料としての施用用途が広いので、汚物・汚
泥の利用価値や利用効率が高まり、汚物・汚泥の処理が
促進される。
[0027] The ordinary fertilizer according to claim 10 of the present invention comprises:
The carbonized material according to claim 9 has a configuration in which the carbonized material is mixed with waste and sludge. With this configuration, the following operation is obtained. (1) The waste material rich in active fertilizer is mixed with the carbonized material, and the fertilizer active component is adsorbed in the micropores of the carbonized material. Obtainable. (2) Since it contains lime, it can be used as a soil active material for activating soil. (3) Since the elution amount of heavy metals regulated as ordinary fertilizer is small, it is excellent in safety. (4) Since slaked lime produced by the reaction of quicklime and sewage or mixed in advance has alkalinity,
When livestock manure is used as sludge, acidic livestock manure is neutralized and a neutral ordinary fertilizer is obtained. For this reason, agricultural fields such as paddy fields, fields, orchards, tea fields, etc.
Since it can be used for various purposes such as garden pots, it is widely used and excellent in versatility. (5) Since the application as an ordinary fertilizer is wide, the utilization value and utilization efficiency of the waste and sludge are increased, and the disposal of the waste and sludge is promoted.

【0028】ここで、汚物・汚泥としては、請求項1で
説明したものが用いられるが、牛,馬,羊,豚等の畜類
の畜糞尿が用いられるのが好ましい。炭化処理物を畜産
施設の糞尿処理施設や放牧場、運動場等に敷設しておけ
ば、炭化処理物と畜糞尿の混合物を容易に大量に入手可
能であるとともに、酸性の畜糞尿がアルカリ性の炭化処
理物によって中和されるからである。なお、畜糞尿とし
ては、水分含有率が95wt%以上の牛,馬,羊及び豚
等の糞尿を用いるのが好ましいが、水分含有率が90w
t%以上に調整された鶏糞を用いることもできる。ま
た、普通肥料には、本発明の目的を損なわない範囲にお
いて、ゼオライト,バーミキュライト,フェライト,ソ
フトシリカ,モンモリナイト,クレイボール,シラスバ
ルーン等の他の副成分を含有させることができる。土壌
の通水性や通気性をさらに向上させ、普通肥料の施肥効
率を向上させるためである。
Here, as the filth / sludge, those described in claim 1 are used, but it is preferable to use animal excrement of livestock such as cows, horses, sheep, and pigs. If carbonized products are laid in manure processing facilities, pastures, playgrounds, etc. at livestock facilities, a large amount of a mixture of carbonized products and animal manure can be easily obtained, and acidic animal manure can be converted to alkaline carbonized materials. This is because it is neutralized by the processed material. It is preferable to use manure of cattle, horses, sheep, pigs and the like having a water content of 95 wt% or more as the animal manure, but the water content is 90w.
Chicken manure adjusted to t% or more can also be used. Further, the ordinary fertilizer may contain other sub-components such as zeolite, vermiculite, ferrite, soft silica, montmorinite, clay ball, and shirasu balloon as long as the object of the present invention is not impaired. This is to further improve the water permeability and air permeability of the soil and improve the fertilizer application efficiency of the ordinary fertilizer.

【0029】[0029]

【実施例】以下、本発明を実施例を用いて具体的に説明
する。なお、本発明はこれらの実施例に限定されるもの
ではない。 (汚物・汚泥処理物の製造) (製造例1)パーライト原鉱300gを1250〜13
00℃で加熱した後冷却し、9〜13倍に発泡させたパ
ーライトを得た。牛の糞尿10lに、生石灰1100g
を添加混合し、次に発泡させたパーライト300gを添
加混合して10分間攪拌した。このようにして製造例1
の粒状の汚物・汚泥処理物を得た。得られた汚物・汚泥
処理物の重量は、汚物(糞尿)の重量の約40%に減量
された。 (製造例2)製造例1の牛の糞尿に代えて豚の糞尿を用
いた以外は、製造例1と同じ条件で、製造例2の粒状の
汚物・汚泥処理物を得た。 (製造例3)製造例1の牛の糞尿に代えて島根県宍道湖
西部浄化センターで得られた脱水ケーキを用いた以外
は、製造例1と同じ条件で、製造例3の粒状の汚物・汚
泥処理物を得た。
DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be specifically described below with reference to embodiments. Note that the present invention is not limited to these examples. (Manufacture of filth / sludge treatment product) (Manufacturing example 1) 300 g of perlite raw ore is 1250 to 13
After heating at 00 ° C., the mixture was cooled to obtain a pearlite foamed 9 to 13 times. 10 l of cow manure, 1100 g of quicklime
Was added and mixed, and then 300 g of expanded perlite was added and mixed, followed by stirring for 10 minutes. Production Example 1
Of granular waste and sludge treatment. The weight of the obtained filth / sludge treatment material was reduced to about 40% of the weight of filth (manure). (Production Example 2) Except that pig manure was used in place of the cow manure of Production Example 1, the granular sludge / sludge treated product of Production Example 2 was obtained under the same conditions as in Production Example 1. (Production Example 3) Under the same conditions as in Production Example 1 except that the dehydrated cake obtained at the West Purification Center in Lake Shinji, Shimane was used in place of the excrement of cattle in Production Example 1, the granular filth of Production Example 3 was used. Sludge treatment was obtained.

