JP2003112989A - Method for manufacturing fertilizer - Google Patents

Method for manufacturing fertilizer

Info

Publication number
JP2003112989A
JP2003112989A JP2001305518A JP2001305518A JP2003112989A JP 2003112989 A JP2003112989 A JP 2003112989A JP 2001305518 A JP2001305518 A JP 2001305518A JP 2001305518 A JP2001305518 A JP 2001305518A JP 2003112989 A JP2003112989 A JP 2003112989A
Authority
JP
Japan
Prior art keywords
component
incineration ash
fertilizer
molten slag
sludge incineration
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
JP2001305518A
Other languages
Japanese (ja)
Inventor
Yoshihiro Iwai
良博 岩井
Takashi Komatsu
貴司 小松
Sadafumi Takagi
禎史 高木
Tetsuharu Sadatsuka
徹治 定塚
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.)
Sanki Engineering Co Ltd
Original Assignee
Sanki Engineering Co Ltd
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 Sanki Engineering Co Ltd filed Critical Sanki Engineering Co Ltd
Priority to JP2001305518A priority Critical patent/JP2003112989A/en
Publication of JP2003112989A publication Critical patent/JP2003112989A/en
Pending legal-status Critical Current

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

Abstract

PROBLEM TO BE SOLVED: To effectively utilize calcareous wastes and sludge incineration ash. SOLUTION: The calcareous wastes 4, such as shells (a) of scallops, shells (b) of oysters and eggshells (c) of eggs, sludge incineration ash 1, coke 2, magnesium oxide 3, and potassium oxide 5 are heated in a fusion furnace 8 to allow molten metals 24 and molten slag 25 to coexist in a two-liquid separated state. Further, the molten slag 25 is selectively discharged to a hydropulping chamber 19 where the slag is rapidly cooled. Granular slag 26 which contains the phosphorus component and calcium component and is get rid of metals is recovered. This slag 26 is used as a fertilizer.

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】本発明は食品加工に付随して
発生するカルシウム質廃棄物と下水汚泥の焼却灰を主な
原料に用いた肥料製造方法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 producing a fertilizer using, as a main raw material, calcium-based waste generated by food processing and incineration ash of sewage sludge.

【0002】[0002]

【従来の技術】従来、ホタテガイ、カキの貝類や鶏卵の
加工により発生する貝殻、卵殻などは、ほとんどが最終
処分場に廃棄されている。
2. Description of the Related Art Conventionally, most of scallops, oyster shells, shells and eggshells generated by processing chicken eggs are disposed of at the final disposal site.

【0003】また、下水処理に付随して発生する汚泥
は、脱水を行ない且つ焼却したうえ、最終処分場に廃棄
されている。
[0003] The sludge generated by the sewage treatment is dehydrated and incinerated, and then disposed of at the final disposal site.

【0004】[0004]

【発明が解決しようとする課題】しかしながら、近年、
最終処分場の廃棄物の受け入れが逼迫しており、貝殻、
卵殻、汚泥焼却灰などの更なる減容(体積を減らす処
置)が望まれている。
However, in recent years,
The acceptance of waste at the final disposal site is tight, shells,
Further volume reduction (volume reduction) of eggshell, sludge incineration ash, etc. is desired.

【0005】本発明は上述した実情に鑑みてなしたもの
で、貝殻、卵殻などのカルシウム質廃棄物及び汚泥焼却
灰の有効利用を図ることを目的としている。
The present invention has been made in view of the above-mentioned circumstances, and an object thereof is to effectively utilize calcium waste such as shells and eggshells and sludge incineration ash.

【0006】[0006]

【発明が解決しようとする課題】上記目的を達成するた
め、本発明の請求項1に記載の肥料製造方法では、カル
シウム質廃棄物、及びリン成分を含んでいる汚泥焼却灰
を還元性雰囲気の溶融炉内で加熱して、溶融金属と溶融
スラグを溶融炉内に二液分離状態で共存させ、当該溶融
スラグを水砕処理によって粒状化させる。
In order to achieve the above object, in the method for producing a fertilizer according to claim 1 of the present invention, the sludge incineration ash containing the calcium waste and the phosphorus component is stored in a reducing atmosphere. The molten metal and molten slag are allowed to coexist in the melting furnace in a two-liquid separated state by heating in the melting furnace, and the molten slag is granulated by water granulation treatment.

