JP7790157B2 - Method for producing crude zinc oxide and method for treating flue dust - Google Patents
Method for producing crude zinc oxide and method for treating flue dustInfo
- Publication number
- JP7790157B2 JP7790157B2 JP2022004576A JP2022004576A JP7790157B2 JP 7790157 B2 JP7790157 B2 JP 7790157B2 JP 2022004576 A JP2022004576 A JP 2022004576A JP 2022004576 A JP2022004576 A JP 2022004576A JP 7790157 B2 JP7790157 B2 JP 7790157B2
- Authority
- JP
- Japan
- Prior art keywords
- zinc oxide
- crude zinc
- copper
- dust
- content
- 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.)
- Active
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
- Inorganic Compounds Of Heavy Metals (AREA)
- Manufacture And Refinement Of Metals (AREA)
Description
本発明は、粗酸化亜鉛の製造方法、及び、煙灰の処理方法に関する。本発明は、詳しくは、銅製錬炉で発生する煙灰を含む原料から粗酸化亜鉛を製造する方法、及び、銅製錬炉で発生する、亜鉛及び銅を含有する煙灰の処理方法に関するものである。 The present invention relates to a method for producing crude zinc oxide and a method for treating flue dust. More specifically, the present invention relates to a method for producing crude zinc oxide from raw materials containing flue dust generated in copper smelting furnaces, and a method for treating flue dust containing zinc and copper generated in copper smelting furnaces.
銅製錬炉で発生する排ガスから回収されるに煙灰は、銅精鉱に含まれる銅の他、揮発の容易な亜鉛、ビスマス等が多く含まれている。一般的には、銅製錬工程で発生する煙灰は、製錬目的の金属を含むため、再び、銅製錬炉へ繰り返して処理される。 The flue gas recovered from the exhaust gases generated in copper smelting furnaces contains not only the copper contained in the copper concentrate, but also large amounts of easily volatile elements such as zinc and bismuth. Generally, flue gas generated in the copper smelting process is recycled and returned to the copper smelting furnace, as it contains the metals that are the target of smelting.
しかしながら、上記の煙灰はビスマスを含有するため、これを銅製錬炉に繰り返すと、銅製錬工程で得られる銅アノード中のビスマス等の不純物品位が増加し、次工程である銅精製工程(電解工程)において得られる電気銅の不純物品位が増加する問題が顕在化する。 However, because the above-mentioned flue dust contains bismuth, if it is repeatedly fed into a copper smelting furnace, the impurity content of bismuth and other substances in the copper anodes obtained in the copper smelting process increases, resulting in the problem of an increased impurity content in the electrolytic copper obtained in the subsequent copper refining process (electrolysis process).
この問題について、特許文献1には、非鉄金属製錬において発生して回収される高濃度で鉛を含有する煙灰を、塩素を含有する鉄鋼ダストとの混合ペレットとしてから、粗酸化亜鉛製造プロセスにおける還元焙焼工程に投入することにより、従来の還元焙焼工程を有する鉄鋼ダストの処理方法と同様の方法で、煙灰を処理する方法が開示されている。 In response to this issue, Patent Document 1 discloses a method for treating flue dust, which contains high concentrations of lead and is generated and recovered during non-ferrous metal smelting, by mixing it with chlorine-containing steel dust to form pellets and then introducing the pellets into a reduction roasting process in a crude zinc oxide production process, in a manner similar to the conventional method for treating steel dust which involves a reduction roasting process.
ここで、粗酸化亜鉛の製造においては、多くの場合に原材料として鉄鋼ダストが用いられている。そして、この鉄鋼ダストを還元焙焼する工程で副産物として得られる還元鉄ペレットは、製鉄メーカーにおいて再び鉄源としてリサイクルされている。しかしながら、上記のように還元焙焼工程で処理される煙灰が、特に「銅」を含んでいる場合には、この銅が、上記の還元鉄ペレットに分配されてしまうことが新たな問題となる。「銅」は、還元鉄ペレットを用いる製鉄メーカーが、鉄源への混入を最も厳しく制限している不純物の一つであるからである。 In the production of crude zinc oxide, steel dust is often used as a raw material. Reduced iron pellets, a by-product of the process of reducing and roasting this steel dust, are recycled by steel manufacturers as a source of iron. However, when the flue gas processed in the reducing and roasting process, as described above, contains copper in particular, a new problem arises: this copper is distributed in the reduced iron pellets. This is because copper is one of the impurities that steel manufacturers that use reduced iron pellets place the strictest restrictions on inclusion in their iron sources.
本発明は、鉄鋼ダストを原材料として用いる粗酸化亜鉛の製造において、副産物であり鉄源として利用可能な還元鉄ペレットへの銅の混入を回避しながら、銅製錬炉で発生する亜鉛及び銅を含有する煙灰を、原材料の一部として有効に利用することができる酸化亜鉛の製造方法を提供することを課題とする。 The objective of the present invention is to provide a method for producing crude zinc oxide using steel dust as a raw material, which can effectively utilize flue dust containing zinc and copper generated in copper smelting furnaces as part of the raw material, while avoiding the contamination of reduced iron pellets, which are a by-product and can be used as an iron source, with copper.
