JP2000109938A - Method for recovering valuable metal from fly ash - Google Patents
Method for recovering valuable metal from fly ashInfo
- Publication number
- JP2000109938A JP2000109938A JP27961798A JP27961798A JP2000109938A JP 2000109938 A JP2000109938 A JP 2000109938A JP 27961798 A JP27961798 A JP 27961798A JP 27961798 A JP27961798 A JP 27961798A JP 2000109938 A JP2000109938 A JP 2000109938A
- Authority
- JP
- Japan
- Prior art keywords
- fly ash
- hydrochloric acid
- acid solution
- valuable metals
- stage
- 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
Links
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
Landscapes
- Manufacture And Refinement Of Metals (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
Description
【０００１】[0001]
【発明の属する技術分野】本発明は、都市ごみや産業廃
棄物を燃焼又は溶融したときに生じる飛灰から鉛、亜
鉛、カルシウムなどの有価金属を回収する方法に関する
ものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for recovering valuable metals such as lead, zinc and calcium from fly ash generated when burning or melting municipal solid waste or industrial waste.
【０００２】[0002]
【従来の技術】これまで都市ごみや産業廃棄物を燃焼又
は溶融したときに生じる燃えがらや飛灰は、最終処分場
に堆積されていた。しかし近年最終処分場に堆積される
飛灰に含まれる鉛、亜鉛などの重金属やダイオキシン類
の有害性が社会問題化している。この問題を解決するた
めに、従来より飛灰から鉛、亜鉛などの有価金属を回収
する方法として、飛灰を硫酸、硝酸又は塩酸により処理
して金属を浸出した後、電解により金属を採取する方法
や、或いは浸出した金属を含む液を中和して沈殿させる
湿式製錬法が知られている。2. Description of the Related Art Hitherto, cinders and fly ash generated when municipal waste and industrial waste are burned or melted have been deposited at a final disposal site. However, in recent years, the harmfulness of heavy metals such as lead and zinc and dioxins contained in fly ash deposited at the final disposal site has become a social problem. In order to solve this problem, conventionally, as a method of recovering valuable metals such as lead and zinc from fly ash, the fly ash is treated with sulfuric acid, nitric acid or hydrochloric acid to extract the metal, and then the metal is collected by electrolysis. A method and a hydrometallurgical method in which a liquid containing leached metal is neutralized and precipitated are known.
【０００３】[0003]
【発明が解決しようとする課題】しかし、電解により金
属を採取する方法は、金属濃度が低いために電解効率が
悪く除去限界値が高い不具合がある。また上記硫酸で直
接飛灰を処理する場合には、飛灰にカルシウム成分が大
量に含まれていると、石膏が同時に大量に生成し、飛灰
に含まれる鉛が石膏ととに沈殿して鉛、シリカ、アルミ
ナを分離できない問題がある。また上記硝酸で飛灰を処
理する場合には、薬品代が高く、しかも最後の廃液中の
窒素の分解手段がないため、大量の飛灰の処理には不適
当である。更に上記塩酸で飛灰を処理する場合には、薬
品代は硝酸よりは安いが硫酸と比べると遥かに高く実用
化は困難である。塩酸での処理はカルシウムが溶け、不
溶性の鉛、シリカ、アルミナと分離できるので鉛以外の
有価金属を分離するには好適であるけれども、大量の塩
酸を使用する場合には大規模な廃水処理施設を必要とす
る。However, the method of collecting metal by electrolysis has a drawback in that since the metal concentration is low, the electrolysis efficiency is poor and the removal limit value is high. In the case of directly treating fly ash with the above sulfuric acid, if the fly ash contains a large amount of calcium, gypsum is simultaneously produced in large quantities, and the lead contained in the fly ash precipitates with the gypsum. There is a problem that lead, silica and alumina cannot be separated. Further, when fly ash is treated with the above-mentioned nitric acid, the cost of chemicals is high and there is no means for decomposing nitrogen in the final waste liquid. Furthermore, when fly ash is treated with the above-mentioned hydrochloric acid, the cost of chemicals is cheaper than that of nitric acid, but it is much higher than that of sulfuric acid, and practical use is difficult. Treatment with hydrochloric acid dissolves calcium and can be separated from insoluble lead, silica and alumina, so it is suitable for separating valuable metals other than lead, but when using a large amount of hydrochloric acid, a large-scale wastewater treatment facility Need.
【０００４】本発明の目的は、飛灰から有価金属を比較
的に安価にかつ効率よく回収する方法を提供することに
ある。本発明の別の目的は、飛灰から有価金属を回収す
る際に廃液の発生量が少なくて済み、廃水処理の負荷が
小さい方法を提供することにある。本発明の更に別の目
的は、飛灰中に含まれるカルシウム成分から高品質な石
膏を回収する方法を提供することにある。An object of the present invention is to provide a method for recovering valuable metals from fly ash relatively inexpensively and efficiently. Another object of the present invention is to provide a method that requires a small amount of waste liquid when recovering valuable metals from fly ash and has a small load on wastewater treatment. Still another object of the present invention is to provide a method for recovering high quality gypsum from calcium components contained in fly ash.
