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Utilization of flotation in copper extraction from polymetallic ore

Abstract

The aim of this study was to examineflotation of utility metals from poor polymetallic ores and verify the potential for profitable yields in connection withpotentially economic deposits of non-ferrous metals.The paper describes results in flotation concentrate research to recover copper from polymetallic ore. The polymetallicore from Zlate Hory deposit (Czech Republic) was subjected to crushing, grinding, and screening to prepare feed for separation with mesh size under 200 microns. The heavy medium separation was performed in tetrabromethane with a density of 2.967 g.cm-3. The float and sink products were obtained and tested for chemical composition. Next, the treated polymetallic ore sample was subjected to flotation. In flotation,various dosages of collector (PAX) and various pH were tested, at which pyrite was depressed. The recovery of metallic copper in the concentrate increased with the collector dose. As the pH of the medium increased, the pyrite content in the concentrate dropped. The lowest contentof pyrite, i.e. 4.01%,was obtained at pH 10. In the original polymetallic ore, the Cu content was 0.41% after subsequent treatment and flotation tests, the Cu content increased to 1.38 % with Cu recovery 86.18%.

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Utilization of flotation in copper extraction from polymetallic ore

Author: Vrlíková, Věra
Publisher: Vysoká škola báňská-Technická Univerzita Ostrava
Year: 2020
DOI: 10.35180/gse-2020-0030
Source: https://dspace.vsb.cz/bitstreams/dc015bad-b8cd-4cc0-a6ce-bdca53dd05d3/download
GeoScience Enginee ing Volume 66 (2020), No. 1
h p://gse. sb.cz p. 53–59, ISSN 1802-5420
DOI 10.35180/gse-2020-0030
UTILIZATION OF FLOTATION IN COPPER EXTRACTION FROM
POLYMETALLIC ORE
Vě a VRLÍKOVÁ, Vladimí ČABLÍK, I a JANÁKOVÁ
Depa men o En i onmen al Enginee ing, Facul y o Mining and Geology, VŠB – TUO, Os a a,
Czech Republic
E-mail: e [email p o ec ed]
ABSTRACT
The aim o his s udy was o examine lo a ion o u ili y me als om poo polyme allic o es and
e i y he po en ial o p o i able yields in connec ion wi h po en ially economic deposi s o non- e ous
me als. The pape desc ibes esul s in lo a ion concen a e esea ch o eco e coppe om polyme allic
o e. The polyme allic o e om Zla e Ho y deposi (Czech Republic) was subjec ed o c ushing, g inding,
and sc eening o p epa e eed o sepa a ion wi h mesh size unde 200 mic ons. The hea y medium
sepa a ion was pe o med in e ab ome hane wi h a densi y o 2.967 g.cm-3. The loa and sink p oduc s
we e ob ained and es ed o chemical composi ion. Nex , he ea ed polyme allic o e sample was subjec ed
o lo a ion. In lo a ion, a ious dosages o collec o (PAX) and a ious pH we e es ed, a which py i e
was dep essed. The eco e y o me allic coppe in he concen a e inc eased wi h he collec o dose. As he
pH o he medium inc eased, he py i e con en in he concen a e d opped. The lowes con en o py i e,
i.e. 4.01 %, was ob ained a pH 10. In he o iginal polyme allic o e, he Cu con en was 0.41 % a e
subsequen ea men and lo a ion es s, he Cu con en inc eased o 1.38 % wi h Cu eco e y 86.18 %.
Keywo ds: Coppe ; Flo a ion, Polyme allic o e; Po assium amylxan ha e (PAX); Zla e Ho y
1 INTRODUCTION
Sepa a ion o mine als om o e is an impo an indus ial p ocess. O he commonly used me hods o
sepa a ion, lo a ion exploi s he hyd ophobic (i is pa ial o incomple e we abili y o a solid phase by he wa e )
and hyd ophilic (solids a e comple ely we ed by wa e ) p ope ies on he mine al su ace. Flo a ion is a me hod
ha is based on di e en su ace p ope ies occu ing a he con ac o h ee phases - solid (mine al pa icles),
liquid (wa e ), and gas (ai ). Hyd ophobic pa icles adhe e o ai bubbles ha mo e o he su ace o o m o h [1].
Sulphide o es a e impo an sou ces o base me als, e.g. coppe , zinc, lead. In mos cases, he mine als o
coppe , lead, zinc and i on coexis on he deposi [2]. Selec i e lo a ion o sulphide o es p esen s se e al p oblems
due o mine alogical p ope ies, incomple e libe a ion, and chemical di e ences be ween o es [3]. Flo a ion is in
many cases he only solu ion o concen a e sulphide mine als [4]. Fo sulphide mine als, hyd ophobici y may
occu due o he addi ion o a collec o o oxida ion leads o he o ma ion o elemen al sulphu , me al-de icien
and sulphu - ich su ace [5]. In lo a ion, xan ha es a e used as collec o s in he sepa a ion o sulphide mine als.
