CN103484680B - Method for leaching copper in waste printed circuit board by using mixed bacteria - Google Patents
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- 241000894006 Bacteria Species 0.000 title claims abstract description 124
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- UXVMQQNJUSDDNG-UHFFFAOYSA-L Calcium chloride Chemical compound [Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 claims description 6
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- BFNBIHQBYMNNAN-UHFFFAOYSA-N ammonium sulfate Chemical compound N.N.OS(O)(=O)=O BFNBIHQBYMNNAN-UHFFFAOYSA-N 0.000 claims description 6
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- ZPWVASYFFYYZEW-UHFFFAOYSA-L dipotassium hydrogen phosphate Chemical compound [K+].[K+].OP([O-])([O-])=O ZPWVASYFFYYZEW-UHFFFAOYSA-L 0.000 claims description 6
- SURQXAFEQWPFPV-UHFFFAOYSA-L iron(2+) sulfate heptahydrate Chemical compound O.O.O.O.O.O.O.[Fe+2].[O-]S([O-])(=O)=O SURQXAFEQWPFPV-UHFFFAOYSA-L 0.000 claims description 6
- WRUGWIBCXHJTDG-UHFFFAOYSA-L magnesium sulfate heptahydrate Chemical compound O.O.O.O.O.O.O.[Mg+2].[O-]S([O-])(=O)=O WRUGWIBCXHJTDG-UHFFFAOYSA-L 0.000 claims description 6
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- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 abstract description 8
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- 229910052751 metal Inorganic materials 0.000 description 11
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- 241000266272 Acidithiobacillus Species 0.000 description 2
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- CILYKUDMVIRMGY-UHFFFAOYSA-N 4-dodecyl-2-(N-hydroxy-C-phenylcarbonimidoyl)phenol Chemical compound CCCCCCCCCCCCC1=CC=C(O)C(C(=NO)C=2C=CC=CC=2)=C1 CILYKUDMVIRMGY-UHFFFAOYSA-N 0.000 description 1
- CWYNVVGOOAEACU-UHFFFAOYSA-N Fe2+ Chemical compound [Fe+2] CWYNVVGOOAEACU-UHFFFAOYSA-N 0.000 description 1
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- 239000004566 building material Substances 0.000 description 1
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- 230000003749 cleanliness Effects 0.000 description 1
- TXKMVPPZCYKFAC-UHFFFAOYSA-N disulfur monoxide Inorganic materials O=S=S TXKMVPPZCYKFAC-UHFFFAOYSA-N 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000004070 electrodeposition Methods 0.000 description 1
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- XTQHKBHJIVJGKJ-UHFFFAOYSA-N sulfur monoxide Chemical compound S=O XTQHKBHJIVJGKJ-UHFFFAOYSA-N 0.000 description 1
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- 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
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Abstract
本发明公开了一种混合菌浸取废弃印刷电路板中铜的方法,将废弃印刷电路板(PCBs)预处理待用,将嗜酸氧化亚铁硫杆菌和嗜酸氧化硫硫杆菌分别进行耐铜驯化培养后,在混合菌培养液中混合培养;在培养时间到达40h~55h时开始添加PCBs粉末,然后在其他时间点逐点加量添加PCBs粉末,进行生物浸取。本发明的混合菌培养时无需调节培养液的pH值两种菌就能均衡生长,同时两种菌生长时生成大量硫酸和Fe3+用于后期废弃PCBs粉末中铜的浸取,整个过程效率高、节省能源。采用前低后高多点添加的方式,在提高废弃PCBs粉末添加量的基础上,铜浸取率显著提高而菌体生长受抑制程度却相对较小。The invention discloses a method for leaching copper in waste printed circuit boards by mixed bacteria. The waste printed circuit boards (PCBs) are pretreated for use, and acidophilic Thiobacillus ferrooxidans and acidophilic Thiobacillus thiooxidans are respectively subjected to After the copper acclimatization culture, mixed culture in the mixed bacteria culture solution; when the culture time reaches 40h ~ 55h, start to add PCBs powder, and then add PCBs powder point by point at other time points for bioleaching. When the mixed bacteria of the present invention is cultivated, the two bacteria can grow in a balanced manner without adjusting the pH value of the culture solution. At the same time, when the two bacteria grow, a large amount of sulfuric acid and Fe 3+ are generated for the leaching of copper in the waste PCBs powder in the later stage, and the efficiency of the whole process is high. High, save energy. By adopting the method of adding low at the front and then high at multiple points, on the basis of increasing the amount of waste PCBs powder added, the copper leaching rate was significantly increased while the growth of bacteria was relatively less inhibited.
Description
技术领域 technical field
本发明涉及一种废弃印刷电路板中铜的回收方法,具体涉及一种混合菌浸取废弃印刷电路板中铜的方法。 The invention relates to a method for recovering copper from waste printed circuit boards, in particular to a method for leaching copper from waste printed circuit boards with mixed bacteria.
背景技术 Background technique
随着信息技术迅猛发展,电子废弃物(Waste Electric and Electronic equipment, WEEE)产量不断上升,废弃印刷电路板 (Printed Circuit Boards, PCBs)作为WEEE重要组分,通常含有40%左右的金属,其中金属铜是主要的成分,含量高达20%~30%。据估计,我国每年需要处理PCBs大约在50万吨以上并且以22%速度增长。如能实现废弃PCB处理及资源化,既能解决环境污染问题,又能实现金属有效回收,将对我国PCBs行业的可持续发展有着重要意义。 With the rapid development of information technology, the output of waste electric and electronic equipment (WEEE) continues to increase. As an important component of WEEE, waste printed circuit boards (PCBs) usually contain about 40% of metals, of which metal Copper is the main component, with a content as high as 20% to 30%. It is estimated that my country needs to process more than 500,000 tons of PCBs every year and it is growing at a rate of 22%. If the disposal and recycling of waste PCBs can be realized, it can not only solve the problem of environmental pollution, but also realize the effective recovery of metals, which will be of great significance to the sustainable development of my country's PCBs industry.