本発明者らは、従来、一次原材料である鉄鋼ダストと共に粗酸化亜鉛の製造プロセス中の上流側工程である還元加熱工程に投入していた煙灰を、二次原材料として下流側の工程である乾燥加熱工程に直接投入するプロセスとすることにより上記課題を解決することができることに想到し、本発明を完成するに至った。本発明は、具体的に、以下のものを提供する。 The inventors of the present invention came up with the idea that the above-mentioned problems could be solved by changing the process so that flue dust, which was previously fed into the reduction heating process, an upstream step in the crude zinc oxide manufacturing process, together with the primary raw material, steel dust, is fed directly into the drying heating process, a downstream step, as a secondary raw material. Specifically, the present invention provides the following:
(1) 鉄鋼ダストを還元焙焼して粗酸化亜鉛ダストを得る、還元焙焼工程と、前記粗酸化亜鉛ダストに湿式処理を行って粗酸化亜鉛ケーキを得る、湿式工程と、前記粗酸化亜鉛ケーキを焼成して、粗酸化亜鉛焼鉱を得る、乾燥加熱工程と、を備える、粗酸化亜鉛の製造方法であって、前記乾燥加熱工程において、前記粗酸化亜鉛ケーキと共に、銅製錬炉で発生して回収された煙灰を焼成する、粗酸化亜鉛の製造方法。 (1) A method for producing crude zinc oxide comprising: a reduction roasting process in which steel dust is reduced and roasted to obtain crude zinc oxide dust; a wet process in which the crude zinc oxide dust is subjected to wet treatment to obtain crude zinc oxide cake; and a dry heating process in which the crude zinc oxide cake is calcined to obtain crude zinc oxide cinder; wherein in the dry heating process, flue dust generated in a copper smelting furnace and recovered is calcined together with the crude zinc oxide cake.
(1)の粗酸化亜鉛の製造方法によれば、鉄鋼ダストを原材料として用いる粗酸化亜鉛の製造において、副産物であり鉄源として利用可能な還元鉄ペレットへの銅の混入を回避しながら、銅を含有する煙灰を、原材料の一部として有効に利用することができる。そのため、還元鉄ペレットを製鉄メーカー向けの鉄源として出荷するに際して、銅品位が高いことにより出荷を見送る可能性を、大幅に低減することができる。 According to the crude zinc oxide manufacturing method (1), in the production of crude zinc oxide using steel dust as a raw material, copper-containing flue dust can be effectively used as part of the raw material while avoiding the contamination of reduced iron pellets, which are a by-product and can be used as an iron source. Therefore, when shipping reduced iron pellets to steel manufacturers as an iron source, the possibility of them being rejected due to high copper content can be significantly reduced.
(2) 鉄鋼ダストを還元焙焼して粗酸化亜鉛ダストを得る、還元焙焼工程と、前記粗酸化亜鉛ダストに湿式処理を行って粗酸化亜鉛ケーキを得る、湿式工程と、前記粗酸化亜鉛ケーキを焼成して、粗酸化亜鉛焼鉱を得る、乾燥加熱工程と、を備える、粗酸化亜鉛の製造方法であって、前記乾燥加熱工程において、前記粗酸化亜鉛ケーキと共に、亜鉛と銅を含み、銅の含有率が10%以上である煙灰を焼成する、粗酸化亜鉛の製造方法。 (2) A method for producing crude zinc oxide, comprising: a reduction roasting process in which steel dust is reduced and roasted to obtain crude zinc oxide dust; a wet process in which the crude zinc oxide dust is subjected to wet treatment to obtain crude zinc oxide cake; and a dry heating process in which the crude zinc oxide cake is calcined to obtain crude zinc oxide cinder, wherein in the dry heating process, flue dust containing zinc and copper, with a copper content of 10% or more, is calcined together with the crude zinc oxide cake.
(2)の粗酸化亜鉛の製造方法によれば、粗酸化亜鉛の製造現場において、亜鉛と銅を含み、特に銅の含有率が高い煙灰を原材料として用いる場合にも、副産物であり鉄源として利用可能な還元鉄ペレットへの銅の混入を回避しながら、銅を含有する煙灰を、原材料の一部として有効に利用することができる。 According to the method for producing crude zinc oxide (2), even when flue dust containing zinc and copper, with a particularly high copper content, is used as a raw material at the crude zinc oxide production site, the copper-containing flue dust can be effectively used as part of the raw material while avoiding the contamination of reduced iron pellets, which are a by-product and can be used as an iron source.
(3) 前記銅製錬炉が、銅製錬転炉である、(1)に記載の粗酸化亜鉛の製造方法。 (3) The method for producing crude zinc oxide described in (1), wherein the copper smelting furnace is a copper smelting converter.
(3)の粗酸化亜鉛の製造方法によれば、(1)に記載の粗酸化亜鉛の製造方法において、熔体から揮発して飛散する、沸点の比較的低い、鉛、亜鉛、ビスマス等を多く含む銅製錬転炉で発生する煙灰を用いることにより、鉛、亜鉛、ビスマスをより効率良く回収することができる。 According to the method for producing crude zinc oxide (3), in the method for producing crude zinc oxide described in (1), lead, zinc, and bismuth can be recovered more efficiently by using flue gas generated in a copper smelting converter, which has a relatively low boiling point and contains large amounts of lead, zinc, bismuth, etc., and which volatilizes and scatters from the molten metal.
(4) 前記煙灰は、鉛の含有率が12%以上で、亜鉛の含有率が4%以上である、(1)から(3)の何れかに記載の粗酸化亜鉛の製造方法。 (4) A method for producing crude zinc oxide according to any one of (1) to (3), wherein the flue dust has a lead content of 12% or more and a zinc content of 4% or more.