【0030】(炭化処理物の製造) (実施例1〜12)製造例1、製造例2及び製造例3の
汚物・汚泥処理物を用い、(表1)に示す種々の条件で
バッチ式炭化炉を用いて炭化処理を60分間行い、実施
例1〜12の炭化処理物を得た。なお、汚物・汚泥処理
物が炭化炉内で燃焼してしまうのを防止するために、炭
化炉内には水蒸気を導入した。得られた実施例1〜12
の炭化処理物の重量は、汚物・汚泥の重量の約5〜10
%に減量された。本発明の汚物・汚泥の処理方法は炭化
工程を有するので、大きな減量率が得られることが明ら
かになった。 (比較例1〜6)製造例1、製造例2及び製造例3の汚
物・汚泥処理物を用い、(表1)に示す種々の条件でバ
ッチ式炭化炉を用いて実施例1〜12と同一の条件で炭
化処理を60分間行い、比較例1〜6の炭化処理物を得
た。
(Production of Carbonized Products) (Examples 1 to 12) Batch-type carbonization was performed using the treated wastes and sludges of Production Examples 1, 2 and 3 under various conditions shown in Table 1. Carbonization was performed for 60 minutes using a furnace to obtain carbonized products of Examples 1 to 12. In addition, steam was introduced into the carbonization furnace in order to prevent the filth / sludge treated material from burning in the carbonization furnace. Examples 1 to 12 obtained
The weight of the carbonized material is about 5 to 10 times the weight of the waste and sludge.
% Was reduced. Since the method for treating waste and sludge of the present invention has a carbonization step, it has been found that a large weight loss rate can be obtained. (Comparative Examples 1 to 6) The wastes and sludge treatment products of Production Example 1, Production Example 2 and Production Example 3 were used, and various conditions shown in (Table 1) were used. Carbonization was performed for 60 minutes under the same conditions to obtain carbonized products of Comparative Examples 1 to 6.

【表1】 [Table 1]

【0031】(炭化処理物の豚尿の処理効果の評価)実
施例1〜8及び比較例1〜4の炭化処理物を各2lを厚
手のポリ袋に入れ、豚尿1.2lを注ぎ十分に湿潤させ
た。炭化処理物に豚尿が十分に湿潤したことを確認し、
ザルを使用して水切りを行った。豚尿を湿潤させていた
時間は約5分間であった。この後、気温約10℃、湿度
40〜60%に保たれた部屋内に豚尿が湿潤された炭化
処理物を3日間放置し、3人のサンプラーが毎日定時刻
に各炭化処理物の臭気を評価した。評価基準は以下のと
おりである。×:喉を刺激し激しく臭う。△:刺激臭は
気にならない。○:やや普通肥料臭がする。評価結果を
(表1)に示す。(表1)から明らかなように、実施例
1〜8の炭化処理物は、発酵促進材として作用し、短期
間で畜糞尿を普通肥料化できることが明らかとなった。
(Evaluation of Pig Urine Treatment Effect of Carbonized Product) 2 l of each of the carbonized products of Examples 1 to 8 and Comparative Examples 1 to 4 were placed in a thick plastic bag, and 1.2 l of pork urine was sufficiently poured. Wet. Confirm that pig urine is sufficiently moistened in the carbonized material,
Draining was performed using a colander. The time that the pig urine was wet was about 5 minutes. Thereafter, the carbonized material in which pig urine is moistened is left in a room maintained at a temperature of about 10 ° C. and a humidity of 40 to 60% for three days, and three samplers are provided with odor of each carbonized material at a fixed time every day. Was evaluated. The evaluation criteria are as follows. ×: Stimulates throat and smells violently. Δ: Irritating odor is not noticeable. ○: Slightly smells of ordinary fertilizer. The evaluation results are shown in (Table 1). As is clear from (Table 1), it was clarified that the carbonized products of Examples 1 to 8 acted as fermentation promoters and could turn animal manure into ordinary fertilizer in a short period of time.

【0032】(炭化処理物の脱臭剤としての効果の評
価)次に、実施例1〜12及び比較例1〜6の炭化処理
物各0.45lを円筒状容器の長手方向の略中心部に充
填した。円筒状容器の一端側には吸引ポンプを接続し、
吸引ポンプを稼働させれば、円筒状容器の他端側から一
端側へ、充填された炭化処理物を通過する気流が発生す
るようにした。気流の流量は、吸引ポンプの能力を調整
して5l/分とした。次に、円筒状容器の他端側にアン
モニアを湿らせた布を置き、(a)充填された炭化処理
物を通過する前の空気中のアンモニア濃度、及び、
(b)充填された炭化処理物を通過した後の空気中のア
ンモニア濃度を測定した。各アンモニア濃度は、30秒
間かけて吸引した100mlの空気中のものを測定し
た。また、アンモニア濃度の測定は、吸引ポンプを起動
させてから8分経過した後に吸引した空気について行っ
た。炭化処理物の脱臭剤としての効果は、上記のアンモ
ニア濃度(a)及び(b)を用いて、除去率((a)−
(b))/(a)を比較することで行った。実施例1〜
12及び比較例1〜6の炭化処理物のアンモニア除去率
を(表1)に示す。(表1)から明らかなように、実施
例1〜12の汚物や汚泥から得られた炭化処理物は、脱
臭剤として著しい効果を発揮することが明らかとなっ
た。
(Evaluation of effect of carbonized product as deodorant) Next, 0.45 liter of each of the carbonized products of Examples 1 to 12 and Comparative Examples 1 to 6 was placed substantially at the center in the longitudinal direction of the cylindrical container. Filled. A suction pump is connected to one end of the cylindrical container,
When the suction pump was operated, an airflow passing through the filled carbonized material was generated from the other end to the one end of the cylindrical container. The flow rate of the airflow was adjusted to 5 l / min by adjusting the capacity of the suction pump. Next, a cloth moistened with ammonia is placed on the other end side of the cylindrical container, and (a) the ammonia concentration in the air before passing through the filled carbonized material; and
(B) The ammonia concentration in the air after passing through the filled carbonized material was measured. Each ammonia concentration was measured in 100 ml of air sucked in over 30 seconds. The measurement of the ammonia concentration was performed on the air sucked 8 minutes after the start of the suction pump. The effect of the carbonized product as a deodorant is determined by using the above-mentioned ammonia concentrations (a) and (b),
(B)) / (a) was compared. Example 1
Table 1 shows the ammonia removal rates of the carbonized products of No. 12 and Comparative Examples 1 to 6. As is clear from (Table 1), the carbonized products obtained from the filth and sludge of Examples 1 to 12 have a remarkable effect as a deodorant.

