JPH1136020A - Treatment of waste printed circuit board - Google Patents

Treatment of waste printed circuit board

Info

Publication number
JPH1136020A
JPH1136020A JP20721397A JP20721397A JPH1136020A JP H1136020 A JPH1136020 A JP H1136020A JP 20721397 A JP20721397 A JP 20721397A JP 20721397 A JP20721397 A JP 20721397A JP H1136020 A JPH1136020 A JP H1136020A
Authority
JP
Japan
Prior art keywords
metal
dissolving
dissolved
acid
printed circuit
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
JP20721397A
Other languages
Japanese (ja)
Inventor
Koichi Takano
恒一 高野
Katsusato Fujiyoshi
克聡 藤好
Masasuke Fujiyoshi
巨介 藤好
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.)
JUSTY KK
Original Assignee
JUSTY KK
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 JUSTY KK filed Critical JUSTY KK
Priority to JP20721397A priority Critical patent/JPH1136020A/en
Publication of JPH1136020A publication Critical patent/JPH1136020A/en
Pending legal-status Critical Current

Links

Classifications

    • HELECTRICITY
    • H05ELECTRIC TECHNIQUES NOT OTHERWISE PROVIDED FOR
    • H05KPRINTED CIRCUITS; CASINGS OR CONSTRUCTIONAL DETAILS OF ELECTRIC APPARATUS; MANUFACTURE OF ASSEMBLAGES OF ELECTRICAL COMPONENTS
    • H05K3/00Apparatus or processes for manufacturing printed circuits
    • H05K3/22Secondary treatment of printed circuits
    • 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
    • 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
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/82Recycling of waste of electrical or electronic equipment [WEEE]

Landscapes

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

Abstract

PROBLEM TO BE SOLVED: To provide a method for the treatment of waste printed circuit boards, etc., capable of efficiently recovering noble metals such as gold, palladium, rhodium and platinum, and recovering the glass fiber reinforced expoxy resin and polyimide, etc., which cannot be dissolved by acids capable of dissolving the metals. SOLUTION: This method includes a metal dissolving process for dissolving the waste printed circuit boards, etc., by feeding the boards, etc., into an acid, such as nitric acid, hydrochloric acid, sulfuric acid, capable of dissolving the metals, a non-pollution treatment stage for gases, etc., for making the vapor and gases generated in this metal dissolving process non-pollutant, a recovering process for the noble metals by adding an alkali to the metal dissolving acids contg. the dissolved metal in the metal dissolving stage described above to adjust the pH thereof to 4 to 5 and recovering the precipitated noble metals, such as Pt, Pd, Rh, Os, Ru and Au, by filtering and a non-dissolved matter removing process for removing the non-dissolved matter, such as glass fiber reinforced expoxy resin and polyimide, which are not dissolved in the metal dissolving process.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は廃家電製品や廃OA
機器等に使用されていたプリント基板等や、製造時に生
じる不良品等の廃プリント基板等の処理方法に関する。
TECHNICAL FIELD The present invention relates to waste home appliances and waste OA
The present invention relates to a method of treating a printed circuit board or the like used for equipment or the like, and a waste printed circuit board or the like of a defective product or the like generated during manufacturing.

【0002】[0002]

【従来の技術】従来、廃プリント基板には金や白金、パ
ラジウム、ロジウム等の貴金属が使用されている部品が
組付けられているため、金が使用されている部品を取り
外し、金を回収することが行なわれている。
2. Description of the Related Art Conventionally, since parts using noble metals such as gold, platinum, palladium, and rhodium are assembled on waste printed circuit boards, parts using gold are removed and gold is collected. Things are going on.

【0003】[0003]

【発明が解決しようとする課題】従来の廃プリント基板
からの金の回収では廃プリント基板から金が使用されて
いる部品の取り外しに手数がかかり、危険なシアンを使
用し、コスト高になるとともに、他の貴金属や金属の回
収ができず、不経済であるとともに、多くは産業廃棄物
として処理されてしまうという欠点があった。
In the conventional recovery of gold from a waste printed circuit board, it takes time and effort to remove parts using gold from the waste printed circuit board. However, other precious metals and metals cannot be recovered, which is uneconomical and has a drawback that most of them are treated as industrial waste.

【0004】本発明は以上のような従来の欠点に鑑み、
金、パラジウム、ロジウム、白金等の貴金属を効率よく
回収することができるとともに、金属を溶解することが
できる酸で溶解できないガラエポやポリミド等を非溶解
物として回収することができる廃プリント基板等の処理
方法を提供することを目的としている。
The present invention has been made in view of the above-mentioned conventional drawbacks,
It is possible to efficiently collect precious metals such as gold, palladium, rhodium, and platinum, and to recover as a non-dissolved substance such as glass epoxy or polyimide that cannot be dissolved by an acid capable of dissolving metals. It is intended to provide a processing method.

【0005】また、本発明は金、パラジウム、ロジウ
ム、白金等の貴金属および銀、スズ、水銀、鉛、マンガ
ン、鉄、銅、ニッケル等の金属も効率よく回収すること
ができるとともに、非溶解物を人造石等に加工すること
ができる廃プリント基板等の処理方法を提供することを
目的としている。
Further, the present invention can efficiently recover noble metals such as gold, palladium, rhodium and platinum and metals such as silver, tin, mercury, lead, manganese, iron, copper, nickel and the like, as well as insoluble materials. It is an object of the present invention to provide a method for treating a waste printed circuit board or the like, which can be processed into artificial stone or the like.

【0006】本発明の前記ならびにそのほかの目的と新
規な特徴は次の説明を添付図面と照らし合わせて読む
と、より完全に明らかになるであろう。ただし、図面は
もっぱら解説のためのものであって、本発明の技術的範
囲を限定するものではない。
The above and other objects and novel features of the present invention will become more fully apparent when the following description is read in light of the accompanying drawings. However, the drawings are for explanation only, and do not limit the technical scope of the present invention.