(4)の粗酸化亜鉛の製造方法によれば、(1)から(3)の何れかに記載の粗酸化亜鉛の製造方法において、目的金属である、亜鉛及び銅、並びに鉛を、高濃度で含有する煙灰を用いることにより、亜鉛及び銅、並びに鉛を、より効率良く、回収することができる。 According to the method for producing crude zinc oxide (4), in the method for producing crude zinc oxide described in any one of (1) to (3), by using flue dust containing high concentrations of the target metals, zinc, copper, and lead, it is possible to more efficiently recover zinc, copper, and lead.
(5) 銅製錬炉で発生して回収された煙灰であって、鉛の含有率が12%以上である煙灰を処理する煙灰処理方法であって、前記煙灰を粗酸化亜鉛製造プロセスにおける乾燥加熱工程に投入する二次原材料として用いる煙灰処理方法。 (5) A flue ash processing method for processing flue ash generated and recovered from a copper smelting furnace, which flue ash has a lead content of 12% or more, and which uses the flue ash as a secondary raw material to be input into a drying and heating step in a crude zinc oxide production process.
(5)の煙灰処理方法によれば、銅製錬炉で発生した煙灰であって高濃度で鉛を含有する煙灰を、鉄鋼ダストを原材料として用いる粗酸化亜鉛の製造において、副産物であり鉄源として利用可能な還元鉄ペレットへの銅の混入を回避しながら、有効に利用することができる。そのため、還元鉄ペレットを製鉄メーカー向けの鉄源として出荷するに際して、銅品位が高いことにより出荷を見送る可能性を、大幅に低減することができる。又、煙灰を、乾燥加熱工程で処理するため、上流側の工程である、還元焙焼工程、湿式工程を経る必要が無く、工程を削減することにより、煙灰処理にかかるコストを圧縮することができる。 According to the flue dust processing method (5), flue dust generated in copper smelting furnaces and containing high concentrations of lead can be effectively utilized in the production of crude zinc oxide using steel dust as a raw material, while avoiding copper contamination in reduced iron pellets, which are a by-product and can be used as an iron source. This significantly reduces the possibility that reduced iron pellets will be rejected due to their high copper content when shipped as an iron source to steel manufacturers. Furthermore, because the flue dust is processed in a dry heating process, there is no need to go through the upstream processes of the reduction roasting process and the wet process. By reducing the number of processes, the cost of flue dust processing can be reduced.
本発明によれば、鉄鋼ダストを原材料として用いる粗酸化亜鉛の製造において、副産物であり鉄源として利用可能な還元鉄ペレットへの銅の混入を回避しながら、銅を含有する煙灰を、原材料の一部として有効に利用することができる。 According to the present invention, in the production of crude zinc oxide using steel dust as a raw material, copper-containing flue dust can be effectively used as part of the raw material while avoiding the contamination of reduced iron pellets, which are by-products and can be used as an iron source.
以下、本発明の好ましい実施態様について適宜図面を参照しながら説明する。図1は、銅製錬において発生する煙灰を原材料の一部として用いる本発明の粗酸化亜鉛の製造方法の流れを示すフロー図である。 Preferred embodiments of the present invention will now be described with reference to the drawings as appropriate. Figure 1 is a flow diagram showing the process for producing crude zinc oxide of the present invention, which uses flue dust generated during copper smelting as part of the raw materials.
<粗酸化亜鉛の製造方法>
本発明の粗酸化亜鉛の製造方法は、鉄鋼業における高炉や電気炉等から発生する亜鉛を含有する鉄鋼ダストを原材料とし、当該原材料から不純物を除去して製品亜鉛の原料となる亜鉛品位65%程度の粗酸化亜鉛を製造するプロセスである。
<Method of producing crude zinc oxide>
The method for producing crude zinc oxide of the present invention is a process that uses zinc-containing steel dust generated from blast furnaces, electric furnaces, etc. in the steel industry as a raw material, and removes impurities from the raw material to produce crude zinc oxide with a zinc content of approximately 65%, which can be used as a raw material for zinc products.
本発明の粗酸化亜鉛の製造方法は、図1に基本的な流れを示す従来公知の粗酸化亜鉛製造プロセスP2を行うためのプロセスである。本発明の粗酸化亜鉛の製造方法においても、基本的な工程の流れは図1に示す従来方法と同様である。 The crude zinc oxide manufacturing method of the present invention is a process for carrying out the conventionally known crude zinc oxide manufacturing process P2, the basic flow of which is shown in Figure 1. In the crude zinc oxide manufacturing method of the present invention, the basic process flow is the same as the conventional method shown in Figure 1.
但し、本発明の粗酸化亜鉛の製造方法は、図1に示すように、銅製錬プロセスP1において銅製錬炉で発生して回収された煙灰等、亜鉛及び銅を少なくとも含有する煙灰(本明細書において「亜鉛・銅含有煙灰」とも言う。)を、二次原材料の一部として、粗酸化亜鉛製造プロセスP2の下流側の一工程である乾燥加熱工程ST23に直接投入することとした点を従来とは異なる新たな特徴とするプロセスである。 However, as shown in Figure 1, the crude zinc oxide production method of the present invention is a process with a new feature that differs from conventional processes in that flue dust containing at least zinc and copper (also referred to in this specification as "zinc-copper-containing flue dust"), such as flue dust generated and recovered from the copper smelting furnace in the copper smelting process P1, is directly input as part of the secondary raw material into the drying and heating process ST23, which is a process downstream of the crude zinc oxide production process P2.
