JPH0796264A - Lead removal method from lead glass cuttings - Google Patents

Lead removal method from lead glass cuttings

Info

Publication number
JPH0796264A
JPH0796264A JP24252993A JP24252993A JPH0796264A JP H0796264 A JPH0796264 A JP H0796264A JP 24252993 A JP24252993 A JP 24252993A JP 24252993 A JP24252993 A JP 24252993A JP H0796264 A JPH0796264 A JP H0796264A
Authority
JP
Japan
Prior art keywords
lead
glass
lead glass
phase
cutting chips
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
Application number
JP24252993A
Other languages
Japanese (ja)
Inventor
Hidetoshi Noda
英俊 野田
Michio Nakayama
道夫 中山
Yoshinori Kato
昌憲 加藤
Hideyuki Yoshikoshi
英之 吉越
Shingo Ikeda
伸晤 池田
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
KOKAN KOGYO KK
Kokan Mining Co Ltd
JFE Engineering Corp
Original Assignee
KOKAN KOGYO KK
Kokan Mining Co Ltd
NKK Corp
Nippon Kokan Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by KOKAN KOGYO KK, Kokan Mining Co Ltd, NKK Corp, Nippon Kokan Ltd filed Critical KOKAN KOGYO KK
Priority to JP24252993A priority Critical patent/JPH0796264A/en
Publication of JPH0796264A publication Critical patent/JPH0796264A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling

Landscapes

  • Manufacture And Refinement Of Metals (AREA)
  • Processing Of Solid Wastes (AREA)

Abstract

PURPOSE:To remove lead from the cut refuse of lead glass by melting and separating the cut refuse of lead glass so as not to elute a lead component in order to prevent environmental pollution. CONSTITUTION:An Na2O component is added to the cut refuse of lead glass to adjust the SiO2/Na2O wt. ratio in lead glass to 1.2-3.0 and, further, a carbon source such as coke or charcoal is mixed with the cut refuse as a reducing agent and the resulting mixture is heated and melted at 800 deg.C or higher in a two-phase or three-phase Heroult electric furnace to separate lead in the cut refuse of lead glass. This method is accepted by both of Japanese and American standards of a Pb elution test and effective for avoiding environmental pollution accompanied by the elution of lead.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】この発明は鉛ガラス切削屑等の廃
棄物から、鉛の溶出を防止するための鉛ガラス切削屑か
らの脱鉛方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for deleading lead glass cutting chips from waste such as lead glass cutting chips to prevent the elution of lead.

【0002】[0002]

【従来の技術】一般に、光学レンズに用いられる鉛ガラ
ス中には20重量%以上のPbOを含有している。この
鉛ガラスを光学レンズに加工する過程では、ガラスの切
断,研磨工程が入るため多量の切削屑を発生する。これ
まで、この鉛ガラスの切削屑はダストとして焼却処理さ
れていたが、近年Pbの溶出の規制が厳しくなり、これ
ら鉛分の溶出防止に対する技術開発が望まれていた。従
来、鉛ガラス切削屑は廃棄物として焼却するか、或いは
セメント又は有機物で被覆して投棄するような方法で処
理されてきた。焼却した場合には、Pb分が大気中に飛
散し、また被覆投棄する場合にはPb分が溶出するた
め、いずれの方法においても公害防止の観点から大きな
問題となっていた。
2. Description of the Related Art Generally, lead glass used for optical lenses contains 20% by weight or more of PbO. In the process of processing this lead glass into an optical lens, a large amount of cutting chips are generated because of the glass cutting and polishing steps. Up to now, the cutting waste of the lead glass has been incinerated as dust, but in recent years the regulation of the elution of Pb has become stricter, and technical development for preventing the elution of these lead components has been desired. Heretofore, lead glass cuttings have been treated by a method such as incineration as waste, or coating with cement or organic matter and disposal. In the case of incineration, the Pb content scatters into the atmosphere, and in the case of coating and discarding, the Pb content elutes. Therefore, any method has been a serious problem from the viewpoint of pollution prevention.

