JP2007186761A - Method for recovering valuable metal - Google Patents
Method for recovering valuable metal Download PDFInfo
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- JP2007186761A JP2007186761A JP2006006461A JP2006006461A JP2007186761A JP 2007186761 A JP2007186761 A JP 2007186761A JP 2006006461 A JP2006006461 A JP 2006006461A JP 2006006461 A JP2006006461 A JP 2006006461A JP 2007186761 A JP2007186761 A JP 2007186761A
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- zinc
- fly ash
- valuable metal
- dechlorinated
- recovering
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- 229910052751 metal Inorganic materials 0.000 title claims abstract description 55
- 239000002184 metal Substances 0.000 title claims abstract description 55
- 238000000034 method Methods 0.000 title claims abstract description 29
- 239000010881 fly ash Substances 0.000 claims abstract description 40
- 229910052725 zinc Inorganic materials 0.000 claims abstract description 29
- 239000011701 zinc Substances 0.000 claims abstract description 29
- XLOMVQKBTHCTTD-UHFFFAOYSA-N Zinc monoxide Chemical compound [Zn]=O XLOMVQKBTHCTTD-UHFFFAOYSA-N 0.000 claims abstract description 28
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 claims abstract description 26
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 claims abstract description 18
- 229910052801 chlorine Inorganic materials 0.000 claims abstract description 18
- 239000000460 chlorine Substances 0.000 claims abstract description 18
- 239000002994 raw material Substances 0.000 claims abstract description 16
- 239000011787 zinc oxide Substances 0.000 claims abstract description 14
- 230000004907 flux Effects 0.000 claims abstract description 10
- 239000003245 coal Substances 0.000 claims abstract description 9
- 238000011084 recovery Methods 0.000 claims abstract description 6
- 150000002739 metals Chemical class 0.000 claims description 33
- 238000003723 Smelting Methods 0.000 claims description 21
- 238000004140 cleaning Methods 0.000 claims description 17
- 239000004484 Briquette Substances 0.000 claims description 12
- 239000011133 lead Substances 0.000 claims description 8
- 239000002893 slag Substances 0.000 claims description 7
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N Iron oxide Chemical compound [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 claims description 6
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 6
- 238000002844 melting Methods 0.000 claims description 6
- 230000008018 melting Effects 0.000 claims description 6
- 239000002956 ash Substances 0.000 claims description 5
- 229910052802 copper Inorganic materials 0.000 claims description 5
- 239000010949 copper Substances 0.000 claims description 5
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 4
- 239000004568 cement Substances 0.000 claims description 3
- 239000000377 silicon dioxide Substances 0.000 claims description 3
- 238000010438 heat treatment Methods 0.000 claims description 2
- 230000006698 induction Effects 0.000 claims description 2
- 229910000831 Steel Inorganic materials 0.000 claims 1
- 239000010959 steel Substances 0.000 claims 1
- 239000007788 liquid Substances 0.000 abstract description 17
- 238000005406 washing Methods 0.000 abstract description 15
- 238000002156 mixing Methods 0.000 abstract description 6
- 239000000203 mixture Substances 0.000 abstract description 5
- 238000001035 drying Methods 0.000 abstract description 3
- 238000007670 refining Methods 0.000 abstract 1
- 239000002002 slurry Substances 0.000 description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 9
- 239000003513 alkali Substances 0.000 description 8
- 239000000243 solution Substances 0.000 description 7
- 229910052736 halogen Inorganic materials 0.000 description 6
- 150000002367 halogens Chemical class 0.000 description 6
- 239000000428 dust Substances 0.000 description 5
- 239000002699 waste material Substances 0.000 description 5
- 239000002253 acid Substances 0.000 description 3
- 238000006298 dechlorination reaction Methods 0.000 description 3
- 229910001385 heavy metal Inorganic materials 0.000 description 3
- 229910052745 lead Inorganic materials 0.000 description 3
- 238000004064 recycling Methods 0.000 description 3
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 2
- 229910052793 cadmium Inorganic materials 0.000 description 2