【0007】[0007]

【課題を解決するための手段】上記目的を達成するため
に、本発明は廃プリント基板等を金属を溶解することが
できる硝酸、塩酸、硫酸等の酸に投入して溶解する金属
溶解工程と、この金属溶解工程で発生する蒸気やガスを
無害化処理するガス等の無害化処理工程と、前記金属溶
解工程で溶解金属を含む金属溶解酸にアリカリを加えて
PHを4〜5にして析出されるPt、Pd、Rh、O
s、Ru、Au等の貴金属等を濾過して回収する貴金属
等の回収工程と、前記金属溶解工程で溶解されないガラ
エポやポリミド等の非溶解物を除去する非溶解物除去工
程とで廃プリント基板等の処理方法を構成している。
In order to achieve the above object, the present invention provides a metal dissolving step in which a waste printed circuit board or the like is put into an acid such as nitric acid, hydrochloric acid, sulfuric acid or the like capable of dissolving a metal. A detoxifying process such as a gas for detoxifying steam or gas generated in the metal dissolving process, and adding a alkali to a metal-dissolving acid containing a dissolving metal in the metal dissolving process to adjust the pH to 4 to 5 to precipitate. Pt, Pd, Rh, O
A waste printed circuit board includes a precious metal recovery step of filtering and recovering precious metals such as s, Ru, and Au, and a non-dissolved substance removing step of removing non-dissolved substances such as glass epoxy and polyimide that are not dissolved in the metal dissolving step. And so on.

【0008】また、本発明は廃プリント基板等を金属を
溶解することができる硝酸、塩酸、硫酸等の酸に投入し
て溶解する金属溶解工程と、この金属溶解工程で発生す
る蒸気やガスを無害化処理するガス等の無害化処理工程
と、前記金属溶解工程で溶解金属を含む金属溶解酸にア
リカリを加えてPHを4〜5にして析出されるPt、P
d、Rh、Os、Ru、Au等の貴金属等を濾過して回
収する貴金属等の回収工程と、前記金属溶解工程で溶解
されないガラエポやポリミド等の非溶解物を除去する非
溶解物除去工程と、この非溶解物除去工程で除去された
非溶解物を洗浄して脱水する洗浄脱水工程と、この洗浄
脱水工程で洗浄脱水された非溶解物を炉芯の温度が約1
0,000℃となるプラズマアーク、アーク放電による
超高温燃焼炉で燃焼させる超高温燃焼工程と、この超高
温燃焼工程で溶解状態で残留する残留物を所定の形状に
成型して人造石等に加工する加工工程とで廃プリント基
板等の処理方法を構成している。
The present invention also relates to a metal dissolving step in which a waste printed circuit board or the like is introduced into an acid such as nitric acid, hydrochloric acid, sulfuric acid or the like capable of dissolving a metal, and a vapor or gas generated in the metal dissolving step is dissolved. Pt, P deposited at a pH of 4 to 5 by adding alkali to a metal-dissolving acid containing a dissolved metal in the metal-dissolving step of detoxifying a gas or the like to be rendered harmless.
d, Rh, Os, Ru, a noble metal recovery step of filtering and collecting noble metals such as Au, and a non-dissolved substance removing step of removing non-dissolved substances such as glass epochs and polyimides that are not dissolved in the metal dissolving step. A washing and dewatering step of washing and dewatering the non-dissolved matter removed in the non-dissolved matter removing step;
An ultra-high-temperature combustion process of burning in an ultra-high-temperature combustion furnace using a plasma arc or arc discharge of 000 ° C., and a residue remaining in a melted state in the ultra-high-temperature combustion process is molded into a predetermined shape into artificial stone or the like. The processing steps for processing constitute a method of processing a waste printed circuit board or the like.

【0009】[0009]

【発明の実施の形態】以下、図面に示す実施の形態によ
り、本発明を詳細に説明する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described below in detail with reference to the embodiments shown in the drawings.

【0010】図1ないし図7に示す本発明の第1の実施
の形態において、1は廃プリント基板等2を金属を溶解
することができる硝酸、塩酸、硫酸等の酸3に投入して
溶解する金属溶解工程で、この金属溶解工程1で使用さ
れる廃プリント基板等2は、廃家電製品や廃OA機器等
に使用されていたプリント基板や製造時に生じる不良品
等のプリント基板や貴金属を用いた接点等を有する電
気、電子部品等である。
In the first embodiment of the present invention shown in FIGS. 1 to 7, reference numeral 1 denotes a waste printed circuit board or the like 2 which is put into an acid 3 such as nitric acid, hydrochloric acid, sulfuric acid or the like capable of dissolving a metal and dissolved. In the metal melting step, the waste printed circuit board 2 used in the metal melting step 1 is made of a printed circuit board used for waste home electric appliances or waste OA equipment, a printed circuit board such as a defective product generated during manufacturing, or a noble metal. It is an electric or electronic component having a used contact or the like.

【0011】なお、酸3への廃プリント基板等2の投入
は、図2に示すように金属溶解酸4を収納する金属溶解
酸収納タンク5と、この金属溶解酸収納タンク5へフィ
ルター6を備えた筒状の樋7を介して、前記酸3を供給
する開閉弁8を備える酸収納タンク9と、前記樋7の上
流側の上部に突出するように取付けられた廃プリント基
板等2の投入装置10とからなる金属溶解装置11を用
いたり、酸3が収納された酸収納タンク9に廃プリント
基板等2を直接投入したりして行なう。
As shown in FIG. 2, the waste printed circuit board 2 and the like 2 are charged into the acid 3 by disposing a metal dissolved acid storage tank 5 for storing a metal dissolved acid 4 and a filter 6 to the metal dissolved acid storage tank 5. An acid storage tank 9 provided with an on-off valve 8 for supplying the acid 3 through a cylindrical gutter 7 provided, and a waste printed circuit board 2 or the like 2 mounted so as to protrude to an upper portion on the upstream side of the gutter 7. This is performed by using a metal dissolving device 11 including a charging device 10 or directly charging a waste printed circuit board 2 or the like 2 into an acid storage tank 9 in which the acid 3 is stored.

