JPH06240377A - Method for concentrating and recovering zinc - Google Patents
Method for concentrating and recovering zincInfo
- Publication number
- JPH06240377A JPH06240377A JP5024410A JP2441093A JPH06240377A JP H06240377 A JPH06240377 A JP H06240377A JP 5024410 A JP5024410 A JP 5024410A JP 2441093 A JP2441093 A JP 2441093A JP H06240377 A JPH06240377 A JP H06240377A
- Authority
- JP
- Japan
- Prior art keywords
- zinc
- ash
- gas
- melting
- vapor
- 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
Links
- 239000011701 zinc Substances 0.000 title claims abstract description 48
- 229910052725 zinc Inorganic materials 0.000 title claims abstract description 43
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 title claims abstract description 42
- 238000000034 method Methods 0.000 title claims description 9
- 238000002844 melting Methods 0.000 claims abstract description 25
- 230000008018 melting Effects 0.000 claims abstract description 25
- 239000003638 chemical reducing agent Substances 0.000 claims abstract description 10
- 238000001816 cooling Methods 0.000 claims abstract description 5
- 239000007787 solid Substances 0.000 claims description 7
- 239000002699 waste material Substances 0.000 abstract description 15
- XLOMVQKBTHCTTD-UHFFFAOYSA-N Zinc monoxide Chemical compound [Zn]=O XLOMVQKBTHCTTD-UHFFFAOYSA-N 0.000 abstract description 8
- 239000011787 zinc oxide Substances 0.000 abstract description 4
- 239000000571 coke Substances 0.000 abstract 2
- 238000010438 heat treatment Methods 0.000 abstract 1
- 239000002440 industrial waste Substances 0.000 abstract 1
- 239000000428 dust Substances 0.000 description 18
- 238000010309 melting process Methods 0.000 description 6
- 239000011343 solid material Substances 0.000 description 6
- 238000005406 washing Methods 0.000 description 6
- 239000002893 slag Substances 0.000 description 4
- 238000002485 combustion reaction Methods 0.000 description 3
- 239000000155 melt Substances 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical group [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 2
- 238000009835 boiling Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 229910001385 heavy metal Inorganic materials 0.000 description 2
- 238000010128 melt processing Methods 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 1
- 229910052753 mercury Inorganic materials 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 239000011780 sodium chloride Substances 0.000 description 1
- 230000000087 stabilizing effect Effects 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
- 150000003751 zinc Chemical class 0.000 description 1
Landscapes
- Processing Of Solid Wastes (AREA)
- Manufacture And Refinement Of Metals (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、各種廃棄物、廃棄物焼
却炉からの焼却灰、ボイラ灰、集塵灰等、廃棄物溶融炉
および冶金用溶融炉等から発生する集塵灰、ボトムアッ
シュ等の固形物から有価物として亜鉛を回収する方法に
関する。The present invention relates to various kinds of waste, incineration ash from a waste incinerator, boiler ash, dust ash, etc., dust ash generated from a waste melting furnace and a metallurgical melting furnace, and a bottom. The present invention relates to a method for recovering zinc as a valuable resource from solid matter such as ash.
【0002】[0002]
【従来の技術】亜鉛を含有する固形物の一例として、廃
棄物焼却炉の集塵灰がある。以下、廃棄物焼却炉の集塵
灰を例にとって説明する。廃棄物焼却炉の集塵灰には、
亜鉛の他鉛、水銀等の重金属が含まれているため、環境
汚染防止の観点から種々の処理技術が検討され、例え
ば、「環境技術」Vol.21(1992)p.243〜252に記載されて
いるように溶融処理することによりこれらの重金属を溶
融スラグ中に封じ込めて安定化し、このスラグを土木資
材として再利用する方法が提案されている。2. Description of the Related Art One example of solid matter containing zinc is dust ash in a waste incinerator. Hereinafter, the dust ash of the waste incinerator will be described as an example. For the dust ash of the waste incinerator,
Since it contains heavy metals such as lead and mercury in addition to zinc, various treatment technologies have been studied from the viewpoint of environmental pollution prevention, and are described, for example, in "Environmental Technology" Vol.21 (1992) p.243-252. As described above, a method of encapsulating and stabilizing these heavy metals in a molten slag by melting and reusing the slag as a civil engineering material has been proposed.