【0033】[0033]

【発明の効果】以上のように、本発明の汚物・汚泥の処
理方法及びその方法で得られた炭化処理物、並びに炭化
処理物を用いた普通肥料によれば、以下のような有利な
効果が得られる。請求項1に記載の発明によれば、 (1)炭化工程によって、汚物・汚泥に含まれる有機物
が熱分解されるので、汚物や汚泥の嵩密度を小さくする
ことができる汚物・汚泥の処理方法を提供することがで
きる。 (2)炭化工程を備えているので、汚物・汚泥処理物に
含まれ悪臭の原因である有機物が熱分解され、臭気の少
ない炭化処理物が得られる汚物・汚泥の処理方法を提供
することができる。 (3)炭化工程によって汚物・汚泥が無定形炭素化し六
角炭素網平面の広がりと重なりが増加し表面積が増大す
るので、吸着性や脱臭性に優れる炭化処理物が得られる
汚物・汚泥の処理方法を提供することができる。 (4)炭化工程によって六角炭素網が構成されるので、
機械的強度や磨耗強度が増し、粉塵化し難く取扱が容易
で、かつ、軽量の炭化処理物が得られる汚物・汚泥の処
理方法を提供することができる。 (5)生石灰が汚物・汚泥の水分によって発熱し水分を
蒸発させる作用やパーライトの吸着作用により、汚物・
汚泥処理物の嵩密度を小さくするので、短時間の炭化で
炭化処理物が得られ、炭化炉内での滞留時間を短くでき
作業性に優れた汚物・汚泥の処理方法を提供することが
できる。 (6)炭化炉内における滞留時間を短くできるので、炭
化炉を小型化でき、処理設備投資を小さくできるととも
に省エネルギー性に優れた汚物・汚泥の処理方法を提供
することができる。 (7)汚物・汚泥は、生石灰のカルシウムイオンを吸収
し凝集し、さらに生石灰と反応して安定な結晶鉱物とな
るので(以下、セメント固化反応という)、汚物・汚泥
に含有されるHg,Cd,As等の重金属を炭化処理物
内に固定化することができ、外部に溶出させず安全性に
優れた汚物・汚泥の処理方法を提供することができる。 (8)生石灰が汚物・汚泥に含まれる水分と発熱反応を
起こし、汚物・汚泥を殺菌処理するとともに、生石灰が
水分と反応して生成されたアルカリ性を有する消石灰に
よっても汚物・汚泥が殺菌され衛生的な汚物・汚泥の処
理方法を提供することができる。
As described above, according to the method for treating sewage and sludge of the present invention, the carbonized material obtained by the method, and the ordinary fertilizer using the carbonized material, the following advantageous effects are obtained. Is obtained. According to the first aspect of the invention, (1) the organic matter contained in the sludge / sludge is thermally decomposed by the carbonization step, so that the sludge / sludge treatment method capable of reducing the bulk density of the sludge / sludge. Can be provided. (2) Since a carbonization step is provided, it is possible to provide a method for treating filth / sludge in which organic substances contained in the filth / sludge treatment and causing odors are thermally decomposed and a carbonization treatment with low odor is obtained. it can. (3) Soil and sludge are formed into amorphous carbon by the carbonization process, and the surface area is increased due to an increase in the spread and overlap of the hexagonal carbon network plane. Therefore, a method of treating waste and sludge that can obtain a carbonized material having excellent adsorption and deodorization properties. Can be provided. (4) Since the carbonization process forms a hexagonal carbon network,
It is possible to provide a method for treating filth and sludge which increases mechanical strength and abrasion strength, is hard to be dusted, is easy to handle, and can obtain a light carbonized product. (5) Quicklime generates heat by the moisture of the waste and sludge, and evaporates the moisture.
Since the bulk density of the sludge treatment product is reduced, a carbonization treatment product can be obtained by short-time carbonization, and the residence time in the carbonization furnace can be shortened, and a waste and sludge treatment method excellent in workability can be provided. . (6) Since the residence time in the carbonization furnace can be shortened, the carbonization furnace can be downsized, the investment in the processing equipment can be reduced, and a method for treating waste and sludge excellent in energy saving can be provided. (7) Soil and sludge absorb calcium ions of quicklime and coagulate, and further react with quicklime to become a stable crystalline mineral (hereinafter referred to as cement solidification reaction), so that Hg and Cd contained in the waste and sludge are contained. It is possible to immobilize heavy metals such as As and As in the carbonized material, and to provide a method for treating filth and sludge which is not eluted outside and is excellent in safety. (8) Quicklime causes an exothermic reaction with the water contained in the waste and sludge to sterilize the waste and sludge, and the sludge and sludge are sterilized by the alkaline slaked lime generated by the reaction of the quicklime with the moisture and sanitation. Wastewater and sludge treatment method can be provided.