【0012】12は前記金属溶解工程1で発生する蒸気
やガスを窒素や酸素となるように無害化処理するガス等
の無害化処理工程で、このガス等の無害化処理工程12
は図2に示すように、樋7内および金属溶解酸収納タン
ク5内で発生する蒸気やガスを外部へ排出する排出通路
13と、この排出通路13に介装された湿式スクラバ排
煙処理装置本体14、この湿式スクラバ排煙処理装置本
体14に水酸化ナトリウム等の中和剤15を中和剤収納
タンク16より供給するポンプ17を備えた供給路1
8、前記湿式スクラバ排煙処理装置本体14より処理済
の中和剤15を前記中和剤収納タンク16へ導く排出路
19とからなる湿式スクラバ排煙処理装置20で無害化
して排出される。
Reference numeral 12 denotes a detoxification process of a gas or the like for detoxifying steam or gas generated in the metal dissolving step 1 so as to be nitrogen or oxygen.
As shown in FIG. 2, a discharge passage 13 for discharging steam and gas generated in the gutter 7 and the metal dissolved acid storage tank 5 to the outside, and a wet scrubber smoke exhaust treatment device provided in the discharge passage 13 are provided. A supply path 1 including a main body 14 and a pump 17 for supplying a neutralizing agent 15 such as sodium hydroxide from a neutralizing agent storage tank 16 to the wet scrubber flue gas treatment apparatus main body 14.
8. The wet scrubber flue gas treatment device 20 is composed of a wet scrubber flue gas treatment device 20 comprising a discharge path 19 for guiding the treated neutralizing agent 15 from the wet scrubber flue gas treatment device main body 14 to the neutralizing agent storage tank 16.

【0013】21は前記金属溶解工程1で溶解金属を含
む金属溶解酸4に、図3に示すようにアルカリ液22を
加えてPHを4〜5にして析出されるPt、Pd、R
h、Os、Ru、Au等の貴金属等を、例えば400メ
ッシュの濾紙23を用いて濾過して回収する貴金属等の
回収工程で、この貴金属等の回収工程21で使用される
アルカリ液22はコスト低減を図るために、製紙工場で
発生する製紙廃液を用いることができる。この貴金属等
の回収工程21で析出させて濾過させて回収するPt、
Pd、Rh、Os、Ru、Au等の貴金属等のそれぞれ
の抽出は液温の設定や、還元剤を用いたりメッキや電解
処理等によって99,999%の高純度の回収を行な
う。
Reference numeral 21 denotes Pt, Pd, and R, which are precipitated by adding an alkaline solution 22 to the metal-dissolving acid 4 containing the dissolving metal in the metal dissolving step 1 to adjust the pH to 4 to 5, as shown in FIG.
In the recovery process of precious metals and the like for filtering and recovering precious metals such as h, Os, Ru, and Au using, for example, a 400-mesh filter paper 23, the alkali liquid 22 used in the recovery process 21 of the precious metals and the like is costly. In order to achieve the reduction, waste papermaking liquid generated in a paper mill can be used. Pt that precipitates in the recovery step 21 of the noble metal and the like, and is collected by filtration;
Extraction of each of the noble metals such as Pd, Rh, Os, Ru, and Au is performed by setting the liquid temperature, recovering a high purity of 99,999% by using a reducing agent, plating, or electrolytic treatment.

【0014】24は前記貴金属等の回収工程21で貴金
属等の回収済の金属溶解液4Aに、図4に示すようにア
ルカリ液22を加えてPHをほぼ8に調整するととも
に、NaCl等のClイオンを加えて浮遊するSnO
をひしゃく25等によって回収し、かつ析出され沈殿す
るAgNOを、例えば400メッシュの濾布23を用
いて濾過して回収するスズ、銀回収工程で、このスズ、
銀回収工程24で回収したSnOは温水洗浄後、遠心
分離し、電解法によって高純度で回収し、AgNO
さらしてCuを還元剤として投入することにより、Ag
が析出して回収でき、これをさらに高純度にする場合に
は電解精練を行なう。
Reference numeral 24 denotes an alkali solution 22 added to the metal solution 4A in which the noble metal or the like has been recovered in the above-mentioned noble metal or the like recovery step 21 to adjust the pH to approximately 8 as shown in FIG. SnO 2 suspended by adding ions
Is collected by a ladle 25 or the like, and AgNO 3 which precipitates and precipitates is collected by filtration using a 400-mesh filter cloth 23, for example.
The SnO 2 recovered in the silver recovery step 24 is washed with warm water, centrifuged, recovered in high purity by an electrolytic method, and AgNO 3 is exposed and Cu is introduced as a reducing agent to obtain Ag.
Can be precipitated and recovered, and if the purity is to be further increased, electrolytic scouring is performed.

【0015】26は前記スズ、銀回収工程24でスズや
銀の回収済の金属溶解液4Bに、図5に示すように還元
剤としてのFeを投入して析出されるHgClを、例
えば400メッシュの濾布23を用いて濾過して回収す
る水銀回収工程で、この水銀回収工程26で回収された
HgClから鉄液還元処理加工等によって高純度のH
gを回収する。
Reference numeral 26 denotes HgCl 2 deposited by introducing Fe as a reducing agent into the metal solution 4B in which tin and silver have been recovered in the tin and silver recovery step 24 as shown in FIG. In a mercury recovery step of filtering and recovering using a mesh filter cloth 23, high-purity H is obtained from the HgCl 2 recovered in the mercury recovery step 26 by iron liquid reduction treatment or the like.
Collect g.