【0003】[0003]

【発明が解決しようとする課題】本発明は、かかる事情
に鑑みてなされたもので、上記の公害防止の課題を解決
するため、鉛ガラス切削屑を溶融し鉛を分離することに
より、Pb分が溶出しない鉛ガラス切削屑からの脱鉛方
法を提供することを目的とする。
SUMMARY OF THE INVENTION The present invention has been made in view of such circumstances, and in order to solve the above-mentioned problem of pollution prevention, by melting lead glass cutting chips and separating lead, Pb content is reduced. It is an object of the present invention to provide a method for removing lead from cutting chips of lead glass that does not elute.

【0004】[0004]

【課題を解決するための手段】本発明は、鉛ガラス切削
屑にコークス又は木炭等の炭素源を還元剤として混合し
800℃以上に加熱溶融処理することにより、鉛を分離
することを特徴とする鉛ガラス切削屑からの脱鉛方法で
あり、この方法において、前記鉛ガラス切削屑にNa2
O成分を添加し、含有SiO2 とNa2 Oの重量比(以
下含有SiO2 重量と含有Na2 O重量比をSiO2
Na2 O重量比という)を1.2〜3.0の範囲となる
ように調整し、加熱溶融処理することを特徴とし、さら
に、加熱溶融処理において、溶融物を溶融状態で排出
し、急冷凝固させた後、鉛を分離することを特徴とし、
また、上記の加熱溶融処理を2相又は3相エール式電気
炉にて行うことを特徴とする鉛ガラス切削屑からの脱鉛
方法である。
The present invention is characterized in that lead glass is separated by mixing lead glass cuttings with a carbon source such as coke or charcoal as a reducing agent and heating and melting the mixture at 800 ° C. or higher. a lead-free process from lead glass swarf which, Na 2 in this method, the lead glass swarf
O component is added, and the weight ratio of the contained SiO 2 and Na 2 O (hereinafter, the weight ratio of the contained SiO 2 and the contained Na 2 O is SiO 2 /
Na 2 O weight ratio) is adjusted to be in the range of 1.2 to 3.0, and the mixture is heated and melted. Further, in the heating and melting treatment, the melt is discharged in a molten state and rapidly cooled. Characterized by separating lead after solidification,
Further, it is a method for removing lead from cutting chips of lead glass, characterized in that the heating and melting treatment is carried out in a two-phase or three-phase ale type electric furnace.

【0005】[0005]

【作用】光学ガラスの加工工程では、成分の異なる各種
のガラスを、ダイヤモンドカッターにより切削後、油性
または水性の研磨材等により研磨するため、切削屑中に
はガラス成分以外のSiO2 ,Al2 3 ,CaO等の
多種の無機物や有機物が不純物として混入している。従
って、ガラス切削屑の構成成分として考えられる無機物
成分の総量は、後述する表1に示す如く、50重量%前
後と極めて低い。鉛ガラス中のPbはPbOの状態で固
溶している。従って鉛ガラス切削屑中のPbOを除去す
るにはコークス又は木炭等の炭素源を還元剤として添加
し、800℃以上に加熱溶融処理することによって、鉛
ガラス中のPbOは還元剤により、次式に示すような反
応が進行する。 PbO+C→Pb+CO 即ち、鉛ガラス中のPbOは還元剤Cにより還元され
bとCOとなり、生成COは揮散する。この場合、ガラ
ス相の流動性が充分に大きいと還元されたPbが溶融ガ
ラス相から分離する。
In the process of processing optical glass, various kinds of glass having different components are cut with a diamond cutter and then polished with an oily or water-based abrasive, so that the cutting chips contain SiO 2 , Al 2 other than glass components. Various inorganic and organic substances such as O 3 and CaO are mixed as impurities. Therefore, the total amount of the inorganic components considered as the constituent components of the glass cutting waste is extremely low, around 50% by weight, as shown in Table 1 described later. Pb in lead glass is in solid solution in the state of PbO. Therefore, in order to remove PbO in the lead glass cutting wastes, a carbon source such as coke or charcoal is added as a reducing agent, and by heating and melting at 800 ° C or higher, PbO in the lead glass is reduced by the following formula. The reaction as shown in FIG. PbO + C → Pb + CO That is, PbO in the lead glass is reduced by the reducing agent C to P
b and CO, and the produced CO is volatilized. In this case, if the fluidity of the glass phase is sufficiently large, the reduced Pb will separate from the molten glass phase.