【０００５】[0005]
【課題を解決するための手段】請求項１に係る発明は、
図１に示すようにカルシウム成分と塩素成分と有価金属
を含む飛灰から前記有価金属を回収する方法において、
飛灰を塩酸酸性液で処理する第１工程１１と、この第１
工程の処理液をろ過し除滓する第２工程１２と、この第
２工程で除滓した液に硫酸を加えて反応させる第３工程
１３と、この第３工程の反応生成液をろ過して石膏と塩
酸酸性液を生成する第４工程１４とを含むことを特徴と
する。請求項２に係る発明は、請求項１に係る発明であ
って、第１工程１１で用いる塩酸酸性液が第４工程１４
で生成した塩酸酸性液の一部又は全部である飛灰からの
有価金属回収方法である。The invention according to claim 1 is
In the method of recovering valuable metals from fly ash containing calcium components, chlorine components and valuable metals as shown in FIG.
A first step 11 of treating fly ash with a hydrochloric acid acid solution;
A second step 12 for filtering and removing the treatment liquid in the step, a third step 13 for adding sulfuric acid to the liquid removed in the second step to cause a reaction, and filtering the reaction product liquid for the third step. A fourth step 14 for producing gypsum and a hydrochloric acid acid solution. The invention according to claim 2 is the invention according to claim 1, wherein the hydrochloric acid solution used in the first step 11 is used in the fourth step 14.
This is a method for recovering valuable metals from fly ash, which is a part or all of the hydrochloric acid solution produced in the above.
【０００６】請求項３に係る発明は、請求項２に係る発
明であって、第４工程１４で生成した塩酸酸性液を第１
工程１１で用いる前の塩酸酸性液の一部又は全部が、塩
酸水溶液であるか、或いは飛灰の一部と水とを混合する
ことにより生成したスラリーをろ過し除滓した液に硫酸
を加えて生成した塩酸酸性液である飛灰からの有価金属
回収方法である。請求項４に係る発明は、請求項１ない
し３いずれかに係る発明であって、第３工程１３で硫酸
を加える前に、処理液をろ過し除滓した液に種石膏を加
える飛灰からの有価金属回収方法である。[0006] The invention according to claim 3 is the invention according to claim 2, wherein the hydrochloric acid acid solution produced in the fourth step 14 is treated with the first acid solution.
Part or all of the hydrochloric acid solution before use in step 11 is a hydrochloric acid aqueous solution, or sulfuric acid is added to a solution obtained by filtering a slurry formed by mixing a part of fly ash and water and removing the slag. This is a method for recovering valuable metals from fly ash, which is a hydrochloric acid solution produced by the above method. The invention according to claim 4 is the invention according to any one of claims 1 to 3, wherein before the addition of sulfuric acid in the third step 13, the treatment liquid is filtered and fly ash is added to the liquid obtained by removing gypsum. Is a method for recovering valuable metals.
【０００７】請求項５に係る発明は、請求項１ないし４
いずれかに係る発明であって、第４工程１４で生成した
塩酸酸性液の一部に炭酸カルシウムを加えて中和する第
５工程１５と、この第５工程で中和した処理液に水酸化
カルシウム又は水酸化ナトリウムを加える第６工程１６
と、この第６工程で中和した処理液をろ過する第７工程
１７とを更に含む飛灰からの有価金属回収方法である。
請求項６に係る発明は、請求項１ないし５いずれかに係
る発明であって、第１工程で飛灰を処理する前に、飛灰
を５００℃以上の温度で加熱処理する第８工程１８を更
に含む飛灰からの有価金属回収方法である。[0007] The invention according to claim 5 is the invention according to claims 1 to 4.
The invention according to any one of the first to fifth aspects, wherein a fifth step 15 is performed by adding calcium carbonate to a part of the hydrochloric acid solution generated in the fourth step 14 to neutralize the solution, and Sixth step 16 of adding calcium or sodium hydroxide
And a seventh step 17 of filtering the treatment liquid neutralized in the sixth step.
The invention according to claim 6 is the invention according to any one of claims 1 to 5, wherein the fly ash is heat-treated at a temperature of 500 ° C. or more before the fly ash is treated in the first step. Is a method for recovering valuable metals from fly ash.
