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JP3025777B2 - Method and apparatus for producing fertilizer from inorganic waste - Google Patents

Method and apparatus for producing fertilizer from inorganic waste

Info

Publication number
JP3025777B2
JP3025777B2 JP6163908A JP16390894A JP3025777B2 JP 3025777 B2 JP3025777 B2 JP 3025777B2 JP 6163908 A JP6163908 A JP 6163908A JP 16390894 A JP16390894 A JP 16390894A JP 3025777 B2 JP3025777 B2 JP 3025777B2
Authority
JP
Japan
Prior art keywords
inorganic waste
raw material
calcium oxide
fertilizer
feeder
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.)
Expired - Fee Related
Application number
JP6163908A
Other languages
Japanese (ja)
Other versions
JPH0826870A (en
Inventor
剛 加藤
Original Assignee
株式会社イヅワ
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 株式会社イヅワ filed Critical 株式会社イヅワ
Priority to JP6163908A priority Critical patent/JP3025777B2/en
Publication of JPH0826870A publication Critical patent/JPH0826870A/en
Application granted granted Critical
Publication of JP3025777B2 publication Critical patent/JP3025777B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

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
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A40/00Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
    • Y02A40/10Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
    • Y02A40/20Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses

Landscapes

  • Fertilizers (AREA)
  • Processing Of Solid Wastes (AREA)
  • Treatment Of Sludge (AREA)

Description

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

【0001】[0001]

【産業上の利用分野】本発明は、ケイソウ土汚泥、炭酸
カルシウムケーキ、ゼオライトケーキ等の食品製造に由
来する無機性廃棄物を原料にした肥料の製造方法及びそ
の装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method and an apparatus for producing fertilizer from inorganic waste derived from the production of foods such as diatomaceous earth sludge, calcium carbonate cake, and zeolite cake.

【0002】[0002]

【従来の技術】上記の無機性廃棄物に対する従来の処理
方法は、できるだけ機械的脱水を行なったあと、そのま
ま最終処分場に埋立て処分したり、場合によっては乾燥
して肥料にしたり、焼却してその灰を最終処分場に投棄
するのが一般的であった。
2. Description of the Related Art In the conventional treatment method for inorganic wastes described above, after mechanically dewatering as much as possible, the wastes are landfilled as they are in a final disposal site, or, in some cases, dried into fertilizer or incinerated. The ash was generally dumped at a final disposal site.

【0003】[0003]

【発明が解決しようとする課題】しかしながら、上記の
機械的脱水を行なったあと、そのまま最終処分場に埋立
て処分することは臭気や運搬上に不都合があり、また、
乾燥・焼却法は安全確実な方法であるが、石油等のエネ
ルギー多量消費型であり、排ガス処理に建設費、維持費
ともに多くかかる。
However, if the above-mentioned mechanical dehydration is performed and then landfilled at the final disposal site as it is, there are inconveniences in odor and transportation, and
Although the drying and incineration method is a safe and reliable method, it consumes a large amount of energy such as petroleum, and requires a large amount of construction and maintenance costs for exhaust gas treatment.

【0004】そこで、本発明は上記事情に鑑みてなされ
たもので、臭気等排ガス処理が容易で設置場所の制約条
件が低く装置構成を簡単にすることで、建設費や維持費
を安くすることができる無機性廃棄物を原料にした肥料
の製造方法及びその装置を提供することを課題とする。
Accordingly, the present invention has been made in view of the above circumstances, and is intended to reduce construction costs and maintenance costs by simplifying exhaust gas treatment such as odor and the like, and reducing the installation conditions with low restrictions on the installation location. It is an object of the present invention to provide a method and an apparatus for producing fertilizer using inorganic waste as a raw material.

【0005】[0005]