目前从废弃印刷电路板中提取铜的方法主要有物理法、化学法和生物法。物理法在再生资源效果、环境友善性、工业应用率方面评价指标较高,但所使用的机械设备投资大、能源消耗量高、维护费用高,因而经济可行性相对较差;而且产物中金属之间难以分离。化学法主要分为火法和湿法,火法虽然具有简单、方便和回收率高的优点,但同时会产生有害气体,排放大量浮渣等缺点;湿法具有废气排放少、提取铜后的残留物易于处理和工艺简单等优点,但铜浸取率低以及浸出液及残渣具有毒性。因此将污染少、成本低、反应条件温和的生物法应用到废弃印刷电路板金属回收中具有独特的优势。 At present, the methods for extracting copper from waste printed circuit boards mainly include physical, chemical and biological methods. The physical method has relatively high evaluation indicators in terms of renewable resource effect, environmental friendliness, and industrial application rate, but the investment in mechanical equipment used is large, energy consumption is high, and maintenance costs are high, so the economic feasibility is relatively poor; and the metal in the product difficult to separate. The chemical method is mainly divided into fire method and wet method. Although the fire method has the advantages of simplicity, convenience and high recovery rate, it will produce harmful gases and discharge a large amount of scum at the same time; The residue is easy to handle and the process is simple, but the copper leaching rate is low and the leaching solution and residue are toxic. Therefore, it has unique advantages to apply the biological method with less pollution, low cost and mild reaction conditions to the metal recycling of waste printed circuit boards.
生物浸取PCBs中的铜具有安全、清洁、高效等特点,已成为国内外研究热点。目前应用最普遍的微生物为嗜酸氧化硫硫杆菌(A.t)和氧化亚铁硫杆菌(A. f)。 Bioleaching of copper from PCBs has the characteristics of safety, cleanliness, and high efficiency, and has become a research hotspot at home and abroad. At present, the most commonly used microorganisms are acidophilus Thiobacillus thiooxidans ( At ) and Thiobacillus ferrooxidans ( A.f ).
例如周培国等(周培国,郑正,彭晓成等.氧化亚铁硫杆菌浸出线路板中铜及过程中铁的变化研究.《环境污染与防治》;2007(02):119~122)利用氧化亚铁硫杆菌浸取废弃电路板粉末(铜质量分数为10.4%)中的铜,当废弃电路板粉末添加量为100 g/L时,15d左右铜浸取率约为90%。 For example, Zhou Peiguo et al. (Zhou Peiguo, Zheng Zheng, Peng Xiaocheng, etc. Research on the change of iron in the copper and iron in the process of leaching circuit boards by Thiobacillus ferrooxidans. "Environmental Pollution and Prevention"; 2007 (02): 119~122) using ferrous sulfur oxide Bacteria leached copper from waste circuit board powder (copper mass fraction 10.4%). When the amount of waste circuit board powder added was 100 g/L, the copper leaching rate was about 90% in about 15 days.
中国专利文献CN 1948524 A(申请号 200610097382.X)公开了一种废弃电路板综合资源化处理方法,向培养基溶液中接种经过驯化的氧化亚铁硫杆菌、氧化亚铁微螺菌或硫化叶菌菌液进行培养,将去除了各种元器件的线路板基板粉碎后,向其中加入培养得到的菌液,在120~160r/min的速度下搅拌浸出10~15天,分离液体和固体;液体用铜萃取剂进行萃取,再进行反萃取及电解沉积得到金属铜。 Chinese patent document CN 1948524 A (application number 200610097382.X) discloses a comprehensive resource treatment method for waste circuit boards, inoculating domesticated Thiobacillus ferrooxidans, Microspiral ferrooxidans or vulcanized leaves into the culture medium solution. Bacteria liquid is cultivated, after the circuit board substrate with various components removed is crushed, the cultured bacterial liquid is added to it, stirred and leached at a speed of 120-160r/min for 10-15 days, and the liquid and solid are separated; The liquid is extracted with a copper extractant, and then back-extracted and electrolytically deposited to obtain metallic copper.
上述方法均是使用单一的微生物进行生物浸取,其金属浸出时间长,浸出效率低。 The above methods all use a single microorganism for bioleaching, and the metal leaching time is long and the leaching efficiency is low.
研究表明,混合菌浸取PCBs中铜是目前最有效的方法。 Studies have shown that the leaching of copper in PCBs by mixed bacteria is currently the most effective method.
例如SADIA等( Sadia I, Munir AA, Shahida BN, Afzal Ghauri M. Bioleaching of metals from electronic scrap by moderately thermophilic acidophilic bacteria. Hydrometallurgy 2007;88:180–8.)利用中温嗜酸混合菌浸取废弃电路板粉末(铜质量分数为8.5%)中的金属,当废弃电路板粉末添加量为10g/L时,18d后铜的浸取率为89%。但是该混合菌浸取方法虽然使用了混合菌,但是浸取时间长、浸取率不如一种细菌浸取的效率高。这是由于混合菌培养时,提供什么样的营养底物和外界条件使混合菌能均衡生长,从而不会出现一种过度繁殖而另一种菌被抑制现象至关重要。此外,细菌浸取铜能力与其自身生长代谢密切相关,PCBs添加过程中会抑制细菌生长进而导致铜浸取能力下降,因而如何优化PCBs添加方式是实现混合菌高效淋滤PCBs中铜的又一关键因子之一。 For example, SADIA et al. ( Sadia I, Munir AA, Shahida BN, Afzal Ghauri M. Bioleaching of metals from electronic scrap by moderately thermophilic acidophilic bacteria. Hydrometallurgy 2007;88:180–8.) use mesophilic acidophilic mixed bacteria to leach waste circuit boards For the metal in the powder (the mass fraction of copper is 8.5%), when the amount of waste circuit board powder added is 10g/L, the leaching rate of copper is 89% after 18 days. But although this mixed bacteria leaching method has used mixed bacteria, the leaching time is long, and the leaching rate is not as high as that of a kind of bacterium leaching. This is because when the mixed bacteria are cultivated, what kind of nutrient substrate and external conditions are provided so that the mixed bacteria can grow in a balanced manner, so that one kind of overgrowth and the other kind of bacteria will not be inhibited is very important. In addition, the ability of bacteria to leach copper is closely related to their own growth and metabolism. The addition of PCBs will inhibit the growth of bacteria and lead to a decrease in copper leaching ability. Therefore, how to optimize the way of adding PCBs is another key to achieve efficient leaching of copper in PCBs by mixed bacteria. one of the factors.