【0006】しかし、鉛ガラス切削屑中には、前述の如
くガラス成分以外に、切削及び研磨工程でSiO2 ,A
2 3 ,CaO等や有機物が混入するため、加熱溶融
処理に当たっては、ガラス構成成分のPbOが上式の如
く還元されて、ガラス成分から分離するためガラス成分
の融点が上昇し、鉛の分離が困難になる。そこで、本発
明者らは種々研究した結果、鉛ガラス切削屑にコークス
又は木炭等の炭素源を還元剤として混合し加熱溶融処理
するに際し、後述する実施例に示す如く、SiO2 /N
2 O重量比を1.2〜3.0の範囲になるように調整
して加熱溶融処理すると、鉛の分離が容易になることを
知見した。そこで、本発明では、必要ならばNa2 O成
分として例えばNa2 CO3 を鉛ガラスの切削屑に配合
し、SiO2 /Na2 O重量比を1.2〜3.0の範囲
になるように調整して、添加したNa2 O成分によって
ガラスの融点を下げ、流動性が上がるように調節し、8
00℃以上に加熱溶融して鉛の分離を容易にするもので
ある。
However, in the lead glass cutting chips, in addition to the glass components as described above, SiO 2 and A
Since l 2 O 3 , CaO and the like and organic substances are mixed in, in the heating and melting treatment, PbO which is a glass component is reduced as shown in the above formula and separated from the glass component so that the melting point of the glass component rises and lead Separation becomes difficult. Therefore, as a result of various studies by the present inventors, when mixing a carbon source such as coke or charcoal as a reducing agent into lead glass cutting waste and heating and melting the mixture, as shown in Examples described later, SiO 2 / N
It was found that when the a 2 O weight ratio is adjusted to be in the range of 1.2 to 3.0 and the heating and melting treatment is performed, the separation of lead is facilitated. Therefore, in the present invention, if necessary, for example, Na 2 CO 3 is mixed as a Na 2 O component into the cutting waste of lead glass so that the SiO 2 / Na 2 O weight ratio is in the range of 1.2 to 3.0. The melting point of the glass is lowered by the added Na 2 O component and the fluidity is adjusted to 8
It is heated and melted at a temperature of 00 ° C. or higher to facilitate the separation of lead.

【0007】SiO2 /Na2 O比が1.2未満又は
3.0を越えた場合では、鉛の分離が不十分であり、ま
た日本環境庁告示第13号に基づく鉛の溶出試験及び米
国EP法に基づく鉛の溶質試験を行った結果、鉛の溶出
試験結果が基準を満たさないことが多いのでSiO2
Na2 O重量比を1.2〜3.0の範囲とした。更に、
本発明の鉛ガラス切削屑の加熱溶融処理を行うに当って
は、溶解容器として外部加熱方式の炉を用いることも出
来るが、工業的には被溶融原料に直接通電が可能な2相
又は3相エール式電気炉の利用が反応効率及び生産性の
点で有利である。また、還元剤の量は、前記の式に示す
C量相当が必要であるが、通常、原料ガラス屑量の外枠
で5重量%程度あればよいが、ガラス切削屑には炭素源
となる有機物が多く含まれる場合があり、その時は炭素
を添加する必要はない。殊に、エール式電気炉を用いた
場合、炉床のカーボンライニングまたは黒鉛電極により
還元剤が供給されるのでエール式電気炉が望ましい。
When the SiO 2 / Na 2 O ratio is less than 1.2 or exceeds 3.0, the separation of lead is insufficient, and the lead elution test based on the Japanese Environmental Agency Notification No. 13 and US As a result of the solute test lead based on EP method, since in many cases it leads dissolution test results do not meet the criteria SiO 2 /
The Na 2 O weight ratio was set in the range of 1.2 to 3.0. Furthermore,
In performing the heating and melting treatment of the lead glass cutting scraps of the present invention, an external heating type furnace can be used as a melting container, but industrially, it is a two-phase or three-phase type capable of directly energizing the material to be melted. The use of the phase ale type electric furnace is advantageous in terms of reaction efficiency and productivity. Further, the amount of the reducing agent needs to be equivalent to the amount of C shown in the above formula, but normally it is sufficient if it is about 5% by weight in the outer frame of the amount of raw glass scraps, but glass cutting scraps become a carbon source. It may contain a large amount of organic matter, and at that time, it is not necessary to add carbon. Particularly, when the ale type electric furnace is used, the ale type electric furnace is preferable because the reducing agent is supplied by the carbon lining of the hearth or the graphite electrode.

