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JP2001029998A - Phosphorus immobilization method - Google Patents

Phosphorus immobilization method

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Publication number
JP2001029998A
JP2001029998A JP11206940A JP20694099A JP2001029998A JP 2001029998 A JP2001029998 A JP 2001029998A JP 11206940 A JP11206940 A JP 11206940A JP 20694099 A JP20694099 A JP 20694099A JP 2001029998 A JP2001029998 A JP 2001029998A
Authority
JP
Japan
Prior art keywords
phosphorus
adjustment index
melting
index ratio
immobilizing
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.)
Granted
Application number
JP11206940A
Other languages
Japanese (ja)
Other versions
JP3926065B2 (en
Inventor
Hideki Iwabe
秀樹 岩部
Norihiro Koide
典宏 小出
Takashi Tamura
隆 田村
Seiji Tateishi
政治 立石
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.)
Kubota Corp
Original Assignee
Kubota Corp
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 Kubota Corp filed Critical Kubota Corp
Priority to JP20694099A priority Critical patent/JP3926065B2/en
Publication of JP2001029998A publication Critical patent/JP2001029998A/en
Application granted granted Critical
Publication of JP3926065B2 publication Critical patent/JP3926065B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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

Abstract

(57)【要約】 【課題】 強還元雰囲気での溶融時にリンを揮散させる
ことなくスラグ中に固定できるリン固定化方法を提供す
る。 【解決手段】 前処理した溶融対象物を溶融炉において
強還元雰囲気中で溶融スラグ化して、溶融対象物に含ま
れたリンをスラグ中もしくは溶融時に還元生成する金属
中に固定化するリン固定化方法であって、前処理におい
て、溶融処理温度で揮散するリンをリン化物として固定
化する金属元素の濃度と、酸性酸化物を生成する酸性酸
化物形成元素の濃度との比を調整指標比Rとし、調整指
標比Rが所定の下限値以上となるように溶融対象物の成
分調整を行なう。
(57) [Problem] To provide a method for immobilizing phosphorus which can be immobilized in slag without volatilizing phosphorus during melting in a strong reducing atmosphere. SOLUTION: Phosphorus immobilization in which a pretreated melting object is melted in a melting furnace in a strong reducing atmosphere to fix phosphorus contained in the melting object in the slag or in a metal that is reduced and generated during melting. In the pretreatment, the ratio between the concentration of the metal element for immobilizing phosphorus volatilized at the melting treatment temperature as a phosphide and the concentration of the acidic oxide forming element for producing an acidic oxide is adjusted by the adjustment index ratio R The component adjustment of the object to be melted is performed so that the adjustment index ratio R is equal to or greater than a predetermined lower limit.

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、産業廃
棄物等の溶融対象物に含まれるリンをスラグ中もしくは
溶融時に還元生成する金属中に固定するリン固定化方法
に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for immobilizing phosphorus contained in an object to be melted, such as sewage sludge or industrial waste, in slag or in a metal that is reduced and generated during melting.

【0002】[0002]

【従来の技術】従来、下水汚泥等を溶融炉で溶融すると
リンが揮散するので、リンをスラグ中に固定化すること
を目的として溶融対象物の成分を調整する方法がある。
この成分調整方法は、溶融対象物中に含まれる酸性酸化
物形成元素であるPとSiの濃度と、塩基性酸化物形成
元素であるCaとFeとAlの濃度との比を酸塩基比と
して導出し、酸塩基比の最低必要限度の下限値を予め経
験則として求め、酸塩基比がこの下限値以上となるよう
に溶融対象物の成分調整を行うものである。
2. Description of the Related Art Conventionally, phosphorus is volatilized when sewage sludge or the like is melted in a melting furnace. Therefore, there is a method of adjusting the components of a melting target in order to fix phosphorus in slag.
This component adjusting method uses the ratio of the concentration of P and Si, which are the acidic oxide-forming elements contained in the object to be melted, and the concentration of Ca, Fe, and Al, which are the basic oxide-forming elements, as an acid-base ratio. The lower limit of the minimum necessary limit of the acid-base ratio is determined in advance as an empirical rule, and the components of the object to be melted are adjusted so that the acid-base ratio is equal to or more than the lower limit.

【0003】[0003]

【発明が解決しようとする課題】しかしながら、上記の
方法においては、溶融炉が比較的還元度の強い溶融雰囲
気である場合に、CaやAlがリン固定化作用を示さな
い場合があり、酸塩基比に基づいた成分調整によっては
十分なリン固定化の効果を得ることができない場合があ
る。これは還元度の強い還元雰囲気で溶融する場合に
は、酸化雰囲気で溶融する場合よりもリンは揮散しやす
くなるためである。
However, in the above-mentioned method, when the melting furnace is in a melting atmosphere having a relatively high degree of reduction, Ca and Al may not exhibit the phosphorus immobilizing action in some cases. Depending on the component adjustment based on the ratio, a sufficient effect of immobilizing phosphorus may not be obtained. This is because phosphorus is more likely to volatilize when melting in a reducing atmosphere having a high degree of reduction than when melting in an oxidizing atmosphere.