发明内容 Contents of the invention
本发明所要解决的技术问题是提供一种混合菌培养方法并用其高效浸取废弃印刷电路板中铜的方法。 The technical problem to be solved by the present invention is to provide a method for cultivating mixed bacteria and using it to efficiently extract copper from waste printed circuit boards.
实现本发明目的的技术方案是一种混合菌浸取废弃印刷电路板中铜的方法,包括以下步骤: The technical solution for realizing the object of the present invention is a method for leaching copper in waste printed circuit boards by mixed bacteria, comprising the following steps:
①废弃印刷电路板的预处理;将拆除了电子元件的废弃印刷电路板PCBs压碎并研磨成粉末,研磨得到的废弃印刷电路板粉末过筛,收集通过筛孔的废弃印刷电路板粉末待处理。 ① Pretreatment of waste printed circuit boards: crush and grind the waste printed circuit boards PCBs from which electronic components have been removed into powder, sieve the waste printed circuit board powder obtained through grinding, and collect the waste printed circuit board powder that passes through the sieve holes for processing .
②菌种的驯化;将嗜酸氧化亚铁硫杆菌A.ferrooxidans和嗜酸氧化硫硫杆菌A.thiooxidans分别进行耐Cu2+的驯化培养,驯化结束分别得到耐100~200mmol/L Cu2+环境的A.ferrooxidans和A.thiooxidans待用。 ②Aclimation of strains: acidophilus A.ferrooxidans and acidophilus A.thiooxidans were respectively domesticated and cultivated for resistance to Cu 2+ . A. ferrooxidans and A. thiooxidans from the environment were used.
③混合菌培养;将步骤②驯化培养后得到的A.ferrooxidans和A.thiooxidans按照接种量之为1∶1.5~2.5在混合菌培养液中进行混合菌培养,培养初始pH为1.5~1.8,混合菌接种量为混合菌培养液体积的10%~20%。 ③Cultivation of mixed bacteria: A. ferrooxidans and A.thiooxidans obtained after step ② domestication and cultivation are carried out in the mixed bacteria culture solution according to the inoculum size of 1:1.5-2.5. The initial pH of the culture is 1.5-1.8, and mixed The amount of bacterial inoculum is 10% to 20% of the volume of the mixed bacterial culture solution.
④废弃印刷电路板粉末的添加;待步骤③混合菌培养时间到达40~55小时,第一次向培养了40~55小时的混合菌培养体系中加入步骤①预处理得到的废弃PCBs粉末,然后每隔20~25小时再次向混合菌培养体系中加入步骤①预处理得到的废弃PCBs粉末,后一次加入的废弃PCBs粉末相比前一次增加1~3g/L,1L混合菌培养体系中所加入的废弃PCBs粉末的总质量为28g~36g;废弃PCBs粉末加毕待混合菌培养时间到达175h~200h时,混合菌浸取反应结束;对反应后的混合物料进行离心分离,收集上层浸出液。 ④ Addition of waste printed circuit board powder; after step ③ the mixed bacteria culture time reaches 40-55 hours, add the waste PCBs powder obtained in step ① pretreatment to the mixed bacteria culture system cultivated for 40-55 hours for the first time, and then Every 20 to 25 hours, add the waste PCBs powder obtained in step ① to the mixed bacteria culture system again. The total mass of the discarded PCBs powder is 28g-36g; when the waste PCBs powder is added and the culture time of the mixed bacteria reaches 175h-200h, the leaching reaction of the mixed bacteria is completed; the mixed material after the reaction is centrifuged and the upper leachate is collected.
⑤后处理;将步骤④得到的浸出液用铜萃取剂进行萃取,对于得到的含铜萃取液,用反萃取剂进行反萃取;然后将得到的含铜反萃液转移入电解槽中进行电积得到铜,完成废弃印刷电路板中铜的回收。 ⑤ post-processing; the leach solution obtained in step ④ is extracted with a copper extractant, and the obtained copper-containing extract is stripped with a stripping agent; then the obtained copper-containing stripping solution is transferred into an electrolytic cell for electrowinning Get copper and complete the recovery of copper from waste printed circuit boards.
上述步骤③混合菌培养时,所用的混合菌培养液中各组分的含量为:单质硫4.0~6.5g/L, 硫酸铵3.5 ~4.5g/L, 磷酸氢二钾0.45~0.65 g/L,七水合硫酸镁0.45~0.65 g/L, 氯化钾0.1~0.15 g/L, 硝酸钙0.008~0.015 g/L, 七水合硫酸亚铁15~18g/L,氯化钙0.10~0.18 g/L;混合菌培养液溶质为水。 In the above step ③ when the mixed bacteria are cultured, the content of each component in the mixed bacteria culture solution used is: elemental sulfur 4.0-6.5g/L, ammonium sulfate 3.5-4.5g/L, dipotassium hydrogen phosphate 0.45-0.65 g/L , magnesium sulfate heptahydrate 0.45~0.65 g/L, potassium chloride 0.1~0.15 g/L, calcium nitrate 0.008~0.015 g/L, ferrous sulfate heptahydrate 15~18g/L, calcium chloride 0.10~0.18 g/L L; the solute of the mixed bacteria culture solution is water.