【0034】請求項2に記載の発明によれば、請求項1
の効果に加え、 (1)最適な量の生石灰が汚物・汚泥に含有される水分
を発熱反応によって蒸発させ、パーライトの細孔が水分
を保持して汚物・汚泥の水分調整材として作用するの
で、汚物・汚泥が混合攪拌工程で粒状化され、成形工程
を用いなくても粒状の炭化処理物が容易に得られ作業性
に優れた汚物・汚泥の処理方法を提供することができ
る。
According to the invention described in claim 2, according to claim 1
In addition to the effects of (1), the optimal amount of quicklime evaporates the moisture contained in the waste and sludge by the exothermic reaction, and the pores of the pearlite retain the moisture and act as a moisture regulator for the waste and sludge. Further, it is possible to provide a method for treating waste and sludge excellent in workability by easily obtaining a granular carbonized product without using a molding step, since the waste and sludge are granulated in the mixing and stirring step.

【0035】請求項3に記載の発明によれば、請求項1
又は2の効果に加え、 (1)得られる炭化処理物のpHが8〜10のアルカリ
性で石灰分を有しているので、土壌の活性化作用に優れ
た汚物・汚泥の処理方法を提供することができる。 (2)得られたアルカリ性の炭化処理物を酸性の牛や豚
等の畜糞尿と混合すると、畜糞尿を中和し略中性の普通
肥料が得られるので、酸性や中性の土壌を好む水田,
畑,樹園地等にも施肥することができ汎用性に優れた汚
物・汚泥の処理方法を提供することができる。
According to the invention described in claim 3, according to claim 1
In addition to the effects of (2), (1) Since the obtained carbonized product has an alkaline pH of 8 to 10 and has a lime content, it provides a method of treating soil and sludge excellent in soil activation. be able to. (2) When the obtained alkaline carbonized product is mixed with acidic manure of cattle and pigs, it neutralizes animal manure and obtains a nearly neutral ordinary fertilizer, and thus prefers acidic or neutral soil. Paddy field,
Fertilizer can be applied to fields, orchards, and the like, and a versatile waste / sludge treatment method can be provided.

【0036】請求項4に記載の発明によれば、請求項1
乃至3の内いずれか1の効果に加え、 (1)消石灰は、生石灰と比較して安定で保管が容易で
あり、作業性や取扱性に優れた汚物・汚泥の処理方法を
提供することができる。 (2)消石灰は炭化炉内で加熱されると580℃で生石
灰となり、セメント固化反応により汚物・汚泥と反応し
て安定な結晶鉱物を生成するので、汚物・汚泥に含有さ
れるHg,Cd,As等の重金属を炭化処理物内に固定
化することができ外部への溶出量が小さく安全性に優れ
た汚物・汚泥の処理方法を提供することができる。
According to the fourth aspect of the present invention, the first aspect is provided.
(1) Slaked lime is more stable and easier to store than quick lime, and provides a method for treating waste and sludge excellent in workability and handling. it can. (2) Slaked lime becomes quicklime at 580 ° C. when heated in a carbonization furnace, and reacts with the dirt and sludge by the cement solidification reaction to produce stable crystalline minerals. Therefore, Hg, Cd, A heavy metal such as As can be immobilized in the carbonized material, and a small amount of elution to the outside can be provided, so that a method for treating waste and sludge excellent in safety can be provided.

【0037】請求項5に記載の発明によれば、請求項1
乃至4の内いずれか1の効果に加え、 (1)六角炭素網の広がりと重なりがより大きくなり、
吸着性に優れる炭化処理物が得られる汚物・汚泥の処理
方法を提供することができる。
According to the invention of claim 5, according to claim 1,
In addition to the effects of any one of (1) to (4), (1) the spread and overlap of the hexagonal carbon network become larger,
It is possible to provide a method of treating waste and sludge from which a carbonized product having excellent adsorption properties can be obtained.