【0016】27は前記水銀回収工程26で水銀の回収
済の金属溶解液4Cに、図6に示すようにアルカリ液2
2を加えてPHをほぼ8に調整すると析出されたり溶媒
抽出等によってPb(OH)、Mn(OH)、Fe
(OH)、Cu(OH)、Ni(OH)、ZnC
dを回収する残存金属回収工程で、この残存金属回収工
程27は、まず析出され濾過によってPbClを回収
し、残った金属溶解液4Dから溶媒クロロホルムを用い
た溶媒抽出によりCuを回収し、残った金属溶解液4E
から溶媒ゲメチルグリオキシムを用いた溶媒抽出により
Niを回収し、残った金属溶解液4FからZnCdを還
元回収し、残った金属溶解液4Gからアルカリ処理によ
ってMn(OH)、Fe(OH)を回収する。
Reference numeral 27 denotes an alkaline solution 2C as shown in FIG.
2 to adjust the pH to approximately 8, Pb (OH) 2 , Mn (OH) 2 , Fe
(OH) 2 , Cu (OH) 2 , Ni (OH) 2 , ZnC
In the residual metal recovery step 27 for recovering d, in the remaining metal recovery step 27, first, PbCl 2 is recovered by filtration and recovered, and Cu is recovered from the remaining metal solution 4D by solvent extraction using a solvent chloroform. Metal solution 4E
From the remaining metal solution 4F by reducing and recovering ZnCd from the remaining metal solution 4F, and Mn (OH) 2 , Fe (OH) from the remaining metal solution 4G by alkali treatment. Collect 2 .

【0017】28は前記残存金属回収工程27で残存金
属の回収済の金属溶解液4Hに、図7に示すようにアル
カリ液22を加えてPHをほぼ8に調整すると、析出さ
れたAlを、例えば400メッシュの濾布23を
用いて濾過して回収するアルミニウム回収工程で、この
アルミニウム回収工程28で残った濾液は希釈して完全
無害化して廃棄する。
[0017] 28 the collected-metal solution 4H residual metal in said remaining metal recovery process 27, when adjusted to approximately 8 with PH by adding an alkali solution 22, as shown in FIG. 7, precipitated the Al 2 O In a step of collecting aluminum by filtration using, for example, a 400-mesh filter cloth 23, the filtrate remaining in the aluminum collecting step 28 is diluted, completely rendered harmless, and discarded.

【0018】29は前記金属溶解工程1で溶解されずに
フィルター6部に残ったガラエポやポリミド等の非溶解
物30を取り出す非溶解物除去工程で、この非溶解物除
去工程29は手作業やフィルター6部に着脱可能な濾枠
やカゴを設置しておき、該濾枠やカゴに流入した状態で
除去回収してもよい。
Reference numeral 29 denotes a non-dissolved substance removing step for removing non-dissolved substances 30 such as glass epoch and polyimide remaining in the 6 parts of the filter without being dissolved in the metal dissolving step 1. A removable filter frame or basket may be installed in the filter 6 part, and may be removed and collected while flowing into the filter frame or basket.

【0019】31は前記非溶解物除去工程29で除去回
収した非溶解物30を洗浄し、脱水する洗浄脱水工程
で、この洗浄脱水工程31は非溶解物除去工程29で除
去回収した非溶解物30をアルカリで中和して洗浄する
第1の洗浄工程32と、この第1の洗浄工程32後に水
洗できれいにする第2の洗浄工程33と、この第2の洗
浄工程33後に遠心脱水機で脱水する脱水工程34とで
構成されている。
Reference numeral 31 denotes a washing and dewatering step of washing and dewatering the undissolved material 30 removed and recovered in the undissolved material removing step 29. A first washing step 32 for neutralizing and washing the base 30 with an alkali, a second washing step 33 for washing with water after the first washing step 32, and a centrifugal dehydrator after the second washing step 33. And a dehydration step 34 for dehydration.

【0020】なお、第1の洗浄工程32で発生する洗浄
液には重金属が含まれているため、濾過、イオン濃度差
で重金属を分離する。
Since the cleaning liquid generated in the first cleaning step 32 contains heavy metals, the heavy metals are separated by filtration and ion concentration difference.

【0021】35は前記洗浄脱水工程31で洗浄脱水さ
れた非溶解物を、濾芯の温度が約10,000℃となる
プラズマアーク、アーク放電を用いた超高温焼却炉で燃
焼させる超高温燃焼工程である。
35 is an ultra-high temperature combustion process in which the undissolved material washed and dehydrated in the cleaning and dehydration process 31 is burned in an ultra-high temperature incinerator using a plasma arc or arc discharge having a filter core temperature of about 10,000 ° C. It is.

【0022】36は前記超高温燃焼工程35で溶解状態
で残留する残留物を型を用いたりして所定の形状に成型
して人造石等に加工する加工工程で、この加工工程36
は床石、壁材、塀材等から、特殊な技法を用いて深橙赤
色、黄色、青緑色、鮮青色、紫色等の発光性(夜行性)
の石材や砂に加工することができる。
Reference numeral 36 denotes a processing step in which the residue remaining in the melted state in the ultrahigh-temperature combustion step 35 is molded into a predetermined shape using a mold or the like and processed into artificial stone or the like.
Is luminescent (nocturnal) in deep orange red, yellow, blue green, bright blue, purple, etc. from floor stones, wall materials, fence materials, etc. using special techniques
Can be processed into stone and sand.

【0023】[0023]

【発明の異なる実施の形態】次に、図8ないし図11に
示す本発明の異なる実施の形態につき説明する。なお、
これらの本発明の異なる実施の形態の説明に当って、前
記本発明の第1の実施の形態と同一構成部分には同一符
号を付して重複する説明を省略する。
Next, different embodiments of the present invention shown in FIGS. 8 to 11 will be described. In addition,
In the description of the different embodiments of the present invention, the same components as those of the first embodiment of the present invention are denoted by the same reference numerals, and duplicate description will be omitted.