作为优选的,步骤③混合菌培养时,所用的混合菌培养液中各组分的含量为:单质硫5.2~5.6g/L, 硫酸铵3.5 ~4.5g/L, 磷酸氢二钾0.45~0.65 g/L,七水合硫酸镁0.45~0.65 g/L, 氯化钾0.1~0.15 g/L, 硝酸钙0.008~0.015 g/L, 七水合硫酸亚铁17~17.5g/L,氯化钙0.10~0.18 g/L;混合菌培养液溶质为水。 As preferred, when step ③ mixed bacteria culture, the content of each component in the mixed bacteria culture solution used is: elemental sulfur 5.2 ~ 5.6g/L, ammonium sulfate 3.5 ~ 4.5g/L, dipotassium hydrogen phosphate 0.45 ~ 0.65 g/L, magnesium sulfate heptahydrate 0.45~0.65 g/L, potassium chloride 0.1~0.15 g/L, calcium nitrate 0.008~0.015 g/L, ferrous sulfate heptahydrate 17~17.5g/L, calcium chloride 0.10 ~0.18 g/L; the solute of the mixed bacterial culture solution is water.
上述步骤④废弃PCBs粉末添加时,待步骤③混合菌培养时间到达40~55小时,向培养了40~55小时的混合菌培养体系中加入步骤①预处理得到的废弃PCBs粉末,每1L混合菌培养体系中添加4g~6g废弃PCBs粉末,加入的废弃PCBs粉末开始进行混合菌浸取反应;待混合菌继续培养20~25小时后,向培养体系中第二次添加步骤①预处理得到的废弃PCBs粉末,每1L混合菌培养体系中添加6g~8g废弃PCBs粉末,加入的废弃PCBs粉末开始进行混合菌浸取反应;待混合菌继续培养20~25小时后,向培养体系中第三次添加步骤①预处理得到的废弃PCBs粉末,每1L混合菌培养体系中添加8g~10g废弃PCBs粉末,加入的废弃PCBs粉末开始进行混合菌浸取反应;待混合菌继续培养20~25小时后,向培养体系中第四次添加步骤①预处理得到的废弃PCBs粉末,每1L混合菌培养体系中添加10g~12g废弃PCBs粉末,废弃PCBs粉末添加完毕。 When adding the waste PCBs powder in the above step ④, after the mixed bacteria culture time in step ③ reaches 40-55 hours, add the waste PCBs powder obtained in step ① pretreatment to the mixed bacteria culture system that has been cultivated for 40-55 hours. Add 4g to 6g of waste PCBs powder to the culture system, and the added waste PCBs powder starts the mixed bacteria leaching reaction; after the mixed bacteria continue to culture for 20 to 25 hours, add the waste PCBs obtained in step ① pretreatment to the culture system for the second time. For PCBs powder, add 6g-8g of waste PCBs powder to every 1L of mixed bacteria culture system, and the added waste PCBs powder will start the mixed bacteria leaching reaction; after the mixed bacteria continue to culture for 20-25 hours, add it to the culture system for the third time Step ① Add 8g-10g of waste PCBs powder to each 1L of mixed bacteria culture system for the waste PCBs powder obtained from pretreatment, and the added waste PCBs powder will start the mixed bacteria leaching reaction; after the mixed bacteria continue to be cultivated for 20-25 hours, add to The fourth addition step in the culture system: ① Pretreatment waste PCBs powder, add 10g ~ 12g waste PCBs powder to each 1L mixed bacteria culture system, and the waste PCBs powder is added.
上述步骤②A.ferrooxidans进行驯化培养时,将从城市污水处理厂的曝气池中提取的污泥富集培养,然后分离纯化而得到A.ferrooxidans;将A.ferrooxidans在9K培养液中培养至对数期;按照菌种接种量为10%~20%(体积比v/v)、吸取上述菌液转移到Cu2+的浓度为10mmol/L的培养液中;培养至对数期后,按照菌种接种量为10%~20%(体积比v/v)、吸取上述菌液转移到Cu2+的浓度为20mmol/L的培养液中培养至对数期;重复上述操作,每增加一代菌株的驯化,所用的培养液中Cu2+的浓度相比上一代增加10mmol/L,从而得到在100~200mmol/L Cu2+环境中培养至对数期的A.ferrooxidans。 When the above step ② A.ferrooxidans is domesticated and cultivated, the sludge extracted from the aeration tank of the urban sewage treatment plant is enriched and cultivated, and then separated and purified to obtain A.ferrooxidans ; A.ferrooxidans is cultivated in 9K culture solution until Logarithmic phase; according to the inoculum amount of the strain is 10% to 20% (volume ratio v/v), absorb the above bacterial solution and transfer it to the culture medium with a Cu 2+ concentration of 10mmol/L; after cultivating to the logarithmic phase, According to the inoculum amount of the bacteria is 10% to 20% (volume ratio v/v), absorb the above bacterial solution and transfer it to the culture solution with a Cu 2+ concentration of 20mmol/L to cultivate to the logarithmic phase; repeat the above operation, each increase For the domestication of the first-generation strain, the concentration of Cu 2+ in the culture medium used was increased by 10mmol/L compared with the previous generation, so as to obtain A.ferrooxidans cultured to the logarithmic phase in an environment of 100-200mmol/L Cu 2+ .
上述步骤②A.thiooxidans进行驯化培养时,将从城市污水处理厂的曝气池中提取的污泥富集培养,然后分离纯化而得到A.thiooxidans;将A.thiooxidans在培养液中培养至对数期;按照菌种接种量为10%~20%(体积比v/v)、吸取上述菌液转移到Cu2+的浓度为10mmol/L的培养液中;培养至对数期后,按照菌种接种量为10%~20%(体积比v/v)、吸取上述菌液转移到Cu2+的浓度为20mmol/L的培养液中培养至对数期;重复上述操作,每增加一代菌株的驯化,所用的培养液中Cu2+的浓度相比上一代增加10mmol/L,从而得到在100~200mmol/L Cu2+环境中培养至对数期的A.thiooxidans。 When the above step ② A.thiooxidans is domesticated and cultivated, the sludge extracted from the aeration tank of the urban sewage treatment plant is enriched and cultivated, and then separated and purified to obtain A.thiooxidans ; A.thiooxidans is cultivated in the culture medium until the Several phases; according to the inoculum amount of the bacteria is 10% to 20% (volume ratio v/v), absorb the above bacterial solution and transfer it to the culture solution with a Cu 2+ concentration of 10mmol/L; after cultivating to the logarithmic phase, follow the The inoculum amount of the bacteria is 10%-20% (volume ratio v/v), absorb the above-mentioned bacterial solution and transfer it to the culture solution with a Cu 2+ concentration of 20mmol/L to cultivate to the logarithmic phase; repeat the above operation, each additional generation For the acclimatization of the strain, the concentration of Cu 2+ in the culture medium used was increased by 10mmol/L compared with the previous generation, so as to obtain A.thiooxidans cultured to the logarithmic phase in an environment of 100-200mmol/L Cu 2+ .