【0004】例えば、リンは下水汚泥中には固形物あた
り2〜3%、下水汚泥焼却灰中には5〜10数%含まれ
ており、これらを溶融処理した場合、溶融対象物中のリ
ンの一部が気体として揮散し、排ガス中に移行したリン
が溶融炉の後段に設けた熱交換器や排煙処理設備で凝縮
して析出し、設備の腐食やダストの肥大堅固化を招き、
この結果、機器破損等の不具合を起こし、溶融設備の運
転に支障を来す可能性がある。また、リンを含んだ排ガ
スを湿式洗浄し、洗浄排水を返流水として水処理系に戻
した場合の悪影響も懸念される。
For example, sewage sludge contains 2 to 3% of solids per solid and sewage sludge incineration ash contains 5 to 10% by weight. Part of the gas is volatilized as gas, and the phosphorus that has migrated into the exhaust gas is condensed and deposited in the heat exchanger and flue gas treatment equipment provided at the later stage of the melting furnace, causing corrosion of the equipment and enlargement and solidification of dust,
As a result, there is a possibility that troubles such as breakage of the equipment may occur and hinder the operation of the melting facility. In addition, there is a concern about the adverse effect when the exhaust gas containing phosphorus is wet-washed and the washing wastewater is returned to the water treatment system as return water.

【0005】本発明は、強還元雰囲気での溶融時にリン
を揮散させることなくスラグ中もしくは溶融時に還元生
成する金属中に固定できるリン固定化方法を提供するこ
とを目的とするものである。
An object of the present invention is to provide a method for immobilizing phosphorus which can be immobilized in slag or in a metal which is reduced and generated during melting without evaporating phosphorus during melting in a strong reducing atmosphere.

【0006】[0006]

【課題を解決するための手段】上記課題を解決するため
に本発明のリン固定化方法は、前処理した溶融対象物を
溶融炉において強還元雰囲気中で溶融スラグ化して、溶
融対象物に含まれたリンをスラグ中もしくは溶融時に還
元生成する金属中に固定化するリン固定化方法であっ
て、前処理において、溶融処理温度で揮散するリンをリ
ン化物として固定化する金属元素の濃度と、酸性酸化物
を生成する酸性酸化物形成元素の濃度との比を調整指標
比Rとし、調整指標比Rが所定の下限値以上となるよう
に溶融対象物の成分調整を行なうものである。
According to the present invention, there is provided a method for immobilizing phosphorus, comprising: converting a pretreated molten object into a molten slag in a strong reducing atmosphere in a melting furnace; A method for immobilizing phosphorus in slag or in a metal that is reduced and generated during melting, wherein the concentration of a metal element for immobilizing phosphorus that volatilizes at a melting treatment temperature as a phosphide in a pretreatment, The ratio of the concentration of the acidic oxide-forming element that forms the acidic oxide to the concentration is referred to as an adjustment index ratio R, and the components of the object to be melted are adjusted such that the adjustment index ratio R is equal to or greater than a predetermined lower limit.

【0007】上記した構成において、溶融炉では酸塩基
反応と酸化還元反応が生じ、酸塩基反応において溶融対
象物中の酸性酸化物(SiO2 ,P25等)が塩基性酸
化物(CaO等)と反応して塩をつくり、酸性酸化物は
その含有割合が多くなるにしたがって、塩基性酸化物と
塩を形成できない割合が増える。この酸性酸化物の増加
がP25の遊離を促し、P25は酸化還元反応において
単体リンとして揮散する。特に強還元雰囲気では酸化還
元反応が速やかに進む。
In the above configuration, an acid-base reaction and an oxidation-reduction reaction occur in the melting furnace, and in the acid-base reaction, acidic oxides (SiO 2 , P 2 O 5, etc.) in the object to be melted are converted into basic oxides (CaO 2 ). ) To form a salt, and as the content ratio of the acidic oxide increases, the ratio at which a salt cannot be formed with the basic oxide increases. This increase in acidic oxide encourage free P 2 O 5, P 2 O 5 is volatilized as a single phosphorus in a redox reaction. In particular, in a strong reducing atmosphere, the oxidation-reduction reaction proceeds rapidly.

【0008】溶融炉においては溶融対象物中の炭素成分
や主燃焼室中の一酸化炭素が還元剤として作用し、リン
揮散を引き起こす。この還元剤として作用する炭素は溶
融対象物中の金属成分(鉄化合物等)を金属(鉄)にま
で還元し、還元生成した金属(鉄)が単体リンとして遊
離したリンをリン化合物(リン化鉄)として金属中に固
定する。つまり強還元雰囲気における溶融では、PやS
i等の酸性酸化物がリン揮散に作用し、Fe等の金属が
リン固定化に作用する。
[0008] In the melting furnace, the carbon component in the object to be melted and carbon monoxide in the main combustion chamber act as a reducing agent, causing phosphorus volatilization. The carbon acting as a reducing agent reduces a metal component (eg, an iron compound) in the object to be melted to a metal (iron), and converts the reduced metal (iron) released as a simple substance to a phosphorus compound (phosphorization). Fix it in metal as iron). In other words, in melting in a strong reducing atmosphere, P or S
An acidic oxide such as i acts on phosphorus volatilization, and a metal such as Fe acts on phosphorus immobilization.