【0003】[0003]
【発明が解決しようとする課題】前述のように従来の溶
融処理の方法では、亜鉛を有価物として回収するまでに
はいたっていない。本発明の目的は、亜鉛を含有する固
形物を溶融処理するにあたり、亜鉛分を濃縮回収する方
法を提供することにある。As described above, the conventional melt processing method does not reach the point of recovering zinc as a valuable resource. It is an object of the present invention to provide a method for concentrating and recovering a zinc content in melt processing a solid material containing zinc.
【0004】[0004]
【課題を解決するための手段】本発明は、亜鉛を含有す
る固形物を溶融炉にて溶融処理する方法において、還元
剤を直接または前記固形物と混合して溶融炉に供給し、
固形物中の亜鉛分を還元し亜鉛蒸気としてガス中に揮発
させ、この亜鉛蒸気を含むガスを溶融炉外で冷却し亜鉛
分を固化して捕集することを特徴とする亜鉛の濃縮回収
方法である。Means for Solving the Problems The present invention provides a method for melting a solid material containing zinc in a melting furnace, and supplying a reducing agent directly or by mixing with the solid material to the melting furnace.
A method for concentrating and recovering zinc, characterized in that the zinc content in the solid matter is reduced and volatilized into gas as zinc vapor, and the gas containing this zinc vapor is cooled outside the melting furnace to solidify and collect the zinc content. Is.
【0005】[0005]
【作用および実施例】以下、廃棄物焼却炉の集塵灰につ
いて電機炉で行った溶融処理の試験結果をもとに説明す
る。表1に、廃棄物焼却炉の集塵灰を大気雰囲気中13
00℃で溶融処理したときの、表2には、同じ集塵灰を
炉内に還元剤としてコークス粉を集塵灰1に対し0.1
の重量割合で供給して1300℃で溶融処理したときの
集塵灰、溶融物および揮発分の成分分析結果を示した。
数値は何れも集塵灰の全量を100とした重量割合で示
している。[Operations and Examples] Hereinafter, the dust ash of the waste incinerator will be described based on the test results of the melting process performed in the electric furnace. Table 1 shows the dust ash from the waste incinerator in the atmosphere.
When melted at 00 ° C., Table 2 shows that the same dust collecting ash was used as a reducing agent in the furnace and coke powder was 0.1 per 1 of dust collecting ash.
The results of analysis of the components of the dust ash, the melt, and the volatile component when melt-treated at 1300 ° C. were supplied at a weight ratio of 1: 1.
All numerical values are shown by weight ratio with the total amount of collected ash as 100.
【0006】表1に示した大気雰囲気中での溶融処理で
は、集塵灰に含有される亜鉛分の大部分が溶融物へ移行
しており、揮発分への亜鉛の顕著な濃縮はおこなわれて
いない。これは集塵灰中の亜鉛分の大部分が酸化物の形
態で存在し、酸化亜鉛の沸点が溶融処理温度に比べて高
いことから、溶融過程で揮発せず溶融物側に移行するた
めと考えられる。In the melting treatment in the air atmosphere shown in Table 1, most of the zinc content contained in the dust ash was transferred to the melt, so that the zinc was remarkably concentrated in the volatile matter. Not not. This is because most of the zinc content in the collected ash exists in the form of oxides, and since the boiling point of zinc oxide is higher than the melting treatment temperature, it does not volatilize in the melting process and moves to the melt side. Conceivable.