本发明具有积极的效果: The present invention has positive effect:
(1)本发明进行混合菌培养时提供的营养底物和培养条件使嗜酸氧化亚铁硫杆菌(Acidithiobacillus.ferrooxidans,A.ferrooxidans)和嗜酸氧化硫硫杆菌(Acidithiobacillus. thiooxidans ,A.thiooxidans)两种菌能均衡生长,没有出现一种菌过度繁殖而另一种菌被抑制现象。此外,本发明优化了废弃PCBs粉末的添加方式,采用前低后高多点添加的方式,在提高废弃PCBs添加量的基础上,铜浸取率显著提高而菌体生长受抑制程度却相对较小。 (1) The nutrient substrate and culture conditions provided by the present invention when carrying out mixed bacterial culture make Acidithiobacillus ferrooxidans ( Acidithiobacillus.ferrooxidans, A.ferrooxidans ) and Acidithiobacillus. ) The two bacteria can grow in a balanced manner, and there is no phenomenon that one kind of bacteria is excessively multiplied while the other is inhibited. In addition, the present invention optimizes the way of adding waste PCBs powder, and adopts the way of low front and high multi-point addition. On the basis of increasing the amount of waste PCBs added, the copper leaching rate is significantly improved while the growth of bacteria is relatively inhibited. Small.
(2)本发明采用混合菌培养,培养时无需调节培养液的pH 两种菌就能均衡生长,同时两种菌生长时生成大量硫酸和Fe3+用于后期废弃PCBs粉末中铜的浸取,整个过程效率高、节省能源。 (2) The present invention adopts mixed bacteria culture, and the two bacteria can grow in a balanced manner without adjusting the pH of the culture solution during culture, and at the same time, when the two bacteria grow, a large amount of sulfuric acid and Fe 3+ are produced for leaching copper from waste PCBs powder in the later stage , the whole process has high efficiency and saves energy.
(3)本发明在进行生物淋滤前,对A.ferrooxidans和A.thiooxidans进行了耐铜处理,显著提高两种菌的耐铜性,促进了废弃PCBs粉末中铜的浸取。 (3) In the present invention, before bioleaching, A. ferrooxidans and A. thiooxidans are treated with copper resistance, which significantly improves the copper resistance of the two bacteria and promotes the leaching of copper in waste PCBs powder.
(4))本发明的整个过程工艺简单、经济、环保,符合循环经济发展的需要,具有良好的工业应用前景。 (4) The entire process of the present invention is simple, economical and environmentally friendly, meets the needs of the development of circular economy, and has good industrial application prospects.
具体实施方式 Detailed ways
(实施例1) (Example 1)
本实施例的混合菌浸取废弃印刷电路板中铜的方法包括以下步骤: The method for the mixed bacteria of the present embodiment to extract copper in waste printed circuit boards may further comprise the steps:
①废弃印刷电路板的预处理。将拆除了电子元件的废弃印刷电路板PCBs压碎并研磨成粉末,研磨得到的废弃PCBs粉末过100μm~200μm的筛孔(本实施例中研磨得到的废弃印刷电路板粉末过100μm的筛孔),收集通过筛孔的废弃PCBs粉末待处理。 ① Pretreatment of waste printed circuit boards. The waste printed circuit board PCBs from which electronic components have been removed are crushed and ground into powder, and the ground waste PCBs powder passes through a sieve of 100 μm to 200 μm (in this example, the waste printed circuit board powder obtained through grinding passes through a 100 μm sieve) , to collect the waste PCBs powder passing through the sieve for processing.
本实施例处理的废弃PCBs经研磨过筛后,对其主要金属含量进行了分析, After the discarded PCBs processed in this embodiment were ground and sieved, their main metal content was analyzed.
主要金属含量如下表1所示: The main metal content is shown in Table 1 below:
表1 废弃印刷电路板粉末中主要金属含量 Table 1 Main metal content in waste printed circuit board powder
②菌种的驯化。 ② Domestication of strains.
(1)嗜酸氧化亚铁硫杆菌(A.ferrooxidans)的驯化。将从城市污水处理厂的曝气池中提取的污泥富集培养,然后分离纯化而得到A.ferrooxidans;将A.ferrooxidans在9K培养液中培养至对数期,此时菌液中菌浓度上升至107细胞 /mL。 (1) Domestication of acidophilic Thiobacillus ferrooxidans ( A.ferrooxidans ). The sludge extracted from the aeration tank of the urban sewage treatment plant is enriched and cultured, and then separated and purified to obtain A.ferrooxidans ; A.ferrooxidans is cultivated in the 9K culture solution to the logarithmic phase, and the bacterial concentration in the bacterial solution is now rise to 10 7 cells/mL.
所用9K培养液每1L中包括:44.7g FeSO4·7H2O, 3.0g (NH4)2SO4, 0.5g K2HPO4, 0.5g MgSO4·7H2O, 0.1g KCl,0.01g Ca(NO3)2,培养液的pH值为2.00。 The 9K culture medium used per 1L includes: 44.7g FeSO 4 7H 2 O, 3.0g (NH 4 ) 2 SO 4 , 0.5g K 2 HPO 4 , 0.5g MgSO 4 7H 2 O, 0.1g KCl, 0.01g Ca(NO 3 ) 2 , the pH of the culture solution is 2.00.