本発明は、銅製錬において発生する「亜鉛・銅含有煙灰」を、粗酸化亜鉛製造プロセスP2における乾燥加熱工程ST23に投入することによって、副産物であり鉄源として利用可能な還元鉄ペレットへの銅の混入を回避しながら、高い回収率で亜鉛を回収して、上記の煙灰を二次原材料として有効利用することができるという点において、優れた粗酸化亜鉛の製造方法である。 The present invention is an excellent method for producing crude zinc oxide in that it recovers zinc at a high recovery rate while avoiding the contamination of reduced iron pellets, which are a by-product and can be used as an iron source, by feeding the "zinc- and copper-containing dust" generated during copper smelting into the drying and heating step ST23 in the crude zinc oxide production process P2, thereby enabling the dust to be effectively used as a secondary raw material.
又、本発明は、銅製錬において発生する「亜鉛・銅含有煙灰」を、既存の粗酸化亜鉛製造プロセス用のロータリーキルン等、新たな設備投資を行うまでもなく、既存設備において低コストで処理ができるという点において、優れた煙灰の処理方法でもある。 The present invention is also an excellent method for treating flue dust, in that it can process the "zinc- and copper-containing flue dust" generated during copper smelting at low cost using existing equipment, without the need for new capital investment, such as rotary kilns used in existing crude zinc oxide manufacturing processes.
<銅製錬プロセスP1>
本発明の粗酸化亜鉛の製造方法において二次原材料として用いる「亜鉛・銅含有煙灰」の供給源となる銅製錬プロセスP1は、銅精鉱から、銅品位98%前後の粗銅を得て最終的に電気銅を得るプロセスである。この銅製錬プロセスP1においては、一般的には、銅製錬の原料である銅精鉱が、先ず、自熔炉で処理されることで、銅品位60%前後のマットとスラグに分離される。ここで得られたマットは次に設けられている転炉工程に送られ、転炉で銅品位98%前後の粗銅となる。この後、次に設けられている精製炉で銅品位99%前後の精製粗銅となり、次に設けられている精製工程で処理するために、アノードとして鋳造される。精製工程では、このアノードから電気銅が得られる。
<Copper smelting process P1>
The copper smelting process P1, which is a supply source of the "zinc- and copper-containing flue dust" used as a secondary raw material in the method for producing crude zinc oxide of the present invention, is a process in which blister copper with a copper content of about 98% is obtained from copper concentrate, and finally electrolytic copper is obtained. In this copper smelting process P1, copper concentrate, which is the raw material for copper smelting, is generally first treated in a flash furnace to be separated into matte with a copper content of about 60% and slag. The matte obtained here is sent to the next converter process, where it is turned into blister copper with a copper content of about 98%. This is then turned into refined blister copper with a copper content of about 99% in the next refining furnace, and cast as anodes for processing in the next refining process. In the refining process, electrolytic copper is obtained from the anodes.
上述の自熔炉、転炉、精製炉では、それぞれ組成や性状の異なる煙灰が発生する。自熔炉で発生する煙灰は、フラッシュ・スメルティングであるため、精鉱等のキャリーオーバーも含まれ、銅品位が高いため、自熔炉へ繰り返し処理することが好ましい。又、精製炉で発生する煙灰は量そのものが非常に少ない。これに対して、転炉で発生する煙灰はバス・スメルティングであるため、熔体から揮発して飛散する沸点の比較的低い、鉛、亜鉛、ビスマス等を多く含む。従って、本発明の粗酸化亜鉛の製造方法において、原材料の一部とする「亜鉛・銅含有煙灰」(或いは、本発明の煙灰の処理方法によって処理対象とする「亜鉛・銅含有煙灰」)は、上記の様々な煙灰のうち、転炉から得られる、鉛、亜鉛品位の高い煙灰とすることが特に好ましい。或いは、本発明の粗酸化亜鉛の製造方法においては、このように銅製錬プロセスの転炉(本明細書において「銅製錬転炉」とも言う)で発生した煙灰を、銅製錬工程内で繰り返し処理した後に得られる、更に、鉛・亜鉛品位の増加した煙灰を用いることもできる。 The above-mentioned flash furnace, converter, and refining furnace each generate flue dust with different compositions and properties. The flue dust generated in a flash furnace is a flash smelting process, which includes carryover of concentrates and other materials. Because it has a high copper content, it is preferable to repeatedly process it in a flash furnace. Furthermore, the amount of flue dust generated in a refining furnace is very small. In contrast, the flue dust generated in a converter is a bath smelting process, which contains large amounts of lead, zinc, bismuth, and other elements with relatively low boiling points that volatilize and scatter from the molten metal. Therefore, in the method for producing crude zinc oxide of the present invention, it is particularly preferable that the "zinc- and copper-containing flue dust" used as part of the raw material (or the "zinc- and copper-containing flue dust" to be treated by the flue dust treatment method of the present invention) be flue dust with a high content of lead and zinc obtained from a converter, among the various flue dusts described above. Alternatively, in the method for producing crude zinc oxide of the present invention, flue dust generated in a converter in a copper smelting process (also referred to as a "copper smelting converter" in this specification) can be used, which is obtained by repeatedly treating the flue dust within the copper smelting process and has an increased content of lead and zinc.