【0007】本発明の請求項2に記載の肥料製造方法で
は、カルシウム質廃棄物、リン成分を含んでいる汚泥焼
却灰、及び還元剤を溶融炉内で加熱して、溶融金属と溶
融スラグを溶融炉内に二液分離状態で共存させ、当該溶
融スラグを水砕処理によって粒状化させる。
In the fertilizer manufacturing method according to the second aspect of the present invention, the calcium metal waste, the sludge incineration ash containing the phosphorus component, and the reducing agent are heated in the melting furnace to melt the molten metal and molten slag. The two liquids are made to coexist in the melting furnace and the molten slag is granulated by water granulation.

【0008】本発明の請求項3に記載の肥料製造方法で
は、カルシウム質廃棄物、リン成分を含んでいる汚泥焼
却灰、還元剤、及びマグネシウム成分を溶融炉内で加熱
して、溶融金属と溶融スラグを溶融炉内に二液分離状態
で共存させ、当該溶融スラグを水砕処理によって粒状化
させる。
In the method for producing a fertilizer according to claim 3 of the present invention, calcium waste, sludge incineration ash containing phosphorus component, reducing agent, and magnesium component are heated in a melting furnace to form molten metal. The molten slag is allowed to coexist in the melting furnace in a two-liquid separated state, and the molten slag is granulated by a water granulation process.

【0009】本発明の請求項4に記載の肥料製造方法で
は、カルシウム質廃棄物、リン成分を含んでいる汚泥焼
却灰、還元剤、及びカリウム成分を溶融炉内で加熱し
て、溶融金属と溶融スラグを溶融炉内に二液分離状態で
共存させ、当該溶融スラグを水砕処理によって粒状化さ
せる。
In the method for producing a fertilizer according to claim 4 of the present invention, calcium waste, sludge incineration ash containing a phosphorus component, a reducing agent, and a potassium component are heated in a melting furnace to form a molten metal. The molten slag is allowed to coexist in the melting furnace in a two-liquid separated state, and the molten slag is granulated by a water granulation process.

【0010】本発明の請求項5に記載の肥料製造方法で
は、カルシウム質廃棄物、リン成分を含んでいる汚泥焼
却灰、還元剤、マグネシウム成分、及びカリウム成分を
溶融炉内で加熱して、溶融金属と溶融スラグを溶融炉内
に二液分離状態で共存させ、当該溶融スラグを水砕処理
によって粒状化させる。
In the method for producing a fertilizer according to claim 5 of the present invention, calcium waste, sludge incineration ash containing a phosphorus component, a reducing agent, a magnesium component, and a potassium component are heated in a melting furnace, Molten metal and molten slag coexist in a melting furnace in a two-liquid separated state, and the molten slag is granulated by a water granulation process.

【0011】本発明の請求項6に記載の肥料製造方法で
は、汚泥焼却灰のリン含有量を予め把握しておき、溶融
スラグの水砕処理により得られる粒状体の五酸化二リ
ン、酸化マグネシウム、並びに酸化カルシウムのモル比
率が、1:2乃至4:2乃至4程度となるように、汚泥
焼却灰に対するカルシウム質廃棄物及びマグネシウム成
分の量を定める。
In the method for producing a fertilizer according to claim 6 of the present invention, the phosphorus content of the sludge incineration ash is grasped in advance, and the granular diphosphorus pentoxide and magnesium oxide obtained by the water granulation treatment of the molten slag , And the molar ratio of calcium oxide is about 1: 2 to 4: 2 to 4 about the amount of calcium waste and magnesium component to sludge incineration ash.

【0012】本発明の請求項1乃至請求項5に記載の肥
料製造方法のいずれにおいても、還元性雰囲気に保持さ
れた溶融炉内に、溶融金属と溶融スラグを二液分離状態
で共存させて金属の分離を図ったうえ、水砕処理を溶融
スラグに行なって、リン成分及びカルシウム成分を含ん
だスラグを取り扱い容易な粒状に形成する。
In any of the fertilizer production methods according to the first to fifth aspects of the present invention, molten metal and molten slag are allowed to coexist in a two-liquid separated state in a melting furnace kept in a reducing atmosphere. After separating the metal, the molten slag is subjected to a water granulation process to form a slag containing a phosphorus component and a calcium component into particles that are easy to handle.

