JP2003112988A - Method for manufacturing phosphorus fertilizer - Google Patents

Method for manufacturing phosphorus fertilizer

Info

Publication number
JP2003112988A
JP2003112988A JP2001305517A JP2001305517A JP2003112988A JP 2003112988 A JP2003112988 A JP 2003112988A JP 2001305517 A JP2001305517 A JP 2001305517A JP 2001305517 A JP2001305517 A JP 2001305517A JP 2003112988 A JP2003112988 A JP 2003112988A
Authority
JP
Japan
Prior art keywords
component
phosphorus
melting furnace
molten slag
incineration ash
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
JP2001305517A
Other languages
Japanese (ja)
Inventor
Matsuji Kuwako
松司 桑子
Fumio Mishina
文雄 三品
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
Japan Sewage Works Agency
Original Assignee
Sanki Engineering Co Ltd
Japan Sewage Works Agency
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, Japan Sewage Works Agency filed Critical Sanki Engineering Co Ltd
Priority to JP2001305517A priority Critical patent/JP2003112988A/en
Publication of JP2003112988A publication Critical patent/JP2003112988A/en
Pending legal-status Critical Current

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  • Disintegrating Or Milling (AREA)
  • Fertilizers (AREA)

Abstract

PROBLEM TO BE SOLVED: To manufacture a fertilizer which is high in concentration of a phosphorus component and is safe from sludge incineration ash. SOLUTION: The sludge incineration ash 1 having the high concentration of the phosphorus component is obtained by adding a ferrous flocculating agent 7 to sewage 6 to settle the phosphorus component included in the sewage 6 and collecting the precipitate 21 together with sludge 22, then dewatering and incinerating the same. Coke 2, magnesium oxide 3, calcium oxide 4 and potassium oxide 5 are added to the sludge incineration ash 1 and the mixture is heated in a fusion furnace 8 to allow molten metals 24 and molten slag 25 to coexist in a two-liquid separation state in the fusion furnace 8. Further, the molten slag 25 is selectively discharged to a hydropulping chamber 19 where the slag is rapidly cooled and is made into a granular form to facilitate its handling as the fertilizer. Granular slag 26 which is high in the concentration of the phosphorus component and is get rid of the metallic components is thus recovered.

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】本発明は下水汚泥の焼却灰を
主な原料に用いたリン肥料製造方法に関するものであ
る。
TECHNICAL FIELD The present invention relates to a method for producing a phosphorus fertilizer using incineration ash of sewage sludge as a main raw material.

【0002】[0002]

【従来の技術】リン肥料の原料であるリン鉱石は、国内
で工業的に利用可能なものが産出されないため、その全
量を海外から輸入している。
2. Description of the Related Art Phosphorous ore, which is a raw material for phosphorus fertilizer, is not industrially available domestically, and therefore is entirely imported from abroad.

【0003】既知の採掘可能なリン鉱石の埋蔵量は、数
量的には多く見積もられているが、実際に採掘したリン
鉱石の品質は、不純物の含有量の増加などに起因して徐
々に低下しており、良質なリン鉱石を得にくくなってい
る。
The known reserves of minable phosphate rocks are estimated to be large in quantity, but the quality of the phosphate rocks actually mined gradually increases due to an increase in the content of impurities. It is decreasing and it is difficult to obtain high quality phosphate rock.

【0004】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
しているが、近年、最終処分場の廃棄物の受け入れが逼
迫しており、下水処理廃棄物の更なる減容(体積を減ら
す処置)を行なう必要がある。
The sludge generated by the sewage treatment is dehydrated and incinerated and then disposed of at the final disposal site. In recent years, however, the acceptance of waste at the final disposal site has become tight. It is necessary to further reduce the volume of sewage treatment waste (volume reduction).

【0005】そこで、汚泥中に存在する窒素、リン、マ
グネシウム、カルシウム、カリウムなどの諸物質に着目
して、乾燥汚泥、あるいは汚泥を原料にしたコンポスト
を、有機肥料として利用することが行なわれている。
Therefore, paying attention to various substances such as nitrogen, phosphorus, magnesium, calcium and potassium existing in sludge, dry sludge or compost made from sludge as a raw material is used as an organic fertilizer. There is.