【0008】[0008]

【実施例】次に本発明の実施例について述べる。 [実施例1]先ず、光学ガラスの加工工程で発生する切
削屑の構成成分の1例を次の表1に示す。表1に示す如
く切削屑の構成成分としての総量は46.7%を示し、
残りの成分は有機物や揮発成分等である。
EXAMPLES Next, examples of the present invention will be described. [Example 1] First, Table 1 below shows an example of the constituent components of cutting chips generated in the process of processing optical glass. As shown in Table 1, the total amount of cutting chips as a constituent component is 46.7%,
The remaining components are organic substances and volatile components.

【0009】[0009]

【表1】 [Table 1]

【0010】表1に示す鉛ガラスの切削屑原料1kgに
還元剤として木炭を外枠で5重量%添加し、シリコニッ
ト電気炉内で1200℃までN2 気流中で加熱還元し
た。その結果、PbOはPbに還元されているが、ガラ
ス成分に混ざったままの状態となり、ガラス成分とPb
の分離が困難であった。これはガラス構成成分のPbO
が還元されてガラス成分から分離したため、ガラス成分
の融点が上昇し、鉛とガラスの分離が困難となったため
であると考えられた。
5% by weight of charcoal as a reducing agent was added to 1 kg of the cutting waste material of the lead glass shown in Table 1 in the outer frame, and the mixture was heated and reduced to 1200 ° C. in a N 2 gas stream in a silicon furnace. As a result, PbO is reduced to Pb, but remains in a state of being mixed with the glass component.
Was difficult to separate. This is PbO which is a glass component
It is considered that this is because the melting point of the glass component increased because it was reduced and separated from the glass component, making it difficult to separate lead and glass.

【0011】[実験1]そこで切削屑原料中のNa2
成分量が約28重量%となるように、Na2 CO3 を添
加し、SiO2 成分と化合せしめて、低融点のガラスと
なるようにガラス化し、これに還元剤として木炭を外枠
で5重量%添加混合した。この配合原料をアルミナルツ
ボに装入し、シリコニット電気炉中で昇温加熱し、80
0℃で30分保持した後再昇温し1200℃に1時間保
持後冷却した。冷却凝固した試料はガラス質部と金属鉛
とに分離しており、ガラス質中の残留鉛は0.2重量%
であり、殆どPbは還元され除去されていた。この結果
について、還元後のガラスを構成する主要成分を100
%として表2に示した。
[Experiment 1] Then, Na 2 O in the cutting waste material was used.
Na 2 CO 3 was added so that the amount of the component was about 28% by weight, and it was combined with the SiO 2 component and vitrified to form a glass with a low melting point. Weight% was added and mixed. This compounded raw material is charged into an alumina crucible and heated up in a silicon knit electric furnace to 80
After holding at 0 ° C. for 30 minutes, the temperature was raised again, at 1200 ° C. for 1 hour, and then cooled. The sample solidified by cooling is separated into a vitreous part and metallic lead, and the residual lead in the vitreous substance is 0.2% by weight.
And almost all Pb was reduced and removed. Based on this result, 100% of the main constituents of the glass after reduction were used.
It is shown in Table 2 as%.