【0013】本発明の請求項3、5に記載の肥料製造方
法のいずれにおいても、マグネシウム成分を別途に加え
ることにより、スラグが含むべきマグネシウム成分の増
加を図る。
In any of the fertilizer manufacturing methods according to the third and fifth aspects of the present invention, the magnesium component to be contained in the slag is increased by adding the magnesium component separately.

【0014】本発明の請求項4、5に記載の肥料製造方
法のいずれにおいても、カリウム成分を別途に加えるこ
とにより、スラグが溶融状態となる温度を低下させると
ともに、スラグが含むべきカリウム成分の増加を図る。
In any of the methods for producing a fertilizer according to claims 4 and 5 of the present invention, by separately adding a potassium component, the temperature at which the slag becomes in a molten state is lowered, and at the same time the potassium component of the slag should be contained. Aim to increase.

【0015】本発明の請求項6に記載の肥料製造方法に
おいては、汚泥焼却灰とともに加熱すべきカルシウム質
廃棄物成分及びマグネシウム成分の量を、水砕処理後の
スラグに含まれる五酸化二リン、酸化マグネシウム、並
びに酸化カルシウムのモル比率が、1:2乃至4:2乃
至4程度になるようにして、最適な成分比率のリン肥料
を得る。
In the method for producing a fertilizer according to the sixth aspect of the present invention, the amounts of the calcium-based waste component and the magnesium component to be heated together with the sludge incineration ash are the phosphorus pentoxide contained in the slag after the water granulation treatment. A phosphorus fertilizer having an optimum component ratio is obtained by adjusting the molar ratio of magnesium oxide, magnesium oxide, and calcium oxide to about 1: 2 to 4: 2 to 4.

【0016】[0016]

【発明の実施の形態】以下、本発明の実施の形態を、図
示例とともに説明する。
BEST MODE FOR CARRYING OUT THE INVENTION Embodiments of the present invention will be described below with reference to the drawings.

【0017】図1は本発明の肥料製造方法の実施の形態
の一例を示すもので、この肥料製造方法では、汚泥焼却
灰1、炭素(C)系還元剤としてのコークス2、酸化マ
グネシウム(MgO)3、カルシウム質廃棄物(Ca)
4、酸化カリウム(K2O)5を、肥料の原料としてい
る。
FIG. 1 shows an example of an embodiment of a fertilizer production method of the present invention. In this fertilizer production method, sludge incineration ash 1, coke 2 as a carbon (C) -based reducing agent, magnesium oxide (MgO) is used. ) 3, Calcium waste (Ca)
4. Potassium oxide (K 2 O) 5 is used as a fertilizer raw material.

【0018】カルシウム質廃棄物4は、ホタテガイの貝
殻a、カキの貝殻b、鶏卵の卵殻cなどであり、ホタテ
ガイの貝殻aの場合、重量比で96%のカルシウムを含
んでいる。
The calcium waste 4 is, for example, a scallop shell a, an oyster shell b, an egg shell c, etc. The scallop shell a contains 96% by weight of calcium.

【0019】また、上記の各原料から肥料を製造するた
めに、溶融炉8を用いる。
A melting furnace 8 is used to produce fertilizer from each of the above raw materials.

【0020】溶融炉8は、炭素質ブロックのライニング
9で囲まれた溶融空間を有する炉体10と、溶融空間下
側に位置するようにライニング9に組み込んだ電極11
と、先端部が溶融空間中心に位置するように炉体10上
部に設けた炭素質の電極12とで構成されている。
The melting furnace 8 has a furnace body 10 having a melting space surrounded by a lining 9 of a carbonaceous block, and an electrode 11 incorporated in the lining 9 so as to be located below the melting space.
And a carbonaceous electrode 12 provided on the upper part of the furnace body 10 so that the tip portion is located at the center of the melting space.