【0009】この金属元素の濃度と酸性酸化物形成元素
の濃度との比は、リン固定化率と相関を有するので、調
整指標比Rを指標として溶融対象物の成分調整を行うこ
とで、溶融時のリン揮散を抑制できる。また、本発明の
リン固定化方法は、リンを固定化する金属元素をFeと
し、酸性酸化物を生成する酸性酸化物形成元素をPおよ
びSiとして、調整指標比R1=Fe/(P+Si)
[mol/mol]を導出し、溶融対象物中に含まれた
リンを固定化するに必要な調整指標比R1の下限値を経
験則として予め求め、調整指標比R1が前記下限値以上
となるように、鉄化合物を成分調整剤として溶融対象物
の成分調整を行なうものである。
The ratio between the concentration of the metal element and the concentration of the acidic oxide-forming element has a correlation with the phosphorus immobilization ratio. Phosphorus volatilization at the time can be suppressed. Further, in the method of immobilizing phosphorus of the present invention, the metal element for immobilizing phosphorus is Fe, the element for forming an acidic oxide that forms an acidic oxide is P and Si, and the adjustment index ratio R1 = Fe / (P + Si)
[Mol / mol] is derived, and the lower limit value of the adjustment index ratio R1 necessary for immobilizing phosphorus contained in the object to be melted is determined in advance as an empirical rule, and the adjustment index ratio R1 is equal to or more than the lower limit value. As described above, the components of the object to be melted are adjusted using an iron compound as a component adjusting agent.

【0010】より好ましくは、調整指標比1の下限値を
0.2に設定するものである。また、本発明のリン固定
化方法は、リンを固定化する金属元素をFeとし、酸性
酸化物を生成する酸性酸化物形成元素をSiとして、調
整指標比R2=Fe/Si[mol/mol]を導出
し、溶融対象物中に含まれたリンを固定化するに必要な
調整指標比R2の下限値を経験則として予め求め、調整
指標比R2が前記下限値以上となるように、鉄化合物を
成分調整剤として溶融対象物の成分調整を行なうもので
ある。
[0010] More preferably, the lower limit value of the adjustment index ratio 1 is set to 0.2. Further, in the method for immobilizing phosphorus of the present invention, an adjustment index ratio R2 = Fe / Si [mol / mol], where Fe is a metal element for immobilizing phosphorus and Si is an element for forming an acidic oxide that generates an acidic oxide. Is derived, and the lower limit value of the adjustment index ratio R2 necessary for immobilizing phosphorus contained in the melting target is determined in advance as an empirical rule, and the iron compound is adjusted so that the adjustment index ratio R2 is equal to or more than the lower limit value. Is used as a component adjuster to adjust the components of the object to be melted.

【0011】より好ましくは、調整指標比R2の下限値
を0.3に設定するものである。また、本発明のリン固
定化方法は、成分調整剤の少なくとも一部は、溶融対象
物が発生する処理工程において、その処理に必要な機能
を果たす薬剤として添加するものである。上記した構成
により、溶融対象物が発生する処理工程、例えば汚泥脱
水工程、汚泥消化工程、濃縮工程、汚泥送泥工程、ある
いは汚泥を発生する水処理工程などにおいて薬剤として
添加する鉄化合物等は溶融対象物中に残留しているの
で、これらを成分調整剤の一部として利用することで、
溶融工程の導入部で成分調整剤として添加する化合物量
を低減できる。
[0011] More preferably, the lower limit of the adjustment index ratio R2 is set to 0.3. In the method of immobilizing phosphorus according to the present invention, at least a part of the component adjusting agent is added as a chemical agent that performs a function necessary for the processing in a processing step in which an object to be melted is generated. With the above-described configuration, the iron compound or the like added as a chemical in a treatment step in which a melting target is generated, such as a sludge dewatering step, a sludge digestion step, a concentration step, a sludge feeding step, or a water treatment step in which sludge is generated, is melted. Since these remain in the object, by using them as part of the component adjuster,
It is possible to reduce the amount of the compound to be added as the component adjuster in the introduction part of the melting step.

