TW201036718A - Method for recovering gold, silver, copper and iron from valuable metal-containing plasma-caused slag - Google Patents
Method for recovering gold, silver, copper and iron from valuable metal-containing plasma-caused slag Download PDFInfo
- Publication number
- TW201036718A TW201036718A TW98111087A TW98111087A TW201036718A TW 201036718 A TW201036718 A TW 201036718A TW 98111087 A TW98111087 A TW 98111087A TW 98111087 A TW98111087 A TW 98111087A TW 201036718 A TW201036718 A TW 201036718A
- Authority
- TW
- Taiwan
- Prior art keywords
- copper
- silver
- iron
- metal
- residue
- Prior art date
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B7/00—Working up raw materials other than ores, e.g. scrap, to produce non-ferrous metals and compounds thereof; Methods of a general interest or applied to the winning of more than two metals
- C22B7/001—Dry processes
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B11/00—Obtaining noble metals
- C22B11/02—Obtaining noble metals by dry processes
- C22B11/021—Recovery of noble metals from waste materials
- C22B11/025—Recovery of noble metals from waste materials from manufactured products, e.g. from printed circuit boards, from photographic films, paper, or baths
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B11/00—Obtaining noble metals
- C22B11/04—Obtaining noble metals by wet processes
- C22B11/042—Recovery of noble metals from waste materials
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B11/00—Obtaining noble metals
- C22B11/04—Obtaining noble metals by wet processes
- C22B11/042—Recovery of noble metals from waste materials
- C22B11/046—Recovery of noble metals from waste materials from manufactured products, e.g. from printed circuit boards, from photographic films, paper or baths
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B15/00—Obtaining copper
- C22B15/0063—Hydrometallurgy
- C22B15/0084—Treating solutions
- C22B15/0089—Treating solutions by chemical methods
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B15/00—Obtaining copper
- C22B15/0063—Hydrometallurgy
- C22B15/0084—Treating solutions
- C22B15/0089—Treating solutions by chemical methods
- C22B15/0091—Treating solutions by chemical methods by cementation
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B3/00—Extraction of metal compounds from ores or concentrates by wet processes
- C22B3/04—Extraction of metal compounds from ores or concentrates by wet processes by leaching
- C22B3/06—Extraction of metal compounds from ores or concentrates by wet processes by leaching in inorganic acid solutions, e.g. with acids generated in situ; in inorganic salt solutions other than ammonium salt solutions
- C22B3/065—Nitric acids or salts thereof
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B3/00—Extraction of metal compounds from ores or concentrates by wet processes
- C22B3/04—Extraction of metal compounds from ores or concentrates by wet processes by leaching
- C22B3/06—Extraction of metal compounds from ores or concentrates by wet processes by leaching in inorganic acid solutions, e.g. with acids generated in situ; in inorganic salt solutions other than ammonium salt solutions
- C22B3/08—Sulfuric acid, other sulfurated acids or salts thereof
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B3/00—Extraction of metal compounds from ores or concentrates by wet processes
- C22B3/20—Treatment or purification of solutions, e.g. obtained by leaching
- C22B3/44—Treatment or purification of solutions, e.g. obtained by leaching by chemical processes
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B3/00—Extraction of metal compounds from ores or concentrates by wet processes
- C22B3/20—Treatment or purification of solutions, e.g. obtained by leaching
