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Gold recovery from parts-per-trillion-level aqueous solutions by a nanostructured Mn2O3 adsorbent

Gold recovery from parts-per-trillion-level aqueous solutions by a nanostructured Mn2O3 adsorbent
Gold recovery from parts-per-trillion-level aqueous solutions by a nanostructured Mn2O3 adsorbent

Separation and Puri?cation Technology43(2005)

9–15

Gold recovery from parts-per-trillion-level aqueous solutions

by a nanostructured Mn2O3adsorbent

H.Koyanaka a,1,K.Takeuchi b,C.-K.Loong c,?

a CRMD/CNRS,Orleans University,45071Orleans,Cedex2,France

b Tokyo University of Science,Oshamanbe,Hokkaido049-3514,Japan

c Argonne National Laboratory,Argonne,IL60439,USA

Received7June2004;received in revised form15September2004;accepted15September2004

Abstract

We introduce a nanostructured Mn2O3-based adsorbent and a low-cost method that is capable of extracting gold,in the form of metallic nano-to-micrometer-size particles,from down to sub-ppm-level aqueous solutions including seawaters with high yield,good selectivity and recyclability,and environmental benignity.The Mn2O3adsorbent,prepared by low-temperature synthesis followed by acid treatments,exhibits a mass-fractal-like morphology of agglomerated nanometer-size crystallite grains covered with active protonated sites and a surface area of about120m2/g.For aqueous solutions containing~100ppm gold,a yield of70mg of gold/g of adsorbent was achieved.A Langmuir-type adsorption isotherm was observed,showing a rapid uptake of gold.The method is well suited to gold recovery from very dilute solutions. For example,over95%of the gold was recovered from seawater samples containing0.1and1ppm of added gold.A pilot study of seawater with1ppt added gold showed similar results.The protonation–suspension–?ltration–washing process can be recycled without noticeable degradation in yield.

?2004Published by Elsevier B.V.

Keywords:Gold recovery;Manganese oxide adsorbent;Gold in seawater;[Au(I)Cl2]?and[Au(III)Cl4]?complexes

1.Introduction

Abundance of gold in the Earth’s crust varies between~10 parts per million(ppm)[1]in commercial ore and~10parts per trillion(ppt)in seawater[2–4].Any method attempting to recover gold from natural waters has to be extremely ef-?cient in order to be economically viable.Dissolved gold ions in chlorinated aqueous solutions form[Au(I)Cl2]?and [Au(III)Cl4]?complexes.[AuCl2]?is more stable in di-lute solutions of nearly neutral pH such as seawater,al-though questions concerning its stability relative to that of the AuOH(H2O)0species under oxic conditions have been raised[2,5].In any case,slight increase of acidity or chlori-nation will stabilize all the species to[AuCl2]?complexes ?Corresponding author.Tel.:+16302525596;fax:+16302524163.

E-mail address:ckloong@https://www.doczj.com/doc/2017688349.html,(C.-K.Loong).

1Permanent address:Dannoharu900-103,Oita-shi,870-1124,Japan.[6].Employment of adsorbents to recover gold from natural waters,due to the extreme dilution,requires effective sus-pension of the adsorbing particles with maximally allowed, chemically active sites that target speci?cally[AuCl2]?com-plexes and exceedingly high rate of Au(I)to Au(0)reduc-tion.Previous methods of gold recovery were either feasi-ble only to specially processed solutions containing rather high gold concentrations or deemed impractical due to low yields,operational dif?culties or environmental concerns. Such adsorbents include silica-polymer composites[7],sur-factants[8],pyrite,goethite,and birnessite[9,10]applicable to acidic hydrochloric solutions(pH<4)or seawater contain-ing1–130ppm of gold,activated carbons or ion-exchange resins for recovering gold from cyanide-leached solutions in the mining industry[11,12],and proposed utilization of algae [13]and micro-organisms[14].Hence an adsorbent capable of recovering gold from natural waters down to ppt levels with high ef?cacy and minimal environmental impact is highly de-

1383-5866/$–see front matter?2004Published by Elsevier B.V. doi:10.1016/j.seppur.2004.09.005

10H.Koyanaka et al./Separation and Puri?cation Technology43(2005)9–15

sirable.Furthermore,cost consideration demands a relatively

simple method of synthesis and chemical processing of the

adsorbent.