【0012】[0012]

【発明の実施の形態】以下、本発明の実施の形態を下水
汚泥溶融プロセスを例に説明する。下水汚泥溶融プロセ
スは、溶融対象物である汚泥中の無機分を約1300〜
1400℃で加熱溶融する点で乾式リン製造法と共通し
ており、乾式リン製造時と同様の以下の反応の結果とし
てリンが揮散していると考えられる。
BEST MODE FOR CARRYING OUT THE INVENTION Hereinafter, embodiments of the present invention will be described using a sewage sludge melting process as an example. The sewage sludge melting process reduces the inorganic content of the sludge to be melted to about 1300-
It is common to the dry phosphorus production method in that it is heated and melted at 1400 ° C., and it is considered that phosphorus is volatilized as a result of the following reaction similar to that in the dry phosphorus production.

【0013】[0013]

【化1】 (1)式の反応は、以下の(2)式の酸塩基反応と
(3)式の酸化還元反応との連続反応と解釈できる。こ
の反応の結果、リンはP4の形態で気体として揮散し、
溶融プロセスの後工程で冷却されて単体リンとして析出
する。
Embedded image The reaction of the formula (1) can be interpreted as a continuous reaction of the acid-base reaction of the following formula (2) and the oxidation-reduction reaction of the formula (3). The result of this reaction, phosphorus volatilized as gas in the form of P 4,
It is cooled in a later step of the melting process and precipitates as elementary phosphorus.

【0014】[0014]

【化2】 Embedded image

【0015】[0015]

【化3】 (2)式の酸塩基反応において、SiO2やP25の酸
性酸化物はO2-を受容する酸として作用し、CaO等の
2-を供与する塩基性酸化物と塩をつくる。この酸性酸
化物の含有割合が多くなると、P25はCaO等の塩基
性酸化物と塩を形成できない割合が増え、P25は遊離
するようになる。遊離したP25は引き続き起こる
(3)式の酸化還元反応によりP4として揮散するの
で、酸性酸化物の増加はリン揮散に作用する。特に強還
元雰囲気のように、(3)式の酸化還元反応が速やかに
進むような条件下では、(2)式の平衡は右向きの反応
が主となる。
Embedded image (2) in an acid base reaction formula, acidic oxide of SiO 2 and P 2 O 5 acts as an acid for receiving the O 2-, make basic oxides and salts of donating O 2- such as CaO . If the content of the acidic oxide increases, P 2 O 5 is increased proportion of not form a basic oxide and salts, such as CaO, P 2 O 5 is as free. Since the released P 2 O 5 is volatilized as P 4 by the subsequent oxidation-reduction reaction of the formula (3), the increase in the amount of acidic oxides affects the volatilization of phosphorus. In particular, under conditions where the oxidation-reduction reaction of equation (3) proceeds rapidly, such as in a strong reducing atmosphere, the equilibrium of equation (2) is mainly a rightward reaction.

【0016】(3)式の反応では炭素が還元剤として作
用しているが、汚泥溶融炉においては汚泥中の炭素成分
や主燃焼室中の一酸化炭素が還元剤として作用し、リン
揮散を引き起こす。この還元剤として作用する炭素は、
以下の(4)式の反応により汚泥中の鉄を金属鉄まで還
元するが、還元生成した金属鉄は(5)式の反応により
単体リンとして遊離したリンをリン化鉄として金属中に
固定する。
In the reaction of the formula (3), carbon acts as a reducing agent. However, in a sludge melting furnace, carbon components in the sludge and carbon monoxide in the main combustion chamber act as a reducing agent, and the phosphorus volatilizes. cause. The carbon acting as this reducing agent is
The iron in the sludge is reduced to metallic iron by the reaction of the following formula (4), and the reduced metallic iron is fixed in the metal as iron phosphide by liberating the phosphorus released as a simple phosphorus by the reaction of the formula (5). .

【0017】[0017]

【化4】 Embedded image

【0018】[0018]

【化5】 つまり強還元雰囲気における溶融では、PやSiの酸性
酸化物がリン揮散に作用し、Feがリン固定化に主に作
用する。このため、所定の溶融温度でリン揮散に作用す
る酸性酸化物形成元素としてPとSiを、揮散したリン
を固定化する金属元素としてFeを取り上げ、各々の濃
度を分母と分子に取り、Fe/(P+Si)で表わされ
る調整指標比R1と、Fe/Siで表される調整指標比
R2を導出した。
Embedded image That is, in melting in a strong reducing atmosphere, acidic oxides of P and Si act on phosphorus volatilization, and Fe mainly acts on phosphorus immobilization. For this reason, P and Si are taken up as acid oxide forming elements acting on phosphorus volatilization at a predetermined melting temperature, and Fe is taken up as a metal element for immobilizing the volatilized phosphorus, and the respective concentrations are taken as a denominator and a molecule, and Fe / An adjustment index ratio R1 expressed by (P + Si) and an adjustment index ratio R2 expressed by Fe / Si were derived.