【0007】これに対し表2に示す炉内に還元剤として
コークス粉を供給した溶融処理では、集塵灰に含有され
る亜鉛分の約98%が揮発分へ移行し軽著な濃縮がおこ
なわれている。これは還元剤を炉内に供給した結果、溶
融過程で集塵灰に含有される酸化亜鉛が金属亜鉛に還元
され、金属亜鉛の沸点が溶融処理温度に比べて低いため
揮発分側に移行したものである。On the other hand, in the melting process in which coke powder was supplied as the reducing agent into the furnace shown in Table 2, about 98% of the zinc content contained in the dust ash was transferred to the volatile content, resulting in a light concentration. Has been. As a result of supplying the reducing agent into the furnace, the zinc oxide contained in the dust ash was reduced to metallic zinc in the melting process, and since the boiling point of metallic zinc was lower than the melting treatment temperature, it moved to the volatile content side. It is a thing.
【0008】この試験結果から、亜鉛を含有する固形物
を溶融処理するにあたって、還元剤を供給することによ
り固形物中の亜鉛分を還元し亜鉛蒸気としてガス中に揮
散濃縮させ冷却固化して回収しうることがわかる。ま
た、回収した固化物を被処理物側に循環し溶融処理を繰
り返す事により更に高濃度での亜鉛の濃縮回収が可能と
なる。From the results of this test, when the solid material containing zinc is melt-processed, the reducing agent is supplied to reduce the zinc content in the solid material, and the zinc content is volatilized and concentrated in the gas as zinc vapor to be cooled and solidified and recovered. I understand that it is possible. Further, by circulating the recovered solidified substance to the object side and repeating the melting process, it becomes possible to concentrate and recover zinc at a higher concentration.
【0009】[0009]
【表1】 [Table 1]
【0010】[0010]
【表2】 [Table 2]
【0011】さらに、回収した固化物はNaCl,KC
l等の水溶性成分を含むことから、これを水洗処理し水
溶性成分を除去したのち被処理物側に循環し溶融処理を
繰り返す事によって、より効果的な濃縮回収が可能とな
る。Further, the recovered solidified product is NaCl, KC.
Since a water-soluble component such as 1 is contained, it can be more effectively concentrated and recovered by washing it with water to remove the water-soluble component and then circulating it to the side of the object to be processed and repeating the melting process.
【0012】図1に本発明を廃棄物焼却炉の集塵灰に適
用した実施例のフローを示す。廃棄物焼却炉の集塵灰a
は、溶融炉のガス灰の一部bとともに水洗処理装置lに
て水洗され、水洗処理灰eとして溶融炉2に供給され
る。ここで、灰中の亜鉛分は溶融炉に供給された還元剤
fの作用により還元され亜鉛蒸気となって、排ガスh1
に移行する。FIG. 1 shows a flow chart of an embodiment in which the present invention is applied to dust ash of a waste incinerator. Waste ash from waste incinerator a
Is washed with a part (b) of the gas ash of the melting furnace in the water washing treatment device l and supplied to the melting furnace 2 as the washing ash e. Here, the zinc content in the ash is reduced by the action of the reducing agent f supplied to the melting furnace to become zinc vapor, and the exhaust gas h 1
Move to.
【0013】溶融炉で発生する溶融スラグgは炉外に排
出され、亜鉛蒸気を含む排ガスh1はガス燃焼炉3で燃
焼され、さらにガス冷却塔4で冷却される。冷却された
排ガスh3は集塵装置5に供給され、排ガス中の固形分
がガス灰として捕集される。ここで、排気ガス中の亜鉛
分は冷却によって固化されガス灰に移行する。亜鉛分が
濃縮した溶融炉のガス灰は、その一部bを溶融炉の供給
側に循環し、一部kを系外に回収する。The molten slag g generated in the melting furnace is discharged to the outside of the furnace, the exhaust gas h 1 containing zinc vapor is burned in the gas combustion furnace 3, and further cooled in the gas cooling tower 4. The cooled exhaust gas h 3 is supplied to the dust collector 5, and the solid content in the exhaust gas is collected as gas ash. Here, the zinc content in the exhaust gas is solidified by cooling and transferred to gas ash. The gas ash of the melting furnace in which the zinc content is concentrated circulates part b of the gas ash on the supply side of the melting furnace and recovers part k out of the system.
