CN1388256A - Method of recovering Pd from low-concentration waste Pd ion liquid with becteria thallus - Google Patents
Method of recovering Pd from low-concentration waste Pd ion liquid with becteria thallus Download PDFInfo
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- 238000000034 method Methods 0.000 title claims abstract description 20
- 239000007788 liquid Substances 0.000 title claims description 11
- 239000002699 waste material Substances 0.000 title claims description 11
- KDLHZDBZIXYQEI-UHFFFAOYSA-N palladium Substances [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 claims abstract description 85
- 238000001179 sorption measurement Methods 0.000 claims abstract description 38
- 230000001580 bacterial effect Effects 0.000 claims abstract description 22
- 229910052763 palladium Inorganic materials 0.000 claims abstract description 22
- 239000000243 solution Substances 0.000 claims abstract description 19
- 241000894006 Bacteria Species 0.000 claims abstract description 18
- 229910052751 metal Inorganic materials 0.000 claims abstract description 9
- 239000002184 metal Substances 0.000 claims abstract description 9
- 230000009471 action Effects 0.000 claims abstract description 5
- 239000000203 mixture Substances 0.000 claims abstract description 4
- 230000010355 oscillation Effects 0.000 claims abstract description 4
- 241000194108 Bacillus licheniformis Species 0.000 claims abstract description 3
- 239000007864 aqueous solution Substances 0.000 claims abstract description 3
- MUJIDPITZJWBSW-UHFFFAOYSA-N palladium(2+) Chemical compound [Pd+2] MUJIDPITZJWBSW-UHFFFAOYSA-N 0.000 claims description 9
- 239000012528 membrane Substances 0.000 claims description 3
- 238000011084 recovery Methods 0.000 claims description 3
- FRXSZNDVFUDTIR-UHFFFAOYSA-N 6-methoxy-1,2,3,4-tetrahydroquinoline Chemical compound N1CCCC2=CC(OC)=CC=C21 FRXSZNDVFUDTIR-UHFFFAOYSA-N 0.000 claims 6
- 241000193830 Bacillus <bacterium> Species 0.000 claims 1
- 239000010970 precious metal Substances 0.000 abstract description 8
- 210000004027 cell Anatomy 0.000 description 20
- 230000000694 effects Effects 0.000 description 4
- 230000008859 change Effects 0.000 description 3
- 230000000813 microbial effect Effects 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 238000004458 analytical method Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 229910021645 metal ion Inorganic materials 0.000 description 2
- 239000011148 porous material Substances 0.000 description 2
- 101150003085 Pdcl gene Proteins 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 239000003463 adsorbent Substances 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 210000002421 cell wall Anatomy 0.000 description 1
- 238000009388 chemical precipitation Methods 0.000 description 1
- 230000007123 defense Effects 0.000 description 1
- 238000005868 electrolysis reaction Methods 0.000 description 1
- 239000000706 filtrate Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 238000005342 ion exchange Methods 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 239000002207 metabolite Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 238000005065 mining Methods 0.000 description 1
- 239000011259 mixed solution Substances 0.000 description 1
- 229910000510 noble metal Inorganic materials 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000005504 petroleum refining Methods 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000000638 solvent extraction Methods 0.000 description 1
- 239000000126 substance Substances 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
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Abstract
涉及一种微量贵金属的回收方法,采用的细菌为地衣芽胞杆菌,株号R08。首先将菌体浓度为0.4~2.0g/L的R08菌体细胞溶液与浓度为30~300mg/L的Pd2+水溶液混合,于5~60℃,pH2.0~3.5的条件下,按130次/min的振荡频率振荡3~90min,然后过滤Pd2+菌体作用液,将过滤后的吸附Pd2+的菌体于室温下放置6~48h,最后经550~800℃灼烧1.5~3h后得金属钯。方法简便,成本低,特别适合于从低浓度的Pd2+溶液中回收钯,Pd2+吸附率可高达99%。The invention relates to a method for recovering trace precious metals, and the bacteria used are bacillus licheniformis, strain number R08. First, mix the R08 bacterial cell solution with a bacterial cell concentration of 0.4-2.0 g/L and a Pd 2+ aqueous solution with a concentration of 30-300 mg/L. Oscillate at an oscillation frequency of 3-90min times/min, then filter the Pd 2+ cell action solution, place the filtered Pd 2+ -adsorbed cell at room temperature for 6-48 hours, and finally burn at 550-800°C for 1.5- After 3h, metal palladium was obtained. The method is simple and low in cost, and is especially suitable for recovering palladium from low-concentration Pd 2+ solution, and the adsorption rate of Pd 2+ can be as high as 99%.