【0021】炉体10には、スクリュー式の原料投入機
13を有し且つ炉体10の外部から溶融空間上部に連通
する原料投入口14と、溶融空間上部から排ガス処理設
備の2次燃焼炉(図示せず)に連通するガス排出口15
と、溶融空間の上下方向中間部分から炉体10外部へ連
通するスラグ排出口16と、溶融空間の内底近傍から炉
体10外部へ連通する金属排出口17とが設けられてい
る。
The furnace body 10 has a screw-type raw material charging machine 13 and a raw material charging port 14 communicating from the outside of the furnace body 10 to the upper part of the melting space, and a secondary combustion furnace of the exhaust gas treatment equipment from the upper part of the melting space. Gas outlet 15 communicating with (not shown)
A slag discharge port 16 that communicates with the outside of the furnace body 10 from an intermediate portion in the vertical direction of the melting space, and a metal discharge port 17 that communicates with the outside of the furnace body 10 from the vicinity of the inner bottom of the melting space.

【0022】また、炉体10外部のスラグ排出口16の
下側には、水18を貯留した水砕槽19が設置されてい
る。
Further, below the slag discharge port 16 outside the furnace body 10, a water granulation tank 19 storing water 18 is installed.

【0023】肥料を製造するときには、原料投入機13
により汚泥焼却灰1、コークス2、酸化マグネシウム
3、カルシウム質廃棄物4、及び酸化カリウム5を、原
料投入口14から炉体10の溶融空間へ送給する。
When the fertilizer is manufactured, the raw material feeding machine 13
The sludge incineration ash 1, the coke 2, the magnesium oxide 3, the calcium waste 4, and the potassium oxide 5 are fed from the raw material charging port 14 to the melting space of the furnace body 10.

【0024】更に、両電極11,12に溶融空間への送
給物質を介して電流を通電し、汚泥焼却灰1、酸化マグ
ネシウム3、カルシウム質廃棄物4、及び酸化カリウム
5をジュール熱で加熱して溶融させ、コークス2の主成
分である炭素により溶融空間を還元性雰囲気に保つ。
Further, an electric current is applied to both electrodes 11 and 12 through a substance to be fed to the melting space to heat sludge incineration ash 1, magnesium oxide 3, calcium waste 4, and potassium oxide 5 by Joule heat. Then, it is melted, and the melting space is kept in a reducing atmosphere by carbon as the main component of the coke 2.

【0025】コークス2の量は、重量比で炉体10の溶
融空間へ送給される物質全量の5%以下(汚泥焼却灰1
中の鉄含有量に応じて調整する)、酸化カリウム5の量
は、炉体10の溶融空間へ送給される物質全量の数%に
する。
The amount of coke 2 is 5% or less by weight of the total amount of the substances fed to the melting space of the furnace body 10 (sludge incineration ash 1
The amount of potassium oxide 5 is adjusted to several% of the total amount of the substance fed to the melting space of the furnace body 10.

【0026】また、炉体10の溶融空間へコークス2を
送給することにより、ライニング9や電極12の消耗を
抑制できる。
Further, by feeding the coke 2 to the melting space of the furnace body 10, the consumption of the lining 9 and the electrode 12 can be suppressed.

【0027】汚泥焼却灰1、酸化マグネシウム3、カル
シウム質廃棄物4、酸化カリウム5が溶融すると、金属
と非金属との比重差に起因して、汚泥焼却灰1が含んで
いた鉄、ニッケル、クロムなどの金属を主体とする溶融
金属24の層が、溶融空間の内底側に形成され、元来、
汚泥焼却灰1が含んでいた五酸化二リン(P25)、酸
化マグネシウム、酸化カルシウム、酸化カリウム、及び
ケイ酸(SiO)や、原料用に添加した酸化マグネシウ
ム3、カルシウム質廃棄物4、酸化カリウム5を主体と
する溶融スラグ25の層が、溶融金属24の層の上側に
形成され、溶融金属24と溶融スラグ25とが、二液分
離状態で共存する。
When the sludge incineration ash 1, the magnesium oxide 3, the calcium waste 4, and the potassium oxide 5 are melted, iron and nickel contained in the sludge incineration ash 1 are caused by the difference in specific gravity between metal and nonmetal. A layer of the molten metal 24 mainly composed of a metal such as chromium is formed on the inner bottom side of the melting space, and originally,
Diphosphorus pentoxide (P 2 O 5 ), magnesium oxide, calcium oxide, potassium oxide, and silicic acid (SiO) contained in sludge incineration ash 1, magnesium oxide 3 added as a raw material, and calcium waste 4 A layer of the molten slag 25 mainly containing potassium oxide 5 is formed on the upper side of the layer of the molten metal 24, and the molten metal 24 and the molten slag 25 coexist in a two-liquid separated state.