【0012】[0012]

【表2】 [Table 2]

【0013】次に、得られたガラス質について日本環境
庁告示第13号に基づく鉛の溶出試験及び米国EP法に
基づく鉛の溶質試験を行った結果、表2に示す如く、日
本の鉛の溶出試験結果は0.2mg/l,米国の溶出試験
結果は0.17mg/lと、夫々の基準値3mg/l以下と
5mg/l以下の値に対しいずれも合格していた。なお、
ガラス質部をX線回析で結晶構造を調べた結果、無定形
のガラス質から成っていることを確認した。以上の実験
1のSiO2 /Na2 O重量比は、表2に示す如く、6
6.7重量%/28.4重量%=2.3であった。
Next, the obtained glassy material was subjected to a lead elution test based on Japan Environmental Agency Notification No. 13 and a lead solute test based on the US EP method. As a result, as shown in Table 2, The dissolution test result was 0.2 mg / l, and the dissolution test result in the United States was 0.17 mg / l, both of which passed the standard values of 3 mg / l or less and 5 mg / l or less. In addition,
As a result of investigating the crystal structure of the vitreous portion by X-ray diffraction, it was confirmed that the vitreous portion was composed of amorphous glass. The SiO 2 / Na 2 O weight ratio in Experiment 1 is 6
The ratio was 6.7% by weight / 28.4% by weight = 2.3.

【0014】[実験2]次に実験2では、鉛ガラス切削
屑のSiO2 /Na2 O重量比を5.6とし、他の条件
については実験1と同じ条件で還元・加熱溶融処理を行
った。その結果、Pbは還元しているが、ガラス質部の
流動性が悪く鉛との分離が不十分であった。還元後の成
分と溶出結果を表2に示した。表2の結果からガラスの
主要成分中のSiO2 /Na2 O重量比が適正でないと
ガラス質部の流動性が悪くガラスと鉛との分離が充分に
進まないため、鉛の溶出も大きくなることが確認でき
た。
[Experiment 2] Next, in Experiment 2, the SiO 2 / Na 2 O weight ratio of the lead glass cutting waste was set to 5.6, and the reduction / heat melting treatment was performed under the same conditions as in Experiment 1 under other conditions. It was As a result, although Pb was reduced, the fluidity of the vitreous part was poor and the separation from lead was insufficient. The components after the reduction and the elution results are shown in Table 2. From the results shown in Table 2, if the SiO 2 / Na 2 O weight ratio in the main components of the glass is not appropriate, the flowability of the vitreous part is poor and the separation of glass and lead does not proceed sufficiently, and lead elution also increases. I was able to confirm that.

【0015】[実験3]そこで適正なSiO2 /Na2
O重量比を見出だすため、SiO2 /Na2 O重量比を
1〜5.75の範囲で鉛ガラス切削屑を溶解、還元しガ
ラスの流動性を観察すると同時に、日本と米国の溶出試
験結果が5mg/l以下になる組成範囲を調べた。その
結果を図1に示す。図1に示す如く、SiO2 /Na2
O重量比が1.2〜3の範囲であれば、溶融物の流動性
は良く、Pbとガラスとの分離も充分に行われガラス中
のPbも0.1〜0.3重量%となり、溶出試験結果も
0.3mg/l以下となることを見出だした。
[Experiment 3] Then, appropriate SiO 2 / Na 2 was used.
In order to find the O weight ratio, the lead / glass cutting chips are melted and reduced in the SiO 2 / Na 2 O weight ratio range of 1 to 5.75 to observe the fluidity of the glass and at the same time the dissolution test in Japan and the United States. The composition range in which the result was 5 mg / l or less was investigated. The result is shown in FIG. As shown in FIG. 1, SiO 2 / Na 2
When the O weight ratio is in the range of 1.2 to 3, the flowability of the melt is good, Pb and glass are sufficiently separated, and Pb in the glass is 0.1 to 0.3% by weight. It was also found that the dissolution test result was also 0.3 mg / l or less.