按照菌种接种量为10%~20%(体积比v/v)、吸取上述菌液转移到已加入100mL新鲜培养液的250mL锥形瓶中,于温度32℃,摇床转速为120~200r/min(本实施例中为150 r/min)条件下培养至对数期完成第一代驯化。第一代驯化所用A.f培养液其余与上述9K培养液相同,不同之处在于培养液中增加了Cu2+,培养液中Cu2+的浓度为10mmol/L。 According to the inoculum amount of the strain is 10%-20% (volume ratio v/v), transfer the above-mentioned bacterial solution to a 250mL conical flask with 100mL fresh culture solution added, at a temperature of 32°C and a shaker speed of 120-200r /min (150 r/min in this example) to the logarithmic phase to complete the first generation of domestication. The rest of the Af culture medium used for the first-generation domestication is the same as the above 9K culture medium, except that Cu 2+ is added to the culture medium, and the concentration of Cu 2+ in the culture medium is 10mmol/L.
按照菌种接种量为10%~20%(体积比v/v)、吸取上述第一代驯化后的菌液至新鲜培养液中进行培养至对数期,本次所用培养液中Cu2+的浓度上升至20mmol/L。 According to the inoculum amount of the strain is 10%-20% (volume ratio v/v), absorb the above-mentioned first-generation domesticated bacteria liquid into the fresh culture medium for cultivation to the logarithmic phase, Cu 2+ in the culture medium used this time The concentration rose to 20mmol/L.
重复上述操作,将菌液依次转入含30、40、50、60、70、80、90、100、110、120、130、140、150、160、170、180、190 和200mmol/L Cu2+的新鲜培养液中驯化培养,培养结束后,离心去除上清液,收集能耐200 mmol/L的Cu2+的浓度的菌体放冰箱待用。 Repeat the above operation, transfer the bacterial solution to the culture medium containing 30, 40, 50, 60, 70, 80, 90, 100, 110, 120, 130, 140, 150, 160, 170, 180, 190 and 200mmol/L Cu2 + in fresh culture medium, after the culture, centrifuge to remove the supernatant, collect the cells that can withstand the concentration of 200 mmol/L Cu 2+ and put them in the refrigerator for later use.
上述驯化过程中,每增加一代菌株的驯化,所用的培养液中Cu2+的浓度相比上一代增加10mmol/L。由于Cu2+浓度升高,所以培养至对数期(菌浓度为107细胞 /mL)所需时间会越来越长。根据处理的粉末情况,将嗜酸氧化亚铁硫杆菌在100 mmol/L的Cu2+的浓度下培养至对数期后也可以停止驯化,从而得到耐100 mmol/L的Cu2+的浓度的A.ferrooxidans。 During the above-mentioned acclimation process, the concentration of Cu 2+ in the culture solution used increased by 10mmol/L for each additional generation of strain acclimatization compared with the previous generation. As the concentration of Cu 2+ increases, the time required for culturing to the logarithmic phase (bacterial concentration of 10 7 cells/mL) will be longer and longer. According to the treated powder, acidophilic Thiobacillus ferrooxidans can be cultured to the logarithmic phase at a concentration of 100 mmol/L Cu 2+ to stop acclimatization, so as to obtain a concentration resistant to 100 mmol/L Cu 2+ A. ferrooxidans .
(2)嗜酸氧化硫硫杆菌(A.thiooxidans)的驯化。将从城市污水处理厂的曝气池中提取的污泥富集培养(污水厂采用A2/O处理污水),然后分离纯化而得到A.thiooxidans;将A.thiooxidans在培养液中培养至对数期,此时菌液中菌浓度上升至107细胞 /mL。 (2) Domestication of Acidophilus Thiobacillus Thiooxidans ( A.thiooxidans ). The sludge extracted from the aeration tank of the urban sewage treatment plant is enriched and cultivated (the sewage plant uses A2/O to treat sewage), and then separated and purified to obtain A.thiooxidans ; A.thiooxidans are cultivated in the culture medium to logarithmic At this time, the bacterial concentration in the bacterial solution rose to 10 7 cells/mL.
所用培养液每1L中包括:10.0g S0, 0.5g (NH4)2SO4, 0.25g K2HPO4, 0.25g MgSO4·7H2O, 0.02g CaCl2·2H2O;培养液的pH值为4.00。 Each 1L of culture medium used includes: 10.0g S 0 , 0.5g (NH 4 ) 2 SO 4 , 0.25g K 2 HPO 4 , 0.25g MgSO 4 ·7H 2 O, 0.02g CaCl 2 ·2H 2 O; The pH value is 4.00.
按照菌种接种量为10%~20%(体积比v/v)、吸取上述菌液转移到已加入100mL新鲜培养液的250mL锥形瓶中,于温度32℃,摇床转速为120~200r/min(本实施例中为150 r/min)条件下培养至对数期得到第一代驯化嗜酸氧化硫硫杆菌。 According to the inoculum amount of the strain is 10%-20% (volume ratio v/v), transfer the above-mentioned bacterial solution to a 250mL conical flask with 100mL fresh culture solution added, at a temperature of 32°C, and a shaker speed of 120-200r /min (150 r/min in this example) was cultivated to the logarithmic phase to obtain the first generation of domesticated acidophilic Thiobacillus thiooxidans.
第一代驯化所用A.t培养液其余与上述培养液相同,不同之处在于第一代驯化所用A.t培养液中增加了Cu2+,培养液中Cu2+的浓度为10mmol/L。 The rest of the At culture medium used for the first-generation domestication is the same as the above-mentioned culture medium, except that Cu 2+ is added to the At culture medium used for the first-generation domestication, and the concentration of Cu 2+ in the culture medium is 10 mmol/L.