【０００８】[0008]
【発明の実施の形態】都市ごみや産業廃棄物の中には塩
化ビニール袋、プラスチック、塩等が存在し、これらを
燃焼又は溶融すると、塩素成分が蒸発する。また焼却炉
や溶融炉の煙道を通過する廃ガス中に含まれるダイオキ
シンや塩素成分を吸着除去するために、通常生石灰粉が
煙道に吹き込まれる。このためバグフィルタ等で回収さ
れた飛灰中には、塩素成分とカルシウム成分が含まれ
る。この実施の形態では飛灰にはカルシウム（Ｃａ）が
３０〜５０重量％、塩素（Ｃｌ）が１０〜２０重量％、
鉄（Ｆｅ）が０．５〜１．０重量％、銅（Ｃｕ）が０．
５〜１．０重量％、鉛（Ｐｂ）が１．０〜２．０重量
％、亜鉛（Ｚｎ）が５．０〜１５．０重量％含まれる。DESCRIPTION OF THE PREFERRED EMBODIMENTS Municipal waste and industrial waste contain vinyl chloride bags, plastics, salts and the like. When these are burned or melted, chlorine components evaporate. Normally, quick lime powder is blown into the flue to adsorb and remove dioxin and chlorine components contained in the waste gas passing through the flue of an incinerator or melting furnace. Therefore, fly ash collected by a bag filter or the like contains a chlorine component and a calcium component. In this embodiment, fly ash contains 30 to 50% by weight of calcium (Ca), 10 to 20% by weight of chlorine (Cl),
0.5% to 1.0% by weight of iron (Fe) and 0.1% of copper (Cu).
5 to 1.0% by weight, 1.0 to 2.0% by weight of lead (Pb), and 5.0 to 15.0% by weight of zinc (Zn).
【０００９】請求項１に係る発明では、図１に示す第１
工程１１で飛灰を塩酸酸性液で処理することにより、主
成分のカルシウムが溶けて鉛以外の重金属が溶出する一
方、鉛とシリカとアルミナの不溶な残渣を生じる。第２
工程１２で処理液をろ過することにより鉛残渣を分離す
ることができる。鉛残渣は鉛製錬工程２１で鉛として回
収される。また第３工程１３でこのろ過液に硫酸を加え
ることにより次式（１）により、 ＣａＣｌ2＋Ｈ2ＳＯ4→ＣａＳＯ4↓＋２ＨＣｌ ……… （１） 石膏と塩酸酸性液が生成される。ここで硫酸の代りに硝
酸を加えても塩酸酸性液は回収できるが、カルシウムが
硝酸カルシウムとなって溶解してしまうため、廃液処理
を行うことができなくなる。また硫酸の代りにシュウ酸
を用いる場合には薬品代が高価になり過ぎる。これらの
ことから硫酸を添加するのが最も良い。また硫酸を加え
るときにろ過液を４０〜６０℃に加熱すると、板状で大
きい良質な石膏が得られる。According to the first aspect of the present invention, the first type shown in FIG.
By treating the fly ash with the hydrochloric acid acid solution in the step 11, calcium as a main component is dissolved and heavy metals other than lead are eluted, while insoluble residues of lead, silica and alumina are generated. Second
In step 12, the residue of lead can be separated by filtering the treatment liquid. The lead residue is recovered as lead in the lead smelting process 21. Further, by adding sulfuric acid to this filtrate in the third step 13, CaCl 2 + H 2 SO 4 → CaSO 4 ↓ + 2HCl (1) gypsum and hydrochloric acid acid solution are produced by the following equation (1). Here, even if nitric acid is added instead of sulfuric acid, the acidic hydrochloric acid solution can be recovered, but since calcium is dissolved as calcium nitrate, waste liquid treatment cannot be performed. When oxalic acid is used instead of sulfuric acid, the cost of chemicals becomes too expensive. For these reasons, it is best to add sulfuric acid. Further, when the filtrate is heated to 40 to 60 ° C. when sulfuric acid is added, a large, high-quality gypsum in a plate shape is obtained.
【００１０】請求項２に係る発明では、第４工程１４で
生成した塩酸酸性液の一部又は全部が第１工程１１にフ
ィードバックされる。この実施の形態では工程１４で生
成した塩酸酸性液の８０重量％が工程１１にフィードバ
ックされ、残りの２０重量％が工程１５で用いられる。
第１工程１１で必要な塩酸酸性液を第４工程１４で自己
生成できるので、塩酸の薬品代が安価で済み、しかも塩
素の負荷が小さな環境に優しい廃水処理を行うことがで
きる。この塩酸酸性液をフィードバックする割合は塩酸
酸性液中の塩素成分とカルシウム成分の含有量に依存す
る。この塩酸酸性液のフィードバックにより第２回目以
降の飛灰の浸出がスムーズに進み、鉛残渣中の鉛の品位
が向上する。また工程１４で石膏を回収するため、鉛残
渣中のカルシウム成分が大幅に減って滓量も減少する。
回収した石膏は水で洗浄してもよい。なお、第４工程１
４で生成した塩酸酸性液を加熱蒸発させて、塩化水素ガ
スとして回収し、これを水に溶解して第１工程１１に供
給してもよい。請求項３に係る発明では、塩酸酸性液を
自己生成する前の飛灰処理用の塩酸酸性液には、図１の
破線で示すように新規な塩酸水溶液を用いる。別の方法
として、やはり図１の破線で示すように飛灰の一部と水
とを混合することにより飛灰に含まれているカルシウム
成分と塩素成分を十分に溶かして塩化カルシウム（Ｃａ
Ｃｌ2）水溶液を主成分とするスラリーを生成し、この
スラリーをろ過し除滓した液に硫酸を加えることによ
り、前述した式（１）により生成した塩酸酸性液を用い
る。この実施の形態では飛灰に対して液体を飛灰：液体
＝１：５（重量比）の割合で混合してスラリーを調製す
る。In the invention according to claim 2, a part or all of the hydrochloric acid acid solution generated in the fourth step 14 is fed back to the first step 11. In this embodiment, 80% by weight of the hydrochloric acid solution produced in Step 14 is fed back to Step 11, and the remaining 20% by weight is used in Step 15.