【0024】図8および図9に示す本発明の第2の実施
の形態において、前記本発明の第1の実施の形態と主に
異なる点は、廃プリント基板等2からポリエチレン、ポ
リエステル、エポキシ樹脂、フェノール樹脂、ポリミド
等の合成樹脂材を除去する合成樹脂材除去工程37を行
なった後、金属溶解工程1を行なった点で、このように
合成樹脂材除去工程37を行なう廃プリント基板等の処
理方法を使用することにより、合成樹脂材の回収も行な
うことができる。
The second embodiment of the present invention shown in FIGS. 8 and 9 is different from the first embodiment of the present invention mainly in that the waste printed circuit board 2 is replaced with polyethylene, polyester and epoxy resin. After performing the synthetic resin material removing step 37 for removing the synthetic resin material such as phenolic resin and polyamide, and then performing the metal dissolving step 1, the waste printed circuit board or the like in which the synthetic resin material removing step 37 is thus performed. By using the treatment method, the synthetic resin material can be recovered.

【0025】なお、前記合成樹脂材除去工程37は手作
業で行なってもよく、あるいは図9に示すように合成樹
脂材が溶解する110℃〜300℃にてんぷら等に使用
された廃植物性油38が加熱できる炉や釜39に投入す
ることにより、廃プリント基板等2に使用されている合
成樹脂材は、溶解して油面上に浮上させて分離除去して
もよい。
The synthetic resin material removing step 37 may be performed manually or, as shown in FIG. 9, waste vegetable oil used for tempura at 110 ° C. to 300 ° C. where the synthetic resin material is dissolved. The synthetic resin material used for the waste printed circuit board 2 or the like may be dissolved and floated on an oil surface to be separated and removed by being put into a furnace or a pot 39 capable of heating the 38.

【0026】図10に示す本発明の第3の実施の形態に
おいて、前記本発明の第1の実施の形態と主に異なる点
は、廃プリント基板等2からハンダを除去するハンダ除
去工程40を行なった後、金属溶解工程1を行なった点
で、このようにハンダ除去工程40を行なう廃プリント
基板等の処理方法を使用することにより、ハンダの回収
も行なうことができる。
The third embodiment of the present invention shown in FIG. 10 is mainly different from the first embodiment of the present invention in that a solder removing step 40 for removing solder from a waste printed circuit board 2 or the like is performed. After the metal dissolving step 1 is performed, the solder can be recovered by using the processing method for the waste printed circuit board or the like in which the solder removing step 40 is performed.

【0027】なお、前記ハンダ除去工程40はハンダが
溶解する温度に加熱した遠心分離機を用いることによ
り、ハンダを分離除去してもよく、あるいはハンダが溶
解する温度に加熱された廃植物性油に投入して合成樹脂
材とハンダの除去を同時に行なってもよい。
In the solder removing step 40, the solder may be separated and removed by using a centrifugal separator heated to a temperature at which the solder dissolves, or a waste vegetable oil heated to a temperature at which the solder dissolves. To remove the synthetic resin material and the solder at the same time.

【0028】図11に示す本発明の第4の実施の形態に
おいて、前記本発明の第2の実施の形態と主に異なる点
は、洗浄脱水工程31後に洗浄脱水された非溶解物を破
砕するとともに、合成樹脂材が溶解する110℃〜30
0℃にてんぷら等に使用された廃植物性油が加熱できる
炉や釜に投入して内部に残留していた合成樹脂材を除去
する合成樹脂材除去工程37を行なつた点で、このよう
な合成樹脂材除去工程37を用いた廃プリント基板等の
処理方法を使用してもよい。なお、処理する廃プリント
基板等によっては洗浄脱水された非溶解物を破砕するこ
となく合成樹脂材が溶解する110℃〜300℃にてん
ぷら等に使用された廃植物性油が加熱できる炉や釜に投
入する合成樹脂材除去工程37を行ってもよい。
The fourth embodiment of the present invention shown in FIG. 11 is mainly different from the second embodiment of the present invention in that the non-dissolved material washed and dehydrated after the washing and dehydrating step 31 is crushed. At the same time, the synthetic resin material dissolves at 110 ° C to 30 ° C.
In this respect, a synthetic resin material removing step 37 of removing the synthetic resin material remaining inside by putting the waste vegetable oil used for tempura etc. at 0 ° C. into a furnace or a kettle capable of heating is performed as described above. A method of processing a waste printed circuit board or the like using the simple synthetic resin material removing step 37 may be used. In addition, depending on the waste printed circuit board to be treated, the synthetic resin material is dissolved without crushing the undissolved material that has been washed and dehydrated. A furnace or a pot capable of heating waste vegetable oil used for tempura at 110 ° C. to 300 ° C. May be performed.

【0029】[0029]

【発明の効果】以上の説明から明らかなように、本発明
にあっては次に列挙する効果が得られる。
As apparent from the above description, the following effects can be obtained in the present invention.

【0030】(1)廃プリント基板等を金属を溶解する
ことができる硝酸、塩酸、硫酸等の酸に投入して溶解す
る金属溶解工程と、この金属溶解工程で発生する蒸気や
ガスを無害化処理するガス等の無害化処理工程と、前記
金属溶解工程で溶解金属を含む金属溶解酸にアリカリを
加えてPHを4〜5にして析出されるPt、Pd、R
h、Os、Ru、Au等の貴金属等を濾過して回収する
貴金属等の回収工程と、前記金属溶解工程で溶解されな
いガラエポやポリミド等の非溶解物を除去する非溶解物
除去工程とからなるので、廃プリント基板等の金属を溶
解してから貴金属等を回収するため、純度の高い状態で
貴金属を回収することができる。したがって、回収品の
商品価値が高く、利益を得ることができる。
(1) A metal dissolving step in which a waste printed board or the like is put into an acid such as nitric acid, hydrochloric acid or sulfuric acid capable of dissolving a metal to dissolve the metal, and steam and gas generated in the metal dissolving step are rendered harmless. Pt, Pd, R deposited at a pH of 4 to 5 by adding alkali to a metal-dissolving acid containing a dissolved metal in the metal dissolving step in the metal dissolving step.
a process of recovering a precious metal such as h, Os, Ru, Au or the like by filtration, and a process of removing a non-dissolved material such as a glass epoxy or a polyimide which is not dissolved in the metal dissolving process. Therefore, since the noble metal and the like are recovered after dissolving the metal of the waste printed circuit board and the like, the noble metal can be recovered in a high purity state. Therefore, the merchandise value of the collected product is high, and profit can be obtained.