按照(1)中嗜酸氧化亚铁硫杆菌(A.f)的驯化方法,将菌液依次转入含20、30、40、50、60、70、80、90、100、110、120、130、140、150、160、170、180、190 和200mmol/L Cu2+的新鲜培养液中驯化培养至对数期,培养结束后,离心去除上清液,收集能耐200 mmol/L的Cu2+的浓度的菌体放冰箱待用。 According to the acclimation method of acidophilic Thiobacillus ferrooxidans ( Af ) in (1), the bacterial liquid was successively transferred into the 140, 150, 160, 170, 180, 190 and 200mmol/L Cu 2+ in the fresh culture medium to acclimatize and cultivate to the logarithmic phase. After the cultivation, centrifuge to remove the supernatant, and collect Cu 2+ that can withstand 200 mmol/L The concentration of bacteria was stored in the refrigerator for later use.
根据处理的粉末情况,将A.thiooxidans在100 mmol/L的Cu2+的浓度下培养至对数期后也可以停止驯化,从而得到耐100 mmol/L的Cu2+的浓度的A.thiooxidans。 According to the treated powder, A.thiooxidans can be cultured to the logarithmic phase at a concentration of 100 mmol/L Cu 2+ to stop acclimatization, so as to obtain A.thiooxidans resistant to a concentration of 100 mmol/L Cu 2+ .
即上述驯化过程中,每增加一代菌株的驯化,所用的培养液中Cu2+的浓度相比上一代增加10mmol/L。由于Cu2+浓度升高,所以培养至对数期(菌浓度为107细胞 /mL)所需时间会越来越长。 That is, during the above domestication process, the concentration of Cu 2+ in the culture solution used increased by 10mmol/L for each additional generation of strain acclimatization compared with the previous generation. As the concentration of Cu 2+ increases, the time required for culturing to the logarithmic phase (bacterial concentration of 10 7 cells/mL) will be longer and longer.
③混合菌培养。将步骤②驯化培养后得到的A.ferrooxidans和A.thiooxidans按照接种量之为1∶1.5~2.5(本实施例中为1∶2)在混合菌培养液中进行混合菌培养,培养初始pH为1.5~1.8(本实施例中为1.6),混合菌接种量为混合菌培养液体积的10%~20%。混合菌培养时控制温度32℃,摇床转速为120~200r/min(本实施例中为150 r/min)。 ③Cultivation of mixed bacteria. The A.ferrooxidans and A.thiooxidans obtained after the step ② domestication culture are carried out in the mixed bacteria culture solution according to the inoculum size of 1:1.5-2.5 (1:2 in this example), and the initial pH of the culture is 1.5 to 1.8 (1.6 in this embodiment), the inoculum amount of the mixed bacteria is 10% to 20% of the volume of the mixed bacteria culture solution. When cultivating mixed bacteria, the temperature was controlled at 32°C, and the rotation speed of the shaker was 120-200 r/min (150 r/min in this example).
混合菌培养液中各组分的含量为:单质硫4.0~6.5g/L, 硫酸铵3.5 ~4.5g/L, 磷酸氢二钾0.45~0.65 g/L,七水合硫酸镁0.45~0.65 g/L, 氯化钾0.1~0.15 g/L, 硝酸钙0.008~0.015 g/L, 七水合硫酸亚铁15~18g/L,氯化钙0.10~0.18 g/L;混合菌培养液溶质为水,pH为1.5~1.8。 The content of each component in the mixed bacterial culture solution is: elemental sulfur 4.0-6.5g/L, ammonium sulfate 3.5-4.5g/L, dipotassium hydrogen phosphate 0.45-0.65 g/L, magnesium sulfate heptahydrate 0.45-0.65 g/L L, potassium chloride 0.1~0.15 g/L, calcium nitrate 0.008~0.015 g/L, ferrous sulfate heptahydrate 15~18g/L, calcium chloride 0.10~0.18 g/L; the solute of the mixed bacteria culture solution is water, The pH is 1.5-1.8.
本实施例中所用的混合菌培养液中各组分的含量为:单质硫5.5g/L, 硫酸铵4.0 g/L, 磷酸氢二钾0.5 g/L,七水合硫酸镁0.5 g/L, 氯化钾0.1 g/L, 硝酸钙0.01 g/L, 七水合硫酸亚铁17.2 g/L,氯化钙 0.13 g/L,pH为1.6。 The content of each component in the mixed bacterial culture solution used in the present embodiment is: elemental sulfur 5.5g/L, ammonium sulfate 4.0 g/L, dipotassium hydrogen phosphate 0.5 g/L, magnesium sulfate heptahydrate 0.5 g/L, Potassium chloride 0.1 g/L, calcium nitrate 0.01 g/L, ferrous sulfate heptahydrate 17.2 g/L, calcium chloride 0.13 g/L, pH 1.6.
④废弃印刷电路板粉末的添加。待步骤③混合菌培养时间到达48小时,向培养了48小时的混合菌培养体系中加入步骤①预处理得到的废弃PCBs粉末,每1L混合菌培养体系中添加4g废弃PCBs粉末,加入的废弃PCBs粉末开始进行混合菌浸取反应。 ④ Addition of waste printed circuit board powder. After step ③ the mixed bacteria culture time reaches 48 hours, add the waste PCBs powder obtained in step ① pretreatment to the mixed bacteria culture system cultivated for 48 hours, add 4g waste PCBs powder to each 1L mixed bacteria culture system, and add waste PCBs The powder begins to undergo mixed bacterial leaching reaction.
待混合菌培养至72小时时,继续向培养体系中添加步骤①预处理得到的废弃PCBs粉末,每1L混合菌培养体系中添加6g废弃PCBs粉末,加入的废弃PCBs粉末开始进行混合菌浸取反应。 When the mixed bacteria culture reaches 72 hours, continue to add the waste PCBs powder obtained in step ① pretreatment to the culture system, add 6g of waste PCBs powder to each 1L mixed bacteria culture system, and the added waste PCBs powder starts the mixed bacteria leaching reaction .
待混合菌培养至96小时时,继续向培养体系中添加步骤①预处理得到的废弃PCBs粉末,每1L混合菌培养体系中添加8g废弃PCBs粉末,加入的废弃PCBs粉末开始进行混合菌浸取反应。 When the mixed bacteria culture reaches 96 hours, continue to add the waste PCBs powder obtained in step ① pretreatment to the culture system, add 8g of waste PCBs powder to each 1L of the mixed bacteria culture system, and the added waste PCBs powder starts the mixed bacteria leaching reaction .