【課題を解決するための手段】本発明は上記の如き課題
を解決するために開発したものであって、ケイソウ土汚
泥の食品製造に由来する無機性廃棄物に水の存在下で酸
化カルシウム(CaO)を添加混合して所定時間反応さ
せる反応工程と、反応後の無機性廃棄物を所定時間放置
して熟成を行なう熟成工程とからなる無機性廃棄物を原
料にした肥料の製造方法において、前記無機性廃棄物10
00に対して酸化カルシウムを1〜60の比率で添加混合し
かつ放置期間中少なくとも1回以上切返して熟成する方
法からなり、該製法により得られる無機性廃棄物を原料
にした肥料の分析値(百分率)が水分23.7、窒素全
量(N)0.58、りん酸全量(P2 5 )0.80、
加里全量(K2 O)1.25、アルカリ分17.0、石
灰全量(CaO)15.5、苦土全量(MgO)0.8
5、SiO2 27.50になること、を特徴とする特殊
肥料製造方法の提供にある。また本発明は、ケイソウ土
汚泥の食品製造に由来する無機性廃棄物を一時貯溜する
と共に定量的に供給する供給機を有してなる原料貯留庫
と、酸化カルシウムを一時貯留すると共に前記供給機の
供給量に対応して酸化カルシウムを定量的に供給する酸
化カルシウム供給機と、前記無機性廃棄物及び酸化カル
シウムを受け入れて水の存在下で混合反応させる攪拌反
応槽と、該攪拌反応槽から排出した反応後の無機性廃棄
物を所定時間放置するヤード及び切返し機を有する熟成
部とからなり、前記無機性廃棄物を収集車に集めてスト
ックヤードまで運搬して直ちにコンベアーにて前記原料
貯留庫のホッパーに投入して貯留しかつホッパーの下部
にある供給機にて無機性廃棄物を一定量攪拌反応槽の原
料受入ホッパーに供給し、一方前記酸化カルシウム供給
機のホッパーにコンテナーに酸化カルシウムを投入して
定量供給機にて無機性廃棄物の供給量に合せて設定した
比率で酸化カルシウムを原料受入ホッパーに供給し、更
に前記原料受入ホッパーの下部にある原料投入装置にて
タンク内に前記原料を平均的に投入しかつ該投入過程で
必要に応じて水圧ポンプを作動させて散水装置にて原料
に水を散布して2基の攪拌機にて原料を7分から15分
ほど攪拌滞留させて脱臭と殺菌をすると共に熟成させて
肥料を製造することを特徴とする無機性廃棄物を原料に
した肥料製造装置の提供にある。
DISCLOSURE OF THE INVENTION The present invention has been developed to solve the above-mentioned problems, and it is an object of the present invention to provide an inorganic waste derived from the production of diatomaceous earth sludge as calcium oxide in the presence of water. A reaction step of adding and mixing CaO) and reacting for a predetermined time; and a fermentation method using an inorganic waste as a raw material, the method comprising: The inorganic waste 10
A method of adding and mixing calcium oxide at a ratio of 1 to 60 with respect to 00, and turning over and ripening at least once during the standing period, and analyzing the fertilizer using the inorganic waste obtained by the production method as a raw material ( %) Water 23.7, total nitrogen (N) 0.58, total phosphoric acid (P 2 O 5 ) 0.80,
Kali total amount (K 2 O) 1.25, alkali content 17.0, lime total amount (CaO) 15.5, magnesite total amount (MgO) 0.8
It is another object of the present invention to provide a method for producing a special fertilizer, which is characterized in that the SiO 2 becomes 27.50. The present invention also provides a raw material storage having a supply device for temporarily storing and quantitatively supplying inorganic waste derived from food production of diatomaceous earth sludge, and a supply device for temporarily storing calcium oxide and the supply device. A calcium oxide feeder that quantitatively supplies calcium oxide in accordance with the supply amount of the above, a stirring reaction tank that receives the inorganic waste and calcium oxide and performs a mixing reaction in the presence of water, A yard for leaving the discharged inorganic waste after the reaction for a predetermined time and a maturing unit having a turning machine. The inorganic waste is collected in a collection vehicle, transported to a stock yard, and immediately stored on a conveyor. A certain amount of inorganic waste is supplied to a raw material receiving hopper of a stirring reaction tank by a feeder at a lower portion of the hopper, and stored in the storage hopper. Calcium oxide is charged into a container in a hopper of a feeder, and calcium oxide is supplied to a raw material receiving hopper at a ratio set in accordance with a supply amount of the inorganic waste by a quantitative feeder, and further, a lower portion of the raw material receiving hopper. In the raw material charging device, the raw materials are averagely charged into a tank, and in the charging process, a water pressure pump is operated as necessary to spray water on the raw materials with a water sprinkler and two stirrers. It is an object of the present invention to provide a fertilizer manufacturing apparatus using inorganic waste as a raw material, wherein a raw material is stirred and retained for about 7 to 15 minutes to perform deodorization and sterilization, and aged to produce a fertilizer.

【0007】[0007]

【作用】上記構成になる無機性廃棄物を原料にした肥料
の製造方法は、その反応機構が不明確であるが酸化カル
シウム(CaO)は、無機性廃棄物中に含有する水と激
しく反応して水酸化カルシウム(Ca(OH)2 )とな
り、この際発熱し同時に酸化カルシウムは二酸化炭素と
結びついて重炭酸カルシウム(Ca(HCO3 2 )と
なり、PH11以上にあげて大腸菌その他有害菌を死滅さ
せ、更に反応して炭酸カルシウムとなる。この酸化カル
シウムは、同時に無機性廃棄物に付着している有機成分
に由来するメチルメルカプタン、カルボン酸化合物、蛋
白質、イオウ化合物に反応して、メルカプチド((CH
3 S)2 Ca)、カルボン酸カルシウム((R−COO
H)2 Ca)、アミノ酸カルシウム塩(R・NH2 ・C
OOH2 )Ca)、硫化カルシウム(CaS)となり、
これらカルシウム化合物は難溶性物質でありその臭気成
分が除去されることになる。
In the method for producing fertilizer using inorganic waste having the above constitution as a raw material, the reaction mechanism is unclear, but calcium oxide (CaO) reacts violently with water contained in the inorganic waste. Then, it becomes calcium hydroxide (Ca (OH) 2 ). At this time, it generates heat and at the same time, calcium oxide is combined with carbon dioxide to become calcium bicarbonate (Ca (HCO 3 ) 2 ). And further react to form calcium carbonate. This calcium oxide simultaneously reacts with methyl mercaptan, carboxylic acid compounds, proteins, and sulfur compounds derived from organic components attached to the inorganic waste to form mercaptides ((CH
3 S) 2 Ca), calcium carboxylate ((R-COO
H) 2 Ca), calcium salt of amino acid (R-NH 2 -C)
OOH 2 ) Ca), calcium sulfide (CaS)
These calcium compounds are hardly soluble substances, and their odor components are removed.