【0038】請求項6に記載の発明によれば、請求項1
乃至5の内いずれか1の効果に加え、 (1)炭化処理物の表面がガス化されて微細孔をつく
り、比表面積が増大し吸着性能の高い炭化処理物が得ら
れる汚物・汚泥の処理方法を提供することができる。 (2)炭化処理物の表面に付着している異物質や組織の
壊れた無定形炭素等が除去されるので、比表面積が増大
し吸着性能の高い炭化処理物が得られる汚物・汚泥の処
理方法を提供することができる。 (3)賦活工程におけるガス化反応の活性化エネルギー
が、混合攪拌工程で混合される生石灰や消石灰に含まれ
るCaによって低下されるので、ガス賦活工程に要する
エネルギーを抑制でき省エネルギー性に優れるととも
に、炭化処理物の表面が容易にガス化して微細孔をつく
り、比表面積が増大し易く吸着性能の高い炭化処理物が
得られる汚物・汚泥の処理方法を提供することができ
る。 (4)ガス賦活法を用いているので、薬品賦活法の場合
に発生する酸性ガス、特に塩素ガスによる金属材料の腐
食や環境汚染の問題が少ない汚物・汚泥の処理方法を提
供することができる。 (5)また、賦活処理に薬品賦活剤を使用していないの
で、薬品賦活剤による炭化処理物への重金属イオンの残
存がなく、得られた炭化処理物を土壌改質剤としても安
全に使用することができ、土壌改質剤の他、水分調整
剤、水浄化剤、脱臭剤、建設資材等の多様な用途で用い
ることができる炭化処理物が得られる汚物・汚泥の処理
方法を提供することができる。 (6)さらに、ガス吸着性に適した微細孔が生成されガ
ス吸着性に優れ脱臭作用に優れる炭化処理物が得られる
汚物・汚泥の処理方法を提供することができる。
According to the invention of claim 6, according to claim 1,
In addition to the effects of any one of (1) to (5), (1) Treatment of filth / sludge in which the surface of the carbonized material is gasified to form micropores, the specific surface area increases, and the carbonized material with high adsorption performance is obtained. A method can be provided. (2) Treatment of filth and sludge that removes extraneous substances and amorphous carbon with broken structure attached to the surface of the carbonized product, thereby increasing the specific surface area and obtaining a carbonized product with high adsorption performance. A method can be provided. (3) Since the activation energy of the gasification reaction in the activation step is reduced by Ca contained in quicklime and slaked lime mixed in the mixing and stirring step, the energy required for the gas activation step can be suppressed, and energy saving is excellent. It is possible to provide a method for treating a filth / sludge in which the surface of the carbonized material is easily gasified to form micropores, the specific surface area is easily increased, and the carbonized material having high adsorption performance is obtained. (4) Since the gas activation method is used, it is possible to provide a method for treating filth and sludge with less problems of corrosion of metal materials and environmental pollution due to acid gas, particularly chlorine gas generated in the case of the chemical activation method. . (5) In addition, since no chemical activator is used in the activation treatment, there is no heavy metal ion remaining in the carbonized material by the chemical activator, and the obtained carbonized material can be safely used as a soil modifier. Provided is a method for treating filth and sludge which can be used in various applications such as a soil conditioner, a water conditioner, a water purifier, a deodorant, a construction material and the like, in addition to a soil modifier. be able to. (6) Further, it is possible to provide a method for treating filth and sludge, in which micropores suitable for gas adsorption are generated, and a carbonized material having excellent gas adsorption and excellent deodorizing action is obtained.

【0039】請求項7に記載の発明によれば、請求項1
乃至6の内いずれか1の効果に加え、 (1)炭化処理物の表面に固定された酸化チタン等の酸
化物が光触媒として作用するので、これに紫外線をあて
ると表面の水分子からヒドロキシラジカルが生成され
る。ヒドロキシラジカルは種々の有機物を分解するの
で、炭化処理物による物理的な吸着による脱臭作用に加
え、ヒドロキシラジカルによる空気中の環境汚染物質の
除去作用、水の浄化作用、殺菌・抗菌作用、脱臭・防臭
作用等に優れる炭化処理物が得られる汚物・汚泥の処理
方法を提供することができる。
According to the invention of claim 7, according to claim 1,
(1) An oxide such as titanium oxide fixed on the surface of the carbonized product acts as a photocatalyst. When ultraviolet light is applied to the photocatalyst, hydroxyl radicals are generated from water molecules on the surface. Is generated. Hydroxy radicals decompose various organic substances, so in addition to the deodorizing effect of physical adsorption by carbonized products, the removal of environmental pollutants in the air by hydroxy radicals, the purification of water, the sterilization / antibacterial effect, the deodorization / It is possible to provide a method for treating filth and sludge from which a carbonized product excellent in deodorization and the like can be obtained.

【0040】請求項8に記載の発明によれば、請求項1
乃至7の内いずれか1の効果に加え、 (1)軽量なので、屋根等に負担をかけず、ビルの屋上
等の緑化材として土と混合して用いることができる炭化
処理物を得ることができる汚物・汚泥の処理方法を提供
することができる。 (2)汚物や汚泥に含有されている有機物が分解されて
除去されるので、臭気が少なく快適性に優れる炭化処理
物を得ることができる汚物・汚泥の処理方法を提供する
ことができる。
According to the invention described in claim 8, according to claim 1,
In addition to the effects of any one of (1) to (7), (1) it is possible to obtain a carbonized product that can be used as a greening material for building rooftops or the like by mixing with soil because it is lightweight and does not put a burden on roofs. A method for treating waste and sludge that can be provided can be provided. (2) Since the organic matter contained in the dirt and sludge is decomposed and removed, it is possible to provide a method for treating dirt and sludge that can obtain a carbonized product having less odor and excellent comfort.