待混合菌培养至120小时时,继续向培养体系中添加步骤①预处理得到的废弃PCBs粉末,每1L混合菌培养体系中添加10g废弃PCBs粉末,加入的废弃PCBs粉末开始进行混合菌浸取反应。 When the mixed bacteria culture reaches 120 hours, continue to add the waste PCBs powder obtained in step ① pretreatment to the culture system, add 10g of waste PCBs powder to each 1L mixed bacteria culture system, and the added waste PCBs powder starts the mixed bacteria leaching reaction .
待混合菌继续培养至175h~200h(本实施例中为180h)时,混合菌浸取反应结束;测得废弃印刷电路板粉末中Cu、 Ni、 Zn 、 Pb 浸出率分别为97.3%、92.5%、93.4% 、89.6%。 When the mixed bacteria continued to be cultivated for 175h to 200h (180h in this example), the leaching reaction of the mixed bacteria was completed; the leaching rates of Cu, Ni, Zn, and Pb in the waste printed circuit board powder were measured to be 97.3% and 92.5% respectively. , 93.4%, 89.6%.
对反应后的混合物料进行离心分离,收集上层浸出液。下层固体经处理后可作为建筑材料。 Centrifuge the reacted mixed material and collect the leachate from the upper layer. The solids in the lower layer can be used as building materials after treatment.
⑤后处理。将步骤④得到的浸出液用铜萃取剂进行萃取,对于得到的含铜萃取液,用反萃取剂进行反萃取;然后将得到的含铜反萃液转移入电解槽中进行电积得到铜,完成废弃印刷电路板中铜的回收。 ⑤ post-processing. Extract the leaching solution obtained in step ④ with a copper extractant, and carry out back extraction with a stripping agent for the obtained copper-containing extraction solution; then transfer the obtained copper-containing stripping solution into an electrolytic cell for electrowinning to obtain copper, and complete Copper recovery from scrap printed circuit boards.
电积时使用钛板做阳极,铜板做阴极。控制电压为2.0V,电流密度为350A/m2,pH值为3,极距为1cm,时间为3h,温度为10℃。 During electrowinning, a titanium plate is used as the anode, and a copper plate is used as the cathode. The control voltage is 2.0V, the current density is 350A/m 2 , the pH value is 3, the pole distance is 1cm, the time is 3h, and the temperature is 10°C.
所用铜萃取剂为2-羟基-5-十二烷基二苯甲酮肟,反萃取剂为铜电解废液。 The copper extraction agent used is 2-hydroxyl-5-dodecylbenzophenone oxime, and the stripping agent is copper electrolysis waste liquid.
电积铜的回收率为99%。回收铜可达到国家GB/T 6516-1997标准。 The recovery rate of electrodeposited copper is 99%. Recycled copper can meet the national GB/T 6516-1997 standard.
为了保持电积条件的基本稳定,电积溶液要不断进行循环。本实施例使用钛板做阳极能高效率地将电流传递到电解液以及供阴离子放电用,使得电积效率提高。另外,电积铜的过程中产生的硫酸,可回收再利用。 In order to keep the electrowinning conditions basically stable, the electrowinning solution should be continuously circulated. In this embodiment, the titanium plate is used as the anode, which can efficiently transfer current to the electrolyte solution and provide anion discharge, so that the electrowinning efficiency is improved. In addition, the sulfuric acid produced during the copper electrodeposition process can be recycled and reused.
本发明混合菌培养时无需调节培养液的pH 两种菌就能均衡生长,同时两种菌生长时生成大量硫酸和Fe3+用于后期废弃PCBs粉末中铜的浸取,整个过程效率高、节省能源。另外,本发明优化了废弃PCBs粉末的添加方式,采用前低后高多点添加的方式,在提高废弃PCBs粉末添加量的基础上,铜浸取率显著提高而菌体生长受抑制程度却相对较小。 When the mixed bacteria of the present invention is cultivated, the two bacteria can grow in a balanced manner without adjusting the pH of the culture solution. At the same time, when the two bacteria grow, a large amount of sulfuric acid and Fe 3+ are generated for the leaching of copper in the waste PCBs powder in the later stage. The whole process has high efficiency and save energy. In addition, the present invention optimizes the way of adding waste PCBs powder, and adopts the way of low front and high multi-point addition. On the basis of increasing the amount of waste PCBs powder added, the copper leaching rate is significantly improved while the growth of bacteria is relatively inhibited. smaller.
(实施例2至实施例6) (Example 2 to Example 6)
实施例2至实施例6的混合菌浸取废弃印刷电路板中铜的方法其余与实施例1相同,不同之处在于:步骤③混合菌培养时所用的混合菌培养液中各组分的含量以及步骤④废弃印刷电路板粉末的添加时间和添加量,具体见下表2和表3。 The mixed bacteria of embodiment 2 to the method of embodiment 6 leaching copper in the waste printed circuit board all the other are the same as embodiment 1, difference is: the content of each component in the mixed bacteria culture solution used when step 3. mixed bacteria culture As well as the addition time and amount of waste printed circuit board powder in step ④, see Table 2 and Table 3 below for details.
表2 步骤③混合菌培养时所用的混合菌培养液中各组分的含量 Table 2 The content of each component in the mixed bacteria culture solution used in step ③ mixed bacteria culture
表3 步骤④废弃印刷电路板粉末的添加时间和添加量 Table 3 Step ④ Addition time and amount of waste printed circuit board powder
注:上表所述添加时间是指自步骤③混合菌开始培养后多少小时时进行粉末添加的时间;所述添加量是指每1L混合菌培养体系中所添加的废弃印刷电路板粉末的重量,单位为克。 Note: The addition time mentioned in the above table refers to the time for powder addition after the start of the mixed bacteria culture in step ③; the added amount refers to the weight of waste printed circuit board powder added per 1L of mixed bacteria culture system , the unit is grams.
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