- C22B3/44—Treatment or purification of solutions, e.g. obtained by leaching by chemical processes
- C22B3/46—Treatment or purification of solutions, e.g. obtained by leaching by chemical processes by substitution, e.g. by cementation
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B4/00—Electrothermal treatment of ores or metallurgical products for obtaining metals or alloys
- C22B4/005—Electrothermal treatment of ores or metallurgical products for obtaining metals or alloys using plasma jets
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B7/00—Working up raw materials other than ores, e.g. scrap, to produce non-ferrous metals and compounds thereof; Methods of a general interest or applied to the winning of more than two metals
- C22B7/005—Separation by a physical processing technique only, e.g. by mechanical breaking
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B7/00—Working up raw materials other than ores, e.g. scrap, to produce non-ferrous metals and compounds thereof; Methods of a general interest or applied to the winning of more than two metals
- C22B7/006—Wet processes
- C22B7/007—Wet processes by acid leaching
-
- 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
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Metallurgy (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Organic Chemistry (AREA)
- Environmental & Geological Engineering (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geology (AREA)
- Life Sciences & Earth Sciences (AREA)
- Geochemistry & Mineralogy (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Inorganic Chemistry (AREA)
- Plasma & Fusion (AREA)
- Physics & Mathematics (AREA)
- Manufacture And Refinement Of Metals (AREA)
Abstract
Description
201036718 六、發明說明: 【發明所屬之技術領域】 本發明係以電漿培燒方式將廢印刷電路板中之樹脂予以 快速焙燒分解,再利用研磨、磁選、篩分等方式,使有價金屬 有效分離,來達成廢印刷電路板中金、銀、銅、鐵有價金屬之 分離,再利用浸潰溶蝕、晶析法、沉澱法、置換法、電解法等 方法來針對金、銀、銅有價金屬之資源回收。本發明屬於環境 保護及廢棄物資源再生技術領域。 〇 · 【先前技術】 廢印刷電路板中所含之有價金屬如金、銀、銅,如任其棄 置無法回收,不但會危害環境,亦甚屬可惜。目前廢印刷電路 板之回收處理技術主要為粉碎回收法及燃燒回收法,由於廢印 刷電路板中含有樹脂成份’具彈性不綠碎,如採用直接粉碎 方式將需耗費較大能源,亦會產生粉塵、噪音及機具損耗等問 題。另如採用傳統燃燒方式,由於燃燒效率差,耗時較久,其 ❹ 能源損耗亦較不符合經濟效益。故本發明將以燃燒效率高之電 漿焙燒方式,將廢印刷電路板中之樹脂成份予以快速焙燒分解 並脆化,以降低研磨所需之耗能與機具損耗,以利後續廢印刷 電路板中有價金屬之分離回收。 經查國内相關廢印刷電路板資源回收之專利,如中華民國 公告編號第247281號『由印刷電路板分離回收有價物質之方 法』及中華民國公告編號第36904號『廢印刷電路板的再資源 化處理方法』’其内容主要係將廢印刷電路板經由直接粉碎後 再進行有價金屬回收。另中華民國公告編號1268184『回收廢 201036718 電路板Γ方法』,其主要是將廢印刷電路板加熱至200 利用㈣ΐ焊錫融溶,再將表面電子零件予於拆除,再 冷H贿等方式來时印刷電路板中之有價物質。 綜合上述結果得知,並未發現有任何相關專利與技術,係 採用電漿培燒、研磨、磁選及篩分等方式來快速分離回收廢印 刷電路板中之有價金屬。 【發明内容】 〇 廢印刷電路板中所含之金、銀、銅金屬具有回收價值,如 無法將其回收再利用,將造成整體金屬資源浪費,因此本發明 經電漿培燒、研磨、磁選及篩分等方式來快速且確實地進行廢 印刷電路板中有價金屬之分離回收,以達到有效回收再利用有 價金屬之功效。 為達上述之目的,本發明係一種將廢印刷電路板經電漿焙 燒及研磨後所得之電漿熔渣以篩分及磁選、浸潰溶蝕、晶析 法、沉澱法、置換法、電解法等方式來回收廢印刷電路板中有 Ο 價金屬之方法’首先再電漿熔渣以0.149mm篩網進行筛分, 再分別以磁選方式將鐵質物質選出,此鐵質金屬可送往煉鋼廠 進行鐵金屬之再生冶煉;而磁選後之不感磁金屬與玻璃纖維顆 粒’大於0.149mm之篩上物質含銅金屬量高,可送至煉銅廠 回收銅金屬’另小於0.149mm之篩下物質,先以一次硫酸浸 潰於18N硫酸、固液比10g/50m卜70°C下浸漬1小時之條件 下,可達成90.56%之銅浸潰回收率,此一次含銅浸潰液直接 在室溫下靜置48小時,可達成浸潰液中58.28%之銅晶析成硫 酸銅晶體之最佳晶析效果。而晶析過後濾液中之殘留銅金屬, 6 201036718 經以鐵粉為置換劑,當添加鐵粉為理論值1〇〇倍時,可將晶析 後濾液中銅1〇0%置換成銅粉回收。另一次硫酸浸潰殘渣之 銅,則以18N硫酸在固液比5g/5〇m卜於7〇。(;下浸潰2小時, T將殘/查中之銅予以浸潰溶餘,此二次含銅浸潰液,再 以鐵粉為置換劑,添加量為150倍鐵粉理論值,可將二次硫酸 浸潰液中之銅100%予以置換回收成銅粉。 而二次硫酸浸潰殘中之銀渣以8N硝酸在固液比 lg/50ml ’於7〇°C下浸潰4小時,可將殘渣中之銀1〇〇%予以 浸潰溶钱,此最佳含銀浸潰液,先以氨水調整其pH值至_ 10 後所得之含銀溶液,再以鹽酸(12N)為沉澱劑,於鹽酸(〇11)/含 銀溶液(ml)=4之條件,可將銀金屬100%沉澱回收成氯化銀。 而硝酸浸潰殘渣中所含之金,經以100%之王水作為浸潰劑, 在固液比0.5g(殘渣)/5〇ml(王水)的條件下,於7〇〇c浸潰4小 時’可將殘渣中之金100%予以浸潰溶蝕,此最佳含金浸潰液, 經以鋅粉為置換劑,可將最佳含金浸漬液中之金99 43%予以 置換回收。 廢印刷電路板經本發明將經電漿焙燒及研磨後所得之電 漿炼渣,以篩分、磁選、浸潰溶钱、晶析法、沉澱法、置換法、 電解法等方式,可以達到廢印刷電路板減量與資源回收之目 的。 【實施方式】 本發明之較佳方法示於第一圖,首先將收集之電漿炼潰, 經以〇.149mm篩網篩分2,大於0.149mm之物質21以磁選3 方式將鐵質物質選出,此鐵質金屬31可送往煉鋼廠進行鐵金 201036718 屬之再生冶煉,而磁選後之非鐵金屬32,含銅金屬量高,可 送至練銅廠回收銅金屬,另小於〇.149mm之篩下物質22,經 以磁選4後所得之鐵金屬41亦可直接送往煉鋼廠進行鐵金屬 之再生冶煉,而磁選後之非鐵物質42(其外觀如附件一所示) 先以一次硫酸浸潰5於18N硫酸、固液比i〇g/5〇ml、7〇°c下 浸潰1小時之條件下,可達成90.56%之銅浸漬回收率,此一 次含銅浸潰液51直接在室溫下晶析靜置48小時),可達成 浸潰液中58.28%之銅晶析成硫酸銅晶體61(其外觀如附件二 〇 所示)之最佳晶析效果。 