【0019】これらの調整指標比R1、R2を下水汚泥
に対して適用し、調整指標比R1、R2とリン固定化率
の関係を調べてみると、リン固定化率は両指標と正の相
関があり、このことから、調整指標比R1、R2を指標
として溶融対象物の成分調整を行うことで、溶融時のリ
ン揮散を抑制できる。このとき下限値として調整指標比
R1は0.2を、調整指標比R2は0.3を設定するの
が適当である。なおリン固定化率は、{(スラグ中のリ
ン濃度×スラグ重量)+(金属中のリン濃度×金属重
量)}として算出した。
By applying these adjustment index ratios R1 and R2 to sewage sludge and examining the relationship between the adjustment index ratios R1 and R2 and the phosphorus immobilization rate, the phosphorus immobilization rate has a positive correlation with both indices. Accordingly, by adjusting the components of the object to be melted using the adjustment index ratios R1 and R2 as an index, phosphorus volatilization during melting can be suppressed. At this time, it is appropriate to set the adjustment index ratio R1 to 0.2 and the adjustment index ratio R2 to 0.3 as the lower limit. The phosphorus immobilization rate was calculated as {(phosphorus concentration in slag × slag weight) + (phosphorus concentration in metal × metal weight)}.

【0020】以上のことは、以下に実施例として示す試
験において、 1)還元雰囲気が強くなるほどスラグ内に生成する金属
の量が増え、同時にリン固定化率が低下したこと、 2)リン固定化率は被溶融物中のリンの形態には依存し
ないこと、 3)弱還元雰囲気ではリン固定化にはCaとFeとAl
の各元素の含有量の増加が効果があるが、強還元雰囲気
ではリン固定化にはFeの含有量の増加のみが効果を示
すことでも裏付けられた。
The above results are shown in the following test examples: 1) As the reducing atmosphere becomes stronger, the amount of metal generated in the slag increases, and at the same time, the phosphorus immobilization rate decreases; The rate does not depend on the form of phosphorus in the material to be melted. 3) Ca, Fe and Al are used for immobilizing phosphorus in a weak reducing atmosphere.
The increase in the content of each element is effective, but it was also supported by the fact that only the increase in the Fe content was effective in immobilizing phosphorus in a strong reducing atmosphere.

【0021】(実施例)下水汚泥の溶融処理を模倣して
以下のようにしてスラグを生成させ、スラグへのリン固
定化率を調べた。
Example A slag was produced as follows by imitating the melting treatment of sewage sludge, and the phosphorus immobilization rate on the slag was examined.

【0022】[0022]

【表1】 上記の表1に示した組成を有する高分子系流動焼却灰
(下水汚泥焼却灰)に、汚泥中の有機分を想定して炭素
粉末を20重量%添加して、原灰とした。この原灰に金
属試薬Fe23、Ca(OH)2、Al23を等モル量
添加して、試料1、試料2、試料3を調整した。
[Table 1] Raw polymer ash (sewage sludge incineration ash) having the composition shown in Table 1 was added with 20% by weight of carbon powder assuming organic components in the sludge to obtain raw ash. Samples 1, 2, and 3 were prepared by adding equimolar amounts of metal reagents Fe 2 O 3 , Ca (OH) 2 , and Al 2 O 3 to the raw ash.

【0023】開口部直径52mm、高さ67mm、容量
90mLのアルミナ製るつぼAと開口部直径88mm、
高さ72mm、容量280mLのアルミナ製るつぼB
に、原灰および各試料を秤量後、容量まで充填し、小型
電気炉にて1400℃で4時間溶融した。2つのるつぼ
A、Bは、高さはほぼ同じであるが、開口部直径がるつ
ぼAの方が小さく、るつぼAの形状は縦長となる。
An alumina crucible A having an opening diameter of 52 mm, a height of 67 mm, and a capacity of 90 mL, an opening diameter of 88 mm,
Alumina crucible B with height of 72 mm and capacity of 280 mL
After weighing the raw ash and each sample, the mixture was filled to capacity and melted at 1400 ° C. for 4 hours in a small electric furnace. The two crucibles A and B have substantially the same height, but the crucible A has a smaller opening diameter and the crucible A has a vertically long shape.

【0024】得られた各スラグの重量を測定するととも
に、溶融前および溶融後の原灰および各試料のリン濃度
を、微粉砕して酸分解したものについてモリブデン(ア
スコルビン酸)吸光光度法により測定した。また、原灰
および各試料について、リン固定化率、すなわち{(ス
ラグ中のリン濃度×スラグ重量)+(金属中のリン濃度
×金属重量)}を算出した。なお溶融時、各るつぼA、
Bにおける溶融雰囲気の還元度が強くなるほどに、各る
つぼA、Bの底部に金属が分離するので、分離された金
属重量割合[金属重量/(金属重量+スラグ重量)]も
併せて算出し、各るつぼA、Bの内部の酸化還元強度の
目安とした。
The weight of each of the obtained slags is measured, and the phosphorus concentration of the raw ash before and after melting and of each sample is measured by a molybdenum (ascorbic acid) absorption spectrophotometric method for the finely pulverized and acid-decomposed materials. did. For the raw ash and each sample, the phosphorus immobilization rate, that is, {(phosphorus concentration in slag × slag weight) + (phosphorus concentration in metal × metal weight)} was calculated. When melting, each crucible A,
As the degree of reduction of the melting atmosphere in B increases, the metal separates at the bottom of each of the crucibles A and B, so the weight ratio of the separated metal [metal weight / (metal weight + slag weight)] is also calculated. It was used as a measure of the oxidation-reduction strength inside each of the crucibles A and B.