Thei consump ion is 300 o 500 g/ . Al hough he e a e a numbe o xan ha es, sodium e hyl xan ha e, isop opyl
xan ha e, sodium isobu yl xan ha e o po assium amylxan ha e a e used in p ac ice [6].
Na u al coppe is a e and ep esen s abou 1 % o all coppe compounds. Coppe may be p esen ei he in
he o m o sulphide o es, o ming 90 % o coppe compounds, o 9 % as oxidic o es [7]. The ypical con en s o
coppe in sulphide o es is 0.6 %, pa icula ly p ima y sulphides (e.g. chalcopy i e and bo ni e) o seconda y
sulphides (e.g. chalcoci e and co elli e) [8]. Chalcopy i e is one o he mos impo an sulphide mine als, which is
he main sou ce o coppe [9]. The p esence o gangue sulphide mine als such as py i e and non-sulphide mine als
educe he quali y o concen a es [10]. I is he only na u ally loa able coppe mine al, o o he sulphide coppe
mine als hiol collec o s a e added o c ea e he hyd ophobic su ace needed o lo a ion [11]. Chalcopy i e loa s
well wi h mode a e amoun s o xan ha e collec o s o e a wide pH ange [12].
Chalcopy i e is associa ed wi h py i e in o e; he e o e, py i e dep ession is equi ed o economic eco e y.
The main p oblem o chalcopy i e and py i e is hei selec i i y, which is caused by acciden al ac i a ion o py i e
by dissol ed Cu2+ ions om complex sulphide o es. This inc eases he in e ac ion o py i e wi h collec o s, he eby
inc easing i s loa abili y [13]. Va ious agen s, such as polyme s, hyd oxides, ca bona es, cyanides, o sulphi es,
a e used o supp ess py i e [14].
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DOI 10.35180/gse-2020-0030
Mukunga [15] in es iga ed he selec i i y and kine ics o PAX and DANA (sodium amyl di hiophospha e)
in he eco e y o coppe om sulphide coppe -cobal o e. Na u al pH and pH 11 we e obse ed. A na u al pH,
he coppe con en o he concen a e ob ained was 16.1 % wi h a yield o 99.63 %. A pH 11, he coppe con en
was 16.1 % wi h a yield o 99.05 %. These esul s showed ha a na u al pH and pH 11, he kine ics o coppe
egene a ion wi h PAX is supe io o DANA.
2 MATERIALS AND METHODS
Fo his wo k, a sample o polyme allic o e was used om Zla e Ho y-Eas (Czech Republic). Fo
labo a o y es s, i was necessa y o p epa e he sample by c ushing and g inding. A o al o 9 kg o polyme allic
o e was c ushed and g ound. This was ollowed by sizing o -200 μm.
This modi ied sample was subjec ed o X- ay di ac ion o de e mine he mine al con en (Tab. 1). A
subs an ial pa o he polyme allic o e p oduc ion was ep esen ed by qua z (87.03 %). O he non-me allic
mine als ep esen ed we e ba i e, albi e, chlo i e and musco i e. Py i e, chalcopy i e and sphale i e we e p esen
as o e mine als. The la ges amoun in he sample was sphale i e (3.64 %). Chalcopy i e was 1.59 %.
Table 1. X- ay di ac ion esul s o o e sample - inpu
mine al
qua z
py i e
chalcopy i e
sphale i e
albi e
chlo i e
musco i e
ba i e
con en
[%]
87.03
2.30
1.59
3.64
1.89
1.28
0.48
1.79
Elemen al composi ion was de e mined using XRF analysis (Tab. 2). O he main o e mine als, Zn con en
was 2.79 % and Cu 0.41 %. In addi ion o he elemen s lis ed in he able in polyme allic o es occu ing elemen s
in ace amoun s.
Table 2. XRF analysis esul s o o e sample - inpu
elemen
Al2O3
SiO2
Fe2O3
Cu
Zn
Pb
S
con en [%]
1.91
76.08
6,95
0.41
2.79
0.11
4.96
To educe he qua z con en o he sample, we used hea y medium sepa a ion. The modi ied sample was
subjec ed o hea y medium sepa a ion. The medium was 1,1,2,2- e ab ome hane 98.8 % wi h a densi y o
2.967 g.cm-3. The sample was washed wi h me hanol and dis illed wa e , and le o d y a 105°C.