Description
(1)技术领域(1) Technical field
本发明涉及一种微量贵金属的回收方法。The invention relates to a method for recovering trace precious metals.
(2)背景技术(2) Background technology
钯等贵金属是国防,化工,石油精炼和电子等工业生产中不可缺少的重要原料。随着工业技术的发展,贵金属的应用愈来愈广泛。然而,钯等贵金属资源稀少且难得。因此,各国对贵金属的再生回收都很重视。目前从溶液中回收钯等贵金属的方法有活性碳吸附,离子交换,化学沉淀,电解和溶剂抽取等。这些方法的过程繁琐且易造成二次污染,特别是当溶液中贵金属离子含量较低时,用上述回收方法是不经济的。Brierly等人(Biohydrometa,Proc Int Symp,1988,477)曾用死的菌体制备成粒状的金属去除剂,从10mgPd2+/L溶液中回收钯。Lloyd等人(ApplEnviron Microbiol,1998,4607)报道,Desulfovibriodesulfuricanns静止细胞能够还原可溶的Pd2+成金属钯(Pd0)。据报道(Mreeoun et al J ApplMicrobiol,1998,84:63),活的或者死的完整的微生物细胞及其代谢产物都可以高效地吸附可溶的和颗粒形式的金属,特别是从低溶度的金属离子中回收贵金属。许多研究表明,死的微生物细胞对金属离子的吸附具有速度快、选择性高、吸附容量大等特点(牛慧等,1993,33(6):459)。Precious metals such as palladium are indispensable and important raw materials in industrial production such as national defense, chemical industry, petroleum refining and electronics. With the development of industrial technology, the application of precious metals is becoming more and more extensive. However, precious metal resources such as palladium are scarce and rare. Therefore, all countries attach great importance to the recycling of precious metals. Currently, methods for recovering precious metals such as palladium from solutions include activated carbon adsorption, ion exchange, chemical precipitation, electrolysis, and solvent extraction. The process of these methods is loaded down with trivial details and easily causes secondary pollution, especially when the noble metal ion content in the solution is low, it is uneconomical to use the above-mentioned recovery method. Brierly et al. (Biohydrometa, Proc Int Symp, 1988, 477) used dead bacteria to prepare granular metal remover to recover palladium from 10mgPd 2+ /L solution. Lloyd et al. (ApplEnviron Microbiol, 1998, 4607) reported that Desulfovibriodesulfuricanns quiescent cells were able to reduce soluble Pd 2+ to metallic palladium (Pd 0 ). It has been reported (Mreeoun et al J ApplMicrobiol, 1998, 84:63) that living or dead intact microbial cells and their metabolites can efficiently adsorb soluble and particulate metals, especially from low-soluble Recovery of precious metals from metal ions. Many studies have shown that the adsorption of dead microbial cells to metal ions has the characteristics of fast speed, high selectivity, and large adsorption capacity (Niu Hui et al., 1993, 33(6): 459).
(3)发明内容(3) Contents of the invention
本发明的目的旨在提供一种利用细菌菌体从低浓度的钯离子废液中回收钯的方法。The purpose of the present invention aims to provide a kind of method that utilizes bacterial cell to reclaim palladium from the palladium ion waste liquid of low concentration.
本发明所用的微生物吸附剂是从金属矿区环境分离筛选出的吸附还原Pa2+能力较强的菌株R08,经鉴定为地衣芽胞杆菌(Bacillus licheniformis)该菌体已保存于中国微生物菌种保藏管理委员会普通微生物中心,登记入册的编号为0503,株号RO8。The microbial adsorbent used in the present invention is a bacterial strain R08 with a strong ability to adsorb and reduce Pa 2+ isolated and screened from the environment of the metal mining area. It has been identified as Bacillus licheniformis. The Committee's General Microbiology Center, the registration number is 0503, and the strain number is RO8.