【0025】原灰および各試料について、調整指標比R
1:Fe/(P+Si)、調整指標比R2:Fe/Si
比、(3Ca+2Fe+Al)/(3P+2Si)[m
ol/mol]で定義する酸塩基比、るつぼAとるつぼ
Bでのリン固定化率および金属重量割合を表2に示す。
For the raw ash and each sample, the adjustment index ratio R
1: Fe / (P + Si), adjustment index ratio R2: Fe / Si
Ratio, (3Ca + 2Fe + Al) / (3P + 2Si) [m
Table 2 shows the acid-base ratio, the phosphorus immobilization ratio in the crucible A and the crucible B, and the metal weight ratio defined by [mol / mol].

【0026】[0026]

【表2】 表2により明らかなように、同一試料ではるつぼAでの
溶融は、るつぼBに比べ金属重量割合が高くなってお
り、このことはるつぼAではるつぼBより強い還元雰囲
気が再現できたことを示している。各るつぼでA、Bの
リン固定化率は試料1を除きいずれもるつぼAの方が大
幅に低い結果となった。
[Table 2] As is clear from Table 2, the melting in the crucible A was higher in the same sample than in the crucible B, indicating that a stronger reducing atmosphere could be reproduced in the crucible A than in the crucible B. ing. In each of the crucibles, except for the sample 1, the phosphorus immobilization ratios of A and B were much lower in the crucible A.

【0027】金属試薬添加の効果は、溶融雰囲気が弱還
元度となるるつぼBでの溶融実験では、Ca,Fe,A
lいずれの金属試薬の添加でも原灰よりリン固定化率は
上がり、酸塩基比の増加に伴うリン固定化率の向上が確
認された。一方、溶融雰囲気が強還元度となるるつぼB
での溶融実験では、Feのみがリン固定効果を示した。
つまり、Fe23の添加により、調整指標比R1は0.
17から0.49に上がり、調整指標比R2は0.25
から0.71に上がり、強還元雰囲気でリンが揮散しに
くい性状となった。
The effect of the addition of the metal reagent is as follows. In a melting experiment using a crucible B in which the melting atmosphere has a weak reduction degree, Ca, Fe, A
l The addition of any metal reagent increased the phosphorus immobilization rate compared to the raw ash, and it was confirmed that the phosphorus immobilization rate increased with an increase in the acid-base ratio. On the other hand, a crucible B in which the melting atmosphere has a strong reduction degree
In the melting experiment at, only Fe showed the phosphorus fixing effect.
That is, the addition of Fe 2 O 3 reduces the adjustment index ratio R1 to 0.1.
From 17 to 0.49, the adjustment index ratio R2 is 0.25
From 0.71 to 0.71 and became a property in which phosphorus hardly volatilized in a strong reducing atmosphere.

【0028】様々な試料についてるつぼAを用いて溶融
した結果について、調整指標比R1および調整指標比R
2とリン固定化率の関係を図1および図2に示す。図1
および図2の各曲線Cより明らかなように、調整指標比
R1および調整指標比R2とリン固定化率には正の相関
が見られ、調整指標比R1:0.2以上、調整指標比R
2:0.3以上でリン固定化率が大幅に上がる結果とな
った。
With respect to the results of melting various samples using crucible A, adjustment index ratio R1 and adjustment index ratio R
1 and 2 show the relationship between No. 2 and the phosphorus immobilization ratio. FIG.
2 and each curve C in FIG. 2, there is a positive correlation between the adjustment index ratio R1 and the adjustment index ratio R2 and the phosphorus immobilization rate, and the adjustment index ratio R1: 0.2 or more and the adjustment index ratio R
When the ratio was 2: 0.3 or more, the phosphorus immobilization ratio was significantly increased.

【0029】これらの結果から、強還元雰囲気での溶融
では、溶融対象物の調整指標比R1または調整指標比R
2を調整することによって、溶融時のリン挙動を制御で
きることが分かる。つまり、溶融時のリン揮散を抑制す
るには、調整指標比R1または調整指標比R2が適当な
値になるように鉄化合物を添加するのが効果的である。
From these results, when melting in a strong reducing atmosphere, the adjustment index ratio R1 or the adjustment index ratio R
It can be seen that by adjusting 2, phosphorus behavior during melting can be controlled. That is, it is effective to add the iron compound so that the adjustment index ratio R1 or the adjustment index ratio R2 has an appropriate value in order to suppress the phosphorus volatilization during melting.