而晶析過後之最佳晶析濾液62中之殘留銅金屬,經以鐵 粉為置換劑7,當添加鐵粉為理論值1〇〇倍時,可將晶析後濾 液中銅100%置換成銅粉71回收。另一次硫酸浸潰殘渣52之 銅’則以18N硫酸在固液比5g/5〇m卜於70〇C下浸潰2小時, 可將殘潰中之銅100%予以浸潰溶餘8,此二次含銅浸漬液 81,再經以鐵粉為置換劑9,添加量為15〇倍鐵粉理論值,可 將二次硫酸浸潰液中之銅100%予以置換回收成銅粉91。 ❹而二次硫酸浸潰殘82中之銀渣以8N硝酸在固液比 lg/50nU,於70°C下浸漬4小時,可將殘渣中之銀1〇〇%予以 浸潰溶蚀10,此最佳含銀浸潰液101,先以氨水調整其pH值 後所得之含銀溶液11 ’再以鹽酸(12N)為沉澱劑12,於鹽酸(ml)/ 含銀溶液(ml)=4之條件,可將銀金屬1〇〇%沉澱回收成氣化銀 121。而硝酸浸潰殘渣中所含之金1〇2,經以1〇〇%之王水作為 浸潰劑,在固液比〇.5g(殘渣)/5〇mi(王水)的條件下,於7〇。匸浸 潰4小時’可將殘渣中之金1〇〇%予以浸潰溶钱13,此最佳含 金/文潰液131 ’以鋅粉為置換劑14,可將最佳含金浸潰液中之 201036718 金99.43%予以置換回收hi。 ,茲將本發明之 為使本發明更加顯現出其進步性與實用性 優點列舉如下: 一 1. 本發明可快速簡易回收廢印刷電路板中之金、銀、銅、 鐵有價金屬,供作金屬冶煉廠之原料,以減少金屬之浪費。 2. 本發明可減対刷電路板之廢棄數量,降低印刷電路板 中有害物質對環境與人體之危害。 3. 本發明具安全性與進步性。201036718 VI. Description of the invention: [Technical field to which the invention pertains] The present invention rapidly decomposes the resin in the waste printed circuit board by means of plasma burning, and then uses grinding, magnetic separation, screening, etc. to make the valuable metal effective. Separation, to achieve the separation of gold, silver, copper, iron valuable metals in waste printed circuit boards, and then use gold, silver, copper and valuable metals by methods such as impregnation, crystallization, precipitation, displacement, and electrolysis. Resource recycling. The invention belongs to the technical field of environmental protection and waste resource regeneration. 〇 · [Prior Art] Valuable metals such as gold, silver, and copper contained in waste printed circuit boards cannot be recycled if they are discarded, which is not only harmful to the environment, but also a pity. At present, the recycling technology of waste printed circuit boards is mainly the pulverization recovery method and the combustion recovery method. Since the resin component contained in the waste printed circuit board is elastic and non-green, if the direct pulverization method is used, it will consume a large amount of energy, and it will also be generated. Dust, noise and loss of implements. Another example is the use of conventional combustion methods. Due to poor combustion efficiency and long time consuming, the energy loss is also less economical. Therefore, the invention will rapidly decompose and embrittle the resin component in the waste printed circuit board by the plasma roasting method with high combustion efficiency, so as to reduce the energy consumption and the tool loss required for the grinding, so as to facilitate the subsequent waste printed circuit board. Separation and recovery of valuable metals. Patent for the recovery of domestic waste printed circuit board resources, such as the Republic of China Bulletin No. 247281 "Method for Separating and Recovering Valuable Substances from Printed Circuit Boards" and Republic of China Announcement No. 36904 "Re-resources of Waste Printed Circuit Boards" The treatment method 』's content mainly involves the direct pulverization of the waste printed circuit board and the recovery of valuable metals. In addition, the Republic of China Announcement No. 1268184 "Recycling Waste 201036718 Circuit Board Method" is mainly to heat the waste printed circuit board to 200. (4) When the solder is melted, the surface electronic components are removed, and then the cold bribes are used. A valuable substance in a printed circuit board. Based on the above results, it has not been found that any related patents and technologies have been used to rapidly separate and recover valuable metals in waste printed circuit boards by means of plasma burning, grinding, magnetic separation and screening. SUMMARY OF THE