Our contemplation of a suitable manganese-oxide ad-

sorbent was motivated by several important properties

common to manganese oxide/hydroxide minerals:(i)the

ubiquitous presence in the ocean?oor,soils,and sed-

iments,which imply environmental benignity[15];(ii)

the high cation-exchange capacity;and(iii)the available

Mn(II),Mn(III)and Mn(IV)states that are amenable to

oxidation–reduction reactions.However,the Mn(IV)oxida-

tion state in MnO2-type compounds is known to promote

dissolution of gold in hydrochloric solutions.For example,

birnessite(Na,K)Mn7O14·2.8H2O)is not effective in ad-sorbing gold[9].We hypothesize that the Mn(III)state in

an Mn2O3-type adsorbent with a nanostructured architec-

ture capable of controlled association/dissociation of pro-

tonic species on/off the particle surfaces is essential to ef-

?cient gold extraction.Such adsorbent was realized by a

low-temperature synthesis of a nanostructured Mn2O3pow-

der,followed by protonation of the particle surfaces by acid

treatments.The Mn2O3adsorbents were systematically ap-

plied to specimens of distilled water and seawater contain-

ing1–100ppm and0.1–1ppm of added gold,respectively,

through a suspension–?ltration–washing procedure.Encour-

aged by the results,we studied a seawater sample containing

1ppt added gold.

2.Experimental

2.1.Low-temperature synthesis and acid treatment

An MnCO3powder(Wako,99%purity)as the start-

ing material was heated using an electric furnace at230?C

in air for4.5h.An acid treatment began with adding the

powder into in a0.5mol/L of nitric or hydrochloric acid

whiling stirring(using a magnetic stirrer)for a chosen pe-

riod of suspension time.Afterward the suspended particles

were?ltered from the solution using a glass?lter(0.2?m

mesh),followed by washing with distilled water.This?rst-

stage processing with a15min suspension time for an initial

acid treatment enabled the growth of nanometer-size crys-

talline Mn2O3grains on the surfaces of micron-size crys-

talline MnCO3particles.Subsequent acid treatments,typ-

ically for1h suspension each,allowed the removal of the

MnCO3component and the self-assembly of adsorbed H+

ions(protons)on the Mn2O3nanoparticles.This second

acid treatment resulted in a substantial increase of the pop-

ulation of the protonated sites.Furthermore,the remain-

ing MnCl2or MnNO3in the solution after an acid treat-

ment and?ltration of the adsorbent can readily be con-

verted to useful high surface area MnO2powder by adding

an appropriate amount of KMnO4to the solution.This

reduces the amount of waste and negative environmental

impacts.2.2.Characterization and chemical analysis

The microstructure and crystal phases were character-ized by small-angle neutron scattering(SANS),neutron powder diffraction(NPD)and synchrotron-radiation X-ray diffraction(SRXD),and the morphology by scanning(SEM) and transmission(TEM)electron microscopy.Inductively coupled plasma atomic-emission/mass-spectroscopy(ICP-AES/MS),energy dispersive X-ray(EDX),and X-ray pho-toelectron(XPS)spectroscopies were employed for chemi-cal analyses.Neutron studies were performed at the Intense Pulsed Neutron Source of Argonne National Laboratory.The SRXD experiment was carried out at the synchrotron X-ray source,SPring8(Hyogo,Japan).ICP-MS measurements were conducted independently by the Centre National de la Recherche Scienti?que Service Central d’Analyse in Or-leans,France.SEM,TEM,ICP-AES,EDX,XPS measure-ments were performed using standard equipments.