【0006】[0006]

【発明が解決しようとする課題】しかしながら、乾燥汚
泥やコンポストに含まれているリン成分の濃度は、リン
鉱石から製造された肥料に比べて低く、土壌に対する施
肥効果をあまり期待できない。
However, the concentration of the phosphorus component contained in the dried sludge and compost is lower than that of the fertilizer produced from phosphate rock, and the fertilizing effect on soil cannot be expected so much.

【0007】更に、汚泥には、鉄、銅、亜鉛、鉛、ニッ
ケル、クロムなどの種々の金属や、ヒ素、カドミウムの
ような有害物質が含まれている場合があり、これらの物
質による土壌の汚染が懸念される。
Further, sludge may contain various metals such as iron, copper, zinc, lead, nickel and chromium, and harmful substances such as arsenic and cadmium. There is concern about pollution.

【0008】本発明は上述した実情に鑑みたもので、リ
ン成分の濃度が高く且つ安全な肥料を汚泥焼却灰から製
造することを目的としている。
The present invention has been made in view of the above circumstances, and an object thereof is to produce a safe fertilizer having a high concentration of phosphorus components from sludge incineration ash.

【0009】[0009]

【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に記載のリン肥料製造方法では、
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、当該溶融スラグに対して水砕処
理を行ない、溶融スラグを粒状化させる。
In order to achieve the above object, in the method for producing phosphorus fertilizer according to claim 1 of the present invention,
The sludge incineration ash containing the phosphorus component is heated in the melting furnace in a reducing atmosphere, the molten metal and the molten slag coexist in the melting furnace in a two-liquid separated state, and the molten slag is subjected to water granulation treatment. And granulate the molten slag.

【0010】本発明の請求項2に記載のリン肥料製造方
法では、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 method for producing a phosphorus fertilizer according to claim 2 of the present invention, sludge incineration ash containing a phosphorus component and a reducing agent are heated in a melting furnace so that molten metal and molten slag are placed in the melting furnace. The two liquids are made to coexist in a separated state, and the molten slag is granulated by water granulation treatment.

【0011】本発明の請求項3に記載のリン肥料製造方
法では、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 phosphorus fertilizer according to claim 3 of the present invention, the sludge incineration ash containing the phosphorus component, the reducing agent, and the magnesium component are heated in a melting furnace to melt the molten metal and the molten slag. The molten slag is made to coagulate in the furnace in a two-liquid separated state and granulated by water granulation.

【0012】本発明の請求項4に記載のリン肥料製造方
法では、リン成分を含んでいる汚泥焼却灰、還元剤、及
びカル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 phosphorus fertilizer according to claim 4 of the present invention, sludge incineration ash containing a phosphorus component, a reducing agent, and a calcium component are heated in a melting furnace to melt the molten metal and the molten slag. The molten slag is made to coagulate in the furnace in a two-liquid separated state and granulated by water granulation.

【0013】本発明の請求項5に記載のリン肥料製造方
法では、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、及びカル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 phosphorus fertilizer according to claim 5 of the present invention, sludge incineration ash containing phosphorus component, reducing agent, magnesium component and calcium component are heated in a melting furnace to melt with molten metal. The slag is allowed to coexist in the melting furnace in a two-liquid separated state, and the molten slag is granulated by water granulation treatment.

【0014】本発明の請求項6に記載のリン肥料製造方
法では、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 phosphorus fertilizer according to claim 6 of the present invention, sludge incineration ash containing a phosphorus component, a reducing agent, and a potassium component are heated in a melting furnace to melt the molten metal and the molten slag. The molten slag is made to coagulate in the furnace in a two-liquid separated state and granulated by water granulation.

【0015】本発明の請求項7に記載のリン肥料製造方
法では、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 phosphorus fertilizer according to claim 7 of the present invention, sludge incineration ash containing phosphorus component, reducing agent, magnesium component and potassium component are heated in a melting furnace to melt with molten metal. The slag is allowed to coexist in the melting furnace in a two-liquid separated state, and the molten slag is granulated by water granulation treatment.

【0016】本発明の請求項8に記載のリン肥料製造方
法では、リン成分を含んでいる汚泥焼却灰、還元剤、カ
ルシウム成分、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 phosphorus fertilizer according to claim 8 of the present invention, sludge incineration ash containing phosphorus component, reducing agent, calcium component, and potassium component are heated in a melting furnace to melt with molten metal. The slag is allowed to coexist in the melting furnace in a two-liquid separated state, and the molten slag is granulated by water granulation treatment.