【0008】同時に、これら複雑な反応過程で発生期の
酸素が発生して、アンモニアを分解して分子状態の窒素
ガスにしたり、硫化水素から単体イオウを遊離したりす
る。また、CaOから造成されるCa(OH)2 、Ca
(HCO3 2 、CaCO3の微粒子の微孔中に臭気成
分が吸着されることもあり臭気の拡散が防がれる。
At the same time, nascent oxygen is generated in these complicated reaction processes, decomposing ammonia into nitrogen gas in a molecular state, and liberating simple sulfur from hydrogen sulfide. Also, Ca (OH) 2 , Ca formed from CaO
The odor component may be adsorbed in the fine pores of the (HCO 3 ) 2 and CaCO 3 fine particles, thereby preventing odor diffusion.

【0009】そして、上記反応工程後の無機性廃棄物を
所定時間放置して1回以上の切り返し作業を行なうこと
により、上記反応が完結し更に新たに無機性廃棄物に付
着している有機成分の好気性発酵が進み低分子化が図れ
肥料化が進む。
Then, the inorganic waste after the above-mentioned reaction step is left for a predetermined period of time to perform one or more switching operations, whereby the above-mentioned reaction is completed and the organic component newly adhering to the inorganic waste is further removed. The aerobic fermentation progresses, the molecular weight is reduced, and the use of fertilizer is advanced.

【0010】また、反応工程と熟成工程との間に乾燥工
程があると、酸化カルシウム反応処理後の無機性廃棄物
に多量に含有している水分を除去できることになり、ボ
リュームが減少して熟成工程での処理を容易にする。
If there is a drying step between the reaction step and the aging step, a large amount of water contained in the inorganic waste after the calcium oxide reaction treatment can be removed, and the volume decreases and the aging step is performed. Facilitates processing in the process.

【0011】また、無機性廃棄物1000に対して酸化カル
シウムが1より少なければ、その効果は期待できず60よ
り多ければ酸化カルシウムが過剰となって弊害が発生す
る。
If the amount of calcium oxide is less than 1 with respect to the inorganic waste 1000, the effect cannot be expected. If the amount is more than 60, the amount of calcium oxide becomes excessive and adverse effects occur.

【0012】[0012]

【実施例】以下、本発明の実施例を添付図面に基づいて
詳述する。図1は本発明の無機性廃棄物を原料にした肥
料製造装置のフローシート図であり、この肥料製造装置
1は、ケイソウ土汚泥の食品製造に由来する無機性廃棄
物2を一時貯溜すると共に定量的に供給する供給機3を
有してなる原料貯留庫4と、酸化カルシウム(CaO)
5を一時貯留すると共に供給機3の供給量に対応して酸
化カルシウム5を定量的に供給する酸化カルシウム供給
機6と、無機性廃棄物2及び酸化カルシウム5を受け入
れて水の存在下で混合反応させる攪拌反応槽7と、この
攪拌反応槽7から排出した反応後の無機性廃棄物2Aを
所定時間放置するヤード8及び切返し機9を有する熟成
部10とからなる。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Embodiments of the present invention will be described below in detail with reference to the accompanying drawings. FIG. 1 is a flow sheet diagram of a fertilizer production apparatus using the inorganic waste of the present invention as a raw material. This fertilizer production apparatus 1 temporarily stores inorganic waste 2 derived from diatomaceous earth sludge food production, and A raw material storage 4 having a feeder 3 for supplying quantitatively, calcium oxide (CaO)
Calcium oxide supply device 6 for temporarily storing calcium oxide 5 and quantitatively supplying calcium oxide 5 in accordance with the supply amount of supply device 3, and receives inorganic waste 2 and calcium oxide 5 and mixes them in the presence of water It comprises a stirring reaction tank 7 for reacting, and a ripening section 10 having a yard 8 and a turning machine 9 in which the reacted inorganic waste 2A discharged from the stirring reaction tank 7 is left for a predetermined time.

【0013】前記無機性廃棄物2は、食品製造の過程で
出るものであるから当然に有機成分が付着しており、そ
の種類は例示のものにのみ限定されず例えば活性炭、貝
化石などがあるが、酸化カルシウム5を添加混合するこ
とにより各種反応を起こし得るものでなければならな
い。
Since the inorganic waste 2 is produced in the course of food production, it naturally has an organic component attached thereto. The type of the inorganic waste 2 is not limited to those exemplified, but includes, for example, activated carbon and shell fossils. Must be capable of causing various reactions by adding and mixing calcium oxide 5.