又、本発明の粗酸化亜鉛の製造方法において、原材料の一部とする「亜鉛・銅含有煙灰」(或いは、本発明の煙灰の処理方法によって処理対象とする「亜鉛・銅含有煙灰」)が、亜鉛と銅を含み、銅の含有率が10%以上である場合に、従来技術に対するより顕著な優位性を発揮する。従来においては、このような銅の含有量の大きな煙灰を用いた場合には、還元鉄ペレットへの銅成分の混入により、鉄源としてのリサイクル利用が阻害されるリスクがあったが、上流側工程での煙灰の処理を回避して、下流側の乾燥加熱工程以降で煙灰処理を集中的に行うようにした本発明によれば、そのようなリスクは完全に回避することができる。 Furthermore, the method for producing crude zinc oxide of the present invention exhibits significant advantages over conventional techniques when the "zinc- and copper-containing flue dust" used as part of the raw material (or the "zinc- and copper-containing flue dust" to be treated by the flue dust treatment method of the present invention) contains zinc and copper, with a copper content of 10% or more. Conventionally, when flue dust with such a high copper content was used, there was a risk that the copper component would be mixed into reduced iron pellets, preventing them from being recycled as an iron source. However, this risk can be completely avoided by the present invention, which avoids flue dust treatment in upstream processes and instead concentrates flue dust treatment downstream after the drying and heating process.
又、本発明の粗酸化亜鉛の製造方法又は煙灰処理方法においては、上記の「亜鉛・銅含有煙灰」は、鉛の含有率が12%以上で、亜鉛の含有率が4%以上であることが好ましい。高濃度の鉛を含有する煙灰は、銅製錬の現場では繰り返し処理しても、再度揮発してしまい、工程内で循環する物量が大幅に増加してしまう。一方で、このような鉛含有量の大きい「亜鉛・銅含有煙灰」を本発明の製造方法・処理方法に投入することにより、粗酸化亜鉛の製造プロセス、及び、これに引き続く鉛・亜鉛の製造プロセスにおいて、鉛及び亜鉛、並びに銅を、より効率良く、回収することができる。 Furthermore, in the crude zinc oxide production method or flue dust treatment method of the present invention, the above-mentioned "zinc- and copper-containing flue dust" preferably has a lead content of 12% or more and a zinc content of 4% or more. Even if flue dust containing high concentrations of lead is repeatedly treated at copper smelting sites, it will volatilize again, significantly increasing the amount of material circulating within the process. On the other hand, by feeding such "zinc- and copper-containing flue dust" with a high lead content into the production and treatment methods of the present invention, lead, zinc, and copper can be recovered more efficiently in the crude zinc oxide production process and the subsequent lead and zinc production process.
<粗酸化亜鉛製造プロセスP2>
粗酸化亜鉛製造プロセスP2は、以下に詳細を説明する、還元焙焼工程ST21、湿式工程ST22、及び、乾燥加熱工程ST23が順次行われるプロセスである。
<Crude zinc oxide production process P2>
The crude zinc oxide production process P2 is a process in which a reduction roasting step ST21, a wet step ST22, and a dry heating step ST23 are sequentially performed, as will be described in detail below.
[還元焙焼工程ST21]
還元焙焼工程ST21では、鉄鋼ダスト等の一次原材料を還元雰囲気中で適当な温度と滞留時間を選んで焙焼することにより、亜鉛、鉛等を還元揮発させて分離し、更に再酸化させることにより粗酸化亜鉛ダストを得る工程である。又、その一方で、この工程では、鉄を固体の還元鉄ペレットとして回収する。この工程を行う還元焙焼炉としてはロータリーキルンを好適に用いることができる。
[Reduction roasting step ST21]
In the reducing roasting step ST21, primary raw materials such as steel dust are roasted in a reducing atmosphere at an appropriate temperature and residence time to reduce and volatilize zinc, lead, and other components, which are then reoxidized to obtain crude zinc oxide dust. Also, in this step, iron is recovered as solid reduced iron pellets. A rotary kiln is preferably used as the reducing roasting furnace for this step.
[湿式工程ST22]
湿式工程ST22は、還元焙焼工程ST21を経て再酸化され、酸化亜鉛及び酸化鉛を含む粗酸化亜鉛ダストから、湿式処理により、更に、塩素、フッ素等の他の残存不純物を除去して粗酸化亜鉛の脱水ケーキ(本明細書において「粗酸化亜鉛ケーキ」とも言う)を得る工程である。湿式工程ST22は、従来公知の方法を用いて行なうことができる。
[Wet process ST22]
The wet process ST22 is a process for obtaining a dehydrated cake of crude zinc oxide (also referred to as "crude zinc oxide cake" in this specification) by further removing remaining impurities such as chlorine and fluorine from the crude zinc oxide dust that has been reoxidized through the reducing roasting process ST21 and contains zinc oxide and lead oxide. The wet process ST22 can be performed using a conventionally known method.
[乾燥加熱工程ST23]
乾燥加熱工程ST23は、湿式工程ST22を経た粗酸化亜鉛ケーキを焼成して粗酸化亜鉛焼鉱を得る工程である。この工程により、亜鉛品位65%程度の粗酸化亜鉛の焼鉱(本明細書において「粗酸化亜鉛焼鉱」とも言う)を得ることができる。
[Drying heating step ST23]
The dry heating step ST23 is a step in which the crude zinc oxide cake that has been subjected to the wet step ST22 is calcined to obtain crude zinc oxide cinder. This step allows for the production of crude zinc oxide cinder (also referred to as "crude zinc oxide cinder" in this specification) with a zinc content of about 65%.