Since the required hydrochloric acid acid solution in the first step 11 can be self-generated in the fourth step 14, the cost of chemicals for hydrochloric acid can be reduced and environmentally friendly wastewater treatment with a small chlorine load can be performed. The rate at which the hydrochloric acid solution is fed back depends on the contents of the chlorine component and the calcium component in the hydrochloric acid solution. By the feedback of the hydrochloric acid acid solution, the leaching of fly ash from the second time onward proceeds smoothly, and the quality of lead in the lead residue is improved. In addition, since gypsum is collected in step 14, the calcium component in the lead residue is significantly reduced, and the amount of slag is also reduced.
The recovered gypsum may be washed with water. The fourth step 1
The hydrochloric acid solution produced in Step 4 may be heated and evaporated to recover hydrogen chloride gas, which may be dissolved in water and supplied to the first step 11. In the invention according to claim 3, a novel hydrochloric acid aqueous solution is used as the hydrochloric acid solution for fly ash treatment before the hydrochloric acid solution is self-generated, as shown by the broken line in FIG. As another method, as shown by the broken line in FIG. 1, a part of the fly ash is mixed with water to sufficiently dissolve the calcium component and the chlorine component contained in the fly ash, thereby obtaining calcium chloride (Ca).
A slurry mainly composed of an aqueous solution of Cl 2 ) is formed, and the slurry is filtered and the residue removed is added with sulfuric acid to use the hydrochloric acid acid solution generated by the above formula (1). In this embodiment, the slurry is prepared by mixing the liquid with the fly ash at a ratio of fly ash: liquid = 1: 5 (weight ratio).
【００１１】請求項４に係る発明では、微粒子の種石膏
を処理液に添加混合した後、硫酸を加えると種石膏から
石膏の結晶が効率良く成長し、高品質で大型の石膏を回
収することができる。請求項５に係る発明では、第４工
程１４で生成した塩酸酸性液のフィードバックを繰返す
ことにより、処理液中の亜鉛その他の金属の濃度が高ま
れば、循環液の一部を抜き出し、第５工程１５で塩酸酸
性液に炭酸カルシウムを加えて塩酸酸性液を次式（２）
に示すように中和する。工程１５の中和剤として炭酸カ
ルシウムを用いるのは、中和剤の薬品代が安価で済むた
めである。 ２ＨＣｌ＋ＣａＣＯ3→ＣａＣｌ2＋ＣＯ2＋Ｈ2Ｏ …… （２） 中和した処理液に更に第６工程１６で水酸化カルシウム
（Ｃａ(ＯＨ)2）又は水酸化ナトリウム（ＮａＯＨ）を
加えて塩酸酸性液を次式（３）に示すように更に中和す
る。工程１６の中和剤としてＣａ(ＯＨ)2又はＮａＯＨ
を用いるのは、亜鉛を水酸化物として濃縮して回収する
ためである。 ＺｎＣｌ2＋Ｃａ(ＯＨ)2→Ｚｎ(ＯＨ)2↓＋ＣａＣｌ2 … （３） 中和した処理液を第７工程１７でろ過することにより亜
鉛を含む残渣を回収することができる。この中和ろ液は
廃水処理工程１９で所定の水質基準に浄化されて放水さ
れる。亜鉛残渣は亜鉛製錬工程２２で亜鉛として回収さ
れる。請求項６に係る発明では、図１の破線で示すよう
に第８工程１８で本発明の飛灰原料を５００℃以上の温
度で加熱処理する。これにより飛灰中に含まれるダイオ
キシンを予め分解しておくことができる。According to the fourth aspect of the present invention, after adding and mixing fine gypsum to the treatment liquid and adding sulfuric acid, gypsum crystals can be efficiently grown from the gypsum and high quality large gypsum can be recovered. Can be. In the invention according to claim 5, by repeating the feedback of the hydrochloric acid solution generated in the fourth step 14, if the concentration of zinc or other metal in the processing liquid increases, a part of the circulating liquid is extracted and the fifth step is performed. In step 15, calcium carbonate is added to the hydrochloric acid acid solution to convert the hydrochloric acid acid solution into the following formula (2)
Neutralize as shown. The reason why calcium carbonate is used as the neutralizing agent in step 15 is that the chemical cost of the neutralizing agent can be reduced. 2HCl + CaCO 3 → CaCl 2 + CO 2 + H 2 O (2) Calcium hydroxide (Ca (OH) 2 ) or sodium hydroxide (NaOH) is further added to the neutralized treatment solution in the sixth step 16 to add a hydrochloric acid solution. Is further neutralized as shown in the following equation (3). Ca (OH) 2 or NaOH as a neutralizing agent in Step 16
Is used to concentrate and recover zinc as a hydroxide. ZnCl 2 + Ca (OH) 2 → Zn (OH) 2 ↓ + CaCl 2 (3) A residue containing zinc can be collected by filtering the neutralized treatment solution in the seventh step 17. This neutralized filtrate is purified to a predetermined water quality standard in a wastewater treatment step 19 and discharged. The zinc residue is recovered as zinc in the zinc smelting process 22. In the invention according to claim 6, the fly ash raw material of the present invention is heat-treated at a temperature of 500 ° C. or more in the eighth step 18, as shown by the broken line in FIG. Thereby, dioxin contained in fly ash can be decomposed in advance.