INVENTION The gold, silver and copper metal contained in the decadent printed circuit board have a recovery value. If it cannot be recycled and reused, the overall metal resource will be wasted. Therefore, the present invention is subjected to plasma burning, grinding, and magnetic separation. And screening and other means to quickly and reliably carry out the separation and recovery of valuable metals in the waste printed circuit board, in order to achieve effective recovery and reuse of valuable metals. For the purpose of the above, the present invention is a plasma slag obtained by plasma baking and grinding a waste printed circuit board by sieving and magnetic separation, impregnation, crystallization, precipitation, displacement, electrolysis The method of recovering the valence metal in the waste printed circuit board by the method of 'first re-pulping the slag with 0.149mm sieve, and then selecting the iron material by magnetic separation, the iron metal can be sent to the refining The steel plant carries out the refining and smelting of iron metal; while the non-magnetic metal and glass fiber particles after magnetic separation have a high content of copper-containing metal on the sieve material larger than 0.149mm, which can be sent to the copper smelting plant to recover the copper metal 'the sieve smaller than 0.149mm The next substance is firstly immersed in 18N sulfuric acid with a single sulfuric acid, and the solid-liquid ratio is immersed at 10 ° C for 50 hours at 70 ° C for 1 hour, and the copper leaching recovery rate of 90.56% can be achieved. After standing at room temperature for 48 hours, the optimum crystallization effect of 58.28% of copper crystallized into copper sulfate crystals in the impregnation solution can be achieved. After the crystallization, the residual copper metal in the filtrate, 6 201036718 is treated with iron powder as a displacer. When the iron powder is added to the theoretical value 1 〇〇 times, the copper in the filtrate after crystallization can be replaced by copper powder. Recycling. In another case, the copper of the residue was leached with sulfuric acid at a solid-liquid ratio of 5 g/5 〇m to 7 以. (; under the dipping for 2 hours, T will be the residue / check the copper to be impregnated and dissolved, the second copper-containing impregnation solution, and then iron powder as a replacement agent, the amount of 150 times the iron powder theoretical value, can 100% of the copper in the secondary sulfuric acid leaching solution is replaced by copper powder. The silver slag in the secondary sulfuric acid immersion residue is immersed in 8N nitric acid at a solid-liquid ratio of lg/50ml 'at 7 ° C. In the hour, 1% of the silver in the residue can be immersed and dissolved. The best silver-containing impregnation solution is first adjusted with ammonia to adjust the pH value to _ 10 to obtain the silver-containing solution, followed by hydrochloric acid (12N). As a precipitant, 100% precipitation of silver metal can be recovered into silver chloride under the conditions of hydrochloric acid (〇11)/silver solution (ml)=4. The gold contained in the nitrate impregnation residue is 100%. As the impregnating agent, the king water can be impregnated with 100% of the gold in the residue under the condition of solid-liquid ratio of 0.5g (residue)/5〇ml (Aqua regia) at 7〇〇c for 4 hours. Corrosion, the best gold-containing impregnation solution, with zinc powder as a displacer, can replace and recover the gold 99 43% in the best gold-containing immersion liquid. The waste printed circuit board is subjected to plasma roasting and grinding by the invention. Electric pulping The method of sieving, magnetic