- 238000009740 moulding (composite fabrication) Methods 0.000 description 2
- 238000010298 pulverizing process Methods 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 229910018072 Al 2 O 3 Inorganic materials 0.000 description 1
- 229910004298 SiO 2 Inorganic materials 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- ODINCKMPIJJUCX-UHFFFAOYSA-N calcium oxide Inorganic materials [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 1
- 150000001805 chlorine compounds Chemical class 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 230000000382 dechlorinating effect Effects 0.000 description 1
- 230000000779 depleting effect Effects 0.000 description 1
- 150000002013 dioxins Chemical class 0.000 description 1
- 239000010791 domestic waste Substances 0.000 description 1
- 238000010828 elution Methods 0.000 description 1
- 239000000706 filtrate Substances 0.000 description 1
- 238000002309 gasification Methods 0.000 description 1
- 239000010903 husk Substances 0.000 description 1
- 239000002440 industrial waste Substances 0.000 description 1
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 1
- CPLXHLVBOLITMK-UHFFFAOYSA-N magnesium oxide Inorganic materials [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 238000011946 reduction process Methods 0.000 description 1
- 229910052709 silver Inorganic materials 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000004575 stone Substances 0.000 description 1
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
-
- 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
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/91—Use of waste materials as fillers for mortars or concrete
Landscapes
- Manufacture And Refinement Of Metals (AREA)
Abstract
Description
本発明は有価金属の回収方法に関し、より詳しくは、有価金属の回収操作に先立って、有価金属及び塩素を含有する焼却飛灰、溶融飛灰等の飛灰の脱塩素洗浄を特定のｐＨ条件下で実施することによって塩素含有量を２質量％以下に低下させるが有価金属が洗浄液中に溶出することを防止する有価金属の回収方法に関する。 The present invention relates to a method for recovering valuable metals, and more particularly, prior to the operation of recovering valuable metals, dechlorinating washing of fly ash such as incinerated fly ash and molten fly ash containing valuable metals and chlorine is performed under specific pH conditions. The present invention relates to a method for recovering valuable metals that lowers the chlorine content to 2% by mass or less by preventing the valuable metals from eluting into the cleaning liquid.
近年、埋め立て処分場の枯渇やダイオキシン低減化対策として、生活ゴミに代表される一般廃棄物や、カーシュレッターダスト等の廃プラスチックに代表される産業廃棄物の処理設備としてガス化溶融炉や灰溶融炉が多数建設されており、それらから排出される溶融飛灰の量は年間１５万トンを超え、今後更に増加することが予想されている。しかしながら、溶融飛灰の大半はキレート材等による不溶出処理をして埋め立て処分場で最終処分されているのが現状である。 In recent years, gasification melting furnaces and ash melting have been used as treatment facilities for general waste represented by household waste and industrial waste represented by waste plastics such as car-shetter litter as a measure for depleting landfill sites and reducing dioxins. Many furnaces have been built, and the amount of molten fly ash discharged from them exceeds 150,000 tons per year, and is expected to increase further in the future. However, at present, most of the molten fly ash is subjected to non-eluting treatment with a chelating material or the like and finally disposed at a landfill site.
溶融飛灰の再資源化処理方法としては、溶融飛灰中に大量に含有されている塩素を利用して溶融飛灰中の重金属成分を塩化物として揮発させ、回収する塩化物揮発法（乾式法）が提案されている（例えば、特許文献１及び２参照。）が、塩化物として揮発したＺｎ、Ｐｂ、Ｃｄ等の重金属ダストを製錬に利用可能な品位になるように塩素濃度を制御することが困難であるか又は複雑であること、回収したダストは吸湿性であるため取り扱いが煩雑であること、製錬原料化のためには複雑な湿式処理を更に必要とすること、排出される燃え殻（クリンカー）中のＰｂ等の有害重金属の含有量が再資源化基準値まで下がりにくいこと等の問題を有している。 As a method for recycling molten fly ash, the chloride volatilization method (dry method) is used to volatilize and recover heavy metal components in molten fly ash as chloride using chlorine contained in large quantities in molten fly ash. (See, for example, Patent Documents 1 and 2), but the chlorine concentration is controlled so that heavy metal dusts such as Zn, Pb, and Cd that have volatilized as chlorides can be used for smelting. It is difficult or complicated to perform, the collected dust is hygroscopic and handling is complicated, and a complicated wet process is required for smelting raw material, and it is discharged. There is a problem that the content of harmful heavy metals such as Pb in the burning husk (clinker) is not easily lowered to the recycling standard value.