【0014】また、これら無機性廃棄物2に対する酸化
カルシウム5の添加率は、基本的にはテスト等を行なっ
て最終的に決定する必要がある。しかし、例示した無機
性廃棄物2に対する酸化カルシウム5の添加量の1例を
示すと次のとおりである。 ケイソウ土汚泥 水分70重量%(±5%)のもの
1tに対して酸化カルシウムを30Kg添加する。 炭酸カルシウムケーキ 水分35〜40重量%のもの
1tに対して酸化カルシウムを30Kg添加する。 ゼオライトケーキ 水分70重量%(±5%)のも
の1tに対して酸化カルシウムを30Kg添加する。 活性炭及び貝化石ケーキはゼオライトケーキに準ず
る。
The rate of addition of calcium oxide 5 to these inorganic wastes 2 must be finally determined by conducting tests and the like. However, one example of the amount of the calcium oxide 5 added to the exemplified inorganic waste 2 is as follows. Diatomaceous earth sludge 30 kg of calcium oxide is added to 1 ton having a water content of 70% by weight (± 5%). Calcium carbonate cake 30 kg of calcium oxide is added to 1 ton having a water content of 35 to 40% by weight. Zeolite cake 30 kg of calcium oxide is added to 1 ton having a water content of 70% by weight (± 5%). Activated carbon and shell fossil cakes conform to zeolite cakes.

【0015】前記原料貯留庫4は、ホッパー20の下部に
供給機3を取り付けることで構成される。ホッパー20
は、無機性廃棄物2を一時貯留して供給機3に無機性廃
棄物2を安定して送り、供給機3の供給量に誤差が生じ
ないようにするためのものである。供給機3はスクリュ
ータイプのものが使用されるが、特にこれに限定されず
無機性廃棄物2を可変して定量的に供給することができ
るものであればいかなるものであっても良い。この実施
例では、スクリューの回転速度を変えることにより無機
性廃棄物2の供給量を可変するものである。
The raw material storage 4 is constructed by mounting the feeder 3 below the hopper 20. Hopper 20
Is for temporarily storing the inorganic waste 2 and stably sending the inorganic waste 2 to the feeder 3 so as to prevent an error in the supply amount of the feeder 3. The feeder 3 is of a screw type, but is not particularly limited thereto, and may be of any type as long as it can supply the inorganic waste 2 variably and quantitatively. In this embodiment, the supply amount of the inorganic waste 2 is varied by changing the rotation speed of the screw.

【0016】前記酸化カルシウム供給機6は、ホッパー
30の下部に定量供給機31を取り付けることで構成され
る。ホッパー30はほぼ密封され、更に充分な防湿対策を
施されたものである。更に、定量供給機31はスクリュー
タイプやテーブルタイプのものが使用されるが、これに
限定されず無機性廃棄物2の供給量に合せて設定した比
率で酸化カルシウム5を可変して定量的に供給すること
ができるものであればいかなるものであっても良い。
The calcium oxide supply device 6 includes a hopper
The fixed quantity feeder 31 is attached to the lower part of 30. The hopper 30 is substantially sealed, and has been subjected to sufficient moisture-proof measures. Further, a screw-type or table-type one is used for the fixed-quantity feeder 31. However, the present invention is not limited to this, and the calcium oxide 5 is varied at a ratio set according to the supply amount of the inorganic waste 2 to quantitatively change the quantity. Anything that can be supplied may be used.

【0017】前記攪拌反応槽7は、原料貯留庫4から供
給された無機性廃棄物2及び酸化カルシウム供給機6か
ら供給された酸化カルシウム5を、一旦受け入れる原料
受入ホッパー40を有している。この原料受入ホッパー40
下部には原料投入装置41が設けられ、この原料投入装置
41には相互に逆方向のスクリュー42、43が同一の軸44に
固定され、この軸44を同一方向に回転することで左右に
無機性廃棄物2及び酸化カルシウム5からなる原料が運
搬され、供給穴(図示せず)からタンク45内に平均的に
投入されるものである。このタンク45は、シャフト46に
4枚羽根の攪拌翼47を複数設けた攪拌機48を2基設け、
更に散水装置49を2基設けてなる。これら2基の攪拌機
48は、その攪拌翼47が千鳥状になるようにタンク45内に
設けられており、更に散水装置49はパイプ50にノズル51
を複数もうけてなる。なお、2基の攪拌機48は可変減速
機付のモータ(図示せず)により回転され、更に散水装
置49は給水源52から受水槽53にて受けた水を水圧ポンプ
54により増圧してなるものである。従って、原料投入装
置41によりタンク45内に平均的に投入された原料はタン
ク45内で所定時間、例えば7〜15分ほど滞留して必要に
応じて散水装置49により水を散布され、更に2基の攪拌
機48により混合させその過程で種々の化学反応が行なわ
れて殺菌消臭等がなされ無害化される。
The agitation reactor 7 has a raw material receiving hopper 40 for temporarily receiving the inorganic waste 2 supplied from the raw material storage 4 and the calcium oxide 5 supplied from the calcium oxide supply device 6. This raw material receiving hopper 40
A raw material input device 41 is provided at a lower portion.
In 41, screws 42 and 43 in opposite directions are fixed to the same shaft 44, and by rotating this shaft 44 in the same direction, the raw material composed of the inorganic waste 2 and the calcium oxide 5 is transported to the left and right, It is supplied into the tank 45 from a supply hole (not shown) on average. This tank 45 is provided with two stirrers 48 in which a plurality of stirring blades 47 of four blades are provided on a shaft 46,
Further, two watering devices 49 are provided. These two stirrers
48 is provided in the tank 45 so that the stirring blades 47 are staggered.
Have more than one. The two agitators 48 are rotated by a motor (not shown) equipped with a variable speed reducer, and a watering device 49 further receives water received in a water receiving tank 53 from a water supply source 52 by a hydraulic pump.
The pressure is increased by 54. Therefore, the raw material that has been averagely charged into the tank 45 by the raw material charging device 41 stays in the tank 45 for a predetermined time, for example, about 7 to 15 minutes, and is sprayed with water by the watering device 49 as necessary. Mixing is performed by the basic stirrer 48, and various chemical reactions are performed in the process to sterilize and deodorize, thereby rendering the mixture harmless.