【0017】本発明の請求項9に記載のリン肥料製造方
法では、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、カルシウム成分、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 phosphorus fertilizer according to claim 9 of the present invention, sludge incineration ash containing a phosphorus component, a reducing agent, a magnesium component, a calcium component, and a potassium component are heated in a melting furnace to obtain a molten metal. And molten slag coexist in a melting furnace in a two-liquid separated state, and the molten slag is granulated by water granulation treatment.

【0018】本発明の請求項10に記載のリン肥料製造
方法では、リン成分を捕捉する鉄系凝集剤を汚水に添加
し、該汚水中に含まれるリン成分を沈降させて汚泥とと
もに収集し、これらを脱水し且つ焼却して、溶融炉内で
加熱すべき汚泥焼却灰を得る。
In the method for producing a phosphorus fertilizer according to claim 10 of the present invention, an iron-based coagulant for trapping phosphorus components is added to sewage, and the phosphorus components contained in the sewage are allowed to settle and collected together with sludge, These are dehydrated and incinerated to obtain sludge incineration ash to be heated in the melting furnace.

【0019】本発明の請求項11に記載のリン肥料製造
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マグネシウム成分及びカルシウ
ム成分の量を定める。
In the method for producing phosphorus fertilizer according to claim 11 of the present invention, the phosphorus content of the sludge incineration ash is grasped in advance, and the granular material obtained by the water granulation process of the molten slag is diphosphorus pentoxide and oxidized. The amounts of magnesium component and calcium component relative to the sludge incineration ash are determined so that the molar ratio of magnesium and calcium oxide is about 1: 2 to 4: 2 to 4.

【0020】本発明の請求項1乃至請求項9に記載のリ
ン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 methods for producing phosphorus fertilizer according to any of claims 1 to 9 of the present invention, molten metal and molten slag are made to coexist in a two-liquid separated state in a melting furnace kept in a reducing atmosphere. The metal is separated from the molten slag, and the molten slag is subjected to water granulation treatment to form the slag containing the phosphorus component into particles that are easy to handle.

【0021】本発明の請求項3、5、7、9に記載のリ
ン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 methods for producing phosphorus fertilizers according to claims 3, 5, 7, and 9 of the present invention, the magnesium component should be increased by separately adding the magnesium component.

【0022】本発明の請求項4、5、8、9に記載のリ
ン肥料製造方法のいずれにおいても、カルシウム成分を
別途に加えることにより、スラグが含むべきカルシウム
成分の増加を図る。
In any of the methods for producing phosphorus fertilizers according to claims 4, 5, 8 and 9, the calcium component is added separately to increase the calcium component to be contained in the slag.

【0023】本発明の請求項7乃至請求項9に記載のリ
ン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 phosphorus fertilizer according to any of claims 7 to 9 of the present invention, by adding a potassium component separately, the temperature at which the slag becomes a molten state is lowered and the slag should be contained. Aim to increase potassium content.

【0024】本発明の請求項10に記載のリン肥料製造
方法においては、鉄系凝集剤の添加により、汚水中に溶
存するリン成分を沈降させて汚泥とともに収集し、汚泥
焼却灰に含まれるリン成分の濃度を高める。
In the method for producing a phosphorus fertilizer according to claim 10 of the present invention, the phosphorus component dissolved in the wastewater is precipitated by adding an iron-based coagulant and collected together with the sludge, and the phosphorus contained in the sludge incineration ash is added. Increase the concentration of ingredients.

【0025】本発明の請求項11に記載のリン肥料製造
方法においては、汚泥焼却灰とともに加熱すべきマグネ
シウム成分及びカルシウム成分の量を、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 phosphorus fertilizer according to claim 11 of the present invention, the amounts of magnesium component and calcium component to be heated together with the sludge incineration ash are determined by adjusting the amount of diphosphorus pentoxide and oxidation contained in the slag after the water granulation treatment. The molar ratio of magnesium and calcium oxide is set to about 1: 2 to 4: 2 to 4 to obtain a phosphorus fertilizer having an optimum component ratio.

【0026】[0026]

【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.