separation, impregnation, crystallization, precipitation, displacement, electrolysis, etc. can achieve the purpose of waste printed circuit board reduction and resource recovery. [Embodiment] The preferred method of the present invention As shown in the first figure, the collected plasma is firstly smelted, and sieved by a 149149mm sieve 2, and a substance 21 larger than 0.149 mm is selected by magnetic separation 3, and the iron metal 31 can be sent to The steelmaking plant carries out the refinery smelting of iron gold 201036718, and the non-ferrous metal 32 after magnetic separation has a high amount of copper metal, which can be sent to the copper processing plant to recover copper metal, and the less than 149. The iron metal 41 obtained after magnetic separation 4 can also be sent directly to the steelmaking plant for regenerative smelting of iron metal, and the non-ferrous substance 42 after magnetic separation (the appearance of which is shown in Annex 1) is first impregnated with primary sulfuric acid by 5 to 18N sulfuric acid. Under the conditions of solid-liquid ratio i〇g/5〇ml and 7〇°c for 1 hour, 90.56% copper impregnation recovery rate can be achieved. This copper-containing impregnation solution 51 is directly crystallized at room temperature. After standing for 48 hours), 58.28% of the copper crystals in the impregnation solution can be crystallized into copper sulfate crystals 61 (external The best crystallization results shown in annex twenty) of. After the crystallization, the residual copper metal in the optimum crystallization filtrate 62 is replaced by iron powder as the displacer 7. When the iron powder is added to the theoretical value of 1 〇〇, the copper in the filtrate after crystallization can be replaced by 100%. Copper powder 71 is recovered. The copper of another sulfuric acid impregnated residue 52 is impregnated with 18N sulfuric acid at a solid-liquid ratio of 5g/5〇m at 70〇C for 2 hours, and 100% of the copper in the residue can be impregnated and dissolved. The secondary copper-containing immersion liquid 81 is further treated with iron powder as a displacer 9, and the added amount is 15 〇 iron powder theoretical value, and 100% of the copper in the secondary sulfuric acid immersion liquid can be replaced and recovered into copper powder 91. . The silver slag in the secondary sulfuric acid leaching residue 82 is immersed in 8N nitric acid at a solid-liquid ratio of lg/50 nU at 70 ° C for 4 hours, and the silver in the residue is immersed and etched by 10%. The best silver-containing impregnation solution 101, the silver-containing solution 11' obtained by adjusting the pH value with ammonia water, and then hydrochloric acid (12N) as a precipitant 12, in hydrochloric acid (ml) / silver-containing solution (ml) = 4 Under the conditions, 1%% of the silver metal precipitate can be recovered into the vaporized silver 121. The gold 1〇2 contained in the nitric acid impregnation residue is treated with 1% by weight of aqua regia as an impregnating agent, under the conditions of solid-liquid ratio 〇5g (residue)/5〇mi (Aqua regia). At 7〇.匸 匸 4 4 4 4 4 ' 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 99.43% of the 201036718 gold in the liquid is replaced by hi. The advantages of the present invention for making the present invention more progressive and practical are as follows: 1. The invention can quickly and easily recover gold, silver, copper and iron valuable metals in waste printed circuit boards for use as Raw materials for metal smelters to reduce metal waste. 2. The invention can reduce the waste quantity of the circuit board and reduce the harm of harmful substances in the printed circuit board to the environment and the human body. 3. The invention is safe and progressive.