【0018】前記攪拌反応槽7において混合反応された
あとの無機性廃棄物2Aは、攪拌反応槽7下部に設けた
ゲート(図示せず)からコンベアー60に落下して、この
コンベアー60にて前記熟成部10に送られる。
The inorganic waste 2A that has undergone the mixing reaction in the stirring reaction tank 7 falls from a gate (not shown) provided in the lower part of the stirring reaction tank 7 to a conveyor 60, and the conveyor 60 It is sent to the aging section 10.

【0019】この熟成部10はヤード8に所定時間、例え
ば2日〜2週間ぐらい反応後の無機性廃棄物2Aを放置
しておき付着している有機成分を発酵させるもので、そ
の間、少なくとも切返し機9により1回以上の切り返し
を行なうものである。ヤード8はコンクリート製であ
り、屋外設置の場合や風雨による影響を防ぐため屋根が
設けられる。切返し機9は、ヤード8上に放置した反応
後の原料を切り返すことができるものであればその型は
問わない。
The aging section 10 is a section for leaving the inorganic waste 2A after the reaction in the yard 8 for a predetermined time, for example, about 2 days to 2 weeks, and fermenting the attached organic components. The machine 9 performs one or more switching operations. The yard 8 is made of concrete, and is provided with a roof for outdoor installation and to prevent the influence of wind and rain. The type of the turning machine 9 is not limited as long as it can turn the reacted raw material left on the yard 8.

【0020】次に上記構成になる特殊肥料製造装置1に
より、その製造方法を説明する。食品製造に由来する無
機性廃棄物2を収集車にて集めてストックヤード等まで
運搬して置き、直ちにコンベアー等の運搬手段にて原料
貯留庫4のホッパー20に投入し貯留する。ホッパー20の
下部ある供給機3にて無機性廃棄物2を一定量攪拌反応
槽7の原料受入ホッパー40に供給する。一方、酸化カル
シウム供給機6のホッパー30にコンテナー等に入った酸
化カルシウム5を投入し、定量供給機31にて無機性廃棄
物2の供給量に合せて設定した比率で酸化カルシウム5
を上記原料受入ホッパー40に供給する。更に、原料受入
ホッパー40の下部にある原料投入装置41にてタンク45内
に上記原料を平均的に投入する。この投入過程で必要に
応じて水圧ポンプ54を作動させて散水装置49にて原料に
水を散布し、2基の攪拌機48にて原料を7分から15分ほ
ど攪拌滞留させることで化学反応させ脱臭、殺菌する。
このあとタンク45から反応後の無機性廃棄物2Aを取り
出し、コンベアー60にてヤード8に運搬し、切返し機9
によりならし、かつ所定のインターバルで原料を切返し
て熟成、すなわち発酵させて発酵肥料ができる。
Next, a method of manufacturing the special fertilizer manufacturing apparatus 1 having the above configuration will be described. The inorganic waste 2 derived from food production is collected by a collection vehicle, transported to a stock yard or the like, placed therein, and immediately put into the hopper 20 of the raw material storage 4 by a transporting means such as a conveyor and stored. A certain amount of the inorganic waste 2 is supplied to the raw material receiving hopper 40 of the stirring reaction tank 7 by the supply device 3 provided below the hopper 20. On the other hand, the calcium oxide 5 contained in a container or the like is charged into the hopper 30 of the calcium oxide feeder 6 and the calcium oxide 5 is supplied at a ratio set according to the supply amount of the inorganic waste 2 by the quantitative feeder 31.
Is supplied to the raw material receiving hopper 40. Furthermore, the above-mentioned raw material is charged into the tank 45 by the raw material charging device 41 below the raw material receiving hopper 40 on average. In this charging process, the hydraulic pump 54 is operated as necessary to spray water on the raw material with the water spray device 49, and the raw material is stirred and retained for 7 to 15 minutes by two stirrers 48 to chemically react and deodorize. ,Sterilize.
After that, the inorganic waste 2A after the reaction is taken out of the tank 45, transported to the yard 8 by the conveyor 60, and
The raw material is turned over at predetermined intervals, and the raw material is turned over and matured, that is, fermented to produce fermented fertilizer.