【0041】請求項9に記載の発明によれば、 (1)悪臭の原因である汚物・汚泥に含有される有機物
が熱分解されているので、臭気が少なく快適性に優れた
炭化処理物を提供することができる。 (2)炭化工程によって構成された六角炭素網を有して
いるので、機械的強度や磨耗強度が大きく、粉塵化し難
く取扱が容易で、かつ、軽量の炭化処理物を提供するこ
とができる。 (3)表面積が大きく吸着性に優れているので、牛,
馬,羊,豚等の畜類の畜糞尿の水分を吸収させる水分調
整剤として使用すると、畜糞尿の垂れ流しを防止できる
ので、畜糞尿に多く含まれる硝酸性窒素による地下水汚
染を防止できる。また、畜糞尿の悪臭を吸収し、畜産施
設から発生する強い糞尿臭気を発生源で効率的に抑える
ことができる炭化処理物を提供することができる。 (4)また、生石灰と汚水とが反応して生成された、又
は、予め混合された消石灰がアルカリ性を有するので、
酸性の畜糞尿の中和剤として作用し、畜産施設の放牧
場、運動場の土壌の酸性化を防止する。また、多孔質で
あり微生物の着床が促進されるので発酵促進材として作
用し、短期間で畜糞尿を普通肥料化できる炭化処理物を
提供することができる。 (5)表面積が大きく吸着性に優れ、さらに機械的強さ
や磨耗強さが大きいので、BOD,COD,SS等の低
減に適した水処理剤の基材として用いることができる炭
化処理物を提供することができる。 (6)セメント固化反応によって、汚物・汚泥に含有さ
れるHg,Cd,As等の重金属が固定化されているの
で、重金属の溶出量が少なく、かつ、石灰分を有するの
で、安全な土壌改質剤として用いることができる炭化処
理物を提供することができる。 (7)表面積が大きく多孔状なので、土壌改質材として
用いた場合は、微生物の着床を促進するとともに、土壌
の通気性・保水性・保肥性を高め植物育成に必要なリン
酸やカリ等の流出を防止する炭化処理物を提供すること
ができる。 (8)酸化チタン等の光触媒機能を有する酸化物が固定
されている場合は、紫外線があたることにより種々の有
機物を分解するので、空気の浄化による環境汚染物質の
除去、水の浄化、殺菌・抗菌、脱臭・防臭等に優れた炭
化処理物を提供することができる。 (9)軽量・多孔質なので、ビル等の屋上に敷設できる
軽量緑化材として、また、法面を防護する植生工に用い
られる法面剤の副資材として、さらには、緊急用土嚢,
高速道路等の防音材・遮音材,壁材や床材等の断熱材と
しても用いることができる炭化処理物を提供することが
できる。
According to the ninth aspect of the present invention, (1) Since the organic matter contained in the filth and sludge which is the cause of the offensive odor is thermally decomposed, a carbonized material having a low odor and excellent comfort can be obtained. Can be provided. (2) Since it has a hexagonal carbon net formed by the carbonization step, it is possible to provide a light carbonized material that has high mechanical strength and abrasion strength, is hard to be dusted, is easy to handle, and is lightweight. (3) Being a cow,
When used as a water regulator to absorb the moisture of animal manure of livestock such as horses, sheep, pigs, etc., it is possible to prevent runoff of animal manure and to prevent groundwater contamination by nitrate nitrogen contained in animal manure. Further, it is possible to provide a carbonized material capable of absorbing the malodor of animal manure and effectively suppressing the strong manure odor generated from the animal husbandry facility at the source. (4) In addition, since slaked lime produced by the reaction of quicklime and sewage or mixed in advance has alkalinity,
It acts as a neutralizer for acidic animal manure and prevents acidification of the soil in pastures and playgrounds in livestock facilities. In addition, since it is porous and promotes implantation of microorganisms, it can act as a fermentation promoting material, and can provide a carbonized material that can convert animal manure into ordinary fertilizer in a short period of time. (5) Provide a carbonized material that can be used as a base material for water treatment agents suitable for reducing BOD, COD, SS, etc. because of its large surface area, excellent adsorbability, and high mechanical strength and abrasion strength. can do. (6) Since heavy metals such as Hg, Cd, and As contained in sewage and sludge are fixed by the cement solidification reaction, the amount of elution of heavy metals is small, and lime is contained. A carbonized product that can be used as a filler can be provided. (7) Since it has a large surface area and is porous, when it is used as a soil modifier, it promotes the implantation of microorganisms and enhances the permeability, water retention, and fertilization of the soil. A carbonized product that prevents outflow of potash and the like can be provided. (8) When an oxide having a photocatalytic function, such as titanium oxide, is fixed, various organic substances are decomposed by exposure to ultraviolet rays. Therefore, removal of environmental pollutants by air purification, water purification, sterilization, It is possible to provide a carbonized product excellent in antibacterial properties, deodorization and deodorization. (9) As it is lightweight and porous, it can be used as a lightweight greening material that can be laid on the roof of a building or the like, as a secondary material of a slope material used for vegetation work to protect the slope, and furthermore, an emergency sandbag,
It is possible to provide a carbonized material that can be used also as a soundproofing material / sound insulating material for a highway or the like, or a heat insulating material such as a wall material or a floor material.