【0028】この溶融スラグ25は、カリウムを加えて
いるので、カリウムを加えない場合と対比すると、50
℃を超過する範囲で溶融温度の低減が図られるという知
見を実験によって得た。
Since this molten slag 25 contains potassium, it is 50 when compared with the case where potassium is not added.
The knowledge that the melting temperature can be reduced in the range exceeding ℃ was obtained by experiments.

【0029】よって、カリウムを加えれば、炉体10の
溶融空間へ投入した物質を加熱するために電極11,1
2へ給電すべき電力の節減を図ることができる。
Therefore, when potassium is added, the electrodes 11 and 1 are heated to heat the substance charged into the melting space of the furnace body 10.
It is possible to reduce the amount of power that should be supplied to 2.

【0030】汚泥焼却灰1に含まれていた鉛、亜鉛、ヒ
素、カドミウムなどの有害物質は、ガス排出口15を経
て炉体10の外部の排ガス処理設備の2次燃焼炉へ送給
され、無害化が図られる。
The harmful substances such as lead, zinc, arsenic and cadmium contained in the sludge incineration ash 1 are sent to the secondary combustion furnace of the exhaust gas treatment facility outside the furnace body 10 through the gas outlet 15. Detoxification is achieved.

【0031】更に、溶融スラグ25を、スラグ排出口1
6から水流トラフ27を介して水砕槽19へ出滓させ、
水18により急冷する水砕処理を行ない、粒状化したス
ラグ26を回収する。
Further, the molten slag 25 is supplied to the slag discharge port 1
6 to the water granulation tank 19 through the water trough 27,
A water granulation process of quenching with water 18 is performed to recover the granulated slag 26.

【0032】このスラグ26は、五酸化二リン、酸化マ
グネシウム、酸化カルシウム、酸化カリウム、ケイ酸を
含んだ溶融スラグ25が固化したものであるので、リン
鉱石を原料としたリン肥料と同等な施肥効果を奏する。
Since the molten slag 25 containing diphosphorus pentoxide, magnesium oxide, calcium oxide, potassium oxide, and silicic acid is solidified, the slag 26 is fertilized in the same manner as a phosphorus fertilizer made of phosphate rock. Produce an effect.

【0033】これに加えて、汚泥焼却灰1が含んでいた
種々の金属は、溶融金属24に含まれるため、スラグ2
6を肥料として撒布しても、土壌を汚染しない。
In addition to this, since various metals contained in the sludge incineration ash 1 are contained in the molten metal 24, the slag 2 is contained.
Spreading 6 as fertilizer does not pollute the soil.

【0034】また、溶融金属24を、金属排出口17か
ら炉体10の外部へ出湯させ、自然風冷により固化した
金属を廃棄する。
Further, the molten metal 24 is discharged from the metal outlet 17 to the outside of the furnace body 10, and the metal solidified by natural air cooling is discarded.

【0035】上述したような手順で、汚泥焼却灰1、酸
化マグネシウム3、カルシウム質廃棄物4を溶融して肥
料を製造する際には、汚泥焼却灰1の単位重量あたりの
リン含有量を予め測定しておき、回収後のスラグ26に
含まれる五酸化二リン、酸化マグネシウム、並びに酸化
カルシウムのモル比率が、1:2乃至4:2乃至4程度
(好ましくは1:3.5:3.5程度)になるように、
汚泥焼却灰1に対する酸化マグネシウム3とカルシウム
質廃棄物4の量を定めれば、最適な配合のリン肥料が得
られる。
When the sludge incineration ash 1, the magnesium oxide 3, and the calcium waste 4 are melted to produce a fertilizer by the procedure as described above, the phosphorus content per unit weight of the sludge incineration ash 1 is previously set. After measurement, the molar ratio of diphosphorus pentoxide, magnesium oxide and calcium oxide contained in the recovered slag 26 is about 1: 2 to 4: 2 to 4 (preferably 1: 3.5: 3. 5),
If the amounts of magnesium oxide 3 and calcium waste 4 relative to the sludge incineration ash 1 are determined, a phosphorus fertilizer having an optimum composition can be obtained.