【0014】[0014]
【発明の効果】本発明によって、従来、亜鉛分の回収が
行われなかった固形物から有価物として亜鉛を回収する
ことが可能となる。Industrial Applicability According to the present invention, it is possible to recover zinc as a valuable resource from a solid material which has not been recovered in the past.
【図1】本発明を廃棄物焼却炉の集塵灰に適用した実施
例のフロー図である。FIG. 1 is a flow chart of an example in which the present invention is applied to dust ash of a waste incinerator.
a:廃棄物焼却炉の集塵灰、 b:溶融炉のガス灰(循
環分)、 c:灰の洗浄用水、 d:洗浄排水、 e:
水洗処理灰、 f:還元剤、 g:溶融スラグ、h1,
h2,h3,h4:排ガス、 i:ガス燃焼用空気、
j:ガス冷却用水、k:溶融炉のガス灰(回収分)、
1:水洗処理装置、 2:溶融炉、 3:ガス燃焼炉、
4:ガス冷却塔、 5:集塵装置。a: Dust ash of waste incinerator, b: Gas ash (circulation) of melting furnace, c: Water for washing ash, d: Washing wastewater, e:
Washed ash, f: reducing agent, g: molten slag, h 1 ,
h 2, h 3, h 4 : exhaust gas, i: Air gas combustion,
j: gas cooling water, k: melting furnace gas ash (recovered portion),
1: Washing treatment device, 2: Melting furnace, 3: Gas combustion furnace,
4: Gas cooling tower, 5: Dust collector.
───────────────────────────────────────────────────── フロントページの続き (72)発明者 鍬塚 峻二 福岡県北九州市戸畑区大字中原46−59 新 日本製鐵株式会社機械・プラント事業部内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Shunji Tsukazuka 46-59 Nakahara, Tobata-ku, Kitakyushu City, Fukuoka Prefecture Nippon Steel Corporation Machinery & Plant Division
Claims (1)
理する方法において、還元剤を直接または前記固形物と
混合して溶融炉に供給し、固形物中の亜鉛分を還元し亜
鉛蒸気としてガス中に揮発させ、この亜鉛蒸気を含むガ
スを溶融炉外で冷却し亜鉛分を固化して捕集することを
特徴とする亜鉛の濃縮回収方法。1. A method for melting and treating a zinc-containing solid in a melting furnace, which comprises supplying a reducing agent directly or mixed with the solid to the melting furnace to reduce the zinc content in the solid to reduce zinc. A method for concentrating and recovering zinc, which comprises volatilizing the gas as a vapor into the gas, cooling the gas containing the zinc vapor outside the melting furnace, solidifying the zinc content, and collecting the zinc content.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5024410A JPH06240377A (en) | 1993-02-12 | 1993-02-12 | Method for concentrating and recovering zinc |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5024410A JPH06240377A (en) | 1993-02-12 | 1993-02-12 | Method for concentrating and recovering zinc |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH06240377A true JPH06240377A (en) | 1994-08-30 |
Family
ID=12137399
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP5024410A Pending JPH06240377A (en) | 1993-02-12 | 1993-02-12 | Method for concentrating and recovering zinc |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH06240377A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5884664A (en) * | 1991-09-10 | 1999-03-23 | Smc Kabushiki Kaisha | Fluid pressure apparatus |
-
1993
- 1993-02-12 JP JP5024410A patent/JPH06240377A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5884664A (en) * | 1991-09-10 | 1999-03-23 | Smc Kabushiki Kaisha | Fluid pressure apparatus |
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Legal Events
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Free format text: JAPANESE INTERMEDIATE CODE: A02 Effective date: 19991019 |