2.3.Seawater experiments

Care was used to collect unpolluted near-surface seawa-ter from Beppu Bay,Japan and to store it in acid-cleaned polyethylene bottles.For the0.1and1ppm added gold con-centrations,the goal was to determine the amount of gold ad-sorption over different suspension times but not the residual concentration of gold in the solution after achieving equilib-rium in saturated adsorption,hence using0.5g of adsorbent in1L of seawater was suf?cient.In the case of1ppt added gold in seawater,5g of adsorbent was suspended in10L of seawater.Here,we did not intend to assess the natural gold content in the seawater but to measure the elution curve of the recovered gold by the adsorbent.The expected ppb level of gold,if present in the solution obtained by washing the?ltered adsorbent with~10mL of0.5mol/L hydrochloric acid,was well within the capability of ICP-MS detection.The ultra-pure water(Wako)and ultra-pure hydrochloric acid(Wako) used in the experiment were found to contain gold,if any,at

a level below the detection limit.

3.Results and discussion

3.1.Structures at micrometer to nanometer scale

We?rst determined the crystal structures of the compos-ite of micrometer-size MnCO3and nanometer-size Mn2O3, obtained from the?rst-stage synthesis.Fig.1shows the re-?ned NPD and SRXD data for the crystal structures which contain4.6wt.%of cubic-Mn2O3[16]and95.4wt.%of rhombohedral-MnCO3[17].No other phases were observed other than an amorphous-like component as evidenced in the residual intensity,presumably originated from atomic dis-order at the interfaces of the particles.The microstructure of the composite was characterized by SANS.The observed intensity pro?le arises from the differences in the neutron

H.Koyanaka et al./Separation and Puri?cation Technology 43(2005)9–15

11

Fig.1.Rietveld re?nements of the room-temperature NPD pattern (dots:data,line:calculated pro?le)of the as-sintered material treated with acid for 15min.The crystal phases include MnCO 3and Mn 2O 3,of which the Bragg-re?ection positions are denoted by the lower and upper tick marks,respectively.The indices of some re?ections are given.The Bragg-peak intensity of the Mn 2O 3phase,albeit tiny,can clearly be seen by neutrons (inset)and synchrotron X-rays (thick line above the tick marks).The absence of the (006)re?ection of the MnCO 3phase in the X-ray data is due to its vanishingly small structure factor.

scattering-length densities of MnCO 3and Mn 2O 3particles and the voids over the (reciprocal)length scale τin terms of the wavevectors Q ,where Q =2π/τ.The SANS pro?le in Fig.2shows a major component of large MnCO 3particles

(at Q <0.006?A

?1)and a minor component of smaller Mn 2O 3particles (a broad shoulder at Q ≈0.02?A

?1).A slope of the curve of slightly higher than ?4(the Porod value)at high Q indicates the rough interfaces of the particles [18].

The neutron and X-ray diffraction studies of the average structure of the samples were complemented by microscopy measurements in the real space.As shown in Fig.3a,TEM con?rmed the morphology of plate-like Mn 2O 3nanoparticles on the surfaces of large MnCO 3particles.The surface area of the material before and after the second acid treatment,estimated from a nitrogen adsorption isotherm measurement and a (Brunauer–Emmett–Teller)BET analysis,was found to be ~90and ~120m 2/g,respectively.Subsequent acid treat-ments did not increase the surface area.Both TEM and BET measurements indicated a microporosity of the adsorbent with an average pore diameter of about 10

nm.

Fig.2.SANS pro?les of the samples obtained after sintering and acid treat-ments.The errors are comparable to the size of the symbols except for

Q >0.4?A

?1where the errors are larger.The slopes of the curves at high Q are slightly higher than ?4.The thick curve represents a ?t of the data (3times acid treatment)with a mass-fractal model.The SANS pro?le of a powder undergone two additional acid-treatments (Fig.2)shows a large decrease of the inten-sity at low-Q and the appearance of a broad maximum at