【0030】このようにしてリン揮散を抑制できる結
果、排ガスへのリン移行を抑制でき、リンに起因する熱
交換器や排煙処理設備での問題を解消し、溶融施設全体
の安定運転を図ることができる。実際の下水汚泥の溶融
処理に当たって成分調整を行うには、溶融対象物が発生
する処理工程、例えば汚泥脱水工程で鉄系の脱水助剤を
添加したり、汚泥が発生する水処理工程で凝集剤として
鉄塩を添加するなど、その処理工程で必要な薬剤として
鉄化合物を選択することで、これらを成分調整剤の一部
として利用することができ、溶融工程の導入部で成分調
整剤として添加する化合物量を低減できる。
As a result of suppressing phosphorus volatilization in this way, transfer of phosphorus to exhaust gas can be suppressed, problems in a heat exchanger and a flue gas treatment facility caused by phosphorus can be solved, and stable operation of the entire melting facility can be achieved. be able to. In order to perform the component adjustment in the actual melting treatment of sewage sludge, it is necessary to add an iron-based dehydration aid in a treatment process in which a melting target is generated, for example, in a sludge dewatering process, or in a coagulant in a water treatment process in which sludge is generated. By selecting an iron compound as a necessary chemical in the treatment process, such as adding an iron salt, these can be used as a part of a component adjuster and added as a component adjuster in the introduction part of the melting process The amount of the compound to be used can be reduced.

【0031】本発明のリン固定化方法は、上記したよう
な下水汚泥焼却灰、下水汚泥の他、産業廃棄物など、リ
ンを含んだその他の溶融対象物にも実施できる。
The method for immobilizing phosphorus of the present invention can be carried out on other sewage sludge incineration ash and sewage sludge as described above, as well as on other molten objects containing phosphorus, such as industrial waste.

【0032】[0032]

【発明の効果】以上のように本発明によれば、リンをリ
ン化物として固定化する金属元素の濃度と、酸性酸化物
を生成する酸性酸化物形成元素の濃度との調整指標比R
が、所定値以上になるように溶融対象物の成分調整を行
うことにより、リンを揮散させることなくスラグ中もし
くは溶融時に還元生成する金属中に固定することがで
き、リン揮散による熱交換機や排煙処理設備の不具合を
防止し、溶融施設全体の安定運転を図ることができる。
As described above, according to the present invention, the adjustment index ratio R between the concentration of the metal element for immobilizing phosphorus as a phosphide and the concentration of the acidic oxide-forming element for forming an acidic oxide.
However, by adjusting the components of the object to be melted so as to be equal to or more than a predetermined value, phosphorus can be fixed in the slag or in the metal that is reduced and generated at the time of melting without volatilizing the phosphorus. Failures in the smoke treatment equipment can be prevented, and stable operation of the entire melting facility can be achieved.

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

【図1】本発明のリン固定化方法において、様々な組成
の下水汚泥試料について、調整指標比R1:Fe/(P
+Si)とスラグと金属中のリン固定化率との関係を示
したグラフである。
FIG. 1 shows an adjusted index ratio R1: Fe / (P) for sewage sludge samples having various compositions in the phosphorus immobilization method of the present invention.
+ Si) is a graph showing the relationship between slag and the immobilization rate of phosphorus in the metal.

【図2】本発明のリン固定化方法において、様々な組成
の下水汚泥試料について、調整指標比R1:Fe/Si
とスラグと金属中のリン固定化率との関係を示したグラ
フである。
FIG. 2 shows a method for immobilizing phosphorus according to the present invention, in which sewage sludge samples having various compositions have adjustment index ratios R1: Fe / Si
4 is a graph showing the relationship between slag and the immobilization rate of phosphorus in metal.

【符号の説明】[Explanation of symbols]

C 相関を示す曲線 C Curve showing correlation

フロントページの続き (72)発明者 田村 隆 大阪府大阪市浪速区敷津東一丁目2番47号 株式会社クボタ内 (72)発明者 立石 政治 福岡県小郡市大板井56−1 Fターム(参考) 4D004 AA02 AA46 AB05 AC04 CA29 CA45 CB02 CC11 DA03 DA10 4D059 AA19 BB04 BK30 DA05 DA19 DA22 DA64 EB11 Continued on the front page (72) Inventor Takashi Tamura 2-47 Shishitsu Higashi, Namiwa-ku, Osaka-shi, Osaka Kubota Co., Ltd. (72) Inventor Tateishi Politics 56-1 Oitai, Ogori-shi, Fukuoka F-term 4D004 AA02 AA46 AB05 AC04 CA29 CA45 CB02 CC11 DA03 DA10 4D059 AA19 BB04 BK30 DA05 DA19 DA22 DA64 EB11