溶融飛灰の再資源化処理方法として湿式処理法も提案されている（例えば、特許文献３及び４参照。）が、処理操作が多段となり複雑であること、また処理の過程で二次的に発生する多量の廃液の処理も複雑であり、最終的に発生する残渣の処理も必要である等により処理コストが高いこと、更に大容量の処理には不向きであること等の問題がある。 A wet processing method has also been proposed as a method for recycling molten fly ash (see, for example, Patent Documents 3 and 4), but the processing operation is multi-stage and complicated, and secondarily in the course of processing. The treatment of a large amount of waste liquid is also complicated, and there is a problem that the treatment cost is high due to the necessity of treatment of the finally generated residue, and that it is unsuitable for large-capacity treatment.
更に、塩素含有焼却塵灰を水又は酸で洗浄して脱塩素処理した後に金属製錬炉に投入し、金属精鉱と共に加熱溶融する際にフラックスとして利用することも提案されている（例えば、特許文献５参照。）。この場合に、酸で洗浄して脱塩素処理を実施すると、焼却塵灰中の有価金属が洗浄液中に溶解して焼却塵灰中の有価金属の含有量が低減し、製錬炉で回収される金属の量が低下することになる。また、単に水で洗浄した場合には、Ｃｄの一部が水中に溶解するのでＣｄを水溶液から回収する必要が生じ、また、焼却塵灰の種類が雑多で品質が安定していないことから塩素の除去が不十分となるケースが発生し、金属製錬炉での目的金属の回収率が悪化し、更に構造物へのハロゲンアタックが発生することもあるという問題がある。 Furthermore, it has also been proposed that chlorine-containing incineration dust ash is washed with water or acid and then dechlorinated before being put into a metal smelting furnace and used as a flux when heated and melted with metal concentrate (for example, (See Patent Document 5). In this case, if the dechlorination treatment is performed by washing with acid, the valuable metals in the incineration dust ash are dissolved in the cleaning liquid, and the content of the valuable metals in the incineration dust ash is reduced and recovered in the smelting furnace. The amount of metal to be reduced will decrease. In addition, when it is simply washed with water, a part of Cd is dissolved in water, so it is necessary to recover Cd from the aqueous solution. In some cases, the removal of the metal becomes insufficient, the recovery rate of the target metal in the metal smelting furnace deteriorates, and a halogen attack to the structure may occur.
本発明は、上記のような諸問題を根本的に解決すること、即ち、有価金属の回収操作に先立って、有価金属及び塩素を含有する焼却飛灰、溶融飛灰等の飛灰の脱塩素洗浄を特定のｐＨ条件下で実施することによって塩素含有量を２質量％以下に低下させるが有価金属が洗浄液中に溶出することを防止する有価金属の回収方法を提供することを目的としている。 The present invention fundamentally solves the above problems, that is, prior to the recovery operation of valuable metals, dechlorination of fly ash such as incinerated fly ash and molten fly ash containing valuable metals and chlorine. An object of the present invention is to provide a method for recovering valuable metals that reduces the chlorine content to 2% by mass or less by carrying out washing under specific pH conditions, but prevents the valuable metals from eluting into the washing liquid.
即ち、本発明の有価金属の回収方法は、有価金属及び塩素を含有する飛灰をｐＨ１０〜１２の洗浄液で脱塩素洗浄し、該脱塩素洗浄した飛灰、亜鉛含有原料、フラックス及び石炭を混合し、乾燥させ、粉砕した後、団鉱とし、該団鉱を溶融還元することを特徴とする。 That is, in the method for recovering valuable metals according to the present invention, fly ash containing valuable metals and chlorine is dechlorinated and washed with a cleaning solution having a pH of 10 to 12, and the dechlorinated and washed fly ash, zinc-containing raw material, flux and coal are mixed. Then, after drying, pulverizing, and forming a briquette, the briquette is melt-reduced.