【0016】[実施例2]次に、具体的な実施例につい
て述べる。図2は本発明の実施例で用いた500KVA
2相エール式電気炉の装置構成の模式図である。図2に
おいて、1は500KVA2相エール式電気炉、2はエ
ール式電気炉1の傾斜式炉体、3は炉体のカーボンライ
ニング、4は平型鋳型、5はエール式電気炉1の電極、
6は500KVA電源のトランス、7はエール式電気炉
1を覆う集塵フード、8は加熱溶融処理時に発生するダ
ストの集塵機である。図2に示すような2相エール式電
気炉の装置を用いて、PbOが7.1〜15.8重量%
を含有し、CaO,Al2 3 の含有量の異なる鉛ガラ
ス切削屑を供用した。
[Embodiment 2] Next, a specific embodiment will be described. FIG. 2 shows the 500 KVA used in the embodiment of the present invention.
It is a schematic diagram of a device configuration of a two-phase ale type electric furnace. In FIG. 2, 1 is a 500 KVA two-phase ale type electric furnace, 2 is a tilt type furnace body of the ale type electric furnace 1, 3 is carbon lining of the furnace body, 4 is a flat mold, 5 is an electrode of the ale type electric furnace 1,
6 is a transformer of 500 KVA power source, 7 is a dust collecting hood that covers the ale type electric furnace 1, and 8 is a dust collector for dust generated during the heating and melting process. Using a two-phase ale type electric furnace apparatus as shown in FIG. 2, PbO is 7.1 to 15.8 wt%.
And lead glass cutting chips containing CaO and Al 2 O 3 having different contents were used.

【0017】次に、鉛ガラス切削屑の主要構成成分であ
るPbO,SiO2 ,Al2 3 ,CaOと添加成分の
Na2 Oの合計を100重量%とし、Al2 3 を3.
4〜18.4重量%,CaOを7.0〜20.4重量%
の範囲で4水準で配合し、更に、実施例1の結果から、
Na2 O成分としてNa2 CO3 を添加し、SiO2
Na2 O重量比をほぼ1.2〜2.8に調整した。この
混合原料を約20kg電気炉に装入し、通電溶解後、約
1300℃に5分間保持した。いずれの試験において
も、通電開始から5分以内に原料が溶解し、さらに13
00℃で約5分保持することで還元が速やかに完了する
ことが確かめられた。その後、傾斜式炉体2を傾斜させ
て溶解物を平型鋳型4に鋳込み、冷却後ガラス質部と金
属鉛を分離し鉛分の溶出試験を行った。表3に溶解試験
後のガラスの主要成分とガラス中の鉛含有及び溶出試験
結果を示す。
Next, the total amount of PbO, SiO 2 , Al 2 O 3 and CaO, which are the main constituents of the lead glass cutting waste, and Na 2 O, which is an additive component, is 100% by weight, and Al 2 O 3 is 3.
4 to 18.4 wt%, CaO 7.0 to 20.4 wt%
4 levels within the range of, and from the results of Example 1,
It was added Na 2 CO 3 as Na 2 O component, SiO 2 /
The Na 2 O weight ratio was adjusted to approximately 1.2 to 2.8. About 20 kg of this mixed raw material was charged into an electric furnace, melted by electric current, and then held at about 1300 ° C. for 5 minutes. In both tests, the raw materials were dissolved within 5 minutes after the start of energization, and
It was confirmed that the reduction was completed promptly by holding at 00 ° C for about 5 minutes. After that, the tilted furnace body 2 was tilted, the melt was cast into the flat mold 4, and after cooling, the vitreous portion and metallic lead were separated and a lead content elution test was performed. Table 3 shows the main components of the glass after the dissolution test, the lead content in the glass, and the elution test results.

【0018】[0018]

【表3】 [Table 3]

【0019】表3に示すごとく、鉛ガラスの切削屑のS
iO2 /Na2 O重量比をほぼ1.2〜3.0に調整し
た結果、ガラス中の鉛は飛躍的に低下し、鉛溶出試験結
果は、日本基準及び米国基準ともに合格基準内に充分満
足する結果となった。一方、加熱溶融処理するための炉
として1.2KVAのシリコニット炉を用いて、試料を
るつぼに入れて外部加熱した場合は、1300℃まで昇
温するのに数時間以上を要し、工業プロセスとして外部
加熱方式は生産性が悪く望ましくない方式であることが
判った。本発明の鉛ガラス切削屑からの脱鉛方法は、鉛
ガラス切削屑に還元剤を添加し、切削屑原料中のSiO
2 /Na2 O重量比を1.2〜3.0の範囲となるよう
に調整することを特徴とするものであるが、この場合、
SiO2 /Na2 O重量比がNa2 O成分を添加しなく
ても、その範囲内にあるならば、そのままで鉛を分離す
ることが可能となることはもちろんである。
As shown in Table 3, S of lead glass cuttings
As a result of adjusting the iO 2 / Na 2 O weight ratio to about 1.2 to 3.0, the lead in the glass is drastically reduced, and the lead elution test results are sufficiently within the passing standards for both Japanese and US standards. The result was satisfactory. On the other hand, when a 1.2 KVA silicon knit furnace is used as a furnace for heating and melting, and a sample is placed in a crucible and externally heated, it takes several hours or more to raise the temperature to 1300 ° C., which is an industrial process. It has been found that the external heating method is undesired due to poor productivity. The lead removal method from lead glass cutting scraps of the present invention is a method of adding a reducing agent to lead glass cutting scraps to obtain SiO in the cutting scrap raw material.
The 2 / Na 2 O weight ratio is adjusted to be in the range of 1.2 to 3.0. In this case,
Needless to say, if the SiO 2 / Na 2 O weight ratio is within the range without adding the Na 2 O component, it becomes possible to separate lead as it is.