The ob ained sink ac ion was subjec ed o lo a ion es s. The p ocedu e scheme is shown in Fig. 1.
Flo a ion es s we e pe o med on a pneuma ic-mechanical lo a ion machine VRF-1 wi h a lo a ion cell olume
o 1dm3. Fo each expe imen , we used 100 g/l o sample. The sample was condi ioned o 2 minu es.
Subsequen ly, he collec o was added, and condi ioning con inued o 2 minu es, he o he was added and
condi ioned o 1 minu e. Concen a e was ob ained a e 10 minu es. Po assium amylxan ha e (PAX) was used as
he collec o , he polye hyleneglycol (PEG) was he o he and Ca(OH)2 was used o adjus he pH. I was used
o lo a ion es s 3180 g/ PEG and 36 g/ , 42 g/ , 56 g/ , 70 g/ and 84 g/ PAX. Following he lo a ion es s in
which he mos app op ia e collec o dose was selec ed, he pH was moni o ed 8, 9, 10, 11.
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Figu e 1. P ocedu e scheme
3 RESULTS AND DISCUSSION
Hea y medium sepa a ion
A 9 kg sample o polyme allic o e was used o hea y medium sepa a ion. O he o al amoun , 1 kg was
ob ained as a sink ac ion and he emaining ac ion was a loa ac ion. Based on XRD analysis, he loa ac ion
was mo e han 90 % qua z, musco i e, albi e and chlo i e. Because o i s composi ion, he loa ac ion was no
u he in e es ing o p ocessing.
Table 3 shows he composi ion o a sample o sink ac ion om hea y medium sepa a ion. The applica ion
o hea y medium sepa a ion was p epa ed using sulphidic concen a e con aining 30.10 % Fe2O3, 11.50 % Zn,
0.99 % Cu, 26.88 % S. The con en o SiO2 was educed om 76.08 % o 30.10 %.
Table 3. XRF analysis esul s o sink ac ion
elemen
Al2O3
SiO2
Fe2O3
Cu
Zn
Pb
S
con en [%]
1.35
30.10
30.10
0.99
11.50
0.14
26.88
Flo a ion
The i s lo a ion ocused on selec ing he mos sui able collec o amoun . The pH was cons an du ing he
lo a ion es s, he pH was 6.1. Figu e 2 and Table 4 show he esul s o lo a ion es s. Wi h inc easing dose o
PAX collec o , Cu eco e y in indi idual concen a es inc eased. The highes Cu eco e y o 94.23 % in he
concen a e was achie ed a a collec o dose o 84 g/ . Wi h inc easing dose o PAX, he lo a ion e iciency
inc eased. A a dose o 84 g/ PAX, an e iciency o 77.22 % was achie ed, while he lowes e iciency was
61.36 % a a dose o 70 g/ . The highes mass eco e y o 60 % was ob ained a he 56 g/ PAX dose, while he
lowes mass eco e y o 45 % was a he 42 g/ PAX dose. The Cu con en in he concen a es anged om 1.12
o 1.13 %, only a a dose o 36 g/ PAX he highes Cu con en o 1.2 % was achie ed. The en ichmen o Cu was
in ange o 1.13-1.20 %. The highes en ichmen o Cu was 1.20 % a he dose 36 g/ and 70 g/ PAX. Acco ding
o he esul s, a dose o 84 g/ PAX was selec ed o u he lo a ion es s.
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Figu e 2. Resul s o lo a ion es s
Rm – Cu eco e y, SE_Cu - sepa a ion e iciency o Cu, - mass eco e y
Table 4. Con en o Cu and en ichmen o Cu in he sample
dose collec o
con en Cu [%]
en ichmen Cu [%]
36 g/
1.2
1.20
42 g/
1.13
1.14
56 g/
1.13
1.14
70 g/
1.19
1.20
84 g/
1.12
1.13
Cu eco e y was calcula ed acco ding o he ollowing o mula [16]:
𝑅𝑚=𝑐∙(𝑓−𝑡)
𝑓∙(𝑐−𝑡)∙100% (1)
whe e:
= Cu in he o e, c = Cu in he concen a e, = Cu in ailings, Rm = he eco e y o he aluable mine al.
Sepa a ion e iciency was calcula ed acco ding o he o mula [17]:
𝑆𝐸𝐶𝑢 = 𝑅𝑚− 𝑅𝑔 (2)
whe e:
SECu = sepa a ion e iciency o Cu (%), Rm = he eco e y o he aluable mine al and Rg = eco e y o he
gangue in o he concen a e.