4. 本發明具工商界與產業界之利用價值。 綜上所述’本發明誠符合發明專利之申請要件並依法提 出申請,祈請鈞局審查委員魏,並辭本發明專利權,實 感德便。 【圖式簡單說明】 第1圖,係本發明之回收流程示意圖。 Q 【主要元件符號說明】 1 · ·電漿熔渣 2 · ·篩分 21 .· +0.149mm 之物質 22· .-0.149mm 之物質 3 · ·磁選(+〇.i49mm) 31 · ·鐵(+0.149mm) 32· ·非鐵物質(+〇.i49mm) 4· ·磁選(-〇.i49mm) 9 201036718 41 . ·鐵(-0.149mm) 42 ··非鐵物質(-0.149mm) 5··—次硫酸浸潰 51 ·. —次含銅浸潰液 52 ·· —次含硫酸浸潰殘渣 6 ·.晶析 61· ·硫酸銅晶體 62 ··最佳晶析滤液 7 .·鐵粉置換(一次含銅浸潰液) 71· ·銅粉(最佳晶析濾液) 8··二次硫酸浸潰 81 ··二次含銅浸潰液 82 ··二次硫酸浸潰殘渣 9 ··鐵粉置換(二次含銅浸潰液) 91 ··銅粉(二次含銅浸潰液) 10 ·.硝酸浸潰 101 ·.最佳含銀浸潰液 102 ··硝酸浸潰液殘渣 11 ··氨水調整pH值 12 · ·鹽酸沉澱 121 ··氯化銀 13 ·.王水浸潰 131 ··最佳含金浸潰液 14· ·鋅粉置換 141 ··置換金4. The invention has the use value of the business community and the industry. In summary, the invention conforms to the application requirements of the invention patent and submits an application according to law, and invites the bureau to examine the member Wei and resign the patent right of the invention. BRIEF DESCRIPTION OF THE DRAWINGS Fig. 1 is a schematic diagram of the recycling process of the present invention. Q [Description of main component symbols] 1 · · Plasma slag 2 · · Screening 21 · · 0.149mm substance 22 · .-0.149mm substance 3 · Magnetic separation (+〇.i49mm) 31 · · Iron ( +0.149mm) 32··Non-ferrous substances (+〇.i49mm) 4··Magnetic selection (-〇.i49mm) 9 201036718 41 . ·Iron (-0.149mm) 42 ··Non-ferrous substances (-0.149mm) 5· · - Sub-sulfuric acid impregnation 51 ·. - Secondary copper-containing impregnation liquid 52 · · - Secondary sulfuric acid impregnation residue 6 ·. Crystallization 61 · · Copper sulfate crystal 62 · · Best crystallized filtrate 7 · Iron powder Replacement (primary copper-containing impregnation solution) 71· · Copper powder (optimal crystallization filtrate) 8··Secondary sulfuric acid impregnation 81 ··Second copper-containing impregnation liquid 82 ··Secondary sulfuric acid impregnation residue 9 · ·Iron powder replacement (secondary copper-containing impregnation solution) 91 ··Copper powder (secondary copper-containing impregnation solution) 10 ·.Nitrate impregnation 101 ·.Optimum silver-containing impregnation solution 102 ··Nitrate leachate Residue 11 ··Ammonia water adjustment pH 12 · · Hydrochloric acid precipitation 121 · · Silver chloride 13 ·. Aqueous water impregnation 131 · · Best gold-containing impregnation liquid 14 · · Zinc powder replacement 141 ·· Replacement gold
Claims (1)
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
TW098111087A TWI372662B (en) | 2009-04-02 | 2009-04-02 | Method for recovering gold, silver, copper and iron from valuable metal-containing plasma-caused slag |
US12/622,551 US20100314242A1 (en) | 2009-04-02 | 2009-11-20 | Method for Recovering Gold, Silver, Copper and Iron from Plasma-Caused Slag Containing Valuable Metals |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
TW098111087A TWI372662B (en) | 2009-04-02 | 2009-04-02 | Method for recovering gold, silver, copper and iron from valuable metal-containing plasma-caused slag |
Publications (2)
Publication Number | Publication Date |
---|---|
TW201036718A true TW201036718A (en) | 2010-10-16 |
TWI372662B TWI372662B (en) | 2012-09-21 |
Family
ID=43305472
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
TW098111087A TWI372662B (en) | 2009-04-02 | 2009-04-02 | Method for recovering gold, silver, copper and iron from valuable metal-containing plasma-caused slag |
Country Status (2)
Country | Link |
---|---|
US (1) | US20100314242A1 (en) |
TW (1) | TWI372662B (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103374659A (en) * | 2012-04-25 | 2013-10-30 | 鑫广再生资源(上海)有限公司 | Method for extracting and recovering precious metal and rare metal from wastes |
CN103981366A (en) * | 2013-02-07 | 2014-08-13 | 欣兴电子股份有限公司 | Method for recovery of metal from circuit board |