本发明用R08菌体吸附还原溶液中的Pd2+,其操作和分析测定方法如下:The present invention uses R08 bacterium to absorb Pd 2+ in the reduction solution, and its operation, analysis and determination methods are as follows:
首先将菌体细胞溶液与Pd2+水溶液混合,菌体浓度为0.4~2.0g/L最好是0.8~1.6g/L,Pd2+浓度为30~300mg/L.于5~60℃温度下,PH1.0~3.8最好是PH2.0~3.5的条件下,按振荡频率130次/min振荡3~90min,最好是30~60min,使细菌充分吸附Pd2+。然后用孔径为0.22um的滤膜过滤Pd2+-菌体作用液,使吸附Pd2+的菌体与残留Pd2+的溶液分开。将过滤所获得的吸附Pd2+的菌体于室温下放置6~48h,最好是18~36h后,经550~800℃高温灼烧1.5h~3h,即可回收金属钯。滤液用WFX-IE2型原子吸收分光光度计测定其残留的Pd2+浓度,按下式计算菌体对Pd2+的吸附率和吸附量:First, mix the bacterial cell solution with the Pd 2+ aqueous solution, the bacterial concentration is 0.4-2.0g/L, preferably 0.8-1.6g/L, and the Pd 2+ concentration is 30-300mg/L. Under the conditions of pH 1.0-3.8, preferably pH 2.0-3.5, shake at an oscillation frequency of 130 times/min for 3-90 minutes, preferably 30-60 minutes, so that the bacteria can fully adsorb Pd 2+ . Then filter the Pd 2+ -bacteria action solution with a filter membrane with a pore size of 0.22um, so as to separate the adsorbed Pd 2+ bacteria from the residual Pd 2+ solution. Pd 2+ adsorbed bacteria obtained by filtration are placed at room temperature for 6-48 hours, preferably 18-36 hours, and then burned at 550-800°C for 1.5-3 hours to recover metal palladium. The residual Pd2 + concentration of the filtrate was measured with a WFX-IE2 atomic absorption spectrophotometer, and the adsorption rate and adsorption amount of the bacteria to Pd2 + were calculated according to the following formula:
吸附率(%)=(Ci-Cf)/Ci×100%Adsorption rate (%)=(C i -C f )/C i ×100%
吸附量(mg/g干菌体)=(Ci-Cf)/Cb Adsorption capacity (mg/g dry cells) = (C i -C f )/C b
式中Ci和Cf分别为Pd2+的起始浓度和终浓度(mg/L),Cb为菌体浓度(g/L)。In the formula, C i and C f are the initial and final concentrations of Pd 2+ (mg/L), respectively, and C b is the bacterial concentration (g/L).
用透射电子显微镜(TEM)观察表明,R08菌体与Pd2+的溶液接触6h~48h之后,在细胞壁上存在Pd0颗粒。本发明提供的方法简便,成本低,特别适合于从低浓度Pd2+溶液中回收钯,Pb2+的吸附率可高达99%。Observation with a transmission electron microscope (TEM) showed that there were Pd 0 particles on the cell wall after the R08 cells were in contact with the Pd 2+ solution for 6h to 48h. The method provided by the invention is simple and low in cost, and is particularly suitable for recovering palladium from a low-concentration Pd 2+ solution, and the adsorption rate of Pb 2+ can be as high as 99%.
(4)具体实施方式(4) specific implementation
下面通过实施例对本发明作进一步说明。The present invention will be further described below by embodiment.
实施例1:Example 1:
将菌体浓度为1.2g/L的R08死菌体细胞溶液与起始浓度为200mg/L的Pd2+溶液混合,调节pH值为3.5,在30℃下,按130次/min的振荡频率振荡混合溶液45min,然后用孔径为0.22mm的过滤膜过滤Pd2+-菌体作用液,将吸附Pd2+的菌体于室温下放置24h,最后经600℃灼烧后回收金属钯。经测定分析,R08菌体对Pd2+的吸附量可达149.0mg/g菌体,吸附率为89.4%。Mix the R08 dead bacterial cell solution with a cell concentration of 1.2g/L and the Pd 2+ solution with an initial concentration of 200mg/L, adjust the pH value to 3.5, and at 30°C, press the oscillation frequency of 130 times/min Shake the mixed solution for 45 minutes, then filter the Pd 2+ - cell action solution with a filter membrane with a pore size of 0.22mm, place the cell adsorbed by Pd 2+ at room temperature for 24 hours, and finally recover metal palladium after burning at 600°C. After determination and analysis, the adsorption capacity of R08 bacteria to Pd 2+ can reach 149.0 mg/g bacteria, and the adsorption rate is 89.4%.