【0042】請求項10に記載の発明によれば、 (1)炭化処理物に肥料有効成分に富む汚物等が混合さ
れ、肥料有効成分が炭化処理物の微細孔に吸着されてい
るので、肥料有効成分がゆっくり土壌に放出され長期に
渡り施肥効果を得ることができる普通肥料を提供するこ
とができる。 (2)石灰分を含有しているので、土壌を活性化する土
壌活性材として用いることができる普通肥料を提供する
ことができる。 (3)普通肥料として規制がされている重金属の溶出量
が少ないので、安全性に優れた普通肥料を提供すること
ができる。 (4)生石灰と汚水とが反応して生成された、又は、予
め混合された消石灰がアルカリ性を有するので、汚物・
汚泥として畜糞尿を用いた場合には、酸性の畜糞尿が中
和され中性の普通肥料が得られる。そのため、農業用の
水田,畑,果樹園,茶畑等の営業用農地や家庭用の庭,
園芸用鉢等の様々な用途に使用することができるので施
用用途が広く、汎用性に優れた普通肥料を提供すること
ができる。 (5)普通肥料としての施用用途が広いので、汚物・汚
泥の利用価値や利用効率が高まり、汚物・汚泥の処理が
促進される普通肥料を提供することができる。
According to the tenth aspect of the present invention, (1) the carbonized material is mixed with filth or the like rich in the effective fertilizer, and the fertilizer effective component is adsorbed in the fine pores of the carbonized material. It is possible to provide an ordinary fertilizer capable of slowly releasing an active ingredient into the soil and obtaining a fertilizing effect over a long period of time. (2) Since it contains lime, an ordinary fertilizer that can be used as a soil activating material for activating soil can be provided. (3) Since the elution amount of heavy metals regulated as ordinary fertilizers is small, it is possible to provide ordinary fertilizers excellent in safety. (4) Since slaked lime produced by the reaction of quicklime and sewage or mixed in advance has alkalinity,
When livestock manure is used as sludge, acidic livestock manure is neutralized and a neutral ordinary fertilizer is obtained. For this reason, agricultural fields such as paddy fields, fields, orchards, tea fields, etc.
Since it can be used for various purposes such as garden pots, it can be applied to a wide range of applications and can provide a general fertilizer excellent in versatility. (5) Since the application use as the ordinary fertilizer is wide, the utilization value and utilization efficiency of the waste / sludge are enhanced, and the ordinary fertilizer in which the disposal of the waste / sludge is promoted can be provided.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) B01J 35/02 C05G 3/00 Z C01B 31/10 103 C05G 3/00 B01D 53/36 C 103 H ZABJ Fターム(参考) 4D048 AA21 AA22 AB03 BA05X BA07Y BA08Y BA15Y BA16Y BA20Y BA21Y BA22Y BA23Y BA24Y BA25Y BA26Y BA27Y BA28Y BA29Y BA32Y BA33Y BA35Y BA36Y BA37Y BA41Y BA42Y EA01 4D059 AA01 AA03 AA07 BB05 BB13 BB14 BJ00 BK01 BK13 BK23 CC01 CC04 CC06 DA04 DA05 DA21 DA53 EB05 EB06 4G046 HA09 HB00 HC09 4G069 AA01 AA03 AA08 BA04A BA05A BA08A BA08B BA31C BA48A BB04A BB06A BC12A BC21A BC22A BC23A BC25A BC31A BC35A BC36A BC50A BC54A BC55A BC56A BC58A BC59A BC60A BC62A BC64A BC66A BC67A BC70A BC71A CA01 CA05 CA10 CA11 CA17 DA05 FA02 FA08 FB07 FB29 FC02 FC07 4H061 AA01 CC01 CC36 CC42 CC51 DD04 EE70 HH03 HH25 HH42 HH46 ──────────────────────────────────────────────────の Continued on the front page (51) Int.Cl. 7 Identification FI FI Theme coat ゛ (Reference) B01J 35/02 C05G 3/00 Z C01B 31/10 103 C05G 3/00 B01D 53/36 C 103 H ZABJ F Term (Reference) 4D048 AA21 AA22 AB03 BA05X BA07Y BA08Y BA15Y BA16Y BA20Y BA21Y BA22Y BA23Y BA24Y BA25Y BA26Y BA27Y BA28Y BA29Y BA32Y BA33Y BA35Y BA36Y BA37Y BA41Y BA42Y EA01 4D059 AA01 BB01 CB01 EB06 4G046 HA09 HB00 HC09 4G069 AA01 AA03 AA08 BA04A BA05A BA08A BA08B BA31C BA48A BB04A BB06A BC12A BC21A BC22A BC23A BC25A BC31A BC35A BC36A BC50A BC54A BC55A BC56A BC70 BC05 BC02 BC01 BC02 4H061 AA01 CC01 CC36 CC42 CC51 DD04 EE70 HH03 HH 25 HH42 HH46

Claims (10)