【００１２】[0012]
【実施例】次に本発明の実施例を比較例とともに説明す
る。 ＜実施例＞新規な塩酸水溶液を全く用いずに、生成した
塩酸酸性液を飛灰に３回繰返し加えて処理した。 (a) 塩酸酸性液の生成 先ず表１に示す有価金属と塩素を含む飛灰１００ｋｇ
に水５００リットルを加えて混合しスラリーを調製し
た。最初は塩酸を生成するためにこのスラリーに硫酸を
直接加えた。即ち、このスラリーに濃度９０重量％の硫
酸９５ｋｇを加えて混合した。この混合液をろ過して石
膏と滓の混合物１２６ｋｇ（乾燥重量）と塩酸酸性液５
０リットルを生成した。最初に生成された石膏の品質は
悪いため別途鉛製錬処理した。 (b) 生成した塩酸酸性液の飛灰への第１回混合 上記(a)で生成した塩酸酸性液５００リットルすべてを
新たな飛灰１００ｋｇに加えて混合してスラリーを調製
した。このスラリーをろ過し除滓した液に濃度９０重量
％の硫酸９５ｋｇを加えて混合した。この混合液をろ過
して石膏１０１ｋｇ（乾燥重量）と塩酸酸性液５００リ
ットルを生成した。 (c) 生成した塩酸酸性液の飛灰への第２回混合 上記(b)で生成した塩酸酸性液４４０リットルと水７２
リットルを新たな飛灰１００ｋｇに加えて混合してスラ
リーを調製した。このスラリーをろ過し除滓した液に濃
度９０重量％の硫酸９５ｋｇを加えて混合した。この混
合液をろ過して石膏１１５ｋｇ（乾燥重量）と塩酸酸性
液５００リットルを生成した。Next, examples of the present invention will be described together with comparative examples. <Example> Without using a novel hydrochloric acid aqueous solution at all, the generated hydrochloric acid acid solution was repeatedly added to the fly ash three times for treatment. (a) Formation of hydrochloric acid acid solution First, 100 kg of fly ash containing valuable metals and chlorine shown in Table 1
Was mixed with 500 l of water to prepare a slurry. Initially, sulfuric acid was added directly to the slurry to produce hydrochloric acid. That is, 95 kg of sulfuric acid having a concentration of 90% by weight was added to the slurry and mixed. The mixture was filtered to obtain 126 kg (dry weight) of a mixture of gypsum and slag and a hydrochloric acid acid solution 5
0 liters were produced. Since the quality of the gypsum initially produced was poor, it was separately lead-smelted. (b) First mixing of the generated hydrochloric acid solution with fly ash All 500 liters of the hydrochloric acid solution generated in (a) were added to 100 kg of fresh fly ash and mixed to prepare a slurry. The slurry obtained by filtering and removing the slurry was mixed with 95 kg of sulfuric acid having a concentration of 90% by weight. The mixture was filtered to produce 101 kg (dry weight) of gypsum and 500 liters of hydrochloric acid acid solution. (c) Second mixing of generated hydrochloric acid solution with fly ash 440 liters of hydrochloric acid solution generated in (b) above and water 72
One liter was added to 100 kg of fresh fly ash and mixed to prepare a slurry. The slurry obtained by filtering and removing the slurry was mixed with 95 kg of sulfuric acid having a concentration of 90% by weight. This mixture was filtered to produce 115 kg (dry weight) of gypsum and 500 liters of hydrochloric acid acid solution.