【0027】図1は本発明のリン肥料製造方法の実施の
形態の一例を示すものであり、このリン肥料製造方法で
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、酸化カルシウム
(CaO)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 the phosphorus fertilizer production method of the present invention. In this phosphorus fertilizer production method, sludge incineration ash 1, coke 2 as a carbon (C) -based reducing agent, oxidation Magnesium (MgO) 3, calcium oxide (CaO) 4, and potassium oxide (K 2 O) 5 are used as fertilizer raw materials.

【0028】また、上記の各原料から肥料を製造するた
めに、塩化鉄を主な成分として汚水6に含まれているリ
ン成分を捕捉する鉄系凝集剤7、並びに溶融炉8を用い
る。
Further, in order to produce a fertilizer from each of the above raw materials, an iron-based coagulant 7 for trapping the phosphorus component contained in the wastewater 6 with iron chloride as a main component, and a melting furnace 8 are used.

【0029】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.

【0030】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.

【0031】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.

【0032】リン肥料を製造するときには、エアレーシ
ョンタンク20に貯留した汚水6に鉄系凝集剤7を添加
した後、汚水6に対する撹拌、あるいは通気などの操作
を行ない、汚水6中に含まれているリン成分を沈降させ
る。
When the phosphorus fertilizer is produced, after adding the iron-based coagulant 7 to the sewage 6 stored in the aeration tank 20, the sewage 6 is stirred or ventilated to be contained in the sewage 6. Allow the phosphorus component to settle.

【0033】この沈降物21、及びエアレーションタン
ク20の内底に沈降した汚泥22を収集し、これらが含
有している水分を、遠心脱水機やベルトプレス脱水機な
どの手段を用いて取り除き、脱水汚泥23とする。
The sediment 21 and the sludge 22 that has settled on the inner bottom of the aeration tank 20 are collected, and the water contained therein is removed by a means such as a centrifugal dehydrator or a belt press dehydrator to dehydrate the sludge. Sludge 23 is used.

【0034】更に、脱水汚泥23を焼却炉(図示せず)
により800℃程度の温度で焼却して、汚泥焼却灰1を
生成する。
Further, the dehydrated sludge 23 is incinerated (not shown).
Is incinerated at a temperature of about 800 ° C. to produce sludge incineration ash 1.

【0035】よって、汚水6を浄化した処理水に残留す
るリン成分の濃度の低減が図られ、また、汚水6中に含
まれていたリン成分が脱水汚泥23へ移行して、汚泥焼
却灰1のリン成分の濃度が高まる。
Therefore, the concentration of the phosphorus component remaining in the treated water obtained by purifying the sewage 6 is reduced, and the phosphorus component contained in the sewage 6 is transferred to the dehydrated sludge 23 and the sludge incineration ash 1 The concentration of the phosphorus component of is increased.

【0036】次いで、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、酸化カルシウム
4、酸化カリウム5を、原料投入口14から炉体10の
溶融空間へ送給したうえ、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、酸化カルシウム4、酸化カリウム5
をジュール熱で加熱して溶融させるとともに、コークス
2の主成分である炭素によって溶融空間を還元性雰囲気
に保つ。
Then, the sludge incineration ash 1, the coke 2, the magnesium oxide 3, the calcium oxide 4, and the potassium oxide 5 are fed from the raw material charging machine 13 to the melting space of the furnace body 10 from the raw material charging port 14, and both electrodes are fed. An electric current is applied to 11 and 12 through a substance to be fed to the melting space, sludge incineration ash 1, magnesium oxide 3, calcium oxide 4, potassium oxide 5
Is heated by Joule heat to be melted, and the melting space is kept in a reducing atmosphere by carbon as the main component of the coke 2.

【0037】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.

【0038】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.

【0039】汚泥焼却灰1、酸化マグネシウム3、酸化
カルシウム4、及び酸化カリウム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、クロムなどの種々の金属、並びに鉄
系凝集剤7の鉄成分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(Si
O)、並びに原料用に添加した酸化マグネシウム3、酸
化カルシウム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, magnesium oxide 3, calcium oxide 4, and potassium oxide 5 are melted, iron, nickel, and chromium contained in the sludge incineration ash 1 are caused due to the difference in specific gravity between metal and nonmetal. Various metals such as, and a layer of the molten metal 24 mainly composed of the iron component of the iron-based coagulant 7,
Diphosphorus pentoxide (P 2 O 5 ), which was originally formed in the sludge incineration ash 1 and was formed on the inner bottom side of the melting space, magnesium oxide,
Calcium oxide, potassium oxide, and silicic acid (Si
O), and a layer of the molten slag 25 mainly composed of magnesium oxide 3, calcium oxide 4, and potassium oxide 5 added for the raw material are formed on the upper side of the layer of the molten metal 24, and the molten metal 24 and the molten slag 25 are formed. However, they coexist in a two-liquid separated state.