CN105833985A (en) * | 2016-03-24 | 2016-08-10 | 清华大学 | Selective separation and recycling method for industrial solid waste slag |
CN113528849A (en) * | 2021-06-02 | 2021-10-22 | 云南滇金投资有限公司 | Method for extracting refined gold from palladium-silver-containing alloy gold |
WO2024062155A1 (en) * | 2022-09-22 | 2024-03-28 | Helsingin Yliopisto | Method of extracting one or more rare and precious metals from a substrate comprising the same |
Families Citing this family (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102218369B (en) * | 2011-04-13 | 2013-01-02 | 济源市东方化工有限责任公司 | Production method of selecting copper from slag after selecting carbon from slag in rotary kiln in zinc industry |
CN103182346A (en) * | 2011-12-30 | 2013-07-03 | 北京有色金属研究总院 | Novel process for improving grade of sulfate cinder iron |
CN103614556B (en) * | 2013-10-08 | 2016-03-23 | 大连东泰产业废弃物处理有限公司 | A kind of process of waste mobile phone wiring board and the method for recovery noble metal |
EP3083016B1 (en) | 2013-12-20 | 2020-07-29 | Greene Lyon Group Inc. | Method and apparatus for recovery of noble metals, including recovery of noble metals from plated and/or filled scrap |
CN104164570B (en) * | 2014-07-25 | 2016-08-24 | 河南中原黄金冶炼厂有限责任公司 | A kind of preprocess method of noble metal smelting slag |
CN104625285A (en) * | 2014-12-23 | 2015-05-20 | 湖南万容科技股份有限公司 | Waste circuit board recovery processing method |
JP2018524480A (en) | 2015-06-24 | 2018-08-30 | グリーン リヨン グループ, インコーポレーテッドGreene Lyon Group, Inc. | Applications related to selective extraction of precious metals using acidic fluids including nitrate-containing fluids |
CN106086417A (en) * | 2016-06-27 | 2016-11-09 | 南开大学 | A kind of method extracting copper and gold from waste mobile phone circuit board |
CN106916512B (en) * | 2017-04-12 | 2019-05-24 | 邹亚静 | A kind of cold galvanizing coating and preparation method thereof |
CN108165754B (en) * | 2017-12-30 | 2019-06-07 | 北京工业大学 | The method that wiring board bath smelting cigarette ash noble metal recycles chlorination enrichment |
CN109402402B (en) * | 2018-12-11 | 2020-08-18 | 西安诺博尔稀贵金属材料股份有限公司 | Method for recovering gold and silver from gold-silver-copper alloy waste |
CN110607458A (en) * | 2019-08-19 | 2019-12-24 | 西北矿冶研究院 | Method for preparing copper powder by using decoppering final solution |
CN111560522A (en) * | 2020-05-22 | 2020-08-21 | 四川君和环保股份有限公司 | Stainless steel pickling sludge treatment method |
CN113862481A (en) * | 2021-09-29 | 2021-12-31 | 杨诤溢 | Method for recycling conductive paste |
Family Cites Families (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4293332A (en) * | 1977-06-08 | 1981-10-06 | Institute Of Nuclear Energy Research | Hydrometallurgical process for recovering precious metals from anode slime |
US5116415A (en) * | 1989-09-25 | 1992-05-26 | Aqs, Inc. | Metal value recovery or removal from aqueous media |
US5490976A (en) * | 1991-08-26 | 1996-02-13 | E. I. Du Pont De Nemours And Company | Continuous ore reaction process by fluidizing |
JP2001259603A (en) * | 2000-03-15 | 2001-09-25 | Sumitomo Metal Mining Co Ltd | Method for discriminating valuable material from used printed circuit board |
US7892505B2 (en) * | 2005-10-29 | 2011-02-22 | Royal Silver Company (Panama) S.A. | Hydrometallurgical process for the treatment of metal-bearing sulfide mineral concentrates |
AU2007231801A1 (en) * | 2006-11-02 | 2008-05-22 | Frank Trask | Leaching of oxidised molybdenum |
TWI343363B (en) * | 2007-04-18 | 2011-06-11 | Univ Da Yeh | A method for the recycling of copper sludge |
-
2009
- 2009-04-02 TW TW098111087A patent/TWI372662B/en not_active IP Right Cessation
- 2009-11-20 US US12/622,551 patent/US20100314242A1/en not_active Abandoned