【0031】(2)前記(1)によって、廃プリント基
板等を酸に溶解した金属と、ガラエポやポリミド等の非
溶解物とに簡単に分離でき、後処理を容易に行なうこと
ができる。
(2) According to the above (1), a metal in which a waste printed board or the like is dissolved in an acid and a non-dissolved substance such as glass epoxy or polyimide can be easily separated, and post-processing can be easily performed.

【0032】(3)前記(1)によって、廃プリント基
板等の金属を酸で溶解するので、該廃プリント基板等に
使用されている高価な貴金属を、効率よく回収すること
ができる。
(3) According to the above (1), the metal of the waste printed circuit board or the like is dissolved by the acid, so that the expensive noble metal used for the waste printed circuit board or the like can be efficiently recovered.

【0033】(4)前記(1)によって、処理中に発生
する有害な蒸気やガスあるいは処理液は無公害化でき、
安全に実施することができる。
(4) By the above (1), harmful vapors, gases or processing liquids generated during processing can be made pollution-free,
It can be implemented safely.

【0034】(5)請求項2〜6も前記(1)〜(4)
と同様な効果が得られる。
(5) Claims 2 to 6 are also the above (1) to (4).
The same effect can be obtained.

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

【図1】本発明の第1の実施の形態の工程図。FIG. 1 is a process chart of a first embodiment of the present invention.

【図2】金属溶解工程の説明図。FIG. 2 is an explanatory view of a metal melting step.

【図3】貴金属等の回収工程の説明図。FIG. 3 is an explanatory diagram of a recovery step of precious metals and the like.

【図4】スズ、銀回収工程の説明図。FIG. 4 is an explanatory diagram of a tin and silver recovery step.

【図5】水銀回収工程の説明図。FIG. 5 is an explanatory diagram of a mercury recovery step.

【図6】残存金属回収工程の説明図。FIG. 6 is an explanatory view of a residual metal recovery step.

【図7】アルミニウム回収工程の説明図。FIG. 7 is an explanatory diagram of an aluminum recovery step.

【図8】本発明の第2の実施の形態の工程図。FIG. 8 is a process chart of the second embodiment of the present invention.

【図9】合成樹脂材除去工程の説明図。FIG. 9 is an explanatory view of a synthetic resin material removing step.

【図10】本発明の第3の実施の形態の工程図。FIG. 10 is a process chart of a third embodiment of the present invention.

【図11】本発明の第4の実施の形態の工程図。FIG. 11 is a process chart of a fourth embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1:金属溶解工程、 2:廃プリント基板等、 3:酸、 4、4A〜4H:金属溶解液、 5:金属溶解酸収納タンク、 6:フィルター、 7:樋、 8:開閉弁、 9:酸収納タンク、 10:投入装置、 11:金属溶解装置、 12:ガス等の無害化処理工程、 13:排出通路、 14:湿式スクラバ排煙処理装置本体、 15:中和剤、 16:中和剤収納タンク、 17:ポンプ、 18:供給路、 19:排出路、 20:湿式スクラバ排煙処理装置、 21:貴金属等の回収工程、 22:アルカリ液、 23:濾布、 24:スズ、銀回収工程、 25:ひしゃく、 26:水銀回収工程、 27:残存金属回収工程、 28:アルミニウム回収工程、 29:非溶解物除去工程、 30、30A:非溶解物、 31:洗浄脱水工程、 32:第1の洗浄工程、 33:第2の洗浄工程、 34:脱水工程、 35:超高温燃焼工程、 36:加工工程、 37:合成樹脂材除去工程、 38:廃植物性油、 39:炉や釜、 40:ハンダ除去工程。 1: Metal dissolving process, 2: Waste printed circuit board, etc. 3: Acid, 4, 4A to 4H: Metal dissolving liquid, 5: Metal dissolving acid storage tank, 6: Filter, 7: Gutter, 8: On-off valve, 9: Acid storage tank, 10: charging device, 11: metal melting device, 12: detoxification process of gas etc., 13: discharge passage, 14: wet scrubber flue gas treatment device main body, 15: neutralizing agent, 16: neutralization Agent storage tank, 17: pump, 18: supply path, 19: discharge path, 20: wet scrubber flue gas treatment device, 21: recovery process of precious metals, etc., 22: alkaline liquid, 23: filter cloth, 24: tin, silver Recovery step, 25: ladle, 26: mercury recovery step, 27: residual metal recovery step, 28: aluminum recovery step, 29: non-dissolved substance removal step, 30, 30A: non-dissolved substance, 31: washing and dewatering step, 32: A first cleaning step, 3: Second washing step, 34: Dehydration step, 35: Ultra high temperature combustion step, 36: Processing step, 37: Synthetic resin material removing step, 38: Waste vegetable oil, 39: Furnace or pot, 40: Solder removal Process.