【0021】図2は無機性廃棄物を原料にした肥料の乾
燥装置のフローシート図であり、この乾燥機70は、主に
反応後の無機性廃棄物2Aの水分値が高い場合に攪拌反
応槽7と熟成部10との間に設けられるものである。この
乾燥装置70は、コンベアー60にて運搬された反応後の無
機性廃棄物2Aを投入タンク71にて受け、この投入タン
ク71の下部に設けられた定量供給機72にてロータリード
ライヤー本体73の一端側に投入され、ロータリードライ
ヤー本体73の回転により無機性廃棄物2Aは徐々に他端
側に移動し、この移動過程で熱発生炉74からの熱風によ
り乾燥される。一方、熱風は温度を下げつつロータリー
ドライヤー本体73から排出されて排ガス処理装置75にて
処理され大気中に放出される。乾燥した無機性廃棄物2
Aは、ロータリードライヤー本体73から排出されコンベ
アー76により製品ホッパー77に投入されて必要に応じて
ホッパーから運搬車等に移して特殊な肥料として使用さ
れるが、上記のようにヤード8にコンベアー76にて運ば
れて所定時間熟成したあとは無機性廃棄物を原料とした
肥料として使用されることもある。
FIG. 2 is a flow sheet diagram of an apparatus for drying a fertilizer using inorganic waste as a raw material. This dryer 70 is mainly used when the water content of the inorganic waste 2A after the reaction is high. It is provided between the tank 7 and the aging section 10. The drying device 70 receives the reacted inorganic waste 2A conveyed by the conveyor 60 in the input tank 71, and feeds the rotary dryer body 73 by the quantitative feeder 72 provided below the input tank 71. It is thrown into one end side, and the inorganic waste 2A is gradually moved to the other end side by the rotation of the rotary dryer main body 73, and is dried by hot air from the heat generating furnace 74 in this moving process. On the other hand, the hot air is discharged from the rotary dryer main body 73 while decreasing the temperature, is processed by the exhaust gas processing device 75, and is discharged into the atmosphere. Dry inorganic waste 2
A is discharged from the rotary dryer main body 73, is charged into the product hopper 77 by the conveyor 76, and is transferred from the hopper to a transport vehicle or the like as necessary, and is used as a special fertilizer. After being aged for a predetermined period of time, it may be used as a fertilizer using inorganic waste as a raw material.

【0022】なお、図1に示す無機性廃棄物を原料とし
た肥料の製造装置にてケイソウ土汚泥から製造された肥
料の分析値は表1のとおりである。
The analytical values of the fertilizer produced from diatomaceous earth sludge by the fertilizer production apparatus using inorganic waste as a raw material shown in FIG. 1 are as shown in Table 1.

【0023】[0023]

【表1】 また、図1に示す肥料製造装置の設置場所から5m離れ
た位置における臭気濃度の測定値は、表2の数値を下ま
わった(なお、濃度測定方法は悪臭防止法に準ず
る。)。
[Table 1] Further, the measured value of the odor concentration at a position 5 m away from the installation location of the fertilizer production apparatus shown in FIG. 1 was lower than the numerical value in Table 2 (the concentration measurement method conforms to the method for preventing bad odor).

【0024】[0024]

【表2】 [Table 2]

【0025】[0025]

【発明の効果】以上詳述したように、本発明の無機性廃
棄物を原料にした肥料製造方法によれば、大規模で複雑
なプロセスを必要としないで、夾雑物、脂質、微生物等
による腐敗臭や凝固性がある食品工場から出るケイソウ
土汚泥、炭酸カルシウムケーキ、ゼオライトケーキ等の
無機性廃棄物を短時間で多量処理し特に付着している有
機成分の脱臭、殺菌を行ない、更に有機成分の凝固性を
破壊して脱水し易くして無機性廃棄物を原料にした肥料
としての利用も可能にする。
As described in detail above, according to the method for producing fertilizer using inorganic wastes of the present invention as a raw material, a large-scale and complicated process is not required, and impurities, lipids, microorganisms and the like are not required. A large amount of inorganic waste such as diatomaceous earth sludge, calcium carbonate cake, and zeolite cake from a food factory with putrefactive odor and coagulation is treated in large quantities in a short time to deodorize and sterilize especially attached organic components. It destroys the coagulability of the components, facilitates dehydration, and enables use as a fertilizer using inorganic waste as a raw material.