实施例2~9:Embodiment 2~9:
在Pd2+起始浓度为200mg/L、菌体浓度0.8g/L、pH3.0和25℃条件下进行不同时间的吸附,测定吸附时间对菌体吸附Pd2+的影响。其它操作同实施例1,结果如下:Under the conditions of initial Pd 2+ concentration of 200 mg/L, cell concentration of 0.8 g/L, pH 3.0 and 25°C, the adsorption was carried out for different times, and the effect of adsorption time on the adsorption of Pd 2+ by cells was determined. Other operations are with embodiment 1, and result is as follows:
实施例 时间(min) 吸附量(mg/g) 吸附率(%)Example Time (min) Adsorption capacity (mg/g) Adsorption rate (%)
2 3 139.4 58.12 3 139.4 58.1
3 8 147.4 61.43 8 147.4 61.4
4 11 152.2 63.44 11 152.2 63.4
5 15 156.3 65.15 15 156.3 65.1
6 30 164.1 68.46 30 164.1 68.4
7 45 177.1 70.87 45 177.1 70.8
8 60 175.2 70.18 60 175.2 70.1
9 90 176.5 70.69 90 176.5 70.6
实施例10~13Examples 10-13
将PdCl2溶液调至不同的PH值,在Pd2+起始浓度为100mg/L,菌浓度0.8g/L和25℃的条件下,吸附45min,测定菌体对Pd2+的吸附率和吸附量。其它同实施例1,将吸附Pb2+的菌体过滤,放置18小时后,经550℃灼烧3h,即可回收到金属钯。结果如下:Adjust the PdCl 2 solution to different pH values, and under the conditions of the initial Pd 2+ concentration of 100 mg/L, the bacterial concentration of 0.8 g/L and 25°C, adsorb for 45 minutes, and measure the adsorption rate and Adsorption capacity. Others are the same as in Example 1, the bacterial cells adsorbing Pb 2+ are filtered, placed for 18 hours, and burned at 550° C. for 3 hours to recover metal palladium. The result is as follows:
实施例 pH值 吸附量(mg/g) 吸附率(%)Example pH value Adsorption capacity (mg/g) Adsorption rate (%)
10 1.0 58.8 47.010 1.0 58.8 47.0
11 2.0 87.9 70.311 2.0 87.9 70.3
12 3.0 107.3 85.812 3.0 107.3 85.8
13 3.5 116.5 93.213 3.5 116.5 93.2
实施例14~19Examples 14-19
改变吸附作用的温度,在Pd2+起始浓度200mg/L,菌浓度0.8g/L和pH3.5的条件下,吸附45min,测定温度对菌体吸附Pd2+的影响。其余同实施例1,最后菌体放置36h后,经800℃的灼烧1.5h,即可回收到金属钯。结果如下:Change the temperature of adsorption, under the conditions of initial Pd 2+ concentration of 200mg/L, bacterial concentration of 0.8g/L and pH3.5, adsorption was carried out for 45min, and the effect of temperature on the adsorption of Pd 2+ by bacteria was determined. The rest are the same as in Example 1. After the bacteria cells are left for 36 hours, they are burned at 800° C. for 1.5 hours to recover metal palladium. The result is as follows:
实施例 温度(℃) 吸附量(mg/g) 吸附率(%)Example Temperature (°C) Adsorption capacity (mg/g) Adsorption rate (%)
14 5 190.4 76.214 5 190.4 76.2
15 20 196.0 78.415 20 196.0 78.4
16 30 196.7 78.716 30 196.7 78.7
17 40 197.6 79.017 40 197.6 79.0
18 50 201.3 81.318 50 201.3 81.3
19 60 202.2 81.319 60 202.2 81.3
实施例20~23Examples 20-23
改变吸附作用的菌体浓度,在Pd2+起始浓度200mg/L、pH3.5和30℃的条件下,吸附45min,测定菌体浓度对菌体吸附Pd2+的影响。结果如下:Change the concentration of bacteria for adsorption, under the conditions of initial Pd 2+ concentration of 200 mg/L, pH 3.5 and 30°C, adsorb for 45 minutes, and determine the effect of bacteria concentration on the adsorption of Pd 2+ by bacteria. The result is as follows:
实施例 菌体浓度(g/L) Ci∶Cb(mg/g) 吸附量(mg/g) 吸附率(%)Example Cell concentration (g/L) C i : C b (mg/g) Adsorption amount (mg/g) Adsorption rate (%)
20 0.4 500 224.8 45.020 0.4 500 224.8 45.0
21 0.8 250 175.2 70.121 0.8 250 175.2 70.1
22 1.6 125 115.5 92.422 1.6 125 115.5 92.4
23 2.0 100 94.4 94.423 2.0 100 94.4 94.4
Ci∶Cb∶Pd2+起始浓度与菌体浓度之比。C i : C b : ratio of initial Pd 2+ concentration to cell concentration.