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】 廃プリント基板等を金属を溶解すること
ができる硝酸、塩酸、硫酸等の酸に投入して溶解する金
属溶解工程と、この金属溶解工程で発生する蒸気やガス
を無害化処理するガス等の無害化処理工程と、前記金属
溶解工程で溶解金属を含む金属溶解酸にアリカリを加え
てPHを4〜5にして析出されるPt、Pd、Rh、O
s、Ru、Au等の貴金属等を濾過して回収する貴金属
等の回収工程と、前記金属溶解工程で溶解されないガラ
エポやポリミド等の非溶解物を除去する非溶解物除去工
程とを含むことを特徴とする廃プリント基板等の処理方
法。
1. A metal dissolving step in which a waste printed circuit board or the like is dissolved in an acid such as nitric acid, hydrochloric acid, sulfuric acid or the like capable of dissolving a metal, and a process of detoxifying steam or gas generated in the metal dissolving step. Pt, Pd, Rh, O deposited by adding alkali to a metal-dissolving acid containing a dissolving metal in the metal dissolving step to make the PH 4-5.
s, Ru, a noble metal or the like that filters and recovers a noble metal such as Au, and a non-dissolved matter removing step of removing undissolved matter such as glass epoxy or polyimide that is not dissolved in the metal dissolving step. A method for treating waste printed circuit boards and the like.
【請求項2】 廃プリント基板等からポリエチレン、ポ
リエステル、エポキシ樹脂、フェノール樹脂、ポリミド
等の合成樹脂材を除去する合成樹脂材除去工程と、この
合成樹脂材除去工程で合成樹脂材が除去された廃プリン
ト基板等を金属を溶解することができる硝酸、塩酸、硫
酸等の酸に投入して溶解する金属溶解工程と、この金属
溶解工程で発生する蒸気やガスを無害化処理するガス等
の無害化処理工程と、前記金属溶解工程で溶解金属を含
む金属溶解酸にアリカリを加えてPHを4〜5にして析
出されるPt、Pd、Rh、Os、Ru、Au等の貴金
属等を濾過して回収する貴金属等の回収工程と、前記金
属溶解工程で溶解されないガラエポやポリミド等の非溶
解物を除去する非溶解物除去工程とを含むことを特徴と
する廃プリント基板等の処理方法。
2. A synthetic resin material removing step for removing a synthetic resin material such as polyethylene, polyester, epoxy resin, phenol resin, or polyimide from a waste printed circuit board or the like, and the synthetic resin material is removed in the synthetic resin material removing step. A metal dissolving process in which waste printed circuit boards and the like are dissolved by adding them to an acid such as nitric acid, hydrochloric acid, and sulfuric acid capable of dissolving metals, and a harmless gas and the like that detoxifies steam and gas generated in the metal dissolving process. Noble metals such as Pt, Pd, Rh, Os, Ru, and Au that are precipitated by adding alkali to a metal-dissolving acid containing a dissolving metal in the metal dissolving step and adding a alkali to the metal-dissolving acid containing the dissolving metal in the metal dissolving step are filtered. Waste printed circuit board comprising a step of recovering precious metals and the like to be recovered and a non-dissolved substance removing step of removing undissolved substances such as glass epoxy and polyimide which are not dissolved in the metal dissolving step. Processing method.
【請求項3】 廃プリント基板等からハンダを除去する
ハンダ除去工程と、このハンダ除去工程でハンダが除去
された廃プリント基板等を金属を溶解することができる
硝酸、塩酸、硫酸等の酸に投入して溶解する金属溶解工
程と、この金属溶解工程で発生する蒸気やガスを無害化
処理するガス等の無害化処理工程と、前記金属溶解工程
で溶解金属を含む金属溶解酸にアリカリを加えてPHを
4〜5にして析出されるPt、Pd、Rh、Os、R
u、Au等の貴金属等を濾過して回収する貴金属等の回
収工程と、前記金属溶解工程で溶解されないガラエポや
ポリミド等の非溶解物を除去する非溶解物除去工程とを
含むことを特徴とする廃プリント基板等の処理方法。
3. A solder removing step for removing solder from a waste printed circuit board or the like, and the waste printed circuit board or the like from which the solder has been removed in the solder removing step is treated with an acid such as nitric acid, hydrochloric acid, sulfuric acid or the like capable of dissolving metal. A metal dissolving step for introducing and dissolving, a detoxifying step such as a gas for detoxifying steam and gas generated in the metal dissolving step, and adding alkali to the metal dissolving acid containing the dissolved metal in the metal dissolving step. , Pt, Rh, Os, R deposited at a pH of 4-5
and a step of removing a noble metal such as a noble metal such as u, Au and the like by filtration, and a step of removing a non-dissolved substance such as a glass epoxy or a polyimide which is not dissolved in the metal dissolving step. Of waste printed circuit boards.
【請求項4】 廃プリント基板等を金属を溶解すること
ができる硝酸、塩酸、硫酸等の酸に投入して溶解する金
属溶解工程と、この金属溶解工程で発生する蒸気やガス
を無害化処理するガス等の無害化処理工程と、前記金属
溶解工程で溶解金属を含む金属溶解酸にアリカリを加え
てPHを4〜5にして析出されるPt、Pd、Rh、O
s、Ru、Au等の貴金属等を濾過して回収する貴金属
等の回収工程と、この貴金属等の回収工程で貴金属等の
回収済みの金属溶解液にアルカリを加えてPHをほぼ8
に調整するとともに、Clイオンを加えて浮遊するSn
を回収し、かつ析出され沈殿するAgNOを濾過
して回収する、スズ、銀回収工程と、このスズ、銀回収
工程でスズや銀の回収済の金属溶解液に還元剤としての
Feを投入して析出されるHgClを濾過して回収す
る水銀回収工程と、この水銀回収工程で水銀の回収済の
金属溶解液にアルカリを加えてPHをほぼ8に調整する
と析出されたり、溶媒抽出等によってPb(OH)
Mn(OH)、Fe(OH)、Cu(OH)、N
i(OH)、ZnCdを回収する残存金属回収工程
と、前記金属溶解工程で溶解されないガラエポやポリミ
ド等の非溶解物を除去する非溶解物除去工程とを含むこ
とを特徴とする廃プリント基板等の処理方法。
4. A metal dissolving step of disposing a waste printed board or the like by dissolving it in an acid such as nitric acid, hydrochloric acid, sulfuric acid or the like capable of dissolving a metal, and detoxifying steam or gas generated in the metal dissolving step. Pt, Pd, Rh, O deposited by adding alkali to a metal-dissolving acid containing a dissolving metal in the metal dissolving step to make the PH 4-5.
a process of recovering a precious metal such as s, Ru, Au or the like by filtering, and an alkali is added to a solution of the metal which has been recovered such as a precious metal in the process of recovering the precious metal to adjust the pH to about 8;