Q >~0.01?A

?1,corresponding to the removal of the MnCO 3and aggregation of the Mn 2O 3nanoparticles.The nature of the aggregation can be described satisfactorily by a mass-fractal geometry,namely,a fractal dimension of 3.02±0.01and a mean particle size of 10.3±0.03nm with a log-normal distribution of sizes characterized by a standard deviation of 1.65±0.01[19,20].The SANS result is corroborated by the TEM data (see Fig.3b).Additional NPD and neutron spectroscopic studies con?rm that protonation of the Mn 2O 3nanoparticles via acid treatments introduced distortions of the crystal lattice,atomic disorder,and defects.Since the proton coverage is large,the modi?cation of the crystal structure and stoichiometry is substantial.For convenient,we refer the acid-treated powders as Mn 2O 3adsorbent but do not imply strictly the crystal structure and stoichiometry of Mn 2O 3[16].3.2.Gold recovery from 1to 100ppm aqueous solutions We ?nd that two additional acid-treatments (total suspen-sion time 2h)of the initially prepared Mn 2O 3powder pro-duced very effective gold adsorbents.The gold adsorption experiments were conducted by suspending 1g of

adsorbent

Fig.3.TEM imagine of the sample:(a)the large MnCO 3grains and small,nm-size plate-like Mn 2O 3are observed;(b)after 3times of acid treatment only an aggregate of the Mn 2O 3crystallites in microporous geometry is evident.The featureless background near the edges is from the carbon grid of the sample holder.

12H.Koyanaka et al./Separation and Puri?cation Technology 43(2005)9–15

in 3L of aqueous solutions containing 1,20,30,50,and 100ppm of gold that were prepared by mixing a standard HAuCl 4solution with distilled water while maintaining a pH of ~6by adding appropriate amounts of a 1mol/L aqueous NaOH solution.A 10mL batch of the ?ltered solution was collected at regular time intervals,from which the gold con-centrations were determined by ICP-AES.Fig.4a shows a rapid decrease of the gold concentration in the 1-ppm solu-tion as a function of suspension time.The obtained

adsorption

Fig.4.(a)Decrease of the gold concentration in the solutions as a function of suspension time of the adsorbent.(b)Yield in units of mg of gold/g adsor-bent vs.the gold concentration of the solutions at equilibrium of saturated adsorption.The initial gold concentrations in units of ppm are given next to the data points.(c)Elution curve of gold recovery from the adsorbent (5g)after suspension in 10L of seawater containing 1ppt added gold by washing with 0.5mol/L ultra-pure hydrochloric acid.The area in a grey box repre-sents the amount of gold in each elution from ICP-MS measurements.The hatched boxes are the error bars of the measurements.The total recovered gold of about 19ng (with an uncertainty of ~35%)is in reasonable agree-ment with the 10ng added gold in 10L plus the natural content of gold in the seawater

sample.

Fig.5.Decline of Au concentration as a function of suspension time for a virgin and once and twice regenerated adsorbent;0.3g of adsorbent was added in a 3L aqueous solution containing 5ppm of gold while maintaining a pH of 5.0–6.0.

isotherm (Fig.4b),in terms of yield versus gold concentra-tion in the solutions at equilibrium of saturated adsorption,shows:(i)an achieved yield of 70mg of gold/g of adsorbent that supersedes those of other methods of gold extraction from aqueous solutions [7–10];and (ii)a sharp rise from the origin typical of the Langmuir-type isotherm [21].The rapid takeoff of isotherm demonstrates the high ef?ciency of this adsorbent,hence the applicability to very dilute solutions.In approaching to the maximal yield of ~70mg gold/g adsor-bent,apparently,on the average each nanoparticle is covered by a monolayer of gold.Re-activation of the adsorbent is sim-ple.Several washings of the ?ltered adsorbent with 10mL of 0.5mol/L hydrochloric acid dissolve all the adsorbed gold and re-protonate the active sites at the same time.After rinsing with distilled water,the adsorbent is ready for re-using with nearly the original ef?cacy.SANS and TEM con?rmed the preservation of the nanostructured morphology in the gold-adsorbed and re-activated adsorbents.Fig.5illustrates the typical performance of a reused adsorbent.About 0.3g of adsorbent was suspended in 3L of 5ppm gold aqueous so-lution while maintaining a pH of 5.0–6.0.Fig.5shows the decline of Au concentration for a virgin and once and twice regenerated adsorbent as a function of suspension time.The adsorption rates are very similar.