また、本発明の有価金属の回収方法は、有価金属及び塩素を含有する飛灰をｐＨ１０〜１２の洗浄液で脱塩素洗浄し、該脱塩素処理した飛灰、亜鉛含有原料、フラックス及び石炭を混合し、乾燥させ、粉砕した後、団鉱とし、該団鉱を溶融還元し、亜鉛を粗酸化亜鉛として回収し、回収した粗酸化亜鉛をｐＨ１０〜１２の洗浄液で更に脱塩素洗浄し、該脱塩素洗浄した粗酸化亜鉛を亜鉛製錬に用いることを特徴とする。 In addition, the method for recovering valuable metals according to the present invention includes deashing and cleaning fly ash containing valuable metals and chlorine with a cleaning solution having a pH of 10 to 12, and mixing the dechlorinated fly ash, zinc-containing raw material, flux and coal. Dried, pulverized, and converted into briquette, the briquette is melt-reduced, zinc is recovered as crude zinc oxide, and the recovered crude zinc oxide is further dechlorinated and washed with a pH 10-12 washing solution, It is characterized by using chlorine-cleaned crude zinc oxide for zinc smelting.
本発明の有価金属の回収方法においては、飛灰の塩素含有量を２質量％以下に低下させるが有価金属が洗浄液中に溶出することを防止することができるので、製錬炉で回収される有価金属の量が増大し、また廃液中にはＣｄ等の有害金属の量が少ないので廃液の処理が容易である。 In the method for recovering valuable metals according to the present invention, the chlorine content of fly ash is reduced to 2% by mass or less, but it is possible to prevent valuable metals from eluting into the cleaning liquid, so that they are recovered in a smelting furnace. The amount of valuable metals increases, and the amount of harmful metals such as Cd is small in the waste liquid, so that the waste liquid can be easily treated.
本発明の有価金属の回収方法は、有価金属及び塩素を含有する焼却飛灰、溶融飛灰等の飛灰をｐＨ１０〜１２の洗浄液で脱塩素洗浄し、該脱塩素洗浄した飛灰、亜鉛含有原料、フラックス及び石炭を混合し、乾燥させ、粉砕した後、団鉱とし、該団鉱を溶融還元する諸工程を含む。本発明においては洗浄液のｐＨは洗浄時のｐＨ、即ち、例えば、飛灰と水とアルカリとを含むスラリー状態時のｐＨである。該脱塩素洗浄は、例えば、飛灰と水とアルカリとを含むｐＨ１０〜１２のスラリーを形成し、該スラリーの固液分離操作によってハロゲン濃度が２質量％以下である残渣を回収することによって実施できる。洗浄液のｐＨが１０未満である場合には塩素の除去が不十分となり、また、洗浄液のｐＨが１２を超えると、洗浄液中へのＰｂ、Ｚｎの溶出が問題となる。 The method for recovering valuable metals according to the present invention includes deashing and washing of fly ash such as incinerated fly ash and molten fly ash containing valuable metals and chlorine with a pH 10 to 12 washing solution, and the dechlorinated and washed fly ash containing zinc. It includes various steps of mixing raw materials, flux and coal, drying, pulverizing, forming briquettes, and smelting the briquettes. In the present invention, the pH of the cleaning liquid is a pH at the time of cleaning, that is, a pH in a slurry state containing, for example, fly ash, water, and alkali. The dechlorination cleaning is performed, for example, by forming a slurry having a pH of 10 to 12 containing fly ash, water, and alkali, and collecting a residue having a halogen concentration of 2% by mass or less by solid-liquid separation operation of the slurry. it can. When the pH of the cleaning liquid is less than 10, chlorine removal is insufficient, and when the pH of the cleaning liquid exceeds 12, elution of Pb and Zn into the cleaning liquid becomes a problem.
上記の飛灰と水とアルカリとを含むスラリーの形成方法としては、飛灰と水とアルカリとを混合装置中にそれぞれ別個に同時に又は順次装入しても、飛灰とアルカリ水溶液とを混合装置中にそれぞれ別個に同時に又は順次装入しても、飛灰を含有する水性スラリーとアルカリとを混合装置中にそれぞれ別個に同時に又は順次装入してもよい。 As a method for forming a slurry containing the above fly ash, water and alkali, the fly ash and the aqueous alkali solution are mixed even if the fly ash, water and alkali are separately or simultaneously charged in the mixing device. The aqueous slurry containing the fly ash and the alkali may be separately and simultaneously or sequentially charged into the mixing device, respectively.