And add Cl ions to float the Sn
A step of recovering O 2 and filtering and recovering AgNO 3 which precipitates and precipitates. A step of recovering tin and silver, and a step of adding Fe or Fe as a reducing agent to a metal solution in which tin or silver has been recovered in the step of recovering tin or silver. A mercury recovery step of filtering and recovering HgCl 2 deposited by introducing the above, and adding an alkali to the molten metal solution in which mercury has been recovered in this mercury recovery step to adjust the pH to about 8, to precipitate or remove the solvent. Pb (OH) 2 ,
Mn (OH) 2 , Fe (OH) 2 , Cu (OH) 2 , N
A waste printed circuit board comprising: a residual metal recovery step of recovering i (OH) 2 and ZnCd; and a non-dissolved substance removing step of removing undissolved substances such as glass epoxy and polyimide which are not dissolved in the metal dissolving step. Processing method.
【請求項5】 廃プリント基板等からポリエチレン、ポ
リエステル、エポキシ樹脂、フェノール樹脂、ポリミド
等の合成樹脂材を溶解して浮遊させるとともに、ハンダ
を溶解して沈殿させることができる温度に加熱した植物
性油に投入して合成樹脂材とハンダを除去する合成樹
脂、ハンダ除去工程と、この合成樹脂、ハンダ除去工程
で合成樹脂材とハンダが除去された廃プリント基板等を
金属を溶解することができる硝酸、塩酸、硫酸等の酸に
投入して溶解する金属溶解工程と、この金属溶解工程で
発生する蒸気やガスを無害化処理するガス等の無害化処
理工程と、前記金属溶解工程で溶解金属を含む金属溶解
酸にアリカリを加えてPHを4〜5にして析出されるP
t、Pd、Rh、Os、Ru、Au等の貴金属等を濾過
して回収する貴金属等の回収工程と、前記金属溶解工程
で溶解されないガラエポやポリミド等の非溶解物を除去
する非溶解物除去工程とを含むことを特徴とする廃プリ
ント基板等の処理方法。
5. A vegetable plant heated to a temperature at which a synthetic resin material such as polyethylene, polyester, epoxy resin, phenol resin, or polyimide is dissolved and suspended from a waste printed circuit board and solder is dissolved and precipitated. Synthetic resin that is put into oil to remove the synthetic resin material and solder, a solder removing step, and metal of the synthetic resin material and the waste printed board from which the solder has been removed in the solder removing step can dissolve metals. A metal dissolving step of dissolving by pouring into an acid such as nitric acid, hydrochloric acid, sulfuric acid, etc .; a detoxifying step of a gas or the like for detoxifying steam or gas generated in the metal dissolving step; P is precipitated by adding alkali to a metal-dissolving acid containing
a process of recovering a precious metal such as t, Pd, Rh, Os, Ru, and Au by filtration and a process of removing a non-dissolved material that removes a non-dissolved material such as a glass epoxy or a polyimide that is not dissolved in the metal dissolving step. And a method for treating a waste printed circuit board or the like.
【請求項6】 廃プリント基板等を金属を溶解すること
ができる硝酸、塩酸、硫酸等の酸に投入して溶解する金
属溶解工程と、この金属溶解工程で発生する蒸気やガス
を無害化処理するガス等の無害化処理工程と、前記金属
溶解工程で溶解金属を含む金属溶解酸にアリカリを加え
てPHを4〜5にして析出されるPt、Pd、Rh、O
s、Ru、Au等の貴金属等を濾過して回収する貴金属
等の回収工程と、前記金属溶解工程で溶解されないガラ
エポやポリミド等の非溶解物を除去する非溶解物除去工
程と、この非溶解物除去工程で除去された非溶解物を洗
浄して脱水する洗浄脱水工程と、この洗浄脱水工程で洗
浄脱水された非溶解物を炉芯の温度が約10,000℃
となるプラズマアーク、アーク放電による超高温燃焼炉
で燃焼させる超高温燃焼工程と、この超高温燃焼工程で
溶解状態で残留する残留物を所定の形状に成型して人造
石等に加工する加工工程とを含むことを特徴とする廃プ
リント基板等の処理方法。
6. A metal dissolving step in which a waste printed circuit board or the like is introduced and dissolved in an acid such as nitric acid, hydrochloric acid, sulfuric acid or the like capable of dissolving a metal, and a process for detoxifying steam or gas generated in the metal dissolving step. Pt, Pd, Rh, O deposited by adding alkali to a metal-dissolving acid containing a dissolving metal in the metal dissolving step to make the PH 4-5.
a process of recovering a precious metal such as s, Ru, Au or the like by filtration, a process of removing a non-dissolved material such as glass epoxy or polymid which is not dissolved in the metal dissolving process, and a process of removing the undissolved material. A washing and dehydrating step of washing and dewatering the non-dissolved matter removed in the substance removing step, and a furnace core having a temperature of about 10,000 ° C.
An ultra-high-temperature combustion process of burning in an ultra-high-temperature combustion furnace by plasma arc and arc discharge, and a processing process of molding the residue remaining in the molten state in this ultra-high-temperature combustion process into a predetermined shape and processing it into artificial stone etc. And a method for treating a waste printed circuit board or the like.
JP20721397A 1997-07-15 1997-07-15 Treatment of waste printed circuit board Pending JPH1136020A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP20721397A JPH1136020A (en) 1997-07-15 1997-07-15 Treatment of waste printed circuit board

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP20721397A JPH1136020A (en) 1997-07-15 1997-07-15 Treatment of waste printed circuit board

Publications (1)

Publication Number Publication Date
JPH1136020A true JPH1136020A (en) 1999-02-09

Family

ID=16536121

Family Applications (1)

Application Number Title Priority Date Filing Date
JP20721397A Pending JPH1136020A (en) 1997-07-15 1997-07-15 Treatment of waste printed circuit board

Country Status (1)

Country Link
JP (1) JPH1136020A (en)

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