3.3.Gold recovery from 0.1and 1ppm and 1ppt seawater

For the seawater sample with 0.1and 1ppm added gold,we ?nd that the adsorbent was equally effective (over 95%re-covery rate)with the exception that up to 18h of suspension was required for full recovery of the gold.Apparently,the presence of high-concentration cations such as Na +,Mg 2+,and Ca 2+within the bilayer surrounding a suspended particle interferes the proton release into the solution and retards the reduction of the AuCl 2?complexes (see Section 3.4below).The estimated contents (in ppm)of these ions in the adsorbent by ICP-AES were Ca (~200)>Na (48)>Mg (7.8).Compar-ing with the nominal content of Na (10770)>Ca (412)>Mg

H.Koyanaka et al./Separation and Puri?cation Technology 43(2005)9–1513

(190)in seawater [22],the selectivity of gold against other ions is good.In the case of 1ppt added gold in seawater,the main purpose was to measure the elution curve of the recovered gold by the adsorbent.The elution was obtained by washing the ?ltered adsorbent with ~10mL of 0.5mol/L hydrochloric acid.Fig.4c show the elution curve of gold recovered from the 1ppt gold-added seawater.The total re-covered gold of about 19ng (with an uncertainty of ~35%)is in reasonable agreement with the 10ng added gold in 10L plus the natural content of gold in the seawater sample.3.4.Adsorbed metallic gold particles

The adsorbed gold on the Mn 2O 3particles were charac-terized by TEM,SEM,XPS and EDX measurements.XPS measurements identi?ed a binding energy of Au 4f 7/2orbital of 84eV which is consistent with the metallic Au(0)state of the adsorbed gold.If the 3+oxidation state is present as it would be the case for a [Au(III)Cl 4]?complex,a binding energy of 85.7–87.1eV is expected [23,24].Figs.6a and b show that initially,polydisperse nanometer-size gold parti-cles were formed.These particles subsequently grew to sub-micron sizes,which was con?rmed by SEM and concurrent EDX characterization (Fig.7a and

7b).

Fig.6.High-resolution (a)and low-resolution (b)TEM images of gold par-ticles (dark)adsorbed on the Mn 2O 3adsorbent (light).

The data demonstrate the effectiveness of our Mn 2O 3ad-sorbent in recovering gold from distilled water and seawater down to ~1ppt concentrations.The mechanism begins with the deposition of AuCl 2?complexes on the surfaces of the positively charged Mn 2O 3nanoparticles.Protons are subse-quently released,as evidenced by an initial decrease in the pH of the solution when the adsorbent was added,and electron transfers take place for decomposition of the AuCl 2?com-plexes into metallic gold via the well-known reaction [6,25]:3AuCl 2?→2Au(s)+AuCl 4?+2Cl ?.

(1)

Nanometer-size seeds of metallic gold are formed initially,many of them grow to micron-size particles subsequently by a self-catalyzed reaction as previously studied by Gammons and coworkers [6].However,the present result is rather surprising.First,the proton-activated,mass-fractal-like nanostructure of the powder drastically enhances the reactivity,hence an ultrahigh ef?ciency of gold recovery,to an unprecedented level.Traditional electrochemical approaches,even with the application of electrodes,can-not produce the high adsorption rate in such very dilute solutions.Any theory of gold reduction via redox reactions (e.g.,Mn(III)→Mn(IV)and Au(III and I)→Au(0)

with

Fig.7.SEM image (a)showing the grown gold particles (with lighter color)on the adsorbent,and the correspondent EDX image (b)showing the distri-bution of the large and small gold particles.