【００１３】(d) 生成した塩酸酸性液の飛灰への第３回
混合 上記(c)で生成した塩酸酸性液４４０リットルと水７２
リットルを新たな飛灰１００ｋｇに加えて混合してスラ
リーを調製した。このスラリーをろ過し除滓した液に濃
度９０重量％の硫酸９５ｋｇを加えて混合した。この混
合液をろ過して石膏１１８ｋｇ（乾燥重量）と塩酸酸性
液５００リットルを生成した。上記のように、最初に飛
灰の水スラリーを直接硫酸で処理して塩酸酸性液を生成
した後、この生成した塩酸酸性液で飛灰を処理したとこ
ろ、ほぼ３回で定常状態に達した。このことから本発明
の方法の有効性を実証することができた。この定常状態
に達したときの石膏析出前の残渣の各成分を表１に、
同じく石膏析出時のろ液の各成分を表１に、同じく析
出した石膏の各成分を表１にそれぞれ示す。(D) Third mixing of the produced hydrochloric acid solution with fly ash 440 liters of hydrochloric acid solution produced in (c) above and water 72
One liter was added to 100 kg of fresh fly ash and mixed to prepare a slurry. The slurry obtained by filtering and removing the slurry was mixed with 95 kg of sulfuric acid having a concentration of 90% by weight. This mixture was filtered to produce 118 kg (dry weight) of gypsum and 500 liters of hydrochloric acid acid solution. As described above, first, a fly ash water slurry was directly treated with sulfuric acid to generate a hydrochloric acid acid solution, and then the fly ash was treated with the generated hydrochloric acid solution, and a steady state was reached almost three times. . This proved the effectiveness of the method of the present invention. Table 1 shows each component of the residue before gypsum precipitation when this steady state was reached.
Similarly, each component of the filtrate at the time of gypsum precipitation is shown in Table 1, and each component of the gypsum similarly deposited is shown in Table 1.
【００１４】(e) (d)で生成した塩酸酸性液の抜き出し
と一次中和 定常状態に達したろ液である(d)で生成した塩酸酸性液
６０リットルを抜き出し、この塩酸酸性液に濃度２５重
量％の炭酸カルシウム（ＣａＣＯ3）水溶液４４ｋｇを
加えて混合し、一次中和した。 (f) 二次中和 一次中和した液に水酸化カルシウム（Ｃａ(ＯＨ)2）粉
末３０ｋｇを加えて混合し、二次中和した。この中和液
をろ過し９２リットルのろ過液と１２．５ｋｇの残渣
（乾燥重量）を生成した。このろ過液及び残渣に含まれ
る各成分の割合を表１及びにそれぞれ示す。(E) Extraction and primary neutralization of the hydrochloric acid solution produced in (d) and 60 liters of the hydrochloric acid solution produced in (d), which is a filtrate which has reached a steady state, is withdrawn, and the hydrochloric acid solution having a concentration of 25 44 kg of an aqueous solution of calcium carbonate (CaCO 3 ) by weight was added and mixed, followed by primary neutralization. (f) Secondary Neutralization 30 kg of calcium hydroxide (Ca (OH) 2 ) powder was added to the primary neutralized liquid, mixed, and secondary neutralized. The neutralized solution was filtered to produce 92 liters of filtrate and 12.5 kg of residue (dry weight). Tables 1 and 2 show the proportion of each component contained in the filtrate and the residue, respectively.
【００１５】＜比較例＞実施例と同一の組成の飛灰を用
いて、新規な塩酸と水のみで飛灰を処理した。比較例で
は塩酸酸性液を生成する必要がないので、石膏を析出す
る工程は不要である。先ず表１に示す有価金属と塩素
を含む飛灰１００ｋｇに濃度３６．５重量％の塩酸（Ｈ
Ｃｌ）１５８ｋｇと水４０５リットルを加えて混合して
ｐＨ１．５のスラリー液に調製した。このスラリー液を
ろ過して５００リットルのろ過液と９．５ｋｇの残渣
（乾燥重量）を生成した。この残渣に含まれる各成分の
割合を表１に示す。一方このろ過液に濃度２５重量％
の炭酸カルシウム（ＣａＣＯ3）水溶液１６ｋｇを加え
て混合し、一次中和した。一次中和した液に水酸化カル
シウム（Ｃａ(ＯＨ)2）粉末１００ｋｇを加えて二次中
和した後、ろ過し４９０リットルのろ過液と１５．５ｋ
ｇの残渣（乾燥重量）を生成した。このろ過液及び残渣
に含まれる各成分の割合を表１及びにそれぞれ示
す。<Comparative Example> Using fly ash having the same composition as in the example, the fly ash was treated only with novel hydrochloric acid and water. In the comparative example, since there is no need to generate a hydrochloric acid acid solution, a step of depositing gypsum is unnecessary. First, 100 kg of fly ash containing valuable metals and chlorine as shown in Table 1 was added with hydrochloric acid (H
158 kg of Cl) and 405 liters of water were added and mixed to prepare a slurry having a pH of 1.5. The slurry was filtered to produce 500 liters of filtrate and 9.5 kg of residue (dry weight). Table 1 shows the proportion of each component contained in the residue. On the other hand, the filtrate has a concentration of 25% by weight.