【0026】また、反応工程と熟成工程との間に乾燥工
程があると、酸化カルシウム反応処理後の無機性廃棄物
に多量に含有している水分を除去できることになり、ボ
リュームが減少して熟成工程での処理を容易にする。従
って、熟成工程のスペースを狭くでき、更に水分値が低
いから運搬が楽でそのまま肥料としても利用することが
できる。
Further, if there is a drying step between the reaction step and the aging step, a large amount of water contained in the inorganic waste after the calcium oxide reaction treatment can be removed, and the volume decreases and the aging step is performed. Facilitates processing in the process. Therefore, the space for the aging step can be narrowed, and since the water content is low, it is easy to transport and can be used as it is as a fertilizer.

【0027】また、無機性廃棄物1000に対して酸化カル
シウムが1より少なければ、その効果は期待できず60よ
り多ければ酸化カルシウムが過剰となって弊害が発生す
る。従って、わずかな酸化カルシウムの添加により無機
性廃棄物の無害化、無臭化が図れるので無機性廃棄物を
原料にした肥料としても利用できる。
If the amount of calcium oxide is less than 1 with respect to the inorganic waste 1000, the effect cannot be expected. If the amount is more than 60, the amount of calcium oxide becomes excessive and adverse effects occur. Therefore, inorganic waste can be rendered harmless and odorless by adding a small amount of calcium oxide, and can be used as a fertilizer using inorganic waste as a raw material.

【0028】また、本発明の肥料製造装置によれば上記
方法を効率よく実現でき酸化カルシウムの使用であるた
めに尿酸等によるサビの発生を防ぎ、しかも耐久性が高
められる。更に、乾燥装置があると上記方法を効率よく
実現できる。
Further, according to the fertilizer manufacturing apparatus of the present invention, the above-mentioned method can be efficiently realized, and the use of calcium oxide prevents the generation of rust due to uric acid and the like, and further enhances the durability. Furthermore, the presence of a drying device enables the above method to be efficiently realized.

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明の特殊肥料製造装置のフローシート図。FIG. 1 is a flow sheet diagram of a special fertilizer production device of the present invention.

【図2】本発明の特殊肥料製造装置に付帯する乾燥装置
のフローシート図。
FIG. 2 is a flow sheet diagram of a drying device attached to the special fertilizer production device of the present invention.

【符号の説明】[Explanation of symbols]

1 特殊肥料製造装置 2 無機性廃棄物 2A 反応後の無機性廃棄物 3 供給機 4 原料貯留庫 5 酸化カルシウ
ム 6 酸化カルシウム供給機 7 攪拌反応槽 8 ヤード 9 切返し機 10 熟成部 70 乾燥機
DESCRIPTION OF SYMBOLS 1 Special fertilizer manufacturing equipment 2 Inorganic waste 2A Inorganic waste after reaction 3 Feeder 4 Raw material storage 5 Calcium oxide 6 Calcium oxide feeder 7 Stirring reaction tank 8 Yard 9 Turning machine 10 Aging unit 70 Drying machine

───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 昭53−2273(JP,A) 特開 昭53−48877(JP,A) 特開 昭52−26754(JP,A) 特開 平5−246789(JP,A) 特開 昭51−69066(JP,A) 特開 昭54−111469(JP,A) (58)調査した分野(Int.Cl.7,DB名) C05F 1/00 - 17/00 ──────────────────────────────────────────────────続 き Continuation of the front page (56) References JP-A-53-2273 (JP, A) JP-A-53-48877 (JP, A) JP-A-52-26754 (JP, A) 246789 (JP, A) JP-A-51-69066 (JP, A) JP-A-54-111469 (JP, A) (58) Fields investigated (Int. Cl. 7 , DB name) C05F 1/00-17 / 00