【0036】なお、本発明の肥料製造方法は上述した実
施の形態のみに限定されるものではなく、汚泥焼却灰の
成分や肥料の用途に応じてマグネシウム成分、カリウム
成分の添加を省くこと、その他、本発明の要旨を逸脱し
ない範囲において変更を加え得ることは勿論である。
The fertilizer production method of the present invention is not limited to the above-described embodiment, and the addition of magnesium and potassium components may be omitted depending on the components of sludge incineration ash and the use of fertilizer. Of course, changes can be made without departing from the scope of the present invention.

【0037】[0037]

【発明の効果】以上述べたように、本発明の肥料製造方
法では下記のような種々の優れた効果を奏し得る。
As described above, the fertilizer manufacturing method of the present invention can exhibit various excellent effects as described below.

【0038】(1)本発明の請求項1乃至請求項5に記
載の肥料製造方法のいずれにおいても、還元性雰囲気に
保持した溶融炉で、汚泥焼却灰とカルシウム質廃棄物を
溶融させ、リン成分及びカルシウム成分を含んだ溶融ス
ラグに水砕処理を行なって、取り扱いが容易な粒状にす
るので、カルシウム質廃棄物及び汚泥焼却灰を、肥料と
して有効に利用することができる。
(1) In any of the fertilizer production methods according to the first to fifth aspects of the present invention, sludge incineration ash and calcium waste are melted in a melting furnace kept in a reducing atmosphere to remove phosphorus. Since the molten slag containing the component and the calcium component is subjected to the water granulation treatment to be granulated for easy handling, the calcium-based waste and the sludge incineration ash can be effectively used as a fertilizer.

【0039】(2)本発明の請求項3、5に記載の肥料
製造方法のいずれにおいても、別途にマグネシウム成分
を加えることによって、肥料に用いるスラグのマグネシ
ウム成分の増加を図ることができる。
(2) In any of the fertilizer manufacturing methods described in claims 3 and 5 of the present invention, the magnesium component of the slag used for the fertilizer can be increased by adding the magnesium component separately.

【0040】(3)本発明の請求項4、5に記載の肥料
製造方法のいずれにおいても、別途にカリウム成分を加
えることにより、スラグが溶融状態を保持可能な温度に
低下させることができ、また、肥料として使用するスラ
グのカリウム成分の増加を図ることができる。
(3) In any of the methods for producing a fertilizer according to claims 4 and 5 of the present invention, the temperature can be lowered to a temperature at which the molten state of the slag can be maintained by adding a potassium component separately, Further, it is possible to increase the potassium component of slag used as fertilizer.

【0041】(4)本発明の請求項6に記載の肥料製造
方法においては、汚泥焼却灰とともに溶融すべきカルシ
ウム質廃棄物及びマグネシウム成分の量を、水砕処理を
した後のスラグに含まれる五酸化二リン、酸化マグネシ
ウム、酸化カルシウムのモル比率が、1:2乃至4:2
乃至4程度になるよう定めるので、ク溶性(2%クエン
酸溶液への溶解性)に優れた緩効性の肥料を得ることが
できる。
(4) In the method for producing a fertilizer according to claim 6 of the present invention, the amounts of calcium waste and magnesium components to be melted together with the sludge incineration ash are contained in the slag after the water granulation treatment. The molar ratio of diphosphorus pentoxide, magnesium oxide and calcium oxide is 1: 2 to 4: 2.
Since it is determined so as to be about 4 to 4, it is possible to obtain a slow-release fertilizer having excellent solubility (solubility in a 2% citric acid solution).