16 kg of an aqueous calcium carbonate (CaCO 3 ) solution was added and mixed, followed by primary neutralization. 100 kg of calcium hydroxide (Ca (OH) 2 ) powder was added to the primary neutralized liquid to perform secondary neutralization, followed by filtration.
g of residue (dry weight) was produced. Tables 1 and 2 show the proportion of each component contained in the filtrate and the residue, respectively.
【００１６】[0016]
【表１】 [Table 1]
【００１７】表１から明らかなように、飛灰１００ｋｇ
当り、比較例の廃水（表１）中のＣｌが約７２ｋｇ
（１４７ｇ／Ｌ×４９０Ｌ）含まれているのに対して、
実施例ではその廃水（表１）中のＣｌの含有量が約１
６ｋｇ（１７５ｇ／Ｌ×９２Ｌ）であり、非常に少なか
った。また高コストの濃度３６．５重量％の塩酸を実施
例では全く使用しないことから、比較例と比べて実施例
では回収コストを著しく低減することができた。更に比
較例では塩酸を含む廃水量が多く廃水処理に多大の負担
が強いられることが判った。As is apparent from Table 1, fly ash 100 kg
Approximately 72 kg of Cl in the wastewater of Comparative Example (Table 1)
(147 g / L × 490 L)
In the example, the content of Cl in the wastewater (Table 1) was about 1
6 kg (175 g / L × 92 L), which was very small. Further, since high-cost hydrochloric acid having a concentration of 36.5% by weight was not used in the examples at all, the recovery cost was significantly reduced in the examples as compared with the comparative examples. Furthermore, in the comparative example, it was found that the amount of wastewater containing hydrochloric acid was large, and a great burden was imposed on wastewater treatment.
【００１８】[0018]
【発明の効果】以上述べたように、本発明によれば、第
１工程で必要な塩酸酸性液を第４工程で自己生成するた
め、飛灰から有価金属を比較的に安価に回収することが
できる。また第４工程から第１工程へのフィードバック
を繰返すことにより、処理液中の有価金属の濃度を高め
て効率よく有価金属を回収することができる。As described above, according to the present invention, since the hydrochloric acid solution required in the first step is self-generated in the fourth step, valuable metals can be recovered from fly ash relatively inexpensively. Can be. Further, by repeating the feedback from the fourth step to the first step, the concentration of the valuable metal in the processing solution can be increased, and the valuable metal can be efficiently recovered.
【００１９】また塩酸酸性液を再利用するため、飛灰か
ら有価金属を回収する際に廃液の発生量が少なくて済
み、廃水処理の負荷が小さくなる特長がある。更に硫酸
を加える前に種石膏を処理液に添加することにより、飛
灰中に含まれるカルシウム成分から高品質な石膏を回収
することができる。Further, since the hydrochloric acid solution is reused, the amount of waste liquid generated when recovering valuable metals from fly ash can be reduced, and the load of waste water treatment can be reduced. By adding seed gypsum to the treatment liquid before adding sulfuric acid, high-quality gypsum can be recovered from calcium components contained in fly ash.
【図１】本発明の飛灰から有価金属を回収する方法を示
す工程図。FIG. 1 is a process chart showing a method for recovering valuable metals from fly ash according to the present invention.
Claims (6)
含む飛灰から前記有価金属を回収する方法において、 前記飛灰を塩酸酸性液で処理する第１工程(11)と、前記
第１工程の処理液をろ過し除滓する第２工程(12)と、前
記第２工程で除滓した液に硫酸を加えて反応させる第３
工程(13)と、前記第３工程の反応生成液をろ過して石膏
と塩酸酸性液を生成する第４工程(14)とを含むことを特
徴とする飛灰からの有価金属回収方法。1. A method for recovering valuable metals from fly ash containing a calcium component, a chlorine component and valuable metals, comprising: a first step (11) of treating the fly ash with a hydrochloric acid acid solution; A second step (12) of filtering and removing the treatment liquid, and a third step of adding sulfuric acid to the liquid removed in the second step to cause a reaction.
A method for recovering valuable metals from fly ash, comprising: a step (13); and a fourth step (14) of filtering the reaction product liquid of the third step to produce gypsum and a hydrochloric acid acid solution.
工程(14)で生成した塩酸酸性液の一部又は全部である請
求項１記載の飛灰からの有価金属回収方法。2. The hydrochloric acid solution used in the first step (11) is a fourth acid solution.
The method for recovering valuable metals from fly ash according to claim 1, which is part or all of the hydrochloric acid acid solution produced in the step (14).