上記のスラリーを固液分離することにより、大部分のハロゲンが濾液中に溶解しているので、ハロゲン濃度の低い残渣が回収される。この残渣中のハロゲン濃度は容易に２質量％以下となり、好ましく１質量％以下となる。 By separating the slurry into solid and liquid, most of the halogen is dissolved in the filtrate, so that a residue having a low halogen concentration is recovered. The halogen concentration in the residue is easily 2% by mass or less, preferably 1% by mass or less.
本発明の有価金属の回収方法においては、亜鉛含有原料として亜鉛を含有する種々の原料を用いることができるが、実用的には製鋼煙灰を用いることが好ましい。また、本発明の有価金属の回収方法においては、飛灰中に含有される有価金属は実用的には亜鉛、鉛、銅であり、亜鉛及び鉛を酸化物として回収し、銅をマットとして回収する。更に、無害化されたスラグを生成する。この場合には、フラックスとして珪石及び酸化鉄を用いてスラグの品質をセメント原料に適するように調整することができる。 In the method for recovering valuable metals according to the present invention, various raw materials containing zinc can be used as the zinc-containing raw material. Moreover, in the valuable metal recovery method of the present invention, the valuable metals contained in the fly ash are practically zinc, lead, and copper, and zinc and lead are recovered as oxides, and copper is recovered as a mat. To do. Furthermore, the harmless slag is generated. In this case, the quality of the slag can be adjusted to be suitable for the cement raw material using silica and iron oxide as the flux.
また、本発明の有価金属の回収方法は、有価金属及び塩素を含有する飛灰をｐＨ１０〜１２の洗浄液で脱塩素洗浄し、該脱塩素処理した飛灰、亜鉛含有原料、フラックス及び石炭を混合し、乾燥させ、粉砕した後、団鉱とし、該団鉱を溶融還元し、亜鉛を粗酸化亜鉛として回収し、回収した粗酸化亜鉛をｐＨ１０〜１２の洗浄液で更に脱塩素洗浄し、該脱塩素洗浄した粗酸化亜鉛を亜鉛製錬に用いる諸工程を含むものであり、団鉱の溶融還元までは上記のように実施し、粗酸化亜鉛の脱塩素洗浄は、例えば、該粗酸化亜鉛と水とアルカリとを含むｐＨ１０〜１２のスラリーを形成し、該スラリーの固液分離操作によってハロゲン濃度が０．５質量％以下である残渣（粗酸化亜鉛）を回収することによって実施できる。また、亜鉛製錬は従来公知の方法で実施することができる。 In addition, the method for recovering valuable metals according to the present invention includes deashing and cleaning fly ash containing valuable metals and chlorine with a cleaning solution having a pH of 10 to 12, and mixing the dechlorinated fly ash, zinc-containing raw material, flux and coal. Dried, pulverized, and converted into briquette, the briquette is melt-reduced, zinc is recovered as crude zinc oxide, and the recovered crude zinc oxide is further dechlorinated and washed with a pH 10-12 washing solution, The process includes the steps of using chlorine-cleaned crude zinc oxide for zinc smelting, and is carried out as described above until the smelting reduction of briquette. It can be carried out by forming a slurry having a pH of 10 to 12 containing water and an alkali, and collecting a residue (crude zinc oxide) having a halogen concentration of 0.5% by mass or less by solid-liquid separation operation of the slurry. Zinc smelting can be carried out by a conventionally known method.
本発明の有価金属の回収方法においては、溶融還元は、例えば、高周波誘導炉、直流型或いは交流型の抵抗加熱電気炉、三井式亜鉛半溶鉱炉（ＭＦ炉）等の溶融炉を用い、還元剤として好ましくは石炭（コークスを包含する）を用いて、例えば１３００℃以上の還元条件下で溶融させることにより実施できる。一般的に、溶融還元の際の処理温度が１３００℃未満である場合には、団鉱中の金属成分の揮発又は溶融が不十分となる傾向がある。 In the method for recovering valuable metals of the present invention, the smelting reduction is performed using a melting furnace such as a high frequency induction furnace, a direct current or alternating current resistance heating electric furnace, a Mitsui zinc semi-molten furnace (MF furnace), and the like. Preferably, coal (including coke) can be used, for example, by melting under reducing conditions of 1300 ° C. or higher. Generally, when the processing temperature at the time of smelting reduction is less than 1300 ° C., the volatilization or melting of the metal component in the briquette tends to be insufficient.