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

【図1】本発明の肥料製造方法の実施の形態の一例を示
す概念図である。
FIG. 1 is a conceptual diagram showing an example of an embodiment of a fertilizer manufacturing method of the present invention.

【符号の説明】[Explanation of symbols]

1 汚泥焼却灰 2 コークス(還元剤) 3 酸化マグネシウム(マグネシウム成分) 4 カルシウム質廃棄物 5 酸化カリウム(カリウム成分) 8 溶融炉 19 水砕槽 24 溶融金属 25 溶融スラグ 26 スラグ(粒状体) 1 Sludge incineration ash 2 coke (reducing agent) 3 Magnesium oxide (magnesium component) 4 Calcium waste 5 Potassium oxide (potassium component) 8 melting furnace 19 water granulation tank 24 Molten metal 25 Molten slag 26 Slag (granular body)

───────────────────────────────────────────────────── 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) B09B 3/00 ZAB C05B 13:02 101 //(C05G 1/00 B09B 3/00 303K C05F 7:00 ZAB C05B 13:02) 101 303L (72)発明者 高木 禎史 東京都千代田区有楽町1丁目4番1号 三 機工業株式会社内 (72)発明者 定塚 徹治 東京都千代田区有楽町1丁目4番1号 三 機工業株式会社内 Fターム(参考) 4D004 AA16 AA36 BA04 CA12 CA14 CA29 CA32 CA37 CB01 CC11 DA03 DA10 4H061 AA02 BB42 CC51 FF08 GG18 GG23 GG26 ─────────────────────────────────────────────────── ─── Continuation of front page (51) Int.Cl. 7 Identification code FI theme code (reference) B09B 3/00 ZAB C05B 13:02 101 // (C05G 1/00 B09B 3/00 303K C05F 7:00 ZAB C05B 13:02) 101 303L (72) Inventor Sadafumi Takagi 1-4-1, Yurakucho, Chiyoda-ku, Tokyo Sanki Kogyo Co., Ltd. (72) Tetsuji Jotsuka 1-1-4, Yurakucho, Chiyoda-ku, Tokyo Sanki Kogyo Co., Ltd. F term (reference) 4D004 AA16 AA36 BA04 CA12 CA14 CA29 CA32 CA37 CB01 CC11 DA03 DA10 4H061 AA02 BB42 CC51 FF08 GG18 GG23 GG26