【0020】[0020]

【発明の効果】本発明の鉛ガラス切削屑からの脱鉛方法
により、鉛ガラスから鉛を分離することにより、ガラス
成分中の鉛は1.0重量%以下となり、本発明の処理を
行った後、ガラス屑を廃棄しても、Pbの溶出は、溶出
試験の日本基準及び米国基準ともに合格でき、鉛溶出に
伴う公害問題を回避することができる。
EFFECTS OF THE INVENTION By separating lead from lead glass by the lead removal method from lead glass cutting waste of the present invention, the lead in the glass component becomes 1.0% by weight or less, and the treatment of the present invention was performed. After that, even if the glass scraps are discarded, the Pb elution can pass both the Japanese standard and the US standard of the elution test, and the pollution problem associated with the elution of lead can be avoided.

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

【図1】本発明の実施例において得られたSiO2 /N
2 O重量比とガラス中の鉛含有及び溶出試験成績との
関係グラフである。
FIG. 1 SiO 2 / N obtained in an example of the present invention
It is a relational graph between the lead-containing and dissolution test results of a 2 O weight ratio and in the glass.

【図2】本発明の実施例において用いた2相エール式電
気炉の装置構成の模式図である。
FIG. 2 is a schematic diagram of a device configuration of a two-phase ale type electric furnace used in an example of the present invention.

【符号の説明】[Explanation of symbols]

1 エール式電気炉 2 傾斜式炉体 3 カーボンライニング 4 平型鋳型 5 電極 6 トランス 7 集塵フード 8 集塵機 1 Ale type electric furnace 2 Tilt type furnace body 3 Carbon lining 4 Flat mold 5 Electrode 6 Transformer 7 Dust collecting hood 8 Dust collector

───────────────────────────────────────────────────── フロントページの続き (72)発明者 加藤 昌憲 東京都千代田区丸の内一丁目1番2号 日 本鋼管株式会社内 (72)発明者 吉越 英之 東京都千代田区丸の内二丁目3番2号 鋼 管鉱業株式会社内 (72)発明者 池田 伸晤 東京都千代田区丸の内二丁目3番2号 鋼 管鉱業株式会社内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Masanori Kato 1-2-1, Marunouchi, Chiyoda-ku, Tokyo Nihon Kokan Co., Ltd. (72) Hideyuki Yoshikoshi 2-3-2, Marunouchi, Chiyoda-ku, Tokyo Steel Tube Mining Co., Ltd. (72) Inventor Shinda Ikeda 2-3-2 Marunouchi, Chiyoda-ku, Tokyo Steel Tube Mining Co., Ltd.