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103374659A (en) * | 2012-04-25 | 2013-10-30 | 鑫广再生资源(上海)有限公司 | Method for extracting and recovering precious metal and rare metal from wastes |
CN103374659B (en) * | 2012-04-25 | 2016-12-14 | 鑫广再生资源(上海)有限公司 | Valuable, the refinement recovery method of rare metal in a kind of garbage |
CN103981366A (en) * | 2013-02-07 | 2014-08-13 | 欣兴电子股份有限公司 | Method for recovery of metal from circuit board |
CN105833985A (en) * | 2016-03-24 | 2016-08-10 | 清华大学 | Selective separation and recycling method for industrial solid waste slag |
CN105833985B (en) * | 2016-03-24 | 2018-05-11 | 清华大学 | A kind of industrial solid waste residue Selective Separation and recoverying and utilizing method |
CN113528849A (en) * | 2021-06-02 | 2021-10-22 | 云南滇金投资有限公司 | Method for extracting refined gold from palladium-silver-containing alloy gold |
CN113528849B (en) * | 2021-06-02 | 2022-12-23 | 云南滇金投资有限公司 | Method for extracting refined gold from palladium-silver-containing alloy gold |
WO2024062155A1 (en) * | 2022-09-22 | 2024-03-28 | Helsingin Yliopisto | Method of extracting one or more rare and precious metals from a substrate comprising the same |
Also Published As
Publication number | Publication date |
---|---|
TWI372662B (en) | 2012-09-21 |
US20100314242A1 (en) | 2010-12-16 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
TW201036718A (en) | Method for recovering gold, silver, copper and iron from valuable metal-containing plasma-caused slag | |
CN106756084B (en) | Method for extracting noble metal by taking iron-based material as trapping agent | |
CN101575715B (en) | Method for extracting valuable metals from electronic waste | |
CN102994747B (en) | Technology for recovering metallic copper from high-lead copper matte | |
CN102719675B (en) | Method for comprehensively recovering zinc, lead and silver from waste residues generated in zinc smelting | |
CN110551897B (en) | Process for preparing pure copper powder by treating waste circuit board through mechanical and physical method | |
CN102459660A (en) | Extraction of gold from cathode associated gold concentrates | |
CN103757420A (en) | Method for recovering lead and silver from zinc leaching residues | |
CN104046785A (en) | Method for processing waste copper/iron-based diamond tool bit | |
CN103589873B (en) | A kind of method of valuable metal in recover silver cadmia | |
TWI428451B (en) | Valuable metal recovery method from lead-free waste solder | |
CN103966421A (en) | Comprehensive recovery method of ferrous metallurgical solid wastes | |
CN102409176A (en) | Comprehensive treatment process of waste gold-bearing activated carbon | |
JP2010528177A (en) | Method for producing pure metal indium from zinc oxide and / or metal-containing solution | |
CN106222421A (en) | Gold mud treatment method | |
JP5628610B2 (en) | Indium recovery method | |
CN101864519A (en) | Method for selectively leaching and separating tin, lead and copper from waste circuit board | |
JP2017137578A (en) | Method for separating zinc, method for producing zinc material, and method for producing iron material | |
JP2010138490A (en) | Method of recovering zinc | |
JP2019527769A (en) | Concentrating and recovering precious metals | |
JP2011214021A (en) | Method of producing valuable metal | |
CN109402402B (en) | Method for recovering gold and silver from gold-silver-copper alloy waste | |
JP2024526497A (en) | Method for treating by-products of zinc hydrometallurgy process with reduced carbon emissions | |
TWI394846B (en) | Recycling of lead-free silver containing tin solder dross | |
CN110453075A (en) | A method of recycling copper from waste printed circuit board metal concentrate powder |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
MM4A | Annulment or lapse of patent due to non-payment of fees |