【0040】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.

【0041】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.

【0042】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.

【0043】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.

【0044】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, this slag 26 is fertilized in the same manner as phosphorus fertilizer using phosphorus ore as a raw material. Produce an effect.

【0045】これに加えて、汚泥焼却灰1が含んでいた
種々の金属、並びに鉄系凝集剤7の鉄成分は、溶融金属
24に含まれるため、スラグ26を肥料として撒布して
も、土壌を汚染しない。
In addition to this, since the various metals contained in the sludge incineration ash 1 and the iron component of the iron-based coagulant 7 are contained in the molten metal 24, even if the slag 26 is sprinkled as fertilizer, the soil Do not pollute.

【0046】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.

【0047】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、酸化カルシウム4を溶融してリン肥
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と酸化カルシ
ウム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, magnesium oxide 3 and calcium oxide 4 are melted to produce a phosphorus fertilizer by the procedure described above, the phosphorus content per unit weight of the sludge incineration ash 1 is measured in advance. Incidentally, 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). Degree)
If the amounts of magnesium oxide 3 and calcium oxide 4 with respect to the sludge incineration ash 1 are determined, a phosphorus fertilizer having an optimum composition can be obtained.

【0048】なお、本発明のリン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、あるいは肥料の用途に応じてマグネシウム成
分、カルシウム成分、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 method for producing phosphorus fertilizer according to the present invention is not limited to the above-mentioned embodiment, but the addition of magnesium component, calcium component, potassium component depending on the component of sludge incineration ash or the use of fertilizer. Omitting,
Of course, other changes can be made without departing from the scope of the present invention.

【0049】[0049]

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

【0050】(1)本発明の請求項1乃至請求項9に記
載のリン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を分離し、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、リ
ン成分の濃度が高く且つ安全な肥料を汚泥焼却灰から製
造ができ、下水処理に付随して発生する汚泥の有効利用
を図ることができる。
(1) In any of the methods for producing phosphorus fertilizer according to any one of claims 1 to 9 of the present invention, molten metal and molten slag are separated into two liquids in a melting furnace kept in a reducing atmosphere. The metal is separated by coexistence, and the molten slag is subjected to water granulation treatment to form granules that are easy to handle, so fertilizer with a high phosphorus concentration and safe fertilizer can be produced from sludge incineration ash, and is associated with sewage treatment. The sludge generated as a result can be effectively used.

【0051】(2)本発明の請求項3、5、7、9に記
載のリン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って、リン肥料として用
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 methods for producing a phosphorus fertilizer according to claims 3, 5, 7, and 9 of the present invention, the magnesium component is added separately to increase the magnesium component of the slag used as the phosphorus fertilizer. Can be planned.

【0052】(3)本発明の請求項4、5、8、9に記
載のリン肥料製造方法のいずれにおいても、カルシウム
成分を別途に加えることによって、リン肥料として用い
るスラグのカルシウム成分の増加を図ることができる。
(3) In any of the methods for producing phosphorus fertilizers according to claims 4, 5, 8 and 9 of the present invention, the calcium component of the slag used as phosphorus fertilizer is increased by adding a calcium component separately. Can be planned.

【0053】(4)本発明の請求項7乃至請求項9に記
載のリン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。
(4) In any of the methods for producing phosphorus fertilizers according to claims 7 to 9 of the present invention, the potassium component is added separately to lower the temperature at which the molten state of the slag can be maintained. In addition, the potassium component of slag used as a fertilizer can be increased.

【0054】(5)本発明の請求項10に記載のリン肥
料製造方法においては、鉄系凝集剤の添加によって、汚
水中に含まれているリン成分を沈降させるので、肥料の
原料に用いる汚泥焼却灰に含まれるリン成分の濃度が高
くなり、また、凝集剤が鉄系であるので、当該鉄成分を
溶融金属へ確実に取り込むことができる。
(5) In the method for producing phosphorus fertilizer according to claim 10 of the present invention, since the phosphorus component contained in the wastewater is precipitated by the addition of the iron-based coagulant, the sludge used as the raw material for the fertilizer. Since the concentration of the phosphorus component contained in the incineration ash is high and the coagulant is iron-based, the iron component can be reliably incorporated into the molten metal.