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】 前処理した溶融対象物を溶融炉において
強還元雰囲気中で溶融スラグ化して、溶融対象物に含ま
れたリンをスラグ中もしくは溶融時に還元生成する金属
中に固定化するリン固定化方法であって、 前処理において、溶融処理温度で揮散するリンをリン化
物として固定化する金属元素の濃度と、酸性酸化物を生
成する酸性酸化物形成元素の濃度との比を調整指標比R
とし、調整指標比Rが所定の下限値以上となるように溶
融対象物の成分調整を行なうことを特徴とするリン固定
化方法。
1. A phosphorus fixing method in which a pretreated molten object is melted into a slag in a strong reducing atmosphere in a melting furnace, and phosphorus contained in the molten object is fixed in the slag or in a metal which is reduced and generated during melting. In the pretreatment, the ratio of the concentration of the metal element for immobilizing phosphorus volatilized at the melting treatment temperature as a phosphide to the concentration of the element for forming an acidic oxide that forms an acidic oxide is an adjustment index ratio. R
And adjusting the components of the object to be melted such that the adjustment index ratio R is equal to or greater than a predetermined lower limit.
【請求項2】 リンを固定化する金属元素をFeとし、
酸性酸化物を生成する酸性酸化物形成元素をPおよびS
iとして、調整指標比R1=Fe/(P+Si)[mo
l/mol]を導出し、溶融対象物中に含まれたリンを
固定化するに必要な調整指標比R1の下限値を経験則と
して予め求め、調整指標比R1が前記下限値以上となる
ように、鉄化合物を成分調整剤として溶融対象物の成分
調整を行なうことを特徴とする請求項1記載のリン固定
化方法。
2. The metal element for immobilizing phosphorus is Fe,
P and S are the acid oxide forming elements that form the acid oxide.
As i, the adjustment index ratio R1 = Fe / (P + Si) [mo
1 / mol], and the lower limit value of the adjustment index ratio R1 necessary for immobilizing phosphorus contained in the melting target is determined in advance as an empirical rule, so that the adjustment index ratio R1 is equal to or more than the lower limit value. 2. The method for immobilizing phosphorus according to claim 1, wherein the component of the object to be melted is adjusted using an iron compound as a component adjusting agent.
【請求項3】 調整指標比R1の下限値を0.2に設定
することを特徴とする請求項2記載のリン固定化方法。
3. The method for immobilizing phosphorus according to claim 2, wherein the lower limit of the adjustment index ratio R1 is set to 0.2.
【請求項4】 リンを固定化する金属元素をFeとし、
酸性酸化物を生成する酸性酸化物形成元素をSiとし
て、調整指標比R2=Fe/Si[mol/mol]を
導出し、溶融対象物中に含まれたリンを固定化するに必
要な調整指標比R2の下限値を経験則として予め求め、
調整指標比R2が前記下限値以上となるように、鉄化合
物を成分調整剤として溶融対象物の成分調整を行なうこ
とを特徴とする請求項1記載のリン固定化方法。
4. A metal element for immobilizing phosphorus is Fe,
The adjustment index ratio R2 = Fe / Si [mol / mol] is derived by setting the acid oxide forming element that generates the acid oxide as Si, and the adjustment index necessary for immobilizing phosphorus contained in the object to be melted. The lower limit of the ratio R2 is determined in advance as an empirical rule,
2. The method for immobilizing phosphorus according to claim 1, wherein the component adjustment of the object to be melted is performed using an iron compound as a component adjuster such that the adjustment index ratio R2 is equal to or more than the lower limit.
【請求項5】 調整指標比R2の下限値を0.3に設定
することを特徴とする請求項4記載のリン固定化方法。
5. The method for immobilizing phosphorus according to claim 4, wherein the lower limit value of the adjustment index ratio R2 is set to 0.3.
【請求項6】 成分調整剤の少なくとも一部は、溶融対
象物が発生する処理工程において、その処理に必要な機
能を果たす薬剤として添加することを特徴とする請求項
2および請求項4記載のリン固定化方法。
6. The method according to claim 2, wherein at least a part of the component adjusting agent is added as an agent which performs a function necessary for the processing in a processing step in which the object to be melted is generated. Phosphorus immobilization method.
JP20694099A 1999-07-22 1999-07-22 Phosphorus immobilization method Expired - Fee Related JP3926065B2 (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006015173A (en) * 2004-06-30 2006-01-19 Kubota Corp Sewage sludge melting treatment method
JP2015033691A (en) * 2013-07-09 2015-02-19 株式会社クボタ Melting treatment method of phosphorus-containing material and operation method of melting furnace
WO2016103474A1 (en) * 2014-12-26 2016-06-30 株式会社クボタ Method for melting treatment of phosphorus-containing substance and melting furnace operation method

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006015173A (en) * 2004-06-30 2006-01-19 Kubota Corp Sewage sludge melting treatment method
JP2015033691A (en) * 2013-07-09 2015-02-19 株式会社クボタ Melting treatment method of phosphorus-containing material and operation method of melting furnace
WO2016103474A1 (en) * 2014-12-26 2016-06-30 株式会社クボタ Method for melting treatment of phosphorus-containing substance and melting furnace operation method
EP3239108A4 (en) * 2014-12-26 2018-07-11 Kubota Corporation Method for melting treatment of phosphorus-containing substance and melting furnace operation method

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