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】 カルシウム質廃棄物、及びリン成分を含
んでいる汚泥焼却灰を還元性雰囲気の溶融炉内で加熱し
て、溶融金属と溶融スラグを溶融炉内に二液分離状態で
共存させ、当該溶融スラグを水砕処理によって粒状化さ
せることを特徴とする肥料製造方法。
1. A calcium waste and sludge incineration ash containing a phosphorus component are heated in a melting furnace in a reducing atmosphere so that molten metal and molten slag coexist in the melting furnace in a two-liquid separated state. A method for producing a fertilizer, characterized in that the molten slag is granulated by a water granulation process.
【請求項2】 カルシウム質廃棄物、リン成分を含んで
いる汚泥焼却灰、及び還元剤を溶融炉内で加熱して、溶
融金属と溶融スラグを溶融炉内に二液分離状態で共存さ
せ、当該溶融スラグを水砕処理によって粒状化させるこ
とを特徴とする肥料製造方法。
2. A calcium-based waste, a sludge incineration ash containing a phosphorus component, and a reducing agent are heated in a melting furnace to allow molten metal and molten slag to coexist in the melting furnace in a two-liquid separated state. A method for producing a fertilizer, which comprises granulating the molten slag by water granulation.
【請求項3】 カルシウム質廃棄物、リン成分を含んで
いる汚泥焼却灰、還元剤、及びマグネシウム成分を溶融
炉内で加熱して、溶融金属と溶融スラグを溶融炉内に二
液分離状態で共存させ、当該溶融スラグを水砕処理によ
って粒状化させることを特徴とする肥料製造方法。
3. The calcium waste, the sludge incineration ash containing the phosphorus component, the reducing agent, and the magnesium component are heated in the melting furnace so that the molten metal and the molten slag are separated into two liquids in the melting furnace. A method for producing a fertilizer, which comprises coexisting and granulating the molten slag by water granulation.
【請求項4】 カルシウム質廃棄物、リン成分を含んで
いる汚泥焼却灰、還元剤、及びカリウム成分を溶融炉内
で加熱して、溶融金属と溶融スラグを溶融炉内に二液分
離状態で共存させ、当該溶融スラグを水砕処理によって
粒状化させることを特徴とする肥料製造方法。
4. Calcium waste, sludge incineration ash containing phosphorus component, reducing agent, and potassium component are heated in a melting furnace to separate molten metal and molten slag into two liquids in a melting furnace. A method for producing a fertilizer, which comprises coexisting and granulating the molten slag by water granulation.
【請求項5】 カルシウム質廃棄物、リン成分を含んで
いる汚泥焼却灰、還元剤、マグネシウム成分、及びカリ
ウム成分を溶融炉内で加熱して、溶融金属と溶融スラグ
を溶融炉内に二液分離状態で共存させ、当該溶融スラグ
を水砕処理によって粒状化させることを特徴とする肥料
製造方法。
5. A calcium-based waste, a sludge incineration ash containing a phosphorus component, a reducing agent, a magnesium component, and a potassium component are heated in a melting furnace, and a molten metal and a molten slag are two-component in the melting furnace. A method for producing a fertilizer, characterized in that the molten slag is made to coexist in a separated state and is granulated by a water granulation process.
【請求項6】 汚泥焼却灰のリン含有量を予め把握して
おき、溶融スラグの水砕処理により得られる粒状体の五
酸化二リン、酸化マグネシウム、並びに酸化カルシウム
のモル比率が、1:2乃至4:2乃至4程度となるよう
に、汚泥焼却灰に対するカルシウム質廃棄物及びマグネ
シウム成分の量を定める請求項3または請求項5のいず
れかに記載の肥料製造方法。
6. The phosphorus content of sludge incineration ash is grasped in advance, and the granular ratio of diphosphorus pentoxide, magnesium oxide and calcium oxide obtained by the water granulation treatment of molten slag has a molar ratio of 1: 2. To 4: The fertilizer manufacturing method according to claim 3 or 5, wherein the amounts of the calcium-based waste and the magnesium component with respect to the sludge incineration ash are determined so as to be about 2 to 4.
JP2001305518A 2001-10-01 2001-10-01 Method for manufacturing fertilizer Pending JP2003112989A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2001305518A JP2003112989A (en) 2001-10-01 2001-10-01 Method for manufacturing fertilizer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001305518A JP2003112989A (en) 2001-10-01 2001-10-01 Method for manufacturing fertilizer

Publications (1)

Publication Number Publication Date
JP2003112989A true JP2003112989A (en) 2003-04-18

Family

ID=19125296

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2001305518A Pending JP2003112989A (en) 2001-10-01 2001-10-01 Method for manufacturing fertilizer

Country Status (1)

Country Link
JP (1) JP2003112989A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2005123629A1 (en) * 2004-06-21 2005-12-29 Sanki Engineering Co., Ltd. Method and apparatus for producing phosphate fertilizer utilizing incineration ash
WO2006072982A1 (en) 2005-01-06 2006-07-13 Sanki Engineering Co., Ltd Process for producing phosphatic fertilizer and apparatus therefor
JP2011177112A (en) * 2010-03-01 2011-09-15 Nippon Steel Engineering Co Ltd Material for promoting growth of turf, and method for growing turf

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2005123629A1 (en) * 2004-06-21 2005-12-29 Sanki Engineering Co., Ltd. Method and apparatus for producing phosphate fertilizer utilizing incineration ash
JP2006001819A (en) * 2004-06-21 2006-01-05 Tokyo Metropolis Method and apparatus for manufacturing phosphorus fertilizer using incineration ash
WO2006072982A1 (en) 2005-01-06 2006-07-13 Sanki Engineering Co., Ltd Process for producing phosphatic fertilizer and apparatus therefor
JP2011177112A (en) * 2010-03-01 2011-09-15 Nippon Steel Engineering Co Ltd Material for promoting growth of turf, and method for growing turf

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