【0055】(6)本発明の請求項11に記載のリン肥
料製造方法においては、汚泥焼却灰とともに溶融すべき
マグネシウム成分及びカルシウム成分の量を、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、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。
(6) In the method for producing a phosphorus fertilizer according to claim 11 of the present invention, the amounts of the magnesium component and the calcium component to be melted together with the sludge incinerated ash are determined by the dipentapentoxide contained in the slag after the water granulation treatment. Since the molar ratio of phosphorus, magnesium oxide and calcium oxide is determined to be about 1: 2 to 4: 2 to 4, a slow-release fertilizer with excellent solubility (solubility in a 2% citric acid solution) should be used. Obtainable.

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

【図1】本発明のリン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 phosphorus fertilizer production 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 酸化カルシウム(カルシウム成分) 5 酸化カリウム(カリウム成分) 6 汚水 7 鉄系凝集剤 8 溶融炉 19 水砕槽 21 沈降物 22 汚泥 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 oxide (calcium component) 5 Potassium oxide (potassium component) 6 dirty water 7 Iron-based coagulant 8 melting furnace 19 water granulation tank 21 sediment 22 sludge 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) C05D 3:02 C05D 5:00 5:00) (72)発明者 岩井 良博 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 小松 貴司 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 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) 4D067 CG04 EE35 GA20 4H061 AA02 BB42 CC08 CC15 CC51 FF08 GG18 GG23 GG26 ─────────────────────────────────────────────────── ─── Continuation of front page (51) Int.Cl. 7 Identification code FI theme code (reference) C05D 3:02 C05D 5:00 5:00) (72) Inventor Yoshihiro Iwai 1-4 Yurakucho, Chiyoda-ku, Tokyo No. 1 Sanki Kogyo Co., Ltd. (72) Inventor Takashi Komatsu 1-4-1, Yurakucho, Chiyoda-ku, Tokyo Sanki Kogyo Co., Ltd. (72) Satoshi Takagi 1-4-4 Yurakucho, Chiyoda-ku, Tokyo No. 1 Sanki Kogyo Co., Ltd. (72) Inventor Tetsuji Kazuka 1-4-1 Yurakucho, Chiyoda-ku, Tokyo F-Term inside Sanki Kogyo Co., Ltd. (reference) 4D067 CG04 EE35 GA20 4H061 AA02 BB42 CC08 CC15 CC51 FF08 GG18 GG23 GG26

Claims (11)