乾燥加熱工程ST23は、ロータリーキルンを使用し、このロータリーキルンの装入端から原料である粗酸化亜鉛ケーキ、及び、その他の二次原材料を装入する。ロータリーキルンの排出端側にはバーナーが設けられており、このバーナーにより、ロータリーキルン内の原料を乾燥、加熱、焼成し、排出端側では800℃から900℃程度に焼成された粗酸化亜鉛焼鉱を得る。 The drying and heating process ST23 uses a rotary kiln, and the raw material, crude zinc oxide cake, and other secondary raw materials are charged into the charging end of the rotary kiln. A burner is installed at the discharge end of the rotary kiln, and this burner dries, heats, and burns the raw materials inside the rotary kiln, producing crude zinc oxide cinder at the discharge end, which has been burned to approximately 800°C to 900°C.
本発明の粗酸化亜鉛の製造方法において、原材料の一部として用いられる上述の銅を含有する煙灰は、この乾燥加熱工程ST23に二次原材料の一部として投入される。 In the crude zinc oxide manufacturing method of the present invention, the copper-containing flue dust used as part of the raw materials is added to this drying and heating step ST23 as part of the secondary raw materials.
尚、煙灰を処理するにあたり、この煙灰に多く含まれる、銅、錫、ビスマスについて、得られる粗酸化亜鉛中の品位を不純物バランスから予想し、粗酸化亜鉛の製造工程の更に下流側の工程として設けられている鉛・亜鉛製錬の脱銅工程で回収されることを前提とした工程基準内となるように、煙灰の処理量を決める。又、乾燥加熱工程ST23において得られた粗酸化亜鉛についても、一定の頻度で分析を行い、上記基準内であることを確認する。 When processing the flue dust, the grade of copper, tin, and bismuth, which are contained in large amounts in the flue dust, is predicted from the impurity balance in the resulting crude zinc oxide, and the amount of flue dust to be processed is determined so that it falls within process standards, assuming that it will be recovered in the copper removal process of the lead-zinc smelting process, which is established as a process further downstream in the crude zinc oxide manufacturing process. The crude zinc oxide obtained in the drying and heating process ST23 is also analyzed at regular intervals to confirm that it falls within the above standards.
又、上記の煙灰を、そのままの形状で乾燥加熱工程に投入すると搬送設備での発塵やロータリーキルンからの排ガスと共にキャリーオーバーしてロータリーキルンに続けて設けられている煙道や洗浄塔の多孔板に付着、これらを閉塞させてしまう。そこで、これを避けるために、煙灰を事前に造粒してペレット状にするか、或いは、事前に、乾燥加熱工程で処理される脱水ケーキ以外の澱物(水分20%~50%)等の原料とローダーで混練して処理することが好ましい。 Furthermore, if the above-mentioned flue dust is introduced into the drying and heating process in its original form, it will be carried over along with dust generated in the conveying equipment and exhaust gas from the rotary kiln, adhering to the perforated plates of the flue and washing tower connected to the rotary kiln and causing blockages. Therefore, to avoid this, it is preferable to granulate the flue dust into pellets in advance, or to mix and process it in advance in a loader with raw materials other than the dehydrated cake to be processed in the drying and heating process, such as sediment (with a moisture content of 20% to 50%).
以下、実施例及び比較例により本発明を更に具体的に説明するが、本発明は、以下の実施例に限定されるものではない。 The present invention will be explained in more detail below using examples and comparative examples, but the present invention is not limited to the following examples.
[実施例]
図1に示す流れで酸化亜鉛製造の試験操業を行った。二次原材料の一部として用いる煙灰としては、銅製錬工場で転炉において発生して回収された煙灰を用いた。この煙灰の組成は下記表1の通りであった。乾燥加熱工程では、上記煙灰を1t/日と、粗酸化亜鉛ケーキ170t/日を、温度800℃~900℃で乾燥、加熱して粗酸化亜鉛焼鉱を得た。粗酸化亜鉛焼鉱の銅品位は、0.21%、錫品位は0.09%、ビスマス品位は0.10%であり、鉛・亜鉛製錬原料として出荷した。又、銅、錫、ビスマスについては、粗酸化亜鉛の製造に続いて行われる、鉛・亜鉛製錬の脱銅工程において、分離・回収した。尚、還元焙焼工程では、鉄鋼ダスト200t/日を、温度1100℃~1200℃で還元焙焼して、酸化亜鉛を含む粗酸化亜鉛ダストと還元鉄ペレットを得て、製鉄メーカー向けの鉄源として出荷した。
[Example]
A trial run for zinc oxide production was conducted according to the flow chart shown in Figure 1. The flue dust used as part of the secondary raw material was flue dust generated in a converter at a copper smelting plant and recovered. The composition of this flue dust was as shown in Table 1 below. In the drying and heating process, 1 ton/day of the flue dust and 170 t/day of crude zinc oxide cake were dried and heated at temperatures of 800 to 900°C to obtain crude zinc oxide cinder. The crude zinc oxide cinder had a copper content of 0.21%, a tin content of 0.09%, and a bismuth content of 0.10%, and was shipped as a raw material for lead-zinc smelting. Copper, tin, and bismuth were separated and recovered in the copper removal process of lead-zinc smelting, which was carried out following the production of crude zinc oxide. In the reduction roasting step, 200 t/day of steel dust was reduced and roasted at a temperature of 1100°C to 1200°C to obtain crude zinc oxide dust containing zinc oxide and reduced iron pellets, which were shipped as iron sources to steel manufacturers.