实施例24~33Examples 24-33
改变吸附作用的Pd2+起始浓度,在菌体浓度0.8g/L、pH3.5和30℃的条件下,吸附45min,测定Pd2+起始浓度对菌体吸附Pd2+的影响。结果如下:Change the initial concentration of Pd 2+ for adsorption, under the conditions of cell concentration 0.8g/L, pH 3.5 and 30°C, adsorb for 45min, and determine the effect of the initial concentration of Pd 2+ on cell adsorption of Pd 2+ . The result is as follows:
实施例 Pd2+浓度(mg/L) 吸附量(mg/g) 吸附率(%)Example Pd 2+ Concentration (mg/L) Adsorption Amount (mg/g) Adsorption Rate (%)
24 30 37.1 99.024 30 37.1 99.0
25 60 74.1 98.725 60 74.1 98.7
26 90 107.2 95.326 90 107.2 95.3
27 120 128.4 85.627 120 128.4 85.6
28 150 149.8 79.928 150 149.8 79.9
29 180 165.4 73.529 180 165.4 73.5
30 210 84.8 70.430 210 84.8 70.4
31 240 192.2 64.131 240 192.2 64.1
32 270 198.8 59.332 270 198.8 59.3
33 300 202.9 55.133 300 202.9 55.1
实施例34-38Examples 34-38
将废钯催化剂处理液的Pd2+起始浓度调至200mg/L左右,在菌体浓度2~10g/L和30℃条件下吸附60min,结果如下:Adjust the initial concentration of Pd 2+ in the waste palladium catalyst treatment solution to about 200mg/L, and adsorb for 60min under the conditions of bacterial cell concentration of 2-10g/L and 30°C, the results are as follows:
实施例 菌体浓度(g/L) 吸附率(%)Example Bacteria Concentration (g/L) Adsorption Rate (%)
34 2 11.734 2 11.7
35 4 36.935 4 36.9
36 6 56.136 6 56.1
37 8 68.337 8 68.3
38 10 78.4Pd2+起始浓度:206mg/L38 10 78.4Pd 2+ initial concentration: 206mg/L
Claims (8)
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100441300C (en) * | 2006-12-31 | 2008-12-10 | 厦门大学 | Method for preparation of supported silver catalyst by microbial reduction |
| CN100500335C (en) * | 2007-02-15 | 2009-06-17 | 厦门大学 | A kind of preparation method of water-soluble nano-silver powder containing biomass |
| CN105714114A (en) * | 2016-04-22 | 2016-06-29 | 江西省科学院应用化学研究所 | Method for adsorbing enriched rare earth ions from low-concentration rare earth lixivium through fungus A-Fu03 thalli |
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2002
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100441300C (en) * | 2006-12-31 | 2008-12-10 | 厦门大学 | Method for preparation of supported silver catalyst by microbial reduction |
| CN100500335C (en) * | 2007-02-15 | 2009-06-17 | 厦门大学 | A kind of preparation method of water-soluble nano-silver powder containing biomass |
| CN105714114A (en) * | 2016-04-22 | 2016-06-29 | 江西省科学院应用化学研究所 | Method for adsorbing enriched rare earth ions from low-concentration rare earth lixivium through fungus A-Fu03 thalli |
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