【特許請求の範囲】[Claims] 【請求項1】 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リン
肥料製造方法。
1. A sludge incineration ash containing a phosphorus component is 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, and the molten slag is mixed with water. A method for producing a phosphorus fertilizer, which comprises granulating by crushing treatment.
【請求項2】 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リン肥
料製造方法。
2. A sludge incineration ash containing a phosphorus component and a reducing agent are heated in a melting furnace so that molten metal and molten slag coexist in the melting furnace in a two-liquid separated state, and the molten slag is mixed with water. A method for producing a phosphorus fertilizer, which comprises granulating by crushing treatment.
【請求項3】 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
とを特徴とするリン肥料製造方法。
3. A sludge incineration ash containing a phosphorus component, a reducing agent, and a magnesium component are heated in a melting furnace so that molten metal and molten slag coexist in the melting furnace in a two-liquid separated state, and the melting is performed. A method for producing a phosphorus fertilizer, which comprises granulating slag by water granulation.
【請求項4】 リン成分を含んでいる汚泥焼却灰、還元
剤、及びカル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
特徴とするリン肥料製造方法。
4. A sludge incineration ash containing a phosphorus component, a reducing agent, and a calcium component are heated in a melting furnace so that molten metal and molten slag coexist in the melting furnace in a two-liquid separated state.
A method for producing a phosphorus fertilizer, which comprises granulating the molten slag by water granulation.
【請求項5】 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、及びカル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リン肥料製造方法。
5. A sludge incineration ash containing a phosphorus component, a reducing agent, a magnesium component, and a calcium component are heated in a melting furnace so that molten metal and molten slag coexist in the melting furnace in a two-liquid separated state. A method for producing phosphorus fertilizer, characterized in that the molten slag is granulated by a water granulation process.
【請求項6】 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
徴とするリン肥料製造方法。
6. A sludge incinerator ash containing a phosphorus component, a reducing agent, and a potassium component are heated in a melting furnace so that molten metal and molten slag coexist in the melting furnace in a two-liquid separated state, and the melting is performed. A method for producing a phosphorus fertilizer, which comprises granulating slag by water granulation.
【請求項7】 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リン肥料製造方法。
7. A sludge incinerator ash containing a phosphorus component, a reducing agent, a magnesium component, and a potassium component are heated in a melting furnace so that molten metal and molten slag coexist in the melting furnace in a two-liquid separated state. A method for producing phosphorus fertilizer, characterized in that the molten slag is granulated by a water granulation process.
【請求項8】 リン成分を含んでいる汚泥焼却灰、還元
剤、カルシウム成分、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リン肥料製造方法。
8. A sludge incineration ash containing a phosphorus component, a reducing agent, a calcium component, and a potassium component are heated in a melting furnace so that molten metal and molten slag coexist in the melting furnace in a two-liquid separated state. A method for producing phosphorus fertilizer, characterized in that the molten slag is granulated by a water granulation process.
【請求項9】 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、カルシウム成分、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リン肥料製造
方法。
9. A sludge incinerator ash containing a phosphorus component, a reducing agent, a magnesium component, a calcium component, and a potassium component are heated in a melting furnace to separate the molten metal and the molten slag into two liquids in the melting furnace. A method for producing a phosphorus fertilizer, which comprises coexisting and granulating the molten slag by water granulation treatment.
【請求項10】 リン成分を捕捉する鉄系凝集剤を汚水
に添加し、該汚水中に含まれるリン成分を沈降させて汚
泥とともに収集し、これらを脱水し且つ焼却して、溶融
炉内で加熱すべき汚泥焼却灰を得る請求項1乃至請求項
9のいずれかに記載のリン肥料製造方法。
10. An iron-based coagulant that captures phosphorus components is added to sewage, the phosphorus components contained in the sewage are precipitated and collected together with sludge, and these are dehydrated and incinerated in a melting furnace. The method for producing phosphorus fertilizer according to any one of claims 1 to 9, wherein sludge incineration ash to be heated is obtained.
【請求項11】 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マグネシウム成分及びカルシ
ウム成分の量を定める請求項5または請求項9のいずれ
かに記載のリン肥料製造方法。
11. The phosphorus content of sludge incineration ash is grasped in advance, and the molar ratio of diphosphorus pentoxide, magnesium oxide, and calcium oxide of the granular material obtained by the water granulation treatment of molten slag is 1: 2. To 4: The method for producing phosphorus fertilizer according to claim 5 or 9, wherein the amounts of the magnesium component and the calcium component with respect to the sludge incineration ash are determined so as to be about 2 to 4.
JP2001305517A 2001-10-01 2001-10-01 Method for manufacturing phosphorus fertilizer Pending JP2003112988A (en)

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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
WO2006072982A1 (en) 2005-01-06 2006-07-13 Sanki Engineering Co., Ltd Process for producing phosphatic fertilizer and apparatus therefor
WO2013175632A1 (en) 2012-05-25 2013-11-28 太平洋セメント株式会社 Method for producing phosphorous fertilizer
JP2016523790A (en) * 2013-05-03 2016-08-12 オウトテック (フィンランド) オサケ ユキチュアOutotec (Finland) Oy Method and plant for separating heavy metals from phosphorus starting materials

Cited By (7)

* 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
KR101277392B1 (en) * 2005-01-06 2013-06-20 산키 고교 가부시키가이샤 Process for producing phosphatic fertilizer and apparatus therefor
WO2013175632A1 (en) 2012-05-25 2013-11-28 太平洋セメント株式会社 Method for producing phosphorous fertilizer
JP2016523790A (en) * 2013-05-03 2016-08-12 オウトテック (フィンランド) オサケ ユキチュアOutotec (Finland) Oy Method and plant for separating heavy metals from phosphorus starting materials
US10081545B2 (en) 2013-05-03 2018-09-25 Outotec (Finland) Oy Process and plant for separating heavy metals from phosphoric starting material

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