[比較例]
上記の煙灰を、従来プロセスと同様、鉄鋼ダスト等の原材料と共に、還元焙焼工程に投入して処理したことの他については、実施例と同一条件で試験操業を行った。還元焙焼工程では、上記煙灰を1t/日と、鉄鋼ダスト200t/日を、温度1100℃~1200℃で還元焙焼して、酸化亜鉛を含む粗酸化亜鉛ダストと還元鉄ペレットを得た。還元鉄ペレットの銅品位は、0.46%、錫品位は0.053%、ビスマス品位は0.092%であり、製鉄メーカー向けの鉄源としての出荷を見送った。
[Comparative Example]
A test run was carried out under the same conditions as in the example, except that the flue dust was fed to a reduction roasting process together with raw materials such as steel dust, as in the conventional process. In the reduction roasting process, 1 ton/day of the flue dust and 200 t/day of steel dust were reduction roasted at temperatures of 1100°C to 1200°C to obtain crude zinc oxide dust containing zinc oxide and reduced iron pellets. The reduced iron pellets had a copper content of 0.46%, a tin content of 0.053%, and a bismuth content of 0.092%, and were therefore not shipped as an iron source to steel manufacturers.
本発明の粗酸化亜鉛の製造方法によれば、既存のプロセス及び設備の流用により、銅製錬において発生する亜鉛及び銅を含有する煙灰処理に要するコストを大幅に削減できる。又、銅による既存プロセスへの悪影響も防止できるため、既存の粗酸化亜鉛製造の操業において、還元鉄ペレットの品質も保持することができ、その上で、煙灰に含有される亜鉛及び銅、並びに鉛を高い回収率で回収することができることが分かる。 The crude zinc oxide production method of the present invention can significantly reduce the costs required to process flue dust containing zinc and copper generated during copper smelting by utilizing existing processes and equipment. Furthermore, because the adverse effects of copper on existing processes can be prevented, the quality of reduced iron pellets can be maintained in existing crude zinc oxide production operations, and the zinc, copper, and lead contained in the flue dust can be recovered at a high recovery rate.
P1 銅製錬プロセス
P2 粗酸化亜鉛製造プロセス
ST21 還元焙焼工程
ST22 湿式工程
ST23 乾燥加熱工程
P1 Copper smelting process P2 Crude zinc oxide production process ST21 Reduction roasting process ST22 Wet process ST23 Dry heating process
Claims (4)
前記粗酸化亜鉛ダストに湿式処理を行って粗酸化亜鉛ケーキを得る、湿式工程と、
前記粗酸化亜鉛ケーキを焼成して、粗酸化亜鉛焼鉱を得る、乾燥加熱工程と、
を備える、粗酸化亜鉛の製造方法であって、
前記乾燥加熱工程において、前記粗酸化亜鉛ケーキと共に、銅製錬炉で発生して回収され、亜鉛と鉛と銅を含み、鉛の含有率が12%以上であり、亜鉛の含有率が4%以上であり、銅の含有率が10%以上である煙灰を焼成する、
粗酸化亜鉛の製造方法。 a reduction roasting step of reducing and roasting the steel dust to obtain crude zinc oxide dust;
a wet process for wet treating the crude zinc oxide dust to obtain a crude zinc oxide cake;
a dry heating step of calcining the crude zinc oxide cake to obtain crude zinc oxide cinder;
A method for producing crude zinc oxide, comprising:
In the drying and heating step, flue dust, which is generated in a copper smelting furnace and recovered, contains zinc, lead, and copper, and has a lead content of 12% or more, a zinc content of 4% or more, and a copper content of 10% or more, is calcined together with the crude zinc oxide cake.
Method for producing crude zinc oxide.
請求項1に記載の粗酸化亜鉛の製造方法。The method for producing crude zinc oxide according to claim 1.
請求項1に記載の粗酸化亜鉛の製造方法。 The copper smelting furnace is a copper smelting converter.
The method for producing crude zinc oxide according to claim 1.