１工程(11)で用いる前の塩酸酸性液の一部又は全部が、
塩酸水溶液であるか、或いは飛灰の一部と水とを混合す
ることにより生成したスラリーをろ過し除滓した液に硫
酸を加えて生成した塩酸酸性液である請求項２記載の飛
灰からの有価金属回収方法。3. A part or all of the hydrochloric acid solution before using the hydrochloric acid solution produced in the fourth step (14) in the first step (11) is as follows:
The fly ash according to claim 2, which is a hydrochloric acid aqueous solution or a hydrochloric acid acid solution produced by adding sulfuric acid to a liquid obtained by filtering a slurry formed by mixing a part of the fly ash with water and removing the slag. Valuable metal recovery method.
液をろ過し除滓した液に種石膏を加える請求項１ないし
３いずれか記載の飛灰からの有価金属回収方法。4. The method for recovering valuable metals from fly ash according to any one of claims 1 to 3, wherein before the addition of sulfuric acid in the third step (13), the treatment liquid is filtered and the gypsum is added to the liquid obtained by removing the slag.
部に炭酸カルシウムを加えて中和する第５工程(15)と、
前記第５工程で中和した処理液に水酸化カルシウム又は
水酸化ナトリウムを加える第６工程(16)と、前記第６工
程で中和した処理液をろ過する第７工程(17)とを更に含
む請求項１ないし４いずれか記載の飛灰からの有価金属
回収方法。5. A fifth step (15) in which calcium carbonate is added to a part of the acidic hydrochloric acid solution produced in the fourth step (14) to neutralize the solution,
A sixth step (16) of adding calcium hydroxide or sodium hydroxide to the treatment liquid neutralized in the fifth step, and a seventh step (17) of filtering the treatment liquid neutralized in the sixth step. The method for recovering valuable metals from fly ash according to any one of claims 1 to 4.
灰を５００℃以上の温度で加熱処理する第８工程(18)を
更に含む請求項１ないし５いずれか記載の飛灰からの有
価金属回収方法。6. The method according to claim 1, further comprising an eighth step (18) of subjecting the fly ash to a temperature of 500 ° C. or more before treating the fly ash in the first step (11). A method for recovering valuable metals from fly ash.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP27961798A JP3536901B2 (en) | 1998-10-01 | 1998-10-01 | Method of recovering valuable metals from fly ash |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP27961798A JP3536901B2 (en) | 1998-10-01 | 1998-10-01 | Method of recovering valuable metals from fly ash |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JP2000109938A true JP2000109938A (en) | 2000-04-18 |
| JP3536901B2 JP3536901B2 (en) | 2004-06-14 |
Family
ID=17613486
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP27961798A Expired - Lifetime JP3536901B2 (en) | 1998-10-01 | 1998-10-01 | Method of recovering valuable metals from fly ash |
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| Country | Link |
|---|---|
| JP (1) | JP3536901B2 (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2005040437A1 (en) * | 2003-10-27 | 2005-05-06 | Dowa Mining Co., Ltd. | Method of wet treatment of fly ash |
| JP2005279637A (en) * | 2004-03-04 | 2005-10-13 | Mitsubishi Materials Corp | Method for removing and collecting heavy metals in soil |
| JP2006219719A (en) * | 2005-02-09 | 2006-08-24 | Dowa Mining Co Ltd | Indium recovery method |
| JP2008264628A (en) * | 2007-04-17 | 2008-11-06 | Mitsubishi Materials Corp | Processing method of molten fly ash |
| JP2012167332A (en) * | 2011-02-15 | 2012-09-06 | Taiheiyo Cement Corp | Method of collecting silver and copper |
| JP2014128744A (en) * | 2012-12-27 | 2014-07-10 | Mitsuboshi Mining Co Ltd | Method for processing water-washed sludge |
-
1998
- 1998-10-01 JP JP27961798A patent/JP3536901B2/en not_active Expired - Lifetime
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2005040437A1 (en) * | 2003-10-27 | 2005-05-06 | Dowa Mining Co., Ltd. | Method of wet treatment of fly ash |
| JP2005279637A (en) * | 2004-03-04 | 2005-10-13 | Mitsubishi Materials Corp | Method for removing and collecting heavy metals in soil |
| JP2006219719A (en) * | 2005-02-09 | 2006-08-24 | Dowa Mining Co Ltd | Indium recovery method |
| JP2008264628A (en) * | 2007-04-17 | 2008-11-06 | Mitsubishi Materials Corp | Processing method of molten fly ash |
| JP2012167332A (en) * | 2011-02-15 | 2012-09-06 | Taiheiyo Cement Corp | Method of collecting silver and copper |
| JP2014128744A (en) * | 2012-12-27 | 2014-07-10 | Mitsuboshi Mining Co Ltd | Method for processing water-washed sludge |
Also Published As
| Publication number | Publication date |
|---|---|
| JP3536901B2 (en) | 2004-06-14 |
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