【特許請求の範囲】[Claims] 【請求項1】 汚物・汚泥に、生石灰とパーライトとを
含有する処理材を混合して攪拌する混合攪拌工程を有す
る汚物・汚泥の処理方法であって、前記混合攪拌工程で
得られた汚物・汚泥処理物を炭化させて炭化処理物を得
る炭化工程を備えていることを特徴とする汚物・汚泥の
処理方法。
1. A method for treating waste and sludge, comprising a mixing and stirring step of mixing and stirring a treatment material containing quicklime and perlite with the waste and sludge, wherein the waste and sludge obtained in the mixing and stirring step are mixed. A method for treating waste and sludge, comprising a carbonization step of carbonizing a sludge treatment product to obtain a carbonized treatment product.
【請求項2】 前記汚物・汚泥40〜90重量部、好ま
しくは50〜80重量部に、前記生石灰0.1〜35重
量部、好ましくは0.5〜25重量部、及び、前記パー
ライト0.1〜30重量部、好ましくは0.5〜20重
量部を混合することを特徴とする請求項1に記載の汚物
・汚泥の処理方法。
2. The lime / sludge 40 to 90 parts by weight, preferably 50 to 80 parts by weight, the quicklime 0.1 to 35 parts by weight, preferably 0.5 to 25 parts by weight, and the pearlite 0.1 to 25 parts by weight. The method according to claim 1, wherein 1 to 30 parts by weight, preferably 0.5 to 20 parts by weight, is mixed.
【請求項3】 前記炭化工程で得られた前記炭化処理物
の溶出液が、pH8〜10であることを特徴とする請求
項1又は2に記載の汚物・汚泥の処理方法。
3. The method for treating waste and sludge according to claim 1, wherein the eluate of the carbonized product obtained in the carbonizing step has a pH of 8 to 10.
【請求項4】 前記生石灰の一部又は全部に代えて、消
石灰を混合することを特徴とする請求項1乃至3の内い
ずれか1に記載の汚物・汚泥の処理方法。
4. The method for treating waste and sludge according to claim 1, wherein slaked lime is mixed instead of part or all of the quick lime.
【請求項5】 前記炭化工程が、温度400〜900
℃、好ましくは500〜800℃で処理されていること
を特徴とする請求項1乃至4の内いずれか1に記載の汚
物・汚泥の処理方法。
5. The method according to claim 1, wherein the carbonization step is performed at a temperature of 400 to 900.
The method for treating filth / sludge according to any one of claims 1 to 4, wherein the treatment is performed at a temperature of 500C, preferably 500C to 800C.
【請求項6】 前記炭化工程で得られた前記炭化処理物
を賦活するガス賦活工程を備えていることを特徴とする
請求項1乃至5の内いずれか1に記載の汚物・汚泥の処
理方法。
6. The method for treating waste and sludge according to claim 1, further comprising a gas activation step for activating the carbonized product obtained in the carbonization step. .
【請求項7】 前記炭化工程前の前記混合攪拌工程にお
いて、前記汚物・汚泥に光触媒機能を有する酸化チタ
ン,酸化亜鉛,酸化スズ,酸化鉄,酸化ジルコニウム,
酸化タングステン,酸化クロム,酸化モリブデン,酸化
ルテニウム,酸化ゲルマニウム,酸化鉛,酸化カドミウ
ム,酸化銅,酸化バナジウム,酸化ニオブ,酸化タンタ
ル,酸化マンガン,酸化コバルト,酸化ロジウム,酸化
レニウム,酸化ビスマス,チタン酸ストロンチウムから
なる群より選ばれる少なくとも1種の酸化物が混合され
ていることを特徴とする請求項1乃至6の内いずれか1
に記載の汚物・汚泥の処理方法。
7. In the mixing and stirring step before the carbonization step, titanium oxide, zinc oxide, tin oxide, iron oxide, zirconium oxide, which has a photocatalytic function for the waste and sludge,
Tungsten oxide, chromium oxide, molybdenum oxide, ruthenium oxide, germanium oxide, lead oxide, cadmium oxide, copper oxide, vanadium oxide, niobium oxide, tantalum oxide, manganese oxide, cobalt oxide, rhodium oxide, rhenium oxide, bismuth oxide, titanate 7. The method according to claim 1, wherein at least one oxide selected from the group consisting of strontium is mixed.
The method for treating filth and sludge according to the above.
【請求項8】 前記炭化工程で得られた前記炭化処理物
の嵩比重が、0.5〜0.9であることを特徴とする請
求項1乃至7の内いずれか1に記載の汚物・汚泥の処理
方法。
8. The filth according to claim 1, wherein a bulk specific gravity of the carbonized product obtained in the carbonizing step is 0.5 to 0.9. Sludge treatment method.
【請求項9】 請求項1乃至8の内いずれか1に記載の
汚物・汚泥の処理方法で得られたことを特徴とする炭化
処理物。
9. A carbonized material obtained by the method for treating filth and sludge according to claim 1.
【請求項10】 請求項9に記載の炭化処理物が、汚物
・汚泥に混合されていることを特徴とする普通肥料。
10. An ordinary fertilizer, wherein the carbonized product according to claim 9 is mixed with waste and sludge.
JP2001019303A 2001-01-26 2001-01-26 A method for treating excrement and sludge, carbonized material produced thereby and common fertilizer using the same Pending JP2002219497A (en)

Priority Applications (1)

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Applications Claiming Priority (1)

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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006088020A (en) * 2004-09-22 2006-04-06 Japan Sewage Works Agency Stabilizing treatment method for carbonized product
JP2007169164A (en) * 2005-12-19 2007-07-05 Beone:Kk Raw material of environment-cleaning cosmetic
JP2007522069A (en) * 2004-02-13 2007-08-09 ナン,ゲリー,ロバート Soluble biogenic silica and uses thereof
JP2008006434A (en) * 2006-06-02 2008-01-17 Excelsior Inc Excreta treating agent and excreta treatment method using it
CN108854957A (en) * 2018-06-28 2018-11-23 普定县石阶农业开发有限公司 A method of administering pig farm exhaust gas

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007522069A (en) * 2004-02-13 2007-08-09 ナン,ゲリー,ロバート Soluble biogenic silica and uses thereof
JP2006088020A (en) * 2004-09-22 2006-04-06 Japan Sewage Works Agency Stabilizing treatment method for carbonized product
JP2007169164A (en) * 2005-12-19 2007-07-05 Beone:Kk Raw material of environment-cleaning cosmetic
JP2008006434A (en) * 2006-06-02 2008-01-17 Excelsior Inc Excreta treating agent and excreta treatment method using it
CN108854957A (en) * 2018-06-28 2018-11-23 普定县石阶农业开发有限公司 A method of administering pig farm exhaust gas

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