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 ケイソウ土汚泥の食品製造に由来する無
機性廃棄物に水の存在下で酸化カルシウム(CaO)を
添加混合して所定時間反応させる反応工程と、反応後の
無機性廃棄物を所定時間放置して熟成を行なう熟成工程
とからなる無機性廃棄物を原料にした肥料の製造方法に
おいて、前記無機性廃棄物1000に対して酸化カルシウム
を1〜60の比率で添加混合しかつ放置期間中少なくとも
1回以上切返して熟成する方法からなり、該製法により
得られる無機性廃棄物を原料にした肥料の分析値(百分
率)が水分23.7、窒素全量(N)0.58、りん酸
全量(P2 5 )0.80、加里全量(K2 O)1.2
5、アルカリ分17.0、石灰全量(CaO)15.
5、苦土全量(MgO)0.85、SiO2 27.50
になることを特徴とする無機性廃棄物を原料にした肥料
の製造方法。
1. A reaction step in which calcium oxide (CaO) is added to and mixed with inorganic waste derived from diatomaceous earth sludge food production in the presence of water and reacted for a predetermined time; A fertilizer production method using an inorganic waste as a raw material, which comprises a maturing step of allowing the mixture to stand for a predetermined time, and adding and mixing calcium oxide at a ratio of 1 to 60 with respect to the inorganic waste 1000, and allowing the mixture to stand. It is a method of turning over and ripening at least once during the period, and the analysis value (percentage) of the fertilizer using the inorganic waste obtained by the production method as a raw material is as follows: moisture 23.7, total nitrogen (N) 0.58, phosphorus Total acid (P 2 O 5 ) 0.80, total potassium (K 2 O) 1.2
5. Alkali content 17.0, total amount of lime (CaO)
5, total amount of magnesia (MgO) 0.85, SiO 2 27.50
A method for producing a fertilizer using inorganic waste as a raw material.
【請求項2】 ケイソウ土汚泥の食品製造に由来する無
機性廃棄物を一時貯溜すると共に定量的に供給する供給
機を有してなる原料貯留庫と、酸化カルシウムを一時貯
留すると共に前記供給機の供給量に対応して酸化カルシ
ウムを定量的に供給する酸化カルシウム供給機と、前記
無機性廃棄物及び酸化カルシウムを受け入れて水の存在
下で混合反応させる攪拌反応槽と、該攪拌反応槽から排
出した反応後の無機性廃棄物を所定時間放置するヤード
及び切返し機を有する熟成部とからなり、前記無機性廃
棄物を収集車に集めてストックヤードまで運搬して直ち
にコンベアーにて前記原料貯留庫のホッパーに投入して
貯留しかつホッパーの下部にある供給機にて無機性廃棄
物を一定量攪拌反応槽の原料受入ホッパーに供給し、一
方前記酸化カルシウム供給機のホッパーにコンテナーに
酸化カルシウムを投入して定量供給機にて無機性廃棄物
の供給量に合せて設定した比率で酸化カルシウムを原料
受入ホッパーに供給し、更に前記原料受入ホッパーの下
部にある原料投入装置にてタンク内に前記原料を平均的
に投入しかつ該投入過程で必要に応じて水圧ポンプを作
動させて散水装置にて原料に水を散布して2基の攪拌機
にて原料を7分から15分ほど攪拌滞留させて脱臭と殺
菌をすると共に熟成させて肥料を製造することを特徴と
する無機性廃棄物を原料にした肥料製造装置。
2. A raw material storage having a supply device for temporarily storing and quantitatively supplying inorganic waste derived from food production of diatomaceous earth sludge, and a supply device for temporarily storing calcium oxide and supplying the same. A calcium oxide feeder that quantitatively supplies calcium oxide in accordance with the supply amount of the above, a stirring reaction tank that receives the inorganic waste and calcium oxide and performs a mixing reaction in the presence of water, A yard for leaving the discharged inorganic waste after the reaction for a predetermined time and a maturing unit having a turning machine. The inorganic waste is collected in a collection vehicle, transported to a stock yard, and immediately stored on a conveyor. A certain amount of inorganic waste is supplied to a raw material receiving hopper of a stirring reaction tank by a feeder at the lower part of the hopper. Calcium oxide is charged into a container in a hopper of a feeder, and calcium oxide is supplied to a raw material receiving hopper at a ratio set in accordance with a supply amount of the inorganic waste by a quantitative feeder, and further, a lower portion of the raw material receiving hopper. In the raw material charging device, the raw materials are averagely charged into a tank, and in the charging process, a water pressure pump is operated as necessary to spray water on the raw materials with a water sprinkler and two stirrers. A fertilizer manufacturing apparatus using inorganic waste as a raw material, wherein the raw material is stirred and retained for about 7 to 15 minutes to perform deodorization and sterilization, and aged to produce a fertilizer.
JP6163908A 1994-07-15 1994-07-15 Method and apparatus for producing fertilizer from inorganic waste Expired - Fee Related JP3025777B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6163908A JP3025777B2 (en) 1994-07-15 1994-07-15 Method and apparatus for producing fertilizer from inorganic waste

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6163908A JP3025777B2 (en) 1994-07-15 1994-07-15 Method and apparatus for producing fertilizer from inorganic waste

Publications (2)

Publication Number Publication Date
JPH0826870A JPH0826870A (en) 1996-01-30
JP3025777B2 true JP3025777B2 (en) 2000-03-27

Family

ID=15783116

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6163908A Expired - Fee Related JP3025777B2 (en) 1994-07-15 1994-07-15 Method and apparatus for producing fertilizer from inorganic waste

Country Status (1)

Country Link
JP (1) JP3025777B2 (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63262091A (en) * 1987-04-20 1988-10-28 Sanyo Electric Co Ltd Controlling method for pump
JP4502196B2 (en) * 2003-10-29 2010-07-14 有限会社オカムラ Mixed sludge fertilizer production equipment and production plant
JP2007175556A (en) * 2004-06-17 2007-07-12 One Uiru:Kk Method for producing novel material with highly functional capability from waste diatomaceous earth, and novel material with highly functional capability by the waste diatomaceous earth
CN111659693A (en) * 2019-03-07 2020-09-15 东莞市金铭信息技术咨询有限公司 Non-combustible processing system

Also Published As

Publication number Publication date
JPH0826870A (en) 1996-01-30

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