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 鉛ガラス切削屑にコークス又は木炭等の
炭素源を還元剤として混合し800℃以上に加熱溶融処
理することにより鉛を分離することを特徴とする鉛ガラ
ス切削屑からの脱鉛方法。
1. Lead removal from lead glass cutting chips, characterized in that lead glass cutting chips are mixed with a carbon source such as coke or charcoal as a reducing agent and heated and melted at 800 ° C. or more to separate lead. Method.
【請求項2】 前記鉛ガラス切削屑にNa2 O成分を添
加し、含有SiO2/Na2 Oの重量比を1.2〜3.
0の範囲となるように調整し、加熱溶融処理することを
特徴とする請求項1記載の鉛ガラス切削屑からの脱鉛方
法。
2. A Na 2 O component is added to the lead glass cutting chips, and the weight ratio of contained SiO 2 / Na 2 O is 1.2 to 3.
The method for removing lead from cuttings of lead glass according to claim 1, wherein the method is adjusted so as to be in the range of 0 and heat-melted.
【請求項3】 前記加熱溶融処理において、溶融物を溶
融状態で排出し、急冷凝固させた後、鉛を分離すること
を特徴とする請求項1記載の鉛ガラス切削屑からの脱鉛
方法。
3. The method for removing lead from cutting chips of lead glass according to claim 1, wherein in the heating and melting treatment, a molten material is discharged in a molten state, rapidly solidified, and then lead is separated.
【請求項4】 前記加熱溶融処理を2相又は3相エール
式電気炉にて行うことを特徴とする請求項1記載の鉛ガ
ラス切削屑からの脱鉛方法。
4. The method for removing lead from cutting chips of lead glass according to claim 1, wherein the heating and melting treatment is performed in a two-phase or three-phase ale type electric furnace.
JP24252993A 1993-09-29 1993-09-29 Lead removal method from lead glass cuttings Pending JPH0796264A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP24252993A JPH0796264A (en) 1993-09-29 1993-09-29 Lead removal method from lead glass cuttings

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP24252993A JPH0796264A (en) 1993-09-29 1993-09-29 Lead removal method from lead glass cuttings

Publications (1)

Publication Number Publication Date
JPH0796264A true JPH0796264A (en) 1995-04-11

Family

ID=17090473

Family Applications (1)

Application Number Title Priority Date Filing Date
JP24252993A Pending JPH0796264A (en) 1993-09-29 1993-09-29 Lead removal method from lead glass cuttings

Country Status (1)

Country Link
JP (1) JPH0796264A (en)

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JP2012097288A (en) * 2010-10-29 2012-05-24 Jfe Engineering Corp Method for recovering lead from lead-containing glass
WO2013118695A1 (en) 2012-02-06 2013-08-15 鳥取県 Method for separating heavy metal from glass
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WO2014073399A1 (en) 2012-11-12 2014-05-15 鳥取県 Method for separating heavy metals from glass
JP2014133931A (en) * 2013-01-11 2014-07-24 Univ Of Fukui Method of recovering lead from lead-containing glass
JP2016130335A (en) * 2015-01-13 2016-07-21 パナソニックIpマネジメント株式会社 Method and apparatus for separating lead from lead glass
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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012097288A (en) * 2010-10-29 2012-05-24 Jfe Engineering Corp Method for recovering lead from lead-containing glass
KR101325782B1 (en) * 2011-04-12 2013-11-08 태영환경개발 주식회사 Method and apparatus for separating lead from glass containing lead
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WO2013118695A1 (en) 2012-02-06 2013-08-15 鳥取県 Method for separating heavy metal from glass
KR20140114070A (en) * 2012-02-06 2014-09-25 톳토리 프리펙쳐 Method for separating heavy metal from glass
JPWO2013118695A1 (en) * 2012-02-06 2015-05-11 鳥取県 Method for separating heavy metals from glass
WO2014073399A1 (en) 2012-11-12 2014-05-15 鳥取県 Method for separating heavy metals from glass
KR20150045454A (en) 2012-11-12 2015-04-28 톳토리 프리펙쳐 Method for separating heavy metals from glass
JP2014133931A (en) * 2013-01-11 2014-07-24 Univ Of Fukui Method of recovering lead from lead-containing glass
KR101367973B1 (en) * 2013-03-28 2014-03-12 태영환경개발 주식회사 Method and apparatus for separating lead from glass containing lead
EP3012333A4 (en) * 2013-06-21 2017-03-08 Tottori Prefecture Method of recovering metal from waste electronic substrates
JP2016130335A (en) * 2015-01-13 2016-07-21 パナソニックIpマネジメント株式会社 Method and apparatus for separating lead from lead glass
JP2017082340A (en) * 2017-01-07 2017-05-18 国立大学法人福井大学 Method for recovering lead from lead-containing glass
WO2024190628A1 (en) * 2023-03-10 2024-09-19 Agc株式会社 Method for producing glass

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