この溶融還元処理において、揮発したＺｎ、Ｐｂ、Ｃｄ等の金属成分をダスト中に濃縮させて、それらの金属の製錬に利用可能な濃度で含有する製錬原料として回収し、溶融しているが揮発しなかったＣｕ、Ａｇ等の金属成分を溶融マット中に濃縮させて、それらの金属の製錬に利用可能な濃度で含有する製錬原料として回収し、残りのＦｅＯ（Ｆｅ2Ｏ3）、ＳｉＯ2、ＣａＯ、Ａｌ2Ｏ3、ＭｇＯ等の成分をセメント原料、細骨材、粗骨材として利用可能な清浄なスラグとして回収することができる。 In this smelting reduction process, volatilized metal components such as Zn, Pb, and Cd are concentrated in the dust, recovered as a smelting raw material containing at a concentration that can be used for smelting those metals, and melted. The metal components such as Cu and Ag that did not volatilize are concentrated in the molten mat and recovered as a smelting raw material containing a concentration usable for smelting of these metals, and the remaining FeO (Fe 2 O 3 ), SiO 2 , CaO, Al 2 O 3 , MgO and other components can be recovered as clean slag that can be used as a cement raw material, fine aggregate, and coarse aggregate.
実施例１及び比較例１〜５
第１表に示す組成、品位の飛灰を第１表に示すｐＨ（飛灰と水とアルカリ又は酸とを含むスラリーのｐＨ）条件下で洗浄した。洗浄後の組成、品位は第１表に示す通りであった。
Example 1 and Comparative Examples 1-5
The composition and quality of fly ash shown in Table 1 were washed under the conditions shown in Table 1 (pH of slurry containing fly ash, water, alkali, or acid). The composition and quality after washing were as shown in Table 1.
実施例２
それぞれ第２表に示す組成、品位を有する、実施例１の条件（ｐＨ１１）で洗浄した飛灰、亜鉛滓、珪石、酸化鉄及び石炭を第２表に示す量で用い、溶融還元処理して、それぞれ第２表に示す組成、品位を有する、粗酸化亜鉛、マット及びスラグを第２表に示す量で得た。
Example 2
Using the fly ash, zinc slag, silica stone, iron oxide, and coal, which have the compositions and grades shown in Table 2 and washed under the conditions of Example 1 (pH 11), the amounts shown in Table 2 were used for smelting reduction treatment. The crude zinc oxide, mat and slag having the composition and quality shown in Table 2 were obtained in the amounts shown in Table 2, respectively.
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| Publication number | Priority date | Publication date | Assignee | Title |
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| KR101493965B1 (en) * | 2014-03-12 | 2015-03-02 | 이계안 | Process for recovering iron and zinc from iron and zinc-bearing waste |
| EP3556468A1 (en) | 2018-04-19 | 2019-10-23 | OiW Process AS | Method and apparatus for forming a suspension of partly dissolved fly ash in a mineral acid |
| CN113862462A (en) * | 2021-09-22 | 2021-12-31 | 日照卓业环保科技有限公司 | Method for joint dechlorination of sintering machine head ash and blast furnace cloth bag ash |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| KR101493965B1 (en) * | 2014-03-12 | 2015-03-02 | 이계안 | Process for recovering iron and zinc from iron and zinc-bearing waste |
| EP3556468A1 (en) | 2018-04-19 | 2019-10-23 | OiW Process AS | Method and apparatus for forming a suspension of partly dissolved fly ash in a mineral acid |
| WO2019201919A1 (en) | 2018-04-19 | 2019-10-24 | Oiw Process As | Method and apparatus for forming a suspension of partly dissolved fly ash in a mineral acid |
| CN113862462A (en) * | 2021-09-22 | 2021-12-31 | 日照卓业环保科技有限公司 | Method for joint dechlorination of sintering machine head ash and blast furnace cloth bag ash |
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