前記粗酸化亜鉛製造プロセスは、鉄鋼ダストを還元焙焼して粗酸化亜鉛ダストを得る還元焙焼工程と、前記粗酸化亜鉛ダストに湿式処理を行って粗酸化亜鉛ケーキを得る湿式工程と、前記粗酸化亜鉛ケーキを焼成して粗酸化亜鉛焼鉱を得る乾燥加熱工程とを備え、
前記煙灰を粗酸化亜鉛製造プロセスにおける前記乾燥加熱工程に投入する二次原材料として用いる煙灰処理方法。 1. A flue ash treatment method for subjecting flue ash generated in a copper smelting furnace and recovered, the flue ash having a lead content of 12% or more, a zinc content of 4% or more, and a copper content of 10% or more, to a process for producing crude zinc oxide , comprising:
The process for producing crude zinc oxide comprises a reduction roasting step of reducing and roasting iron and steel dust to obtain crude zinc oxide dust, a wet process of subjecting the crude zinc oxide dust to wet treatment to obtain crude zinc oxide cake, and a dry heating step of calcining the crude zinc oxide cake to obtain crude zinc oxide cinder,
The flue ash treatment method uses the flue ash as a secondary raw material to be input into the drying and heating step in the process for producing crude zinc oxide.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2022004576A JP7790157B2 (en) | 2022-01-14 | 2022-01-14 | Method for producing crude zinc oxide and method for treating flue dust |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2022004576A JP7790157B2 (en) | 2022-01-14 | 2022-01-14 | Method for producing crude zinc oxide and method for treating flue dust |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JP2023103823A JP2023103823A (en) | 2023-07-27 |
| JP7790157B2 true JP7790157B2 (en) | 2025-12-23 |
Family
ID=87378405
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2022004576A Active JP7790157B2 (en) | 2022-01-14 | 2022-01-14 | Method for producing crude zinc oxide and method for treating flue dust |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP7790157B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN117804234B (en) * | 2023-12-29 | 2025-09-23 | 安徽锦华氧化锌有限公司 | An oxygen injection calcination device for zinc oxide production |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2013139618A (en) | 2012-01-06 | 2013-07-18 | Sumitomo Metal Mining Co Ltd | Treatment method for smoke ash |
| JP2018079456A (en) | 2016-11-18 | 2018-05-24 | 住友金属鉱山株式会社 | Exhaust gas treatment method in zinc oxide ore production plant |
| JP2020097760A (en) | 2018-12-17 | 2020-06-25 | 住友金属鉱山株式会社 | Manufacturing method of zinc oxide ore |
| JP2021123778A (en) | 2020-02-07 | 2021-08-30 | 住友金属鉱山株式会社 | Method of manufacturing zinc oxide ore |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2848003B2 (en) * | 1991-03-13 | 1999-01-20 | 住友金属鉱山株式会社 | Method for recovering lead and zinc from copper converter dust leach residue |
-
2022
- 2022-01-14 JP JP2022004576A patent/JP7790157B2/en active Active
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2013139618A (en) | 2012-01-06 | 2013-07-18 | Sumitomo Metal Mining Co Ltd | Treatment method for smoke ash |
| JP2018079456A (en) | 2016-11-18 | 2018-05-24 | 住友金属鉱山株式会社 | Exhaust gas treatment method in zinc oxide ore production plant |
| JP2020097760A (en) | 2018-12-17 | 2020-06-25 | 住友金属鉱山株式会社 | Manufacturing method of zinc oxide ore |
| JP2021123778A (en) | 2020-02-07 | 2021-08-30 | 住友金属鉱山株式会社 | Method of manufacturing zinc oxide ore |
Also Published As
| Publication number | Publication date |
|---|---|
| JP2023103823A (en) | 2023-07-27 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JP5862305B2 (en) | Smoke ash treatment method | |
| JP6094467B2 (en) | Method for producing zinc oxide ore | |
| JP5904073B2 (en) | Method for producing zinc oxide ore | |
| JP6098499B2 (en) | Method for producing zinc oxide ore | |
| JP7151404B2 (en) | Method for producing zinc oxide ore | |
| JP7790157B2 (en) | Method for producing crude zinc oxide and method for treating flue dust | |
| JP6094468B2 (en) | Method for producing zinc oxide ore | |
| JP2014084509A (en) | Production method of zinc oxide ore | |
| JP2016166381A (en) | Method for producing zinc oxide ore | |
| JP6123930B2 (en) | Method for producing zinc oxide ore | |
| JP2008545888A (en) | Separation of valuable metal from zinc leaching residue | |
| EA033630B1 (en) | Treatment of complex sulfide concentrate | |
| UA130003C2 (en) | METHOD FOR PRODUCING A PRODUCT CONTAINING SECONDARY RAW MATERIAL FROM INDUSTRIAL DUST AND A PRODUCT PRODUCED BY THE SAME METHOD | |
| JP7400401B2 (en) | Method for producing zinc oxide ore | |
| JP2020132970A (en) | Producing method of zinc oxide ore | |
| JPH0461043B2 (en) | ||
| RU2051193C1 (en) | Method for elimination of rhenium and osmium into gaseous phase from plumbous rhenium-bearing dusts and copper production sulfuric acid sludges | |
| JP6090080B2 (en) | Operation method of reduction roasting furnace | |
| JP7183502B2 (en) | Method for producing zinc oxide ore | |
| Fang et al. | Improving the applicability of F/Cl/Tl removal processes in secondary high ZnO dusts produced from a rotary hearth furnace by adjusting the feed composition | |
| RU2842910C1 (en) | Method of extracting volatile fractions from industrial dust | |
| CN85106965A (en) | Method for recovery of valuable metal components from contaminated copper feedstock | |
| JP7654994B2 (en) | Clinker manufacturing method | |
| JP7669899B2 (en) | Method for producing iron-containing clinker | |
| RU2051192C1 (en) | Method for elimination of rhenium and osmium into gaseous phase from plumbous rhenium-bearing dusts and copper production sulfuric acid sludges |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| A621 | Written request for application examination |
Free format text: JAPANESE INTERMEDIATE CODE: A621 Effective date: 20241015 |
|
| A131 | Notification of reasons for refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A131 Effective date: 20250805 |
|
| A977 | Report on retrieval |
Free format text: JAPANESE INTERMEDIATE CODE: A971007 Effective date: 20250805 |
|
| A521 | Request for written amendment filed |
Free format text: JAPANESE INTERMEDIATE CODE: A523 Effective date: 20251002 |
|
| TRDD | Decision of grant or rejection written | ||
| A01 | Written decision to grant a patent or to grant a registration (utility model) |
Free format text: JAPANESE INTERMEDIATE CODE: A01 Effective date: 20251111 |
|
| A61 | First payment of annual fees (during grant procedure) |
Free format text: JAPANESE INTERMEDIATE CODE: A61 Effective date: 20251124 |
|
| R150 | Certificate of patent or registration of utility model |
Ref document number: 7790157 Country of ref document: JP Free format text: JAPANESE INTERMEDIATE CODE: R150 |