14H.Koyanaka et al./Separation and Puri?cation Technology43(2005)9–15

redox potentials of0.54V at pH=8and1.002–1.154V, respectively[26]),if present additionally,has to take into account of the interfacial interactions between the AuCl2?complexes and the protonated Mn2O3layers at a nanoscale.Perhaps,the ultrahigh ef?ciency is made possible by the replenishment of Au(III)Cl2?species in Eq.(1)via oxidation of Mn(III)of Mn2O3to form MnO2. However,the partial conversion of Mn(III)to Mn(IV) cannot be con?rmed by XPS measurement because of the overlapping binding energies of these two states from the 2p3/2orbital.Secondly,the pro?ciency of dissolving all the metallic gold by washing the Mn2O3adsorbent with only dilute(~0.5mol/L)hydrochloric solutions,as consistently shown by the ICP measurements of the gold contents in the adsorbent and in the extracted solutions,is unusual. The extracted solutions display a gold color of dissolved Au complexes as in the standard HAuCl4solution as opposed to the red color of metallic gold colloids.Normally, special acids such as aqua regina are required to dissolve metallic gold.We speculate a mechanism of dissolving the adsorbed gold via a crossover of the redox potentials of Mn(IV)→Mn(II)and Au(0)→Au(III)in the reaction: 3MnO2+12H++2Au+8Cl?→3Mn2++6H2O+2AuCl4?, which presumably can only occur at a nanometer scale.

4.Conclusions

We summarize the synthesis,processing,and characteri-zation of the Mn2O3-based adsorbent and the gold recovery as follows:

(1)A composite consisting of crystallite,micron-size

MnCO3and nm-size Mn2O3particles was synthesized by a low-temperature method.

(2)Acid treatments of the composite removed the MnCO3

component and protonated the Mn2O3nanoparticle sur-faces.This process produced an adsorbent having a fractal-like morphology with a surface area of120m2/g.

(3)The adsorption isotherm,elution curves and the prod-

uct of gold recovery from aqueous solutions and seawater samples containing gold through a suspen-sion/?ltration/washing procedure were described.Chem-ical analysis showed that for20–100ppm gold concen-trations where the equilibrium saturated concentration could be measured,a maximal yield of70mg gold/g ad-sorbent was achieved.For lower concentrations down to~1ppt level,elution curves showed that essentially all the gold could be recovered.The adsorbed gold was metallic Au(0)particles,which could subsequently be extracted by dissolution in dilute HCl solutions via wash-ing.

(4)The adsorbent can be reused with sustainable ef?ciency

simply by washings with dilute HCl solutions.

(5)A conjecture of the unique capabilities of this method,

namely,ultrahigh ef?ciency of gold recovery from very

dilute solutions and the solubility of the extracted metal-lic gold particles by dilute HCl solutions was given,em-phasizing the redox character of the nanoscaled man-ganese oxide adsorbent.

The high yield and selectivity,excellent ef?ciency,and recyclable usage of this gold adsorbent in an environmen-tally benign manner clearly demonstrated the feasibility of recovering gold from aqueous solutions and seawater down to ppb levels.The tantalizing result of the1ppt added gold in seawater might merit an industrially scale-up evaluation for economical viability of the method.To reduce the cost of initial investment,testing can be integrated with the ex-isted infrastructure of the desalination plants and power re-actors that use seawater as coolant[27],as previously demon-strated for the case of lithium collection from seawater using a manganese-spinel adsorbent[28].Moreover,preliminary tests showed that our Mn2O3adsorbent(0.5g)could recover 60%of silver and70%of palladium from40ppm,1L aque-ous solutions.Post-sintering can control the nanometer size distribution of the Ag and Pd particles.Therefore,in addition to preparing ef?cient Mn2O3adsorbents for extract useful metals from aqueous solutions,our synthesis method can in principle produce useful Mn2O3-based catalysts supporting different metallic nanoparticles.

Acknowledgement

We thank N.Koura,J.W.Richardson,Jr.,V.Komenko and P.Azais for the helpful discussions.The assistance in sample characterization from C.Clinard and T.Cacciaguerra with TEM,E.Veron and A.Uchida with SEM,P.Baillif with ICP-AES,D.Wozniak and L.Guo with SANS,and S.Kohara with SRXD is gratefully acknowledged.HK thanks Des Bourses 2003du Gouvernement Francais for the?nancial support and M.-L.Saboungi for the kind hospitality during the stay at CRMD.Work performed at Argonne National Laboratory is supported by the U.S.DOE-Basic Energy Science under the contract No.W-31-109-ENG-38.

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实时频谱仪—工作原理

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