Vizca a e al. [18] s udied he e ec o pa icle shape p ope ies on chalcopy i e lo a ion kine ics. The
esul s o he s udy showed ha he pa icle shape p ope ies a e only impo an o mine als ha a e cha ac e ized
by slow lo a ion kine ics, so hey a e likely o be o g ea e impo ance o weakly hyd ophobic pa icles. In he
p esence o PAX, he shape p ope ies we e no ound o con ibu e signi ican ly o he a e a which he pa icles
loa .
0
10
20
30
40
50
60
70
80
90
100
36 g/ 42 g/ 56 g/ 70 g/ 84 g/
[%]
Collec o
Rm
SE_Cu
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The aim o he second pa o he lo a ion es s was o selec he op imal pH, a which py i e was dep essed.
Dep ession o py i e in coppe concen a e occu s a high pH. Lime is mos o en used o dep ess py i e a pH 11
[19]. The amoun o collec o used in hese es s was 84 g/ . Figu e 3 and Table 5 show he esul s o lo a ion es s
o di e en pH alues. Wi h inc easing pH, Cu eco e y in di e en concen a es inc eased. The e y highes Cu
eco e y o 86.22 % was ob ained a pH 11. The e iciency o indi idual lo a ions inc eased wi h inc easing pH.
The e y highes e iciency o 55.98 % was achie ed a pH 11, while he lowes e iciency o 14.15 % was a pH
8. The mass eco e y o concen a e inc eased wi h inc easing pH. The highes mass eco e y 60.37 % was
ob ained a pH 11. In con as , he lowes mass eco e y a pH 8 was 40.0 %. Wi h inc easing pH, he Cu con en
in he concen a e dec eased. A pH 8, he Cu con en was 1.86 %, bu a pH 11 only 1.25 %. Concu en ly wi h
inc easing pH, he Cu en ichmen in he concen a e dec eased. A pH 8, he Cu en ichmen was 1.88 %, bu a pH
11 was 1.26 %.
Figu e 3. Resul s o lo a ion es s
Rm - Cu eco e y, SE_Cu - sepa a ion e iciency o Cu, - mass eco e y
Table 5. Con en o Cu and en ichmen o Cu in he sample
pH
con en Cu [%]
en ichmen Cu [%]
8
1.86
1.88
9
1.72
1.74
10
1.38
1.40
11
1.25
1.26
Figu e 4 shows he esul s o dep essing py i e a di e en pH alues. Wi h inc easing pH, he con en o
py i e in he concen a e dec eased. A pH 8 he py i e con en o 9.26 %, bu a pH 11 py i e con en was only
4.20 %. The lowes amoun o py i e was a pH 10, he con en was 4.01 %. Based on he esul , in which py i e
was dep essed he bes pH was 10. A pH 10 he g ea es dep essing o py i e showed, whe ein he con en was
4.01 % and he con en chalcopy i e in he concen a e was 13.16 %.
0
10
20
30
40
50
60
70
80
90
100
8 9 10 11
[%]
pH
Rm
SE_Cu

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Figu e 4. Resul s o py i e dep ession
4 CONCLUSION
A sample o polyme allic o es om he Zla e Ho y-Eas deposi was subjec ed o lo a ion. The sample was
adjus ed o a sui able g ain size and subjec ed o X- ay and XRF analysis. On he basis o he ob ained esul s, he
sepa a ion o qua z in hea y medium sepa a ion and subsequen lo a ion was pe o med. Fi s , he e ec a ious
dosages o collec o on he lo a ion e iciency was obse ed. The second se ies o lo a ion was used o de e mine
pH a which o achie e maximum dep essing o py i e. Wi h inc easing he dose o PAX collec o , Cu eco e y in
indi idual concen a es inc eased. As a esul , i u ned ou ha he dose o 84 g/ PAX was he bes dose o nex
lo a ion. As he pH o he medium inc eased, he py i e con en o he concen a e was educed. The con en py i e
in concen a e was 4.01 % o pH 10. Concu en ly wi h inc eased pH, lo a ion e iciency inc eased. In he o iginal
polyme allic o e, he Cu con en was 0.41 % a e subsequen ea men and lo a ion es s, he Cu con en was
inc eased o 1.38 % wi h Cu eco e y 86.18 %.
ACKNOWLEDGMENTS
This wo k was suppo ed by S uden G an P ojec SP2019/63 Was e om mining ac i i ies - aw ma e ial
esou ces. P ojec sus ainabili y No. LO1406 - Ins i u e o Clean Technologies o Mining and Use o Ene gy Raw
Ma e ials and he g an p og am "Suppo o Science and Resea ch in he Mo a ian-Silesian Region 2018" (RRC
/ 10/2018) and inanced om he budge o he Mo a ian-Silesian Region.
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